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    MP 12-P-02 TDS 1 of 1

    June 1998 Page 1 of 7

    Technical Data Sheet (T1202M01) - Oil and Ga Se!a"ato"

    Met"ic #nit

    $acilit% &a'e Pu"chae O"de" &o

    *ocation +e,uiition &o

    te' &a'e Mo.il P"o/ect &ote' &o ont"acto" P"o/ect &o

    1 Deign +e,ui"e'ent

    2 Type: Separator Scrubber Liquid Knockout

    3 Trap Flash Vessel Other:

    4 Orientation: Vertical ori!ontal

    " #hase Separation: T$o Three

    % &a'( )llo$able *orkin+ #ressure: ,,,,, k#a+ - ,,,,, ./

    0 &a'( as #ressure rop k#a:

    5 Super6icial as Velocity 78sec as per )#9 12:

    ; &ini7u7 Liquid o ?es

    14 #ara66in #roble7: >o ?es 9ndicate /loudpoint ./:

    1" Foa7in+ Tendency: >il &oderate Se@ere

    1% A'ternal 9nsulation: >o ?es Thickness 77:

    10 9nsulation Type: ot /old

    15 9nternal /oatin+: >o ?es

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    MP 12-P-02 TDS 1 of 1

    June 1998 Page 2 of 7

    Technical Data Sheet (T1202M01) - Oil and Ga Se!a"ato"

    32 &a'( Liquid in Vapor l87C:

    33 O!e"ating ondition

    34 >or7al &a'i7u7 &ini7u7

    3" Operatin+ #ressure k#a+:

    3% Operatin+ Te7perature ./

    30 as

    35 Flo$ 77C8d:

    3; ensity k+873:

    4= Speci6ic ra@ity - ST#:

    41 &olecular *ei+ht:

    42 Viscosity cp:

    43 Oil8/ondensate

    44 Flo$ o ?es

    "4 nte"nal Deign +e,ui"e'ent

    "" 9nlet i@erter: >o ?es 9nlet istributor: >o ?es

    "% istribution Ba66le: >o ?es *a@e Ba66le: >o ?es

    "0 o$nco7er: >o ?es Aquali!in+ #ipe: >o ?es

    "5 *eirs: >o ?es Oil Buckets: >o ?es

    "; &ist A'tractor: >o ?es

    %= Oil Outlet Vorte' Breaker: >o ?es

    %1 *ater Outlet Vorte' Breaker: >o ?es

    %2 Sand o ?es >u7ber Sand Flush >o!!les:

    %3 >u7ber Sand rains:

    %4 Sand

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    MP 12-P-02 TDS 1 of 1

    June 1998 Page of 7

    Technical Data Sheet (T1202M01) - Oil and Ga Se!a"ato"

    &ote

    +eiion *og

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    /o77ents

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    1 /O&&A>T: ) separator /O&&A>T: Scrubber E a /O&&A>T:

    2 is a @essel used to separate @essel desi+ned to handle knockout is th

    a 7i'ed phase stea7 into 6luid strea7s $ith hi+h $hich 6alls int

    +as and liquid phases that +asEtoEliquid ratios( The 6ree $ater an

    are relati@ely 6ree o6 each liquid is +enerally entrained knockouts( Fr

    other( ThreeEphase as 7ist in the +as or is 6reeD is a ter7 6or a

    separators separate +as 6lo$in+ alon+ the pipe $all( separate 6ree

    6ro7 t$o i77iscible liquids These @essels usually ha@e strea7 o6 +as

    o6 di66erent densities e(+(D s7all liquid collection

    +asD $aterD and oil( T$oE sections(

    phase separators re7o@e

    the total liquid 6ro7 the +as(

    /O&&A>T: Trap E /O&&A>T: Flash Vessel E

    3 typically used in pipelines a @essel used to separate

    $ith @ery hi+h +asEtoEliquid the +as e@ol@ed 6ro7 liquid

    ratios to re7o@e only 6ree 6lashed 6ro7 a hi+her to a

    liquid 6ro7 the +as strea7D lo$er pressure(

    and not necessarily all the

    liquid( Traps pro@ide a

    place 6or 6ree liquids to

    separate and accu7ulate(

    " /O&&A>T: *here required by local situations or o@ern7ent T: Slu+ Flo$ E 9n

    so7e installationsD the

    separator desi+n liquid

    handlin+ capacity should

    consider the possibility o6

    slu+ liquid 6lo$( The de+ree

    o6 slu+ 6lo$ $ill be a 6unction

    o6 the pro6ile o6 the upstrea7

    pipin+ or +atherin+ syste7(

    There are accepted

    7ethods o6 appro'i7atin+

    slu+ @olu7es( 9n se@ere

    slu++in+ circu7stancesD

    slu+ catchin+ 6acilities are

    installed upstrea7 o6

    separation( or7al Operatin+ #ressure is thecontinuous operatin+ pressure 6or this ser@ice(

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    /o77ents

    #a+e "

    &a'i7u7 operatin+ pressure is the hi+hest

    continuous e'pected pressure 6or sustained

    operation $ithout causin+ shutdo$n or relie@in+

    conditions( The lar+est sur+es occur at

    7ini7u7 operatin+ pressureD there6ore the

    7ini7u7 operatin+ pressure is used in

    deter7inin+ the 7a+nitude o6 sur+e @olu7es(

    "3 /O&&A>T: 9nlet Fluid Flo$ and /o7position E

    "4 /ritical to the separator desi+n are an accurate

    assess7ent o6 inlet 6luid 6lo$rates and

    co7position( For a separator in a $ellstrea7

    applicationD +asD liquid hydrocarbonD and $ater

    6lo$ rates as $ell as a reco7bined 6luid

    co7positional analysis should be taken 6ro7 a

    stabili!ed $ell 6lo$ test( 9n a plant or battery

    inlet applicationD all $ells in the syste7 7ust be

    considered( For a separator in a plant process

    ser@iceD inlet 6luid co7positional and 6lo$ data

    $ill co7e 6ro7 the process 6lo$ desi+n(

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    /o77ents

    #a+e %

    nockout E a

    e type o6 separator

    o t$o cate+ories:

    total liquid

    ee $ater knockout

    @essel used to

    $ater 6ro7 a 6lo$

    D oil and $ater(

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    #a+e 0