Method for producing synthetic ammonia and methanol raw material gas by fixed-bed intermittent oxygen-increasing natural gasification

A technology for producing synthetic ammonia and a fixed bed, which is applied in the manufacture of combustible gas, petroleum industry, etc., can solve the problems of large heat loss, low environmental pollution, and high methane content, and achieve the effects of easy adjustment and reduced operation difficulty.

Active Publication Date: 2011-12-14
ANHUI HUAIHUA
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Problems solved by technology

[0020] The characteristics of oxygen-enriched continuous gasification process: mature technology, unstable operation (for existing low-quality raw materials); supporting air separation unit is required, one-time investment is large, and industrialized equipment has not yet been popularized; strong selectivity to coal types; high carbon dioxide in gas , high methane content, effective gas 65-72%; single furnace gas production is high, more than twice that of intermittent gasification; continuous upward blowing gas is always used, no blowing air is vented, and environmental pollution is small
[0021] After years of practice in optimizing the fixed-bed batch gasification process, the fixed-bed batch gasification process is simple, and air and steam gasification agents are used to make gas in stages. The overall quality is good, especially in ...

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  • Method for producing synthetic ammonia and methanol raw material gas by fixed-bed intermittent oxygen-increasing natural gasification
  • Method for producing synthetic ammonia and methanol raw material gas by fixed-bed intermittent oxygen-increasing natural gasification
  • Method for producing synthetic ammonia and methanol raw material gas by fixed-bed intermittent oxygen-increasing natural gasification

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Embodiment Construction

[0046] To further illustrate the present invention, it will be specifically described in conjunction with the following embodiments:

[0047] A fixed-bed intermittent oxygen-enhanced natural gasification method for producing synthetic ammonia and methanol feed gas is based on the traditional fixed-bed intermittent gasification process, which improves the blowing efficiency and shortens the blowing stage by increasing the oxygen concentration in the furnace air time. When the oxygen concentration reaches a certain level, the time of the blowing stage is zero. At this time, the two stages of blowing and air purging in the fixed-bed intermittent gasification process are combined into the recovery stage of the intermittent oxygen-enriching autothermal gasification process. The process flow is as follows: (see Figure 4 ) One cycle of the fixed-bed intermittent oxygen-enhancing natural gasification process is divided into four stages: recovery, upward blowing, downward blowing, and s...

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Abstract

The invention relates to a method for producing and synthetizing ammonia and methyl alcohol raw material gas by virtue of fixed bed intermittence type oxygenation nature gas, and the method is characterized by improving the concentration of oxygen in charged air of the traditional fixed bed intermittence gasification process to 22-65%. By utilizing the method, the defects of low blowing efficiency, low single-furnace output, high coal consumption, serious environment pollution, unstable oxygen enrichment continuous gasification operation, high gas carbon dioxide and methane and the like of the traditional intermittence gasification process are overcome, and the advantages of high enrichment continuous gasification gas production rate and low coal consumption are carried on, two gasification process advantages are innovatively integrated, and the purpose of playing up strengths and avoiding weaknesses is realized.

Description

Technical field [0001] The invention relates to the production of synthetic ammonia and methanol feed gas by using a fixed-bed gasifier batch gasification process. Background technique [0002] A cycle of the traditional fixed-bed intermittent gasification process is divided into five stages: blowing, up blowing, down blowing, second up blowing, and purge. The process flow is described as follows: (see figure 1 ) [0003] 1. Hair dryer: [0004] Air→Blower 1→Air manifold 2→Blowing valve 3→Gas stove→Upper air duct→Dust collector→Recovery valve 11→Blowing air recovery main 13→Blowing air waste heat centralized recovery→Venting (blowing air waste heat recovery process); or [0005] Air → blower 1 → air main pipe 2 → blowing valve 3 → gas stove → upper air duct → dust collector → upper blowing gas valve 7 → gas main valve 8 → gas main 12 → gas waste heat boiler → gas scrubber → gas holder (blowing Gas recovery process); or [0006] Air→Blower 1→Air manifold 2→Blowing valve 3→Gas stove→Upp...

Claims

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Application Information

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IPC IPC(8): C10J3/16
Inventor 陆军
Owner ANHUI HUAIHUA
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