daily activity report january 2014

7/23/2019 Daily Activity Report January 2014

1/56

South Sumatera NGL Project

Operation Team Daily Activity Report

01st January, 2014 (Day Shift)

ACTIVITY TODAY R!AR"S

1 Plant Status. The #ractionation Plant Runnin$ Normal

2 Total Production Hours. 11.15 Hours

3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 01st, 2014.

4 Daily %cti&iti#s.

%ssist a'. T#chnician for sa$lin at *! +##d Pu$, Static i-#r P! Tan/s #ry 4 Hours.

0.45 % +ractionation Plant Start $

0.4 % Sicth +illin P! Product +ro Tan/61 to Tan/62

5 Daily o Sh##ts.

0.00 % onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r.036PDT6532 (22.53 8nH29)

9utstandin Pro'l# +ractionation Plant.%&'()'*(%+ Strainer ,p-tream !eterin$ LPG to Ga-.om !u-t /e Replace 0Strainer have +1 Cleanin$2

+'%('*(%+ 0OPR3PSG3(&42 Gate valve line recycle Tan5 % 0+3GA6378(82 plea-e repair .ue to har. to operate.9

+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a- arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (114 Psi)= 036?65504 (115 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (.2 Psi).

0.00 % onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 250 = Th# $r#ssur# at +ir# @at#r Distri'utionH#ad#r is 120 Psi

0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 404.03 Psi= Diff Pr#ss : 1A.0A inH29 and +lorat#

%&r : 0.50A2 Scf)

%8'(4'*(%+ 0OPR3PSG3(7*2 @ P37((% A 0NGL #ee. Pump A2*ot %&aila'l#.

%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#adyr#$lac#d,und#r onitorin no).

(8'(&'*(%+ 0OPR3PSG3(%(2 @ AT37+(% 0RVP AnalyBer Do;n-tream Static !i1er2 is still nfinish#d to s#ttin and cali'ration.

(8'(&'*(%+ 0OPR3PSG3(%%2 @ AT37*(7 0Con.en-ate RVP AnalyBer2 Still n##d to


2/56




1 Plant Status. The #ractionation Runnin$ Normal

2 Total Production Hours. 22.5A Hours

3

4 Daily %cti&iti#s.


0.4A P 6 12.2 % Start P64504 7, "irculat#d Tan/61. for sa$lin a'. $ur$os#

12.00 %


3/56



02nd January, 2014 (Day Shift)


1 Plant Status. The #ractionation Plant Runnin$ A/normal

2 Total Production Hours. 12 Hours

3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 02nd, 2014.Note: Total moving level of Tank-3 = -0.38 MT, Tank-4 = 0.30 Total LP P!o"#$t in$l#"e" a moving level = 320.24 MT

4 Daily %cti&iti#s.


0A.45 % Sicth +illin P! Product +ro Tan/62 to Tan/61 du# to Hih Bthan# "o$osition (9ff S$#c Product)

03.00 P Start "irculation P! Product at Tan/62

04.05 P Sicth +illin P! Product fro Tan/61 to Tan/62 (9n S$#c Product)

5 Transf#r a P! Product fro Tan/64 to D#$ot P! P. ayan (200 T). 04.10 P Start Transf#r P! Product to Do!as Pulau ayan fro Tan/64 (200 T)

04.25 P Start 8nC#ction #rca$tan to Do!as Pulau ayan (Bstiation Sto$ 8nC#ction #rcha$tan on 0.04 P)

5 Daily o Sh##ts.

0.00 % onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r.036PDT6532 (22.3A 8nH29)

9utstandin Pro'l# +ractionation Plant. %&'()'*(%+ Strainer ,p-tream !eterin$ LPG to Ga-.om !u-t /e Replace 0Strainer have +1 Cleanin$2


+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a- arrel-2



0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 412.4 Psi= Diff Pr#ss : 15.1 inH29 and +lorat#

%&r : 0.455 Scf)


%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump2 8ndication #a/a# on #chanical S#al (#ch s#al alr#adyr#$lac#d,und#r onitorin no).

(8'(&'*(%+ 0OPR3PSG3(%(2 @ AT37+(% 0RVP AnalyBer Do;n-tream Static !i1er2is still nfinish#d to s#ttin and cali'ration.



4/56






3

Note: Total moving level of Tank- 1 = -1.21 MT, Tank-3 = -1.88 MT. Total LP P!o"#$t in$l#"e" a moving level = 34&.24 MT.

4 Daily %cti&iti#s.


0.0 P Sto$ P64501 %, +inish "irculat#d Tan/62.

12.00 % /l-9

Note: Total moving level of Tank-3 = -2.63 MT an" Tank-4 = -1.13 MT. Total LP P!o"#$t in$l#"e" a moving level = 66%.60MT.

Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 02nd, 2013.

Total %ctual Production P! fro *!: +(%984 !Tand "ond#nsat# :%(:(97) >/l-9

0.1 P 6 05.2 % Start P64502 (


5/56






3

4 Daily %cti&iti#s.


11.05611.20 % Stich D#67utani#r Stora# Pu$s % to 7 ("h#c/in otor at D#67utani#r Stora# Pu$s %)

11.10611.20 % %ssist a' T#chnician and Suryor too/ sa$l# P! Product at Tan/62

11.22 % Sto$ "irculation at Tan/62

02.25 P 6 04.50 P %ssist 8nstru#nt T#a to "ali'ratin +8"64011 (


6/56






3

4 Daily %cti&iti#s.


0.41 P Start P64502 (P! /l-9

Note: Total moving level of Tank-3 = -1.19 MT. Total 'e-'#n = &2.43 MT. Total LP P!o"#$t in$l#"e" a moving level =629.24 MT

Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 03 th, 2013.

Total %ctual Production P! fro *!: *4%97& !Tand "ond#nsat# :)++9*8 >/l-9

Note: Total moving level of Tank-2 = -2.9% MT, Tank-3 = -1.&% MT. Total 'e-'#n = &2.42 MT. Total LP P!o"#$t in$l#"e" amoving level = 329.33 MT

0.33 P Sto$ Transf#r a P! Product +ro Tan/63 to D#$ot P! P. ayan . Total Fuantity Transf#rr#d, 7as#d on Tan/ Ta'l#: *779%: !T and 7as#d on "oriolis #t#rin : *((9%*( !T

0.00 % onitor#d th# l#l of i-#d P! Product (9ff S$#c.) in i-#d P! Stora# S$h#r# %:%)9(& 0*)49%7 !Ton2?i-#d P! Stora# S$h#r# 7:4898+ 0*(&%9+) !Ton2? Pro$an# Stora# S$h#r# % :&%9%& 047(944 !Ton2? Pro$an#Stora# S$h#r# 7 :849%: 0:)+97: !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :+49* 0%*)&89&( >arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (103 Psi, #ad) = 036;655017 (103 Psi, a)= 036;65502 (645.4>")= 036?65503 (10 Psi)= 036?65504 (102 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (.3 Psi).



%&r : 0.010 Scf)






7/56






3

4 Daily %cti&iti#s.


0.4560A.45 % BGuali# Pr#ssur# fro Tan/64 to Tan/63

0.00610.30 % Su$$ort aint#nanc# T#a for 8nstall PS?6401 at Do!as #t#rin in# P.ayan

11.00 %612.00 P BGuali# Pr#ssur# fro Tan/64 to Tan/61

02.306 04.00 P BGuali# Pr#ssur# fro Tan/64 to Tan/61

04.30 P Sto$


8/56






3

4 Daily %cti&iti#s.


0.4A P 6 10.45 P Start P64504 7 (P! Transf#r Pu$ 7) circulat# Tan/61, for la' analy# sa$lin $ur$os#.

12.00 % ")= 036?65503 (10 Psi)= 036?65504 (101 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (100.12 Psi).


0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 4A1.A2 Psi= Diff Pr#ss : 15. inH29 and +lorat#

%&r : 0.550 Scf)






9/56






3

4 Daily %cti&iti#s.


02.30 P Start "irculat# P! Product at Tan/61

5 oadin P! Product +ro Tan/62 to T. %sian !as (1500 T 5 I )

0.33 % Sto$ 8nC#ction #rca$tan to P! J#tty Pi$#lin#

Daily o Sh##ts.

0.00 % onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r.036PDT6532 (22..05 8nH29)



+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a- /l-9

Note: Total moving level of Tank-2 = -0.8% MT ,Tan-3=-0.6& an" Tank-4 = -2.0& MT. Total LP P!o"#$t in$l#"e" a movinglevel = 289.4% MT

11.3 % "o$l#t# oadin fro Tan/62 to T.%sian !as (1500 T 5 I ). 7as#d on Tan/ Ta'l# :%&4&9:( !T, #t#rin :%8*(9)*) !Tand Shi$ "aro : %8(%944) !T

0.00 % onitor#d th# l#l of i-#d P! Product (9ff S$#c.) in i-#d P! Stora# S$h#r# %:7%9)7 04:(978 !Ton2? andi-#d P! Product (9n S$#c.) ini-#d P! Stora# S$h#r# 7:**9%4 0+&+9:4 !Ton2? Pro$an# Stora# S$h#r# % :7:977 0&%)9** !Ton2? Pro$an# Stora# S$h#r# 7 ::)9)8 0%%(:9** !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 7)9+ 0%&(%*9+) >arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto


10/56






3

4 Daily %cti&iti#s.


12.00 %


11/56






3Note: Total moving Tank-3=(3.&9 an" Tank-4 = -1.%1 MT. Total LP P!o"#$t in$l#"e" a moving level = 2&1.&9 MT

4 Daily %cti&iti#s.


0.55 % Sicth +illin P! Product +ro Tan/61 to Tan/62

0.5A60.50 % Transf#r P! Product at Tan/61 to Tan/62

0.00 % Su$$ort a'. T#chnician and Suryor for Too/ Sa$l# at "ond#nsat# Stora# Tan/

0.30 % Su$$ort a'. T#chnician for Too/ Sa$l# P! Product at Tan/64

0.50 % Sto$ "irculat# P! Product at Tan/64

10.00 % Sitch +illin P! Product fro Tan/62 to Tan/61


5 oadin "ond#nsat# Product to T. Ja&a 7onitos 13.000 7'ls (10I)01.30 P Start "ond#nsat# oadin Pu$ % for Pr#$aration "ond#nsat# oadin to T. Ja&a 7onitos 13.000 7'ls (10I)

02.42 P Start oadin "ond#nsat# to T. Ja&a 7onitos 13.000 7'ls (10I)

Transf#r P! Product fro Tan/63 to Do!as P. ayan (200 T)

03.00 P Start P! Do!as Pu$ % for Pr#$aration P! Transf#r fro Tan/63 to Do!as P. ayan

03.21 P Start Transf#r P! Product fro Tan/63 to Do!as Pulau ayan (200 T)

04.0060.3 P 8nC#ct #rca$tan to Do!as P! in# Pulau ayan

Daily o Sh##ts.


A 9utstandin Pro'l# +ractionation Plant. %&'()'*(%+ Strainer ,p-tream !eterin$ LPG to Ga-.om !u-t /e Replace 0Strainer have +1 Cleanin$2



0.00 % onitor#d th# l#l of i-#d P! Product in i-#d P! Stora# S$h#r# %:8*9*( 0%%&49&7 !Ton2? i-#d P!Stora# S$h#r# 7:+%9)) 08))9(% !Ton2? Pro$an# Stora# S$h#r# % :7(9+& 08(79:( !Ton2? Pro$an# Stora# S$h#r# 7::)9+) 0%%((97( !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : +:9) 0%*44+9*& >arrel-2



12/56






3Note: Total moving level of Tank-3= 1.%2 MT, Tank-4= -6.&3 MT.Total LP P!o"#$t in$l#"e" a moving level = &26.29 MT

4 Daily %cti&iti#s.


12.00 % /l-

0.00 % onitor#d th# l#l of i-#d P! Product (9ff S$#c.) in i-#d P! Stora# S$h#r# %::798( 0%:))94+ !Ton2?i-#d P! Stora# S$h#r# 7:+*9(: 0&(%9(4 !Ton2? Pro$an# Stora# S$h#r# % :79&8 08&94+ !Ton2? Pro$an# Stora#S$h#r# 7 ::)9(4 0%()&984 !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :&9: 07+%)9++ >arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (101 Psi, a) = 036;655017 (103 Psi, #ad)= 036;65502 (645.5>")= 036?65503 (10 Psi)= 036?65504 ( Psi) and 8nstru#nt %ir Su$$ly H#ad#r (A.51 Psi).

0.00 % onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 2A0 = Th# $r#ssur# at +ir# @at#r Distri'utionH#ad#r is 121 Psi


%&r : 0.54A0 Scf)






13/56




1 Plant Status. The #ractionation Plant Runnin$ Normal9

2 Total Production Hours. 12 Hours.

3Note: Total moving Tank-4 = -1.48 MT. Total LP P!o"#$t in$l#"e" a moving level = 2%9.2% MT

4 Daily %cti&iti#s.


0.10 % 6 01.40 % BGuali# Pr#ssur# at Pi$#lin# !asdo to Tan/63.

0.00 % %ssist a' T#chnician and Suryor to Ta/# P! Sa$l# at Tan/61.

0.22 % Sto$ "irculation P! Product at Tan/61.

0.30 % 6 10.40 % BGuali# Hih Pr#ssur# Tan/61 to Tan/62.

11.00 % Sitch +illin P! Product fro Tan/61 to Tan/63.

02.10 P Sitch +illin P! Product fro Tan/63 to Tan/62.

03.00 P 6 03.3A P "ali'ration !" 9nlin# %T64202.

5

11.30 % ? !as #lai %lr#ady %ll +ast.

11.40 % Start "irculation P! Product at Tan/61 to Pr#$ar# oadin to ? !as #lai.

11.54 % "onn#ct arin# oadin %r to ? !as #lai.

11.5A % Start oadin P! to !as #lai.

02.3 P Start 8nC#ction #rca$tan to Pi$#lin# J#tty.

02.40 P Start P! Do!as Pu$ % for Pr#$aration P! Transf#r fro Tan/64 to Do!as P. ayan

03.25 P Start Transf#r P! Product fro Tan/64 to Do!as Pulau ayan.

12.00 P 6 02.3 P 8nC#ct #rca$tan to Do!as P! in# Pulau ayan.

Daily o Sh##ts.


A 9utstandin Pro'l# +ractionation Plant. %&'()'*(%+ Strainer ,p-tream !eterin$ LPG to Ga-.om !u-t /e Replace 0Strainer have +1 Cleanin$2



oadin P! to ? !as #lai0%8(( !T29

Transf#r P! Product fro Tan/64 to Do!as P. ayan 0*(( !T29

0.00 % onitor#d th# l#l of i-#d P! Product in i-#d P! Stora# S$h#r# %:849)& 0%+&:9%+ !Ton2? i-#d P!

Stora# S$h#r# 7:+894% 0:((9%8 !Ton2? Pro$an# Stora# S$h#r# % :%*9%( 0%*%9%( !Ton2? Pro$an# Stora# S$h#r# 7:&898% 0)(49() !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : %(9( 08**89%+ >arrel-2



14/56






3Note: Total moving level of Tank-4= -&.%0 MT.Total LP P!o"#$t in$l#"e" a moving level = &%%.18 MT

4 Daily %cti&iti#s.%ssist a'. T#chnician for sa$lin at *! +##d Pu$, Static i-#r P! Tan/s #ry 4 Hours.

12.00 % /l-9

Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 0 th, 2013.

Total %ctual Production P! fro *!: *::9%7 !Tand "ond#nsat# :4*+978 >/l-9

Note: Total moving level of Tank-1 = 0.18 MT, Tank-3 = 2.00 MT an" Tank-4= -2.66 MT. Total LP P!o"#$t in$l#"e" amoving level = 2%6.66 MT

0.1A P Sto$ Transf#r a P! Product +ro Tan/64 to D#$ot P! P. ayan . Total Fuantity Transf#rr#d, 7as#d on Tan/ Ta'l#: *7*9&* !T and 7as#d on "oriolis #t#rin : *((9(++ !T

02.15 % "o$l#t# oadin P! to ?.!as #lai (1500 T 5 I ). 7as#d on Tan/ Ta'l# :%:(+9+4 T, #t#rin :%8849%:4 !Tand Shi$ "aro : %8+*9**) T

0.00 % onitor#d th# l#l of i-#d P! Product (9ff S$#c.) in i-#d P! Stora# S$h#r# %:%79&+ 0*%79(7 !Ton2?i-#d P! Stora# S$h#r# 7:789&& 0)::9*) !Ton2? Pro$an# Stora# S$h#r# % :%*9+( 0%*+9%( !Ton2? Pro$an#Stora# S$h#r# 7 :&%9:+ 047)94* !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :%+9( 0&(77498) >arrel-2



15/56






3

4 Daily %cti&iti#s.


0.10 % 6 03.10 P BGuali# Pr#ssur# at Pi$#lin# !asdo to Tan/64.

0.15 % 6 05.00 P BGuali# Pr#ssur# at Pi$#lin# J#tty to Tan/63.

5

0A.00 % Start P! Do!as Pu$ % for Pr#$aration P! Transf#r fro Tan/64 to Do!as P. ayan.

03.20 P 6 05.04 P 8nC#ct #rca$tan to Do!as P! in# Pulau ayan.

0.2A % Start P! Do!as Pu$ 7 for Pr#$aration P! Transf#r fro Tan/64 to Do!as P. ayan.

0.33 P Start 8nC#ct #rca$tan to Do!as P! in# Pulau ayan.

Daily o Sh##ts.





Note: Total moving Tank-1 = 0.%0 MT, Tank-3 = 11.46 MT an" Tank-4 = 3.%& MT. Total LP P!o"#$t in$l#"e" a moving level= 29&.&& MT.

03.14 P Start Transf#r P! Product fro Tan/61 to Do!as Pulau ayan 0>atch % @ %8( !T29

0.25 P Sto$ Transf#r a P! Product +ro Tan/61 to D#$ot P! P. ayan . Total Fuantity Transf#rr#d, 7as#d on Tan/ Ta'l#: %&)9** !T and 7as#d on "oriolis #t#rin : %7)9)(4 !T9

0.30 P Start Transf#r P! Product fro Tan/64 to Do!as Pulau ayan 0>atch * @ %8( !T29

0.00 % onitor#d th# l#l of i-#d P! Product in i-#d P! Stora# S$h#r# %:+9*) 08&97+ !Ton2? i-#d P!

Stora# S$h#r# 7:889*( 0%*8&9)* !Ton2? Pro$an# Stora# S$h#r# % :%+97* 0%+798& !Ton2? Pro$an# Stora# S$h#r# 7:&%9): 048+98: !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : %&9+ 0&)879+) >arrel-2



16/56






3

Note: Total moving level of Tank-3 = 1.1& MT an" Tank-4= -1.96 MT. Total LP P!o"#$t in$l#"e" a moving level = 301.26 MT

4 Daily %cti&iti#s.


12.00 %


17/56






3Note: Total moving Tank-3 = 0.21 MT Total LP P!o"#$t in$l#"e" a moving level = 29&.8% MT.

4 Daily %cti&iti#s.


0.10 % 6 01.20 P BGuali# Pr#ssur# at Pi$#lin# !asdo to Tan/64.

0.4A % Sto$ "irculation P! Product at Tan/62

01.50 P Sitch +illin P! Product +ro Tan/62 to Tan/61

5 Transf#r P! Product fro Tan/64 to Do!as P. ayan (350 T)

0A.00 % Start "irculat# P! Product at Tan/64 Pr#$ar# for Transf#r to!asdo Pulau ayan.

01.30 P 6 0.51 P Start 8nC#ct #rca$tan to Do!as P! in# Pulau ayan.

Daily o Sh##ts.





01.50 P Start Transf#r P! Product fro Tan/64 to Do!as Pulau ayan 0+8( !T29

0.00 % onitor#d th# l#l at Tan53% %(98( 0%7&9+: !Ton2? Tan53* :*9:7 0%:8+9:)!Ton2? Tan53+ %+988 0%+79)*!Ton2? Tan537 +&9:& 077:94& !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : **9) 04:&89)) >arrel-2



18/56






3Note: Total moving level of Tank-3=1.99 MT an" Tank-4= -0.44 MT.Total LP P!o"#$t in$l#"e" a moving level = &60.&0 MT

4 Daily %cti&iti#s.


10.00610.15 P /l-9

Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 0th, 2013.

Total %ctual Production P! fro *!: *%:97% !Tand "ond#nsat# ::%+9&& >/l-9

Note: Total moving level of Tank-2=-2.38,Tank-3 = 1.68 MT an" Tank-4= -2.09 MT. Total LP P!o"#$t in$l#"e" a movinglevel = 214.61 MT

0.35 P Sto$ Transf#r a P! Product +ro Tan/64 to D#$ot P! P. ayan (350 T) . Total Fuantity Transf#rr#d, 7as#d onTan/ Ta'l# : +4)9:( !T and 7as#d on "oriolis #t#rin : +8(9%(+ !T

0.00 % onitor#d th# l#l of i-#d P! Product (9n S$#c.) in i-#d P! Stora# S$h#r# %:**9%4 0+&+9:4 !Ton2?i-#d P! Stora# S$h#r# 7::*9&8 0%:8%97( !Ton2? Pro$an# Stora# S$h#r# % :%+9:% 0%+:9&( !Ton2? Pro$an#Stora# S$h#r# 7 :*&977 0*)79:( !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :*898 0)7:)9&8 >arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (11 Psi)= 036?65504 (115 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (3. Psi).



%&r : 0.40A Scf)






19/56






3

4 Daily %cti&iti#s.


0.40 % 6 0.55 % /l-9

Note: Total moving Tank-2 = -1.06 MT, Tank-3 = 0.32 MT an" Tank-4 = 0.28 MT. Total LP P!o"#$t in$l#"e" a moving level= 20%.02 MT.

0A.00 % Start Transf#r P! Product fro Tan/64 to Do!as Pulau ayan 0>atch % @ *8( !T29

01.1 P Sto$ Transf#r a P! Product +ro Tan/64 to D#$ot P! P. ayan 0>atch % @ *8( !T29 Total Fuantity Transf#rr#d,7as#d on Tan/ Ta'l# : *&:9(* !T and 7as#d on "oriolis #t#rin : *8(9(4% !T9

01.3A P Start Transf#r P! Product fro Tan/62 to Do!as Pulau ayan 0>atch * @ 78( !T29

0.00 % onitor#d th# l#l at Tan53% +(9)% 08:%9*: !Ton2? Tan53* &*988 0%7:%9%: !Ton2? Tan53+ %+9:7 0%+:9)% !Ton2? Tan537 ((9(( 0*:9)& !Ton29

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :*49% 0%(%)+9+% >arrel-29

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (100 Psi)= 036?65504 (10 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (4.3 Psi).


0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 444.A Psi= Diff Pr#ss : 14.A inH29 and +lorat#%&r : 0.41 Scf)






20/56






3

Note: Total moving level of Tank-3=-3.&3 MT an" Tank-3=)0.11 MT. Total LP P!o"#$t in$l#"e" a moving level = 21&.81 MT

4 Daily %cti&iti#s.


0.00 P Sto$ +illin @at#r to +illin @at#r Tan/

10.30 P Hot 9il H#at#r Tri$ du# to +la# Saf#uard Shutdon

10.45 P arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (10, #ad) = 036;655017 (D#adlin#)= 036;65502 (64. >")= 036?65503 (10 Psi)= 036?65504 (104 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (.0 Psi).

0.00 % onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 240 = Th# $r#ssur# at +ir# @at#r Distri'ution H#ad#r is11A Psi

0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 424.3 Psi= Diff Pr#ss : 12.2 inH29 and +lorat# %&r: 0.454 Scf)






21/56






3Note: Total moving Tank-2 = -0.30 MT an" Tank-3 = 0.21 MT. Total LP P!o"#$t in$l#"e" a moving level = 281.%3 MT.

4 Daily %cti&iti#s. %ssist a'. T#chnician for sa$lin at *! +##d Pu$, Static i-#r P! Tan/s #ry 4 Hours.

5

0.25 % Start "irculat# P! Product at Tan/62 Pr#$ar# for Transf#r to !asdo Pulau ayan.

0.5 % Start Transf#r P! Product fro Tan/62 to Do!as Pulau ayan.

0.30 % Start 8nC#ct #rca$tan to Do!as P! in# Pulau ayan.

Daily o Sh##ts.

0.00 P onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r.036PDT6532 (22..4 8nH29)

9utstandin Pro'l# +ractionation Plant.

%&'()'*(%+ Strainer ,p-tream !eterin$ LPG to Ga-.om !u-t /e Replace 0Strainer have +1 Cleanin$2


+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a- 2 Trip .ue to !otor lectric Pro/lem9

Day /l-9

Transf#r P! Product fro Tan/620:*( !T2 to Do!as P. ayan.

0.00 P onitor#d th# l#l at Tan53% 749)* 0%(:*9+% !Ton2? Tan53* ++94) 0&749:& !Ton2? Tan53+ %+9:: 0%+49*+ !Ton2? Tan537 ((9(( 0*:9)& !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : ++9: 0%%:+(97* >arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (105 Psi)= 036?65504 (10 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (5.0 Psi).

0.00 P onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 240 = Th# $r#ssur# at +ir# @at#r Distri'utionH#ad#r is 120 Psi

0.00 P onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 4A.50 Psi= Diff Pr#ss : 1.0 inH29 and +lorat#

%&r : 0.55A Scf)






22/56






3Note: Total moving level of Tank-2=-3.88 MT an" Tank-3=0.11 MT.Total LP P!o"#$t in$l#"e" a moving level = &4%.34 MT

Note: Total moving level of Tank-2=-0.94 MT an" Tank-3=0.32 MT. Total LP P!o"#$t in$l#"e" a moving level = 319.2& MT

4 Daily %cti& iti#s.


0.1560.30 P /l-9


Total %ctual Production P! fro *!:+%)94: !Tand "ond#nsat# :%(%898) >/l-9

10.1 P Sto$ Transf#r P! Product +ro Tan/62 to D#$ot P! P. ayan (:*(T) . Total Fuantity Transf#rr#d, 7as#d on Tan/Ta'l# : :4)9:4 !T and 7as#d on "oriolis #t#rin : :*(9(8( !T

0.00 % onitor#d th# l#l of i-#d P! Product (9n S$#c.) in i-#d P! Stora# S$h#r# %:8)94* 0%+)*9%) !Ton2? i-#dP! Stora# S$h#r# 7:*89&( 077%9*( !Ton2? Pro$an# Stora# S$h#r# % :%+94( 0%+4987 !Ton2? Pro$an# Stora# S$h#r# 7:(9(( 0*:9)& !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :+:97 0%*:7&9(* >arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (10 Psi)= 036?65504 (100 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (A.5 Psi).

0.00 % onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 240 = Th# $r#ssur# at +ir# @at#r Distri'ution H#ad#r is11 Psi

0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 451.4 Psi= Diff Pr#ss : 1.5A inH29 and +lorat# %&r

: 0.504 Scf)



(8'(&'*(%+ 0OPR3PSG3(%(2 @ AT37+(% 0RVP AnalyBer Do;n-tream Static !i1er2 is stil l nfinish#d to s#ttin and cali'ration.



23/56






3No Moving Level

4 Daily %cti&iti#s.


11.00 %602. 00 P BGuali# Pr#ssur# +ro Tan/61 to Tan/64.

5

0A.30 % Start "irculat# P! Product at Tan/62 Pr#$ar# for Transf#r to Do!as Pulau ayan.

10.00 % Start Transf#r P! Product fro Tan/62 to Do!as Pulau ayan 7atch 1

10.30 %613.35 P 8nC#ction #rca$tan to Do!as P! in# Pulau ayan, 7atch 1

03.00 P Start Transf#r P! Product fro Tan/62 to Do!as Pulau ayan 7atch 2

03.05 P 8nC#ction #rca$tan to Do!as P! in# Pulau ayan, 7atch 2

Daily o Sh##ts.


A 9utstandin Pro'l# +ractionation Plant.+'%('*(%+ 0OPR3PSG3(&42 Gate valve line recycle Tan5 % 0+3GA6378(82 plea-e repair .ue to har. to operate.9


Day /l-9

11.05 % Sitch +ilt#r +u#l !as #t#rin, +ro !T3#3%(% >to !T3#3%(% A, Du# to Hih Diff#r#ntial Pr#ssur#.

02.10 P602.50 P %ssist #chanical aint#nanc# to "l#an Strain#r, atch %02.00 P "o$l#t# Transf#r P! Product fro Tan/62 to Do!as Pulau ayan 7atch 1, Total Fuantity Transf#rr#d, >a-e. onTan5 Ta/le %:&944 !T= and >a-e. on Corioli- !eterin$ %:%9+&% !T

Transf#r P! Product fro tan/62 (1A0 T) to Do!as P. ayan,>atch *

0.00 P onitor#d th# l#l at Tan53% :%9(7 0%:(497( !Ton2? Tan53* 49+8 0%%89&* !Ton2? Tan53+ %+94( 0%+4987!Ton2? Tan537 ((9(( 0*:9)& !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 7%9% 0%+:&%9&% >arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (103 Psi)= 036?65504 (10 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (..0 Psi).


0.00 P onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 44.0 Psi= Diff Pr#ss : 1.0 inH29 and +lorat#

%&r : 0.55A2 Scf)

%*'(%'*(%7 0OPR3PSG3%*(2 Pl#as# "l#an #uel Ga- #ilter >Du# to Hih DP.

%8'(4'*(%+ 0OPR3PSG3(7*2 @ P37((% A 0NGL #ee. Pump A2 *ot %&aila'l#.





24/56






3

Note: Total moving level of Tank-2=0.&% MT an" Tank-4=28.66 MT. Total LP P!o"#$t in$l#"e" a moving level = 340.&3 MT

4 Daily %cti&iti#s.


0.0560.20 P /l-9

Note: Total moving level of Tank-2=0.64 MT ,Tank-3=0.&3 MT an" Tank-4=2%.23 MT.Total LP P!o"#$t in$l#"e" a moving level= 660.26 MT


Total %ctual Production P! fro *!:+%%9+% !Tand "ond#nsat# :%(7+9(7 >/l-9

Transf#r P! Product fro tan/62 (1A0 T) to Do!as P. ayan >atch3*0.2 P Sto$ Transf#r P! Product +ro Tan/62 to D#$ot P! P. ayan (%4( !T) . Total Fuantity Transf#rr#d, 7as#d on Tan/Ta'l# : %4&98* !T and 7as#d on "oriolis #t#rin : %:)9)88 !T

0.00 % onitor#d th# l#l of i-#d P! Product (9n S$#c.) in i-#d P! Stora# S$h#r# %:4+9&% 0*(%)9:% !Ton2? i-#dP! Stora# S$h#r# 7:897( 0:49:4 !Ton2? Pro$an# Stora# S$h#r# % :%+94( 0%+4987 !Ton2? Pro$an# Stora# S$h#r# 7 :79&* 08&9&% !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :779) 0%74(79&8 >arrel-2


0.00 % onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 240 = Th# $r#ssur# at +ir# @at#r Distri'ution H#ad#r is12A Psi

0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 43.42 Psi= Diff Pr#ss : 1A.11 inH29 and +lorat# %&r :

0.5 Scf)






25/56






3

Note: Total moving Tank-1 = 1.10 MT. Total LP P!o"#$t in$l#"e" a moving level = 293.10 MT.

4 Daily %cti&iti#s.


11.30 % Hot 9il H#at#r Tri$ du# to "o'ution %ir 7lo#r Sto$.

11.3A % Sitch +illin P! Product +ro Tan/63 to Tan/64 du# to 9ffs$#c Product.

11.45 % 6 02.00 P 9$#n T#$orary in# +or Transf#r *! Product to Tan/64.

12.40 P Start Hot 9il H#at#r.

02.0 P Sitch +illin P! Product +ro Tan/64 to Tan/63 du# to 9ns$#c Product.

502.4 P Start Transf#r P! Product fro Tan/61 to Do!as Pulau ayan.

02.30 P start 8nC#ction #rca$tan to Do!as P! in# Pulau ayan.

Daily o Sh##ts.


9utstandin Pro'l# +ractionation Plant. +'%('*(%+ 0OPR3PSG3(&42 Gate valve line recycle Tan5 % 0+3GA6378(82 plea-e repair .ue to har. to operate.9


Day /l-9

Transf#r P! Product fro tan/61 07(( !T2 to Do!as P. ayan.

0.00 P onitor#d th# l#l at Tan53% :79)) 0%4%*97: !Ton2? Tan53* 897( 0:49:4 !Ton2? Tan53+ +*9%% 0+:&9:*!Ton2? Tan537 %%9(% 0%%(97* !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 7498 0%8:)*94( >arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (A Psi)= 036?65504 (10 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (3.3 Psi).


0.00 P onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 42.50 Psi= Diff Pr#ss : 1A.51 inH29 and +lorat#

%&r : 0.552 Scf)






26/56






3Note: Total moving level of Tank-2=0.23 MT.Total LP P!o"#$t in$l#"e" a moving level = 610.48 MT

Note: Total moving level of Tank 1 = -3.%3 MT, Tank-2=0.11 MT an" Tank-4=0.96 MT. Total LP P!o"#$t in$l#"e" a moving level = 308.2& MT

4 Daily %cti&iti#s.


0.20 6 .50 P /l-9


Total %ctual Production P! fro *!:+%(9)% !Tand "ond#nsat# :)449%8 >/l-9

10.22 P Sto$ Transf#r P! Product +ro Tan/61 to D#$ot P! P. ayan ( 7(( !T) . Total Fuantity Transf#rr#d, 7as#d on Tan/ Ta'l# : 78+97(!T and 7as#d on "oriolis #t#rin : 7((9(4( !T

0.00 % onitor#d th# l#l of i-#d P! Product (9n S$#c.) in i-#d P! Stora# S$h#r# %:&894% 0%8&79(7 !Ton2? i-#d P! Stora#S$h#r# 7:897% 0:494) !Ton2? Pro$an# Stora# S$h#r# % :8%9&+ 0&4:9&+ !Ton2? Pro$an# Stora# S$h#r# 7 :%%9%% 0%%%9+) !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 8*9% 0%&:4(9)7 >arrel-2

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503(110 Psi)= 036?65504 (101 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (.3 Psi).

0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 43.A0 Psi= Diff Pr#ss : 1A.05 inH29 and +lorat# %&r : 0.415

Scf)

%8'(4'*(%+ 0OPR3PSG3(7*2 @ P37((% A 0NGL #ee. Pump A2 *ot %&aila'l#.

%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,und#r onitorinno).




27/56






3Note: Total moving Tank-1 = (&.11, an" Tank-3 = -1.69 MT. Total LP P!o"#$t in$l#"e" a moving level = 320.02 MT.

4 Daily %cti&iti#s.


0.22 % Sto$ circulat#d a P! Product in Tan/62 and sto$ 036P64504 7

01.45 P 6 02.1 P @##/ly cali'ration th# 036%T64102. 0(+3"!388(% >2 Trip .ue to !otor lectric Pro/lem9

Day


28/56






3Note: Total moving level of Tank-1= 1.98 MT an" Tank-3 = -6.16 MT. Total LP P!o"#$t in$l#"e" a moving level = 629.10 MT.

Note: Total moving level of Tank-3 = -3.%6 MT. Total LP P!o"#$t in$l#"e" a moving level = 312.%9 MT

4 Daily %cti&iti#s.


0.20 P Start "irculation P! Product in Tan/62.

0.45 P 6 0.40 P %ssists aint#nanc# T#a for installin a Bl#ctrical otor of 8nstru#nt %ir "o$r#ssor 7. arrel-29

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503(10 Psi)= 036?65504 (105 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (. Psi).

0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 44.11 Psi= Diff Pr#ss : 1.0 inH29 and +lorat# %&r : 0.55

Scf)


%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,und#r onitorinno).




29/56






3Note: Total moving Tank-1 = -0.94 "an Tank-3 = -1.34 MT, Total LP P!o"#$t in$l#"e" a moving level = 302.3& MT.

4 Daily %cti&iti#s.


11.15 % 6 04.0 P BGuali# $r#ss fro Tan/62 to Tan/61

04.55 P 6 05.04 P Start P601 (%$i S#$arator Pu$), drain l#l o$#n drain fro A.1 I to .2I

5

02.4 P Start transf#r a P! Product fro Tan/61 to D#$ot P! P. ayan.

02.52 P Start inC#ct#d a #rca$tan to D#$ot P! P. ayan.

04.2 P Start Transf#r P! Product fro Tan/63 to D#$ot Pulau ayan

Daily o Sh##ts.

A 9utstandin Pro'l# +ractionation Plant.


+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a- atch *

0.00 P onitor#d th# l#ls of P! Product in Tan53% 89(( 0:79*4 !Ton2? Tan53* :49)* 0%)%(9:* !Ton2? Tan53+ :%9)4 0%((*9:* !Ton2? and Tan537 (9(( 0*:9)& !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : *798 0)*(89%& >arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (A Psi)= 036?65504 (10 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (.4A Psi).

0.00 P onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r (036PDT6532 : 22. inH29)


0.00 P onitor#d th# +u#l !as #t#rin (Pr#ss. %&r : 443. Psi= Diff Pr#ss : 1A.25 inH29 and +lorat# %&r : 0.545

Scf)


%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump2 8ndication #a/a# on #chanical S#al (#ch s#al alr#adyr#$lac#d,'ut th# &i'ration still hih).




30/56






3Note: Total moving level of Tank-1= -1.41 MT an" Tank-3 = -4.&3 MT. Total LP P!o"#$t in$l#"e" a moving level = 61&.%2 MT.

Note: Total moving level of Tank-3 = -2.&% MT. Total LP P!o"#$t in$l#"e" a moving level = 2%4.99 MT.

4 Daily %cti&iti#s.


0.21 P Sitch +illin P! Product 9ns$#c +ro Tan/62 to Tan/64.


00.00 % /l-9


Total %ctual Production P! fro *!:*::988 !T an."ond#nsat# :)++9*8 >/l-9

Transf#r P! Product fro Tan/61 and Tan/63 0+8( !T2 to Do!as P. ayan.

0.45 P Sto$ Transf#r P! Product +ro Tan/63 to D#$ot P! P. ayan 0>atch * *:8 !T) . Total Fuantity Transf#rr#d, 7as#d on Tan/ Ta'l# :+%%9*4 !T and 7as#d on "oriolis #t#rin : *:89%&( !T9

Total Transf#r >atch % an. >atch *, 7as#d on Tan/ Ta'l# : +):9%4 !Tand 7as#d on "oriolis #t#rin : +8(9*4: !T9

0.00 P onitor#d th# l#l at Tan53% (89(( 0:79*4 !Ton2? Tan53* 4*9&( 0%)):9(: !Ton2? Tan53+ 8:94& 0:4498% !Ton2? Tan537 *(9:8 0*%)9%& !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : *:9) 0%(%+497% >arrel-29



31/56






3Note: Total moving Tank-2 = -2.2% "an Tank-3 = 0.48 MT, Total LP P!o"#$t in$l#"e" a moving level = 300.39 MT.

4 Daily %cti&iti#s.


0A.51 % %ssist a'. T#ch and Suryor "itra 7uana too/ sa$l# P! at Tan/62

0A.52 % 6 10.05 % %ssist Bl#ctric T#ch. continu# r#$air a$ at Toil#t ""< 1 B%.

0.11 % Sto$ P64504 7 (Transf#r Pu$ 7), finish circulation Tan/2..

0.14 % 6 11.1A % Start P64504 7 (Transf#r Pu$ 7), circulat# Tan/64 for a'. %naly# $ur$os#.

5

01.34 P Start transf#r a P! Product fro Tan/63 to D#$ot P! P. ayan.

01.3A P Start inC#ct#d a #rca$tan to D#$ot P! P. ayan.

Daily o Sh##ts.



+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a-


32/56






3Note: Total moving level of Tank-2= -8.84MT an" Tank-3 = -3.38 MT. Total LP P!o"#$t in$l#"e" a moving level = &%0.01 MT.

Note: Total moving level of Tank-2 = -6.3% MT. Total LP P!o"#$t in$l#"e" a moving level = 282.18 MT.

4 Daily %cti&iti#s.


11.50 P605.10 % BGuali# Pr#ssur# +ro Tan/64 to Tan/61

00.00 % arrel-29



33/56






3

4 Daily %cti&i ti#s.


0.4A % Sto$ circulat#d a P! Product in Tan/64 and sto$ 036P64504 %

0.01 P Sitch fill in a P! Product fro Tan/64 to Tan/61

5 Daily o Sh##ts.



*('%%'*(%+ 0OPR3PSG3()+2 Plea-e Create. Pipe In-ulation to Outlet ")= 036?65503 (112 Psi)= 036?65504 (114 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (A.0 Psi).

0.00 P onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r (036PDT6532 : 22.34 inH29)

0.00 P onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 20 = Th# $r#ssur# at +ir# @at#rDistri'ution H#ad#r is 11 Psi

0.00 P onitor#d th# +u#l !as #t#rin (Pr#ss. %&r : 42.0 Psi= Diff Pr#ss : 1A.25 inH29 and +lorat# %&r :

0.545 Scf)


%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#alalr#ady r#$lac#d,'ut th# &i'ration still hih).

(8'(&'*(%+ 0OPR3PSG3(%(2 @ AT37+(% 0RVP AnalyBer Do;n-tream Static !i1er2is still nfinish#d to s#ttin andcali'ration.



34/56






3Note: Total moving level of Tank-2= -8.22 MT an" Tank-3 = 3.98 MT. Total LP P!o"#$t in$l#"e" a moving level = 606.1% MT.

4 Daily %cti&iti#s.



00.00 % /l-9


Total %ctual Production P! fro *!:+()9%+ !T an."ond#nsat# :4:49+8 >/l-9

Note: Total moving level of Tank-2 = -&.2% MT, Tank-3 = 1.&3 MT an" Tank-4 = -%.41 MT. Total LP P!o"#$t in$l#"e" a moving level = 29%.9%MT.

0.00 P onitor#d th# l#l at Tan53% *+9(: 0+4+97% !Ton2? Tan53* 4%944 0%)4(9&7 !Ton2? Tan53+ +7988 07%+9&4 !Ton2? Tan537 4(94% 0%%%:98* !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 7%97 0%+47+9)& >arrel-29



35/56






3

4 Daily %cti&iti#s.


0.0 % Sto$ circulat#d a P! Product in Tan/64 and sto$ 036P64504 7

5

01.05 P Start 036P64504 % and circulat#d a P! Product in Tan/63

01.0A P Start transf#r a P! Product fro Tan/63 to D#$ot P! P. ayan.

01.12 P 6 03.12 P 8nC#ct#d a #rca$tan to D#$ot P! P. ayan.

03.12 P Start 036P64501 % and circulat#d a P! Product in Tan/62

03.3 P Start loadin a P! Product in Tan/62 to ? %sian !as

03.45 P Start inC#ct#d a #rca$tan to J#tty (? %sian !as)

Daily o Sh##ts.

A 9utstandin Pro'l# +ractionation Plant.


+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a-


36/56






3Note: Total moving level of Tank-3= -1.&4 MT an" Tank-4= -10.34 MT. Total LP P!o"#$t in$l#"e" a moving level = &%3.&8 MT.

Note: Total moving level of Tank-4 = -4.68 MT an" moving level of Tank-2 = -0.40 MT Total LP P!o"#$t in$l#"e" a moving level = 29&.34 MT.


00.00 % /l-9


Total %ctual Production P! fro *!:+((97* !T an."ond#nsat# :48(9)( >/l-9

0.00 P Sto$ Transf#r P! Product +ro Tan/63 to D#$ot P! P. ayan 0+(( !T) . Total Fuantity Transf#rr#d, 7as#d on Tan/ Ta'l# :+%(9%( !Tand 7as#d on "oriolis #t#rin : +(%9+7 !T9

oadin a P! Product fro Tan/62 to ? %sian !as 0%8(( !T2 04.24 % Sto$ oadin P! Product to ? %sian !as 0%8(( !T2.Total Fuantity 7as#d on Tan/ Ta'l# : %&:&97( !T, 7as#d on #t#rin : %8*&9)7(!T= and 7as#d on Shi$ : %8(*9*)( !T

0.00 P onitor#d th# l#l at Tan53% 789:* 0):)9(+ !Ton2? Tan53* %)9%& 0+((9%& !Ton2? Tan53+ %(9(& 0%(%9(& !Ton2? Tan537 4(9%( 0%%()9(+ !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 7:9) 0%8&*49%% >arrel-29



37/56






3

4 Daily %cti&iti#s.


10.00 % %ssist a' T#chnician and Suryor for Too/ "ond#nsat# Sa$l# at "ond#nsat# Stora# Tan/

10.00 %602.30 P "irculat# P! Product at Tan/61

10.10 % Sitch /l-9

Note: Total moving Tank-2 = -2.03, Tank-3 = -0.09 MT "an Tank-4 = -2.%8 MT, Total LP P!o"#$t in$l#"e" a moving level =2%6.46 MT.

Transf#r P! Product fro Tan/64 to D#$ot P! P. ayan ( +(( !T)

0.00 P onitor#d th# l#ls of P! Product in Tan53% 889%4 0%*8&9+7 !Ton2? Tan53* +(*9%) 0+(*9%) !Ton2? Tan53+ %(9(8 0%(%9+: !Ton2? and Tan537 &*9:* 04&89*& !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 8(9) 0%&78%98& >arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto ")= 036?65503 (101 Psi)= 036?65504 (10 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (A.4 Psi).



0.00 P onitor#d th# +u#l !as #t#rin (Pr#ss. %&r : 42.04 Psi= Diff Pr#ss : 1.A0 inH29 and +lorat# %&r : 0.544

Scf)






38/56






3Note: Total moving level of Tank 2 = -&.24 MT, Tank-3=-0.28 MT an" Tank-4= -6.68 MT. Total LP P!o"#$t in$l#"e" a moving level = &34.%2 MT.


00.00 %


39/56






3

4 Daily %cti&iti#s.


0.15 %60.30 % /l-2

0.00 P onitor#d th# l#ls of P! Product in Tan53% :%974 0%:*(9*+ !Ton2? Tan53* %)9+7 0+(+94* !Ton2? Tan53+ )94% 0))9%& !Ton2? and Tan537 +)9)* 07):9&) !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ :*:9& 0%((8&9(: >arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (%uto


40/56






3

Note: Total moving level of Tank 2 = 2.44 MT+ Tank-3= 1.11 MT an" Tank-4= -2.29 MT. Total LP P!o"#$t in$l#"e" a moving level = 4%4.3% MT.

4 Daily %cti&iti#s.


12.00 % /l- E %( 20.0 P Sto$ oadin "ond#nsat# to T Ja&a 7onitos. Total Fuantity Transf#rr#d, 7as#d on #t#rin : %+8449))& >/l-= and 7as#d on Shi$ :%+&&)9((( >/l-

0.00 % onitor#d th# l#l of P! Product in Tan53% 4%9&( 0%):79%) !Ton2 Tan53* %)9+8 0+(79(* !Ton2 Tan53+ %(97% 0%(79:+!Ton2 and Tan537 +79&4 07%89&4 !Ton29

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : :9) 07&749:% >arrel-29



41/56






3Note: Total moving Tank-2 = 0.41 MT, an" Tank-4 = 2.61 MT, Total LP P!o"#$t in$l#"e" a moving level = 249.14 MT.

4 Daily %cti&iti#s.



0A.10 % Sitch +illin P! Product fro Tan/61 to Tan/63

10.35 % 6 11.30 % Su$$ort #chanic T#a "h#c/ %nd


42/56






3

Note: Total moving level of Tank 2 = -0.20 MT an" Tank-4= 3.84 MT. Total LP P!o"#$t in$l#"e" a moving level = &11.26 MT.

Note: Total moving level of Tank-1 = -6.%3 MT an" moving level of Tank-4 = 0.01 MT Total LP P!o"#$t in$l#"e" a moving level = 263.06 MT.

4 Daily %cti&iti#s.


12.00 %


43/56



24th January, 2014 (Day Shift)




3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 24th, 2014.Note: Total moving Tank-1 = -2.26Tank-2 = 0.41 MT Total LP P!o"#$t in$l#"e" a moving level = 2%8.%6 MT.

4 Daily %cti&iti#s.


0.1060.20 % /l-9

Transf#r P! Product fro Tan/61 to D#$ot P! P. ayan 0+8( !T2

0.00 P onitor#d th# l#ls of P! Product in Tan53% :*94% 0%:889&7 !Ton2? Tan53* %)9+) 0+(7947 !Ton2? Tan53+ &*9&4 04&79&+ !Ton2? and Tan537 *9)8 0789*( !Ton29

0.00 P onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : %:9( 0:%7&98+ >arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (10A Psi, #ad) = 036;655017 (%uto ")= 036?65503 (10 Psi)= 036?65504 (105 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (.3 Psi).



0.00 P onitor#d th# +u#l !as #t#rin (Pr#ss. %&r : 41.5A Psi= Diff Pr#ss : 1.3 inH 29 and +lorat# %&r : 0.522Scf)






44/56






3

4 Daily %cti&i ti#s.


12.00 % ")= 036?65503 (10A Psi)= 036?65504 ( Psi) and 8nstru#nt %ir Su$$ly H#ad#r (5. Psi).


0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 41.32 Psi= Diff Pr#ss : 1A.34 inH29 and +lorat# %&r :

0.543 Scf)


%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,'utth# &i'ration still hih).




45/56







3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 25th, 2014.

4 Daily %cti&iti#s.


10.42 % Sitch arrel-29

0.00 P onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (102 Psi, #ad) = 036;655017 (%uto ")= 036?65503 (10A Psi)= 036?65504 (100 Psi) and 8nstru#nt %ir Su$$ly H#ad#r (. Psi).

0.00 P onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r (036PDT6532 : 22.3A inH29)


0.00 P onitor#d th# +u#l !as #t#rin (Pr#ss. %&r : 41.34 Psi= Diff Pr#ss : 1A.3A inH29 and +lorat# %&r : 0.542

Scf)






46/56






3

4 Daily %cti&iti#s.


12.00 % /l-9

Note: Total moving level of Tank-1 = -4.1" MT# Tank-$= -4.$7 and Tank-4 = +".%1MT. Total LPG Prod!t in!lded a moving level = 289.9&MT.

0.00 % onitor#d th# l#l of P! Product in Tan53% 8+9+7 0%*(*9*( !Ton2 Tan53* 7*9*) 044(97% !Ton2 Tan53+ 4+9:7 0%%8%9(( !Ton2 and Tan537 79(& 08*9&& !Ton29

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : *&94 0)4+&974 >arrel-29

0.00 % onitor#d th# 8nstru#nt %ir "o$r#ssors. 036;65501% (A Psi, #ad) = 036;655017 ( Psi, a)= 036;65502 (64.3 >")= 036?65503 (10A Psi)= 036?65504 ( Psi) and 8nstru#nt %ir Su$$ly H#ad#r (5. Psi).


0.00 % onitor#d th# +u#l !as Syst#. +u#l !as #t#rin (Pr#ss. %&r : 430.41 Psi= Diff Pr#ss : 1.3 inH29 and +lorat# %&r :

0.545A Scf)


%8'(4'*(%+ 0OPR3PSG3(772 @ P378(% > 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,'utth# &i'ration still hih).




47/56







3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 2th, 2014.

4 Daily %cti&iti#s.


10.00 %604.35 P "irculat# P! Product at Tan/63 usin P! !asdo# Pu$ %

04.10 P %ssist Suryor and a' T#chnician Too/ Sa$l# at Tan/63

5 Daily o Sh##ts.



+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a- 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#adyr#$lac#d,'ut th# &i'ration still hih).




48/56






3Note: Total moving level of Tank-1=-2.3& MT, Tank-3= -6.61 MTan" Tank-4=3.0% MT.Total LP P!o"#$t in$l#"e" a moving level = &9%.10 MT

Note: Total moving level of Tank 1 = -0.&9 MT, Tank-3=-4.6% MT an" Tank-4=0.8& MT. Total LP P!o"#$t in$l#"e" a moving level = 296.06 MT


12.00 % 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,und#r onitorinno).




49/56






3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours).Note: Total moving level of Tank-1 = 2.2% MT an" Tank-2 = -1.92 MT. Total LP P!o"#$t in$l#"e" a moving level = 291.22 MT

4 Daily %cti&iti#s.


0.15 % 6 02.20 P BGuali# Pr#ssur# P! Do!as Pi$#lin# to Tan/61.

0A.00 % 6 05.00 P BGuali# Pr#ssur# P! J#tty Pi$#lin# to Tan/62.

0A.00 % 6 01.40 P "irculation a P! Product in Tan/62 +or Ta/# Sa$l# 'y Suryor.

0A.00 % %ssist #chanical 036P64202611.

0.35 % Start /l-9

Transf#r P! Product +ro Tan/61 to Do!as0+(( !T29

0.00 % onitor#d th# l#l of Tan53% ++9)) 0&8%97% !Ton2? Tan53* 489%4 0*(8+9)+ !Ton2? Tan53+ +&9%% 07+:9:7 !Ton2? F Tan537

((9(( 0*:9)& !Ton29

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : 7+9* 0%7++49(+ >arrel-2



50/56






3Note: Total moving level of Tank-1=6.4& MT.Total LP P!o"#$t in$l#"e" a moving level = &8&.48 MT

Note: Total moving level of Tank 1 = 6.%9 MT, Tank-2=-&.1& MT . Total LP P!o"#$t in$l#"e" a moving level = 312.16 MT

4 Daily %cti&iti#s.


0.1560.45 P 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,und#r onitorinno).




51/56






3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours).Note: Total moving level of Tank-1 = 0 MT an" Tank-2 = 0 MT. Total LP P!o"#$t in$l#"e" a moving level = 31&.3& MT

4 Daily %cti&iti#s.



0A.00 % 6 05.00 P BGuali# Pr#ssur# P! J#tty Pi$#lin# to Tan/62.

0.15 % 6 0.45 P %ssist #chanical aint#nanc# to P otor +in +an "ool#r D#'utani#r B64202621, 9E.

03.00 P a/# $ 9il 7#arin D#'utani#r


52/56






3 Note: Total moving level of Tank-1=3.46 MT.Total LP P!o"#$t in$l#"e" a moving level = 648.6& MT

Note: Total moving level of Tank 1 = 0.%3 MT. Total LP P!o"#$t in$l#"e" a moving level = 32&.03 MT

4 Daily %cti&ity.


0A.45 P Sitch +illin P! Product fro Tan/63 to Tan/62





53/56






3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours).Note: Total moving level of Tank-1 = 8.%3 MT an" Tank-3 = - 2.&% MT. Total LP P!o"#$t in$l#"e" a moving level = 33%.02 MT.

4 Daily %cti&iti#s.



0.15 % 6 0.30 % %ssist #chanical aint#nanc# to P otor +in +an "ool#r D#'utani#r (036B64202622), 9E.

0.30 % Sto$ "irculation P! Product in Tan/63.

0.30 % %ssist Ta/# Sa$l# "ond#nsat# Product in "ond#nsat# Stora# Tan/ 'y Suryor.

03.20 P 6 04.30 P BGuali# Pr#ssur# +ro Tan/62 to Tan/61.

0.30 P Sitch +illin Product P! +ro Tan/ 2 to Tan/ 4.

5

0A.10 % Start "irculation a P! Product in Tan/61 Pr#$ar# Transf#r to Do!as.

02.00 P 6 05.2 P 8nC#ct #rca$tan to Do!as Pi$#lin#.

0.25 P Start "irculation a P! Product in Tan/63 Pr#$ar# Transf#r to Do!as.

Daily o Sh##ts.

0.00 % onitor#d th# %ir 7lo#r 8nta/# at Hot 9il H#at#r.036PDT6532 (22.0 8nH29)

0.00 % onitor#d th# +ir# @at#r Syst#. Th# +ir# @at#r Tan/ l#l is 250 = Th# $r#ssur# at +ir# @at#r Distri'ution H#ad#r is 121 Psi



+'%%'*(%+ 0OPR3PSG3(:42 Pilot % at #larin$ Sy-tem cannot I$nite an. There ;a- 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,und#r onitorinno).




54/56



30th January, 2014 (*iht Shift)




3Note: Total moving level of Tank-1=9.29 MT an" Tank-3=-9.46 MT.Total LP P!o"#$t in$l#"e" a moving level = 643.%2 MT

Note: Total moving level of Tank 2 = -0.8% MT an" Tank-3=-4.26 MT. Total LP P!o"#$t in$l#"e" a moving level = 326.24 MT

4 Daily %cti&ity.






55/56






3 Total Production of P! and "ond#nsat# $#r Day Shift (12 hours).Note: Total moving level of Tank-2 =-2.83 MT an" Tank-3 = -0.%2 MT. Total LP P!o"#$t in$l#"e" a moving level = 303.86 MT.

4 Daily %cti&iti#s.


0.15 % 6 01.30 P BGuali# Pr#ssur# Do!as Pi$#lin# to Tan/61.

0.35 % Sitch 0LPG Loa.in$ Pump28ndication #a/a# on #chanical S#al (#ch s#al alr#ady r#$lac#d,und#r onitorinno).




56/56






3Note: Total moving level of Tank-2=-9.&% MT an" Tank-3=-4.04 MT.Total LP P!o"#$t in$l#"e" a moving level = 643.%2 MT

Note: Total moving level of Tamk-1=14.30 MT, Tank 2 = -&.03 MT an" Tank-3=-2.12 MT. Total LP P!o"#$t in$l#"e" a moving level = 342.&% MT

4 Daily %cti&ity.


12.00 % /l-9

Total Production of P! and "ond#nsat# $#r Day Shift (12 hours) on January 31st, 2013.

Total %ctual Production P! fro *!:++897* !Tand "ond#nsat# :)&(9:( >/l-9

0.2 P "o$l#t# Transf#r P! fro Tan/63 to Do!as P.ayan. Total Fuantity Transf#rr#d +((9():MT (7as#d on #t#rin),34%.2& MT(7as#d on Tan/ Ta'l#)

0.00 % onitor#d th# l#l of i-#d P! Product (9n S$#c.) in i-#d P! Stora# S$h#r# %:*98( 0749)8 !Ton2? i-#d P! Stora#S$h#r# 7:479%8 0*(+%9&% !Ton2? Pro$an# Stora# S$h#r# % :7:948 0&*89)% !Ton2? Pro$an# Stora# S$h#r# 7 ::%9)7 0%((*9%& !Ton2

0.00 % onitor#d th# l#l of "ond#nsat# Product in "ond#nsat# Stora# Tan/ : %89+ 0&&:)9)( >arrel-2


daily activity report january 2014

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