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A.
B.
C.
centrifugal
1-
Horizontal
2.
VerticaL
3.
In-1ine
Rotary
I
-
Gear
2-
cam
3
-
scre ,
Reciprocating
1. Piston
2- Plunger
(simplex
and Duplex)
3- Diaphragm
Ii.
?ump Drivers
A. Electric
motor
B.
Turblne (steam, gas,
oit)
lII-
Pump
Location
Consideratj-ons
A-
Close
to
source,
space available
and
size of
pump
1-
under
pipeway
2-
Adjacent to vessel
a- Trenches may be
requj-red
3. In tank area - outside diked area
a-
crouping
of
purl{)s
may be requi.red
b.
Avoid
direct runs from tank to
pump
suction
c. 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
NIJMB ER
LESSON
9
PAGE
1
oATE
Rev.
1/80
'l'
FLUoR
P
IP INC
TRAIIIINC
)r
lluaLs
PIIASE
IIl
PI]HPS AND TURBINES
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5.
B.
3.
4-
5.
6.
2.
Do
not
lines -
step continuouslY
dollrl
to
punP
3. Temporary
start-up strainers
required
4. Reducers
at
pump
nozzle
-
refer to
Fluor
standard
I,lhen
source
is
Lon,
PiPing
can
determine
elevation
of
punp
foundation
-
check
this in
your
studY.
Discharge
piping
1
. Tl'pes:
top, side
Nozzle
normally smaller
than suction
Piping
2-
Check
valve required
to
Prevent backflor,,
on
centrifugal
Pumps
not
mandatory on
positive
disPlacement
prrftps
-
Line
support
From
grade, pipe\ray,
pipeway
struts,
and
possibly separate
supports
Side
discharge
- requires more
sPace- Verify
requirements
during
PumP
study before
locating
PumP
-
vertlcal
purnps
_
orient discharge
to most
suitabte
and
econoni-
cal
focation
on sump tlpe,
verify
that
sump
is at
Proper
depth
to
accePt
pumps
Ir-1ine
pumps
Liqht
veight
pr.rmps
caD be supPorted
from
piPing;
heavy
Pumps
from
concrete
foundation
Reciprocating
pumps
Keep
discharge
pj.ping
close
to
grade,
may
require
hold-dovns
supporting
suction line6
a-
Top
suction -
normallY
b-
End and
side suction -
from
overhead
from
grade
or
from
Pump
founalation
'l'eLuon
PIPING
TRAINING
MANUALS
PHASE III
PUI'IPS
AND TIJRB]NES
NUI{BER
LESSOI
PlcE
'
DATE]
9
2
Rev-
1/80
7-
P3C-1-013
8/10/2019 Flour PUMP&VESSEL -.pdf
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trLUOR
-:rrNG
.:N ALS
rurbine
Pir,iho
A.
steam
inlet -
checking
freezing
conditions
1.
Piping
should
come
from
9P
of
suPply
header
for
driest
steam
Possible-
2-
val.ves
located
Per
Fluor
standard
3.
Proper
suPPorts
Provided?
4.
Bootleg
Provided
for
condensate?
B.
Steafi
er<haust
1.
Line
to
toP
of
header
2-
Line(s)
stress
checked
i.
cfru"i
alrain
-
from
e:,haust
or
casing?
verify
this
fron
turbine
outline
NUMBER
LES5ON
9
pAcE 3
of 3
OAIE
Rev-
1/80
PHASE
lII
PI,I{PS
AND
IIJRBINES
P3C- t"'013
8/10/2019 Flour PUMP&VESSEL -.pdf
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P34-
/
-o/9
s4
I
Pumps
and Turblnes
?.frrt
))
.ld-tt,
t'/i.
d'J
t1
{
I
3
a
{
9
e
o
+
tE1
r':\
s
r\
B
i
{
c
s
I
vl
ls
P./@B
Sfabrhzer
bo+foms
PumPz
FiBuro 1-'1.
Horizontal
conlrllugal
pumpg
shown on
llow
dlagram
Courtdy
ol
FIuo'
Enolne6r3
Constsuctors,
lnc.
and
q
v
8/10/2019 Flour PUMP&VESSEL -.pdf
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+
d1
C
o
.:
o
q
E
G
o
oj
o
o-
o,
A
t
Er
Ei
o
€
o
-9
.t
-
s
PJ
ta
t-
t=
Ir
t-
-
s
s
5:
;
:
;.
3i
=
t
N
'\
N
=
-
-
PsC-/-O/'
sH,
5
Process
Piping
Deslgn
;.E
E
i
-E
=:
r
€
i;
:; i
l
;E
g;;
i= 3-ie
FeE;EEii
EE3:iF5
:.' :=
-:
EEsE iEE=
I
tr
_P,q
Effi1j
#
--
l
:le
i
t
I
:i
E
t
:
I
a
l=
l5
tl
t:
t;
li
t-
l=
I
IE
lr
t-
l6
IE
li
t;
It
E
rlr
li
2
B
a
t-
_t_t
I
ll
@I
8/10/2019 Flour PUMP&VESSEL -.pdf
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6
lr
r
I
L.J
I
r-1
(
Lr
I
r,a
l*u9
Irr
1ur
[rE
,.:..
:
.--
t
i o€
i _or 2 E
EG
.
u :HEs_
q
,
i-. :s
sEsiP'I
i:r
sii i.': iui':i i'"
: i i : I :
:,i
.' ;
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.' i
9
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Y
"r
i
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i
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:-
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z
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i-
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Ev
J1r:c
ry'J
I
I
I
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3
:
al
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h
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iisi
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EE.,Ei
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lt
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trl
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iii::i:::::lEtE
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5r
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p
L ceee
cee
i.
d"ir.
rr:=
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ir :Flnt,t.++
.r.
r
litl I
I
Ele
i:
ilr;:'
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r$
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s
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iz
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t 136
SO
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I
i2
IE
l:
-
L---J
--ii
ti
8/10/2019 Flour PUMP&VESSEL -.pdf
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P31-
a
a/3
Process
Plpins
D€slgn
Figure
1-32.
c,osg
seaton,
Type
vR
turdlne
Courtesy
of
Elllot
comPsny'
l r'r
; ,
jl
li'-
.-
g
r'.--'
t4:
j
.
F
-. re
1.33.
Turbino.
Courtesy
ol Elliott
Company'
Should
the
oPerating
PumJ'
l I an rmDulse
line
opens
the control
valve'
supply-
i:: sream
io the
turbine
immediately
withthistype
..a'r::siallation.
steam
traps
are
supplied
at
every
low
I}ri]lt
in
lhe
inlet
system
to
immedi:rtely
collect
any
c.:riensate
\ hich
maY
form'
i I rr bolh
manual
and
dutomatic
starl_up'
steam
1.,..
'f',r-fO
be
provided
to
keep
the
turbine
ca'int
Iter
of
condensate.
These
can
be
inltalled
either
a(
il.
*'ing
.
to"
poinL
rI
a
connection
is
provided
or
,
-
'""
",,Lt.L
oioine
'f
the
ccting
drain5
into
the
out_
l€t syslem.
The.€
must
be
rise which
*ould
form
a
would
collect.
a
trap
before
anY
vertical
where
cond€nsate
.
lnlet
BY'Pass
All
automatic
start_up
turbines
need
a l"
globc
bodv
valve
to
b)'pass lhe
control
valre
Mdn
operating
companies
insist
on
the
warm"up
b)_PdS
even
with
manual
start_uP.
8/10/2019 Flour PUMP&VESSEL -.pdf
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Manhum
initialpr63ur.
(psr8)
. . .
... .
M.rimum
initiEr
t mpe6tu.. (.F).
.
..
.
.
yarimum
cxh.ust
pr.siur.s
(p6i8)
.. ..
.
sp..d r.ns
(rpm)...
...
Nlmb.rotstrs.s(impulseVpe).......
Numb€.
ol.o$s
ol rorating btades.
.
. .
.
.
lnletsizes
(in.)..........
l.l.t lodtion
(facing
Sovemo.)........
Lh.ust
slzc
(in.)........
Erhaust
location
(1.
H.
Siandard). .
..
..
Centedin€
heisht
(in.).
. . .
Approrim.tc
r..g.
oicapacities
(hp)-
.
. .
Approrim.tc
shlppln8 welght
(b.).
-
.
.. .
P,oc€ss Piping
Oesign
General Specificalions
7s4-/-d/3
sH.g
.ight
8
7@
750
vrc.l25
800-7000
lg
1
2
2,3&4
.ight
8
ro 14oo
r275
704
750
8CO-5760
2?
t
2
2 3,4 &6
riSht
10
t7
to
25Oo
2050
ac05o00
I
800.7350
700
750
rlght
L2
to 3500
26oO
ro
3000
2300
700
750
250
2
1
2
2,3,4
&6
2,3,4 &6
R. H.
opt'o.al
R.
H. optaonal
22
\7
S.. Butr.rin
H29ror ayRH.nd
AyiHH
d.r.it:
sr
All.rin tt32
ror AYR
d.r.it'
Approximate
Dimensions
(in
lnches)
45t/s
5tt/,
5t
t/a
555h
55./.
'ilill"?'lilil,lli'llll,TioYR.(''i'
din'|'o
aYiH md aYRaH
('
n'.n'|'o
,
Figure
1.35
App.o>imat6 drmsnsions,
othor
YR turblnes. Couri€sy
of
Elliot Company.
700
750
375
4oo.7350
t3
1
2
2,3,4&6
ight
a
17
to 30OO
2300
t2Y2
12Yz
r2Y2
t2j/2
t2t/2
t2,/"
l6'rl
t6Y.
l6t/.
l4
l7
22
t7
't7
7
at/z
12
9
9
161/,
19%
\at/.
ra.t
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FUJOR
PIPIXG
TRAINIHG
rur{uALs
1.
2.
6.
SEOUENCE
FOR
RECEIVINC
CERTIFIED DI}IE}ISIONAL
OUILINE
Process
engineer
6ends
punp
calculation sheet to the
pump
mechanical
engineer- This
shouLd
be done
shortly
after
process
flov
diagrarns are
completed.
This calculation sheet contains the operating
conditions for
one
particular
6ervj.ce. the
process
engi.neer
may
aLso
request
punp
tlpe
if
he
has a
preference.
llechalical
engineer uormalLy determines
pump
tipe
ba6ed
on calculation
sheet
information-
He
fiUs in
the
I'Pump
specification Sheet-rr He will
only
fill in
information
noted
as
"to
be
corpleted
by purchaser."
3.
ltechanical engineer then selects
possible
vendorE
based
on avaifable
catalog
information.
4.
l.techanical engineer
fills
i.u
"pump
1i6t"
(6ee
attached sheet)- this
gives
Piping very
prelj.minary
information
thich
can be
used
for
plot
development or
possi-ble
p ..ulP
6tudy
work-
the
puilp
list
refers to
an
l,l-E-D- drawing nunber- This drawing
(see
attached 6heet)
provides
a
visual
picture
of
proposed
pump,
5.
llechanical engineering then
goes
ortt
"Reque6t
for
Quote"
to
several
vendors-
Each
vendor
fj.11s
in
their
portj"on
of
the
Punp
specification
sheet.
They
give
Fluor a
price,
pump
modeL, and size
r,rhich
they offer
for
that
particular
service. The vendors
send
the specification
sheets
and
quote
sheets
to Fluor
for
consideration-
tlechanj.cal
engineer $il1
seoal
revised information to Piping
if
vendor's
recomme[dation significantly inpacts
us-
ltore accurate infonnation
from
veardor
I
s catalog is noll available
-
7.
llechanical engineering
places
order
to
the selected venalor. Approximately
six to eight lreeks later Fluor
recej.ves a
C-D.o.
8.
t,Ihen
c-D-o.
is
"in-house,"
our
Vendor Data
Control
croup
eilI
send ?iping
and
other
di6ciplines
a
reference
copy-
c-D.O-
is
then routed
for
6quad
check-
Piping wonrt normally be included on the routing of the squad
check- However, ee
{ifl squad
check our reference copy and any
questions
or
problems
ve have
can
be
dj.scussed
with
the mechanical engineer- He
lhen can
include
our
corunenta ,/ith his when
he formal"ly
squad
checks
the
c.D.o.
Piping and other disciplines
wiLl
then receive a copy
of
'Isquad
check conulents" which is traEsmitted back to
vendor.
PIIASE
III
PI'T{PS
AND
TURBINES
NUI,{88 R
LESSON
9
pAG€
1
of
6
DATE
Rev. 1/80
P3C-1-014
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/
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F
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SPECIFICATIOII
SHEET
CENTRIFUGAL
PUMP
)
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0,
fr
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d
7I, s. -Ca-
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oxv& $^tF r rD .Y,
o
rfit
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o
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o
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racrlNc,
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fr
r
nrr
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sE^L
El^4'r
.
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.oNNrcr,
trvrNt tror
lx
Bc
G
urrElrEr Dl^.t
or
ED---
Elnrr.
nouxr:
olrflvrEx.ros
ooYtrriuNa
cou.lrxc,
trnrr
_='=- Er^ooat
l.^ Ncs.llrE:
Dr
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flNG
o[
D
rtooD Oort
,{lsr
tr.trNoEr
tr
rrls$rt
tu{rr
c
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craito-
CONIIIUCIION
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-
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a-
loaftD lotor
lr
ts
avB o
vss
HTR.|TE|4 NO. r orcr-
TUlilNE-
oaEialrNc
coNolrloNs,
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lEffom^Nca
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exo
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ut GPn d fi, Nor-urEo
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PUTPS AND TLRBINES
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1
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Rev-
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STE?S TO
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2.
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5-
6.
'1
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such as
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calculate elevations-
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b.
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c.
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to
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discrePancies
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F.D.
and spec
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for
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b-
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pumps
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to
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detennine
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dead
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a
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,
hanger
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relieve dead
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tbe
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\'ri11
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qualit)-,
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designer
uhen he berths lines.
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NUMBE
R
LESSON
8
PAGE
1
of I
DATE
Rev-
1/80
PHASE
lII
TRTICAL
VESSEIS
'l'ruuon
PIPING
TRAINING
MANUALS
1.
2.
STEPS
TO
ACCO}IPLISH
VERIICAI
VESSEL ORIENTATION
Update
your
flo ,
diagran
from
master.r'
Conpare
vessel
outline
to
fLo"r diagram'
a.
Vessel
I.D.
b.
Tangent-to-tangent
dihension.
c.
I.linjmurn
skj.rt
height.
d.
Nunber
of
Passes.
e.
N.L.L.
_
f.
size,
rating,
and
quantiiy of nozzles'
3-
Calculate
elevations.
a.
Bottom
tangent
line
based
on minimun
height
on
flo\,t
diagran'
b- Process
nozzles
based
on
vessel
outllne-
c- verify or
set insinuient
nozzles
based
on
flot,
diagram
and instrument
standard
dral,j.ng-
4.
Determine
vhich items
require
platforms
or
ladder
access'
a.
Establish
elevation
ranges
for
platforns
that nust
be'
b.
Draw
a
rough
freehand
elevation
of
vessel
indicating
platforms
that
are
definilelY
required.
c.
Nov
add
laalders
and
any
aalditionaf
platforms
that
may
be
required
just
to
get
uP
the vessef.
Do this
a couple
of
different
uays until
You
havi min_i-'nized
the
quantitY of
platfoms
and/or
Ladders'
5.
study
Piping
transPosition-
6.
Draw
several
oullines
of
vessel
to
scale
on
scratch
paPer'
?.
on these
outlines
do rouoh
sketches
of
piping,
nozzle
orientations'
ladder
and
platform arrangemen
Eo6llne
ana
ihingi
sketches
for
optimun
design
and
Piping
fogic-
oo will
always
be
due north'
g.
coMence
actual
sludY.
You
must
be
accurate
and
drau
to scale'
However'
-'
;;;ia
worry about
dr;fting
quality, linesork,
or Letteriog'
"Rough
and
dirty,"
but l-eg1ble
and
comPlete.
P3C-1-001A
I
I
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HORIZONTAL
VESSEL
.
-. .;,I::l
-'."
t.:t
.',.
"'"'"6dSi6ruEn'
n
EsPorvst
etllrY
'
"
1.
vESSEt-rloimtoru
,
A.
COORDINATES
2.
ORIENTATION
OF
A.
PIPING
EOUIPMENT
CONNECTIONS
B.
INSTRUMENT
CONNECTIONS
C.
MANHOLE
&
VENT
'D.
PLATFORM
HEIGHTT&rSIZE
',,
il
l
E.
LADDER
&
CAGE
F. ANCHORED
SUPPORT
-
ONE
END
G.
ROUTING
&
SUPPORT
OF
PIPING
TO
AND
FROM
EOUIPMENT
NOZZLES
PHASE
3#7-2
4-7A
:
'
'i li.',,t
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LS'
,.
GE
A.
B.
c.
D.
E.
F.
G.
H.
K.
INLET
OUTLET
CONOEI{SATE
BRAIN OR
DRAIY-0ff
FEED
LEVEL
GA
OR 6AGE GLASS
HANDHOLE
PUMF
OUT
L.
LEVEL
INSTRUITENT
tT.
MANHOLE
-a
'
, 1.
REBOILER
C0i':NECTION
i-r..
P.
PRESSURE
CBNNECTION
R. REFLUX
S. STEAI'I 0R
SAIiIPLE
-
comnrcnoil
T.
THERMO
CONNECTION
-l
Y. VAPOR
()R
VENT
W. REIIIF VALVE
-
connrcttoll
-Syutgots
"8"
ANo
NOZZLES.
s7-4-5o81
to-73'
.'K''
ARE
USED
SOIiIETIMES
FOR
SPECIAL
pgAs€
fr.
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IESSE
ENGINEE:RING
DESIGN
GU,IDE
2-4.1.9
2#29
4-7A
22
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t).in
A.
VESSEI,
ORIENTAT]ON
".:
6es6ion
is
to
help
you
becdtre
nore.failj-ILar
rrith
vegsel
orientation,
baseal
ou
Fluor
1
Thelmaterial
and.
instruction
-you
ret-dii'i
-'ffo[
this
lddi;i6;,.
iliolila"enable
you
to:
.
,1:
rj
xho ,
.ho i
,te
.
aSsirilate.:t}te.
inforuttioD
to
start
.a
-vesbel
,iiriintation
OBJEC?IVE
The
objective of this
the
Fluor approach to
Drarrings.
TBAY
TYPES
:,
2.
?roperly
piepare\orientdtirin
"iturlies
of both
vertii:al dnal horizontaL
vessels.
:
:.''
'
B.
BIIBBI,E;CAP
TRAY
ADV}NTAGES
,
I
DISADVAI{TAGES
1-
3-
I.
2.
1.
2-
3-
Very
efficient
l{eed not
be installed Leve}
"
)r: r'xr f,j'
_,i-
Corrosion
not
.a
factor
.-:.1}1,]^
.
:_.: r:1,
l,Iost
efficient
of
al1
tlpes
IDeapen6ive and
Iighhreight
Need
not
be in6tal1ed
]evel
Corrosion
not
a factor
Inexpensive
Lightweight
cood
for
heavl'
liquids
1.
2.:
4.
occasionally
1.
2-
3.
4.
1-
VAIVE TRAY
SIEVEJ TRAY
Cast iron
caps
break
ounting
bolts rust
None
l,lust
be
instafled
level
corrosion a factor
P38-1-013
Expensive
8/10/2019 Flour PUMP&VESSEL -.pdf
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NUMEER
, PHASE, III
,j,Hofr?6ffi,ffi6sELs
c. REI{OVABLE TRAYS
D.
vessels
ln
heavy
(dirty)
.
service or
vith a high corro6ion rate
:of,ten
have
tray6
that
are
built in
sectLons- Ihese tray6 caE be dismaltled aDil
irejlovejFlhtgg[jh.tl]e
4v.es6e1
[6trho].es for
lleaDing,
repairing
or-
replacing.
i.t;.,r.i;ir,- lr,rr,
''
r.a
FIXED TRAYS
(Nonremovabl-e
)
problem
usually
E
E.
JRIEF.PROCESS
DESCRIfIIOT{ OF-
A
JTPICaL
DISTILLATI0}I
.OR
'FRACIIONATIoN
COLU}rN
Heat
for.vapor.lzation i6 6r.rpplied by
heating the crude
feeal
6tock ilr
a
furnace.l*$ilprehgated
crude
(f,eed)
is charged ilto
the'bottoD
of
the
fractionatloD
colunn onto
the feed tray at it6
boiltng
poi-nt,.at
a
pres6ure
sughtly above
atmo6pheric-
This is called
the
I'f1ash
zone.I
In
the
fLash zolre, the feeal separates
into liquial
and
vapors.
the vaPors
rise
up under the bubble-caps
and
bubble
out through
the reflux liquld
on
each
tray- The
vapors rise
through
the
col.uilrl
contacting the doi|trflowing
reflux strean at each
tray;
as a
result the
tightest material"s
concen-
trate at th€..top
of
the colunn
(overhead
vaPor).
The vapor out
the top
of
the colt n'i6
condeDsed
into
liquid
by the
o-H- conden6ar.
The liquid
is
then
acctrmulated
ilr
the o.H-
reflux
accunulator-. Part
of
the
liquid
is retumed to the column'6 top tray
as
reflux-
The
reflux flow6
across
each trgy.ro-nititq:xray dowa.
the cofulul
by say of
dosncoBers
and btrbble_caps-
rhe
poiii6ii
6i
ule ioLrann
bet$een
the
overhead
and the feed
i6 called
ttte
t'rectifying
lection-'r
Thi6 is
$here
the
cou.ntercurrettt flolt
of
reflura
and
vapor reach an. equili.brium-
This means
the
liquid
head
on
each traY
i6
just
enouqh
to allow
the vapor
to
rise through the
liquid aod
the
.
vapor
.ve1ocity,.:isr,:iust
fast enough to allolt
sone
of the liquid
to
droP
through
the
same opening ilr the
tray. The
heavier
materials
concentrate
at
the bottom of
the
column
(bottoms
)
and the intermediate
materials
in-bet\reen- De6ired
"6ide
cut"
products
are \rj.thdralrn
at
aPpropriate
1eve1s
(drar,-off6).
The
portion
of
the
column
betreen
the feed and the
botton
tray
is
calLed
the
"Etrippihq
section.t' This
is
\,rhere
additional
light
haterial-.
are
relea6ed
a6
vapor
(6tripped)
from
the
beavier
liquid
portion
of
the
feed
by
the
addition of
stripping stean ioto
the
Isurge
section'
of
the
column-
The
portion
of the
feed that reaches
the
bottom
of the vessel
is
the residue or bottoms
liquid.
fhe top tray must
be
continuously
fed
lrith coollDg
reflux
liqui.d or
the
trays vould
soon become
dry-
Reflux must
be
increased
as side cuts
are
dlra\am
off
at several
1eve1s-
Thd
inateriaL on
each tray is at its
boiling
point
and the dollnflowing
material
is
constantly
changinq
composition
as
it
picks
up heat from
the
rising vapors. The
vapor is
always
hotter
than
.the
liquid on the tray
from shich
it is rising. The
vapors
are
coDstantly
being cooled by the cooler
reflux on each
tray. The
vapor on
the
top
tray
is
condensed
into
liquid.
The
fiquid
that
is
not
returned
to
the
colum[
as ref].ux is
one finaL
product-
P B; --P13
l'.'
:.1,-.
.,Vesse16
have fl can
be steamed.but
in
place.
iirl
i
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LI
r .
''yn
ri.i
r-
to
the
1.
2-
4.
5.
6-
7-
:.
10-
vessel
or
Drun Height
Process
NonBal
Instrument
NozzIe
Nozzle
liquid
Elevations
Levef
and
other
,
^|::.
Elevations
Custolner
Requirements
Ilanholes
are
generally
18 nominal
size
except for
columns
with removable
trays, in
uhiih a
savings may
be realized
by iltcieasing
the
size of the
manloIe to
permit
].arge
tray sectioD6
to be
removed.
In
those cases
generalLy
only
one
laiger rnanhole
i5
Provided,
preferably belolt
the
bottom
tray.
H. TADDERS
}ND PIATFORIIS
G.
I'IANHOI,XS
1-
Platforms
on
horizontal
vessels
anal
top
platforms
(above head)
on
vertical
vessels
should
be
square
or
rectangular.
P3B-1-013
I
-
custoher
via ?roject
l{alager,
Desiqn
coordinator
aod
Pipiug
Desiqm
supervisor*
*,',l,,,,
;i'
3,,
r
,
DATE
-J.
Revl
l.-r:_-1.,.'1
]oesroir
I
r
r,:_ i, r;.soIIPaE
,
8/10/2019 Flour PUMP&VESSEL -.pdf
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I.
HORIZOTIIAI
VESSEL ORIENTATION
,cenerally,
vessel
anal
nozzle
orientation
should
be as
follows:
1.
rnlet
should
be at
the
opposite
end
of
vessel
f'om
tlle
liquid
and
-
".po.
outlets
to
prevent'
i'short
circuiting"
of
the floi'''
They
shouLd
also
be
maximurn
distance
aPart-
2.
3.
4.
The inlet
is normally
located
on the
end of
the
vessel
a 'ay
from
the
pipeway. This
arraugement
then locates
the
Ievel
instruments
next
.
to-
the- operating
aisie
for
good
accessiSility
Per
s?-5'1'1'
5- The
setting
of the
suPPort
Iegs on
a horizontal_
vessel
is
normally
done
by the
computer
tut
sometires
we
stutly
and
orient
-vessels
beiore'thi.s
information
is
available
to
Piplng'
A
good
"rule
of
thutnb[
to
follow
is:
Leeel
.instr\reetrts
anal
boot should
Ue
a1 tUe
opposiie;
eaa
of
vessel
from
inlet.
There
is
les6 liquid
turbulence
at
the
outlet
end'
They
should
also
be
maximum
distance
apart.
'
To
alLov for
the
horizontal
grouth
due
to
ther&al
eq>ansion,
one
irrpport
of the
vess;l
is anciored
anil
the other
end
i6 allo 'ed
to
qr'oi,
ly
".y
of a
slide
Plate
and
glotted
holes
at
the
opPo6ite
Juppo.ll
e'av.ntage
should
be
taken
of
this
vessel
growth by
making
it'vork
for
you-
-For
exaEple,
by
anchoring
the
vessel
at the
support
,,.ur""t
thu
iipevay
and
tetting
ihe
vessel
gros
al'ray
from-the
Pipe\day'
the grovth
oi'tt"
ves".t
i{i}l
cance}
out the
grosth
of
a
lioe
from
the
tipeway
to
the rmanchored
end
of
the vessel.
?3B-1-013
@
.- The
6ize
'ossovdrs
biti6iit lidildis.-"
rhe
si
alves
anal equlPnent.
anal
for c
"t
t1,"""
pf"if"i1trs.shoultl
be kept
to
a minimre-
.The
viaU.r
(z':s"
io.iioo"1si-a."a)
is usually
onty
e@ughtqir;eroit
oPening
of
t}re
""ot
oi"
"o.r".
or to
provl<le
a-niai.ntrm
of-18"incba;6
clearance
betveen
r,.ndiiir
.na
pipi"g
such
as level
controller,
gage
glasslrevel
,
...3.
-,1
proj;ction
of.rio'lzLes
erteudin{'
thi6ughtirtoi
pletforus
mirst
be
such
exteuding
t
plqtforus
are abovt
the.Diitfoi:m
lever.
. -l :.J1.i'4,".: .j l
.
"
not
be iupDo:'tedl
from
platforns
unless
abso-
slritch
or
saflty.:rilves
-
PlatforniDg
qee.+
not
eatentl
underneath
{itch
or
safety-valves.
PlatforniDg
need
not
extend
valves
and equiphent
to
Dake
then
accessible.
'
ila;it";;;;;";.y.-:,,rf
it
is
fo-und
necessary
to
6uPport
piping
i.o. i
pl"tforrn, t'otify
tfr"
vessel
GrouP.
The vessel
Designer
..qay-have
to
"be;f--trl,:'
ahe
platform
st{rport-'brackets
rto
rtake
the
added 1oad.
8/10/2019 Flour PUMP&VESSEL -.pdf
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';,.
1.
r.
.l'
or
che
-ca11y
changing
6toring
Iiquids
and
&
€
vertical
the
horizontal
uithout internal
fractionation
6ervice
the
frac-
catalyst
(from
a
the
catalYBt
for
1.1-
3
Flat
B.ottom
oDen
toD:
For
storage
of
non-volatile
productg'
Flat
Bottoo
conical
top3
for
stoilge
of
loir
volatility
Pro'tuct-
Flat
Bottom
Floatinq
Roof:
For
storage
of
volatile
liquid6
'
Gas
tlolders:
These
have
flat
bottoms
an'l
roof6
or
dones
shich
rise
anE-EaII
ulth
the
quautitY
of
ga6
6tored'
1.I.4
SOUE
TSPES
OF STORAGE
VESSELS
P 9{9C,
a
spherical.
shaped
ves6el
6rPPorted
-by
a
series
of
fegs
around
the
"qo""ot, "'oi"f"o"tiias
presiurizea
gases? or
liquid
and
gas
-
?38-1-013
t.L.2
l€
gaae6
8/10/2019 Flour PUMP&VESSEL -.pdf
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,:','{;ii".riirjl+i.
:'i
''l/FiJoR
DESIGN
driors
vessel
rxeixrentxc
oEslcN
GUIDE
VESSEL,}IOUEIICLATI'RE
.
{r
.i,t.
r
::
.ijj.,;r
P g :
shape
anal
has
special
BuUet:
A
largr
:;::;;:-;--,ri***..--:a
-
."
resenbleE
a
alroP
of
nercury
resting
on
a flat
surface,
t ,pe
glpports.
ilseat
to contaih
pres6urized liquids
'
rroitzontai
veasgl'
c6ntiini.ng,p.ieaiurlzetl{ases,
or
Uquid
and
gas
.
.
..-. 1,.1.
:r:
1.1.5
VESSEL AND
IANK
PArrS.
.
.
,i
:.
I ,
,.
,,The,:cyrilalrlcal.pgrtion
9f
a.yq96e1
I
c/.-
]L
L
.F
,'
Heroispharical
Head:
Bpher:.
conicaL Head3 .Heaal
foracd
ToricooicaL
.Ileail:
Heatl
forEed
in
the
6bape-of,
a
cone
aEd
having
a
ffiAG-ra6;-?angent
to
tlr.
cotre.
rnal
thelI.
-
n.t
u";a
r;i
i#;i iliit;ii
"i'iii4piiid
ii"ri.a
o"
a
shell-
skj-rt: Cyliniter
BlJlilar
to
6hcu,
ihtch
vessels-
skirt Vent6:
of alangerou6
skirt
Access
openinq:
Circular
hole6
in
the
;i."n;@;t
etc. tn6l&
of.
slirt-
ls
used
for
BrPPdrtlDg
vertical
rL
'/
SDall circuf.r
hole5
ln tbe
skirt
to
preveDt collection
gases
rithfu
thc
6klrt.
Base
Plate:
Flat
plate
relded
to
the botton
skirt
to allos
rorkman
to
of
ve6seL
Eupports
and
b"JCq
on
the
foundation-
anchor' BoIt
chairs:
.
GuBBets
.nat
p1ate6
selded
to ba6e
plate
and
ekirt
t.EilA;-Ei
a".h.r
bolt attaciuent-
lnchor Bolts:
Bolts
i-mbeatttetl
in
concrete
foundation
and
boLted
to
il;;r;E6r
bolt
chairs
-
sadalLes:
steel
supports
for itorizontal
vessels,
P3B-1-013
I
I
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'l'Fi-rffi-'
DESIGN
-J
citidEs
$
.,1
iEssElj
ENGTNEERING
DESIGN
GUIDE
VESSEL IOI.IENCI.ATT'RE
"{
i
NUIIBER
2-1,1
PAGE
4
olTE
._5-?6
i,t,
.i
:l:
irsiile
Used
of
to
fractionatioD
prevent
vsPor
Iiquid
traY
of,
the
srDDort
icrli :]r
Gratirig
or
IIfi
iE-carlpisr:through-
ra8chig
rings, €tc.
,a
rtLre
he6b
pad
helal
Ln
placc
bettree tito
light
elisLaator
iliiengages
liquids
contaiue'l
irr
the
vapor'
66e
othcr
t 'Pc
of
sqrport
$hlcb
vapor
or
U6ed
to
6ubp;;t
to('er
packi-ng
such
a6
catalyst,
@i<ts
-
rtre
oiet
skirt Pircproofhq:
BrLch
or
concr'te
aPPIicd
iJi'Ide'
artd
outside
of
;Ef.a
6Ee""rE-a"rage
to 6kirt
in
the
event
of
a f ire
'
'
'
1?tatfort6:
-. '.tfottt
bolteat
to.
'nd
sirpPorted
by
cl'ips
o
the outalde
'
:fffifr;"et]'-c.a.Lirv
bcltid
justLeloi'
a
oanholc.
aid
't
rcricf
;1r;;
i;tiU.t'rai".e
oi
conacctiong
a'ttch
n'r't f,requ'at
scrv''ce
'
Lealtler6 and
caqes:
ItLurg-ttDe
ladders
with
cagc6
bu1lt
of
structural
-
-'ita
t"ltias
tlbeD
cuDbirrg
t}e la'liler
'
These
shap.s
to
Pravent
a
Dan
ar
"..
fott"a
to
anat supported
by
clip-
on
the
out6jde
of
the vessel'
Ir6eal
fo
aecesE
uP
arA
alown
to
tJle
Platforlns'
trays,
bubble
caPs,
etc-
1.1.6
ASI'E
BOII.ER
}ND
PRESSI'RE
VESSEL
CODE
Standard
rules
for
the
construction
of,
boilers
and
pressure
vc66e1s
divtated
into
sections
shich
establL6heE
desigEr forDulas'
loaterial
Eelection,allosablestressvalueE,rnetho'IsofcoDstructio['itrsPec-
iioo ulra
norra."t."ctive
examj.nation
procedures
for
preasure
contaliment
vessel-
column
Davitr
a hoi-stiDg
&vice
attached
by
heans
of
a socket
to the
iffiifitii..,i.I;;-;il;
-
used
eor
haniliaq
relLer
valves'
bubble
P3B-1-013
r
v.ssel.'
A Derforatea
tray
whLch
Provlde8
equal
dlstrilutlon
,ressel
are",
Bl-sere
o thc
tray
extend
above
the
to
fgrD
cavLtatLon
in
the
8/10/2019 Flour PUMP&VESSEL -.pdf
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'{c1:r.,1i..1
I
j
.
supDo;t
Leqs:
LcgE
vertlcal
.vesEel6.
Bade of
plpe.
Itarlhole Hlnoea
or Davlt6:
Itlnqe6
i.nd cover
platc
which
alLoss
cover
rianhole opeEilg.
or
structural
EbaPes,.used
to
slqrPort
bol-tirlg
used
or davit8
attached
.lo-.tlaDhoie
ffar,g.
plate to be
dtl.urld-dsldc
'fron
t-he
rnsuletioD Rinqs.
,
Ri.ngs
nade
of flat
bar
or
angte,
.attached
aroutrd
EF;iiEilc-ifiroferenEe)
of
verticar
vessels
and
siiaccd-aPProaiuatery
l2-;
-[- 7t'
'apart;
uee<t
io
et4port-the
eelqht
of
the veeaef
iD6uletloa'
vacuum Stiff.ner
Rilqs
t{irgs
Dade
of
flat
bar or
plate,
or
structural
"h-;E;;Ii;a=;ffi-the
circunference
of
ttt€
vessel.
rhe6e
rlngs
are
insialled
on
ves6els
operatlng
untler
e8ternal
Pressure
i order
to
prevent collapse
of
thl
vesseL.
vacute
stLffener
rings
are
also
uti.Liz.d
a6
LDEulation
6ulrPort
ringE.
FractioBatinq
Travs:
Circular
flat
plates
bolted
to
the
6heII
ihside
;f-i.."i$ftio-[EluDns -
useal
to obtain
vapor
liquid
contact
lrhich
results
in
fractlonation-
Dortacorler6:
Rectanqular
flat
plate6 bolted
to 5hel1
and
trays,
inside
6?-?ilfif6.,ation
coiunns-
used for
directing
process
liquld
and
to
prevent blPassing
of
vaPor.
P38-t-013
E
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'l'puuon
.,tlflIqil,.r
,Tf,AlNlNG,1,
I,IANUAI.s
P}IASE
III
HoRrzmEGSsELs
IIA}IDOUT
NUMEER
LE55ON
piee
OATE
5of5
Rev. 1/80
J.
'rD
=
Vessel
diameter,
"L"
=
vessel lenqth
rrs(
=
Distance from
tan- to centerline of
Normal
shefl thickness
vessel6
s=L/s
3.
Take the
pump
out of the
punp
roe and locate
vessel
out
of
the operating
aisle.
Do Dot
pocket pwlp
6uction
Lines- The vessel
or
be increased
to
elimjrate
a
condition-
RTACTORS AND AIVANCED
DESIGN
VESSELS
tan-
to
tan.,
support Ieg
it
near
t}le
base
of the
skirt height
may
have to
Thin shel1
thiclxless vessels
s
=
Dl4
Note:
In this case the vessel
head acts as a sti.ffelrer
to the shell
6. Vent is
located at the opposite
end
of
the vessel from
the
steam out
and
a
maximum
tlistance
a$aY-
SKTBT
TCIGITI AND
HEIGIIT OF TIORIZOMAL
VESSELS
Skirt height and
height of horizontal vessels
are sho'rn ou
the flo ,
diagrah-
The
Process Englneer
determines irhat the
skirt
height
rill
be
by the N-P-S-H-
(Net
Positive
suction
Head)
-
This
is
the
liquid head
required
to
keep
t}1e
punp
suction
pri,iled-
Ptutp
suction
lines fron the
vessel bottoms
shall
have a
8.0.?-
minimun of 8'-0" above
H-P-F-S-
If
this
requirement
is not met, there
are three aLternatives:
l.
The
vessel
or skirt height
can be increased
to
meet the 8'-0u
head
rooro requirement-
2- Block the
operating ai6le
vith
a
lot
suction
line.
K.
tleaq,
\ra1l,
vessels sith heni-spherical
heads
are a speciaf
design
challenge.
Careful
consideration
should
be given
to
1adder6,
platforns,
pipe
supPorts,
etc. No
velding
to the shell- welding
to the
heads
and
skirt
only.
P3B-1-013
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'1.
ruuon
PIPING
TRAINING
I.IANUALS
PIIASE ]II
NIJMB
E
R
Lrssot
7
PAGE
1
DATE
Rev.
HORIZOMAL
VBSSEI,S
HANDOOT
t/
B.
A.
1.
2-
3-
4.
1.
2-
3.
1-
2-
3.
4-
VESSEL ORIENTATION
OBJECTIVE
The objective
of this
session is
to
help
you
become
rnore
famlliar
sith
the Fluor
approach to
vessel
orientation, based
or Fluor Standard
Drawings.
The haterial
anal
instruction
you
receive
from thj.s session shoulal enable
you
to:
1.
K oq
hos
to
assimilate
the
information
to start
a vessel
orientation
study.
2-
lroperly
prepare
orientati.on studies of both vertical
and horizontaL
vessels.
TRAY TYPES
BIEBLE.CAP TRAY
ADVANIAGES DI SADVANIAGES
1-
2.
Very
efflcient
Need
not be
in6talled
level
corrosi.on
not a factor
uost efficient of all
tlpes
Ine>q)ensive
and
lightr,,eight
Need
not be installed level
Corrosion nol a factor
Inexpensive
Lightweight
Good
for
healy
liquids
Expensive
Heavl' and
bulky
cast iro[ caps
occasionally
break
ltounting bolts rust
VA],VE TRAY
SIEVE
TRAY
1-
None
1.
2.
tlust
be install-ed leve1
corrosion
a
factor
P3B-1-013
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'l'FLUoR
PIPING
IRAINING
IIANUALS
PHASE
III
NUMBE
R
LESSON
7
PAGE
3
DATE
Rev.
HORIZONTAI
VESSELS
HANDOT}T
7/
1.
2-
3.
6-
F.
INFORI.IATION REQUIRED TO START
IESSEL ORIENTATION
INFORI'IATION
*Prirary
source
Designer
SOURCE
to
the
-
Piping
Design super-visor
or Roller
Board
-
P
j.ping
Design supervisor
anal Fluor
Standards. Job
Book*
-
Project
llanager,
Desiqn
coordunator
or Piping
Design
supervisor*
- Piplnq
Design Supewisor
- vessel
Design
supervisor
or
Piping
Design
supervisor*
- Floi,sheet*,
Process
Engineer or
vessel
Dra',ring
(vertical)
-
vessel
Dralring*
or
Process Engineer
-
Vessel
Drat
ing, Flow
Diagram*
or Process
Engineer
-
vessel
Dra\.ring,
?rocess
or
Instrument
Engineer,
Instrument
standard
Drarings*
-
custoher
via Project l'lanager,
Design
coordinator
and
Piping
Design
supervisor*
FLov Dlagrafis
Job Specifications,
Drafting
Instruction6 and
standards
?relirinary
Job
Informatiotr
Room
vessels
and top
platforms
(above
head)
on
be
square
or
rectangular.
Flovsheet
Transpositioo
vessel
Drasing
or
vessel
Quote
Dralring
skirt
Height
or Druin Height
Process
Nozzle
Elevatiotls
Nomal
Liquid Levef
and
other
Iiquid Levels
9. Instrlment
Nozzle
El,evations
Requlrements
0.
Customer
G.
}IANHOLES
I{anholes
are
generafly
18rr nominal
size
except
for columns
\rith
removable
trays,
in
whiih a savings
may
be realized
by increasing
the size
of the
manhole to
permit
larqe
tray
sections
to
be
removed-
In those
cases
generally
only
one larger
manhole
is
provided,
preferably
beloH
the
bottom
tray.
I,ADDERS
AND
PLATFOR},IS
1-
Platforms
on horizontal
vertical
vessels
should
H.
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lluMBER
2-1-1
PAGE
1 of 5
DATE
g-76
VESSEL ENGINEERING
D€SIGN
GUIDE
'l'ru.Pn
DESIGN
GUIDES
1.1.I
GENERAI,
VESSEL
NO}IENCI,ATT'BE
Process
Vessel:
A contailrer
for
han'lling
or
cheDLcally
changing
lIfrIE-li?@ses
uithin
a
process Ey6ten'
Storaqe
Vessel
enq
q 9leSglgE'
A container
for
storjng
liquid6
and
A"*-F;ffi
to
;-?;i1o"ijrgiEe
process svsteo'
vertical
vessel:
A ves6el
vhose
longitudi_nal
axiE
is
in
the
vertical
poBitlon-
tlorizontal
Vessel:
A
ve6ae1
uho6e
longitudiral
axis
ls
la
the
horizontal
'
position.
1.1.2
SOt{8
rr?Es
of
PRocEss
vEssELs
FractionationcolulEl.Generalliaverticalve66elcontaillngtraYsor
''t
txt ."ct_"
frorn
the
process 6ystelr
a
certain
packing t hen
in 6ervi(
requireal
fraction
Euch
aa butane
or
Propane
'
RefluxAccunulator:GenerallyahorizoEtalve66el'andt'ithoutiDterDaL
"".tf,tri=--"*;i."-ioir""i"
anal
tranebltB
back
to
a fractionation
:;i;; th"
fraction
which
is
Proce6sed
by
that
colunm
'
Reactor:
a vertLcal
vessel
contaitd'tg
catalyst'
tdhich
ih
service
i-iii6g""
the
nolecular
structure,
'nd
thcrefore
chaDge6
ttre
trac-
tions
in a
Proces6
sYste$'
Redenerato :
A
vertical
vessel
coDtalning
used
catalyst
(from
a
iiid)fri"r,
itt-"".oi""
t"gt"ttttc6
(restoreg) the
catalyst
for
re_use
in
the
reactor-
1.1.3
SOI{E
TYPES
OF SMRAGE
TANITS
Flat
Botton
oDen
Top:
For
storage
of
non_volatil'e
productE'
Flat
Botto$
cooic.l
Top:
For
ltorag€
of
lotr'
volatility
product-
Roof:
For
storage
of
volatile
liqui&'
Cas
Holders:
These
have
flat
bottoms
and
roof6
or
dones
whlch
rise
;A-?;TIti-t}r
the
guantity
of
gas
6torcd'
SOI.IE
TYPES
OF
STORAGE
IESSELS
sbheres: tr
sDherical
shaped
ves6e1
supPorted
by a
series-of
legs
#ffi=;.-.;;;;i,
*r'ilt'"o"t'in"
preiiurized
qases' or liquid
and
gas.
r-1,4
P3B-1-013
E"
8/10/2019 Flour PUMP&VESSEL -.pdf
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'l'ruron
DESICN
cut0cs
VESSEL ENGINEERI
G DESIGII
GUIDE
VESSEL
NO}'ENCLATI'88
NU|{BER
2-1-1
PAGE
4
DAIE
5-76
Seal
?ans:
column
6hell
bypassing
up
Distrilutor
Tray:
a
perforated tray
which
provideE
equal
alistri.butLon
;i-iIqnIa
ov.r
the vea6el
area-
RLeers
on
th.
tray
ettenal
abov€
the
Itqqtd Lev.l
to
perEit
lr 63age
of vaporE rislng
uprrard-
chi-onev
Trav:
A tray coqroscil
of
chimncy6
e8teldlng
above
th. Uquid
ledI;f
the tray
pemlttirg
pa66age of the vaPor6 upra.d-
the tray
collectd
aual
r.movea
afl
liquLl
product
from
a
al,ccLfic
Portion
of
the
vessel-
FIat
pLates
bolted
or
lrelded to Lnside
of
fractionation
belou
dor,Dcomer of
loeest
tray-
Used to
Prcvent
vapor
through
the
alo$ncoDer.
vortea
Breaker:
I alevice
locateal
E6
IEIlon
ceuerally
coasL6ting
the
6hape of
a cro66.
fhe vorte8
Iiquid
pa6sing
th 'ouqh
the outlet
ilsLde
a ves3el
at
tbe
outlet
of
plate.
sctdctl together
to
fotn
brelker
preventa
cavLtatLon
jn
the
coEnactlon.
ui6t
Elinlnator:
I xire
mesh
pad
hcld
ln
place
betue.n
two
liqht
srla;:--fr;-E.t
elLoLnator
disengagea
liqulats
contalned
in
the vaPor-
support
Grld:
Grati.ng
or
sooe
other tlPe
of
Blqrport
-uhlch
vaPor or
ITfrIE-5laas
throuEh. u6ed
to
6upport
to er
PactLng
such
as catalyst
ra6chig
rings,
etc.
Shirt
Fir.prooflrrg:
BrLck or concrete
applLed
hEide aDd
outsL'le
of
;II.t
t.Eeve-"Ld"ra9€
to .kirt
Ln the
evEitt of
a
fLr.i.
P1atfo 'Es: Platforo6
boltcat
to
aad
4Pporteit by
ctiPs
ou the outsi-de
6?ltle ve-r""l.
cenerally
located
Just
belo,
a oaDhole,
aat
at
rell.f
vrlves
or othea valv.6
or
connections
l,lrlch
nacal
frequeDt
6ervLcc.
Ladiler5 apd
Caqes:
Rung_tlDe
lqdders
lrith cage6
bulLt of
Etructural
;Eapcs
to
p;evcnt
a D.n
f,rom
fallilg
whe
cli-ubirtg
the Ladder.
These
are bolteal
to and supported
by cliPs
on
the outside
of
the vess61_
uaed
for
acce6E
r{,
and
down
to
the Platforns.
Colunn Dry :
A
hoisting
device
attached by
means of
a socket
to
the
JiiZfionatioo
col;mns
-
used
for
handling
reli.ef
valves.
bubble
bubble cap6,
etc.
1.1.6
AS}IE
BOILER
AND PRTSSURE
VESSEL
CODE
top of
tral,s,
standard
rules for
the construction
of
boilers
and
Pressure
vessels
divlded into
section6
$hich e6tabllshes
design forDulas,
material
selection,
alLowable
stress
values, methods
of
construction,
insPec_
tj,on
anal
nonilestructive
exanination
procedures
for
Pressure
contaii'nent
vessef.
P3B-1-013
I
I
I
8/10/2019 Flour PUMP&VESSEL -.pdf
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'l'rluoa
PIPING
TRAINING
TTANUALS
PHASE
III
NUMBER
LEssoN
7
PAGE
5 Of
oATE
Rev-
HORIZONTAL
VBSSELS
-----ffiotn
5
L/
rrD
=
vessel
diameter,
'rl-r
=
vessel
length
,,S,,
=
Distance
from
ta -
to centerline
of
Normal shelf
thickness
vessels
s=L/5
Thin shell
thicknes6
vessels
s
=
Dl4
Note:
In this
case
head acts
as
to the
shell
tan. to tan.
support
Ieg
the
vessel
a stiffener
5.
vent
is
located
at the
and
a
lnaximlnn
alistance
opposite
end
of the
vessel
from the
steam
out
a$ay.
HORIZONTAL
VESSELS
.
(.
skilt
height
and
height
of horizontal
vessels
are
shown
on the
flos
diaoram.
The
Procesl
Enqineer
determine6
what
the
skirt height
t'til}
be
Uy itre
N-p.s.tt.
(Net
Positive
suction
Head).
This
is
the liquid
head
requi.red
to
keep
the
Pump
suction
primed-
PumP
suction
lineE
fron
the
vessel bottoms
sfratl
i'r"vl a
B-o-P. ninimui
of 8'-0" above
H.P'F'S'
If
this
requi.rement
is
not met, there
are
three
alteroatives:
1.
The
vessel
or
skirt
height
can be
increased
to meet
the
8'-0'
head
room
requirement.
SKIRT
}IEIC}l1 AND
IIEIGHT
OF
2. Block
the
operating
aisle
with a
1o r
suction
3. Take
the
pump
vessel
out of
1ine.
it near the
base
of the
Do not
ptstP
suction
lines
be increaseal
to eliminate
a
REACIORS AND
ADVANCED
DESIGN
VESSE1S
Hea\rr-
\raI1 vessels
with
hemispherical
heads
are
a speclal
design
chal]enqe_
careiul
consideration
should be
given
to
ladder6,
platforms,
Pipe
supports,
etc.
No
\,,elding
to the
shell.
|elding
to
the
heads
and
skirt
only'
out
the
of the
pump
rot,
and locate
operating
aisle.
The
ves6e1
or
skirt
height
may
have
to
condition.
P3B-1-013
I
8/10/2019 Flour PUMP&VESSEL -.pdf
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'l'rluon
PIPING
TRAIXING
flANUALS
PHASE
IIl
HORIZONTAI
VESSEiS
HANDOI'T
NUI.,IBER
Lgssox
7
PAGE
1 Of
1
DATE
Rev.
1/
STEPS
TO
ACCOI{PLISH
HORIZON]AL
VESSEL
STIJDY
2-
1-
4-
6.
7-
a.
b-
c.
Update
your
floi,
diagram
from
rllaster,l
Compare
vessel
outlille
to
flow
diagram
-
a-
Vessel
I.D,
b-
Tangent
to
tangent
dilnension
c.
N.L.L-
d.
Size,
rating
and quantity
of
nozzles
Calculate
elevations
centeru.ne
of
vessel
based
on
mini-oum
height
on
f1o ,
aliaqram
Process
nozzles
based
on
vessel
outtine
-
verify
or
6et
instrument
nozzles
based
on
standard
dra\ring
flolr
diagram
and
instrunent
Determine
vhat
items
require platform
or
Iaalder
access
study piping
transposition
Drav
vessel
outline
to
scale
and
get
xerox
copies
On these
copies
do
rgug\
skeqches
of
piping
and
nozzle
arranqements,
comDrne
anal
change
sketches
for
optijnun
design
using
piping
iogic.
Pipj.ng
logic
considerations
or
priorities
.
F1olr
diagran
Stress
Economics
Support
and stability
Lines
run
at
standard
Looks
Operation,
Daintenance
Job
standards
efevations per
unit
plot
drawing
and
safety
Your
order
of
inportance
will
change
in
each
situation.
For
instance
econonics
-
vrould
be
more
important
than lgoks
on
a large
a1loy
line-
'
on
a smaLl
carbon
steel
1ine,
looks
nay be
more
irnporiant
than
economics-
Conunence
actual
study.
you
must
be
donrt
worry
about
draftihg qualiry,
dirtyr' but
legible
and complete.
accurate
and
drav to
scafe;
houever,
li.Ilework,
or lettering.
,,Rough
and
9.
P3B-1-019
a-
b.
c.
d.
f.
s-
h.
8/10/2019 Flour PUMP&VESSEL -.pdf
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GUIDE
2-4.1.2
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ENGINEEIUNG
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