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Modified method to produce biomass synthetic natural gas

A technology for synthesizing natural gas and biomass, applied in the direction of gas fuel, petroleum industry, fuel, etc., can solve the problem of low methane rate, achieve broad application prospects, improve efficiency, and reduce the possibility of deactivation

Inactive Publication Date: 2019-05-24
HENAN POLYTECHNIC UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The gas after methanation still contains saturated water vapor, unreacted CO 2 and H 2, The methane is further purified through the upgrading process, and the methane rate obtained in this way is not high

Method used

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  • Modified method to produce biomass synthetic natural gas
  • Modified method to produce biomass synthetic natural gas

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Comparison scheme
Effect test

Embodiment 1

[0028] An improved method for producing biomass synthetic natural gas, the specific steps are as follows:

[0029] Step 1, a conventional gasification step;

[0030] Step 2, conventional purification and adjustment steps;

[0031] Step 3, conventional methanation step;

[0032] Step 4, hydration step: cooling the methanated product, then using the FICFB method to synthesize SNG through a single-stage fluidized bed, passing SNG into a 3mol / L tetrabutylammonium fluoride solution and maintaining it at a constant temperature, CH 4 Hydrates are formed in the solution, and other gases will escape, and then the hydrates and gases can be separated by filtration, that is, methane is obtained. Most of the gases escaped during the hydration step are CO 2 , can be used as a raw material for generating methane. Since the methanation reaction is a reversible reaction, increasing the concentration of reactants will inevitably lead to the positive reaction. The gas escaped from the hydratio...

Embodiment 2

[0034] An improved method for producing biomass synthetic natural gas, the specific steps are as follows: conventional gasification steps, purification and adjustment steps are performed, and the biomass gas after the second desulfurization is collected in a fluidized bed methanation reactor for In the process of tempering and methanation, the exported gas is denitrified. Since the FICFB method is used to produce methane, the conversion rate of methane in the methanation reactor is only 64%, which means that the biomass gas after denitrification treatment still contains a lot of H 2 , CO, CO 2No methanation was performed. Since the gases coming out of the methanation reactor are all high-temperature gases, the formation of hydrates requires a temperature close to the atmosphere of 302K. Therefore, the surface cooler can be directly used to cool down the biomass gas, and the hot water from the surface cooler can be used as domestic hot water, and the heat will not be wasted. ...

Embodiment 3

[0036] An improved method for producing biomass synthetic natural gas, the specific steps are as follows:

[0037] Step 1, a conventional gasification step;

[0038] Step 2, conventional purification and adjustment steps;

[0039] Step 3, the conventional methanation step, the temperature in the methanation step is 300°C, this temperature is more suitable for the methanation reaction, the methanation reaction is an exothermic process, if the temperature is not properly controlled, the temperature will rise too high , resulting in catalyst deactivation;

[0040] Step 4, hydration step: The methanation product is a high-temperature gas and needs to be cooled before the hydration step, because the hydration process needs to be close to the ambient temperature, and the methanation product is cooled by a surface cooler and comes out of the surface cooler The hot water can be recycled to achieve energy reuse, and then the FICFB method is used to synthesize SNG through a single-sta...

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Abstract

The invention discloses a modified method to produce biomass synthetic natural gas, relates to the technical field of energy and is intended to solve the problem that existing means have low methane yield. The modified method comprises the specific steps of conventional gasification, purification and adjustment, and methanation, as well as hydration, to be specific, synthesizing SNG (synthetic natural gas) with a methanation product by means of an FICFB (fast internal circulating fluidized bed) method, introducing the SNG into tetrabutylammonium fluoride, holding the constant temperature, andfiltering to obtain methane. The quality improving process is replaced with the hydration process; methane can be separated alone according to difference balance points of different gases in a configuration solution, other gases are returned again to the methanation process to generate methane again; the temperature of the methanation process and the quantity of reaction materials are controlled,deactivation chances of a catalyst are slimmed, methanation efficiency is improved at the premise of changing original equipment as little as possible, and reaction heat is recycled.

Description

technical field [0001] The invention relates to the field of energy technology, in particular to an improved method for producing biomass synthetic natural gas. Background technique [0002] Biomass refers to all organisms on the earth that obtain energy through photosynthesis, including all plants, animals and microorganisms on the earth. These organisms store solar energy in the form of chemical energy in the organism through direct or indirect photosynthesis. At present, biomass energy has become the fourth largest energy source besides coal, oil, and natural gas, and occupies an extremely important position in the energy application field of the entire human being. As a large agricultural country, our country has a very rich reserve of biomass. According to statistics, the total amount of various biomass resources in our country is about 5×10 9 Ton. [0003] Biomass gas refers to the conversion of carbohydrates in biomass into H under certain conditions 2 、CH 4 , CO...

Claims

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Application Information

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IPC IPC(8): C10L3/08
Inventor 王发辉陈京宁温小萍赵伟龙陈国艳邓浩鑫张永胜
Owner HENAN POLYTECHNIC UNIV