Dehydrogenation

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: Chemical_Process_Equipment.pdf : Chemical Process Equipment Selection and Design : : Stanley M. Walas : Referex

Page:  585 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  586 catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page:  587 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page:  588 for hydrodealkylatisn and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page:  595 operation feasible; butane dehydrogenation, for example, is done this way. Because of their

long

File Title Subject Author Keywords

: B568F9B71AFF6F12BB1B9F5694CE1.pdf : : : :

Page:  10 and hydrogenation and dehydrogenation reactions. Hydrogen Blistering. Hydrogen blistering is caused by atomic hydrogen

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: Air_Pollution_Prevention_Control_Handbook.pdf : Handbook of Air Pollution Prevention and Control : : Nicholas P. Cheremisinoff : Referex

Page:  110 processes: (1) dehydrogenation of naphthenes to aromatics; (2) dehydrocyclization of paraffins to 4) hydrocracking. The dehydrogenation reactions are very endothermic, requiring that the hydrocarbon stream be

Page:  116 and propylene, catalytic dehydrogenation of isobutane, and conversion of tertiary butyl alcohol recovered as

Page:  571 85, 88 catalytic dehydrogenation of isobutane, 99 catalytic hydrocracking, 85, 90 catalytic reforming, 85,

Page:  572 of paraffins, 93 dehydrogenation reactions, 93 dehydrogenation of naphthenes, 93 density, 160 deoxyribonucleic acid dehydrogenation reactions, 93 dehydrogenation of naphthenes, 93 density, 160 deoxyribonucleic acid (DNA), 13

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: Modeling_of_Chemical_Kinetics_and_Reactor_Design.pdf : : : :

Page:  412 homogeneous, vapor-phase dehydrogenation of benzene in a tubular-flow reactor considered two reactions:

Page:  418 F for the dehydrogenation of benzene using the Runge-Kutta fourth order method

Page:  419 of reactions for dehydrogenation of benzene. Rates of reaction (lb mol/ft3 •

Page:  549 125) Examples: decomposition, dehydrogenation, and sublimation reactions If k1 and k2 denote the forward

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: Pollution_Prevention_Through_Process_Integration.pdf : 92188.pdf : : : Referex

Page:  167 produced by the dehydrogenation of ethylbenzene using live steam over an oxide catalyst at

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: Intro_to_ChemE_Analysis_Using_MATHEMATICA.pdf : : : : Referex

Page:  374 The hydrogenation and dehydrogenation of alkenes and alkanes are reversible processes that favor the

Page:  511 For example, the dehydrogenation of saturated alkanes and alkyl aromatics to produce alkenes and that is, the dehydrogenation of alkanes to alkenes and hydrogen, continuous removal of either hydrogen by a dehydrogenation of alkane. The extent to which the hydrogen is removed

File Title

: Applied_Process_Design_VOLUME1_3E.pdf : APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition Subject : Author : Ernest E. Ludwig Keywords : Referex

Page:  543 inch stack) 0 Dehydrogenation unit X Hydrogen (31-inch stack) y Hydrogen (

File Title Subject Author Keywords

: Chemistry_of_Petrochemical_Processes_2E.pdf : : : : Referex

Page:  4 of Propane, 172, Dehydrogenation of Propane 172, Nitration of Propane 173 n-Butane Chemicals

Page:  44 developed for the dehydrogenation of propane to propylene for petrochemical use. Propylene has always

Page:  45 for olefin production. Dehydrogenation of n-butane to butenes and to butadiene is an (Chapter 3). Dehydrogenation of isobutane produces isobutene, which is a reactant for the

Page:  46 production except the dehydrogenation of propane. Catalyst CH3CH2–CH3 r CH3CH=CH2+H2Table

Page:  47 for ethylene production. Dehydrogenation of butanes is a second source of butenes. However, this

Page:  50 are the catalytic dehydrogenation of butanes and butenes, and dehydration of 1,4butanediol. Butadiene isoprene is the dehydrogenation of C5 olefins (tertiary amylenes) obtained by the extraction

Page:  74 such as the dehydrogenation of naphthenes and the dehydrocyclization of paraffins to aromatics. Catalytic

Page:  75 catalytic sites, hydrogenation-dehydrogenation sites and acid sites. The former sites are provided by best known hydrogenation-dehydrogenation catalyst and the latter (acid sites) promote carbonium ion

Page:  76

aromatics are the dehydrogenation of naphthenes and the dehydrocyclization of paraffins. The first reaction represented by the dehydrogenation of cyclohexane to benzene. This reaction is fast; it reaches lower than the dehydrogenation of cyclohexanes. Table 3-6 shows the effect of temperature

Page:  78 to aromatics (dehydrogenation of naphthenes and dehydrocyclization of paraffins) produce hydrogen and are

Page:  81 important because the dehydrogenation of naphthenes to aromatics can reach equilibrium faster than the paraffins. Because the dehydrogenation of naphthenes and the dehydrocyclization of paraffins are highly endothermic,

Page:  92 sites and hydrogenation-dehydrogenation sites. Amorphous silica-alumina, zeolites, or a mixture of them 30 The hydrogenation-dehydrogenation activity, on the other hand, is provided by catalysts such

Page:  93 catalyst with hydrogenation-dehydrogenation activity, the olefins are hydrogenated to paraffinic compounds. This reaction

Page:  101 formation and hydrogenation-dehydrogenation reactions. The reaction may start by forming a carbocation via

Page:  104 a free radical dehydrogenation reaction, where hydrogen is a coproduct: CH3CH3 r CH2=CH2

Page:  105 tube alloys catalyze dehydrogenation and formation of coke. Coke formation reduces product yields, increases

Page:  116 by the catalytic dehydrogenation of butanes or a butane/butene mixture. CH3CH2CH2CH3 r CH2= first step involves dehydrogenation of the butanes to a mixture of butenes which are Lummus fixed-bed dehydrogenation of C4 mixture to butadiene.52 The process may also used for the dehydrogenation of mixed amylenes to isoprene. In the process, the hot

Page:  117 uses an oxidative-dehydrogenation catalyst in the presence of air and steam. The C4 Hydrogen released from dehydrogenation reacts with oxygen, thus removing it from the equilibrium mixture of the oxidative dehydrogenation process was made by Welch et al. They concluded that

Page:  118 comes from the dehydrogenation of C5 olefin fractions from cracking processes, several schemes are for isoprene production. Dehydrogenation of Tertiary Amylenes (Shell Process) t-Amylenes (2aqueous sulfuric acid. Dehydrogenation of t-amylenes over a dehydrogenation catalyst produces isoprene. The amylenes over a dehydrogenation catalyst produces isoprene. The overall conversion and recovery of t-

Page:  142 olefin by a dehydrogenation step: The carbide mechanism, however, does not explain the formation

Page:  185 as a fumigant. DEHYDROGENATION OF PROPANE (Propene Production) The catalytic dehydrogenation of propane Production) The catalytic dehydrogenation of propane is a selective reaction that produces mainly propene: Lummus-Crest Catofin dehydrogenation process.3 For a given dehydrogenation system, i.e., operating For a given dehydrogenation system, i.e., operating temperature and pressure, thermodynamic theory provides

Page:  186 Lummus Crest Catofin dehydrogenation process:3 (1) reactor, (2) compressor, (3) temperature on the dehydrogenation of different light paraffins.4 NITRATION OF PROPANE (Production

Page:  187 temperature on the dehydrogenation of light paraffins at one atmosphere.4 Nitropropane reacts with

Page:  191 to be the dehydrogenation of propane and butane to the corresponding olefins followed by the predominance of dehydrogenation and cracking. Methane and ethane are by-products from the

Page:  193 hydrogen (from dehydrogenation of propane) through the reverse water gas shift reaction. CO2

Page:  194 isomerization followed by dehydrogenation to isobutene. The Catofin process is currently used to dehydrogenate

Page:  211 activated copper-catalyzed dehydrogenation of ethanol. Currently, acetaldehyde is obtained from ethylene by using oxidation or the dehydrogenation of ethanol (approximately 500°C for the oxidation and C for the dehydrogenation). Ethylene oxidation is carried out through oxidation-reduction (redox).

Page:  219 are produced by dehydrogenation of nparaffins, dehydrochlorination of monochloroparaffins, or by oligomerization of ethylene complexes catalyze the dehydrogenation of n-paraffins to α-olefins. The reaction uses a

Page:  242 isopropanol by a dehydrogenation, oxidation, or a combined oxidation dehydrogenation route. The dehydrogenation reaction a combined oxidation dehydrogenation route. The dehydrogenation reaction is carried out using either copper dehydrogenation route. The dehydrogenation reaction is carried out using either copper or zinc oxide

Page:  243 used for the dehydrogenation reaction. Acetone can also be coproduced with allyl alcohol in produced from the dehydrogenation of isopropanol and adsorbed on the catalyst surface selectively hydrogenates

Page:  255 by the catalyzed dehydrogenation of sec-butanol over zinc oxide or brass at about

Page:  258 produce MEK by dehydrogenation, as mentioned earlier. 2-Butanol is also used as a

Page:  269 remainder comes from dehydrogenation of n-butane or n-butene streams (Chapter 3).

Page:  279

11 billion pounds. Dehydrogenation of ethylbenzene to styrene occurs over a wide variety of used for the dehydrogenation reaction. Typical reaction

Page:  280 followed by catalytic dehydrogenation to styrene:8 Figure 10-3. Schematic diagram of the

Page:  283 α-methylstyrene by dehydrogenation. α-Methylstyrene is used as a monomer for polymer manufacture

Page:  288 corresponding n-paraffins. Dehydrogenation of nparaffins to monoolefins using a newly developed dehydrogenation catalyst a newly developed dehydrogenation catalyst by UOP has been reviewed by Vora et al. monoolefins. Because the dehydrogenation product contains a higher concentration of olefins for a given 9) combines the dehydrogenation of n-paraffins and the alkylation of benzene.17 Monoolefins Monoolefins from the dehydrogenation section are introduced to a fixed-bed alkylation reactor over

Page:  289 (1) pacol dehydrogenation reactor, (2) gas-liquid separation, (3) reactor for

Page:  295 to benzene. The dehydrogenation of cyclohexane Figure 10-12. Effect of hydrogen purity and

Page:  297 over a hydrogenation-dehydrogenation catalyst such as nickel. The hydrodealkylation is essentially a hydrocracking

Page:  393 from, 259 from dehydrogenation of C4, 103–104 polymerization with Li compounds, 308 polymers 62–65 Catofin dehydrogenation process, 173 Cellulose, 301 Chain addition polymerization, 304–308 Charactenzation

Page:  394 from, 315 Cycloparaffins dehydrogenation of, 63 in crude oils, 13 DDT, 278 DEA ( to butadiene, 104 Dehydrogenation of ter-amylenes, 105 butanes and butenes, 103 cycloparaffins, 63

Page:  398

process for C4 dehydrogenation, 103 Malathion, 243 Maleic anhydride 1,4-butanediol from, 242–243

Page:  400 scheme, 297 Lummus dehydrogenation process for butadiene, 103 Physical absorption, 3 Physical adsorption, 3,

Page:  401 173 cracking, 97 dehydrogenation, 172 Lummus-Crest process, 173 temperature effect on, 172 heating

File Title Subject Author Keywords

: Adhesion_Science_and_Engineering_VOLUME2.pdf : Surfaces, Chemistry & Applications : : M. Chaudhury and A.V. Pocius : Referex

Page:  614 through hydrogenation and dehydrogenation reactions. Hydrogenation of the first conjugated carbon-carbon double bond

Page:  624 catalyst, followed by dehydrogenation; a-methylstyrene is obtained as a byproduct in the production toluene followed by dehydrogenation.

File Title Subject Author Keywords

: Coulson_Richardsons_Chemical_Engineering_Volume_2.pdf : : : : Referex

Page:  568 formed by the dehydrogenation of ethyl benzene are shown. It may be seen that,

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: Fluid_Catalytic_Cracking_Handbook_2E.pdf : 92155.pdf : : :

Page:  77 reactions, such as dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation means polymerization,

Page:  78 matrix. Nickel promotes dehydrogenation reactions, removing hydrogen from stable compounds and making unstable olefins,

Page:  79 activity to promote dehydrogenation reactions, A small amount of nickel in the FCC feed to increase the dehydrogenation reactions. Chlorides in the feed reactivate aged nickel, resulting in an indicator of dehydrogenation reactions. However, the ratio is sensitive to the reactor temperature

Page:  80 Vanadium also promotes dehydrogenation reactions, but less than nickel. Vanadium"s contribution to hydrogen yield

Page:  119 indicative of the dehydrogenation activity of the metals on the catalyst. The addition of

Page:  123 catalyst. They cause dehydrogenation reactions, which increase hydrogen production and decrease gasoline yields. Vanadium

Page:  137 with nickel, the dehydrogenation reactions that are

Page:  141 7. 8. Naphthenes Dehydrogenation Dealkylation Condensation C7H14 - n-C8H18 lso-C3H Ar-C3H

Page:  150

prominent reactions are dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a "clean" feedstock molecular hydrogen. Therefore, dehydrogenation reactions will proceed only if the catalyst is contaminated with

Page:  152 Transalkylation Cyclization Dealkylation Dehydrogenation Polymerization Alkylation Specific Reaction n-C10H22 -> n-C7H16 +

Page:  340 catalyst, promoting undesirable dehydrogenation and condensation reactions. These nonselective reactions increase gas and coke

Page:  381 Nickel, 63, 108 dehydrogenation, 135 and hydrogen, 64 passivation, 122 Nitrogen basic, 54 effects,

Page:  382 3§7 dehydrogenation, 135 hydrogen transfer, 134 isomerization, 133 thermal cracking, 126, 283

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: Organic_Chemistry.pdf : : : :

Page:  811 the product of dehydrogenation of the natural product guaiol with elemental sulfur. From the

Page:  1095 RNH2 PThis dehydrogenation is the reverse of palladium-catalysed hydrogenation. NH2 HN R

Page:  1289 of FAD involve dehydrogenations—as in double bond formation from single bonds. Of course,

Page:  1312 a sulfur-promoted dehydrogenation has been suggested for the removal of the hydrogen atoms.

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: Renewable_Energy_3E_.pdf : : : :

Page:  507 second stage involves dehydrogenation (removing hydrogen atoms from the biomass material), such as

Page:  508 4.152) followed by dehydrogenation: 2C2H5OH + CO2 → 2CH3COOH + CH4 (4.153) The

Page:  571 of hydrogenation and dehydrogenation multistage adia5.2 ENERGY STORAGE 553

Page:  572 nitrogen in the dehydrogenation and hydrogen in the hydrogenation units. A number of ammoniated

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: BRETHERICK_Handbook_Reactive_Chemical_Hazards_6E_VOLUME1.pdf : : : : Referex

Page:  628 1978, 88, 120946 Dehydrogenation of the ‘Hantzsch’ ester in a melt with the

File Title Subject Author Keywords

: Chemical_Process_Equipment.pdf : Chemical Process Equipment Selection and Design : : Stanley M. Walas : Referex

Page:  585 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  586 catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page:  587 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page:  588 for hydrodealkylatisn and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page:  595 operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

File Title Subject Author Keywords

: 84607_01.pdf : c01 1..44 : : :

Page:  31 intermediate reduction step. Dehydrogenation of the alcohol to the aldehyde is followed by aldol

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: 84607_16.pdf : c01 1..60 : : :

Page:  13 procedure, desaturation or dehydrogenation, offers more attractive prospects. Flavor deterioration in fat-rich milk

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: 84607_32.pdf : c03 49..66 : : :

Page:  10 be explained by dehydrogenation and rearrangement of a- and g-terpinene, and hydrogenation and

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: 84607_41.pdf : c12 319..360 : : :

Page:  12 lycopene by hydrogenation, dehydrogenation, cyclization, and oxidation, or a combination of these processes (

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: 84607_80.pdf : c08 279..306 : : :

Page:  11 begins with the dehydrogenation of unsaturated fatty acids, such as linolenic acid, by means

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: 84607_81.pdf : c09 307..352 : : :

Page:  9 to be the dehydrogenation from the a-methylene group to form a radical. Since

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: Instrumentation_Reference_Book_3E.pdf : Instrumentation Reference Book Third Edition : : Walt Boyes : Referex

Page:  217 co-doping and dehydrogenation of the fiber to increase its photosensitivity. Gratings have also

File Title Subject Author Keywords

: Rules_of_Thumb_for_Chemical_Engineers_3E.pdf : RULES OF THUMB FOR CHEMICAL ENGINEERS : : CARL BRANAN : Referex

Page:  226 proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page:  271 development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

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: M26.pdf : Section 26 — Members : : :

Page:  11 Quorum & Associates DEHYDROGENATION SYSTEMS Aker Kvaerner, Inc. CB&I Howe-Baker Process &

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: J.G.Speight - Chemical and process design handbook.pdf : : : :

Page:  4 Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

Page:  27 DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen. very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig. from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page:  28 distillation follows. The dehydrogenation of n-paraffins yields detergent alkylates and nolefins. The rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

Page:  43 higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page:  44 desired temperature. See Dehydrogenation.

Page:  74 alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

Page:  96

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

Page:  153 and by the dehydrogenation of butane or the butenes using an iron oxide (

Page:  158 to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page:  160 butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page:  176 this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

Page:  270 through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to 2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

Page:  302 oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

Page:  315 is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

Page:  331 hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page:  338 produced by the dehydrogenation of iso-pentane in the same plant used for the

Page:  353 by cracking and dehydrogenation of n-paraffins, as practiced in the petrochemical section of

Page:  422 nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

Page:  440 such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

Page:  548 from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page:  561 are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page:  565 oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

Page:  582 yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

Page:  627 of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

File Title

: Applied_Process_Design_VOLUME1_3E.pdf : APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition Subject : Author : Ernest E. Ludwig Keywords : Referex

Page:  542 inch stack) 0 Dehydrogenation unit X Hydrogen (31-inch stack) y Hydrogen (

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: F585A1265F4FE23F5629236910CA9E78.pdf : : : :

Page:  9 which decreases the dehydrogenation poisoning activity of Ni and V. The catalytic cracker is reforming reaction is dehydrogenation of naphthenes, or removal of hydrogen from the molecule. Important

File Title Subject Author Keywords

: Coulson_Richardsons_Chemical_Engineering_Volume_2.pdf : : : : Referex

Page:  568 formed by the dehydrogenation of ethyl benzene are shown. It may be seen that,

File Title Subject Author Keywords

: Rules_of_Thumb_for_Chemical_Engineers_3E.pdf : RULES OF THUMB FOR CHEMICAL ENGINEERS : : CARL BRANAN : Referex

Page:  226 proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page:  271 development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

File Title Subject Author Keywords

: Renewable_Energy_3E_.pdf : : : :

Page:  507 second stage involves dehydrogenation (removing hydrogen atoms from the biomass material), such as

Page:  508 4.152) followed by dehydrogenation: 2C2H5OH + CO2 → 2CH3COOH + CH4 (4.153) The

Page:  571 of hydrogenation and dehydrogenation multistage adia5.2 ENERGY STORAGE 553

Page:  572 nitrogen in the dehydrogenation and hydrogen in the hydrogenation units. A number of ammoniated

File Title Subject Author Keywords

: Chemical_Process_Equipment.pdf : Chemical Process Equipment Selection and Design : : Stanley M. Walas : Referex

Page:  585 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  586 catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page:  587 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page:  588 for hydrodealkylatisn and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page:  595 operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

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: 677rev.pdf : Microsoft Word - 677rev.doc : : Administrator :

Page:  3 a set of dehydrogenation and cyclization reactions finally yielding a graphitic coke layer. Several

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: Borsa_20PhD_20Thesis_20Defense.PDF : Defense : : Tom McKinnon :

Page:  23 subsequent impingement and dehydrogenation on the reactor surface. » Iron plays a role in

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: ccl4 effect on pyrolysis reaction.pdf : No Job Name : : :

Page:  3 for EDC pyrolysis. Dehydrogenation of C2H4 is also known to be one of the

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: coking.pdf : Defense : : Tom McKinnon :

Page:  23 subsequent impingement and dehydrogenation on the reactor surface. » Iron plays a role in

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: Experiments in Catalytic Reaction Engineering (J. M. Berty).pdf : Experiments in Catalytic Reaction Engineering : : J. M. Berty : Referex

Page:  60 such as butane dehydrogenation. For exothermic reactions, very small diameter tubes with a single

Page:  165 presented for the dehydrogenation of butane.

Page:  199 for an endothermic dehydrogenation in the synthetic rubber program during World War 11 were

Page:  202 vehicle fLels. Ethylbenzene dehydrogenation to styrene is another example. On Figure 8.:2.2 the

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: Fluid catalytic cracking Handbook.pdf : 92155.pdf : : :

Page:  77 reactions, such as dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation means polymerization,

Page:  78 matrix. Nickel promotes dehydrogenation reactions, removing hydrogen from stable compounds and making unstable olefins,

Page:  79 activity to promote dehydrogenation reactions, A small amount of nickel in the FCC feed to increase the dehydrogenation reactions. Chlorides in the feed reactivate aged nickel, resulting in an indicator of dehydrogenation reactions. However, the ratio is sensitive to the reactor temperature

Page:  80 Vanadium also promotes dehydrogenation reactions, but less than nickel. Vanadium"s contribution to hydrogen yield

Page:  119 indicative of the dehydrogenation activity of the metals on the catalyst. The addition of

Page:  123 catalyst. They cause dehydrogenation reactions, which increase hydrogen production and decrease gasoline yields. Vanadium

Page:  137 with nickel, the dehydrogenation reactions that are

Page:  141 7. 8. Naphthenes Dehydrogenation Dealkylation Condensation C7H14 - n-C8H18 lso-C3H Ar-C3H

Page:  150

prominent reactions are dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a "clean" feedstock molecular hydrogen. Therefore, dehydrogenation reactions will proceed only if the catalyst is contaminated with

Page:  152 Transalkylation Cyclization Dealkylation Dehydrogenation Polymerization Alkylation Specific Reaction n-C10H22 -> n-C7H16 +

Page:  340 catalyst, promoting undesirable dehydrogenation and condensation reactions. These nonselective reactions increase gas and coke

Page:  381 Nickel, 63, 108 dehydrogenation, 135 and hydrogen, 64 passivation, 122 Nitrogen basic, 54 effects,

Page:  382 3§7 dehydrogenation, 135 hydrogen transfer, 134 isomerization, 133 thermal cracking, 126, 283

File

: BRANAN, C. R. (2002). Rules of Thumb for Chemical Engineers (3rd ed.).pdf Title : RULES OF THUMB FOR CHEMICAL ENGINEERS Subject : Author : CARL BRANAN Keywords : Referex

Page:  226 proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page:  271 development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

File Title Subject Author Keywords

: Chemical Reaction Engineering & kinetics.pdf : : : :

Page:  28 independent equations. The dehydrogenation of ethane (C,H,) is used to produce ethylene

Page:  106 1) Dehydration and dehydrogenation of C$H,OH VV QH,OH + GH, +

Page:  124 metal catalyst favors dehydrogenation of an alcohol to an aldehyde, but an oxide catalyst

Page:  134 ‘In the dehydrogenation of &He to produce CzH4, CH4 is a minor

Page:  156 in the ethane dehydrogenation mechanism of Section 6.1.2: Ho + C,H; + C,

Page:  157 rate of ethane dehydrogenation. These and similar reactions have a substantial influence in reactions

Page:  172 process like ethane dehydrogenation, where detailed molecular models of the free-radical chemistry are

Page:  183 kinetics of ethane dehydrogenation to produce ethylene, the relatively simple mechanism given in Section

Page:  190 6.1.2 for the dehydrogenation of CzH6, obtain the rate law for CzH6 + Cz&

Page:  191 11 on the dehydrogenation of ethane to produce ethylene. It can be treated as

Page:  195

good hydrogenation and dehydrogenation catalysts. (7) Although it may be correct to say

Page:  234 and subsequently catalyze dehydrogenation reactions. In this case, the yield of gasoline is reduced,

Page:  238 kinetics of ethanol dehydrogenation over Cu in the presence of water vapor, acetone, or

Page:  295 S) by a dehydrogenation reaction catalyzed by yeast alcohol dehydrogenase (YADH). Nikolova et

Page:  304 Examples are the dehydrogenation of C,H6 to produce C,H, (noncatalytic, low

Page:  384 such as the dehydrogenation of ethane for production of ethylene, take place in such example, in the dehydrogenation of ethylbenzene for the production of styrene monomer, or in

Page:  385 as in the dehydrogenation of ethane to ethylene. We consider next the three types

Page:  397 Nonisobaric Operation The dehydrogenation of ethane (A) to ethene (B) is conducted

Page:  445 which may undergo dehydrogenation to form benzene and isomerization to form methylcyclopentane, as follows:

Page:  531 styrene monomer by dehydrogenation of ethylbenzene: CsH,, * CsH, + H, (W This

Page:  538 we use the dehydrogenation of ethylbenzene, reaction (D) in Section 21.1. This is example. For the dehydrogenation of ethylbenzene at equilibrium, CsH,, (EB) + CsH, (

Page:  540 such as the dehydrogenation of ethylbenzene), as also shown in Section 5.3 and illustrated

Page:  549 ethylbenzene (EB) dehydrogenation reactor in Sarnia, Ontario, as it existed at that time.

involving only the dehydrogenation reaction ((D) in Section 21.1), and use the kinetics

Page:  565 stages, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer), a) For the dehydrogenation of ethylbenzene (A), reaction (D) in Section 21.1,

Page:  566 flow, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer). flow, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer). flow, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer).

Page:  682 517,574,575 Ethane, CzH,+ dehydrogenation, 35-36,154,286,366, 376-377,379-380 mechanism, 116,124-125,137,138-139,158 165,172,173314,445 Ethylbenzene, CsHrs: dehydrogenation to styrene, 176,366,513,522 equilibrium considerations, 520-521,522, 547 reactor calculations,

Page:  685 273,275 for ethane dehydrogenation, 116,124-125, 137,138-139,158,165,172,173-175 for formation of HBr, 160-

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Page:  121 for the catalytic dehydrogenation of ethylbenzene to form styrene: C8H10 !C8H8

Page:  145 favorable equilibrium. Ethylbenzene dehydrogenation fits this situation. Repeat Problem 3.7 but substitute an annular

Page:  263 HR for the dehydrogenation of ethylbenzene to styrene at 298.15K and 1 bar. Solution:

Page:  264 for the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. Solution: From Example 7.8,

Page:  265 R for the dehydrogenation of ethylbenzene to styrene at 298.15 K. Solution: Table 7.2

Page:  272 of the ethylbenzene dehydrogenation reaction at 298.15K and 0.5 atm. Consider two cases: 1.

Page:  273 from the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. The starting composition is amount of a dehydrogenation catalyst. The reaction rate has the form kf A

Page:  274 trajectory for ethylbenzene dehydrogenation.

Page:  394 process for the dehydrogenation of ethylbenzene uses 3-mm spherical catalyst particles. The rate

Page:  407 10.5. The ethylbenzene dehydrogenation catalyst of Example 3.1has a firstorder rate

constant of 3.752

Page:  410 C., ‘‘Catalytic dehydrogenation of ethylbenzene,’’ Chem. Eng. Prog., 44, 275–286 (1948).

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Page:  4 Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

Page:  27 DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen. very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig. from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page:  28 distillation follows. The dehydrogenation of n-paraffins yields detergent alkylates and nolefins. The rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

Page:  43 higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page:  44 desired temperature. See Dehydrogenation.

Page:  74 alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

Page:  96

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

Page:  153 and by the dehydrogenation of butane or the butenes using an iron oxide (

Page:  158 to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page:  160 butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page:  176 this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

Page:  270 through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to 2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

Page:  302 oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

Page:  315 is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

Page:  331 hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page:  338 produced by the dehydrogenation of iso-pentane in the same plant used for the

Page:  353 by cracking and dehydrogenation of n-paraffins, as practiced in the petrochemical section of

Page:  422 nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

Page:  440 such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

Page:  548 from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page:  561 are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page:  565 oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

Page:  582 yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

Page:  627 of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

File

: Cheremisinoff - Pressure Safety Design Practices for Refinery and Chemical Operations.pdf Title : Subject : Author : Keywords :

Page:  21 cracking, isomerization, alkylation, dehydrogenation, etc., taking place in a cat reactor, they are complicated,

Page:  99 as feedstock for dehydrogenation to butadiene. The rich acid extract is flashed to about

Page:  100 1-butenes for dehydrogenation feed, the isobutylene dimer being added to the motor gasoline

Page:  102 isobutylene extraction, butene dehydrogenation, or used in further refinery processing. Isoprene The demand for

Page:  106 from Ethylbenzene by Dehydrogenation Ethylbenzene is dehydrogenated to styrene over a fixed bed of

File

: Ed Peters and Timmerhaus - Plant Design and Economics for Chemical Engineer - 4th Edition.pdf Title : Subject : Author : Keywords :

Page:  20 by catalytic t dehydrogenation of

Page:  855 produced by the dehydrogenation of isopropanol according to the following reaction: CH3\ /H

Page:  880 production by catalytic dehydrogenation are to be analyzed with respect to three variables. These

File

: Ludwig Applied_Process_Design_For_Chemical_And_Petrochemical_Plants__Volume_1 3rd Ed 1999.pdf Title : APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition Subject : Author : Ernest E. Ludwig Keywords : Referex

Page:  543 inch stack) 0 Dehydrogenation unit X Hydrogen (31-inch stack) y Hydrogen (

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Page:  368 of acetone. Catalytic dehydrogenation of ethyl benzene. Hydrochlorination of methanol. Catalytic dehydrogenation of nof methanol. Catalytic dehydrogenation of n-butenes; feedstock of liquid mixed hydrocarbon stream containing

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Page:  568 formed by the dehydrogenation of ethyl benzene are shown. It may be seen that,

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: Soares - Process Engineering Equipment Handbook - 2002.pdf : : : :

Page:  1220 of naphthenes through dehydrogenation and of paraffins through isomerization and dehydrocyclization. The reformer catalyst, reformers do. The dehydrogenation and dehydrocyclization reactions produce large amounts of hydrogen as a

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Page:  5 Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

Page:  28 DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen. very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig. from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page:  29 distillation follows. The dehydrogenation of n-paraffins yields detergent alkylates and nolefins. The rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

Page:  44 higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page:  45 desired temperature. See Dehydrogenation.

Page:  75 alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

Page:  97

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

Page:  154 and by the dehydrogenation of butane or the butenes using an iron oxide (

Page:  159 to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page:  161 butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page:  177 this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

Page:  271 through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to 2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

Page:  303 oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

Page:  316 is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

Page:  332 hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page:  339 produced by the dehydrogenation of iso-pentane in the same plant used for the

Page:  354 by cracking and dehydrogenation of n-paraffins, as practiced in the petrochemical section of

Page:  423 nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

Page:  441 such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

Page:  549 from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page:  562 are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page:  566 oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

Page:  583 yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

Page:  628 of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

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Page:  581 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  582 catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page:  583 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page:  584 for hydrodealkylation and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page:  592 operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

Page:  597 from ethanol 18. Dehydrogenation of isopropanol 19. Isomerization of n-butane 20. Postchlorination

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Page:  13 by cracking and dehydrogenation of n-paraffins, as practiced in the petrochemical section of

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Page:  15 alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

Page:  37 by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

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Page:  2 is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

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Page:  16 such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

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Page:  10 higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page:  11 desired temperature. See Dehydrogenation.

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Page:  38 from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page:  51 are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page:  55 oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

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Page:  3 hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page:  10 produced by the dehydrogenation of iso-pentane in the same plant used for the

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Page:  26 nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

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Page:  7 through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to 2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

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Page:  29 and by the dehydrogenation of butane or the butenes using an iron oxide (

Page:  34 to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page:  36 butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page:  52 this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

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Page:  3 DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen. very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig. from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page:  4 distillation follows. The dehydrogenation of n-paraffins yields detergent alkylates and nolefins. The rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

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Page:  4 of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

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Page:  14 yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

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Page:  10 oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

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Page:  1 Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

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Page:  1 BY VAPOR PHASE DEHYDROGENATION ACETONITRILE ACETONITRILE RECOVERY IN ACRYLONITRILE MANUFACTURE ACETYLENE ACETYLENE FROM CALCIUM

Page:  2 BUTENES BY OXIDATIVE DEHYDROGENATION BUTADIENE RECOVERY BY DIMETHYLFORMAMIDE EXTRACTIVE DISTILLATION BUTADIENE RECOVERY BY N-

Page:  5 FROM ETHANE BY OXYDEHYDROGENATION ETHYLENE FROM ETHANE BY CONVENTIONAL CRACKING WITH FRONT-END DEETHANIZATION

Page:  8 BY THE OLEFLEX DEHYDROGENATION PROCESS ISOBUTYLENE FROM ISOBUTANE BY THE SNAMPROGETTI/YARSINTEZ PROCESS ISODECYL

Page:  9 BY VAPOR PHASE DEHYDROGENATION OF METHANOL METHYL ISOBUTYL CARBINOL METHYL ISOBUTYL CARBINOL FROM METHYL

Page:  14 PROPANE BY CATALYTIC DEHYDROGENATION PROPYLENE, POLYMER GRADE, FROM REFINERY GRADE PROPYLENE (66 WT

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: Dipo Baskoro - Prarancangan Pabrik Metil Tersier Butil Eter dari Isobutylene dan Metanol.pdf Title : Microsoft Word - Dipo Baskoro - Prarancangan Pabrik Metil Tersier Butil Eter dari Isobutylene dan Metanol.doc Subject : Author : Dipo Keywords :

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: Levenspiel O. Chemical reaction engineering (3ed., Wiley, 19.pdf : : : :

Page:  513 21.12. In catalytic dehydrogenation of hydrocarbons the catalyst activity decays with use because of

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Page:  557 Provide oxygenates Isobutane dehydrogenation Feedstock for oxygenate synthesis Catalytic cracker naphtha fractionation Increase alkylate

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Page:  160 balances. The ethanol dehydrogenation reaction is carried out with the feed entering at 300 chart of ethanol dehydrogenation process.

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Page:  20 by catalytic t dehydrogenation of

Page:  855 produced by the dehydrogenation of isopropanol according to the following reaction: CH3\ /H

Page:  880 production by catalytic dehydrogenation are to be analyzed with respect to three variables. These

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Page:  226 proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page:  271 development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

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Page:  12 of LAS. The dehydrogenation of paraffins, followed by alkylation of benzene with a mixed

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Page:  20 hydrogen over hydrogenation-dehydrogenation catalysts, which may be supported on alumina or silica-alumina.

Page:  21 a suitable feed. Dehydrogenation is a main chemical reaction in catalytic reforming, and hydrogen is to promote dehydrogenation and hydrogenation reactions, that is, the production of aromatics,

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Page:  24 Condensation Dehydrogenation Esterification Halogenation and manufacture of halogens Hydrogenation

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Page:  38 cracking, oxidation, alkylation, dehydrogenation, hydration, and chlorination. Most processes use proprietary catalysts to increase

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Page:  10 fractionation section. The dehydrogenation of isobutane to isobutene is represented by iCH,CH(CH,), The gas phase dehydrogenation of isobutane to isobutene iC,Hlo 3 iC,H, +

Page:  11 process flowsheet for dehydrogenation of isobutane Mixing Point 4 unknowns (itAl, itBl, it4,

Page:  12 of gas phase dehydrogenation of isobutane before convergence.

Page:  13 of gas phase dehydrogenation of isobutane after convergence. The enthalpy of formation of iC, Formulas for the Dehydrogenation of lsobutene D3 = 0.35 (given fractional conversion of

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Page:  9 which decreases the dehydrogenation poisoning activity of Ni and V. The catalytic cracker is reforming reaction is dehydrogenation of naphthenes, or removal of hydrogen from the molecule. Important

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Page:  11 benzene to cyclohexane Dehydrogenation of ethylbenzene to styrene Tarhan (Catalytic Reactor Design, McGraw-

Page:  14 reaction in the dehydrogenation of ethylbenzene is to styrene and hydrogen, C6H5C2H5 C6H5C2H3 +

Page:  25 is a suitable dehydrogenation accelerator but possibly with a different most-favorable temperature. Catalytic

Page:  28 They catalyze hydrogenation/dehydrogenation as well as many of the reactions catalyzed by acids, 4. Dehydration and dehydrogenation combined utilizes dehydration agents together with mild dehydrogenation agents. Included together with mild dehydrogenation agents. Included in this class are phosphoric acid, silicamagnesia, 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Raney nickel or

Page:  29 are the hydrogenation/ dehydrogenation component of the catalyst and alumina is the acid component

Page:  32 and polyphosphazene membranes. Dehydrogenation processes in particular have been studied, with conversions in most

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Page:  35 studies of the dehydrogenation of heptane to toluene. Incomplete reaction, deterioration of catalyst performance,

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Page:  47 37 2-68 dehydrogenation 23-14 ethyl benzoate 2-37 2-52 2-68

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: 9614x_18.pdf : : : :

Page:  4 of naphthenes through dehydrogenation and of paraffins through isomerization and dehydrocyclization. The reformer catalyst, reformers do. The dehydrogenation and dehydrocyclization reactions produce large amounts of hydrogen as a

File Title Subject Author Keywords

: Process Engg Equipment Handbook_Soares.pdf : : : :

Page:  645 of naphthenes through dehydrogenation and of paraffins through isomerization and dehydrocyclization. The reformer catalyst, reformers do. The dehydrogenation and dehydrocyclization reactions produce large amounts of hydrogen as a

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Page:  4 of naphthenes through dehydrogenation and of paraffins through isomerization and dehydrocyclization. The reformer catalyst, reformers do. The dehydrogenation and dehydrocyclization reactions produce large amounts of hydrogen as a

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: Air_Pollution_Prevention_Control_Handbook.pdf : Handbook of Air Pollution Prevention and Control : : Nicholas P. Cheremisinoff : Referex

Page:  110 processes: (1) dehydrogenation of naphthenes to aromatics; (2) dehydrocyclization of paraffins to 4) hydrocracking. The dehydrogenation reactions are very endothermic, requiring that the hydrocarbon stream be

Page:  116 and propylene, catalytic dehydrogenation of isobutane, and conversion of tertiary butyl alcohol recovered as

Page:  571 85, 88 catalytic dehydrogenation of isobutane, 99 catalytic hydrocracking, 85, 90 catalytic reforming, 85,

Page:  572 of paraffins, 93 dehydrogenation reactions, 93 dehydrogenation of naphthenes, 93 density, 160 deoxyribonucleic acid dehydrogenation reactions, 93 dehydrogenation of naphthenes, 93 density, 160 deoxyribonucleic acid (DNA), 13

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Page:  568 formed by the dehydrogenation of ethyl benzene are shown. It may be seen that,

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Page:  427 removed in a dehydrogenation process that requires acidophilic (acid-forming) bacteria. The net

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: Finlayson B.A. - Introduction to Chemical Engineering Computing.pdf : Introduction to chemical engineering computing : : Bruce A. Finlayson. :

Page:  84 make acetaldehyde by dehydrogenation of ethanol over a silver catalyst (Aguilo´ and Acetaldehyde production by dehydrogenation of ethanol.

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: Harriot - Chemical Reactor Design.pdf : CHEMICAL REACTOR DESIGN : FM: Chemical Reactor Design : Peter Harriott :

Page:  70 the literature. The dehydrogenation of sec-butyl alcohol to methyl ethyl ketone on brass

Page:  71 Reaction rate for dehydrogenation of sec-butyl alcohol. (From Ref. 10.) Copyright ©

Page:  81 a chromia-alumina dehydrogenation catalyst, the catalyst activity and coke formation rate were measured

Page:  130 H2S-promoted oxidative dehydrogenation of butene was studied by Vodekar and Pasternak [12].

Page:  131 by the catalytic dehydrogenation of ethyl benzene (EB) in a two-stage fixed-

Page:  228 temperatures. 5.9 The dehydrogenation of ethyl benzene (EB) to styrene (S) is

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: Hill - An Introduction to Chemical Engineering Kinetics.pdf : : : :

Page:  28 will involve the dehydrogenation of ethane over a suitable catalyst (yet to be

Page:  31 produced by the dehydrogenation of butene over an appropriate catalyst. C4H8 H2 C4H6 In

Page:  80 a gas phase dehydrogenation reaction that occurs at a constant temperature of 1000 °

Page:  171 the catalytic oxidative dehydrogenation of various butene isomers to form 1,3-butadiene. Over a

Page:  176 6. Polymerization 7. Dehydrogenation Reactants N2 + H2 NH3 + O2 SO2 + O2

Page:  212 then act as dehydrogenation catalysts. The product distribution is markedly affected with lower yields

Page:  236 reduction, polymerization, dehydration, dehydrogenation, etc. Their versatility is a reflection of the range and

Page:  536 studied the catalytic dehydrogenation of cyclohexane to benzene over a platinum-onalumina catalyst.

Page:  537 have studied the dehydrogenation of cyclohexane to benzene over a platinum on alumina pelleted

Page:  547 judgment. 17. Oxidative Dehydrogenation of Butene to Butadiene UW Chemical Corporation Madison, Wisconsin To:

for the butene dehydrogenation reaction is effectively removed since hydrogen is converted to water for the endothermic dehydrogenation reaction. For preliminary discussions of the proposed expansion program, it to other oxidative dehydrogenation catalysts. Select a promising catalyst material and prepare a reactor

Page:  594 158-160 Butene, dehydrogenation, 22, 538-539 isomerization, 20 d-s-Butyl a-chloroacrylate

Page:  595 164-165 Cyclohexane, dehydrogenation, 527-529 Cyclohexanol, reaction with acetic acid, 69 Cyclohexene, from of tetrachloroethane, 307 Dehydrogenation, butene, 22, 162 cyclohexane, 527-529 ethane, 19-21 ethylbenzene,

Page:  596 equation, 493 Ethane, dehydrogenation, 19, 21 Ethanol, via hydration of ethylene, 12-14 reaction

Page:  599 536-537 Oxidative dehydrogenation of butene, 538-539 Ozone decomposition, 97-98, 123124

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: Licker M.D. - McGraw Hill Dictionary of Chemistry 2E.pdf : McGraw-Hill Dictionary of Chemistry : : :

Page:  76 formed by spontaneous dehydrogenation of tetrahydrocannabinol from cannabis. { kanə

Page:  116 ¯n } dehydrogenation [CHEM] Removal of hydrogen from a compound. { de

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: Licker M.D. - McGraw Hill Dictionary of Engineering 2E.pdf : : : :

Page:  93 hard, smooth butane dehydrogenation [CHEM ENG] A procrounded edge or surface; used for

Page:  162 } involving both dehydrogenation and cyclization, degradation [THERMO] The conversion of en- as

Page:  289 a Houdry butane dehydrogenation [CHEM ENG] refractory slurry. { ha¨ t

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: Nauman E.B. - Chemical reactor design, optimization, and scaleup.pdf : : : :

Page:  120 for the catalytic dehydrogenation of ethylbenzene to form styrene: C8H10 !C8H8

Page:  144 favorable equilibrium. Ethylbenzene dehydrogenation fits this situation. Repeat Problem 3.7 but substitute an annular

Page:  263 HR for the dehydrogenation of ethylbenzene to styrene at 298.15K and 1 bar. Solution:

Page:  264 for the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. Solution: From Example 7.8,

Page:  265 R for the dehydrogenation of ethylbenzene to styrene at 298.15 K. Solution: Table 7.2

Page:  272 of the ethylbenzene dehydrogenation reaction at 298.15K and 0.5 atm. Consider two cases: 1.

Page:  273 from the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. The starting composition is amount of a dehydrogenation catalyst. The reaction rate has the form kf A

Page:  274 trajectory for ethylbenzene dehydrogenation.

Page:  394 process for the dehydrogenation of ethylbenzene uses 3-mm spherical catalyst particles. The rate

Page:  407 10.5. The ethylbenzene dehydrogenation catalyst of Example 3.1 has a firstorder rate

constant of

Page:  410 C., ‘‘Catalytic dehydrogenation of ethylbenzene,’’ Chem. Eng. Prog., 44, 275–286 (1948).

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: Nunes - Membrane Technology.pdf : : : :

Page:  9 5.3.2 Large-scale dehydrogenations with inorganic membranes 210 5.3.3 OTM syngas process 212 5.3.4

Page:  14 debottlenecking 284, 285 dehydrogenation 201, 210–212 dense membrane 6 Desal-5 15, 16,

Page:  208 methane, several oxidative dehydrogenations have been investigated, including the conversion of ethane to ethene

Page:  209 up is the dehydrogenation of methanol and butane using A microporous g-alumina and

Page:  214 relatively simple alkane dehydrogenations. For the dehydrogenation of ethane catalytically active tubular membranes have dehydrogenations. For the dehydrogenation of ethane catalytically active tubular membranes have been used [ 72], whereas cyclohexane dehydrogenation was performed in packed-bed membrane reactors [73, 74]. e.g. the dehydrogenation of propane [79–82], isobuta-

Page:  215 industrial application of dehydrogenation membrane reactors. These are: defects in metallic membranes at elevated of commercially available dehydrogenation catalysts. Anew development in this field is the use of

Page:  217 assisted esterifications and dehydrogenations will be discussed as well as the OTM process for

Page:  223

5.3.2 Large-scale dehydrogenations with inorganic membranes Over the years, several processes for the for the catalytic dehydrogenation of propane to propylene have been developed, which can be process. As the dehydrogenation of propane to propylene comprises an equilibrium reaction (11), membranes in different dehydrogenation processes. As the Oleflex process uses four reactor beds in

Page:  224 feasibility, the propane dehydrogenation process requires membranes with a selectivity much higher than Knudsenviable membrane-assisted dehydrogenation process of propane. The potential application of ceramic membranes for membranes for the dehydrogenation of ethylbenzene to styrene (12) has also been evaluated 12) For the dehydrogenation of ethylbenzene in a packed bed ceramic membrane reactor, three mixture. By oxidative dehydrogenation, the oxygen burns the hydrogen which is formed (C).

Page:  225 configurations for the dehydrogenation of ethylbenzene [126].According to the study by van process for the dehydrogenation of ethylbenzene. The profit from the higher styrene yield by Aviable membrane-assisted dehydrogenation of ethylbenzene asks for cheaper membranes, being highly selective with

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: Odian G. - Principles of Polymerization. 4th edition.pdf : Principles of Polymerization : Team DDU : George Odian :

Page:  33 oxidative coupling (dehydrogenation) of p-xylene: nCH3 CH3 H CH2 CH2 H +

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: Schmidt - The Engineering of Chemical Reactions.pdf : : : :

Page:  33 is obtained by dehydrogenation of ethane. (a) Write out these reactions. (b)

Page:  69 much heat, while dehydrogenation reactions are fairly endothermic and oxidation reactions are fairly exothermic.

Page:  82 branched alkanes and dehydrogenation of cyclics to aromatics would enhance the octane enormously. In

Page:  85 These alkanes undergo dehydrogenation and cracking reactions. A higher-molecular-weight fraction of alkanes,

Page:  86 reaction is simple dehydrogenation, Cd6 -+ C2H4 + Hz In modern steam cracking processes

Page:  97 reactor stages, ethane dehydrogenation, ethylene oxidation, and ethylene oxide hydration. (a) What are (b) Both dehydrogenation and hydration have nearly 100% selectivity (with recycle of

Page:  99 all cracking and dehydrogenation reactions are strongly endothermic, while in the regenerator, strongly exothermic

Page:  101 is made by dehydrogenation of ethane. HCN is made by reacting CH4, NHs, and

Page:  124 l l C, dehydrogenation maleic anhydride l l FCC 400 - CH,OH l

Page:  216

by the oxidative dehydrogenation of ethane. Over a suitable catalyst the reactions and rates

Page:  220 The gas-phase dehydrogenation of ethane to ethylene C2H6 + CzH4 + H2 proceeds

Page:  260 causes the oxidative dehydrogenation of ethane to ethylene CzH6 + $2 -+ C2H4 causes the oxidative dehydrogenation of ethane to ethylene C2& + $2 -+ C2H4

Page:  281 causes the oxidative dehydrogenation of ethane to ethylene C2H6 + $2 + C2H4 causes the oxidative dehydrogenation of ethane to ethylene C2H6 + 502 + C2H4 +

Page:  501 concentrations. Hydrogenation and dehydrogenation reactor Another example of a gasphase membrane reactor is

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: Soares - Process Engineering Equipment Handbook.pdf : : : :

Page:  1220 of naphthenes through dehydrogenation and of paraffins through isomerization and dehydrocyclization. The reformer catalyst, reformers do. The dehydrogenation and dehydrocyclization reactions produce large amounts of hydrogen as a

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: Vannice - Kinetics of Catalytic Reactions.pdf : Kinetics of Catalytic Reactions : : :

Page:  166 is isopropyl alcohol dehydrogenation to produce acetone, and this is discussed in Illustration 7.2.

Page:  167 7.2 – Isopropanol Dehydrogenation on Cu: A L-H Reaction Model Isopropyl alcohol dehydrogenation Model Isopropyl alcohol dehydrogenation over copper catalysts has been studied by Rioux and Vannice

Page:  169 for Isopropyl Alcohol Dehydrogenation over 0.98% Cu/Activated Carbona (Reprinted from ref.

Page:  175 to hydrogenation or dehydrogenation reactions, such as those involving hydrocarbons and organic molecules, because

Page:  186 obtained if concurrent dehydrogenation reactions occur to create carbonaceous species on the surface which

Page:  191 Illustration 7.5 – Dehydrogenation of Methylcyclohexane on Pt: no RDS One of the easiest reactions – the dehydrogenation of methylcyclohexane (MCH) to toluene (TOL): C6H11CH3 ¼ used for a dehydrogenation reaction? Answer: To minimize deactivation by inhibiting the build-up

Page:  251 of freedom, 110 Dehydrogenation, 151, 175, 203 Density of sites (see Site density)

Page:  252 9, 175 Isopropanol dehydrogenation, 151 Isotherm Freundlich (see Freundlich isotherm) Langmuir (see

Page:  253 85, 205 Methylcyclohexane dehydrogenation, 175 Michaelis constant, 224 Michaelis-Menten enzyme kinetics, 224 Micropores,

Page:  255 (see Methylcyclohexane dehydrogenation) Tortuosity, 69 Total surface area (see Specific surface area)

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: Vogel - Fermentation and Biochemical Engineering Handbook.pdf : : : :

Page:  153 NAD in biochemical dehydrogenation. Microorganisms share similar chemical compositions and universal pathways. They all

Page:  809 Biocatalysts 3 Biochemical dehydrogenation 128 Bioenergetics 128 Biomedical device 677 Bioprocess Expert 702 Bioprocess

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: An introduction to chemical engineering kinetics.pdf : : : :

Page:  28 will involve the dehydrogenation of ethane over a suitable catalyst (yet to be

Page:  31 produced by the dehydrogenation of butene over an appropriate catalyst. C4H8 H2 C4H6 In

Page:  80 a gas phase dehydrogenation reaction that occurs at a constant temperature of 1000 °

Page:  171 the catalytic oxidative dehydrogenation of various butene isomers to form 1,3-butadiene. Over a

Page:  176 6. Polymerization 7. Dehydrogenation Reactants N2 + H2 NH3 + O2 SO2 + O2

Page:  212 then act as dehydrogenation catalysts. The product distribution is markedly affected with lower yields

Page:  236 reduction, polymerization, dehydration, dehydrogenation, etc. Their versatility is a reflection of the range and

Page:  536 studied the catalytic dehydrogenation of cyclohexane to benzene over a platinum-onalumina catalyst.

Page:  537 have studied the dehydrogenation of cyclohexane to benzene over a platinum on alumina pelleted

Page:  547 judgment. 17. Oxidative Dehydrogenation of Butene to Butadiene UW Chemical Corporation Madison, Wisconsin To:

for the butene dehydrogenation reaction is effectively removed since hydrogen is converted to water for the endothermic dehydrogenation reaction. For preliminary discussions of the proposed expansion program, it to other oxidative dehydrogenation catalysts. Select a promising catalyst material and prepare a reactor

Page:  594 158-160 Butene, dehydrogenation, 22, 538-539 isomerization, 20 d-s-Butyl a-chloroacrylate

Page:  595 164-165 Cyclohexane, dehydrogenation, 527-529 Cyclohexanol, reaction with acetic acid, 69 Cyclohexene, from of tetrachloroethane, 307 Dehydrogenation, butene, 22, 162 cyclohexane, 527-529 ethane, 19-21 ethylbenzene,

Page:  596 equation, 493 Ethane, dehydrogenation, 19, 21 Ethanol, via hydration of ethylene, 12-14 reaction

Page:  599 536-537 Oxidative dehydrogenation of butene, 538-539 Ozone decomposition, 97-98, 123124

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: ChemicalProcessDesignHandbook_muyac.pdf : : : :

Page:  4 Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

Page:  27 DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen. very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig. from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page:  28 distillation follows. The dehydrogenation of n-paraffins yields detergent alkylates and nolefins. The rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

Page:  43 higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page:  44 desired temperature. See Dehydrogenation.

Page:  74 alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

Page:  96

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

Page:  153 and by the dehydrogenation of butane or the butenes using an iron oxide (

Page:  158 to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page:  160 butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page:  176 this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

Page:  270 through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to 2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

Page:  302 oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

Page:  315 is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

Page:  331 hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page:  338 produced by the dehydrogenation of iso-pentane in the same plant used for the

Page:  353 by cracking and dehydrogenation of n-paraffins, as practiced in the petrochemical section of

Page:  422 nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

Page:  440 such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

Page:  548 from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page:  561 are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page:  565 oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

Page:  582 yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

Page:  627 of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

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: Coulson & Richardson"s Chemical Engineering. Vol. 6, Chemical Engineering Design, 4th Ed.pdf Title : Subject : Author : Keywords :

Page:  193 it undergoes catalytic dehydrogenation to acetone. The reactor exit gases (acetone, water, hydrogen

Page:  209 manufactured by the dehydrogenation of 2-butanol. A simplified description of the processes listing

Page:  325 manufactured by the dehydrogenation of 2-butanol using a shell and tube type reactor.

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: 1699_03.pdf : Heat Transfer in Industrial Combustion : Chapter 3: Heat Transfer Modes : Charles E. Baukal, Jr. :

Page:  38 hypothesized that the dehydrogenation and polymerization of hydrocarbon fuels occurs in the liquid phase, particles agglomerate after dehydrogenation and polymerization are completed. Gray et al. (1976) noted

File Title Subject Author Keywords

: Chemistry of Petrochemical Processes 2E.pdf : : : : Referex

Page:  4 of Propane, 172, Dehydrogenation of Propane 172, Nitration of Propane 173 n-Butane Chemicals

Page:  44 developed for the dehydrogenation of propane to propylene for petrochemical use. Propylene has always

Page:  45 for olefin production. Dehydrogenation of n-butane to butenes and to butadiene is an (Chapter 3). Dehydrogenation of isobutane produces isobutene, which is a reactant for the

Page:  46 production except the dehydrogenation of propane. Catalyst CH3CH2–CH3 r CH3CH=CH2+H2Table

Page:  47 for ethylene production. Dehydrogenation of butanes is a second source of butenes. However, this

Page:  50 are the catalytic dehydrogenation of butanes and butenes, and dehydration of 1,4butanediol. Butadiene isoprene is the dehydrogenation of C5 olefins (tertiary amylenes) obtained by the extraction

Page:  74 such as the dehydrogenation of naphthenes and the dehydrocyclization of paraffins to aromatics. Catalytic

Page:  75 catalytic sites, hydrogenation-dehydrogenation sites and acid sites. The former sites are provided by best known hydrogenation-dehydrogenation catalyst and the latter (acid sites) promote carbonium ion

Page:  76

aromatics are the dehydrogenation of naphthenes and the dehydrocyclization of paraffins. The first reaction represented by the dehydrogenation of cyclohexane to benzene. This reaction is fast; it reaches lower than the dehydrogenation of cyclohexanes. Table 3-6 shows the effect of temperature

Page:  78 to aromatics (dehydrogenation of naphthenes and dehydrocyclization of paraffins) produce hydrogen and are

Page:  81 important because the dehydrogenation of naphthenes to aromatics can reach equilibrium faster than the paraffins. Because the dehydrogenation of naphthenes and the dehydrocyclization of paraffins are highly endothermic,

Page:  92 sites and hydrogenation-dehydrogenation sites. Amorphous silica-alumina, zeolites, or a mixture of them 30 The hydrogenation-dehydrogenation activity, on the other hand, is provided by catalysts such

Page:  93 catalyst with hydrogenation-dehydrogenation activity, the olefins are hydrogenated to paraffinic compounds. This reaction

Page:  101 formation and hydrogenation-dehydrogenation reactions. The reaction may start by forming a carbocation via

Page:  104 a free radical dehydrogenation reaction, where hydrogen is a coproduct: CH3CH3 r CH2=CH2

Page:  105 tube alloys catalyze dehydrogenation and formation of coke. Coke formation reduces product yields, increases

Page:  116 by the catalytic dehydrogenation of butanes or a butane/butene mixture. CH3CH2CH2CH3 r CH2= first step involves dehydrogenation of the butanes to a mixture of butenes which are Lummus fixed-bed dehydrogenation of C4 mixture to butadiene.52 The process may also used for the dehydrogenation of mixed amylenes to isoprene. In the process, the hot

Page:  117 uses an oxidative-dehydrogenation catalyst in the presence of air and steam. The C4 Hydrogen released from dehydrogenation reacts with oxygen, thus removing it from the equilibrium mixture of the oxidative dehydrogenation process was made by Welch et al. They concluded that

Page:  118 comes from the dehydrogenation of C5 olefin fractions from cracking processes, several schemes are for isoprene production. Dehydrogenation of Tertiary Amylenes (Shell Process) t-Amylenes (2aqueous sulfuric acid. Dehydrogenation of t-amylenes over a dehydrogenation catalyst produces isoprene. The amylenes over a dehydrogenation catalyst produces isoprene. The overall conversion and recovery of t-

Page:  142 olefin by a dehydrogenation step: The carbide mechanism, however, does not explain the formation

Page:  185 as a fumigant. DEHYDROGENATION OF PROPANE (Propene Production) The catalytic dehydrogenation of propane Production) The catalytic dehydrogenation of propane is a selective reaction that produces mainly propene: Lummus-Crest Catofin dehydrogenation process.3 For a given dehydrogenation system, i.e., operating For a given dehydrogenation system, i.e., operating temperature and pressure, thermodynamic theory provides

Page:  186 Lummus Crest Catofin dehydrogenation process:3 (1) reactor, (2) compressor, (3) temperature on the dehydrogenation of different light paraffins.4 NITRATION OF PROPANE (Production

Page:  187 temperature on the dehydrogenation of light paraffins at one atmosphere.4 Nitropropane reacts with

Page:  191 to be the dehydrogenation of propane and butane to the corresponding olefins followed by the predominance of dehydrogenation and cracking. Methane and ethane are by-products from the

Page:  193 hydrogen (from dehydrogenation of propane) through the reverse water gas shift reaction. CO2

Page:  194 isomerization followed by dehydrogenation to isobutene. The Catofin process is currently used to dehydrogenate

Page:  211 activated copper-catalyzed dehydrogenation of ethanol. Currently, acetaldehyde is obtained from ethylene by using oxidation or the dehydrogenation of ethanol (approximately 500°C for the oxidation and C for the dehydrogenation). Ethylene oxidation is carried out through oxidation-reduction (redox).

Page:  219 are produced by dehydrogenation of nparaffins, dehydrochlorination of monochloroparaffins, or by oligomerization of ethylene complexes catalyze the dehydrogenation of n-paraffins to α-olefins. The reaction uses a

Page:  242 isopropanol by a dehydrogenation, oxidation, or a combined oxidation dehydrogenation route. The dehydrogenation reaction a combined oxidation dehydrogenation route. The dehydrogenation reaction is carried out using either copper dehydrogenation route. The dehydrogenation reaction is carried out using either copper or zinc oxide

Page:  243 used for the dehydrogenation reaction. Acetone can also be coproduced with allyl alcohol in produced from the dehydrogenation of isopropanol and adsorbed on the catalyst surface selectively hydrogenates

Page:  255 by the catalyzed dehydrogenation of sec-butanol over zinc oxide or brass at about

Page:  258 produce MEK by dehydrogenation, as mentioned earlier. 2-Butanol is also used as a

Page:  269 remainder comes from dehydrogenation of n-butane or n-butene streams (Chapter 3).

Page:  279

11 billion pounds. Dehydrogenation of ethylbenzene to styrene occurs over a wide variety of used for the dehydrogenation reaction. Typical reaction

Page:  280 followed by catalytic dehydrogenation to styrene:8 Figure 10-3. Schematic diagram of the

Page:  283 α-methylstyrene by dehydrogenation. α-Methylstyrene is used as a monomer for polymer manufacture

Page:  288 corresponding n-paraffins. Dehydrogenation of nparaffins to monoolefins using a newly developed dehydrogenation catalyst a newly developed dehydrogenation catalyst by UOP has been reviewed by Vora et al. monoolefins. Because the dehydrogenation product contains a higher concentration of olefins for a given 9) combines the dehydrogenation of n-paraffins and the alkylation of benzene.17 Monoolefins Monoolefins from the dehydrogenation section are introduced to a fixed-bed alkylation reactor over

Page:  289 (1) pacol dehydrogenation reactor, (2) gas-liquid separation, (3) reactor for

Page:  295 to benzene. The dehydrogenation of cyclohexane Figure 10-12. Effect of hydrogen purity and

Page:  297 over a hydrogenation-dehydrogenation catalyst such as nickel. The hydrodealkylation is essentially a hydrocracking

Page:  393 from, 259 from dehydrogenation of C4, 103–104 polymerization with Li compounds, 308 polymers 62–65 Catofin dehydrogenation process, 173 Cellulose, 301 Chain addition polymerization, 304–308 Charactenzation

Page:  394 from, 315 Cycloparaffins dehydrogenation of, 63 in crude oils, 13 DDT, 278 DEA ( to butadiene, 104 Dehydrogenation of ter-amylenes, 105 butanes and butenes, 103 cycloparaffins, 63

Page:  398

process for C4 dehydrogenation, 103 Malathion, 243 Maleic anhydride 1,4-butanediol from, 242–243

Page:  400 scheme, 297 Lummus dehydrogenation process for butadiene, 103 Physical absorption, 3 Physical adsorption, 3,

Page:  401 173 cracking, 97 dehydrogenation, 172 Lummus-Crest process, 173 temperature effect on, 172 heating

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: Fluid_Catalytic_Cracking_Handbook_2E.pdf : 92155.pdf : : :

Page:  77 reactions, such as dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation means polymerization,

Page:  78 matrix. Nickel promotes dehydrogenation reactions, removing hydrogen from stable compounds and making unstable olefins,

Page:  79 activity to promote dehydrogenation reactions, A small amount of nickel in the FCC feed to increase the dehydrogenation reactions. Chlorides in the feed reactivate aged nickel, resulting in an indicator of dehydrogenation reactions. However, the ratio is sensitive to the reactor temperature

Page:  80 Vanadium also promotes dehydrogenation reactions, but less than nickel. Vanadium"s contribution to hydrogen yield

Page:  119 indicative of the dehydrogenation activity of the metals on the catalyst. The addition of

Page:  123 catalyst. They cause dehydrogenation reactions, which increase hydrogen production and decrease gasoline yields. Vanadium

Page:  137 with nickel, the dehydrogenation reactions that are

Page:  141 7. 8. Naphthenes Dehydrogenation Dealkylation Condensation C7H14 - n-C8H18 lso-C3H Ar-C3H

Page:  150

prominent reactions are dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a "clean" feedstock molecular hydrogen. Therefore, dehydrogenation reactions will proceed only if the catalyst is contaminated with

Page:  152 Transalkylation Cyclization Dealkylation Dehydrogenation Polymerization Alkylation Specific Reaction n-C10H22 -> n-C7H16 +

Page:  340 catalyst, promoting undesirable dehydrogenation and condensation reactions. These nonselective reactions increase gas and coke

Page:  381 Nickel, 63, 108 dehydrogenation, 135 and hydrogen, 64 passivation, 122 Nitrogen basic, 54 effects,

Page:  382 3§7 dehydrogenation, 135 hydrogen transfer, 134 isomerization, 133 thermal cracking, 126, 283

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: Chemical Process- Design and Integration.pdf : : 0470011912.pdf : :

Page:  58 produced by the dehydrogenation of an aqueous solution of isopropanol according to the reaction:

Page:  101 produced by the dehydrogenation of 2- propanol. In this process, the product from the

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: Coulson & Richardson"s Chemical Engineering. Vol. 6, Chemical Engineering Design, 4th Ed.pdf Title : Subject : Author : Keywords :

Page:  193 it undergoes catalytic dehydrogenation to acetone. The reactor exit gases (acetone, water, hydrogen

Page:  209 manufactured by the dehydrogenation of 2-butanol. A simplified description of the processes listing

Page:  325 manufactured by the dehydrogenation of 2-butanol using a shell and tube type reactor.

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: Biochemistry The Chemical Reactions of Living Cells 2e Vols .pdf : : : :

Page:  500 Oxidoreductases. Enzymes catalyzing dehydrogenation or other oxidation and reduction reactions. E. Classification of Enzymes

Page:  514 there are two dehydrogenation steps. The first (step b) removes hydrogen atoms from than does the dehydrogenation of an alcohol, for which NAD+ is adequate. Addition of

Page:  515 acids, like the dehydrogenation of pyruvate to acetyl-CoA, takes place within the inner

Page:  519 in the four dehydrogenation steps are indicated. Their reduced forms are reoxidized by the

Page:  708 concerted decarboxylation and dehydrogenation may sometimes occur,241–242 the enzymes of this group

Page:  767 15-2 Some Dehydrogenation Reactions Catalyzed by Flavoproteins Table 15-3 SingleCarbon Compounds keto reductases 3. Dehydrogenation of Amino Acids and Amines 4. Glyceraldehyde-3Phosphate Dehydrogenase Potentials 2. Typical Dehydrogenation Reactions Catalyzed by Flavoproteins 3. More Flavoproteins 4. Modified Flavin

Page:  768 Reactions 15 The dehydrogenation of an alcohol to a ketone or aldehyde (Eq. becomes reduced by dehydrogenation of an alcohol, one of the hydrogen atoms removed from that these biological dehydrogenations may be viewed as removal of a hydride ion (

Page:  769 oxidant) BC Dehydrogenation of an alcohol Alcohol dehydrogenase (NAD+) HC OH H–

C O H+ Dehydrogenation of an amine Amino acid dehydrogenases, amine oxidases (NAD+ NH4C O Dehydrogenation of adduct of thiol and aldehyde Glyceraldehyde 3-phosphate dehydrogenase + H D Dehydrogenation of acyl-CoA, acyl-ACP, or carboxylic acid Reduction of

Page:  778 775 3. Dehydrogenation of Amino Acids and Amines The dehydrogenation of an amine and Amines The dehydrogenation of an amine or the reverse reaction, the reduction of 8, step a). Dehydrogenation of such a hydrate yields an acid (Eq. 15cleavage to the dehydrogenation, it drives the [NADPH] / [NADP+] ratio to

Page:  780 carry out the dehydrogenation of an acyl-CoA (reaction type D of Table

Page:  781 oxo group by dehydrogenation is essential. Bound NAD+ is also present in Sadenosylhomocysteine

Page:  784 variety of other dehydrogenations. (2) Flavins can be reduced either by one- or

Page:  785 acceptor. 2. Typical Dehydrogenation Reactions Catalyzed by Flavoproteins The functions of flavoprotein enzymes are

Page:  786 sequence to link dehydrogenation of glucose to the iron-containing catalyst that interacted with

Page:  787 15-2, the dehydrogenation of an acyl-coenzyme A (CoA), could not be reduced pyridine nucleotide.) Dehydrogenation reactions of this type are important in the energy metabolism the α,β dehydrogenation of fatty acyl-CoA derivatives. The pro-R hydrogen atoms 15-2 Some Dehydrogenation Reactions Catalyzed by Flavoproteinsa AB B. –2[H]

Page:  788 acid cycle is dehydrogenation of succinate to fumarate by succinate dehydrogenase (Eq. 1521).177a The dehydrogenation also involves trans removal of one of the two hydrogens,

Page:  793 for this reason dehydrogenation may often take place by proton transfer mechanisms.

Experimental support

Page:  794 mechanism of flavin dehydrogenation consists of consecutive transfer of a hydrogen atom and of

Page:  802 by a simple dehydrogenation. However, the pyruvate dissociates slowly and in the presence of

Page:  847 by decarboxylation and dehydrogenation of two of the carboxyethyl side chains of uroporphyrin III

Page:  888 chemical reactions of dehydrogenation, hydroxylation, or oxygenation. Galactose oxidase (Fig. 16-29), from

Page:  889 hydroxylation followed by dehydrogenation (Eq. 16-57). First identified in mushrooms, the enzyme

Page:  896 passes electrons from dehydrogenation of formate to FAD and then to the deazaflavin coenzyme

Page:  908 288 Acyl-ACP, dehydrogenation of 766 Acyl adenylate 507 Acyl carrier protein (ACP)

Page:  909 to carbonyl 677 dehydrogenation of 765 – 767 Alcohol dehydrogenase(s) 766 isoenzymes 774 covalent hydrates 775 dehydrogenation of 766 oxidation of 775 Aldehyde dehydrogenases 776 Aldehyde oxidases to carbonyl 677 dehydrogenation of 766 Amine oxidases 766, 782 Amino acid(s) 51– 57 configurations 42 dehydrogenation of 775 as dipolar ions 42, 51 essential 52, 53

Page:  913 activation of 507 dehydrogenation of 766 Carboxylic acid reductase 893 Carboxyltransferase 724 of propionic

Page:  916 768 – 775 Dehydrogenation of alcohols 765 – 767 of amines 775 of amino

Page:  919

s) 513, 788 dehydrogenation reactions 782 – 787 table 784 reduction potentials of 782

Page:  922 equation 308 for dehydrogenation reactions 771 for multisubstituted compounds 309 table of constants 308

Page:  938 group 677 adduct, dehydrogenation of 766 binding of mercury ions 125 Thiol – disulfide

Page:  942 CoA molecule is dehydrogenation. Removal of the α hydrogen as a proton is made

Page:  944 that catalyze the dehydrogenation of acyl-CoA molecules to unsaturated enoyl-CoAs (step is a normal dehydrogenation to a 2-trans-5-cis-dienoyl-CoA. In pathway

Page:  945 rapidly, perhaps by dehydrogenation to the oxo acids (Eq. 17-3, step b)

Page:  946 new type of dehydrogenation with concurrent decarboxylation. Alpha oxidation also occurs to some extent

Page:  953 that gained from dehydrogenation and use of an electron transport chain.78 The solution

Page:  965 understood chemically. The dehydrogenation of glyceraldehyde 3-P and the accompanying ATP formation (

Page:  966 (i) a dehydrogenation–decarboxylation system, (ii) an isomerizing system, and (iii) rearrangement system. The dehydrogenation–decarboxylation system cleaves glucose 6-P to CO2 and the opening. A second dehydrogenation is catalyzed by 6-phosphogluconate dehydrogenase (Eq. 17-12,

Page:  967 product. Since the dehydrogenation system works only on glucose 6-P, a part of

Page:  983 liver cells, the dehydrogenations catalyzed by lactate dehydrogenase, sn-glycerol 3phosphate dehydrogenase, and

that several other dehydrogenation reactions are nearly at equilibrium. This conclusion has been confirmed

Page:  988 51).198 Further dehydrogenation to formate and of formate to CO2 via formate dehydrogenase

Page:  994 cycle), (3) dehydrogenation, and (4) β decarboxylation. In many cases steps 3

Page:  1014 a thioester by dehydrogenation b. Substrate-level phosphorylation c. Thiamin-dependent α condensation d.

Page:  1025 are oxidized by dehydrogenation is usually attributed to H. Wieland. During the years 1912–

Page:  1052 glycolysis and other dehydrogenations in the cytoplasm quickly reduce available NAD+ to NADH. For

Page:  1060 the idea of dehydrogenation dominated thinking about biological oxidation. Many scientists assumed that the bond followed by dehydrogenation of the resulting alcohol. Nevertheless, it was observed that small

Page:  1062 usually followed by dehydrogenation or oxidative decarboxylation by NAD+ to give a catechol, whose

Page:  1068 aromatic amines and dehydrogenation of the resulting catechols or o-aminophenols (Eq. 16-

Page:  1089 by O2. c) Dehydrogenation of ascorbate by O2. How would the ratio of ATP

Page:  1137 step process involving dehydrogenation and enolization (steps c and d), is converted to 24 However, the dehydrogenation step is lacking in human beings and other primates, in

Page:  1141 carbonyl group by dehydrogenation with tightly bound NAD+ (Eq. 20-10, step a)

Page:  1198 apparently occurs by dehydrogenation of – CH = CH –. Examples of naturally occurring

Page:  1248 enzyme catalyzes the dehydrogenation of the 3-OH group to a ketone allowing for

Page:  1255 a. Hydroxylation b. Dehydrogenation c. Isomerization f. Hydroxylation g. Hydroxylation and oxidation to acyl-

Page:  1256 O2-dependent steps. Dehydrogenation of the 3-OH group of pregnenolone to C =

Page:  1320 The four-electron dehydrogenation of two water Figure 23-35 Proposed sequence of Sstates

Page:  1327 P2NADP+ 2NADPH Dehydrogenation– decarboxylationsteps of oxidative pentose phosphate pathway (Eq. 17-12)

Page:  1382 to γ-guanidinobutyraldehyde. Dehydrogenation and hydrolysis lead, again, to γaminobutyrate.189 Specific arginine

Page:  1394 most organisms is dehydrogenation (Eq. 24-37, step c)336 to form 2-

Page:  1396 by NAD+-dependent dehydrogenation,357 to the corresponding 2-oxoacid and oxidative decarboxylation of

Page:  1398 after the initial dehydrogenation in the β-oxidation sequence, carbon dioxide is added using

Page:  1400 20) that involves dehydrogenation, transamination, and hydrolysis by a phosphatase. It can also be

Page:  1404 IX Decarboxylation and dehydrogenation H H NH3 e f g d h + Porphobilinogen

Page:  1440

Fig. 13-5) dehydrogenation, and side-chain cleavage as shown in Eq. 25-8

Page:  1452 Ring to histidinol. Dehydrogenation of this alcohol Regulation of histidine synthesis. In all, ten

Page:  1921 1655s Acyl-ACP, dehydrogenation of 766 Acyl adenylate 507 of tRNA 1672, 1695, 1696

Page:  1922 to carbonyl 677 dehydrogenation of 765 – 774 Alcohol dehydrogenase(s) 479, 766 – covalent hydrates 775 dehydrogenation of 766 oxidation of 775 Aldehyde dehydrogenases 776 Aldehyde oxidases to carbonyl 677 dehydrogenation of 766 Amine oxidases 766, 782 Amino acid(s) 51– C-terminal 57 dehydrogenation of 775 as dipolar ions 42, 51 essential 52, 53,

Page:  1928 activation of 507 dehydrogenation of 766 Carboxylic acid reductase 893 Carboxyltransferase 724, 971 of

Page:  1933 1026 – 1028 Dehydrogenation 1022 of alcohols 765 – 767 of amines 775 of of, table 766 Dehydrogenation- decarboxylation system of pentose phosphate pathway 963 3-Dehydroquinate 1423s,

Page:  1939 s) 513, 788 dehydrogenation reactions 782 – 787 table 784 reduction potentials of 782

Page:  1943 equation 308 for dehydrogenation reactions 771 for multisubstituted compounds 309 table of constants 308

Page:  1971 group 677 adduct, dehydrogenation of 766 binding of mercury ions 125 Thiol–disulfide equilibria

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Page:  93 include isomerization, hydrogenation, dehydrogenation, and dehydrocyclization. Fundamental catalysis Work that develops the basic principles

Page:  94 KCl/Al2O3 Paraffin dehydrogenation Pt/Al2O3 (S-poisoned) Phthalic anhydride V2O5 Steam reforming

Page:  96 Butadiene by Humble dehydrogenation 1964 Molex paraffin UOP separation 1970 Methanol —low ICI pressure

Page:  97 it has a hydrogenationdehydrogenation component to promote arene and cyclization reactions. 3. Alkylation. Reactions

Page:  101 synthesis, hydrogenation, and dehydrogenation. A. Scale-Up and Development Catalyst scale-up is a

Page:  104 catalyst. Oxidation, hydrogenation– dehydrogenation, isomerization, alkylation, and hydrotreating are carried out in such reactors.

Page:  362 e.g., propane dehydrogenation, natural gas steam reforming, these membrane reactors show good transport

Page:  395 Limitations Membrane concept Dehydrogenation Ethyl benzene to styrene 500−600◦C; FeCr-

Page:  409 (1968). “Dehydrogenation of cyclohexane on a hydrogenporous membrane,” J. Catal. 11(1),

Page:  496

produced by catalytic dehydrogenation of butylene and the liquid butadiene is then extracted with

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Page:  811 the product of dehydrogenation of the natural product guaiol with elemental sulfur. From the

Page:  1095 RNH2 PThis dehydrogenation is the reverse of palladium-catalysed hydrogenation. NH2 HN R

Page:  1289 of FAD involve dehydrogenations—as in double bond formation from single bonds. Of course,

Page:  1312 a sulfur-promoted dehydrogenation has been suggested for the removal of the hydrogen atoms.

Page:  1377 shikimate pathway 1402 dehydrogenation of guaiol with sulfur 830 of heterocycles 1175, 1212 with

Page:  1381 NMR 830 guaiol, dehydrogenation of 830 guanidine, basicity of 202, 587 guanidine, reaction with

Page:  1386 as catalyst for dehydrogenation 1175 as catalyst for hydrogenation 623–7, 1164, 1198 tetrakistriphenylphosphine

Page:  1390 of) 1251 in dehydrogenation of guaiol by 830 oxidation states of 1248–9 stabilisation

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Page:  137 Prostaglandin synthetase cooxidation Dehydrogenation Acetaminophen, benzidine, epinephrine N-Dealkylation Benzphetamine, dimethylaniline Epoxidation/hydroxylation Benzo(

Page:  571 Dehalogenation, 112, 465 Dehydrogenation, 112 Delaney Amendment—see Food, Drug and Cosmetics Act Demeton,

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Page:  38 hypothesized that the dehydrogenation and polymerization of hydrocarbon fuels occurs in the liquid phase, particles agglomerate after dehydrogenation and polymerization are completed. Gray et al. (1976) noted

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Page:  28 will involve the dehydrogenation of ethane over a suitable catalyst (yet to be

Page:  31 produced by the dehydrogenation of butene over an appropriate catalyst. C4H8 H2 C4H6 In

Page:  80 a gas phase dehydrogenation reaction that occurs at a constant temperature of 1000 °

Page:  171 the catalytic oxidative dehydrogenation of various butene isomers to form 1,3-butadiene. Over a

Page:  176 6. Polymerization 7. Dehydrogenation Reactants N2 + H2 NH3 + O2 SO2 + O2

Page:  212 then act as dehydrogenation catalysts. The product distribution is markedly affected with lower yields

Page:  236 reduction, polymerization, dehydration, dehydrogenation, etc. Their versatility is a reflection of the range and

Page:  536 studied the catalytic dehydrogenation of cyclohexane to benzene over a platinum-onalumina catalyst.

Page:  537 have studied the dehydrogenation of cyclohexane to benzene over a platinum on alumina pelleted

Page:  547 judgment. 17. Oxidative Dehydrogenation of Butene to Butadiene UW Chemical Corporation Madison, Wisconsin To:

for the butene dehydrogenation reaction is effectively removed since hydrogen is converted to water for the endothermic dehydrogenation reaction. For preliminary discussions of the proposed expansion program, it to other oxidative dehydrogenation catalysts. Select a promising catalyst material and prepare a reactor

Page:  594 158-160 Butene, dehydrogenation, 22, 538-539 isomerization, 20 d-s-Butyl a-chloroacrylate

Page:  595 164-165 Cyclohexane, dehydrogenation, 527-529 Cyclohexanol, reaction with acetic acid, 69 Cyclohexene, from of tetrachloroethane, 307 Dehydrogenation, butene, 22, 162 cyclohexane, 527-529 ethane, 19-21 ethylbenzene,

Page:  596 equation, 493 Ethane, dehydrogenation, 19, 21 Ethanol, via hydration of ethylene, 12-14 reaction

Page:  599 536-537 Oxidative dehydrogenation of butene, 538-539 Ozone decomposition, 97-98, 123124

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Page:  226 proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page:  271 development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

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Page:  226 proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page:  271 development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

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Page:  14 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  15 catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page:  16 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page:  17 for hydrodealkylation and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

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Page:  6 operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

Page:  11 from ethanol 18. Dehydrogenation of isopropanol 19. Isomerization of n-butane 20. Postchlorination

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Page:  581 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  582 catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page:  583 used. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page:  584 for hydrodealkylation and dehydrogenation reactions G-58 Palladium-on-alumina catalyst, for selective hydrogenation

Page:  591 operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

Page:  596 from ethanol 18. Dehydrogenation of isopropanol 19. lsomerization of n-butane 20. Postchlorination

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Page:  568 formed by the dehydrogenation of ethyl benzene are shown. It may be seen that,

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Page:  260 by the catalytic dehydrogenation of ethylbenzene according to the reaction: C6H5 · CH2 ·

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Page:  189 it undergoes catalytic dehydrogenation to acetone. The reactor exit gases (acetone, water, hydrogen

Page:  208 manufactured by the dehydrogenation of 2-butanol. A simplified description of the processes listing

Page:  325 manufactured by the dehydrogenation of 2-butanol using a shell and tube type reactor.

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Page:  724 for hydrogenation and dehydrogenation reactions. It is alloyed and used in jewelry trades. White

Page:  729 the dehydration and dehydrogenation of ethyl alcohol. It is used in infrared absorbing glass

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Page:  12 I-Bu~ene Dehydrogenation into Butudiene, 571 11.10 Two-Dimensional Heterogeneous &lodeis 12

Page:  116 calcium-nickel phosphate dehydrogenation synthesis) Hydrogenation of aromatics and aromatization Platinum-acid alumina and

Page:  118 with hydrogenations and dehydrogenations. (Note that, except for noble metals, they would not

Page:  119 + H2 (dehydrogenation) catalyst With hydrocarbons, the two types of catalysts cause cracking versus hydrogenation or dehydrogenations. An interesting and very practical example of these phenomena concerns

Page:  120 the metal site dehydrogenation step could not readily move to the acid sites for

Page:  133 reaction rate form. Dehydrogenation reactions are of the form and a specific example will

Page:  141 sequence consisting of dehydrogenation, isomerization, and hydrogenation. The dehydrogenation and hydrogenation steps occur on and hydrogenation. The dehydrogenation and hydrogenation steps occur on platinum sites, represented by I; the overall reaction: Dehydrogenation A + [ - A1 K I = CA JP, steps of the dehydrogenation or hydrogenation reactions is considered to be rate determining, the

Page:  142 the treatment of dehydrogenation reactions given above. Since these pressure dependent

rate equations are K,is theequilibriumconstant fordehydrogenation,and K, = K,K9KroK,, is the equilibrium constant for

Page:  147 They studied the dehydrogenation of ethanol into acetaldehyde in an integral type flow reactor

Page:  149 b-2 Ethanol dehydrogenation. Conversion versus space time at various temperatures. (W/F,,)(

Page:  150 b-3 Ethanol dehydrogenation. Initial rate versus total pressure at various temperatures. PA, ( b-4 Ethanol dehydrogenation. Rearranged initial rate data.

Page:  152 b-6 Ethanol dehydrogenation. Arrhenius plot for rate coeficient and adsorption constants. From the

Page:  158 discrimination in the dehydrogenation of I-butene into butadiene Dumez and Froment studied the Froment studied the dehydrogenation of 1-butene into butadiene on a chromium-aluminium oxide (a) Atomic Dehydrogenation ; Sugace Recombination of Hydrogen where B = n-butene; (b) Atomic Dehydrogenation; Gas Phase Hydrogen Recombination KINETICS OF HETEROGENEOUS CATALYTIC REACTIONS

Page:  159 (c) Molecular Dehydrogenation (d) Atomic Dehydrogenation; Intermediate Complex with Short Lqetime; Surface (d) Atomic Dehydrogenation; Intermediate Complex with Short Lqetime; Surface Recombination of Hydrogen (

Page:  160 discrimination in butene dehydrogenation. Operability region, equi/ibrium surface, location of preliminary and designed

Page:  161 Table 1 Dehydrogenation of I-butene. Evolution of sequential model discrimination Number of

Page:  162

l-2 Ethanol Dehydrogenation. Sequential Discrimination Using the Integral Method of Kinetic Analysis The Froment on ethanol dehydrogenation 1401 three rate equations were retained. They were already referred

Page:  163 qure I Ethanol dehydrogenation. Operability region, location of preliminary and ojdesigned experimentsfor optimal discrimination.

Page:  164 discrimination in the dehydrogenation of ethanol into acetaldehyde, using integral reactor duta as such

Page:  170 study of the dehydrogenation over a brass catalyst of sec-butyl alcohol to methyl

Page:  171 l for the dehydrogenation of methylcyclohexane to toluene. In addition, they found that the

Page:  172 step of the dehydrogenation reaction were rate controlling. Contrast this with the corre rate

Page:  173 steps. 2.12 The dehydrogenation of ethanol was carried out in an integral reactor at

Page:  188 Gradients in Ethanol Dehydrogenation Experiments The dehydrogenation of ethanol into acetaldehyde C,H,OH Dehydrogenation Experiments The dehydrogenation of ethanol into acetaldehyde C,H,OH = CH,CHO

Page:  254 Selectivity in Butene Dehydrogenation An experimental investigation of this industrially significant process was reported

Page:  321 of naphtha, and dehydrogenation of ethyl- 284 CHEMICAL ENGINEERING KINETICS

Page:  326 19] in butene dehydrogenation. If the coke precursor would be formed from a reaction

Page:  331 Coking in the Dehydrogenation of I-Butene into Butadiene on a Chromia-Alumina Catalyst

In the catalytic dehydrogenation of 1-butene into butadiene, which will be described in

Page:  332 Figure I Butene dehydrogenation. Partial pressure and coke profiles inside a cata[yst particle.

Page:  333 study of butene dehydrogenation Dumez and Froment [19] were able to take samples 30] in the dehydrogenation of isobutene for which they derived a hyperbolic deactivation function

Page:  334 53.e-I Dehydrogenation of I-Bufene into Butadiene Dumez and Froment [I93 I93 studied the dehydrogenation of 1-butene into butadiene in the temperature range 480 derived from various dehydrogenation schemes and ratedetermining steps. The discrimination between these models was corresponding to molecular dehydrogenation and surface reaction on dual sites as a ratedetermining step,

Page:  335 Figure I Butene dehydrogenation. Coke content of catalyst as a function of time.in

Page:  337 function for the dehydrogenation was also determined by means of the microbalance, by measuring

Page:  338 Figure 2 Butene dehydrogenation. Deactication fwrction for the main reaction, mH. versus rime. Problems

Page:  502 or with ethylbenzene dehydrogenation into styrene. Strongly exothermic reactions lead to a temperature rise

Page:  557 study of the dehydrogenation of butene into butadiene, Dumez Bnd Froment [I411 observed

Page:  558 1393. In butene dehydrogenation into butadiene on a chromium-aluminium-oxide catalyst at 59S°

Page:  608 for I-Butene Dehydrogenation into Butadiene This is an example, taken from Dumez and

The 1-butene dehydrogenation process considered here is carried out at temperatures of about

Page:  610 owing to the dehydrogenation and to a certain extent to the coking. The right-

Page:  612 the 1-butene dehydrogenation reactor. The molecular diffusivities were calculated from a weighted average

Page:  613 in I-butene dehydrogenation reactor. 576 CHEMICAL REACTOR DESIGN

Page:  614 but as the dehydrogenation rate is lowered the bed temperature slowly rises, thus favoring

Page:  619 produced by catalytic dehydrogenation of ethylbenzene. The reaction is endothermic and reversible and takes

Page:  795 of, 37 Butene dehydrogenation, coking in, 294, 297 effect of particle size in, 217

Page:  796 of polymerization, 40 Dehydrogenation, of 1-butene, see Butene dehydrogenation of ethanol, see Ethanol butene, see Butene dehydrogenation of ethanol, see Ethanol dehydrogenation Design, see Reactor design Differential ethanol, see Ethanol dehydrogenation Design, see Reactor design Differential method of kinetic analysis, with

Page:  797 simulation, 410 Ethanol dehydrogenation, calculations for, 151 model discrimination for, 125 Ethylene oxidation, catalytic,

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Page:  513 21.12. In catalytic dehydrogenation of hydrocarbons the catalyst activity decays with use because of

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Page:  120 for the catalytic dehydrogenation of ethylbenzene to form styrene: C8H10 !C8H8

Page:  144 favorable equilibrium. Ethylbenzene dehydrogenation fits this situation. Repeat Problem 3.7 but substitute an annular

Page:  263 HR for the dehydrogenation of ethylbenzene to styrene at 298.15K and 1 bar. Solution:

Page:  264 for the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. Solution: From Example 7.8,

Page:  265 R for the dehydrogenation of ethylbenzene to styrene at 298.15 K. Solution: Table 7.2

Page:  272 of the ethylbenzene dehydrogenation reaction at 298.15K and 0.5 atm. Consider two cases: 1.

Page:  273 from the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. The starting composition is amount of a dehydrogenation catalyst. The reaction rate has the form kf A

Page:  274 trajectory for ethylbenzene dehydrogenation.

Page:  394 process for the dehydrogenation of ethylbenzene uses 3-mm spherical catalyst particles. The rate

Page:  407 10.5. The ethylbenzene dehydrogenation catalyst of Example 3.1 has a firstorder rate

constant of

Page:  410 C., ‘‘Catalytic dehydrogenation of ethylbenzene,’’ Chem. Eng. Prog., 44, 275–286 (1948).

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Page:  120 for the catalytic dehydrogenation of ethylbenzene to form styrene: C8H10 !C8H8

Page:  144 favorable equilibrium. Ethylbenzene dehydrogenation fits this situation. Repeat Problem 3.7 but substitute an annular

Page:  263 HR for the dehydrogenation of ethylbenzene to styrene at 298.15K and 1 bar. Solution:

Page:  264 for the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. Solution: From Example 7.8,

Page:  265 R for the dehydrogenation of ethylbenzene to styrene at 298.15 K. Solution: Table 7.2

Page:  272 of the ethylbenzene dehydrogenation reaction at 298.15K and 0.5 atm. Consider two cases: 1.

Page:  273 from the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. The starting composition is amount of a dehydrogenation catalyst. The reaction rate has the form kf A

Page:  274 trajectory for ethylbenzene dehydrogenation.

Page:  394 process for the dehydrogenation of ethylbenzene uses 3-mm spherical catalyst particles. The rate

Page:  407

10.5. The ethylbenzene dehydrogenation catalyst of Example 3.1 has a firstorder rate constant of

Page:  410 C., ‘‘Catalytic dehydrogenation of ethylbenzene,’’ Chem. Eng. Prog., 44, 275–286 (1948).

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Page:  416 is produced by dehydrogenation of ethylbenzene in an adiabatic, fixedbed reactor. Although Sheel and

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Page:  1220 of naphthenes through dehydrogenation and of paraffins through isomerization and dehydrocyclization. The reformer catalyst, reformers do. The dehydrogenation and dehydrocyclization reactions produce large amounts of hydrogen as a

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Page:  193 it undergoes catalytic dehydrogenation to acetone. The reactor exit gases (acetone, water, hydrogen

Page:  209 manufactured by the dehydrogenation of 2-butanol. A simplified description of the processes listing

Page:  325 manufactured by the dehydrogenation of 2-butanol using a shell and tube type reactor.

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Page:  614 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  616 They catalyze hydrogenation– dehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid, 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and

Page:  617 are the hydrogenation–dehydrogenation component of the catalyst and alumina is the acid component

Page:  618 for hydrodealkylation and dehydrogenation reactions G-58 Palladium-on-alumina catalyst, for selective hydrogenation

Page:  624 operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

Page:  630 from ethanol 18. Dehydrogenation of isopropanol 19. Isomerization of n-butane 20. Postchlorination

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Page:  470 aldehyde stage. 1) Dehydrogenation of an organic compound corresponds to oxidation, whereas hydrogenation corresponds

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Page:  543 inch stack) 0 Dehydrogenation unit X Hydrogen (31-inch stack) y Hydrogen (

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Page:  226 proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page:  271 development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

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Page:  33 is obtained by dehydrogenation of ethane. (a) Write out these reactions. (b)

Page:  69 much heat, while dehydrogenation reactions are fairly endothermic and oxidation reactions are fairly exothermic.

Page:  82 branched alkanes and dehydrogenation of cyclics to aromatics would enhance the octane enormously. In

Page:  85 These alkanes undergo dehydrogenation and cracking reactions. A higher-molecular-weight fraction of alkanes,

Page:  86 reaction is simple dehydrogenation, Cd6 -+ C2H4 + Hz In modern steam cracking processes

Page:  97 reactor stages, ethane dehydrogenation, ethylene oxidation, and ethylene oxide hydration. (a) What are (b) Both dehydrogenation and hydration have nearly 100% selectivity (with recycle of

Page:  99 all cracking and dehydrogenation reactions are strongly endothermic, while in the regenerator, strongly exothermic

Page:  101 is made by dehydrogenation of ethane. HCN is made by reacting CH4, NHs, and

Page:  124 l l C, dehydrogenation maleic anhydride l l FCC 400 - CH,OH l

Page:  216

by the oxidative dehydrogenation of ethane. Over a suitable catalyst the reactions and rates

Page:  220 The gas-phase dehydrogenation of ethane to ethylene C2H6 + CzH4 + H2 proceeds

Page:  260 causes the oxidative dehydrogenation of ethane to ethylene CzH6 + $2 -+ C2H4 causes the oxidative dehydrogenation of ethane to ethylene C2& + $2 -+ C2H4

Page:  281 causes the oxidative dehydrogenation of ethane to ethylene C2H6 + $2 + C2H4 causes the oxidative dehydrogenation of ethane to ethylene C2H6 + 502 + C2H4 +

Page:  501 concentrations. Hydrogenation and dehydrogenation reactor Another example of a gasphase membrane reactor is

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: Walas - Chemical Process Equipment.pdf : Chemical Process Equipment Selection and Design : : Stanley M. Walas : Referex

Page:  585 is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page:  586 catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids 4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page:  587 13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page:  588 for hydrodealkylatisn and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page:  595 operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

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: Wilson I.D, et al. (eds.) Encyclopedia of separation science (AP, 2000)(T)(4927s).pdf Title : Subject : Author : Keywords :

Page:  1678 equilibrium of the dehydrogenation reaction cyclohexane to cyclohexene. Conclusions The mechanism of water dissociation demonstrated that the dehydrogenation of cyclohexane to cyclohexene could be increased if the hydrogen to catalyse the dehydrogenation reaction. A membrane reactor of this type is illustrated in a myriad of dehydrogenation reactions. In the dehydrogenation reactions, hydrogen leaves the reactor by reactions. In the dehydrogenation reactions, hydrogen leaves the reactor by permeating through the semipermeable reactions (often dehydrogenations). The thermodynamic equilibrium of the reactants and products at the given reaction. For dehydrogenation reactions, increasing temperature and decreasing pressure promote an enhanced reaction.

Page:  1679 equilibrium of the dehydrogenation reaction cyclohexane to cyclohexene. Conclusions The mechanism of water dissociation demonstrated that the dehydrogenation of cyclohexane to cyclohexene could be increased if the hydrogen to catalyse the dehydrogenation reaction. A membrane reactor of this type is illustrated in a myriad of dehydrogenation reactions. In the dehydrogenation reactions, hydrogen leaves the reactor by reactions. In the dehydrogenation reactions, hydrogen leaves the reactor by permeating through the semipermeable reactions (often dehydrogenations). The thermodynamic equilibrium of the reactants and products at the given reaction. For dehydrogenation reactions, increasing temperature and decreasing pressure promote an enhanced reaction.

Page:  1680 addition of hydrogen Dehydrogenation CyclohexanePbenzene#3H2 Remove hydrogen to shift equilibrium limitation Partial oxidation highly active butane dehydrogenation catalyst operating at 1 atm total pressure (pure

normal removal on the dehydrogenation of butane. Based on pure butane feed with 1.1 atm illustrative purposes, the dehydrogenation of a compound to form hydrogen will be considered. The

Page:  1681 especially hydrogenation and dehydrogenation reactions. Thus, using this material to achieve both functions was gas in catalytic dehydrogenation membrane systems has been reported. At dehydrogenation temperatures (300} been reported. At dehydrogenation temperatures (300}6003C), oxygen can react with hydrogen to In contrast, the dehydrogenation reaction is endothermic. Thus, thermal matching of the heat released consumed by the dehydrogenation reaction would allow for an isothermal system. Because the hydrogenation

Page:  1684 membrane reactors, including dehydrogenation of hydrocarbons, hydrogenations and partial oxidation reactions are high temperature reactor for the dehydrogenation of butane, the system performance increased markedly. With no membrane,

Page:  1685 selectivity on a dehydrogenation reaction in a membrane-enclosed catalytic reactor. Journal of Membrane

Page:  1686 selectivity on a dehydrogenation reaction in a membrane-enclosed catalytic reactor. Journal of Membrane

Page:  1937 10.) on enzymatic dehydrogenation of D--hydroxybutyrate into acetoacetate and subsequent decarboxylation

Page:  2144 position, by enzymatic dehydrogenation and via formation of nicotinamide adenine dinucleotide (NADH), spectrometric

Page:  2257 cyclization, oxidation or dehydrogenation. The oxygenated derivatives are known as xanthophylls and bare either

Page:  2265 alkanes and the dehydrogenation of cyclohexanes to aromatics; and (2) steam reforming of

Page:  2270 achieve virtually complete dehydrogenation of cylcohexane to benzene at temperatures where the equilibrium constant

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: McGraw.Hill.Dictionary.Of.Engineering.eBook-LiB.pdf : : : :

Page:  94 hard, smooth butane dehydrogenation [CHEM ENG] A procrounded edge or surface; used for

Page:  163 } involving both dehydrogenation and cyclization, degradation [THERMO] The conversion of en- as

Page:  290 a Houdry butane dehydrogenation [CHEM ENG] refractory slurry. { ha¨ t

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: Nauman E.B. Chemical reactor design, optimization, and scaleup (MGH, 2002)(T)(618s).pdf Title : Subject : Author : Keywords :

Page:  120 for the catalytic dehydrogenation of ethylbenzene to form styrene: C8H10 !C8H8

Page:  144 favorable equilibrium. Ethylbenzene dehydrogenation fits this situation. Repeat Problem 3.7 but substitute an annular

Page:  263 HR for the dehydrogenation of ethylbenzene to styrene at 298.15K and 1 bar. Solution:

Page:  264 for the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. Solution: From Example 7.8,

Page:  265 R for the dehydrogenation of ethylbenzene to styrene at 298.15 K. Solution: Table 7.2

Page:  272 of the ethylbenzene dehydrogenation reaction at 298.15K and 0.5 atm. Consider two cases: 1.

Page:  273 from the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. The starting composition is amount of a dehydrogenation catalyst. The reaction rate has the form kf A

Page:  274 trajectory for ethylbenzene dehydrogenation.

Page:  394 process for the dehydrogenation of ethylbenzene uses 3-mm spherical catalyst particles. The rate

Page:  407

10.5. The ethylbenzene dehydrogenation catalyst of Example 3.1 has a firstorder rate constant of

Page:  410 C., ‘‘Catalytic dehydrogenation of ethylbenzene,’’ Chem. Eng. Prog., 44, 275–286 (1948).

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: Wypych G. (ed.) Handbook of solvents (ChemTec Pub., 2001)(1694s).pdf : : : :

Page:  100 major reactions occur: dehydrogenation of naphthenes to aromatics, dehydrocyclization of paraffins to aromatics, isomerization,

Page:  101 hydration, dehydration, hydrogenation, dehydrogenation, dimerization and esterification. For example methyl ethyl ketone is manufactured butanol then a dehydrogenation step converts it to methyl ethyl ketone. The production of

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: M26.pdf : Section 26 — Members : : :

Page:  11 Quorum & Associates DEHYDROGENATION SYSTEMS Aker Kvaerner, Inc. CB&I Howe-Baker Process &

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: O.Levenspiel - Chemical reaction engineering. 3rd edition.pdf : : : :

Page:  513 21.12. In catalytic dehydrogenation of hydrocarbons the catalyst activity decays with use because of

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: biodiversity in prod.pdf : DK3816_C000.fm : : Scott A. Suckling :

Page:  315 C4, followed by dehydrogenation and aromatization of the ring to yield p-hydroxybenzoate, which