CN104762236B - 餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法 - Google Patents

餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法 Download PDF

Info

Publication number
CN104762236B
CN104762236B CN201510182883.7A CN201510182883A CN104762236B CN 104762236 B CN104762236 B CN 104762236B CN 201510182883 A CN201510182883 A CN 201510182883A CN 104762236 B CN104762236 B CN 104762236B
Authority
CN
China
Prior art keywords
culture
parts
acid
anaerobic
bacillus
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.)
Expired - Fee Related
Application number
CN201510182883.7A
Other languages
English (en)
Other versions
CN104762236A (zh
Inventor
尹小波
吴波
李强
张敏
邓雅月
王星
李政伟
代莉蓉
周正
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.)
Biogas Institute of Ministry of Agriculture
Original Assignee
Biogas Institute of Ministry of Agriculture
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 Biogas Institute of Ministry of Agriculture filed Critical Biogas Institute of Ministry of Agriculture
Priority to CN201510182883.7A priority Critical patent/CN104762236B/zh
Publication of CN104762236A publication Critical patent/CN104762236A/zh
Application granted granted Critical
Publication of CN104762236B publication Critical patent/CN104762236B/zh
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • 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
    • C12P39/00Processes involving microorganisms of different genera in the same process, simultaneously
    • 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

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biomedical Technology (AREA)
  • Virology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Medicinal Chemistry (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Fodder In General (AREA)

Abstract

本发明提供了餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法,制备方法包括如下步骤:(1)亮黄梭状芽孢杆菌DSM19732的培养;(2)嗜糖污水杆菌DSM 22681的培养;(3)解蛋白粪热杆菌DSM5265的培养;(4)嗜热厌氧绳菌DSM14523;(5)速生栖热分枝菌DSM8682的培养;(6)岸栖高温杆菌DSM21630;(7)互营单胞菌DSM4212的培养;(8)热自养甲烷热杆菌DSM1053、卢米尼马赛产甲烷球菌DSM25720、甲酸甲烷杆菌DSM3637的培养;(9)嗜热甲烷八叠球菌DSM1852的培养;将上述菌的培养物以一定比例混合,即得菌剂。本发明制备方法制备的菌剂能实现餐厨垃圾厌氧消化的快速启动和高效运行。

Description

餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法
技术领域
本发明属于固体废弃物处理技术领域,具体涉及餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法。
技术背景
厌氧消化的启动期在餐厨垃圾的处理过程当中非常关键,它可使厌氧消化过程尽快稳定,并决定了厌氧消化的效率,因此其影响因素得到了广泛的研究,例如接种物性质、底物成分、性质以及有机负荷或者过程控制(如温度、发酵类型)等。但直到现在,不同文献报道的启动效率差异仍然较大,其中接种物是影响启动的最重要因素。
在现有研究当中,利用复合菌加速发酵启动的研究不多。中国专利CN 101705199A报道了一种产甲烷复合菌剂及其制备方法,但对于发酵产沼气的加速效果有限,且未考虑如何才能稳定的加速厌氧消化启动,而加速启动的稳定性是至关重要的。
更为重要的是,餐厨垃圾的成分性质的差异巨大,现有技术中,尚未出现能稳定且大幅缩短餐厨垃圾厌氧消化启动的方法。而据2011年的统计,餐厨垃圾的产量已达8千万吨以上,并呈快速上升的趋势。
因此,亟待发开一种能加速餐厨垃圾厌氧消化启动和高效运行的菌剂的制备方法。
发明内容
针对现有技术的缺点,本发明的目的在于提供餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法,该制备方法包括如下步骤:
(1)亮黄梭状芽孢杆菌DSM19732的培养:培养基为CM3培养基,除培养基中的Na2CO3、纤维二糖和半胱氨酸外,先将其它成分溶解,除氧后后进行高压灭菌,加入过滤除菌的Na2CO3、纤维二糖和半胱氨酸,用质量体积比为5%的Na2CO3 调整 pH 至 7.2,充氮条件下接种,55˚C培养20天;
(2)嗜糖污水杆菌DSM 22681的培养:培养基为PY + X培养基,通氮气条件下接种,55˚C厌氧培养20天;
(3)解蛋白粪热杆菌DSM5265的培养:培养基为:0.4g H2HPO4 ,1.0g NH4Cl,2g 酵母膏,2g 胰酶解酪蛋白蛋白胨,1g MgCl2, 0.4g CaCl2, 0.001g 刃天青, 5.0g NaHCO3,0.3g Na2S∙9 H2O,1.5g/L 氨三乙酸三酸, 3g/L MgSO4∙7H2O, 0.5g /L MnSO4∙H2O, 1g /LNaCl,0.1g /L FeSO4∙7H2O,0.18 g/L CoSO4∙7H2O,0.1g/L CaCl2∙2H2O,0.18g/L ZnSO4∙7H2O,0.01g/L CuSO4∙5H2O,0.02g /L KAl(SO4)2∙12H2O,0.01g/L H3BO3,0.01g/L Na2MoO4∙2H2O,0.03g/L NiCl2∙6H2O,0.3g /L Na2SeO3∙5H2O,0.4g/L Na2Wo4∙2H2O;通氮气条件下接种,55˚C厌氧培养15-20天;
(4)嗜热厌氧绳菌DSM14523:培养基为:0.14g KH2PO4 , 0.2 g MgCl2, 0.15gCaCl2, 0.54g NH4Cl, 1ml 微量元素SL-11,1ml钨酸亚硒酸溶液,10 ml维生素, 0.001刃天青,2.3g 酵母膏,2.2g 葡萄糖,2.5g NaHCO3,0.25g Cysteine-HCl,0.25g Na2S,所述微量元素SL-11的配方为:5.2g/L Na2-EDTA,1.5g/L FeCl2,0.07g/L ZnCl2,0.1g/L MnCl2,0.006g/L H3BO3,0.19g/L CoCl2,0.002g/L CuCl2,0.024g NiCl2,0.036g Na2Mo4,所述钨酸亚硒酸溶液配方为:0.5g/L NaOH, 0.003g/L Na2SeO3, 0.004g/L Na2WO4,所述维生素溶液配方为:2mg/L 生物素,2mg/L 叶酸,10mg/L 盐酸吡哆醇,5mg/L 盐酸硫胺素,5mg/L 核黄素, 5mg/L 烟酸, 5mg/L D-泛酸钙,0.1mg/L 维生素B12,5mg/L p-氨基苯甲酸,5mg/L 硫辛酸,于厌氧条件下55˚C培养20-30天;
(5)速生栖热分枝菌DSM8682的培养:培养基为YTG培养基,在55˚C下厌氧培养20-30天;
(6)岸栖高温杆菌DSM21630:培养基为:0.9g NH4Cl,0.9g NaCl,0.4g MgCl2,0.75gKH2PO4, 1.5g H2HPO4,9 mL 微量元素,3g FeSO4, 1g 刃天青,5g 维生素,1g Na2S, 3g 酵母膏, 10g 胰蛋白胨, 5g 葡萄糖,所述微量元素的配方为:1.5g/L 氨三乙酸三酸, 3g/LMgSO4∙7H2O,0.5g /L MnSO4∙H2O,1g /L NaCl,0.1g /L FeSO4∙7H2O,0.18 g/L CoSO4∙7H2O,0.1g/L CaCl2∙2H2O,0.18g/L ZnSO4∙7H2O,0.01g/L CuSO4∙5H2O,0.02g /L KAl(SO4)2∙12H2O,0.01g/L H3BO3,0.01g/L Na2MoO4∙2H2O,0.03g/L NiCl2∙6H2O,0.3g /L Na2SeO3∙5H2O,0.4g/L Na2Wo4∙2H2O,所述维生素的配方为:2mg/L 生物素,2mg/L 叶酸,10mg/L 盐酸吡哆醇,5mg/L 盐酸硫胺素,5mg/L 核黄素, 5mg/L 烟酸, 5mg/L D-泛酸钙,0.1mg/L 维生素B12,5mg/L p-氨基苯甲酸,5mg/L 硫辛酸,通氮气条件下接种,55˚C厌氧培养7-10天;
(7)互营单胞菌DSM4212:培养基为互营单胞菌SD2培养基,按照50%体积接种,25˚C培养8-15天;
(8)热自养甲烷热杆菌DSM1053、卢米尼马赛产甲烷球菌DSM25720、甲酸甲烷杆菌DSM3637的培养:使用产甲烷杆菌培养基,厌氧条件下55˚C培养8-15天;
(9)嗜热甲烷八叠球菌DSM1852的培养:采用八叠球菌培养基,厌氧条件下于55˚C培养10-20天;
按菌液体积份数计,将亮黄梭状芽孢杆菌17-19份、嗜糖污水杆菌120-130份、解蛋白粪热杆菌85-93份、嗜热厌氧绳菌23-25份、速生栖热分枝菌16-18份、岸栖高温杆菌11-13份、互营单胞菌127-141份、热自养甲烷热杆菌470-520份、嗜热甲烷八叠球菌190-210份、卢米尼马赛产甲烷球菌166-182份、甲酸甲烷杆菌19-21份混合,即得所述菌剂。
本发明选择了可有效降解纤维素的亮黄梭状芽孢杆菌DSM19732;降解糖类的嗜糖污水杆菌DSM22681;降解蛋白类的解蛋白粪热杆菌DSM5265、岸栖高温杆菌DSM21630、嗜热厌氧绳菌DSM14523、速生栖热分枝菌DSM8682,嗜热厌氧绳菌DSM14523可能还具备降解氨氮的能力,可能对缓解厌氧发酵氨毒害起作用。
本发明制备方法所得的菌剂,能十分显著的获得加速餐厨垃圾厌氧消化启动的效果。需指出的是,任何基于本发明的制备方法所做的可预见性改动,均不背离本发明的保护范围和精神,本发明所公布的制备方法仅仅为可获得最佳效果的组合而已。
需指出的是,本发明不对各步骤的先后顺序有所限定,任何将本发明各步骤顺序进行调整的方法,均不影响本发明的实质效果,均视为与本发明实质相同。
优选的,各菌种的菌浓为1-4×108个/ml。
本发明的有益效果
本发明所制备的菌剂能显著的加速餐厨垃圾厌氧消化的启动并使之高效运行;
本发明的制备方法工艺简单,条件不苛刻,具有巨大应用前景。
具体实施方式
下面通过实施例对本发明进行具体描述,有必要在此指出的是以下实施例只是用于对本发明进行进一步的说明,不能理解为对本发明保护范围的限制,该领域的技术熟练人员根据上述发明内容所做出的一些非本质的改进和调整,仍属于本发明的保护范围。
实施例1
(1)亮黄梭状芽孢杆菌DSM19732的培养:培养基为CM3培养基,除培养基中的Na2CO3、纤维二糖和半胱氨酸外,先将其它成分溶解,除氧后进行高压灭菌,加入过滤除菌的Na2CO3、纤维二糖和半胱氨酸,用质量体积比为5%的Na2CO3 调整 pH 至 7.2,充氮条件下接种,55˚C培养20天;
(2)嗜糖污水杆菌DSM 22681的培养:培养基为PY + X培养基,通氮气条件下接种,55˚C厌氧培养20天;
(3)解蛋白粪热杆菌DSM5265的培养:培养基为:0.4g H2HPO4 ,1.0g NH4Cl,2g 酵母膏,2g 胰酶解酪蛋白蛋白胨,1g MgCl2, 0.4g CaCl2, 0.001g 刃天青, 5.0g NaHCO3,0.3g Na2S∙9 H2O,1.5g/L 氨三乙酸三酸, 3g/L MgSO4∙7H2O, 0.5g /L MnSO4∙H2O, 1g /LNaCl,0.1g /L FeSO4∙7H2O,0.18 g/L CoSO4∙7H2O,0.1g/L CaCl2∙2H2O,0.18g/L ZnSO4∙7H2O,0.01g/L CuSO4∙5H2O,0.02g /L KAl(SO4)2∙12H2O,0.01g/L H3BO3,0.01g/L Na2MoO4∙2H2O,0.03g/L NiCl2∙6H2O,0.3g /L Na2SeO3∙5H2O,0.4g/L Na2Wo4∙2H2O。通氮气条件下接种,55˚C厌氧培养15天。
(4)嗜热厌氧绳菌DSM14523:培养基为:0.14g KH2PO4 , 0.2 g MgCl2, 0.15gCaCl2, 0.54g NH4Cl, 1ml 微量元素SL-11,1ml钨酸亚硒酸溶液,10 ml维生素, 0.001刃天青,2.3g 酵母膏,2.2g 葡萄糖,2.5g NaHCO3,0.25g Cysteine-HCl,0.25g Na2S,所述微量元素SL-11的配方为:5.2g/L Na2-EDTA,1.5g/L FeCl2,0.07g/L ZnCl2,0.1g/L MnCl2,0.006g/L H3BO3,0.19g/L CoCl2,0.002g/L CuCl2,0.024g NiCl2,0.036g Na2Mo4,所述钨酸亚硒酸溶液配方为:0.5g/L NaOH, 0.003g/L Na2SeO3, 0.004g/L Na2WO4,所述维生素溶液配方为:2mg/L 生物素,2mg/L 叶酸,10mg/L 盐酸吡哆醇,5mg/L 盐酸硫胺素,5mg/L 核黄素, 5mg/L 烟酸, 5mg/L D-泛酸钙,0.1mg/L 维生素B12,5mg/L p-氨基苯甲酸,5mg/L 硫辛酸,于厌氧条件下55˚C培养20天;
(5)速生栖热分枝菌DSM8682的培养:培养基为YTG培养基,在55˚C下厌氧培养20天;
(6)岸栖高温杆菌DSM21630:培养基为:0.9g NH4Cl,0.9g NaCl,0.4g MgCl2,0.75gKH2PO4, 1.5g H2HPO4,9 mL 微量元素,3g FeSO4, 1g 刃天青,5g 维生素,1g Na2S, 3g 酵母膏, 10g 胰蛋白胨, 5g 葡萄糖,所述微量元素的配方为:1.5g/L 氨三乙酸三酸, 3g/LMgSO4∙7H2O,0.5g /L MnSO4∙H2O,1g /L NaCl,0.1g /L FeSO4∙7H2O,0.18 g/L CoSO4∙7H2O,0.1g/L CaCl2∙2H2O,0.18g/L ZnSO4∙7H2O,0.01g/L CuSO4∙5H2O,0.02g /L KAl(SO4)2∙12H2O,0.01g/L H3BO3,0.01g/L Na2MoO4∙2H2O,0.03g/L NiCl2∙6H2O,0.3g /L Na2SeO3∙5H2O,0.4g/L Na2Wo4∙2H2O,所述维生素的配方为:2mg/L 生物素,2mg/L 叶酸,10mg/L 盐酸吡哆醇,5mg/L 盐酸硫胺素,5mg/L 核黄素, 5mg/L 烟酸, 5mg/L D-泛酸钙,0.1mg/L 维生素B12,5mg/L p-氨基苯甲酸,5mg/L 硫辛酸,通氮气条件下接种,55˚C厌氧培养7天.
(7)互营单胞菌DSM4212:培养基为互营单胞菌SD2培养基,按照50%体积接种,25˚C培养8天;
(8)热自养甲烷热杆菌DSM1053、卢米尼马赛产甲烷球菌DSM25720、甲酸甲烷杆菌DSM3637的培养:使用产甲烷杆菌培养基,厌氧条件下55˚C培养8天;
(9)嗜热甲烷八叠球菌DSM1852的培养:采用八叠球菌培养基,厌氧条件下于55˚C培养10天;
以每毫升含有1×108个菌体,将18份亮黄梭状芽孢杆菌DSM19732、125份嗜糖污水杆菌DSM22681、89份解蛋白粪热杆菌DSM5265、24份嗜热厌氧绳菌DSM14523、17份速生栖热分枝菌DSM8682、12份岸栖高温杆菌DSM21630、134份互营单胞菌DSM4212、494份热自养甲烷热杆菌DSM1053、202份嗜热甲烷八叠球菌DSM1825、174份卢米尼马赛产甲烷球菌DSM25720、20份甲酸甲烷杆菌DSM3637混合,即得所述菌剂。
实施例2
除各菌的配比为:
17份亮黄梭状芽孢杆菌DSM19732、120份嗜糖污水杆菌DSM22681、85份解蛋白粪热杆菌DSM5265、23份嗜热厌氧绳菌DSM14523、16份速生栖热分枝菌DSM8682、11份岸栖高温杆菌DSM21630、127份互营单胞菌DSM4212、470份热自养甲烷热杆菌DSM1053、190份嗜热甲烷八叠球菌DSM1825、166份卢米尼马赛产甲烷球菌DSM25720、19份甲酸甲烷杆菌DSM3637;各菌种的菌浓每毫升为2×108个菌体;以及除(3)中培养时间为20天,(4)中培养时间为30天,(5)中培养时间为30天,(6)中培养时间为10天,(7)中培养时间为15天,(8)中培养时间为15天,(9)中培养时间为20天之外,其余与实施例1一致。
实施例3
除各菌的配比为:
19份亮黄梭状芽孢杆菌DSM19732、130份嗜糖污水杆菌DSM22681、93份解蛋白粪热杆菌DSM5265、25份嗜热厌氧绳菌DSM14523、18份速生栖热分枝菌DSM8682、13份岸栖高温杆菌DSM21630、141份互营单胞菌DSM4212、520份热自养甲烷热杆菌DSM1053、210份嗜热甲烷八叠球菌DSM1825、182份卢米尼马赛产甲烷球菌DSM25720、21份甲酸甲烷杆菌DSM3637;各菌种的菌浓每毫升为4×108个菌体;以及除(3)中培养时间为18天,(4)中培养时间为25天,(5)中培养时间为25天,(6)中培养时间为8天,(7)中培养时间为12天,(8)中培养时间为12天,(9)中培养时间为15天之外,其余与实施例1一致。
实施例4
实验采用两相厌氧消化工艺进行,具体步骤如下:
1)酸化罐的构建
酸化罐体积400L,有效容积320L,33℃恒温发酵,发酵浓度(TS)10%,pH值5.5,HRT为3d;每天进/出料一次,出料作为厌氧罐的进料。
2)厌氧罐的构建
厌氧罐体积1600L,有效容积1300L,55℃恒温发酵;加入130L实施例1或实施例2或实施例3中的复合菌剂;
3)厌氧罐的运行
以0.5kgVS/m3•d的有机负荷为启动负荷,后期根据发酵液中的VFA、氨氮、pH值等发酵参数来逐步提升负荷;通过调整进料量(原料VS计)来调整发酵罐的HRT和有机负荷。实验共运行150d,考察稳定运行状态下的各种工艺参数。
对比实施例1
仅实施例4步骤2)中所述复合菌剂以脱水污泥代替,其他均采用相同操作。
对比实施例2
仅实施例4步骤2)中所述复合菌剂以沼气池沼液代替;其他采用相同操作。

Claims (2)

1.餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法,其特征在于,所述制备方法包括如下步骤:
(1)亮黄梭状芽孢杆菌DSM19732的培养:培养基为CM3培养基,除培养基中的Na2CO3、纤维二糖和半胱氨酸外,先将其它成分溶解,除氧后进行高压灭菌,加入过滤除菌的Na2CO3、纤维二糖和半胱氨酸,用质量体积比为5%的Na2CO3调整 pH 至 7.2,充氮条件下接种,55˚C培养20天;
(2)嗜糖污水杆菌DSM 22681的培养:培养基为PY + X培养基,通氮气条件下接种,55˚C厌氧培养20天;
(3)解蛋白粪热杆菌DSM5265的培养:培养基为:0.4g H2HPO4,1.0g NH4Cl,2g 酵母膏,2g 胰酶解酪蛋白蛋白胨,1g MgCl2, 0.4g CaCl2, 0.001g 刃天青, 5.0g NaHCO3,0.3gNa2S∙9 H2O,1.5g/L 氨三乙酸三酸, 3g/L MgSO4∙7H2O, 0.5g /L MnSO4∙H2O, 1g /L NaCl,0.1g /L FeSO4∙7H2O,0.18 g/L CoSO4∙7H2O,0.1g/L CaCl2∙2H2O,0.18g/L ZnSO4∙7H2O,0.01g/L CuSO4∙5H2O,0.02g /L KAl(SO4)2∙12H2O,0.01g/L H3BO3,0.01g/L Na2MoO4∙2H2O,0.03g/L NiCl2∙6H2O,0.3g /L Na2SeO3∙5H2O,0.4g/L Na2Wo4∙2H2O;通氮气条件下接种,55˚C厌氧培养15-20天;
(4)嗜热厌氧绳菌DSM14523:培养基为:0.14g KH2PO4 , 0.2 g MgCl2, 0.15g CaCl2,0.54g NH4Cl, 1ml 微量元素SL-11,1ml钨酸亚硒酸溶液,10 ml维生素, 0.001刃天青,2.3g 酵母膏,2.2g 葡萄糖,2.5g NaHCO3,0.25g Cysteine-HCl,0.25g Na2S,所述微量元素SL-11的配方为:5.2g/L Na2-EDTA,1.5g/L FeCl2,0.07g/L ZnCl2,0.1g/L MnCl2,0.006g/LH3BO3,0.19g/L CoCl2,0.002g/L CuCl2,0.024g NiCl2,0.036g Na2Mo4,所述钨酸亚硒酸溶液配方为:0.5g/L NaOH, 0.003g/L Na2SeO3, 0.004g/L Na2WO4,所述维生素溶液配方为:2mg/L 生物素,2mg/L 叶酸,10mg/L 盐酸吡哆醇,5mg/L 盐酸硫胺素,5mg/L 核黄素, 5mg/L 烟酸, 5mg/L D-泛酸钙,0.1mg/L 维生素B12,5mg/L p-氨基苯甲酸,5mg/L 硫辛酸,于厌氧条件下55˚C培养20-30天;
(5)速生栖热分枝菌DSM8682的培养:培养基为YTG培养基,在55˚C下厌氧培养20-30天;
(6)岸栖高温杆菌DSM21630:培养基为:0.9g NH4Cl,0.9g NaCl,0.4g MgCl2,0.75gKH2PO4, 1.5g H2HPO4,9 mL 微量元素,3g FeSO4, 1g 刃天青,5g 维生素,1g Na2S, 3g 酵母膏, 10g 胰蛋白胨, 5g 葡萄糖,所述微量元素的配方为:1.5g/L 氨三乙酸三酸, 3g/LMgSO4∙7H2O,0.5g /L MnSO4∙H2O,1g /L NaCl,0.1g /L FeSO4∙7H2O,0.18 g/L CoSO4∙7H2O,0.1g/L CaCl2∙2H2O,0.18g/L ZnSO4∙7H2O,0.01g/L CuSO4∙5H2O,0.02g /L KAl(SO4)2∙12H2O,0.01g/L H3BO3,0.01g/L Na2MoO4∙2H2O,0.03g/L NiCl2∙6H2O,0.3g /L Na2SeO3∙5H2O,0.4g/L Na2Wo4∙2H2O,所述维生素的配方为:2mg/L 生物素,2mg/L 叶酸,10mg/L 盐酸吡哆醇,5mg/L 盐酸硫胺素,5mg/L 核黄素, 5mg/L 烟酸, 5mg/L D-泛酸钙,0.1mg/L 维生素B12,5mg/L p-氨基苯甲酸,5mg/L 硫辛酸,通氮气条件下接种,55˚C厌氧培养7-10天;
(7)互营单胞菌DSM4212:培养基为互营单胞菌SD2培养基,按照50%体积接种,25˚C培养8-15天;
(8)热自养甲烷热杆菌DSM1053、卢米尼马赛产甲烷球菌DSM25720、甲酸甲烷杆菌DSM3637的培养:使用产甲烷杆菌培养基,厌氧条件下55˚C培养8-15天;
(9)嗜热甲烷八叠球菌DSM1852的培养:采用八叠球菌培养基,厌氧条件下于55˚C培养10-20天;
按菌液体积份计,将亮黄梭状芽孢杆菌17-19份、嗜糖污水杆菌120-130份、解蛋白粪热杆菌85-93份、嗜热厌氧绳菌23-25份、速生栖热分枝菌16-18份、岸栖高温杆菌11-13份、互营单胞菌127-141份、热自养甲烷热杆菌470-520份、嗜热甲烷八叠球菌190-210份、卢米尼马赛产甲烷球菌166-182份、甲酸甲烷杆菌19-21份混合,即得所述菌剂。
2.根据权利要求1所述的方法,其特征在于,各菌种的菌浓为1-4×108个/ml。
CN201510182883.7A 2015-04-17 2015-04-17 餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法 Expired - Fee Related CN104762236B (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510182883.7A CN104762236B (zh) 2015-04-17 2015-04-17 餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510182883.7A CN104762236B (zh) 2015-04-17 2015-04-17 餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法

Publications (2)

Publication Number Publication Date
CN104762236A CN104762236A (zh) 2015-07-08
CN104762236B true CN104762236B (zh) 2018-04-27

Family

ID=53644331

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510182883.7A Expired - Fee Related CN104762236B (zh) 2015-04-17 2015-04-17 餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法

Country Status (1)

Country Link
CN (1) CN104762236B (zh)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109609415B (zh) * 2019-01-25 2021-08-17 南京农业大学 一种甲烷菌及其应用
NZ783635A (en) 2019-07-04 2022-08-26 Incitec Fertilizers Pty Ltd Improved fertiliser

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102559499A (zh) * 2012-01-31 2012-07-11 农业部沼气科学研究所 一种沼气干发酵复合菌剂的制备方法
CN103215213A (zh) * 2013-05-20 2013-07-24 黑龙江八一农垦大学 一种用于餐厨垃圾厌氧发酵的复合菌剂

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102559499A (zh) * 2012-01-31 2012-07-11 农业部沼气科学研究所 一种沼气干发酵复合菌剂的制备方法
CN103215213A (zh) * 2013-05-20 2013-07-24 黑龙江八一农垦大学 一种用于餐厨垃圾厌氧发酵的复合菌剂

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
垃圾堆肥高效复合微生物菌剂的制备;席北斗;《环境科学研究》;20031231;58-64 *

Also Published As

Publication number Publication date
CN104762236A (zh) 2015-07-08

Similar Documents

Publication Publication Date Title
Chen et al. Recent advance in inhibition of dark fermentative hydrogen production
Hernández et al. Use of coffee mucilage as a new substrate for hydrogen production in anaerobic co-digestion with swine manure
Ras et al. Experimental study on a coupled process of production and anaerobic digestion of Chlorella vulgaris
Passanha et al. Increasing polyhydroxyalkanoate (PHA) yields from Cupriavidus necator by using filtered digestate liquors
US11898140B2 (en) Hyperthermophilic aerobic fermentation inoculant prepared by using municipal sewage sludge and its method
Wieczorek et al. Microalgae-bacteria flocs (MaB-Flocs) as a substrate for fermentative biogas production
Lozano et al. Microbiological characterization and specific methanogenic activity of anaerobe sludges used in urban solid waste treatment
Noike et al. Continuous hydrogen production from organic waste
Li et al. Enhancement of bio-hydrogen yield and pH stability in photo fermentation process using dark fermentation effluent as succedaneum
Rosas-Mendoza et al. Anaerobic digestion of citrus industry effluents using an Anaerobic Hybrid Reactor
Yezza et al. Production of Bacillus thuringiensis‐based biopesticides in batch and fed batch cultures using wastewater sludge as a raw material
CN103421735A (zh) 一种受损厌氧氨氧化菌群的快速修复方法
CN104762236B (zh) 餐厨垃圾厌氧消化快速启动和高效运行的菌剂的制备方法
CN103468608A (zh) 污水处理用复合菌菌群及其培养方法
CN101260389A (zh) 一种白腐真菌的产酶方法
Zandvoort et al. Effect of long‐term cobalt deprivation on methanol degradation in a methanogenic granular sludge bioreactor
Costa et al. Pre-treatment and temperature effects on the use of slow release electron donor for biological sulfate reduction
Matos et al. Application of electromagnetic field in anaerobic biodigestion in batch reactors
Asikong et al. Microorganisms associated with biogas production using vegetable (Telfairia occidentalis) wastes, banana peel and pig dung as substrates
Huang et al. Long-term performance on volatile fatty acids production improved in a kitchen wastewater fermenter by co-fermentation of sludge and membrane separation
CN103966128A (zh) 一株那不勒斯硫杆菌及其在生物脱硫中的应用
CN104862342A (zh) 利用污泥调控果蔬废弃物强化单相发酵产沼气的方法
CN104862259A (zh) 高有机负荷中温沼气发酵复合菌剂、其制备方法和用途
CN104762361B (zh) 餐厨垃圾厌氧消化快速启动和高效运行的方法
Zhou et al. Environment-enhancing energy: a novel wastewater treatment system that maximizes algal biofuel production and minimizes greenhouse gas emissions

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180427

Termination date: 20210417