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Energy-saving decarbonization process for biogas

A biogas and decarbonization technology, applied in the petroleum industry, gas fuel, fuel, etc., can solve the problems of energy consumption, affecting the absorption capacity, increasing the amount of circulating water, etc., and achieve the effect of saving water and improving yield

Inactive Publication Date: 2013-01-16
BIOLOGICAL CHEM ENG CENT ZHENGZHOUUNIV
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Problems solved by technology

[0007] The energy in the above-mentioned decarbonization process is not effectively utilized, the energy consumption is high, the absorption water temperature is low, refrigeration equipment is required, and energy is consumed
CO dissolved in water 2 Relying on flash analysis, there are more residues, which affects the absorption capacity and increases the amount of circulating water

Method used

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  • Energy-saving decarbonization process for biogas

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Embodiment Construction

[0020] Such as figure 1 As shown, the desulfurized biogas is compressed by a compressor to increase the pressure to 2MPa, and then enters the first-stage absorption tower, where water at room temperature at 25°C is used as an absorbent for CO 2 Absorption, the exhaust phase at the top of the primary absorption tower is methane gas with a purity of 97%, which is used as a product; the liquid phase at the bottom of the primary absorption tower is sent to the primary hydraulic turbine for energy recovery, and then sent to to the first-level desorption tower; the pressure inside the first-level desorption tower is maintained at 0.7 MPa, and the temperature is 25°C. The gas phase discharged from the top of the first-level desorption tower is sent to the second-level absorption tower for further absorption of CO 2 ; The pressure inside the secondary absorption tower is maintained at 0.7 MPa, and the temperature is 25°C. The exhaust phase at the top of the secondary absorption tower ...

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Abstract

The invention discloses an energy-saving decarbonization process for biogas. Biogas which is subjected to desulfurization is compressed by a compressor, then the compressed biogas flows through an absorption tower, CO2 is absorbed, and methane is discharged; a liquid phase at the tower bottom of the absorption tower flows through a hydraulic turbine for energy recovery, then the liquid phase which is subjected to energy recovery flows through an analytic tower for analysis, CO2 is discharged, and the liquid phase at the tower bottom of the analytic tower is conveyed to the absorption tower and is used as an absorbent to be recycled. In the decarbonization process, freeze water is not needed, washing water is water at the normal temperature of less than 30 DEG C, absorption and analysis are performed at normal temperature, and energy required by freezing is not needed to be provided; by the hydraulic turbine, energy can be recycled; and a two-stage absorption tower is used for absorption, so that the yield of methane is improved, and energy consumption and cost are greatly reduced.

Description

technical field [0001] The invention relates to a biogas energy-saving decarbonization process. Background technique [0002] With the shortage of petrochemical resources, the development of secondary energy has become the main development strategy of all countries in the world. Biogas is not only rich in raw materials, but also low in cost, cheap, high in combustion thermal efficiency, and renewable. It is a clean fuel with excellent performance and is also the main aspect of the current new energy development. [0003] Biogas usually contains about (55~60)% methane, (40~45)% carbon dioxide and other small amounts of impurity gases. Domestic biogas is mainly used as fuel for rural stoves, which is not widely used and has low use value. After biogas is purified and decarbonized, its methane content can reach more than 95%, which can be called bio-natural gas, which can be used as vehicle fuel gas and chemical raw materials. wider. [0004] At present, the decarbonization ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10L3/10
Inventor 李洪亮陈俊英马晓建刘利平
Owner BIOLOGICAL CHEM ENG CENT ZHENGZHOUUNIV
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