LEMIGAS DIREKTORAT JENDERAL MIGAS SCA-SCB GGR STUDY BRAVO SATTELITE FIELD PREPARED BY LEMIGAS GGR TEAM RESERVOIR ENGINEER April, 29th 2024 www.lemigas.esdm.go.id OUTLINE 1. GENERAL WORKFLOW 2. DATA AVAILABILITY 3. ROCK ANALYSIS 4. PVT ANALYSIS 5. PRODUCTION 6. PRESSURE ANALYSIS LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 2 GENERAL WORKFLOW DATA GATHERING AND QC Not Started PVT Analysis SCAL-RCAL Analysis Production Analysis Pressure Analysis INTEGRATION Critical Initialization Results • Fluid distribution and contacts • OOIP & OGIP volumes • Aquifer to HC ratio • Initial datum pressures and temperatures Equilibration validation: • No saturation or pressure changes with time • No liberated solution gas • consistent fluid contact, bubble point pressures & fluid densities • Stability model validation Pressure Matching validation : • Liquid production (Field, Reservoir, and Well basis) • Pressure profile: • SFT(RFT), SBHP, PBU, SFL from SWAB Test Saturation Matching validation (Field, Reservoir, and Well basis) : • Water cut • Oil production • GOR performance • Water production • Gas production Calibrating to FBHP by adjusting PI multiplier from last workover LEMIGAS | DIREKTORAT JENDERAL MIGAS In-Progress STATIC MODEL Completed Dynamic Modeling Initialization In place? Match Not match Adjust model parameters Equilibration NO Stable? YES Pressure Matching NO Good Match? YES Adjust model parameters Saturation Matching Good Match? YES NO Adjust model parameters Calibration Production Forecast • Adjust Capillary pressure • Fluid Contact Global Pressure adjustments : • Transmissibility XYZ multipliers • Aquifer pore volume factors • Aquifer strength • Rock compressibility • Kv/Kh ratio • Aquifer transmissibility • Completion review Global Saturation adjustments : • Oil-water relative permeability curve • Swir and Sorw • Krw and Krow • Vertical transmissibility (Tz) • Adjust layer PIs to change layer production allocations • Transmissibility multiplier • Completion review End your excellent partner in oil and gas 3 PROGRESS Scope of Work Data Review and Analysis DST and RFT Analysis, Production History History Matching Analytical-Based Remaining Oil Initiallization History Matching Reservoir Model Based Production Forecast Depletion Plan Precentage (%) 3 from 3 1.5 from 3 - Remarks Prelimenary SCAL, PVT Pressure Analysis, Completion, and Production History - Last Week To Do List - Pressure SBHP Recap per sand Menampilkan timeline zona yang dibuka saat produksi LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 2. DATA AVAILABILITY LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 5 DATA AVAILABILITY SB-SC SB-SC NO 1 2 DATA Fluid Data PVT Water Analysis Rock Properties RCAL 3 4 5 6 7 8 9 SCAL Pressure Data Production Data Production Performance Well/Workover History Production Profile SFL/WFL Swab Data Well Completion Well Diagram Completion History Well Test PBU/PDD DST RFT Well Report Dynamic Model Data Grid Model Property Distribution Fault ETC Completion Log LEMIGAS | DIREKTORAT JENDERAL MIGAS CHECK REMARKS √ √ SB-1 (DST-1 & DST-2B), SC-1 (DST-1 & DST-3), SC-6 (DST-1 & DST-4) SB-1, SC-1, SC-2, SC-6 √ √ √ SB-1 (SWC), SBA-2 (Full Diameter Core & Conventional), SB-4 (Conventional core), SC-1 (SWC), SC-2 (SWC), SC-3 (SWC), SC-4 (SWC), SC-5 (Conventional) Analog (BZ-2, BZZA-7, BZZA-8, BZZA-9) SBHP SURVEY (SBA-2, SBA-4ST, SBA-5, SCA3L, SCA3S) √ √ SBA (1, 2, 4ST, 5) ; SCA (1L, 1S, 2L, 2S, 3L, 3S, 5) SBA (1, 2, 4ST, 5) ; SCA (1L, 1S, 2L, 2S, 3L, 3S, 5) SBA (1, 2, 4ST, 5, 5ST) ; SCA (1L, 1S, 2L, 2S, 3L, 3S, 5) √ √ SBA (1, 2, 4ST, 5) ; SCA (1, 2, 3, 5) SBA (1, 2, 4ST, 5) ; SCA (1L, 1S, 2L, 2S, 3L, 3S, 5) √ √ √ √ SB-1, SC-1, SC-2, SC-3, SC-4, SC-6 SB (1 & 2) ; SC (1, 2, 3, 4, 5, & 6) SB-1, SC-1, SC-4, SC-5 ALL WELLS √ ALL WELLS WELL NAME EQUAL WELL NAME SBA-1 SB-1 SBA-2 SBA-3 SBA-4 SB-2 SBA-4ST SBA-5 SBA-5ST SCA-1 SC-1 SCA-2 SC-2 SCA-3 SC-3 SC-4 SC-5 SCA-5 SC-6 Required Data : • SBHP after production for MBAL • Perforation date for splitting • Well History, Prod Performance, Well Diagram SBA-5 ST Note : S = Short L = Long your excellent partner in oil and gas 6 PVT DATA AVAILABILITY PVT = 6 PTA = 14 DST DATA Explo Wells Prod Well SB-1 SB-1 SB-1 SB-2 SC-1 SC-1 SC-1 SC-1 SC-1 SC-1 SC-2 SC-2 SC-2 SC-3 SC-3 SC-3 SC-3 SC-3 SC-3 SC-3 SC-4 SC-4 SC-4 SC-4 SC-4 SC-5 SC-6 SC-6 SC-6 SC-6 SC-6 SC-6 SC-6 SC-6 SC-6 SBA-1 SBA-1 SBA-1 SBA-4 SBA-5 SBA-5 SBA-5 SCA-1 SCA-1 SCA-1 SCA-1 SCA-1 SCA-1 SCA-2 SCA-2 SCA-2 DST# Chk 1 2A 2B 1 #N/A #N/A #N/A 1 1 (PERF) 2 1/2" 1/2" 1/2" 3/8" 3A 3A (retest) 1 2 3 1 1A 2 3 4 5 6 1 2 2A 2B 3 #N/A 1 1 1 2 3 4 4 4 5 1/2" 3/8" #N/A 3/8" 1/2" 1/2" 1/2" 1/2" 1/2" 3/8" 1/2" 1/2" 1/2" 3/4" 3/4" #N/A 3/8" 3/8" 3/8" 3/8" 3/8" 1/2" 3/4" 1" 3/8" 3/8" 1/2" 1" 5/8" 3/8" Top Depth Bot Depth Commingle Top Commingle Depth 7933 7724 7724 9838 8438 8095 7784 8110 8139 7846 7654 7600 7600 8566 8215 8002 10634 10634 10582 10382 10134 8992 7848 8562 8362 8450 8362 7591 #N/A 10828 10828 10828 10378 10192 10036 10036 10036 8978 7950 7744 7765 9868 8456 8150 7792 8132 8156 7876 7664 7664 7664 8578 8290 8056 10740 10740 10602 10392 10150 9004 7887 8574 8376 8456 8376 9604 #N/A 10858 10858 10858 10356 10201 10064 10064 10064 8986 LEMIGAS | DIREKTORAT JENDERAL MIGAS 7880 7884 8308 8318 8456 8450 10232 10247 Form Zone Lith TAF TAF TAF #N/A #N/A TAF #N/A TAF SB-78 SB-76 SB-76 #N/A #N/A SB-76 #N/A SC-80 Sand Sand Sand #N/A #N/A Sand #N/A Sand fluid Remarks Condensate Oil Oil No Fluid #N/A Oil #N/A Oil #N/A TAF SC-77B Sand No Fluid TAF SC-75 Sand Oil TAF SC-76 Sand Oil TAF SC-77 Sand Oil TAF SC-80 Sand Oil TAF SC-77 Sand Water TAF SC-75 Sand Oil TAF Intra Talang AkarSand Gun not Fired TAF Intra Talang AkarSand Condensate TAF SC-74B Sand Condensate TAF SC-72 Sand N2 Lifting TAF SC-71 Sand Condensate TAF SC-68 Sand Condensate Massive MassiveSand/Limestone No Fluid TAF SC-80 Sand Oil TAF SC-78 Sand Oil TAF SC-78 Sand Oil TAF SC-77B Sand Oil TAF SC-72 Sand Wet Gas #N/A TAF SC-77B Sand Condensate TAF SC-77B Sand Condensate TAF SC-77B Sand Condensate TAF SC-76 Sand N2 Lifting / No Fluid TAF SC-75 Sand N2 Lifting / No Fluid TAF SC-74C Sand Condensate TAF SC-74C Sand Condensate TAF SC-74C Sand Condensate TAF SC-69 Limestone Condensate API SG Gas GOR BOPD BWPD MMCFPD WC GOR CALC 57 40.1 33.6 #N/A #N/A #N/A #N/A 35.8 #N/A #N/A 16 38.5 37.5 44.3 #N/A 43.5 #N/A 55.2 51 #N/A 60.7 68.1 #N/A 30.8 30 #N/A 30.2 64.7 #N/A 52.8 53 53 #N/A #N/A 60.8 60.8 60.8 69.5 0.971 1.112 1.14 #N/A #N/A #N/A #N/A 1.03 #N/A #N/A 1.054 1.05 1.048 #N/A #N/A 0.958 #N/A 0.814 0.843 #N/A 0.838 0.844 #N/A 1.165 1.2 #N/A 1.23 0.964 24033 2402 1051 #N/A #N/A 1732 #N/A 648 #N/A #N/A 5763 13629 11350 1622 #N/A 11199 #N/A #N/A 9939 #N/A 403 15194 #N/A 276 1170 #N/A 970 165500 #N/A #N/A #N/A #N/A #N/A #N/A 15757 13905 14444 #N/A 64.6 1648 2189 #N/A #N/A 1624 #N/A 662 #N/A #N/A 475 510.7491 648 971 0 834 #N/A 660 1090 #N/A 295 1030 #N/A 98.5 345 11.25 325 7 #N/A 391 444 522 #N/A #N/A 527 1264 816 12 197 0 0 #N/A #N/A 8 #N/A #N/A #N/A #N/A #N/A #N/A #N/A #N/A 586 #N/A #N/A #N/A #N/A #N/A #N/A #N/A #N/A 150 153 #N/A #N/A 67 #N/A 0 52 77 #N/A #N/A 0 256 18 #N/A 1.552 3.959 2.3 #N/A #N/A 2.817 #N/A 0.428 #N/A #N/A 2.737 6.961 7.357 1.578 0 9.34 #N/A 6.56 5.22 #N/A 4.52 15.902 #N/A 0.0277 0.404 #N/A 0.315 1.2 #N/A 6.5 9.1 11.6 #N/A #N/A 8.304 17.579 11.791 0.6 75.3% 0.0% 0.0% #N/A #N/A 0.5% #N/A #N/A #N/A #N/A #N/A #N/A #N/A #N/A 100.0% #N/A #N/A 18.0% 8.0% #N/A 10.0% 7.0% #N/A 60.4% 30.7% #N/A #N/A 90.5% #N/A 0.0% 10.5% 12.9% #N/A #N/A 0.0% 16.8% 2.2% #N/A 24024.8 2402.3 1050.7 #N/A #N/A 1734.6 #N/A 646.5 #N/A #N/A 5762.1 13629.0 11353.4 1625.1 #N/A 11199.0 #N/A 9939.4 4789.0 #N/A 15322.0 15438.8 #N/A 281.2 1171.0 #N/A 969.2 171428.6 #N/A 16624.0 20495.5 22222.2 #N/A #N/A 15757.1 13907.4 14449.8 50000.0 0.89 0.89 0.89 #N/A #N/A 0.956 0.902 0.956 0.878 • • • • • • SB-1 DST#1 (SB-78) SB-1 DST#2B (SB-76) SC-1 DST#1 (SC-80) SC-1 DST#3 (SC-75) SC-6 DST#1 (SC-77B) SC-6 DST#4 (SC-74C) PTA • • • • • • • • • • • • • • SB-1 DST#1 (SB-78) SB-1 DST#2B (SB-76) SC-1 DST#1 (SC-80) SC-1 DST#2 (SC-77B) SC-1 DST#3 (SC-75) SC-1 DST#3A (SC-75) SC-2 DST#1 (SC-80) SC-2 DST#3 (SC-75) SC-3 DST#4 (SC-71) SC-3 DST#5 (SC-68) SC-4 DST#1 (SC-80) SC-4 DST#2 (SC-78) SC-6 DST#4 (SC-74C) SC-6 DST#5 (SC-69) your excellent partner in oil and gas 7 Daily Rate (FIELD) DATA AVAILABILITY (Production) SB-1 (SBA-1) SB-2 (SBA-2) SBA-4ST SBA-5 SCA • • • • • • • SCA-1L SCA-1S SCA-2L SCA-2S SCA-3L SCA-3S SCA-5 Source : SCA SCB Production.xls Start : 01/11/1992 Last date : 01/04/2018 LEMIGAS | DIREKTORAT JENDERAL MIGAS 1992 6000.0 1996 2000 Water Rate (Field) 2004 2008 2012 Gas Rate (Field) 2016 2020 2024 50000.0 45000.0 5000.0 40000.0 35000.0 4000.0 30000.0 3000.0 25000.0 20000.0 2000.0 15000.0 Gas Rate (MSCFD) • • • • Oil Rate/Water Rate (BOPD/BWPD) SBA Oil Rate (Field) 10000.0 1000.0 5000.0 0.0 1992 1996 2000 2004 2008 2012 2016 2020 0.0 2024 Date Well List Oil Cummulative (MMBO) Gas Cummulative (MMSCF) Water Cummulative (MMBW) SBA-1 1.44 8506.95 2.20 SBA-2 0.76 2363.82 0.43 SBA-4ST 0.26 1548.83 0.06 SBA-5 0.50 1349.75 0.18 SBA-5ST 0.23 6346.76 0.11 SCA-1L 0.41 1572.52 0.02 SCA-1S 0.11 4199.87 0.56 SCA-2L 0.15 1962.13 0.05 SCA-2S 0.14 4203.30 0.32 SCA-3L 0.15 3917.82 0.11 SCA-3S 0.15 5015.76 0.07 SCA-5 0.52 5997.90 1.04 SBA 3.18 20115.11 4.03 SCA 1.62 26869.28 2.18 FIELD 4.80 46984.39 your excellent partner 6.21 in oil and gas 8 ROCK - ANALYSIS - SCAL LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 9 SCAL Analysis (Sample Oil-Water Selection BZ-2 ANALOG) Krw Sw 0.50 LEMIGAS | DIREKTORAT JENDERAL MIGAS Kro Kro Krw 1.0 0.8 0.6 0.4 0.2 0.0 0.00 0.50 Sw Krw Kro Krw Krw 1.0 0.8 0.6 0.4 0.2 0.0 0.00 0.50 1 0.8 0.6 0.4 0.2 0 1.00 Kro Krw Sw Relative Permeability BZ-2 (36) Kro 1 0.8 0.6 0.4 0.2 0 1.00 Krw Kro Sw 1 0.8 0.6 0.4 0.2 0 1.00 Sw Relative Permeability BZ-2 (138) 1.0 0.8 0.6 0.4 0.2 0.0 0.00 0.50 Kro Relative Permeability BZ-2 (60) Kro Kro 1.0 0.8 0.6 0.4 0.2 0.0 0.00 Krw Relative Permeability BZ-2 (64) Kro Krw Kro 1 0.8 0.6 0.4 0.2 0 1.00 0.50 1 0.8 0.6 0.4 0.2 0 1.00 Sw 1 0.8 0.6 0.4 0.2 0 1.00 Relative Permeability BZ-2 (33) Kro Krw Kro 0.50 Krw Sw Relative Permeability BZ-2 (101) 1.0 0.8 0.6 0.4 0.2 0.0 0.00 Kro 1.0 0.8 0.6 0.4 0.2 0.0 0.00 Krw Sw 0.50 Relative Permeability BZ-2 (124) 1.0 0.8 0.6 0.4 0.2 0.0 0.00 0.50 1 0.8 0.6 0.4 0.2 0 1.00 Krw Krw 1 0.8 0.6 0.4 0.2 0 1.00 Krw Kro 1.0 0.8 0.6 0.4 0.2 0.0 0.00 Krw 0.50 1 0.8 0.6 0.4 0.2 0 1.00 Relative Permeability BZ-2 (104) Kro 1.0 0.8 0.6 0.4 0.2 0.0 0.00 Krw Kro Relative Permeability BZ-2 (131) Kro Krw Sw *Sample 101, 60,138, and 33 Reversed at the end of Krw Test, caused of fine migration your excellent partner in oil and gas 10 SCAL Analysis (Sample Oil-Water Selection BZZA-7 ANALOG) Sw Kro 1.0 0.5 0.0 0.00 0.50 1.0 0.8 0.6 0.4 0.2 0.0 1.00 Krw Relative Permeability BZZA-7 (37A) Kro Krw Sw 1.0 0.8 0.6 0.4 0.2 0.0 0.5 0.0 0 0.5 1 Kro Krw Krw Krw Relative Permeability BZZA-7 (1) A K A R 1.0 0.8 0.6 0.4 0.2 0.0 1.0 0.8 0.6 0.4 0.2 0.0 0 0.5 Kro Krw 1 Sw Relative Permeability BZZA-7 (2) 1.0 0.8 0.6 0.4 0.2 0.0 1.0 0.8 0.6 0.4 0.2 0.0 0 Sw LEMIGAS | DIREKTORAT JENDERAL MIGAS 0.50 Kro Sw Kro Kro 1.0 Krw Relative Permeability BZZA-7 (99A) B A T U R A J A 1 0.8 0.6 0.4 0.2 0 1.00 Krw 0.50 Krw 1.0 0.8 0.6 0.4 0.2 0.0 0.00 0.5 Krw 0.0 0.00 Kro T A L A N G Kro 0.5 1.0 0.8 0.6 0.4 0.2 0.0 1.00 Relative Permeability BZZA-7 (3) Kro Kro 1.0 Krw Relative Permeability BZZA-7 (39A) Kro Krw 1 Sw *Sample only taken from Talang Akar Formation your excellent partner in oil and gas 11 SCAL Analysis (Sample Oil-Water Selection BZZA-8 ANALOG) 0.0 0.00 0.50 Sw Krw 0.5 0.0 0.00 0.50 1.0 Kro Krw Sw 1.0 0.8 0.6 0.4 0.2 0.0 0.5 0.0 0 0.5 Krw Kro 1.0 0.8 0.6 0.4 0.2 0.0 1.00 Relative Permeability BZZA-8 (120) Kro 1.0 Kro 0.5 1.0 0.8 0.6 0.4 0.2 0.0 1.00 Krw Kro 1.0 Relative Permeability BZZA-8 (217) Krw Relative Permeability BZZA-8 (229) Kro Krw 1 Sw *Sample 217 and 120 Reversed at the end of Krw Test LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 12 SCAL Analysis (Sample Oil-Water Selection BZZA-9 ANALOG) 0.50 0.0 0.00 Krw 0.50 Sw Kro 1.0 0.8 0.6 0.4 0.2 0.0 0.5 0.0 Krw 0 0.5 Sw 0.0 0.00 0.50 Sw Krw 1 Relative Permeability BZZA-9 (117) Kro Krw Kro Krw Kro 0.5 1.0 0.8 0.6 0.4 0.2 0.0 1.00 Kro Sw Relative Permeability BZZA-9 (112) 1.0 Krw 0.5 1.0 1.0 1.0 0.5 0.5 0.0 0.00 0.50 0.0 1.00 Krw 0.0 0.00 Kro 1.0 0.8 0.6 0.4 0.2 0.0 1.00 Relative Permeability BZZA-9 (61) Kro 0.5 1.0 Kro 1.0 0.8 0.6 0.4 0.2 0.0 1.00 Krw Kro 1.0 Relative Permeability BZZA-9 (65) Krw Relative Permeability BZZA-9 (72) Kro Krw Sw *All sample from BZZA-9 Reversed on Krw Test LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 13 SCAL Analysis (Normalization) SCAL Normalization (LET) SCAL Normalization (Corey) 1 1 0.9 0.9 0.8 0.8 0.7 0.7 0.6 0.6 0.5 0.5 0.4 Kr Kr 0.4 0.3 0.3 0.2 0.2 0.1 0.1 0 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 Sw 0 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 Sw Krw Kro krw correy MEAN kro correy MEAN kro correy MIN krw correy MIN Krw Kro krw LET MEAN kro LET MEAN kro correy MAX krw correy MAX Poly. (Krw) kro LET MIN krw LET MIN kro LET MAX krw LET MAX Log. (Kro) Poly. (Kro) Poly. (Krw) Log. (Kro) Poly. (Kro) BASE now nw LEMIGAS | DIREKTORAT JENDERAL MIGAS 4 1.5 MIN BASE MAX 9 2.3 1 0.95 Low Eow Tow Lw Ew Tw 1 10 1 1.2 2.8 1.5 MIN 3 15 0.7 1.8 2 1 MAX MIN OIL MAX OIL 1.8 3 1 1.1 15 1.1 1.9 0.8 1 0.6 0.6 1.8 2.7 2.8 2 2 2 1 your excellent partner in oil and gas 14 SCAL Analysis (End Point Correlation - Swc) y = -0.0217x + 0.2612 R² = 0.6861 0 2 4 6 8 10 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 1.00 y = -2E-05x + 0.1941 R² = 0.3759 10.00 FZI Krw @Sor Sor 0.4000 0.6000 Swc LEMIGAS | DIREKTORAT JENDERAL MIGAS 1000.00 10000.00 y = 0.0946x + 0.2583 R² = 0.0056 0.2000 0.4000 0.8000 1.0000 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 0.0000 RT 1 y = -0.8764x + 0.7301 R² = 0.3006 2 3 4 0.2000 0.4000 0.6000 0.6000 0.8000 1.0000 Swc kro @Swc vs Swc y = -1.5537x + 0.5168 R² = 0.2658 0.2000 100.00 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 0.0000 Perm, mD krw @Sor vs Swc 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 0.0000 Sor vs Swc Sor 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 Swc vs k Swc Swc Swc vs FZI 0.8000 EP Type FZI Swc FZI Swc FZI Swc FZI Swc swc 0.140 0.140 0.195 0.195 0.229 0.229 0.246 0.246 sor 0.264 0.272 0.285 0.277 0.297 0.280 0.303 0.282 krw @ sor 0.322 0.300 0.189 0.213 0.108 0.160 0.068 0.134 kro @ swc 0.614 0.608 0.552 0.559 0.514 0.529 0.495 0.514 1.0000 Swc your excellent partner in oil and gas 15 SCAL Analysis (End Point Correlation - FZI) y = -0.0217x + 0.2612 R² = 0.6861 0 2 4 6 8 10 10 9 8 7 6 5 4 3 2 1 0 y = 0.0014x + 2.7812 R² = 0.8347 Sor 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 1 10 FZI Krw @Sor Sor 2 4 6 FZI LEMIGAS | DIREKTORAT JENDERAL MIGAS 1000 10000 y = -0.008x + 0.3089 R² = 0.058 0 2 4 8 10 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 RT 1 2 3 4 y = 0.0242x + 0.4784 R² = 0.3339 0 2 4 6 8 10 FZI kro @Swc vs FZI y = 0.0516x + 0.0326 R² = 0.4259 0 100 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 Perm, mD krw @Sor vs FZI 1.0000 0.9000 0.8000 0.7000 0.6000 0.5000 0.4000 0.3000 0.2000 0.1000 0.0000 Sor vs FZI FZI vs k FZI Swc Swc vs FZI 6 8 EP Type FZI Swc FZI Swc FZI Swc FZI Swc swc 0.140 0.140 0.195 0.195 0.229 0.229 0.246 0.246 sor 0.264 0.272 0.285 0.277 0.297 0.280 0.303 0.282 krw @ sor 0.322 0.300 0.189 0.213 0.108 0.160 0.068 0.134 kro @ swc 0.614 0.608 0.552 0.559 0.514 0.529 0.495 0.514 10 FZI your excellent partner in oil and gas 16 SCAL Analysis (Denormalization) BASE CASE (Swc End Point Correlation - Corey) BASE CASE (FZI End Point Correlation - Corey) BASE CASE (Swc End Point Correlation - LET) BASE CASE (FZI End Point Correlation - LET) LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 17 SCAL Analysis (Sample Oil-Gas BZ-2 ANALOG) Krg 0.400 0.600 0.800 1.000 Krg 0.200 Sg Kro/Krg Kro/Krg Krg 0.400 0.600 0.800 1.000 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Krg 0.600 0.800 Sg LEMIGAS | DIREKTORAT JENDERAL MIGAS 1.000 Kro/Krg Kro/Krg Krg 0.200 0.400 0.600 1.0 0.8 0.6 0.4 0.2 0.0 0.000 0.800 1.000 0.600 Sg 1.000 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Kro Krg 0.200 0.400 0.600 0.800 1.000 Relative Permeability BZ-2 (138) Krg 0.400 0.800 Sg Kro 0.200 0.600 Relative Permeability BZ-2 (104) Krg 0.200 0.400 Sg Relative Permeability BZ-2 (131) Kro 0.400 Kro Sg Relative Permeability BZ-2 (124) 0.200 1.000 Kro Sg 1.0 0.8 0.6 0.4 0.2 0.0 0.000 0.800 Relative Permeability BZ-2 (101) Kro 0.200 0.600 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Sg Relative Permeability BZ-2 (64) 1.0 0.8 0.6 0.4 0.2 0.0 0.000 0.400 Kro/Krg 0.200 Kro Kro/Krg Kro 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Relative Permeability BZ-2 (60) 0.800 1.000 Kro/Krg 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Relative Permeability BZ-2 (36) Kro/Krg Kro/Krg Relative Permeability BZ-2 (33) 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Kro Krg 0.200 0.400 0.600 0.800 1.000 Sg your excellent partner in oil and gas 18 SCAL Analysis (Sample Oil-Gas BZZA-7 ANALOG) Relative Permeability BZZA-7 (3) Kro 0.0 0.000 Krg 0.200 0.400 0.600 0.800 1.000 Sw Relative Permeability BZZA-7 (37A) Kro/Krg 1.0 0.5 Kro 0.0 0.000 Krg 0.200 0.400 0.600 0.800 1.000 Sw Relative Permeability BZZA-7 (99A) Kro/Krg 1.0 0.5 0.0 0.000 Kro Krg 0.200 0.400 0.600 Sg LEMIGAS | DIREKTORAT JENDERAL MIGAS 0.800 1.000 B A T U R A J A T A L A N G A K A R 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Kro Krg 0.200 0.400 0.600 0.800 1.000 Sg Relative Permeability BZZA-7 (1) Kro/Krg 0.5 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Kro Krg 0.200 0.400 0.600 0.800 1.000 Sg Relative Permeability BZZA-7 (2) Kro/Krg Kro/Krg 1.0 Kro/Krg Relative Permeability BZZA-7 (39A) 1.0 0.8 0.6 0.4 0.2 0.0 0.000 Kro Krg 0.200 0.400 0.600 0.800 1.000 Sg your excellent partner in oil and gas 19 SCAL Analysis (Sample Oil-Gas BZZA-8 ANALOG) Relative Permeability BZZA-8 (229) Relative Permeability BZZA-8 (217) 0.5 0.0 0.000 Kro Krg 0.200 0.400 0.600 Sg LEMIGAS | DIREKTORAT JENDERAL MIGAS 0.800 1.000 1.0 0.5 0.0 0.000 Kro Krg 0.200 0.400 0.600 Sg 0.800 1.000 Kro/Krg 1.0 Kro/Krg Kro/Krg 1.0 Relative Permeability BZZA-8 (120) 0.5 0.0 0.000 Kro Krg 0.200 0.400 0.600 0.800 1.000 Sg your excellent partner in oil and gas 20 SCAL Analysis (Sample Oil-Gas BZZA-9 ANALOG) Relative Permeability BZZA-9 (72) Relative Permeability BZZA-9 (65) 0.5 0.0 0.000 Kro 0.400 0.600 0.800 0.5 0.0 0.000 Krg 0.200 1.000 1.0 Kro 0.400 0.600 0.800 0.5 0.0 0.000 Krg 0.200 Sg 1.000 Kro Krg 0.200 0.400 Sg 1.000 1.0 0.5 Kro Krg 0.200 0.400 0.600 Sg 0.800 1.000 Kro Kro 0.800 Relative Permeability BZZA-9 (117) 1.0 0.0 0.000 0.600 Sg Relative Permeability BZZA-9 (112) LEMIGAS | DIREKTORAT JENDERAL MIGAS Kro 1.0 Kro Kro 1.0 Relative Permeability BZZA-9 (61) 0.5 0.0 0.000 Kro Krg 0.200 0.400 0.600 0.800 1.000 Sg your excellent partner in oil and gas 21 SCAL Analysis (Normalization) The data used are 20 selected Cores from Talang Akar COREY TA only SCAL Normalization LET TA only SCAL Normalization 1.0 1.0 0.9 0.9 0.8 0.8 0.7 0.7 0.6 0.6 0.5 0.5 0.4 0.4 0.3 0.3 0.2 0.2 0.1 0.1 0.0 0.0 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.0 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 Krg Kro Kro Base Krg Base Kro Min Krg Kro Kro Base Krg Base Kro Min Krg Min Kro Max Krg Max Poly. (Krg) Poly. (Kro) Krg Min Kro Max Krg Max Poly. (Krg) Poly. (Kro) BASE nog ng LEMIGAS | DIREKTORAT JENDERAL MIGAS 3 2.15 MIN 4.5 3.5 MAX 1.5 0.8 Lo Eog Tog Lg Eg Tg BASE 1.45 3.80 0.98 1.42 2.20 0.95 MIN 1.50 6.00 0.90 2.50 2.50 0.70 1.0 MAX MIN OIL MAX OIL 0.90 0.9 1.5 5.50 6 3.8 2.40 0.9 2.4 1.30 1.3 2.5 0.65 0.65 2.5 1.30 1.3 0.7 your excellent partner in oil and gas 22 SCAL Analysis (End Point Correlation - Sgcr) y = 0.0007x + 0.0222 R² = 0.0055 0 2 4 6 8 10 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 y = -1E-06x + 0.0268 R² = 0.0098 1 10 FZI Kro@Sgi Krg@Sogcr 0.04 1000 10000 y = -0.9267x + 0.5125 R² = 0.1037 0 0.02 0.04 0.06 Sgcr LEMIGAS | DIREKTORAT JENDERAL MIGAS 0.08 0.10 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 0.00 RT 1 y = 1.7773x + 0.3393 R² = 0.1233 2 3 4 0.02 0.04 0.06 0.06 0.08 0.1 Sgcr Krg@Sogcr vs Sgcr y = 0.6734x + 0.606 R² = 0.0215 0.02 100 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 Perm, mD kro@Sgi vs Sgcr 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 0.00 Sogcr vs Sgcr Sogcr 0.1 0.09 0.08 0.07 0.06 0.05 0.04 0.03 0.02 0.01 0 Sgcr vs k Swc Sgcr Sgcr vs FZI 0.08 EP Type FZI Sgcr FZI Sgcr FZI Sgcr FZI Sgcr sgcr 0.0261 0.0261 0.0243 0.0243 0.0232 0.0232 0.0227 0.0227 sogcr krg @ sogcr 0.4782 0.3660 0.4883 0.3857 0.5021 0.4051 0.4900 0.3825 0.5167 0.4289 0.4910 0.3806 0.5240 0.4408 0.4915 0.3796 kro @sgi 0.6294 0.6236 0.6153 0.6224 0.6066 0.6216 0.6023 0.6213 0.10 Sgcr your excellent partner in oil and gas 23 SCAL Analysis (End Point Correlation - FZI) y = 0.0007x + 0.0222 R² = 0.0055 0 2 4 6 8 10 9 8 7 6 5 4 3 2 1 0 10 y = 0.0014x + 2.7479 R² = 0.8329 1 10 FZI Kro@Sgi Krg@Sogcr 2 4 6 FZI LEMIGAS | DIREKTORAT JENDERAL MIGAS 1000 10000 y = -0.0093x + 0.5303 R² = 0.1322 0 2 4 8 10 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 RT 1 y = -0.0152x + 0.4511 R² = 0.1136 2 3 4 0 2 4 6 8 10 FZI Krg@Sogcr vs FZI y = 0.0055x + 0.5986 R² = 0.0182 0 100 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 Perm, mD kro@Sgi vs FZI 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 Sogcr vs FZI Sogcr 0.1 0.09 0.08 0.07 0.06 0.05 0.04 0.03 0.02 0.01 0 FZI vs k FZI Sgcr Sgcr vs FZI 6 8 EP Type FZI Sgcr FZI Sgcr FZI Sgcr FZI Sgcr sgcr 0.0261 0.0261 0.0243 0.0243 0.0232 0.0232 0.0227 0.0227 sogcr krg @ sogcr 0.4782 0.3660 0.4883 0.3857 0.5021 0.4051 0.4900 0.3825 0.5167 0.4289 0.4910 0.3806 0.5240 0.4408 0.4915 0.3796 kro @sgi 0.6294 0.6236 0.6153 0.6224 0.6066 0.6216 0.6023 0.6213 10 FZI your excellent partner in oil and gas 24 Pc Analysis (RT use Conventional only) J-Function Model Capillary Pressure 120 HWFL vs Sw 50 1000 45 900 40 800 35 700 30 600 80 RT-2 60 RT-3 Pc, Psi J(Sw) RT-1 RT-1 25 RT-2 20 Power (RT-1) Power (RT-2) Power (RT-3) 40 20 0 0 0.5 Sw 1 RT-3 HWFL 100 RT-2 400 15 300 10 200 5 100 0 RT-1 500 RT-3 0 0.0 0.2 0.4 0.6 Sw 0.8 1.0 0.0 0.2 0.4 0.6 0.8 1.0 Sw Only Available for 3 rock type, the samples for the 4th rock type does not exist LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 27 PVT - ANALYSIS - PVT DATA LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 33 PVT COMPOSITION (SB-SC) DATA AVAILABILITY (PVT) • • • • • • Mol (%) PVT SB-1 DST#1 (SB-78) – Wet Gas/Condensate SB-1 DST#2B (SB-76) – Black Oil SC-1 DST#1 (SC-80) – Black Oil SC-1 DST#3 (SC-75) – Volatile Oil SC-6 DST#1 (SC-77B) – Condensate SC-6 DST#4 (SC-74C) – Condensate *Fluid Determination Type is based on Mc Cain Category and PVT Report description and result Component SBA-1 (DST-1) Well Stream Mol% GPM SBA-1 (DST-2B) Well Stream Mol% Wt % 100.00 90.00 80.00 70.00 60.00 50.00 40.00 30.00 20.00 10.00 0.00 H2S CO2 N2 C1 C2 C3 iC4 nC4 iC5 nC5 C6 C7+ SBA-1 (DST-1) 0.00 21.35 0.60 52.29 4.57 12.00 2.92 2.22 1.12 0.52 0.57 1.84 SBA-1 (DST-2B) 0.00 17.27 0.23 27.66 4.78 13.80 3.35 3.66 1.68 1.07 3.16 23.34 SCA-1 (DST-1) 0.00 12.82 0.20 27.01 4.80 14.74 3.98 4.27 2.15 1.30 1.79 26.94 SCA-1 (DST-3) 0.00 21.99 0.24 34.41 3.24 10.50 3.56 3.16 2.16 1.21 2.07 17.46 SCA-5 (DST-1) 0.00 40.07 0.08 34.45 5.05 10.19 2.21 1.87 0.62 0.42 0.54 4.50 SCA-5 (DST-4) 0.00 39.34 0.16 39.57 3.06 7.55 2.17 1.66 0.93 0.54 1.08 3.94 SCA-1 (DST-1) Well Stream Mol% Wt % SCA-1 (DST-3) Well Stream Mol% Wt % SCA-5 (DST-1) Well Stream Mol% GPM SCA-5 (DST-4) Well Stream Mol% GPM H2 S Hydrogen Sulfide 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 CO2 Carbon Dioxide 21.35 17.27 9.19 12.82 6.17 21.99 16.36 40.07 39.34 N2 Nitrogen 0.60 0.23 0.08 0.20 0.06 0.24 0.11 0.08 0.16 C1 Methane 52.29 27.66 5.36 27.01 4.74 34.41 9.33 34.45 39.57 C2 Ethane 4.57 1.22 4.78 1.74 4.80 1.58 3.24 1.65 5.05 1.35 3.06 0.82 C3 Propane 12.00 3.31 13.80 7.36 14.74 7.11 10.50 7.83 10.19 2.80 7.55 2.07 iC4 Iso-Butane 2.92 0.96 3.35 2.35 3.98 2.53 3.56 3.50 2.21 0.72 2.17 0.71 nC4 N-Butane 2.22 0.70 3.66 2.57 4.27 2.71 3.16 3.11 1.87 0.59 1.66 0.52 iC5 Tso-Pentane 1.12 0.41 1.68 1.47 2.15 1.70 2.16 2.63 0.62 0.23 0.93 0.34 nC5 N-Pentane 0.52 0.19 1.07 0.93 1.30 1.03 1.21 1.48 0.42 0.15 0.54 0.19 C6 Hexanes 0.57 0.22 3.16 3.21 1.79 1.64 2.07 2.94 0.54 0.22 1.08 0.44 C7+ Heptanes plus 1.84 1.04 23.34 65.74 26.94 70.73 17.46 51.06 100.00 8.04 100.00 100.00 100.00 100.00 100.00 100.00 4.50 100.00 2.23 8.28 3.94 100.00 1.94 7.03 Properties of Heptanes plus: °API Gravity at 60 °F Density, gm/cc at 60 °F Molecular Weight LEMIGAS | DIREKTORAT JENDERAL MIGAS SBA-1 (DST-1) 45.6 0.797 142 SBA-1 (DST-2B) 29.3 0.8791 233 SCA-1 (DST-1) 30.5 0.873 240 SCA-1 (DST-3) 36.1 0.8434 173 SCA-5 (DST-1) 46.33 0.7949 124.78 SCA-5 (DST-4) 44.8 0.8018 124.84 your excellent partner in oil and gas 34 DATA AVAILABILITY (PVT) There are 6 samples of PVT (Gas, Black Oil, Volatile Oil and Condensate) PVT SB-SC No Well Name Test Date of Sampling 1 SBA-1 (SB-1) DST-1 13/02/1990 Talang Akar 2 SBA-1 (SB-1) DST-2B 18/02/1990 3 SCA-1 (SC-1) DST-1 04/04/1990 4 SCA-1 (SC-1) DST-3 07/04/1990 5 SCA-5 (SC-6) DST-1 31/03/1994 6 SCA-5 (SC-6) DST-4 15/04/1944 Formation Sampling Surface Sampling Surface Talang Akar Sampling Surface Talang Akar Sampling Surface Talang Akar Sampling Surface Talang Akar Sampling Surface Talang Akar Sampling Zone SB-78 SB-76 SC-80 SC-75 Interval Depth (ft) 7933-7950 7863-7880 7724-7765 7654-7695 8152-8156 8110-8132 7654-7664 7584-7594 Pressure °API @60 Reservoir Reservoir Depth (ft F Pressure (Psig) Temperature (°F) SSD) Saturation Pressure (Psig) FVF Oil @Pb 3297 GOR @Pb Density@ Visco Oil Pb @Pb 57 7942 3462 280 33.6 7675 3327 265 3122 2.295 1894 0.6288 0.258 35.8 8082 3515 264 2743 2.074 1477 0.6418 0.707 16 7586 3324 247 3324 4.348 4808 0.5663 0.252 SC-77B 10843-10873 52.8 10858 3640 280 3435 SC-74C 10036-10064 60.8 10050 3432 263 3310 ALL LEMIGAS | DIREKTORAT JENDERAL MIGAS Dew Point (Psig) SC 23396 SB your excellent partner in oil and gas 35 PVT - ANALYSIS - PVT QUALITY CHECK AND MATCHING LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 36 PVT QUALITY CHECK Compositional Check (𝟐) Sum xi Sum yi Sum zi Mass Balance QC PVT Samples Integrated Validity and Consistency Analysis Parameters and Criteria • • • • Leakage Check P Lab vs P Field Condition ≤ 10 Psi Yes No Integrated Validity and Consistency Analysis of Qualified PVT samples LEMIGAS | DIREKTORAT JENDERAL MIGAS 2) GOR MB Plot Vs GOR Reported < 5% Difference 4) Impurities, Original Components, and Pseudo Components Deviation of Eliminate Sample Reference : Hoffman QC Plot : Plotting Hoffman factor versus Log k for all the components, nearly straight line means good quality separation. 2. 3. 4. Consider to Use 3,5) R-Squared of Mass Balance Plot ≈ 1 Hoffman Quality Plot <5% • 2) R-Squared Difference of CCE Check <1% 1. • Compositional Check • Separator Check (Hoffman Quality Plot) • CCE/CVD/DLE Check 3) Sum. Mol Fraction = 100 % 5. Laing, L.K. et.al., “Comprehensive PVT Data Review, Fluid Characterization and Grouping Study for Block X in Sarawak, Malaysia”, OTC-31417-MS, Offshore Technology Conference Asia, Kuala Lumpur, 2022. DOI : https://doi.org/10.4043131417-MS Ameen, M , “PVT Quality Check", Reservoir Solutions, Egypt, 2021. https://reservoir-solution.odoo.com Lawrence, John J. et at, “Quality Assessment and Consistency Evaluation of Hydrocarbon PVT Data", IPTC 13784, International Petroleum Technology Conference, Doha, Qatar, 2009. DOI : https://doi.org/10.2523.IPTC-13784-MS Hoffman, A. E. et al., “Equilibrium Constants for a Gas-Condensate Systems, SPE 219-G, Petroleum Transactions, AIME, Houston, Texas, 1953, Vol 198,1-10. DOI : https://doi.org/10.2118/219-G Akpabio, J. U. et al, “PVT Fluid Characterization and Consistency Check for Retrograde Condensate Reservoir Modeling’, SPE-172359MS, SPE Nigeria Annual International Conference and Exhibition, Lagos. 2014 DOI : https://doi.org/10.2118/172359-MS your excellent partner in oil and gas 37 OLD ZONE : SB-78 NEW ZONE : fs_3.1 PVT QUALITY CHECK Checking method Opening Pressure Vs Sampling Pressure Sum xi (Liquid Comp) Compositional Sum yi (Gas Comp) Analysis Sum zi (Wellstream Comp) Material Balance QC Separator Hoffman Check Y-function CCE Rel. vol. straight untill pb Liquid Drop out with CCE Note Not Valid 22 Psi Difference, Leakage Indication Valid Valid Valid Not Valid Y function vs Pressure 7.16% Valid 1.4000 1.2000 1.0000 0.8000 0.6000 0.4000 0.2000 0.0000 Calc Yfunction y = 0.0002x + 0.774 R² = 0.9936 0 1000 2000 3000 Linear (Calc Yfunction) 4000 Pressure Valid Valid Insufficient Data Relative Volume Relative Volume CVD Validity Y Function Item Leakage Check SB-1 DST#1 (SB-78) 7.000 6.000 5.000 4.000 3.000 2.000 1.000 0.000 y = -0.0001x + 1.3805 R² = 0.9867 Calcualted Rel. Vol. Reported Rel. Vol Above Pb 0 2000 4000 Pressure 6000 Reported Rel.Vol. Below Pb Hoffman Plot SB-1 (DST-1) Sampling Condition T : 84 deg F P : 187 Psig R² : 0.9518 LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 39 PVT Analysis SB-1 (DST-1) SB-1 DST#1 Liq Dropout WELL STREAM Gas Z Factor Last Reservoir Pressure/Bubble Point @3462 Psig Component H2S CO2 N2 C1 C2 C3 iC4 nC4 iC5 nC5 C6 C7+ TOTAL Properties of Heptane + API gravity @ 60 F Density,gm/cc at 60 F Molecular Weight Mol Percent Weight Percent 0 21.35 0.6 52.29 4.57 12 2.92 2.22 1.12 0.52 0.57 1.84 100 - 45.6 0.7984 144 Sampling Condition Last Reservoir Pressure 3462 Dew Point Pressure 3297 Reservoir Temperature 280 Prim. Sep. Pressure 187 Prim. Sep. Temperature 84 Field Stock Tank Liq. Gravity 57 Prim Sep Gas Prod Rate 1589 Lab Gas Gravity Original GOR Prim. Sep Gas/ Stock Liq Ratio Lab Gas Liq Ratio Z init Bg LEMIGAS | DIREKTORAT JENDERAL MIGAS Two Phase Z factor Separator Condition @187 Psig 1.008 23396 23029 PSIG PSIG F PSIG F API @ 60 F MSCF/day SCF/STB SCF/BBL SCF/BBL ft3/scf • As the GOR and the C7+ Composition Shown as Wet Gas Fluid Type. • The last reservoir pressure is above the dew point pressure • The phase envelope still shown as a little bit oily or need to be improved. Due to matching the liquid dropout, the Gas z factor didn’t match fairly. your excellent partner in oil and gas 41 OLD ZONE : SB-76 NEW ZONE : fs_2.3 PVT QUALITY CHECK Checking method Opening Pressure Vs Sampling Pressure Sum xi Compositional Sum yi Analysis Sum zi Material Balance QC Separator Hoffman Check Y-function CCE Rel. vol. straight untill pb Validity Y function vs Pressure Note 3.0000 Valid y = 0.0005x + 0.9182 R² = 0.9895 2.5000 Y Function Item Leakage Check Valid Valid Valid Not Valid SB-1 DST#2B (SB-76) 2.0000 Calc Yfunction 1.5000 1.0000 Linear (Calc Yfunction) 0.5000 Close to 5% Diff 0.0000 Valid Not Valid Valid 0 1000 2000 3000 4000 Pressure Above 1% Very Close Relative Volume Relative Volume 6.000 Calculated Rel.vol 5.000 4.000 3.000 y = -2E-05x + 1.073 R² = 0.9963 2.000 1.000 Reported Rel.vol Above Pb Reported Below Pb 0.000 0 2000 4000 6000 Pressure LEMIGAS | DIREKTORAT JENDERAL MIGAS Slope Oil Density, lb/cuft Oil MW, lb/lbmol MB GOR, scf/stb Lab GOR, scf/stb Difference, % 0.71 53.45 155 1035.22 962 7.61 Hoffman Plot SB-1 (DST-2B) Sampling Condition T : 90 deg F P : 155 Psig R² : 0.8895 R² Without C7+ = 0.9895 your excellent partner in oil and gas 42 PVT Analysis SB-1 (DST-2B) SBA-1 (DST-2B) Component Well Stream Mol% Wt% 0.00 0.00 H2S Hydrogen Sulfide CO2 Carbon Dioxide 17.27 9.19 0.08 N2 Nitrogen 0.23 C1 Methane 27.66 5.36 C2 Ethane 4.78 1.74 C3 Propane 13.80 7.36 iC4 Iso-Butane 3.35 2.35 nC4 N-Butane 3.66 2.57 iC5 Tso-Pentane 1.68 1.47 N-Pentane 1.07 0.93 Hexanes 3.16 3.21 23.34 100.00 65.74 100.00 nC5 C6 C7+ Heptanes plus Properties of Heptanes plus: °API Gravity at 60 °F Density, gm/cc at 60 °F Molecular Weight Sampling Condition Last Reservoir Pressure 3327 Bubble Point Pressure 3122 Reservoir Temperature 265 Prim. Sep. Pressure 155 Prim. Sep. Temperature 90 Field Stock Tank Liq. Gravity 33.6 Prim Sep Gas Prod Rate 2088.08 Prim Sep Liq Prod Rate 2170 Lab Gas Gravity 1.076 Prim. Sep Gas/ Sep Liq Ratio 962 Boi 2.28123 LEMIGAS | DIREKTORAT JENDERAL MIGAS SBA-1 (DST-2B) 29.3 0.8791 233 PSIG PSIG F PSIG F API @ 60 F MSCF/day BBL/day Reservoir Condition @3122 Psig Separator Condition @155 Psig • As the GOR and the C7+ Composition Shown as Black Oil Fluid Type. • The last reservoir pressure is above the bubble point pressure • The phase envelope still shown as Black oil SCF/BBL rb/stb your excellent partner in oil and gas 44 PVT Analysis SB-1 (DST-2B) LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 45 OLD ZONE : SB-80 NEW ZONE : fs_3.4 PVT QUALITY CHECK Checking method Validity Opening Pressure Vs Valid Leakage Check Sampling Pressure Sum xi Valid Valid Compositional Sum yi Analysis Sum zi Valid Material Balance QC Not Valid Separator Hoffman Valid Check Y-function Valid CCE Rel. vol. straight untill pb Valid CVD Liquid Drop out with CCE DLE Insufficient Data MBE check Y function vs Pressure Note 19 Psi Difference, Leakage Indication Different Temperature 9.15% 3.0000 y = 0.0005x + 1.0454 R² = 0.9994 2.5000 Y Function Item SC-1 DST#1 (SB-80) 2.0000 Calc Yfunction 1.5000 1.0000 Linear (Calc Yfunction) 0.5000 0.0000 0 1000 2000 3000 Pressure Relative Volume Relative Volume 5 4 Calcualted Rel. Vol. 3 y = -2E-05x + 1.0551 R² = 0.9943 2 Reported Rel.vol Above Pb 1 0 0 2000 4000 6000 Pressure Hoffman Plot LEMIGAS | DIREKTORAT JENDERAL MIGAS Slope Oil Density, lb/cuft Oil MW, lb/lbmol MB GOR, scf/stb Lab GOR, scf/stb Difference, % 0.71 53.45 155 1035.22 962 7.61 SC-1 (DST-1) Sampling Condition T : 102 deg F P : 246 Psig R² : 0.9785 your excellent partner in oil and gas 46 PVT Analysis SC-1 (DST-1) Component SCA-1 (DST-1) Well Stream Mol% Wt % H2S Hydrogen Sulfide 0.00 0.00 CO2 Carbon Dioxide 12.82 6.17 N2 Nitrogen 0.20 0.06 C1 Methane 27.01 4.74 C2 Ethane 4.80 1.58 C3 Propane 14.74 7.11 iC4 Iso-Butane 3.98 2.53 nC4 N-Butane 4.27 2.71 iC5 Tso-Pentane 2.15 1.70 nC5 N-Pentane 1.30 1.03 C6 Hexanes 1.79 1.64 Heptanes plus 26.94 100.00 70.73 100.00 Properties of Heptanes plus: °API Gravity at 60 °F Density, gm/cc at 60 °F Molecular Weight SCA-1 (DST-1) 30.5 0.873 240 C7+ Sampling Condition Last Reservoir Pressure 3515 Bubble Point Pressure 2743 Reservoir Temperature 264 Prim. Sep. Pressure 246 Prim. Sep. Temperature 102 Field Stock Tank Liq. Gravity 35.8 Prim Sep Gas Prod Rate 434094 Prim Sep Liq Prod Rate 682 Lab Gas Gravity 1.006 Prim. Sep Gas/ Sep Liq Ratio 637 Boi LEMIGAS | DIREKTORAT JENDERAL MIGAS PSIG PSIG F PSIG F API @ 60 F MSCF/day BBL/day Reservoir Condition @3515 Psig Separator Condition @246 Psig • As the GOR and the C7+ Composition Shown as Black Oil Fluid Type. • The last reservoir pressure is above the bubble point pressure • The phase envelope still shown as Black oil SCF/BBL rb/stb your excellent partner in oil and gas 48 PVT Analysis SC-1 (DST-1) LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 49 PVT QUALITY CHECK Checking method Opening Pressure Vs Sampling Pressure Sum xi Validity Sum yi Valid Sum zi Valid Material Balance QC Not Valid 17% diff Hoffman Valid Y-function Valid C7+ Quite far 1 Outlier at Yfunction @3157 Psig adjusted Valid CVD Rel. vol. straight untill pb Liquid Drop out with CCE DLE MBE check Leakage Check Compositional Analysis Separator Check Y function vs Pressure Valid 2.0000 Valid 1.5000 Y Function 1.0000 Linear (Y Function) 0.5000 y = 0.0003x + 0.8166 R² = 0.9973 0.0000 0 1000 2000 3000 4000 Pressure Relative Volume Insufficient Data 6 Relative Volume CCE Note Y Function Item SC-1 DST#3 (SC-75) Calcualted Rel. Vol. 5 4 Series2 3 y = -5E-05x + 1.1602 R² = 0.9845 2 1 0 0 2000 4000 6000 Reported Below Pb Linear (Series2) Pressure LEMIGAS | DIREKTORAT JENDERAL MIGAS Slope Oil Density, lb/cuft Oil MW, lb/lbmol MB GOR, scf/stb Lab GOR, scf/stb Difference, % 0.54 59.83 110 2161.93 2615 17.33 Hoffman Plot SC-1 (DST-3) Sampling Condition T : 90 deg F P : 240 Psig R² : 0.9864 your excellent partner in oil and gas 51 PVT Analysis SC-1 (DST-3) Component H2S SCA-1 (DST-3) Well Stream Mol% Wt % Hydrogen Sulfide 0.00 0.00 CO2 Carbon Dioxide 21.99 16.36 N2 Nitrogen 0.24 0.11 C1 Methane 34.41 9.33 C2 Ethane 3.24 1.65 C3 Propane 10.50 7.83 iC4 Iso-Butane 3.56 3.50 nC4 N-Butane 3.16 3.11 iC5 Tso-Pentane 2.16 2.63 nC5 N-Pentane 1.21 1.48 C6 Hexanes 2.07 2.94 Heptanes plus 17.46 100.00 51.06 100.00 Properties of Heptanes plus: °API Gravity at 60 °F Density, gm/cc at 60 °F Molecular Weight SCA-1 (DST-3) 36.1 0.8434 173 C7+ Sampling Condition Last Reservoir Pressure 3324 Bubble Point Pressure 3324 Reservoir Temperature 247 Prim. Sep. Pressure 240 Prim. Sep. Temperature 90 Field Stock Tank Liq. Gravity 16 Prim Sep Gas Prod Rate 1103.548 Prim Sep Liq Prod Rate 422 Lab Gas Gravity 1.034 Prim. Sep Gas/ Sep Liq Ratio 2615 Boi 2.074 LEMIGAS | DIREKTORAT JENDERAL MIGAS PSIG PSIG F PSIG F API @ 60 F MSCF/day BBL/day SCF/BBL rb/stb Last Reservoir Pressure/Bubble Point @3324 Psig Separator Condition @240 Psig • As the GOR and the C7+ Composition Shown as Volatile Oil Fluid Type. • The last reservoir pressure is the same as bubble point pressure • The phase envelope still shown as Black Oil/Volatile Oil • The API reported in PVT and Completion log is 16 API, minwhile the zone above on the dst (3A and 3A retest) and completion log stated the API are 38.5 and 3.75 your excellent partner in oil and gas 53 PVT Analysis SC-1 (DST-3) Old Completion Log LEMIGAS | DIREKTORAT JENDERAL MIGAS New Completion Log your excellent partner in oil and gas 54 PVT Analysis SC-1 (DST-3) LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 55 PVT QUALITY CHECK Leakage Check Compositional Analysis Checking method Opening Pressure Vs Sampling Pressure Sum xi Sum yi Sum zi Material Balance QC Validity Not Valid Y function vs Pressure Note 20 Psi Difference, Leakage Indication. Different Temperature Valid Valid Valid Not Valid 30.99% 1.4 1.2 Y Function Item SC-6 DST#1 (SC-77B) 1 0.8 Calc Yfunction y = 0.0001x + 0.7497 R² = 0.9995 0.6 0.4 Linear (Calc Yfunction) 0.2 Separator Check Hoffman Valid CCE Y-function Rel. vol. straight untill pb CVD Liquid Drop out with CCE Valid Valid Insufficient Data 0 0 1000 2000 3000 4000 Pressure Relative Volume Relative Volume 5.000 y = -0.0001x + 1.4767 R² = 0.9826 4.000 Calculated Rel. Vol 3.000 Reported Rel. Vol. Above Pb 2.000 1.000 0.000 0 2000 4000 6000 Reported Rel. Vol. Below Pb Pressure OLD ZONE : SC-77B NEW ZONE : mfs_4 LEMIGAS | DIREKTORAT JENDERAL MIGAS Slope Oil Density, lb/cuft Oil MW, lb/lbmol MB GOR, scf/stb Lab GOR, scf/stb Difference, % 0.12 47.88 81 10199 14779 30.99 Hoffman Plot SC-6 (DST-1) Sampling Condition T : 32 deg F P : 185 Psig R² : 0.9069 your excellent partner in oil and gas 56 PVT Analysis SC-6 (DST-1) SC-6 DST#1 SC-6 DST#1 (SC-77B) Last Reservoir Pressure/Bubble Point @3432 Psig WELL STREAM Component H2S CO2 N2 C1 C2 C3 iC4 nC4 iC5 nC5 C6 C7+ TOTAL Properties of Heptane + API gravity @ 60 F Density,gm/cc at 60 F Molecular Weight Mol Weight Percent Percent 0 40.07 0.08 34.45 5.05 10.19 2.21 1.87 0.62 0.42 0.54 4.5 100 46.33 0.7949 124.78 Separator Condition @3310 Psig Lab Gas Gravity Prim. Sep Gas/ Stock Liq Ratio Lab Gas Liq Ratio Z init Bg LEMIGAS | DIREKTORAT JENDERAL MIGAS Gas Z Factor Two Phase Z factor Sampling Condition Last Reservoir Pressure 3432 Dew Point Pressure 3310 Reservoir Temperature 263 Prim. Sep. Pressure 310 Prim. Sep. Temperature 55 Field Stock Tank Liq. Gravity 60.8 Prim Sep Gas Prod Rate Liq Dropout 11792 0.956 PSIG PSIG F PSIG F API @ 60 F MSCF/da y 14444 SCF/BBL 14138 SCF/BBL 0.8346 0.0199674 01 ft3/scf • As the GOR and the C7+ Composition Shown as Condensate Fluid Type. • The last reservoir pressure is above the dew point pressure • The phase envelope still shown as Condensate. Due to matching the liquid dropout, the Gas z factor didn’t match fairly. your excellent partner in oil and gas 58 PVT QUALITY CHECK Compositional Analysis Checking method Opening Pressure Vs Sampling Pressure Sum xi Validity Not Valid Sum yi Valid Valid Valid Not Valid Separator Check Hoffman Valid CCE Y-function Rel. vol. straight untill pb CVD Liquid Drop out with CCE Valid Valid Insufficient Data 1.4 1.2 42.48% 1 0.8 Calc Yfunction y = 0.0001x + 0.7341 R² = 0.9991 0.6 0.4 Linear (Calc Yfunction) 0.2 0 0 1000 2000 3000 4000 Pressure Relative Volume 5.000 Relative Volume Sum zi Material Balance QC Y function vs Pressure Note 47 Psi Difference, Leakage Indication Different Temperature Y Function Item Leakage Check SC-6 DST#4 (SC-74C) y = -0.0001x + 1.4488 R² = 0.9809 4.000 Calculated Rel. Vol 3.000 Reported Rel. Vol. Above Pb 2.000 1.000 0.000 0 2000 4000 6000 Reported Rel. Vol. Below Pb Pressure OLD ZONE : SC-77C NEW ZONE : mfs_3 LEMIGAS | DIREKTORAT JENDERAL MIGAS Slope Oil Density, lb/cuft Oil MW, lb/lbmol MB GOR, scf/stb Lab GOR, scf/stb Difference, % 0.16 45.89 72 8309 14444 42.48 Hoffman Plot SC-6 (DST-4) Sampling Condition T : 55 deg F P : 310 Psig R² : 0.9938 your excellent partner in oil and gas 60 PVT Analysis SC-6 (DST-4) SC-6 DST#4 Component H2S CO2 N2 C1 C2 C3 iC4 nC4 iC5 nC5 C6 C7+ TOTAL Properties of Heptane + API gravity @ 60 F Density,gm/cc at 60 F Molecular Weight Liq Dropout Last Reservoir Pressure/Bubble Point @3640 Psig WELL STREAM Mol Percent Weight Percent 0 39.34 0.16 39.57 3.06 7.55 2.17 1.66 0.93 0.54 1.08 3.94 100 - 44.8 0.8018 124.84 LEMIGAS | DIREKTORAT JENDERAL MIGAS Gas Z Factor Separator Condition @3345 Psig Two Phase Z factor Sampling Condition Last Reservoir Pressure 3640 Dew Point Pressure Reservoir Temperature Prim. Sep. Pressure Prim. Sep. Temperature 3345 280 185 32 PSIG PSIG F PSIG F API @ 60 F MSCF/day Field Stock Tank Liq. Gravity 52.8 Prim Sep Gas Prod Rate 6596 Lab Gas Gravity 0.89 Prim. Sep Gas/ Stock Liq Ratio 16852.3 SCF/BBL Lab Gas Liq Ratio 14779 SCF/BBL Z init 0.8346 Bg 0.03562 ft3/scf • As the GOR and the C7+ Composition Shown as Condensate Fluid Type. The composition quite similar with DST-1. • The last reservoir pressure is above the dew point pressure • The phase envelope still shown as Condensate. Due to matching the liquid dropout, the Gas z factor didn’t match fairly. your excellent partner in oil and gas 62 PTA Analysis from DST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 64 PTA SB-1 DST-1 DST Operation Summary WET GAS : 12/Feb/1990 – 14/Feb/1990 : 7933 – 7950 ft : 17 ft : : Wet Gas : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 57 @ 60 F Gas/Oil Ratio : 14014 (SCF/STB) Gas Gravity (SG) : 1.03 Well Properties Hole Temperature Hole/Casing Size Tubing : 277.5 F : 7 in : 2.875 in (OD) , 2.441 in (ID) Available Rate N2 Only LEMIGAS | DIREKTORAT JENDERAL MIGAS No Hydrocarbon Rate in the 1st Build Up, the analysis can’t be yourdone excellent partner in oil and gas 65 PTA SB-1 DST-2B Date Perforation Interval Net Pay Zone Major Phase Available Rate : 12/Feb/1990 – 14/Feb/1990 : 7724 – 7765 ft : 41 ft : : Black Oil : Gas Rate & Liquid Rate This DST operation and has 2 build up phase. The phase can be analyzed is the 2nd Build Up Phase with 417.6 Min test duration BLACK OIL DST Operation Summary Hydrocarbon Properties Oil Gravity : 33.6 @ 60 F Gas/Oil Ratio : 989 (SCF/STB) Gas Gravity (SG) : 1.11 Well Properties Hole Temperature Hole/Casing Size Tubing : 275.83 F : 7 in : 2.875 in (OD) , 2.441 (ID) Available Rate LEMIGAS | DIREKTORAT JENDERAL MIGAS 2nd Build Up Phase your excellent partner in oil and gas 66 BLACK OIL PTA SB-1 DST-2B 2nd PBU (4th Periode) h K Skin Pi = 41 ft = 519 mD = 15.2 = 3223.63 Psi The Type-curve of the 2nd PBU period represent the response of homogeneous model. The down phase of the derivative curves suspected as a disturbance during the test. The 1st Build Up Model doesn’t have the production rate before the well shut in. LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 67 BLACK OIL PTA SC-1 DST-1 : 3/Apr/1990 – 5/Apr/1990 : (8110-8132 & 8139-8156) ft : 39 ft : : Black Oil : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate DST Operation Summary Hydrocarbon Properties Oil Gravity : 35.8 @ 60 F Gas/Oil Ratio : 669.3 (SCF/STB) Gas Gravity (SG) : 1.03 Well Properties Hole Temperature Hole/Casing Size Tubing : 275.15 F : 7 in : 2.875 in (OD) , 2.441 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 68 PTA SC-1 DST-1 2nd PBU (4th Periode) BLACK OIL h K Skin Pi = 39 ft = 8.14 mD = 6.01 = 3400.85 Psi This model build as the shape of pressure response. We have tried the dual layers model as the log and perforation shown, but it’s difficult to match the graph. h K Skin Pi = 39 ft = 8.38 mD = 6.33 = 3423.1 Psi This analysis was suggested by A.I. as the suspected profile of the pressure model. The validation may be required after the structure map done. LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 69 PTA SC-1 DST-3 VOLATILE OIL DST Operation Summary : 6/Apr/1990 – 8/Apr/1990 : 7654-7664 ft : 10 ft : : Volatile Oil : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 16 @ 60 F Gas/Oil Ratio : 3156.8 (SCF/STB) Gas Gravity (SG) : 1.05 Well Properties Hole Temperature Hole/Casing Size Tubing : 253.55 F : 7 in : 2.875 in (OD) , 2.441 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 70 PTA SC-1 DST-3 VOLATILE OIL 2nd PBU (4th Periode) h K Skin Pi = 10 ft = 12100 mD = 25.1 = 3244.02 Psi This model build as the shape of pressure response. No A.I. suggestion for this kind of pressure responses.The homogeneous reservoir with rectangle boundary choosen. The rectangle boundary model choosen because of the derivatives curved downwards as the response of the pressure transient has reached the boundaries. LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 71 PTA SC-1 DST-3a VOLATILE OIL DST Operation Summary : 8/Apr/1990 – 10/Apr/1990 : 7600-7664 ft : 64 ft : : Volatile Oil : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 39.5 @ 60 F Gas/Oil Ratio : 11190.3 (SCF/STB) Gas Gravity (SG) : 1.05 Well Properties Hole Temperature Hole/Casing Size Tubing : 252.32 F : 7 in : 2.875 in (OD) , 2.441 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 72 PTA SC-1 DST-3a From the pressure and the derivative profile, there’s two possible model that should be validated by the structure map. Circle and Rectangle boundary choosen because the curve downwards as the result of the pressure transient has reached the boundary. LEMIGAS | DIREKTORAT JENDERAL MIGAS VOLATILE OIL h K Skin Pi = 64 ft = 1860 mD = 24 = 3230.67 Psi h K Skin Pi = 64 ft = 1840 mD = 24.1 = 3230.6 Psi your excellent partner in oil and gas 73 PTA SC-2 DST-1 BLACK OIL DST Operation Summary : 31/Aug/1991 – 2/Sep/1991 : 8566-8688 ft : 12 ft : : Black Oil : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 39.5 @ 60 F Gas/Oil Ratio : 1622 (SCF/STB) Gas Gravity (SG) : 0.95 Well Properties Hole Temperature Hole/Casing Size Tubing : 278 F : 7 in : 3.5 in (OD) , 2.992 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 74 PTA SC-2 DST-1 BLACK OIL h K Skin Pi = 10 ft = 20.3 mD = -1.04 = 3775.54 Psi Limited Entry happened when the perforation column is less than total reservoir thickness. This caused various flow type showed in the picture. 1.) Radial flow 2.) Spherical Flow and 3.) Back to Radial Flow LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 75 PTA SC-2 DST-3 CONDENSATE DST Operation Summary : 4/Sep/1991 – 7/Sep/1991 : 8002-8056 ft : 54 ft : : Condensate : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 43.5 @ 60 F Gas/Oil Ratio : 71361 (SCF/STB) Gas Gravity (SG) : 0.96 Well Properties Hole Temperature Hole/Casing Size Tubing : 264 F : 7 in : 3.5 in (OD) , 2.991 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 76 PTA SC-2 DST-3 CONDENSATE h K Skin Pi = 54 ft = 508 mD = 13.8 = 3259.59 Psi From the log above, the hydrocarbon comes out from the same body sand. The boundary needs to be checked later LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 77 CONDENSATE PTA SC-3 DST-4 : 21/Jul/1991 – 23/Jul/1991 : 10134 – 10150 ft : 16 ft : : Condensate : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate DST Operation Summary Hydrocarbon Properties Oil Gravity : 60.7 @ 60 F Gas/Oil Ratio : 16232 (SCF/STB) Gas Gravity (SG) : 0.838 Well Properties Hole Temperature Hole/Casing Size Tubing : 268 F : 7 in : 3.5 in (OD) , 2.992 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 78 PTA SC-3 DST-4 Composite model could be identified from the double IARF which rising or decreasing dependant to its M and D LEMIGAS | DIREKTORAT JENDERAL MIGAS CONDENSATE h K Skin Pi = 16 ft = 11.2 mD = 19 = 3535.21 Psi h K Skin Pi = 16 ft = 11.2 mD = 19 = 3500.94 Psi your excellent partner in oil and gas 79 PTA SC-3 DST-5 CONDENSATE DST Operation Summary : 21/Jul/1991 – 2/Sep/1991 : 8992 – 9004 ft : 12 ft : : Condensate : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 68.1 @ 60 F Gas/Oil Ratio : 15194 (SCF/STB) Gas Gravity (SG) : 0.844 Well Properties Hole Temperature Hole/Casing Size Tubing : 259 F : 7 in : 3.5 in (OD) , 2.992 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 80 PTA SC-3 DST-5 CONDENSATE Homogeneous h K Skin Pi = 12 ft = 5510 mD = 7.49 = 3157.27 Psi Intersecting Fault Limited Entry Limited Entry happened when the perforation column is less than total reservoir thickness. This caused various flow type showed in the picture. 1.) Radial flow 2.) Spherical Flow and 3.) Back to Radial Flow LEMIGAS | DIREKTORAT JENDERAL MIGAS h K Skin Pi = 12 ft = 5100 mD = 6.56 = 3158.23 Psi This model also suggested by A.I. your excellent partner in oil and gas 81 PTA SC-4 DST-1 BLACK OIL DST Operation Summary : 31/Dec/1991 – 1/Jan/1992 : 8562-8574 ft : 12 ft : : Black Oil : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 36.5 @ 60 F Gas/Oil Ratio : 272 (SCF/STB) Gas Gravity (SG) : 1.17 Well Properties Hole Temperature Hole/Casing Size Tubing : 282 F : 7 in : 2.875 in (OD) , 2.442 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 82 BLACK OIL PTA SC-4 DST-1 h K Skin Pi = 12 ft = 8.59 mD = -0.648 = 3506.04 Psi If K1>K2, the pressure drop in layer 1 will be higher than 2. Therefore there will be flow from layer 2 to layer 1 Double permeability model is identified by the cave before the total IARF of 2 layer with different permeability LEMIGAS | DIREKTORAT JENDERAL MIGAS h K Skin Pi = 12 ft = 8.59 mD = -1.17 = 4033.96 Psi your excellent partner in oil and gas 83 PTA SC-4 DST-2 BLACK OIL DST Operation Summary : 1/Jan/1992 – 3/Jan/1992 : (8362-8574 & 8450-8456) ft : 20 ft : : Black Oil : Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 30 @ 60 F Gas/Oil Ratio : 1.7 (SCF/STB) Gas Gravity (SG) : 1.2 Well Properties Hole Temperature Hole/Casing Size Tubing : 280 F : 7 in : 2.875 in (OD) , 2.442 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 84 PTA SC-4 DST-2 BLACK OIL Homogeneous h K Skin Pi Homogeneous h K Skin Pi LEMIGAS | DIREKTORAT JENDERAL MIGAS Parallel Faults = 20 ft = 7.36 mD = -0.428 = 3481.87 Psi One Fault = 20 ft = 7.05 mD = -0.681 = 3452.09 Psi your excellent partner in oil and gas 85 PTA SC-6 DST-1a CONDENSATE DST Operation Summary : 29/Mar/1992 – 1/Apr/1992 : 10828 – 10858 ft : 30 ft : : Condensate : Gas Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 52.8 @ 60 F Gas/Oil Ratio : 16624 (SCF/STB) Gas Gravity (SG) : 0.89 Well Properties Hole Temperature Hole/Casing Size Tubing : 259 F : 7 in : 2.875 in (OD) , 2.441 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 86 PTA SC-6 DST-1A CONDENSATE Two Layers Rectangle h K Skin Pi = 12 ft = 30 mD = -0.8 = 3526.14 Psi Double permeability model is identified by the cave before the total IARF of 2 layer with different permeability If K1>K2, the pressure drop in layer 1 will be higher than 2. Therefore there will be flow from layer 2 to layer 1 LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 87 PTA SC-6 DST-4 CONDENSATE DST Operation Summary : 14/Apr/1994 – 16/Apr/1994 : 10036 – 10064 ft : 28 ft : : Condensate : Gas Rate & Liquid Rate Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 60.8 @ 60 F Gas/Oil Ratio : 14630 (SCF/STB) Gas Gravity (SG) : 0.96 Well Properties Hole Temperature Hole/Casing Size Tubing : 268 F : 7 in : 2.875 in (OD) , 2.441 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 88 PTA SC-6 DST-4 LEMIGAS | DIREKTORAT JENDERAL MIGAS CONDENSATE h K Skin Pi = 28 ft = 30 mD = 10.3 = 3432.34 Psi h K Skin Pi = 28 ft = 201 mD = 9.77 = 3434.41 Psi your excellent partner in oil and gas 89 PTA SC-6 DST-5 CONDENSATE DST Operation Summary : 17/Apr/1994 – 20/Apr/1992 : 8978 – 8986 ft : 28 ft : : Condensate : Gas Rate only before B.U. Date Perforation Interval Net Pay Zone Major Phase Available Rate Hydrocarbon Properties Oil Gravity : 69.5 @ 60 F Gas/Oil Ratio : 16624 (SCF/STB) Gas Gravity (SG) : 0.88 Well Properties Hole Temperature Hole/Casing Size Tubing : 234.7 F : 7 in : 2.875 in (OD) , 2.441 (ID) Available Rate 2nd Build Up Phase LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 90 CONDENSATE PTA SC-6 DST-5 h K Skin Pi = 28 ft = 1.42 mD = 45.8 = 3130.29 Psi The Rate data doesn’t inline with the pressure LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 91 PRODUCTION Production Profile and Splitting Preparation LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 94 PRODUCTION PROFILE SB PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC LEMIGAS | DIREKTORAT JENDERAL MIGAS 3705 BOPD 4/1/1994 734 BOPD 12/1/1992 5% 7 BOPD 4/1/2018 86% your excellent partner in oil and gas 95 PRODUCTION PROFILE SC PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC LEMIGAS | DIREKTORAT JENDERAL MIGAS 2502 BOPD 8/1/1996 617 BOPD 6/1/1996 11% 12 BOPD 3/1/2017 89% your excellent partner in oil and gas 96 PRODUCTION PROFILE SBA-1 Min Date 01-Dec-92 Max Date 01-Apr-18 Well SBA-1 Cum Oil (MMBO) 1.44 Cum Gas (BCF) 8.51 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 97 PRODUCTION PROFILE SBA-1 PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 1624 BOPD 7/1/1993 450 BOPD 12/1/1992 6% 7 BOPD 4/1/2018 86% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 334 MSCFD 743 SCF/STB 3969 MSCFD 8/1/1993 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 98 PRODUCTION PROFILE SBA-2 Min Date 01-Dec-92 Max Date Well SBA-2 01-Jul-07 Cum Oil (MMBO) 0.76 Cum Gas (BCF) 2.36 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 99 PRODUCTION PROFILE SBA-2 PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 1706 BOPD 9/1/1993 284 BOPD 12/1/1992 2% 31 BOPD 7/1/2007 87% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 967 MSCFD 3407 SCF/STB 8788 MSCFD 6/1/1993 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Multilayer Channeling LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 0 PRODUCTION PROFILE SBA-4st Min Date 01-Sep-99 Max Date 01-Jun-07 Well SBA-4ST Cum Oil (MMBO) 0.26 Cum Gas (BCF) 1.55 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 1 PRODUCTION PROFILE SBA-4st PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 751 BOPD 8/1/2000 188 BOPD 5/1/2000 26% 145 BOPD 6/1/2007 51% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 2530 MSCFD 13476 SCF/STB 3062 MSCFD 11/1/1999 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 2 PRODUCTION PROFILE SBA-5 Min Date 01-Nov-93 Max Date 01-Sep-95 Well SBA-5 Cum Oil (MMBO) 0.49 Cum Gas (BCF) 1.35 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 3 PRODUCTION PROFILE SBA-5 PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 1540 BOPD 9/1/1994 273 BOPD 11/1/1993 0% 5 BOPD 9/1/1995 50% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 576 MSCFD 2108 SCF/STB 4549 MSCFD 3/1/1995 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 4 PRODUCTION PROFILE SBA-5st Min Date 01-Mar-00 Max Date 01-Oct-13 Well SBA-5ST Cum Oil (MMBO) 0.23 Cum Gas (BCF) 6.35 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 5 PRODUCTION PROFILE SBA-5st PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 419 BOPD 4/1/2000 316 BOPD 3/1/2000 20% 1 BOPD 10/1/2013 86% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 3391 MSCFD 10722 SCF/STB 6399 MSCFD 6/1/2000 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 6 PRODUCTION PROFILE SCA-1L Min Date 01-Jun-96 Max Date 01-Feb-08 Well SCA-1L Cum Oil (MMBO) 0.41 Cum Gas (BCF) 1.57 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 7 PRODUCTION PROFILE SCA-1L PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 651 BOPD 2/1/2005 53 BOPD 6/1/1996 4% 61 BOPD 2/1/2008 6% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 85 MSCFD 1614 SCF/STB 4344 MSCFD 2/1/1997 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 8 PRODUCTION PROFILE SCA-1S Min Date 01-Jun-96 Max Date 01-Jun-98 Well SCA-1S Cum Oil (MMBO) 0.11 Cum Gas (BCF) 4.20 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 10 9 PRODUCTION PROFILE SCA-1S PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 465 BOPD 12/1/1996 84 BOPD 6/1/1996 6% 1 BOPD 6/1/1998 96% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 804 MSCFD 9532 SCF/STB 10629 MSCFD 1/1/1997 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 0 PRODUCTION PROFILE SCA-2L Min Date 01-Jun-96 Max Date 01-Dec-00 Well SCA-2L Cum Oil (MMBO) 0.15 Cum Gas (BCF) 1.96 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 1 PRODUCTION PROFILE SCA-2L PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 335 BOPD 7/1/1996 35 BOPD 6/1/1996 17% 11 BOPD 12/1/2000 3% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 87 MSCFD 2499 SCF/STB 5124 MSCFD 7/1/2000 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 2 PRODUCTION PROFILE SCA-2S Min Date 01-Jun-96 Max Date 01-Dec-00 Well SCA-2S Cum Oil (MMBO) 0.14 Cum Gas (BCF) 4.20 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 3 PRODUCTION PROFILE SCA-2S PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 458 BOPD 7/1/1996 109 BOPD 6/1/1996 6% 9 BOPD 12/1/2000 10% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 1043 MSCFD 9604 SCF/STB 10449 MSCFD 7/1/1997 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Normal Displacement with High WOR LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 4 PRODUCTION PROFILE SCA-3L Min Date 01-Jun-96 Max Date Well SCA-3L 01-Jan-06 Cum Oil (MMBO) 0.15 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS Cum Gas (BCF) 3.92 SCA-3L your excellent partner in oil and gas 11 5 PRODUCTION PROFILE SCA-3L PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 531 BOPD 10/1/1996 257 BOPD 6/1/1996 17% 1 BOPD 1/1/2006 90% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 1754 MSCFD 6823 SCF/STB 11232 MSCFD 10/1/1996 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Multilayer Channeling with Production Changes LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 6 PRODUCTION PROFILE SCA-3S Min Date 01-Aug-96 Max Date 01-Mar-17 Well SCA-3S Cum Oil (MMBO) 0.15 Cum Gas (BCF) 5.02 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 7 PRODUCTION PROFILE SCA-3S WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Multilayer Channeling with Production Changes LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 8 PRODUCTION PROFILE SCA-5 Min Date 01-Jun-96 Max Date 01-Mar-17 Well SCA-5 Cum Oil (MMBO) 0.52 Cum Gas (BCF) 6.00 WELL PRODUCTION TEST LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 11 9 PRODUCTION PROFILE SCA-5 PEAK OIL PROD PEAK OIL DATE INITIAL OIL RATE INITIAL PROD. DATE INITIAL WC LAST OIL PROD LAST PROD. DATE LAST WC 1106 BOPD 12/1/2003 79 BOPD 6/1/1996 0% 11 BOPD 3/1/2017 86% INITIAL GAS RATE INITIAL GOR PEAK GAS RATE PEAK GAS DATE 1216 MSCFD 15356 SCF/STB 12595 MSCFD 7/1/1996 WATER DIAGNOSTIC PLOT Water Control Diagnostic Plot (K.S. Chan, 1995) GOR Multilayer Channeling with Production Changes LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 12 0 PRESSURE SBHP Pressure Profile LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 12 1 SBHP Pressure Structure PF WELL 1 SB SB SB SB SB SB SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SBA SBA SBA SBA SBA SBA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SBA-2 SBA-2-BHP SB-73A/74 SBA-2 SBA-2-BHP SB-73A/74 SBA-4ST SBA-4ST-BHP B-28BC SBA-4ST SBA-4ST-BHP B-28BC SBA-4ST SBA-4ST-BHP B-28BC SBA-4ST SBA-4ST-BHP B-28BC SCA-1S SCA-1S-BHP SCA-1S SCA-1S-BHP SCA-2L SCA-2L-BHP SC-80 SCA-2S SCA-2S-BHP SC-75 SCA-3L SCA-3L-BHP SCA-3L SCA-3L-BHP SCA-3L SCA-3L-BHP SCA-3L SCA-3L-BHP SCA-3L SCA-3L-BHP SCA-3S SCA-3S-BHP1 SCA-3S SCA-3S-BHP1 SCA-3S SCA-3S-BHP1 SCA-3S SCA-3S-BHP2 SCA-3S SCA-3S-BHP3 SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC SCA-5L SCA-5L-BHP B-28BC 2 3 4 5 6 7 8 9 10 LEMIGAS | DIREKTORAT JENDERAL MIGAS Old Zone New Zone FS SC-73 fs_2.1 SC-75 fs_2.3 SC-75 fs_2.2 SC-77B mfs_3 SC-78 SB-1_BSAT SC-77C SB-1_BSAT SC-74B fs_2.1 SC-75 fs_2.3 SC-80A fs_3.4 SC-75 fs_2.3 SC-75 fs_2.3 SC-76B fs_3.2 SC-77C fs_3.4 SC-79 mfs_3 SC-80B SB-1.2_BSAT SC-69 fs_2.2 SC-69B mfs_1 SC-74B SB-1_BSAT SC-69 mfs_1 SC-69 mfs_1 SC-70 fs_1.3 SC-71 fs_2.2 SC-71B fs_2.3 SC-72 fs_2.4 SC-74B mfs_2 SC-75 mfs_3 SC-76B mfs_4 SC-77B SB-1_BSAT SC-81 SB-1_BSAT Remarks Date of Test Type of test Commingle Commingle Commingle Commingle Commingle Commingle Commingle Commingle Single Single Commingle Commingle Commingle Commingle Commingle Commingle Commingle Commingle Single Single Commingle Commingle Commingle Commingle Commingle Commingle Commingle Commingle Commingle 9/5/2005 9/5/2005 9/4/2005 9/4/2005 9/4/2005 9/4/2005 6/19/2007 6/19/2007 7/13/2002 5/27/2002 6/18/2006 6/18/2006 6/18/2006 6/18/2006 6/18/2006 6/18/2007 6/18/2007 6/18/2007 7/2/2002 7/2/2002 9/1/2005 9/1/2005 9/1/2005 9/1/2005 9/1/2005 9/1/2005 9/1/2005 9/1/2005 9/1/2005 SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP SBHP TEST DEPTH MD 7950.00 7950.00 6800.00 6800.00 6800.00 6800.00 5935.00 5935.00 8566.00 6000.00 10000.00 10000.00 10000.00 10000.00 10000.00 8942.00 8942.00 8942.00 8950.00 8950.00 9993.00 9993.00 9993.00 9993.00 9993.00 9993.00 9993.00 9993.00 9993.00 TEST DEPTH TVD 7273.89 7273.89 6341.78 6341.78 6341.78 6341.78 5865.00 5865.00 8059.46 5668.24 7955.08 7955.08 7955.08 7955.08 7955.08 7118.27 7118.27 7118.27 7124.43 7124.43 9925.00 9925.00 9925.00 9925.00 9925.00 9925.00 9925.00 9925.00 9925.00 DATUM 6989 FIELD Pressure Profile 4000 3500 3000 P@ Datum WELL NAME PETREL NO 2500 2000 SBHP 1500 1000 500 0 1987 1990 1993 1995 1998 2001 2004 2006 2009 Date your excellent partner in oil and gas 12 2 DST Pressure NO Structure PF WELL 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 SB SB SB SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SC SB SB SC SC SC SC SC SC SC SC SC SBA SBA SBA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SCA SBA SBA SCA SCA SCA SCA SCA SCA SCA SCA SCA SB-1 SB-1 SB-1 SC-1 SC-1 SC-1 SC-1 SC-2 SC-2 SC-2 SC-3 SC-3 SC-4 SC-4 SC-4 SC-6 SC-6 SC-6 SC-6 SB-1 SB-1 SC-1 SC-1 SC-2 SC-3 SC-3 SC-4 SC-4 SC-6 SC-6 WELL NAME PETREL LEMIGAS | DIREKTORAT JENDERAL MIGAS Old Zone New Zone SB-78 SB-76 SB-76 SC-80 SC-77B SC-75 SC-76 SC-80 SC-77 SC-75 SC-71 SC-68 SC-80 SC-78 SC-72 SC-77B SC-75 SC-74C SC-69 SB-76 SB-76 SC-75 SC-76 SC-80 SC-71 SC-68 SC-80 SC-78 SC-77B SC-74C FS SC-77B fs_3.1 SC-75 fs_2.3 SC-75 fs_2.3 SC-80A fs_3.4 SC-77B fs_3.1 SC-75 fs_2.3 SC-75 fs_2.3 SC-79B fs_3.4 SC-75 fs_3.1 SC-73 fs_2.3 SC-76B SB-1.2_BSAT SC-68 mfs_1 SC-80C fs_3.5 SC-79B SB-2_BSAT SC-81 mfs_2 SC-81 mfs_4 SC-78 fs_3.2 SC-77B mfs_3 SC-70 SB-1_BSAT SC-75 fs_2.3 SC-75 fs_2.3 SC-75 fs_2.3 SC-75 fs_2.3 SC-79B fs_3.4 SC-76B SB-1.2_BSAT SC-68 mfs_1 SC-80C fs_3.5 SC-79B SB-2_BSAT SC-81 mfs_4 SC-77B mfs_3 Remarks Date of Test Type of test Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single Single 12/2/1990 2/14/1990 2/18/1990 4/3/1990 5/4/1990 6/4/1990 8/4/1990 8/31/1991 2/9/1991 4/9/1991 7/21/1991 7/23/1991 12/31/1992 1/1/1992 8/1/1992 3/23/1994 11/4/1994 4/14/1994 4/17/1994 2/14/1990 2/18/1990 6/4/1990 8/4/1990 8/31/1991 7/21/1991 7/23/1991 12/31/1992 1/1/1992 3/23/1994 4/14/1994 EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU EO PBU P* PTA P* PTA P* PTA P* PTA P* PTA P* PTA P* PTA P* PTA P* PTA P* PTA P* PTA TEST DEPTH MD 7933 7724 7724 8110 7846 7654 7600 8566 8215 8002 10134 8992 8562 8362 7591 10828 10192 10036 8978 7724 7724 7654 7600 8566 10134 8992 8562 8362 10828 10036 TEST DEPTH P @ Depth TVD 7863 3352.99 7654 3213.73 7654 3220.61 8040 3408.88 7776 3203.05 7584 3229.68 7530 3214.16 8059.46 3395.1 7721.19 3280.81 7517.59 3243.73 8061.42 3484.79 7149 3138.72 8483 3452.75 8283 3389.84 7512 3223.26 8531 3638.19 8060 3489.5 7957.98 3437.59 7171.04 3131.8 7654 3223.63 7654 3400.85 7584 3244.02 7530 3230.67 8059.46 3775.54 8061.42 3535.21 7149 3158.23 8483 3506.04 8283 3481.87 8531 3526.14 7957.98 3434.41 your excellent partner in oil and gas 12 3 Mfs 1 Pressure PVT & DST Overview Mfs_1 LEMIGAS | DIREKTORAT JENDERAL MIGAS SC-3(SCA-3) #DST 5 8992-9004 ft MD / 7156.76-7166.03 ft TVDSS 1030 BOPD, GOR 15438.8 SCF/STB Fluid Type : Wet Gas your excellent partner in oil and gas 12 4 SB-1_Bsat Pressure PVT & DST Overview SB-1_Bsat LEMIGAS | DIREKTORAT JENDERAL MIGAS SC-6(SCA-5) #DST 5 8978-8986 ft MD / 7170.99-7177.37 ft TVDSS 12 BOPD, GOR 50000 SCF/STB Fluid Type : Wet Gas your excellent partner in oil and gas 12 5 Fs_1.2 Bsat Pressure No Pressure Profile PVT & DST Overview No Test/DST/PVT Fs_1.2 LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 12 6 Fs_1.3 Pressure PVT & DST Overview No Test/DST/PVT Fs_1.3 LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 12 7 Mfs_2 Pressure PVT & DST Overview No Test/DST/PVT Mfs_2 LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 12 8 fs_2.1 Pressure PVT & DST Overview fs_2.1 LEMIGAS | DIREKTORAT JENDERAL MIGAS SBA-5 #NA your excellent partner in oil and gas 12 9 fs_2.2 Pressure PVT & DST Overview No Test/No DST/No PVT fs_2.2 LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 13 0 fs_2.3 Pressure PVT & DST Overview SCA-1(SC-1) #DST 3 fs_2.3 7654-7664 ft MD/7584-7594 ft TVDSS 475 BOPD, GOR 5762.1 SCF/STB Fluid Type : Volatile Oil PVT DATA AVAILABLE SCA-1(SC-1) #DST 3A Retest 7600-7664 ft MD / 7530-7594 TVDSS 648 BOPD, GOR 11353.4 SCF/STB Fluid Type : Volatile Oil SCA-1(SC-1) #DST 3A SCA-2(SC-2) #DST 3A 7600-7664 ft MD / 7530-7594 ft TVDSS 7600-7664 ft MD / 7517.54-7793.14 ft TVDSS 510.749 BOPD, GOR 13629 SCF/STB Fluid Type : Volatile Oil 834 BOPD, GOR 11199 SCF/STB Fluid Type : Condensate SBA-1(SB-1) #DST 2A 7724-7744 ft MD/7654-7674 ft TVDSS 1648 BOPD, GOR 2402.3 SCF/STB Fluid Type : Volatile Oil SBA-1(SB-1) #DST 2B 7724-7765 ft MD//7654-7695 TVDSS SBA-5 DST #NA 2189 BOPD, GOR 1050.7 SCF/STB Fluid Type : Black Oil PVT DATA AVAILABLE 8095-8150 ft MD/7859.38-7912.25 ft TVDSS LEMIGAS | DIREKTORAT JENDERAL MIGAS 1624 BOPD, GOR 1734.6 SCF/STB Fluid Type : Black Oil your excellent partner in oil and gas 13 1 SB 1.2_BSAT Pressure PVT & DST Overview SB 1.2_BSAT SC-3(SCA-3) #DST 4 7654-7664 ft MD/8061.37-8074 ft TVDSS 475 BOPD, GOR 5762.1 SCF/STB Fluid Type : Wet Gas LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 13 2 Fs_2.4 Pressure PVT & DST Overview Fs_2.4 No Test/No DST/No PVT LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 13 3 PVT & DST Overview mfs_3 Mfs_3 Pressure SCA-5(SC-6) #DST 4 Choke 5/8” 10036-10064 ft MD/7957.93-7976.26 ft TVDSS 256 BOPD, GOR 14449.8 SCF/STB Fluid Type : Condensate PVT DATA AVAILABLE SCA-5(SC-6) #DST 4 Choke 1” 10036-10064 ft MD/7957.93-7976.26 ft TVDSS 1264 BOPD, GOR 13907 SCF/STB Fluid Type : Condensate PVT DATA AVAILABLE SCA-5(SC-6) #DST 4 Choke ½” 10036-10064 ft MD 527 BOPD, GOR 15757.1 SCF/STB Fluid Type : Wet Gas PVT DATA AVAILABLE LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 13 4 fs 3.1 Pressure PVT & DST Overview fs_3.1 SCA-1(SC-1) #DST 2 SCA-2(SC-2) #DST 2 7846-7876; 7880-7884 ft MD/ 7776-7806; 7810-7814 ft TVDSS 8215-8290; 8308-8318 ft MD/ 7721.15-7793.14; 7810,44-7820.06 Fluid Type : No Fluid Fluid Type : Water SBA-1(SBA-1) #DST 1 7933-7950 ft MD/ 7863-7880 ft TVDSS 527 BOPD, GOR 24024.8 SCF/STB Fluid Type : Wet Gas LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 13 5 fs 3.2 Pressure PVT & DST Overview fs_3.2 SCA-3(SC-3) #DST 3 10382-10392 ft MD 8255.88-8263.68 ft TVDSS Fluid Type : N2 Lifting LEMIGAS | DIREKTORAT JENDERAL MIGAS SCA-6(SC-5) #DST 3 10192-10201; 10232-10247 ft MD 325 BOPD, GOR 969.2 SCF/STB Fluid Type : N2 Lifting your excellent partner in oil and gas 13 6 PVT & DST Overview SB-2_BSAT Pressure SB-2_BSAT SC-4 #DST 2B 8362-8376 ft MD / 8284-8298 ft TVDSS 325 BOPD, GOR 969.2 SCF/STB Fluid Type : Black Oil SC-4) #DST 2 8362-8376 ft MD / 8284-8298 ft TVDSS 345 BOPD, GOR 1171 SCF/STB Fluid Type : Black Oil LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 13 7 Fs_3.4 Pressure PVT & DST Overview fs_3.4 SCA-3(SC-3) #DST 1 (3/8”) 10634-10740 ft MD 8450.24-8529.66 ft TVDSS Note : Gun Not Fired SCA-1(SC-1) #DST 1 8110-8132 ft MD 8040-8062 ft TVDSS 662 BOPD, GOR 645 SCF/STB Fluid Type : Black Oil PVT DATA AVAILABLE SC-4 #DST 2A 8450-8456 ft MD / 8450-8372 ft TVDSS 11 BOPD fluid Type : Black Oil LEMIGAS | DIREKTORAT JENDERAL MIGAS SCA-1(SC-1) #DST 1 (PERF) 8139-8156 ft MD 8069-8086 ft TVDSS Note : Gun not fired SCA-2(SC-2) #DST 1 8566-8578 ft MD 8059.40-88071.02 ft TVDSS 971 BOPD, GOR 1625.1 SCF/STB Fluid Type : Black Oil SCA-3(SC-3) #DST 1A (1/2”) 10634-10740 ft MD 8450.24-8529 ft TVDSS 660 BOPD, GOR 9939.4 SCF/STB Fluid Type : Condensate SCA-3(SC-3) #DST 2 10634-10740 ft MD 8410.68-7820.06 ft TVDSS 1090 BOPD, GOR 4789 SCF/STB Fluid Type : Condensate SCA-5(SC-6) #DST 2 10356-10378 ft MD 8171.27-8186.63 ft TVDSS Note : #NA your excellent partner in oil and gas 13 8 PVT & DST Overview fs_3.4 SBA-4(SB-2) #DST 1 9838-9868 ft MD / 8622.61-8651.09 ft TVDSS Fluid Type : No fluid LEMIGAS | DIREKTORAT JENDERAL MIGAS SBA-5(SC-5) #DST N/A 8438-8456 ft MD / 8189.11-8206.41 ft TVDSS Fluid Type : No fluid your excellent partner in oil and gas 13 9 PVT & DST Overview Fs_3.5 Pressure fs_3.5 SC-4 #DST 1 8562-8574 ft MD/8484-8496 ft TVDSS 98.5 BOPD, GOR 281.2 SCF/STB Fluid Type : Black Oil LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 14 0 PVT & DST Overview Mfs_4 Mfs_4 Pressure SCA-5(SC-6) #DST 1 Choke 1” 10828-10858 ft MD/8531.09-8555.74 ft TVDSS 391 BOPD, GOR 14449.8 SCF/STB Fluid Type : Wet Gas PVT DATA AVAILABLE SCA-5(SC-6) #DST 1 Choke 3/4” 10828-10858 ft MD/8531.09-8555.74 ft TVDSS 444 BOPD, GOR 20495.5 SCF/STB Fluid Type : Wet Gas PVT DATA AVAILABLE SCA-5(SC-6) #DST 1 Choke ½” 10828-10858 ft MD/8531.09-8555.74 ft TVDSS 522 BOPD, GOR 22222.2 SCF/STB Fluid Type : Wet Gas PVT DATA AVAILABLE LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 14 1 NEXT TARGET 1. Prelimenary Production Splitting after the marker fix 2. ’ Permeability for validation LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas 14 2 Terima Kasih www.lemigas.esdm.go.id LEMIGAS | DIREKTORAT JENDERAL MIGAS your excellent partner in oil and gas
0
You can add this document to your study collection(s)
Sign in Available only to authorized usersYou can add this document to your saved list
Sign in Available only to authorized users(For complaints, use another form )