R 336.1631
R 336.1631 Emission of volatile organic compounds from existing process equipment utilized in manufacture of polystyrene or other organic resins.
Cite as Mich. Admin. Code R 336.1631
Rule 631. (l) A person shall not cause or allow the emission of volatile organic compounds from
existing process equipment that is utilized in the manufacturing of polystyrene or other organic
resins located in any of the following counties, unless all of the provisions of subrules (2) to (10)
of this rule are met or unless an equivalent control method, as approved by the department under
R 336.1602(2), is implemented:
(a) Western portion of Allegan.
(b) Berrien.
(c) Kent.
(d) Livingston.
(e) Macomb.
(f) Monroe.
(g) Muskegon.
(h) Oakland.
(i) Ottawa.
(j) St. Clair.
(k) Washtenaw.
(l) Wayne.
(2) The emission of volatile organic compounds from existing material recovery equipment that
is utilized in the manufacture of polystyrene resin by a continuous process must not be more than
0.12 pounds per 1,000 pounds of polystyrene resin produced.
(3) A person shall not operate an existing reactor, thinning tank, or blending tank that is utilized
in the manufacture of a completed organic resin unless either of the following provisions is
complied with:
(a) All volatile organic compounds emitted from existing reactors, thinning tanks, and blending
tanks must be vented to control equipment that is designed and operated to reduce the quantity of
volatile organic compounds by not less than 95 weight percent. Reflux condensers that are essential
to the operation of the resin reactor are not considered to be control equipment.
(b) The total volatile organic compounds emitted to the atmosphere from the reactors, thinning
tanks, and blending tanks do not exceed 0.5 pounds per 1,000 pounds of completed organic resin
produced.
(4) Notwithstanding the provisions of subrule (3) of this rule, a person shall not operate an
existing reactor, thinning tank, or blending tank utilized in the manufacture of a dry organic resin
at the Solutia, Inc. of Trenton unless 1 of the following provisions is complied with:
(a) All volatile organic compounds emitted from existing reactors, thinning tanks, and blending
tanks must be vented to control equipment that is designed and operated to reduce the quantity of
volatile organic compounds by not less than 95 weight percent. Reflux condensers that are essential
to the operation of the resin reactor are not considered to be control equipment.
(b) The total volatile organic compounds emitted to the atmosphere from the reactors, thinning
tanks, and blending tanks do not exceed 2.6 pounds per 1,000 pounds of dry organic resin
produced.
(5) Compliance with the emission limits specified in subrules (2), (3), and (4) of this rule must
be determined using the method described in R 336.2060 or an alternate method acceptable to the
department. Upon request by the department, a person that is responsible for processes that are
subject to the provisions of subrule (2), (3), or (4) of this rule shall submit, to the department, test
data necessary for a determination of compliance.
(6) Compliance with the emission limits specified in subrules (2), (3), and (4) of this rule must
be determined using the method described in R 336.2060 or an alternate method acceptable to the
department under R 336.1602(2). Upon request by the department, a person that is responsible for
processes that are subject to the provisions of subrule (2), (3), or (4) of this rule shall submit, to
the department, test data necessary for a determination of compliance including, but not limited
to, the following:
(a) Emissions test data.
(b) Material balance calculations.
(c) Process production rates.
(d) Control equipment specifications and operating parameters.
(7) A person that is responsible for the operation of existing process equipment that is subject to
the provisions of this rule shall submit, to the department, a written program for compliance with
this rule or evidence of compliance with this rule. The written program for compliance must be
submitted to the department before October 19, 1989.
(8) The program required by subrule (7) of this rule must include the method by which
compliance with this rule must be achieved, a description of new equipment to be installed or
modifications to existing equipment to be made, and a timetable that specifies, at a minimum, all
of the following dates:
(a) The date or dates equipment must be ordered.
(b) The date or dates construction, modification, or process changes must begin.
(c) The date or dates initial start-up of equipment must begin.
(d) The date or dates final compliance must be achieved.
(9) A person may discontinue the operation of a natural gas-fired afterburner that is used to
achieve compliance with the emission limits in this rule, between November 1 and March 31,
unless the afterburner is used to achieve compliance with, or is required by, any of the following:
(a) Another provision of these rules.
(b) A permit to install.
(c) A permit to operate.
(d) A voluntary agreement.
(e) A performance contract.
(f) A stipulation.
(g) An order of the department.
(10) If the operation of a natural gas-fired afterburner is discontinued between November 1 and
March 31 pursuant to the provisions of subrule (9) of this rule, then both of the following
provisions apply during this time period:
(a) All other provisions of this rule, except for the emission limits, remain in effect.
(b) All other measures that are used to comply with the emission limits in this rule between April
1 and October 31 must continue to be used.