CN113636536B - Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes - Google Patents

Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes Download PDF

Info

Publication number
CN113636536B
CN113636536B CN202110645593.7A CN202110645593A CN113636536B CN 113636536 B CN113636536 B CN 113636536B CN 202110645593 A CN202110645593 A CN 202110645593A CN 113636536 B CN113636536 B CN 113636536B
Authority
CN
China
Prior art keywords
hydrothermal
carbon
solid
wood fiber
acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202110645593.7A
Other languages
Chinese (zh)
Other versions
CN113636536A (en
Inventor
余强
谢君
钟家伟
毕桂灿
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
South China Agricultural University
Original Assignee
South China Agricultural University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by South China Agricultural University filed Critical South China Agricultural University
Priority to CN202110645593.7A priority Critical patent/CN113636536B/en
Publication of CN113636536A publication Critical patent/CN113636536A/en
Application granted granted Critical
Publication of CN113636536B publication Critical patent/CN113636536B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/05Preparation or purification of carbon not covered by groups C01B32/15, C01B32/20, C01B32/25, C01B32/30
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P5/00Preparation of hydrocarbons or halogenated hydrocarbons
    • C12P5/02Preparation of hydrocarbons or halogenated hydrocarbons acyclic
    • C12P5/023Methane
    • 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

Landscapes

  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Inorganic Chemistry (AREA)
  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention discloses a method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes, which is characterized in that choline chloride and ferric chloride are added into water to form an autocatalytic dissolution system, so that the hydrothermal carbonization reaction temperature is obviously reduced, the process energy consumption is reduced, the specific surface area of hydrothermal carbon can be increased, and the adsorption capacity of the hydrothermal carbon is improved. Meanwhile, while solid carbon is obtained, acid-rich micromolecule liquid products are generated, and the products are inoculated into anaerobic fermentation strains to quickly generate biological methane. Compared with other synergistic methods such as acid-base pretreatment and the like, the method has the advantages of simple process, better sustainability and larger application potential.

Description

Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes
Technical Field
The invention belongs to the field of organic solid waste resource utilization, and particularly relates to a method for co-producing biomethane by hydrothermal carbonization of wood fiber waste.
Background
Hydrothermal carbonization is an important way for recycling organic solid wastes, is widely concerned due to the advantages of mild reaction conditions, strong raw material adaptability and the like, and hydrothermal carbon has proved to have the characteristics of high carbon content, low oxygen content, strong hydrophobicity, high calorific value, energy density and the like, and can be used in the fields of carbon fixation, soil improvement, solid fuels, adsorption, catalysis and the like. Organic solid waste that has been currently reported for hydrothermal carbonization and carbonization temperatures thereof are: mushroom dregs, such as edible mushroom dregs 200-250 ℃ (CN 104312590A), biogas dregs 200-240 ℃ (CN 111847938A), algae dregs algae mud 160-220 ℃ (CN 105668564A), vegetable and fruit peel, such as cane shoot 150-350 ℃ (CN 106044745B), shaddock peel 230 ℃ (CN 112547009A), shinyleaf yellowhorn 200-240 ℃ (CN 106044745B), longan core 160-320 ℃ (CN 10596503962A), watermelon peel 170 ℃ (CN 109503526B), sludge and feces, such as municipal sludge 200-260 ℃ (CN 10987676770A), municipal refuse 250-400 ℃ (CN 10610667461B), livestock and poultry feces 200-350 ℃ (CN 110523767A), and wood fiber, such as Chinese hemp stalk 74747409A, chinese soapberry dregs CN 200-200 ℃ (CN 1101947095B), chinese hemp stalk 1101105241160 ℃ (CN 11012A), wheat straw 112112220-11269290 ℃ and CN 110753220 (CN 1117095B). Although the hydrothermal reaction temperature of the prior art is greatly reduced compared with that of the prior art for preparing the carbon by pyrolysis (300-800 ℃), the carbonization temperature is still higher, and the reduction of the energy consumption in the carbonization process has great significance for improving the economic efficiency of resource utilization of the organic solid waste. Chinese patent CN109628499A discloses a high-temperature hydrothermal method for improving the biogas production of garden wastes, which is to pretreat garden waste raw materials or/and other lignocellulose biomass by using water and choline chloride as reaction solutions, remove lignin to the maximum extent under the condition of retaining fermentable sugars such as cellulose, hemicellulose and the like, and obviously improve the fermentation efficiency of biogas of the garden wastes, thereby realizing the high-efficiency energy conversion of the garden wastes, but does not relate to the hydrothermal carbonization of organic solid wastes.
Disclosure of Invention
The invention aims to overcome the defects in the prior art and provide a method for preparing hydrothermal carbon by hydrothermal carbonization of wood fiber wastes.
The second purpose of the invention is to provide the application of the method for preparing the hydrothermal carbon by the hydrothermal carbonization of the wood fiber wastes in the preparation of the biomethane
The above purpose of the invention is realized by the following technical scheme:
a method for preparing hydrothermal carbon by hydrothermal carbonization of wood fiber wastes is characterized by mixing choline chloride and water according to a mass ratio of 2-5: 10 to 20g/ml is mixed with agricultural and forestry waste and FeCl is added 3 Reacting for 3-9 h at 140-180 ℃ in a high-pressure reaction kettle; after the reaction is finished, carrying out solid-liquid separation, and drying the solid product to obtain the agricultural and forestry waste hydrothermal carbon.
The choline chloride-water-ferric chloride-based autocatalytic dissolution system provided by the invention can realize high-efficiency carbonization of the lignocellulose component at low temperature, remarkably reduce the carbonization reaction temperature, reduce the process energy consumption, improve the specific surface area of the hydrothermal carbon and improve the adsorption capacity of the hydrothermal carbon. Meanwhile, while solid carbon is obtained, acid-rich micromolecule liquid products are generated, and further, biological methane can be generated through rapid anaerobic fermentation.
Preferably, said FeCl 3 The addition amount of the catalyst is 1-4 g/g material.
Further preferably, the FeCl 3 The addition amount of the catalyst is 2-4 g/g material.
Preferably, the solid-to-liquid ratio is 1.
Preferably, the mass ratio of the choline chloride to the water is 2-3.
Preferably, the reaction is carried out at 160-180 ℃ for 3-5.
Preferably, the stirring speed of the high-pressure reaction kettle is 200-400 rpm.
Further preferably, the solid-liquid ratio is 1.
The invention also provides application of any one of the methods in preparation of biomethane, wherein liquid products obtained after solid-liquid separation are inoculated into anaerobic fermentation strains for biological fermentation to obtain biomethane.
Compared with the prior art, the invention has the following beneficial effects:
according to the hydrothermal carbon preparation method, choline chloride and ferric chloride are added into water to form an autocatalytic dissolution system, so that the carbonization reaction temperature can be remarkably reduced, the process energy consumption is reduced, the specific surface area of the hydrothermal carbon can be increased, and the adsorption capacity of the hydrothermal carbon is improved. Meanwhile, while solid carbon is obtained, acid-rich micromolecule liquid products are generated, and the products are inoculated into anaerobic fermentation strains to quickly generate biological methane. Compared with other synergistic methods such as acid-base pretreatment and the like, the method has the advantages of simple process, better sustainability and larger application potential.
Detailed Description
The present invention will be further described with reference to the following specific examples, which are not intended to limit the invention in any manner. Reagents, methods and apparatus used in the present invention are conventional in the art unless otherwise indicated.
Unless otherwise indicated, reagents and materials used in the following examples are commercially available.
Example 1
Mixing choline chloride and water according to a mass ratio of 5:1, adding garden waste according to a solid-liquid ratio of 1 to 20 (g/ml), and adding FeCl 3 2g/g of catalyst, the reaction conditions in a high-pressure reaction kettle are 140-9 h, the stirring speed of the reaction kettle is 200rpm, after the reaction is finished, the solid-liquid mixture is filtered and separated, and the solid product is dried to obtain the gardenThe waste hydrothermal carbon has an adsorption capacity of 118mg/g for methylene blue, the same raw materials are used for preparing carbon under the conventional hydrothermal condition (only pure water and the same reaction conditions are used), the adsorption capacity of the methylene blue is only 21mg/g, the same raw materials are directly pyrolyzed to prepare carbon (800-1 h in a tubular furnace and under the nitrogen flow), and the adsorption capacity of the methylene blue is 98mg/g. Liquid products produced in the conventional hydrothermal carbon preparation process are rich in furan or benzene ring compounds such as furfural, 5-hydroxymethylfurfural and coumarin, and need to be subjected to complex directional catalytic reforming for utilization, a pyrolytic carbon liquid product is bio-oil with more complex components, the liquid product obtained by the method is rich in small molecular acid, wherein acetic acid is 5.4g/l, formic acid is 3.5g/l, and levulinic acid is 1.5g/l, the product is easier to be directly and mildly converted by microorganisms, anaerobic fermentation strains are directly inoculated according to a method reported in the literature (Bioresource. Technol.2018,55, 205-212), and the biomethane can be obtained after fermentation for 5 hours.
Example 2
Mixing choline chloride and water according to a mass ratio of 3:1, adding garden waste according to a solid-liquid ratio of 1 to 15 (g/ml), and adding FeCl 3 The method comprises the following steps of preparing 3g/g of a material by using a catalyst in a high-pressure reaction kettle under the reaction condition of 160-5 h, stirring the reaction kettle at the rotating speed of 400rpm, filtering and separating a solid-liquid mixture after the reaction is finished, drying a solid product to obtain the hydrothermal carbon of the garden waste, wherein the adsorption capacity of the carbon to methylene blue is 141mg/g, the same raw materials are used for preparing the carbon under the conventional hydrothermal condition (only pure water and the other reaction conditions are the same), the adsorption capacity of the methylene blue is only 34mg/g, the same raw materials are directly pyrolyzed to prepare the carbon (a tubular furnace is 800-1 h, nitrogen flow), and the adsorption capacity of the methylene blue is 98mg/g. Liquid products produced in the conventional hydrothermal carbon preparation process are rich in furan or benzene ring compounds such as furfural, 5-hydroxymethylfurfural and coumarin, and need complicated directional catalytic reforming for utilization, and a pyrolytic carbon liquid product is bio-oil with more complicated components, the liquid product obtained by the method is rich in small molecular acid, wherein the acetic acid is 6.2g/l, the levulinic acid is 1.8g/l, the formic acid is 0.6g/l, and the glycolic acid is 0.2g/l, so that the product is easier to be directly and mildly converted by microorganisms, anaerobic fermentation strains are directly inoculated according to a method reported in the literature (Bioresource, technol.2018,55, 205-212), and the biomethane can be obtained after fermentation for 3h.
Example 3
Choline chloride and water are mixed according to the mass ratio of 2:1, adding garden waste according to a solid-liquid ratio of 1 to 10 (g/ml), and adding FeCl 3 4g/g of catalyst is put in a high-pressure reaction kettle under the reaction condition of 180-3 h, the stirring speed of the reaction kettle is 300rpm, after the reaction is finished, solid-liquid mixture is filtered and separated, a solid product is dried to obtain the hydrothermal carbon of the garden waste, the adsorption quantity of the carbon to methylene blue is 169mg/g, the same raw materials are used for preparing the carbon under the conventional hydrothermal condition (pure water, the other reaction conditions are the same), the adsorption quantity of the methylene blue is only 40mg/g, the same raw materials are directly pyrolyzed to prepare the carbon (a tubular furnace is 800-1 h, nitrogen flow), and the adsorption quantity of the methylene blue is 98mg/g. Liquid products produced in the conventional hydrothermal carbon preparation process are rich in furan or benzene ring compounds such as furfural, 5-hydroxymethylfurfural and coumarin, and need complicated directional catalytic reforming for utilization, and a pyrolytic carbon liquid product is bio-oil with more complicated components, the liquid product obtained by the method is rich in small molecular acid, wherein 10.4g/l of acetic acid, 3.5g/l of levulinic acid, 0.8g/l of formic acid and 0.7g/l of glycolic acid are easy to directly and mildly convert by microorganisms, anaerobic fermentation strains are directly inoculated according to a method reported in the literature (Bioresource, technol.2018,55, 205-212), and biomethane can be obtained after 2h of fermentation.
Comparative example 1
The effects of different treatment conditions on the elemental composition, BET specific surface area and total pore volume of the samples were compared. Wherein GW: garden waste; GHC op : choline chloride/water/FeCl 3 The system has a solid-liquid ratio of 1 to 10g/ml, and the mass ratio of choline chloride to water is 2 3 The adding amount of the catalyst is 4g/g of material, and the reaction condition is that the reaction is carried out for 3 hours at 180 ℃; reference GHC op The temperature, time and solid-to-liquid ratio conditions are that GHC-1 is a single hydrothermal system; GHC-2 is choline chloride/water system.
The results are shown in Table 1, along with untreated material GW and carbon GHC-1 from a single hydrothermal system and carbon GHC-2,GHC from a choline chloride/water system op Under the condition, the content, specific surface area and total pore volume of the charcoal element of the biological charcoal are greatly improved, which is beneficial to improving the adsorption capacity.
Table 1 elemental composition, BET specific surface area and Total pore volume of the samples
Figure RE-GDA0003298613780000041
Comparative example 2
By comparing the influence of different metal salt promoters on the adsorption performance of the hydrothermal carbon. Conditions are as follows: 1g/g of garden waste, wherein the solid-liquid ratio is 1. The results show that when FeCl is used 3 The adsorption capacity of the prepared biochar to methylene blue is maximum when the temperature is 180 ℃ and 5 hours.
TABLE 2 influence of various metal salt co-catalysts on adsorption performance of hydrothermal charcoal
Figure RE-GDA0003298613780000051
The above examples and comparative examples prove that an autocatalytic dissolution system is formed by adding choline chloride-ferric chloride into water, the temperature of the hydrothermal carbonization reaction of the wood fiber raw material is remarkably reduced, the carbonization efficiency of garden waste is improved, the problems of high energy consumption, poor carbon adsorption capacity and the like of the existing hydrothermal carbonization technology are solved, and meanwhile, the hydrothermal carbonization liquid product can be quickly started to generate the biological methane by being inoculated with an anaerobic fermentation strain, so that the application prospect is wide.

Claims (3)

1. A method for preparing hydrothermal carbon by hydrothermal carbonization of wood fiber wastes is characterized by mixing choline chloride and water according to a mass ratio of 2 3 Reacting for 3 hours at 180 ℃ in a high-pressure reaction kettle; after the reaction is finished, carrying out solid-liquid separation, and drying a solid product to obtain the agricultural and forestry waste hydrothermal carbon; the FeCl 3 The amount of catalyst added was 4g/g of batch.
2. The method of claim 1, wherein the stirring speed of the autoclave is 200 to 400rpm.
3. The method of any one of claims 1 to 2, wherein the liquid product after solid-liquid separation is inoculated into an anaerobic fermentation strain for biological fermentation to obtain the biomethane.
CN202110645593.7A 2021-06-09 2021-06-09 Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes Active CN113636536B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202110645593.7A CN113636536B (en) 2021-06-09 2021-06-09 Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202110645593.7A CN113636536B (en) 2021-06-09 2021-06-09 Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes

Publications (2)

Publication Number Publication Date
CN113636536A CN113636536A (en) 2021-11-12
CN113636536B true CN113636536B (en) 2023-01-06

Family

ID=78415899

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202110645593.7A Active CN113636536B (en) 2021-06-09 2021-06-09 Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes

Country Status (1)

Country Link
CN (1) CN113636536B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114618870B (en) * 2022-04-25 2023-02-24 江苏泓润生物质能科技有限公司 Multi-source waste resource utilization method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105883753A (en) * 2016-06-03 2016-08-24 浙江科技学院 Preparation method and application of bamboo shoot shell biochar
CN106065332A (en) * 2016-06-03 2016-11-02 浙江科技学院 A kind of method and the application that utilize pomelo peel hydro-thermal carbonization to prepare charcoal
CN109628499A (en) * 2019-01-16 2019-04-16 中国科学院广州能源研究所 It is a kind of for improving the high temperature hydrothermal method of garden waste generation combustion gas
CN110358599A (en) * 2019-07-15 2019-10-22 北京科技大学 A kind of agriculture and forestry organic waste material dealkalize charing method based on hydro-thermal reaction
CN110510613A (en) * 2019-08-29 2019-11-29 东北大学 A kind of preparation method of two-dimensional metallic carbonitride MXene

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10549997B2 (en) * 2016-11-07 2020-02-04 Council Of Scientific & Industrial Research Process for the production of graphene sheets with tunable functionalities from seaweed promoted by deep eutectic solvents

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105883753A (en) * 2016-06-03 2016-08-24 浙江科技学院 Preparation method and application of bamboo shoot shell biochar
CN106065332A (en) * 2016-06-03 2016-11-02 浙江科技学院 A kind of method and the application that utilize pomelo peel hydro-thermal carbonization to prepare charcoal
CN109628499A (en) * 2019-01-16 2019-04-16 中国科学院广州能源研究所 It is a kind of for improving the high temperature hydrothermal method of garden waste generation combustion gas
CN110358599A (en) * 2019-07-15 2019-10-22 北京科技大学 A kind of agriculture and forestry organic waste material dealkalize charing method based on hydro-thermal reaction
CN110510613A (en) * 2019-08-29 2019-11-29 东北大学 A kind of preparation method of two-dimensional metallic carbonitride MXene

Also Published As

Publication number Publication date
CN113636536A (en) 2021-11-12

Similar Documents

Publication Publication Date Title
Wang et al. Effect of process wastewater recycling on the chemical evolution and formation mechanism of hydrochar from herbaceous biomass during hydrothermal carbonization
Xiao et al. Speciation and transformation of nitrogen for spirulina hydrothermal carbonization
CN102134616B (en) Method for fully utilizing biobased products prepared by semicellulose of straws as well as components thereof
Ran et al. Hydrothermal pretreatment on the anaerobic digestion of washed vinegar residue
WO2002018610A1 (en) Ethanol production with dilute acid hydrolysis using partially dried lignocellulosics
CN110846345B (en) Production process of cotton straw fulvic acid and cellulosic ethanol
EP1641713A1 (en) Fermentation media comprising wastewater and use hereof
CN111018309A (en) Efficient sludge energy treatment method based on hydrothermal pretreatment
CN102516209A (en) Method for coproducing furfural, ethanol and lignin from corncob
Yu et al. Effect of microwave/hydrothermal combined ionic liquid pretreatment on straw: Rumen anaerobic fermentation and enzyme hydrolysis
CN113636536B (en) Method for co-producing biomethane by hydrothermal carbonization of wood fiber wastes
CN116037066A (en) Biogas residue-based modified biochar and preparation method and application thereof
CN108117652B (en) Extraction method of enzymatic hydrolysis lignin
CN114772722A (en) Method for improving anaerobic digestion performance of hydrothermal wastewater by utilizing homologous hydrothermal carbon
CN113604510A (en) Method for improving efficiency of methane production through hydrothermal carbon enhanced anaerobic digestion
CN109851689B (en) Method for preparing levoglucosan by using agricultural and forestry waste
CN110499341B (en) Method for simultaneously producing ethanol, fulvic acid and carbon dioxide by using straws
CN111394401A (en) Method for preparing medium-chain fatty acid by anaerobic fermentation of wood fiber raw material
CN106753479B (en) Method for treating lignocellulose by coupling biogas fermentation and rapid pyrolysis with poly-generation
CN106755125B (en) Treatment method for mixed fermentation of cellulosic ethanol waste liquid and agricultural wastes
Li et al. Integrated production of humic-like acid, fulvic-like acid, and fermentable sugars from industrial xylooligosaccharides manufacturing waste residues via hydrothermal pretreatment
CN113308497A (en) Method for improving biogas production efficiency and gas production rate of lignocellulose raw material through anaerobic digestion
CN114181977A (en) Pretreatment method for enhancing methane production performance of straws by using anaerobic fermentation self-product and application
CN106544375B (en) Method for preparing full biomass-based aviation biofuel
CN113183266A (en) Method for pretreating poplar fibers by hydrothermal-peroxyacetate metal salt cooperation

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant