Safety Incidents OSHA Severe Injury Reports · 2015–2025
5,189,992Inspections Most recent open 2026-07-18 Last loaded 2026-07-22

OSHA Inspection: FUJIFILM HUNT CHEMICALS USA INC

Accident-driven inspection · Health discipline

On , OSHA opened an accident-driven health inspection of FUJIFILM HUNT CHEMICALS USA INC in 411 MANUFACTURERS ROAD, DAYTON, TN 37321 (NAICS 325110). OSHA activity number 309632040.

What this inspection record means

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employer broke any rule; any findings appear as the citations listed below, and citations can be contested, reduced, or withdrawn.

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Site address
411 MANUFACTURERS ROAD
City
DAYTON
State
TN
ZIP
37321
Inspection type
Accident-driven (A)
Scope
Partial (B)
Discipline
Health
Advance notice
No
Union status
N
Opened
Closing conference
Case closed
Last modified
Data loaded
NAICS code
325110
SIC code (legacy)
2869
Employees
78
Ownership type
A

46 citations on file for this inspection.

1910.119 D01 IV

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

1910.119 D01 VI

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

1910.119 D02 ID

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

1910.119 D02 IE

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

1910.119 D03 II

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or serious
physical harm to employees, in that employees were exposed to fire and
explosion from use of
flammable and combustible materials in an OXAD Mother Liquor (ML)
distillation process on
August 2 and 3, 2006, without equipment having recognized and generally
accepted engineering
controls to avert and/or abate a runaway reaction, and to alert
potentially exposed employees that
action, including controls and evacuation, was necessary.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation process
in tank T-644, in line 3 of building 6.  There was a reported 3,451 pounds
of flammable liquid
(methanol) in tank T-644 at the beginning of the distillation.  (There
were more flammable
liquids in tanks in the same line and in the building that could have also
been involved in a fire
or explosion.)
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations Manager,
were potentially exposed to a fire and/or explosion when working on the
process.  An explosion
and fire did occur on 8/3/06.
This hazard was reasonably foreseeable in that it was recognized by
employer representatives
and the industry.
Among other methods, one feasible and acceptable abatement method for
correcting this hazard
is to have electronic monitoring of heating jacket vs. batch temperatures
that automatically
initiates control actions when an (unwanted or unexpected) exothermic
reaction occurs.  Such
control actions might include cooling jacket activation, dumping batch
contents to an unheated
tank, a form of quenching (when possible), or a combination of such
controls.  A necessary
element of the control system would be automatic alarm activation to
notify
exposed employees
of necessary control actions and evacuation.
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E01

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or
serious physical harm to employees, in that employees were exposed to fire
and explosion
from use of flammable liquids in an OXAD Mother Liquor (ML) distillation
process on
August 2 and 3, 2006, before job and expert hazard analyses were conducted
to identify and
control hazards in the process.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation
process in tank T-644, in line 3 of building 6.  There was a reported
3,451 pounds of
flammable liquid (methanol) in tank T-644 at the beginning of the
distillation.
(There were
more flammable liquids in tanks in the same line and in the building that
could have also
been involved in a fire or explosion.)
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations
Manager, were potentially exposed to a fire and/or explosion when working
on the process.
An explosion and fire did occur on 8/3/06.
No job or expert hazard analysis was performed before the distillation to
identify and control
the potential hazards in the OXAD ML distillation process.  Such hazard
analyses are
elements of an effective safety and health program.
This hazard was reasonably foreseeable in that it was recognized by
employer
representatives, the industry, and common sense.
Among other methods, one feasible and acceptable abatement method for
correcting this
hazard is to perform a hazard analysis that is adequate for the complexity
of the process.
The hazard analysis would include differential scanning calorimetry (DSC)
or similar tests,
on all mixtures in the distillation.  In an OXAD ML distillation operation
the hazard analyses
would include analyses of: 1.PYM, 2. OXAD Mother liquor, and 3. OXAD
Mother liquor
after the methyl alcohol distillation removed most of the methyl alcohol.
A DSC on the Mother liquor before and after the methyl alcohol was
distilled off would help
the employer develop the temperature parameters under which it must
operate.  A DSC on
the Mother liquor after the methyl alcohol distillation is necessary
because there are many
compounds in the Mother liquor which may undergo thermal decomposition at
the
temperatures used for the methyl alcohol distillation, and their breakdown
products may
affect the temperatures at which the PYM is distilled.  The company must
define the
temperature limitations of such a distillation before performing it,
including
boiling points at
the pressure of the vacuum, and DSC test exotherm points with respect to
the pressure of the
vacuum, to avoid thermal decomposition.
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E03 I

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E03 III

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E03 IV

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E03 V

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E03 VI

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E03 VII

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 E04

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or serious
physical harm to employees, in that employees were exposed to fire and
explosion from use of
flammable liquids in an OXAD Mother Liquor (ML) distillation process on
August 2 and 3,
2006, without an effective safe work practice (which is an element of an
effective safety and
health program) in place.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation process
in tank T-644, in line 3 of building 6.  (OXAD was
3-(4-nitrophenyl)-5-(2-oxo-3,3-dimethyl
butyl)-1,2,4-oxadiazole.)  There was a reported 3,451 pounds of flammable
liquid (methanol)
in tank T-644 at the beginning of the distillation.  (There were more
flammable liquids in tanks
in the same line and in the building that could have also been involved in
a fire or explosion.)
The written work practice for the distillation, which was the "Plant
Operating Standard for
OXAD Mother Liquor Distillation in T-644," was not effectively safe.  For
example, no safe
upper temperature limit for the OXAD ML was provided in the procedure for
the last phase of
the distillation.
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations Manager,
were potentially exposed to a fire and/or explosion when working on the
process.  An explosion
and fire did occur on 8/3/06.
This hazard was reasonably foreseeable in that it was recognized by
employer
representatives,
the industry, and common sense.
Among other methods, one feasible and acceptable abatement method for
correcting this hazard
is to develop an effectively safe work practice for the OXAD ML
distillation procedure, with
upper batch temperature limits (and limits on the length of time that the
batch can be held at
elevated temperatures).
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IB

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 II

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IIA

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IIB

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IIIA

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IIIB

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IIID

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IIIE

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IV

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 ID

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

Recent events (2)
  • — I (S) $7000.00
  • — Z (S) $7000.00

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or serious
physical harm to employees, in that employees were exposed to fire and
explosion from use of
flammable liquids in an OXAD Mother Liquor (ML) distillation process on
August 2 and 3,
2006, without proper preparation for emergency situations (which is an
element
of an effective
safety and health program) in place.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation process
in tank T-644, in line 3 of building 6.  (OXAD was
3-(4-nitrophenyl)-5-(2-oxo-3,3-dimethyl
butyl)-1,2,4-oxadiazole.)  There was a reported 3,451 pounds of flammable
liquid (methanol)
in tank T-644 at the beginning of the distillation.  (There were more
flammable liquids in tanks
in the same line and in the building that could have also been involved in
a fire or explosion.)
The written work practice for the distillation, which was the "Plant
Operating Standard for
OXAD Mother Liquor Distillation in T-644," did not have instructions for
dealing with
emergency situations.  Such an emergency situation was the development of
a runaway
exothermic reaction in the distillation tank.
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations
Manager,
were potentially exposed to a fire and/or explosion when working on the
process.  An explosion
and fire did occur on 8/3/06.
This hazard was reasonably foreseeable in that it was recognized by
employer representatives,
the industry, and common sense.
Among other methods, one feasible and acceptable abatement method for
correcting this hazard
is to develop proper emergency procedures for the OXAD ML distillation
procedure.  The
emergency preparation would include instructions for dealing with
emergency situations, such
as the development of a runaway exothermic reaction in the distillation
tank.
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 F01 IV

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 G01 I

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or serious
physical harm to employees, in that employees were exposed to fire and
explosion from use of
flammable liquids in an OXAD Mother Liquor (ML) distillation process on
August 2 and 3,
2006, without appropriate safety training in the "Plant Operating Standard
for OXAD Mother
Liquor Distillation in T-644."  Such appropriate safety training is an
element of an effective
safety and health program.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation process
in tank T-644, in line 3 of building 6.  (OXAD was
3-(4-nitrophenyl)-5-(2-oxo-3,3-dimethyl
butyl)-1,2,4-oxadiazole.)  There was a reported 3,451 pounds of flammable
liquid (methanol)
in tank T-644 at the beginning of the distillation.  (There were more
flammable liquids in tanks
in the same line and in the building that could have also been involved in
a fire or explosion.)
The Operators and Shift Leaders of the distillation process had not
received training in the
procedure before it was utilized on August 2 and 3, 2006.  The procedure
was reportedly
composed on 7/31/06 and signed for approval on 8/1/06.
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations Manager,
were potentially exposed to a fire and/or explosion when working on the
process.  An explosion
and fire did occur on 8/3/06.
This hazard was reasonably foreseeable in that it was recognized by
employer representatives,
the industry, and common sense.
Among other methods, one feasible and acceptable abatement method for
correcting this hazard
is to ensure that all employees operating a procedure are trained on the
procedure and its safety
aspects before it is used.
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 G03

Serious 6 instances 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

1910.119 I02 II

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or serious
physical harm to employees, in that employees were exposed to fire and
explosion from use of
flammable liquids in an OXAD Mother Liquor (ML) distillation process on
August 2 and 3,
2006, without effective safety change analysis of the newly-developed
process, including its
operating procedures, before the distillation process was conducted.  Such
change analysis for
new processes would be a necessary sub-element of an effective safety and
health program's
hazard anticipation and detection element.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation process
in tank T-644, in line 3 of building 6.  (OXAD was
3-(4-nitrophenyl)-5-(2-oxo-3,3-dimethyl
butyl)-1,2,4-oxadiazole.)  There was a reported 3,451 pounds of flammable
liquid
(methanol)
in tank T-644 at the beginning of the distillation.  (There were more
flammable liquids in tanks
in the same line and in the building that could have also been involved in
a fire or explosion.)
The written work practice for the distillation, which was the "Plant
Operating Standard for
OXAD Mother Liquor Distillation in T-644," was not effectively safe.  For
example, no safe
upper temperature limit for the OXAD ML was provided in the procedure for
the last phase of
the distillation.  The OXAD ML distillation procedure was reportedly
composed on 7/31/06,
signed for approval on 8/1/06, and used on 8/2/06.  No effective safety
change analysis of the
newly-developed process, including its operating procedures, was conducted
before the
distillation process was performed.
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations Manager,
were potentially exposed to a fire and/or explosion when working on the
process.
An explosion
and fire did occur on 8/3/06.
This hazard was reasonably foreseeable in that it was recognized by
employer representatives,
the industry, and common sense.
Among other methods, one feasible and acceptable abatement method for
correcting this hazard
is to conduct effective safety change analysis of a newly-developed
process, including its
operating procedures, before the process is performed.
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 I02 IV

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

1910.119 L01

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or serious
physical harm to employees, in that employees were exposed to fire and
explosion from use of
flammable liquids in an OXAD Mother Liquor (ML) distillation process on
August
2 and 3,
2006, without change analysis being performed whenever a change in process
procedures
occurred that could have an effect on safety.  Such change analysis is an
element of an effective
safety and health program.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation process
in tank T-644, in line 3 of building 6.  (OXAD was
3-(4-nitrophenyl)-5-(2-oxo-3,3-dimethyl
butyl)-1,2,4-oxadiazole.)  There was a reported 3,451 pounds of flammable
liquid (methanol)
in tank T-644 at the beginning of the distillation.  (There were more
flammable liquids in tanks
in the same line and in the building that could have also been involved in
a fire or explosion.)
The written distillation process procedure, which was the "Plant Operating
Standard for OXAD
Mother Liquor Distillation in T-644," was deviated from in that the
temperature was raised
beyond any temperature listed in the procedure (and beyond a safe
temperature
level).  No
change analysis was performed when temperatures in the distillation were
raised to unsafe levels.
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations Manager,
were potentially exposed to a fire and/or explosion when working on the
process.  An explosion
and fire did occur on 8/3/06.
This hazard was reasonably foreseeable in that it was recognized by
employer representatives,
the industry, and common sense.
Among other methods, one feasible and acceptable abatement method for
correcting this hazard
is to perform change analysis whenever a change in facilities, equipment,
materials, or processes
procedures occurs.
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.119 C02

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

503010501

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

T.C.A. 50-3-105(1):  The employer did not furnish employment and a place
of employment
which were free from recognized hazards that were causing or likely to
cause death or serious
physical harm to employees, in that employees were exposed to fire and
explosion from use of
flammable liquids in an OXAD Mother Liquor (ML) distillation process on
August 2 and 3,
2006, without having employee participation, including Operators and/or
Operator/Shift Leaders,
in the development of work practice procedures and in any hazard analysis
for the process.
Such employee participation is an element of an effective safety and
health program.
On August 2 and 3, 2006, the employer ran an OXAD Mother Liquor (ML)
distillation process
in tank T-644, in line 3 of building 6.  (OXAD was
3-(4-nitrophenyl)-5-(2-oxo-3,3-dimethyl
butyl)-1,2,4-oxadiazole.)  There was a reported 3,451 pounds of flammable
liquid (methanol)
in tank T-644 at the beginning of the distillation.  (There were more
flammable liquids in tanks
in the same line and in the building that could have also been involved in
a fire or explosion.)
The written work practice for the distillation, which was the "Plant
Operating Standard for
OXAD Mother Liquor Distillation in T-644," was reportedly developed by one
person, a Process
Engineer, on 7/31/06, signed for approval by several management personnel
on 8/1/06, and used
on 8/2/06.  No Operators or Operator/Shift Leaders were consulted in the
development of the
OXAD ML distillation procedure.  Operators or Operator/Shift Leaders also
were not consulted
on the development of any hazard analysis for the operation.
Employees such as Operators, Shift Leaders, a Process Engineer, and an
Operations Manager,
were potentially exposed to a fire and/or explosion when working on the
process.  An explosion
and fire did occur on 8/3/06.
This hazard was reasonably foreseeable in that it was recognized by
employer representatives,
the industry, and common sense.
Among other methods, one feasible and acceptable abatement method for
correcting this hazard
is to ensure employee participation, including Operators and/or
Operator/Shift Leader
participation, in the development of work practice procedures for
processes and in any hazard
analysis for the processes.  Such employee participation is an element of
an effective safety and
health program.
ABATEMENT VERIFICATION IS REQUIRED
Recent events (2)
  • — I (S)
  • — Z (S)

1910.106 H04 IC

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

Recent events (2)
  • — I (S) $7000.00
  • — Z (S) $7000.00

1910.132 A

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Apr 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

Recent events (2)
  • — P (S) $7000.00
  • — Z (S) $7000.00

1910.132 D01

Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Apr 17, 2007

Hazardous substances 8880

Recent events (2)
  • — P (S)
  • — Z (S)

1910.1200 G01

Serious 10 instances 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

1910.1200 H01

Deleted Serious 1 instance 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007
Penalty
Initial $7,000 · Current $7,000

Hazardous substances 8880

Recent events (2)
  • — I (S) $7000.00
  • — Z (S) $7000.00

1910.1200 H03 II

Deleted Serious 10 instances 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

1910.1200 H03 III

Deleted Serious 10 instances 14 exposed
Issued
Jan 26, 2007
Abate by
Mar 17, 2007

Hazardous substances 8880

Recent events (2)
  • — I (S)
  • — Z (S)

View Fujifilm Hunt Chemicals USA INC's full OSHA safety record →

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 309632040.

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