01 So/id fuels (preparation) 97101639 Preparation of activated carbons from bituminous coals with CO2 activation. 1. Emts of oxygen content in raw coals Teng. H. et ul. /,I</. E/IS. Chem. Res., 1996, 35. (I I), 4043-4049. Activated carbons were prepared from three Australian bituminous coals. The pr
97/00939 Optimization of hydrogenation of coal from the Karaxhara deposit by hydrogenation in the synthesis-gas medium
- Publisher
- Elsevier Science
- Year
- 1997
- Weight
- 189 KB
- Volume
- 38
- Category
- Article
- ISSN
- 0140-6701
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β¦ Synopsis
02 Liquid fuels (derived liquid fuels) compctitivc with natural ga\ in the production of these fuels. A carbon tax that would increase the cost of owing and operating fuel cell vehicles on natural gas-derived fuels hy less than 2% would he adequate to tip the economic balance in favour of hiomass.
97/#927
Method for upgrading a hydrocarbon gas contatning a hydrocarbon and sulfur species by cracking against the regenerated sorbent Caldcron. A.
PCT Int. Appl. WO Yh 20. Y06 (Cl. CO7C4104). I I Jul 1996. U.S. Appl. 36.5, 911.7, 30 Dee lYY4, IO pp. Deals with the upgrading of a gas containing a hydrocarbon and a species of sultur hy the cracking of the gas against the regenerated sorbent. During regeneratron, the sorhent is heated by the exothermic reactions of carbon burn-off and sulfur oxidation. During cracking, the heat in the sorbent adsorbed from the exothermic reactions supplies at least a portion of the heat needed for cracking. The process is conducted under pressure with minimum degradation of the corbent and without conversion of the sorhent to a \ulfatc. The apparatus IO carry out the process includes a regeneration chamber with an oxidant inlet and gas outlet, a means for discharging the \orhent from the regeneration chamber to the cracking chamber, a cracking chamber with a hydrocarbon inlet port and upgraded gas outlet port, and a means for transporting the sorhent from the cracking chamber to the regeneration chamhcr.
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The structure and carbonization behavior of the pitches from the products of gas-coking coal hydrogenation performed at 420Β°C and 455Β°C in a continuous bench scale unit were estimated. The pitches, prepared as residues from vacuum distillation of purified hydrogenation products, were characterized b
Gaseous fuels (sources, properties, recovery, treatment) both with nitrogen and by mercury porosimetry. Simultaneously, activity tests for fresh tar destruction have been carried out for each type of calcined dolomite in a fixed bed 6 cm in diameter. The results suggest that the tar elimination act