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Chem Systems Inc

TerephthalicHdd and Dimethyl Terephthalate, reportno. 75-1, Chem. Systems, Inc., New York, July 1975. [Pg.348]

MIBK Direct Conversion ofMcetone over Heterogeneous Catalyst-Sumitomo, Process Evaluation Research Planning (PERP), Topical Reports, Vol. Ill, Chem Systems Inc., Tarrytown, NY, 1988. [Pg.502]

Chem Systems Inc. proposed a process in which ben2yl alcohol obtained by an undisclosed direct oxidation of toluene is homologated with synthesis gas to yield 2-phen5iethyl alcohol, which is then readily dehydrated to styrene (57). This process eliminates the intermediate formation of methanol from synthesis gas but does require the independent production of ben2yl alcohol. [Pg.190]

VinylProducts Eifeycle Assessment, Chem Systems, Inc., Tarrytown, N.Y., Mar. 1992. [Pg.512]

Chemical Economics Handbook, SRI International, Menlo Park, Calif. Petrochemicals Primary, Chem Systems Inc., New York, 1987. [Pg.375]

W. M. Weiss, personal communication, Monsanto Enviro-Chem Systems Inc., St. Louis, Mo., 1991. [Pg.231]

DAVID B. BLUM, MARTIN B. SHERWIN, and MARSHALL E. FRANK Chem Systems, Inc., Research Center, 275 Hudson St., Hackensack, N. J. 07061... [Pg.158]

US/UK Seminar on TNT Chemistry Manufacture , ERDE-TR-106, Waltham Abbey, Engl (1972) (Limited distrib) 13) Anon, Computer Control Study of Radford TNT Plant , Final Tech Rept, Chem Systems Inc, NY (1972) (Limited distrib) 14) R.S. Kukuvka K. Gandhi, Propagation Tests of 55-Pound Boxes of Bulk TNT and 60-Pound Boxes of Bulk Composition B , PATR 4622 (1973) 15) G. [Pg.736]

Figure 9.2. Single Pressure Nitric Add Plant. (Reproduced by Permission of Monsanto Emiro-Chem Systems, Inc.)... Figure 9.2. Single Pressure Nitric Add Plant. (Reproduced by Permission of Monsanto Emiro-Chem Systems, Inc.)...
Reproduced by permission of Monsanto Enviro-Chem Systems, Inc.) a DCN Destmction by Catalysis of NOx HEA High Efficiency Absorption... [Pg.238]

Fig. 6. UOP-BP Cydar process for LPG aromatization (38). Courtesy of Chem Systems Inc. Fig. 6. UOP-BP Cydar process for LPG aromatization (38). Courtesy of Chem Systems Inc.
Production Economics For Hydrogen, Ammonia And Methanol During The 1980-2000 Period, Exxon Research and Engineering Company, Government Research Contract No. 368150-S April 1977, Appendix A by Chem Systems Inc.", Cost of Production Estimates For Hydrogen, Ammonia And Methanol, October 21, 1976, P. 127-166. [Pg.81]

As is explained in Reference 1, investment and operating cost data for various hydrogen manufacturing processes were provided for this study by Chem Systems, Inc., New York, New York. These economics data were developed using identical methods and assumptions, thereby permitting side-by-side comparisons of the several processes. [Pg.82]

Fig. 10.3. Methanol via natural gas reforming. (Chem Systems Report No. 93-1. Copyright Nexant Chem Systems, Inc. and used by permission of the copyright owner.)... [Pg.349]


See other pages where Chem Systems Inc is mentioned: [Pg.176]    [Pg.396]    [Pg.397]    [Pg.397]    [Pg.193]    [Pg.181]    [Pg.181]    [Pg.182]    [Pg.182]    [Pg.183]    [Pg.183]    [Pg.11]    [Pg.346]    [Pg.193]    [Pg.502]    [Pg.181]    [Pg.182]    [Pg.182]    [Pg.183]   


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