WO2024036996A1 - Method for producing bacterial cellulose gel by directly utilizing livestock and poultry slaughtering tail water - Google Patents

Method for producing bacterial cellulose gel by directly utilizing livestock and poultry slaughtering tail water Download PDF

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WO2024036996A1
WO2024036996A1 PCT/CN2023/087720 CN2023087720W WO2024036996A1 WO 2024036996 A1 WO2024036996 A1 WO 2024036996A1 CN 2023087720 W CN2023087720 W CN 2023087720W WO 2024036996 A1 WO2024036996 A1 WO 2024036996A1
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tail water
bacterial cellulose
livestock
cellulose gel
culture medium
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PCT/CN2023/087720
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French (fr)
Chinese (zh)
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冯玉红
牛成
林强
赵振东
李嘉诚
刘海芳
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海南大学
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/03Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
    • C08J3/075Macromolecular gels
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L1/00Compositions of cellulose, modified cellulose or cellulose derivatives
    • C08L1/02Cellulose; Modified cellulose
    • 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
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/04Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12RINDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/01Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • C12R2001/02Acetobacter

Definitions

  • the invention relates to a resource recycling method for livestock and poultry animal slaughter tail water, and specifically relates to a method of directly utilizing livestock and poultry animal slaughter tail water to produce bacterial cellulose gel, which belongs to the technical field of comprehensive utilization of industrial waste.
  • Wastewater from livestock and poultry slaughtering and related meat processing is a typical organic wastewater. It is rich in protein and oil and does not contain toxic substances such as heavy metals.
  • the main nutrients are carbon (C), nitrogen (N), and phosphorus (P). , which belongs to high-concentration organic wastewater.
  • nitrogen mainly exists in the form of organic nitrogen or ammonium salt (NH 4 + ), while phosphorus mainly exists in the form of organic phosphorus or phosphate (PO 4 3- ).
  • Nitrogen and phosphorus are considered to be one of the main factors leading to eutrophication of water bodies, which are toxic to aquatic organisms.
  • the new standard clearly requires direct TN ⁇ 25mg/L, TP ⁇ 2mg/L in discharged wastewater, TN ⁇ 70mg/L, TP ⁇ 8mg/L in indirect discharged wastewater.
  • biological treatment processes or biochemical-based physicochemical and biochemical combination processes are often used at home and abroad to treat slaughtering wastewater. Therefore, it is technically difficult to treat slaughter tailwater as industrial wastewater discharge, and the treatment cost is high, which places a heavy burden on enterprises and causes a waste of biomass resources.
  • Bacterial cellulose is a natural macromolecule with a super-fibrous network structure connected by ⁇ -1,4 glycosidic bonds. Its diameter is only 1.5nm. It has high crystallinity, chemical purity, Mechanical strength, adsorption capacity and good biodegradability. Bacterial cellulose gel is prepared by biological culture method. In recent years, Feng Yuhong and others have biosynthesized bacterial cellulose with low relative molecular weight and in situ biosynthesized glyceraldehyde-modified bacterial cellulose. Niu Cheng et al. synthesized a three-dimensional structure nanobacterial cellulose gel by static culture in Acetobacter xylinum culture medium using coconut water as raw material.
  • the present invention provides a method for directly utilizing the tail water from the slaughter of livestock and poultry animals to produce bacterial cellulose gel. This method directly utilizes the tail water from the slaughter of livestock and poultry animals.
  • Small molecule peptides, nitrogen, phosphorus, inorganic salts and other nutrients in the tail water are used to produce bacterial cellulose gel, which eliminates the need for nutrients in plant-derived culture media that cannot be directly utilized by Acetobacter xylin and must undergo pre-fermentation before they can be used as culture media.
  • the process and time of synthesizing bacterial cellulose also solve the multiple problems of livestock and poultry slaughter tailwater being discharged as wastewater, such as high nitrogen and phosphorus content, high COD, high oil content, and high processing cost, and fully recycle and utilize the biomass in the tailwater.
  • the tail water from livestock and poultry slaughter can be directly used to produce bacterial cellulose with only simple filtration. Not only is the culture medium resource rich and cheap, it also simplifies and shortens the process, greatly reducing the production cost of bacterial cellulose. , achieving the effect of "killing two birds with one stone", in line with the concept of industrial green development.
  • the invention opens up a new situation in the biosynthesis of bacterial cellulose using animal-derived culture media, and eliminates the need for fermentation of plant-derived culture media before it can be used as a bacterial cellulose culture medium, thus opening up resources for livestock and poultry animal slaughter tail water.
  • a new way of chemical utilization has opened up new resources of high-quality, abundant and low-price culture media for bacterial cellulose, which has greatly reduced the production cost of bacterial cellulose.
  • a method for producing bacterial cellulose gel directly by using tail water from slaughtering livestock and poultry animals includes the following steps:
  • the tail water from livestock and poultry animal slaughter refers to the blood-containing wastewater produced during the slaughtering process of livestock and poultry animals, such as livestock pigs, cattle, sheep and poultry chickens, ducks, geese, etc. produced during the slaughtering process.
  • tailwaters and their mixtures Tail water mainly contains a large amount of blood, oil, fur, bone residue, meat residue, visceral debris and some undigested food. These tailwaters generally have the characteristics of high COD, high oil content and high solids.
  • the COD value in the tailwater is generally greater than 10 4 mg/L.
  • the main nutrients in the filtered tail water are carbon (C), nitrogen (N), and phosphorus (P). Nitrogen is mainly in the form of organic nitrogen or ammonium salt (NH 4 + ).
  • Formula exists, and phosphorus mainly exists in the form of organic phosphorus or phosphate (PO 4 3- ). These substances can provide rich nutrients for the growth of Acetobacter xylinum and its synthesis of bacterial cellulose. If the nutrients in the tailwater do not meet this requirement, appropriate nutrients can be added to it to meet the requirements.
  • step (1) the tail water from slaughtering livestock and poultry animals is first filtered to remove solid matter. Filtration is carried out using a filter screen with a mesh size of 60-100 mesh.
  • step (2) in order to meet the needs of Acetobacter xylin fermentation, components required for fermentation such as carbon source, nitrogen source and inorganic salt can be added in appropriate amounts according to the conditions of the tail water.
  • the carbon source, nitrogen source and inorganic salts can be selected from the carbon sources, nitrogen sources and inorganic salts reported in the prior art that can be used for Acetobacter xylin fermentation.
  • the carbon source can be at least one of sucrose, fructose and glucose.
  • the nitrogen source is at least one of ammonium sulfate, yeast powder, peptone and corn steep liquor, preferably ammonium sulfate
  • the inorganic salt is at least one of potassium dihydrogen phosphate, magnesium sulfate and sodium acetate, preferably phosphoric acid A mixture of potassium dihydrogen, magnesium sulfate, and sodium acetate.
  • Potassium dihydrogen phosphate can provide the phosphorus and potassium elements needed for the metabolism of Acetobacter xylin.
  • Magnesium sulfate can provide the magnesium element needed for the metabolism of Acetobacter xylin.
  • Sodium acetate can also act as a buffer to avoid degradation of the culture medium during the culture process. Large changes in pH value affect the growth of bacteria, and can also be used as a nutrient source for Acetobacter xylinum.
  • the content of the carbon source in the tail water filtrate is 0-4wt%, preferably 2.5-4wt%; the content of the nitrogen source in the tail water is 0-0.4wt%, preferably 0-0.3 wt%; the content of inorganic salt in tail water is 0.3-1.3wt%, preferably 0.3-1.1wt%.
  • the carbon source is sucrose with a content of 2.5-4wt%;
  • the nitrogen source is ammonium sulfate with a content of 0-0.3%;
  • the inorganic salt is a mixture of potassium dihydrogen phosphate, magnesium sulfate and sodium acetate.
  • the content of potassium dihydrogen phosphate in the tail water culture medium is 0-0.4wt%
  • the content of magnesium sulfate in the tail water culture medium is 0.05-0.5wt%
  • the content of sodium acetate in the tail water culture medium is 0.2- 0.5wt%.
  • acetic acid is used to adjust the pH to 4-4.5.
  • the acetic acid can be table vinegar or glacial acetic acid.
  • Acetic acid and sodium acetate can form a stable buffer to avoid excessive changes in the pH value of the culture solution during the culture process, which may affect the growth of Acetobacter xylinum and the synthesis of bacterial cellulose.
  • the slaughter tail water culture medium is first sterilized at high temperature, and then inoculated with Acetobacter xylinum.
  • the inoculum amount of Acetobacter xylinum is 3-10wt%.
  • High temperature sterilization can use commonly used sterilization conditions, such as sterilization at 100-120°C for 10-20 minutes. If the temperature is too high or the heating time is too long, the nutrients in the culture medium will be destroyed.
  • the fermentation temperature is 25-35°C. Too low a temperature is not conducive to the growth of Acetobacter xylinum, and too high a temperature will also inhibit the growth of the bacteria. Fermentation time is generally 5-9 days.
  • step (3) the bacterial cellulose gel obtained after fermentation can be washed with water and then compressed and dehydrated to obtain a bacterial cellulose gel product; the liquid obtained by washing and compressing and dehydrating is reused to prepare the slaughter tail water culture medium.
  • the bacterial cellulose gel formed is washed with water.
  • the purpose of water washing is to remove bacterial contaminants on the surface.
  • the washed bacterial cellulose gel can be used directly, or it can be compressed and dehydrated to obtain a concentrated bacterial cellulose gel product. Compression and dehydration can save a lot of storage space and transportation costs.
  • the operation method is: using a large tablet press for compression processing, the compression rate can reach 1/12.
  • the bacterial cellulose gel product obtained by compression and dehydration can adjust the pH value to Sterilize and store after 3.5-5 minutes. The lower pH value is beneficial to the long-term storage of bacterial cellulose gel.
  • the bacterial cellulose gel product finally obtained is of excellent quality and has a bacterial cellulose content of 0.7-20wt%.
  • the tail water obtained by washing the bacterial cellulose gel is filtered to filter out the solid waste.
  • the filtered washing water and the tail water obtained during the compression and dehydration process can be recycled and added to the next batch of tail water to continue. Treating according to the method of the present invention reduces the discharge of tail water.
  • the present invention uses livestock and poultry slaughter tail water as raw material and is directly used as Acetobacter xylinum culture medium to synthesize bacterial cellulose gel. Compared with the existing technology, this method has the following advantages:
  • the present invention directly utilizes livestock and poultry slaughtering tailwater to produce high value-added bacterial cellulose gel and products.
  • the obtained bacterial cellulose gel and products meet the requirements for industrial production of bacterial cellulose.
  • the present invention opens up a new situation in the biosynthesis of bacterial cellulose using animal-derived culture media, and eliminates the need for fermentation of plant-derived culture media before it can be used as a bacterial cellulose culture medium. It simplifies the industrial production process of bacterial cellulose and saves money. Reduce costs such as energy and production cycle and improve production efficiency.
  • the present invention can not only solve multiple problems such as high COD, high oil content, high treatment cost, and environmental pollution in tail water discharged as wastewater during the slaughtering and processing of livestock and poultry animals, but also can fully recycle and utilize the rich biomass resources in the tail water. It has realized the transformation of industrial waste into high value-added products, achieved the purpose of turning waste into treasure, extended the livestock and poultry slaughtering and processing industry chain, increased the added value of the slaughtering and processing industry, and is in line with the concept of industrial green development.
  • the present invention effectively increases the added value of the livestock and poultry slaughtering and processing industry, reduces or even eliminates the cost of tail water treatment for slaughtering and processing enterprises. At the same time, it breaks through the dilemma of limited sources of plant-derived culture media and opens up new opportunities for high-quality, abundant and affordable products.
  • the low-cost animal-derived culture medium greatly reduces the production cost of bacterial cellulose gel, achieving the effect of "killing two birds with one stone". It not only brings huge economic benefits to enterprises, but also has social and ecological benefits of extending the industrial chain and reducing pollution. It is very significant and will help promote the sustainable and healthy development of my country's breeding and slaughtering industry and its related processing industries.
  • slaughter tail water of the present invention only needs simple filtration to produce bacterial cellulose.
  • the process is simple, low cost, green and environmentally friendly, and can be recycled to synthesize bacterial cellulose.
  • the tail water recycling rate can reach more than 99.9wt%, which greatly reduces emissions of three wastes.
  • the present invention makes full use of the rich carbon, nitrogen, phosphorus and other nutrients in the slaughter tail water of livestock and poultry animals to synthesize bacterial cellulose, and realizes the conversion of slaughter tail water into bacterial cellulose gel products, and the obtained bacterial cellulose gel
  • the product meets the requirements for industrial production of bacterial cellulose.
  • Figure 1 is a diagram of the slaughter tail water after filtration.
  • Figure 2 is a diagram of the bacterial cellulose gel obtained in Example 1.
  • Acetobacter xylinum used is A. Microbial Products Company
  • yeast, Aspergillus and acetic acid bacteria can be purchased from commercial products.
  • the yeast used in this study was purchased from Angel Yeast Co., Ltd., and the Aspergillus and acetic acid bacteria used were purchased from Yiyuan Kangyuan Biotechnology Co., Ltd.
  • the appearance of the washed bacterial cellulose gel is shown in Figure 2. It is slightly brown and transparent and has no peculiar smell.
  • the cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/10, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 7wt%.
  • the bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
  • slaughter tail water filtrate 1-tail
  • the solid content in water is approximately 99.9wt%.
  • the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell.
  • the cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/8, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 6wt%.
  • the bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
  • slaughter tail water filtrate 1-tail
  • the solid content in water is approximately 99.9wt%.
  • the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell.
  • the cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/12, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 11wt%.
  • the bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
  • slaughter tail water filtrate 1-tail
  • the solid content in water is approximately 99.9wt%.
  • the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell.
  • the cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/10, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 7wt%.
  • the bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
  • slaughter tail water filtrate 1-tail
  • the solid content in water is approximately 99.9wt%.
  • the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell.
  • the cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/12, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 12wt%.
  • the bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
  • slaughter tail water filtrate 1-tail
  • the solid content in water is approximately 99.9wt%.
  • Example 1 of patent CN201010113232 Potassium dihydrogen phosphate 1g/L, sodium acetate 2g/L, and the rest are supplemented with tap water, pH 4.2), sterilized at 100°C for 30 minutes; add 5% of the inoculum amount to the production medium, and maintain it at 25-35°C Let it stand for 5-7 days; compress and decolorize, and the compressed liquid will be precipitated, filtered, and recovered.
  • Reconstitute the culture medium with the recovery liquid as the main culture medium 600g/L recovery liquid, 100g/L fermented coconut water, 20g/L sucrose, 3g/L diammonium phosphate, 0.5g/L magnesium sulfate, 1g/L potassium dihydrogen phosphate/ L, sodium acetate 2g/L, the rest is supplemented with tap water, pH 4.2), Sterilize at 100°C for 30 minutes; insert 5% of the inoculum into the production medium, and incubate at 25-35°C for 5-7 days; compress and decolorize, the compressed liquid is precipitated and filtered, and the culture medium can be re-configured for repeated cultivation , the weight ratio of the compressed coconut fruit to the coconut fruit before compression is 1:5; the compressed fruit slices are rehydrated and then cut and sterilized to make the finished coconut fruit. It can be seen that using coconut water as raw material requires pre-fermentation of coconut water in advance, which increases the operating process and production cycle, and the corresponding production
  • Acetobacter xylinum liquid species according to the amount of 7wt% of the production medium, and culture it at 30°C for 6 days to obtain bacterial cellulose gel. Rinse the bacterial cellulose gel with tap water to remove impurities such as bacteria attached to the surface of the gel. The resulting debris is filtered and discharged, accounting for approximately 0.1wt% of the tail water mass.
  • the washed bacterial cellulose gel is milky white and transparent, with no odor.
  • the cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/10, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 8wt%.
  • the bacterial cellulose gel product has a slightly yellow appearance and no peculiar smell.
  • tail water from coconut juice production as raw material also requires fermentation pretreatment, which increases the operating process and production cycle, and the corresponding production cost will be higher.

Abstract

Disclosed is a method for producing a bacterial cellulose gel by directly utilizing livestock and poultry slaughtering tail water. In the method, the livestock and poultry animal slaughtering tail water is precipitated, filtered, and prepared into a tail water culture medium, then acetobacter xylinum is inoculated into the prepared slaughtering tail water culture medium, and fermentation is performed to prepare the bacterial cellulose gel. The present invention solves the problems of an insufficient source of a plant-derived culture medium and high cost, omits the process that a traditional plant-derived culture medium needs to be fermented before it can be fully utilized by acetobacter xylinum to synthesize bacterial cellulose, and develops a new way for livestock and poultry slaughtering tail water treatment with difficult technology and high cost. The present invention directly utilizes rich nutrients in the livestock and poultry slaughtering tail water to synthesize the bacterial cellulose and achieves the conversion of the livestock and poultry slaughtering tail water into a bacterial cellulose gel product. The utilization rate of the tail water reaches 99.9% or more, and the obtained bacterial cellulose gel product meets the requirements of bacterial cellulose industrial production. The present invention opens a new scenario of biosynthesis of bacterial cellulose by using an animal-derived culture medium.

Description

一种直接利用畜禽屠宰尾水生产细菌纤维素凝胶的方法A method of directly utilizing livestock and poultry slaughter tail water to produce bacterial cellulose gel 技术领域Technical field
本发明涉及一种畜禽类动物屠宰尾水的资源化再利用方法,具体涉及一种直接利用畜禽类动物屠宰尾水生产细菌纤维素凝胶的方法,属于工业废弃物综合利用技术领域。The invention relates to a resource recycling method for livestock and poultry animal slaughter tail water, and specifically relates to a method of directly utilizing livestock and poultry animal slaughter tail water to produce bacterial cellulose gel, which belongs to the technical field of comprehensive utilization of industrial waste.
背景技术Background technique
联合国粮农组织报告显示,在过去的30年中,全球肉类生产量翻了1倍,预计到2050年底将再次翻倍,那么其屠宰尾水量也随之增加。2004年美国环境保护署(USEPA)将屠宰尾水作为废水排放被列为农业和食品范畴内最有害的工业废水之一,其排放会导致地面水体富营养化以及地下水的污染。中国城镇人口约9亿人,以家畜猪为例,按照每人年均至少消耗0.5头猪肉,每头猪屠宰产生尾水05-0.7吨来计算,则在中国每年猪的屠宰尾水至少产生2.25亿吨。目前,屠宰及肉类加工废水约占全国工业废水排放总量的6%、农副食品加工业废水排放总量的36.7%,是我国重要的工业废水之一。According to a report by the Food and Agriculture Organization of the United Nations, global meat production has doubled in the past 30 years and is expected to double again by the end of 2050, so the amount of slaughter tail water will also increase. In 2004, the U.S. Environmental Protection Agency (USEPA) listed slaughter tailwater as wastewater discharge as one of the most harmful industrial wastewaters in the agricultural and food categories. Its discharge can lead to eutrophication of surface water bodies and pollution of groundwater. China's urban population is about 900 million. Taking livestock pigs as an example, based on the average annual consumption of at least 0.5 pigs per person and the production of 0.5-0.7 tons of tail water per pig slaughter, the pig slaughter tail water in China will produce at least 0.5 tons of tail water every year. 225 million tons. At present, wastewater from slaughtering and meat processing accounts for about 6% of the total industrial wastewater discharge in the country and 36.7% of the total wastewater discharge from the agricultural and sideline food processing industry. It is one of the important industrial wastewaters in my country.
畜禽类动物屠宰及相关肉类加工废水是一种典型的有机废水,富含蛋白质及油脂,不含重金属等有毒物质,主要营养物质为碳(C)、氮(N)、磷(P),属于高浓度有机废水。其中,氮主要以有机氮或铵盐(NH4 +)形式存在,而磷主要以有机磷或磷酸盐(PO4 3-)形式存在。氮、磷被认为是导致水体富营养化的最主要因素之一,对水中生物有毒害作用。国家环境保护部会同国家质量监督检验总局于2017年开展了对《肉类加工工业水污染物排放标准》(GB 13457-1992)的修订工作(以下简称新标准),在新标准中明确要求直接排放废水中TN≤25mg/L、TP≤2mg/L,间接排放废水中TN≤70mg/L、TP≤8mg/L。目前,国内外常采用生物处理工艺或以生化为主的物化生化组合工艺来处理屠宰废水。因此,屠宰尾水作为工业废水排放处理技术难度大,处理成本较高,给企业带来沉重的负担,也造成生物质资源的浪费。Wastewater from livestock and poultry slaughtering and related meat processing is a typical organic wastewater. It is rich in protein and oil and does not contain toxic substances such as heavy metals. The main nutrients are carbon (C), nitrogen (N), and phosphorus (P). , which belongs to high-concentration organic wastewater. Among them, nitrogen mainly exists in the form of organic nitrogen or ammonium salt (NH 4 + ), while phosphorus mainly exists in the form of organic phosphorus or phosphate (PO 4 3- ). Nitrogen and phosphorus are considered to be one of the main factors leading to eutrophication of water bodies, which are toxic to aquatic organisms. The Ministry of Environmental Protection, together with the General Administration of Quality Supervision and Inspection, launched the revision of the "Water Pollutant Discharge Standard for the Meat Processing Industry" (GB 13457-1992) in 2017 (hereinafter referred to as the new standard). The new standard clearly requires direct TN≤25mg/L, TP≤2mg/L in discharged wastewater, TN≤70mg/L, TP≤8mg/L in indirect discharged wastewater. At present, biological treatment processes or biochemical-based physicochemical and biochemical combination processes are often used at home and abroad to treat slaughtering wastewater. Therefore, it is technically difficult to treat slaughter tailwater as industrial wastewater discharge, and the treatment cost is high, which places a heavy burden on enterprises and causes a waste of biomass resources.
细菌纤维素(bacterial cellulose,BC)是由β-1,4糖苷键连接而成的一种超纤维网状结构的天然大分子,直径仅为1.5nm,具有较高的结晶度、化学纯度、力学强度、吸附容量及良好的生物可降解性。细菌纤维素凝胶是通过生物培养法制备而成。近年来,冯玉红等生物合成出相对分子质量低的细菌纤维素和原位生物合成出甘油醛改性细菌纤维素。牛成等在木醋杆菌培养基中以椰子水为原料静置培养合成了三维结构纳米细菌纤维素凝胶。马英辉等探讨了以秸秆水解液作为唯一碳源生产细菌纤维素的工艺参数,并将细菌纤维素与漂白硫酸盐阔叶木浆复合,可增强纸张的耐磨度、断裂强度。细菌纤维素凝胶独特的织态结构、优异的性能, 传统椰子水培养基合成的细菌纤维素已在食品工业、造纸工业、膜材料、医用材料等领域得到广泛应用。截止目前,关于木醋杆菌生物合成细菌纤维素的文献研究报道多采用植物源培养基或Hestrin S.-Schramm M.标准培养基,尚未见采用动物源培养基生物合成细菌纤维素。Bacterial cellulose (BC) is a natural macromolecule with a super-fibrous network structure connected by β-1,4 glycosidic bonds. Its diameter is only 1.5nm. It has high crystallinity, chemical purity, Mechanical strength, adsorption capacity and good biodegradability. Bacterial cellulose gel is prepared by biological culture method. In recent years, Feng Yuhong and others have biosynthesized bacterial cellulose with low relative molecular weight and in situ biosynthesized glyceraldehyde-modified bacterial cellulose. Niu Cheng et al. synthesized a three-dimensional structure nanobacterial cellulose gel by static culture in Acetobacter xylinum culture medium using coconut water as raw material. Ma Yinghui et al. discussed the process parameters of producing bacterial cellulose using straw hydrolyzate as the only carbon source, and compounding bacterial cellulose with bleached sulfate hardwood pulp can enhance the abrasion resistance and breaking strength of paper. The unique texture structure and excellent performance of bacterial cellulose gel, Bacterial cellulose synthesized from traditional coconut water culture media has been widely used in the food industry, paper industry, membrane materials, medical materials and other fields. Up to now, literature research reports on the biosynthesis of bacterial cellulose by Acetobacter xylin mostly use plant-derived culture media or Hestrin S.-Schramm M. standard culture media. There has been no use of animal-derived culture media to biosynthesize bacterial cellulose.
发明内容Contents of the invention
针对因植物源培养基来源受限造成细菌纤维素生产成本高的问题,且植物源培养基中营养物质不能被木醋杆菌直接利用而是须经发酵才能作为培养基合成细菌纤维素的问题,以及畜禽类动物屠宰产生的大量尾水处理技术难成本高的问题,本发明提供了一种直接利用畜禽屠宰尾水生产细菌纤维素凝胶的方法,该方法直接利用畜禽类动物屠宰尾水中的小分子多肽、氮、磷、无机盐等营养成分生产细菌纤维素凝胶,既省去了植物源培养基中营养物质不能被木醋杆菌直接利用而须经预发酵才能作为培养基合成细菌纤维素的工序和时间,又解决了畜禽类动物屠宰尾水作为废水排放氮磷含量高、COD高、油脂含量高、处理成本高等多重难题,并充分回收利用了尾水中的生物质资源,实现了废弃物高值化转化,达到变废为宝的目的,很大程度降低或免除了屠宰尾水处理成本,且提高了畜禽屠宰加工业的附加值,延长了畜禽屠宰加工产业链,同时,畜禽类动物屠宰尾水仅需简单过滤即可直接用于生产细菌纤维素,不仅培养基资源富足价格低廉而且简化缩短了工艺流程,极大降低了细菌纤维素的生产成本,达到“一箭双雕”的效果,符合工业绿色化发展理念。In view of the problem of high production cost of bacterial cellulose due to the limited source of plant-derived culture medium, and the problem that the nutrients in the plant-derived culture medium cannot be directly utilized by Acetobacter xylinum but must be fermented to be used as a culture medium to synthesize bacterial cellulose. As well as the problem of technical difficulty and high cost in treating a large amount of tail water produced by the slaughter of livestock and poultry animals, the present invention provides a method for directly utilizing the tail water from the slaughter of livestock and poultry animals to produce bacterial cellulose gel. This method directly utilizes the tail water from the slaughter of livestock and poultry animals. Small molecule peptides, nitrogen, phosphorus, inorganic salts and other nutrients in the tail water are used to produce bacterial cellulose gel, which eliminates the need for nutrients in plant-derived culture media that cannot be directly utilized by Acetobacter xylin and must undergo pre-fermentation before they can be used as culture media. The process and time of synthesizing bacterial cellulose also solve the multiple problems of livestock and poultry slaughter tailwater being discharged as wastewater, such as high nitrogen and phosphorus content, high COD, high oil content, and high processing cost, and fully recycle and utilize the biomass in the tailwater. resources, realize the high-value transformation of waste, achieve the purpose of turning waste into treasure, greatly reduce or eliminate the cost of slaughtering tail water treatment, and increase the added value of the livestock and poultry slaughtering and processing industry, extending the time of livestock and poultry slaughtering and processing. Industrial chain, at the same time, the tail water from livestock and poultry slaughter can be directly used to produce bacterial cellulose with only simple filtration. Not only is the culture medium resource rich and cheap, it also simplifies and shortens the process, greatly reducing the production cost of bacterial cellulose. , achieving the effect of "killing two birds with one stone", in line with the concept of industrial green development.
本发明开启了采用动物源培养基生物合成细菌纤维素的新局面,而且省去了植物源培养基需发酵才能用作细菌纤维素培养基的工序,为畜禽类动物屠宰尾水开辟了资源化利用新途径,为细菌纤维素开拓了优质富足又价格低廉的培养基新资源,极大降低了细菌纤维素生产成本。具体技术方案如下:The invention opens up a new situation in the biosynthesis of bacterial cellulose using animal-derived culture media, and eliminates the need for fermentation of plant-derived culture media before it can be used as a bacterial cellulose culture medium, thus opening up resources for livestock and poultry animal slaughter tail water. A new way of chemical utilization has opened up new resources of high-quality, abundant and low-price culture media for bacterial cellulose, which has greatly reduced the production cost of bacterial cellulose. The specific technical solutions are as follows:
一种直接利用畜禽类动物屠宰尾水生产细菌纤维素凝胶的方法,该方法包括以下步骤:A method for producing bacterial cellulose gel directly by using tail water from slaughtering livestock and poultry animals, the method includes the following steps:
(1)将畜禽类动物屠宰尾水过滤,得尾水滤液;(1) Filter the tail water from slaughtering livestock and poultry animals to obtain the tail water filtrate;
(2)向尾水滤液中加入木醋杆菌发酵所需的碳源、氮源和无机盐中的至少一种,然后调整pH至4-4.5,配成屠宰尾水培养基;(2) Add at least one of the carbon source, nitrogen source and inorganic salt required for Acetobacter xylinum fermentation to the tailwater filtrate, and then adjust the pH to 4-4.5 to prepare a slaughter tailwater culture medium;
(3)向配制好的屠宰尾水培养基中接种木醋杆菌,发酵制得细菌纤维素凝胶。(3) Inoculate Acetobacter xylinum into the prepared slaughter tail water culture medium and ferment it to obtain bacterial cellulose gel.
进一步的,所述畜禽类动物屠宰尾水指的是畜禽类动物在屠宰的过程中产生的含血废水,例如家畜猪、牛、羊和家禽鸡、鸭、鹅等在屠宰过程中产生的尾水及其混合物。尾水主要包含大量血液、油脂、皮毛、骨渣、肉类残渣、内脏杂物以及若干未消化的食物。这些尾水一般具有COD高、油脂含量高和固形物高等特点,尾水中COD值一般大于104mg/L。过滤后的尾水中的主要营养物质为碳(C)、氮(N)、磷(P),氮主要以有机氮或铵盐(NH4 +)形 式存在,而磷主要以有机磷或磷酸盐(PO4 3-)形式存在。这些物质可以为木醋杆菌的生长及其合成细菌纤维素提供丰富的营养物质。如果尾水的营养物质不满足该要求,可以对其进行适当的添加营养物质,以满足要求。Furthermore, the tail water from livestock and poultry animal slaughter refers to the blood-containing wastewater produced during the slaughtering process of livestock and poultry animals, such as livestock pigs, cattle, sheep and poultry chickens, ducks, geese, etc. produced during the slaughtering process. tailwaters and their mixtures. Tail water mainly contains a large amount of blood, oil, fur, bone residue, meat residue, visceral debris and some undigested food. These tailwaters generally have the characteristics of high COD, high oil content and high solids. The COD value in the tailwater is generally greater than 10 4 mg/L. The main nutrients in the filtered tail water are carbon (C), nitrogen (N), and phosphorus (P). Nitrogen is mainly in the form of organic nitrogen or ammonium salt (NH 4 + ). Formula exists, and phosphorus mainly exists in the form of organic phosphorus or phosphate (PO 4 3- ). These substances can provide rich nutrients for the growth of Acetobacter xylinum and its synthesis of bacterial cellulose. If the nutrients in the tailwater do not meet this requirement, appropriate nutrients can be added to it to meet the requirements.
进一步的,步骤(1)中,先将畜禽类动物屠宰尾水过滤去除固形物。过滤采用滤网进行,所述滤网的目数为60-100目。Further, in step (1), the tail water from slaughtering livestock and poultry animals is first filtered to remove solid matter. Filtration is carried out using a filter screen with a mesh size of 60-100 mesh.
进一步的,步骤(2)中,为了满足木醋杆菌发酵的需要,可以根据尾水的情况适量添加碳源、氮源和无机盐等发酵所需的成分。碳源、氮源和无机盐可以选自现有技术中报道的可以用于木醋杆菌发酵的碳源、氮源和无机盐,例如碳源可以为蔗糖、果糖、葡萄糖中的至少一种,优选为蔗糖;氮源为硫酸铵、酵母粉、蛋白胨、玉米浆中的至少一种,优选为硫酸铵;无机盐为磷酸二氢钾、硫酸镁和醋酸钠中的至少一种,优选为磷酸二氢钾、硫酸镁、醋酸钠的混合物。磷酸二氢钾可以提供木醋杆菌代谢所需的磷元素和钾元素,硫酸镁可以提供木醋杆菌代谢所需的镁元素,醋酸钠既可起到缓冲液的作用避免培养过程中培养基的pH值变化较大影响菌种的生长,也可以作为木醋杆菌的营养源使用。Further, in step (2), in order to meet the needs of Acetobacter xylin fermentation, components required for fermentation such as carbon source, nitrogen source and inorganic salt can be added in appropriate amounts according to the conditions of the tail water. The carbon source, nitrogen source and inorganic salts can be selected from the carbon sources, nitrogen sources and inorganic salts reported in the prior art that can be used for Acetobacter xylin fermentation. For example, the carbon source can be at least one of sucrose, fructose and glucose. Preferably it is sucrose; the nitrogen source is at least one of ammonium sulfate, yeast powder, peptone and corn steep liquor, preferably ammonium sulfate; the inorganic salt is at least one of potassium dihydrogen phosphate, magnesium sulfate and sodium acetate, preferably phosphoric acid A mixture of potassium dihydrogen, magnesium sulfate, and sodium acetate. Potassium dihydrogen phosphate can provide the phosphorus and potassium elements needed for the metabolism of Acetobacter xylin. Magnesium sulfate can provide the magnesium element needed for the metabolism of Acetobacter xylin. Sodium acetate can also act as a buffer to avoid degradation of the culture medium during the culture process. Large changes in pH value affect the growth of bacteria, and can also be used as a nutrient source for Acetobacter xylinum.
进一步的,步骤(2)中,碳源在尾水滤液中的含量为0-4wt%,优选为2.5-4wt%;氮源在尾水中的含量为0-0.4wt%,优选为0-0.3wt%;无机盐在尾水中的含量为0.3-1.3wt%,优选为0.3-1.1wt%。Further, in step (2), the content of the carbon source in the tail water filtrate is 0-4wt%, preferably 2.5-4wt%; the content of the nitrogen source in the tail water is 0-0.4wt%, preferably 0-0.3 wt%; the content of inorganic salt in tail water is 0.3-1.3wt%, preferably 0.3-1.1wt%.
在本发明某一具体实施方式中,碳源为蔗糖,含量为2.5-4wt%;氮源为硫酸铵,含量为0-0.3%;无机盐为磷酸二氢钾、硫酸镁和醋酸钠的混合物,磷酸二氢钾在尾水培养基中的含量为0-0.4wt%,硫酸镁在尾水培养基中的含量为0.05-0.5wt%,醋酸钠在尾水培养基中的含量为0.2-0.5wt%。In a specific embodiment of the invention, the carbon source is sucrose with a content of 2.5-4wt%; the nitrogen source is ammonium sulfate with a content of 0-0.3%; the inorganic salt is a mixture of potassium dihydrogen phosphate, magnesium sulfate and sodium acetate. , the content of potassium dihydrogen phosphate in the tail water culture medium is 0-0.4wt%, the content of magnesium sulfate in the tail water culture medium is 0.05-0.5wt%, and the content of sodium acetate in the tail water culture medium is 0.2- 0.5wt%.
进一步的,步骤(2)中,用醋酸调节pH至4-4.5。醋酸为食醋或冰醋酸均可,醋酸和醋酸钠可以形成稳定的缓冲液,避免培养过程中培养液pH值变化过大,影响木醋杆菌的生长和细菌纤维素的合成。Further, in step (2), acetic acid is used to adjust the pH to 4-4.5. The acetic acid can be table vinegar or glacial acetic acid. Acetic acid and sodium acetate can form a stable buffer to avoid excessive changes in the pH value of the culture solution during the culture process, which may affect the growth of Acetobacter xylinum and the synthesis of bacterial cellulose.
进一步的,步骤(3)中,屠宰尾水培养基先高温灭菌,然后再接种木醋杆菌。木醋杆菌的接种量为3-10wt%。高温灭菌可以采用常用的灭菌条件,例如100-120℃灭菌10-20min,温度过高或加热时间过长将对培养基中的营养物质造成破坏。Further, in step (3), the slaughter tail water culture medium is first sterilized at high temperature, and then inoculated with Acetobacter xylinum. The inoculum amount of Acetobacter xylinum is 3-10wt%. High temperature sterilization can use commonly used sterilization conditions, such as sterilization at 100-120°C for 10-20 minutes. If the temperature is too high or the heating time is too long, the nutrients in the culture medium will be destroyed.
进一步的,步骤(3)中,发酵温度为25-35℃,温度过低不利于木醋杆菌的生长,温度过高也会抑制菌体的生长。发酵时间一般为5-9天。Further, in step (3), the fermentation temperature is 25-35°C. Too low a temperature is not conducive to the growth of Acetobacter xylinum, and too high a temperature will also inhibit the growth of the bacteria. Fermentation time is generally 5-9 days.
步骤(3)中,发酵后得到的细菌纤维素凝胶可以进行水洗后压缩脱水,得到细菌纤维素凝胶产品;水洗和压缩脱水所得的液体回用,用于配制屠宰尾水培养基。 In step (3), the bacterial cellulose gel obtained after fermentation can be washed with water and then compressed and dehydrated to obtain a bacterial cellulose gel product; the liquid obtained by washing and compressing and dehydrating is reused to prepare the slaughter tail water culture medium.
进一步的,木醋杆菌发酵完成后,对形成的细菌纤维素凝胶进行水洗,水洗的目的是去除表面的菌种污物。水洗后的细菌纤维素凝胶可以直接利用,也可以进行压缩脱水,得到浓缩细菌纤维素凝胶产品。压缩脱水可以节省大量的贮存空间和节省运输成本,其操作方式为:使用大型压片机进行压缩处理,压缩率可达1/12,压缩脱水得到的细菌纤维素凝胶产品可以调节pH值至3.5-5后灭菌保存,较低的pH值有利于细菌纤维素凝胶的长期保存。最终得到的细菌纤维素凝胶产品品质优良,细菌纤维素含量为0.7-20wt%。Further, after the Acetobacter xylinum fermentation is completed, the bacterial cellulose gel formed is washed with water. The purpose of water washing is to remove bacterial contaminants on the surface. The washed bacterial cellulose gel can be used directly, or it can be compressed and dehydrated to obtain a concentrated bacterial cellulose gel product. Compression and dehydration can save a lot of storage space and transportation costs. The operation method is: using a large tablet press for compression processing, the compression rate can reach 1/12. The bacterial cellulose gel product obtained by compression and dehydration can adjust the pH value to Sterilize and store after 3.5-5 minutes. The lower pH value is beneficial to the long-term storage of bacterial cellulose gel. The bacterial cellulose gel product finally obtained is of excellent quality and has a bacterial cellulose content of 0.7-20wt%.
进一步的,洗涤细菌纤维素凝胶所得的尾水进行过滤,将固形废弃物滤出,过滤后的洗涤用水以及压缩脱水过程中所得的尾水可以回收利用,加入下一批次的尾水中继续按照本发明的方法进行处理,减少了尾水的排放。Further, the tail water obtained by washing the bacterial cellulose gel is filtered to filter out the solid waste. The filtered washing water and the tail water obtained during the compression and dehydration process can be recycled and added to the next batch of tail water to continue. Treating according to the method of the present invention reduces the discharge of tail water.
本发明以畜禽类屠宰尾水为原料,直接用作木醋杆菌培养基合成细菌纤维素凝胶,该方法与现有技术相比具有以下优势:The present invention uses livestock and poultry slaughter tail water as raw material and is directly used as Acetobacter xylinum culture medium to synthesize bacterial cellulose gel. Compared with the existing technology, this method has the following advantages:
1.本发明直接利用畜禽类屠宰尾水生产高附加值的细菌纤维素凝胶及产品,所得细菌纤维素凝胶及产品符合细菌纤维素工业生产的要求。本发明开启了采用动物源培养基生物合成细菌纤维素的新局面,且省去了植物源培养基需发酵才能用作细菌纤维素培养基的工序,简化了细菌纤维素工业化生产工艺流程,节省了能源和生产周期等成本开支,提高了生产效率。1. The present invention directly utilizes livestock and poultry slaughtering tailwater to produce high value-added bacterial cellulose gel and products. The obtained bacterial cellulose gel and products meet the requirements for industrial production of bacterial cellulose. The present invention opens up a new situation in the biosynthesis of bacterial cellulose using animal-derived culture media, and eliminates the need for fermentation of plant-derived culture media before it can be used as a bacterial cellulose culture medium. It simplifies the industrial production process of bacterial cellulose and saves money. Reduce costs such as energy and production cycle and improve production efficiency.
2.本发明既可解决畜禽类动物屠宰加工过程中尾水作为废水排放COD高、油脂含量高、处理成本高、污染环境等多重问题,又可以充分回收利用尾水中富含的生物质资源,实现了工业废弃物到高附加值产品的转化,达到变废为宝的目的,延长了畜禽屠宰加工产业链,提高了屠宰加工业的附加值,符合工业绿色化发展理念。2. The present invention can not only solve multiple problems such as high COD, high oil content, high treatment cost, and environmental pollution in tail water discharged as wastewater during the slaughtering and processing of livestock and poultry animals, but also can fully recycle and utilize the rich biomass resources in the tail water. It has realized the transformation of industrial waste into high value-added products, achieved the purpose of turning waste into treasure, extended the livestock and poultry slaughtering and processing industry chain, increased the added value of the slaughtering and processing industry, and is in line with the concept of industrial green development.
3.本发明有效地提高了畜禽屠宰加工业的附加值,降低甚至免除了屠宰加工企业尾水处理费用,同时,突破了因植物源培养基来源受限的困境,开拓了优质富足且价格低廉的动物源培养基,极大降低了细菌纤维素凝胶的生产成本,达到“一箭双雕”的效果,给企业带来巨大的经济效益的同时,延长产业链、减少污染的社会和生态效益也非常显著,有利于促进我国养殖屠宰业及其相关加工产业的持续健康发展。3. The present invention effectively increases the added value of the livestock and poultry slaughtering and processing industry, reduces or even eliminates the cost of tail water treatment for slaughtering and processing enterprises. At the same time, it breaks through the dilemma of limited sources of plant-derived culture media and opens up new opportunities for high-quality, abundant and affordable products. The low-cost animal-derived culture medium greatly reduces the production cost of bacterial cellulose gel, achieving the effect of "killing two birds with one stone". It not only brings huge economic benefits to enterprises, but also has social and ecological benefits of extending the industrial chain and reducing pollution. It is very significant and will help promote the sustainable and healthy development of my country's breeding and slaughtering industry and its related processing industries.
4、本发明屠宰尾水仅需要简单过滤即可用于生产细菌纤维素,工艺简单、成本低、绿色环保,可以循环用于合成细菌纤维素,尾水循环利用率可以达到99.9wt%以上,大大减少了三废的排放。4. The slaughter tail water of the present invention only needs simple filtration to produce bacterial cellulose. The process is simple, low cost, green and environmentally friendly, and can be recycled to synthesize bacterial cellulose. The tail water recycling rate can reach more than 99.9wt%, which greatly reduces emissions of three wastes.
5、本发明充分利用了畜禽类动物屠宰尾水中丰富的碳、氮、磷等营养物质合成细菌纤维素,实现了屠宰尾水到细菌纤维素凝胶产品的转化,所得细菌纤维素凝胶产品符合细菌纤维素工业生产的要求。 5. The present invention makes full use of the rich carbon, nitrogen, phosphorus and other nutrients in the slaughter tail water of livestock and poultry animals to synthesize bacterial cellulose, and realizes the conversion of slaughter tail water into bacterial cellulose gel products, and the obtained bacterial cellulose gel The product meets the requirements for industrial production of bacterial cellulose.
附图说明Description of drawings
图1为过滤后屠宰尾水图。Figure 1 is a diagram of the slaughter tail water after filtration.
图2为实施例1得到的细菌纤维素凝胶图。Figure 2 is a diagram of the bacterial cellulose gel obtained in Example 1.
具体实施方式Detailed ways
下面通过具体实施例对本发明进行进一步解释和说明,下述说明仅是示例性的,并不对其内容进行限制。下述实施例中,如无特别说明,所述浓度均为质量浓度。The present invention will be further explained and described below through specific embodiments. The following description is only exemplary and does not limit its content. In the following examples, unless otherwise stated, the concentrations mentioned are mass concentrations.
下述实施例中,所用木醋杆菌为A.xylinum HN001(海南大学本团队保藏),或者为Gluconacetobacter xylinus(Brown)Yamada et al.(采购自河南省工业微生物菌种工程技术研究中心或市售微生物制品公司);酵母、曲霉菌和醋酸菌,购自市售产品均可,本研究所用酵母购自安琪酵母股份有限公司,所用曲霉菌和醋酸菌购自沂源康源生物科技有限公司。In the following examples, the Acetobacter xylinum used is A. Microbial Products Company); yeast, Aspergillus and acetic acid bacteria can be purchased from commercial products. The yeast used in this study was purchased from Angel Yeast Co., Ltd., and the Aspergillus and acetic acid bacteria used were purchased from Yiyuan Kangyuan Biotechnology Co., Ltd.
实施例1Example 1
1.取屠宰猪尾水,沉淀1-3h,过100目的滤网,除去大颗粒固形物,得屠宰尾水滤液,如图1所示。1. Take the slaughtered pig tail water, let it settle for 1-3 hours, pass it through a 100-mesh filter, remove large solid particles, and get the slaughtered tail water filtrate, as shown in Figure 1.
2.取上述尾水滤液,以尾水滤液计加入3wt%的蔗糖、0.1wt%的硫酸铵、0.2wt%的磷酸二氢钾、0.3wt%的醋酸钠、0.05wt%的硫酸镁,醋酸调pH值为4.5,得到生产培养基。将生产培养基装盘、封口,120℃保持10min灭菌,备用。2. Take the above tail water filtrate, add 3wt% sucrose, 0.1wt% ammonium sulfate, 0.2wt% potassium dihydrogen phosphate, 0.3wt% sodium acetate, 0.05wt% magnesium sulfate, acetic acid based on the tailwater filtrate. Adjust the pH value to 4.5 to obtain the production medium. Put the production culture medium into a plate, seal it, and keep it at 120°C for 10 minutes for sterilization and set aside.
3.按照生产培养基7wt%的量接种木醋杆菌液体种,30℃条件下培养6d,得到细菌纤维素凝胶,将细菌纤维素凝胶用自来水漂洗除去凝胶表面的附着菌种等杂物,所得杂物过滤后排放,约占尾水质量的0.1wt%。3. Inoculate Acetobacter xylinum liquid species according to the amount of 7wt% of the production medium, and culture it at 30°C for 6 days to obtain bacterial cellulose gel. Rinse the bacterial cellulose gel with tap water to remove impurities such as bacteria attached to the surface of the gel. The resulting debris is filtered and discharged, accounting for approximately 0.1wt% of the tail water mass.
4.清洗后的细菌纤维素凝胶外观如图2所示,呈微棕色透明状,无异味。将清洗后的细菌纤维素进行压缩得压缩率为1/10的细菌纤维素凝胶,调节pH值为4,灭菌保存,得细菌纤维素含量约为7wt%的细菌纤维素凝胶产品,该细菌纤维素凝胶产品外观呈微棕色,无异味。4. The appearance of the washed bacterial cellulose gel is shown in Figure 2. It is slightly brown and transparent and has no peculiar smell. The cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/10, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 7wt%. The bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
5.压缩出的溶液以及过滤后的洗涤用水添加到下一批次的屠宰尾水中,进行循环再利用,培养细菌纤维素凝胶,屠宰尾水滤液利用率(尾水利用率=1-尾水中固形物的含量)约为99.9wt%。5. The compressed solution and the filtered washing water are added to the next batch of slaughter tail water for recycling and reuse, and the bacterial cellulose gel is cultured. The utilization rate of the slaughter tail water filtrate (tail water utilization rate = 1-tail The solid content in water) is approximately 99.9wt%.
实施例2Example 2
1.取屠宰牛尾水,沉淀1-3h,过80目的滤网,除去大颗粒固形物,得屠宰尾水滤液。1. Take the slaughtered ox tail water, let it settle for 1-3 hours, pass it through an 80-mesh filter to remove large solid particles, and get the slaughtered tail water filtrate.
2.取上述尾水滤液,以尾水滤液计加入3.5wt%的蔗糖、0.2wt%的硫酸铵、0.4wt%的磷酸二氢钾、0.4wt%的醋酸钠、0.05wt%的硫酸镁,醋酸调pH值为4.4,得到生产培养基。将 生产培养基装盘、封口,115℃保持10min灭菌,备用。2. Take the above tail water filtrate and add 3.5wt% sucrose, 0.2wt% ammonium sulfate, 0.4wt% potassium dihydrogen phosphate, 0.4wt% sodium acetate, and 0.05wt% magnesium sulfate based on the tailwater filtrate. Adjust the pH value to 4.4 with acetic acid to obtain the production medium. Will The production culture medium is loaded into plates, sealed, and sterilized at 115°C for 10 minutes before use.
3.按照生产培养基6wt%的量接种木醋杆菌液体种,32℃条件下培养7d,得到细菌纤维素凝胶,将细菌纤维素凝胶用自来水漂洗除去凝胶表面的附着菌种等杂物,所得杂物过滤后排放,约占尾水质量的0.1wt%。3. Inoculate Acetobacter xylinum liquid species at an amount of 6wt% of the production culture medium, and culture it at 32°C for 7 days to obtain bacterial cellulose gel. Rinse the bacterial cellulose gel with tap water to remove impurities such as bacteria attached to the surface of the gel. The resulting debris is filtered and discharged, accounting for approximately 0.1wt% of the tail water mass.
4.清洗后的细菌纤维素凝胶呈微棕色透明状,无异味。将清洗后的细菌纤维素进行压缩得压缩率为1/8的细菌纤维素凝胶,调节pH值为4,灭菌保存,得细菌纤维素含量约为6wt%的细菌纤维素凝胶产品,该细菌纤维素凝胶产品外观呈微棕色,无异味。4. After cleaning, the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell. The cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/8, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 6wt%. The bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
5.压缩出的溶液以及过滤后的洗涤用水添加到下一批次的屠宰尾水中,进行循环再利用,培养细菌纤维素凝胶,屠宰尾水滤液利用率(尾水利用率=1-尾水中固形物的含量)约为99.9wt%。5. The compressed solution and the filtered washing water are added to the next batch of slaughter tail water for recycling and reuse, and the bacterial cellulose gel is cultured. The utilization rate of the slaughter tail water filtrate (tail water utilization rate = 1-tail The solid content in water) is approximately 99.9wt%.
实施例3Example 3
1.取屠宰羊尾水,沉淀1-3h,过60目的滤网,除去大颗粒固形物,得屠宰尾水滤液。1. Take the slaughtered sheep tail water, let it settle for 1-3 hours, pass it through a 60-mesh filter, remove large solid particles, and get the slaughtered tail water filtrate.
2.取上述尾水滤液,以尾水滤液计加入4wt%的蔗糖、0.3wt%的硫酸铵、0.5wt%的磷酸二氢钾、0.5wt%的醋酸钠、0.05wt%的硫酸镁,醋酸调pH值为4.3,得到生产培养基。将生产培养基装盘、封口,115℃保持10min灭菌,备用。2. Take the above tail water filtrate, add 4wt% sucrose, 0.3wt% ammonium sulfate, 0.5wt% potassium dihydrogen phosphate, 0.5wt% sodium acetate, 0.05wt% magnesium sulfate, acetic acid based on the tailwater filtrate. Adjust the pH value to 4.3 to obtain the production medium. Put the production culture medium into a plate, seal it, and keep it at 115°C for 10 minutes for sterilization and set aside.
3.按照生产培养基5wt%的量接种木醋杆菌液体种,32℃条件下培养8d,得到细菌纤维素凝胶,将细菌纤维素凝胶用自来水漂洗除去凝胶表面的附着菌种等杂物,所得杂物过滤后排放,约占尾水质量的0.1wt%。3. Inoculate Acetobacter xylinum liquid species at an amount of 5wt% of the production culture medium, and culture it at 32°C for 8 days to obtain a bacterial cellulose gel. Rinse the bacterial cellulose gel with tap water to remove impurities such as bacteria attached to the surface of the gel. The resulting debris is filtered and discharged, accounting for approximately 0.1wt% of the tail water mass.
4.清洗后的细菌纤维素凝胶呈微棕色透明状,无异味。将清洗后的细菌纤维素进行压缩得压缩率为1/12的细菌纤维素凝胶,调节pH值为4,灭菌保存,得细菌纤维素含量约为11wt%的细菌纤维素凝胶产品,该细菌纤维素凝胶产品外观呈微棕色,无异味。4. After cleaning, the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell. The cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/12, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 11wt%. The bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
5.压缩出的溶液以及过滤后的洗涤用水添加到下一批次的屠宰尾水中,进行循环再利用,培养细菌纤维素凝胶,屠宰尾水滤液利用率(尾水利用率=1-尾水中固形物的含量)约为99.9wt%。5. The compressed solution and the filtered washing water are added to the next batch of slaughter tail water for recycling and reuse, and the bacterial cellulose gel is cultured. The utilization rate of the slaughter tail water filtrate (tail water utilization rate = 1-tail The solid content in water) is approximately 99.9wt%.
实施例4Example 4
1.取屠宰鸡尾水,沉淀1-3h,过80目的滤网,除去大颗粒固形物,得屠宰尾水滤液。1. Take the slaughtered chicken tail water, let it settle for 1-3 hours, and pass it through an 80-mesh filter to remove large solid particles to obtain the slaughtered chicken tail water filtrate.
2.取上述尾水滤液,以尾水滤液计加入3.5wt%的蔗糖、0.05wt%的硫酸铵、0.1wt%的磷酸二氢钾、0.3wt%的醋酸钠、0.05wt%的硫酸镁、醋酸调pH值为4.2,得到生产培养基。将生产培养基装盘、封口,105℃保持10min灭菌,备用。2. Take the above tail water filtrate and add 3.5wt% sucrose, 0.05wt% ammonium sulfate, 0.1wt% potassium dihydrogen phosphate, 0.3wt% sodium acetate, 0.05wt% magnesium sulfate based on the tailwater filtrate. Adjust the pH value to 4.2 with acetic acid to obtain the production medium. Put the production culture medium into a plate, seal it, and keep it at 105°C for 10 minutes for sterilization and set aside.
3.按照生产培养基8wt%的量接种木醋杆菌液体种,33℃条件下培养6d,得到细菌纤维 素凝胶,将细菌纤维素凝胶用自来水漂洗除去凝胶表面的附着菌种等杂物,所得杂物过滤后排放,约占尾水质量的0.1wt%。3. Inoculate Acetobacter xylinum liquid species according to 8wt% of the production medium, and culture it at 33°C for 6 days to obtain bacterial fiber. To make bacterial cellulose gel, rinse the bacterial cellulose gel with tap water to remove impurities such as bacteria attached to the gel surface. The obtained impurities are filtered and discharged, accounting for approximately 0.1wt% of the tail water mass.
4.清洗后的细菌纤维素凝胶呈微棕色透明状,无异味。将清洗后的细菌纤维素进行压缩得压缩率为1/10的细菌纤维素凝胶,调节pH值为4,灭菌保存,得细菌纤维素含量约为7wt%的细菌纤维素凝胶产品,该细菌纤维素凝胶产品外观呈微棕色,无异味。4. After cleaning, the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell. The cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/10, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 7wt%. The bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
5.压缩出的溶液以及过滤后的洗涤用水添加到下一批次的屠宰尾水中,进行循环再利用,培养细菌纤维素凝胶,屠宰尾水滤液利用率(尾水利用率=1-尾水中固形物的含量)约为99.9wt%。5. The compressed solution and the filtered washing water are added to the next batch of slaughter tail water for recycling and reuse, and the bacterial cellulose gel is cultured. The utilization rate of the slaughter tail water filtrate (tail water utilization rate = 1-tail The solid content in water) is approximately 99.9wt%.
实施例5Example 5
1.取屠宰猪尾水和鸭尾水混合,沉淀1-3h,过100目的滤网,除去大颗粒固形物,得屠宰尾水滤液。1. Mix the slaughtered pig tail water and duck tail water, let settle for 1-3 hours, pass through a 100-mesh filter to remove large solid particles, and obtain the slaughtered tail water filtrate.
2.取上述尾水滤液,以尾水滤液计加入2.5wt%的蔗糖、0.2wt%的醋酸钠、0.05wt%的硫酸镁,醋酸调pH值为4.0,得到生产培养基。将生产培养基装盘、封口,105℃保持15min灭菌,备用。2. Take the above tail water filtrate, add 2.5wt% sucrose, 0.2wt% sodium acetate, 0.05wt% magnesium sulfate based on the tailwater filtrate, and adjust the pH value to 4.0 with acetic acid to obtain a production medium. Put the production culture medium into a plate, seal it, and keep it at 105°C for 15 minutes for sterilization and set aside.
3.按照生产培养基10wt%的量接种木醋杆菌液体种,35℃条件下培养5d,得到细菌纤维素凝胶,将细菌纤维素凝胶用自来水漂洗除去凝胶表面的附着菌种等杂物,所得杂物过滤后排放,约占尾水质量的0.1wt%。3. Inoculate Acetobacter xylinum liquid species according to 10wt% of the production medium, and culture it at 35°C for 5 days to obtain bacterial cellulose gel. Rinse the bacterial cellulose gel with tap water to remove impurities such as bacteria attached to the surface of the gel. The resulting debris is filtered and discharged, accounting for approximately 0.1wt% of the tail water mass.
4.清洗后的细菌纤维素凝胶呈微棕色透明状,无异味。将清洗后的细菌纤维素进行压缩得压缩率为1/12的细菌纤维素凝胶,调节pH值为4,灭菌保存,得细菌纤维素含量约为12wt%的细菌纤维素凝胶产品,该细菌纤维素凝胶产品外观呈微棕色,无异味。4. After cleaning, the bacterial cellulose gel is slightly brown and transparent, with no peculiar smell. The cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/12, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 12wt%. The bacterial cellulose gel product has a slightly brown appearance and no peculiar smell.
5.压缩出的溶液以及过滤后的洗涤用水添加到下一批次的屠宰尾水中,进行循环再利用,培养细菌纤维素凝胶,屠宰尾水滤液利用率(尾水利用率=1-尾水中固形物的含量)约为99.9wt%。5. The compressed solution and the filtered washing water are added to the next batch of slaughter tail water for recycling and reuse, and the bacterial cellulose gel is cultured. The utilization rate of the slaughter tail water filtrate (tail water utilization rate = 1-tail The solid content in water) is approximately 99.9wt%.
对比例1Comparative example 1
参照专利CN201010113232.X实施例1的步骤,以发酵椰子水为主要培养基质配制初始培养基(发酵椰子水500g/L,蔗糖20g/L,磷二铵3g/L,硫酸镁0.5g/L,磷酸二氢钾1g/L,醋酸钠2g/L,其余以自来水补充,pH 4.2),100℃灭菌30min;按培养基5%的接种量接入生产培养基,在25-35℃的条件下静置培养5-7d;压缩脱色,压缩液经沉淀、过滤、回收。以回收液为主要培养基质重新配置培养基(回收液600g/L,发酵椰子水100g/L,蔗糖20g/L,磷二铵3g/L,硫酸镁0.5g/L,磷酸二氢钾1g/L,醋酸钠2g/L,其余以自来水补充,pH 4.2), 100℃灭菌30min;按5%的接种量接入生产培养基,在25-35℃的条件下静置培养5-7d;压缩脱色,压缩液经沉淀、过滤,重新配置培养基可重复培养,压缩后的椰果与压缩前的椰果的重量比为1:5;压缩果片复水后经切割、杀菌处理制成成品椰果。由此可见,以椰子水为原料需要对椰子水进行提前预发酵,增加了操作流程,生产周期也增加,相应的生产成本就会高一些。Referring to the steps of Example 1 of patent CN201010113232. Potassium dihydrogen phosphate 1g/L, sodium acetate 2g/L, and the rest are supplemented with tap water, pH 4.2), sterilized at 100°C for 30 minutes; add 5% of the inoculum amount to the production medium, and maintain it at 25-35°C Let it stand for 5-7 days; compress and decolorize, and the compressed liquid will be precipitated, filtered, and recovered. Reconstitute the culture medium with the recovery liquid as the main culture medium (600g/L recovery liquid, 100g/L fermented coconut water, 20g/L sucrose, 3g/L diammonium phosphate, 0.5g/L magnesium sulfate, 1g/L potassium dihydrogen phosphate/ L, sodium acetate 2g/L, the rest is supplemented with tap water, pH 4.2), Sterilize at 100°C for 30 minutes; insert 5% of the inoculum into the production medium, and incubate at 25-35°C for 5-7 days; compress and decolorize, the compressed liquid is precipitated and filtered, and the culture medium can be re-configured for repeated cultivation , the weight ratio of the compressed coconut fruit to the coconut fruit before compression is 1:5; the compressed fruit slices are rehydrated and then cut and sterilized to make the finished coconut fruit. It can be seen that using coconut water as raw material requires pre-fermentation of coconut water in advance, which increases the operating process and production cycle, and the corresponding production cost will be higher.
对比例2Comparative example 2
参照专利202210484679.0实施例1的步骤,如下:Refer to the steps of Example 1 of patent 202210484679.0 as follows:
1.取椰子汁生产尾水,过60目的滤网,除去大颗粒固形物,得COD值约为1.2×104mg/L的乳白色尾水。1. Take coconut juice production tail water, pass it through a 60-mesh filter, remove large solid particles, and obtain milky white tail water with a COD value of approximately 1.2×10 4 mg/L.
2.在除杂后的生产尾水中加入尾水质量1wt%的淀粉,搅拌均匀,煮沸10min,冷却至室温,接种尾水质量3×10-5的复合微生物,32℃敞口发酵,至尾水无气泡产生且表面无明显的油脂层后停止发酵,过100目滤网,除去发酵的漂浮物和沉淀物,得到椰子汁生产尾水发酵液,有机酸总酸度约为0.6wt%,过滤得到的固形废弃物约占尾水质量的0.3%,整个过程无恶臭气味产生。2. Add 1wt% starch of the tail water mass to the production tail water after impurity removal, stir evenly, boil for 10 minutes, cool to room temperature, inoculate compound microorganisms with a tail water mass of 3×10 -5 , and conduct open fermentation at 32°C until the end Stop the fermentation after the water has no bubbles and no obvious oil layer on the surface. Pass it through a 100-mesh filter to remove fermented floating matter and sediment to obtain the tail water fermentation liquid of coconut juice production. The total acidity of organic acids is about 0.6wt%. Filter The solid waste obtained accounts for about 0.3% of the tail water mass, and no foul smell is produced in the whole process.
3.取上述尾水发酵液,以尾水发酵液计加入2wt%的蔗糖、0.5wt%的硫酸铵、0.3wt%的磷酸二氢钾、0.3wt%的醋酸钠、0.05wt%的硫酸镁、调pH值为4.5,得到生产培养基。将生产培养基装盘、封口,120℃保持10min灭菌,备用。3. Take the above tail water fermentation liquid and add 2wt% sucrose, 0.5wt% ammonium sulfate, 0.3wt% potassium dihydrogen phosphate, 0.3wt% sodium acetate, and 0.05wt% magnesium sulfate based on the tail water fermentation liquid. , adjust the pH value to 4.5 to obtain the production medium. Put the production culture medium into a plate, seal it, and keep it at 120°C for 10 minutes for sterilization and set aside.
4.按照生产培养基7wt%的量接种木醋杆菌液体种,30℃条件下培养6d,得到细菌纤维素凝胶,将细菌纤维素凝胶用自来水漂洗除去凝胶表面的附着菌种等杂物,所得杂物过滤后排放,约占尾水质量的0.1wt%。4. Inoculate Acetobacter xylinum liquid species according to the amount of 7wt% of the production medium, and culture it at 30°C for 6 days to obtain bacterial cellulose gel. Rinse the bacterial cellulose gel with tap water to remove impurities such as bacteria attached to the surface of the gel. The resulting debris is filtered and discharged, accounting for approximately 0.1wt% of the tail water mass.
5.取清洗后的细菌纤维素凝胶呈乳白色透明状,无异味。将清洗后的细菌纤维素进行压缩得压缩率为1/10的细菌纤维素凝胶,调节pH值为4,灭菌保存,得细菌纤维素含量约为8wt%的细菌纤维素凝胶产品,该细菌纤维素凝胶产品外观呈微黄色,无异味。5. The washed bacterial cellulose gel is milky white and transparent, with no odor. The cleaned bacterial cellulose is compressed to obtain a bacterial cellulose gel with a compression rate of 1/10, the pH value is adjusted to 4, and sterilized and stored to obtain a bacterial cellulose gel product with a bacterial cellulose content of approximately 8wt%. The bacterial cellulose gel product has a slightly yellow appearance and no peculiar smell.
6.压缩出的溶液以及过滤后的洗涤用水添加到下一批次的椰子汁生产尾水中,且保持COD值不低于5×103mg/L,进行循环再利用培养细菌纤维素凝胶,椰子汁加工尾水利用率(尾水利用率=1-尾水中固形物的含量)约为99.6wt%。6. Add the compressed solution and filtered washing water to the next batch of coconut juice production tail water, and keep the COD value not less than 5×10 3 mg/L for recycling and culturing bacterial cellulose gel. , the tail water utilization rate of coconut juice processing (tail water utilization rate = 1-the solid content in the tail water) is about 99.6wt%.
由此可见,以椰子汁生产尾水为原料也需要进行发酵预处理,增加了操作流程,生产周期也增加,相应的生产成本就会高一些。 It can be seen that using tail water from coconut juice production as raw material also requires fermentation pretreatment, which increases the operating process and production cycle, and the corresponding production cost will be higher.

Claims (10)

  1. 一种直接利用畜禽类动物屠宰尾水生产细菌纤维素凝胶的方法,其特征是:A method for producing bacterial cellulose gel directly using the tail water from slaughtering livestock and poultry animals, which is characterized by:
    (1)将畜禽类动物屠宰尾水过滤,得尾水滤液;(1) Filter the tail water from slaughtering livestock and poultry animals to obtain the tail water filtrate;
    (2)向尾水滤液中加入木醋杆菌发酵所需的碳源、氮源和无机盐中的至少一种,然后调整pH至4-4.5,配成屠宰尾水培养基;(2) Add at least one of the carbon source, nitrogen source and inorganic salt required for Acetobacter xylinum fermentation to the tailwater filtrate, and then adjust the pH to 4-4.5 to prepare a slaughter tailwater culture medium;
    (3)向配制好的屠宰尾水培养基中接种木醋杆菌,发酵制得细菌纤维素凝胶。(3) Inoculate Acetobacter xylinum into the prepared slaughter tail water culture medium and ferment it to obtain bacterial cellulose gel.
  2. 根据权利要求1所述的方法,其特征是:所述畜禽类动物屠宰尾水指的是畜禽类动物在屠宰的过程中产生的含血废水;所述畜禽类动物主要选自猪、牛、羊、鸡、鸭或鹅。The method according to claim 1, characterized in that: the livestock and poultry animal slaughter tail water refers to the blood-containing wastewater produced during the slaughter of livestock and poultry animals; the livestock and poultry animals are mainly selected from pigs , cow, sheep, chicken, duck or goose.
  3. 根据权利要求1所述的方法,其特征是:步骤(1)中,过滤采用滤网进行,所述滤网的目数为60-100目。The method according to claim 1, characterized in that: in step (1), filtering is performed using a filter screen, and the mesh number of the filter screen is 60-100 mesh.
  4. 根据权利要求1所述的方法,其特征是:步骤(2)中,所述碳源为蔗糖、果糖、葡萄糖中的至少一种;所述氮源为硫酸铵、酵母粉、蛋白胨、玉米浆中的至少一种;所述无机盐为磷酸二氢钾、硫酸镁、醋酸钠中的至少一种。The method according to claim 1, characterized in that: in step (2), the carbon source is at least one of sucrose, fructose, and glucose; the nitrogen source is ammonium sulfate, yeast powder, peptone, and corn steep liquor. At least one of them; the inorganic salt is at least one of potassium dihydrogen phosphate, magnesium sulfate, and sodium acetate.
  5. 根据权利要求1或4所述的方法,其特征是:步骤(2)中,碳源在尾水滤液中的含量为0-4wt%;氮源在尾水滤液中的含量为0-0.4wt%;无机盐在尾水中的含量为0.3-1.3wt%。The method according to claim 1 or 4, characterized in that: in step (2), the content of the carbon source in the tail water filtrate is 0-4wt%; the content of the nitrogen source in the tail water filtrate is 0-0.4wt %; the content of inorganic salts in tail water is 0.3-1.3wt%.
  6. 根据权利要求1所述的方法,其特征是:步骤(2)中,所述碳源为蔗糖,所述氮源为硫酸铵,所述无机盐为磷酸二氢钾、硫酸镁、醋酸钠的混合物;步骤(2)中,碳源在尾水滤液中的含量为2.5-4wt%,氮源在尾水滤液中的含量为0-0.3wt%,无机盐在尾水中的含量为0.3-1.1wt%。The method according to claim 1, characterized in that: in step (2), the carbon source is sucrose, the nitrogen source is ammonium sulfate, and the inorganic salt is potassium dihydrogen phosphate, magnesium sulfate, or sodium acetate. Mixture; in step (2), the content of the carbon source in the tail water filtrate is 2.5-4wt%, the content of the nitrogen source in the tail water filtrate is 0-0.3wt%, and the content of inorganic salts in the tail water is 0.3-1.1 wt%.
  7. 根据权利要求1所述的方法,其特征是:步骤(2)中,用醋酸调节pH至4-4.5。The method according to claim 1, characterized in that: in step (2), acetic acid is used to adjust the pH to 4-4.5.
  8. 根据权利要求1所述的方法,其特征是:步骤(3)中,屠宰尾水培养基先高温灭菌,然后再接种木醋杆菌。The method according to claim 1, characterized in that: in step (3), the slaughter tail water culture medium is first sterilized at high temperature, and then inoculated with Acetobacter xylinum.
  9. 根据权利要求1所述的方法,其特征是:步骤(3)中,木醋杆菌的接种量为3-10wt%。The method according to claim 1, characterized in that in step (3), the inoculum amount of Acetobacter xylinum is 3-10wt%.
  10. 根据权利要求1所述的方法,其特征是:步骤(3)中,发酵温度为25-35℃,发酵时间为5-9天;步骤(3)中,发酵后得到的细菌纤维素凝胶进行水洗后压缩脱水,得到细菌纤维素凝胶产品,水洗和压缩脱水所得的液体回用,用于配制屠宰尾水培养基。 The method according to claim 1, characterized in that: in step (3), the fermentation temperature is 25-35°C, and the fermentation time is 5-9 days; in step (3), the bacterial cellulose gel obtained after fermentation Wash with water and then compress and dehydrate to obtain a bacterial cellulose gel product. The liquid obtained by washing and compressing and dehydrating is reused to prepare the slaughter tail water culture medium.
PCT/CN2023/087720 2022-08-15 2023-04-12 Method for producing bacterial cellulose gel by directly utilizing livestock and poultry slaughtering tail water WO2024036996A1 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0416470A2 (en) * 1989-09-04 1991-03-13 Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. Process for making cellulose membranes from bacteria produced cellulose
WO2004108609A1 (en) * 2003-06-06 2004-12-16 Forskningscenter Risø Fermentation media comprising wastewater and use hereof
CN104531802A (en) * 2014-12-11 2015-04-22 无锡市善源生物科技有限公司 Method for preparing edible bacterial cellulose by using rice immersing water and product of method
CN105776574A (en) * 2016-05-20 2016-07-20 佛山市聚成生化技术研发有限公司 Microbial flocculant and application thereof in slaughter wastewater treatment

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0416470A2 (en) * 1989-09-04 1991-03-13 Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. Process for making cellulose membranes from bacteria produced cellulose
WO2004108609A1 (en) * 2003-06-06 2004-12-16 Forskningscenter Risø Fermentation media comprising wastewater and use hereof
CN104531802A (en) * 2014-12-11 2015-04-22 无锡市善源生物科技有限公司 Method for preparing edible bacterial cellulose by using rice immersing water and product of method
CN105776574A (en) * 2016-05-20 2016-07-20 佛山市聚成生化技术研发有限公司 Microbial flocculant and application thereof in slaughter wastewater treatment

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