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Reactor for producing acetylene by coal pyrolysis under thermal plasma action

A thermal plasma and plasma technology, applied in chemical instruments and methods, chemical/physical/physical chemical processes of energy application, feeding devices, etc., can solve the problems of low energy conversion efficiency and low energy utilization rate, etc. The effect of improving the conversion rate of raw coal and the utilization rate of energy

Active Publication Date: 2016-07-13
SHENWU TECH GRP CO LTD
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  • Claims
  • Application Information

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Problems solved by technology

This part of the solid semi-coke is not converted and utilized in the process of coal-to-acetylene, and is directly quenched and discharged from the reactor. Not only is the energy conversion efficiency low, but the high-temperature sensible heat brought out is not utilized in the process through the quenching process, and the energy utilization rate of the system is greatly improved. reduce

Method used

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  • Reactor for producing acetylene by coal pyrolysis under thermal plasma action

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Embodiment Construction

[0019] Embodiments of the invention are described in detail below, examples of which are illustrated in the accompanying drawings. The embodiments described below by referring to the figures are exemplary and are intended to explain the present invention and should not be construed as limiting the present invention.

[0020] Refer below figure 1 The reactor 100 for thermal plasma cracking coal to acetylene according to an embodiment of the present invention is described in detail.

[0021] According to the embodiment of the present invention, the reactor 100 for producing acetylene from thermal plasma cracking coal includes a housing 10, which defines a gas-solid mixing chamber 20, a coal cracking reaction chamber 30, and a calcium carbide synthesis reaction sequentially connected from top to bottom. Chamber 40, cooling hydrolysis reaction chamber 50 and gas-solid-liquid separation chamber 60, gas-solid mixing chamber 20 has coal inlet 21, hydrogen inlet 22 and plasma spray g...

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Abstract

The invention discloses a reactor for producing acetylene by coal pyrolysis under thermal plasma action.The reactor comprises a shell, and a gas-solid mixing chamber, a coal pyrolysis reaction chamber, a calcium carbide synthetic reaction chamber, a cooling hydrolysis reaction chamber and a gas-solid-liquid separation chamber are defined in the shell and communicated sequentially from top to bottom.The gas-solid mixing chamber is provided with a coal inlet, a hydrogen inlet and plasma torch insertion ports, the calcium carbide synthetic reaction chamber is provided with a calcium carbide outlet, the cooling hydrolysis reaction chamber is provided with a water inlet, and the gas-solid-liquid separation chamber is provided with a gas outlet and a solid-liquid mixture outlet.The reactor has the advantage that raw coal conversion rate and energy utilization rate can be increased.

Description

technical field [0001] The invention relates to the technical field of acetylene production, in particular to a reactor for thermal plasma cracking coal to produce acetylene. Background technique [0002] In related technologies, the research on thermal plasma cracking coal to acetylene process mainly starts from the perspective of acetylene yield. Acetylene yield and specific energy consumption are important indicators to measure the feasibility of thermal plasma cracking to acetylene, and the reactor structure is It has a significant impact on the yield of acetylene and specific energy consumption. Looking at all plasma coal-to-acetylene reactors, in the process of thermal plasma cracking coal to acetylene, only the volatile matter in the cracked coal is converted into acetylene gas, the yield of acetylene is only 20%-40%, and the conversion rate of raw coal is low, accounting for 50%. More than 100% of the solid semi-coke does not participate in the reaction, and is disc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J8/08B01J19/08B01J4/00C07C11/24C07C1/00
CPCB01J8/004B01J8/008B01J8/08B01J8/085B01J8/087B01J19/088C07C1/00C07C11/24
Inventor 郭启海丁力肖磊吴道洪
Owner SHENWU TECH GRP CO LTD