Revised October 23, 2006 POLYURETHANE Page 1 of 3 MSDS MATERIAL SAFETY DATA SHEET

Revised October 23, 2006 Page 1 of 3

POLYURETHANE MSDS MATERIAL SAFETY DATA SHEET I.

PRODUCT IDENTIFICATION PRODUCT NAME:

Thermoset Polyurethane Elastomer

PHONE NUMBERS: PRODUCT INFORMATION: CHEMTREC:

II.

1-800-667-0999 1-800-424-9300

PHYSICAL AND CHEMICAL PROPERTIES APPEARANCE:

Molded parts or sheets

ODOR:

Slight odor

PERCENT VOLATILES:

None

MELTING POINT:

N/A

SOLUBILITY IN WATER: Insoluble SPECIFIC GRAVITY:

III.

1.1 – 1.2

STABILITY AND REACTIVITY STABILITY: Stable at ambient temperatures and pressures CONDITIONS TO AVOID:

IV.

None known

EXPOSURE CONTROLS/PERSONAL PROTECTION VENTILATION: Local exhaust at processing equipment. Grinding and machining of parts should be reviewed to assure that particulate levels are kept below recommended standards. PROTECTIVE EQUIPMENT SKIN:

Protective gloves, long sleeve cotton shirt and long pants are required when handling molten material.

EYE:

Safety glasses are recommended to prevent particulate from entering eyes while grinding or machining.

RESPIRATOR:

None under normal processing, if ventilation is adequate


V.

HEALTH HAZARDS IDENTIFICATION ACUTE OR IMMEDIATE EFFECTS SKIN:

Molten material may cause thermal burns

INHALATION: Shapes are not considered an inhalation hazard INGESTION:

Not a probable route of exposure

LONG TERM DELAYED EFFECTS:

None known

MEDICAL CONDITIONS AGGRAVATED BY EXPOSURE:

None known

CHRONIC EFFECTS: As with most high molecular weight polymer, this material is considered inert.

VI.

FIRST AID MEASURES SKIN:

If molten polymer contacts skin, cool rapidly with cold water. Do not attempt to peel polymer from skin. Obtain medical attention for thermal burns.

EYES:

In case of eye contact, immediately flush eyes with plenty of water for at least 15 minutes. Consult a physician if symptoms persist.

INHALATION:

If exposure to fumes from overheating, move to fresh air. Consult a physician if symptoms persist.

VII.

TOXICOLOGICAL INFORMATION

CHRONIC TOXICITY: Harmless MEDICAL CONDITIONS PRONE TO AGGRAVATION BY EXPOSURE: No information available

VIII. FIRE FIGHTING MEASURES AUTOIGNITION TEMPERATURE: N/A HAZARDOUS PRODUCTS OF COMBUSTION: Oxides of carbon, water and smoke under burning conditions. Other combustion products are hydrogen cyanide, aromatic and aliphatic hydrocarbons.


IX.

ACCIDENTAL RELEASE MEASURES SPILL OR RELEASE: N/A

X.

HANDLING AND STORAGE HANDLING: Open containers only in well-ventilated area STORAGE:

XI.

Store away from sources of direct heat

DISPOSAL CONSIDERATIONS DISPOSAL:

XII.

Treatment and disposal must be in accordance with federal, state, provincial and local regulations.

DISCLAIMER OF EXPRESSED AND IMPLIED WARRANTIES

The information presented in the Material Safety Data Sheet is based on data believed to be accurate as of the date this Material Safety Data Sheet was prepared. HOWEVER, NO WARRANTY OF MERCHANTABILITY, FITNESS FOR ANY PARTICULAR PURPOSE, OR ANY OTHER WARRANTY IS EXPRESSED OR IS TO BE IMPLIED REGARDING THE ACCURACY OR COMPLETENESS OF THE INFORMATION PROVIDED ABOVE, THE RESULTS TO BE OBTAINED FROM THE USE OF THIS INFORMATION OR THE PRODUCT, THE SAFETY OF THIS PRODUCT, OR THE HAZARDS RELATED TO ITS USE. No responsibility is assumed for any damage or injury resulting from abnormal use or from any failure to adhere to recommended practices. The information provided above, and the product, are furnished on the condition that the person receiving them shall make their own determination as to the suitability of the product for their particular purpose and on the condition that they assume the risk of their use. In addition, no authorization is given nor implied to practice any patented invention without a license.

MATERIAL SAFETY DATA SHEET (Polyurethane Paints) Issue Date Printing Date

: 13 – 05 - 2004 : 13 – 05 – 2004.

1. CHEMICAL PRODUCT AND COMPANY IDENTIFICATION Product Name Chemical Description

: Polyurethane Paints Clear Or Pigmented : A blend of Saturated hydroxylated polyester and pigments in organic solvents : MAS Paints & Chemicals Industry. : 00971 – 06 – 5311777, 00971 – 06 - 5311330

Supplier Telephone & Fax No

2. COMPOSITION / INFORMATION ON INGREDIENTS Hazardous components with in the meaning of EEC directive 67 / 548 and corresponding classification : 32% xylene N. 67.548/CEE: 601-022-00-9 CAS: 1330-20-7 EINECS: 215-535-7 Xn Harmful R38 Irritating to skin. R20/21 Harmful by inhalation and in contact with skin. 8% ethylbenzene N. 67.548/CEE: 601-023-00-4 CAS: 100-41-4 EINECS: 202-849-4 Xn Harmful R20 Harmful by inhalation. 3. HAZARD INDENTIFICATION The product is a liquid that can catch fire at temperatures in excess of 21 o C if exposed to an ignition source. The product is harmful following acute exposure to it and poses a serious health threat if inhaled or if brought into contact with the skin. If brought into contact with the skin, the product causes appreciable inflammation, with erythema, scabs, and oedema 4. FIRST AID MEASURES Contact with skin

Contact with eyes

Swallowing

Inhalation

: Immediately take off all contaminated clothing. : Areas of the body that have – or are only even suspected of having – come into contact with the product must be rinsed immediately with plenty of running water and possibly with soap. : Do not use wash or ointment of any kind (before obtaining an examination or advice from an eyes specialist). Wash immediately with water for at least 10 minutes. : Do not under any circumstance induce vomiting. OBTAIN A MEDICAL EXAMINATION IMMEDIATELY. : Give liquid paraffin to drink; do not give milk or animal or vegetable fats of any kind. : Ventilate the premises. The patient is to be removed immediately from the contaminated premises to rest in a well ventilate area. OBTAIN MEDICAL ATTENTION.

5. FIRE FIGHTING MEASURES Recommended extinguishers Extinguishers not to be used Risks arising from combustion Protective equipment

: : : :

Foam, sand and Co3 None in particular Avoid inhaling the fumes. Use protection for the respiratory tract: Cool the containers exposed to the fire with water.

6. ACCIDENTIAL RELEASE MEASURE Measures for Personal safety : Use a mask, gloves and protective clothing. Environmental Measures : Limit leakages with earth or sand. : Eliminate all unguarded flames and possible sources of ignition. Do not smoke. : If the product has escaped into a water course, into the drainage system, or has contaminated the ground or vegetation, notify the competent authorities. Cleaning Methods : Rapidly recover the product. To do so, wear a mask and protective clothing. : If the product is in a liquid form. Stop it from entering the drainage system. : Recover the product for re-use if possible, or for elimination. The product might, where appropriate, be absorbed by inert material. : After the product has been recovered, rinse the area and materials involved with water. 7. HANDLING AND STORAGE Handling precautions

Storage Conditions

: : : :

Avoid contact and inhalation of the vapours. See, too, paragraph 8 below. Do not eat or drink while working. Do not smoke while working. Keep away from unguarded flame, sparks, and heat sources. Avoid direct exposure to sunlight.

Instructions as regards storage premises

: Cool and adequately ventilated.

8. EXPOSURE CONTROL / PERSONAL PROTECTION Precautionary measures

: Give adequate ventilated to the premises where the product is stored and /or handled. Respiratory protection : Use adequate protective respiratory equipment, e.g. CEN/FFP-2(S) or : CEN/FFP-3 (S). Protection for hands : Use protective gloves that provides comprehensive protection e.g. P.V.C. neoprene or rubber. Eye Protection : Use close fitting safety goggles and /or visor conforming to BS 2092 GRADE 1). Protection for skin : Use clothing that provides comprehensive protection to the skin, e.g. cotton, Rubber P.V.C. or viton. Exposure limit (s) (ACGIH) : Xylene : TLV TWA : 436mg /m3, 100ppm TLV STEL : 651 mg /m3, 150ppm Ethylbenzene : TLV TWA : 434mg /m3, 100ppm TLV STEL : 543 mg /m3, 125ppm 9. PHYSICAL AND CHEMICAL PROPERTIES Appearance and colour Odour Boiling point Flash point Autoignition Flammable limits Lower (Vol.%) Upper (Vol.%)

: : : : : : : :

Colourless liquid Or Pigmented. Solvents 138 0C 24 0C 500 0C 1.1 6.6

Expositive Properties Vapour pressure Relative density Viscosity Solubility in water

: : : : :

6.6 8 mbar @ 20 0C 1.00 to 1.5 Kg / ltr @ 20 0C 1400 to 20,000 mPa.s @ 25 0C Almost insoluble

10. STABILITY AND REACTIVITY Conditions to avoid Substances to avoid Hazardous decomposition products

: stable under normal conditions. : avoid contact with combustible materials. The product could catch fire : it may match fire on contact with oxidising mineral acids, and powerful oxidising agents.

11. TOXICOLOGICAL INFORMATION The concentration of each substance be borne in mind in assessing the toxicological effects deriving from the preparation. Set out below is the toxicological information relating to the main substances in the preparation. Xylene : OBSERVATION ON HUMAN SUBJECTS NON-PROFESSIONAL EXPOSURE – Effects Following acute exposure: : Symptoms of intense exposure are: dermatitis, eczema, irritation to the eyes and to the respiratory tract. Inhaling the vapours can cause dizziness, headache, nausea, incoordination, excitability, narcosis, anaemia, and paraesthesia, of the hands and feet. PROFESSIONAL EXPOSURE – effect following acute exposure: Narcotic at high concentrations. Irritation through inhalation at 200 ppm (TCLo). Inhalation of 200 ppm has irritation effect in human subjects. Human subjects (oral)(LDLo): 50 mg / kg. Inhalatory human subject (LCLo) 10000 ppm /6h. 12. ECOLOGICAL INFORMATION Adopt good working practices. So that the product is not released into the environment. 13. DISPOSAL CONSIDERATIONS Recover, if possible. Send authorised disposal plants or for incineration under controlled conditions. In so doing comply with the local and national regulations currently in force. 14. TRANSPORT INFORMATION ROAD (ADR/ RAIL (RID) : Class :3 Item : 31 0C Label :3 Risk identification : 30 SEA (IMDG/IMO) Class : 3.3 Packing group Item : III EmS number : 3 –05 MFAG number : 310 page 3379 Label :3 AIR (ICAO/ IATA) Class :3 Packing group Item : III Packing Instruction : 309 (passengers) 310 Cargo UN number UN 1866 Proper Shipping name: Polyurethane Paints, Flammable.

15. REGULATORY INFORMATION Label information 88 / 379 EEC ( Classification and Labelling ): Symbols

: Xn Harmful

Risk phrases

: R 10 Flammable : R 20 /21 Harmful by inhalation and in contact with skin. : R 38 Irritating to skin.

Safety phrases

: S 43 in case of fire, use … (indicate in the space the precise type of the fire -fighting equipment. If water increases risk, add –‘Never use water’) : 25. Avoid contact with eyes. : S 36/37 Wear Suitable protective clothing and gloves. : Xylene

Contents Where applicable, refer to the following regulatory provisions: Directive 82/501/EEC (‘Activates linked to risks of serious accidents’) and subsequent amendments. 16. OTHER INFORMATION Main bibliographic sources

: ECDIN – Environmental Chemicals Data and Informatio0n Networking – Joint Research Centre, Commission of the European Communities. SAX’s DANGEROUS PROPERTIES OF INDUSTRIAL MATERIALS –Eight Editions – Van Nostrand Reinold. ACGIH – Treshold Limited Values –1997 edition. This information only concerns the above-mentioned product and does not need to be valid if used with other product(s) or in any process. The information is to our best knowledge correct and complete and is given in good faith but without warranty. It remains the user’s own responsibility to make sure that the information is appropriate and complete for his special use of this product. This MSDS cancels and replaces any preceding release. Editor : MAS Paints & Chemicals Industry.

LAPORAN PAGI Tanggal : 05 Desember 2011 Data Injeksi Air

Cuaca : Cerah Tekanan (psig) line sumur

Uraian Produksi WIP2 Produksi WIP1 Total Injeksi Sumur TBN - A1 Sumur TBN - A2 Sumur TBN - A3 Sumur TBN - A9 Sumur TBN - C6 Sumur TBN - D45 Sumur TBN - D28 Sumur TBN - F17 Sumur TBN - F19 Sumur TBN - H27 Sumur TBN - U40 Sumur TBN - U61 Sumur PDT-6

Kualitas air

berat jenis Ca solid

TSS D Oxygen B Peralatan MUARA TAWAR

Intake Pump (P - 01) Feed Pump (P - 02) Outfall Canal Tank (T - 101) Pemakaian listrik hari ini Pemakaian listrik s/d hari ini Transfer Genset

-

200 200 200 230 1300 1300 1350 1300

200 170 200 220 1300 1200 1300 1300

1.24 2.76 0.27 0.89 2.22 1.39 2.49 3.24

18,977.00 8,787.00 27,764.00 1,781.00 3,975.00 394.00 1,279.00 3,199.00 2,003.00 3,585.00 4,662.00

250 1350 1350 1350

200 1350 1300 1350

0.94 0.14 1.33 2.38

1,358.00 195.00 1,912.00 3,421.00

Unit

Standar

Nilai

Kg/lt ppm micromtr

1.02 420 <10 +-7 <5 <50

mg/lt ppb

Running Devices

13.18 6.10

Totalizer Barel

Hari ini barrel

1650 500

Kumulatif barrel

3,190,209.00 -

30,822,164.68 6,623,056.17 37,445,220.85 6,504,370.02 273,383.56 136,425.23 2,122,052.82 7,365,563.29 2,301,905.70 3,421,444.87 2,363,693.90 2,498,899.87 4,936,655.68 362,294.67 172,261.00 438,109.81

76,923.00 103,182.00 16,858.00 4,504.00 7,174.00 40,973.00 3,507.00 159,040.00 17,515.00 77,758.00 Siang

Malam

Tambahan Kimia

Unit

Kumulatif (bulan)

-

liter liter

-

liter

-

liter

340C 360C

Depan Ruang Genset : Di Header Pompa Injeksi : Arah angin :

6.93 0.84 0

260C 290C Barat

Running hours

24 24 12 x 160 (kWH) 23033 x 160 (kWH) tek.pompa tek.line (psi) Rate Hari ini (Barel) Totalizer 160 150 6.55 9,436.00 G#1-163764 kwh / G#2-158805 kwh. A B 116 A A A

B

Injection Pump (P - 04)

A

B

Filter Feed Pump (P - 03) Back Wash Pump (P - 08) Vacuum Pump (P - 09) Clean Water Pump (P - 10) Re-Cycle Pump (P - 05) Air Compressor (K - 01) Clarifier (T - 102) Media Filter (V - 101) Cartridge Filter (F - 102) Deaerator (V - 103) Raw Water Tank (T - 103) Clean Water Tank (T - 104) Pit Tank (T - 105) Fuel Gas Filter (F - 01) Produce Water Treatment Plant

A A A A A A A A A A A A A A

B B B B B B

Pompa Bahan Kimia

Aliran Bpm

C

C

B B B

Running Devices E I

RH

23 17 10 24 23 23 23 23 23 23 Volume ( liter ) 251

PAC Polimer 12 Caustic Soda Corrosion Inhibitor B C 23 43 Scale Inhibitor A D 23 51 Oxygen Scavenger F Biocide G 12 176 HCl Kegiatan Pemeliharaan & Catatan Penting Operasi Operasi

Kumulatif 6,363,641.80

Running pompa : A = H89/ B = H798/ C = H1067 Backwash pk …...dan pk …….

Cerat masuk : 0 / 1.685.032 BBL Produksi WTP hari ini : sekarang : BBL Kumulatif Tambahan Unit Kimia (bulan) liter gram 4000 -

liter liter liter liter

300 400 300

Pemeliharaan

* Pk.00.30 WIP2 selesai perbaikan P3, lanjut operasi. * Pk.22.00 G#1 shut down & P4B stop (G#1 low coolant water engine). * Pk.00.45 WIP2 stop pompa injeksi P2 (rubber piston bocor). * Pk.22.40 pengisian air radiator/coolant water G#1. * Pk.02.30 WIP2 start P2 (selesai perbaikan). * Pk.23.00 start G#1 & P4B, lanjut injeksi ke sumur cluster (Tbn-A & Tbn-H). * WIP2 injeksi line 6" dgn 3 pompa (P2, P3 & P4) frek,24 Hz press 1650 psi.

PERTAMINA TAMBUN

Diperiksa :

Disiapkan :

Operator :

Indra Yudha Ka. Ops. & Pml.

Fariz Syawaludin Pws. Operasi

Fathul Rahman

LAPORAN PAGI Tanggal : 06 Desember 2011 Data Injeksi Air

Cuaca : Cerah Tekanan (psig) line sumur

Uraian Produksi WIP2 Produksi WIP1 Total Injeksi Sumur TBN - A1 Sumur TBN - A2 Sumur TBN - A3 Sumur TBN - A9 Sumur TBN - C6 Sumur TBN - D45 Sumur TBN - D28 Sumur TBN - F17 Sumur TBN - F19 Sumur TBN - H27 Sumur TBN - U40 Sumur TBN - U61 Sumur PDT-6

Kualitas air

berat jenis Ca solid

TSS D Oxygen B Peralatan MUARA TAWAR

Intake Pump (P - 01) Feed Pump (P - 02) Outfall Canal Tank (T - 101) Pemakaian listrik hari ini Pemakaian listrik s/d hari ini Transfer Genset

-

150 200 180 200 1300 1250 1250 1250

150 150 180 180 1300 1200 1200 1250

1.24 2.51 0.26 0.83 2.21 1.36 2.43 3.13

18,764.00 8,295.00 27,059.00 1,785.00 3,610.00 379.00 1,197.00 3,189.00 1,955.00 3,502.00 4,507.00

220 1250 1250 1250

190 1250 1200 1200

0.92 0.13 1.40 2.36

1,324.00 192.00 2,017.00 3,402.00

Unit

Standar

Nilai

Kg/lt ppm micromtr

1.02 420 <10 +-7 <5 <50

mg/lt ppb

Running Devices

Kumulatif barrel

3,207,870.00 -

30,838,825.68 6,656,236.17 37,445,220.85 6,506,155.02 276,993.56 136,804.23 2,123,249.82 7,368,752.29 2,303,860.70 3,424,946.87 2,368,200.90 2,498,899.87 4,937,979.68 362,486.67 173,840.00 441,511.81

78,708.00 106,792.00 17,237.00 5,701.00 7,175.00 42,928.00 7,009.00 163,547.00 18,839.00 79,775.00 Siang

Malam

Tambahan Kimia

Unit

Kumulatif (bulan)

-

liter liter

-

liter

-

liter

330C 350C

Depan Ruang Genset : Di Header Pompa Injeksi : Arah angin :

6.93 0.84 0

240C 280C Timur

Running hours

24 24 10 x 160 (kWH) 23043 x 160 (kWH) tek.pompa tek.line (psi) Rate Hari ini (Barel) Totalizer 110 100 5.80 8,352.00 G#1-163884 kwh / G#2-158805 kwh. A B 24 A A A

B

A

B

Filter Feed Pump (P - 03) Back Wash Pump (P - 08) Vacuum Pump (P - 09) Clean Water Pump (P - 10) Re-Cycle Pump (P - 05) Air Compressor (K - 01) Clarifier (T - 102) Media Filter (V - 101) Cartridge Filter (F - 102) Deaerator (V - 103) Raw Water Tank (T - 103) Clean Water Tank (T - 104) Pit Tank (T - 105) Fuel Gas Filter (F - 01) Produce Water Treatment Plant

A A A A A A A A A A A A A A

B B B B B B

C

C

B B B

Running Devices E I

RH

24 17 10 24 24 24 24 24 24 24 Volume ( liter ) 13 541

PAC 8 Polimer 16 Caustic Soda Corrosion Inhibitor B C 24 17 Scale Inhibitor A D 24 57 Oxygen Scavenger F Biocide G 0 0 HCl Kegiatan Pemeliharaan & Catatan Penting Operasi Operasi * Pk.09.30 P4 wip2 stop (Rubber piston bocor) * Pk.10.10 P4 WIP2 selesai perbaikan,lanjut operasi * P1 WIP2 Lanjut perbaikan oleh teknisi Mudking * WIP2 Operasi Dengan 3 pompa (P2,P3&P4)

PERTAMINA TAMBUN

13.03 5.76

Totalizer Barel

Hari ini barrel

1550 500

Injection Pump (P - 04)

Pompa Bahan Kimia

Aliran Bpm

Kumulatif 6,371,993.80

Running pompa : A = H89/ B = H799/ C = H1067 Backwash pk …...dan pk …….

Cerat masuk : 0 / 1.685.032 BBL Produksi WTP hari ini : sekarang : BBL Kumulatif Tambahan Unit Kimia (bulan) 2000 liter gram 4000 -

liter liter liter liter

300 400 300

Pemeliharaan * WIP2 Operasi dengan 2 Genset (G#1 & G#3) * Penambahan bahan kimia Di WIP 1, PAC ( 2000 L ) * Pk. 08.00 Melepas motor P4A untuk perbaikan,dan memindahkan motor P4C Ke P4A.WIP 1

Diperiksa :

Disiapkan :

Operator :

Indra Yudha Ka. Ops. & Pml.

Fariz Syawaludin Pws. Operasi

Sapuan

PLANT

: WIP - TAMBUN

BULAN / TAHUN: Desember 2011 HAL

: Laporan Operasi WIP Tambun

Tgl

Hari

Injeksi Perhari (barel)

1

Kamis

25,167.00

Injeksi dengan WIP 2 , WIP 1 stand by.

2

Jumat

27,732.00

18.15 start G#01 after install turbocharge by vendor (ABB), start P04A, 23.30 G#01 shutdown, switch injection to WIP 2

3

Sabtu

28,283.00

08.00 start G#01 & P04A injeksi to TBN A & H.

4

Minggu

29,912.00

rubber piston pompa injeksi P-3 bocor injeksi dengan P- 1 dan 4

5

Senin

27,764.00

rubber piston pompa injeksi P-2 bocor, injeksi dengan P-1 dan 4

6

Selasa

27,059.00

rubber piston pompa injeksi P-4bocor, injeksi dengan P-1 dan 3

7

Rabu

27,502.00

Injeksi dengan WIP 2 , dan WIP 1.

8

Kamis

25,652.00

Injeksi dengan WIP 2 , dan WIP 1. 18.20 Shut Off G#01 ada rembesan oli pada turbocharge

9

Jumat

20,959.00

10

Sabtu

27,702.00

08. 15 sd 17. 50 tutup jalur injeksi TBN A&H ada kebocoran. 17 . 50 start G#01 & P04A injeksi ke TBN A&H rubber piston pompa injeksi P-4bocor, injeksi dengan P-1 dan 3

11

Minggu

27,325.00


12

Senin

24,039.00


13

Selasa

24,537.00


14

Rabu

24,138.00


15

Kamis

24,363.74


16

Jumat

24,047.00


17

Sabtu

24,315.40


18

Minggu

23,426.00


19

Senin

24,713.00


20

Selasa

24,714.00


21

Rabu

24,827.00

11.00 stop operasi WIP 1, switch to WIP 2

22

Kamis

23,880.00


23

Jumat

24,885.00


24

Sabtu

24,486.00


25

Minggu

24,475.00


26

Senin

24,862.00

rubber piston pompa injeksi P-3 bocor, injeksi dengan P-1 dan 4

27

Selasa

24,250.00


28

Rabu

24,664.00


29

Kamis

24,380.00


30

Jumat

24,868.00

Injeksi dengan WIP 2 , WIP 1 cleaning Raw Water Storage ( T-103 )

31

Sabtu

22,908.00


Rata-Rata Injeksi

Kejadian - Kejadian

25,220.49 Bpwd

34

PLANT

: WIP - TAMBUN

BULAN / TAHUN : Januari 2012 HAL

: Laporan Operasi WIP

Tgl

Hari


1

Sabtu

18,837.00

Operasi Lancar

2

Minggu

16,464.00

20.00 Terjadi kebocoran jalur Pipa PVC di daerah Kobak pelung

3

Senin

10,467.00

21.30 start P02 selesai perbaikan Jalur pipa.

4

Selasa

18,976.65

08.00 start Injeksi 2 pompa. Tekanan P02 maksimal sudah 200 psi

5

Rabu

20,431.68

Operasi Lancar

6

Kamis

21,478.87

Operasi Lancar

7

Jumat

21,084.36

Operasi Lancar

8

Sabtu

21,814.62

08.30 - 12.00 Service E-30 G#2.

9

Minggu

19,532.00

Operasi Lancar

10

Senin

17,318.49

18.25 P04B trip, 20.00 Jalur Pipa Muara Tawar - Tambun Bocor.

11

Selasa

9,888.36

12.00 Recycle full to raw water. 23.00 start P02 M. tawar setelah perbaikan.

12

Rabu

18,868.42

07.25 start P04C, injeksi 2 pompa.

13

Kamis

20,501.55

Operasi Lancar

14

Jumat

19,081.46

Operasi Lancar

15

Sabtu

23,444.50

Operasi Lancar

16

Minggu

21,353.49

19.30 sd 20.00 G#1 trip.

17

Senin

20,064.05

Operasi Lancar

18

Selasa

13,573.17

10.30 Stop P02 M. tawar, info kebocoran. 20.30 start P02 M. tawar setelah perbaikan Kebocoran.

19

Rabu

16,382.68

02.00 sd 09.30 Stop P02 m. tawar, terjadi korslet Power.

20

Kamis

22,662.90

Operasi Lancar

21

Jumat

20,491.20

Operasi Lancar

22

Sabtu

21,568.20

14.40 sd 15.00 stop P04C, test running P04A

23

Minggu

20,363.08

02.40 sd 03.25 trip P04B&C.

24

Senin

21,068.43

08.50 - 10.10 Stop P04B&C, test running P04A.

25

Selasa

21,694.62

Operasi Lancar

26

Rabu

21,674.88

15.45 sd 16.45 Stop P04B&C, test running P04A.

27

Kamis

15,780.23

06.00 sd 15.00 Stop P02 M. tawar, kebocoran jalur pipa.

28

Jumat

19,856.37

08.40 injeksi 2 pompa.

29

Sabtu

21,574.54

23.00 G#1 Triped. 23.15 injeksi 1 pompa.

30

Minggu

21,823.34

00.30 pengisian coolent. 01.30 start injeksi 2 pompa.

31

Senin

20,733.64

08.40 sd 14.45 stop P04B&C, test Injeksi dengan P04A.

Rata-Rata Injeksi

19,317.86

Kejadian - Kejadian

Bpwd

PLANT

: WIP - TAMBUN

BULAN / TAHUN: Februari 2012 HAL

: Laporan Operasi WIP Tambun

Tgl

Hari


1

Rabu

24,650.00

Injeksi dengan WIP 2

2

Kamis

24,858.00


3

Jumat

24,624.00


4

Sabtu

25,941.00


5

Minggu

25,112.00


6

Senin

25,850.00


7

Selasa

26,138.00


8

Rabu

26,107.00


9

Kamis

24,510.00

07.45 sd 13.15 Injeksi jalur WIP 1 dengan P04B WIP 1.

10

Jumat

25,007.00


11

Sabtu

23,277.00


12

Minggu

25,897.00


13

Senin

25,651.00


14

Selasa

24,482.00


15

Rabu

26,339.00


16

Kamis

25,890.00

14.00 Start G#2 Persiapan Injeksi P04B ke jalur eks-Mudking (Cluster A&H)

17

Jumat

25,612.00

Injeksi dengan WIP 1 & 2

18

Sabtu

23,020.00


19

Minggu

23,029.00

04.00 sd 08.30 Stop G#2 & P04B Turbocharger Over heat.start kembali injeksi WIP 1 & 2.

20

Senin

20,370.00

03.15 P04B trip. 08.55 Start G#1 dan P04A ( persiapan running test P04A )

21

Selasa

20,194.00


22

Rabu

21,329.00

11.00 WIP 1 , switch P04A ke P04B ( Kopling chamber P04A patah )

23

Kamis

10,370.00

10.40 Switch P04B ke P04A ( Ganti Chamber P04B), 14.25 WIP Stop ( Kopling chamber patah ). 17.00 Start P04B

24

Jumat

25,122.00

07.30 sd 07.45 , 11.00 sd 11.15 P04B WIP 1 trip, ( High Voltage ), lanjut kembali start 1 pompa.

25

Sabtu

26,777.00


26

Minggu

24,549.00


27

Senin

24,292.00


28

Selasa

25,913.00


29

Rabu

25,764.00


Rata-Rata Injeksi

Kejadian - Kejadian

24,161.17 Bpwd

36

PLANT

: WIP - TAMBUN

BULAN / TAHUN : Maret 2012 HAL

: Laporan Operasi WIP

Tgl

Hari


1

Sabtu

22,311.00

Injeksi dr WIP 1 & 2

2

Minggu

22,556.00


3

Senin

22,298.00


4

Selasa

22,693.00

kondisi Genset Guascore WIP 2 ( G#1&3 trouble, Running G#2 ). injeksi dr WIP 1 & 2.

5

Rabu

22,553.00


6

Kamis

23,767.00


7

Jumat

24,710.90

09.00 Stop Injeksi TBN A1 ( Pengasaman )

8

Sabtu

24,420.00

15.00 Buka jalur Injeksi TBN A1, 15.45 Switch jalur WIP1 injeksi jalur WIP1, WIP2 Injeksi jalur Ex-Mudking

9

Minggu

24,709.00


10

Senin

24,940.00

09.00 Start G#1 & start P04B ( injeksi 2 pompa WIP 1 ). 19.30 Stop P04B ada suara berisik.

11

Selasa

26,005.00

09.00 Start G#1 & start P04B ( injeksi 2 pompa WIP 1 ). 16.00 info kebocoran jalur PVC M. Tawar. 19.00 Stop P0B injeksi 1 pompa ( Raw water Tekor )

12

Rabu

20,644.00

19.00 Selesai perbaikan Pipa PVC, start P02A 50 psi

13

Kamis

26,415.00

Perbaikan kebocoran Pipa PVC. 09.30 Start G#2 & P04B injeksi 2 pompa. 10.45 sd 21.40 pengasaman TBN A3

14

Jumat

27,772.00

11.30 Stop P04B ada suara gesekan yg fatal.

15

Sabtu

26,185.00


16

Minggu

25,805.00

16.00 P02 M. Tawar bagi jalur untuk WIP 1 & 2 ( P. artha Trouble ). Injeksi dr WIP 1 & 2

17

Senin

22,128.00

Suplay P02 untuk WIP 1&2, 08.44 P. artha normal kembali. Injeksi dr WIP 1 & 2

18

Selasa

21,067.00

06.30 sd 23.00 Suplay P02 untuk WIP 1&2, Breaker P. muara tawar artha terbakar

19

Rabu

25,430.00

Perbaikan kebocoran Pipa PVC. 15.00 selesai perbaikan start P02 50 psi

20

Kamis

27,013.00

21.15 Rubber piston pompa injeksi P01 WIP2 jebol. Injeksi dr WIP 1 & 2

21

Jumat

26,146.00

10.00 tutup TBN F17 pengasaman.

22

Sabtu

26,445.00

06.10 G#2 Triped, 08.10 Start G#2 dan P04A lanjut injeksi . 10.00 buka sumur TBN F17.

23

Minggu

27,840.00


24

Senin

27,560.00

08.30 Stop P04A bersihkan strainer dan persiapan switch jalur injeksi ( WIP 1 injeksi ke jalur Mudking)

25

Selasa

28,356.00


26

Rabu

28,604.00


27

Kamis

28,797.00

11.30 sd 17.45 P02A suplay WIP1 & 2, pompa muara tawar artha trip.

28

Jumat

27,419.00


29

Sabtu

28,220.11


30

Minggu

28,328.00


31

Senin

28,135.00

07.00 sd 19.00 tutup injeksi TBN U61 pengasaman.

Rata-Rata Injeksi

25,460.39

Bpwd

Kejadian - Kejadian

37

Revised October 23, 2006 POLYURETHANE Page 1 of 3 MSDS MATERIAL SAFETY DATA SHEET

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