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Biogas deoxidization technology

A biogas and process technology, which is applied in the field of comprehensive utilization of biogas catalytic deoxidation process and reaction heat, can solve the problems of gas temperature rise, heat energy waste, energy consumption, etc., and achieve the effect of fully and rationally using heat and reducing the use range

Inactive Publication Date: 2013-04-03
张仕霖
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

If the oxygen content is too high, the outlet temperature will be too high, causing methane cracking and catalyst sintering
[0005] On the other hand, the processing cost of the biogas deoxidation process mainly comes from the power consumption of the raw material booster and the cycle gas compressor, and the power consumption accounts for about 50% of the processing cost of the entire deoxidation process.
In the process of biogas deoxygenation, methane and oxygen undergo a catalytic combustion reaction, which releases a large amount of heat and causes the temperature of the deoxidized gas to rise. If the heat is not properly utilized, it will even cost energy and equipment to cool it, resulting in a large amount of heat energy. waste

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] The oxygen content in the raw material mixed gas is 0.4%. Under the action of the catalyst, the methane and oxygen in the raw material biogas undergo a catalytic combustion reaction to deoxidize. The reaction process is accompanied by the release of a large amount of reaction heat, and the high temperature gas after the reaction is recovered. For: a single 4-layer adiabatic reactor is selected for the catalytic reactor, the raw material mixture is preheated to the initial reaction temperature of 180°C, the temperature in the adiabatic reactor is 350-390°C, the pressure is 0.6MPa, and the space velocity is 4000h -1 , the raw material gas after deoxidation treatment is returned to the deoxygenation reaction system to become a circulating gas, which is mixed with the untreated raw material gas; the deoxygenation temperature after the reaction is 450-550 °C, and the high-temperature deoxygenation after the reaction is heated recovered and used to heat boilers.

Embodiment 2

[0028] The oxygen content in the raw material mixed gas is 3%. Under the action of the catalyst, the methane and oxygen in the raw material biogas undergo a catalytic combustion reaction to deoxidize. The reaction process is accompanied by the release of a large amount of reaction heat, and the high temperature gas after the reaction is recovered. For the catalytic reactor, three adiabatic reactors in series are selected, the raw material mixture gas is preheated to the initial reaction temperature of 300°C, and the gas entering other reactors is mixed with the high-temperature gas from the previous reactor without preheating. Reach the initial reaction temperature. The temperature in the first adiabatic reactor is 400-440°C, the pressure is 1.0MPa, and the space velocity is 5000h -1 ; The temperature in the second and third adiabatic reactors is 440-490°C, the pressure is 1.0MPa, and the space velocity is 4000h -1 . The raw material gas after deoxidation treatment is return...

Embodiment 3

[0030] The oxygen content in the raw material mixed gas is 6%. Under the action of the catalyst, the methane and oxygen in the raw material biogas undergo a catalytic combustion reaction to deoxidize. The reaction process is accompanied by the release of a large amount of reaction heat, and the high-temperature gas after the reaction is recovered. Specifically For: the catalytic reactor selects 4 adiabatic reactors connected in series, and the circulating gas is mixed with the raw material gas to control the oxygen content of the gas entering the reactor at about 2%. The gas in the reactor is not preheated, and reaches the initial reaction temperature after mixing with the high-temperature gas from the previous reactor. The temperature in the first adiabatic reactor is 350-400°C, the pressure is 0.8MPa, and the space velocity is 4000h -1 ;The temperature in other adiabatic reactors increases sequentially, 400-600°C, pressure 1.0-1.2MPa, space velocity 4000h -1 . The raw mate...

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PUM

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Abstract

The invention discloses a biogas deoxidization technology. Under the action of a catalyst, methane in the raw material biogas is subjected to catalytic combustion reaction with oxygen so as to be deoxidized, a large amount of reaction heat is discharged along with the reaction process, the high-temperature gas after the reaction is subjected to heat recovering, the raw material gas after the deoxidization treatment is returned back to the deoxidization reaction system as recycling gas which is mixed with the un-treated raw material gas, and the amount of the recycling gas is reduced by multi-stage feeding; the catalytic reactor is a single multi-layer adiabatic reactor or multiple serially connected insulation reactors; and the high-temperature deoxidized gas after the reaction is subjected to heat recovering, and the produced superheated steam is returned back to the deoxidization system to provide power for the system or heat the boiler. By adoption of the biogas deoxidization technology disclosed by the invention, the oxygen in the biogas with the oxygen concentration of 0.4% to 12% can be removed effectively and safely, the heat is used completely and reasonably by the recovering of the reaction heat, and the energy consumption in the deoxidization technology process is effectively reduced, thus the technology is a clean biogas deoxidization technology with low energy consumption.

Description

technical field [0001] The invention relates to a mixed gas deoxygenation technology, in particular to a biogas catalytic deoxidation process and comprehensive utilization of reaction heat. Background technique [0002] Biogas is a mixture of various gases, generally containing 50-70% methane, the rest is 20%-40% carbon dioxide, 0%-5% nitrogen, less than 1% hydrogen, less than 0.4% oxygen and 0. 1% ~ 3% hydrogen sulfide, etc., its characteristics are similar to natural gas. The explosion limit of methane in air at normal temperature and pressure is between 5% and 15%. If the air contains 8.6% to 20.8% (by volume) of biogas, an explosive gas mixture will be formed. Due to the air mixed in the pumping process, there are great safety hazards in the pipeline transportation or separation and concentration production process of biogas, so the deoxygenation treatment of biogas is the premise and basis for further utilization. [0003] The biogas deoxygenation method currently ava...

Claims

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Application Information

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IPC IPC(8): C10L3/10
Inventor 张仕霖
Owner 张仕霖
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