PROJNo.:__________ CALC No.:_________
Self Chck:__________ Date:________
Chkd:________ Apprvd:________ Date:________ Date:________
INTRODUCTION TO HORIZONTAL HORIZONTAL VESSEL SIZING PROGRAM Progr Program am Name Name Version Reision A"or Da"e
#REF! #REF! #REF! #REF! R As$ina%% #REF!
Pr$ose -h(# pro)ra (# de#()&ed to a##(#t /(th #(0(&) of 2 pha#e a&d pha#e hor(0o&tal #eparator#. -h(# pro)ra (# 5a#ed o& the )'(del(&e# for hor(0o&tal hor(0o&tal #eparator# (& AP% 12J
CLIC& ON HIGHLIGHTED 'UTTONS
Lee% Con"ro% Gi(e%ines -he follo/(&) l('(d level# are o3ered o3ered o&l4 a# a& appro"(ate appro"(ate )'(de. here pro7ect pro7ect #pec(c level co&trol data (# ava(la5le9 the follo/(&) a4 5e ()&ored. ()&ored. or e"pla&at(o& of l('(d level# cl(ck o& 5o"e# h()hl()hted (& 4ello/.
Ins"r)"ions *or se
1. $ $ $ $ $ $ $
%&p't re'(red proce## data (& the ;Data %&p't; #heet: l'(d
(#co#(t4 Separator operat(&) pre##'re Separator Separa tor -4pe -4pe $ (e 2 or pha#e Separat(o& Dev(ce >e##el A#pect Rat(o ?Le&)th+ D(aeter@ Level co&#tra(&t# ?See d(a)ra# d(a)ra# oppo#(te or '(del(&e#@ -here are 2 opt(o&# for e&ter(&) l('(d level co&#tra(&t#: 1@ Defa'lt level co&#tra(&t# a4 5e cho#e& 54 cl(ck(&) o& the ;Defa'lt Level Co&#tra(&t#; 5'tto& 2@ B#er #pec(ed level co&#tra(&t# a4 5e e&tered d(rectl4 $ Re'(red O(l = ater ater or l('(d ?for 2 pha#e #eparator#@ Re#(de&ce -(e# $
+ Pase Se$ara"or *.D or ** (& LL
LLLL Settl(&) e()ht for l()ht pha#e or ** (&
ater No00le 1* fro ve##el 5a#e
. %f e(ther the AP% cr(ter(a or other cr(ter(a (# &ot et ad7'#t d(a a&d+ or a"(' O(l+ %&terface level# a&d rer'& pro)ra 1. When actual liquid levels are known, these may be entered by clicking on the 'enter liquid levels' button in the 'Data 'Data Input' sheet. This will take take the user to the main calculation sheet and the liquid levels can be entered in the highlighted cells. nce these are entered, go back to the Data Input !heet and complete input. "oto '#alculations $1% sheet' and enter the vessel diameter. diameter. There is no nee d to e&ecute the program since this calculates liquid levels based on the le vel constraints. . The water outlet no((le is )&ed * 1+mm above the vessel base. This may be ad-usted to a user preerred value by overwriting the deault value in 'calculations$%' worksheet worksheet Limi"a"ions 1. Doe# &ot take (&to acco'&t ve##el head# therefore the #eparat(o& vol'e '#ed (& calc'lat(o&# (# co&#ervat(ve FEED'AC&- A%% *ee(.a)/ so%( .e sen" "o "e O0ner $/ssigned #ustodian%0 $ #ee Rev(#(o& Stat'# #ht.
D
%L
e(r
L%L
6 (&'te heav4 pha#e hold'p or ** (&
. %&p't a& (&(t(al )'e## for the ve##el d(aeter 5a#ed o& the e#t(ated d(aeter a&d e&ter a"(' (&terface a&d l('(d level# a# a pe rce&ta)e of the ve##el d(aeter. d(aeter. . (t the ;E"ec'te Pro)ra; 5'tto& a&d check re#(de&ce t(e# to #ee (f re'(ree&t# are et. ( Note1: the calculated default liquid levels are based on the user input level constraints) ( Note2: the program will give a warning if input dia is too small (based on user input level constraints))
1 $ (&'te hold'p l()ht pha#e or 2* (&
LL LLL
LL%L
Dead O(l Le&)th
1 (&'te hold'p or * (& -+- Le&)th Le&)th Separat(o& Le&)th
, Pase Se$ara"or *.D or ** (& LL 1 (&'te hold'p or 2* (& 1 (& hold'p 1 (&'te hold'p or ** (&
LL D LLL LLLL
ater No00le 1* fro ve##el 5a#e -+- Le&)th Le&)th
PROJNo.:__________ CALC No.:_________
Self Chck:__________ Date:________
INPUT
DATA
Chkd:________ Apprvd:________ Date:________ Date:________
SHEET
C%ien" 1o. NoPro2e)"Vesse% NameTag NoCasePROCESS DATA
Operat(&) Pre##'re
?5ara@
6
O(l >(#co#(t4
?cP@
O(l
?k)+h@ ?F)+h@
* 191
O(l De&#(t4 a# De&#(t4
?k)+@ ?k)+@
28.** ,6.2
*.*,
ater
*
ater De&#(t4 ?k)+@
1***.**
SEPARATION &3Va%e 4m5s6
2 or Pha#e
,
a#$L('(d Separat(o& Dev(ce
(ree#h De(#ter
hase !eparator
Defa'lt
A#pect Rat(o ?L+D@
*.1*,
Wiremesh D
?Opt(o&al@ Selected *.11
+78
CONSTRAINTS Li9i( Lee%s From "o:
Gater o'tlet &o00le to L%LL or LLLL %&terface lo/$lo/ to (&terface lo/ ?LL%L to L%L @ (&terface lo/ to (&terface h()h ?L%L to %L@ %&terface ()h ?%L@ to e(r e(r to O(l Lo/ Lo/ ?LLLL@ O(l lo/ lo/ to o(l lo/ ?LLLL to LLL@ O(l lo/ to o(l h()h ?LLL to LL@ O(l h()h to o(l h()h h()h ?LL to LL@
<(& he()ht ?@ 1*
<(& -(e ?#ec#@ *
N+A
1* 1* 2*
N+A * 6* 6*
<(&. hold'p t(e for o(l do/&#trea of e(r to preve&t )a# 5lo/54 (Required for dead oil length calc) Minimm Resi(en)e5 Ho%($ Times O(l Re#(de&ce -(e ?(&'te#@ ater Re#(de&ce -(e ?(&'te#@ 2 Pha#e L('(d old'p -(e ?(&'te#@
1 1
?Not Re'(red@ ?Not Re'(red@
2$level to 3I33 or 4 phase separator or 3333 or phase separator% NOZZLE DATA
G%&let No00le $ a" allo/a5le rhov2 ?k)+#2@ >apo'r O'tlet No00le $ a" allo/a5le rhov2 ?k)+#2@ L('(d O'tlet &o00le $ a" allo/a5le veloc(t4 ?+#@
6*** ,* 1
25or no separation device ma& allowable rhov 6 1
*.1*,
PROJNo.:__________ CALC No.:_________
Self Chck:__________ Date:________
C A LC U LA TI ON
C%ien" 1o. NoPro2e)"Vesse% NameTag NoCase-
Chkd:________ Apprvd:________ Date:________ Date:________
SHEET
8 8 8 8 8 8
Vesse% Si;ing Varia.%es
E#t(ated >e##el D(aeter B#er Selected >e##el D(aeter Dead O(l Le&)th >e##el Separat(o& Le&)th <
?@ ?@ ?@ ?@
* <<88 * **
Maimm Li9i( Lee%s =8 ,> Not Re'(red
Ca%)%a"e(
O(l Re#(de&ce -(e ?N%L to NLL@ ater Re#(de&ce -(e ?Iot to N%L@ -otal L('(d Re#(de&ce -(e ?Iot to NLL@ (To NLL for 2 phase separator onl)
?(&@ ?(&@ ?(&@
N5A N5A #DIV58!
!"# 12 $ Recommended
(min)
1%&& 2 phase
?@
1
S%g Han(%ing Ca$a)i"@
ro NLL to LL
7ote 10 / good starting point is 89 or :I3 and ;9 or ::33
User S$e)i?e(
N+A N+A *
