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15A NCAC 02D .0944 MANUFACTURE OF POLYETHYLENE: POLYPROPYLENE AND POLYSTYRENE



(a) For the purpose of this Regulation, the following definitions apply:



(1) (2) (3) (4) (5)



(6) (7) (8) (9) (10)



"By-product and diluent recovery operation" means the process that separates the diluent from the by-product (atactic) and purifies and dries the diluent for recycle. "Continuous mixer" means the process that mixes polymer with anti-oxidants. "Decanter" means the process that separates the diluent/crude product slurry from the alcohol-water solution by decantation. "Ethylene recycle treater" means the process that removes water and other impurities from the recovered ethylene. "High-density polyethylene plants using liquid phase slurry processes" means plants that produce high-density polyethylene in which the product, polyethylene, is carried as a slurry in a continuous stream of process diluent, usually pentane or isobutane. "Neutralizer" means the process that removes catalyst residue from the diluent/crude produce slurry. "Polypropylene plants using liquid phase process" means plants that produce polypropylene in which the product, polypropylene, is carried as a slurry in a continuous stream of process diluent, usually hexane. "Polystyrene plants using continuous processes" means plants which produce polystyrene in which the product, polystyrene, is transferred in a continuous stream in a molten state. "Product devolatilizer system" means the process that separates unreacted styrene monomer and by products from the polymer melt. "Reactor" means the process in which the polymerization takes place.



(b) This Regulation applies to:



(1) (2) (3) polypropylene plants using liquid phase processes, high-density polyethylene plants using liquid phase slurry processes, and polystyrene plants using continuous processes.



(c) For polypropylene plants subject to this Regulation, the emissions of volatile organic compounds shall be reduced by 98 percent by weight or to 20 ppm, whichever is less stringent, from:



(1) (2) (3) (4) (5) (6) reactor vents, decanter vents, neutralizer vents, by-product and diluent recovery operation vents, dryer vents, and extrusion and pelletizing vents.



(d) For high-density polyethylene plants subject to this Regulation, the emissions of volatile organic compounds shall be reduced by 98 percent by weight or to 20 ppm, whichever is less stringent, from:



(1) (2) (3) ethylene recycle treater vents, dryer vents, and continuous mixer vents.



(e) For polystyrene plants subject to this Regulation, the emissions of volatile organic compounds shall not exceed 0.24 pounds per ton of product from the product devolatilizer system. (f) If flares are used to comply with this Regulation all of the following conditions shall be met:



(1) (2) (3)



(4)



Visible emissions shall not exceed five minutes in any two-hour period. A flame shall be present. If the flame is steam-assisted or air-assisted, the net heating value shall be at least 300 BTU per standard cubic foot. If the flame is non-assisted, the net heating value shall be at least 200 BTU per standard cubic foot. If the flare is steam-assisted or non-assisted, the exit velocity shall be no more than 60 feet per second. If the flare is air-assisted, the exit velocity shall be no more than (8.706 + 0.7084 HT) feet per second, where HT is the net heating value.



Aflare that meets the conditions given in Subparagraphs (1) through (4) of this Paragraph are presumed to achieve 98 percent destruction of volatile organic compounds by weight. If the owner or operator of the source chooses to use a flare that fails to meet one or more of these conditions, he shall demonstrate to the Director that the flare shall destroy at least 98 percent of the volatile organic compounds by weight. To determine if the specifications for the flare are being met, the owner or operator of a source using the flare to control volatile organic compound emissions shall install, operate, and maintain necessary monitoring instruments and shall keep necessary records as required by Regulation .0903 of this Section.





History Note:



Authority G.S. 143-215.3(a)(1); 143-215.107(a)(5); Eff. May 1, 1985.






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Last Modified: Mon Mar 10 08:15:37 2008
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