Chinese Academy of Sciences

China Kingsun Material Technology Co., Ltd

Guangwen Xu

Shiqiu Gao

Jian Yu

Yin Wang

Qiang Li

Feng Guo

Qi Zhou

Xufei Xu

Chun Xiao Zhang

Li Dong

Jiao Liu

Juan Yang

Rongcheng Wu

Jiangze Han

Pengwei Dong

Juwei Zhang

Dianmiao Cui

A dry distillation reactor for a raw material of hydrocarbon with a solid heat carrier is provided. An inner component with a pore path or a pore space is arranged inside the reactor to form a flow channel for the gas-phase product of the dry distillation. Also a dry distillation method using the dry distillation reactor is provided. The dry distillation method includes moving the reacting materials from top to bottom; moving a gas-phase product of the dry distillation along a designed path in the reactor; and finally leading same out through an outlet arranged in a central collecting channel for the gas-phase product of the dry distillation.

Dry distillation reactor and method for raw material of hydrocarbon with solid heat carrier

The method for catalytic methanation of synthesis gas includes the following steps: 1) feeding the synthesis gas into the bottom of a reactor of an upward concurrent flow transporting bed so as to adequately mix and preheat with methanation catalyst entering the bottom of the reactor until the activation temperature of the catalyst is reached and then the methanation reaction begins; and 2) after the methanation reaction, immediately passing the product gas and the catalyst grains outputted from the transporting bed into a gas-solid separator to perform a rapid separation so as to obtain the product gas.

Method and device for catalytic methanation of synthesis gas

This invention relates to an apparatus and a method for multistage hierarchical pyrolysis and gasification of solid fuels. The apparatus comprises a feeding device, a multistage fluidized bed reactor, a residual discharging valve, a cycloneand a condenser. A gas inlet is provided at the bottom of the multistage fluidized bed reactorand a number of stages of fluidized bedsare provided within the multistage fluidized bed, wherein the fluidized bedsare separated by a number of perforated distributors. The top stage fluidized bedis connected with the feeding deviceand the coal fed thereto is heated by char obtained from pyrolysis in this stage and the mixture of high temperature ascending pyrolysis and gasification gas to undergo pyrolysis reactions at low temperature, thereby to obtain solid particles after preliminary pyrolytic process. The solid particles flow downwards through an overflow standpipe/the perforated distributorto the next stage of the fluidized bed and then are pyrolyzed through being heated by char and the mixture of pyrolysis and gasification gas. The solid particles in turn pass into the next stage of the fluidized bed and finally enter into the bottom stage fluidized bed to undergo gasification reactions. More light fractions in tar can be produced using the present apparatus and method.

Apparatus and method for multistage hierarchical pyrolysis and gasification of solid fuels

This invention relates to the cleaning of flue gas released from various combustion processes, particularly a surface deposition NH&#x2014;SCR honeycomb catalyst and its preparation method. The catalyst is composed of framework material, TiO, VOand WO, wherein the framework material is composed of clay, coal ash, mineral waste residue or their mixture. The mass fractions for framework material, TiO, VO, and WOare 60 wt. % to 80 wt. %, 13 wt. % to 33 wt. %, 1 wt. % to 5 wt. %, and 0.1 wt. % to 2 wt. %, respectively. The nano VO&#x2014;WO&#x2014;TiOparticles were deposited on the surface of particle pore or honeycomb, and the performance of the catalyst could be greatly improved.

Surface deposition-type honeycomb catalyst for flue gas denitrification and preparation method thereof

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Beijing, China

Guangwen Xu