CN109266696A - A kind of method that white-rot fungi preconditioning technique improves mushroom residue anaerobic fermentation efficiency - Google Patents

A kind of method that white-rot fungi preconditioning technique improves mushroom residue anaerobic fermentation efficiency Download PDF

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CN109266696A
CN109266696A CN201811173049.1A CN201811173049A CN109266696A CN 109266696 A CN109266696 A CN 109266696A CN 201811173049 A CN201811173049 A CN 201811173049A CN 109266696 A CN109266696 A CN 109266696A
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mushroom residue
fermentation
white
rot fungi
anaerobic fermentation
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房玮
张涛
曲波
刘娅
王中玮
姜宁
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Research Center for Eco Environmental Sciences of CAS
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    • 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
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/40Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
    • C12P7/54Acetic acid
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    • 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
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/40Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
    • 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
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/40Preparation of oxygen-containing organic compounds containing a carboxyl group including Peroxycarboxylic acids
    • C12P7/52Propionic acid; Butyric acids

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
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  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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  • General Chemical & Material Sciences (AREA)
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Abstract

The present invention relates to organic solid castoff resource technology fields, and in particular to a kind of method that white-rot fungi preconditioning technique improves mushroom residue hydrolysis acidification efficiency.Preparation method is as follows: being pretreatment substrate with high lignin content mushroom residue, mushroom residue after drying is mechanically pulverized, under sterile conditions by 0.1-0.5 mass inoculation Pleurotus Sajor Caju (MES 03464), pre-processed 4-6 weeks under conditions of 25 DEG C, humidity 75%.Anaerobically digested sludge is seed sludge, and water is added to be configured to the mixed liquor of solid content 12%-18%, and mixed liquor is mixed with seed sludge by volatile organic matter amount ratio 1:2, nitrogen 3-5min is filled with;Controlling reaction temperature is 37 DEG C, and mixing speed 150-160r/min carries out fermentation 6-9d under anaerobic environment;The mixed liquor after fermentation is centrifugated using centrifuge, centrifugal speed 15000r/min, the supernatant after centrifugation is VFA fermentation liquid.The technological operation is simple, economic cost is cheap, has a good application prospect.The present invention provides a kind of new method for mushroom residue disposal of resources.

Description

A kind of method that white-rot fungi preconditioning technique improves mushroom residue anaerobic fermentation efficiency
Technical field
The present invention relates to organic solid castoff resource technology fields, and in particular to a kind of to be pre-processed using white-rot fungi The choice of technology cracks the method that lignin promotes mushroom residue anaerobic fermentation production volatile fatty acid (VFA).
Background technique
Mushroom residue is the by-product in mushroom production process, is mainly made of cellulose, hemicellulose and lignin, carbon nitrogen Than high, while the elements such as nitrogen rich in, phosphorus, potassium.Currently, measure is effectively treated in most of mushroom residue shortage, by random heap It puts, results in waste of resources, while being easy to bring the secondary pollution to environment.Although there is small part mushroom residue to be used for soil improvement Agent or animal feed, but these method disposing capacities are low, added value of product is low, cannot be effectively relieved that mushroom residue largely accumulates asks Topic, also limits the large-scale production of mushroom to a certain extent.Therefore, it rationally disposes and further increases to the comprehensive of mushroom residue It closes and utilizes, reduce potential risk of environmental pollution, or even its resource utilization is of great significance.
Anaerobic digestion techniques obtain extensively in the stabilisation, recycling and minimizing of the biomass such as whole world lignocellulosic Using.Organic substrates pass through hydrolysis acidification, generate a large amount of metal carboxylate, and main component is the short chains such as acetic acid, propionic acid, butyric acid Fatty acid.These short chain carboxy acid's salt are the important raw materials for production of organic chemical industry's industry, and added value is much larger than methane, are moulded in biology The synthesis of material, the production of bioenergy and the denitrogenation dephosphorizing of waste water etc. the potentiality that have a wide range of applications.In mushroom residue structure Lignin the accessible property of cellulose and enzyme is limited to the unformed biodegradation process that is bundled in of cellulose, hinder micro- life Object further utilizes substrate, it is caused to reduce in anaerobic digestion efficiency.Can effectively it be changed by preprocess method appropriate Lignocellulosic structure improves the anaerobism biodegradability of lignocellulose-like biomass.White-rot fungi is extracellular wooden by secreting Plain degrading enzyme, such as lignin-degrading enzymes, manganese peroxidase, laccase, can effectively lignin degrading.In addition, some white Rotten fungi has the function of Selective lignin-degradation, i.e., only loses a small amount of cellulose, improves substrate cellulose and lignin Ratio promotes the anaerobic digestion efficiency of lignocellulose-like biomass.
This patent is pre-processed using high lignin content mushroom residue as raw material by white-rot fungi, and effective selectivity cracks wood Quality carries out anaerobic fermentation under conditions of no pH is controlled and produces VFA, and the organic acid of generation is as the production having compared with high added value Product can be used as producing the materials such as medium chain fatty acid, provide a new approaches for the disposal of resources of mushroom residue.This method produces work Skill is simple, with good economic, society and environment benefit.
Summary of the invention
1. goal of the invention
It is an object of the present invention to reduce mushroom residue aiming at the problem that anaerobic fermentation efficiency high lignin content, provide A kind of lignin using in white-rot fungi preconditioning technique degradation selectivity mushroom residue, improve mushroom residue anaerobism biodegradability and VFA yield, the minimizing of realization mushroom residue waste, innoxious, recycling.The VFA produced by means of the present invention has wide Wealthy application prospect.
2. technical solution
The present invention provides a kind of acid production rate of white-rot fungi pretreatment raising high lignin content mushroom residue, is efficiently waved The process of hair property fatty acid, comprising the following steps:
(1) white-rot fungi culture: white-rot fungi of the present invention using Pleurotus Sajor Caju (P.sajor-caju, MES 03464) bacterial strain, conservation is in 3% malt-agar culture.Aseptically, the bacterium of 3-5 block diameter 1-2cm is accessed Cake to be equipped with 1.5L sterilizing sorghum bead culture box.Sufficiently shaking culture box is uniformly distributed mycelia, places about 15 at room temperature It, until sorghum surface covers with white hypha.
(2) mushroom residue pre-processes: taking a certain amount of mushroom residue, dries after 48h to constant weight, be mechanically pulverized to partial size 1.5-3.0cm being used for subsequent white-rot fungi preprocessing process;
(3) white-rot fungi pre-processes: by pretreated mushroom residue in 121 DEG C of sterilizing 30min, pressing 0.1~0.5 after cooling Mass ratio adds the sorghum bead with mycelia into preatreating reactors, and inoculation volume accounted for about the 1/3 of entire reactor.It connects After kind, sufficiently stirring mushroom residue comes into full contact with fungi with it.Sample is transferred to 25 DEG C, is pre-processed under conditions of humidity 75% 4-6 weeks;
(4) seed sludge pre-processes: by anaerobically digested sludge in 105 DEG C of heating 20-30min, removing methane phase therein Bacterium, the seed sludge as mushroom residue fermentation;
(5) mushroom residue anaerobic fermentation: by seed sludge in pretreated mushroom residue in step (3) and step (4) by waving Anaerobic fermentation reactor is added in hair property organic matter mass ratio 1:2, adds water to be configured to the mixed liquor of solid content 12%-18%, nitrogen charging Gas 3-5min, control reaction temperature are 37 DEG C, mixing speed 150-160r/min, stir interval 60s after 3min, fermentation process In pH is not adjusted.Anaerobic fermentation process continues 6-9d;
(6) fermentative acidification liquid extracts: the mixed liquor after mushroom residue fermentation in step (5) is centrifugated using centrifuge, Centrifugal speed is 15000r/min, supernatant, that is, VFA fermentation liquid after being centrifuged 20-30min.
3. beneficial effects of the present invention
The beneficial effects of the present invention are using white-rot fungi pre-process, after pretreatment can Selective lignin-degradation, Cellulose/lignin ratio is improved, subsequent anaerobic fermentation VFA yield is promoted to promote 65%-72%.Fermentation substrate is after pre-processing Mushroom residue, inoculum be anaerobic digester sludge, raw material sources are extensive, and anaerobic fermentation process without pH adjust, run at This is low, added value of product is high, realizes the minimizing of mushroom residue, innoxious and recycling treatment.It is inoculated with Pleurotus Sajor Caju (MES03464) pre-processes 6 weeks mushroom residues, carries out intermediate temperature anaerobic fermentation under conditions of initial solid content 15%, ferments 7d, VFA concentration reaches about 7352mg/L in fermentation liquid, does not pre-process mushroom residue control group VFA concentration and improves nearly 70%.The work Skill is easy to operate, preprocessing process and anaerobic fermentation conditions are easily controllable, economic cost is cheap, has a good application prospect.
Detailed description of the invention
The distribution of variety classes fatty acid in Fig. 1 fermentation liquid.
Specific embodiment
The present invention is further described below by specific embodiment, but is not intended to limit the present invention.
Instrument used in the present invention and material are commercially available.Wherein seed sludge is derived from certain anaerobic digester, mushroom residue It is derived from certain mushroom plantation factory.
Embodiment 1:
(1) mushroom residue of certain a certain amount of mushroom factory is taken, it is content of cellulose 12.3%, hemicellulose level 8.3%, wooden Cellulose content 21.7% is mechanically pulverized after drying 48h in 60 DEG C of baking ovens, is sieved, particle size 2.5-1.0cm, sieving Mushroom residue afterwards is used for subsequent pretreatment in 121 DEG C of sterilizing 30min;
(2) sterile, under room temperature, in mass ratio 0.1 is inoculated with Pleurotus Sajor Caju (MES 03464) In the reactor equipped with sterilizing mushroom residue, inoculation volume accounted for about the 1/3 of entire reactor.Have in 25 DEG C, humidity 75% It is cultivated 6 weeks under the conditions of oxygen.
(3) mushroom residue obtained in step (2) is taken to be put into fermentor, be added distilled water be configured to solid content be 15% it is mixed Close liquid;Seed sludge is added into mixed liquor, mixeding liquid volume and seed sludge volatile organic content ratio are 1:2;
(4) it seals after being passed through nitrogen 5min into the fermentor of step (3), ferments under anaerobic.Control machinery stirs Mixing revolving speed is 120r/min, controls temperature after 37 ± 2 DEG C, anaerobic fermentation 7d, and the VFA concentration of generation is maximum, is 7159.2mg/ L。
Embodiment 2:
(1) mushroom residue of certain a certain amount of mushroom factory is taken, it is content of cellulose 17.5%, hemicellulose level 6.8%, wooden Cellulose content 24.7% is mechanically pulverized after drying 48h in 60 DEG C of baking ovens, is sieved, particle size 3.0-1.8cm, sieving Mushroom residue afterwards is used for subsequent pretreatment in 121 DEG C of sterilizing 30min;
(2) sterile, under room temperature, in mass ratio 0.1 is inoculated with Pleurotus Sajor Caju (MES 03464) In the reactor equipped with sterilizing mushroom residue, inoculation volume accounted for about the 1/3 of entire reactor.Have in 25 DEG C, humidity 75% It is cultivated 6 weeks under the conditions of oxygen.
(3) mushroom residue obtained in step (2) is taken to be put into fermentor, be added distilled water be configured to solid content be 12% it is mixed Close liquid;Seed sludge is added into mixed liquor, mixeding liquid volume and seed sludge volatile organic content ratio are 1:2;
(4) it seals after being passed through nitrogen 5min into the fermentor of step (3), ferments under anaerobic.Control machinery stirs Mixing revolving speed is 120r/min, controls temperature after 37 ± 2 DEG C, anaerobic fermentation 7d, and the VFA concentration of generation is maximum, is 6982.6mg/ L。
Embodiment 3:
(1) mushroom residue of certain a certain amount of mushroom factory is taken, it is content of cellulose 15.2%, hemicellulose level 8.1%, wooden Cellulose content 19.3% is mechanically pulverized after drying 48h in 60 DEG C of baking ovens, is sieved, particle size 2.7-1.6cm, sieving Mushroom residue afterwards is used for subsequent pretreatment in 121 DEG C of sterilizing 30min;
(2) sterile, under room temperature, in mass ratio 0.1 is inoculated with Pleurotus Sajor Caju (MES 03464) In the reactor equipped with sterilizing mushroom residue, inoculation volume accounted for about the 1/3 of entire reactor.Have in 25 DEG C, humidity 75% It is cultivated 6 weeks under the conditions of oxygen.
(3) mushroom residue obtained in step (2) is taken to be put into fermentor, be added distilled water be configured to solid content be 15% it is mixed Close liquid;Seed sludge is added into mixed liquor, mixeding liquid volume and seed sludge volatile organic content ratio are 1:2;
(4) it seals after being passed through nitrogen 5min into the fermentor of step (3), ferments under anaerobic.Control machinery stirs Mixing revolving speed is 120r/min, controls temperature after 37 ± 2 DEG C, anaerobic fermentation 7d, and the VFA concentration of generation is maximum, is 7352.3mg/ L, the distribution of variety classes fatty acid is as shown in Figure 1.

Claims (3)

1. a kind of method that white-rot fungi preconditioning technique improves mushroom residue anaerobic fermentation efficiency, it is characterised in that the method packet Include following steps:
(1) white-rot fungi culture: the present invention uses Pleurotus Sajor Caju (P.sajor-caju, BNCC230025) bacterium Strain, aseptically, conservation accesses 3-5 block diameter 1- from slant medium in 3% malt-agar culture, with oese The bacteria cake of 2cm is to the culture box that 1.5L sterilizing sorghum bead is housed, and sufficiently shaking culture box is uniformly distributed mycelia, room temperature decentralization It sets about 15 days, until sorghum surface covers with white hypha;
(2) mushroom residue pre-processes: taking a certain amount of mushroom residue, dries after 48h to constant weight, be mechanically pulverized to partial size 3.0- 1.5cm is used for subsequent white-rot fungi preprocessing process;
(3) white-rot fungi pre-processes: by pretreated mushroom residue in 121 DEG C of sterilizing 30min, throwing after cooling by 0.1 mass ratio Lengthening has the sorghum bead of mycelia into preatreating reactors, and inoculation volume accounted for about the 1/3 of entire reactor, after inoculation, fills Point agitation mushroom residue comes into full contact with fungi with it, and sample is transferred to 25 DEG C, is cultivated 4~6 weeks under conditions of humidity 75%;
(4) seed sludge pre-processes: by anaerobically digested sludge in 105 DEG C of heating 20-30min, removing methanogen therein, makees For the seed sludge of mushroom residue fermentation;
(5) seed sludge in pretreated mushroom residue in step (3) and step (4) mushroom residue anaerobic fermentation: is pressed into volatility Anaerobic fermentation reactor is added in organic matter mass ratio 1:2, and inflated with nitrogen 3-5min, control reaction temperature is 37 DEG C, and mixing speed is 150-160r/min stirs interval 60s after 3min, pH is not adjusted in fermentation process, anaerobic fermentation process continues 6-9d;
(6) fermentative acidification liquid extracts: being centrifugated the mixed liquor after mushroom residue fermentation in step (5) using centrifuge, centrifugation Speed is 12000r/min, supernatant, that is, VFA fermentation liquid after being centrifuged 30min.
2. according to method described in right 1, which is characterized in that after Pleurotus Sajor Caju is pre-processed six weeks, fermentation It when system total solid concentration 15%, is controlled without pH, ferment 7d, and Vfa Concentration reaches about in fermentation liquid The pretreated control group Vfa Concentration of 6982.6mg/L, less fungi improves nearly 70%.
3. according to method described in right 1, which is characterized in that volatile fatty acid is mainly by acetic acid and propionic acid group in fermentation liquid At the content of acetic acid and propionic acid accounts for the 72%-75% of general volatile fatty acid.
CN201811173049.1A 2018-10-09 2018-10-09 A kind of method that white-rot fungi preconditioning technique improves mushroom residue anaerobic fermentation efficiency Pending CN109266696A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111892165A (en) * 2020-07-24 2020-11-06 温州大学 Method for improving denitrification efficiency of pig raising wastewater
CN113214497A (en) * 2021-05-06 2021-08-06 西华大学 Method for recovering lignin from enzymolysis residues of lignocellulose

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CN107435053A (en) * 2016-05-25 2017-12-05 东北林业大学 A kind of white-rot fungi pretreatment agricultural crop straw quickly produces the fermentation process of biogas

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111892165A (en) * 2020-07-24 2020-11-06 温州大学 Method for improving denitrification efficiency of pig raising wastewater
CN113214497A (en) * 2021-05-06 2021-08-06 西华大学 Method for recovering lignin from enzymolysis residues of lignocellulose

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Application publication date: 20190125