## 10 Engines (power generation and propulsion, electrical vehicles) tion zone has to be included. In addition to the radiant fraction, another scaling parameter accounting for the radiation losses from the post-flame region is needed.
98/00532 Combustion reactivity of char from copyrolysis of coal with coke-oven gas
- Publisher
- Elsevier Science
- Year
- 1998
- Weight
- 210 KB
- Volume
- 39
- Category
- Article
- ISSN
- 0140-6701
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β¦ Synopsis
chemical moved through oxidative volatiies pyrolysis, volatiles combustion, soot combustion, and char oxidation. However, only with the low volatility coal were the different fuel components consumed sequentially. Char, soot, and non-condensable fuels burned simultaneously with the sub-bituminous coal and, to a lesser degree, with the Pit. #8. Consequently, hydrocarbon gases from these coals were present while most of the soot and char was converted into gases. 9aloo523 Co-combustion of sewage sludge in a lignite-fired industrial power station Bierbaum, K. et al. Chemical-Ing.-Tech.. 1997, 69, (7), 973-976. (In German) A summary of the operation of a large-scale test about co-combustion of mechanical dehydrated sewage sludge in a circulating fluidized-bed steam generator. A plant concept consisting of steam generator, units for sewage sludge deliverance and flue gas fine cleaning is introduced. The advantages of sewage sludge co-combustion are valued under aspects of energy balance, environmental protection, reduction of costs, and restrictions of recycle and waste orders.
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extraction apparatus for the melting furnace. It is possible to carry out waste treatment at high energy-use efficiency, while preventing tar from adhering to a dry distillation gas transportation pipe.
To improve the economy of the hydropyrolysis process by reducing the hydrogen cost, it has been suggested to use coke-oven gas instead of pure hydrogen. The results presented here describe some characteristics of the chars obtained by pyrolysis carried out at 765Β°C under 3 MPa of various gas mixture