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Process Economic Program

H. C. Ries, Process Economics Program 2SA, Stanford Research Institute, Menlo Park, California, July 1970, pp. 41—53. [Pg.426]

Ref. 13, p. 604.5000 F. Detailed process information is available in Phenol, PeportNo. 22B, Process Economics Program, SRI International, Menlo Park, Calif., December 1977. [Pg.100]

Terephthalic A.ddand Dimethyl Terephthalate, Report 9, private report from SRI International s Process Economics Program, Menlo Park, Calif., Feb. 1966, Sept. 1970, and Aug. 1976. [Pg.348]

Process Economics Program 134, SRI International, Menlo Park, Calif., 1979. [Pg.452]

S. A.cetone, Methj/ Ethj/ Ketone, and Methyl Isohutyl Ketone, Process Economics Program, Report No. 77, SRI, Menlo Park, Calif., May 1972. [Pg.502]

G. E. Haddeland and S. Monkawa, Titanium Dioxide Pigment, Process Economics Program Report No. 117, Stanford Research Institute International, Menlo Park, Calif., 1978. [Pg.112]

Sucralose—A High Intensity, Noncaloric Sweetener. PEP Review 90-1-4, Process Economics Program, SRI Consulting,... [Pg.207]

Chadwick, J. L. 1977. Economics of chemical refineries. Process Economic Program Report 107. Menlo Park SRI. [Pg.364]

Moore, E. R. and Bray, R. G., 1,3-Propanediol and Polytrimethylene Terephthalate, Process Economics Program Report 227, SRI International, Menlo Park, CA, 1999. [Pg.392]

SRI International (1979) Isocyanates/polyisocyanates process economics program report 1C/1 2. SRI Consulting, Menlo Park, CA. Available at http //www.sriconsulting.com/PEP/ Pubhc/Reports/Phase 78/RP01Cl/RP01Cl toc.pdl. Accessed 30 May 2011... [Pg.354]

E. Matsunaga and R. G. Muller, Secondary Butyl Alcohol via Direct Hydration, Process Economics Program, Review No. 84-2-2, SRI International,... [Pg.501]

Process Economics Program Yearbook International, SRI Consulting, Menlo Park, CA. [Pg.884]

Process Economics Program Report SRI International. Menlo Park, CA, Isocyanates IE, Propylene Oxide 2E, Vinyl Chloride 5D, Terephthalic Acid and Dimethyl Terephthalate 9E, Phenol 22C, Xylene Separation 25C, BTX, Aromatics 30A, o-Xylene 34 A, m-Xylene 25 A, p-Xylene 93-3-4, Ethylbenzene/Styrene 33C, Phthalic Anhydride 34B, Glycerine and Intermediates 58, Aniline and Derivatives 76C, Bisphenol A and Phosgene 81, C1 Chlorinated Hydrocarbons 126, Chlorinated Solvent 48, Chlorofluorocarbon Alternatives 201, Reforming for BTX 129, Aromatics Processes 182 A, Propylene Oxide Derivatives 198, Acetaldehyde 24 A2, 91-1-3, Acetic Acid 37 B, Acetylene 16A, Adipic Acid 3 B, Ammonia 44 A, Caprolactam 7 C, Carbon Disulfide 171 A, Cumene 92-3-4, 22 B, 219, MDA 1 D, Ethanol 53 A, 85-2-4, Ethylene Dichloride/Vinyl Chloride 5 C, Formaldehyde 23 A, Hexamethylenediamine (HMDA) 31 B, Hydrogen Cyanide 76-3-4, Maleic Anhydride 46 C, Methane (Natural Gas) 191, Synthesis Gas 146, 148, 191 A, Methanol 148, 43 B, 93-2-2, Methyl Methacrylate 11 D, Nylon 6-41 B, Nylon 6,6-54 B, Ethylene/Propylene 29 A, Urea 56 A, Vinyl Acetate 15 A. [Pg.403]

S. Naqvi, Process Economics Program (PEP) Review 97-3, SRI Consulting, Menlo Park, CA, (1998). [Pg.237]

Leiby, S.M. Options for refinery hydrogen. Menlo Park, CA Process Economics Program, SRI International. PEP Report No. 212, February 1994. [Pg.447]

See other pages where Process Economic Program is mentioned: [Pg.250]    [Pg.521]    [Pg.35]    [Pg.402]    [Pg.1078]    [Pg.250]    [Pg.521]    [Pg.627]    [Pg.205]    [Pg.444]    [Pg.250]   


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