KAPOLEI, HI —
OSHA Inspection: TESORO HAWAII CORP
Planned inspection · Health discipline
At a glance
On , OSHA opened a planned health inspection of TESORO HAWAII CORP in 91-325 KOMOHANA ST, KAPOLEI, HI 96707 (NAICS 324110). OSHA activity number 313080269.
OSHA opens inspections for many reasons — routine scheduling under a national or local emphasis program, an employee complaint or referral, or a follow-up after a reported injury. Opening or conducting an inspection is not itself an allegation or a finding that this employer broke any rule; any findings appear as the citations listed below, and citations can be contested, reduced, or withdrawn.
Where did this inspection happen?
- Establishment
- TESORO HAWAII CORP
- Site address
- 91-325 KOMOHANA ST
- City
- KAPOLEI
- State
- HI
- ZIP
- 96707
What kind of inspection was it?
- Inspection type
- Planned (H)
- Scope
- Partial (B)
- Discipline
- Health
- Advance notice
- No
- Union status
- Y
When did the case open and close?
- Opened
- Closing conference
- Case closed
- Last modified
- Data loaded
Establishment context
- NAICS code
- 324110
- SIC code (legacy)
- 2911
- Employees
- 230
- Ownership type
- A
- Industry flags
- Manufacturing health.
Citations
13 citations on file for this inspection.
1910.23 E01
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
- Penalty
- Initial $1,375 · Current $1,375
General-duty citation text
29 CFR 1910.23(e)(1) [Refer to chapter 12-72.1, HAR] was violated because: A walking/working platform for R-603 reactor tower that was 44 feet above ground had a top guard railing height of 34 inches from the platform surface. A low top guard railing height exposed employees to fall hazards with the potential for serious injuries. 29 CFR 1910.23(e)(1) states "Railing, toe boards, and cover specifications. A standard railing shall consist of top rail, intermediate rail, and posts, and shall have a vertical height of 42 inches nominal from upper surface of top rail to floor, platform, runway, or ramp level. The top rail shall be smooth-surfaced throughout the length of the railing. The intermediate rail shall be approximately halfway between the top rail and the floor, platform, runway, or ramp. The ends of the rails shall not overhang the terminal posts except where such overhang does not constitute a projection hazard." Location: Reactor R-603 of the Distillate Hydrocracker Unit (DHC)
Recent events (2)
- — F (S) $1375.00
- — Z (S) $1375.00
1910.38 C04
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
- Penalty
- Initial $1,375 · Current $1,375
Recent events (2)
- — F (S) $1375.00
- — Z (S) $1375.00
1910.119 D02 ID
- Issued
- Jan 19, 2011
- Abate by
- Feb 7, 2011
- Penalty
- Initial $1,375 · Current $1,375
General-duty citation text
29 CFR 1910.119(d)(2)(i)(D) [Refer to chapter 12-74.11, HAR] was violated because: 1.The employer's Process Safety Information (P.S.I.) was inaccurate in that the safe operating limits for process pumps P602A, P602B, and P602C had differing minimum operating limits in the document titled "Tesoro Hawaii Corp. Safe Operating Parameters and Consequences of Deviation" (Document 17-01-02), and the Management of Change titled "MOC 2010029-001-DHC: R2009136 Modify Procedures for Feed Min Flow" (Document 14-12-02). Documents that provide conflicting set points may lead to confusion and the possibility of Operator error in handling the process and lead to "Sudden loss of feed could lead to high furnace outlet temperature and reactor runaway, with potential catastrophic explosion hazard." 2.The employer's Process Safety Information was inaccurate in that the employer provided several differing temperatures for heat exchangers in the Naphtha Hydrotreater Unit. Document 03-01-01 listed vessel maximum design temperatures that differed from the maximum design temperatures listed in the vessel's equipment file. The maximum design temperature for Exchangers E-401A through E-401F differed 40 to 300 degrees Fahrenheit between Document 03-01-01 and their individual equipment file. Pressure vessel shell and tube temperatures that are not maintained or accurately tracked may hinder the evaluation of possible temperature related damage associated with the mechanical integrity of the pressure vessels and can result in catastrophic failure. 3.The employer's Process Safety Information was inaccurate in that the employer provided differing pressures for a heat exchanger in the Naphtha Hydrotreater Unit. Process flow and instrumentation diagram (P& I D) drawing A-600-B-049, revision 20, 9/15/09 (Document 03-03-02, Page 001069) indicates a the shell design pressure for E-632 of 150 psi which does not concur with the design information from the U-1 form for E-632 manufactured by Kobe Steel in 1985 (Document 08-01i-01, Page 007149) which indicates that the maximum allowable working pressure is 140 psi for the shell. Pressure vessel shell pressures that are not maintained or accurately tracked may hinder the evaluation of possible temperature related damage associated with the mechanical integrity of the pressure vessels and can result in catastrophic failure. 29 CFR 1910.119(d)(2)(i)(D) states "Process safety information. In accordance with the schedule set forth in paragraph (e)(1) of this section, the employer shall complete a compilation of written process safety information before conducting any process hazard analysis required by the standard. The compilation of written process safety information is to enable the employer and the employees involved in operating the process to identify and understand the hazards posed by those processes involving highly hazardous chemicals. This process safety information shall include information pertaining to the hazards of the highly hazardous chemicals used or produced by the process, information pertaining to the technology of the process, and information pertaining to the equipment in the process. Information pertaining to the technology of the process. (i) Information concerning the technology of the process shall include at least the following: (D) Safe upper and lower limits for such items as temperatures, pressures, flows or Compositions." Location: Establishment
Recent events (2)
- — F (S) $1375.00
- — Z (S) $1375.00
1910.119 D03 IA
- Issued
- Jan 19, 2011
- Abate by
- Feb 7, 2011
General-duty citation text
29 CFR 1910.119(d)(3)(i)(A) [Refer to chapter 12-74.1, HAR] was violated because: The U-1 form for the E-401B heat exchanger constructed by Waner Corporation of Tulsa, OK in 1974 contained in the Tesoro equipment file does not reflect a change in the tube bundle material which occurred since the original heat exchanger was installed. Inaccurate metallurgy can lead to hazards associated with deterioration, corrosion, and embrittlement and lead to leakage within the vessel. 29 CFR 1910.119(d)(3)(i)(A) states "Process safety information. In accordance with the schedule set forth in paragraph (e)(1) of this section, the employer shall complete a compilation of written process safety information before conducting any process hazard analysis required by the standard. The compilation of written process safety information is to enable the employer and the employees involved in operating the process to identify and understand the hazards posed by those processes involving highly hazardous chemicals. This process safety information shall include information pertaining to the hazards of the highly hazardous chemicals used or produced by the process, information pertaining to the technology of the process, and information pertaining to the equipment in the process. Information pertaining to the equipment in the process. (i) Information pertaining to the equipment in the process shall include: (A) Materials of construction." Location: Establishment
Recent events (2)
- — F (S)
- — Z (S)
1910.119 D03 IB
- Issued
- Jan 19, 2011
- Abate by
- Feb 7, 2011
General-duty citation text
29 CFR 1910.119(d)(3)(i)(B) [Refer to chapter 12-74.11, HAR] was violated because: Piping Instrument & Diagrams (P&IDs) A-400-B-003 and A-600-A-1025 for the Naphtha Hydrotreater Unit and the Distillate Hydrocracker Unit did not mirror field conditions. The following conditions were found where the P&IDs differed from the field conditions: 1.Temperature Indicator (TI-422 off of D-402) on P&ID A-400-B-003 was not found in the field; 2.Spectacle Blinds (off of D-602 bottoms) on P&ID A-600-A-1025 were not found in the field at the locations indicated on the PI & D; 3.A valve on a line from D-623 to D-604 (6"-P60681-AD2) was found not to be car sealed open, where P&ID A-600-A-1025 states that the valve is car sealed open; 4. An extra three inch gate valve downstream of PSV-425 was found in the field but not indicated on PI &D A-400-B-003. 5.P&ID A-400-B-003 had a note that PSV-423 was reset to 242 PSIG that was not reflected on PSV-423's tag in the field. 6.A Chloride Injection line indicated on the PI & D A-400-B-002 was previously noted to be disconnected in the field according to a Process Hazard Analysis conducted in 2009, however was not shown as disconnected on the PI &D provided. P&IDs that do not mirror field conditions can lead to process upsets and deviations during normal operations, and confusion and delay during emergency operations, and may result in catastrophe if a process upset cannot be brought under control. 29 CFR 1910.119(d)(3)(i)(B) states "Process safety information. In accordance with the schedule set forth in paragraph (e)(1) of this section, the employer shall complete a compilation of written process safety information before conducting any process hazard analysis required by the standard. The compilation of written process safety information is to enable the employer and the employees involved in operating the process to identify and understand the hazards posed by those processes involving highly hazardous chemicals. This process safety information shall include information pertaining to the hazards of the highly hazardous chemicals used or produced by the process, information pertaining to the technology of the process, and information pertaining to the equipment in the process. Information pertaining to the equipment in the process. (i) Information pertaining to the equipment in the process shall include: (B) Piping and instrument diagrams (P&ID's)." Location: Distillate Hydrocracker and Naphtha Hydrotreater Units. (Refer to A-400-B-003, A-600-A-1025, and A-400-B-002)
Recent events (2)
- — F (S)
- — Z (S)
1910.119 D03 ID
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
- Penalty
- Initial $1,375
General-duty citation text
29 CFR 1910.119(d)(3)(i)(D) [Refer to chapter 12-74.1-1, HAR] was violated because: The employer did not comply with RAGAGEP when it failed to provide adequate controls to ensure that intervening valves on the upstream lines to relief devices PSV-H113 and PSV- H125 remained in the open position during operation when a pressure vessel was the possible source of a relieving event (ASME Boiler and Pressure Vessel Code, Division 1 (BPVC), Section VIII, UG-135(d) and Appendix M are examples of RAGAGEP for controlling intervening stop valves on relief lines. A closed intervening valve upstream or downstream of a pressure relief device during a process upset could lead to catastrophic failure of the vessel. 29 CFR 1910.119(d)(3)(i)(D) states "Process safety information. In accordance with the schedule set forth in paragraph (e)(1) of this section, the employer shall complete a compilation of written process safety information before conducting any process hazard analysis required by the standard. The compilation of written process safety information is to enable the employer and the employees involved in operating the process to identify and understand the hazards posed by those processes involving highly hazardous chemicals. This process safety information shall include information pertaining to the hazards of the highly hazardous chemicals used or produced by the process, information pertaining to the technology of the process, and information pertaining to the equipment in the process. Information pertaining to the equipment in the process shall include: (F) Design codes and standards employed." Location: Catalytic Reformer Unit and Distillate Hydrocracker Unit
Recent events (2)
- — D (S)
- — Z (S) $1375.00
1910.119 D03 II
- Issued
- Jan 19, 2011
- Abate by
- Feb 7, 2011
- Penalty
- Initial $1,375 · Current $1,375
General-duty citation text
29 CFR 1910.119(d)(3)(ii) [Refer to chapter 12-74.1, HAR] was violated because: The employer did not comply with RAGAGEP when it failed to protect employees inside inadequately protected main control room structure that could be exposed to toxic material as a result of a toxic release from process equipment. RAGAGEP for facility siting include, but are not limited to, CCPS [Ref. 38 and 39], API 752, and AIChE/Dow Fire and Explosion Index. An inadequately protected structure exposes employees to toxic material hazards with the potential for serious injuries. 29 CFR 1910.119(d)(3)(ii) states "The employer shall document that equipment complies with recognized and generally accepted good engineering practices." Location: Main Control Room
Recent events (2)
- — F (S) $1375.00
- — Z (S) $1375.00
1910.119 E05
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
- Penalty
- Initial $1,375
General-duty citation text
29 CFR 1910.119(e)(5) [Refer to chapter 12-74.1-1, HAR] was violated because: The employer failed to assure that the recommendations were resolved in that R2009114-016 stated that a PHA item with a risk rank of 3 and rejected by management is acceptable. All other recommendations that were rejected included language under the justification for why the recommendations were rejected. Additionally, R2008001-001, R2008001-002 and R2008001-004 with recommendations that were not approved did not list the justification. 29 CFR 1910.119(e)(5) states "The employer shall establish a system to promptly address the team's findings and recommendations; assure that the recommendations are resolved in a timely manner and that the resolution is documented; document what actions are to be taken; complete actions as soon as possible; develop a written schedule of when these actions are to be completed; communicate the actions to operating, maintenance and other employees whose work assignments are in the process and who may be affected by the recommendations or actions." Location: Establishment
Recent events (2)
- — D (S)
- — Z (S) $1375.00
1910.119 F04
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
- Penalty
- Initial $1,375 · Current $1,375
General-duty citation text
29 CFR 1910.119(f)(4) [Refer to chapter 12-74.1, HAR] was violated because: The employer did not implement its safe work practice for motorized equipment and other equipment with sources of ignition when used within operating units that contain flammable or combustible materials. A diesel mobile crane, Super Heat F6H equipment, and Whisperwatt Diesel Powered AC Generator were not listed on hot work permits for hot work being conducted at the Distillate Hydrocracker Unit (DHC). Failure to list equipment with sources of ignition on hot work permits exposed employees to fire hazards with the potential for serious injuries. 29 CFR 1910.119(f)(4) states "The employer shall develop and implement safe work practices to provide for the control of hazards during operations such as lockout/tagout; confined space entry; opening process equipment or piping; and control over entrance into a facility by maintenance, contractor, laboratory, or other support personnel. These safe work practices shall apply to employees and contractor employees." Location: Distillate Hydrocracker Unit (DHC)
Recent events (2)
- — F (S) $1375.00
- — Z (S) $1375.00
1910.120 Q03 V
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
- Penalty
- Initial $1,375 · Current $1,375
General-duty citation text
29 CFR 1910.120(q)(3)(v) [Refer to chapter 12-74.1, HAR] was violated because: The buddy system was not specifically listed as a component of the employer's written Emergency Response Plan and the employer failed to provide any information on the manner in which this would be performed by the Emergency Response Team in the event of chemical release, fire or other emergencies. The lack of a buddy system puts individual Emergency Response Team personnel at risk should they enter a unit alone, become overwhelmed, and need assistance or rescue. 29 CFR 1910.120(q)(3)(v) states "The individual in charge of the ICS shall limit the number of emergency response personnel at the emergency site, in those areas of potential or actual exposure to incident or site hazards, to those who are actively performing emergency operations. However, operations in hazardous areas shall be performed using the buddy system in groups of two or more." Location: Establishment
Recent events (2)
- — F (S) $1375.00
- — Z (S) $1375.00
1910.120 Q03 VI
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
General-duty citation text
29 CFR 1910.120(q)(3)(vi) [Refer to chapter 12-74.1, HAR] was violated because: The provision for back up personnel was not included in the employer's Emergency Response Plan and the employer failed to provide information on the manner in which this would be performed by employees in the event of chemical release, fire, or other emergency. The lack of back up personnel puts Emergency Response Team personnel at risk should they enter a unit, become overwhelmed, and need assistance or rescue. 29 CFR 1910.120(q)(3)(vi) states "Back-up personnel shall stand by with equipment ready to provide assistance or rescue. Advance first aid support personnel, as a minimum, shall also stand by with medical equipment and transportation capability." Location: Establishment
Recent events (2)
- — F (S)
- — Z (S)
1910.134 H03 IB
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
- Penalty
- Initial $1,375 · Current $1,375
General-duty citation text
29 CFR 1910.134(h)(3)(i)(B) [Refer to chapter 12-64.1, HAR] was violated because: Self Contained Breathing Apparatuses (SCBAs) used by the Emergency Response Team and Fire Brigade were not being inspected at least monthly. Use of a malfunctional SCBA in an emergency situation can expose the user to an oxygen deficient and toxic environment, leading to asphyxiation. 29 CFR 1910.134(h)(3)(i)(B) states "The employer shall ensure that respirators are inspected as follows: (B) All respirators maintained for use in emergency situations shall be inspected at least monthly and in accordance with the manufacturer's recommendations, and shall be checked for proper function before and after each use." Location: Establishment
Recent events (2)
- — F (S) $1375.00
- — Z (S) $1375.00
1910.134 H03 III
- Issued
- Jan 19, 2011
- Abate by
- Jan 24, 2011
General-duty citation text
29 CFR 1910.134(h)(3)(iii) [Refer to chapter 12-64.1, HAR] was violated because: Self Contained Breathing Apparatuses (SCBAs) used by the Emergency Response Team and Fire Brigade were not being inspected at least monthly. Use of a malfunctional SCBA in an emergency situation can expose the user to an oxygen deficient and toxic environment, leading to asphyxiation. 29 CFR 1910.134(h)(3)(iii) states "In addition to the requirements of paragraphs (h)(3)(i) and (ii) of this section, self-contained breathing apparatus shall be inspected monthly. Air and oxygen cylinders shall be maintained in a fully charged state and shall be recharged when the pressure falls to 90of the manufacturer's recommended pressure level. The employer shall determine that the regulator and warning devices function properly." Location: Establishment
Recent events (2)
- — F (S)
- — Z (S)
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Source
This record is reproduced from the U.S. Department of Labor Open Data API (OSHA inspection dataset). The original IMIS detail view is available at OSHA's Establishment Search for activity number 313080269.
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