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| ABS RESIN BY EMULSION/MASS POLYMERIZATION |
| ACETALDEHYDE FROM ETHYLENE BY ONE-STEP OXIDATION |
| ACETIC ACID FROM MEOH BY LOW PRESSURE CARBONYLATION, SUPPORTED Rh CATALYST |
| ACETIC ACID FROM MEOH BY THE BP CATIVA PROCESS |
| ACETIC ACID FROM MEOH BY THE CELANESE PROCESS |
| ACETIC ANHYDRIDE FROM ACETIC ACID VIA KETENE |
| ACETONE FROM ISOPROPANOL BY VAPOR PHASE DEHYDROGENATION |
| ACETYLENE FROM NATURAL GAS BY PARTIAL OXIDATION |
| ACRYLIC ACID (ESTER GRADE) BY NIPPON SHOKUBAI PROCESS |
| (METH)ACRYLIC RESIN PELLETS BY A CONTINUOUS BULK POLYMERIZATION PROCESS |
| ACRYLONITRILE FROM PROPYLENE BY AMMOXIDATION |
| ACRYLONITRILE, PROPANE-BASED (ASAHI PROCESS) |
| ACRYLONITRILE, PROPANE-BASED (MITSUBISHI PROCESS) |
| ACRYLONITRILE, PROPANE-BASED PROCESS USING ANTIMONY-BASED CATALYSTS(SOHIO CATALYST) |
| ACRYLONITRILE, PROPYLENE-BASED (SOHIO PROCESS) |
| ADIPIC ACID FROM BENZENE VIA CYCLOHEXANOL |
| ADIPIC ACID FROM CYCLOHEXANE |
| ADIPIC ACID FROM PHENOL VIA CYCLOHEXANOL |
| ALCOHOLS, PRIMARY LINEAR, C6-C20, BY ETHYLENE OLIGOMERIZATION |
| AMMONIA FROM NATURAL GAS BY STEAM REFORMING (ICI "AMV" PROCESS) |
| AMMONIA FROM NATURAL GAS BY STEAM REFORMING (ICI "LCA" PROCESS) |
| AMMONIA FROM NATURAL GAS BY STEAM REFORMING (M. W. KELLOGG'S IMPROVED PROCESS: KAAP-KRES) |
| AMMONIA FROM NATURAL GAS BY THE KBR PURIFIERPLUS PROCESS |
| AMMONIA FROM NATURAL GAS BY THE UDHE DUAL PRESSURE PROCESS |
| ANILINE FROM NITROBENZENE BY VAPOR-PHASE REDUCTION |
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| BENZENE REMOVAL BY HYDROISOMERIZATION OF C5-C6 NAPHTHA |
| BENZENE(MIXED XYLENES BY-PROD)FROM REFOR HEART CUT BY SULFOLANE EXTRACT.&DISTILL. |
| BIODIESEL FROM ALGAL OIL VIA ALKALINE CATALYSIS |
| BIODIESEL FROM REFINED VEGETABLE OIL VIA ALKALINE CATALYSIS |
| BIODIESEL FROM REFINED VEGETABLE OIL VIA CD PROCESS |
| BIODIESEL VIA HETEROGENGOUS CATALYSIS CATILIN PROCESS |
| BISPHENOL A FROM ACETONE AND PHENOL BY AN ION-EXCHANGE CATALYZED PROCESS |
| BITUMEN PRODUCTION VIA STEAM ASSISTED GRAVITY DRAINAGE (SAGD) |
| BITUMEN PRODUCTION VIA SURFACE MINING |
| BTX REFORMATE FROM NAPHTHA |
| N-BUTANOL AND 2-ETHYLHEXANOL FROM PROPYLENE VIA N-BUTYRALDEHYDE, Rh CATALYST |
| N-BUTYL ACRYLATE |
| N-BUTYRALDEHYDE FROM PROPYLENE (WATER-SOL Rh CATALYST) |
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| C3-C4 OLIGOMERIZATION |
| CAPROLACTAM FROM PHENOL BY THE HYDROXYLAMINE PHOSPHATE OXIME PROCESS |
| CARBON BLACK BY THE OIL-FURNACE PROCESS USING AIR AS THE OXIDANT GAS |
| CARBON BLACK BY THE OIL-FURNACE PROCESS USING OXYGEN AS THE OXIDANT GAS |
| CARBON MONOXIDE FROM SYNTHESIS GAS BY CRYOGENIC SEPARATION |
| CHLORINE (CAUSTIC SODA BY-PRODUCT) BY ELECTROLYSIS OF NaCl IN DIAPHRAGM CELLS |
| CUMENE FROM BENZENE AND PROPYLENE |
| CYCLOHEXANE FROM BENZENE BY HYDROGENATION |
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| DIAMMONIUM PHOSPHATE GRANULAR FERTILIZER (18-46-0) |
| DIESEL, FISCHER-TROPSCH FROM BIOMASS |
| DIMETHYL ETHER BY A SINGLE-STEP PROCESS |
| DIMETHYL ETHER FROM COAL VIA HALDOR TOPSOE PROCESS |
| DIMETHYL ETHER FROM COAL VIA JFE SLURRY PROCESS |
| DIMETHYL TEREPHTHALATE FROM P-XYLENE BY SUCCESSIVE OXIDATIONS AND ESTERIFICATIONS |
| DINITROTOLUENE FROM TOLUENE BY NITRATION |
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| EPDM RUBBER CONTAINING ETHYLIDENE NORBORNENE BY A GAS PHASE PROCESS |
| EPTA PRODUCTION BY A PROCESS SIMILAR TO EASTMAN CHEMICAL PROCESS |
| ETHANOL FROM BAGASSE |
| ETHANOL FROM CORN DRY MILL PROCESS |
| ETHANOL FROM CORN STOVER* |
| ETHANOL FROM ETHYLENE BY CATALYTIC HYDRATION |
| ETHANOL FROM SUGARCANE |
| ETHANOL FROM WHEAT STRAW* |
| ETHANOL VIA HYDRATION OF ETHYLENE |
| ETHANOLAMINES FROM AMMONIA AND ETHYLENE OXIDE, 20:1 MOLAR REACTOR FEED RATIO |
| ETHYLBENZENE FROM BENZENE BY LIQUID-PHASE ALKYLATION, AlCl3 CAT. |
| ETHYLBENZENE FROM BENZENE BY LIQUID-PHASE ALKYLATION, ZEOLITE CAT. |
| ETHYLBENZENE FROM BENZENE BY VAPOR-PHASE ALKYLATION |
| ETHYLENE DICHLORIDE BY DIRECT CHLORINATION: LIQUID-PHASE HTC PROCESS (OXY VINYLS) |
| ETHYLENE DICHLORIDE BY OXYCHLORINATION: FLUIDIZED-BED REACTOR, OXYGEN-BASED (OXY VINYLS) |
| ETHYLENE FROM ATOMOSPHERIC GAS OIL BY MILLISECOND(TM) CRACKING/DEMETHANIZATION |
| ETHYLENE FROM ETHANE BY CONVENTIONAL CRACKING WITH FRONT-END DEETHANIZATION |
| ETHYLENE FROM ETHANE-PROPANE BY CONVENTIONAL CRACKING/FRONT-END DEETHANIZATION |
| ETHYLENE FROM LIGHT NAPHTHA BY CONVENTIONAL CRACKING/FRONT-END DEETHANIZATION |
| ETHYLENE FROM N-BUTANE BY CONVENTIONAL CRACKING WITH FRONT-END DEETHANIZATION |
| ETHYLENE FROM PROPANE BY CONVENTIONAL CRACKING WITH FRONT-END DEETHANIZATION |
| ETHYLENE FROM REFINERY GAS, INCLUDING STEAM CRACKING OF ETHANE AND PROPANE |
| ETHYLENE FROM VACUUM GAS OIL BY MILLISECOND(TM) CRACKING/ DEMETHANIZATION |
| ETHYLENE FROM WIDE-RANGE NAPHTHA BY MILLISECOND(TM) CRACKING/ HIGH SEVERITY |
| ETHYLENE FROM WIDE-RANGE NAPHTHA BY MILLISECOND(TM) CRACKING/ MILD SEVERITY |
| ETHYLENE GLYCOL FROM ETHYLENE AND OXYGEN VIA EO (ALL EO FOR EG) |
| ETHYLENE OXIDE FROM ETHYLENE BY AIR OXIDATION(ALL MARKETABLE ETHYLENE OXIDE) |
| ETHYLENE OXIDE FROM ETHYLENE BY OXYGEN OXIDATION (ALL MARKETABLE ETHYLENE OXIDE) |
| ETHYLENE/VINYL ACETATE COPOLYMER USING A TUBULAR REACTOR |
| 2-ETHYLHEXANOL FROM PROPYLENE, COBALT HYDROCARBONYL CATALYST |
| EXTRACTIVE DISTILLATION OF BENZENE AND TOLUENE FROM C5-C7 REFORMATE |
| EXTRACTIVE DISTILLATION OF BENZENE AND TOLUENE FROM C5-C7 REFORMATE |
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| FORMALDEHYDE FROM METHANOL, FERRIC-MOLYBDATE CATALYST |
| FORMALDEHYDE FROM METHANOL, SILVER CATALYST |
| FORMIC ACID (85%) BY BASF PROCESS |
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| GAS TO LIQUIDS TECHNOLOGY SASOL FISCHER TROPSCH PROCESS * |
| GAS TO LIQUIDS TECHNOLOGY SHELL FISCHER TROPSCH PROCESS* |
| GASOLINE (102 RONC) CATALYTIC REFORMING OF DEHEXANIZED PARAFFINIC NAPHTHA |
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| HMDA FROM ACRYLONITRILE BY ELECTROHYDRODIMERIZATION IN UNDIVIDED CELLS(EMULSION) |
| HMDA FROM ACRYLONITRILE VIA ADIPONITRILE BY AMMONIATION AND HYDROGENATION |
| HMDA FROM ACRYLONITRILE VIA ADIPONITRILE BY ELECTROHYDRODIMERIZATION |
| HMDA FROM BUTADIENE VIA ADIPONITRILE BY HYDROCYANATION |
| HMDA FROM BUTADIENE VIA DICHLOROBUTENE, DICYANOBUTENE, AND ADN |
| HYDROGEN FLUORIDE FROM FLUORSPAR |
| HYDROGEN FROM NATURAL GAS BY STEAM REFORMING |
| HYDROGEN PEROXIDE BY THE ANTHRAQUINONE PROCESS |
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| ISODECYL ALCOHOL FROM NONENES, COBALT CATALYST |
| ISONONYL ALCOHOL FROM OCTENES, RHODIUM CATALYST |
| ISOPHTHALIC ACID FROM M-XYLENE BY BROMINE-PROMOTED CATALYTIC AIR OXIDATION |
| ISOPHTHALOYL CHLORIDE FROM M-XYLENE |
| ISOPROPANOL FROM CHEMICAL PROPYLENE, SILICOTUNGSTATE CATALYST |
| ISOPROPANOLAMINES FROM PROPYLENE OXIDE AND AMMONIA (NH3:PO=5:1) |
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| LDPE BY A HIGH PRESSURE AUTOCLAVE PROCESS |
| LDPE PRODUCTION BY A HIGH-PRESSURE TUBULAR PROCESS SIMILAR TO EXXONMOBIL PROCESS |
| LDPE PRODUCTION BY A HIGH-PRESSURE TUBULAR PROCESS SIMILAR TO SABTEC CTR PROCESS |
| LLDPE PRODUCTION BY A GAS-PHASE PROCESS SIMILAR TO THE UNIPOL™ PE PROCESS |
| LLDPE PRODUCTION BY A SLURRY PROCESS SIMILAR TO THE CHEVRON-PHILLIPS SLURRY LOOP PROCESS |
| LLDPE PRODUCTION BY A SOLUTION PROCESS SIMILAR TO NOVA CHEMICALS ADVANCED SCLAIRTECH™ PROCESS |
| LLDPE PRODUCTION BY A SOLUTION PROCESS SIMILAR TO NOVA CHEMICALS SCLAIRTECH™ PROCESS |
| LNG BY CASCADE REFRIGERATION* |
| LNG REGASIFICATION* |
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| MALEIC ANHYDRIDE FROM BENZENE, FIXED BED REACTOR, DIRECT DEHYDRATION |
| MALEIC ANHYDRIDE FROM N-BUTANE, FLUID BED REACTOR, DIRECT DEHYDRATION |
| MALEIC ANHYDRIDE FROM N-BUTANE, FLUID BED REACTOR, ORGANIC SOLVENT ABSORBER |
| MALEIC ANHYDRIDE FROM N-BUTANE, MOVING BED REACTOR |
| MALEIC ANHYDRIDE FROM N-BUTENES, FLUID BED REACTOR, DIRECT DEHYDRATION |
| MELAMINE FROM UREA BY THE MELAMINE CHEMICALS M-II PROCESS |
| METHANOL FROM COAL BY THE SCGP AND ICI/SYNETIX LPM PROCESS |
| METHANOL FROM NATURAL GAS BY THE ICI COPPER-BASED CATALYST PROCESS |
| METHANOL FROM NATURAL GAS BY THE ICI LCM PROCESS |
| METHANOL FROM NATURAL GAS BY THE LURGI COMBINED REFORMING PROCESS |
| METHANOL ON "MEGA" SCALE |
| METHANOL PRODUCTION VIA TOYO TECHNOLOGY |
| METHYL CHLORIDE FROM METHANOL AND EXCESS HCl IN LIQUID PHASE |
| METHYL METHACRYLATE FROM ACETONE, HCN, AND SULFURIC ACID |
| METHYL METHACRYLATE FROM T-BUTANOL VIA METHACROLEIN AND METHACRYLIC ACID |
| METHYL T-BUTYL ETHER FROM A CAT-CRACKED C4 STREAM |
| METHYLAMINES FROM METHANOL AND AMMONIA |
| METHYLENE DIPHENYLENE ISOCYANATE (MDI) & POLYMERIC FORM (PMPPI) BY PHOSGENATION |
| P-METHYLSTYRENE FROM TOLUENE AND ETHYLENE VIA P-ETHYLTOLUENE |
| MMA VIA ASAHI TECHNOLOGY (C3 BASED)* |
| MMA VIA LUCITE TECHNOLOGY (C3 BASED)* |
| MMA VIA MITSUBISHI TECHNOLOGY (C2 BASED)* |
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| NAPHTHA FROM CRUDE OIL INCLUDING EXTRACTION AND TRANSPORTATION |
| NATURAL GAS RECOVERY AND PROCESSING |
| NEAR ZERO SULFUR DIESEL HYDROTREATING |
| NITRIC ACID, 60%, FROM AMMONIA BY CATALYTIC OXIDATION |
| NITROBENZENE FROM BENZENE BY ADIABATIC NITRATION |
| NITROBENZENE FROM BENZENE BY CONVENTIONAL NITRATION |
| NITROGEN OF 95% PURITY FROM AIR BY PRESSURE SWING ADSORPTION (PSA) |
| NYLON 6 MELT FROM CAPROLACTAM FOR DIRECT SPINNING |
| NYLON 66 CHIPS FROM ADIPIC ACID AND HEXAMETHYLENEDIAMINE |
| NYLON CARPET YARN FROM A NYLON SALT AQUEOUS SOLUTION |
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| OLEFINS, LINEAR ALPHA, BY SHELL HIGHER OLEFINS PROCESS |
| OLEFINS, LINEAR ALPHA, BY TWO-STAGE OLIGOMERIZATION-DISPLACEMENT PROCESS |
| OXYGEN VAPOR VIA CRYOGENIC AIR SEPARATION |
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| PERACETIC ACID FROM ACETALDEHYDE BY ACID-CATALYZED LIQUID-PHASE OXIDATION |
| PHENOL (ACETONE BY-PRODUCT) FROM CUMENE |
| PHENOL BY LIQUID PHASE OXIDATION OF TOLUENE |
| PHENOL-FORMALDEHYDE RESOL SYRUP, 50% SOLIDS, BATCH PROCESS |
| PHOSGENE FROM CHLORINE AND CARBON MONOXIDE BY ACTIVE CARBON CATALYSIS |
| PHOSPHORIC ACID BY THE HEMIHYDRATE WET PROCESS |
| PHTHALIC ANHYDRIDE FROM O-XYLENE IN A FIXED-BED REACTOR (BASF) |
| POLYBUTADIENE BY LITHIUM-CATALYZED POLYMERIZATION |
| POLYCARBONATE, BATCH INTERFACIAL PROCESS WITH C7 ANTISOLVENT POLYMER RECOVERY |
| POLYCARBONATE, BATCH INTERFACIAL PROCESS WITH POLYMER RECOVERY FROM AQUEOUS PHASE |
| POLYCARBONATE, BATCH INTERFACIAL PROCESS WITH POLYMER RECOVERY FROM TOLUENE PHASE |
| POLYCARBONATE, BATCH INTERFACIAL PROCESS WITH RECYCLE OF SATURATED SALT SOLUTION |
| POLYETHYLENE TEREPHTHALATE BY A PROCESS SIMILAR TO THE EASTMAN CHEMICAL PROCESS |
| POLYETHYLENE TEREPHTHALATE BY CONVENTIONAL MELT-PHASE PLUS SOLID-STATE POLYMERIZATION |
| POLYETHYLENE TEREPHTHALATE PELLETS (IV=0.6) FROM TEREPHTHALIC ACID AND EG |
| POLYETHYLENE, HD, BY CHEVRON-PHILLIPS SLURRY DOUBLE-TUBE LOOP REACTOR |
| POLYETHYLENE, HI DENSITY, BY A LOOP REACTOR PROCESS (PHILLIPS) |
| POLYETHYLENE, HI DENSITY, BY A STIRRED-TANK HEAVY DILUENT PRODESS |
| POLYETHYLENE, HI DENSITY, BY GAS PHASE FLUIDIZED-BED PROCESS (UCC) |
| POLYETHYLENE, HI DENSITY,BY A MEDIUM PRESSURE SOLUTION PROCESS (DU PONT) |
| POLYETHYLENE, LINEAR LD, BY A HIMONT TYPE PROCESS |
| POLYETHYLENE, LINEAR LD, BY A LOW PRESSURE SOLUTION PROCESS (MITSUI) |
| POLYETHYLENE, LLD, BY SLURRY PROCESS- STIRRED-TANK REACTORS WITH A SINGLE-SITE CATALYST |
| POLYETHYLENE, LLD, SLURRY PROCESS- DOUBLE-TUBE LOOP SINGLE SITE CAT. ORGANO-ALUMINOXY COMP. |
| POLYETHYLENE, VERV LD, BY HIGH PRESSURE AUTOCLAVE REACTOR PROCESS (CdF) |
| POLYETHYLENE, VERV LD, BY HIGH PRESSURE AUTOCLAVE REACTOR PROCESS USING EXXPOL |
| POLYETHYLENE, VERV LD, BY HIGH PRESSURE TUBULAR REACTOR PROCESS USING EXXPOL |
| POLYETHYLENE, VERV LD, BY LOW PRESSURE ADIABATIC SOLUTION PROCESS |
| POLYPROPYLENE BLOCK COPOLYMER BY A GAS PHASE PROCESS (SUMITOMO) |
| POLYPROPYLENE BY A BULK SLURRY PHASE LOOP REACTOR PROCESS |
| POLYPROPYLENE COPOLYMER BY A HIMONT TYPE PROCESS |
| POLYPROPYLENE COPOLYMER BY A HORIZONTAL STIRRED BED GAS PHASE PROCESS (AMOCO/CHISSO) |
| POLYPROPYLENE COPOLYMER BY A VERTICAL STIRRED BED GAS PHASE PROCESS (BASF) |
| POLYPROPYLENE HOMOPOLYMER BY A VERTICAL STIRRED BED GAS PHASE PROCESS (BASF) |
| POLYSILICON PRODUCTION VIA SIEMANS REACTORS |
| POLYSILICON PRODUCTION VIA SIEMANS REACTORS |
| POLYSTYRENE, EXPANDABLE, BY BATCH SUSPENSION POLYMERIZATION |
| POLYSTYRENE, GENERAL PURPOSE, BY CONTINUOUS BULK POLYMERIZATION |
| POLYSTYRENE, GENERAL PURPOSE, BY THE SDS PROCESS |
| POLYSTYRENE, HIGH IMPACT, BY CONTINUOUS BULK POLYMERIZATION |
| POLYSTYRENE, HIGH IMPACT, BY THE SDS PROCESS |
| POLYTETRAMETHYLENE ETHER GLYCOL BY POLYMERIZATION AND ALCOHOLYSIS, POLYFLUOROSULFONIC ACID CATALYST |
| POLYURETHANE FOAM BOARDSTOCK (RIGID) FROM REDUCED CFC FORMULATION |
| POLYVINYL ACETATE BEADS BY SUSPENSION POLYMERIZATION |
| POLYVINYL ACETATE LATEX BY EMULSION POLYMERIZATION |
| POLYVINYL ACETATE PELLETS BY SOLUTION POLYMERIZATION |
| POLYVINYL CHLORIDE BY BULK POLYMERIZATION |
| POLYVINYL CHLORIDE BY BULK POLYMERIZATION UPDATE |
| POLYVINYL CHLORIDE BY EMULSION POLYMERIZATION |
| POLYVINYL CHLORIDE BY SUSPENSION POLYMERIZATION UPDATE |
| PRODUCTION OF HYDROPHOBIC [bmim][PF6] IONIC LIQUID |
| 1,3-PROPANEDIOL FROM WHOLE CORN BIOREFINER |
| PROPYLENE DIMERIZATION |
| PROPYLENE OXIDE BY THE CONVENTIONAL CHLOROHYDRIN PROCESS |
| PROPYLENE, POLYMER GRADE, FROM ETHYLENE AND BUTYLENES BY METATHESIS |
| PROPYLENE, POLYMER GRADE, FROM PROPANE BY CATALYTIC DEHYDROGENATION |
| PROPYLENE, POLYMER GRADE, FROM REFINERY GRADE PROPYLENE (66 WT % C3H6) |
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| REFINERY PROPYLENE FROM FCC |
| REFORMATE BENZENE SATURATION BY CATALYTIC DISTILLATION |
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| SODIUM TRIPOLYPHOSPHATE FROM WET PROCESS PHOSPHORIC ACID |
| STTP FROM INDUSTRIAL GRADE PHOSPHORIC ACID |
| STYRENE FROM BENZENE AND ETHYLENE VIA VAPOR-PHASE ALKYL.&ADIABATIC DEHYDRO |
| STYRENE-ACRYLONITRILE RESIN BY CONTINUOUS MASS POLYMERIZATION |
| STYRENE-BUTADIENE RUBBER BY EMULSION POLYMERIZATION |
| SULFURIC ACID FROM SULFUR |
| SYNTHESIS GAS (2:1) FROM BITUMINOUS COAL BY GASIFICATION |
| SYNTHESIS GAS (2:1) FROM NATURAL GAS BY PARTIAL OXIDATION |
| SYNTHESIS GAS (2:1) FROM NATURAL GAS BY STEAM REFORMING WITH CO2 IMPORT |
| SYNTHESIS GAS (2:1) FROM VACUUM RESIDUE BY PARTIAL OXIDATION |
| SYNTHESIS GAS (3:1) FROM NATURAL GAS BY STEAM REFORMING WITH CO2 RECYCLE |
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| T-BUTANOL (GASOLINE GRADE) FROM MIXED BUTENES |
| TEREPHTHALIC ACID (HIGH PURITY) FROM P-XYLENE BY BROMINE-PROMOTED AIR OXIDATION |
| TEREPHTHALIC ACID, PURIFIED, BY THE CONVENTIONAL CATALYTIC AIR OXIDATION PROCESS |
| TETRAHYDROFURAN FROM MALEIC ACID |
| TOLUENE DIISOCYANATE BY PHOSGENATION |
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| UPGRADED METALLURGICAL GRADE SILICON (UMG-Si) PRODUCTION |
| UREA, AGRICULTURAL GRADE, BY THE STAMICARBON PROCESS |
| UREA-FORMALDEHYDE MOLDING COMPOUND |
| UREA-FORMALDEHYDE RESIN SYRUP, 65% SOLIDS |
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| VACUUM GAS OIL CONVENTIONAL FLUID CATALYTIC CRACKING |
| VINYL ACETATE FROM ACETYLENE AND ACETIC ACID |
| VINYL ACETATE FROM ETHYLENE AND ACETIC ACID BY VAPOR PHASE PROCESS |
| VINYL CHLORIDE BY A BALANCED PROCESS WITH HEAT AND HCl RECOVERY (OXY VINYLS) |
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| P-XYLENE FROM HEAVY REFORMATE/MSTDP XYLENE BY PAREX(R) ADSORPTION PROCESS |
