MINI FRAC & AFTER CLOSURE ANALYSIS REPORT
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1 MINI FRAC & AFTER CLOSURE ANALYSIS REPORT Company Ld. Name Field Name Formaion February 6 18, 013 DISTRIBUTION: Clien Name/Company Ld. DEFINITIVE PROJECT COORDINATOR: PREPARED BY: Definiive Opimizaion DATE: March 7, 013 Definiive Opimizaion AER/OGC Requiremens Oil/Gas Opimizaion - Technical Services 300, 80-6 TH Ave SW, Calgary, Albera TP 3E5 Tel: 1 (855) Fax: 1 (03) Websie:
2 SUMMARY OF RESULTS (MINI-FRAC) 1. Fracure closure ime ( c) was deermined o be min.. Fracure closure pressure (P c) was deermined o be 9033 psia a he oe sleeve (D daum = fkb-tvd), 10 psia a surface. 3. The insananeous shu-in pressure was deermined o be 11 psia a D daum, 6518 psia a surface, and herefore, he ne fracure pressure was calculaed o be 11 psi. Closure ime was iniially difficul o assess, however, was furher confirmed uilizing oher available echniques.. Fracure gradien was deermined o be psi/f. 5. Based on he G-funcion ime (Gc) of 106.5, he fluid efficiency for he waer injecion was deermined o be 98.%. SUMMARY OF RESULTS (AFTER-CLOSURE) 6. The derivaive plo used for afer closure flow regime idenificaion indicaes a ransiion ino a lae-ime rend of approximae -1/ slope signifying linear flow. The presence of pseudo-radial flow was no observed. 7. Alhough pseudo-radial flow was no observed, a lae-ime exrapolaion was conduced on he radial plo o obain a maximum permeabiliy and pressure esimae. In addiion, a lae-ime exrapolaion was also conduced on he linear plo o obain a minimum pressure esimae. Esimaes from he sraigh-line analyses were used as saring parameers for simulaion. The analysis was conduced using a fracure model. Since pseudo-radial flow was no observed, confidence in he resuls is low. However, he esimaed reservoir pressure from simulaion is wihin he pressure range obained. 8. The iniial reservoir pressure of 8698 psia a D daum was obained from simulaion. 9. The flow capaciy (kh) o was also obained from simulaion and was deermined o be md-f. The effecive permeabiliy o oil (k o) was herefore esimaed o be md, based on a ne pay of 15.0 fee. (P098) Definiive Opimizaion AER/OGC Requiremens Oil/Gas Opimizaion - Technical Services 300, 80-6 TH Ave SW, Calgary, Albera TP 3E5 Tel: 1 (855) Fax: 1 (03) Websie:
3 RESULTS Injecion Pressure a D daum, P inj (psia) Insananeous Shu In Pressure a Surface, ISIP (psia) Insananeous Shu In Pressure a D daum, ISIP (psia) Fracure Closure Pressure a Surface, P c (psia) Fracure Closure Pressure a D daum, P c (psia) Ne Fracure Pressure a D daum, pne (psi) Fracure Closure Time, c (min) G-Funcion Time, G c Fracure Gradien, (psi/f) Fluid Efficiency, (%) Esimaed Iniial Reservoir Pressure a D daum, P Ri (psia) Toal Fluid-Loss/Leakoff Coefficien, C (f/min 1/ )... T.e- Reservoir Fluid-Loss/Leakoff Coefficien, C (f/min 1/ )... R 1.69e- Flow Capaciy, (kh) o (md.f) Permeabiliy o Oil, k o (md) Fracure Half-Lengh, X f (f) Choked Fracure Skin, s c Skin equivalen o X f, s xf Apparen Skin, s Amospheric Pressure: psi RESERVOIR PARAMETERS Ne Pay, h (f) Effecive Horizonal Well Lengh, L e (f) Porosiy, φ (%) Gas Sauraion, S g (%) Oil Sauraion, S o (%) Waer Sauraion, S w (%) Temperaure, T R ( F) Source : Company Energy Inc. GAS PROPERTIES Gas Relaive Densiy, G (air = 1)... Gas Composiion, N (%)... Gas Composiion, CO (%)... Gas Composiion, H S (%)... Pseudo Criical Pressure, P c (psi)... Pseudo Criical Temperaure, T c (K)... N/A N/A N/A N/A N/A N/A Source : N/A OIL PROPERTIES Oil API, ( o API) Oil Densiy, (lb/f 3 ) Source : Company Energy Inc. (P098) Definiive Opimizaion AER/OGC Requiremens Oil/Gas Opimizaion - Technical Services 300, 80-6 TH Ave SW, Calgary, Albera TP 3E5 Tel: 1 (855) Fax: 1 (03) Websie:
4 WATER PROPERTIES (Treaing Fluid) Waer Specific Graviy Fluid Composiion... Fresh Waer Surface Fluid Temperaure ( F)... N/A Source : Company Energy Inc. INJECTION Final Injecion/Pump Rae (bbl/min) Final Injecion/Pump Rae (bbl/d) Waer Injecion Volume (bbl) * Pump Time (min) Source : Company Energy Inc., * Includes bbl, 9.9 ppg brine, ** Final pump ime. min. DOWNHOLE CONFIGURATION Well Type... Horizonal Oil Well License KB, (f) GL, (f) KB - GL, (f) Frac Sring Deph, (fkb-md) Frac Sring Deph, (fkb-tvd) Frac Sring O.D., (in) Frac Sring Densiy, (lb/f) Inermediae Casing Deph, (fkb-md) Inermediae Casing Deph, (fkb-tvd) Casing O.D. (in) Casing Densiy, (lb/f) Producion Casing/Liner, (fkb-md) Producion Casing/Liner, (fkb-tvd) Casing/Liner O.D. (in) Casing/Liner Densiy, (lb/f) PBTD, (fkb-md) PBTD, (fkb-tvd) Packer Deph, (fkb-md) Packer Deph, (fkb-tvd) Sage Top, (fkb-md) Sage Top, (fkb-tvd) Sage Boom, (fkb-md) Sage Boom, (fkb-tvd) D daum, (fkb-md) D daum, (fkb-tvd) Source : Company Energy Inc. (P098) Definiive Opimizaion AER/OGC Requiremens Oil/Gas Opimizaion - Technical Services 300, 80-6 TH Ave SW, Calgary, Albera TP 3E5 Tel: 1 (855) Fax: 1 (03) Websie:
5 Liquid Rae (bbl/d) 1000 Company Energy Inc. Name Field / Name Formaion February 6 18, 013 DFIT End Injecion Well Shu In For Falloff Toal Tes Measured pressures were convered from surface o fkb-tvd (Ddaum). 0 Dae 013/0/06 13:19: q w.90 h 0.1 h psi(a) bbl/d ISIP (surface) psi(a) ISIP (D) psi(a) D daum Frac grad f psi/f -000 Pressure (psi(a)) ISIP.91 h 0.00 h psi(a) End of Tes Dae 013/0/18 08:01: h 8.69 h psi(a) Analysis q waer Time (h) WellTes3 TM Ver
6 Liquid Rae (bbl/d) 1000 Company Energy Inc. 100/ W0/0 (Surfac 00-00) Name Field / Name Formaion February 6 18, 013 DFIT Measured pressures were convered from surface o fkb-tvd (Ddaum). Toal Tes (Magnified) End Injecion Well Shu In For Falloff Dae 013/0/06 13:19:3.90 h 0.1 h q w psi(a) bbl/d ISIP (surface) psi(a) ISIP (D) psi(a) D daum Frac grad f psi/f ISIP Pressure (psi(a)) End Injecion Dae 013/0/06 10:36: h 0.03 h q w psi(a) bbl/d End Injecion Dae 013/0/06 11:39:33 1. h 0.0 h q w psi(a) bbl/d.91 h 0.00 h psi(a) Analysis Began Final Injecion Dae 013/0/06 10:3: h 0.00 h q w psi(a) bbl/d End of Falloff Began Injecion Dae 013/0/06 11:38:9 q w 1. h 1.0 h psi(a) 0.00 bbl/d Dae 013/0/06 1:5:57.50 h 1.6 h q w psi(a) 0.00 bbl/d q waer Time (h) WellTes3 TM Ver
7 Firs Derivaive dp/dg (psi(a)) p (psi(a)) Company Energy Inc. Name Field / Name Formaion February 6 18, 013 DFIT 50 G-Funcion Pump Time ISIP (surface) ISIP (D) D daum Frac grad. min psi(a) psi(a) f psi/f Analysis Semilog Derivaive G dp/dg (psi(a)) Fracure Closure Dae 013/0/09 :10:37 G c c c pc (surface) p c p ne min min psi(a) psi(a) % 10.7 psi Semilog Derivaive Firs Derivaive G-funcion ime WellTes3 TM Ver
8 Firs Derivaive dp/d( 1/ ) (psi(a)/hr 1/ ) p (psi(a)) Company Energy Inc. Name Field / Name Formaion February 6 18, 013 DFIT 700 MiniFrac Sqr() Semilog Derivaive ( 1/ ) dp/d( 1/ ) (psi(a)) Pump Time ISIP (surface) ISIP (D) D daum. min psi(a) psi(a) f Frac grad psi/f Fracure Closure Dae 013/0/09 :10:37 c c pc (surface) p c p ne min min psi(a) psi(a) 10.7 psi Semilog Derivaive Firs Derivaive Analysis / (h) WellTes3 TM Ver
9 Firs Derivaive d p/d( ) (psi/hr) Company Energy Inc. Name Field / Name Formaion February 6 18, 013 DFIT 10 5 Derivaive Derivaive daa PPD daa p, Semilog Derivaive ( )d p/d( ) (psi(a)) User Defined Slope Slope -1/ Fracure Closure Dae 013/0/09 :10: (h) WellTes3 TM Ver
10 Company Energy Inc. Name Field / Name Formaion February 6 18, 013 DFIT 900 Minifrac Radial (Nole) p (psi(a)) Pseudo-radial flow was no observed. Permeabiliy is maximum esimae Analysis kh md.f h f k 0.01 md p* psi(a) 8750 Upper range esimae of reservoir pressure F R1 WellTes3 TM Ver
11 Company Energy Inc. Name Field / Name Formaion February 6 18, 013 DFIT 900 Minifrac Linear (Nole) 9100 p (psi(a)) Analysis 1 pc psi(a) C R 1.69e-0 f/min 1/ C T.e-0 f/min 1/ p* psi(a) Lower range esimae of reservoir pressure F L WellTes3 TM Ver
12 p (PPD) (psi/hr) Error (%) Pressure (psi(a)) p (psi(a)) p model Ex. p model Early Time Hisory (h) WellTes3 TM Ver C:\Users\Jean\Documens\Well Tes Analysis\PeraCa Energy Services\ Lawlar 1-15SH\XTO Energy-Lawlar 1-15SH-DFIT ( ).fk 07-Mar-13 Impulse Derivaive ( ) d p/d( ) p model Lae Time 6000 Ex. pmodel Simulaion aemps were conduced wih a primary focus on he lae-ime and early-ime daa o obain esimaes of pressure and permeabiliy. p i (syn) psi(a) p wo (syn) psi(a) Derivaive daa Derivaive model PPD daa PPD model 1 / (h -1 ) Derivaive kh md.f s' h f s Xf k md X f f s c % Error Time (h) (psi hr) p (psi(a)) p model (h)
13 Gauge 1 Casing Temperaure, F Company Energy Inc. Sar Tes Dae: 01/1/13 Final Tes Dae: 013/0/ Surface Pressure and Temperaure Plo Formaion: Well Name Name = p = /0/06 11:39:33 End Injecion = p = /0/06 13:19:3 End of Injecion Well Shu In For Falloff 300 Gauge 1 Casing Pressure, psi(a) = p = /0/06 10:36:03 End Injecion Pressure = p = /0/18 08:01: = p = /0/06 1:5:57 End of Falloff Began Final Injecion = p = /0/06 10:3:0 Began Injecion = p = /0/06 11:38:9 End of Falloff Began Injecion = p = /0/18 08:3: Temperaure :00 1:00 0:00 1:00 0:00 1:00 0:00 1:00 0:00 1:00 0:00 013// /5 /7 /8 /10 /11 /13 /1 /16 /17 /19 Gauge 1 Time
14 Company Energy Inc. Sar Tes Dae: 01/1/13 Final Tes Dae: 013/0/ Surface Pressure Plo (Magnified) Formaion: Well Name Name = p = /0/06 13:19:3 End of Injecion Well Shu In For Falloff Gauge 1 Casing Pressure, psi(a) = p = /0/06 10:36:03 End Injecion = p = /0/06 11:39:33 End Injecion = p = /0/06 11:38:9 End of Falloff Began Injecion = p = /0/06 1:5:57 End of Falloff Began Final Injecion = p = /0/06 10:3:0 Began Injecion 0 10:00 013//6 10:30 11:00 11:30 1:00 1:30 13:00 13:30 1:00 Gauge 1 Time
15 Company Ld. Well Name Name Field Name Formaion February 6 18, 013 * TERMS: The inerpreaions and conclusions presened in his repor are he opinions based on informaion from geological, engineering and oher available daa. This repor embodies he auhor s bes, sound engineering pracices and effors and he resuls are no and should no be guaraneed. The auhor does no guaranee he accuracy of geological, engineering and oher available daa and inerpreaion provided for use in his analysis. The auhor does no accep any responsibiliy and shall no be liable in negligence or oherwise, for any loss or damage resuling from he possession or use of he repor in erms of correcness or oherwise. The use and applicaion of his repor in whole or par is exclusively a he user s own risk. The release of liabiliy shall also be binding upon he clien s permied assigns, adminisraors, heirs, execuors and successors. The auhor s liabiliy o he clien shall no exceed he amoun of fees i received for performing he services under his agreemen under no circumsances. (P098)
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