EPA-600/2-77-023K February 1977 Environmental Protection Technology Series INDUSTRIAL PROCESS PROFILES FOR ENVIRONMENTAL USE: Chapter 11. The Synthetic Fiber Industry Industrial Environmental Research Laboratmy Office of Research and Development U.S. Environmental Protection Agency Cincinnati, Ohio 45268 ------- RESEARCH REPORTING SERIES Research reports of the Office of Research and Development, U.S. Environmental Protection Agency, have been grouped into five series. These five broad categories were established to facilitate further development and application of environmental technology. Elimination of traditional grouping was consciously planned to foster technology transfer and a maximum interface in related fields. The five series are: 1. Environmental Health Effects Research 2. Environmental Protection Technology 3. Ecological Research 4. Environmental Monitoring 5. Socioeconomic Environmental Studies This report has been assigned to the ENVIRONMENTAL PROTECTION TECHNOLOGY series. This series describes research performed to develop and demonstrate instrumentation, equipment, and methodology to repair or prevent environmental degradation from point and non-point sources of pollution. This work provides the new or improved technology required for the control and treatment of pollution sources to meet environmental quality standards. This document is available to the public through the National Technical Informa- tion Service, Springfield, Virginia 22161. ------- EPA-600/2-77-023k February 1977 INDUSTRIAL PROCESS PROFILES FUR ENVIRONMENTAL USE CHAPTER 11 THE SYNTHETIC FIBER INDUSTRY by Jerry L. Parr Radian Corporation Austin, Texas 78766 Contract No. 68-02-1319 Project Officer Alfred B. Craig Metals and Inorganic Chemicals Branch Industrial Environmental Research Laboratory Cincinnati, Ohio 45268 INDUSTRIAL ENVIRONMENTAL RESEARCH LABORATORY OFFICE OF RESEARCH AND DEVELOPMENT U.S. ENVIRONMENTAL PROTECTION AGENCY CINCINNATI, OHIO 45268 ------- DISCLAIMER This report has been reviewed by the Industrial Environmental Research Laboratory - Cincinnati, U.S. Environmental Protection Agency, and approved for publication. Approval does not signify that the contents necessarily reflect the views and policies of the U.S. Environmental Protection Agency, nor does mention of trade names or commercial products constitute endorsement or recommendation for use. ii ------- TABLE OF CONTENTS CHAPTER 11 Page INDUSTRY DESCRIPTION 1 Raw Materials 3 Products 4 Companies 6 Environmental Impact 6 Bibliography 9 INDUSTRY ANALYSIS 11 Synthetic Fiber Processing 11 Process No. 1. Mel t Spi nni ng 13 Process No. 2. Wet Spinning 16 Process No. 3. Dry Spinning 19 Process No. 4. Lubrication 21 Process No. 5. Drawing 23 Process No. 6. Fiber Modifications 25 APPENDIX A - Raw Materials Lists 27 APPENDIX B - Products 31 APPENDIX C - Producers 41 m ------- LIST OF FIGURES CHAPTER 11 Figure Page 1 SYNTHETIC FIBER INDUSTRY FLOW DIAGRAM 12 IV ------- LIST OF TABLES CHAPTER 11 Table Page 1 1975 PRODUCTION OF SYNTHETIC FIBERS 2 2 TEN LARGEST SYNTHETIC FIBER PRODUCERS 2 3 FUELS & ELECTRICAL ENERGY CONSUMED BY COMPANIES IN SIC CODE 2824 IN 1971 3 4 RAW MATERIAL CONSUMPTION FOR PRODUCTION OF SYNTHETIC FIBERS BY COMPANIES IN SIC CODE 2824 IN 1971 4 5 GENERIC NAMES OF SYNTHETIC FIBERS 5 6 END USES OF SYNTHETIC FIBERS, 1973 CONSUMPTION (Gg), 5 7 CAPACITY OF TEN LARGEST SYNTHETIC FIBER PRODUCERS 6 8 SUMMARY OF WASTEWATER DATA FOR SELECTED FIBERS 7 9 SOURCE CLASSIFICATION CODES FOR SYNTHETIC FIBERS 8 10 INPUT POLYMERS FOR MELT SPINNING 13 11 TYPICAL MELT SPINNING OPERATING PARAMETERS 14 12 INPUT MATERIALS FOR WET SPINNING 16 13 OPERATING SUMMARY OF PARAMETERS FOR PRODUCTION OF ACRYLIC FIBERS BY WET SPINNING 17 14 INPUT MATERIALS FOR DRY SPINNING 19 15 OPERATING PARAMETERS FOR SYNTHETIC FIBER DRAWING 23 A-l FIBER RAW MATERIALS 28 A-2 TYPICAL ADDITIVES USED IN FIBER PRODUCTION 29 A-3 SOLVENTS USED IN FIBER PRODUCTION 30 B-l PRODUCTS OF THE SYNTHETIC FIBERS INDUSTRY 32 B-2 CHEMICAL AND PHYSICAL PROPERTIES OF SOME TEXTILE FIBERS .. 38 C-l SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES 42 C-2 LOCATION OF U.S. SYNTHETIC FIBER PRODUCING PLANTS 49 ------- ACKNOWLEDGEMENTS Some of the technical information used in preparing this catalog entry was supplied to EPA by Monsanto Research Corporation, Dayton Laboratory, under Contract No. 68-02-1320, Task 17. The contribution of Duane E. Earley is gratefully acknowledged. Mr. William Medley was Project Leader. This catalog entry was prepared for EPA by Radian Corporation under Contract No. 68-02-1319, Task 52. The author was Jerry L. Parr, with contributions made by Terry B. Parsons and Judith D. Whiting. Eugene C. Cavanaugh was the Program Manager. Helpful review comments from Robert W. Lenz were received and incorporated in this chapter. vi ------- SYNTHETIC FIBER INDUSTRY INDUSTRY DESCRIPTION Synthetic*fibers are defined as noncellulosic fibers of synthetic origin. The category includes manufactured fibers in which the fiber-forming substance is a long-chain, organic synthetic polymer. Cellulosic fibers such as rayon and acetate and the inorganic fibers such as boron, fiberglass, and graphite are excluded. Synthetic fiber industry activities start with a synthetic, long- chain polymer and terminate with the formation of a marketable filament or threadlike material. The major raw material for the synthetic fiber industry is bulk polymer obtained from the plastics and resins industry. For descriptive purposes it was assumed that the polymer is received by the synthetic fiber industry in the form of polymer chips. In actuality, however, some processes use molten or dissolved polymer directly from the polymerization vessel. The processes involved in the manufacture of synthetic fibers are melt spinning, dry-spinning, wet spinning, lubrication, drawing, and fiber modifi- cation. A flow diagram has been prepared which illustrates the sequence in which these processes are combined to produce a marketable product. The synthetic fiber industry employs 97,000 people in 149 plants. Most of the production is from a few large plants with capacities from 50 to 150 Gg x per year. There are many small specialty plants in which products are cap- (Z^-H*?*^Tj tively consumed. Capacities of these plants are from 0.5 to 5 Gg per year. Capacities are approximate because equipment may be used to produce more than one product and producers may shift product lines depending on market conditions. Synthetic fibers comprise about 43 percent of the total fiber production in the United States with 2700 Gg produced in 1975. Of this total more than 99 percent was either acrylic, nylon, olefin, or polyester. Production data for 1975 are summarized in Table 1. Of the 149 plants in operation on January 1, 1976, 85 are located in the states of North Carolina, South Carolina, Virginia, and Tennessee. Another 44 are located in seven adjoining mid-atlantic and southern states. The re- maining 20 are scattered throughout 11 states and Puerto Rico. Table C-2 in the appendix shows the number of plants in each state and the fiber pro- duced. Several of these plants are associated with polymerization processes in the plastics and resins industry or with downstream industries such as the textile or tire producing industries. Table 2 lists the ten largest producers and their major products. These ten companies account for 85 percent of the total production capacity. ------- Table 1. 1975 PRODUCTION OF SYNTHETIC FIBERS Fiber Polyester Nylon Acrylic Olefin Other TOTAL Production 1360 843 238 226 5 2672 , Gg (106lbs) (2995) (1857) ( 525) ( 497) ( ID (5885) Source: C & EN's Top 50 Chemical Products and Producers. Chemical and Engin- eering News, 54.09): 33-39, May 3, 1976. Production Fell, Often Sharply, Last Year for Almost All Major Chemi- cal Products. Chemical and Engineering News, 54J24): 35, June 7, 1976. Table 2. TEN LARGEST SYNTHETIC FIBER PRODUCERS Producer Acrylic Major Products Nylon Olefin Polyester Akzona, Inc. Allied Chemical Corporation American Cyanamid Company x American Hoechst Corporation Celanese Corporation Dow Badische Company x E. I. duPont de Nemours & Co., Inc. x Eastman Kodak Company x Monsanto Company x Phillips Petroleum Company x x x x x x x x x x x x x x x x x x Source: Directory of Chemical Producers, 1976. ------- A decline in production of synthetic fibers started in 1973 and resulted in substantial losses for fiber producers during 1975. Despite increased fiber demand production dropped to only 72 percent of existing capacity^be- cause of stocks accumulated by textile companies as a hedge against antici- pated shortages and price rises. Price increases in raw materials and util- ities also affected producers, and many smaller companies were forced out of business. However, by late 1975 production was almost back to full capacity and the outlook for 1976 is optimistic, especially for polyester. Plant capacities are expected to increase 22 percent to 4200 Gg by 1980, although growth rates of per capita fiber consumption are expected to taper off. Fiber demand is closely tied to a variety of complex market conditions such as disposable income levels (apparel), housing starts (home furnishings) and automobile sales (tire cord). Thus, the major influences on future fiber growth are population increases and continued replacement of natural and cell- ulosic fibers. Energy requirements for the synthetic fibers industry for 1971 are summarized in Table 3. Table 3. FUELS & ELECTRICAL ENERGY CONSUMED BY COMPANIES IN SIC CODE 2824 in 1971 Purchased fuels Coal (Gg) 2883 Fuel Oil (Mm3) 702 Natural Gas (Gm3) 1160 Purchased Electrical Energy (GWh) 4843 Generated Electrical Energy (GWh) 1528 Total Energy Consumed (TWh equiv.) 43.4 Source: U. S. Bureau of Census. Census of Manufacturers, 1972. Industries Series: Plastics Materials, Synthetic Rubber, and Man-made Fibers. MC72(2)-28B. Washington, D. C., GPO, 1974. Raw Materials Relatively pure materials are required in the fibers industry because of the deleterious effect of impurities on the properties of the fiber. The primary raw material used in the synthetic fiber industry is bulk polymer ob- tained either directly from the polymerization process or indirectly in the form of dried polymer chips. The polymers used and their chemical compositions are summarized in Table A-l in the appendix. Table 4 gives 1974 industry con- sumption figures for major raw materials. Many additives are blended with the polymer before fiber production. Examples are delustrants, pigments, dyeing assistants, dye receptors, optical brighteners, heat stabilizers, antioxidant stabilizers, and light stabilizers. Ordinarily, the total amount of additives does not exceed five percent. Mat- erials added to the fiber to enhance product utility include lubricating agents, ------- bacteriostats, humectants, anti-static agents, and other similar additives. Both organic solvents and aqueous solutions of inorganic salts are used in some processes. Tables A-2 and A-3 in the appendix list some of these raw materials. The synthetic fiber industry, like the plastics and resins industry, is dependent on basic petrochemicals as feedstocks for production. The major chemical feedstocks used directly to produce polymers for fiber raw materials are benzene, butadiene, ethylene, propylene, and xylene. The shortage of these raw materials has affected fiber producers in a variety of ways. At present, feedstocks seem ample to meet demand. Table 4. RAW MATERIAL CONSUMPTION FOR PRODUCTION OF SYNTHETIC FIBERS BY COMPANIES IN SIC CODE 2824 in 1971. Raw Material Consumption, Gg Acrylonitrile Acrylates and methacrylates Caprolactam Glycols 290 12 347 518 Source: U. S. Bureau of Census. Census of Manufacturers, 1972. Industries Series: Plastics Materials, Synthetic Rubber, and Man-made Fibers. MC72(2)-28B. Washington, D. C. , GPO, 1974. Products Synthetic fibers have been grouped into nine classes by the Federal Trade Commission. The accepted generic names for the synthetic fibers produced in the United States are acrylic, modacrylic, nylon, aramid, olefin, polyester, saran, spandex, and vinyon. Definitions of these classes are found in Table 5. Other fibers which are now being produced but have not yet been assigned generic names are fluorocarbon, polycarbonate, and novoloid (phenolic) fibers. Table B-l in Appendix B gives a complete product list and properties of major products are given in Table B-2. Fibers are generally marketed as yarn, staple, or tow. Other forms are monofi lament, split film, fiberfill, and nonwoven fabrics. The major uses of synthetic fibers are summarized in Table 6. Over 80 percent of the fiber used in home furnishings is for rugs, carpets, and carpet backing. Most of the re- mainder is used for draperies and upholstery. The major industrial use (70 percent) for synthetic fibers is for automobile tire cord. Other uses of syn- thetic fibers are automobile seat covers; belting; electrical wire insulation; hose; recreational surfaces (Astroturf); roofing; rope and twine; sewing thread; tents, parachutes, sails, etc.; tarp; and webbing for outdoor furniture. ------- Table 5. GENERIC NAMES OF SYNTHETIC FIBERS Generic Name Definition *Acrylic At least 85 percent acrylonitrile by weight *Modacrylic 35-85 percent acrylonitrile by weight *Nylon Polyamide with less than 85 percent of the amide linkages attached to two aromatic rings. Aramid Polyamide with at least 85 percent of amide linkages attached to two aromatic rings. *01efin At least 85 percent ethylene, propylene, or other olefin units by weight. *Polyester At least 85 percent by weight of an ester of a substituted aromatic carboxylic acid, including but not limited to the ester of a dihydric alcohol and terephthalic acid. Saran At least 80 percent vinylidene chloride by weight. Spandex At least 85 percent of a segmented polyurethane. Vinyon At least 85 percent vinyl chloride * These classes account for 99 percent of production. Table 6. END USES OF SYNTHETIC FIBERS, 19731 CONSUMPTION (Gg) Home Industrial Apparel Furnishings & Other Total Acrylic and Modacrylic Nylon Olefin2 Polyester TOTAL 165 192 < 1 898 1255 84 356 121 234 795 5 205 49 280 539 254 753 170 1412 2589 Includes imports 21972 figures Sources: Harper, C. A. Handbook of Plastics and Elastomers. N.Y., McGraw-Hill, 1975. Wallace, P. T. Fibers-Introduction, and Fibers-Synthetic. In: Chemical and Economics Handbook. Menlo Park, California, Stanford Research Inst., August and December 1974, 541.1000A-541 1000K; 543.1000-543.1400E; 543.3521J. ------- Companies As of 1 January 1976 there were 61 companies which comprised the synthetic fibers industry. The companies operated 149 plants in 22 states and Puerto Rico. Table 7 lists the 10 largest companies and the production capacity of each along with the combined capacity of the other 51 companies. A complete listing of all plants, by company, is given in Appendix C. Production capa- cities were not available for some plants which produce low-volume specialty items. As is evident from the company list, many of the fiber producers are also major synthetic polymer producers. Fiber plants are generally not loca- ted near polymer plants although the trend in newer plants is toward integra- tion of these two industries. Table 7. CAPACITY OF TEN LARGEST SYNTHETIC FIBER PRODUCERS Company E. I. duPont de Nemours & Co., Inc. Celanese Corporation Monsanto Company Eastman Kodak Company Akzona, Inc. Allied Chemical Corporation American Hoechst Corporation Dow Badische Company Phillips Petroleum Company American Cyanamid Company All Others Number of Plants 16 5 9 3 5 4 2 2 3 2 98 149 Capacity (Gg/yr) >1169 (1387)* 382 > 373 (433)* 195 (308)* 135 129 (143)* 116 (127)* 100 91 80 506 3276 (3748)* *Planned increases for 1976 Environmental Impact Relatively little data were available on the environmental impact of the synthetic fibers industry. It can be assumed that the industry produces all three types of waste (gaseous, solid, and liquid) in varying degrees. Aqueous emissions appear to represent the largest potential source of pollution. ------- In general, the polymer raw materials are not toxic or otherwise hazard- ous unless heated to temperatures at which decomposition can occur. Emissions from the fiber industry usually arise from mechanical treatment of the polymer or are associated with solvents, additives, lubricants, or finishes used in processing. Companies which use integrated polymerization spinning systems produce waste which contains unreacted monomer. The major sources of gaseous emissions are from cooling chambers, con- ditioning chamber^.^l^ntYemQval chambers, and from solvent make-up. The use~bTTiof^solvents in several processes results in the entrainment of solvent by the fibers. Solvent may be subsequently emitted as vapor during processes such as drawing or heat-setting. "~" ' Particulate emissions of the solid polymer are possible from most of the processes but primarily from the Quitting, winding, crimping., and baling pro- cess steps. Other solid wastes resuTt from disposal of sub-standard material, filter solids, and water treatment sludge. Some four percent of fiber pro- duced is of sub-standard quality. This waste fiber may be buried, incinerated, reprocessed, or sold depending on supply and demand, __. Liquid emissions generally are termed "spin-finish wastes." Included in this category are water used for purging the spinning baths and washing the filaments, lubricants used in finish applications, and solvent wastes from dry and wet spinning. Other liquid effluents arise from wash water in filtration steps, solvent spills, and drawing baths. Periodic cleaning of process equipment also contributes significantly to the total wastewater load. Sanitary wastes resulting from the large number of people employed at fiber plants are a significant portion of the total effluent load. Cool- ing water blowdown also contributes to the liquid effluent from melt spinn- ing. Wastewater emissions from some operations have been classified according to waste load and treatability. This information is summarized in Table 8. Analysis of samples from a settling pond at an acrylic fibers production facility indicated the presence of acrylonitrile (100 mg/A), 2,3-dibromo-l- propanol (0.5 mgl/£), an isomer of dibromopropene, and 2,4-dimethyldiphenyl- sulfone. Table 8. SUMMARY OF WASTEWATER DATA FOR SELECTED FIBERS Fiber Nylon Olefin1 Spandex Wastewater Loading (mVkkg) 1.3-30.9 8.3-14.2 - Raw Waste Loads (kg/kkg) BOD5 COD SS 0.1-60 0.2-90 0.1-6 0.4-1.1 1.8-2.6 0.2-2.2 20Z 402 polypropylene Estimated ------- EPA Source Classification Codes for the synthetic fibers industry are summarized in Table 9. Table 9. SOURCE CLASSIFICATION CODES FOR SYNTHETIC FIBERS Operation Code Nylon General 3-01-024-01 Dacron General 3-01-024-01 Orion 3-01-024-03 Elastic 3-01-024-04 Teflon 3-01-024-05 Polyester 3-01-024-06 Nomex 3-01-024-08 Acrylic 3-01-024-12 Tynex 3-01-024-12 Olefins 3-01-024-14 Others 3-01-024-99 ------- Bibliography (1) American Home Economics Association. Textile Handbook, 4th Ed. Washington, D. C., 1970. (2) Billmeyer, F. W., Jr. Fiber Technology. In: Textbook of Polymer Science. N. Y., Interscience Publishers, 1962. (3) C&EN's Top 50 Chemical Products and Producers. Chemical and Engineering News, 54(19):33-39, May 3, 1976. (4) Directory of Chemical Producers - U.S.A. Chemical Information Services, Menlo Park, California, Stanford Research Institute, 1976. (5) Environmental Protection Agency, Effluent Guidelines Division. Develop- ment Document for Effluent Limitations Guidelines and New Source Per- formance Standards for the Synthetic Polymers Segment of the Plastics and Synthetic Materials Manufacturing Point Source Category. EPA 440/1- 75/036-b. Washington, D. C., Jan. 1975. (6) Environmental Protection Agency, (Office of Air and Water Program, Eff- luent Guidelines Div.). Development Document for Effluent Limitations Guidelines and New Source Performance Standards for the Synthetic Resins Segment of the Plastics and Synthetic Materials Manufacturing Point Source Category. (7) Federal Energy Administration, Office of Economic Empact. Report to Congress on Petrochemicals. Public Law 93-275, Section 23, GPO, 1974. (8) Fiber Makers Took a Beating in 1975. Chemical and Engineering News, 54_(6):12, Feb. 9, 1976. (9) Harper, C. A. Handbook of Plastics and Elastomers. N.Y., McGraw-Hill, 1975. (10) Man-Made Fiber Producers' Directory. Textile Organon, 65_(9), 1974. (11) 1975 Man-Made Fiber Deskbook. Modern Textiles 1975 (March), 17. (12) Polyester Raw Materials Allow Fiber Growth. Chemical and Engineering News, 53J39): 11-13, Sept. 29, 1975. (13) Production Fell, Often Sharply, Last Year for Almost All Major Chemical Products. Chemical and Engineering News, 54_(24):35-38, June 7, 1976. (14) Recession Clamped a Lid on Growth in Chemical Output Last Year, With Production Down for Many Major Products. Chemical and Engineering News, 53_(22):31-38, June 2, 1975. (15) Sorenson, W. R. and T. W. Campbell. Preparative Methods of Polymer Chemistry, 2nd Ed. N.Y., Interscience Publishers, 1968. ------- (16) Stanford Research Institute. 1975 Directory of Chemical Producers, U.S.A. Menlo Park, California, 1975. (17) U. S. Bureau of Census. Census of Manufacturers, 1972, Industry Series: Plastics Materials, Synthetic Rubber, and Man-Made Fibers. MC72(2)-28B. Washington, D. C., 6PO, 1974. (18) U. S. Makes World's Lowest-Cost Fibers. Chemical and Engineering News, 53(48), 10-11, Dec. 1, 1975. (19) Wallace, P. T. Fibers-Introduction, and Fibers-Synthetic. In: Chemi- cal and Economics Handbook. Menlo Park, California, Stanford Research Inst., August and December 1974, 541.1000A-541.1000K: 543.1000-543.1400E; 543.3521J. (20) Work, R. W. Man-Made Textile Fibers. In: Riegel's Handbook of In- dustrial Chemistry, 7th Ed. J. A. Kent, ed. N.Y., Van Nostrand Rein- hold, 1974. 10 ------- INDUSTRY ANALYSIS Data for the analysis of the fiber industry are presented in six process modules. There are three processes describing filament formation and three which describe fiber treatment. Variations on these processes occur both in order of processing and in operating conditions. The processes are presented graphically in Figure 1. They have been numbered consecutively from 1 to 6. The numbers assigned to the modules on the flow sheet correspond to process description numbers. Some data were available on operating parameters for the spinning and drawing processes, but not for all fibers. Waste stream data were available mainly in the form of general comments about the production of a particular fiber. Data on utilities were unavailable. The data given should be viewed as being generally representative of industry and not descriptive of the var- iation in waste management practices from company to company. Synthetic Fiber Processing Synthetic fibers are formed by three different processes: melt spinning (Process No. 1), wet spinning (Process No. 2), and dry spinning (Process No. 3). The choice of method depends primarily on several simple polymer characteris- tics such as melting point, melt stability, and solubility in organic solvents. The spinning processes accomplish the extrusion of the polymer in liquid form through fine orifices called spinnerets. The processes differ in the manner in which the polymer is liquefied, which in turn determines the manner in which the extruded filaments are solidified. Melt spinning uses heat to melt the polymer and then uses cool air to solidify the extruded liquid stream. In dry spinning, solidification of the fiber occurs by evaporation of the solvent used to dissolve and extrude the polymer. In wet spinning, the liquid polymer is spun (extruded) into a liquid coagulating bath. The essential feature of this process is the mass transfer of the organic solvent or inorganic salt solution from the polymer to the co- agulating bath. The fiber thus formed can be wound on a bobbin at either constant speed or constant tension to give "continuous filament yarn" or it can be cut into small pieces called "staple" which may be processed into bundles called "tow." The yarn, staple, or tow must be lubricated (Process No. 4) to reduce the friction encountered in the processing machinery and to reduce the static electric charge on the fiber. The lubricated fiber is then drawn (Process No. 5) to give orientation and increase strength and modified (Process No. 6) by a variety of process steps to give a finished product. 11 ------- STEAM AIR ro itasm O GASEOUS EMISSIONS QSOUO EMISSIONS £ UQUB EMISSIONS FIGURE 1. SYNTHETIC RBER INDUSTRY FLOW DIAGRAM ------- SYNTHETIC FIBERS PROCESS NO. 1 Melt Spinning 1. Function - Melt spinning is used to convert polymer chips into synthetic fibers called filaments. This process is used for polymers which can be melted under reasonable conditions without degradation of the polymer and thus is used mainly for the production of nylon, polyester, olefin, and saran filaments. The polymer chips can be melted in a variety of ways. The trend is towards extrusion of the polymer chips in an electrically heated screw extruder. The molten polymer is processed in a nitrogen atmosphere and metered through an accurately machined gear pump to a filter assembly consisting of either a series of metal gauzes or layers of graded sand. The filtered molten polymer is then extruded at a constant rate, under high pressure, through a nickel or stainless steel spinneret. The extruded liquid polymer streams are cooled using an air stream and the solid filaments thus formed converge at a guide to give a "spun yarn." For fibers such as nylon 66 the filaments pass through a steam conditioning tube before converging. After the fiber is converged it is given further treatments which are dictated by the end use. These treatments probably include drawing and lub- rication. Crimping, heat-setting, winding, cutting, or twisting may also be done. 2. Input Materials - The polymers treated in melt spinning and their chem- ical composition are summarized in Table 10. Table 10. INPUT POLYMERS FOR MELT SPINNING Fiber Generic Type Input Polymer Nylon 66 Nylon 6 Nylon 610 Dacron Kodel Nylon Nylon Nylon Polyester Polyester Polypropylene Olefin Polyethylene Olefin Saran Saran Poly(hexamethylene adipamide) Polycaprolactam Poly(hexamethylene sebacamide) Poly(ethylene terephthai ate) Poly(l,4 dimethyl dicyclohexyl terephthai ate) Polypropylene Polyethylene Poly(vinylidene chloride) The input polymer may contain other copolymers, dyes, or additives as listed in Table A-2 in the appendix. Other input materials in the process include air, nitrogen and steam. 13 ------- 3. Operating Parameters - Operating parameters for the melt spin processing of major fibers are given in Table 11. Table 11. TYPICAL MELT SPINNING OPERATING PARAMETERS Fiber Nylon Polyester Olefin Saran Spin Temperature (°C) 270-290 280-300 250-360 175 Pressure (MPa) - 7-35 - - Spinneret Hole Diam. (urn) 200-300 - >100 - Spin Speed (m/min) 600-1200 500-1000 - - 4. Utility Requirements - Quantitative data were not found in the sources consulted for this study. 5. Waste Streams - Gaseous emissions resulting from the use of air to solid- ify the filament and steam to condition nylon could contain unreacted monomer or other volatile hydrocarbon species. Solid wastes resulting from filtering the molten polymer are disposed of by landfill. Water used for rinsing the spinneret and other process equipment contributes to the spin-finish wastes which have high BOD and oil and grease contents. Large quantities of water are used for cooling and air conditioning. Liquid effluents arise from cool- ing tower blowdown. 6- EPA Source Classification Code - See industry description. 7. References - (1) Billmeyer, F. W., Jr. Textbook of Polymer Science, 2nd Ed. N.Y., Wiley, 1971. (2) Environmental Progection Agency, (Office of Air and Water Programs, Effluent Guidelines Div.). Development Document for Effluent Limitations Guidelines and New Source Performance Standards for the Synthetic Resins Segment of the Plastics and Synthetic Materials Manufacturing Point Source Category. EPA 440/1-74-010-a. Washington, D. C., 1974. (3) Environmental Protection Agency, Effluent Guidelines Division. Development Document for Effluent Limitations Guidelines and New Source Performance Standards for the Synthetic Polymers Segment of the Plastics and Synthetic Materials Manufacturing Point Source Category. EPA 440/1-75/036-b. Washington, D. C., Jan. 1975. (4) Erlich, Victor L. Olefin Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 9. H. F. Mark, ed. N.Y., Wiley, 1968, p. 403-40. 14 ------- (5) Farrow, G. and E. S. Hill. Polyester Fibers. In: Kirk-Othmer Encyclopedia of Chemical Technology, 2nd Ed., Vol 16. Anthony Standen, ed. N.Y., Wiley, 1968, p. 143-158. (6) Farrow, G., et al. Polyester Fibers. In: Encyclopedia of Poly- mer Science and Technology, Vol 11. H. F. Mark, ed. N.Y., Wiley, 1969, p. 1-41. (7) Lewis, P. F. Polyolefin Fibers. In: Chemical and Economics Hand- book, Menlo-Park, California, Stanford Research Institute, July 1969, 543.5520F. (8) Mark, H. F., S. M. Atlas and E. Cernia, eds. Man-Made Fibers, Science and Technology, Vol 1. N.Y., Wiley Interscience, 1967. (9) Mark, H. F., S. M. Atlas and E. Cernia, eds. Man-Made Fibers, Science and Technology, Vol 2. N. Y., Wiley Interscience, 1968. (10) Mclntyre, J. E. Man-Made Fibers, Manufacture. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed. N.Y., Wiley, 1968, p. 374-404. (11) Repka, Benjamin C., Jr. Olefin Polymers. In: Kirk-Othmer Encyclo- pedia of Chemical Technology, 2nd Ed., Vol 16. Anthony Standen, ed. N.Y., Wiley, 1968, p. 217-309. (12) Snider, 0. E. and R. J. Richardson. Polyamides (Fibers). In: Kirk- Othmer Encyclopedia of Chemical Technology, 2nd Ed., Vol 16. Anthony Standen, ed. N.Y., Wiley, 1968, p. 46-87. (13) Snider, 0. E. and J. Richardson. Polyamide Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 10. H. F. Mark, ed. N.Y., Wiley, 1969, p. 347-460. (14) Wallace, P. T. Nylon Fibers. In: Chemical and Economics Handbook. Menlo Park, California, Stanford Research Institute, April 1973, 453.4122E-F. (15) Wallace, P. T. Polyester Fibers. In: Chemical and Economics Handbook. Menlo Park, California, Stanford Research Institute, October 1974, 543.482E-F. (16) Work, R. W. Man-Made Textile Fibers. In: ReigeTs Handbook of Industrial Chemistry, 7th Ed. J. A. Kent, ed. N.Y., Van Nostrand Reinhold, 1974, p. 323-330. 15 ------- SYNTHETIC FIBERS PROCESS NO. 2 Wet Spinning 1. Function - Wet spinning is also used to produce filaments from polymer chips. This process is used for polymers which can be dissolved in solvents. Wet spinning requires slower spinning speeds than either melt or dry spinning. This production method is usually reserved for the manufacture of heavy tow, which also requires slow speeds for downstream processing steps. This method is used primarily to produce acrylic, modacrylic and spandex tow. Equipment required for wet spinning includes a solution vessel, a metering pump, a filter, a spinneret, and a coagulant tank. Products which require "aging" of the polymer solution before spinning employ a holding tank and all processes include a recovery system to separate the coagulant and solvent. As in melt spinning, the extruded filaments are further processed in a variety of ways depending on end use. Wet spinning requires a washing step immediately after extrusion to remove solvent and other impurities. This wash- ing step can occur either continuously or by a batch method. 2. Input Materials - The main input materials include polymer, solvent, and coagulant. Some examples are summarized in Table 12. Although water is gen- erally used to clean the fibers, aqueous ammonia is sometimes used for fil- aments spun from inorganic salt solutions. Table 12. INPUT MATERIALS FOR WET-SPINNING Fiber Acryl i c Polymer Polyacrylonitrile Solvent Dime thy! ace tamide Coagulant Aqueous DMAc (DMAc) Aqueous ZnCl2 Aqueous Zn€l2 Aqueous NaSCN Aqueous NaSCN Modacrylic Polyacrylonitrile- poly(vinyl chloride) Acetonitrile Aqueous Acetonitrile copolymer . . .. ^ v Acetone Water Spandex Polyurethane Dimethylformamide Water (DMF) 16 ------- 3- Operating Parameters - The important variables affecting fiber properties are concentration and temperature of the polymer solution (dope) and spin-bath composition, concentration, and temperature. The values for these variables differ from fiber to fiber and solvent to solvent but should be within the range given below. Spinneret: Coagulate Bath Temperature: Concentration of Polymer: Mind-Up Speed: Spinning Speeds: Spin Temperature: 1,000 to 12,000 holes, 50 to 100 ym diameter. May be made of platinum or tantalum if corrosive liquids are used. -15 to 10°C 10 to 30 % 15 to 60 m/min 50 to 100 m/min 0 to 200°C Specific operating parameters for wet-spinning of some acrylic fibers are summarized in Table 13. Table 13. OPERATING SUMMARY OF PARAMETERS FOR PRODUCTION OF ACRYLIC FIBERS BY WET SPINNING Fiber Producer Polymer Solvent Concentration Composition (wt. %) Coagulent Bath Temp. Composition (°C) (wt %) Acrilan- 16 Acrilan-1656 Creslan Creslan Zefran Zefran Zefran 61 58 Monsanto Monsanto American Cyanamid ^American Cyanamid Dow Badische Dow Badische Dow Badische DMAc DMAc 45-50% 45-50% NaSCN NaSCN 60% ZnCl2 60% ZnCl2 54-60% ZnCl2 25 19 10 to 13 10 to 13 10 10 10 20 20 -5 -5 10 15 15 to to to to to to 32 +5 +5 25 30 30 45-65% DMAc 66% DMAc 10% NaSCN 10% NaSCN 43-47% ZnCl 32-39% ZnCl 32-39% ZnCl 2 2 2 4. Utilities - No data were found in the sources consulted for this study. 5- Waste Streams - Gaseous emissions may result from solvent evaporation. Solid wastes resulting from filtration of the polymer solution and from the solvent recovery unit may be incinerated or sent to landfill. Sub-standard fiber, often termed spinning waste, is also either incinerated or sent to landfill. Gaseous emissions are produced from polymer incineration. Liquid effluents are produced from cooling water discharge and blowdown and a once 17 ------- through cooling system with discharge to a storm sewer is employed at one plant. Regeneration wastes are generated by the deionizing unit used to pro- vide spin bath make-up water. The spin-finish waste includes water used to clean the fibers and rinse water used to clean out various pieces of equip- ment. A wet spinning process variation termed reaction or chemical spinning is employed by one company to produce spandex fiber. Effluent from fiber washing is a mixture of water, toluene, and ethylene/diamine. Toluene and water are separated in a continuous decanter. The waste water has a faint odor of toluene and is discharged to a municipal sewage system. The toluene is purified by distillation. Still bottoms are drummed and sent to landfill. Nitriles (acrylic fiber), cyanides (spandex fiber), vinyl chloride (modacrylic fiber), or thiocyanates could be present in waste waters from other processes. Wastes from the solvent purification and recycle process contains inorganic salts or organic solvents which contribute significantly to the total waste load. 6. EPA Source Classification Code - See Industry Description. 7. References - (1) Billmeyer, F. W., Jr. Fiber Technology. In: Textbook of Polymer Science. N.Y., Interscience Publishers, 1962, (2) Chaney, David W. Acrylic and Modacrylic Fibers. In: Kirk«0thmer Encyclopedia of Chemical Technology, 2nd Ed., Vol. I. Anthony Standen, ed. N,Y., Wiley, 1968, p. 313-338, (3) Davis, 0. W, and Paul Shapiro, Acrylic Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 1, H. F. Mark, ed. N.Y., Wiley, 1964, p. 342-73. (4) Environmental Protection Agency, Effluent Guidelines Division. De- velopment Document for Effluent Limitations Guidelines and New Source Performance Standards for the Synthetic Polymers Segment of the Plastics and Synthetic Materials Manufacturing Point Source Category. EPA 4407 1-75/036-b. Washington, D. C., Jan, 1975. (5) Kennedy, R, K. Modacrylic Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed. N.Y., Wiley, 1968, p. 812-39. (6) Mclntyre, J. E. Man-Made Fibers, Manufacture. In: Encyclopedia of Polymer Science and Technology, Vol 8, H. F, Mark, ed. N.Y., Wiley, , 1968, p. 374-404. (7) Wallace, P. T. Acrylic and Modacrylic Fibers. In: Chemical Economics Handbook. Menlo Park, California, Stanford Research Institute, October 1975. (8) Work, R. W. Man-Made Textile Fibers. In: Reigel's Handbook of Indus- trial Chemistry, 7th Ed. J. A. Kent, ed. N.Y., Van Nostrand Reinhold, 1974, p. 323-330. 18 ------- SYNTHETIC FIBERS PROCESS NO. 3 Dry Spinning 1. Function - Dry spinning is the third process used for converting polymer chips into filaments. A polymer solution is extruded into a zone of heated gas or vapor. The volatile solvent readily evaporates, leaving a solidified filament which is then further processed. This process is used for easily dissolved polymers such as acrylonitrile, poly(vinyl chloride), or polyure- thane. Dry spinning is generally used to make continuous filament yarn be- cause of the higher spinning speeds possible. The equipment used for dry spinning is the same as that used for wet spinning up to the spinneret. After leaving the spinneret the solution pass- es through a spinning cell which consists of a cabinet about 25 feet long. Hot, solvent-lean gas or vapor enters at one end and solvent-rich gas or va- por emerges from the other. The solidified filament is further treated by the processes listed in melt spinning. An efficient solvent recovery system is required. 2. Input Materials - The two major input materials, polymer and solvent, are summarized in Table 14 for the various fibers. Table 14. INPUT MATERIALS FOR DRY SPINNING Fi ber Acryl i c Modacryl i c Spandex Polymer Polyacrylonitrile Poly acrylonitrile/ poly (vinyl chloride) polyu re thane Solvent DMF, DMAc tetramethylene sulfone acetone DMF, DMAc The gas used to evaporate the solvent may be air, inert gas (nitrogen or carbon dioxide), superheated steam, or superheated solvent vapor. 3. Operating Parameters - The major operating parameters are summarized below: Spinneret: Gas temperature: 25 to 200 ym diameter holes 80 to 130°C for low boiling solvents 200 to 400°C for higher boiling solvents (DMF, DMAc) The cell walls may be heated to 500°C Polymer concentration: 10 to 30% Yarn wind-up speed: 500 to 1200 m/min 19 ------- 4. Utilities - No data were found in the sources consulted for this study. 5. Haste Streams - Gaseous emissions probably include solvent vapors. Fil- tration of the polymer solution (dope) feed to spinning produces solid wastes which are either incinerated or sent to landfill. Liquid effluents include waste solution from the solution preparation step, waste from solvent purification and cooling water discharge. The waste stream from the solution preparation step is incinerated, while the waste from solvent purification and equipment washing is sent to biological treatment. Waste polymer and unrecovered solvent are termed "spinning wastes" and are either incinerated or added to the spin-finish waste stream. 6. EPA Source Classification Code - See Industry Description 7. References - (1) Billmeyer, F. W., Jr. Fiber Technology. In: Textbook of Polymer Science. N.Y., Interscience Publishers, 1962. (2) Chaney, David W. Acrylic and Modacrylic Fibers. In: Kirk-Othmer Encyclopedia of Chemical Technology, 2nd Ed., Vol. I. Anthony Standen, ed. N.Y., Wiley, 1968, p. 313-338. (3) Davis, C. W. and Paul Shapiro. Acrylic Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 1. H. F. Mark, ed. N.Y., Wiley, 1964, p. 342-73. (4) Environmental Protection Agency, Effluent Guidelines Division. Development Document for Effluent Limitations Guidelines and New Source Performance Standards for the Synthetic Polymers Segment of the Plastics and Synthetic Materials Manufacturing Point Source Category. EPA 440/1-75/036-b. Washington, D. C., Jan. 1975. (5) Environmental Protection Agency, (Office of Air and Water Program, Effluent Guidelines Div,). Development Document for Effluent Limita- tions Guidelines and New Source Performance Standards for the Synthe- tic Resins Segment of the Plastics and Synthetic Materials Manufactur- ing Point Source Category. EPA 440/1-74-010-a. Washington, D. C. 1974. (6) Kennedy, R. K. Modacrylic Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed. N.Y., Wiley, 1968, p. 812-39. (7) Mclntyre, J. E. Man-Made Fibers, Manufacture. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed, N.Y., Wiley, 1968, p. 374-404. (8) Wallace, P. T. Acrylic and Modacrylic Fibers. In: Chemical Econ- omics Handbook. Menlo Park, California, Stanford Research Institute, October 1975, 543.3522G. (9) Work, R. W. Man-Made Textile Fibers. In: Reigel's Handbook of Industrial Chemistry, 7th Ed. J. A. Kent, ed. N.Y., Van Nostrand Reinhold, 1974, p. 323-330. 20 ------- SYNTHETIC FIBERS PROCESS NO. 4 Lubrication 1. Function - The three main functions of lubrication (spin finishing) are surface lubrication, plasticizing action and static protection. The applica- tion of a lubricant immediately after filament formation improves subsequent handling and processing. For melt spun and dry spun yarns, the lubricant is applied before winding on a spin bobbin. In staple finishing the lubricant may be applied by pass- ing through a bath or by spraying. For wet spun fibers the lubricant is usually added after the cleaning step. Most applications occur at the spinning stage. The lubricant is contacted with the filament immediately after spinning by means of a ceramic wheel. An aqueous solution or emulsion of the lubricant is pumped to a holding or stor- age tank. From this tank, the lubricant is circulated into feeding trays where it contacts the ceramic applicator. 2. Input Materials - The input materials to the process are the spun filament from Process 1, 2, or 3, the antistatic lubricant, and water. Typical anti- static lubricants are polyoxyethylene attached to aliphatic hydrocarbon chains, long-chain alkyl quarternary ammonium salts, hydroxyalkylamine salts of long- chain fatty acids, high-boiling aliphatic esters, hydrocarbon oils, and fluid silicones. The lubricant is applied as a solution or emulsion in water. 3. Operating Parameters - Both the composition of the lubricant and the amount applied to the fiber depend on the chemical composition of the fiber and on the end use. The application is made at ambient pressure and temper- ature. The application speed is the same as the yarn wind-up speed. 4. Utilities - No data were found in the sources consulted for this study. 5. Waste Streams - Spent lubricant is the major contributor to spin-finish waste streams. Occasional cleaning of spin finish tanks also adds to the total plant waste load in the form of oil and grease. At one plant these waste streams are sent to municipal sewage treatment plants. In-plant biological treatment is employed at another plant. 6. EPA Source Classification Code - See Industry Description 7. References - (1) Billmeyer, F. W., Jr. Textbook of Polymer Science, 2nd Ed. N.Y.. Wiley, 1971. (2) Environmental Protection Agency, Effluent Guidelines Division. Development Document for Effluent Limitations Guidelines and New Source Performance Standards for the Synthetic Polymers Segment of the Plastics and Synthetic Materials Manufacturing Point Source Category. EPA 440/1-75/036-b. Washington, D. C., Jan. 1975. 21 ------- (3) Environmental Protection Agency, (Office of Air and Water Programs, Effluent Guidelines Div.). Development Document for Effluent Limit- ations Guidelines and New Source Performance Standards for the Syn- thetic Resins Segment of the Plastics and Synthetic Materials Manu- facturing Point Source Category. EPA 440/1-74-010-a. Washington, D. C., 1974. (4) Mclntyre, J. E. Man-Made Fibers, Manufacture. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed. N.Y., Wiley, 1968, p. 374-404. 22 ------- SYNTHETIC FIBERS PROCESS NO. 5 Drawing 1. Function - The function of drawing (stretching) is to introduce molecular orientation to the spun fiber and thus produce a stronger fiber. An optimum draw ratio exists for each type of fiber as shown in Table 15. Yarns and tows are drawn by stretching between two rolls, one to feed the undrawn yarn and the other, moving at a faster velocity, to collect the drawn yarn. The ratio of the surface speeds of the feed and draw rolls is defined as the draw ratio. Many fibers are drawn as an integral part of the spinning process. In other cases it is preferable to store the fibers or carry out some other oper- ation first. The drawing process may be aided by heating the fiber either through direct metal-to-fiber contact or by passing the fiber through a bath containing a heated plasticizing liguid or other solution. In these cases drawing may be combined with other processes such as cleaning or lubrication. The drawn fiber may be wound, cut into tow, or modified by further treatment depending on end use. 2. Input Materials - The input material is the lubricated fiber or tow from Process 4. Superheated steam, hot water, or hot inert liquids may be used depending on drawing arrangement. 3. Operating Parameters - The operating parameters are summarized in Table 15. Table 15. OPERATING PARAMETERS FOR SYNTHETIC FIBER DRAWING Fiber Modacrylic Acryl i c Polyester Nylon Polypropylene Polyethylene Draw Ratio - - 3 to 6 3 to 6 5 to 8 4 to 10 Draw Temperature (°C) - 70 to 110 75 to 100 15 100 to 120 - Percent Elongation 400 to 1400 300 to 1000 400 250 to 600 - - Yarn and tow are drawn at different speeds. Drawing speeds vary from 100 to 1500 m/min. 4. Utilities - No data were found in the sources consulted for this study. 5. Waste Streams - Possible emissions from drawing include vapors of solvents entrained in the fiber or waste liquids used in drawing baths. 23 ------- 6. EPA Source Classification Code - See Industry Description 7. References - (1) Billmeyer, F. W., Jr. Textbook of Polymer Science, 2nd Ed. N.Y., Wiley, 1971. (2) Davis, C. W. and Paul Shapiro. Acrylic Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 1. H. F. Mark, ed. N.Y., Wiley, 1964, p. 342-73. (3) Erlich, Victor L. Olefin Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 9. H. F. Mark, ed. N.Y., Wiley, 1968, p. 403-40. (4) Farrow, 6. and E. S. Hill. Polyester Fibers. In: Kirk-Othmer Encyclopedia of Chemical Technology, 2nd Ed., Vol 16. Anthony Standen, ed. N.Y., Wiley, 1968, p. 143-58. (5) Kennedy, R. K. Modacrylic Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed. N.Y., Wiley, 1968, p. 812-39. (6) Mark, H. F., S. M. Atlas and E. Cernia, eds. Man-Made Fibers, Science and Technology, Vol 2. N.Y., Wiley Interscience, 1968. (7) Snider, 0. E. and J. Richardson. Polyamide Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 10. H. F. Mark, ed. N.Y., Wiley, 1969, p. 347-460. 24 ------- SYNTHETIC FIBERS PROCESS NO. 6 Fiber Modifications 1. Function - The function of these process steps is to modify the fiber into a marketable product. Modifications include twisting to produce inter- filament cohesion, heat setting or heat relaxation to produce dimensional stability, crimping to add bulk and resilience, and cutting to produce staple products similar to natural fibers. Other processing steps such as dyeing; sizing; treating with water-repellant, fire-retardant, or other finishes; or blending different fibers may be done by the fiber manufacturer but are usually performed after manufacture and sale of the fiber. The procedure used by a particular plant to transform the drawn fiber into a marketable product depends on the end use. The following processing steps are those used most often. False-twist Texturing: This method of adding twist to yarns has replaced many of the other twisting procedures because of the high speed (300,000 to 700,000 rpm) of operation. In this procedure the yarn is heated close to the melting point, twisted to 28 to 40 turns per centimeter and then cooled and unwound. Heat Treating: Heat treating procedures are carried out by passing the fiber through an oven or over a heated roll. If the fiber is under tension, the procedure is called heat setting; if the procedure is carried out under little or no tension it is called heat relaxation. Heat setting procedures are often combined with texturizing process steps in order to "set" the crimp or twist. Crimping: Staple or yarn is crimped by mechanically distorting the fiber. Crimping may be done at various stages during fiber production but is usually done during or immediately after the drawing process. Crimping procedures include gear crimping, edge crimping, and stuffer-box crimping. Gear crimping is accomplished by passing the yarn through a pair of meshed gears. The permanency of the crimp depends on the yarn temper- ature during crimping and the setting temperature thereafter. In edge crimping the yarn is passed over a blunt knife edge. The distortions and strains which develop are retained by passing the yarn over a cooling roll. Stuffer-tube crimping of yarn or stuffer-box crimping of tow are accomplished by forcing the yarn into an electrically-heated, thermo- statically controlled tube or box. The yarn pushes up on a weighted in- sert which is free to rise and fall in the vessel. The crimped yarn is pulled from the tube at constant speed. The temperature of the oven and the yarn residence time control the amount of crimp. Cutting: Continuous filament or tow is chopped into staple using cutting machines. The fiber can be cut by rotating knives as it advances on roll- ers or it can be advanced by centrifugal force and cut by stationary knives as it advances. 25 ------- 2. Input Materials - Synthetic filament or tow is the only input material to this process. 3. Operating Parameters - Roller speeds approximate the speeds used in spinning and drawing. Heat setting temperatures are generally close to the melting point of the fiber. 4. Utilities - No data were found in the sources consulted for this study. 5. Waste Streams - Emissions from fiber modification processes are primarily particulate wastes resulting from physical manipulation of the fiber. Heat treatment of fibers could release gaseous emissions of entrained solvent. 6. EPA Source Classification Code - See Industry Description 7. References - (1) Kennedy, R. K. Modacrylic Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed. N.Y., Wiley, 1968, p. 812-39. (2) Mark, H. F., S. M. Atlas and E. Cernia, eds. Man-Made Fibers, Science and Technology, Vol 1. N.Y., Wiley Interscience, 1967. (3) Mclntyre, J. E. Man-Made Fibers, Manufacture. In: Encyclopedia of Polymer Science and Technology, Vol 8. H. F. Mark, ed. N.Y., Wiley, 1968, p. 374-404. (4) Snider, 0. E. and J. Richardson. Polyamide Fibers. In: Encyclopedia of Polymer Science and Technology, Vol 10. H. F. Mark, ed. N.Y., Wiley, 1969, p. 347-460. 26 ------- APPENDIX A RAW MATERIALS LISTS 27 ------- Table A-l. FIBER RAW MATERIALS Generic Name and Trade Name Polymer Raw Materials Acryli c ' Aramid1 Nomex Fiber B (Kevlar) Qi ana Tajmi r Fluorocarbon Modacrylic Nylon Nylon 62 Nylon 662 Nylon 610 Nylon 612 Olefin Polyester Dacron/Fortrel Kodel Saran1 Spandex1 Vinyon1 acrylonitrile with 7 to 8% neutral acrylate comonomers m-phenylene diamine and isophthaloyl chloride p-phenylene diamine and terephthaloyl chloride trans, trans-bis-(4 aminocyclohexyl)-methane and dodecanoic acid 2-pyrrolidone tetra fluoroethylene and fluorinated ethylene- propylene copolymers acrylonitrile and vinyl chloride or other comonomers hexamethylenediamine and adipic acid caprolactam hexamethylenediamine and sebacic acid hexamethylene diamine and dodecanoic acid ethylene, propylene, or other olefin dimethyl terephthalate or terephthalic acid and ethylene glycol dimethylterephthalate and 1, 4 cyclo hexylene diglycol vinylidene chloride and vinyl chloride diisocyanates, polyester, polyester glycols diamines vinyl chloride and vinyl acetate 1These fibers represent less than 2% of total fiber production 2Nylon 6 and 66 represent 99% of nylon production Sources: Wallace, P. T. Fibers - Introduction, and Fibers - Synthetic. In: Chemical and Economic Handbook. Menlo Park, California. Stanford Research Inst., August and December 1974, 541.1000A- 541.1000K; 543.1000-543.1400E; 543.3521J. 28 ------- Table A-2. TYPICAL ADDITIVES USED IN FIBER PRODUCTION Delustrants - Optical Brighteners - Antioxidant Stabilizers - Light Stabilizers - Dyeing assistants - Lucricants and Other Finishes - Usually titanium dioxide Stiblene Phenyl coumarin derivatives Alkylated phenols p-cresols mixed with sulfides Thio compounds such as dilauryl or distearyl thio dipropionate Long-chain alkyl benzophenones derivatives of hydroxy 2-methyl-5-vinyl pyridine 2-vinyl pyridine p-vinyl-benzene sulfonic acid Sulphocinamic acid Polyoxyethylene attached to aliphatic hydrocarbon chains Long-chain alkyl quartenary Hydroxyalkyl amine salts of Aliphatic esters Hydrocarbons Fluid silicones ammonium salts fatty acids 29 ------- Table A-3. SOLVENTS USED IN FIBER PRODUCTION Dimethyl acetanride Dimethyl formamide Acetonitrile Acetone Aqueous ZnCl2 Aqueous NaSCN Tetrarnethylene sulfone 30 ------- APPENDIX B PRODUCTS 31 ------- Table B-l. PRODUCTS OF THE SYNTHETIC FIBERS INDUSTRY Trademark A-Acrilan Acrilan Acrilan Plus Acrilan 2000+ Acttonwear Amco Polyethylene Amco Polypropylene American Polyethylene American Polypropylene Anso Anso-X Antron AstroTurf Autowine Avlin (fiber 200) Beaunit Nylon Beaunit Polyester Bi-Loft Blue "C" Cadon, C-Cadon Camalon Cantrece Caprolan Celanese Nylon Chadolene Chadolon Cordura Courtaulds Nylon Crepeset Crepeset Anti-Cling Creslan C-Cumuloft Cumuloft Generic Name acrylic acrylic acrylic acrylic nylon olefin olefin olefin olefin nylon nylon nylon nylon olefin polyester nylon polyester acrylic nylon, polyester nylon nylon nylon nylon, polyester nylon olefin nylon nylon nylon nylon nylon acrylic nylon nylon Producer Monsanto Monsanto Monsanto Monsanto Monsanto American Mfg. American Mfg. American Mfg. American Mfg. Allied Chemical Allied Chemical DuPont Monsanto Indian Head IMC- El Paso Natural Gas El Paso Natural Gas Monsanto Monsanto Monsanto Camac Corp. DuPont Allied Chemical Celanese Diversified Ind. Chadbourn Ind. DuPont Courtaulds Akzona Akzona American Cyanamid Monsanto Monsanto Types and Special Characteristics1 FST F (solution dyed) S F (solution dyed) F (producer-textured) M (incl. slit film) M (incl. slit film) M (incl. slit film) M (inc. slit film) F, S F, S FST Ribbon Slit Processed high modulus FS F (multibobal) , S FST S (bi-component) T FS F (multilobal) S F FM (bi-component) FMS F F (fibrillated) FM F F M (inherent crepe effect built in during manufac- ture) M (inherent crepe and anti-ding proper- ties built in dur- ing manufacture ST F (textured) F (textured) End-Use Areas2 AHI AH H H A I I I I H H AH I R AH HITC TCA A AHI, TC H AH A AHITC AHITC HIS A LI A A A AHI H H 32 ------- Table B-l. PRODUCTS OF THE SYNTHETIC FIBERS INDUSTRY (CONTINUED) Trademark Dacron DLP 17 Polyethylene DLP 21 Polyethylene DLP 31 Polyethylene DLP 40 Polypropylene DLP 47 Polypropylene DLP 50 Polypropylene DLP 57 Polypropylene DLP 61 Polypropylene DLP 70 Polypropylene DLP 77 Polypropylene DLP 90 Polypropylene DuPont nylon Ektafill Elura Encron Encron 8 Encron Golden Touch Encron Plyloc Enkaloft TWIX Generic Name polyester olefin olefin olefin olefin olefin olefin olefin olefin olefin olefin olefin nylon polyester modacrylic polyester polyester polyester polyester nylon Producer DuPont Thiokol Thiokol Thiokol Thiokol Thiokol Thiokol Thiokol Thiokol Thiokol Thiokol Thiokol DuPont Eastman Monsanto Akzona Akzona Akzona Akzona Akzona Types and Special Characteristics1 FST M (round shrinker yarn) M (round) M (ribbon) M (round & flat) M (round & flat) M (round & flat) M (round & flat) M (round, hi-tenacity M (ribbon) M (ribbon) F (round) FSTM S (fiberfill) T FS F (multilobal cross section, reduces sparkle in outer- wear fabrics) F (high filament count) F (producer-textured two-ply stretch) F (bulked, multilobal; End-Use Areas2 AHITC I I AHI HI HI HI HI I I HI HI AHITC H Wigs AHITC A A A H Enkaloft Stria nylon Enkaloft Super Bulk nylon Enkaloft TWIX nylon Enkalure nylon Enkalure II nylon Akzona Akzona Akzona Akzona Akzona space differential, normal, cationic, light dyeing types) S (crimpset or non- crimpset, normal ca- tionic, dyeing types) F (bulked, modified twist, plied; cation- ic and light dyeing types; random pattern effect) F (high bulk) F (bulked, modified twist, plied; cation- ic, light dyeing types; tweed pattern effect F (multilobal, delayed soiling) AH F (bulked, multilobal, soil hiding) S (multilobal), crimpset or non-crimpset) H H H 33 ------- Table B-l. PRODUCTS OF THE SYNTHETIC FIBERS INDUSTRY (CONTINUED) Trademark Enkalure III Enka Nylon Enka Polyester Enkasheer Esterweld Fib rl lawn Fib ri Ion Firestone nylon Firestone polyester FMC Vinyon Fortrel Fortrel 5 Fortrel 7 Fortrel PCP Glospan/Cleerspan Goldcres Goodyear Polyester Hamlon Hanover Nylon Hanover Polyester Herculon Herculon IV Hoechst Polyester Kevlar Kevlar 29 Kevlar 49 Kodel Kynar Kynol Lo-Pic Generic Name nylon nylon polyester nylon polyester olefin olefin nylon polyester vinyon polyester polyester polyester polyester spandex olefin polyester olefin nylon polyester olefin olefin polyester araraid aramid aramid polyester fluorocarbon novoloid olefin Producer Akzona Akzona Akzona Akzona American Cyanamide Fibron Fib r on Firestone Firestone IMC Cleanese Celanese Celanese Celanese Globe Shuford Mills Goodyear Tire ACS Industries Falk Fibers & Fabrics Falk Fibers & Fabrics Hercules Hercules Amer. Hoechst DuPont DuPont DuPont Eastman Monofilaments Carborundum Fibron Types and Special End-Use Characteristics1 Areas2 F (inherent anti-ding properties built in during manufacture) MFS (type 6.) FS M (producer modified torque yarn) F (treated) F (fibrillated) F (fibrillated) MF F F or S (modified) FST F T S (producer-colored) F (fused) M (flat) F (fibrillated) F F MF MF F (bulked) FST FS SF (high tenacity, low pilling for cotton, woolen & worsted systems) F F F FS (several types avail- able) M S M (flat) A AHITC AHITC A I H, I HI ITC TCI AH AHITC A AH H AHI AHI AHI TC HI AI AHI AHI H AHI TC I I AHI I AHI HI 34 ------- Table B-l. PRODUCTS OF THE SYNTHETIC FIBERS INDUSTRY (CONTINUED) trademark Lycra Marvess Marvess III Marvess CG Mont re 1 Monvelle Multisheer MX6020 MX6020-H MX108 Newton Polyester NM1000 NM1103 NM1200 NM1400 NM1500 Nomex Numa Nylon by Amtech Nypel Halar Nypel Nylon Nypel Polyester Nypel Polypro Olefin Olefin Oletex Orion Parapro Pat Ion PE3100 Phillips 66 Nylon PolarGuard • Polycarbonate Polyester Generic Name spandex olefin olefin olefin olefin biconstituent nylon/ spandex nylon polyester polyester nylon polyester nylon nylon nylon nylon nylon aramld spandex nylon fluoro carbon nylon polyester olefin olefin olefin olefin acrylic, modacryllc olefia olefin polyester nylon polyester polycarbonate polyester Producer DuPont Phillips Phillips Phillips Wellington Monsanto Akzona Shakespeare Shakespeare Shakespeare Albany Inter. Monofilaments Monofilaments Monofilaments Monofilaments Monofilaments DuPont Ameliotex Amtech Allied Chetn. Allied Chem- Allied Chem. Allied Chem. Waltrich Indian Head Poncar DuPont Wall Standard Oil Co. (Ind.) Monofilaments Phillips Celanese Corp. Monofilaments Inc. American Cyanamide Types and Special End-Use Characteristics1 Areas2 F FS F (BCF, modified cross- section, high luster, solution dyed.) S (heavy-denier sol. dyed) (low shrinkage, very high modulus) M,F F (stretch yarns) M-Round, reg. , med. & low shrink M-Round, hydrolysis re- sistant, Reg., med. & low shrink M-Round opaque, HM F M (clear melt-dyed) M (clear melt-dyed) M (clear melt-dyed) M (clear melt-dyed) M (clear melt-dyed) FS F M (round) M M M M M Slit-film, high mod. M ST F F M (clear melt-dyed) F F,T M F A AHI AH H HI A (Hosiery) A I I I I AHI AHI AHI AHI A AHI AHI I I I I I AHI I IR AH H H AHI AHI AI AI TC 35 ------- Table B-l. PRODUCTS OF THE SYNTHETIC FIBERS INDUSTRY (CONTINUED) Trademark Polyester by Amtech Polyethylene by Amtech Polyloom I Polyloom II Polypropylene by Amtech Polywrap Poncar Pro-Tuft Qlana Quintess Random-set Random-tone Ruvea S-3 Saran by Amtech SEF Shakespeare Nylon Shakespeare Polyester Shareen Shoeflex Shurti Sooflex Spectran Starbrite Strialine Stryton Synflex-N Synthetic Ind Tango Teflon Textura Travira TW 6208 Ty EZ Generic Name polyester olefin olefin olefin olefin olefin olefin olefin nylon polyester nylon nylon nylon nylon saran modacrylic nylon polyester nylon nylon olefin nylon polyester nylon polyester nylon nylon olefin nylon fluorocarbon polyester polyester olefin olefin Producer Amtech Amtech Standard Oil Co. (Calif.) Standard Oil Co. (Calif.) Amtech Indian Head Poncar Bemis DuPont Phillips Rohm and Haas Rohm and Haas DuPont Shakespeare Amtech Monsanto Shakespeare Shakespeare Court aulds Shakespeare Shuford Mills Shakespeare Monsanto Star Fibers Akzona Phillips Wall Industries Diversified Ind. Allied Chemical DuPont Rohm and Haas Amer. Hoechst Fib r on Indian Head Types and Special End-Use Characteristics1 Areas2 M (round) M (round) F (fibr illated) F (fibrillated) M (round and flat) Slit processed high modulus M P (ribbon) M F Twisted and heat-set Heat-set and dyed " M (ribbon) M (clear, melt-dyed) M (round and flat) S (flame retardant) M (round) M M, F M (clear, melt-dyed) F (fibrillated) M (clear, melt-dyad) S S F (thick & thin, color contrast dyeing) F (undulating variable cross-section) M Slit Film F FM Producer textured FS (high tenacity) F Slit processed high IH I HI HI IH R IR HIT AH AH H H AHI I IH AH I I A (Hosiery) I R I A AHI AH AH H IH A I A AHI R R modulus 36 ------- Table B-l. PRODUCTS OF THE SYNTHETIC FIBERS INDUSTRY (CONTINUED) Trademark Tytite Ultron Unifil Vectra Verel Voplex Voplex Vylor Wall Polypropylene Waltrich Polypropylene Wellene Wellon Wellstrand WSF PE WSF PP X-static Zefran Zefran Zefran Generic Name olefin nylon olefin olefin modacrylic olefin vinyon nylon olefin olefin polyester nylon nylon & polyester (heavy den.) olefin olefin nylon acrylic nylon polyester Producer Indian Head Monsanto Wall Vectra Eastman Voplex Voplex DuPont Wall Waltrich Wellman Wellman Wellman Wellington Wellington Rohm and Haas Dow Dow Dow Types and Special Characteristics1 Slit processed high modulus F M FS S (assorted types for specialized uses) M (round or flat polypropylene and polyethylene) M (flat) M M M and ribbon S S (monofil) M (round, high tenacity (slit film) M (round, high tenacity) (slit) F (fibrillated) F (anti-static modified) S (dyeable copolymer, producer - colored homopolymer) FS F End-Use Areas2 R A H AIH AHI I I I I IH HI AHI HI I I AH AHI AH A IType: M=monofilament: F=multifilament; S=staple fiber; T=tow. Identification of end-use areas: A»apparel; H»carpets, home furnishings; l«industrial fabrics: TC»tire cord: R=twine Source: Directory of Chemical Producers - U.S.A. Directory Information Services, Menlo Park, California, Stanford Research Institute, 1976. 1975 Man-made Fiber Deskbook. Modern Textiles 1975 (March), 17. 37 ------- Table B-2. CHEMICAL AND PHYSICAL PROPERTIES OF SOME TEXTILE FIBERS1 Fiber Acryl i c Acrilan Creslan Orion Modacryl i c Dynel Verel Nylon 6 regular monofi lament staple Nylon 66 regular monofi lament staple and tow Nomex Olefin Polypropylene- isotatic monofi lament staple and tow Polyesters, regular tenacity Avlin, staple Blue C, staple Dacron, staple Encron, filament Fortrel, staple Kodel, staple Quintess, staple Trevira, staple Vycron, staple Specific Gravity 1.17 1.18 1.16 1.3 1.33-1.37 1.14 1.14 1.14 1.14 1.38 0.9-0.91 0.9-0.91 1.38 1.39 1.38 1.38 1.38 1.38 1.38 1.38 1.38 Tenacity2 (grams per denier) 2-2.7 2-3 2.2-2.6 3.5-4.2 2-2.8 4-7 3.8-5.5 3-6 3.5-7.2 4-5.3 3.5-7 3-6.5 3.5-5 4.6 2.2-6 4.4-5 4.8 4.5-5.5 4.5-5.5 3.1-6.6 3.8-5.8 Tenacity (Wet)2 (grams per denier) 1.6-2.2 1.6-2.7 1.8-2.1 3.5-4.2 2-2.7 3.7-6.2 - 2.6-5.2 3-6.1 3-4.1 3.5-7 3-6.5 3.5-5 4.5 2.2-6 4.4-5 4.8 4.5-5.5 4.5-5.5 3.1-6.6 3.8-5.8 Moisture Regain (percent) 1.5 1-1.5 1.5 0.4 3-4.25 2.8-5 2.8-5 4.2-4.5 4.2-4.5 6.5 0.01-0.1 0.01-0.1 0.4 0.4 0.4-0.8 0.4 0.4 0.4 0.4 0.4 0.6 Extensibility3 (percent) 34-50 35-45 20-28 14-34 25-43 17-45 37-50 25-65 16-66 22-32 14-30 20-80 35-50 40-50 12-55 27-36 45-55 35-45 40-50 18-55 22-67 Elasticity1* (percent) 99(2) 89(5) 55-65(3) 40-60(5) - 100(2) 98(5) 88(4) 55(10) 99-100(2-100) 100(2) 100(5) 99-100(10) - - 98(5) 95(10) 97-100(2) 94-100(5) 90-95(2) 55-65(5) 92(2) 75(5) 100(1) 55-65(5) 75-80(5) 75-85(2) 35-45(5) 67-86(2) 57-74(5) 44(5) 33(10) ------- Table B-2. CHEMICAL AND PHYSICAL PROPERTIES OF SOME TEXTILE FIBERS1 (CONTINUED) CO Fiber Saran Spandex Fulflex Glospan Lycra Numa Unel Vyrene Fluorocarbon Teflon, staple Teflon, monofi lament Biconstituent Fiber Source-ACOOOl Specific Gravity 1.7 1.41 1.2 1.21 1.2 1.2 1.2 2.1 2.1 1.22 Tenacity2 (grams per denier up to 1.5 0.34 0.7 0.7-0.9 0.6-0.9 0.55-0.85 - 1.2-1.4 0.5 up to 9 Tenacity (Wet)2 (grams per denier up to 1.5 _ 0.6-0.9 - - - - 1.2-1.4 0.5 — Moisture Regain (percent) None <0.5 <1 1.3 1 1.3 0.3 _ - 2.7 Extensibility3 (percent) 15-25 600-625 600-700 444-555 500-600 500-700 650-700 15-33 52 45 maximum Elasticity1* (percent) - 97(50) 99(50) 98(200) 97(50) 98(300) 96-98.5(50) 98(600) _ - 100(4) Because natural fibers inevitably vary in properties and man-made fibers may be produced in various forms, values given should be interpreted as indicating order of magnitude of the fibers as used in textile applications. 2Tested at 21 °C (70°F) with relative humidity 65 percent. Percentage of elongation at 65 percent relative humidity. "Percentage of recovery from strain indicated. Source: American Home Economics Association. Textile Handbook, 4th Ed., Washington, D. C., 1970. ------- APPENDIX C PRODUCERS 41 ------- Table C-l. SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES Company ACS Industries Akzona Inc. American Enka Co., Div Albany International Corp. Albany Felt Co., Div. Newton Line Co., Inc. Allied Chem. Corp. Fibers Div. -pa ro Nypel, Inc., Subsid. Alrac Corp. Aroeliotex, Inc. American Cyanamid Co. Fibers Div. IRC Fibers Co. Subsid. American Hoechst Corp. Film Div. Hoechst Fibers Indust. Div. American Mfg. Co. Inc. St. Loin's Cordage Mills Div. AMTECH, Inc. Location Walthourville, Ga. Woonsocket, R.I. Central, S.C. Enka, N.C. Lowland, Tenn. Central, S.C. Lowland, Tenn. Homer, N.Y. Homer, N.Y. Homer, N.Y. Homer, N.Y. Chesterfield, Va. Irmo, S.C. Irmo, S.C. Moncure, N.C. West Conshohocken, Pa. Stamford, Conn. Rocky Hill, N.J. Milton, Fla. Painesville, Ohio Delaware City, Del. Spartanburg, S.C. Homesdale, PA St. Louis, MO Odenton, Md. Odenton, Md. Odenton, Md. Odenton, Md. Products5 Olefin (P) Olefin Nylon Nylon Nylon Polyester Polyester Fluorocarbon Nylon Polyester Olefin (E&P) Nylon Nylon Polyester Polyester Nylon Nylon Spandex Acrylic and modacrylic Polyester Polyester Polyester Olefin (E&P) Olefin (E&P) Nylon Olefin (E&P) Polyester Saran Form5 Capacity (Gg/Yr)1 Remarks Y,F Y,F Y.F.S Y.F.S Y,F,S Y,S Y,S F F F F Y.F.S Y.F.S Y.S Y,S F Y,S F S.T Y Y.F.S.T Y.F.S.T F,0 F,0 F F,0 F F na na 7 34 45 "I j na 1 <.5 na 59 45 9 Experimental Capacity 16 (14)2 na >1(23)2 Pilot <.5 57 23 2 114 (II)2 na na 5 na 0.5 na ------- Table C-l. SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES (CONTINUED) CO Company Arlln Mfg. Co., Inc. Benris Co., Inc. Berkley & Co., Inc. Camac Corp. The Carborundum Co. Polymers Venture Celanese Corp. Fiber Industries, Inc., Subsid. » Chadboum, Inc. Chadbourn Indus t. Div. Chadol Div. Columbian, Rope Co. The Cordage Group Div. Courtalds North America, Inc. Andrew Crowe & Sons, Inc. Crowe Rope Co. , Div. Deering Mil liken, Inc. Indust. Div. Dow Badische Co. Location Lowell, Mass. St. Louis, Mo. Talladega, Ala. Spirit Lake, Iowa Spirit Lake, Iowa Bristol , Va. Bristol, Va. Niagra Falls, N.Y. Greenville, S.C. Florence, S.C. Greenville, S.C. Salisbury, N.C. Shelby, N.C. Gainesville, Ga. Auburn, N.Y. LeMoyne, Ala. Warren, Me. Laurens, S.C. Laurens, S.C. Spartanburg, S.C. Williamsburg, Va. Anderson, S.C. Anderson, S.C. Products 5 Olefin (E&P) Olefin (P) Olefin (P) Olefin (E&P) Nylon Nylon Olefin Novoloid Nylon Polyester Polyester Polyester Polyester Nylon Olefin (E&P) Nylon Olefin (P) Nylon Olefin Olefin Acrylic and modacrylic Nylon Polyester Form5 F,0 F,0 F,0 F F Y Y.S Y,S,T Y,S,T Y.S.T Y.S.T Y,F F.O Y.F F F F S,T Y.S Y Capacity (Gg/Yr)1 Remarks na na na na Captive Use 0.5 5 na na 40 45 30 57 210 2 na 2 na 0.5 Captive Use na na 33 39 28 ------- Table C-l. SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES (CONTINUED) Company Diversified Indust. Inc. Synthetic Indust. Inc., Subsid. Tennessee Fibers, Subsid. E.I. duPont de Nemours & Co., Inc. Textile Fibers Dept. Plastic Products & Resins Dept. Eastman Kodak Co. Eastman Chem. Products, Inc., Subsid. Carolina Eastman Co. Div. Tennessee Eastman Co., Div. El Paso Natural Gas Co. Beaunit Corp., Subsid. Beaunit Fibers Div. Falk Fibers & Fabrics Inc. Hanover Mills, Inc., Subsid. Universal Polymer Products, Co. Subsid. FIBRON, Inc. The Firestone Tire & Rubber Co. Firestone Synthetic Fibers Co., Div. Location Chickamauga, Ga. Pecatur, Tenn. Camden, S.C. Waynesboro, Va. Richmond, Va. Richmond, Va. — Camden, S.C. Chattanooga, Tenn. Marti nsville, Va. Richmond, Va. Seaford, Del. Camden, S.C. Cape Fear, N.C. Chatanooga, Tenn. Kinston, N.C. Old Hickory, Tenn. Waynesboro, Va. Parkersburg, W. Va. Columbia, S.C. Kings port, Tenn. Elizabethton, Tenn. Etowah, Tenn. Elizabethton, Tenn. Yanceyville, N.C. Fuquay-Varina, N.C. Chatanooga, Tenn. Hopewell , Va. Products5 Olefin (P) Olefin (P) Acrylic and Modacrylic Acryl i c Flurocarbon - Arami d Nylon Nylon Nylon Nylon Nylon Polyester Polyester Polyester Polyester Polyester Spandex Nylon Polyester Polyester, Acrylic & Modacrylic Nylon Nylon Polyester Olefin (P) Nylon Polyester Olefin (P) Nylon Polyester Form5 0 0 S.T S,T Y.F.S.T Y.F.S.T Y,F,S.T Y.F.S.T Y.F.S.T Y,F,S,T V.S.T Y,S,T Y.S.T Y.S.T Y,S,T F F Y,S S S.T Y,S Y,T Y.F Y,F Y,F Y Capacity (Gg/Yr)1 na na Il38 J na , (23)2;) >450 (70)2 " 570 (115)2 . 5 11 Il77 (113)3 18 4 33 29 / A % O / «« *• \ Q (9)2 (27)3 2 5 na 25 14 Remarks Captive Use Captive Use Captive Use ------- Table C-l. SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES (CONTINUED) 01 Company FMC Corp. Chem. Group Fiber Div. FNT Indust. Inc. Georgia Synthetics, Inc. Globe Mfg. Co. The Goodyear Tire & Rubber Co. Chem. Div. Hercules Inc. Polymers Dept. Fibers Div. Film Div. Indian Head, Inc. Indian Head Yarn & Thread, Div. Kay ser- Roth Corp. Yarn Processing Div. Lambeth Corp. Clarence L. Meyer & Co. Meyers Fibers, Inc. Monofi laments, Inc. Location Front Royal, Va. Lew is town, Pa. Meadville, Pa. Menominee, Mich. Elberton, Ga. Fall River Mass. Gas torn' a, N.C. Point Pleasant, W. Va. Scottsboro, Ala. Covington, Va. Oxford, Ga. Covington, Va. Blue Mountain, Ala. Creedmoor, N.C. New Bedford, Mass. Ansonville, N.C. Waynes bo ro, Va. Waynesboro, Va. Waynes bo ro, Va. Products5 Polyester Polyester Vi nyon Olefin (E) Olefin (P) Spandex Spandex Polyester Olefin (P) Olefin (P) Olefin (P) Nylon Olefin (P) Polyester Nylon Polyester Polycarbonate Form5 Y,S Y,S S F 0 F F F.Y Y.S.T 0 0 Y,F F F F F Capacity (Gg/Yr)1 Remarks 1 20 23 2 na na 0.7 0.9 6.5 Captive Use 14 45" na na 5 Captive Use na 5 <.5 <.5 na ------- Table C-l. SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES (CONTINUED) en Company Monsanto Co. Monsanto Textiles Co. The Osterneck Co. . Phillips Petroleum Co. Phillips Fibers Corp., Subsid. Fibers International Corp., Subsid. PI atari 1 Co. Poncar Plastic Corp. Rohm and Haas Co. Rohm and Haas N.C. Inc., Subsid. Shakespeare Co. Monofi lament Oiv. Shuford Mills, Inc. Standard Oil Co. of California Chevron Chem. Co., Subsid. Location Decatur, Ala. Pensacola, Fla. Decatur, Ala. Greenwood, S.C. Pensacola, Fla. Sand Mountain Decatur, Ala. Sand Mountain, Ala. Lumberton, N.C. Rocky Mount, N.C. Spartanburg, S.C. Guayama, P.R. Guayama, P.R. Birdsboro, Pa. Mi ami , Fl a . Fayetteville, N.C. Fayetteville, N.C. Columbia, S.C. Columbia, S.C. Hickory, N.C. Dayton, Tenn. Products s Acrylic and Modacrylic Nylon-Spandex Nylon Nylon Nylon Nylon Polyester Polyester Olefin (P) Polyester Olefin (P) Nylon Polyester Nylon Olefin (P) Nylon Polyester Nylon Polyester Olefin (P) Olefin (P) Form5 SJ Y Y.F.S Y.F.S Y.F.S Y,F,S Y,S Y,S 0 Y Y,S,T Y Y F F Y,F,T Y,T F F F 0 Capacity (Gg/Yr)1 Remarks 120 (30)2 Bi constituent fiber, pilot 11 91 68 10 43 30 (30)2 Captive Use 23 25* 29 14 1 na 18 30 (3D)2 2 1 na «• *• 5* ------- Table C-l. SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES (CONTINUED) Company Standard 011 Co. (Indiana) Amoco Chems. Corp. Subsid. Amoco Fabrics Co., Subsid. Patchogue Plymouth Co. Div. Star Fibers, Inc. Texfl Indust., Inc. Texfi Yarn and Fibers Group Thiokol Corp. Fibers Div. Tubbs Cordage Co. Uni royal, Inc. Unlroyal Fiber & Textile Div. Voplex Corp. Canadaigua Plastics Div. Well Indust., Inc. Maltrich Plastic Corp. Wellington Computer Graphics, Inc. Wellington Synthetic Fibers, Inc. subsid._ Montair Div. Plastic Woven Products Div. Poly Fibers Div. Location Bainbridge Ga. Hazelhurst, Ga. Nashville, Ga. Edgefield, S.C. Asheboro, N.C. New Bern, N.C. Waynesboro, Va. Orange, Calif. Winnsboro, S.C. Winnsboro, S.C. Canadaigua, N.Y. Canadaigua, N.Y. Beverly, N.J. Tennet, N.J. Pilot Mountain, N.C. Lees vi lie, S.C. Trusville, Ala. Products b Olefin (P) Olefin (P) Olefin (P) Nylon Polyester Polyester Olefin (E&P) Olefin (P) Nylon Olefin Olefin (E&P) Vinyon Olefin (E&P) Olefin (P) Olefin (E&P) Olefin (P) Olefin (P) Form5 0 0 0 S Y Y Y,F,0 F F F.S F F F F F.O F F,0 Capacity (Gg/Yr)1 Remarks na 18" na 6 8 11 14" na <.5 9" na 0.5 na na na na na ------- Table C-l SYNTHETIC FIBER PRODUCERS, PLANT LOCATIONS, PRODUCTS, AND CAPACITIES (CONTINUED) Company Location Products5 Form5 Capacity (Gg/Yr)1 Remarks Wellman, Inc. Wellman Indust., Inc., Subsid. Man-Made Fiber Div. Johnsonville, S.C. Nylon S,T 14 Johnsonville, S.C. Polyester S,T 16 'On-line 1 January 1976 unless otherwise noted. Capacity data from 1976 Directory of Chemical Producers unless otherwise noted. 2Capacity increase scheduled in 1976 'Capacity increase under construction or planning ''Capacity data from 1975 Directory of Chemical Producers ABBREVIATIONS.: P-polypropylene, E-polyethylene, Y-yarn, F-filament, mono or raulti, S-staple, T-tow, 0-other, na-not available Sources: Man-Made Fiber Producers' Directory. Textile Organon, 65(9), 1974. Directory of Chemical Producers, 1976. oo ------- TABLE C-2 LOCATION OF U.S. SYNTHETIC FIBER PRODUCING PLANTS STATES AND AREA ACRYLIC New England Connecticut Maine Massachusetts Rhode Island Mid-Atlantic Del aware Maryl and New Jersey New York Pennsylvania Piedmont 3 N. Carolina S. Carolina 1 Virginia 2 W. Virginia South 3 Alabama 1 Florida 1 Georgia Tennessee 1 Puerto Rico Midwest & West California Iowa Michigan Missouri Ohio TOTAL 6 NYLON 1 1 5 1 1 1 2 23 4 11 7 1 13 3 2 1 6 1 1 1 43 OLEFIN 4 1 2 1 8 2 2 3 1 12 3 5 4 16 3 1 7 5 5 1 1 1 2 45 POLYESTER 4 1 1 1 1 28 11 11 4 2 9 3 5 1 1 1 42 OTHER 1 1 6 1 1 3 1 5 1 4 1 1 13 TOTAL 6 1 1 3 1 23 2 5 3 8 5 71 19 28 21 3 42 10 5 8 17 2 7 1 2 1 2 1 149 Sources: Textile Organon 1976 Ch. P.O. 49 ------- TECHNICAL REPORT DATA (Please read Inunctions on ilie reverse before completing} 1. REPORT NO. EPA-600/2-77-023k 2. 4. TITLE AND SUBTITLE Industrial Process Profiles for Environmental Use: Chapter 11. The Synthetic Fiber Industry 3. RECIPIENT'S ACCESSION-NO. 5. REPORT DATE February 1977 6. PERFORMING ORGANIZATION CODE 7. AUTHOR(S) Jerry L. Parr 8. PERFORMING ORGANIZATION REPORT NO. 9. PERFORMING ORGANIZATION NAME AND ADDRESS Radian Corporation 8500 Shoal Creek Boulevard P.O. Box 99U8 Austin, Texas 78766 10. PROGRAM ELEMENT NO. 1AB015 11. CONTRACT/GRANT NO. 68-02-1319, Task 31* 12. SPONSORING AGENCY NAME AND ADDRESS Industrial Environmental Research Laboratory Office of Research and Development U.S. ENVIRONMENTAL PROTECTION AGENCY Cincinnati. Ohio, 1*5268 13. TYPE OF REPORT AND PERIOD COVERED Initial: 8/75-11/76 14. SPONSORING AGENCY CODE EPA/600/12 15. SUPPLEMENTARY NOTES 16. ABSTRACT The catalog of Industrial Process Profiles for Environmental Use was developed as an aid in defining the environmental impacts of industrial activity in the United States. Entries for each industry are in consistent format and form separate chapters of the study. Synthetic fibers are defined as noncellulosic fiber of synthetic origin. The category includes manufactured fibers in which the fiber-forming substances is a Icng- chain, organic synthetic polymer. Cellulosic fibers such as rayon and acetate arid the inorganic fibers such as boron, fiberglass, and graphite are excluded. Syn- thetic fiber industry activities start with a synthetic, long-chain polymer and terminate with the formation of a marketable filament or thread-like material. One process flow sheet and six process descriptions have been prepared to characterize the industry. Three of the process descriptions are involved with filament formation and three describe fiber treatment. Within each process description available data have been presented on input materials, operating parameters, utility requirements and waste streams. Data related to the subject matter, including company and product data, are included as appendices. 17. KEY WORDS AND DOCUMENT ANALYSIS a. DESCRIPTORS Pollution Synthetic Fibers Organic Synthetic Polymer Polymerization Process Description 19. DISTRIBUTION STATEMENT Release to Public b.lDENTIFIERS/OPEN ENDED TERMS Air Pollution Control Water Pollution Control Solid Waste Control Textile Industry Synthetic Fibers 19. SECURITY CLASS (This Jit-port) Unclassified 20. SECURITY CLASS (Tins page) Unclassified 0. COSATI I ;iclii/Group 07C HE 13C 21. NO. OF RAGfcS 56 22. PRICE EPA Form 2220-1 (9-73) 50 iHJSGPO: 1978 — 757-086/0807 ------- |