E-Gas technology

Wabash river (USA) 1995 262 No CCS included [11 ] Bituminous coal and petroleum coke E-GAS technology two stage entrained-flow gasifier. General Electric s MS 7001 gas turbine and overall plant efficiency of 40%... 

Figure 623 Enhanced design configurations for E-Gas technology (a) high-pressure design (adapted from patent application WO 2009/ 020809A1 [93]), (b) entrained slagging transport reactor (E-STR) design without residence vessel (HP - high pressure) (adapted from patent application WO 2010/080525A2 [94),...

Amick, P. (2010) E-Gas Technology 2010 Outlook. Proceedings of the Gasification Technologies Conference, www. gasification.org. 

E. E. Fant. Odorization—a regulatory perspective. In Odorization, volume 3, pages 109-118. Institute of Gas Technology, Chicago, IL, 1993. 

Large-scale gasification reactor technology based on EF gasification from (a) General Electric (GE Texaco process) and (b) Conoco-Phillips (E-Gas). (Adapted from Meier, D. Faix, O. Fast pyrolysis A route for energy and chemicals from wood—fluidized vs. ablative pyrolysis. In Wood and Biomass Utilization for the Carbon Uptake, Seoul National University, Seoul, 2005, pp. 55-68.)... 

S. N. Simons, R.B. King, P.R. Prokopius, in Symposium Proceedings Fuel Cells Technology Status and Applications, Edited by E. H. Camara, Institute of Gas Technology, Chicago, IE, p. 45, 1982. 

T.G. Benjamin, E.H. Camara, E G. Marianowski, Handbook of Fuel Cell Performance, prepared by the Institute of Gas Technology for the United States Department of Energy under Contract No. EC-77-C-03-1545, May 1980. 

Gasifier technology Sasol/Lurgi Texaco/GE Energyf BGL) E-Gas/ConocoPhillips Shell/Uhde ... 

In a 1996 report compiled by EANE, cost estimates were prepared for seven innovative off-gas treatment technologies as well as for three off-gas technologies currently in use. Results of the estimate for SDP are summarized in Table 1. It was estimated that SDP was most cost effective in treating high concentrations of specific contaminants at low flow rates. It was found that cost was independent of VOC concentration but was dependent on the desired destruction and removal efficiency (DRE) and the flow rate. Energy costs drop for gas matrices other than air (e.g., off-gas from a pyrolizer or low-temperature desorber or gas streams carried by an inert gas such as argon) (D130756, p. 21). 

Foster, N., R. Mammucari, F. Dehghani, A. Barrett, K. Bezanehtak, E. Coen, G. Combes, L. Meure, A. Ng, H. L. Regtop, and A. Tandya. 2003. Processing pharmaceutical compounds using dense gas technology.1 nd Eng Chem Pre42 6476-6493. 

E-Gas (Destec) whose technology uses petroleum coke as a feedstock and produces over-the-fence syngas, and... 

Benjamin T. G., Camara E. H., Marianowski L. G., Handbook of Fuel Cell Performance, Institute of Gas Technology, U.S. Department of Energy, Washington, DC, 1980. 

Escher, W.J.D., Donakowski, T.D. and Foh, S.E., Dedicated Nuclear Facilities for Electrolytic Hydrogen Production, Institute of Gas Technology, Presented at the Hydrogen for Energy Distribution Symposium, July 24-28, 1974. 

All analyses were performed by the Institute of Gas Technology. The crude protein content is estimated by multiplying the nitrogen value by 6.25. RDF is refuse-derived fuel i.e, the combustible fraction of municipal solid waste. 

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