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Difference between revisions of "34-059-24341"

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__TOC__
+
__TOC__
 
== Well Details ==
 
== Well Details ==
 
{| class="wikitable welldetails" width="95%"
 
{| class="wikitable welldetails" width="95%"
 
| Well ID: 34-059-24341
 
| Well ID: 34-059-24341
−
| style="height=100%; align=center" rowspan="15" | {{#display_map: 40.12758403, -81.34572085 | width=100% | height=100% }}  
+
| style="height=100%; align=center" rowspan="17" | {{#display_map: 40.127514585, -81.34588591 | width=100% | height=100% }}
 
|-
 
|-
−
| County: [[Guernsey County, Ohio|Guernsey]]
+
| Country: United States
 
|-
 
|-
−
| Municipality:  
+
| State: Ohio
 
|-
 
|-
−
| Operator Name: [[AMERICAN ENERGY UTICA LLC]]
+
| County: [[Guernsey_County,_Ohio|Guernsey]]
 
|-
 
|-
−
| Well Pad ID:  
+
| Municipality: [[Madison_Township,_Guernsey_County,_Ohio|Madison Township]]
 
|-
 
|-
−
| Farm/Lease Name:  
+
| Operator Name: [[ASCENT RESOURCES UTICA LLC]]
 
|-
 
|-
−
| First Permit Date:  
+
| Well Pad ID: [[US-OH-000908]]
 
|-
 
|-
−
| Last Permit Date:  
+
| Farm/Lease Name: RED HILL FARM MDS GR
 +
|-
 +
| License Status: Producing
 +
|-
 +
| License Date: 2014-05-07
 
|-
 
|-
 
| Spud Date: 2014-06-25
 
| Spud Date: 2014-06-25
 
|-
 
|-
−
| Unconventional: No
+
| Spud Drilling Contractor: [[NOMAC DRILLING CORP]]
−
|-
 
−
| Configuration: Vertical
 
 
|-
 
|-
−
| Well Status: Drilling
+
| Final Drill Date: 2014-11-14
 
|-
 
|-
−
| Violations: 0
+
| Well Total Depth: 15985 ft
 
|-
 
|-
−
| Latitude: 40.12758403
+
| Configuration: Horizontal
 
|-
 
|-
−
| Longitude: -81.34572085
+
| Latitude: 40.127514585
 
|-
 
|-
 +
| Longitude: -81.34588591
 
|}
 
|}
−
== Inspection Data ==
+
For data sources see<ref>{{cite web
 +
| title = Risk Based Data Management System - Well, tblLocational, tblPlugWell, tblInspection, tblCivilTownships and tblPad Tables
 +
|publisher = [[Ohio Department of Natural Resources]]
 +
| date =  2019-05-07
 +
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
 +
| accessdate = 2019-05-21 }}</ref>
 +
== Well History ==
 
{| class="wikitable sortable" width="95%"
 
{| class="wikitable sortable" width="95%"
−
!scope="col" | INSPECTION ID
+
!scope="col" style="text-align: center"| Well Status
−
!scope="col" | DATE
+
!scope="col" style="width: 15%;text-align: center"| Well Status Date
−
!scope="col" | DESCRIPTION
+
!scope="col" style="text-align: center"| Comment
−
!scope="col" | COMMENT
 
−
!scope="col" | VIOLATION ID
 
−
!scope="col" | VIOLATION CODE
 
−
!scope="col" | VIOLATION COMMENT
 
 
|-
 
|-
−
| 12335113
+
| APP
−
| 2014-11-13
+
| 2014-03-05
−
|  
+
| Proposed Formations:TRENTON, Issued Date:3/5/2014, Expired Date:3/4/2016 12:00:00 PM, Drilling unit acres:0, Proposed Well Type:ST, Proposed Well Class:STRT
−
| On the day of my inspection I found that Nomac Drilling rig 80 had reached a total depth of 15985'. They were in the process of running new 5.5 production casing. AEU reported that a spill had just occurred prior to my arrival. They estimated that 20 gallons of oil based mud had been released from a CurryVac truck. The mud was released outside of containment. No fluid made it off of the drilling pad. The spill had been cleaned up by the time I was notified. The contaminated gravel had been scraped up and sent to the landfill. I did not observe any residual contamination at the spill site.
 
−
|
 
−
|
 
−
|
 
 
|-
 
|-
 +
| APP
 +
| 2014-05-07
 +
| Proposed Formations:POINT PLEASANT, Issued Date:5/7/2014, Expired Date:5/6/2016 12:00:00 PM, Drilling unit acres:639.87, Proposed Well Type:OG, Proposed Well Class:EDPW
 
|-
 
|-
−
| 1403786729
+
| APP
−
| 2014-06-26
+
| 2014-05-13
−
|  
+
| Proposed Formations:POINT PLEASANT, Issued Date:5/13/2014, Expired Date:5/12/2016 12:00:00 PM, Drilling unit acres:639.87, Proposed Well Type:OG, Proposed Well Class:EDPW
−
| On the day of my inspection accompanied by ODNR Inspector Brandon Trigg, I witnessed Precision Rathole Inc. drilled a 36 inch diameter hole to the depth of 100 feet and ran 100 feet of 30 inch 118.65#/ft. conductor pipe. O-Tex Pumping LLC was on site and gained circulation with 5bbls of fresh water, 15bbls of gel and 5bbls of fresh water. O-Tex cemented pipe with 370 sacks of class H cement with 2%CaCl, .4% C41P and
 
−
|
 
−
|
 
−
|
 
−
|-
 
 
|-
 
|-
−
| 1414428206
+
| Reached Total Depth
−
| 2014-10-27
+
| 2014-11-14
−
|
 
−
| On the date of inspection I was informed by American Energy Utica (AEU) consultant Van Dietrich that the Nomac 80 rig had drilled a 17.5 inch diameter hole to a depth of 970 feet. Wyoming Casing Crew set 13.375 inch 54.50lbs/ft casing on bottom. O-Tex Pumping, LLC pumped 1270sk of Class H cement, 15.6ppg, 1.2 yield, 2% CaCl, 0.25lbs/sk flake, 0.4% C-41P. O-Tex released the plug and approximately 2bbl into displacement the pressure spiked to 625psi. O-Tex stopped pumping and bled off pressure but still continued to pressure up. AEU plans to drill out the plug and cement, run a Cement Bond Log to find the top of cement, and then decide how to bring cement to surface from there.
 
−
|
 
−
|
 
 
|  
 
|  
 
|-
 
|-
 +
| Correction to Well
 +
| 2015-01-09
 +
| CHANGE IN TARGET AND TAKE-POINT INFORMATION (FOOTAGES AND COORDINATES) FROM AS DRILLED SURVEY PLAT.
 
|-
 
|-
−
| 1428589695
+
| Change of Owner
−
| 2015-04-09
+
| 2015-08-19
−
|  
+
| Operator changed from 9193, AMERICAN ENERGY UTICA LLC to 9520, ASCENT RESOURCES UTICA LLC
−
| On the day of my inspection production equipment has been installed and awaiting on frac. The site passed preliminary restoration according to ORC 1509.072A.
 
−
|
 
−
|
 
−
|
 
 
|-
 
|-
−
|-
+
| Completion Report Received
−
| -1866798004
+
| 2015-09-30
−
| 2014-06-25
 
−
|
 
−
| On the day of my inspection I was on location to set conductor and I witnessed that Precision Rathole Inc. was drilling a 36 inch diameter hole at a depth of 90 feet with a planned td of 100
 
−
|
 
−
|
 
 
|  
 
|  
 
|-
 
|-
−
|-
+
| Construction Permit Expires
−
| -382273940
+
| 2016-05-06
−
| 2014-06-26
 
−
|
 
−
| On the date of inspection I accompanied ODNR Inspector Doug Bennett to witness a conductor cement string. Refer to Doug Bennett's report for further details.
 
−
|
 
−
|
 
 
|  
 
|  
 
|-
 
|-
−
|-
+
| Record Last Modified
−
| 750026647
+
| 2017-10-24
−
| 2014-07-09
 
−
|
 
−
| On the day of my inspection I witnessed Precision Rathole Inc. was on site drilling mouse holes. I met with Drilling Supervisor Garry Reynolds and verified that top of cement was tagged inside conductor at 77 feet.
 
−
|
 
−
|
 
−
|
 
−
|-
 
−
|-
 
−
| 975637734
 
−
| 2014-11-05
 
−
|  
 
−
| On the day of my inspection I found that Nomac Drilling rig 80 had new 9.625 casing ran to a depth of 6486'. The casing was equipped with a DV tool at 3516'. They were circulating when I arrived. O-Tex Pumping attempted to cement the casing to surface in one stage. Although good circulation was maintained throughout the job, no cement was circulated to surface. There were approximately 3 barrels of gel spacer circulated to surface when O-Tex reached their maximum displacement volume. Nomac 80 opened the DV tool and circulated for 12 hours. O-Tex cemented the second stage of the job. Good circulation was maintained throughout the job with approximately 80 barrels of cement returns.
 
−
|
 
−
|
 
 
|  
 
|  
 
|-
 
|-
 
|}
 
|}
 
For data sources see<ref>{{cite web
 
For data sources see<ref>{{cite web
−
  | title = Ohio Department of Natural Resources RBDMS
+
  | title = Risk Based Data Management System - Well and WellHistry Tables
−
  | publisher = [http://oilandgas.ohiodnr.gov/]
+
  |publisher = [[Ohio Department of Natural Resources]]
−
  | date = 2015-06-19
+
  | date = 2019-05-07
−
  | url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources#Inspection
+
  | url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
−
  | accessdate = 2015-06-20 }}</ref>
+
  | accessdate = 2019-05-21 }}</ref>
−
[[Category:Has Chemical Data]]
+
<!--== Perforation Treatments ==
−
==Chemical Data==
 
 
{| class="wikitable sortable" width="95%"
 
{| class="wikitable sortable" width="95%"
−
!scope="col" | HF Fluid Concentration
+
!scope="col" style="text-align: center"| Perforation Date
−
!scope="col" | Ingredient
+
!scope="col" style="text-align: center"| Interval Top (ft)
−
!scope="col" | Additive Concentration
+
!scope="col" style="text-align: center"| Interval Base (ft)
−
!scope="col" | Trade Name
+
!scope="col" style="text-align: center"| Number of Shots
−
!scope="col" | Purpose
 
−
!scope="col" | CAS number
 
−
!scope="col" | Supplier
 
 
|-
 
|-
−
| 0.0189922
+
|}-->
−
| Water
+
== Fracking Activities ==
−
| 81.0
+
==== Fracking Jobs ====
−
| CS-250 SI
+
{| class="wikitable sortable" width="95%"
−
| Scale Inhibitor
+
!scope="col" style="text-align: center"| Job Number
−
| 7732-18-5
+
!scope="col" style="text-align: center"| Job Start Date
−
| FTSI
+
!scope="col" style="text-align: center"| Job End Date
 +
!scope="col" style="text-align: center"| True Vertical Depth (ft)
 +
!scope="col" style="text-align: center"| Total Water Volume (gal)
 +
!scope="col" style="text-align: center"| Total Non-Water Volume (gal)
 
|-
 
|-
 +
| 1
 +
| 06/12/2015
 +
| 06/30/2015
 +
| style="text-align: right;" | 7310
 +
| style="text-align: right;" | 12,516,700.0
 +
| style="text-align: right;" | 0
 
|-
 
|-
−
| 0.00234471
+
|}
−
| Sodium Polyacrylate
+
==== Fluid Composition Data ====
−
| 10.0
+
{| class="wikitable sortable" style="width: 100%"
−
| CS-250 SI
+
!scope="col" style="text-align: center"| Job Number
−
| Scale Inhibitor
+
!scope="col" style="text-align: center"| Trade Name
−
| 9003-04-7
+
!scope="col" style="text-align: center"| Supplier
−
| FTSI
+
!scope="col" style="text-align: center"| Purpose
 +
!scope="col" style="text-align: center"| Ingredient Name
 +
!scope="col" style="white-space: nowrap;text-align: center"| CAS Number
 +
!scope="col" style="text-align: center"| Additive Percentage by Mass
 +
!scope="col" style="text-align: center"| Job Percentage by Mass
 +
!scope="col" style="text-align: center"| Mass Used (lb)
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="79"| 1
 +
| rowspan="1"| 100 Mesh Sand
 +
| rowspan="1"| FTSI
 +
| rowspan="1"| proppant
 +
| Silica, Quartz
 +
| 14808-60-7
 +
| style="text-align: right;" | 100
 +
| style="text-align: right;" | 1.74498
 +
| style="text-align: right;" | 2,077,330.0
 
|-
 
|-
−
| 0.00234471
+
|- valign="top"
−
| Ethylene glycol
+
| rowspan="8"| FE-200L
−
| 10.0
+
| rowspan="8"| FTSI
−
| CS-250 SI
+
| rowspan="8"| Iron Control
−
| Scale Inhibitor
+
| Water
−
| 107-21-1
+
| 7732-18-5
−
| FTSI
+
| style="text-align: right;" | 60
 +
| style="text-align: right;" | 0.00441723
 +
| style="text-align: right;" | 5258.52
 
|-
 
|-
 +
| Ethylenediaminetriaceticacid, trisodium salt
 +
| 19019-43-3
 +
| style="text-align: right;" | 0.8
 +
| style="text-align: right;" | 0.00005890
 +
| style="text-align: right;" | 70.11
 
|-
 
|-
−
| 0.00140683
+
| Trisodium Nitrilotriacetic acid
−
| Sodium chloride
+
| 5064-31-3
−
| 6.0
+
| style="text-align: right;" | 2
−
| CS-250 SI
+
| style="text-align: right;" | 0.000147241
−
| Scale Inhibitor
+
| style="text-align: right;" | 175.28
−
| 7647-14-5
 
−
| FTSI
 
 
|-
 
|-
 +
| Iminodiacetate disodium salt
 +
| 17593-73-6
 +
| style="text-align: right;" | 0.2
 +
| style="text-align: right;" | 0.00001472
 +
| style="text-align: right;" | 17.53
 
|-
 
|-
−
| 1.12965e-06
+
| Sodium glycolate
−
| Fatty Acid
+
| 2836-32-0
−
| 0.1
+
| style="text-align: right;" | 1.5
−
| CI-150
+
| style="text-align: right;" | 0.000110431
−
| Acid Corrosion Inhibitor
+
| style="text-align: right;" | 131.46
−
| Proprietary
 
−
| FTSI
 
 
|-
 
|-
 +
| Tetrasodium EDTA
 +
| 64-02-8
 +
| style="text-align: right;" | 41
 +
| style="text-align: right;" | 0.00301844
 +
| style="text-align: right;" | 3593.32
 
|-
 
|-
−
| 0.000112965
+
| Sodium Hydroxide
−
| Alkylene Oxide Block Polymer
+
| 1310-73-2
−
| 10.0
+
| style="text-align: right;" | 2
−
| CI-150
+
| style="text-align: right;" | 0.000147241
−
| Acid Corrosion Inhibitor
+
| style="text-align: right;" | 175.28
−
| Proprietary
 
−
| FTSI
 
 
|-
 
|-
 +
| Sodium formate
 +
| 141-53-7
 +
| style="text-align: right;" | 0.6
 +
| style="text-align: right;" | 0.00004417
 +
| style="text-align: right;" | 52.59
 
|-
 
|-
−
| 1.12965e-05
+
|- valign="top"
−
| Diethylene glycol
+
| rowspan="1"| 30/50 White
−
| 1.0
+
| rowspan="1"| FTSI
−
| CI-150
+
| rowspan="1"| proppant
−
| Acid Corrosion Inhibitor
+
| Silica, Quartz
−
| 111-46-6
+
| 14808-60-7
−
| FTSI
+
| style="text-align: right;" | 100
 +
| style="text-align: right;" | 9.09288
 +
| style="text-align: right;" | 10,824,700.0
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="4"| LTB-1
 +
| rowspan="4"| FTSI
 +
| rowspan="4"| Breaker
 +
| Ammonium Persulfate
 +
| 7727-54-0
 +
| style="text-align: right;" | 100
 +
| style="text-align: right;" | 0.000547689
 +
| style="text-align: right;" | 652
 
|-
 
|-
−
| 0.000338895
+
| Cured acrylic resin
−
| Ethylene Glycol
+
| Proprietary
−
| 30.0
+
| style="text-align: right;" | 100
−
| CI-150
+
| style="text-align: right;" | 0.000547689
−
| Acid Corrosion Inhibitor
+
| style="text-align: right;" | 652
−
| 107-21-1
 
−
| FTSI
 
 
|-
 
|-
 +
| Silica, Crystalline- Quartz
 +
| 14808-60-7
 +
| style="text-align: right;" | 10
 +
| style="text-align: right;" | 0.00005477
 +
| style="text-align: right;" | 65.2
 
|-
 
|-
−
| 5.64825e-05
 
−
| Water
 
−
| 5.0
 
−
| CI-150
 
−
| Acid Corrosion Inhibitor
 
−
| 7732-18-5
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 0.000112965
 
−
| Quaternary ammonium compound
 
−
| 10.0
 
−
| CI-150
 
−
| Acid Corrosion Inhibitor
 
 
| Proprietary
 
| Proprietary
−
| FTSI
+
| Proprietary
 +
| style="text-align: right;" | 0
 +
| style="text-align: right;" | 0
 +
| style="text-align: right;" | 0
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="8"| NE-100
 +
| rowspan="8"| FTSI
 +
| rowspan="8"| Non-emulsifier
 +
| Benzene, C10-16 Alkyl Derivatives
 +
| 68648-87-3
 +
| style="text-align: right;" | 0.04
 +
| style="text-align: right;" | 0.00001674
 +
| style="text-align: right;" | 19.93
 
|-
 
|-
−
| 0.000112965
+
| Sulfur Dioxide
−
| Dimethylformamide
+
| 7446-09-5
−
| 10.0
+
| style="text-align: right;" | 0
−
| CI-150
+
| style="text-align: right;" | 0.00000056
−
| Acid Corrosion Inhibitor
+
| style="text-align: right;" | 0.66
−
| 68-12-2
 
−
| FTSI
 
 
|-
 
|-
 +
| Sulfuric Acid
 +
| 7664-93-9
 +
| style="text-align: right;" | 0.01
 +
| style="text-align: right;" | 0.00000558
 +
| style="text-align: right;" | 6.64
 
|-
 
|-
−
| 0.000338895
+
| 2-Propanol
−
| Organic amine resin salt
 
−
| 30.0
 
−
| CI-150
 
−
| Acid Corrosion Inhibitor
 
−
| Proprietary
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 0.000338895
 
−
| Isopropanol
 
−
| 30.0
 
−
| CI-150
 
−
| Acid Corrosion Inhibitor
 
 
| 67-63-0
 
| 67-63-0
−
| FTSI
+
| style="text-align: right;" | 10
 +
| style="text-align: right;" | 0.00398687
 +
| style="text-align: right;" | 4746.2
 
|-
 
|-
 +
| Water
 +
| 7732-18-5
 +
| style="text-align: right;" | 90
 +
| style="text-align: right;" | 0.0358818
 +
| style="text-align: right;" | 42715.8
 
|-
 
|-
−
| 0.000112965
+
| 2-Butoxyethanol
−
| Aromatic aldehyde
+
| 111-76-2
−
| 10.0
+
| style="text-align: right;" | 10
−
| CI-150
+
| style="text-align: right;" | 0.00398687
−
| Acid Corrosion Inhibitor
+
| style="text-align: right;" | 4746.2
−
| Proprietary
 
−
| FTSI
 
 
|-
 
|-
 +
| Dodecylbenzenesulfonic acid
 +
| 27176-87-0
 +
| style="text-align: right;" | 5
 +
| style="text-align: right;" | 0.00199344
 +
| style="text-align: right;" | 2373.1
 
|-
 
|-
−
| 1.12965e-06
+
| Unsulphonated Matter
−
| Aliphatic alcohol
 
−
| 0.1
 
−
| CI-150
 
−
| Acid Corrosion Inhibitor
 
 
| Proprietary
 
| Proprietary
−
| FTSI
+
| style="text-align: right;" | 0.03
 +
| style="text-align: right;" | 0.00001116
 +
| style="text-align: right;" | 13.29
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="2"| Hydrochloric Acid (HCl)
 +
| rowspan="2"| FTSI
 +
| rowspan="2"| Acid
 +
| Water
 +
| 7732-18-5
 +
| style="text-align: right;" | 63
 +
| style="text-align: right;" | 0.828995
 +
| style="text-align: right;" | 986882
 
|-
 
|-
−
| 1.12965e-06
+
| Hydrogen Chloride
−
| Fatty Acid Salt
+
| 7647-01-0
−
| 0.1
+
| style="text-align: right;" | 37
−
| CI-150
+
| style="text-align: right;" | 0.48687
−
| Acid Corrosion Inhibitor
+
| style="text-align: right;" | 579598
−
| Proprietary
 
−
| FTSI
 
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="9"| NE-100W
 +
| rowspan="9"| FTSI
 +
| rowspan="9"| Non-emulsifier
 +
| Water
 +
| 7732-18-5
 +
| style="text-align: right;" | 80
 +
| style="text-align: right;" | 0.0005834
 +
| style="text-align: right;" | 694.51
 
|-
 
|-
−
| 0.000546009
 
−
| Ammonium Persulfate
 
−
| 100.0
 
−
| APB-1
 
−
| Gel breaker
 
−
| 7727-54-0
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 1.11632e-05
 
 
| Unsulphonated Matter
 
| Unsulphonated Matter
−
| 0.03
 
−
| NE-100
 
−
| Non-emulsifier
 
 
| Proprietary
 
| Proprietary
−
| FTSI
+
| style="text-align: right;" | 0.03
 +
| style="text-align: right;" | 0.00000020
 +
| style="text-align: right;" | 0.24
 
|-
 
|-
 +
| Methanol
 +
| 67-56-1
 +
| style="text-align: right;" | 15
 +
| style="text-align: right;" | 0.000109387
 +
| style="text-align: right;" | 130.22
 
|-
 
|-
−
| 0.00398687
 
−
| 2-Butoxyethanol
 
−
| 10.0
 
−
| NE-100
 
−
| Non-emulsifier
 
−
| 111-76-2
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 5.58162e-06
 
 
| Sulfuric Acid
 
| Sulfuric Acid
−
| 0.01
 
−
| NE-100
 
−
| Non-emulsifier
 
 
| 7664-93-9
 
| 7664-93-9
−
| FTSI
+
| style="text-align: right;" | 0.01
 +
| style="text-align: right;" | 0.00000010
 +
| style="text-align: right;" | 0.12
 
|-
 
|-
 +
| Sulfur Dioxide
 +
| 7446-09-5
 +
| style="text-align: right;" | 0
 +
| style="text-align: right;" | 0.00000001
 +
| style="text-align: right;" | 0.01
 
|-
 
|-
−
| 0.0358818
+
| Dodecylbenzenesulfonic acid
−
| Water
+
| 27176-87-0
−
| 90.0
+
| style="text-align: right;" | 5
−
| NE-100
+
| style="text-align: right;" | 0.00003646
−
| Non-emulsifier
+
| style="text-align: right;" | 43.41
−
| 7732-18-5
 
−
| FTSI
 
 
|-
 
|-
 +
| Benzene, C10-16 Alkyl Derivatives
 +
| 68648-87-3
 +
| style="text-align: right;" | 0.04
 +
| style="text-align: right;" | 0.00000031
 +
| style="text-align: right;" | 0.36
 
|-
 
|-
−
| 5.58162e-07
+
| 2-Butoxyethanol
−
| Sulfur Dioxide
+
| 111-76-2
−
| 0.0
+
| style="text-align: right;" | 10
−
| NE-100
+
| style="text-align: right;" | 0.00007292
−
| Non-emulsifier
+
| style="text-align: right;" | 86.81
−
| 7446-09-5
 
−
| FTSI
 
 
|-
 
|-
−
|-
 
−
| 0.00398687
 
 
| 2-Propanol
 
| 2-Propanol
−
| 10.0
 
−
| NE-100
 
−
| Non-emulsifier
 
 
| 67-63-0
 
| 67-63-0
−
| FTSI
+
| style="text-align: right;" | 10
 +
| style="text-align: right;" | 0.00007292
 +
| style="text-align: right;" | 86.81
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="1"| Water
 +
| rowspan="1"| Operator
 +
| rowspan="1"| Carrier
 +
| Water
 +
| 7732-18-5
 +
| style="text-align: right;" | 100
 +
| style="text-align: right;" | 87.6882
 +
| style="text-align: right;" | 104,389,000.0
 
|-
 
|-
−
| 0.00199344
+
|- valign="top"
−
| Dodecylbenzenesulfonic acid
+
| rowspan="3"| ICI-3240
−
| 5.0
+
| rowspan="3"| FTSI
−
| NE-100
+
| rowspan="3"| Biocide
−
| Non-emulsifier
+
| Sodium Hydroxide
−
| 27176-87-0
+
| 1310-73-2
−
| FTSI
+
| style="text-align: right;" | 23
 +
| style="text-align: right;" | 0.00562889
 +
| style="text-align: right;" | 6700.95
 
|-
 
|-
 +
| Dazomet (Tetrahydro-3, 5-dimethyl-2H-1, 3, 5-thiadiazine-2-thione.
 +
| 533-74-4
 +
| style="text-align: right;" | 24
 +
| style="text-align: right;" | 0.00587362
 +
| style="text-align: right;" | 6992.29
 
|-
 
|-
−
| 0.828995
 
 
| Water
 
| Water
−
| 63.0
 
−
| Hydrochloric Acid (HCl)
 
−
| Acid
 
 
| 7732-18-5
 
| 7732-18-5
−
| FTSI
+
| style="text-align: right;" | 55
 +
| style="text-align: right;" | 0.0134604
 +
| style="text-align: right;" | 16024
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="4"| CS-250 SI
 +
| rowspan="4"| FTSI
 +
| rowspan="4"| Scale Inhibitor
 +
| Sodium chloride
 +
| 7647-14-5
 +
| style="text-align: right;" | 6
 +
| style="text-align: right;" | 0.00140683
 +
| style="text-align: right;" | 1674.77
 
|-
 
|-
−
| 0.48687
+
| Water
−
| Hydrogen Chloride
+
| 7732-18-5
−
| 37.0
+
| style="text-align: right;" | 81
−
| Hydrochloric Acid (HCl)
+
| style="text-align: right;" | 0.0189922
−
| Acid
+
| style="text-align: right;" | 22609.4
−
| 7647-01-0
 
−
| FTSI
 
 
|-
 
|-
 +
| Ethylene glycol
 +
| 107-21-1
 +
| style="text-align: right;" | 10
 +
| style="text-align: right;" | 0.00234471
 +
| style="text-align: right;" | 2791.28
 
|-
 
|-
−
| 100.0
+
| Sodium Polyacrylate
−
| Silica
+
| 9003-04-7
−
| 14808.0
+
| style="text-align: right;" | 10
−
| 100 Mesh Sand
+
| style="text-align: right;" | 0.00234471
−
| proppant
+
| style="text-align: right;" | 2791.28
−
| Quartz
 
−
| FTSI
 
 
|-
 
|-
 +
|- valign="top"
 +
| rowspan="1"| APB-1
 +
| rowspan="1"| FTSI
 +
| rowspan="1"| Gel breaker
 +
| Ammonium Persulfate
 +
| 7727-54-0
 +
| style="text-align: right;" | 100
 +
| style="text-align: right;" | 0.000546009
 +
| style="text-align: right;" | 650
 
|-
 
|-
−
| 0.000874922
+
|- valign="top"
−
| Water
+
| rowspan="7"| FRW-900
−
| 40.0
+
| rowspan="7"| FTSI
−
| FRW-900
+
| rowspan="7"| Friction Reducer
−
| Friction Reducer
+
| Anionic polymer
−
| 7732-18-5
+
| 25085-02-3
−
| FTSI
+
| style="text-align: right;" | 40
 +
| style="text-align: right;" | 0.000874921
 +
| style="text-align: right;" | 1041.56
 
|-
 
|-
 +
| Sorbitan, mono-(9Z)-9-octadecenoate
 +
| 1338-43-8
 +
| style="text-align: right;" | 5
 +
| style="text-align: right;" | 0.000109365
 +
| style="text-align: right;" | 130.19
 
|-
 
|-
−
| 0.000109365
 
 
| Sodium chloride (NaCl)
 
| Sodium chloride (NaCl)
−
| 5.0
 
−
| FRW-900
 
−
| Friction Reducer
 
 
| 7647-14-5
 
| 7647-14-5
−
| FTSI
+
| style="text-align: right;" | 5
 +
| style="text-align: right;" | 0.000109365
 +
| style="text-align: right;" | 130.19
 
|-
 
|-
−
|-
 
−
| 0.000656191
 
 
| Hydrotreated Light Distillate
 
| Hydrotreated Light Distillate
−
| 30.0
 
−
| FRW-900
 
−
| Friction Reducer
 
 
| 64742-47-8
 
| 64742-47-8
−
| FTSI
+
| style="text-align: right;" | 30
 +
| style="text-align: right;" | 0.000656191
 +
| style="text-align: right;" | 781.17
 
|-
 
|-
−
|-
 
−
| 0.00021873
 
 
| Alkyl Alcohol
 
| Alkyl Alcohol
−
| 10.0
 
−
| FRW-900
 
−
| Friction Reducer
 
 
| Proprietary
 
| Proprietary
−
| FTSI
+
| style="text-align: right;" | 10
 +
| style="text-align: right;" | 0.00021873
 +
| style="text-align: right;" | 260.39
 
|-
 
|-
−
|-
 
−
| 0.000109365
 
 
| Oxyalkylated alcohol A
 
| Oxyalkylated alcohol A
−
| 5.0
 
−
| FRW-900
 
−
| Friction Reducer
 
 
| Proprietary
 
| Proprietary
−
| FTSI
+
| style="text-align: right;" | 5
 +
| style="text-align: right;" | 0.000109365
 +
| style="text-align: right;" | 130.19
 
|-
 
|-
 +
| Water
 +
| 7732-18-5
 +
| style="text-align: right;" | 40
 +
| style="text-align: right;" | 0.000874921
 +
| style="text-align: right;" | 1041.56
 
|-
 
|-
−
| 0.000874922
+
|- valign="top"
−
| Anionic polymer
+
| rowspan="18"| FRW-200
−
| 40.0
+
| rowspan="18"| FTSI
−
| FRW-900
+
| rowspan="18"| Friction reducer
−
| Friction Reducer
+
| Ammonium Chloride
−
| 25085-02-3
+
| 12125-02-9
−
| FTSI
+
| style="text-align: right;" | 12
 +
| style="text-align: right;" | 0.00692796
 +
| style="text-align: right;" | 8247.43
 
|-
 
|-
 +
| Alcohols (C10-C16), ethoxylated
 +
| 68002-97-1
 +
| style="text-align: right;" | 4
 +
| style="text-align: right;" | 0.00230932
 +
| style="text-align: right;" | 2749.14
 
|-
 
|-
−
| 5.0
+
| Surfactant
−
| Sorbitan
 
−
| 1338.0
 
−
| FRW-900
 
−
| Friction Reducer
 
−
|  mono-(9Z)-9-octadec
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 2.0419e-07
 
−
| Unsulphonated Matter
 
−
| 0.03
 
−
| NE-100W
 
−
| Non-emulsifier
 
 
| Proprietary
 
| Proprietary
−
| FTSI
+
| style="text-align: right;" | 7
 +
| style="text-align: right;" | 0.00404131
 +
| style="text-align: right;" | 4811
 
|-
 
|-
 +
| Polyethylene glycol monooleate
 +
| 9004-96-0
 +
| style="text-align: right;" | 3
 +
| style="text-align: right;" | 0.00173199
 +
| style="text-align: right;" | 2061.86
 
|-
 
|-
−
| 7.2925e-05
+
| Sorbitan Monooleate
−
| 2-Propanol
+
| 1338-43-8
−
| 10.0
+
| style="text-align: right;" | 3
−
| NE-100W
+
| style="text-align: right;" | 0.00173199
−
| Non-emulsifier
+
| style="text-align: right;" | 2061.86
−
| 67-63-0
 
−
| FTSI
 
 
|-
 
|-
 +
| Hydrotreated heavy paraffinic
 +
| 64742-54-7
 +
| style="text-align: right;" | 5
 +
| style="text-align: right;" | 0.00288665
 +
| style="text-align: right;" | 3436.43
 
|-
 
|-
−
| 7.2925e-05
+
| Sorbitol Tetraoleate
−
| 2-Butoxyethanol
+
| 61723-83-9
−
| 10.0
+
| style="text-align: right;" | 2
−
| NE-100W
+
| style="text-align: right;" | 0.00115466
−
| Non-emulsifier
+
| style="text-align: right;" | 1374.57
−
| 111-76-2
 
−
| FTSI
 
 
|-
 
|-
 +
| Ammonium Acrylate
 +
| 10604-69-0
 +
| style="text-align: right;" | 0.5
 +
| style="text-align: right;" | 0.000288665
 +
| style="text-align: right;" | 343.64
 
|-
 
|-
−
| 0.0005834
+
| Dewaxed heavy paraffinic
−
| Water
+
| 64742-65-0
−
| 80.0
+
| style="text-align: right;" | 1.5
−
| NE-100W
+
| style="text-align: right;" | 0.000865995
−
| Non-emulsifier
+
| style="text-align: right;" | 1030.93
−
| 7732-18-5
 
−
| FTSI
 
 
|-
 
|-
 +
| Petroleum distillate hydrotreated light
 +
| 64742-47-8
 +
| style="text-align: right;" | 26
 +
| style="text-align: right;" | 0.0150106
 +
| style="text-align: right;" | 17869.4
 
|-
 
|-
−
| 1.02095e-07
+
| Alkyloxypolyethyleneoxyethanol
−
| Sulfuric Acid
+
| 84133-50-6
−
| 0.01
+
| style="text-align: right;" | 1
−
| NE-100W
+
| style="text-align: right;" | 0.00057733
−
| Non-emulsifier
+
| style="text-align: right;" | 687.29
−
| 7664-93-9
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 3.64625e-05
 
−
| Dodecylbenzenesulfonic acid
 
−
| 5.0
 
−
| NE-100W
 
−
| Non-emulsifier
 
−
| 27176-87-0
 
−
| FTSI
 
 
|-
 
|-
 +
| Alcohols (C12-C16), ethoxylated
 +
| 68551-12-2
 +
| style="text-align: right;" | 4
 +
| style="text-align: right;" | 0.00230932
 +
| style="text-align: right;" | 2749.14
 
|-
 
|-
−
| 1.02095e-08
 
−
| Sulfur Dioxide
 
−
| 0.0
 
−
| NE-100W
 
−
| Non-emulsifier
 
−
| 7446-09-5
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 0.000109387
 
−
| Methanol
 
−
| 15.0
 
−
| NE-100W
 
−
| Non-emulsifier
 
−
| 67-56-1
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 87.6882
 
 
| Water
 
| Water
−
| 100.0
 
−
| Water
 
−
| Carrier
 
 
| 7732-18-5
 
| 7732-18-5
−
| Operator
+
| style="text-align: right;" | 48
 +
| style="text-align: right;" | 0.0277118
 +
| style="text-align: right;" | 32989.7
 
|-
 
|-
 +
| Acrylamide
 +
| 79-06-1
 +
| style="text-align: right;" | 0.1
 +
| style="text-align: right;" | 0.00005773
 +
| style="text-align: right;" | 68.73
 
|-
 
|-
−
| 0.8
+
| Acrylamide P/W acrylic acid, ammonium salt
−
| Ethylenediaminetriaceticacid
+
| 26100-47-0
−
| 19019.0
+
| style="text-align: right;" | 25
−
| FE-200L
+
| style="text-align: right;" | 0.0144332
−
| Iron Control
+
| style="text-align: right;" | 17182.2
−
| trisodium salt
 
−
| FTSI
 
 
|-
 
|-
 +
| Copolymer of acrylamide and sodium acrylate
 +
| 25987-30-8
 +
| style="text-align: right;" | 33
 +
| style="text-align: right;" | 0.0190519
 +
| style="text-align: right;" | 22680.4
 
|-
 
|-
−
| 0.000147241
+
| Alcohols (C12-C14), ethoxylated
−
| Trisodium Nitrilotriacetic acid
+
| 68439-50-9
−
| 2.0
+
| style="text-align: right;" | 4
−
| FE-200L
+
| style="text-align: right;" | 0.00230932
−
| Iron Control
+
| style="text-align: right;" | 2749.14
−
| 5064-31-3
 
−
| FTSI
 
 
|-
 
|-
 +
| Isopropanol
 +
| 67-63-0
 +
| style="text-align: right;" | 0.3
 +
| style="text-align: right;" | 0.000173199
 +
| style="text-align: right;" | 206.19
 
|-
 
|-
−
| 0.00301844
+
|- valign="top"
−
| Tetrasodium EDTA
+
| rowspan="12"| CI-150
−
| 41.0
+
| rowspan="12"| FTSI
−
| FE-200L
+
| rowspan="12"| Acid Corrosion Inhibitor
−
| Iron Control
+
| Quaternary ammonium compound
−
| 64-02-8
+
| Proprietary
−
| FTSI
+
| style="text-align: right;" | 10
−
|-
+
| style="text-align: right;" | 0.000112965
−
|-
+
| style="text-align: right;" | 134.48
−
| 0.000147241
 
−
| Sodium Hydroxide
 
−
| 2.0
 
−
| FE-200L
 
−
| Iron Control
 
−
| 1310-73-2
 
−
| FTSI
 
−
|-
 
−
|-
 
−
| 0.000110431
 
−
| Sodium glycolate
 
−
| 1.5
 
−
| FE-200L
 
−
| Iron Control
 
−
| 2836-32-0
 
−
| FTSI
 
−
|-
 
 
|-
 
|-
−
| 0.00441723
 
 
| Water
 
| Water
−
| 60.0
 
−
| FE-200L
 
−
| Iron Control
 
 
| 7732-18-5
 
| 7732-18-5
−
| FTSI
+
| style="text-align: right;" | 5
 +
| style="text-align: right;" | 0.00005648
 +
| style="text-align: right;" | 67.24
 
|-
 
|-
 +
| Fatty Acid Salt
 +
| Proprietary
 +
| style="text-align: right;" | 0.1
 +
| style="text-align: right;" | 0.00000113
 +
| style="text-align: right;" | 1.34
 
|-
 
|-
−
| 1.47241e-05
+
| Organic amine resin salt
−
| Iminodiacetate disodium salt
+
| Proprietary
−
| 0.2
+
| style="text-align: right;" | 30
−
| FE-200L
+
| style="text-align: right;" | 0.000338895
−
| Iron Control
+
| style="text-align: right;" | 403.44
−
| 17593-73-6
 
−
| FTSI
 
 
|-
 
|-
 +
| Diethylene glycol
 +
| 111-46-6
 +
| style="text-align: right;" | 1
 +
| style="text-align: right;" | 0.00001130
 +
| style="text-align: right;" | 13.45
 
|-
 
|-
−
| 4.41723e-05
+
| Isopropanol
−
| Sodium formate
+
| 67-63-0
−
| 0.6
+
| style="text-align: right;" | 30
−
| FE-200L
+
| style="text-align: right;" | 0.000338895
−
| Iron Control
+
| style="text-align: right;" | 403.44
−
| 141-53-7
 
−
| FTSI
 
 
|-
 
|-
 +
| Aliphatic alcohol
 +
| Proprietary
 +
| style="text-align: right;" | 0.1
 +
| style="text-align: right;" | 0.00000113
 +
| style="text-align: right;" | 1.34
 
|-
 
|-
−
| 0.000547689
+
| Aromatic aldehyde
−
| Ammonium Persulfate
+
| Proprietary
−
| 100.0
+
| style="text-align: right;" | 10
−
| LTB-1
+
| style="text-align: right;" | 0.000112965
−
| Breaker
+
| style="text-align: right;" | 134.48
−
| 7727-54-0
 
−
| FTSI
 
 
|-
 
|-
−
|-
+
| Fatty Acid
−
| 0.0
 
 
| Proprietary
 
| Proprietary
−
| 0.0
+
| style="text-align: right;" | 0.1
−
| LTB-1
+
| style="text-align: right;" | 0.00000113
−
| Breaker
+
| style="text-align: right;" | 1.34
−
| Proprietary
 
−
| FTSI
 
 
|-
 
|-
−
|-
+
| Alkylene Oxide Block Polymer
−
| 0.000547689
 
−
| Cured acrylic resin
 
−
| 100.0
 
−
| LTB-1
 
−
| Breaker
 
 
| Proprietary
 
| Proprietary
−
| FTSI
+
| style="text-align: right;" | 10
 +
| style="text-align: right;" | 0.000112965
 +
| style="text-align: right;" | 134.48
 
|-
 
|-
 +
| Dimethylformamide
 +
| 68-12-2
 +
| style="text-align: right;" | 10
 +
| style="text-align: right;" | 0.000112965
 +
| style="text-align: right;" | 134.48
 
|-
 
|-
−
| 10.0
+
| Ethylene Glycol
−
| Silica
+
| 107-21-1
−
| 14808.0
+
| style="text-align: right;" | 30
−
| LTB-1
+
| style="text-align: right;" | 0.000338895
−
| Breaker
+
| style="text-align: right;" | 403.44
−
| Crystalline- Quartz
 
−
| FTSI
 
 
|-
 
|-
 +
|}
 +
For data sources see<ref>{{cite web
 +
| title = FracFocus Fracking Chemicals Database
 +
| date = 2019-04-02
 +
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
 +
| accessdate = 2019-06-19 }}</ref>
 +
== Stimulations Data ==
 +
{| class="wikitable sortable" width="95%"
 +
!scope="col" style="text-align: center"| Stimulation Date
 +
!scope="col" style="text-align: center"| Chemical Agent
 +
!scope="col" style="text-align: center"| Chemical Agent Concentration (%)
 +
!scope="col" style="text-align: center"| Fracking Fluid Volume
 +
!scope="col" style="text-align: center"| Mass of Proppant Used (lb)
 +
!scope="col" style="text-align: center"| Fracking Company
 +
!scope="col" style="text-align: center"| Comments
 
|-
 
|-
−
| 0.00562889
+
| 2015-06-30
−
| Sodium Hydroxide
+
| H2O
−
| 23.0
+
| style="text-align: right;" | 8
−
| ICI-3240
+
| style="text-align: right;" | 5418 Bbl
−
| Biocide
+
| style="text-align: right;" | 249071
−
| 1310-73-2
+
| [[Frac Tech Services]]
−
| FTSI
+
| STAGE 54/54
 +
30 SHOTS
 
|-
 
|-
 +
| 2015-06-21
 +
| H2O
 +
| style="text-align: right;" | 8
 +
| style="text-align: right;" | 5495 Bbl
 +
| style="text-align: right;" | 228463
 +
| [[Frac Tech Services]]
 +
| STAGE 1/54
 +
30 SHOTS
 +
STAGES 2-53 SEE IMAGES
 
|-
 
|-
−
| 5.0
+
|}
−
| Dazomet (Tetrahydro-3
+
For data sources see<ref>{{cite web
−
| 3.0
+
| title = Risk Based Data Management System - tblStimulation Table
−
| ICI-3240
+
|publisher = [[Ohio Department of Natural Resources]]
−
| Biocide
+
| date =  2019-05-07
−
| 5-dimethyl-2H-1
+
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
−
| FTSI
+
| accessdate = 2019-05-21 }}</ref>
 +
== Production Data ==
 +
{| class="wikitable sortable" width="95%"
 +
!scope="col" style="text-align: center"| Period
 +
!scope="col" style="text-align: center"| Operator Name
 +
!scope="col" style="text-align: center"| Gas Quantity (mcf)
 +
!scope="col" style="text-align: center"| Oil Quantity (bbl)
 +
!scope="col" style="text-align: center"| Production Days
 
|-
 
|-
 +
| 2015
 +
| [[ASCENT RESOURCES UTICA LLC]]
 +
| style="text-align: right;" | 233763
 +
| style="text-align: right;" | 97305
 +
| style="text-align: right;" | 155
 
|-
 
|-
−
| 0.0134604
+
| 2016
−
| Water
+
| [[ASCENT RESOURCES UTICA LLC]]
−
| 55.0
+
| style="text-align: right;" | 418658
−
| ICI-3240
+
| style="text-align: right;" | 92745
−
| Biocide
+
| style="text-align: right;" | 365
−
| 7732-18-5
 
−
| FTSI
 
 
|-
 
|-
 +
| 2017
 +
| [[ASCENT RESOURCES UTICA LLC]]
 +
| style="text-align: right;" | 240843
 +
| style="text-align: right;" | 37781
 +
| style="text-align: right;" | 365
 
|-
 
|-
−
| 100.0
+
| 2018
−
| Silica
+
| [[ASCENT RESOURCES UTICA LLC]]
−
| 14808.0
+
| style="text-align: right;" | 98482
−
| 30/50 White
+
| style="text-align: right;" | 12909
−
| proppant
+
| style="text-align: right;" | 187
−
| Quartz
 
−
| FTSI
 
 
|-
 
|-
 +
| 2019
 +
| [[ASCENT RESOURCES UTICA LLC]]
 +
| style="text-align: right;" | 18
 +
| style="text-align: right;" | 0
 +
| style="text-align: right;" | 1
 
|-
 
|-
−
| 0.00173199
+
|}
−
| Polyethylene glycol monooleate
+
For data sources see<ref>{{cite web
−
| 3.0
+
| title = Risk Based Data Management System - Production Table - Oil and Gas Data
−
| FRW-200
+
|publisher = [[Ohio Department of Natural Resources]]
−
| Friction reducer
+
| date =  2019-05-07
−
| 9004-96-0
+
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
−
| FTSI
+
| accessdate = 2019-05-21 }}</ref>
 +
<ref>{{cite web
 +
| title = Combined Production - Oil and Gas Data
 +
|publisher = [[Ohio Department of Natural Resources]]
 +
| date = 2019-05-07
 +
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
 +
| accessdate = 2019-05-21 }}</ref>
 +
== Waste Data ==
 +
{| class="wikitable sortable"
 +
!scope="col" style="text-align: center"| Period
 +
!scope="col" style="text-align: center"| Operator Name
 +
!scope="col" style="text-align: center"| Waste Type
 +
!scope="col" style="text-align: center"| Quantity (bbl)
 +
!scope="col" style="text-align: center"| Production Days
 
|-
 
|-
 +
| 2015
 +
| [[ASCENT RESOURCES UTICA LLC]]
 +
| Brine
 +
| style="text-align: right;" | 10202
 +
| style="text-align: right;" | 155
 
|-
 
|-
−
| 4.0
+
| 2016
−
| Alcohols (C12-C16)
+
| [[ASCENT RESOURCES UTICA LLC]]
−
| 68551.0
+
| Brine
−
| FRW-200
+
| style="text-align: right;" | 10081
−
| Friction reducer
+
| style="text-align: right;" | 365
−
| ethoxylated
 
−
| FTSI
 
 
|-
 
|-
 +
| 2017
 +
| [[ASCENT RESOURCES UTICA LLC]]
 +
| Brine
 +
| style="text-align: right;" | 4900
 +
| style="text-align: right;" | 365
 
|-
 
|-
−
| 0.00404131
+
| 2018
−
| Surfactant
+
| [[ASCENT RESOURCES UTICA LLC]]
−
| 7.0
+
| Brine
−
| FRW-200
+
| style="text-align: right;" | 1757
−
| Friction reducer
+
| style="text-align: right;" | 187
−
| Proprietary
 
−
| FTSI
 
 
|-
 
|-
 +
| 2019
 +
| [[ASCENT RESOURCES UTICA LLC]]
 +
| Brine
 +
| style="text-align: right;" | 3
 +
| style="text-align: right;" | 1
 
|-
 
|-
−
| 0.00173199
+
|}
−
| Sorbitan Monooleate
+
For data sources see<ref>{{cite web
−
| 3.0
+
| title = Risk Based Data Management System - Production Table - Brine Data
−
| FRW-200
+
|publisher = [[Ohio Department of Natural Resources]]
−
| Friction reducer
+
| date =  2019-05-07
−
| 1338-43-8
+
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
−
| FTSI
+
| accessdate = 2019-05-21 }}</ref>
 +
<ref>{{cite web
 +
| title = Combined Production - Brine Data
 +
|publisher = [[Ohio Department of Natural Resources]]
 +
| date = 2019-05-07
 +
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
 +
| accessdate = 2019-05-21 }}</ref>
 +
== Inspection Data ==
 +
==== Inspections Performed ====
 +
{| class="wikitable sortable" width="95%"
 +
!scope="col" style="text-align: center"| Inspection ID
 +
!scope="col" style="text-align: center"| Inspection Date
 +
!scope="col" style="text-align: center"| Inspection Type
 +
!scope="col" style="text-align: center"| Inspection Result
 +
!scope="col" style="text-align: center"| Inspection Comments
 
|-
 
|-
 +
| 0012335113
 +
| 2014-11-13
 +
| Drill / Deepen /  Reopen
 +
| No Violations
 +
| On the day of my inspection I found that Nomac Drilling rig 80 had reached a total depth of 15985. They were in the process of running new 5.5 production casing. AEU reported that a spill had just occurred prior to my arrival. They estimated that 20 gallons of oil based mud had been released from a CurryVac truck. The mud was released outside of containment. No fluid made it off of the drilling pad. The spill had been cleaned up by the time I was notified. The contaminated gravel had been scraped up and sent to the landfill. I did not observe any residual contamination at the spill site.
 
|-
 
|-
−
| 0.00288665
+
| 0382273940
−
| Hydrotreated heavy paraffinic
+
| 2014-06-26
−
| 5.0
+
| Casing String Witnessed
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| On the date of inspection I accompanied ODNR Inspector Doug Bennett to witness a conductor cement string. Refer to Doug Bennetts report for further details.
−
| 64742-54-7
 
−
| FTSI
 
 
|-
 
|-
 +
| 0447510505
 +
| 2018-09-04
 +
| Production Wells
 +
| No Violations
 +
| The purpose of my inspection was a status check. The well was not in production while Patterson 577 was on location drilling 34059245250000.I spoke with Ascent Company man and he stated that the well is checked at least one time a day.
 
|-
 
|-
−
| 0.00115466
+
| 0658550140
−
| Sorbitol Tetraoleate
+
| 2016-12-14
−
| 2.0
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| On the day of my inspection I witnessed the ground was snow covered and that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 600 pounds per square inch and the tubing was at 480 pounds per square inch with annular pressure monitoring in place.  Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400 barrel tanks all within containment and shared with the 1H and 3H.
−
| 61723-83-9
 
−
| FTSI
 
 
|-
 
|-
 +
| 0750026647
 +
| 2014-07-09
 +
| Drill / Deepen /  Reopen
 +
| No Violations
 +
| On the day of my inspection I witnessed Precision Rathole Inc. was on site drilling mouse holes. I met with Drilling Supervisor Garry Reynolds and verified that top of cement was tagged inside conductor at 77 feet.
 
|-
 
|-
−
| 0.000173199
+
| 0962833462
−
| Isopropanol
+
| 2019-02-21
−
| 0.3
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| The purpose of my inspection was a status check. During my inspection the well was equipped with a production tree style wellhead with open valves. The production equipment on location consisted on seven sand traps, seven gas production units, three horizontal heater treaters, four compressors, six 400-barrel tanks, five 500-barrel tanks, two vapor recovery towers, and one combustor. The four recently completed wells on location were flowing back. The flow back equipment on location consisted of three gas buster tanks, one frac tank, and three horizontal line heaters.
−
| 67-63-0
 
−
| FTSI
 
 
|-
 
|-
 +
| 0975637734
 +
| 2014-11-05
 +
| Casing String Witnessed
 +
| No Violations
 +
| On the day of my inspection I found that Nomac Drilling rig 80 had new 9.625 casing ran to a depth of 6486. The casing was equipped with a DV tool at 3516. They were circulating when I arrived. O-Tex Pumping attempted to cement the casing to surface in one stage. Although good circulation was maintained throughout the job, no cement was circulated to surface. There were approximately 3 barrels of gel spacer circulated to surface when O-Tex reached their maximum displacement volume. Nomac 80 opened the DV tool and circulated for 12 hours. O-Tex cemented the second stage of the job. Good circulation was maintained throughout the job with approximately 80 barrels of cement returns.
 
|-
 
|-
−
| 5.7733e-05
+
| 1094596750
−
| Acrylamide
+
| 2019-03-18
−
| 0.1
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| The purpose of my inspection was a status check. During my inspection the well was equipped with a production tree style wellhead with open valves. Gauges present read 0 pounds per square inch on the 13.375-inch diameter surface casing, 0 pounds per square inch on the 9.625-inch diameter intermediate casing, 1500 pounds per square inch on the 5.5-inch diameter production casing, 400 pounds per square inch on the production tubing. The production equipment on location consisted on seven sand traps, seven gas production units, three horizontal heater treaters, four compressors, six 400-barrel tanks, five 500-barrel tanks, two vapor recovery towers, and one combustor.
−
| 79-06-1
 
−
| FTSI
 
 
|-
 
|-
 +
| 1209332509
 +
| 2018-06-28
 +
| Production Wells
 +
| No Violations
 +
| The inspection is conducted as a simultaneous operation. The well is shut in and idle. The lubricator has been removed and there is no pressure at surface. The intermediate casing is locked out and tagged out. Cage has been placed around the well.
 
|-
 
|-
−
| 4.0
+
| 1403786729
−
| Alcohols (C12-C14)
+
| 2014-06-26
−
| 68439.0
+
| Drill / Deepen /  Reopen
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| On the day of my inspection accompanied by ODNR Inspector Brandon Trigg, I witnessed Precision Rathole Inc. drilled a 36 inch diameter hole to the depth of 100 feet and ran 100 feet of 30 inch 118.65#/ft. conductor pipe. O-Tex Pumping LLC was on site and gained circulation with 5bbls of fresh water, 15bbls of gel and 5bbls of fresh water. O--Flake. Cement returns came back early with returns of 34bbls and cement stayed surface. I Instructed AEU Drilling Superintendent to notify ODNR prior to re-spud so verification of top of cement inside conductor can be seen and if any remedial work will be necessary.
−
| ethoxylated
 
−
| FTSI
 
 
|-
 
|-
 +
| 1414428206
 +
| 2014-10-27
 +
| Casing String Witnessed
 +
| No Violations
 +
| On the date of inspection I was informed by American Energy Utica (AEU) consultant Van Dietrich that the Nomac 80 rig had drilled a 17.5 inch diameter hole to a depth of 970 feet. Wyoming Casing Crew set 13.375 inch 54.50lbs/ft casing on bottom. O-Tex Pumping, LLC pumped 1270sk of Class H cement, 15.6ppg, 1.2 yield, 2% CaCl, 0.25lbs/sk flake, 0.4% C-41P. O-Tex released the plug and approximately 2bbl into displacement the pressure spiked to 625psi. O-Tex stopped pumping and bled off pressure but still continued to pressure up. AEU plans to drill out the plug and cement, run a Cement Bond Log to find the top of cement, and then decide how to bring cement to surface from there.
 
|-
 
|-
−
| 25.0
+
| 1428589695
−
| Acrylamide P/W acrylic acid
+
| 2015-04-09
−
| 26100.0
+
| Preliminary Restoration
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| On the day of my inspection production equipment has been installed and awaiting on frac. The site passed preliminary restoration according to ORC 1509.072A.
−
| ammonium salt
 
−
| FTSI
 
 
|-
 
|-
 +
| 1473166835
 +
| 2016-09-06
 +
| Production Wells
 +
| No Violations
 +
| On the day of my inspection I witnessed that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 750 pounds per square inch and the tubing was at 420 pounds per square inch with annular pressure monitoring in place.  Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400 barrel tanks all within containment and shared with the 1H and 3H.
 
|-
 
|-
−
| 0.00057733
+
| 1500640982
−
| Alkyloxypolyethyleneoxyethanol
+
| 2018-10-11
−
| 1.0
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| During my inspection Patterson 577 was no longer on location and the well was awaiting to be put back into production after being decommissioned for drilling operations on 4 new wells on pad.
−
| 84133-50-6
 
−
| FTSI
 
 
|-
 
|-
 +
| 1506587146
 +
| 2019-01-18
 +
| Production Wells
 +
| No Violations
 +
| The well remains temporarily abandon with two cast iron bridge plugs. Ascent plans to drill out the plugs and install 2.875-inch diameter production tubing and bring the well back into production. Fortis Energy Services had a derrick service rig on location to drill out plugs.
 
|-
 
|-
−
| 0.0277118
+
| 1850834846
−
| Water
+
| 2018-09-25
−
| 48.0
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| The purpose of my inspection was a status check on drilling operations. Accompanied by ODNR Kenn Frye, during our inspection we completed a walk around with Ascent Resources Superintendent James McGee. Patterson 577 was on location in the process of drilling the 10H. This well had been decommissioned prior to rig Patterson 577 moving onto location. The well was equipped with valves on all casing strings. All valves showed 0 pounds per square inch and the a cage was placed over the well.
−
| 7732-18-5
 
−
| FTSI
 
 
|-
 
|-
 +
| 1866798004
 +
| 2014-06-25
 +
| Drill / Deepen /  Reopen
 +
| No Violations
 +
 
|-
 
|-
−
| 0.00692796
+
| 1870546719
−
| Ammonium Chloride
+
| 2015-08-10
−
| 12.0
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| On the day of my inspection I witnessed that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 2500psi and the tubing was a 2250psi. Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400bbl tanks all within containment and shared with the 1Hand 3H. The well has been online for two weeks and current production levels are 800bbls of oil, 168bbls of water and 2MMCF of gas per day.
−
| 12125-02-9
 
−
| FTSI
 
 
|-
 
|-
 +
| 1974025980
 +
| 2018-09-25
 +
| Production Wells
 +
| No Violations
 +
| The purpose of my inspection was to witness the status of temporary abandonment on well #2-4341.  Guernsey County Inspector Austin Gutridge was present during the inspection.  While on location we met with Ascent Drilling Superintendent James McGee. At the time of inspection, Patterson #577 was on location drilling on well Red Hill Farm 10H- #2-4526.  The drilling crew was making a trip to change the drilling assembly.  Well 5H was temporarily abandoned.  The production tree was removed and night cap was in place.  Annular valve had pressure gauges installed for monitoring.  Pressure transducers were installed on the night cap monitoring port to allow for constant monitoring with alarms.  A steel cage was located over the well head.  A total of three (3) wells were temporarily abandoned.  The surface production equipment had been removed.  The transfer point was isolated.  No simultaneous operations or anti-collision issues were identified during the inspection.
 
|-
 
|-
−
| 4.0
+
| 2007709957
−
| Alcohols (C10-C16)
+
| 2018-12-28
−
| 68002.0
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| During my inspection the well was temporarily abandoned and equipped with a night cap. Annular pressure monitoring was present and the well was caged. Four additional wells on pad had just finished hydraulic stimulation operations and the frac equipment was demobilizing off pad.
−
| ethoxylated
 
−
| FTSI
 
 
|-
 
|-
 +
| 2036034107
 +
| 2015-09-28
 +
| Production Wells
 +
| No Violations
 +
| On the day of my inspection I witnessed that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 2350psi and the tubing was a 1750psi. Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400bbl tanks all within containment and shared with the 1Hand 3H.
 
|-
 
|-
−
| 0.000865995
+
| 2094270362
−
| Dewaxed heavy paraffinic
+
| 2017-02-07
−
| 1.5
+
| Production Wells
−
| FRW-200
+
| No Violations
−
| Friction reducer
+
| On the day of my inspection I witnessed that the well was equipped with a plunger lift system with valves in the open position. Casing pressure was at 650 pounds per square inch and the tubing was at 500 pounds per square inch with annular pressure monitoring in place. The production equipment included 12-400 barrel tanks within containment, 2-NGL tanks, a vapor recovery tower, 2-compressor units, 2-horizontal heater treaters, 2-oil stabilizer units and a gas combustor all shared with the 1H and 3H. Also present a GP Unit and a sand trap with identification present and production records current.
−
| 64742-65-0
 
−
| FTSI
 
 
|-
 
|-
 +
|}
 +
<!--==== Violations Commited ====
 +
{| class="wikitable sortable" width="95%"
 +
!scope="col" style="text-align: center"| Inspection ID
 +
!scope="col" style="text-align: center"| Violation ID
 +
!scope="col" style="text-align: center"| Violation Date
 +
!scope="col" style="text-align: center"| Violation Code
 +
!scope="col" style="text-align: center"| Violation Comments
 
|-
 
|-
−
| 0.0150106
+
|}-->
−
| Petroleum distillate hydrotreated light
+
For data sources see<ref>{{cite web
−
| 26.0
+
| title = Risk Based Data Management System - tblInspection, tblInspFail and tblinspFlDesc Tables
−
| FRW-200
+
|publisher = [[Ohio Department of Natural Resources]]
−
| Friction reducer
+
| date = 2019-05-07
−
| 64742-47-8
+
| url = http://wellwiki.org/wiki/Ohio_Oil_and_Gas_Data_Sources
−
| FTSI
+
| accessdate = 2019-05-21 }}</ref>
−
|-
+
==References==
−
|-
+
<references/>
−
| 0.000288665
 
−
| Ammonium Acrylate
 
−
| 0.5
 
−
| FRW-200
 
−
| Friction reducer
 
−
| 10604-69-0
 
−
| FTSI
 
−
|-
 
−
|}
 
−
For data sources see<ref>{{cite web | title = FracFocus Chemical Disclosure Registry |publisher = [http://www.fracfocusdata.org/DisclosureSearch/]| date = 2015-08-10 | url = http://wellwiki.org/wiki/Well_Chemicals_Data_Sources | accessdate = 2015-08-10 }}</ref>
 
−
== References ==
 
−
{{reflist}}
 
 
__NOEDITSECTION__
 
__NOEDITSECTION__
−
[[Category:Wells]]
+
[[Category:Ohio Wells]]
 +
[[Category:FracFocus]]

Revision as of 21:23, 30 July 2019

Well Details

Well ID: 34-059-24341
Loading map...
Country: United States
State: Ohio
County: Guernsey
Municipality: Madison Township
Operator Name: ASCENT RESOURCES UTICA LLC
Well Pad ID: US-OH-000908
Farm/Lease Name: RED HILL FARM MDS GR
License Status: Producing
License Date: 2014-05-07
Spud Date: 2014-06-25
Spud Drilling Contractor: NOMAC DRILLING CORP
Final Drill Date: 2014-11-14
Well Total Depth: 15985 ft
Configuration: Horizontal
Latitude: 40.127514585
Longitude: -81.34588591

For data sources see[1]

Well History

Well Status Well Status Date Comment
APP 2014-03-05 Proposed Formations:TRENTON, Issued Date:3/5/2014, Expired Date:3/4/2016 12:00:00 PM, Drilling unit acres:0, Proposed Well Type:ST, Proposed Well Class:STRT
APP 2014-05-07 Proposed Formations:POINT PLEASANT, Issued Date:5/7/2014, Expired Date:5/6/2016 12:00:00 PM, Drilling unit acres:639.87, Proposed Well Type:OG, Proposed Well Class:EDPW
APP 2014-05-13 Proposed Formations:POINT PLEASANT, Issued Date:5/13/2014, Expired Date:5/12/2016 12:00:00 PM, Drilling unit acres:639.87, Proposed Well Type:OG, Proposed Well Class:EDPW
Reached Total Depth 2014-11-14
Correction to Well 2015-01-09 CHANGE IN TARGET AND TAKE-POINT INFORMATION (FOOTAGES AND COORDINATES) FROM AS DRILLED SURVEY PLAT.
Change of Owner 2015-08-19 Operator changed from 9193, AMERICAN ENERGY UTICA LLC to 9520, ASCENT RESOURCES UTICA LLC
Completion Report Received 2015-09-30
Construction Permit Expires 2016-05-06
Record Last Modified 2017-10-24

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 06/12/2015 06/30/2015 7310 12,516,700.0 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)
1 100 Mesh Sand FTSI proppant Silica, Quartz 14808-60-7 100 1.74498 2,077,330.0
FE-200L FTSI Iron Control Water 7732-18-5 60 0.00441723 5258.52
Ethylenediaminetriaceticacid, trisodium salt 19019-43-3 0.8 0.00005890 70.11
Trisodium Nitrilotriacetic acid 5064-31-3 2 0.000147241 175.28
Iminodiacetate disodium salt 17593-73-6 0.2 0.00001472 17.53
Sodium glycolate 2836-32-0 1.5 0.000110431 131.46
Tetrasodium EDTA 64-02-8 41 0.00301844 3593.32
Sodium Hydroxide 1310-73-2 2 0.000147241 175.28
Sodium formate 141-53-7 0.6 0.00004417 52.59
30/50 White FTSI proppant Silica, Quartz 14808-60-7 100 9.09288 10,824,700.0
LTB-1 FTSI Breaker Ammonium Persulfate 7727-54-0 100 0.000547689 652
Cured acrylic resin Proprietary 100 0.000547689 652
Silica, Crystalline- Quartz 14808-60-7 10 0.00005477 65.2
Proprietary Proprietary 0 0 0
NE-100 FTSI Non-emulsifier Benzene, C10-16 Alkyl Derivatives 68648-87-3 0.04 0.00001674 19.93
Sulfur Dioxide 7446-09-5 0 0.00000056 0.66
Sulfuric Acid 7664-93-9 0.01 0.00000558 6.64
2-Propanol 67-63-0 10 0.00398687 4746.2
Water 7732-18-5 90 0.0358818 42715.8
2-Butoxyethanol 111-76-2 10 0.00398687 4746.2
Dodecylbenzenesulfonic acid 27176-87-0 5 0.00199344 2373.1
Unsulphonated Matter Proprietary 0.03 0.00001116 13.29
Hydrochloric Acid (HCl) FTSI Acid Water 7732-18-5 63 0.828995 986882
Hydrogen Chloride 7647-01-0 37 0.48687 579598
NE-100W FTSI Non-emulsifier Water 7732-18-5 80 0.0005834 694.51
Unsulphonated Matter Proprietary 0.03 0.00000020 0.24
Methanol 67-56-1 15 0.000109387 130.22
Sulfuric Acid 7664-93-9 0.01 0.00000010 0.12
Sulfur Dioxide 7446-09-5 0 0.00000001 0.01
Dodecylbenzenesulfonic acid 27176-87-0 5 0.00003646 43.41
Benzene, C10-16 Alkyl Derivatives 68648-87-3 0.04 0.00000031 0.36
2-Butoxyethanol 111-76-2 10 0.00007292 86.81
2-Propanol 67-63-0 10 0.00007292 86.81
Water Operator Carrier Water 7732-18-5 100 87.6882 104,389,000.0
ICI-3240 FTSI Biocide Sodium Hydroxide 1310-73-2 23 0.00562889 6700.95
Dazomet (Tetrahydro-3, 5-dimethyl-2H-1, 3, 5-thiadiazine-2-thione. 533-74-4 24 0.00587362 6992.29
Water 7732-18-5 55 0.0134604 16024
CS-250 SI FTSI Scale Inhibitor Sodium chloride 7647-14-5 6 0.00140683 1674.77
Water 7732-18-5 81 0.0189922 22609.4
Ethylene glycol 107-21-1 10 0.00234471 2791.28
Sodium Polyacrylate 9003-04-7 10 0.00234471 2791.28
APB-1 FTSI Gel breaker Ammonium Persulfate 7727-54-0 100 0.000546009 650
FRW-900 FTSI Friction Reducer Anionic polymer 25085-02-3 40 0.000874921 1041.56
Sorbitan, mono-(9Z)-9-octadecenoate 1338-43-8 5 0.000109365 130.19
Sodium chloride (NaCl) 7647-14-5 5 0.000109365 130.19
Hydrotreated Light Distillate 64742-47-8 30 0.000656191 781.17
Alkyl Alcohol Proprietary 10 0.00021873 260.39
Oxyalkylated alcohol A Proprietary 5 0.000109365 130.19
Water 7732-18-5 40 0.000874921 1041.56
FRW-200 FTSI Friction reducer Ammonium Chloride 12125-02-9 12 0.00692796 8247.43
Alcohols (C10-C16), ethoxylated 68002-97-1 4 0.00230932 2749.14
Surfactant Proprietary 7 0.00404131 4811
Polyethylene glycol monooleate 9004-96-0 3 0.00173199 2061.86
Sorbitan Monooleate 1338-43-8 3 0.00173199 2061.86
Hydrotreated heavy paraffinic 64742-54-7 5 0.00288665 3436.43
Sorbitol Tetraoleate 61723-83-9 2 0.00115466 1374.57
Ammonium Acrylate 10604-69-0 0.5 0.000288665 343.64
Dewaxed heavy paraffinic 64742-65-0 1.5 0.000865995 1030.93
Petroleum distillate hydrotreated light 64742-47-8 26 0.0150106 17869.4
Alkyloxypolyethyleneoxyethanol 84133-50-6 1 0.00057733 687.29
Alcohols (C12-C16), ethoxylated 68551-12-2 4 0.00230932 2749.14
Water 7732-18-5 48 0.0277118 32989.7
Acrylamide 79-06-1 0.1 0.00005773 68.73
Acrylamide P/W acrylic acid, ammonium salt 26100-47-0 25 0.0144332 17182.2
Copolymer of acrylamide and sodium acrylate 25987-30-8 33 0.0190519 22680.4
Alcohols (C12-C14), ethoxylated 68439-50-9 4 0.00230932 2749.14
Isopropanol 67-63-0 0.3 0.000173199 206.19
CI-150 FTSI Acid Corrosion Inhibitor Quaternary ammonium compound Proprietary 10 0.000112965 134.48
Water 7732-18-5 5 0.00005648 67.24
Fatty Acid Salt Proprietary 0.1 0.00000113 1.34
Organic amine resin salt Proprietary 30 0.000338895 403.44
Diethylene glycol 111-46-6 1 0.00001130 13.45
Isopropanol 67-63-0 30 0.000338895 403.44
Aliphatic alcohol Proprietary 0.1 0.00000113 1.34
Aromatic aldehyde Proprietary 10 0.000112965 134.48
Fatty Acid Proprietary 0.1 0.00000113 1.34
Alkylene Oxide Block Polymer Proprietary 10 0.000112965 134.48
Dimethylformamide 68-12-2 10 0.000112965 134.48
Ethylene Glycol 107-21-1 30 0.000338895 403.44

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
2015-06-30 H2O 8 5418 Bbl 249071 Frac Tech Services STAGE 54/54

30 SHOTS

2015-06-21 H2O 8 5495 Bbl 228463 Frac Tech Services STAGE 1/54

30 SHOTS STAGES 2-53 SEE IMAGES

For data sources see[4]

Production Data

Period Operator Name Gas Quantity (mcf) Oil Quantity (bbl) Production Days
2015 ASCENT RESOURCES UTICA LLC 233763 97305 155
2016 ASCENT RESOURCES UTICA LLC 418658 92745 365
2017 ASCENT RESOURCES UTICA LLC 240843 37781 365
2018 ASCENT RESOURCES UTICA LLC 98482 12909 187
2019 ASCENT RESOURCES UTICA LLC 18 0 1

For data sources see[5] [6]

Waste Data

Period Operator Name Waste Type Quantity (bbl) Production Days
2015 ASCENT RESOURCES UTICA LLC Brine 10202 155
2016 ASCENT RESOURCES UTICA LLC Brine 10081 365
2017 ASCENT RESOURCES UTICA LLC Brine 4900 365
2018 ASCENT RESOURCES UTICA LLC Brine 1757 187
2019 ASCENT RESOURCES UTICA LLC Brine 3 1

For data sources see[7] [8]

Inspection Data

Inspections Performed

Inspection ID Inspection Date Inspection Type Inspection Result Inspection Comments
0012335113 2014-11-13 Drill / Deepen / Reopen No Violations On the day of my inspection I found that Nomac Drilling rig 80 had reached a total depth of 15985. They were in the process of running new 5.5 production casing. AEU reported that a spill had just occurred prior to my arrival. They estimated that 20 gallons of oil based mud had been released from a CurryVac truck. The mud was released outside of containment. No fluid made it off of the drilling pad. The spill had been cleaned up by the time I was notified. The contaminated gravel had been scraped up and sent to the landfill. I did not observe any residual contamination at the spill site.
0382273940 2014-06-26 Casing String Witnessed No Violations On the date of inspection I accompanied ODNR Inspector Doug Bennett to witness a conductor cement string. Refer to Doug Bennetts report for further details.
0447510505 2018-09-04 Production Wells No Violations The purpose of my inspection was a status check. The well was not in production while Patterson 577 was on location drilling 34059245250000.I spoke with Ascent Company man and he stated that the well is checked at least one time a day.
0658550140 2016-12-14 Production Wells No Violations On the day of my inspection I witnessed the ground was snow covered and that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 600 pounds per square inch and the tubing was at 480 pounds per square inch with annular pressure monitoring in place. Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400 barrel tanks all within containment and shared with the 1H and 3H.
0750026647 2014-07-09 Drill / Deepen / Reopen No Violations On the day of my inspection I witnessed Precision Rathole Inc. was on site drilling mouse holes. I met with Drilling Supervisor Garry Reynolds and verified that top of cement was tagged inside conductor at 77 feet.
0962833462 2019-02-21 Production Wells No Violations The purpose of my inspection was a status check. During my inspection the well was equipped with a production tree style wellhead with open valves. The production equipment on location consisted on seven sand traps, seven gas production units, three horizontal heater treaters, four compressors, six 400-barrel tanks, five 500-barrel tanks, two vapor recovery towers, and one combustor. The four recently completed wells on location were flowing back. The flow back equipment on location consisted of three gas buster tanks, one frac tank, and three horizontal line heaters.
0975637734 2014-11-05 Casing String Witnessed No Violations On the day of my inspection I found that Nomac Drilling rig 80 had new 9.625 casing ran to a depth of 6486. The casing was equipped with a DV tool at 3516. They were circulating when I arrived. O-Tex Pumping attempted to cement the casing to surface in one stage. Although good circulation was maintained throughout the job, no cement was circulated to surface. There were approximately 3 barrels of gel spacer circulated to surface when O-Tex reached their maximum displacement volume. Nomac 80 opened the DV tool and circulated for 12 hours. O-Tex cemented the second stage of the job. Good circulation was maintained throughout the job with approximately 80 barrels of cement returns.
1094596750 2019-03-18 Production Wells No Violations The purpose of my inspection was a status check. During my inspection the well was equipped with a production tree style wellhead with open valves. Gauges present read 0 pounds per square inch on the 13.375-inch diameter surface casing, 0 pounds per square inch on the 9.625-inch diameter intermediate casing, 1500 pounds per square inch on the 5.5-inch diameter production casing, 400 pounds per square inch on the production tubing. The production equipment on location consisted on seven sand traps, seven gas production units, three horizontal heater treaters, four compressors, six 400-barrel tanks, five 500-barrel tanks, two vapor recovery towers, and one combustor.
1209332509 2018-06-28 Production Wells No Violations The inspection is conducted as a simultaneous operation. The well is shut in and idle. The lubricator has been removed and there is no pressure at surface. The intermediate casing is locked out and tagged out. Cage has been placed around the well.
1403786729 2014-06-26 Drill / Deepen / Reopen No Violations On the day of my inspection accompanied by ODNR Inspector Brandon Trigg, I witnessed Precision Rathole Inc. drilled a 36 inch diameter hole to the depth of 100 feet and ran 100 feet of 30 inch 118.65#/ft. conductor pipe. O-Tex Pumping LLC was on site and gained circulation with 5bbls of fresh water, 15bbls of gel and 5bbls of fresh water. O--Flake. Cement returns came back early with returns of 34bbls and cement stayed surface. I Instructed AEU Drilling Superintendent to notify ODNR prior to re-spud so verification of top of cement inside conductor can be seen and if any remedial work will be necessary.
1414428206 2014-10-27 Casing String Witnessed No Violations On the date of inspection I was informed by American Energy Utica (AEU) consultant Van Dietrich that the Nomac 80 rig had drilled a 17.5 inch diameter hole to a depth of 970 feet. Wyoming Casing Crew set 13.375 inch 54.50lbs/ft casing on bottom. O-Tex Pumping, LLC pumped 1270sk of Class H cement, 15.6ppg, 1.2 yield, 2% CaCl, 0.25lbs/sk flake, 0.4% C-41P. O-Tex released the plug and approximately 2bbl into displacement the pressure spiked to 625psi. O-Tex stopped pumping and bled off pressure but still continued to pressure up. AEU plans to drill out the plug and cement, run a Cement Bond Log to find the top of cement, and then decide how to bring cement to surface from there.
1428589695 2015-04-09 Preliminary Restoration No Violations On the day of my inspection production equipment has been installed and awaiting on frac. The site passed preliminary restoration according to ORC 1509.072A.
1473166835 2016-09-06 Production Wells No Violations On the day of my inspection I witnessed that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 750 pounds per square inch and the tubing was at 420 pounds per square inch with annular pressure monitoring in place. Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400 barrel tanks all within containment and shared with the 1H and 3H.
1500640982 2018-10-11 Production Wells No Violations During my inspection Patterson 577 was no longer on location and the well was awaiting to be put back into production after being decommissioned for drilling operations on 4 new wells on pad.
1506587146 2019-01-18 Production Wells No Violations The well remains temporarily abandon with two cast iron bridge plugs. Ascent plans to drill out the plugs and install 2.875-inch diameter production tubing and bring the well back into production. Fortis Energy Services had a derrick service rig on location to drill out plugs.
1850834846 2018-09-25 Production Wells No Violations The purpose of my inspection was a status check on drilling operations. Accompanied by ODNR Kenn Frye, during our inspection we completed a walk around with Ascent Resources Superintendent James McGee. Patterson 577 was on location in the process of drilling the 10H. This well had been decommissioned prior to rig Patterson 577 moving onto location. The well was equipped with valves on all casing strings. All valves showed 0 pounds per square inch and the a cage was placed over the well.
1866798004 2014-06-25 Drill / Deepen / Reopen No Violations
1870546719 2015-08-10 Production Wells No Violations On the day of my inspection I witnessed that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 2500psi and the tubing was a 2250psi. Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400bbl tanks all within containment and shared with the 1Hand 3H. The well has been online for two weeks and current production levels are 800bbls of oil, 168bbls of water and 2MMCF of gas per day.
1974025980 2018-09-25 Production Wells No Violations The purpose of my inspection was to witness the status of temporary abandonment on well #2-4341. Guernsey County Inspector Austin Gutridge was present during the inspection. While on location we met with Ascent Drilling Superintendent James McGee. At the time of inspection, Patterson #577 was on location drilling on well Red Hill Farm 10H- #2-4526. The drilling crew was making a trip to change the drilling assembly. Well 5H was temporarily abandoned. The production tree was removed and night cap was in place. Annular valve had pressure gauges installed for monitoring. Pressure transducers were installed on the night cap monitoring port to allow for constant monitoring with alarms. A steel cage was located over the well head. A total of three (3) wells were temporarily abandoned. The surface production equipment had been removed. The transfer point was isolated. No simultaneous operations or anti-collision issues were identified during the inspection.
2007709957 2018-12-28 Production Wells No Violations During my inspection the well was temporarily abandoned and equipped with a night cap. Annular pressure monitoring was present and the well was caged. Four additional wells on pad had just finished hydraulic stimulation operations and the frac equipment was demobilizing off pad.
2036034107 2015-09-28 Production Wells No Violations On the day of my inspection I witnessed that the well is online and equipped with a Universal Wellhead LLC casing and production wellhead along with a Universal Wellhead LLC production tree with valves in the open position. Casing pressure was at 2350psi and the tubing was a 1750psi. Production equipment included a sand trap, a GP Unit, a line heater, a vapor recovery system, 2-NGL tanks, 2 compressor units, a combustor unit and a total of 12-400bbl tanks all within containment and shared with the 1Hand 3H.
2094270362 2017-02-07 Production Wells No Violations On the day of my inspection I witnessed that the well was equipped with a plunger lift system with valves in the open position. Casing pressure was at 650 pounds per square inch and the tubing was at 500 pounds per square inch with annular pressure monitoring in place. The production equipment included 12-400 barrel tanks within containment, 2-NGL tanks, a vapor recovery tower, 2-compressor units, 2-horizontal heater treaters, 2-oil stabilizer units and a gas combustor all shared with the 1H and 3H. Also present a GP Unit and a sand trap with identification present and production records current.

For data sources see[9]

References

  1. ↑ "Risk Based Data Management System - Well, tblLocational, tblPlugWell, tblInspection, tblCivilTownships and tblPad Tables". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
  2. ↑ "Risk Based Data Management System - Well and WellHistry Tables". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
  3. ↑ "FracFocus Fracking Chemicals Database". 2019-04-02. Retrieved 2019-06-19. 
  4. ↑ "Risk Based Data Management System - tblStimulation Table". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
  5. ↑ "Risk Based Data Management System - Production Table - Oil and Gas Data". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
  6. ↑ "Combined Production - Oil and Gas Data". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
  7. ↑ "Risk Based Data Management System - Production Table - Brine Data". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
  8. ↑ "Combined Production - Brine Data". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
  9. ↑ "Risk Based Data Management System - tblInspection, tblInspFail and tblinspFlDesc Tables". Ohio Department of Natural Resources. 2019-05-07. Retrieved 2019-05-21. 
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