MOUNT PLEASANT, WI —
OSHA Inspection: S. C. JOHNSON & SON, INC.
Complaint inspection · Safety discipline
At a glance
On , OSHA opened a complaint safety inspection of S. C. JOHNSON & SON, INC. in 8311 16TH ST., MOUNT PLEASANT, WI 53403 (NAICS 325612). OSHA activity number 344494042.
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employer broke any rule; any findings appear as the citations listed below, and citations can be contested, reduced, or withdrawn.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
- S. C. JOHNSON & SON, INC.
- Site address
- 8311 16TH ST.
- City
- MOUNT PLEASANT
- State
- WI
- ZIP
- 53403
- Mailing
- 1525 HOWE ST., RACINE, WI 53403
What kind of inspection was it?
- Inspection type
- Complaint (B)
- Scope
- Partial (B)
- Discipline
- Safety
- Advance notice
- No
- Union status
- B
When did the case open and close?
- Opened
- Closing conference
- Case closed
- Last modified
- Data loaded
Establishment context
- NAICS code
- 325612
- Employees
- 1096
- Ownership type
- A
Citations
6 citations on file for this inspection.
1910.119 D02 I E
- Issued
- May 29, 2020
- Abate by
- Jul 16, 2020
- Penalty
- Initial $7,229 · Current $0 Reduced
General-duty citation text
29 CFR 1910.119(d)(2)(i)(E): Process safety information pertaining to the technology of the process did not include a description of the specific employee impact during the qualitative evaluation of the consequence of deviations (a) On or about February 20, 2020, the Process Hazard Analysis (PHA) and operating procedures for the Acetone System developed by the employer did not qualitatively assess the range of the possible safety and health consequences of deviations on employees in the workplace. The potential cause-consequence pairs identified in the Hazard and Operability (HAZOP) Study for the PHA nor the consequences of deviations in the operating procedures do not discuss the possible number of employees affected by process deviations, the possible severity of injuries, or an evaluation of the potential for other employees to be affected by potential deviations in the process. This exposes chemical process operators of the Acetone System to fire, explosion, and chemical contact hazards while present in the production environment. (b) On or about December 5, 2019, the PHA and the operating procedures for the Liquified Petroleum Gas (LPG) System developed by the employer did not qualitatively assess the range of the possible safety and health consequences of deviations on employees in the workplace. The potential cause-consequence pairs identified in the Hazard and Operability (HAZOP) Study for the PHA and the consequences of deviations in the operating procedures do not discuss the possible number of employees affected by process deviations, the possible severity of injuries, or an evaluation of the potential for other employees to be affected by potential deviations in the process. This exposes chemical process operators of the LPG system to fire, explosion, and chemical contact hazards while present in the production environment. (c) On or about December 5, 2019, the PHA for the Liquified Petroleum Gas (LPG) Railcar Delivery System developed by the employer did not qualitatively assess the range of the possible safety and health consequences of deviations on employees in the workplace. The potential cause-consequence pairs identified in the Hazard and Operability (HAZOP) Study for the PHA did not discuss the possible number of employees affected by process deviations, the possible severity of injuries, or an evaluation of the potential for other employees to be affected by potential deviations in the process. This exposes chemical process operators of the LPG Railcar Delivery system to fire, explosion, and chemical hazards while present in the production environment. (d) On or about December 5, 2019, the PHA Ethanol System developed by the employer did not qualitatively assess the range of the possible safety and health consequences of deviations on employees in the workplace. The potential cause-consequence pairs identified in the Hazard and Operability (HAZOP) Study for the PHA nor the consequences of deviations in the operating procedures do not discuss the possible number of employees affected by process deviations, the possible severity of injuries, or an evaluation of the potential for other employees to be affected by potential deviations in the process. This exposes chemical process operators of the Ethanol System to fire, explosion, and chemical contact hazards while present in the production environment. (e) On or about December 5, 2019, the PHA for the Isopropanol System developed by the employer did not qualitatively assess the range of the possible safety and health consequences of deviations on employees in the workplace. The potential cause-consequence pairs identified in the Hazard and Operability (HAZOP) Study for the PHA nor the consequences of deviations in the operating procedures do not discuss the possible number of employees affected by process deviations, the possible severity of injuries, or an evaluation of the potential for other employees to be affected by potential deviations in the process. This exposes chemical process operators of the Isopropanol System to fire, explosion, and chemical contact hazards while present in the production environment. (f) On or about December 5, 2019, the PHA for the Isopentane System developed by the employer did not qualitatively assess the range of the possible safety and health consequences of deviations on employees in the workplace. The potential cause-consequence pairs identified in the Hazard and Operability (HAZOP) Study for the PHA nor the consequences of deviations in the operating procedures do not discuss the possible number of employees affected by process deviations, the possible severity of injuries, or an evaluation of the potential for other employees to be affected by potential deviations in the process. This exposes chemical process operators of the Isopentane System to fire, explosion, and chemical contact hazards while present in the production environment. (g) On or about December 5, 2019, the PHA for the Naphtha System developed by the employer did not qualitatively assess the range of the possible safety and health consequences of deviations on employees in the workplace. The potential cause-consequence pairs identified in the Hazard and Operability (HAZOP) Study for the PHA did not discuss the possible number of employees affected by process deviations, the possible severity of injuries, or an evaluation of the potential for other employees to be affected by potential deviations in the process. This exposes chemical process operators of the Naphtha System to fire, explosion, and chemical contact hazards while present in the production environment.
Recent events (2)
- — I (O) $0
- — Z (S) $7229
1910.119 M05
- Issued
- May 29, 2020
- Abate by
- Jul 1, 2020
- Penalty
- Initial $4,337 · Current $4,337
General-duty citation text
29 CFR 1910.119(m)(5): The employer shall establish a system to promptly address and resolve the incident report findings and recommendations. Resolutions and corrective actions shall be documented. (a) On or about December 5, 2019, the employer did not promptly address and resolve incident report findings, in-that recommendations and findings that were determined to be an appropriate resolution on September 30, 2019, regarding an incident involving the release of Liquified Petroleum Gas (LPG) on September 20, 2019. The recommendations that had been made during the incident investigation were not incorporated into normal shutdown procedures or emergency shutdown procedures by May 26, 2020. Although stickers were placed on the electrical boxes for the power system advising employees of the possibility of LPG releases when the power was disconnected, no guidance was provided as part of the operating procedures as to what thresholds should be used, or factors to consider when deciding if overriding the air line shutdown is required in order to prevent the hydrostatic expansion of LPG in the line and subsequent release.
Recent events (2)
- — I (O) $4337
- — Z (S) $4337
1910.119 D01
- Issued
- May 29, 2020
- Abate by
- Jul 16, 2020
- Penalty
- Initial $0 · Current $0
General-duty citation text
29 CFR 1910.119(d)(1): Process safety information pertaining to the hazards of the highly hazardous chemicals in the process did not consist of the elements specified in 29 CFR 1910.119 (d)(1)(i) through (vii): (a) On or about December 5, 2019, the employer did not consider all tanks in the Building 51 tank enclosure, T-3001-6, T-3008-9, and T-3117, that could impact the Acetone System or create additional hazards during a deviation in the Acetone System to be part of the Acetone System Process Safety Information under the PSM standard. This deficiency may expose employees in the building 51 vicinity and/or the truck unloading zone near the T-3XXX series tank enclosure to hazards including chemical contact hazards or fire and explosion hazards.
Recent events (2)
- — I (O) $0
- — Z (O) $0
1910.119 D03 I B
- Issued
- May 29, 2020
- Penalty
- Initial $0 · Current $0
General-duty citation text
29 CFR 1910.119(d)(3)(i)(B): The employer's piping and instrument diagrams did not include information that provided specific identification of equipment that is part of the process. (a) On or about February 11, 2020, inspection of Acetone process in Building 51, identified that P&IDs did not reflect current piping configuration within the Roach Bait room (R.B. Room). Pipe number P-710 and pipe line 374 were interconnected by stainless steel pipe section. The P&ID reflected pipe P-710 and pipe line 374 terminated with a hand valve quick connection point.
Recent events (2)
- — I (O) $0
- — Z (O) $0
1910.147 C04 II B
- Issued
- May 29, 2020
- Abate by
- Jul 16, 2020
- Penalty
- Initial $0 · Current $0
General-duty citation text
29 CFR 1910.147(c)(4)(ii)(B): The energy control procedures did not clearly and specifically outline the steps for shutting down, isolating, blocking and securing machines or equipment to control hazardous energy. (a) On or about December 5, 2019, in building 63, for the work of removing a blind for a condensate line, the process break permit (Pre-Job #13046) did not specify hazardous energy control isolation points for shutting down and isolating energy sources. (b) On or about January 8, 2020, in building 63, for the work of connecting pipe to peroxide piping to T-10004, the process break permit (Pre-Job # 13003) did not specify hazardous energy control isolation points for shutting down and isolating energy sources.
Recent events (2)
- — I (O) $0
- — Z (O) $0
1910.147 C04 II C
- Issued
- May 29, 2020
- Abate by
- Jul 16, 2020
- Penalty
- Initial $0 · Current $0
General-duty citation text
29 CFR 1910.147(c)(4)(ii)(C): The energy control procedure did not clearly and specifically outline the steps for placement, removal and transfer of lockout devices or tagout devices and the responsibility for them. (a) On or about December 5, 2019, in building 63, for the work of removing a blind for a condensate line, the process break permit (Pre-Job #13046) did not specify placement, removal and/or transfer location of isolation/lockout devices. (b) On or about January 8, 2020, in building 63, for the work of connecting pipe to peroxide piping to T-10004, the process break permit (Pre-Job # 13003), did not specify placement, removal and/or transfer location of isolation/lockout devices.
Recent events (2)
- — I (O) $0
- — Z (O) $0
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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 344494042.
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