WO2021062887A1 - Straw biodegradable composite bacterial agent and application thereof - Google Patents

Straw biodegradable composite bacterial agent and application thereof Download PDF

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Publication number
WO2021062887A1
WO2021062887A1 PCT/CN2019/111574 CN2019111574W WO2021062887A1 WO 2021062887 A1 WO2021062887 A1 WO 2021062887A1 CN 2019111574 W CN2019111574 W CN 2019111574W WO 2021062887 A1 WO2021062887 A1 WO 2021062887A1
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straw
pulping
pulp
bacillus
bacterial agent
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PCT/CN2019/111574
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French (fr)
Chinese (zh)
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周辉
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广东普洛宇飞生物科技有限公司
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    • 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
    • C12N1/14Fungi; Culture media therefor
    • 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
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/14Disintegrating in mills
    • D21B1/16Disintegrating in mills in the presence of chemical agents
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C5/00Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
    • D21C5/005Treatment of cellulose-containing material with microorganisms or enzymes

Definitions

  • the invention relates to the technical field of straw degradation, in particular to a straw biodegradable composite fungus agent and its application.
  • Straw cellulose is a very precious biomass energy resource on the earth, and it is widely present in various agricultural production systems. As a large grain-producing country, my country produces nearly 700 million tons of crop straw every year. However, due to the lack of guidance and effective treatment methods, the problem of straw treatment has become increasingly prominent. Most of the straw treatment methods are burning or discarding. This has also become a new source of rural environmental pollution. The current treatment of straw not only wastes valuable renewable resources, but also brings various hazards, causing air pollution, soil mineralization, fires and traffic accidents. How to comprehensively and effectively use crop stalks to avoid the waste of biomass energy and increase the income of farmers has become the focus of solving the stalk problem.
  • the purpose of the present invention is to overcome the above-mentioned shortcomings of the prior art and provide a straw biodegradable composite microbial agent.
  • the technical solution adopted by the present invention is: a straw biodegradable composite inoculum, the composite inoculum is Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and The compound of Trametes versicolor.
  • Phanerochaete chrysosporium and Trametes versicolor mainly remove lignin from straw, and are helpful for bleaching and dye decolorization; Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus Mainly carry out the decomposing of hemicellulose.
  • the ratio of the colony numbers of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and Trametes versicolor is: (1-3): (1-3): (1) ⁇ 3):(1 ⁇ 3):(1 ⁇ 3).
  • the ratio of the number of colonies of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and Trametes versicolor is 1:1:1:1:1.
  • the present invention also provides a preparation method of the straw biodegradable composite microbial agent, which includes the following steps:
  • Colony activation Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor are respectively inoculated on solid plates under aseptic conditions to activate the colonies;
  • Seed culture inoculate the above-mentioned activated strains in liquid culture medium under aseptic conditions, and cultivate in a shaker at 150-180rpm;
  • Fermentation culture inoculate the above-mentioned seed liquid in a liquid medium, and ferment culture;
  • Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus are inoculated on YPD plates and cultured for 1-3 days; Phanerochaete chrysosporium and Trametes versicolor are inoculated on potato culture medium (PDA ) Plate culture for 3-5 days.
  • PDA potato culture medium
  • Bacillus subtilis, Bacillus amyloliquefaciens and Bacillus cereus are inoculated in YPD liquid medium at 25°C-30°C and cultured on a shaker for 2-4 days; Bacteria and Trametes versicolor were inoculated into potato liquid medium and cultured on a shaker for 3-5 days at 25°C-30°C.
  • the inoculation amount of the seed liquid is 0.5-2% of the volume of the liquid culture medium.
  • the inoculation amount of the seed liquid is 1% of the volume of the liquid culture medium.
  • the present invention also provides an application of the straw biodegradable composite bacterial agent in a pulping process.
  • the pulping process includes the following steps:
  • Biodegradation The straw after cooking and sterilization is sent to the degradation tank, and after cooling, the active fermentation broth containing the straw biodegradable compound bacterial agent is added to the degradation tank, mixed evenly, and fermented and degraded until the straw is fluffy to obtain the pulp raw material ;
  • the added amount of the active fermentation broth is 20%-40% of the total weight of the plant fiber.
  • the addition amount of the above-mentioned active fermentation broth in this application is based on comprehensive consideration of the use and degradation effect of the fermentation broth. It is found that the addition amount in the above range can save the usage of the fermentation broth, the processing time is moderate, and the degradation effect is suitable. The choice made, although increasing the amount of use can accelerate the degradation, but the cost is also relatively high.
  • the fermentation temperature is 20-30°C, and the fermentation time is 48-120 hours.
  • the selection of the fermentation temperature and time of the above-mentioned composite bacterial agent in this application can better ensure the effective decomposition of cellulose.
  • the fermentation time is 80-120h; when the fermentation temperature is 25-30°C, the fermentation time is 48-80h.
  • the pulping aid includes the following components by weight: 20-30 parts of urea, 10-20 parts of DTPA, 15-25 parts of fatty alcohol polyoxyalkyl ether and fatty alcohol polyoxyethylene 15-25 parts of oxyethylene ether.
  • the pulping auxiliary agent further comprises an excipient in which calcium powder and sodium sulfate are mixed in equal proportions.
  • DTPA can eliminate the influence of heavy metal ions on subsequent hydrogen peroxide; urea can promote the stable and rapid decomposition of hydrogen peroxide; fatty alcohol polyoxyalkyl ether and fatty alcohol polyoxyethylene ether play a role in osmotic emulsification.
  • the refining is that the pulp is brought into a high-consistency refiner through a conveyor belt, and 30-45° C. water is added, and the fibers in the slurry are decomposed through a high-speed refining sheet.
  • the bleaching is: adding hydrogen peroxide to the pulp after refining for bleaching treatment for 2-3 hours, and raising the temperature to 90° C. to decompose the hydrogen peroxide after the bleaching treatment.
  • the process of squeezing the moisture is: transporting the bleached pulp to the filter screen to filter out part of the moisture in the pulp, wherein the water is discharged to the reservoir at the lower part of the filter screen, and the filtered pulp passes through
  • the squeezing machine squeezes out 40-50% of the moisture, and then passes through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp is 50-60%.
  • the invention belongs to an environmentally-friendly technology, which uses Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor compound inoculants to process crop straws, thereby avoiding the traditional pulping process
  • Bacillus subtilis Bacillus amyloliquefaciens
  • Bacillus cereus Phanerochaete chrysosporium
  • Trametes versicolor compound inoculants to process crop straws, thereby avoiding the traditional pulping process
  • the use of a large number of chemical reagents pollutes the environment.
  • water can be recycled without discharging any sewage containing organic compounds and suspended solids, avoiding the process of sewage treatment, saving production costs, and reducing energy. Consumption and consumption, no heating required during all production processes, decomposition at room temperature, and bleaching at room temperature.
  • the technology has novel and unique design, clear thinking, strong adaptability and universality, and a high degree of industrialization; the use of composite microbial agents for pulping avoids the use of a large number of chemical agents and solves the problem of wastewater treatment in the traditional pulping process , which reduces the production cost of the enterprise, has advanced technology, and is environmentally friendly, in line with the national energy-saving emission reduction strategy.
  • Figure 1 is a flow chart of the pulping process of the invention.
  • potato culture medium The components of potato culture medium (PDA) are as follows: potato extract 1.0L, glucose 20.0g, KH 2 PO 4 3.0 g, MgSO 4 .7H 2 O 1.5 g, agar 15.0 g (no need for liquid medium), pH 6.0.
  • the preparation method of the potato extract take 200g of peeled potatoes, cut into small pieces, add 1.0L of water and boil for 30min, filter out the potato pieces, and make up the filtrate to 1.0L;
  • the composition of YPD medium is as follows: yeast extract 1%, tryptone 2%, glucose 2%, agar 1% (liquid medium is not required).
  • An embodiment of the straw biodegradable composite inoculum of the present invention the preparation method of the straw biodegradable composite inoculum in this embodiment is as follows:
  • Slant culture Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus were inoculated on YPD plates and activated for 3 days; Phanerochaete chrysosporium and Trametes versicolor were inoculated on potato medium (PDA) plates and activated for 4 days.
  • PDA potato medium
  • the crushed plant stalks are subjected to steaming sterilization treatment, the steaming sterilization time is 20 minutes, and the temperature is 120°C;
  • the boiled and sterilized plant stalks are sent to the degradation tank. After cooling, add 30% of the dry weight of wheat straw stalks to the degradation tank, mix them evenly, and carry out fermentation and degradation at 30°C for 72 hours until the stalks are fluffy.
  • the shape is the pulp raw material
  • pulping auxiliary agent 3% pulping auxiliary agent to it, stir and mix, based on 100 parts by weight, the pulping auxiliary agent
  • the ingredients are: 20 parts of urea, 10 parts of DTPA, 15 parts of fatty alcohol polyoxyalkyl ether and 25 parts of fatty alcohol polyoxyethylene ether.
  • the balance is an excipient mixed with calcium powder and sodium sulfate in equal proportions;
  • the above-mentioned pulp is sent to the high-consistency refiner for refining.
  • the refining is the pulp that is brought into the high-consistency refiner through a conveyor belt, and water at 30°C is added to make the fibers in the slurry through high-speed refining. break down;
  • step 8 Transport the bleached pulp in step 8 to the filter screen to filter out part of the water in the pulp, where the water is drained to the reservoir at the bottom of the filter screen, and the filtered pulp is then passed through a squeezer and extruded 40-50% of the moisture is passed through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp will be 50-60%.
  • An embodiment of the straw biodegradable composite inocula of the present invention the preparation method of the straw biodegradable composite inocula in this embodiment is as follows:
  • Slant culture Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus were inoculated on YPD plates and activated for 1 day; Phanerochaete chrysosporium and Trametes versicolor were inoculated on potato medium (PDA) plates and activated for 3 days.
  • PDA potato medium
  • the number of colony forming units is 1:3:1:3:1 to obtain a straw-degrading bacterial system.
  • the straw biodegradable composite inoculum prepared above is applied to plant straw biodegradable pulping, and the specific method is as follows:
  • the crushed plant stalks are subjected to steaming sterilization treatment, the steaming sterilization time is 20 minutes, and the temperature is 120°C;
  • the boiled and sterilized plant stalks are sent to the degradation tank. After cooling, add 20% of the dry weight of the wheat straw stalks to the degradation tank, mix them evenly, and carry out fermentation and degradation at 25°C for 48 hours until the stalks are fluffy.
  • the shape is the pulp raw material
  • pulping auxiliary agent put the pulp raw material filtered out by the filter into the pulping tank, add water and stir to form pulp, add 4% pulping auxiliary agent to it, stir and mix, based on 100 parts by weight, the pulping auxiliary agent
  • the ingredients are: 30 parts of urea, 20 parts of DTPA, 25 parts of fatty alcohol polyoxyalkyl ether and 15 parts of fatty alcohol polyoxyethylene ether.
  • the balance is an excipient mixed with calcium powder and sodium sulfate in equal proportions;
  • the above-mentioned pulp is sent to a high-consistency refiner for refining.
  • the refining is the pulp that is brought into the high-consistency refiner through a conveyor belt, and water at 45°C is added to make the fibers in the slurry through high-speed grinding. break down;
  • step 8 Transport the bleached pulp in step 8 to the filter screen to filter out part of the water in the pulp, where the water is drained to the reservoir at the bottom of the filter screen, and the filtered pulp is then passed through a squeezer and extruded 40-50% of the moisture is passed through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp will be 50-60%.
  • An embodiment of the straw biodegradable composite inoculum of the present invention the preparation method of the straw biodegradable composite inoculum in this embodiment is as follows:
  • Slant culture Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus were inoculated on YPD plates and activated for 2 days; Phanerochaete chrysosporium and Trametes versicolor were inoculated on potato medium (PDA) plates and activated for 5 days.
  • PDA potato medium
  • the number of colony forming units of Bacillus subtilis is 1:1:1:1:1 to obtain a straw-degrading bacteria system.
  • the straw biodegradable composite inoculum prepared above is applied to plant straw biodegradable pulping, and the specific method is as follows:
  • the crushed plant straws are subjected to steaming and sterilization treatment, the steaming and sterilization time is 15 minutes, and the temperature is 118°C;
  • the boiled and sterilized plant stalks are sent to the degradation tank. After cooling, add the composite bacteria yeast solution of 40% of the dry weight of wheat straw stalks to the degradation tank, mix well, and carry out fermentation and degradation at 20°C for 120 hours until the straws are fluffy.
  • the shape is the pulp raw material
  • pulping auxiliary agent 5% pulping auxiliary agent to it, stir and mix well, based on 100 parts by weight, the pulping auxiliary agent
  • the ingredients are: 25 parts of urea, 15 parts of DTPA, 22 parts of fatty alcohol polyoxyalkyl ether and 18 parts of fatty alcohol polyoxyethylene ether.
  • the balance is an excipient mixed with calcium powder and sodium sulfate in equal proportions;
  • the above-mentioned pulp is sent to a high-consistency refiner for refining.
  • the refining is the pulp that is brought into the high-consistency refiner through a conveyor belt, and water at 40°C is added to make the fibers in the slurry through high-speed grinding. break down;
  • step 8 Transport the bleached pulp in step 8 to the filter screen to filter out part of the water in the pulp.
  • the water is drained to the reservoir at the bottom of the filter screen.
  • the filtered pulp is then passed through a squeezer and extruded. 40-50% of the moisture is passed through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp will be 50-60%.
  • the pulp yield, whiteness, breaking length and ring pressure index of the paper pulp prepared under the conditions of the straw bioenzymatic degradation pulping process of the present invention are respectively tested, and the formula for calculating the pulp yield: (m 1 /m)*100% (m 1 refers to the dry weight of coarse pulp, m refers to the dry weight of raw materials), the whiteness and the breaking length of the paper and the ring pressure index were measured with a whiteness measuring instrument and a paper tensile strength measuring instrument.
  • Table 1 As shown in Table 1 below.
  • Example 2 Pulp yield (%) 75.2 74.3 77.6 Whiteness (%ISO) 86 85 89 Break length (Km) 4.71 4.85 4.68 Ring pressure index (N.m/g) 11.2 11.3 11.5
  • the method for biological pulping of straw using composite biological inoculants provided in the embodiments of the present invention has a pulp yield of more than 70%, whiteness of more than 85%, and a break length of more than 70%.
  • the ring pressure index is higher than 11.2Nm/g, and when the ratio of the bacteria is 1:1:1:1:1, the pulp yield and whiteness are 77.6% and 89%, respectively, and the effect is good. It shows that the method for biological pulping with a composite biological inoculum provided by the present invention meets the requirements in terms of pulp yield and whiteness, and the mechanical properties of the prepared paper are also excellent.

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Abstract

Provided is a straw biodegradable composite bacterial agent, said compound bacterial agent being a composition of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor. Biodegradation of plant straw replaces the chemical pulping method commonly used in current pulping technologies, thus avoiding the environmental pollution caused by the use of a large number of chemical reagents in conventional pulping processes; in the pulping production process, water can be recycled and reused without discharging any sewage containing organic compounds and suspended matter, thus eliminating the sewage treatment phase and reducing production costs; no heating is required during the entire production process, decomposition takes place at ambient temperature, and bleaching takes place at ambient temperature. Also disclosed are a preparation method and application of said straw biodegradable composite bacterial agent.

Description

一种秸秆生物降解复合菌剂及其应用Straw biodegradable composite microbial agent and its application 技术领域Technical field
本发明涉及秸秆降解技术领域,尤其是一种秸秆生物降解复合菌剂及其应用。The invention relates to the technical field of straw degradation, in particular to a straw biodegradable composite fungus agent and its application.
背景技术Background technique
秸秆纤维素是地球上一种十分宝贵的生物质能资源,它广泛存在于各种农业生产系统中。我国作为产粮大国,据统计每年产生近7亿吨农作物秸秆,但是由于缺乏引导以及行之有效的处理方式,秸秆的处理问题也日益凸显,对于秸秆的处理方式多数以燃烧或者废弃为主,这也成为农村环境污染的新源头,目前对于秸秆的处理方式,不仅浪费了宝贵的可再生资源,同时还带来了各种危害,造成大气污染、土壤矿化、火灾和交通事故等。如何综合有效的利用农作物秸秆避免生物质能源的浪费,又能带来农民收入的提升成为解决秸秆问题的重点。Straw cellulose is a very precious biomass energy resource on the earth, and it is widely present in various agricultural production systems. As a large grain-producing country, my country produces nearly 700 million tons of crop straw every year. However, due to the lack of guidance and effective treatment methods, the problem of straw treatment has become increasingly prominent. Most of the straw treatment methods are burning or discarding. This has also become a new source of rural environmental pollution. The current treatment of straw not only wastes valuable renewable resources, but also brings various hazards, causing air pollution, soil mineralization, fires and traffic accidents. How to comprehensively and effectively use crop stalks to avoid the waste of biomass energy and increase the income of farmers has become the focus of solving the stalk problem.
近年来,随着现代工业的发展,能源短缺以及环境污染的问题也日益凸显,秸秆资源的综合利用逐渐成为社会密切关注的热点。秸秆造纸是其中的一个重要方向。造纸工业是污染源中的大户,而制浆又是污染的重中之重。制浆是造纸工业的第一道工序,目前全球范围内基本上都是采用化学制浆或化学机械浆法,主要是碱法、亚硫酸铵法等,因此传统制浆工艺在制浆蒸煮过程中均会在一定程度上伴随着大量的黑液废液的排出,严重地污染着环境。随着环境保护要求日益严格,传统制浆造纸企业需要投入大量的成本来对生产过程中产生的含有高毒性和强致癌性物质的污水进行处理,增加了企业生产成本的同时也降低了企业产品的市场竞争能力。因此有必要对传统工艺进行改进,提高制浆工艺的环境友好性。In recent years, with the development of modern industry, the problems of energy shortage and environmental pollution have become increasingly prominent, and the comprehensive utilization of straw resources has gradually become a hot spot that the society pays close attention to. Straw papermaking is one of the important directions. The paper industry is a major source of pollution, and pulping is the most important pollution source. Pulping is the first process in the paper industry. At present, chemical pulping or chemical-mechanical pulping methods are basically used worldwide, mainly alkaline methods, ammonium sulfite methods, etc. Therefore, traditional pulping processes are used in the pulping and cooking process. To a certain extent, Zhongjun will be accompanied by the discharge of a large amount of black liquor waste, which seriously pollutes the environment. With the increasingly stringent environmental protection requirements, traditional pulp and paper companies need to invest a lot of costs to treat sewage containing highly toxic and strong carcinogenic substances generated during the production process, which increases the production cost of the company and reduces the company's products. Market competitiveness. Therefore, it is necessary to improve the traditional process to improve the environmental friendliness of the pulping process.
自二十世纪五十年代起,生物技术得到了突飞猛进的发展,利用生物学方法去替代解决工业生产中的某些工艺成为研究的热点,在制浆领域,生物法因其利用微生物自身产生的纤维素酶来降解木质纤维素,高效经济且安全受到了 广泛关注。因此有必要对传统工艺进行改进,提高制浆工艺的环境友好性。Since the 1950s, biotechnology has developed by leaps and bounds. The use of biological methods to replace and solve certain processes in industrial production has become a research hotspot. In the field of pulping, biological methods are due to the use of microorganisms themselves. Cellulase is used to degrade lignocellulose, which is highly efficient, economical and safe, and has attracted widespread attention. Therefore, it is necessary to improve the traditional process to improve the environmental friendliness of the pulping process.
发明内容Summary of the invention
基于此,本发明的目的在于克服上述现有技术的不足之处而提供一种秸秆生物降解复合菌剂。Based on this, the purpose of the present invention is to overcome the above-mentioned shortcomings of the prior art and provide a straw biodegradable composite microbial agent.
为实现上述目的,本发明所采取的技术方案为:一种秸秆生物降解复合菌剂,所述复合菌剂为枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌和变色栓菌的复配。In order to achieve the above objective, the technical solution adopted by the present invention is: a straw biodegradable composite inoculum, the composite inoculum is Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and The compound of Trametes versicolor.
本申请复合菌剂中,黄孢原毛平革菌和变色栓菌主要对秸秆中的木质素进行脱除,且有助于漂白、染料脱色;枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌主要进行半纤维素的疏解。Among the compound bacteria in this application, Phanerochaete chrysosporium and Trametes versicolor mainly remove lignin from straw, and are helpful for bleaching and dye decolorization; Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus Mainly carry out the decomposing of hemicellulose.
优选地,所述枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌和变色栓菌的菌落数配比为:(1~3):(1~3):(1~3):(1~3):(1~3)。Preferably, the ratio of the colony numbers of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and Trametes versicolor is: (1-3): (1-3): (1) ~3):(1~3):(1~3).
更优选地,所述枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌和变色栓菌的菌落数配比为:1:1:1:1:1。More preferably, the ratio of the number of colonies of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and Trametes versicolor is 1:1:1:1:1.
同时,本发明还提供一种所述的秸秆生物降解复合菌剂的制备方法,包括如下步骤:At the same time, the present invention also provides a preparation method of the straw biodegradable composite microbial agent, which includes the following steps:
1)菌落活化:将枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌、变色栓菌在无菌条件下分别接种于固体平板,活化菌落;1) Colony activation: Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor are respectively inoculated on solid plates under aseptic conditions to activate the colonies;
2)种子培养:将上述活化的菌种在无菌条件下分别接种于液体培养基,在150-180rpm摇床培养;2) Seed culture: inoculate the above-mentioned activated strains in liquid culture medium under aseptic conditions, and cultivate in a shaker at 150-180rpm;
3)发酵培养:将上述种子液接种于液体培养基中,发酵培养;3) Fermentation culture: inoculate the above-mentioned seed liquid in a liquid medium, and ferment culture;
4)复合菌剂的制备:将上述发酵培养液按照配比进行混合,配制得到所述复合菌剂。4) Preparation of the compound bacterial agent: the above-mentioned fermentation culture broth is mixed according to the ratio to prepare the compound bacterial agent.
优选地,所述步骤1)中,枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌接种于YPD平板培养1-3天;黄孢原毛平革菌、变色栓菌接种于马铃薯培养基(PDA)平板培养3-5天。Preferably, in step 1), Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus are inoculated on YPD plates and cultured for 1-3 days; Phanerochaete chrysosporium and Trametes versicolor are inoculated on potato culture medium (PDA ) Plate culture for 3-5 days.
优选地,所述步骤2)中,枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌于25℃-30℃条件下接种YPD液体培养基中摇床培养2-4天;黄孢原毛平革菌、变色栓菌在25℃-30℃条件下接种于马铃薯液体培养基中摇床培养3-5天。Preferably, in the step 2), Bacillus subtilis, Bacillus amyloliquefaciens and Bacillus cereus are inoculated in YPD liquid medium at 25°C-30°C and cultured on a shaker for 2-4 days; Bacteria and Trametes versicolor were inoculated into potato liquid medium and cultured on a shaker for 3-5 days at 25°C-30°C.
优选地,所述步骤3)中,种子液的接种量为液体培养基体积的0.5-2%。Preferably, in the step 3), the inoculation amount of the seed liquid is 0.5-2% of the volume of the liquid culture medium.
更优选地,所述步骤3)中,种子液的接种量为液体培养基体积的1%。More preferably, in the step 3), the inoculation amount of the seed liquid is 1% of the volume of the liquid culture medium.
此外,本发明还提供一种所述的秸秆生物降解复合菌剂在制浆工艺中的应用。In addition, the present invention also provides an application of the straw biodegradable composite bacterial agent in a pulping process.
优选地,所述制浆工艺包括如下步骤:Preferably, the pulping process includes the following steps:
1)秸秆的预处理:将秸秆进行去杂粉碎;1) Pretreatment of straws: the straws are removed and crushed;
2)蒸煮灭菌:将粉碎后的秸秆进行蒸煮灭菌处理,灭菌温度为115-121℃,灭菌时间为15-20min;2) Retort and sterilize: the crushed straw is subjected to retort sterilization, the sterilization temperature is 115-121℃, and the sterilization time is 15-20min;
3)生物降解:将蒸煮灭菌后的秸秆送入降解池,待冷却后向降解池内加入含有秸秆生物降解复合菌剂的活性发酵液,混合均匀,发酵降解至秸秆呈蓬松状,得到纸浆原料;3) Biodegradation: The straw after cooking and sterilization is sent to the degradation tank, and after cooling, the active fermentation broth containing the straw biodegradable compound bacterial agent is added to the degradation tank, mixed evenly, and fermented and degraded until the straw is fluffy to obtain the pulp raw material ;
4)过滤:将滤网滤出的纸浆原料放入浆池中,加水搅拌成纸浆,加入制浆助剂后再搅拌混匀,其中,所述制浆助剂的质量为所述纸浆质量的3%-5%;4) Filtration: Put the pulp raw material filtered by the filter into the pulp tank, add water and stir to form pulp, add the pulping auxiliary agent and then stir and mix, wherein the quality of the pulping auxiliary agent is equal to the quality of the pulp 3%-5%;
5)磨浆;5) Refining;
6)漂白;6) Bleaching;
7)挤干水分。7) Squeeze out the water.
优选地,所述步骤3)中,所述活性发酵液的加入量为植物纤维总重量的20%-40%。Preferably, in the step 3), the added amount of the active fermentation broth is 20%-40% of the total weight of the plant fiber.
本申请上述活性发酵液的加入量是在综合考虑发酵液的使用与降解效果基础上,发现上述范围的加入量,在既可以节省发酵液的使用量,处理时间适中,降解效果适合的情况下进行的选择,虽然增加使用量可以加快降解,但是成本也比较高。The addition amount of the above-mentioned active fermentation broth in this application is based on comprehensive consideration of the use and degradation effect of the fermentation broth. It is found that the addition amount in the above range can save the usage of the fermentation broth, the processing time is moderate, and the degradation effect is suitable. The choice made, although increasing the amount of use can accelerate the degradation, but the cost is also relatively high.
优选地,所述步骤3)中,发酵的温度为20-30℃,发酵的时间为48-120小时。本申请上述复合菌剂发酵温度及时间的选择,可以更好的保证纤维素进行 有效的分解。Preferably, in the step 3), the fermentation temperature is 20-30°C, and the fermentation time is 48-120 hours. The selection of the fermentation temperature and time of the above-mentioned composite bacterial agent in this application can better ensure the effective decomposition of cellulose.
更优选地,当发酵温度为20-25℃时,发酵时间为80-120h;当发酵温度为25-30℃时,发酵时间为48-80h。More preferably, when the fermentation temperature is 20-25°C, the fermentation time is 80-120h; when the fermentation temperature is 25-30°C, the fermentation time is 48-80h.
优选地,所述步骤4)中,所述制浆助剂包含以下重量份的成分:尿素20-30份、DTPA 10-20份、脂肪醇聚氧烷基醚15-25份和脂肪醇聚氧乙烯醚15-25份。Preferably, in the step 4), the pulping aid includes the following components by weight: 20-30 parts of urea, 10-20 parts of DTPA, 15-25 parts of fatty alcohol polyoxyalkyl ether and fatty alcohol polyoxyethylene 15-25 parts of oxyethylene ether.
更优选地,所述制浆助剂还包含钙粉与元明粉以等比例混合的赋形剂。More preferably, the pulping auxiliary agent further comprises an excipient in which calcium powder and sodium sulfate are mixed in equal proportions.
其中,DTPA能够消除重金属离子对后续过氧化氢的影响;尿素能够促进过氧化氢稳定快速的分解;脂肪醇聚氧烷基醚与脂肪醇聚氧乙烯醚起到渗透乳化的作用。Among them, DTPA can eliminate the influence of heavy metal ions on subsequent hydrogen peroxide; urea can promote the stable and rapid decomposition of hydrogen peroxide; fatty alcohol polyoxyalkyl ether and fatty alcohol polyoxyethylene ether play a role in osmotic emulsification.
优选地,所述磨浆为纸浆通过输送带带入高浓磨浆机,加入30-45℃的水,经过高速磨片使浆料中的纤维分解。Preferably, the refining is that the pulp is brought into a high-consistency refiner through a conveyor belt, and 30-45° C. water is added, and the fibers in the slurry are decomposed through a high-speed refining sheet.
优选地,所述漂白为:磨浆结束后向纸浆中加入过氧化氢进行漂白处理2-3h,漂白处理后升温至90℃使过氧化氢分解。Preferably, the bleaching is: adding hydrogen peroxide to the pulp after refining for bleaching treatment for 2-3 hours, and raising the temperature to 90° C. to decompose the hydrogen peroxide after the bleaching treatment.
优选地,所述挤干水分的过程为:将经过漂白处理的制浆输送到滤网中过滤掉纸浆中的部分水分,其中水排到滤网下部的蓄水池,过滤后的纸浆再通过挤干机,挤出40-50%的水分,再通过打包机,挤出水分10%,纸浆成品干度在50-60%。Preferably, the process of squeezing the moisture is: transporting the bleached pulp to the filter screen to filter out part of the moisture in the pulp, wherein the water is discharged to the reservoir at the lower part of the filter screen, and the filtered pulp passes through The squeezing machine squeezes out 40-50% of the moisture, and then passes through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp is 50-60%.
相对于现有技术,本发明的有益效果为:Compared with the prior art, the beneficial effects of the present invention are:
本发明属于环保型技术,通过采用枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌和变色栓菌复合菌剂对农作物秸秆进行处理,因而避免了传统制浆工艺中大量化学试剂的使用对环境的污染,在制浆的生产工艺过程中水可以循环使用,不排放任何含有有机化合物和悬浮物的污水,避免了污水治理的环节,节约了生产成本,降低了能耗消耗,全部生产工艺过程中无需加热,常温分解,常温漂白。The invention belongs to an environmentally-friendly technology, which uses Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor compound inoculants to process crop straws, thereby avoiding the traditional pulping process The use of a large number of chemical reagents pollutes the environment. During the pulping production process, water can be recycled without discharging any sewage containing organic compounds and suspended solids, avoiding the process of sewage treatment, saving production costs, and reducing energy. Consumption and consumption, no heating required during all production processes, decomposition at room temperature, and bleaching at room temperature.
该技术设计新颖、独特,思路清晰,适应性和普遍性强,产业化程度高; 利用复合微生物菌剂进行制浆,避免了大量化学制剂的使用,解决了传统制浆工艺中废水的处理问题,降低了企业的生产成本,技术先进,同时兼具环保性,符合国家节能减排战略。The technology has novel and unique design, clear thinking, strong adaptability and universality, and a high degree of industrialization; the use of composite microbial agents for pulping avoids the use of a large number of chemical agents and solves the problem of wastewater treatment in the traditional pulping process , Which reduces the production cost of the enterprise, has advanced technology, and is environmentally friendly, in line with the national energy-saving emission reduction strategy.
附图说明Description of the drawings
图1为本发明制浆工艺流程图。Figure 1 is a flow chart of the pulping process of the invention.
具体实施方式Detailed ways
为更好的说明本发明的目的、技术方案和优点,下面将结合附图和具体实施例对本发明作进一步说明。In order to better illustrate the objectives, technical solutions and advantages of the present invention, the present invention will be further described below with reference to the accompanying drawings and specific embodiments.
实施例中培养基的配制:The preparation of the culture medium in the embodiment:
马铃薯培养基(PDA)成分如下:马铃薯提取液1.0L,葡萄糖20.0g,KH 2PO 43.0g,MgSO 4.7H 2O 1.5g,琼脂15.0g(液体培养基无需),pH 6.0。所述马铃薯提取液的制备方法:取去皮马铃薯200g,切成小块,加水1.0L煮沸30min,滤去马铃薯块,将滤液补足至1.0L; The components of potato culture medium (PDA) are as follows: potato extract 1.0L, glucose 20.0g, KH 2 PO 4 3.0 g, MgSO 4 .7H 2 O 1.5 g, agar 15.0 g (no need for liquid medium), pH 6.0. The preparation method of the potato extract: take 200g of peeled potatoes, cut into small pieces, add 1.0L of water and boil for 30min, filter out the potato pieces, and make up the filtrate to 1.0L;
YPD培养基的成分如下:酵母提取物1%,胰蛋白胨2%,葡萄糖2%,琼脂1%(液体培养基无需)。The composition of YPD medium is as follows: yeast extract 1%, tryptone 2%, glucose 2%, agar 1% (liquid medium is not required).
实施例1Example 1
本发明所述秸秆生物降解复合菌剂的一种实施例,本实施例所述秸秆生物降解复合菌剂的制备方法如下:An embodiment of the straw biodegradable composite inoculum of the present invention, the preparation method of the straw biodegradable composite inoculum in this embodiment is as follows:
1)斜面培养:将枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌接种于YPD平板活化3天;黄孢原毛平革菌,变色栓菌接种于马铃薯培养基(PDA)平板活化4天。1) Slant culture: Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus were inoculated on YPD plates and activated for 3 days; Phanerochaete chrysosporium and Trametes versicolor were inoculated on potato medium (PDA) plates and activated for 4 days.
2)将上述活化的菌种在无菌条件下分别接种于对应的液体培养基,30℃,180rpm摇床培养。其中枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌2天;黄孢原毛平革菌,变色栓菌培养5天;2) The above-mentioned activated strains were respectively inoculated into the corresponding liquid medium under aseptic conditions, and cultured on a shaker at 30°C and 180 rpm. Among them, Bacillus subtilis, Bacillus amyloliquefaciens and Bacillus cereus were cultured for 2 days; Phanerochaete chrysosporium and Trametes versicolor were cultured for 5 days;
3)将上述种子液接种于液体培养基中,发酵培养。接种量为液体培养基的体 积的1%,发酵时间为7天。3) Inoculating the above seed liquid in a liquid medium, and fermenting it. The inoculation amount was 1% of the volume of the liquid medium, and the fermentation time was 7 days.
4)按照枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌,黄孢原毛平革菌,变色栓菌的菌落形成单位数目3:1:3:1:3混合配制即得秸秆降解菌系。4) According to the number of colony forming units of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor, the number of colony forming units 3:1:3:1:3 is mixed to obtain a straw-degrading bacterial system.
将上述制备得到的秸秆生物降解复合菌剂应用于植物秸秆生物降解制浆,具体方法如附图1所示:The straw biodegradable composite microbial agent prepared above is applied to plant straw biodegradable pulping, and the specific method is shown in Figure 1:
1、将秸秆使用切碎机进行切段处理,切断长度为5-10cm,切断后对秸秆进行清洗,去除秸秆上的杂质,清洗后晒干;1. Use a shredder to cut the straw into sections with a length of 5-10cm. After cutting, clean the straw to remove impurities on the straw, and then dry it after cleaning;
2、使用立式粉碎机将秸秆进行粉碎处理;2. Use a vertical crusher to crush the straw;
3、将粉碎后的植物秸秆进行蒸煮灭菌处理,蒸煮灭菌时间为20分钟,温度为120℃;3. The crushed plant stalks are subjected to steaming sterilization treatment, the steaming sterilization time is 20 minutes, and the temperature is 120°C;
4、蒸煮灭菌后的的植物秸秆送入降解池,待冷却后向降解池内加入麦草秸秆干重30%的复合菌发酵母液,混合均匀,在30℃进行发酵降解72小时至秸秆呈蓬松状即为纸浆原料;4. The boiled and sterilized plant stalks are sent to the degradation tank. After cooling, add 30% of the dry weight of wheat straw stalks to the degradation tank, mix them evenly, and carry out fermentation and degradation at 30°C for 72 hours until the stalks are fluffy. The shape is the pulp raw material;
5、使用滤网将降解池中的滤液排出至贮备罐,贮备罐中的降解液可继续投入复合菌发酵罐以循环利用;5. Use a filter screen to discharge the filtrate in the degradation tank to the storage tank, and the degradation liquid in the storage tank can continue to be put into the compound bacteria fermentation tank for recycling;
6、将滤网滤出的纸浆原料放入制浆池中,加水搅拌成纸浆,向其中加入3%的制浆助剂,搅拌混匀,以100重量份计,所述制浆助剂的成分为:尿素20份、DTPA 10份、脂肪醇聚氧烷基醚15份和脂肪醇聚氧乙烯醚25份,余量为钙粉与元明粉以等比例混合的赋形剂;6. Put the pulp raw material filtered by the filter into the pulping tank, add water and stir to form pulp, add 3% pulping auxiliary agent to it, stir and mix, based on 100 parts by weight, the pulping auxiliary agent The ingredients are: 20 parts of urea, 10 parts of DTPA, 15 parts of fatty alcohol polyoxyalkyl ether and 25 parts of fatty alcohol polyoxyethylene ether. The balance is an excipient mixed with calcium powder and sodium sulfate in equal proportions;
7、将上述纸浆送入高浓磨浆机内进行磨浆,所述磨浆为纸浆通过输送带带入高浓磨浆机,加入30℃的水,经过高速磨片使浆料中的纤维分解;7. The above-mentioned pulp is sent to the high-consistency refiner for refining. The refining is the pulp that is brought into the high-consistency refiner through a conveyor belt, and water at 30°C is added to make the fibers in the slurry through high-speed refining. break down;
8、磨浆结束后向上述纸浆中加入秸秆20%干重的过氧化氢进行漂白处理,处理时间为2h,漂白结束后升温至90℃使过氧化氢分解;8. After refining, add 20% hydrogen peroxide of dry weight of straw to the pulp for bleaching treatment. The treatment time is 2h. After bleaching, the temperature is increased to 90°C to decompose the hydrogen peroxide;
9、将步骤8中的经过漂白处理的制浆输送到滤网中过滤掉纸浆中的部分水分,其中水排到滤网下部的蓄水池,过滤后的纸浆再通过挤干机,挤出40-50%的水分,再通过打包机,挤出水分10%,纸浆成品干度在50-60%。9. Transport the bleached pulp in step 8 to the filter screen to filter out part of the water in the pulp, where the water is drained to the reservoir at the bottom of the filter screen, and the filtered pulp is then passed through a squeezer and extruded 40-50% of the moisture is passed through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp will be 50-60%.
实施例2Example 2
本发明所述秸秆生物降解复合菌剂的一种实施例,本实施例所述秸秆生物 降解复合菌剂的制备方法如下:An embodiment of the straw biodegradable composite inocula of the present invention, the preparation method of the straw biodegradable composite inocula in this embodiment is as follows:
1)斜面培养:将枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌接种于YPD平板活化1天;黄孢原毛平革菌,变色栓菌接种于马铃薯培养基(PDA)平板活化3天。1) Slant culture: Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus were inoculated on YPD plates and activated for 1 day; Phanerochaete chrysosporium and Trametes versicolor were inoculated on potato medium (PDA) plates and activated for 3 days.
2)将上述活化的菌种在无菌条件下分别接种于对应的液体培养基,30℃,180rpm摇床培养。其中枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌3天;黄孢原毛平革菌,变色栓菌培养3天;2) The above-mentioned activated strains were respectively inoculated into the corresponding liquid medium under aseptic conditions, and cultured on a shaker at 30°C and 180 rpm. Among them, Bacillus subtilis, Bacillus amyloliquefaciens and Bacillus cereus were cultured for 3 days; Phanerochaete chrysosporium and Trametes versicolor were cultured for 3 days;
3)将上述种子液接种于液体培养基中,发酵培养。接种量为液体培养基的体积的0.5%,发酵时间为5天。3) Inoculating the above seed liquid in a liquid medium, and fermenting it. The inoculation amount is 0.5% of the volume of the liquid medium, and the fermentation time is 5 days.
4)按照枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌,黄孢原毛平革菌,变色栓菌的菌落形成单位数目1:3:1:3:1混合配制即得秸秆降解菌系。4) According to the 1:3:1:3:1 mixture of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor, the number of colony forming units is 1:3:1:3:1 to obtain a straw-degrading bacterial system.
将上述制备得到的秸秆生物降解复合菌剂应用于植物秸秆生物降解制浆,具体方法如下:The straw biodegradable composite inoculum prepared above is applied to plant straw biodegradable pulping, and the specific method is as follows:
1、将秸秆使用切碎机进行切段处理,切断长度为5-10cm,切断后对秸秆进行清洗,去除秸秆上的杂质,清洗后晒干;1. Use a shredder to cut the straw into sections with a length of 5-10cm. After cutting, clean the straw to remove impurities on the straw, and then dry it after cleaning;
2、使用立式粉碎机将秸秆进行粉碎处理;2. Use a vertical crusher to crush the straw;
3、将粉碎后的植物秸秆进行蒸煮灭菌处理,蒸煮灭菌时间为20分钟,温度为120℃;3. The crushed plant stalks are subjected to steaming sterilization treatment, the steaming sterilization time is 20 minutes, and the temperature is 120°C;
4、蒸煮灭菌后的的植物秸秆送入降解池,待冷却后向降解池内加入麦草秸秆干重20%的复合菌发酵母液,混合均匀,在25℃进行发酵降解48小时至秸秆呈蓬松状即为纸浆原料;4. The boiled and sterilized plant stalks are sent to the degradation tank. After cooling, add 20% of the dry weight of the wheat straw stalks to the degradation tank, mix them evenly, and carry out fermentation and degradation at 25°C for 48 hours until the stalks are fluffy. The shape is the pulp raw material;
5、使用滤网将降解池中的滤液排出至贮备罐,贮备罐中的降解液可继续投入复合菌发酵罐以循环利用;5. Use a filter screen to discharge the filtrate in the degradation tank to the storage tank, and the degradation liquid in the storage tank can continue to be put into the compound bacteria fermentation tank for recycling;
6、将滤网滤出的纸浆原料放入制浆池中,加水搅拌成纸浆,向其中加入4%的制浆助剂,搅拌混匀,以100重量份计,所述制浆助剂的成分为:尿素30份、DTPA 20份、脂肪醇聚氧烷基醚25份和脂肪醇聚氧乙烯醚15份,余量为钙粉与元明粉以等比例混合的赋形剂;6. Put the pulp raw material filtered out by the filter into the pulping tank, add water and stir to form pulp, add 4% pulping auxiliary agent to it, stir and mix, based on 100 parts by weight, the pulping auxiliary agent The ingredients are: 30 parts of urea, 20 parts of DTPA, 25 parts of fatty alcohol polyoxyalkyl ether and 15 parts of fatty alcohol polyoxyethylene ether. The balance is an excipient mixed with calcium powder and sodium sulfate in equal proportions;
7、将上述纸浆送入高浓磨浆机内进行磨浆,所述磨浆为纸浆通过输送带带入高浓磨浆机,加入45℃的水,经过高速磨片使浆料中的纤维分解;7. The above-mentioned pulp is sent to a high-consistency refiner for refining. The refining is the pulp that is brought into the high-consistency refiner through a conveyor belt, and water at 45°C is added to make the fibers in the slurry through high-speed grinding. break down;
8、磨浆结束后向上述纸浆中加入秸秆20%干重的过氧化氢进行漂白处理,处理时间为2h,漂白结束后升温至90℃使过氧化氢分解;8. After refining, add 20% hydrogen peroxide of dry weight of straw to the pulp for bleaching treatment. The treatment time is 2h. After bleaching, the temperature is increased to 90°C to decompose the hydrogen peroxide;
9、将步骤8中的经过漂白处理的制浆输送到滤网中过滤掉纸浆中的部分水分,其中水排到滤网下部的蓄水池,过滤后的纸浆再通过挤干机,挤出40-50%的水分,再通过打包机,挤出水分10%,纸浆成品干度在50-60%。9. Transport the bleached pulp in step 8 to the filter screen to filter out part of the water in the pulp, where the water is drained to the reservoir at the bottom of the filter screen, and the filtered pulp is then passed through a squeezer and extruded 40-50% of the moisture is passed through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp will be 50-60%.
实施例3Example 3
本发明所述秸秆生物降解复合菌剂的一种实施例,本实施例所述秸秆生物降解复合菌剂的制备方法如下:An embodiment of the straw biodegradable composite inoculum of the present invention, the preparation method of the straw biodegradable composite inoculum in this embodiment is as follows:
1)斜面培养:将枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌接种于YPD平板活化2天;黄孢原毛平革菌,变色栓菌接种于马铃薯培养基(PDA)平板活化5天。1) Slant culture: Bacillus subtilis, Bacillus amyloliquefaciens, and Bacillus cereus were inoculated on YPD plates and activated for 2 days; Phanerochaete chrysosporium and Trametes versicolor were inoculated on potato medium (PDA) plates and activated for 5 days.
2)将上述活化的菌种在无菌条件下分别接种于对应的液体培养基,30℃,180rpm摇床培养。其中枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌4天;黄孢原毛平革菌,变色栓菌培养4天;2) The above-mentioned activated strains were respectively inoculated into the corresponding liquid medium under aseptic conditions, and cultured on a shaker at 30°C and 180 rpm. Among them, Bacillus subtilis, Bacillus amyloliquefaciens and Bacillus cereus were cultured for 4 days; Phanerochaete chrysosporium and Trametes versicolor were cultured for 4 days;
3)将上述种子液接种于液体培养基中,发酵培养。接种量为液体培养基的体积的2%,发酵时间为6天。3) Inoculating the above seed liquid in a liquid medium, and fermenting it. The inoculation amount was 2% of the volume of the liquid medium, and the fermentation time was 6 days.
4)按照枯草芽孢杆菌,解淀粉芽孢杆菌,蜡样芽孢杆菌,黄孢原毛平革菌,变色栓菌的菌落形成单位数目1:1:1:1:1混合配制即得秸秆降解菌系。4) According to the number of colony forming units of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor, the number of colony forming units is 1:1:1:1:1 to obtain a straw-degrading bacteria system.
将上述制备得到的秸秆生物降解复合菌剂应用于植物秸秆生物降解制浆,具体方法如下:The straw biodegradable composite inoculum prepared above is applied to plant straw biodegradable pulping, and the specific method is as follows:
1、将秸秆使用切碎机进行切段处理,切断长度为5-10cm,切断后对秸秆进行清洗,去除秸秆上的杂质,清洗后晒干;1. Use a shredder to cut the straw into sections with a length of 5-10cm. After cutting, clean the straw to remove impurities on the straw, and then dry it after cleaning;
2、使用立式粉碎机将秸秆进行粉碎处理;2. Use a vertical crusher to crush the straw;
3、将粉碎后的植物秸秆进行蒸煮灭菌处理,蒸煮灭菌时间为15分钟,温度为118℃;3. The crushed plant straws are subjected to steaming and sterilization treatment, the steaming and sterilization time is 15 minutes, and the temperature is 118°C;
4、蒸煮灭菌后的的植物秸秆送入降解池,待冷却后向降解池内加入麦草秸秆干重40%的复合菌发酵母液,混合均匀,在20℃进行发酵降解120小时至秸秆呈蓬松状即为纸浆原料;4. The boiled and sterilized plant stalks are sent to the degradation tank. After cooling, add the composite bacteria yeast solution of 40% of the dry weight of wheat straw stalks to the degradation tank, mix well, and carry out fermentation and degradation at 20°C for 120 hours until the straws are fluffy. The shape is the pulp raw material;
5、使用滤网将降解池中的滤液排出至贮备罐,贮备罐中的降解液可继续投入复合菌发酵罐以循环利用;5. Use a filter screen to discharge the filtrate in the degradation tank to the storage tank, and the degradation liquid in the storage tank can continue to be put into the compound fermentation tank for recycling;
6、将滤网滤出的纸浆原料放入制浆池中,加水搅拌成纸浆,向其中加入5%的制浆助剂,搅拌混匀,以100重量份计,所述制浆助剂的成分为:尿素25份、DTPA 15份、脂肪醇聚氧烷基醚22份和脂肪醇聚氧乙烯醚18份,余量为钙粉与元明粉以等比例混合的赋形剂;6. Put the pulp raw material filtered by the filter into the pulping tank, add water and stir to form pulp, add 5% pulping auxiliary agent to it, stir and mix well, based on 100 parts by weight, the pulping auxiliary agent The ingredients are: 25 parts of urea, 15 parts of DTPA, 22 parts of fatty alcohol polyoxyalkyl ether and 18 parts of fatty alcohol polyoxyethylene ether. The balance is an excipient mixed with calcium powder and sodium sulfate in equal proportions;
7、将上述纸浆送入高浓磨浆机内进行磨浆,所述磨浆为纸浆通过输送带带入高浓磨浆机,加入40℃的水,经过高速磨片使浆料中的纤维分解;7. The above-mentioned pulp is sent to a high-consistency refiner for refining. The refining is the pulp that is brought into the high-consistency refiner through a conveyor belt, and water at 40°C is added to make the fibers in the slurry through high-speed grinding. break down;
8、磨浆结束后向上述纸浆中加入秸秆20%干重的过氧化氢进行漂白处理,处理时间为2h,漂白结束后升温至90℃使过氧化氢分解;8. After refining, add hydrogen peroxide of 20% dry weight of straw to the pulp for bleaching. The treatment time is 2h. After bleaching, the temperature is raised to 90°C to decompose hydrogen peroxide;
9、将步骤8中的经过漂白处理的制浆输送到滤网中过滤掉纸浆中的部分水分,其中水排到滤网下部的蓄水池,过滤后的纸浆再通过挤干机,挤出40-50%的水分,再通过打包机,挤出水分10%,纸浆成品干度在50-60%。9. Transport the bleached pulp in step 8 to the filter screen to filter out part of the water in the pulp. The water is drained to the reservoir at the bottom of the filter screen. The filtered pulp is then passed through a squeezer and extruded. 40-50% of the moisture is passed through the baler to squeeze out 10% of the moisture, and the dryness of the finished pulp will be 50-60%.
对本发明的秸秆生物酶降解制浆工艺条件下制得的纸浆浆料分别进行浆得率,白度和所制得纸张的断裂长及环压指数检测,浆得率的计算公式:(m 1/m)*100%(m 1指粗浆干重,m指原料干重),白度以及纸张的断裂长和环压指数分别使用白度测定仪器、纸张抗张强度测定仪测定,检测结果如下表1所示。 The pulp yield, whiteness, breaking length and ring pressure index of the paper pulp prepared under the conditions of the straw bioenzymatic degradation pulping process of the present invention are respectively tested, and the formula for calculating the pulp yield: (m 1 /m)*100% (m 1 refers to the dry weight of coarse pulp, m refers to the dry weight of raw materials), the whiteness and the breaking length of the paper and the ring pressure index were measured with a whiteness measuring instrument and a paper tensile strength measuring instrument. The test results As shown in Table 1 below.
表1 本发明的秸秆生物酶降解制浆工艺条件下制得的纸浆性能Table 1 The properties of pulp prepared under the conditions of the straw bioenzymatic degradation pulping process of the present invention
 To 实施例1Example 1 实施例2Example 2 实施例3Example 3
浆得率(%)Pulp yield (%) 75.275.2 74.374.3 77.677.6
白度(%ISO)Whiteness (%ISO) 8686 8585 8989
断裂长(Km)Break length (Km) 4.714.71 4.854.85 4.684.68
环压指数(N.m/g)Ring pressure index (N.m/g) 11.211.2 11.311.3 11.511.5
由表1可以看出,本发明实施例提供的使用复合生物菌剂对秸秆进行生物制浆的方法,所得造纸浆料的浆得率高于70%,白度高于85%,断裂长大于4.6Km,环压指数高于11.2N.m/g,且当各菌的比例为1:1:1:1:1时,浆得率、白度分别为77.6%、89%,效果较好。表明本发明提供的复合生物菌剂生物制浆的方法在得浆率和白度上满足需求,所制成纸张的机械性能也较优异。It can be seen from Table 1 that the method for biological pulping of straw using composite biological inoculants provided in the embodiments of the present invention has a pulp yield of more than 70%, whiteness of more than 85%, and a break length of more than 70%. 4.6Km, the ring pressure index is higher than 11.2Nm/g, and when the ratio of the bacteria is 1:1:1:1:1, the pulp yield and whiteness are 77.6% and 89%, respectively, and the effect is good. It shows that the method for biological pulping with a composite biological inoculum provided by the present invention meets the requirements in terms of pulp yield and whiteness, and the mechanical properties of the prepared paper are also excellent.
最后所应当说明的是,以上实施例仅用以说明本发明的技术方案而非对本 发明保护范围的限制,尽管参照较佳实施例对本发明作了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的实质和范围。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit the protection scope of the present invention. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that, The technical solution of the present invention can be modified or equivalently replaced without departing from the essence and scope of the technical solution of the present invention.

Claims (10)

  1. 一种秸秆生物降解复合菌剂,其特征在于,所述复合菌剂为枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌和变色栓菌的复配。A straw biodegradable composite inoculum is characterized in that the composite inoculum is a combination of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor.
  2. 如权利要求1所述的秸秆生物降解复合菌剂,其特征在于,所述枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌和变色栓菌的菌落数配比为:(1~3):(1~3):(1~3):(1~3):(1~3)。The straw biodegradable composite inoculum according to claim 1, wherein the ratio of the number of colonies of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and Trametes versicolor is : (1~3):(1~3):(1~3):(1~3):(1~3).
  3. 如权利要求2所述的秸秆生物降解复合菌剂,其特征在于,所述枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌和变色栓菌的菌落数配比为:1:1:1:1:1。The straw biodegradable compound inoculum according to claim 2, wherein the ratio of the colony numbers of Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium and Trametes versicolor is :1:1:1:1:1.
  4. 一种如权利要求1~3任一项所述的秸秆生物降解复合菌剂的制备方法,其特征在于,包括如下步骤:A method for preparing a straw biodegradable composite microbial agent according to any one of claims 1 to 3, characterized in that it comprises the following steps:
    1)菌落活化:将枯草芽孢杆菌、解淀粉芽孢杆菌、蜡样芽孢杆菌、黄孢原毛平革菌、变色栓菌在无菌条件下分别接种于固体平板,活化菌落;1) Colony activation: Bacillus subtilis, Bacillus amyloliquefaciens, Bacillus cereus, Phanerochaete chrysosporium, and Trametes versicolor are respectively inoculated on solid plates under aseptic conditions to activate the colonies;
    2)种子培养:将上述活化的菌种在无菌条件下分别接种于液体培养基,在150-180rpm摇床培养;2) Seed culture: inoculate the above-mentioned activated strains into liquid culture medium under aseptic conditions, and cultivate in a shaker at 150-180rpm;
    3)发酵培养:将上述种子液接种于液体培养基中,发酵培养;3) Fermentation culture: inoculate the above-mentioned seed liquid in a liquid medium, and ferment culture;
    4)复合菌剂的制备:将上述发酵培养液按照配比进行混合,配制得到所述复合菌剂。4) Preparation of the compound bacterial agent: the above-mentioned fermentation culture broth is mixed according to the ratio to prepare the compound bacterial agent.
  5. 如权利要求4所述的秸秆生物降解复合菌剂的制备方法,其特征在于,所述步骤3)中,种子液的接种量为液体培养基体积的0.5-2%。The method for preparing a straw biodegradable composite inoculum according to claim 4, wherein in the step 3), the inoculum of the seed liquid is 0.5-2% of the volume of the liquid culture medium.
  6. 一种如权利要求1~3任一项所述的秸秆生物降解复合菌剂在制浆工艺中的应用。An application of the straw biodegradable composite bacterial agent according to any one of claims 1 to 3 in a pulping process.
  7. 如权利要求6所述的应用,其特征在于,所述制浆工艺包括如下步骤:The application according to claim 6, wherein the pulping process includes the following steps:
    1)秸秆的预处理:将秸秆进行去杂粉碎;1) Pretreatment of straws: the straws are removed and crushed;
    2)蒸煮灭菌:将粉碎后的秸秆进行蒸煮灭菌处理,灭菌温度为115-121℃,灭菌时间为15-20min;2) Retort and sterilize: the crushed straw is subjected to retort sterilization, the sterilization temperature is 115-121℃, and the sterilization time is 15-20min;
    3)生物降解:将蒸煮灭菌后的秸秆送入降解池,待冷却后向降解池内加入含有秸秆生物降解复合菌剂的活性发酵液,混合均匀,发酵降解至秸秆呈蓬松状,得到纸浆原料;3) Biodegradation: The straw after cooking and sterilization is sent to the degradation tank, and after cooling, the active fermentation broth containing the straw biodegradable compound bacterial agent is added to the degradation tank, mixed evenly, and fermented and degraded until the straw is fluffy to obtain the pulp raw material ;
    4)过滤:将滤网滤出的纸浆原料放入浆池中,加水搅拌成纸浆,加入制浆助剂后再搅拌混匀,其中,所述制浆助剂的质量为所述纸浆质量的3%-5%;4) Filtration: Put the pulp raw material filtered by the filter into the pulp tank, add water and stir to form pulp, add the pulping auxiliary agent and then stir and mix, wherein the quality of the pulping auxiliary agent is equal to the quality of the pulp 3%-5%;
    5)磨浆;5) Refining;
    6)漂白;6) Bleaching;
    7)挤干水分。7) Squeeze out the water.
  8. 如权利要求7所述的应用,其特征在于,所述步骤3)中,所述活性发酵液的加入量为植物纤维总重量的20%-40%。The application according to claim 7, characterized in that, in the step 3), the added amount of the active fermentation broth is 20%-40% of the total weight of the plant fiber.
  9. 如权利要求7或8所述的应用,其特征在于,所述步骤3)中,发酵的温度为20-30℃,发酵的时间为48-120小时。The application according to claim 7 or 8, characterized in that, in the step 3), the temperature of fermentation is 20-30°C, and the time of fermentation is 48-120 hours.
  10. 如权利要求7所述的应用,其特征在于,所述步骤5)中,所述制浆助剂包含以下重量份的成分:尿素20-30份、DTPA 10-20份、脂肪醇聚氧烷基醚15-25份和脂肪醇聚氧乙烯醚15-25份。The application according to claim 7, characterized in that, in the step 5), the pulping aid contains the following components by weight: 20-30 parts of urea, 10-20 parts of DTPA, fatty alcohol polyoxane 15-25 parts of base ether and 15-25 parts of fatty alcohol polyoxyethylene ether.
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