CN111575072A - Environment-friendly and efficient landfill gas collection, purification and power generation process - Google Patents

Environment-friendly and efficient landfill gas collection, purification and power generation process Download PDF

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CN111575072A
CN111575072A CN202010375469.9A CN202010375469A CN111575072A CN 111575072 A CN111575072 A CN 111575072A CN 202010375469 A CN202010375469 A CN 202010375469A CN 111575072 A CN111575072 A CN 111575072A
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landfill gas
gas
collecting
landfill
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刘田田
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Xinyi Baichuan Changyin New Energy Co ltd
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Xinyi Baichuan Changyin New Energy Co ltd
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/54Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms
    • B01D46/543Particle separators, e.g. dust precipitators, using ultra-fine filter sheets or diaphragms using membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/266Drying gases or vapours by filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/50Sulfur oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/48Sulfur compounds
    • B01D53/52Hydrogen sulfide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/62Carbon oxides
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • C10L3/102Removal of contaminants of acid contaminants
    • C10L3/103Sulfur containing contaminants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • C10L3/102Removal of contaminants of acid contaminants
    • C10L3/104Carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • C10L3/106Removal of contaminants of water
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/50Carbon oxides
    • B01D2257/504Carbon dioxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/80Water
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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Abstract

The invention discloses an environment-friendly and efficient landfill gas collecting, purifying and power generating process which comprises the steps of landfill gas collection, solid-gas separation and gas-liquid separation, adsorption dehumidification, desulfurization by a desulfurizing tower, water washing decarburization, condensation drying, fine filtration, storage, power generation and the like.

Description

Environment-friendly and efficient landfill gas collection, purification and power generation process
Technical Field
The invention relates to the field of landfill gas power generation, in particular to an environment-friendly and efficient landfill gas collection, purification and power generation process.
Technical Field
The Landfill gas is a mixed gas containing methane and carbon dioxide as main components, which is generated by decomposing domestic garbage by microorganisms in a Landfill after the Landfill, and LFG is english abbreviation (Landfill gas) of the Landfill gas. According to different sources and compositions of landfill garbage, landfill gas contains 30-55% of methane by volume, 30-45% of carbon dioxide by volume, and a small amount of air, malodorous gas and other trace gases. Each cubic meter of landfill gas corresponds to about 0.5m3The natural gas or the fuel oil with the heat value of 0.5L, namely the untreated landfill gas has the heat value of 27.8-30.5 MJ/kg, and has high fuel recovery value. In order to solve the problem of the pollution of the buried garbage in the garbage enclosed city and the saturated garbage landfill, the garbage incineration power generation technology is becoming the mainstream, but the garbage incineration power generation technology urgently needs to solve the problems of purification of the garbage landfill gas and serious pollutant emission after the garbage landfill gas is combusted.
Disclosure of Invention
Aiming at the defects, the invention provides the environment-friendly and efficient landfill gas collection, purification and power generation process, which has the advantages of refined process flow, good purification effect and less waste gas generation.
In order to achieve the purpose, the invention provides the following technical scheme:
an environment-friendly and efficient landfill gas collection, purification and power generation process is characterized by comprising the following steps:
a. collecting landfill gas: collecting landfill gas through gas collecting devices uniformly distributed in a landfill site and collecting the landfill gas to a collecting station through a pipeline;
b. solid-gas separation and gas-liquid separation: introducing the landfill gas raw material of the collection station into a separator for solid-gas separation and gas-liquid separation;
c. adsorption and dehumidification: introducing the separated landfill gas into an adsorption dehumidification device for primary drying to remove part of water vapor;
d. desulfurizing in a desulfurizing tower: introducing the landfill gas from which part of water vapor is removed in the previous step into a desulfurizing tower for desulfurization and purification;
e. washing with water for decarburization: introducing the desulfurized landfill gas into a water washing tower for water washing to remove most of carbon dioxide;
f. condensing and drying, namely introducing the decarbonized landfill gas into condensing and drying equipment, and reducing the temperature of the landfill gas to be lower than the dew point temperature by a refrigerating system to condense water vapor in the landfill gas, wherein the condensation heat is taken away by the refrigerating equipment;
g. fine filtering, namely introducing the dried landfill gas into a fine filter for fine filtering;
h. a detector: the detector detects that the landfill gas is qualified and then enters the next step;
i. and (3) storage: storing the qualified landfill gas into a double-layer membrane gas storage cabinet;
j. generating electricity: after being pressurized, the gas enters a gas power generation system to generate power, and the concentration of the waste gas is detected.
Further, according to the environment-friendly and efficient landfill gas collection, purification and power generation process, the step a specifically comprises the following steps: the vertical collecting shafts are arranged in the vertical collecting shafts of the pipelines with holes in the landfill vertical shaft at intervals of 20-30 m, each 6-8 collecting shafts are provided with a gas collecting cabinet to form a group of conveying systems, and each gas collecting cabinet is provided with an independent pipeline connected to a collecting station.
Furthermore, according to the environment-friendly and efficient landfill gas collecting, purifying and power generating process, the separator in the step b is a defoaming separator, landfill gas output by the collecting station enters the defoaming separator from the upper part of the defoaming separator, impurities such as soil dust and sewage are discharged from the lower part of the defoaming separator, and the separated landfill gas is output from the upper part of the defoaming separator.
Further, according to the environment-friendly and efficient landfill gas collection, purification and power generation process, the step c specifically comprises the following steps: introducing landfill gas into an adsorption bed formed by stacking solid adsorbents, and adsorbing water gas on the solid adsorbents by utilizing the capillary action; the solid adsorbent is selected from one or more of activated carbon, zeolite, calcium chloride and silica gel.
Further, according to the environment-friendly and efficient landfill gas collection, purification and power generation process, the step d specifically comprises the following steps: the landfill gas enters from the bottom of the desulfurization tower and is in countercurrent contact reaction with sodium hydroxide liquid, the purified landfill gas is discharged from the top of the tower, and oxygen is used for regenerating the absorption liquid.
Further, in the environment-friendly and efficient landfill gas collection, purification and power generation process, the step e specifically comprises the following steps: and (3) compressing the desulfurized landfill gas, compressing the gas to be more than 2.5MPa by using a compressor, entering the lower part of the water absorption washing tower, and carrying out heat and mass exchange by countercurrent contact with cooling water sprayed from the upper part of the water absorption washing tower to absorb carbon dioxide until the concentration of the carbon dioxide in the landfill gas is lower than 2%.
Further, in the environment-friendly and efficient garbage landfill gas collecting, purifying and power generating process, the fine filter in the step g is provided with a multilayer film filtering structure.
Further, according to the environment-friendly and efficient garbage landfill gas collecting, purifying and power generating process, the multilayer film filtering structure sequentially comprises a polydimethylsiloxane film, a polysulfone film, a cellulose acetate film, an ethyl cellulose film and a polycarbonate film.
Further, in the environment-friendly and efficient landfill gas collection, purification and power generation process, the qualified standard of the landfill gas in the step h is as follows: methane content above 95%, carbon dioxide content below 2%, sulfide content below 10mg/m3Hereinafter, the relative humidity is 75% or less.
Further, in the environment-friendly and efficient landfill gas collecting, purifying and power generating process, HC in the exhaust gas emission in the step j is lower than 40pm, CO is lower than 0.010%, and NOx is lower than 100 ppm.
The scheme shows that the invention at least has the following beneficial effects: the invention discloses an environment-friendly and efficient landfill gas collection, purification and power generation process, which effectively removes water, sulfur and carbon dioxide impurities in landfill gas in a landfill site through steps of landfill gas collection, solid-gas separation and gas-liquid separation, adsorption dehumidification, desulfurization by a desulfurizing tower, water washing for decarbonization, condensation drying, fine filtration, storage, power generation and the like, and has good purification effect, the obtained gas has a methane content of more than 95 percent, a carbon dioxide content of less than 2 percent and a sulfide content of 10mg/m3The relative humidity is less than 75%, the requirements of gas power generation on gas quality are met, power generation equipment is protected, waste gas generated after power generation can meet the environmental protection standard for emission, the whole purification process flow is refined, the requirements on equipment are low, the cost is low, and the environment is protected.
Drawings
Fig. 1 is a flow chart of an environment-friendly and efficient landfill gas collection, purification and power generation process described in examples 1-3.
Detailed Description
The invention will be further elucidated by means of several specific examples, which are intended to be illustrative only and not limiting.
Example 1
The environment-friendly and efficient landfill gas collection, purification and power generation process shown in the figure 1 comprises the following steps:
a. collecting landfill gas: collecting vertical shafts are arranged at intervals of 20 m through vertical perforated pipelines arranged in the vertical shafts of the landfill, a gas collecting cabinet is arranged in each 6 collecting wells to form a group of conveying systems, and each gas collecting cabinet is provided with an independent pipeline connected to a collecting station;
b. solid-gas separation and gas-liquid separation: introducing a landfill gas raw material of a collecting station into a defoaming separator, wherein the landfill gas output by the collecting station enters the defoaming separator from the upper part of the defoaming separator, impurities such as soil dust and sewage are discharged from an outlet at the lower part of the defoaming separator, and the separated landfill gas is output from the upper part of the defoaming separator;
c. adsorption and dehumidification: introducing the landfill gas obtained in the previous step into an adsorption bed formed by stacking solid adsorbents, and adsorbing water vapor on the solid adsorbents by utilizing the capillary action; the solid adsorbent is selected from activated carbon: zeolite =1:1 (volume ratio);
d. desulfurizing in a desulfurizing tower: introducing the landfill gas from which part of water vapor is removed into a desulfurization tower for desulfurization and purification, wherein the landfill gas enters from the bottom of the desulfurization tower and is in countercurrent contact reaction with sodium hydroxide liquid, the purified landfill gas is discharged from the top of the tower, and oxygen is used for regenerating absorption liquid;
e. washing with water for decarburization: compressing the desulfurized landfill gas, compressing the gas to be more than 2.5Mpa by a compressor, entering the lower part of a water absorption washing tower, and carrying out heat and mass exchange by countercurrent contact with cooling water sprayed from the upper part of the water absorption washing tower to absorb carbon dioxide gas until the concentration of the carbon dioxide in the landfill gas is lower than 2%;
f. condensing and drying, namely introducing the decarbonized landfill gas into condensing and drying equipment, and reducing the temperature of the landfill gas to be lower than the dew point temperature by a refrigerating system to condense water vapor in the landfill gas, wherein the condensation heat is taken away by the refrigerating equipment;
g. fine filtering, namely introducing the dried landfill gas into a fine filter for fine filtering; a multilayer film filtering structure is arranged in the fine filter; the multilayer film filtering structure sequentially comprises a polydimethylsiloxane film, a polysulfone film, a cellulose acetate film, an ethyl cellulose film and a polycarbonate film;
h. a detector: the detector detects that the landfill gas is qualified and then enters the next step; the qualified standard is as follows: methane content is more than 95%, carbon dioxide content is less than 2%, sulfide content is less than 10mg/m3, and relative humidity is less than 75%;
i. and (3) storage: storing the qualified landfill gas into a double-layer membrane gas storage cabinet;
j. generating electricity: after being pressurized, the gas enters a gas power generation system to generate power, and the concentration of the waste gas is detected.
Example 2
The environment-friendly and efficient landfill gas collection, purification and power generation process shown in the figure 1 comprises the following steps:
a. collecting landfill gas: collecting vertical shafts are arranged at intervals of 25 m through vertical perforated pipelines arranged in the vertical shafts of the landfill, gas collecting cabinets are arranged in 7 collecting wells to form a group of conveying systems, and each gas collecting cabinet is provided with an independent pipeline connected to a collecting station;
b. solid-gas separation and gas-liquid separation: introducing a landfill gas raw material of a collecting station into a defoaming separator, wherein the landfill gas output by the collecting station enters the defoaming separator from the upper part of the defoaming separator, impurities such as soil dust and sewage are discharged from an outlet at the lower part of the defoaming separator, and the separated landfill gas is output from the upper part of the defoaming separator;
c. adsorption and dehumidification: introducing the landfill gas obtained in the previous step into an adsorption bed formed by stacking solid adsorbents, and adsorbing water vapor on the solid adsorbents by utilizing the capillary action; the solid adsorbent is selected from calcium chloride: silica gel =2:1 (volume ratio);
d. desulfurizing in a desulfurizing tower: introducing the landfill gas from which part of water vapor is removed into a desulfurization tower for desulfurization and purification, wherein the landfill gas enters from the bottom of the desulfurization tower and is in countercurrent contact reaction with sodium hydroxide liquid, the purified landfill gas is discharged from the top of the tower, and oxygen is used for regenerating absorption liquid;
e. washing with water for decarburization: compressing the desulfurized landfill gas, compressing the gas to be more than 3.0Mpa by a compressor, entering the lower part of a water absorption washing tower, and carrying out heat and mass exchange by countercurrent contact with cooling water sprayed from the upper part of the water absorption washing tower to absorb carbon dioxide gas until the concentration of the carbon dioxide in the landfill gas is lower than 1.8%;
f. condensing and drying, namely introducing the decarbonized landfill gas into condensing and drying equipment, and reducing the temperature of the landfill gas to be lower than the dew point temperature by a refrigerating system to condense water vapor in the landfill gas, wherein the condensation heat is taken away by the refrigerating equipment;
g. fine filtering, namely introducing the dried landfill gas into a fine filter for fine filtering; a multilayer film filtering structure is arranged in the fine filter; the multilayer film filtering structure sequentially comprises a polydimethylsiloxane film, a polysulfone film, a cellulose acetate film, an ethyl cellulose film and a polycarbonate film;
h. a detector: the detector detects that the landfill gas is qualified and then enters the next step; the qualified standard is as follows: methane content above 95%, carbon dioxide content below 2%, sulfide content below 10mg/m3Hereinafter, the relative humidity is 75% or less;
i. and (3) storage: storing the qualified landfill gas into a double-layer membrane gas storage cabinet;
j. generating electricity: after being pressurized, the gas enters a gas power generation system to generate power, and the concentration of the waste gas is detected.
Example 3
The environment-friendly and efficient landfill gas collection, purification and power generation process shown in the figure 1 comprises the following steps:
a. collecting landfill gas: collecting vertical shafts are arranged at intervals of 30 m through vertical perforated pipelines arranged in the vertical shafts of the landfill, a gas collecting cabinet is arranged in each 8 collecting wells to form a group of conveying systems, and each gas collecting cabinet is provided with an independent pipeline connected to a collecting station;
b. solid-gas separation and gas-liquid separation: introducing a landfill gas raw material of a collecting station into a defoaming separator, wherein the landfill gas output by the collecting station enters the defoaming separator from the upper part of the defoaming separator, impurities such as soil dust and sewage are discharged from an outlet at the lower part of the defoaming separator, and the separated landfill gas is output from the upper part of the defoaming separator;
c. adsorption and dehumidification: introducing the landfill gas obtained in the previous step into an adsorption bed formed by stacking solid adsorbents, and adsorbing water vapor on the solid adsorbents by utilizing the capillary action; the solid adsorbent is selected from activated carbon: silica gel =1:2 (volume ratio);
d. desulfurizing in a desulfurizing tower: introducing the landfill gas from which part of water vapor is removed into a desulfurization tower for desulfurization and purification, wherein the landfill gas enters from the bottom of the desulfurization tower and is in countercurrent contact reaction with sodium hydroxide liquid, the purified landfill gas is discharged from the top of the tower, and oxygen is used for regenerating absorption liquid;
e. washing with water for decarburization: compressing the desulfurized landfill gas, compressing the gas to be more than 3.0Mpa by a compressor, entering the lower part of a water absorption washing tower, and carrying out heat and mass exchange by countercurrent contact with cooling water sprayed from the upper part of the water absorption washing tower to absorb carbon dioxide gas until the concentration of the carbon dioxide in the landfill gas is lower than 1.8%;
f. condensing and drying, namely introducing the decarbonized landfill gas into condensing and drying equipment, and reducing the temperature of the landfill gas to be lower than the dew point temperature by a refrigerating system to condense water vapor in the landfill gas, wherein the condensation heat is taken away by the refrigerating equipment;
g. fine filtering, namely introducing the dried landfill gas into a fine filter for fine filtering; a multilayer film filtering structure is arranged in the fine filter; the multilayer film filtering structure sequentially comprises a polydimethylsiloxane film, a polysulfone film, a cellulose acetate film, an ethyl cellulose film and a polycarbonate film;
h. a detector: the detector detects that the landfill gas is qualified and then enters the next step; the qualified standard is as follows: the methane content is more than 95 percent, the carbon dioxide content is less than 2 percent, and sulfuration is carried outThe content of the substance is 10mg/m3Hereinafter, the relative humidity is 75% or less;
i. and (3) storage: storing the qualified landfill gas into a double-layer membrane gas storage cabinet;
j. generating electricity: after being pressurized, the gas enters a gas power generation system to generate power, and the concentration of the waste gas is detected.
Example 4
Test example
Through tests, as shown in examples 1-3, the disclosed environment-friendly and efficient landfill gas collection, purification and power generation process can effectively remove water, sulfur and carbon dioxide impurities in the landfill gas, and has good purification effect, wherein the obtained gas has a methane content of more than 95%, a carbon dioxide content of less than 2%, and a sulfide content of 10mg/m3The relative humidity is below 75%, so that the requirement of gas power generation on gas quality is met, and power generation equipment is protected; meanwhile, in the exhaust emission detection after power generation, HC is lower than 40pm, CO is lower than 0.010%, and NOx is lower than 100ppm, so that the exhaust emission detection method meets the environmental emission standard.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that modifications can be made by those skilled in the art without departing from the principle of the present invention, and these modifications should also be construed as the protection scope of the present invention.

Claims (10)

1. An environment-friendly and efficient landfill gas collection, purification and power generation process is characterized by comprising the following steps:
a. collecting landfill gas: collecting landfill gas through gas collecting devices uniformly distributed in a landfill site and collecting the landfill gas to a collecting station through a pipeline;
b. solid-gas separation and gas-liquid separation: introducing the landfill gas raw material of the collection station into a separator for solid-gas separation and gas-liquid separation;
c. adsorption and dehumidification: introducing the separated landfill gas into an adsorption dehumidification device for primary drying to remove part of water vapor;
d. desulfurizing in a desulfurizing tower: introducing the landfill gas from which part of water vapor is removed in the previous step into a desulfurizing tower for desulfurization and purification;
e. washing with water for decarburization: introducing the desulfurized landfill gas into a water washing tower for water washing to remove most of carbon dioxide;
f. condensation and drying: introducing the decarbonized landfill gas into a condensation drying device, and reducing the temperature of the landfill gas to be below the dew point temperature by a refrigeration system to condense water vapor in the landfill gas, wherein the condensation heat is taken away by the refrigeration device;
g. fine filtering, namely introducing the dried landfill gas into a fine filter for fine filtering;
h. and (3) detection: the detector detects that the landfill gas is qualified and then enters the next step;
i. and (3) storage: storing the qualified landfill gas into a double-layer membrane gas storage cabinet;
j. generating electricity: after being pressurized, the gas enters a gas power generation system to generate power, and the concentration of the waste gas is detected.
2. The environment-friendly and efficient landfill gas collecting, purifying and power generating process of claim 1, wherein the step a specifically comprises: the vertical collecting shafts are arranged in the vertical collecting shafts of the pipelines with holes in the landfill vertical shaft at intervals of 20-30 m, each 6-8 collecting shafts are provided with a gas collecting cabinet to form a group of conveying systems, and each gas collecting cabinet is provided with an independent pipeline connected to a collecting station.
3. The environment-friendly and efficient landfill gas collecting, purifying and power generating process as claimed in claim 1, wherein the separator in the step b is a defoaming separator, the landfill gas output by the collecting station enters the defoaming separator from the upper part of the defoaming separator, impurities such as soil dust and sewage are discharged from the lower outlet of the defoaming separator, and the separated landfill gas is output from the upper part of the defoaming separator.
4. The environment-friendly and efficient landfill gas collecting, purifying and power generating process of claim 1, wherein the step c specifically comprises: introducing landfill gas into an adsorption bed formed by stacking solid adsorbents, and adsorbing water gas on the solid adsorbents by utilizing the capillary action; the solid adsorbent is selected from one or more of activated carbon, zeolite, calcium chloride and silica gel.
5. The environment-friendly and efficient landfill gas collecting, purifying and power generating process of claim 1, wherein the step d specifically comprises: the landfill gas enters from the bottom of the desulfurization tower and is in countercurrent contact reaction with sodium hydroxide liquid, the purified landfill gas is discharged from the top of the tower, and oxygen is used for regenerating the absorption liquid.
6. The environment-friendly and efficient landfill gas collection, purification and power generation process according to claim 1, wherein the step e specifically comprises: and (3) compressing the desulfurized landfill gas, compressing the gas to be more than 2.5MPa by using a compressor, entering the lower part of the water absorption washing tower, and carrying out heat and mass exchange by countercurrent contact with cooling water sprayed from the upper part of the water absorption washing tower to absorb carbon dioxide until the concentration of the carbon dioxide in the landfill gas is lower than 2%.
7. The environment-friendly and efficient landfill gas collecting, purifying and power generating process of claim 1, wherein a multi-layer membrane filtering structure is arranged in the fine filter in the step g.
8. The environment-friendly and efficient landfill gas collecting, purifying and power generating process of claim 7, wherein the multi-layer membrane filtering structure is a polydimethylsiloxane membrane, a polysulfone membrane, a cellulose acetate membrane, an ethyl cellulose membrane, and a polycarbonate membrane in sequence.
9. The environment-friendly and efficient landfill gas collecting, purifying and power generating process of claim 1, wherein the landfill gas qualification standard of the step h is as follows: methane content above 95%, carbon dioxide content below 2%, sulfide content below 10mg/m3Hereinafter, the relative humidity is 75% or less.
10. The environment-friendly and efficient landfill gas collecting, purifying and power generating process of claim 1, wherein the exhaust emission in the step j has HC below 40pm, CO below 0.010%, and NOx below 100 ppm.
CN202010375469.9A 2020-05-07 2020-05-07 Environment-friendly and efficient landfill gas collection, purification and power generation process Pending CN111575072A (en)

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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1554491A (en) * 2003-12-23 2004-12-15 南京大学 Comprehensive utilization system for garbage burying gas resource
WO2009002969A2 (en) * 2007-06-27 2008-12-31 H R D Corporation System and process for gas sweetening
CN101502736A (en) * 2009-01-21 2009-08-12 东莞市康达机电工程有限公司 Landfill gas power generation pretreatment method and pretreatment device thereof
CN102190541A (en) * 2010-03-12 2011-09-21 北京环卫集团环境研究发展有限公司 Method for recovering methane for industrial production of clean fuel through deep purification of landfill gas
KR20130122903A (en) * 2010-05-14 2013-11-11 캠브리언 에너지 디벨롭먼트 엘엘씨 Bio vapor stimulation system
CN204897857U (en) * 2015-08-31 2015-12-23 南通天蓝环保能源成套设备有限公司 Landfill gas is collected and is utilized system
CN107858184A (en) * 2017-12-13 2018-03-30 北京环境工程技术有限公司 A kind of landfill gas purification produces the method and system of natural gas
CN207445784U (en) * 2017-09-20 2018-06-05 深圳相控科技股份有限公司 A kind of landfill gas power generation pretreatment unit
CN208526055U (en) * 2018-03-19 2019-02-22 海南康达新能源有限公司 A kind of stable garbage loading embeading gas pretreating system
CN210332167U (en) * 2019-05-22 2020-04-17 无锡天顺环境技术有限公司 Pretreatment device with modular air-cooled cold and hot water unit

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1554491A (en) * 2003-12-23 2004-12-15 南京大学 Comprehensive utilization system for garbage burying gas resource
WO2009002969A2 (en) * 2007-06-27 2008-12-31 H R D Corporation System and process for gas sweetening
CN101502736A (en) * 2009-01-21 2009-08-12 东莞市康达机电工程有限公司 Landfill gas power generation pretreatment method and pretreatment device thereof
CN102190541A (en) * 2010-03-12 2011-09-21 北京环卫集团环境研究发展有限公司 Method for recovering methane for industrial production of clean fuel through deep purification of landfill gas
KR20130122903A (en) * 2010-05-14 2013-11-11 캠브리언 에너지 디벨롭먼트 엘엘씨 Bio vapor stimulation system
CN204897857U (en) * 2015-08-31 2015-12-23 南通天蓝环保能源成套设备有限公司 Landfill gas is collected and is utilized system
CN207445784U (en) * 2017-09-20 2018-06-05 深圳相控科技股份有限公司 A kind of landfill gas power generation pretreatment unit
CN107858184A (en) * 2017-12-13 2018-03-30 北京环境工程技术有限公司 A kind of landfill gas purification produces the method and system of natural gas
CN208526055U (en) * 2018-03-19 2019-02-22 海南康达新能源有限公司 A kind of stable garbage loading embeading gas pretreating system
CN210332167U (en) * 2019-05-22 2020-04-17 无锡天顺环境技术有限公司 Pretreatment device with modular air-cooled cold and hot water unit

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
沈剑山: "《生物质能源沼气发电》", 31 March 2009 *

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