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- W2379656871 abstract "A pilot scale study is done by batch chemical vapour deposition(CVD)to optimize the structure of fluidized-bed reactor for production of carbon nanotubes,and to achieve semi-continuous mode of operation by changing the way of unloading.The results show that when the heater is working,the CNTs yield drops by 15% and the bed resistance increases by 67%.When the height of preheat zoon is 0 cm and the reaction time is 4 h,the yield is the highest,i.e.,9.2 g/g.Under the optimal conditions and the amount of catalyst is 100 g,the ideal height of the sagger is 35 cm.With the new mode,the production period of CNTs will be shortened from 24.0 h to 8.5 h." @default.
- W2379656871 created "2016-06-24" @default.
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- W2379656871 date "2010-01-01" @default.
- W2379656871 modified "2023-09-25" @default.
- W2379656871 title "Optimization of a pilot-scale reactor for carbon nanotubes production by catalytic pyrolysis" @default.
- W2379656871 hasPublicationYear "2010" @default.
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