category: coal liquefaction

Report on the Petroleum and Synthetic Oil Industry of Germany to the Right Hon. Emanuel Shinwell

... catalyst , butane and combustion gases is concurrent . MAKE - UP ... space which is brick- The tube bundles , which represent the reaction space ... dead space . The total catalyst capacity of each reactor is 2.2m3 . The catalyst is ...

EDS Coal Liquefaction Process Development: Phases IIIB/IV

... Coal Liquefaction Plant . The two major streams to be handled are bed purge ... differences between coal ashes and the EDS solids . If the dry solids are ... coke streams . An additional ash / coke stream is the venturi scrubber fines ...

Second European Conference on Coal Liquid Mixtures: A Three Day Symposium Organised by the Institution of Chemical Engineers in Association with the Institute of Energy and Held in London, 16-18 September 1985

... compromise between available signal - to - noise ratio and the desire to perturb the test sample ... 998 samples are generally more viscous than QR - 819 samples , and the QR ... 998 system exhibits the greatest elastic modulus and addition of ...

Coal Hydrogenation: The Effect of Variations in the Coal-to-vehicle Ratio

... data of table 4 can be com- pletely useful . TABLE 4 . 3 Batch hydrogenation of coal in the presence of Zn - Sn alloy catalyst ... paper . The coal - hydrogenation ... 3850 C. is shown in figure 7. The results of the experiments described ...

Coal Liquefaction: Quarterly report

... design of the process development unit reactor was changed to improve ebullition and to permit withdrawal of a ... pipe racks . The process design for the hydrogena- tion section was reviewed . A question was raised concerning the amount ...

First European Conference on Coal Liquid Mixtures

... COM burner experience is helpful , but not totally useful for CWM development ... COEN burner used with the 700 - Hp watertube boiler was modified for CWM ... burners are shown in Table 14 . When the holes were enlarged from 7 / 32 ...

Chemistry and Technology of Synthetic Liquid Fuels

... below 200 ° C below 300 ° C above 300 ° C gas + losses Composition of the fraction boiling below 300 ° , % on initial paraffin alkenes aromatics cyclo- alkanes alkanes Over - all density of product at 15 ° C 32.9 37.8 Cracking ...

This website uses cookies and collects data for optimal performance. Your continued use signifies agreement to our Privacy Policy.