Flour PUMP&VESSEL -.pdf
April 18, 2017 | Author: FREDIELABRADOR | Category: N/A
Short Description
Download Flour PUMP&VESSEL -.pdf...
Description
t I I I ! ! ! ! t I
t !
T
I I
T
I I I
NIJMB ER
'l' FLUoR P
PIIASE
IIl
LESSON 9
PI]HPS AND TURBINES
IP INC
TRAIIIINC
PAGE
)r lluaLs
oATE Rev.
A.
1
1/80
centrifugal
1- Horizontal 2. VerticaL 3. In-1ine B.
Rotary I23-
C.
?ump
cam
scre!,
Reciprocating
1. 23Ii.
Gear
Piston Plunger (simplex and Duplex) Diaphragm
Drivers
A. Electric motor B. Turblne (steam, gas, oit) lII-
Pump
Location Consideratj-ons
A-
Close
12-
to source,
available and size of
pump
under pipeway Adjacent to vessel
a3.
space
Trenches may be requj-red
In tank area - outside diked area ab. c.
crouping of purl{)s may be requi.red Avoid direct runs from tank to pump suction Check tank settlement - affects suction piping
clearances
1.2'-6"
around pump (ninimum $aIklray) maintained by rnanual equipnent
Ffexibifity Important factor - can affect pu,np location and vessel orientation P3C-1-013
!
t
NUI{BER
'l'eLuon
PHASE III PUI'IPS AND TIJRB]NES
PIPING TRAINING
-I
LESSOI
PlcE
' 2
Rev- 1/80
DATE]
MANUALS
9
_r
I I I I I I
-I -I
I I I I
t! ! I
2. 3. 4.
Do not pocket lines - step continuouslY dollrl to punP Temporary start-up strainers required Reducers at pump nozzle - refer to Fluor standard I,lhen source
foundation 5.
is
Lon, PiPing can determine elevation check this in your studY.
of
punp
supporting suction line6
abB.
-
Top suction - normallY from overhead End and side suction - from grade or from Pump founalation
Discharge piping 1
.
Tl'pes: top, side Nozzle normally smaller than suction Piping
valve required to Prevent backflor,, on centrifugal not mandatory on positive disPlacement prrftps -
2-
Check
3.
Line support From grade, pipe\ray, pipeway
struts,
and
Pumps
possibly separate
supports 4-
Side discharge - requires more sPacePumP study before locating PumP -
5.
vertlcal purnps _ orient discharge to most suitabte and econonical focation on sump tlpe, verify that sump is at Proper depth to accePt
6.
Verify requirements during
pumps
Ir-1ine
pumps
pr.rmps caD be supPorted from piPing; heavy concrete foundation from
Liqht veight 7-
Reciprocating
Pumps
pumps
Keep discharge pj.ping close P3C-1-013
to grade,
may require hold-dovns
I I
I I I I I I
I I I I
NUMBER
trLUOR
PHASE lII PI,I{PS AND IIJRBINES
-:rrNG
LES5ON 9
pAcE 3 of 3 OAIE Rev- 1/80
.:N!ALS
rurbine Pir,iho A.
steam
inlet -
checking freezing conditions
1. Piping should come from !9P of suPply Possible2- val.ves located Per Fluor standard 3. Proper suPPorts Provided? 4. Bootleg Provided for condensate? B.
header
for driest
steam
Steafi ert E t 6l rll f,l .,JFE: ol
iisi
ol II
ilJI
{fi'.....r.,.1$ -l \
c
\{
a::
i
Et.,/
!L\y'
€
s
\
a
I;3
t
es
\!
sa
$
qa
:
Ael
3r
.
{
s trJ
-.r
: r 'fili a
Fl\ a- t r. zl
al rql
a loltr-l Ie x ",1 I
(.)
Olt{ =
>l
I
-'8 aL ?
r.-l
so -tt
s
s
\il r..j
el E
It nqd
\! (' c\l
-J
tl
\,.1
s
Is
a
o\ d.
^*^
11
S:t r-rS
s
ti\
p + s
\:c
{
r;-p*
U
.Brl i l\l
9)
s
S \$6-
rl (.)
.
:\\ = N
NS
\t
s* y.r
$ \:
\e ql
a
tSr
TST
s(s
i:,lt *fi"i \:,!.J.<
.I{
+
H lr\^.l
Si\
is :S !
N^ \o\
\i \-\ r c1.IS
R
'.,\d -k,. q{
\slr
S \ R
\ld \\:J
\>.- = S\
iHH s
:.,
\
t>
\ :l
il
t
L
a
s
\
s \= =
\
T
N
.,r\
s s*
Str
\\ NS \ (r)s
!
*u.
!.j
NS
H
rrXl3 +gt \o,
\
E
s#s! \ -i<
3l
Is d.s'
lr).\
F T
\
\L (4, c(\
xs
-\q :sf,
!s +4. i l. -a
r
N
:. tN> !') J Q
5!{
c
/
t S
tl
s
-/' -.r
g q
(]1
:{ \li;
B1
:l
f
--.1
,1
=.1r)
'toI +
isss
ilfl' ililE
H \)
s.
EE*&
^t
S F-a a,-r
S Svi
S r.,
ss\
sl
.S I**, [S
s
( N
ea
{
N
TRsS Esilxt \ ..,N\ {= ts8 t'J
(r)
il3
'3{s : S A:
Nir.i F ==s S.- :s 3e\ '"\'N \pS
\N
^\\v) Srs =ad
t\
--
\Jl:
{
.t.
l
L I-
\-. >-.^
<
Q3 s
P \U LS
N\. =
S;ss *F9.u $ = *tNU /i
i- /X
it
\t
I
tix t= |q
h
v I
i"xN \ ,,r o >i N
l.lj
?N r{
l
+
:s
:sss !;i.';
r-
\H
P
lla il
{
-u.,S:. {
Is te
qJ<
t
o!
q-
st{ tatJ:.
(,l S r.J J
St SC
s3
t3
;F}
is! iss
q\
I-t
r.{
=i
a r.
$
s\.r
qt
o N
ta H
\u
ts
!o
$ o'
Y
t-
LI
N \l il-i
t
>l NI \t
sl ol
)l I \)
o sD
\
o
a s
s t-J qr
I tr
LV\AJdld
=l
*s'l
!l\l \nl
utl
E
rs
ur< ags
/U\ \
--l
,/
\n
\\
!J!q
\
.!s8T -.\n { ^
View more...
Comments