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Novel pulverized coal pyrolytic hydrogenation reactor and pyrolytic hydrogenation reaction method

A hydrogenation reactor and a hydrogenation reaction technology are applied in the petroleum industry, the preparation of liquid hydrocarbon mixtures, etc., and can solve the problems of the reaction condition requirements of the polluted coal-to-liquid method, the low utilization rate of heat energy recovery, and the low utilization rate of raw materials, etc. Achieve the effect of lower material requirements, lower cost investment, and shorter response time

Active Publication Date: 2015-09-02
中美新能源技术研发(山西)有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] The purpose of the present invention is to solve the problems of high cost, low heat energy recovery utilization rate, low raw material utilization rate, serious waste, serious pollution and harsh reaction conditions and low oil yield in the existing coal-to-oil equipment. problem, provide a new pulverized coal pyrolysis hydrogenation reactor and pyrolysis hydrogenation reaction method

Method used

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  • Novel pulverized coal pyrolytic hydrogenation reactor and pyrolytic hydrogenation reaction method

Examples

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Effect test

Embodiment 1

[0027] Such as figure 1 As shown, a novel pulverized coal pyrolysis hydrogenation reactor in the present embodiment includes a reaction chamber 1 provided with pulverized coal nozzles, 2 converter furnaces 2 provided with process burners, 2 synthesis gas nozzles 8, Quenching chamber 4, primary separator 3, two constant force cranes 5, secondary separator 6 and tertiary separator 7, the two converter furnaces 2 are symmetrically arranged on both sides of the reaction chamber 1, and the converter furnace 2 The gas outlet of the synthetic gas nozzle 8 is connected with the air inlet of the synthesis gas nozzle 8, and the gas outlet of the synthesis gas nozzle 8 is connected with the air inlet arranged at the middle part of the side wall of the reaction chamber 1, and the axis of the synthesis gas nozzle 8 is connected with the reaction chamber 1 air intake. The included angle of the horizontal line of the mouth is 15 degrees, and the reaction chamber 1 is arranged on the top of t...

Embodiment 2

[0035] The novel pulverized coal pyrolysis hydrogenation reactor in this example is the same as the novel pulverized coal pyrolysis hydrogenation reactor in Example 1.

[0036] A method of using the novel pulverized coal pyrolysis hydrogenation reactor described in this embodiment to carry out pulverized coal pyrolysis hydrogenation reaction comprises the following steps:

[0037] 1) The raw coal is sent to the grinding and drying system to produce coal powder with a particle size of less than 90 microns, a moisture content of less than 3%, and a temperature of 100-105°C;

[0038] 2) The mixed gas composed of natural gas and oxygen is sent to the conversion furnace (2) through the process burner for combustion, and a high-temperature gas of 1600°C is produced and mixed with hydrogen entering the conversion furnace (2) through the hydrogen port to form a temperature of 1400°C The mixed gas is sent into the reaction chamber (1) as a pyrolysis source, and the mixed gas pressure i...

Embodiment 3

[0043] The novel pulverized coal pyrolysis hydrogenation reactor in this example is the same as the novel pulverized coal pyrolysis hydrogenation reactor in Example 1.

[0044] A method of using the novel pulverized coal pyrolysis hydrogenation reactor described in this embodiment to carry out pulverized coal pyrolysis hydrogenation reaction comprises the following steps:

[0045] 1) The raw coal is sent to the grinding and drying system to produce coal powder with a particle size of less than 90 microns, a moisture content of less than 3%, and a temperature of 100-105°C;

[0046] 2) The mixed gas composed of natural gas and oxygen is sent to the conversion furnace (2) through the process burner for combustion, and a high-temperature gas of 1500 ° C is produced and mixed with hydrogen entering the conversion furnace (2) through the hydrogen port to form a temperature of 1300 ° C The mixed gas is sent into the reaction chamber (1) as a pyrolysis source, and the mixed gas pressu...

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Abstract

The invention belongs to the technical field of pulverized coal pyrolytic hydrogenation reaction devices and processes, and particularly relates to a novel pulverized coal pyrolytic hydrogenation reactor and a pyrolytic hydrogenation reaction method. The novel pulverized coal pyrolytic hydrogenation reactor and the pyrolytic hydrogenation reaction method mainly solve the technical problems of high cost, low heat recycling rate, low utilization rate of raw materials, severe waste and severe pollution of existing coal-to-liquid equipment and strict requirements on reaction conditions and low oil yield of a coal-to-liquid method. The novel pulverized coal pyrolytic hydrogenation reactor adopts the technical scheme by comprising a reaction chamber, at least one conversion furnace, at least one syngas nozzle, a quick-cooling chamber, a first-stage separator, at least two constant-force hangers, a second-stage separator and a third-stage separator, wherein the reaction chamber is provided with a pulverized coal nozzle, the at least one conversion furnace is provided with a process burner, and the number of the syngas nozzle is the same as that of the conversion furnace. The novel pulverized coal pyrolytic hydrogenation reactor has the advantages of simple structure, energy conservation, environmental friendliness, low energy consumption, high heat recycling rate and high coal-to-liquid rate.

Description

technical field [0001] The invention belongs to the field of pulverized coal pyrolysis hydrogenation reaction device and process technology, and in particular relates to a novel pulverized coal pyrolysis hydrogenation reactor and a pyrolysis hydrogenation reaction method. Background technique [0002] The domestic coal-to-oil technology mainly uses direct liquefaction or indirect liquefaction. The reaction conditions of direct liquefaction are relatively harsh. The liquefaction pressure of the old German process is even as high as 70MPa, and the modern process is also 17-30MPa, and the liquefaction temperature is 420-470°C. The applicable range of coal types is narrow, and direct liquefaction is mainly suitable for young coals such as lignite, long-flame coal, gas coal, non-caking coal, and weakly caking coal. The composition of the product exiting the liquefaction reactor is complex, and the liquid-solid two-phase mixture is relatively difficult to separate due to its high...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G1/06
Inventor 郑琪扶振安英保陈裕彬邹家富
Owner 中美新能源技术研发(山西)有限公司
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