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34-059-24234

Well Details

Well ID: 34-059-24234
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Country: United States
State: Ohio
County: Guernsey
Municipality: Oxford Township
Operator Name: ASCENT RESOURCES UTICA LLC
Well Pad ID: US-OH-000490
Farm/Lease Name: ATMOS W OXF GR
License Status: Producing
License Date: 2013-01-07
Spud Date: 2013-01-28
Spud Drilling Contractor: H&P DRILLING
Final Drill Date: 2013-04-29
Well Total Depth: 13704.00 ft
Configuration: Horizontal
Latitude: 40.050000
Longitude: -81.260000

For data sources see[1]

Well History

Well Status Well Status Date Comment
APP 2012-09-11 Proposed Formations:POINT PLEASANT, Issued Date:9/11/2012, Expired Date:9/11/2014 12:00:00 PM, Drilling unit acres:151.742, Proposed Well Type:OG, Proposed Well Class:EDPW
APP 2013-01-07 Proposed Formations:POINT PLEASANT, Issued Date:1/7/2013, Expired Date:1/7/2015 12:00:00 PM, Drilling unit acres:151.742, Proposed Well Type:OG, Proposed Well Class:EDPW
Reached Total Depth 2013-04-29
Correction to Well 2013-06-28 CORRECTION TO TARGET INFORMATION (FOOTAGE & X,Y COORDINATES) FROM AS DRILLED SURVEY PLAT. UNIT SIZE CHANGED TO 149.915 ACRES.
Completion Report Received 2014-05-08
Construction Permit Expires 2015-01-07
Change of Owner 2018-10-15 Operator changed from 8870, HESS OHIO DEVELOPMENTS LLC to 9520, ASCENT RESOURCES UTICA LLC
Record Last Modified 2018-10-25
Correction to Well 2018-10-26 CHANGE TO WELL NAME AND NUMBER. PREVIOUS--CNXGUE 10N7W #2H-8.

For data sources see[2]

Fracking Activities

Fracking Jobs

Job Number Job Start Date Job End Date True Vertical Depth (ft) Total Water Volume (gal) Total Non-Water Volume (gal)
1 09/24/2013 09/28/2013 7999 5,786,260.0 0

Fluid Composition Data

Job Number Trade Name Supplier Purpose Ingredient Name CAS Number Additive Percentage by Mass Job Percentage by Mass Mass Used (lb)
1 Sand, White, 100 mesh Baker Hughes Proppant Crystalline Silica (Quartz) 14808-60-7 100 2.36788 1,350,630.0
Scaletrol 720 Baker Hughes Scale Inhibitor Ethylene Glycol 107-21-1 30 0.0070449 4018.4
Calcium Chloride 10043-52-4 5 0.0011742 669.734
BF-9L, 300 gal tote Baker Hughes Buffer Potassium Carbonate 584-08-7 60 0.0001289 73.5394
Potassium Hydroxide 1310-58-3 30 0.00006450 36.7697
Sand, White, 30/50 Baker Hughes Proppant Crystalline Silica (Quartz) 14808-60-7 100 11.6633 6,652,700.0
HCl, 10.1 - 15% Baker Hughes Acidizing Water 7732-18-5 85 0.446597 254737
Hydrochloric Acid 7647-01-0 15 0.0788113 44953.6
MaxPerm-20A, 265 gallon tote Baker Hughes Friction Reducer Petroleum Distillates 64742-47-8 30 0.0841468 47997
Sodium Chloride 7647-14-5 3 0.0084147 4799.7
Oxyalkylated Alcohol Trade Secret 5 0.0140245 7999.49
Polyacrylate Trade Secret 60 0.168294 95993.9
Other Chemicals Water 7732-18-5 0 0.144664 82515.7
Copolymer Trade Secret 0 0.0004953 282.502
Formaldehyde 50-00-0 0 0.00002220 12.6875
Modified Thiorea Polymer 68527-49-1 0 0.0001557 88.8125
Polysorbate 9005-65-6 0 0.0084147 4799.7
Potassium Chloride 7447-40-7 0 0.00001170 6.6973
Sodium Chloride 7647-14-5 0 0.00000700 4.0184
2-butoxy-1-propanol 15821-83-7 0 0.00000300 1.7322
Oleate Ester 1338-43-8 0 0.0084147 4799.7
Hydrochloric Acid 7647-01-0 0 0.00002220 12.6875
Polyacrylate Trade Secret 0 0.0046966 2678.93
GBW-5 Baker Hughes Breaker Ammonium persulphate 7727-54-0 100 0.0026245 1497
GasFlo G, 330 gal tote Baker Hughes Surfactant Methanol 67-56-1 30 0.0003725 212.454
Oxyalkylated Amine Trade Secret 3 0.00003720 21.2454
Oxyalkylated Alkylphenol (1) Trade Secret 10 0.0001242 70.818
Polyoxyalkylene Trade Secret 10 0.0001242 70.818
Oxyalkylated Alkylphenol (2) Trade Secret 10 0.0001242 70.818
Water Operator Carrier Water 7732-18-5 100 84.581 48,244,600.0
HCl, 15.1 - 20% Baker Hughes Acidizing Hydrochloric Acid 7647-01-0 20 0.0067795 3866.98
Water 7732-18-5 80 0.0271179 15467.9
GW-3LDF Baker Hughes Gelling Agent 1-butoxy-2-propanol 5131-66-8 5 0.0001518 86.6085
Petroleum Distillates 64742-47-8 30 0.000911 519.651
Guar Gum 9000-30-0 60 0.0018221 1039.3
Paraffinic Petroleum Distillate 64742-55-8 30 0.000911 519.651
Isotridecanol, ethoxylated 9043-30-5 5 0.0001518 86.6085
Crystalline Silica: Quartz 14808-60-7 5 0.0001518 86.6085
HCl, 5.1 - 7.5% Baker Hughes Acidizing Hydrochloric Acid 7647-01-0 7.5 0.0270755 15443.8
Water 7732-18-5 92.5 0.333931 190473
CI-14 Baker Hughes Corrosion Inhibitor Propargyl Alcohol 107-19-7 5 0.0001112 63.4375
Methanol 67-56-1 100 0.0022243 1268.75
Fatty Acids Trade Secret 10 0.0002224 126.875
Polyoxyalkylenes Trade Secret 30 0.0006673 380.625
Olefin Trade Secret 5 0.0001112 63.4375
XLW-32, 260 gal tote Baker Hughes Crosslinker Methyl Borate 121-43-7 30 0.00004770 27.18
Methanol 67-56-1 60 0.00009530 54.36
Boric Acid 10043-35-3 30 0.00004770 27.18
NE-900, tote Baker Hughes Non-emulsifier Nonyl phenyl polyethylene glycol ether 9016-45-9 10 0.0001238 70.6254
Methanol 67-56-1 30 0.0003715 211.876
Ferrotrol 300L Baker Hughes Iron Control Citric Acid 77-92-9 60 0.0057915 3303.47

For data sources see[3]

Stimulations Data

Stimulation Date Chemical Agent Chemical Agent Concentration (%) Fracking Fluid Volume Mass of Proppant Used (lb) Fracking Company Comments
2013-09-24 H2O 8 9000 Bbl 483020 BAKER-HUGHES STAGE 5

36 STAGES

2013-09-27 H2O 8 7366 Bbl 484020 BAKER-HUGHES STAGE 16

36 STAGES

2013-09-25 H2O 8 7432 Bbl 468666 BAKER-HUGHES STAGE 3

36 STAGES

2013-09-25 H2O 8 7485 Bbl 477960 BAKER-HUGHES STAGE 8

36 STAGES

2013-09-26 H2O 8 7450 Bbl 475230 BAKER-HUGHES STAGE 9

36 STAGES

2013-09-27 H2O 8 7541 Bbl 478260 BAKER-HUGHES STAGE 15

36 STAGES

2013-09-26 H2O 8 7843 Bbl 479300 BAKER-HUGHES STAGE 10

36 STAGES

2013-09-24 H2O 8 6445 Bbl 250280 BAKER-HUGHES STAGE 1

36 STAGES

2013-09-28 H2O 8 7381 Bbl 466860 BAKER-HUGHES STAGE 17

36 STAGES

2013-09-27 H2O 8 7747 Bbl 400990 BAKER-HUGHES STAGE 13

36 STAGES

2013-09-26 H2O 8 7455 Bbl 472320 BAKER-HUGHES STAGE 12

36 STAGES

2013-09-24 H2O 8 4628 Bbl 9314 BAKER-HUGHES STAGE 2

36 STAGES

2013-09-25 H2O 8 7776 Bbl 514990 BAKER-HUGHES STAGE 6

36 STAGES

2013-09-26 H2O 8 7450 Bbl 494220 BAKER-HUGHES STAGE 11

36 STAGES

2013-09-27 H2O 8 7327 Bbl 476780 BAKER-HUGHES STAGE 14

36 STAGES

8 0 0
2013-09-28 H2O 8 7921 Bbl 487780 BAKER-HUGHES STAGE 19

36 STAGES

2013-09-25 H2O 8 7751 Bbl 492420 BAKER-HUGHES STAGE 4

36 STAGES

H2O 8 7631 Bbl 507480 BAKER-HUGHES STAGE 7

36 STAGES

2013-09-28 H2O 8 8339 Bbl 491460 BAKER-HUGHES STAGE 18

36 STAGES

For data sources see[4]

Production Data

Period Operator Name Gas Quantity (mcf) Oil Quantity (bbl) Production Days
2013 HESS OHIO DEVELOPMENTS LLC 0 1839 30
2014 HESS OHIO DEVELOPMENTS LLC 286382 26991 237
2015 HESS OHIO DEVELOPMENTS LLC 338762 15824 342
2016 HESS OHIO DEVELOPMENTS LLC 173742 5245 326
2017 HESS OHIO DEVELOPMENTS LLC 147158 5336 351
2018 ASCENT RESOURCES UTICA LLC 124834 3726 333
2019 ASCENT RESOURCES UTICA LLC 23760 1067 89

For data sources see[5] [6]

Waste Data

Period Operator Name Waste Type Quantity (bbl) Production Days
2013 HESS OHIO DEVELOPMENTS LLC Brine 1758 30
2014 HESS OHIO DEVELOPMENTS LLC Brine 7053 237
2015 HESS OHIO DEVELOPMENTS LLC Brine 6972 342
2016 HESS OHIO DEVELOPMENTS LLC Brine 2809 326
2017 HESS OHIO DEVELOPMENTS LLC Brine 3422 351
2018 ASCENT RESOURCES UTICA LLC Brine 2101 333
2019 ASCENT RESOURCES UTICA LLC Brine 402 89

For data sources see[7] [8]

Inspection Data

Inspections Performed

Inspection ID Inspection Date Inspection Type Inspection Result Inspection Comments
-1590930038 2016-10-13 0:00 PW No Violations 0.50
-1662868601 2018-4-25 0:00: PW No Violations 0.50
-1961397855 2017-7-5 0:00:0 PW No Violations 0.50
-804792893 2020-6-17 0:00: PW No Violations 1.00
0279939349 2016-06-08 Production Wells No Violations On the day of my inspection I witnessed the production equipment included a line heater, a bulk separator, a flash gas compressor, a fuel gas skid, a vapor recovery system, 3-400bbl condensate tanks and a 400bbl produced water tank within containment and a flare stack. The well was equipped with Crown wellheads and a combination of Neeco and Cameron valves making up the production tree. Gauges present read 1250psi on the casing and 430psi on the tubing. Identification was present and current production records.
0957820017 2015-12-10 Production Wells No Violations On the day of my inspection I witnessed the production equipment included a line heater, a bulk separator, a flash gas compressor, a fuel gas skid, a vapor recovery system, 3-400bbl condensate tanks and a 400bbl produced water tank within containment and a flare stack. The well was equipped with Crown wellheads and a combination of Neeco and Cameron valves making up the production tree. Gauges present read 1600psi on the casing with proper identification and current production records.
1539279745 2019-03-05 Production Wells No Violations The purpose of my inspection was a status check. During my inspection the well was equipped with a plunger lift system with production valves in the open position. Annular pressure monitoring was present with gauges reading 0 pounds per square inch on the 13.375-inch surface casing and 0 pounds per square inch on the 9.625-inch diameter intermediate casing. The production equipment consisted of four horizontal indirect line heaters, four horizontal separators, one gas compression skid, four 400-barrel tanks, and a flare stack. Identification was present and production records were current.
1590930038 2016-10-13 Production Wells No Violations On the day of my inspection I witnessed the production equipment included a line heater and a bulk separator. Also present a flash gas compressor, a fuel gas skid, a vapor recovery system, 3-400 barrel condensate tanks and a 400 barrel produced water tank within containment and a flare stack and shared with the 4H-8, 3H-8 and 1H-8. The well was equipped with a plunger lift system with the valves in the closed position. Gauges present read 1200 pounds per square inch on the casing and 1150 pounds per square inch on the tubing with annular pressure monitoring in place. Identification was present and current production records.
1662868601 2018-04-25 Production Wells No Violations The purpose of my inspection was a status check. During my inspection the well was equipped with a plunger lift system with production valves in the open position. Annular pressure monitoring was present. The production equipment consisted of four 400 barrel tanks, four line heaters, and four horizontal separators. A gas compression skid, horizontal vent scrubber, and a flare stack to capture tank vapors were located on the west side of the pad. A flame was present coming from the flare stack that was roughly 4 feet high at global positioning coordinates 40.05750 -81.26691. Identification was present and production records were current.
1819548724 2014-01-23 Preliminary Restoration No Violations Site passed preliminary restoration according to 1509.072A.
1961397855 2017-07-05 Production Wells No Violations On the day of my inspection I witnessed the production equipment included a line heater and a bulk separator. Also present a flash gas compressor, a fuel gas skid, a vapor recovery system, 4-400 barrel tanks within containment and a flare stack and shared with the 4H-8, 3H-8 and 1H-8. The well was equipped with a plunger lift system with the valves in the closed position. Gauge present read 455 pounds per square inch on the tubing with annular pressure monitoring in place. Identification was present and current production records.
279939349 2016-6-8 0:00:0 PW No Violations 0.50
957820017 2015-12-10 0:00 PW No Violations 0.50

For data sources see[9]

References