Technical Information and Design Characteristic-mark III

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Pump Division

Technical Information and Design Characteristics Flowserve Durco Mark 3 Alloy Pumps • ASME (ANSI) B73.1 Standard • Sealmatic • Unitized Self-Priming • Recessed Impeller • Lo-Flo

Bulletin P-10-501b (E)

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Pump Division

Flowserve Durco Mark 3 ANSI Process Pumps

Flowserve Durco Mark 3 ANSI Process Pumps

Pumps delivered worldwide are manufactured in Flowserve facilities certified to ISO 9001.

Mark 3 Pump and Enhancements Mark 3 ASME (ANSI) B73.1 Standard Pump ............Page 4 Power Ends .............................5 Shafts & Sleeves .....................6 Shaft Materials & Data ............7 Shafts & Bearings....................8 Deflection Graphs ....................9 Isocorrosion Graphs..............10 SealSentry™ .....................11-14 DurcoShield™ ........................15 Impellers ..........................16-17 Lo-Flo™ .................................18 Casing Options ......................19 Ultralign™..............................20 Low/High Temperature ..........21 BaseLine™........................22-27

Heavy-duty chemical service pumps are preferred around the globe. Exclusive features improve pump reliability and extend mean time between planned maintenance (MTBPM).

Mark 3 Pump and Enhancements

Technical Data

Technical Data Performance Curves ..........................Page 28 Interchangeability ..................29 Pressure/Temperature Ratings................................30 Suction Pressure Ratings ......31 General Data ..........................32 Minimum Flow.......................33 Fastener Standards................33 Group 1 Parts ........................34 Group 2 & 3 Parts .................35 Pump/Baseplate Dimensions .........................36 Materials................................37 How To Specify......................38

Sealmatic Mark 3 Sealmatic ...............pages 39-43

Sealmatic 2

Quality System Certificate

Flowserve Durco pumps are among the industry leaders in hydraulic coverage and efficiency.

Dynamically sealed pump eliminates the need for conventional mechanical seals.

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Pump Division

Flowserve Durco Mark 3 ANSI Process Pumps Mark 3 Self-Priming...........Pages 44-48 Priming Tanks...................49-51

Located out of the sump. Reduces costs of vertical pump options and simplifies maintenance.

Mark 3 Recessed Impeller..................Pages 52-55

Vortex action assures trouble-free pumping of large diameter solids and slurries. Also selected for shear sensitive media.

Power Monitor ..................Pages 56-57

Protects pumps from costly damage due to improper operation at both high and low horsepower load points.

Good Pump Practice ..................Pages 58-59

Observing these seven principles of “Good Pump Practice” can significantly extend MTBPM.

Self-Priming

Recessed Impeller

Power Monitor

Good Pump Practice

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 ANSI Standard

Unique Features Extend MTBPM Improved pump reliability and extended MTBPM are achieved with exclusive features including: • Optional ANSI 3A™ power end (See page 5) • SealSentry™ seal chambers featuring the FML model with flow modifiers and large tapered bore (See page 11)

• The unique reverse vane impeller (See page 17) • Ultralign™ with C-Plus precision motor and pump shaft alignment (See page 20) • BaseLine family of pre-engineered baseplates (See page 22)

How To Identify Flowserve Durco Mark 3 Process Pumps An example of the nameplate used on the Mark 3 pump is shown below. This nameplate is always mounted on the Mark 3 bearing housing.

Pump Division

2 K 6 X 4 M – 1 3 A / 12.5 R V 2 indicates a medium size pump frame – in this example, a Group 2 1 = Group 1 (small frame) 2 = Group 2 (medium frame) 3 = Group 3 (large frame) K = Mark 3 style power end J = Mark 3 style PE arranged for Mark 2 wet end No letter and no preceding number indicates a Mark 2 power end Nominal suction port size Nominal discharge port size Modifier for “specialty pumps” blank or no letter = Standard pump M = Sealmatic L = Non-metallic wet end R = Recessed impeller H = High silicon iron US = Unitized self-priming S = Old style self-priming V = Vertical in-line T = PFA lined wet end LF = Lo-Flo E = Durcon wet end Nominal maximum impeller diameter 13 = 13 inch Pump design variation A= This pump has been redesigned from an earlier version. The impeller and casing are no longer interchangeable with the earlier version. H = This pump is designed for a higher flow capacity than another pump with the same basic designation. Examples: 4X3-10 and 4X3-10H; 6X4-10 and 6X4-10H; 10X8-16 and 10X8-16H. In each case the pump with the “H” is designed for a higher flow capacity. HH = This pump is designed for a higher head than another pump with the same basic designation. Example: 4X3-13 and 4X3-13HH Actual impeller size 12.5 = 121/2 in diameter; 8.13 = 81/8 in; 10.75 = 10 6/8 or 10 3/4 in Previous annotation: 124 = 124/8 or 121/2 in diameter; 83 = 8 3/8 in Impeller style RV = Reverse vane impeller; OP = Open impeller

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Serial No. Equipment No. Purchase Order Model Size MDP Material Date, DD/MMM/YY

2K6X4M-13A/12.5RV

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 ANSI Standard Power Ends

A Choice of Power Ends Standard Mark 3A power ends feature: • Double row angular contact outboard/single row, deep groove inboard bearings for excellent axial and radial load support • Double lip oil seals • Top mounted vent and oil filler • Trico oiler • Large 25 mm (1 in) diameter reflective sight glass • Micrometer adjustment (See page 8) • Optional oil slinger

ANSI 3A™ power end is so advanced it carries a three-year MTBPM bearing guarantee • Certified clean room assembly • Inpro/Seal’s VBXX noncontact Vapor Block Bearing Isolator keeps lubricants in and contaminants out • Magnetic drain plug collects metallic contaminants • Top vent replaced with plug

All Flowserve Durco Power Ends Feature: • Metal-to-metal construction to assure a true running and concentric shaft, thereby extending bearing and mechanical seal life • Ductile iron frame adapter meeting ASME B.73.1 criteria

Lubrication Options • Synthetic lubricants can allow up to three years between oil changes • Oil mist systems • Shielded and grease lubricated bearings (two-year MTBPM guarantee) Note: Adherence to proper installation, operation and maintenance program is necessary for three-year MTBPM bearing guarantee.

Optional Finned Oil Cooler

Optional Swing-Away Bearing Housing Foot

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 Shafts and Sleeves

Shaft Choices

Composite: a steel shaft end-to-end with an integral sleeve of DC8, SD77 high silicon iron, ceramic (alumina or zirconia)

Friction-Welded: a steel power end friction welded to a solid alloy wet end

Flowserve Durco shafts and sleeves are designed to improve pump reliability.

Solid: steel end-to-end or stainless alloy end-to-end

Shaft Material Choices Standard: investment cast or high alloy bar stock available in a wide range of materials, including proprietary DC8 and SD77 wet ends. DC8 and SD77 offer superior corrosion resistance and hardness to minimize shaft fret corrosion and maximize shaft wet end performance. • DC8 – a cobalt base alloy with chromium and molybdenum • SD77 – or Superchlor is a high silicon iron alloy Flowserve recommends the use of solid shafts rather than shaft sleeves to reduce the harmful effects of deflection and vibration. Shaft sleeves may simplify maintenance but solid shafts reduce it.

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Hook Sleeve: a steel shaft end-to-end or a steel power end friction-welded to a stainless wet end accommodating a hook sleeve

➀ ➁ ➂

Radiused “sled-runner” keyways improve strength at this stress point. Offset keyways aid shaft balance. Alloy identification on every shaft and sleeve ensures that the right parts go in every time.

➃ ➄



Large radii fillets add strength. Accurate machining under bearings ensures perfect bearing fits without vibration or hot running.



Steel power ends handle higher horsepower loads than stainless.





Run-out of < 0.03 mm (0.001 in) at mechanical seal allows seal faces to run true. Critical surfaces ground to a surface finish of 0.4 micron (16 µin) ensure the secondary sealing ability of mechanical seals.

Minimally radiused edges ensure full contact with impeller for reduced run-out.

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Pump Division

ANSI Pump and Enhancements Special Shaft and Sleeve Alloys There are three important considerations in the selection of a suitable shaft material for a pump application: • corrosion resistance • wear resistance, and • shock resistance – both thermal and mechanical. To meet these criteria, Flowserve developed DC8 specifically as a shaft sleeve material.

Exclusive DC8 Composite Shaft DC8 is an ideal sleeve material because of its optimum combination of strength (tensile strength equals 4136 bar [60,000 psi]), hardness (Brinell of 300), and corrosion resistance (superior to Alloy 20 in many cases).

Shaft is machined as an integral unit after DC8 alloy is permanently affixed. Single machining tolerance means better concentricity and lower runout.

Fully contained PTFE encased silicone O-ring protects shaft thread.

Flowserve Alloy Identification – Shafts* Shafts

Symbol

Alloy (power end/wet end)

Brinell Hardness

Composite

BBC8 BB77 BBC3 BBSZ

(1144 Steel/DC8) (1144 Steel/SD77 Hi Si Iron) (High purity ceramic [alumina]) (1144 Steel/Ceramic [zirconia])

300 520 – –

Friction Welded

ZH ZC20 EHB EHC C450

(Steel/316SS)* (steel/C20) (304SS/Hast B2)® (304SS/Hast C276)® (Steel/450 SS)**

160 130 230 220

Solid

BB 304 316 HB HC 4140 CK45 4462 2205

(1144 Steel)* (304 SS) (316 SS)* (Hast B2)® (Hast C276)® (4140 Steel)* Carbon Steel Duplex SS Duplex SS

200 155 160 230 220 260 240 250 250

*Also available in hook shaft **Group 1 T-Line only

Flowserve Alloy Identification – Sleeves* Symbol

Alloy

Brinell Hardness

DC2 DC3 DC8 M DNI 316 A20 TIW TIPW ZRW

Chlorimet 2 (Hast B2) Chlorimet 3 (Hast C276) Cobalt-based, proprietary Monel® Nickel 316 SS Durimet 20 Titanium Titanium, Palladium stabilized Zirconium

230 220 300 150 130 160 130 200 200 200

Shafts and sleeves are clearly marked with the material symbol.

*Other alloys available upon request

22.225 mm Ø (.8750 in) 22.212 mm Ø (.8745 in)

34.93 mm Ø (1.375 in) 34.88 mm Ø (1.373 in)

98.4 (3 7/ 8)

151.6 (5 31/ 32)

28.58 mm Ø under opt. sleeve (11/ 8 in)

Group 1 Shaft 91.3 (3 19/ 32)

47.62 mm Ø (1.875 in) 47.57 mm Ø (1.873 in)

*28.575 mm Ø (1.1250 in) 28.562 mm Ø (1.1245 in)

38 mm Ø under opt. sleeve (11/ 2 in)

Group 2 Shaft 125 (4 15/ 16)

175 (6 7/ 8)

195 (7 11/ 16)

*6 x 4-10 pump shaft coupling end 38.100 mm Ø (1.5000 in) 38.087 mm Ø (1.4995 in) 60.32 mm Ø (2.375 in) 60.30 mm Ø (2.374 in)

66.68 mm Ø (2.625 in) 66.62 mm Ø (2.623 in)

53.98 mm Ø under opt. sleeve (21/ 8 in)

Group 3 Shaft

® Hastelloy is a registered trademark of Haynes International, Inc. ® Monel is a registered trademark of International Nickel Co. Inc. 183 (7 3/ 16 )

267 (10 1/ 2 )

260 (10 1/ 4 )

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 Heavy-Duty Shafts and Bearings

Unique External Micrometer Impeller Adjustment It reduces maintenance time and, most importantly, is precisely accurate.

The Heart of the Pump: Shaft and Bearing Design Flowserve offers the largest shaft and bearing components available in standard ANSI pumps. The following comparison of a Flowserve Durco Group 2 power end with that of a major competitor demonstrates the benefits of heavy-duty design. Flowserve Durco bearings are designed to last up to 61% longer.

Table 1 Bearing Comparison Group 2 Flowserve

I.B. Bearing 6310

Dynamic Load Rating 6078 kg (13 400 lb)

O.B. Bearing 5310

Dynamic Load Rating 8709 kg (19 200 lb)

Major Competitor

6309

5398 kg (11 900 lb)

5309

7439 kg (16 400 lb)

Bearings (see Table 1) Greater load handling rating means extended MTBPM. Extended bearing life comparison is the ratio of the load ratings to the third power, or: 13 400 3 I.B.= 11 900 =1.43 (+43%) 19 200 3 O.B.= 16 400 =1.61 (+61%) 43-252% greater stiffness, indicated by lower index numbers, results in longer MTBPM.

Table 2 Deflection Comparison Group 2

Overhang Length

Flowserve 189 mm (7 11/16 in) Major Competitor 213 mm (8 3/8 in)

Solid Shaft Deflection Shaft Deflection Diameter Index w/sleeve Index 48 mm (17/8 in)

37

38 mm (11/2 in)

90

45 mm (13/4 in)

63

38 mm (11/2 in)

116

Shafts (see Table 2) Solid shafts are recommended over shaft sleeves because they reduce the harmful effects of deflection and vibration. While shaft sleeves may simplify maintenance, solid shafts reduce it. Proper selection of wet end materials of construction and mechanical seal design offset positive features of the shaft sleeve option.

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Simply loosen the set screws. Using a wrench rotate the bearing carrier counterclockwise until the impeller lightly touches the rear cover plate.

Select the impeller setting. Each notch on the carrier ring represents exactly 0.10 mm (0.004 in) of clearance. For an impeller setting of 0.5 mm (0.020 in) count five notches counterclockwise.

The formula I=L3/D4 offers an index of deflection to compare pump designs where: I = index of deflection L = length of shaft overhang from bearing D = rigid shaft diameter Note: The Deflection Index provides an approximate comparison of shaft stiffness. A detailed analysis should be made to determine actual shaft deflection.

Move the bearing carrier clockwise the selected number of notches. Tighten the setscrews and check the impeller clearance with the feeler gauge.

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Pump Division

ANSI Pump and Enhancements

The following shaft deflection curves are based on the maximum size reverse vane impeller pumping 1.0 specific gravity liquid. Shaft deflection varies directly with specific gravity and by the square of the pump speed. The graphs show that as flow is increased to BEP, the deflection decreases. The measurement given is deflection at the face of the seal chamber. Flowserve recommends the use of solid shafts rather than shaft sleeves to reduce the harmful effects of deflection and vibration. Shaft sleeves may simplify maintenance but solid shafts reduce it.

Group 1 & 2 3500 RPM

Group 1 & 2 1750 RPM

Group 3

SCALE CHANGE

Flowserve Durco Mark 3 Deflection Graphs

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Pump Division

ANSI Pump and Enhancements For Standard Shaft and Wet-End Materials Note: Various materials are acceptable in the areas under the curves as indicated.

PUMP SHAFT/SLEEVE ISOCORROSION CHART

HYDROCHLORIC ACID

220

200

ZONES FOR CORROSION RATES LESS THAN 10 MILS PER YEAR

82

600

71

500

60

140

49

120 SD77* 100

38

SD77 SD51

80

60 10

20

30

* IF NO OXIDIZING CONTAMINANTS

SULFURIC ACID

ZONES FOR CORROSION RATES LESS THAN 10 MILS PER YEAR

149

SD77 SD51

200

100

16

0

93 SD77 SD51 DC8 D20 10

20

30

40

% HCI

50

38

60

70

80

90

100

% H2SO4

PUMP SHAFT/SLEEVE ISOCORROSION CHART

NITRIC ACID

SODIUM HYDROXIDE

316

600

ZONES FOR CORROSION RATES LESS THAN 10 MILS PER YEAR

260

500 ZONES FOR CORROSION RATES LESS THAN 10 MILS PER YEAR BOILING CURVE 300

149

DC8 D20

93

200 DC8 D20 D4

100

SD51 SD77

DC8 D20 D4

38

TEMPERATURE °F

BOILING CURVE 204

400

TEMPERATURE °C

TEMPERATURE °F

204

300

PUMP SHAFT/SLEEVE ISOCORROSION CHART

121

250

200

SD51 SD77

D20 DC8 D4 D20 D4 DC8 SD51 SD77

150

100

93

66 D20 D4 SD51 SD77

38

10

50

0 10

20

30

40

50 % NaOH

10

260

BOILING CURVE

400

27

40

316

60

70

80

90

100

10

20

30

40

50 % HNO3

60

70

80

90

100

TEMPERATURE °C

TEMPERATURE °F

160

104

93

CERAMIC DC2* Zr*

180

PUMP SHAFT/SLEEVE ISOCORROSION CHART

116

TEMPERATURE °C

BOILING CURVE

TEMPERATURE °C

240

TEMPERATURE °F

Isocorrosion Graphs

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Pump Division

ANSI Pump and Enhancements

SealSentry FM Series Seal Chambers

Advanced FM SealSentry Design Technology • Self-Flushing • Self-Venting • Self-Draining Seal life is extended due to superior purging of heat, solids and vapors. Single seals can often be selected where dual seals or external flush and throat bushing combinations had been used, such as on solids, slurry and liquor services. Flush plans 11, 32, 52, 53, etc. can be eliminated. Costs are reduced. Pump reliability is increased.

The FM (Flow Modifiers) series features an enlarged, tapered bore with cast-in flow modifiers

Maximizing seal life involves proper selection of the seal chamber and seal and gland combination. Generally, the seal faces should be located directly in the flush path. For SealSentry video and proof of performance contact the local Flowserve sales office.

Flow Modifiers Extend Mechanical Seal MTBPM • Flow modifiers redirect flow from circumferential to axial • Balanced flow with low pressure drop in the chamber helps keep solids in suspension, minimizing erosive characteristics of the process • A mechanical seal creates a centrifuging action away from its parts and into the returning flow path of the process liquid • Solids and slurry merge in the returning flow path and are flushed out of the seal chamber

Winner of the Vaaler Award for Design Innovation

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Pump Division

ANSI Pump and Enhancements

SealSentry FM Series Seal Chamber

Flowserve Durco superior self-flushing seal chambers will: • Extend seal MTBPM • Improve pump reliability • Reduce costs

SealSentry FM – Opportunities

Results and Comments

The SealSentry FM provides improved internal seal chamber flush, with better solids handling, superior heat dissipation and vapor purging. These features extend mechanical seal life in both single, internal and the process side seal of dual seals.

On most applications, a bypass line such as ANSI Plan 11, which can be subject to failure, can be eliminated. Save on capital and power costs and improve system reliability while extending seal MTBPM.

For best performance, select seals and glands that locate the process side seal faces directly in the flush path.

However, a bypass flush is recommended when negative suction pressures or self-priming pumps are applied. Note: Single external seals are discouraged particularly if solids, slurry, or liquor may be present, regardless of flush mechanism.

Save on capital, power, and perhaps evaporation costs and improve On most applications the FM self-flush can eliminate the need for an external flush such as ANSI Plans 11 and 32. system reliability while extending seal MTBPM.

On most other applications, single seals without a bypass flush may be applied. Save on capital, avoid product contamination, and improve system reliability.

SealSentry FM improves internal process seal flush and allows consideration of single seals with potentially no other flush required.

On some applications, single seals with a quench may be preferred. Save on capital cost, reduce contamination, and improve system reliability while extending seal MTBPM.

Note: Abrasive services require careful consideration of the concentration and hardness of the abrasive. Pump and seal metallurgy, speed, and seal selection should be reviewed with the manufacturer.

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When a dual seal is required, such as toxic or environmental applications, seal life will be extended with SealSentry’s improved self-flush. Longer seal MTBPM means cost savings.

Dual seals are often specified on solids, slurry, and liquor services due to difficulties in properly flushing single seals. External flush on these dual seals adequately lubricates internal/external seal faces, but seal life can be reduced by process buildup and temperature rise on the internal side seal. This is caused by poor process circulation.

When extremely abrasive and high concentration slurries exist, dual seals that isolate the seal chamber may be preferred.

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Pump Division

ANSI Pump and Enhancements

SealSentry Types and Recommendations FML

Oversized, tapered bore with 8 specially shaped and evenly spaced cast-in flow modifiers. Designed for seals with large gland bolt and gasket circles.

• Single internal cartridge seals • Dual internal/external cartridge seals • Single internal component seals with flexibly mounted seats* • Dual internal “true” tandem cartridge seals Note: Bypass flush to internal seal normally not required. Barrier fluid or external flush may apply to dual seals (Plans 52, 53, etc.).

FMS

Same chamber design as FML but accommodates seals with small gland bolt and gasket circles.

Same seal and flush plan recommendations as for FML. Single seals with all types of seat mounting configurations can be installed. FMS design is provided for the convenience of customers with seal standards that include small glands. Secondary to the FML, Flowserve recommends the FMS.*

FMI

Same chamber design as FMS, but includes a cast-in integral gland.

• Single internal, flexibly mounted seals. Uses sleeve for seal setting and fast installation • “Sanitary-type” applications. Less prone to bacteria build up Note: Bypass flush is normally not required.

CBL

Oversized, cylindrical step bore design for seals with large gland bolt and gasket circles.

• Dual internal component seals. Isolates the seal chamber from the process. Allows less expensive seal materials. Recommended in tough slurry applications Note: Use External Flush Plan 54. Others (i.e., Plans 52, 53) not recommended without close tolerance pumping mechanism.

(Preferred seal chamber design for nearly all applications)

• Single internal component or cartridge seals when applied with a throat bushing. Usually selected to increase stuffing box pressure above the vapor pressure to avoid cavitation, etc. Note: Applied with Plan 11, etc.

CBS

Cylindrical bore design for packing arrangements and conventional seals with small gland bolt and gasket circles.

*All seal selections perform best when the faces are located directly within the flush path, particularly if solids, liquors, or slurries are present. Component seals with clamped seat gland designs locate the seal faces reasonably well. Flexibly mounted seat glands should include the vent and drain option to better locate the seal faces. The FML is always the first-choice chamber for maximum self-flush path benefits.

• Dual internal component seals. Isolates the seal chamber from the process. Allows less expensive seal materials. Recommended in tough slurry applications. Allows for thermal convection type flush plans; however, pumping ring devices are recommended Note: External Flush Plans 52, 53, 54 • Single internal component or cartridge seals when applied with a throat bushing. Usually selected to increase stuffing box pressure above the vapor pressure to avoid cavitation, etc. • Usually preferred over the CBL when jacketing is selected for increased effectiveness in cooling or heating Note: Applied with Plan 11, etc.

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 Seal Chamber Dimensions



H

H 1

C

1

C

G2

B G1

B G1

D J*



K E F

D J*

K F

Standard Group 1, 2 & 3 CBL

Standard Group 1, 2 & 3 FML

C Drilled B

No. of Holes

Size

B.C.

D

E

F

G1

G2

H

J*

K

1

A

1

FML/CBL

Mark 3 GROUP 1

35 mm (13/8 in)

86 mm (3 3/8 in)

4

3

102 mm (4 in)

60 mm (2 11/32 in)

51 mm (2 in)

5 mm (3/16 in)

73 mm (27/8 in)

54 mm (21/8 in)

19 mm (3/4 in) Annulus

131 mm (25/32 in)

58 mm (29/32 in)

Mark 3 GROUP 2

48 mm (17/8 in)

105 mm (41/8 in)

4

1

127 mm (5 in)

92 mm (3 5/8 in)

51 mm (2 in)

5 mm (3/16 in)

92 mm (35/8 in)

67 mm (25/8 in)

22 mm (7/8 in) Annulus

79 mm (31/8 in)

57 mm (2 1/4 in)

Mark 3 GROUP 3

67 mm (2 5/8 in)

130 mm (5 1/8 in)

4

1

152 mm (6 in)

98 mm (3 27/32 in)

76 mm (3 in)

5 mm (3/16 in)

117 mm (45/8 in)

92 mm (35/8 in)

25 mm (1 in) Annulus

86 mm (33/8 in)

84 mm 35/16 in)

/8-16

/2-13 /2-13

*Face of seal chamber to end of optional shaft sleeve

D2 J2*





F

B G

B G

F

C

H1

H2

C Standard Group 1, 2 & 3 CBS

Standard Group 1, 2 & 3 FMS

FMS/CBS

C Drilled No. of Holes Size B.C.

A

B

35 mm (13/8 in)

67 mm (25/8 in)

4

3

83 mm 131 mm 131 mm 56 mm 5 mm 54 mm (3 1/4 in) (25/32 in) (25/32 in) (23/16 in) (3/16 in) (2 1/8 in)

Mark 3 GROUP 2

48 mm (17/8 in)

79 mm (31/8 in)

4

3

95 mm (3 3/4 in)

Mark 3 GROUP 3

67 mm 108 mm (25/8 in) (4 1/4 in)

4

1

140 mm 91 mm 98 mm 83 mm 5 mm 92 mm (51/2 in) (3 19/32 in) (3 27/32 in) (31/4 in) (3/16 in) (3 5/8 in)

Mark 3 GROUP 1

/8-16 /8-16 /2-13

K1 E

D1 J1*

K2

D1

D2

76 mm (3 in)

E

F

G

H1 10 mm (3/8 in) Annulus

76 mm 67 mm 5 mm 67 mm 10 mm (3/8 in) (3 in) (2 5/8 in) (3/16 in) (2 5/8 in) Annulus 13 mm (1/2 in) Annulus

H2

J1*

J2*

22 mm (7/8 in) Annulus

64 mm (21/2 in)

64 mm (21/2 in)

73 mm (2 7/8 in)

25 mm (1 in) Annulus

79 mm (31/8 in)

86 mm (3 3/8 in)

90 mm 84 mm (3 9/16 in) (3 5/16 in)

E

Mark 3 GROUP 1 Mark 3 GROUP 1 Mark 3 GROUP 3

A

E

G

H

60 mm (2 3/8 in)

54 mm (2 1/8 in)

19 mm ( 3/4 in) Annulus

48 mm (17/8 in) 67 mm (25/8 in)

56 mm (2 3/16 in) 92 mm (3 3/8 in)

67 mm (2 5/8 in) 92 mm (3 5/8 in)

22 mm ( 7/8 in) Annulus 25 mm (1 in) Annulus

NOTE: All dimensions are for reference. Not to be used for seal or gland construction

14

G



35 mm (13/8 in)

K2

19 mm (3/4 in) 49 mm 49 mm 63 mm 63 mm Annulus (115/16 in) (115/16 in) (215/32 in) (215/32 in)

*Face of seal chamber to end of optional shaft sleeve

FMI

K1

H

Standard Group 1, 2 & 3 FMI

73 mm (2 7/8 in)

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Pump Division

ANSI Pump and Enhancements

DurcoShield™ Pump Safety Accessory

DurcoShield is easy to install or to remove. Simply spread the shield apart... fit around the bearing housing adapter... and snap into place. The spring-like tension holds the shield firmly in place. • Its transparency permits visual inspection of the seal area • Optionally available in PVDF • Applications from -57°C (-70°F) to 149°C (300°F) • Available for Mark 2, Mark 3 and Chemstar® pumps

This splash and shaft guard is a one-piece shield that envelopes the open areas between the bearing housing and the casing. • Fluid spray from a malfunctioning seal is deflected by the shield • Provides protection from the rotating shaft in the area of the mechanical seal as required by safety regulations of many countries, including the USA’s OSHA Section 29 CFR 1910 and EU Machinery Directory Protection from the potential dangers of: • Process fluid spray • Rotating shaft and seal components

Contact your local Flowserve representative today for complete information.

Slots or holes to accommodate seal support piping/tubing can be easily located and drilled or cut.

This device is not a containment system, nor a seal backup system. It is a limited protection device. It will reduce, but not eliminate, the probability of injury. PATENT PENDING

15

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Pump Division

ANSI Pump and Enhancements

Impeller Options

Flowserve Durco reverse vane impellers deliver unequalled efficiency and performance. This exclusive impeller design extends bearing and seal life. Low, Predictable Seal Chamber Pressure and thrust loads resulting from back vane pumping action and balance holes Low Required NPSH, lowest overall of any standard pump Rear Cover Plate Wear Surface as the flow path exits the rear of the impeller, placing abrasive wear on the rear cover rather than the more expensive casing

Exclusive Reverse Vane Impeller with balance holes offers important performance enhancing, maintenance reducing advantages.

In Shop Impeller Adjustment with the only impeller design that takes full advantage of the back pull out feature. Since the critical running clearance is set between the rear of the impeller and the rear cover plate, both impeller and mechanical seal settings can be done in the shop, “on the bench,” instead of under adverse field conditions Repeatable Performance Assurance with the only impeller design that offers repeatability in seal chamber pressure and bearing thrust loads

Front Vane Open Style Impeller is fully interchangeable with the reverse vane impeller. Excellent choice for stringy and certain applications requiring high shear against the casing.

In-shop Impeller Adjustment…Practical and Productive!

For Low Flow and/or High Head Applications see page 18

Low predictable seal chamber pressure means longer seal life Clearance is set to the rear cover in the shop – not with casing which is left in the piping

Lowest overall required NPSH of any standard pump

Rear cover wear surface versus casing means lower replacement parts costs

16

Note: Recessed impeller pumps offer excellent solids handling capabilities. See pages 52-55 for details.

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Pump Division

ANSI Pump and Enhancements

Reverse Vane Impeller and Repeatable Performance

Only a Flowserve Durco reverse vane impeller offers repeatable performance after wear and impeller adjustment.

An impeller cannot be adjusted to two locations.

Performance Life Cycle: Flowserve Durco Reverse Vane Impeller with Balance Holes

Performance Life Cycle: Front Vane Open Style Impeller with Pump Out Vanes

Effects of Wear • Thrust loads decrease as seal chamber gap widens • Chamber pressure increases as gap widens Effects of Impeller Adjustment to Seal Chamber • Original pressures and loads re-established after adjustment • Repeatable MTBPM cycle life The Reverse Vane Impeller has only one set of pumping vanes and one critical tolerance location – between the impeller and rear cover – to establish: • Performance • Efficiencies • Seal chamber pressures (i.e., mechanical seal MTBPM) • Thrust/axial loads (i.e., bearing life)

Seal and bearing life are reduced due to increased loads after wear and maintenance adjustment.

Effects of Wear • Thrust loads increase as seal chamber gap widens • Chamber pressure increases as gap widens Effects of Impeller Adjustment to Casing • Chamber pressures and bearing loads increase after each adjustment • Non-repeatable MTBPM cycle life

Pump Performance Vanes

Only One Tolerance Impeller Vanes To Cover

Reverse Vane Impeller Adjustment

Pump Out Vanes

Front Vane Impeller Adjustment

Since an impeller can only be set in one direction, the reverse vane impeller has inherent advantages. Reverse Vane Impeller

Front Vane Open Style Impeller Diminished Performance

Consistent, Like-New Repeatable Performance Thrust

Thrust

Original Axial Thrust

Seal Chamber Pressure Original Chamber Pressure

Cycles Repeat

Effects of Wear & Impeller Readjustment

Seal Chamber Pressure/Axial Thrust

Seal Chamber Pressure/Axial Thrust

The Front Vane Open Style Impeller has two sets of pumping vanes and two critical tolerance locations: • The front vane of the impeller clearance to the casing establishes: – performance – efficiencies • The impeller pump out vanes clearance to the rear cover establishes: – seal chamber pressures and seal life – thrust loads and bearing life

Original Axial Thrust

Seal Chamber Pressure Original Chamber Pressure

Cycles Reduce

Effects of Wear & Impeller Readjustment

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 Lo-Flo™ Pumps

Improved Pump Reliability with Extended MTBPM at Low Flow Rates Flowserve extends its ANSI pump design for high head/low flow rates. • 1K1.5 x 1LF-4 • 1K1.5 x 1LF-8 • 2K2 x 1LF-10 • 2K3 x 1.5LF-13 Offered in a wide selection of metallurgy.

Low Flow Applications • Flows to 50 m3/h (220 gpm) • Heads to 300 m (985 ft) • Pressures to 3100 kPa (450 psi) • Temperatures to 370˚C (700˚F) (See composite performance curve page 28)

Flowserve Durco Superior Impeller Design Provides: • Minimal thrust loads • Reduced NPSH requirements • Low seal chamber pressures • Standard Mark 3A or ANSI 3A™ power ends • Broader applications range • Longer seal and bearing life

Conforms to standard ASME B73.1 dimensions Standard Mark 3 power end maximizes interchangeability

Percent of maximum vibration of the standard pump

100%

SHAFT VIBRATION

75% Expanding Volute Casing

50% 25% 0%

0 0

Lo-Flo Standard

18

Circular concentric casing and radial vane impeller with… “a unique twist.”

100 25

200

gpm

50

m3/h

Flow

Circular Concentric Casing

Extend MTBPM over standard pumps • Radial loads are reduced up to 90% at low flows • Shaft vibration is reduced up to 50% (See graph) • Bearing life is extended • Mechanical seal life is extended

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 Casing Options

Standard Casings have fully machined wet face

Centerline Mounted Casings may be used to reduce loads caused by thermal expansion. Jacketed feet with inlet/outlet coolant ports further assure effective temperature control

Optional Connections TAP III

Flange Options include: DIN/PN16 (Class 150) flat flanges (standard); DIN/PN40 (Class 300) flat flanges; and raised face flanges

TAP VI (AVAIL. GR II 10 &13'', GR III)

Jacketed Casings for temperature control. Integral jacketed casing is shown here. Also available: Bolt-on aluminum jackets; and thermonized heat transfer tubes

TAP V (1/4 NPT. STD.)

TAP IV (OPP.) SIDE) TAP II

TAP I

TAP VII

Flowserve Durco Casing Flanges are finished in accordance with the ASME B16.5 standard which, in summary, says that the surface must have a serrated finish having from 24 to 40 grooves per 25 mm (1 inch), and the surface finish must have a Ra roughness of 3.1 µm (125 µin) to 12.5 µm (500 µin)

JACKET PRESSURE – P.S.I.G.

Pressure/Temperature Rating For Cast Jackets on Pump – Casing, Cover, and Stuffing Box

Hydrostatic Test Pressure is 150% of Rated Pressure at -20 to 100°F

TAP IV

Item Part

Typical Size

I

Casing Drain

3/4-10

3/4

NPT

II

Suction Nozzle Gage Connection

1/ 4

NPT

III

Discharge Nozzle Gage Connection

1/ 4

NPT

IV

Connection for Line to Seal Chamber

1/ 4

NPT

V

Connection for Line to Seal Chamber

1/ 4

NPT

VI

Flush Connection for Mechanical Seal

1/ 4

NPT

VII

Bottom Tap in Seal Chamber

1/ 4

NPT

Flange Drilling Standard Class 150 Size mm (in) 25 (1) 40 (1-1/2) 50 (2) 80 (3) 100 (4) 150 (6) 200 (8) 250 (10)

Optional Class 300

No.

Hole Size mm (in)

B.C. mm (in)

No.

Hole Size mm (in)

B.C. mm (in)

4 4 4 4 8 8 8 12

16 (5/8) 16 (5/8) 19 (3/4) 19 (3/4) 19 (3/4) 22 (7/8) 22 (7/8) 25 (1)

79 (3-1/8) 98 (3-7/8) 121 (4-3/4) 152 (6) 190 (7-1/2) 241 (9-1/2) 298 (11-3/4) 362 (14-1/4)

4 4 8 8 8 12 12 16

19 (3/4) 22 (7/8) 19 (3/4) 22 (7/8) 22 (7/8) 22 (7/8) 25 (1) 29 (1-1/8)

89 (3-1/2) 114 (4-1/2) 127 (5) 168 (6-5/8) 200 (7-7/8) 270 (10-5/8) 330 (13) 387 (15-1/4)

Class 150 smooth flat face is standard. Class 300 smooth flat face and Class 150 and Class 300 raised faces are available. JACKET – TEMPERATURE °F

19

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 Pump/Motor Shaft Alignment

Motor

Spacer Ring Jam Nut Motor Adjuster

Rigid coupling guard side plates exceed ASME B15.1 requirements and permits visual indication of rotation.

Adapter

Motor Mounting Stud Nut

Unique C-Plus Precision Alignment System With Four-Point Motor Adjustment To achieve the best process pump and motor MTBPM requires shaft alignments of less than 0.05 mm (0.002 in). But the stackup tolerances of even the most perfectly crafted C-Flange adapted pump and motor package can often produce misalignments up to 0.38 mm (0.015 in). This unique C-Plus precision alignment system routinely delivers shaft alignments below 0.05 mm (0.002 in) in less than thirty minutes.

20

Ultralign™ C-flange adapter with the C-Plus precision alignment option delivers fast, repeatable, precisely accurate pump/motor shaft alignment.

Standard Footed Motors • Special machine-cut C-Face of assembled unit ensures shaft perpendicularity • Motor is cantilevered, or free hung. (Footed design provides support during shipping.) • Tested and proven through 405TC frame to 75 kW (100 hp), to ensure rigid assembly and freedom from excessive vibration and deflection Motor and Bearing Housing Foot Mounting to Base Is Not Required or Recommended • Reduces soft foot potential • Helps eliminate alignment distortion caused by fulcrum effect of soft foot bolting to the base • Optimizes the ability of the C-Flange design to move the motor with the pump shaft, maintaining alignment

Adjustable Rigid Foot Mount • Assures accurate alignment to the baseplate and piping • Designed to support all normal loads C-Flange Adapter • Parallel shaft alignment of 0.18 mm (0.007 in) nominal as governed by tolerance stackups • Angular shaft alignment within 0.001 mm/mm (0.001 in/in)

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ANSI Pump and Enhancements

Flowserve Durco Mark 3 Specifications For Low and High Temperature Services

Centerline Mounted Casing

With special attention to materials and component options Mark 3 pumps can be used to handle liquids ranging in temperature from as low as -130°C (-200°F) to as high as 370°C (700°F). It is always essential that the pressure and temperature of the application never exceed the pressure/temperature limits of the pump. These limits may be found in the chart on page 30 of this bulletin. Operation at either low or high temperatures could require modification of the standard pump design to provide strength of materials for pressure containment and resistance to thermal shock, a method for cooling or heating pump components, mechanical seal protection, special gaskets, and/ or maintenance of pump/motor shaft alignment. The Ultralign C-flange motor adapter is recommended on any application with temperature fluctuations of more than 38°C (100°F).

Low Temperature Applications Special recommendations for temperatures < -29°C (-20°F).

Casing Stainless steel alloys with jacketing. Seal Chamber Stainless steel with jacketing. SealSentry designs with customized seal and flush plan as required by the application. Shaft and Sleeve Stainless steel alloy with optional replaceable alloy sleeves. Friction welded 1144/316 (ZH) is recommended. Gaskets Temperature/liquid compatible. Coupling Flexible member spacer-type. Power End Stainless steel bearing housing and adapter. ANSI 3A with synthetic lubricant recommended. High Temperature Modifications Special recommendations for temperatures > 149°C (300°F).

Bearing Housing ANSI 3A power end is recommended. For temperatures > 177°C (350°F) oil cooling system is recommended. For temperatures > 260°C (500°F), stainless steel bearing housings are required on Group 1 pumps and stainless steel adapters are required on Groups 2 and 3 pumps.

Jacketed SealSentry Seal Chambers Ultralign C-Flange Motor Adapter (See page 20)

Jacketed standard bore (CBS) is recommended when cooling the seal chamber is the objective.

® Grafoil is a registered trademark of Union Carbide Corporation

Rear Cover For temperatures > 177°C (350°F) jacketing is recommended. In addition, CBL or CBS with throat bushing is recommended to allow cooling jacket to be more effective. Shaft Friction welded 1144/316 (ZH) is recommended.

Cooling Coil Oil Temperature Control

Jacketed Casing

Casing For heat transfer liquids, recommend using DIN/PN40 (ANSI Class 300) flanges. Temperatures > 149°C (300°F) require Grafoil ® impeller and casing gaskets. If Ultralign heavy-duty rigid design C-flange adapter is not used and temperature is > 177°C (350°F), then centerline mounting of the casing with cooling of mounting legs is recommended. If Ultralign is used, centerline mounting is not recommended until temperature exceeds 260°C (500°F).

Jacketed FM chamber is preferred when protection of the process temperature is important.

Baseplate Rigid reinforced base with stilt/spring mounting. Motor Mounting Ultralign C-flange adapter is recommended on Groups 1 and 2. Hot alignment is always recommended.

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ANSI Pump and Enhancements Flowserve offers a family of five (5) types of pre-engineered baseplate designs to extend MTBPM and reduce costs. Reducing internal stress and vibration extends MTBPM of pump/motor packages Pump users specify rigid baseplate designs to: • Provide torsional lateral and longitudinal rigidity • Improve vibration dampening through greater mass and design stiffness • Protect against transit damage • Resist twisting during installation • Maintain designed-in shaft alignment • Reduce installation and shaft alignment time • Reduce diaphragming or separation from grout • Improve pump/motor/seal MTBPM • Reduce total life cycle pump/motor/seal costs BaseLine can handle the stress. Rigid design begins with thick plate construction. Metal baseplate sizes: • 139 to 258 feature 13 mm (1/2 in) steel plate construction • 264 to 280 feature 16 mm (5/8 in) steel plate construction • 368 to 398 feature 19 mm (3/4 in) steel plate construction Polybase baseplates are constructed of 76 mm (3 in) to 102 mm (4 in) solid polymer concrete. Baseplate Types B, C, D and E are reinforced with added structural support for improved rigidity.

22

Baseplates Provide the Backbone for Extended MTBPM The test stand provided three corner support of the ungrouted baseplates. The addition of weights on the unsupported fourth corner caused baseplate

distortion. This distortion resulted in measurable shaft movement that can cause problems with field installations and negatively affect MTBPM. The twist test is a means of comparing rigid baseplate designs. Correctly installed rigid baseplates should not experience these twist effects. For more information about the results of baseplate testing contact the local Flowserve sales representative. Baseplate Rigidity Test – Twist Mode A

1.78 (0.070) 1.52 (0.060)

Deflection – mm (inch)

Flowserve Durco Mark 3 BaseLine™ Baseplate System

D

1.27 (0.050) 1.02 (0.040) 0.08 (0.030) 0.51 (0.020)

E

0.25 (0.010)

B C

0.00 (0.000)

0

45 (100) Load - kg (lb)

91 (200)

Maximum Parallel Shaft Deflection at Applied Force Type A

0.56 mm (0.022 in)

Type B

0.01 mm (0.004 in)

Type C

0.08 mm (0.003 in)

Type D

0.41 mm (0.016 in)

Type E

0.13 mm (0.005 in)

Baseplates A through E are shown on pages 24 through 27.

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Pump Division

ANSI Pump and Enhancements

BaseLine™ Most Commonly Requested Baseplate Features Item Standard Options No. 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 Y= O=

Type A Gp I & II Gp III

Type B

Type C

Machined coplanar mounting surfaces to 0.17 mm/m O O O O (0.002 in/ft) with 3.2 micron (125 µin) finish Added structural (cross member) support N N Y Y Added torsional support with end caps NR Y Y D Tapped holes for four (4) motor adjuster bolts O O O Y Four (4) - SS transverse jack bolts - motor adjusters O O O Y Sloped surface to an integral drain 25 mm (1 in) N N C N Integral sloped drip rim around base N N N N 102 mm (4 in) diameter grout holes max. 762 mm (30 in) run to vent Y Y Y N 13 mm (1/2 in) vent holes at corner of each chamber NR O NR NA Lower surface shaped to anchor in grout N N N NA Integral lifting eyes at four (4) corners O Y O O Tapped leveling holes four (4) corners O O N S Continuous seam weld construction NA Y NA O Welded raised lip around grout hole(s) NR NR NR NA Stilt mounting options with floor cups NR NR O Y Spring mounted load designs NA NA O O Catch basin (304SS or other materials) O O O O Option for eight (8) total motor adjusters D D O D Dimensions to ASME B73.1-2001 Y Y Y Y Standard N = Not available NR = Not recommended Optional NA = Not applicable C = Sloped catch basin with 25 mm (1 inch) drain (option)

Type D

Type D with Rim

Type E

O

O

Y

Y O O O N N

Y O O O N Y

Y Y Y Y Y Y

Y Y Y Y Y Y NR D D O D Y

Y Y Y Y Y Y Y Y Y Y Y Y NR O D D D D NR Y D D Y Y D = Needs design time S = Stilts for leveling

See pages 24-27 for BaseLine model descriptions

Flowserve Durco Baseplate Dimensions Specify (new) ASME B73.1-2001 dimensions to avoid costly confusion between manufacturer and designer. Flowserve Durco ANSI Pump Size Group

Base No.

1K

139

2K

3K

Flowserve Durco ANSI Polybase*

Min./ Max. NEMA Frame

Overall Dimensions LxW mm (inches)

Anchor Bolt C LxW mm (inches)

Pump Size Group

Base No.

Min./ Max. NEMA Frame

Overall Dimensions LxW mm (inches)

Anchor Bolt C LxW mm (inches)

326T

927 x 229 (361/2 x 9) 1156 x 305 (451/2 x 12) 1283 x 381 (501/2 x 15)

139

153

991 x 381 (39 x 15) 1219 x 457 (48 x 18) 1346 x 533 (53 x 21)

1K

148

143T 184T 256T

148

143T 184T 256T

153

326T

991 x 330 (39 x 13) 1219 x 406 (48 x 16) 1346 x 483 (53 x 19)

927 x 229 (361/2 x 9) 1156 x 305 (451/2 x 12) 1283 x 381 (501/2 x 15)

245

184T 215T

258

286T

264

365T

268

405TS

280

449TS

1080 x 229 (421/2 x 9) 1257 x 305 (491/2 x 12) 1410 x 381 (551/2 x 15) 1562 x 381 (611/2 x 15) 1664 x 483 (651/2 x 19) 1969 x 483 (771/2 x 19)

2K

252

1143 x 381 (45 x 15) 1321 x 457 (52 x 18) 1473 x 533 (58 x 21) 1626 x 559 (64 x 22) 1727 x 660 (68 x 26) 2032 x 660 (80 x 26)

245

184T

252

215T

258

286T

264

365T

268

405TS

280

449TS

1143 x 330 (45 x 13) 1321 x 406 (52 x 16) 1473 x 483 (58 x 19) 1626 x 559 (64 x 22) 1727 x 660 (68 x 26) 2032 x 660 (80 x 26)

1040 x 229 (421/2 x 9) 1257 x 305 (491/2 x 12) 1410 x 381 (551/2 x 15) 1562 x 381 (611/2 x 15) 1664 x 483 (651/2 x 19) 1969 x 483 (771/2 x 19)

368

286T 405T

398

449T

1664 x 483 (651/2 x 19) 1969 x 483 (771/2 x 19) 2426 x 483 (951/2 x 19)

3K

380

1727 x 660 (68 x 26) 2032 x 660 (80 x 26) 2489 x 660 (98 x 26)

368

286T

380

405T

398

449T

1727 x 660 (68 x 26) 2032 x 660 (80 x 26) 2489 x 660 (98 x 26)

1664 x 483 (651/2 x 19) 1969 x 483 (771/2 x 19) 2426 x 483 (951/2 x 19)

*330 mm (13 in) wide sizes are 92 mm (3 5/8 in) thick, 660 mm (26 in) wide sizes are 108 m (41/4 in) thick, while remaining sizes are 102 mm (4 in) thick.

23

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Mark 3 BaseLine™ Baseplate System

Type A Standard Baseplate, Foundation or Stilt Mounted 13 mm (1/2 in) plate through #258 size 16 mm (5/8 in) plate through #280 • Designed for grout installation with 102 mm (4 in) diameter hole • Stilt mounting recommended only on minimal stress installations • Stilt cross bars 25 mm (1 in) thick located at ends, mounted through anchor bolt holes • Not available with spring load Style D stilts Group 3 • 19 mm (3/4 in) top plate construction all sizes • Side plate and reinforcement members 13 mm (1/2 in) • Designed for grout installations with 102 mm (4 in) diameter holes

Traditional Motor Adjuster Jack Bolts To align shafts to critical tolerances with minimal disturbance of indicators. Refer to page 25 to learn more about the new Flowserve 8-Point™ Adjustment.

Baseplate Options Optional Steel Mounting Blocks Below 67 mm (2 5/8 in) In Height Solid machined steel bar. Polybloc™ units are standard (page 25)

Optional Mounting Box 67 mm (2 5/8 in) And Above In Height 10 mm (3/8 in) min. seam welded plate. Mounting blocks are optional 24

Centering Nut – Factory Pre-Alignment Procedure All assemblies are prealigned at the factory using centering nuts which are replaced with fastener nuts for shipment. This allows the maximum movement of the motor in the field to avoid bolt binding during final shaft alignment efforts

Drip Rim Pump End Only Type A and C For full rim use Type D with drain rim

304SS Catch Basin Type A, C, and D

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Pump Division

ANSI Pump and Enhancements

Flowserve Durco Solid Polymer Concrete Polybase™

• Polybase is available with or without catch basin or grout holes • Inserts can be located to accommodate various pump/motor type configurations • Polybloc is available for alternate equipment applications

Type B Foundation or Stilt Mounted Featuring Flowserve Durco Solid Polymer Concrete Polybase™ and Polybloc™ Adjustment System

Polybase • Low installed cost • Superior vibration dampening • Corrosion resistant • Superior resistance to twisting or diaphragming • Designed to be flat • Available with or without catch basin or grout holes • Inserts can be located to mount alternate equipment configuration requirements Solid cast reinforced polymer construction makes Polybase extremely strong and rigid. It easily handles pump and motor loads without flexing problems commonly associated with cast iron or FRP baseplates. Its excellent corrosion resistant properties enable it to outperform and outlast typical cast iron or even steel baseplates.

Vibration Damping Comparison The extraordinary vibration damping characteristics of polymer concrete significantly reduce wear and tear on pumps, seals and motors. Greater dampening characteristics mean easier vibration analysis during preventive maintenance. Vibration damping of polymer concrete versus cast iron

Cast Iron 0.125 Sec.

Polymer Concrete 0.125 Sec. © John F. Kane, Composites Institute, The Society of the Plastics Industry, Inc.

Polybloc™ – Motor Mounting Block • Flatter and more repeatable height tolerances than steel • Corrosion resistant • Superior vibration dampening • Full foot support (no overhang) • Shown with optional Bloc-lock and fastener support • Available for alternate equipment applications Motor Foot

8-Point™ Adjuster • Allows precise motor adjustment to reduce alignment time • Used with recessed bloc-lock device • Can be used to help lock motor in place once alignment is established

Adjuster Bracket

Transverse Jack Bolt (Axial Jack Bolt is at 90°, not shown)

Shim Allowance Jam Nut Polybloc

Baseplate All-Thread Mounting Stud

25

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ANSI Pump and Enhancements

Flowserve Durco Mark 3 BaseLine™ Baseplate System

Special Support of Sizes 268 and 280 • Cross bracing provided • Cross bars added • Additional gussets

Type C Reinforced Baseplate, Stilt Mounted • Reinforced with 13 mm (1/2 in) bottom plate • Gussets add strength and dampen vibration • Standard with four (4) tapped holes for motor adjuster jack bolts • Designed without grout hole for maximum strength • Stilts located under center of pump and center of motor

Group 3 Group 3 has similar profile to Standard Type A baseplate. Note the addition of extensive structural support and the added features that are standard with the Type C design.

Type D Reinforced Baseplate, Foundation Mounted • End caps are a recommended option to add stiffness • I-beam adds torsional rigidity and anchors grout • Bottom allows complete grout contact

Reinforced Baseplate with Drain Rim • Drain rim is sloped to 25 mm (1 in) drain 26

Group 3 has similar profile to Standard Type A baseplate. Note the addition of extensive structural support and the added features that are standard with the Type D design.

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Pump Division

ANSI Pump and Enhancements Type E “Ten Point” Heavy-Duty Foundation • Ten major features are standard (See chart page 23) • Extensive double reinforcement • Bottom allows complete grout contact and grout anchoring

Benefits of Epoxy Grout • Better corrosion resistance • Less shrinkage • Better bond to properly prepared base • Better long-term life cycle costs • Superior vibration dampening

API 610 Comments • Sometimes specified for rigidity and special features • Types B, D, and E meet the intent of API 610 rigidity • Type E offers all design criteria except grout hole is 102 mm (4 in) diameter vs.

Grouted Baseplate Installations • Better dissipation of vibration • Better resistance to torsional stress • Best design if piping designed and installed free of stress loads • Pipe loads stress pump and cause greater misalignment with the motor shaft, etc. Stilt with Floor Cup Options

123 cm2 (19 in2) and our vent holes limit to 762 mm (30 in) maximum run vs. 458 mm (18 in). Raised lip around grout hole is an option

Group 3 has similar profile to Standard Type A baseplate. Note the addition of extensive structural support and the added features that are standard with the Type E design.

Rigid Stilt Mounted Installations • Better relief of pipe load stress • Pump moves to point of least resistance • Lowest installation cost – Base must supply added rigidity – Vibration levels are higher than in grouted installations Style C For Types A, B, and C Baseplate

Style A For Types A, B, and C Baseplate 19 mm (3/4 in) rod; 92 mm (35/8 in) to 229 mm (9 in) height Group 3 = 25 mm (1 in) rod

51 mm (2 in) pipe with cross bracing > 419 mm (161/2 in) height

Style B For Types A, B, and C Baseplate

Style D With Spring Load For Types B and C Baseplate

51 mm (2 in) pipe; 229 mm (9 in) to 419 mm (161/2 in) height

241 mm (91/2 in) to 292 mm (111/2 in) height

Optional PTFE Slide Plate adds 38 mm (115/32 in) to height

27

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Pump Division

Technical Data

Mark 3 Standard Group 1

Mark 3 Standard Performance Curves 0 m 320

20

40

ft 0 1120

60

FLOW – 50 Hz (2900 RPM) 100 120 140 160 180

80

200

400

600

200

220

800

240

260 m3/h m

ft

1000 gpm

750

1040 960

280

18

720 200

150 450

20

640 19

560 160

10 480

100 21

120

400

80

11

5

13

240

4

3x2-6

5

11/2 x1LF-8

6

11/2 x1-8

7

3x11/2 -8

8

3x2-8

9

4x3-8

16 6x4-10 17 6x4-10H 18 3x11/2 LF-13 19 3x11/2 -13 20 3x2-13 21 4x3-13

Mark 3 Standard Group 3

0 0

200

0

50

22 4x3-13HH 23 6x4-13A

9

4

3

1

50

150 8

2

80

3x11/2 -6

14 4x3-10 15 4x3-10H

14

7

6

40

3

12 3x11/2 -10A 13 3x2-10A

16

160

0

300

12

320

11/2 x1-6

10 2x1LF-10 11 2x1-10A

TDH – 50 Hz (2900 RPM)

TDH – 60 Hz (3500 RPM)

240

600

800

11/2 x1LF-4

2

Mark 3 Standard Group 2

200

880

1

400

600

100

800

1000

150 200 FLOW – 60 Hz (3500 RPM)

24 8x6-14A 25 10x8-14

0 0 1400 gpm

1200 250

26 6x4-16 27 8x6-16A

300 m /h 3

28 10x8-16 29 10x8-16H 30 10x8-17* *Max. speed 1450 RPM

0 m

80

50

ft 0 300

FLOW – 50 Hz (1450 RPM) 150 190 500

100

200

400

600

800

800

2300

1100

3800

5300

1400 m3/h 6800 gpm ft 200

m 60

250

SCALE

18

200

40 22 23

150 40

19

10

20

21

12

25

28

7 8

2

3

20

16

50 10

9 14

4

1 0 0

30

29

17 15

6

50

0

27

13

5 20

0

100

24

100 11

28

150

200 50

400 100

600

800 150

1000

200 227 400 FLOW – 60 Hz (1750 RPM)

2800

4600 800

6400 1200

0 8200 gpm 1600 m3/h

0

TDH – 50 Hz (1450 RPM)

TDH – 60 Hz (1750 RPM)

60

CHANGE

50 26

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Pump Division

Technical Data

• • • • •



CASINGS

OR

FRONT VANE OPEN STYLE IMPELLERS



REVERSE VANE IMPELLERS

POWER END

REAR COVERS

Mark 3 Standard Group 1

• • • • • • •

• • • • • • •

11/2X1LF-4 11/2X1-6 3X11/2-6 3X2-6 11/2X1LF-8 11/2X1-8 3X11/2-8





• • • • • • • • • • • • • •





CASINGS



REVERSE VANE IMPELLERS

REAR COVERS



OR

FRONT VANE OPEN STYLE IMPELLERS



ADAPTERS

Mark 3 Standard Group 2

POWER END

• • • • • • • • • • • • • • •

• • • • • • • • • • • • • • • •

3X2-8 4X3-8 2X1LF-10 2X1-10A 3X11/2-10A 3X2-10A 4X3-10 4X3-10H 6X4-10 6X4-10H 3X11/2LF-13 3X11/2-13 3X2-13 4X3-13 4X3-13HH 6X4-13A

• •

• •

• • •

• • • • • • •

• • • • • •

CASINGS

OR

FRONT VANE OPEN STYLE IMPELLERS

REVERSE VANE IMPELLERS

REAR COVERS

Mark 3 Standard Group 3

ADAPTERS

The thirty (30) pumps in the Mark 3 family are built with only three different power frames. SealSentry provides a choice of five (5) different seal chamber options to best meet customers’ specific needs.

POWER END

Interchangeability

• • • • • • •

8X6-14A 10X8-14 6X4-16 8X6-16A 10X8-16 10X8-16H 10X8-17

29

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Pump Division

Technical Data

Pressure Temperature Ratings ANSI Std. GP2-10" GP2-13" Curve A Curve A Curve C Curve B

GP2-8" Curve A Curve C

GP3 Curve A Curve B

GP1 Curve A Curve C

In-Line GP2-10" Curve A Curve C

Curve A

Lo-Flo GP2-10" Curve A Curve C

GP1 Curve A Curve C

200

300

Sealmatic

Unitized

Curve A Curve B

Curve A Curve B

Curve A Curve B

DC2 DC3 Ti TiP Zr

CD4M DS

2000

500

600

300 D2 D2L

D4 D4L DV

DMM

250

1500 DINC

200

1250 DNI

1000

150

D20

DS DCI Low Limit

750

D2O CD4M DNI Upper Limit

500 CR28 CR29 CR35

250

-100

700 350

-50

0

50

0

100

200

300

CD4M

DCI

1750

TEMPERATURE °F

400

100 50

DCI Upper Limit

400

500

600

700 400

DINC DC2 DC3

2500

350

DCI

2250

DS

300

2000

DMM D20

1750

Ti TiP Zr

DNI

1500 DS DCI Low Limit

1250 1000

100 150 200 250 300 350

250 D2 D2L D4 D4L DV

200

D2O CD4M DNI Upper Limit

150

DCI Upper Limit

750

0

-50

0

TEMPERATURE °C

50

100

100 150 200 250 300 350

TEMPERATURE °C

Curve C

Curve D TEMPERATURE °F

TEMPERATURE °F 100

200

3000

300

400

500

600

CD4M

400 DS

DINC

D2/D2L D4/D4L/DV

2500 2250

350

DCI

2000

300

DMM DNI

1750

250 D20 Ti/TiP/Zr

1500 DS DCI Low Limit

1250 -50

0

50

0

100

200

D2O/CD4M/DNI Upper Limit DCI Upper Limit

100 150 200 250 300 350

TEMPERATURE °C

200

400

500

600

700 500

DINC DC2 DC3

3000

450 DCI DS

2750 Ti TiP Zr

2500

2000

DNI DMM

1750

DS DCI Low Limit

1500 1250

D2 D2L D4 D4L DV

D2O CD4M DNI Upper Limit DCI Upper Limit

750 -50

0

50

400 350

D20

2250

1000 150

300

CD4M

3250

DC2/DC3

2750

-100

700 450

MAX. DISCHARGE PRESSURE-kPa

0

MAX. DISCHARGE PRESSURE-PSI

-100

MAX. DISCHARGE PRESSURE-kPa

Recessed

MAX. DISCHARGE PRESSURE-PSI

100

TEMPERATURE °F

MAX. DISCHARGE PRESSURE-PSI

0

2250

30

GP2-13" NA Curve D

Curve B

-100

MAX. DISCHARGE PRESSURE-kPa

GP2-13" Curve A Curve B

100 150 200 250 300 350

TEMPERATURE °C

300 250 200 150 100

MAX. DISCHARGE PRESSURE-PSI

150 300

GP1 Curve A Curve C

MAX. DISCHARGE PRESSURE-kPa

Class

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Pump Division

Technical Data Curves shown are for standard double row outboard bearings. Duplex angular contact bearings normally will allow higher suction pressures.

Suction Pressure Ratings

0

40

Contact Engineering for more information.

MAXIMUM ALLOWABLE SUCTION PRESSURE – lbf / in2 120 160 200 240 280

80

2.4

3K8x6-14A

360

400

1K3x1.5-6 1K3x2-6 2K3x2-8 2K4x3-8 2K3x1.5-10A 2K3x2-10A 2K6x4-10H 2K4x3-13HH

1K3x1.5-8 2K4x3-10H

2.0 SPECIFIC GRAVITY

320

MARK 3 REVERSE VANE IMPELLER MAX. SUCTION PRESURE 1750 RPM

2K4x3-10 2K3x2-13 2K6x4-10

1.6

2K3x1.5-13 2K2x1-10A

1.2

1K1.5x1-6 1K1.5x1-8 2K6x4-13A 2K4x3-13

.8 SUCTION PRESSURE IS LIMITED ONLY BY THE PRESSURE TEMPERATURE RATINGS FOR ALL OPEN IMPELLER PUMP SIZES AT ALL SPECIFIC GRAVITIES AND FOR SEMI-OPEN IMPELLER PUMP SIZES 10x8-14, 8x6-16A, 10x8-16 AND 10x8-16H THROUGH 2.0 SPECIFIC GRAVITY. CONSULT DURCO SALES ENGINEERS FOR SPECIFIC GRAVITIES ABOVE 2.0.

.4

0

0

0

2.5

5

40

7.5 10 12.5 15 17.5 20 MAXIMUM ALLOWABLE SUCTION PRESSURE – Bar MAXIMUM ALLOWABLE SUCTION PRESSURE – lbf / in2 120 160 200 240 280

80

1K1.5x1-6 2K6x4-10 2K3x2-8

2.4

2K4x3-8 1K3x1.5-6

2.0

22.5

320

360

400

MARK 3 GROUP 1 & 2 REVERSE VANE IMPELLER MAX. SUCTION PRESSURE 3500 RPM

1K3x2-6 1K1.5x1-8

SPECIFIC GRAVITY

25

2K3x1.5-10A

1.6

1.2

2K2x1-10A

.8

2K4x3-13/110 2K4x3-10 2K3x2-13

1K3x1.5-8

.4 2K3x1.5-13

0

0

2.5

5

2K3x2-10A

FOR ALL OPEN IMPELLER PUMPS SUCTION PRESSURE IS LIMITED ONLY BY THE PRESSURE TEMPERATURE RATINGS.

7.5 10 12.5 15 17.5 20 MAXIMUM ALLOWABLE SUCTION PRESSURE – Bar

22.5

25

31

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Pump Division

Technical Data

Flowserve Durco Mark 3 General Technical Data

Pump Group

GP 1

GP 2

GP 3

Min. Max. Sphere Thru Imp. Casing Pump Thickness Rev. Vane Open Size mm (in) mm (in) mm (in) 1 3 1K1 / 2x1LF-4 10 ( / 8) N/A 9 (1/ 4) 1K11/ 2x1-6 10 (3/ 8) 10 (3/ 8) 10 (13/ 32) 1K3x11/ 2-6 10 (3/ 8) 11 (7/ 16) 11 (7/ 16) 1K3x2-6 10 (3/ 8) 11 (7/ 16) 10 (3/ 8) 1K11/ 2x1LF-8 10 (3/ 8) N/A 9 (1/ 4) 1K11/ 2x1-8 10 (3/ 8) 9 (11/ 32) 12 (15/ 32) 1K3x11/ 2-8 11 (7/ 16) 14 (9/ 16) 10 (13/ 32) 2K3x2-8 11 (7/ 16) 14 (17/ 32) 14 (9/ 16) 2K4x3-8 11 (7/ 16) 13 (1/ 2) 13 (1/ 2) 2K2x1LF-10 11 (7/ 16) N/A 21 (13/ 16) 2K2x1-10A 11 (7/ 16) 10 (13/ 32) 8 (5/ 16) 2K3x11/ 2-10A 11 (7/ 16) 12 (15/ 32) 12 (15/ 32) 2K3x2-10A 11 (7/ 16) 14 (17/ 32) 11 (7/ 16) 2K4x3-10 13 (1/ 2) 17 (21/ 32) 14 (9/ 16) 2K4x3-10H 13 (1/ 2) 20 (25/ 32) 18 (11/ 16) 2K6x4-10 13 (1/ 2) 18 (11/ 16) 16 (5/ 8) 2K6x4-10H 13 (1/ 2) 14 (9/ 16) 16 (5/ 8) 2K3x11/ 2LF-13 11 (7/ 16) N/A 8 (5/ 16) 2K3x11/ 2-13 11 (7/ 16) 15 (19/ 32) 10 (3/ 8) 2K3x2-13 11 (7/ 16) 10 (13/ 32) 10 (13/ 32) 2K4x3-13 11 (7/ 16) 18 (11/ 16 ) 18 (11/ 16) 2K4x3-13HH 11 (7/ 16) 18 (11/ 16) N/A 2K6x4-13A 11 (7/ 16) 26 (11/ 32) 25 (1) 3K8x6-14A 13 (1/ 2) 41 (15/ 8) 32 (11/ 4) 3K10x8-14 16 (5/ 8) 38 (11/ 2) 32 (11/ 4) 3K6x4-16 16 (5/ 8) 30 (13/ 16) 27 (11/ 16) 3K8x6-16A 14 (9/ 16) 32 (11/ 4) 32 (11/ 4) 3K10x8-16 14 (9/ 16) 40 (19/ 16) 32 (11/ 4) 3K10x8-16H 13 (1/ 2) 41 (15/ 8) 32 (11/ 4) 3K10x8-17 14 (9/ 16) 40 (19/ 16) N/A

Impeller Eye Area Coros. Allow. Rev.2 Vane Open cm (in2) cm2 (in2) mm (in) N/A 5 (0.80) 3 (1/ 8) 20 (3.1) 23 (3.6) 28 (4.4) 28 (4.4) 36 (5.6) 45 (7.0) N/A 15 (2.4) 20 (3.1) 24 (3.7) 36 (5.5) 34 (5.3) 44 (6.8) 45 (7.0) 3 (1/ 8) 80 (12.4) 77 (12) N/A 15 (2.4) 23 (3.5) 26 (4.1) 35 (5.5) 36 (5.6) 41 (6.4) 41 (6.4) 85 (13.2) 77 (12) 85 (13.2) 66 (10.3) 127 (19.6) 127 (19.6) 142 (22) 171 (26.5) N/A 32 (4.9) 48 (7.5) 39 (6.1) 48 (7.5) 51 (7.9) 98 (15.2) 81 (12.5) 98 (15.2) N/A 187 (29) 188 (29.1) 292 (45.3) 288 (44.7) 3 (1/ 8) 410 (63.6) 385 (59.6) 172 (26.7) 172 (26.7) 292 (45.3) 270 (41.8) 410 (63.6) 415 (64.4) 506 (78.5) 508 (78.7) 515 (71.8) N/A

Min. Temp. °C (°F) -29 (-20) to -212 (-350) with modif.

Max. Temp. Max. Temp. w/o with Cooling Cooling °C (°F) °C (°F) 260 (500) 260 (500) to 350 to 350 (700) (700) with with modif. modif.

-29 (-20) to -212 (-350) with modif.

175 (350)

260 (500) to 350 (700) with modif.

-29 (-20) to -212 (-350) with modif.

350 (175)

260 (500) to 350 (700) with modif.

Max. Allow. Horsepower 1150 kw (hp) 10 (13)

1750 kw (hp) 15 (20)

38 (50)

56 (75) 112 (150) 0.03 (0.001)

157 (210) 242 (325)

3500 kw (hp) 30 (40)

Max. Shaft End Play mm (in) 0.03 (0.001)



0.03 (0.001)

Bearing Size (SKF) (I.B.) 6207C3 (O.B.) 5306AC3

(I.B.) 6310C3 (O.B.) 5310AC3

(I.B.) 6314C3 (O.B.) 5314AC3

6x4-10 maximum 175 hp (130 kW) Mechanical Properties Material Designations Ductile Iron Carbon Steel CF-8 CF-3 CF-8M CF-3M Durcomet 100 Durimet 20 CY-40 M-35 Nickel Chlorimet 2 Chlorimet 3 DC-8 Titanium Titanium-Pd Zirconium

Symbol DCI DS D2 D2L D4 D4L CD4M D20 DINC DM DNI DC2 DC3 DC8 Ti Ti-Pd Zr

ACI Designation None None CF8 CF3 CF8M CF3M CD4MCuN CN7M CY40 M351 CZ100 N7M CW6M None None None None

Equivalent Wrought Designation None Carbon Steel 304 304L 316 316L Ferralium Alloy 20 Inconel 600 Monel 400 Nickel 200 Hastelloy B2 Hastelloy C-276 None Titanium Titanium-Pd Zirconium

ASTM Specifications* A395 A216 Gr. WCB A744 & A351, Gr. CF-8 A744 & A351, Gr. CF-3 A744 & A351, Gr. CF-8M A744 & A351, Gr. CF-3M A995, Gr. 1B A744 & A351, Gr. CN-7M A494, Gr. CY-40 A494, Gr. M-35-1 A494, Gr. CZ-100 A494, Gr. N-7M A494, Gr. CW-6M None B367, Gr. C-3 B367, Gr. C-8A B752, Gr. 702C or 705C

Min. Tensile Strength, MPa psi 414 60,000 483 70,000 483 70,000 483 70,000 483 70,000 483 70,000 690 100,000 428 62,000 483 70,000 448 65,000 345 50,000 525 76,000 497 72,000 448 448 380

65,000 65,000 55,000

Min. Yield Point MPa psi 276 40,000 248 36,000 207 30,000 207 30,000 207 30,000 207 30,000 483 70,000 172 25,000 193 28,000 172 25,000 124 18,000 276 40,000 276 40,000 380 380 276

*Whenever an ASTM specification is cited, the alloy will conform to the chemical and mechanical requirements of the latest edition of the specification.

32

55,000 55,000 40,000

Min. % Elongation 18 22 35 35 30 30 16 35 30 25 10 20 25 15 15 12

Nominal Hardness (Brinell) 143-187 150 150 150 154 154 224 133 147 130 118 180 180 300 200 200 190

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Pump Division

Technical Data

Flowserve Durco Mark 3 Minimum Flow & Fasteners

Flowserve Definition: Minimum continuous stable flow is the lowest flow at which the pump can operate and still conform to the bearing life, shaft deflection and bearing housing vibration limits of ASME B73.1-2001. Minimum continuous thermal flow is the lowest flow at which the pump can operate and still maintain the pumped liquid temperature below that which will have an adverse effect on the pump or seal performance, or on the quality of the pumped liquid.

Minimum Continuous Flow Dimension Designation AA AB AC AD AB A60 A70 A05 A50 A60 A70 A80 A20 A30 A40 A80 A90 A100 A105 A110 A120 A120

Pump Size 1.5x1-6 3x1.5-6 3x2-6 1.5x1-8 3x1.5-8 3x2-8 4x3-8 2x1-10 3x1.5-10 3x2-10 4x3-10 4x3-10H 6x4-10 6x4-10H 3x1.5-13 3x2-13 4x3-13 4x3-13HH 6x4-13 8x6-14 10x8-14 6x4-16 8x6-16 10x8-16 10x8-17

3500/2900 RPM 10% 10% 20% 10% 10% 20% 20% 10% 10% 30% 30% NA 40% NA 30% 40% 40% NA 60% NA NA NA NA NA NA

* In some cases, the 3K6x4-16 can be used at lower than 50% of BEP, by making an impeller modification.

MCF, % BEP 1750/1450 RPM 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 20% 10% 10% 20% 50% 40% 40% 40% 50% 50% 50% 50%

1180/960 RPM 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 10% 30% 10% 15% 10% 10% 10% 10% 10%

Contact Flowserve Engineering if there is a need to use this pump at a lower flow.

Flowserve Standards for Pressure Containing Fasteners Pump Alloy

Type of Fastener

New Alloy Code

Description

Alloy/Non-metallic

Casing Fastener

B7TF*

ASTM A193 Grade B7 (AISI 4140, 4142, 4145, 4140H, 4142H, or 4145H steel w/PTFE coating & Zinc rich primer)

Casing Nut

SRTF*

ASTM A194 Grade 2H (Carbon Steel w/PTFE coating & Zinc rich primer)

Gland Fastener

B81

ASTM A193 Grade B8 class 1 (304 stainless steel)

Gland Nut

E8

ASTM A194 Grade 8 (304 stainless steel)

Cover/Repeller Cover Fastener (Sealmatic)

B7TF*

same as above

High Silicon Iron (HSI)

Carbon Steel or Ductile Cast Iron (DS/DCI)

Mag Drive

HSI Pump Fasteners

In general, same materials as alloy pump fasteners listed above

Stuffing Box Yoke Fastener (HSI)

B81

same as above

Stuffing Box Yoke Nut (HSI)

E8

same as above

Casing Fastener

B7*

Casing Nut Gland Fastener Gland Nut Cover/Repeller Cover Fastener (Sealmatic)

SR2H* B81 E8 B7*

ASTM A193 Grade B7 (AISI 4140, 4142, 4145, 4140H, 4142H, OR 4145H steel) ASTM A194 Grade 2H (Carbon Steel) same as above same as above same as above

Shell/Holder Fastener Shell/Ring Fastener

B7TF* B7TF*

same as above same as above

* For temperatures < -29°C (-20°F), fastener alloy must be B8C2, which is ASTM A193 Grade B8 class 2 (304,

304N, 305, 321, 347 stainless steel). Nut alloy must be E8.

33

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Pump Division

Technical Data Pump Parts Group 1

Option for duplex angular contact bearings

34

ITEM

DESCRIPTION

100

CASING

103

IMPELLER

104

IMPELLER GASKET

105

SHAFT

106

REAR COVER PLATE

107

REAR COVER GASKET

108

BEARING HOUSING ADAPTER

109

BEARING HOUSING FOOT

109A

SHIM

110

GLAND - PACKING

111

STUD - GLAND

111A

HEXNUT - GLAND

112

PACKING SEAL CAGE HALVES

113

PACKING

OPT.

114

DEFLECTOR INBOARD

OPT.

115

STUD - CASING

115A

HEXNUT - CASING

118

OIL SEAL INBOARD

119

BEARING HOUSING

120

BEARING INBOARD

121

BEARING OUTBOARD

122

OIL SLINGER

124

LOCKNUT - BEARING

125

LOCKWASHER - BEARING

129

OIL SEAL OUTBOARD

130

KEY - SHAFT/COUPLING

131

O-RING - ADAPTER

133

TRICO OILER (Not Shown)

134

BEARING HOUSING DRAIN PLUG

135

BEARING HOUSING VENT PLUG

136

CAPSCREW - FOOT

139

CAPSCREW - BEARING HOUSING

140

CAPSCREW - COVER/ADAPTER

153

MECHANICAL SEAL

177

HOOK SLEEVE

190

GLAND - MECHANICAL SEAL

190G

GLAND GASKET

200

SIGHT GAGE - BEARING HOUSING

201

BEARING CARRIER

201A

SET SCREW - BEARING CARRIER

201B

O-RING - BEARING CARRIER

N/A

OPT.

OPT.

OPT.

N/A

N/A

OPT.

201C

BEARING CARRIER RETAINER

201D

CLAMP RING BEARING HOUSING

OPT.

201E

SOC-CAPSCREW CLAMP

OPT.

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Pump Division

Technical Data Pump Parts Group 2 and Group 3

Group 2 bearing retainer (201C) shown

ITEM

DESCRIPTION

100

CASING

103

IMPELLER

104

IMPELLER GASKET

105

SHAFT

106

REAR COVER PLATE

107

REAR COVER GASKET

108

BEARING HOUSING ADAPTER

109

BEARING HOUSING FOOT

109A

SHIM

110

GLAND - PACKING

111

STUD - GLAND

111A

HEXNUT - GLAND

112

PACKING SEAL CAGE HALVES

113

PACKING

OPT.

114

DEFLECTOR INBOARD

OPT.

115

STUD - CASING

115A

HEXNUT - CASING

118

OIL SEAL INBOARD

119

BEARING HOUSING

OPT.

120

BEARING INBOARD

121

BEARING OUTBOARD

122

OIL SLINGER

124

LOCKNUT - BEARING

125

LOCKWASHER - BEARING

129

OIL SEAL OUTBOARD

130

KEY - SHAFT/COUPLING

131

O-RING - ADAPTER

133

TRICO OILER (Not Shown)

134

BEARING HOUSING DRAIN PLUG

135

BEARING HOUSING VENT PLUG

136

CAPSCREW - FOOT

139

CAPSCREW - BEARING HOUSING

140

CAPSCREW - COVER/ADAPTER

153

MECHANICAL SEAL

177

HOOK SLEEVE

190

GLAND - MECHANICAL SEAL

190G

GLAND GASKET

200

SIGHT GAGE - BEARING HOUSING

OPT.

OPT.

OPT.

201

BEARING CARRIER

201A

SET SCREW - BEARING CARRIER

201B

O-RING - BEARING CARRIER

201C

BEARING CARRIER RETAINER

201D

CLAMP RING BEARING HOUSING*

201E

SOC-CAPSCREW CLAMP*

*OPTIONAL GROUP 2

Option for duplex angular contact bearings

35

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Technical Data Pump and Baseplate Dimensions

Pump Dimensions Pump ANSI Group Desig.

GP 1 1K

AA AB AC AA A60 A70

GP 2 2K

A05 A50 A60 A70 A70 A80 A80 A20 A30 A40 A40 A80 A90 A100

GP 3 3K

A110 A120 A120

Size Suction X Discharge Max. Imp. Dia. 1K11/2 x1LF-4 1K11/2 x1-6 1K3x11/2-6 1K3x2-6 1K11/2 x1LF-8 1K11/2 x1-8 1K3x11/2-8 2K3x2-8 2K4x3-8 2K2x1LF-10 2K2x1-10A 2K3x11/2-10A 2K3x2-10A 2K4x3-10 2K4x3-10H 2K6x4-10 2K6x4-10H 2K3x11/ 2LF-13 2K3x11/ 2-13 2K3x2-13 2K4x3-13 2K4x3-13HH 2K6x4-13A 3K8x6-14A 3K10x8-14 3K6x4-16 3K8x6-16A 3K10x8-16 3K10x8-16H 3K10x8-17

Pump Weight X kg (lb) mm (in) 47 (103) 165 (6 1/2) 44 (97) 51 (112) 53 (116) 47 (103) 47 (103) 56 (124) 190.5 (71/2) 90 (200) 242 (9 1/2) 103 (227) 280 (11) 95 (210) 216 (8 1/2) 95 (210) 216 (8 1/2) 100 (220) 216 (8 1/2) 103 (226) 242 (9 1/2) 101 (225) 280 (11) 112 (249) 318 (12 1/2) 130 (290) 343 (131/2) 149 (328) 343 (131/2) 112 (250) 266 (10 1/2) 112 (250) 266 (10 1/2) 116 (258) 292 (111/2) 126 (281) 318 (12 1/2) 126 (281) 318 (12 1/2) 145 (324) 343 (131/2) 306 (680) 406 (16) 408 (899) 457 (18) 291 (641) 406 (16) 377 (832) 457 (18) 416 (917) 483 (19) 450 (992) 483 (19) 379 (835) 508 (20)

U O D mm (in) mm (in) 298 (113/4) 133 (51/4)

E1 mm (in) 76 (3)

E2 mm (in) 0

CP F mm (in) mm (in) 445 (171/2) 184 (7 1/4)

H mm (in) 16 (5/ 8)

Dia. mm (in) 22.23 (7/ 8)

Keyway mm (in) 4.76 x 2.38 (3/ 16 x 3/ 32)

V Min. mm (in) 56 (2 3/ 16) 51 (2)

Y mm (in) 102 (4)

56 (2 3/ 16) 51 (2) 368 (141/2) 177.8 (7) 450 (17 3/4) 210 (81/4) 124 (4 7/ 8) 92 (3 5/ 8) 597 (231/2) 318 (12 1/2) 490 (191/4) 425 (16 3/4) 425 (16 3/4) 425 (16 3/4) 450 (173/4) 490 (19 1/4) 572 (22 1/2) 254 (10) 597 (231/2) 597 (231/ 2) 520 (201/2) 520 (201/2) 546 (211/2) 572 (22 1/2) 572 (22 1/2) 597 (23 1/2) 775 (30 1/2) 368 (141/2) 203.2 (8) 114.3 (41/2) 860 (33 7/ 8) 476 (18 3/4) 826 (32 1/2) 775 (30 1/2) 826 (32 1/2) 851 (33 1/2) 851 (33 1/2) 876 (34 1/2)

16 (5/ 8)

28.58 (11/ 8)

6.35x3.18 (1/ 4 x 1/ 8)

67 (2 5/ 8)

102 (4)

70 (2 3/ 4) 67 (2 5/ 8)

22 (7/ 8)

38.1 (11/ 2) (28.58) (11/ 8)

9.5x4.76 (3/ 8 x 3/ 16) (6.35x3.18) (1/ 4 x1/ 8)

60.33 (2 3/ 8)

15.88x7.94 ( 5/ 8 x 5/ 16)

70 (2 3/ 4) 67 (2 5/ 8)

102 (4)

152 (6)

Baseplate Mounting Dimensions Pump Group

Max. Motor Baseplate Frame 139 148

GP 1 1K

GP 2 2K

GP 3 3K

36

153 245 252 258 264 268 280 368 380 398

184T 215T 256T 286T 326TS 184T 215T 286T 326T 365T 405TS 449TS 286T 405T 449T

Weight kg (lb) 50 (111) 74 (163)

HA mm (in) Metal Poly. 381 (15) 330 (13) 457 (18)

406 (16)

HB mm (in) 991 (39) 1219 (48)

96 (212)

533 (21)

483 (19)

1346 (53)

59 (129) 80 (177) 106 (234)

381 (15) 457 (18) 533 (21)

330 (13) 406 (16) 483 (19)

1143 (45) 1321 (52) 1473 (58)

149 (328)

559 (22)

559 (22)

1626 (64)

186 (409) 218 (481) 213 (470) 273 (601) 338 (746)

660 (26)

660 (26)

*HD1▲ mm (in) Metal Poly. 229 (9) 226 (87/ 8) 241 (91/ 2) 238 (9 3/ 8) 267 (101/ 2) 264 (10 3/ 8) 302 (117/ 8) 283 (111/ 8) 327 (12 7/ 8) 308 (121/ 8) 305 (12) 302 (117/ 8) 319 (12 3/ 8) 312 (121/ 4) 330 (13) 312 (121/ 4) 330 (13) 312 (121/ 4) 352 (13 7/ 8) 334 (131/ 8) 378 (147/ 8) 365 (143/ 8) 403 (15 7/ 8) 391 (153/ 8)

1727 (68) 2032 (80) 1727 (68) 2032 (80) 489 (191/ 4) 2489 (98)

*GP 1 – HD2 applies to 3x11/ 2-8 only. ▲ Includes spacer under pump, as necessary. GP 2 – HD1 applies to 3x2-8, 4x3-8, 2x1-10A, 3x11/ 2-10A, 3x2-10A, and 4x3-10. HD2 applies to 4x3-10H, 6x4-10, 6x4-10H, 3x11/ 2-13, 3x2-13, 4x3-13, 4x3-13HH, and 6x4-13A. GP 3 – HD1 applies to all GP3 sizes.

483 (19)

*HD2▲ mm (in) Metal Poly. 273 (10 3/ 4) 269 (10 5/ 8) 283

(111/ 8)

280 (11)

302 (117/ 8) 283 (111/ 8) 327 (12 7/ 8) 308 (121/ 8) 349 (13 3/ 4) 346 (13 5/ 8) 359 (141/ 8) 355 (14) 375 (14 3/ 4) 355 (14) 375 (14 3/ 4) (14 7/ 8)

378 403 (15 7/ 8)

355 (14) 365 (143/ 8) 391 (153/ 8)

HE mm (in)

HF mm (in)

114 (41/ 2)

927 (361/ 2)

**HG mm (in) HH mm (in) Metal Poly. 95 (3 3/ 4) 92 (3 5/ 8)

1156 (451/ 2) 105 (41/ 8)

102 (4)

191 (71/ 2) 1283 (501/ 2) 121 (4 3/ 4)

102 (4)

114 (41/ 2) 1080 (421/ 2) 95 (3 3/ 4) 152 (6) 1257 (491/ 2) 105 (41/ 8) 1410 (551/ 2) 191 (71/ 2) 1562 (611/ 2) 121 (4 3/ 4) 1664 (651/ 2) 1969 (771/ 2) 241 (91/ 2) 1664 (651/ 2) 308 (121/ 8) 1969 (771/ 2) 232 (91/ 8) 2426 (951/ 2) 206 (81/ 8)

92 (3 5/ 8) 102 (4) 102 (4)

152 (6)

102 (4) 108 (41/ 4) 108 (41/ 4) 108 (41/ 4) 108 (41/ 4) 108 (41/ 4)

** “HG” Dimensions applied to the lower pad height. With some bases this will occur at pump end and with others at motor end.

19 (3/ 4)

25 (1)

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Pump Division

Technical Data

Alloy Materials

Flowserve foundries are widely regarded as among the best in the world pouring alloys from common austenitic stainless steels to light reactive alloys such as titanium. All Flowserve Durco wet end castings carry a limited lifetime guarantee. Attesting to the world class quality of its castings, Flowserve was the first high alloy foundry in the United States of America to have earned approval by Germany’s Technischer Überwachungs Verein (TUV).

Alloy Materials

Designation

Symbol

ACI Designation

Ductile Iron Carbon Steel CF-8M Durcomet 100 Durimet 20 Durcomet 5 CY-40 M-35 Nickel Chlorimet 2 Chlorimet 3 Duriron® Durichlor 51® Superchlor® DC-8 Titanium Titanium-Pd Zirconium

DCI DS D4 CD4M D20 DV DINC DM DNI DC2 DC3 D D51 SD77 DC8 Ti Ti-Pd Zr

None None CF8M CD4MCuN CN7M None CY40 M351 CZ100 N7M CW6M None None None None None None None

Equivalent Wrought Designation

ASTM Specifications*

None Carbon Steel 316 Ferralium® 255 Alloy 20 None Inconel® 600 Monel® 400 Nickel 200 Hastelloy® B-2 Hastelloy® C-276 None None None None Titanium Titanium-Pd Zirconium

A395 A216 Gr. WCB A744, Gr. CF-8M A995, Gr. 1B A744, Gr. CN-7M None A494, Gr. CY-40 A494, Gr. M-35-1 A494, Gr. CZ-100 A494, Gr. N-7M A494, Gr. CW-6M A518, Gr. 1 A518, Gr. 2 None None B367, Gr. C-3 B367, Gr. C-8A B752, Gr. 702C

*Alloys conform to the chemical and mechanical requirements of the latest edition of the ASTM specification. ® Duriron, Durichlor 51 and Superchlor are registered trademarks of Flowserve Corporation. ® Ferralium is a registered trademark of Langley Alloys. ® Hastelloy is a registered trademark of Haynes International, Inc. ® Inconel and Monel are registered trademarks of International Nickel Co. Inc.

37

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Pump Division

Technical Data

Flowserve Durco Mark 3 How To Specify Process Pumps

Flowserve Suggests the Following Specifications When Purchasing ANSI Pumps: Design: Shall be of a horizontal, end suction, single stage, centerline discharge, “back pull-out” construction, meeting the design criteria of the ASME B73.1-2001 standard. General: All wetted parts shall be permanently marked with the material of construction. Cast parts shall have a conditional lifetime casting guarantee. Stainless steel parts shall be cast to the ASME A744 standard. Casing: Shall have a fully machined wet face and shall be capable of being foot or centerline mounted. Flange finishes shall conform to ASME/ANSI B16.5 and shall be available in DIN/PN16 or 40 (150 or 300 Class), flat or raised faces. Casing and rear cover plate shall have 3 mm (1/8 in) corrosion allowance.

38

Impeller: Shall be the reverse vane design, and shall be open on the back and shrouded on the front. The impeller clearance shall be set against the rear cover, not the casing, allowing all settings to be done in the maintenance shop, without the casing. The impeller shall maintain low seal chamber pressures, which shall be published on the pump performance curve, and shall be repeatable after maintenance. The impeller clearance shall be set externally. The impeller-toshaft connection shall be a metal-to-metal fit. A silicon O-ring encapsulated in PTFE shall be used to protect the impeller threads. Impeller shall be balanced to ISO 1940 Grade 6.3 criteria. Shaft: Shall be of solid construction to maximize strength and rigidity. The shaft shall consist of a steel power end friction welded to an alloy wet end. Shaft deflection shall not exceed 0.05 mm (0.002 in). The shaft key slot shall be designed with a machined radius “sled runner” edge to provide maximum strength at the coupling. Critical surfaces shall be ground to 0.005 mm (±0.0002 in), maximum roughness at the seal chamber shall be 0.40 µm (16 µin). Rear Cover: Shall be suitable for accepting various seal designs from all major seal manufacturers. Cylindrical bore standard, cylindrical bore oversize, and tapered options shall be available. Tapered options shall include eight evenly spaced, tapered and sloped flow modifying devices integrally cast into the seal chamber. The flow modifiers shall facilitate movement of solids, vapors, and heat away from the mechanical seal. The tapered seal chambers shall be designed

to be self-flushing. For optimum performance the seal and gland shall be selected to locate the seal faces directly in the flush path. Integrally cast jackets shall be available. Bearings: Shall be large, heavyduty, ball bearings. The inboard bearing shall be a single row, deep groove. The outboard shall be double row angular contact, deep groove. An optional duplex angular contact outboard bearing shall be available for high thrust load applications. Both bearings shall be located by a shoulder on the shaft. The inboard bearing shall float in the bearing housing, while the outboard bearing shall be locked in place in the bearing carrier. The bearings shall exceed B10 life of 17,500 hours and allow less than 0.025 mm (0.001 in) end play. Bearing Housing: Shall be sealed to prevent contamination of the lubricant. The oil fill hole at the top of the housing shall be plugged. No vented constant level oiler shall be used. The housing shall be sealed with Inpro VBXX bearing isolators. A magnetic drain plug shall be used. A large easy to read one inch NPT sight glass shall be used. The impeller clearance shall be set by the micrometer

adjustment method. This method shall cause the shaft and impeller to move axially. Indicators shall be cast into the bearing carrier which represent 0.102 mm (0.004 in) of axial impeller travel. This allows accurate impeller clearance to be established externally without the use of measurement devices. The bearing carrier threads shall be protected by two O-rings. Coupling Guard: Shall conform to ASME B15.1 and shall be of the “clamshell” design. It shall extend from the motor to the bearing housing, but shall not be attached to either. The guard shall be bolted to the baseplate. Baseplate: Shall be of a reinforced rigid design and shall conform to the dimension requirements of ASME B73.1-2001.

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Pump Division

Mark 3 Sealmatic

Flowserve Durco Mark 3 Sealmatic

Dynamically sealing repeller eliminates the need for conventional mechanical seals. Advanced static seal options are available. Dimensionally interchangeable with all ANSI pumps.

Dynamically Sealing Repeller

The Sealmatic Principle This pump does not leak while running because the Sealmatic design utilizes a repeller, a dynamic sealing device, to evacuate liquid from the seal chamber. This is accomplished by creation of a liquid interface seal in the repeller chamber that prevents leakage along the shaft during operation. For sealing while the pump is stopped, three types of sealing arrangements are offered for maximum application flexibility: Checkmatic end face lip seal arrangement; dry-running end face seal designs; and the packed stuffing box design.

Applications • Tough sealing applications where a flush is impractical • Evaporator service • Continuously running pumps

This family of repellers allows the Sealmatic to be used in applications having a wide range of suction pressures. Hydraulic performance conforms to the Standard Mark 3 reverse vane impeller curves.

A choice of sealing arrangements

Repeller chamber Repeller Liquid/air interface

The Sealmatic design is also available with unitized selfpriming and recessed impeller pumps. Stopped

Running 39

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Pump Division

Mark 3 Sealmatic Sealmatic Performance Curves

0 m

20

40

ft 0 900

60

FLOW – 50 Hz (2900 RPM) 100 120 140 160 180

80

200

400

600

200

800

220

240

260 m3/h ft

1000 gpm

800

240

500 700

150

600

400

3X1.5M-13

160 500 100

4X3M-13

300

400

120

TDH – 50 Hz (2900 RPM)

3X2M-13

200 TDH – 60 Hz (3500 RPM)

m

600

3X1.5M-10A 6X4M-10

2X1M-10A

300

200

3X2M-10A

80

50

4X3M-10

200

100

40 100

0

0

0

200

0

0 m

80

40

50

ft 0 300

400

600

80

120

1000

160 200 FLOW – 60 Hz (3500 RPM)

400

600

800

0 0 1400 gpm

1200

240

280 m3/h

FLOW – 50 Hz (1450 RPM) 150 190 500

100

200

800

800

2300

1100

3800

5300

1400 m3/h 6800 gpm ft 200

m 60

250

SCALE

8X6M-16A

40 10X8M-16

150

6X4M-13A

3X2M-13

3X1.5M-13

30

4X3M-13

100

8X6M-14A

6X4M-10H

20

6X4M-10

20

0

2X1M-10A

0 0

50

10X8M-16H

4X3M-10H

3X2M-10A

50

0

100 10X8M-14

40

3X1.5M-10A

40

150

10 4X3M-10

200 50

400 100

600

800 150

1000

200 227 400 FLOW – 1750 RPM (60 Hz)

2800

4600 800

6400 1200

0 8200 gpm 1600 m3/h

0

TDH – 50 Hz (1450 RPM)

TDH – 60 Hz (1750 RPM)

60

200

CHANGE

50 6X4M-16

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Pump Division

Mark 3 Sealmatic Sealmatic Shaft Seal Designs

Checkmatic® Seal Design • Individual elastomeric lip seals run in light contact against the radial faces of a standard mechanical seal seat • Lip seals turn with the shaft so the seat, not the shaft or sleeve, is the wear part • PFA encapsulated silicon rubber O-rings help secure the lip seals to the shaft • Lip seals available in Viton1, EPDM and Fluoraz2

Dry-Running End Face Seal Design • State-of-the-art technology utilizing various seals such as the John Crane 28LD seal designed to run completely dry • Positive sealing during shutdown • Easy installation • Also available in double cartridge design, typically used with a nitrogen barrier

Packed Stuffing Box Design • Self-lubricating, flexible graphite packing • Simple, trouble-free design • Recommended use of DC8 shafts or DC8 sleeves for abrasion and corrosion resistance

1 Registered trademark of E.I. duPont Company 2 Registered trademark of Green, Tweed and Company

41

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Pump Division

Mark 3 Sealmatic Sealmatic Dimensions

Pump Dimensions Suction Discharge Pump Size Size Weight X O D E1 E2 CP F Pump mm (in) mm (in) kg (lb) mm (in) mm (in) mm (in) mm (in) mm (in) mm (in) mm (in) 1 3 1 7 5 1 2K2x1M-10A 50 (2) 25 (1) 94 (210) 216 (8 / 2) 425 (16 / 4) 210 (8 / 4) 124 (4 / 8) 92 (3 / 8) 597 (23 / 2) 318 (12 1/ 2) 2K3x11/ 2M-10A 76 (3) 38 (11/ 2) 100 (220) 216 (8 1/ 2) 425 (16 3/ 4) 2K3x2M-10A 76 (3) 50 (2) 103 (226) 242 (9 1/ 2) 450 (173/ 4) 2K4x3M-10 102 (4) 76 (3) 101 (225) 280 (11) 490 (19 1/ 4) 2K4x3M-10H 102 (4) 76 (3) 112 (249) 318 (12 1/ 2) 572 (22 1/ 2) 254 (10) 2K6x4M-10 152 (6) 102 (4) 130 (290) 343 (131/ 2) 597 (231/ 2) 2K6x4M-10H 152 (6) 102 (4) 149 (328) 343 (131/ 2) 597 (231/ 2) 2K3x11/ 2M-13 76 (3) 38 (11/ 2) 112 (250) 266 (10 1/ 2) 520 (201/ 2) 2K3x2M-13 76 (3) 50 (2) 116 (258) 292 (111/ 2) 546 (211/ 2) 2K4x3M-13 102 (4) 76 (3) 126 (281) 318 (12 1/ 2) 572 (22 1/ 2) 2K6x4M-13A 152 (6) 102 (4) 145 (324) 343 (131/ 2) 597 (23 1/ 2) 3K8x6M-14A 203 (8) 152 (6) 306 (680) 406 (16) 775 (30 1/ 2) 368 (141/ 2) 203.2 (8) 114.3 (41/ 2) 860 (33 7/ 8) 476 (18 3/ 4) 3K10x8M-14 254 (10) 203 (8) 408 (899) 457 (18) 826 (32 1/ 2) 3K6x4M-16 152 (6) 102 (4) 291 (641) 406 (16) 775 (30 1/ 2) 3K8x6M-16A 203 (8) 152 (6) 377 (832) 457 (18) 826 (32 1/ 2) 3K10x8M-16 254 (10) 203 (8) 416 (917) 483 (19) 851 (33 1/ 2) 3K10x8M-16H 254 (10) 203 (8) 450 (992) 483 (19) 851 (33 1/ 2)

U H mm (in) 16 (5/ 8)

22 (7/ 8)

Dia. mm (in) 28.58 (11/ 8)

Keyway mm (in) 6.35x3.18 (1/4 x 1/ 8)

38.1 (11/ 2) 28.58 (11/ 8)

9.5x4.76 (3/ 8 x 3/ 16) 6.35x3.18 (1/ 4x1/ 8)

60.33 (2 3/ 8)

15.88x7.94 (5/ 8 x 5/ 16)

V Min. mm (in) 67 (2 5/ 8)

Y mm (in) 102 (4)

102 (4)

152 (6)

Baseplate Mounting Dimensions Pump Group

GP 2 2K

GP 3 3K

Max. Motor Baseplate Frame 245 252 258 264 268 280 368 380 398

184T 215T 286T 326T 365T 405TS 449TS 286T 405T 449T

59 (129) 80 (177) 106 (234)

HA mm (in) Metal Poly. 381 (15) 330 (13) 457 (18) 406 (16) 533 (21) 483 (19)

1143 (45) 1321 (52) 1473 (58)

149 (328)

559 (22)

1626 (64)

Weight kg (lb)

186 (409) 218 (481) 213 (470) 273 (601) 338 (746)

660 (26)

559 (22)

26 (660)

HB mm (in)

HD1 mm (in) Metal Poly. 305 (12) 302 (117/8) 314 (12 3/8) 312 (121/4) 330 (13) 312 (121/4) 330 (13) 312 (121/ 4) 352 (13 7/8) 333 (131/8) 378 (147/8) 365 (143/8) 403 (15 7/8) 391 (153/8)

1727 (68) 2032 (80) 1727 (68) 2032 (80) 489 (191/4) 2489 (98)

19 (483)

HD1 for the following pumps: 2x1M-10A, 3x11/ 2M-10A, 3x2M-10A, 4x3M-10 HD2 for the following pumps: 4x3M-10H, 6x4M-10, 6x4M-10H, 3x11/ 2M-13, 3x2M-13, 4x3M-13, 6x4M-13A

42

HD2 mm (in) Metal Poly. 349 (13 3/4) 346 (13 5/8) 359 (141/8) 355 (14) 375 (14 3/4) 355 (14) 375 (14 3/4) (14 7/8)

378 403 (15 7/8)

355 (14) 365 (143/8) 391 (153/8)

*HG mm (in) HH mm (in) Metal Poly. 114 (41/ 2) 1080 (421/ 2) 95 (3 3/4) 92 (3 5/8) 19 (3/4) 152 (6) 1257 (491/ 2) 105 (41/ 8) 102 (4) 19 (3/4) 1410 (551/ 2) 102 (4) 191 (71/ 2) 102 (4) 1562 (611/ 2) 121 (4 3/4) 1 1664 (65 / 2) 108 (41/4) 25 (1) 1969 (771/ 2) 108 (41/4) 241 (91/ 2) 1664 (651/ 2) 308 (121/8) 108 (41/4) 1969 (771/ 2) 232 (91/8) 108 (41/4) 2426 (951/ 2) 206 (81/8) 108 (41/4) HE mm (in)

HF mm (in)

* “HG” Dimensions applied to the upper pad height. With some bases this will occur at pump end and with others at motor end.

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Pump Division

Mark 3 Sealmatic Sealmatic Parts Group 2 and Group 3

Group 2 bearing retainer (201C) shown

Group 3 double row bearing retainer

ITEM

DESCRIPTION

100

CASING

103

IMPELLER

104

IMPELLER GASKET

105

SHAFT

106

REAR COVER PLATE

107

REAR COVER GASKET

108

BEARING HOUSING ADAPTER

109

BEARING HOUSING FOOT

109A

SHIM

110

GLAND - PACKING

111

STUD - GLAND

111A

HEXNUT - GLAND

112

PACKING SEAL CAGE HALVES

113

PACKING

OPT.

114

DEFLECTOR INBOARD

OPT.

115

STUD - CASING

115A

HEXNUT - CASING

118

OIL SEAL INBOARD

119

BEARING HOUSING

OPT.

120

BEARING INBOARD

121

BEARING OUTBOARD

122

OIL SLINGER

124

LOCKNUT - BEARING

125

LOCKWASHER - BEARING

129

OIL SEAL OUTBOARD

130

KEY - SHAFT/COUPLING

131

O-RING - ADAPTER

133

TRICO OILER (Not Shown)

134

BEARING HOUSING DRAIN PLUG

135

BEARING HOUSING VENT PLUG

136

CAPSCREW - FOOT

139

CAPSCREW - BEARING HOUSING

140

CAPSCREW - COVER/ADAPTER

153

MECHANICAL SEAL

177

HOOK SLEEVE

180

COVER - REPELLER

181

REPELLER

OPT.

OPT.

OPT.

190

GLAND - MECHANICAL SEAL

190G

GLAND GASKET

200

SIGHT GAGE - BEARING HOUSING

201

BEARING CARRIER

201A

SET SCREW - BEARING CARRIER

201B

O-RING - BEARING CARRIER

201C

BEARING CARRIER RETAINER

201D

CLAMP RING BEARING HOUSING*

201E

SOC-CAPSCREW CLAMP*

330

MECHANICAL SEAL

*OPTIONAL GROUP 2

43

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Pump Division

Mark 3 Self-Priming

Unitized Self-Priming

Costs less to buy, install and service than submersible pumps. Utilizes the same power end, shaft, seal chamber and impeller as the Standard ANSI Pump. Only the casing is special.

Applications • Sump service • Tank car unloading • Duplex pumping lift stations • Flyash pond transfer • Waste acid transfer • Waste treatment lagoon service





44

Priming Cycle Cutaway Illustrations 1. Sump Filling, Pump Stopped The casing is shown with the initial prime liquid, which permanently stays in the casing. This serves as the priming liquid necessary to entrain the air contained in the suction line. 2. Pump Start-Up As the impeller spins, the priming liquid entrains air from the suction pipe and is pumped into the air separator/priming tank portion of the casing. In this chamber the air separates from the priming liquid and vents out the discharge while the priming liquid flows through the bypass slot in the bottom of the casing and back into the impeller eye.

As the priming liquid circulates, it re-entrains more air, creating a partial vacuum in the suction line. The sump liquid is then pushed upward by atmospheric pressure. 3. Priming Achievement After the priming cycle has evacuated all of the air from the suction pipe, the sump liquid floods the volute, air separator and priming chamber, and pumping out of the discharge pipe begins. The Unitized Self-Priming is fully primed and now operates exactly as a standard flooded-suction Flowserve Durco pump. 4. Sump Empty, Pump Stopped When the pump stops, the liquid in the discharge piping flows back through the pump, leaving the priming chamber filled with sufficient liquid for the next priming cycle. Except for the first fill-up of the priming chamber and an occasional “topping off” in dry climates, the Flowserve Durco Unitized Self-Priming is automatic and trouble-free.





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Pump Division

Mark 3 Self-Priming Unitized Self-Priming Performance Curves

60 Cycle CAPACITY CUBIC METERS PER HOUR T.D.H IN FEET

0

20

40

60

80

CAPACITY CUBIC METERS PER HOUR

100

440

120

140

160

T.D.H IN METERS

FLOWSERVE DURCO MARK 3 UNITIZED SELF-PRIMING 3500 RPM PUMPS

400

0

20

40

60

80

100

140

120

320

180

260

220

300

60

SCALE CHANGE

180 160

100

T.D.H IN METERS

FLOWSERVE DURCO MARK 3 UNITIZED SELF-PRIMING 1750 RPM PUMPS

200

360

280

T.D.H IN FEET

50

140

2 X 1.5US-10A

80

240 200

40

120

3 X 2US-10

3 X 2US-13

6 X 4US-13A

100 4 X 3US-13

60

1.5 X 1.5US-82

30

80

160 40

120

60

1.5 X 1 US-6

80

2 X 1.5 US-10A

4 X 3US-10H

40 1.5X1.5 US-82

20

20

3 X 2US-10

10

20

40 0 80

0

160

240

320

400

480

0

0

560

1.5 X 1US-6/60

100

0

200

300

400

600

800

1000

0

1200

CAPACITY US GALLONS PER MINUTE

CAPACITY US GALLONS PER MINUTE

CAPACITY CUBIC METERS PER HOUR T.D.H IN FEET

0

20

40

60

80

100

120

140

160

200

180

T.D.H IN METERS

FLOWSERVE DURCO MARK 3 UNITIZED SELF-PRIMING 1150 RPM PUMPS

100

30

90 80

25

70 60

20

4 X 3US-13 6 X 4US-13A

50

3 X 2US-13

15 40 3X

30

4 X 3US-10H 2U S-

20

10

10

5 10 2 X 1.5US-10A

0 100

0

200

300

400

500

600

0

800

700

CAPACITY US GALLONS PER MINUTE

50 Cycle CAPACITY US GALLONS PER MINUTE T.D.H IN METERS

0

100

200

300

CAPACITY US GALLONS PER MINUTE

400

T.D.H IN FEET

T.D.H IN METERS

0

100

200

300

400

500

600

FLOWSERVE DURCO MARK 3 UNITIZED SELF-PRIMING 2900 RPM PUMPS

800

1200

T.D.H IN FEET

FLOWSERVE DURCO MARK 3 UNITIZED SELF-PRIMING 1450 RPM PUMPS

SCALE CHANGE

350

50

100

160

300

140 40

80

250

60

200

2 X 1.5US-10A

150

1.5 X 1U

10

S-6

10

3X

2US

60

4 X 2US-10H

- 10

40

50

0 0

4 X 3US-13

2X1.5 US-10A

100

80

6 X 4US-13A

20

1.5 X 1.5US-82

20

100

30 3 X 2US-13

3 X 2US-10

40

120

20

30

40

50

60

70

80

CAPACITY CUBIC METERS PER HOUR

90

100

0

20 1.5 X 1.5US-82

0 0

20

40

60

80

100

120

140

200

250

300

0

CAPACITY CUBIC METERS PER HOUR

45

Pump Division

Flowserve Durco Mark 3 ANSI MarkProcess 3 Self-Priming Pumps

mm (6

0.066

150

VOLUME, m3

0.082

LENGTH OF PIPE, ft 40 50 60 70

80

90

100 7000 6000

PE

D

m

80

0.049

PI

(3

in)

ST

5000 4000

m

2

m(

50 m

0.033

TD in) S

40 mm

E

PIP

3000

E

PIP ) STD

(1.5 in

2000

0.016 0

1000 0

3

6

9

12 15 18 21 LENGTH OF PIPE, m

Graph A

gravities lower than 1.0, use 1.0 in the equation. The practical limit of a self-priming pump is 6.1 m (20 ft), divide this amount by specific gravity to determine the actual lift limit. For example: 6.1 m (20 ft) ÷ 1.4 = 4.4 m (14.3 ft) maximum possible lift. Suction Pipe Size The self-priming pump primes by evacuating the air in the suction piping. The priming time curves are based on the volume of air contained in a pipe length equal to the actual static lift shown plus that contained in 1 m (3 ft) of horizontal run into the pump. The pump example lifting liquid 3 m (10 ft) and horizontally 1 m (3 ft) contains 0.0188 m3 (1150 in3) of air in the suction

Specific Gravity As specific gravity increases, priming times also increase. For example: A pump previously lifting 3 m (10 ft) of water (1.0 sp.Gr.) is now pumping a liquid with a specific gravity of 1.4. The 3 m (10 ft) actual lift x 1.4 sp.gr. becomes an effective lift of 4.3 m (14 ft), for a priming time of 26 seconds. To be conservative for specific

Graph C S = Minimum Submergence, ft

2

4

6

8

10

12

14

16

293

16

220

12

146

8

73

4 0.6

1.2

1.8

2.4

3.0

3.6

S = Minimum Submergence, m

4.2

4.8

Suction Pipe Velocity, f/s

0

24

27

30

0

Graph B

Static Suction Lift The higher the lift, the greater the amount of air in the suction pipe to evacuate and the longer the priming time. Example illustrated: A 3x2US-13 pump with a 330 mm (13 in) impeller lifting water 3 m (10 ft) would take 18 seconds (Graph A). A lift of 4.6 m (15 ft) would take 30 seconds.

Suction Pipe Velocity, m/s

Individual pump curves found in Bulletin P-12-102 contain graphs of both hydraulic performance and priming time. Once a pump has been selected based on speed, efficiency, flow and head, priming times may be determined from these graphs. As pump performance varies with RPM and impeller diameter, priming times also change. Factors such as static suction lift distance, specific gravity and suction pipe size also have a direct bearing upon priming times.

VOLUME, in3

0.098

30

IPE

in) S TD P IPE

0.115

20

TD P

10

(4 in) S

0

10 0m m

Unitized Self-Priming Technical Data

pipe (Graph B). Extending the pipe’s horizontal run to 2.7 m (9 ft) gives an additional 0.0090 m3 (530 in3) of air to evacuate before achieving prime. 1680 1150 x 18 sec = 26 seconds, or 8 seconds longer priming time.

When a self-priming pump primes, a significant volume of air is evacuated from the suction line. A selfpriming pump will not work unless there is a way for the air to be vented. Flowserve suggests that a vent line be run from the discharge as shown on the diagram to the above. 46

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Pump Division

Mark 3 Self-Priming Unitized Self-Priming Dimensions

Pump Dimensions Pump Weight Pump kg (lb) 54 (120) 1J11/ 2x1US-6 1K11/ 2x11/ 2US-8 70 (154) 2K2x11/ 2US-10A 145 (320) 2K3x2US-10 154 (340) 2K3x2US-13 191 (420) 2K4x3US-10H 195 (430) 2K4x3US-13 236 (520) 2K6x4US-13A 286 (630)

U X mm (in) 121 (43/ 4) 98 (3 7/ 8) 152 (6) 165 (61/ 2) 203 (8) 191 (71/ 2) 216 (81/ 2) 254 (10)

O CP mm (in) mm (in) 1 318 (12 / 2) 511 (201/ 8) 378 (147/ 8) 521 (201/ 2) 464 (181/ 4) 725 (28 9/ 16) 476 (18 3/ 4) 559 (22) 725 (28 9/ 16) 572 (221/ 2) 776 (30 9/ 16) 597 (231/ 2) 660 (26) 813 (32)

D mm (in) 133 (51/ 4) 178 (7) 210 (81/ 4)

254 (10) 279 (11)

D5 mm (in) 115 (4 9/ 16) 140 (51/ 2) 175 (67/ 8) 185 (71/ 4) 225 (87/ 8)

D6 mm (in) 115 (4 9/ 16) 140 (51/ 2) 175 (67/ 8) 185 (71/ 4) 225 (87/ 8)

243 (9 9/ 16) 243 (9 9/ 16) 268 (10 9/ 16) 268 (10 9/ 16)

D9 mm (in) 102 (4) 127 (5)

F mm (in) 168 (6 5/ 8) 178 (7)

H mm (in) 64 (21/ 2) 102 (4)

Dia. mm (in) 22 (7/ 8) 22 (7/ 8)

Keyway mm (in)

V Min. mm (in)

4.8x2.4 (3/ 16 x 3/ 32)

56 (2 3/ 16)

133 (51/ 4)

229 (9)

102 (4)

29 (11/ 8)

6x3 (1/ 4x1/ 8)

(51/ 4)

229 (9)

102 (4) 29 (11/ 8)

6x3 (1/ 4x1/ 8)

29 (11/ 8)

6x3 (1/ 4x1/ 8)

133

146 (5 3/ 4)

279 (11)

127 (5)

152 (6)

316 (12 7/ 16)

127 (5)

70 (2 3/ 4)

Baseplate Mounting Dimensions Max. Pump Base- Motor Group plate Frame 139 148 GP 1 1K

GP 2 2K

153 245 252 258 264 268 280

184T 215T 256T 286T 326TS 184T 215T 286T 326T 365T 405TS 449TS

HA Weight mm (in) kg (lb) Metal Poly. 50 (111) 381 (15) 330 (13)

991 (39)

74 (163) 457 (18) 406 (16)

1219 (48)

HB mm (in)

96 (212) 533 (21) 483 (19)

1346 (53)

59 (129) 381 (15) 330 (13) 80 (177) 457 (18) 406 (16) 106 (234) 533 (21) 483 (19)

1143 (45) 1321 (52) 1473 (58)

149 (328) 559 (22) 559 (22)

1626 (64)

186 (409) 660 (26) 660 (26) 218 (481)

1727 (68) 2032 (80)

GP 1 – HD1 applies to 1J11/ 2x1US-6 HD2 applies to 1K11/ 2x11/ 2US-82 GP 2 – HD1 applies to 2L2x11/ 2US-10A and 2K3x2US-10 HD2 applies to 2K3x2US-13, 2K4x3US-13 and 2K4x3US-10H HD3 applies to 6x4US-13A

HD1▲ mm (in) Metal Poly. 229 (9) 226 (8 7/ 8) 241 (9 1/ 2) 245 (9 5/ 8) 267 (10 1/ 2) 270 (10 5/ 8) 302 (117/ 8) 289 (113/ 8) 327 (12 7/ 8) 314 (12 3/ 8) 305 (12) 302 (117/ 8) 319 (12 3/ 8) 302 (117/ 8) 330 (13) 312 (12 1/ 4) 330 (13) 318 (12 1/ 2) 352 (13 7/ 8) 340 (13 3/ 8) 378 (14 7/ 8) 365 (14 3/ 8) 403 (15 7/ 8) 391 (15 3/ 8)

HD2▲ mm (in) Metal Poly. 273 (10 3/ 4) 269 (10 5/ 8) 283 (111/ 8) 286 (111/ 4) 302 (117/ 8) 327 (12 7/ 8) 349 (13 3/ 4) 359 (141/ 8) 375 (14 3/ 4)

HD3 mm (in) Metal Poly.

HE mm (in)

HF mm (in)

114 (4 1/ 2) 927 (36 1/ 2) 152 (6)

289 (113/ 8) 191 (7 1/ 2) 314 (12 3/ 8) 346 (13 5/ 8) 375 (14 3/ 4) 372 (145/ 8) 114 (4 1/ 2) 346 (13 5/ 8) 384 (15 1/ 8) 372 (145/ 8) 152 (6) 355 (14) 400 (15 3/ 4) 381 (15) 191 (7 1/ 2) 3 375 (14 / 4) 362 (14 1/ 4) 400 (15 3/ 4) 381 (15)

HG mm (in) HH Metal Poly. mm (in) 95 (3 3/ 4) 92 (3 5/ 8)

1156 (45 1/ 2) 105 (41/ 8) 108 (41/ 4) 1283 (50 1/ 2) 121 (4 3/ 4) 108 (41/ 4)

19 (3/ 4)

1080 (42 1/ 2) 95 (3 3/ 4) 92 (3 5/ 8) 1257 (49 1/ 2) 105 (41/ 8) 92 (3 5/ 8) 1410 (55 1/ 2) 1562 (61 1/ 2)

121 (4 3/ 4) 108 (41/ 4) 25 (1)

378 (14 7/ 8) 365 (14 3/ 8) 400 (15 3/ 4) 381 (15) 1664 (65 1/ 2) 241 (9 1/ 2) 403 (15 7/ 8) 391 (15 3/ 8) 403 (15 7/ 8) 384 (15 1/ 8) 1969 (77 1/ 2)

▲ Includes spacer under pump, as necessary.

47

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Pump Division

Mark 3 Self-Priming Unitized Self-Priming Parts Group 1 and Group 2

Group 2 shown. See page 32 for Group 1 pumping unit details.

ITEM

DESCRIPTION

100

CASING

103

IMPELLER

104

IMPELLER GASKET

105

SHAFT

106

REAR COVER PLATE

107

REAR COVER GASKET

108

BEARING HOUSING ADAPTER*

109

BEARING HOUSING FOOT

109A

SHIM

110

GLAND - PACKING

111

STUD - GLAND

111A

HEXNUT - GLAND

112

PACKING SEAL CAGE HALVES

113

PACKING

OPT.

114

DEFLECTOR INBOARD

OPT.

115

STUD - CASING

115A

HEXNUT - CASING

118

OIL SEAL INBOARD

119

BEARING HOUSING

OPT.

120

BEARING INBOARD

121

BEARING OUTBOARD

122

OIL SLINGER

124

LOCKNUT - BEARING

125

LOCKWASHER - BEARING

129

OIL SEAL OUTBOARD

130

KEY - SHAFT/COUPLING

131

O-RING - ADAPTER*

133

TRICO OILER (Not Shown)

134

BEARING HOUSING DRAIN PLUG

135

BEARING HOUSING VENT PLUG

136

CAPSCREW - FOOT

139

CAPSCREW - BEARING HOUSING*

140

CAPSCREW - COVER/ADAPTER

153

MECHANICAL SEAL

177

HOOK SLEEVE

190

GLAND - MECHANICAL SEAL

190G

GLAND GASKET

200

SIGHT GAGE - BEARING HOUSING

OPT.

OPT.

OPT.

201

BEARING CARRIER

201A

SET SCREW - BEARING CARRIER

201B

O-RING - BEARING CARRIER

201C

BEARING CARRIER RETAINER

201D

CLAMP RING BEARING HOUSING

OPT.

201E

SOC-CAPSCREW CLAMP

OPT.

* GROUP 2 ONLY. Option for duplex angular contact bearings

48

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Pump Division

Mark 3 Self-Priming

Flowserve Durco Pre-Engineered Priming Tanks

Combine Flowserve Durco Priming Tanks with most standard pumps to create simple and reliable self-priming systems. Benefits • Allows the pump to sit high and dry. Easy access for maintenance. No need for troublesome vertical sump pumps or elaborate hoisting equipment. • Zero priming time reduces stress on seals and bearings that occurs during priming cycle with self-priming pump designs. • Air bleed line from pump discharge common with selfpriming pump is not required. Applications • Sump pump service • Tank car unloading • Flows to 1364 m3/h (6000 gpm) Special designs to 5682 m3/h (25 000 gpm)

Common Pump Types • Standard ANSI/ISO • Sealless pumps • Recessed impeller/vortex type pumps Solids to 100 mm (4 in) • Low flow/high head • Non-metallic

Materials of Construction • Carbon Steel • 316SS • FRP • Others on request • Capacities to 318 m3/h (1400 gpm) • Heads to 52 m (170 ft) Also available: the original unitized self-priming pump

49

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Pump Division

Mark 3 Self-Priming

Flowserve Durco Pre-Engineered Priming Tanks

Selection Criteria 1. Select priming tank with maximum design capacity equal to or greater than the maximum process flow rate from Table 3 on page 51. 2. Determine NPSHa for the pump, including head loss thru priming tank from Table 1. 3. Confirm from Table 3 that suction lift required does not exceed tank capabilities. 4. Select pump to assure NPSH r of pump is less than NPSH a of system. Good Pump Practice recommends the difference be 1.5 m (5 ft) or 20%, whichever is greater.

Design/Installation Criteria 1. Provide suction pipe prior to the priming tank the same size as tank inlet and outlet. Pipe length from the tank to the liquid level should be limited to 6 m (20 ft). This provides the maximum volume of air the tank will prime. A change in pipe dimensions must not result in greater air volume to be primed. NPSH and submergence factors must also be considered. 2. Provide 10 diameters of straight suction pipe to pump inlet where possible. Suction pipe between the priming tank and pump may be reduced (eccentric reducer) to match pump suction size.

6

11

Curve 1 Curve 2 Curve 3 Curve 4

57

85

➁ ➂

➀ 0

34

25

50









150 250 375 500 750 1000 1500 2000 3000 4000 5000 6000 Flow –– gpm gpm Flow

GB 50/GBM11 GB 250/GBM57 GB 500/GBM114 GB1000/GBM227

Curve 5 GB 2000/GBM454 Curve 6 GB 4000/GBM908 Curve 7 GB 6000/GBM1363

2.4 2.1 1.8 1.5 1.2 0.9 0.6 0.3 0

Denotes scale change

Table 2: Submergence Table 2: Submergence

Ft/s m/s2 16 4.9 12 3.7

2 .6

8

2.4

4

1.2

4 6 8 10 12 14 16 ft 1.2 1.8 2.4 3.0 3.7 4.3 4.9 m S = Min. Submergence

50

Head Loss – m

0

Suction Pipe InletVelocity Velocity Suction Pipe

8 7 6 5 4 3 2 1 0

3 Flow Flow –– m m3/h /h 114 170 227 341 454 681 908 1136 1363

Head Loss – m

Head – ft– ft HeadLoss Loss

Table 1: 1: Priming Tank Head Loss Head Curves Loss Curves Table Priming Tank

3. Install a low level switch in the sump to ensure that the minimum submergence is maintained. The minimum submergence depends on the fluid velocity at the pipe inlet. That fluid velocity varies with the inlet diameter. If the liquid level in the sump allows air into the suction pipe, the tank will lose prime and the pump will empty the tank of liquid. See Submergence Table 2. 4. Provide a check valve on discharge pipe to avoid siphon problems. 5. Seal all pipe connections and the pump to prevent air ingress and loss of prime. 6. Anchor the priming tank to the foundation through holes in pads on bottom of tank legs. See certified dimension prints for size and locations. 7. Provide proper piping support.

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Pump Division

Mark 3 Self-Priming 1. Ensure maximum test pressure limited to 100 kPa (14.7 psig). Priming tanks operate in vacuum conditions and are designed as “containment vessels”.

Operating Criteria

Check Valve (Required)

2. Remove the tank fill plug to vent tank while initially filling the sump. This avoids an air pocket in submerged pipe. 3. Fill priming tank with pump discharge isolation valve closed and pump suction isolation valve open. A tank

fill port and an overfill port are provided to assure proper filling and operation. 4. Apply suitable sealant to fill port and overfill port plugs and replace prior to operating.

25 mm (1 in) NPT Tank Fill Port



6 m (20 ft) maximum piping length (see design/installation notes 1 and 2)

E



C



Suction Isolation Valve

B





;;;;;;;; ;;;;;;;; ;;;;;;;; ;;;;;;;; ;;;;;;;; Discharge Isolation Valve

15 mm (1/2 in) NPT Tank Overfill Port





D ▼



Anchor Pads

F





High level switch

A Maximum

NOTICE: Internal chamber design is proprietary technology and critical to successful operation









3F



300 mm (12 in) minimum liquid level to pipe inlet ▼ (see submergence)

Low level switch recommended to avoid air entering the pipe inlet, causing loss of prime

F min ▲

Table 3: Pre-Engineered Priming Tank Dimensional Data

Tank Model*

Maximum Flow m3/h (gpm) GB50 (GBM11) 11 (50) GB250 (GBM57) 57 (250) GB500 (GBM114) 114 (500) GB1000 (GBM227) 227 (1000) GB2000 (GBM454) 454 (2000) GB4000 (GBM908) 908 (4000) GB6000 (GBM1363) 1363 (6000)

A Maximum Lift** m (ft) 5.2 (17) 5.2 (17) 5.2 (17) 5.2 (17) 5.2 (17) 4.0 (13) 4.0 (13)

B Tank Diameter mm (in) 650 (24) 800 (30) 950 (36) 1100 (42) 1300 (48) 1400 (54) 1600 (60)

All dimensions are approximate and for illustration purposes only. For exact dimensions request certified dimensional prints.

C Tank Height mm (in) 1100 (43) 1360 (54) 1540 (61) 1740 (69) 2200 (87) 2240 (88) 2600 (102)

D Flange Height mm (in) 360 (14) 460 (18) 490 (19) 590 (23) 770 (30) 970 (38) 1200 (47)

E Inlet/Outlet Width mm (in) 770 (30) 970 (38) 1120 (44) 1270 (50) 1530 (60) 1680 (66) 1930 (76)

* GB - ASME Flanges - U.S. customary GBM - ISO Flanges - S.I. (metric)

F Piping Diameter mm (in) 40 (11/ 2) 80 (3) 100 (4) 150 (6) 200 (8) 250 (10) 300 (12)

** Divide by specific gravity for each application. Engineered designs can provide greater lift capabilities.

51

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Pump Division

Mark 3 Recessed Impeller

Recessed Impeller

Trouble-free pump ing of solid, stringy or fibrous slurries. Delivers efficient operation and low NPSHr. Vortex Pumping Action is your Best Choice for: • Erosive/corrosive slurries • Degradation sensitive crystals • Shear sensitive liquids • Stringy solids • Waste water Impeller Dynamics The vortex created by the spinning impeller does the pumping with less than 20% of the media actually contacting the impeller. Abrasive wear is minimized and solids integrity is maintained. Precision-cast impellers ensure peak energy efficiency and low NPSH requirements. Rear pump-out vanes are used as necessary to ensure low, positive seal chamber pressure and to expel solids from the seal area, thus maximizing mechanical seal and packing life. The impeller is set to the rear cover plate – just like the standard reverse vane impeller.

52

Casing Dynamics The cylindrical volute design combined with the impeller spinning “out of the flow” minimize radial loads on the impeller. The result is longer seal life as well as maximized radial bearing life. The circular flow path and tangential discharge also contribute to maximum pump life.

Applications • Abrasive waste water • Biological sludge • Clarifier underflow • 5% coke slurry • Diatomaceous earth slurry • Floculant sludge • Latex • Lime mud slurry • Organic slurry • Polymer slurry • Resin slurry • Rubber crumb slurry • Sodium hydroxide • Catalyst slurry

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Pump Division

Mark 3 Recessed Impeller Recessed Impeller Performance Curves

60 Cycle CAPACITY CUBIC METERS PER HOUR T.D.H IN FEET

0

10

20

30

40

50

60

70

FLOWSERVE DURCO MARK 3 COMPOSITE GROUP 1 & 2 RECESSED IMPELLER PUMP 3500 R.P.M.

440 400 360

CAPACITY CUBIC METERS PER HOUR

T.D.H IN METERS

80

0

140

280

2 x 2R-10 (CLAW)

240

80

100

200

300

4 X 3R-13

2 X 2R-10

20

150

200

250

300

10

2X2R-6

0

0

0 100

350

0 0

100

200

CAPACITY U S GALLONS PER MINUTE

20

40

60

80

100

200

400

800

1200

1600

2000

CAPACITY CUBIC METERS PER HOUR

300

400

FLOWSERVE DURCO MARK 3 COMPOSITE GROUP 1 & 2 RECESSED IMPELLER PUMP 1150 R.P.M. SCALE

100

300

CAPACITY U S GALLONS PER MINUTE

CAPACITY CUBIC METERS PER HOUR

0

20

3 X 3R-10

40

40 50

60

30

6 X 4R-13

40 2 x 2R-6

0

T.D.H IN METERS

40

120

80

80

500

50

60

120

400

FLOWSERVE DURCO MARK 3 COMPOSITE GROUP 1 & 2 RECESSED IMPELLER PUMP 1750 R.P.M.

160

160

T.D.H IN FEET

60

200

120

80

200

40

SCALE CHANGE

100

320

20

T.D.H IN FEET

T.D.H IN FEET

T.D.H IN METERS

0

40

80

120

160

50

30

200

240

280

FLOWSERVE DURCO MARK 3 COMPOSITE GROUP 2 RECESSED IMPELLER PUMP 860 R.P.M.

T.D.H IN METERS

16 14

CHANGE

25

80

20

4 X 3R-13

60

40

12 10

4 X 3R-13

30

8 15 40

6 X 4R-13

20

6 X 4R-13

6

10

2 X 2R-10

3 X 3R-10

4

20

10

5

2

2X2R-6

0 0

80

160

240

320

400

800

1200

0

0

0 1600

0

160

320

CAPACITY U S GALLONS PER MINUTE

480

640

800

960

1120

1280

CAPACITY U S GALLONS PER MINUTE

50 Cycle CAPACITY U S GALLONS PER MINUTE T.D.H IN METERS

0

50

100

150

200

250

300

FLOWSERVE DURCO MARK 3 COMPOSITE GROUP 1 & 2 RECESSED IMPELLER PUMP 2900 R.P.M.

80 70

0

80

160

240

320

400

480

T.D.H IN METERS

280

560 640

1000

1500

2000

FLOWSERVE DURCO MARK 3 COMPOSITE GROUP 1 & 2 RECESSED IMPELLER PUMP 1450 R.P.M.

240 48

T.D.H IN FEET

200

SCALE CHANGE

200

2 X 2R-10 (CLAW)

60

CAPACITY U S GALLONS PER MINUTE

T.D.H IN FEET

350

40

50

160

160

32

4 X3R-13

40

120 120

24

80

16

30

6 X 4R-13

20

2 X 2R-10

2 X 2R-6

0

0

0 0

10

20

30

40

50

60

70

40

8

40

10

80

3 X 3R-10

80

0

20

2X2R-6 40 60

0 80

100

120

140

200

300

400

500

CAPACITY CUBIC METERS PER HOUR

CAPACITY CUBIC METERS PER HOUR CAPACITY U S GALLONS PER MINUTE

0

200

400

600

800

1000

T.D.H IN METERS

1200

1400

1600

1800

FLOWSERVE DURCO MARK 3 COMPOSITE GROUP 2 RECESSED IMPELLER PUMP 960 R.P.M.

24

T.D.H IN FEET

100 20 80

16

60

4 X 3R-13

12

6 X 4R-13

8

40

4

20

0

0 0

40

80

120

160

200

240

280

320

360

CAPACITY CUBIC METERS PER HOUR

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Mark 3 Recessed Impeller Recessed Impeller Dimensions

Pump 1J2x2R-6 2K2x2R-10 2K3x3R-10 2K4x3R-13 2K6x4R-13

Suction Size mm (in) 50 (2) 50 (2) 80 (3) 100 (4) 150 (6)

Discharge Size mm (in) 50 (2) 50 (2) 80 (3) 80 (3) 100 (4)

Pump Weight kg (lb) 45 (100) 118 (260) 136 (300) 163 (360) 177 (390)

Pump Dimensions X mm (in) 165 (61/ 2) 216 (81/ 2) 229 (9) 267 (101/ 2) 292 (111/ 2)

O mm (in) 298 (113/ 4) 425 (163/ 4) 438 (17 1/ 4) 521 (201/ 2) 546 (211/ 2)

C mm (in) 70 (2 3/ 4) 133 (51/ 4) 130 (51/ 8) 168 (65/ 8) 168 (65/ 8)

D mm (in) 133 (51/ 4) 210 (81/ 4) 210 (81/ 4) 254 (10) 254 (10)

D5 mm (in) 109 (4 3/ 8) 173 (6 13/ 16) 182 (7 3/ 16) 221 (8 11/ 16) 233 (9 3/ 16)

D6 mm (in) 109 (4 3/ 8) 173 (6 13/ 16) 182 (7 3/ 16) 221 (8 11/ 16) 233 (9 3/ 16)

D9 mm (in) 70 (31/ 4) 89 (31/ 2) 108 (4 1/ 4) 105 (4 1/ 8) 121 (4 3/ 4)

F mm (in) 141 (5 9/ 16) 146 (53/ 4) 190 (71/ 2) 181 (71/ 8) 213 (83/ 8)

CP mm (in) 484 (191/ 16) 641 (251/ 4) 680 (27) 676 (26 5/ 8) 708 (27 7/ 8)

D dimension is from shaft center line to bottom of casing feet. See HD and HG dimensions to determine shims under pump if required. Baseplate Mounting Dimensions Pump Group

Max. Motor Baseplate Frame 139 148

GP 1 1J

GP 2 2K

153 245 252 258 264 268 280

184T 215T 256T 286T 326TS 184T 215T 286T 326T 365T 405TS 449TS

50 (111)

HA mm (in) Metal Poly. 381 (15) 330 (13)

991 (39)

74 (163)

457 (18)

406 (16)

1219 (48)

96 (212)

533 (21)

483 (19)

1346 (53)

59 (129) 80 (177) 106 (234)

381 (15) 457 (18) 533 (21)

330 (13) 406 (16) 483 (19)

1143 (45) 1321 (52) 1473 (58)

149 (328)

559 (22)

559 (22)

1626 (64)

Weight kg (lb)

186 (409) 218 (481)

HD1 for the following pumps: 2x2R-10, 3X3R-10 HD2 for the following pumps: 4x3R-13, 6X4R-13

54

660 (26)

660 (26)

HB mm (in)

1727 (68) 2032 (80)

HD1** mm (in) Metal Poly. 229 (9) 226 (87/ 8) 241 (91/ 2) 245 (9 5/ 8) 267 (101/ 2) 270 (10 5/ 8) 302 (117/ 8) 289 (113/ 8) 327 (12 7/ 8) 314 (123/ 8) 305 (12) 302 (117/ 8) 319 (12 3/ 8) 308 (121/ 8) 330 (13) 312 (121/ 4) 330 (13) 312 (121/ 4) 352 (13 7/ 8) 334 (131/ 8) 378 (147/ 8) 365 (143/ 8) 403 (15 7/ 8) 391 (153/ 8) 1

HD2** mm (in) Metal Poly.

HE mm (in)

HF mm (in)

114 (41/ 2)

927 (361/ 2)

1156 (451/ 2) 105 (41/ 8)

102 (4)

191 (71/ 2) 1283 (501/ 2) 121 (4 3/ 4)

102 (4)

152 (6)

349 (13 3/ 4) 346 (13 5/ 8) 359 (141/ 8) 355 (14) 375 (14 3/ 4) 355 (14) 375 (14 3/ 4) (14 7/ 8)

378 403 (15 7/ 8) 3

3

*Shaft Extension 38 mm (1 / 2 in) Dia. 10 x 5 mm ( / 8 x / 16 in) Keyway on 4 x 3R-13 and 6 x 4R-13 Pumps

355 (14) 365 (143/ 8) 391 (153/ 8)

HG mm (in) HH mm (in) Metal Poly. 95 (3 3/ 4) 92 (3 5/ 8)

114 (41/ 2) 1080 (421/ 2) 95 (3 3/ 4) 92 (3 5/ 8) 152 (6) 1257 (491/ 2) 105 (41/ 8) 102 (4) 1410 (551/ 2) 191 (71/ 2) 102 (4) 1562 (611/ 2) 121 (4 3/ 4) 108 (41/ 4) 1664 (651/ 2) 241 (91/ 2) 1969 (771/ 2)

**Includes spacer under pump, as necessary.

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25 (1)

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Mark 3 Recessed Impeller Recessed Impeller Parts Group 2

ITEM

DESCRIPTION

100

CASING

103

IMPELLER

104

IMPELLER GASKET

105

SHAFT

106

REAR COVER PLATE

107

REAR COVER GASKET

108

BEARING HOUSING ADAPTER

109

BEARING HOUSING FOOT

109A

SHIM

110

GLAND - PACKING

111

STUD - GLAND

111A

HEXNUT - GLAND

112

PACKING SEAL CAGE HALVES

OPT.

113

PACKING

OPT.

113L

LIP SEAL

114

DEFLECTOR INBOARD

115

STUD - CASING

115A

HEXNUT - CASING

118

OIL SEAL INBOARD

119

BEARING HOUSING

120

BEARING INBOARD

121

BEARING OUTBOARD

122

OIL SLINGER

124

LOCKNUT - BEARING

125

LOCKWASHER - BEARING

129

OIL SEAL OUTBOARD

130

KEY - SHAFT/COUPLING

131

O-RING - ADAPTER

133

TRICO OILER (Not Shown)

134

BEARING HOUSING DRAIN PLUG

135

BEARING HOUSING VENT PLUG

136

CAPSCREW - FOOT

139

CAPSCREW - BEARING HOUSING

140

CAPSCREW - COVER/ADAPTER

153

MECHANICAL SEAL

177

HOOK SLEEVE

190

GLAND - MECHANICAL SEAL

190G

GLAND GASKET

200

SIGHT GAGE - BEARING HOUSING

201

BEARING CARRIER

201A

SET SCREW - BEARING CARRIER

201B

O-RING - BEARING CARRIER

OPT.

OPT.

OPT.

OPT.

201C

BEARING CARRIER RETAINER

201D

CLAMP RING BEARING HOUSING

OPT.

201E

SOC-CAPSCREW CLAMP

OPT.

Option for duplex angular contact bearings

Abrasive packing arrangement 55

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Power Monitor

Flowserve Durco KW941 Pump Power Monitor™

The KW941 Pump Power Monitor monitors and displays actual power to the pump offering simultaneous protection from underload and overload operating conditions. The KW941 helps to eliminate costly downtime and expensive pump repairs caused by: • Dry running • Pump overloads • Cavitation • Blocked lines • Closed suction or discharge valves • Excessive wear or rubbing By sensing power and not just amperes, linear measurements are given which help to eliminate unwanted nuisance trips. Broad Application Range • Works on all pumps having steady (non-pulsating) loads: centrifugal; gear; turbine; ANSI; API; paper stock; sealed; mag drive; can motor; self-priming Easy Installation • Simple wiring procedure • Easily installed on existing pump installations Easy Setup and Calibration • Settings controlled from front panel push buttons; no internal adjustments, dip switches or potentiometers • Large digital display for easy viewing and accurate settings • One step calibration can be performed without operating pump. No need to run pump at off-operating conditions to calibrate power monitor • Settings can be viewed or adjusted during normal pump operation

56

Premium Features for Reliable Protection • Push buttons display horsepower or kilowatts; automatic conversion when switching displays • Adjustable low power and high power set points protect pump from underload and overload operation. Alarms can be tripped or pumps shut down before damage occurs • Adjustable trip delay timers filter out nuisance trips caused by temporary power fluctuations • Adjustable start up delay timer is particularly useful in unloading applications • Optional 4 to 20 milliamp analog output. Facilitates remote displays, operator interface and output to PLC or DCS • Two form C relay outputs for low and high power trips. Outputs can be used to shut down pump or trip alarms • Automatic, manual and remote reset options for versatile operation

The KW941 Power Monitor is easy to install on new or existing pump installations. All connections and controls are located at motor starter electrical enclosure as shown above. Costly instrumentation wiring to the pump is eliminated.

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Flowserve Durco KW941 Pump Power Monitor™

Specifications Display/Control Module

Full Scale Range Adjustable 0.7 to 112 kW (1 to 150 hp). To 447 kW (600 hp) using current transformer (not included). Display 3 digit, 15 mm (0.6 in) high, 7 segment, red LED digital display. Red LED indicators for display mode, trip delays and trip points. Enclosure Polycarbonate, NEMA 4X/IP66 with see-through cover. Four #8 (4 mm) mounting holes. Enclosure can be drilled, sawed or punched on bottom or back for wiring access. Power 110 VAC (220/240 VAC optional), 50/60 Hz @ 0.125 amperes. Power is obtained from a control voltage transformer (not supplied) connected between two phases of the three-phase motor power source. Operating Temperature -44° to 70°C (-40° to 158°F) Adjustable Trip Set Points • High Power: When power exceeds the trip point setting, the trip delay is activated. When the trip delay has timed out, an alarm contact relay will trip.

• Low Power: When power falls below the trip point setting, the trip delay is activated. When the trip delay has timed out, an alarm contact relay will trip.

Adjustable Trip Delay Timers Delay timers eliminate trips during motor starting and false trips due to temporary power fluctuations. Individual timers are adjustable from 0-to-999 seconds: • Start-up Delay • Lower Power Trip Delay • High Power Trip Delay Alarm Relay Contacts Form C relays for low power and high power trip points. • Ratings – 5 amps @ 125 VAC – 3 amps @ 277 VAC – 5 amps @ 30 VDC Analog Output (Optional) 4 to 20 milliamp output proportional to full scale setting. Maximum loop load resistance – 600 ohms. Trip Reset Options • Automatic: Automatic trip reset may be selected on the display/control module. • Manual: Trips may be reset manually on the display/ control module. • Remote: Trips may be reset remotely using a momentary external mechanical or solid state switch.

Power/Current

Power Monitor

0%

r we Po nt rre Cu

Motor Load

100%

Typical Low Flow/ No Flow Pump Protection Zone

At low loads, motor amperes do not change much with small changes in pump loads. Small signal changes can cause false trips or allow equipment to operate below the desired minimum operating point. At low loads, power is linear. Small changes in pump operating loads provide greater signal changes. The KW941 is more sensitive to pump load changes and offers easier setup, more reliable equipment protection and no false trips.

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Good Pump Practice

Good Pump Practice

Extending MTBPM by Reducing Internal Stress and Vibration in the Process Pump System Package Flowserve is recognized worldwide as the premier name in ANSI pump performance. Its technologically advanced product enhancements have extended MTBPM to new levels. By implementing Good Pump Practice, peak operating performance and economy can be further improved. These seven general principles apply to sealed and sealless pumps.

58

Selection • Sizing with less than maximum synchronous speed rpm where practical • Impeller trim from 95 to 60% of maximum with 75% optimal • Operate from 85% to 110% of BEP • NPSHa 20% or 1.5 m (5 ft) over NPSHr, whichever is greater • Consider variable speed technology for multiple operating point conditions Balance • Impeller balanced to 20 gmmm/kg (0.011 oz in/lb), after trimming. Two-plane spin balance when outside diameter to width ratio < 6 and single plane when ≥ 6 • Coupling balanced to AGMA 8 (AGMA 10 over 56 kW [75 hp]). Coupling to be elastomer type for soft start • Offset pump and motor shaft/coupling hub keyways 180° and cut keys to one-half unfilled keyway length

Installation • Level pump/base/motor – free of soft foot conditions • Provide 10 diameters of straight pipe to suction inlet. Flow conditioning technology may be an option • Rigid baseplate design – reinforced stilt – grout installed baseplate • Grout with low shrink cement; epoxy grout preferred • Special cleaning and primer to bond base with epoxy-type grout • Piping design to assure minimal stress (fasteners installed without force)

Alignment • Use laser or reverse dial indicator technology. Recommended tolerances to: parallel 0.05 mm (0.002 in) FIM; angular 0.0005 mm/mm (0.0005 in/in) FIM • Align before and after pipe-pump bolt-up • Specify bolting to fit without force to connect pump and pipe • Consider C-flange motor adapter for pumping temperatures > 93°C (200°F) or hot align after start-up • Consider C-flange adapters when minimum and maximum pumping temperatures are more than > 56°C (100˚F) apart • For pumping temperatures > 177°C (350°F) consider centerline mounted casing and include C-flange adapter > 260°C (500°F)

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Good Pump Practice Preventive Maintenance • Change lubricant at recommended intervals • Protect lubricant from contamination • Use sealed or “vapor block” power end protection and synthetic lubricant to reduce relubrication intervals • Maintain mechanical seal flush environment. Eliminate the need for flush with alternate seal and seal chamber designs when possible • Maintain power end and mechanical seals in a “clean room” • Predictive maintenance, vibration monitoring and lubricant analysis are still good practice

Operation • Develop suitable start-up procedures and checklists • Avoid rapid closing of process valves (no water hammer) • Use a power monitor for minimum/maximum flow protection • Add minimum flow bypass as required • Consider soft start for frequent on-off duty • Consider variable speed technology for inherent soft start, reduced RPM and increased efficiency • Do not run dry. Check for submergence conditions, particularly in batch operation. Select pump/seal type accordingly • Operate spare pump every three (3) months

Design/Specifications • Use solid shafts – Index of Deflection: (I = L3D4) Group 1 < 75 Group 2 3500 rpm < 40 1800 rpm < 65 Group 3 ≤ 25 • Use cartridge seals designed to reduce fretting corrosion and for proper setting 100% of time • Maintain critical impeller setting tolerances to hold low thrust load and seal chamber pressure • Specify state of the art seal chamber designs that offer anti-rotation features to reduce abrasion, vaporization, heat and cavitation at the mechanical seal • Pump manufacturer to be responsible for “Total Engineered Seal System” (TESS) • Rigid, cast iron motor foot construction with ≥ 182T(S) frame sizes

Note: Some items are more critical for longer term installations and become economical when life cycle cost considerations are applied. For further information, contact a Flowserve salesperson.

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Flowserve... Supporting Our Customers With The World’s Leading Pump Brands

Jeumont-Schneider™ USA and Canada Flowserve Corporation Pump Division 5215 North O’Connor Blvd. Suite 2300 Irving, Texas 75039-5421 USA Telephone: 1 972 443 6500 Telefax: 1 972 443 6800 Europe, Middle East, Africa Worthington S.P.A. Flowserve Corporation Via Rossini 90/92 20033 Desio (Milan), Italy Telephone: 39 0362 6121 Telefax: 39 0362 303396

Pump Division

Latin America and Caribbean Flowserve Corporation Pump Division 6840 Wynnwood Lane Houston, Texas 77008 USA Telephone: 1 713 803 4434 Telefax: 1 713 803 4497

Your local Flowserve representative:

To find your local Flowserve representative please use the Sales Support Locator System found at www.flowserve.com

Asia Pacific Flowserve Pte. Ltd. Pump Division 200 Pandan Loop #06-03/04 Pantech 21 Singapore 128388 Telephone: 65 6775 3003 Telefax: 65 6779 4607

Or call toll free: 1 800 728 PUMP Printed in U.S.A. February 2004 © Flowserve Corporation

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