CN104388317A - A kind of organic chlorella production method rich in trace elements - Google Patents

A kind of organic chlorella production method rich in trace elements Download PDF

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CN104388317A
CN104388317A CN201410721855.3A CN201410721855A CN104388317A CN 104388317 A CN104388317 A CN 104388317A CN 201410721855 A CN201410721855 A CN 201410721855A CN 104388317 A CN104388317 A CN 104388317A
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俞建中
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Abstract

本发明公开了一种富含微量元素的有机小球藻生产方法,其包括微生物厌氧发酵培养基配制,液体有机肥厌氧发酵和有机小球藻生产等工艺步骤;本发明适用于中试级别以上的实验性生产和规模化小球藻生产;本发明通过厌氧发酵的方法,实现了小球藻的液体有机肥的生产,在小球藻养殖培养基配置的环节即实现了微量元素的富集和有机化,利用此富含有机化微量元素的液体肥料养殖小球藻,即可获得富集了各个微量元素的有机小球藻产品,该小球藻产品中的各微量元素已经有机化,更易被人体吸收;本发明利用生物质废弃物为源头物料,实现了废弃物资源化和高值化,小球藻生产过程的有机化,带来环境和经济双重效应。The invention discloses a method for producing organic chlorella rich in trace elements, which comprises the steps of preparing a microbial anaerobic fermentation medium, anaerobic fermentation of liquid organic fertilizer and producing organic chlorella. The invention is suitable for experimental production above the pilot level and large-scale chlorella production. The invention realizes the production of liquid organic fertilizer of chlorella through the anaerobic fermentation method, and the enrichment and organicization of trace elements are realized in the link of configuring the chlorella cultivation medium. The liquid fertilizer rich in organic trace elements is used to cultivate chlorella, so that an organic chlorella product enriched with various trace elements can be obtained. The various trace elements in the chlorella product have been organicized and are more easily absorbed by the human body. The invention uses biomass waste as source material, realizes the resource utilization and high value of waste, and the organicization of the chlorella production process brings both environmental and economic effects.

Description

一种富含微量元素的有机小球藻生产方法A kind of organic chlorella production method rich in trace elements

技术领域 technical field

本发明涉及一种富含微量元素的有机小球藻的生产方法。具体而言,是利用富含微量元素的液体有机肥料培养富含铁、锌、碘、铬、硒等微量元素的小球藻,属生物工程领域。  The invention relates to a production method of organic chlorella rich in trace elements. Specifically, the liquid organic fertilizer rich in trace elements is used to cultivate chlorella rich in iron, zinc, iodine, chromium, selenium and other trace elements, which belongs to the field of bioengineering. the

背景技术 Background technique

铁、锌、铜、锰、铬、硒、钼、钴、氟等元素在人体中只占总重量0.1%以下,这些元素被称为人体的微量元素,微量元素与人体的健康息息相关,对人的生命起至关重要的作用。根据研究,到目前为止,已被确认与人体健康和生命有关的必需微量元素有18种,即有铁、铜、锌、钴、锰、铬、硒、碘、镍、氟、钼、钒、锡、硅、锶、硼、铷、砷等,尽管它们在人体内含量极小,但它们是维持人体中的一些决定性的新陈代谢不可或缺的物质,如铁是血红素酶的辅基,碘是甲状腺激素结构成分,铜是细胞色素氧化酶的辅基,锰是精氨酸酶等的辅因子,锌是脱氧酶、DNA聚合酶、碳酸酐酶的辅因子,硒是谷胱甘肽过氧化物酶等的辅因子,钴是维生素B12的成分,钒是硝酸还原酶的辅因子,钼是黄嘌呤氧化酶的辅因子,镍是尿素酶的辅因子。微量元素摄入过量、不足、不平衡或缺乏都会不同程度地引起人体生理的异常或发生疾病。目前,比较明确的是约30%的疾病直接是微量元素缺乏或不平衡所致,同时研究发现,微量元素在抗病、防癌、延年益寿等方面都还起着非常重要的作用。 Iron, zinc, copper, manganese, chromium, selenium, molybdenum, cobalt, fluorine and other elements only account for less than 0.1% of the total weight in the human body. These elements are called trace elements of the human body. Trace elements are closely related to the health of the human body. vital role in life. According to research, so far, 18 kinds of essential trace elements have been confirmed to be related to human health and life, namely iron, copper, zinc, cobalt, manganese, chromium, selenium, iodine, nickel, fluorine, molybdenum, vanadium, Tin, silicon, strontium, boron, rubidium, arsenic, etc., although their content in the human body is very small, they are indispensable substances to maintain some decisive metabolism in the human body, such as iron is the prosthetic group of heme enzyme, iodine Copper is the cofactor of cytochrome oxidase, manganese is the cofactor of arginase, zinc is the cofactor of deoxygenase, DNA polymerase, carbonic anhydrase, selenium is the cofactor of glutathione cofactor of oxidase, etc., cobalt is a component of vitamin B12, vanadium is a cofactor of nitrate reductase, molybdenum is a cofactor of xanthine oxidase, and nickel is a cofactor of urease. Excessive, insufficient, unbalanced or deficient intake of trace elements will cause abnormalities in human physiology or diseases to varying degrees. At present, it is relatively clear that about 30% of diseases are directly caused by the lack or imbalance of trace elements. At the same time, studies have found that trace elements still play a very important role in disease resistance, cancer prevention, and longevity.

微量元素在自然界中主要存在于土壤和岩石中,以无机物的形式存在,人体所需的微量元素需要通过饮食来摄入,但实际生活中,人体对无机形式微量元素的吸收效率不高,大部分人往往不能通过饮食获得足够的微量元素,需要额外进行补偿。 Trace elements mainly exist in soil and rocks in nature, and exist in the form of inorganic substances. The trace elements needed by the human body need to be ingested through diet, but in actual life, the absorption efficiency of the inorganic form of trace elements by the human body is not high. Most people often do not get enough trace elements through diet and need to make additional compensation.

小球藻是一种天然的营养均衡的食物,具有多功能保健的功效,含有对人体生长发育、健康长寿所必需的多种营养物质,小球藻中蛋白质蛋白含量高,且氨基酸含量均衡,符合人体营养需求,且其蛋白肽具有多种生物活性,能起到活化人体细胞,修复受损基因,促进器官组织生长等作用;小球藻中含有多种天然高效维生素,具有抗氧化、清除自由基、延缓衰老、改善心、肺功能等功能,小球藻藻多糖和多种微量元素,具有抗疲劳、抗动脉粥样硬化、预防心血管疾病和糖尿病等功效;小球藻独有的CGF活性因子,具有调节免疫功能、抗肿瘤、诱发干扰素、增强细胞吞噬功能等功能;小球藻中天然高浓缩叶绿素和植物纤维素,具有排除体内化学毒素、重金属、保护肝、肾免受毒害、预防癌症等功效。 Chlorella is a natural food with balanced nutrition. It has multi-functional and health-care effects. It contains a variety of nutrients necessary for human growth, health and longevity. Chlorella has high protein content and balanced amino acid content. It meets the nutritional needs of the human body, and its protein peptide has a variety of biological activities, which can activate human cells, repair damaged genes, and promote the growth of organ tissues; Free radicals, anti-aging, improving heart and lung functions and other functions, chlorella polysaccharides and a variety of trace elements, have anti-fatigue, anti-atherosclerosis, prevent cardiovascular disease and diabetes and other effects; chlorella unique CGF active factor has the functions of regulating immune function, anti-tumor, inducing interferon, and enhancing cell phagocytosis; the natural high-concentration chlorophyll and plant cellulose in Chlorella can eliminate chemical toxins and heavy metals in the body, protect the liver and kidney from Toxicity, cancer prevention and other effects.

 小球藻在生长过程中,具有一个显著的生物学特征是能够富集培养液中的微量元素金属离子,并且具有将环境中的无机微量元素转化为有机化的微量元素的功能,更加利于人体吸收,但是在实际生产中,小球藻培养多采用光合自养的方式,直接向培养基中施加无机微量元素,难以控制藻细胞内的微量元素浓度,且有相当部分只是吸附在细胞表面,依然是无机态,不易被人体吸收;另外,培养基的水体中依然可能存在大量的微量元素残余,排放容易造成环境污染。 During the growth process of Chlorella, a remarkable biological feature is that it can enrich the trace element metal ions in the culture medium, and has the function of converting the inorganic trace elements in the environment into organic trace elements, which is more beneficial to the human body Absorption, but in actual production, chlorella culture mostly adopts the method of photoautotrophy, directly adding inorganic trace elements to the medium, it is difficult to control the concentration of trace elements in the algae cells, and a considerable part is only adsorbed on the cell surface, It is still in an inorganic state and is not easily absorbed by the human body; in addition, there may still be a large amount of trace element residues in the water body of the culture medium, and the discharge may easily cause environmental pollution.

本发明提供了一种富含微量元素的有机小球藻的生产方法,利用小球藻能够以有机物进行异养培养的生物学特性,用微生物菌体发酵的方法生产富集了有机化微量元素的培养基,该培养基进一步调配之后用于小球藻养殖,即可生产获得富含各种微量元素的小球藻。  The invention provides a production method of organic chlorella rich in trace elements, utilizing the biological characteristics that chlorella can carry out heterotrophic culture with organic matter, and producing enriched organic trace elements by the method of microbial cell fermentation The medium, which is further formulated and used for chlorella cultivation, can produce chlorella rich in various trace elements. the

发明内容 Contents of the invention

本发明的目的在于针对现有技术的不足而提供一种富含微量元素的小球藻的生产方法,该方法可以用于培养、生产富含各类微量元素的小球藻,并较为准确的控制藻体中的微量元素含量,且藻体中微量元素有机化程度高,更利于人体吸收,提高了小球藻产品的品质,实现了小球藻产品多元化、有机化和进一步高值化。另外,该方法利用工农业废弃生物质作为主要原料,实现了废物资源化,环境效益和社会效益明显 The purpose of the present invention is to provide a method for producing chlorella rich in trace elements for the deficiencies of the prior art, which can be used to cultivate and produce chlorella rich in various trace elements, and more accurately Control the content of trace elements in the algae body, and the degree of organicization of the trace elements in the algae body is high, which is more conducive to human body absorption, improves the quality of chlorella products, and realizes the diversification, organicization and further high value of chlorella products . In addition, the method utilizes industrial and agricultural waste biomass as the main raw material, realizes the recycling of waste, and has obvious environmental and social benefits

为达到上述目的,本发明通过以下技术方案来实现。 In order to achieve the above object, the present invention is achieved through the following technical solutions.

一种富含微量元素的有机小球藻的生产方法,包括有以下工艺步骤,具体为: A method for producing organic chlorella rich in trace elements, comprising the following process steps, specifically:

a.   微生物厌氧发酵培养基配制:利用废弃生物质为主要原料,根据其营养组分进行配料,根据需求补充氮、磷、钾等大量元素调节培养基诸元素平衡,同时添加锌、铬(Cr3+)、硒、碘等元素的无机盐作为微量元素配料;原料粉碎、混合后通入蒸汽灭菌,加无菌水调配成厌氧发酵培养基; a. Preparation of microbial anaerobic fermentation medium: use waste biomass as the main raw material, make ingredients according to its nutrient components, supplement nitrogen, phosphorus, potassium and other large elements according to demand to adjust the balance of various elements in the medium, and add zinc, chromium ( Cr 3+ ), selenium, iodine and other inorganic salts are used as trace element ingredients; the raw materials are crushed and mixed, then steam sterilized, and sterile water is added to prepare an anaerobic fermentation medium;

b.  液体有机肥厌氧发酵:将步骤a配制的培养基中加入纤维素分解菌和蛋白质水解菌菌种,在厌氧条件下发酵,获得含有单糖、寡糖、低元有机酸、游离氨基酸、蛋白肽、菌体等有机物的发酵液,发酵液中同时富含有锌、铬(Cr3+)、硒、碘等微量元素; b. Anaerobic fermentation of liquid organic fertilizer: add cellulolytic bacteria and proteolytic bacteria strains to the culture medium prepared in step a, and ferment under anaerobic conditions to obtain Fermentation liquid of amino acids, protein peptides, bacteria and other organic matter, the fermentation liquid is also rich in zinc, chromium (Cr 3+ ), selenium, iodine and other trace elements;

c.   有机小球藻生产:将步骤b获得的富含微量元素的发酵液灭菌,经调配后,添加入小球藻养殖容器,进行小球藻培养;小球藻养殖完成后,离心采收、干燥,即获得富集了各类微量元素的有机小球藻产品,可供后续进一步加工开发。 c. Production of organic chlorella: sterilize the fermented liquid rich in trace elements obtained in step b, after deployment, add it into the chlorella culture container for chlorella cultivation; After harvesting and drying, organic chlorella products enriched with various trace elements are obtained, which can be used for further processing and development.

其中,步骤a所述的废弃生物质,指的各类工农业生产产生的废弃物和副产物,含有蛋白质、多糖(主要为淀粉和纤维素)等可供微生物发酵的生物质资源,如发酵废水、酿酒废水、酒糟、木薯渣、甘蔗渣、豆粕、花生粕、米糠、麦麸、农业秸秆等等。 Among them, the waste biomass mentioned in step a refers to various wastes and by-products produced in industrial and agricultural production, containing protein, polysaccharides (mainly starch and cellulose) and other biomass resources that can be fermented by microorganisms, such as fermentation Wastewater, brewing wastewater, distiller's grains, cassava residue, bagasse, soybean meal, peanut meal, rice bran, wheat bran, agricultural straw, etc.

其中,步骤a所述的营养组分,主要指的是废弃生物质中能被微生物利用的蛋白质和多糖等物质;步骤a所述的调配,指的是根据不同废弃生物质原料中蛋白、多糖等成分含量,按一定比例配比原料,并对应的补充加入氮、磷、钾等肥料,达到适于微生物发酵生长所需的营养和元素配比;步骤a所述的微量元素的添加,指根据目标小球藻产品的需要,对应的加入锌、铬(Cr3+)、硒、碘等微量元素的无机盐。 Among them, the nutritional components described in step a mainly refer to substances such as proteins and polysaccharides in waste biomass that can be utilized by microorganisms; equal component content, proportion raw materials according to a certain proportion, and correspondingly add fertilizers such as nitrogen, phosphorus, potassium, etc., to reach the nutrient and element proportion suitable for microbial fermentation growth; the addition of trace elements described in step a refers to According to the needs of the target chlorella products, correspondingly add zinc, chromium (Cr 3+ ), selenium, iodine and other inorganic salts of trace elements.

其中,步骤b所述的液体有机肥厌氧发酵,指的是无氧条件下,在步骤a配制的培养基培养中培养纤维素分解菌、淀粉分解菌、脂肪分解菌和蛋白质水解菌的过程,其原理是利用纤维素分解菌,淀粉分解菌和脂肪分解菌在培养基中生长繁殖的过程中分解培养基中的纤维素、淀粉、脂肪等物质成为其他菌类或小球藻可以直接利用的单糖、寡糖、低元有机酸等;利用蛋白质水解菌,在培养基中生长繁殖的过程中,分解蛋白类物质,如菌体、蛋白等物质为小球藻可以直接利用的游离氨基酸、蛋白小肽的过程。 Wherein, the liquid organic fertilizer anaerobic fermentation described in step b refers to the process of cultivating cellulolytic bacteria, amylolytic bacteria, lipolytic bacteria and proteolytic bacteria in the culture medium prepared in step a under anaerobic conditions The principle is to use cellulolytic bacteria, amylolytic bacteria and lipolytic bacteria to decompose cellulose, starch, fat and other substances in the medium during the growth and reproduction process in the medium to become other fungi or chlorella that can be directly used Monosaccharides, oligosaccharides, low-yuan organic acids, etc.; use proteolytic bacteria to decompose protein substances during the growth and reproduction process in the medium, such as bacteria, proteins and other substances into free amino acids that Chlorella can directly use , The process of small protein peptides.

进一步的,步骤b所述的纤维素分解菌,指的是能够在厌氧条件下,通过菌体生产和代谢,分解生物质中的纤维素为单糖、寡糖和甲酸、乙酸、丙酸、丁酸等低元碳水化合物的菌种,如芽孢梭菌属的各个种株。 Further, the cellulolytic bacteria described in step b refers to the ability to decompose cellulose in biomass into monosaccharides, oligosaccharides and formic acid, acetic acid, and propionic acid under anaerobic conditions through bacterial production and metabolism. , butyric acid and other low-carbohydrate strains, such as various strains of Clostridium sporogenes.

进一步的,步骤b所述的淀粉分解菌,指的是能够在厌氧条件下,通过菌体生产和代谢,分解生物质中的淀粉为单糖、寡糖和甲酸、乙酸、丙酸、丁酸等低元碳水化合物的菌种,如枯草杆菌的一些种株。 Further, the amylolytic bacteria described in step b refers to the bacteria that can decompose the starch in the biomass into monosaccharides, oligosaccharides and formic acid, acetic acid, propionic acid, butyric acid under anaerobic conditions through the production and metabolism of bacteria. Sour and other low-carbohydrate strains, such as some strains of Bacillus subtilis.

进一步的,步骤b所述的脂肪分解菌,指的是能够在厌氧条件下,通过菌体生产和代谢,分解生物质中的脂肪为单糖、寡糖和甲酸、乙酸、丙酸、丁酸等低元碳水化合物的菌种,如芽孢梭菌和枯草杆菌。 Further, the lipolytic bacteria described in step b refers to the bacteria that can decompose the fat in biomass into monosaccharides, oligosaccharides and formic acid, acetic acid, propionic acid, butyric acid under anaerobic conditions through bacterial body production and metabolism. Sour and other low-carbohydrate strains, such as Clostridium sporogenes and Bacillus subtilis.

进一步的,步骤b所述的蛋白质分解菌,指的是能够在厌氧条件下,通过菌体生产和代谢,分解生物质中的蛋白质为游离氨基酸和蛋白小肽的菌种,环境中多数厌氧菌均具有分解蛋白的功能。 Further, the proteolytic bacteria described in step b refers to bacteria that can decompose proteins in biomass into free amino acids and small protein peptides through bacterial production and metabolism under anaerobic conditions. Most anaerobic bacteria in the environment Oxygen bacteria have the function of decomposing protein.

其中,步骤c所述的小球藻养殖,指的是利用步骤b获得的富含单糖、寡糖、低元有机酸、游离氨基酸、蛋白小肽和各微量元素的发酵液作为培养基,作为小球藻培养的原料,在培养容器中培养小球藻的过程。进一步的,小球藻培养容器指的得是发酵罐、密闭式光生物反应器和开放池,以及以上不同容器的串联组合。  Wherein, the chlorella cultivation described in step c refers to using the fermented liquid rich in monosaccharides, oligosaccharides, low-basic organic acids, free amino acids, small protein peptides and various trace elements obtained in step b as a culture medium, The process of growing chlorella in a culture container as a raw material for chlorella culture. Further, the chlorella culture container refers to a fermenter, a closed photobioreactor, an open pool, and a series combination of the above different containers. the

其中,步骤c所述的离心采收,指的是利用碟片式离心机离心采收小球藻获得小球藻浓浆的过程。 Wherein, the centrifugal harvesting described in step c refers to the process of using a disc centrifuge to centrifugally harvest the chlorella to obtain a concentrated chlorella slurry.

其中,步骤c所述的干燥,指的是利用喷雾干燥塔干燥小球藻浓浆,获得小球藻干粉的过程。 Wherein, the drying described in step c refers to the process of using a spray drying tower to dry the chlorella thick slurry to obtain the chlorella dry powder.

本发明的有益效果为:本发明所述的一种富含微量元素的有机小球藻生产方法,其包括微生物厌氧发酵培养基配制,液体有机肥厌氧发酵和有机小球藻生产等工艺步骤。通过以上工艺步骤,生产获得富含各种微量元素的有机小球藻产品。本发明适用于中试级别以上的实验性生产和规模化小球藻生产;本发明通过厌氧发酵的方法,实现了小球藻的液体有机肥的生产,在小球藻养殖培养基配置的环节即实现了微量元素的富集和有机化,利用此富含有机化微量元素的液体肥料养殖小球藻,即可获得富集了各个微量元素的有机小球藻产品,该小球藻产品中的各微量元素已经有机化,更易被人体吸收。本发明利用生物质废弃物为源头物料,实现了废弃物资源化和高值化,小球藻生产过程的有机化,带来环境和经济双重效应。 The beneficial effects of the present invention are: a method for producing organic chlorella rich in trace elements according to the present invention, which includes the preparation of microbial anaerobic fermentation medium, the anaerobic fermentation of liquid organic fertilizer and the production of organic chlorella step. Through the above process steps, organic chlorella products rich in various trace elements are produced and obtained. The present invention is suitable for experimental production and large-scale chlorella production above the pilot test level; the present invention realizes the production of liquid organic fertilizer for chlorella through the method of anaerobic fermentation, and is configured in the chlorella culture medium The link realizes the enrichment and organicization of trace elements. Using this liquid fertilizer rich in organic trace elements to cultivate chlorella, one can obtain organic chlorella products enriched with various trace elements. The chlorella products The trace elements in the milk have been organicized and are more easily absorbed by the body. The invention utilizes the biomass waste as the source material, realizes waste resource and high value, and organicizes the production process of chlorella, bringing double effects of environment and economy.

具体实施方式 Detailed ways

下面结合具体的实施方式来对本发明进行说明,其中,本发明所指的小球藻为分类学中定义为小球藻属(Chlorella)的各个小球藻种株,且本发明所采用的设备均指中试以及中试以上规模设备。 The present invention will be described below in conjunction with specific embodiments, wherein the chlorella referred to in the present invention refers to various strains of Chlorella defined as Chlorella in taxonomy, and the equipment used in the present invention Both refer to pilot scale and above-scale equipment.

实施例一,利用啤酒糟为主要原料配置微生物厌氧发酵培养基,啤酒糟取自东莞金威啤酒厂,经分析,干物质中含有粗蛋白24.7%、粗脂肪7.5%、粗纤维14.2%;取含水量为45%的啤酒糟700公斤加入到3吨不锈钢灭菌罐中,加糖蜜50公斤,加水750公斤并搅拌混匀,通蒸汽,120℃加热灭菌0.5小时以上,降至室温后,转入消毒后的5吨塑料桶中。 Example 1, brewer's grains were used as the main raw material to configure microbial anaerobic fermentation medium. Brewer's grains were taken from Dongguan Kingway Brewery. After analysis, the dry matter contained 24.7% of crude protein, 7.5% of crude fat, and 14.2% of crude fiber; Take 700 kg of brewer's grains with a water content of 45% and add them to a 3-ton stainless steel sterilization tank, add 50 kg of molasses, add 750 kg of water, stir and mix well, pass steam, heat and sterilize at 120°C for more than 0.5 hours, and cool down to room temperature , into a sterilized 5-ton plastic bucket.

  取尿素20公斤、食盐15公斤、磷酸二氢钾10公斤、七水硫酸镁15公斤、氯化铁2公斤、七水硫酸锌3公斤、亚硒酸钠0.75克、碘酸钾1克、硝酸铬[Cr(NO3)3]0.75克,分别充分融解过滤除菌后,加入5吨塑料桶中,补加无菌水至总体积为3.5吨,即配置完成微生物厌氧发酵培养基。 Take 20 kg of urea, 15 kg of salt, 10 kg of potassium dihydrogen phosphate, 15 kg of magnesium sulfate heptahydrate, 2 kg of ferric chloride, 3 kg of zinc sulfate heptahydrate, 0.75 g of sodium selenite, 1 g of potassium iodate, nitric acid Chromium [Cr(NO 3 ) 3 ] 0.75 g was fully melted and sterilized by filtration, then added to a 5-ton plastic bucket, and sterile water was added until the total volume was 3.5 tons, and the microbial anaerobic fermentation medium was configured.

  实施例二,小球藻液体有机肥生产, 在实施例一获得的微生物厌氧发酵培养基中,在装液量为3.5吨的5吨塑料大桶中,按每吨培养基10g的添加量,添加市售EM菌粉,该菌粉含双岐菌、乳酸菌、芽孢杆菌、光合细菌、酵母菌、放线菌、醋酸菌等菌种,每克含总菌数≥500亿 CFU。塑料桶加盖密封后,放置于室外,EM菌粉中的各厌氧菌利用自然的温度条件进行生长,厌氧发酵时间为7天以上。取发酵上清液,经120℃高温灭菌0.5小时后,即获得浓缩的液体有机肥,其中富含铁、锌、硒、三价铬和碘等微量元素。由于厌氧发酵条件不受控制,不同批次生产的有机肥中各个营养元素的浓度不定,需测定氮元素含量为参照指标,作为下步稀释后配置小球藻有机培养基的依据。 Embodiment two, the production of chlorella liquid organic fertilizer, in the microorganism anaerobic fermentation culture medium that embodiment one obtains, in the 5 tons of plastic vats that liquid filling capacity is 3.5 tons, by the addition amount of 10g per ton of culture medium, Add commercially available EM bacteria powder, which contains bifidobacteria, lactic acid bacteria, bacillus, photosynthetic bacteria, yeast, actinomycetes, acetic acid bacteria and other bacteria species, and the total number of bacteria per gram is ≥ 50 billion CFU. After the plastic bucket is covered and sealed, it is placed outdoors, and the anaerobic bacteria in the EM bacteria powder use natural temperature conditions to grow, and the anaerobic fermentation time is more than 7 days. Take the fermentation supernatant and sterilize it at 120°C for 0.5 hours to obtain concentrated liquid organic fertilizer, which is rich in trace elements such as iron, zinc, selenium, trivalent chromium and iodine. Due to the uncontrolled anaerobic fermentation conditions, the concentration of each nutrient element in different batches of organic fertilizers is variable, and the nitrogen element content needs to be measured as a reference index, which is used as the basis for configuring the chlorella organic medium after dilution in the next step.

  实施例三,小球藻异养发酵培养,本实施例以10吨级发酵罐为培养容器,加入无菌的异养发酵小球藻液为种子液和无菌的浓缩液体有机肥,补加无菌水,至7吨的反应体积。控制起始发酵液中,小球藻干重密度为0.25g±0.05/L,培养基中氮元素终浓度为0.22~0.25gN/L,发酵培养的参数:搅拌速率180~200rpm,溶氧控制为50±5%,发酵温度为28±0.5℃,pH控制为7±0.2,发酵24小时后,收获藻液,利用碟片式离心机离心浓缩,离心速率为4500rpm以上,再经过反复清洗-离心3遍后,将浓缩液(干重含量约为10%)经喷雾干燥塔干燥,干燥温度控制在180℃,干燥后即获得发酵生产的有机小球藻藻粉。经检测,发酵液中小球藻干重含量为0.82g/L,该有机生产的小球藻中蛋白含量48.7%,水分<5%,灰分<7%,锌含量为5.2mg/g,三价铬含量为22μg/g,铁含量为2.5mg/g,硒含量为19μg/g,碘含量为31μg/g。 Embodiment 3, Chlorella heterotrophic fermentation culture, this embodiment uses 10 tons fermenter tank as culture container, adds sterile heterotrophic fermented Chlorella liquid as seed liquid and aseptic concentrated liquid organic fertilizer, supplements Sterile water, to a reaction volume of 7 tons. Control the initial fermentation liquid, the dry weight density of Chlorella is 0.25g±0.05/L, the final concentration of nitrogen in the medium is 0.22-0.25gN/L, the parameters of fermentation culture: stirring rate 180-200rpm, dissolved oxygen control 50±5%, the fermentation temperature is 28±0.5℃, and the pH is controlled at 7±0.2. After 24 hours of fermentation, the algae liquid is harvested and concentrated by disc centrifuge at a centrifugal rate of 4500rpm or more. After repeated cleaning- After centrifugation for 3 times, the concentrated solution (with a dry weight content of about 10%) is dried in a spray drying tower, and the drying temperature is controlled at 180°C. After drying, the organic chlorella algae powder produced by fermentation is obtained. After testing, the dry weight content of chlorella in the fermentation broth is 0.82g/L, the protein content in the organically produced chlorella is 48.7%, the water content is <5%, the ash content is <7%, the zinc content is 5.2mg/g, and the trivalent The chromium content is 22 μg/g, the iron content is 2.5 mg/g, the selenium content is 19 μg/g, and the iodine content is 31 μg/g.

    实施例四,利用密闭式光生物反应器培养小球藻,本实施例以消毒后的立袋式光生物反应器为培养容器,立袋的直径为25cm,高为2.2米,工作液高为1.75米,工作体积为85L,12个立袋为一组,总工作体积为1立方米。加入小球藻种子液和无菌的浓缩液体有机肥,补充无菌水,控制起始培养液中,小球藻干重密度为0.15g±0.05/L,培养基中氮元素终浓度为0.12~0.15gN/L,充气搅拌,充气比为0.05vvm,在自然光下,充入二氧化碳气体以补充碳源,并控制pH为8±0.2,每天上午和下午各补加一次浓缩液体有机肥至培养液中氮元素终浓度为~0.15gN/L,在室外培养,利用自然光进行生产。测定培养期间,水温为22~31℃,最大光照强度为55~65klux,培养三天后,收获藻液, 利用碟片式离心机离心浓缩,离心速率为4500rpm以上,再经过反复清洗-离心3遍后,将浓缩液(干重含量约为10%)经喷雾干燥塔干燥,干燥温度控制在180℃,干燥后即获得有机小球藻藻粉。经检测,发酵液中小球藻干重含量为1.25g/L,该有机生产的小球藻中蛋白含量61.2%,水分<5%,灰分<7%,锌含量为6.4 mg/g,三价铬含量为26μg/g,铁含量为3.2 mg/g,硒含量为23μg/g,碘含量为37μg/g。 Embodiment four, utilizing the closed photobioreactor to cultivate Chlorella, the present embodiment takes the sterilized vertical bag photobioreactor as the culture container, the diameter of the vertical bag is 25cm, the height is 2.2 meters, and the height of the working fluid is 1.75 meters, the working volume is 85L, 12 stand-up bags as a group, the total working volume is 1 cubic meter. Add chlorella seed liquid and sterile concentrated liquid organic fertilizer, supplement sterile water, control the initial culture medium, the dry weight density of chlorella is 0.15g±0.05/L, and the final concentration of nitrogen in the medium is 0.12 ~0.15gN/L, inflate and stir, the aeration ratio is 0.05vvm, under natural light, fill in carbon dioxide gas to supplement the carbon source, and control the pH to 8±0.2, add concentrated liquid organic fertilizer once every morning and afternoon to cultivate The final concentration of nitrogen in the liquid is ~0.15gN/L, cultivated outdoors, and produced using natural light. During the measurement and cultivation period, the water temperature is 22-31°C, and the maximum light intensity is 55-65klux. After three days of cultivation, the algae liquid is harvested, concentrated by centrifugation in a disc centrifuge, and the centrifugation speed is above 4500rpm, and then washed and centrifuged repeatedly for 3 times. Finally, the concentrated solution (dry weight content is about 10%) is dried in a spray drying tower, and the drying temperature is controlled at 180°C. After drying, the organic chlorella algae powder is obtained. After testing, the dry weight content of chlorella in the fermentation broth is 1.25g/L, the protein content in the organically produced chlorella is 61.2%, the water content is <5%, the ash content is <7%, the zinc content is 6.4 mg/g, and the trivalent The chromium content is 26 μg/g, the iron content is 3.2 mg/g, the selenium content is 23 μg/g, and the iodine content is 37 μg/g.

  实施例五,利用发酵罐和立袋式反应器串联进行小球藻培养,本实施例以10吨级发酵罐为培养容器,培养步骤和参数同实施例三,发酵24小时后,转入至立袋式光生物反应器中,培养步骤和参数同实施例四,培养24小时后(下午18点接种,经过1次日照),收获藻液, 利用碟片式离心机离心浓缩,离心速率为4500rpm以上,再经过反复清洗-离心3遍后,将浓缩液(干重含量约为10%)经喷雾干燥塔干燥,干燥温度控制在180℃,干燥后即获得有机小球藻藻粉。经检测,发酵液中小球藻干重含量为1.02g/L,该有机生产的小球藻中蛋白含量>60.2%,水分<5%,灰分<7%,锌含量为5.7 mg/g,三价铬含量为23μg/g,铁含量为2.9mg/g,硒含量为21μg/g,碘含量为34μg/g。 Embodiment five, utilize fermentor and stand-up bag reactor to carry out chlorella culture in series, present embodiment uses 10 ton level fermenter as culture vessel, culture steps and parameters are the same as embodiment three, after fermenting for 24 hours, transfer to In the vertical bag photobioreactor, the cultivation steps and parameters are the same as those in Example 4. After 24 hours of cultivation (inoculation at 18:00 p.m., after one exposure to sunlight), the algae liquid is harvested and concentrated by centrifugation with a disc centrifuge at a centrifugation rate of Above 4500rpm, after repeated washing and centrifugation for 3 times, the concentrated solution (dry weight content is about 10%) is dried in a spray drying tower, and the drying temperature is controlled at 180°C. Organic chlorella algae powder can be obtained after drying. After testing, the dry weight content of chlorella in the fermentation broth is 1.02g/L, the protein content in the organically produced chlorella is >60.2%, the water content is <5%, the ash content is <7%, and the zinc content is 5.7 mg/g. The valent chromium content is 23 μg/g, the iron content is 2.9 mg/g, the selenium content is 21 μg/g, and the iodine content is 34 μg/g.

   实施例六,开放池中进行小球藻培养,以1000平方米开放圆形池为培养容器,加入10cm深度的水,加入小球藻种子液浓缩液体有机肥,补充水至养殖深度为20cm,控制起始培养液中,小球藻干重密度为0.12g±0.02/L,培养基中氮元素终浓度为,利用搅拌车进行搅拌,转速为每72s一圈,每天上午添加一次浓缩有机肥至培养基中氮元素终浓度为0.12~0.15gN/L。在室外培养,利用自然光进行生产。测定培养期间,水温为24~32℃,最大光照强度为58~67klux,培养四天后,收获藻液, 利用碟片式离心机离心浓缩,离心速率为4500rpm以上,再经过反复清洗-离心3遍后,将浓缩液(干重含量约为10%)经喷雾干燥塔干燥,干燥温度控制在180℃,干燥后即获得有机小球藻藻粉。经检测,发酵液中小球藻干重含量为0.58g/L,该有机生产的小球藻中蛋白含量59.7%,水分<5%,灰分<7%,锌含量为6.4 mg/g,三价铬含量为32μg/g,铁含量为3.5mg/g,硒含量为27μg/g,碘含量为42μg/g。 Embodiment six, carry out chlorella cultivation in the open pond, take the open circular pond of 1000 square meters as the culture container, add the water of 10cm depth, add the concentrated liquid organic fertilizer of chlorella seed liquid, add water to the cultivation depth is 20cm, Control the initial culture medium, the dry weight density of chlorella is 0.12g±0.02/L, the final concentration of nitrogen in the culture medium is , use a mixer truck to stir, the speed is every 72s, and add concentrated organic fertilizer once every morning Until the final concentration of nitrogen in the medium is 0.12-0.15gN/L. Cultivated outdoors with natural light for production. During the measurement and cultivation period, the water temperature is 24-32°C, and the maximum light intensity is 58-67klux. After four days of cultivation, the algae liquid is harvested, concentrated by centrifugation in a disc centrifuge, and the centrifugation speed is above 4500rpm, and then washed and centrifuged repeatedly for 3 times. Finally, the concentrated solution (dry weight content is about 10%) is dried in a spray drying tower, and the drying temperature is controlled at 180°C. After drying, the organic chlorella algae powder is obtained. After testing, the dry weight content of chlorella in the fermentation broth is 0.58g/L, the protein content in the organically produced chlorella is 59.7%, the water content is <5%, the ash content is <7%, the zinc content is 6.4 mg/g, and the trivalent The chromium content is 32 μg/g, the iron content is 3.5 mg/g, the selenium content is 27 μg/g, and the iodine content is 42 μg/g.

以上内容仅为本发明的较佳实施例,对于本领域的普通技术人员,依据本发明的思想,在具体实施方式及应用范围上均会有改变之处,如添加微量元素的种类和配料中各个原料的配比,发酵培养中各个参数的变动,养殖过程中有机肥的施用浓度等,本说明书内容不应理解为对本发明的限制。  The above content is only a preferred embodiment of the present invention. For those of ordinary skill in the art, according to the idea of the present invention, there will be changes in the specific implementation and application range, such as the types of added trace elements and ingredients. The ratio of each raw material, the change of each parameter in the fermentation culture, the application concentration of organic fertilizer in the cultivation process, etc., the content of this specification should not be understood as a limitation of the present invention. the

Claims (4)

1. an organic chlorella production method for rich trace elements, is characterized in that: it comprises the following steps, and the first step is the preparation of microbiological anaerobic fermention medium; Second step is producing of fertilizer anaerobic fermented liquid; 3rd step is in culture vessel, using the cultivation raw material of fertilizer anaerobic fermented liquid as chlorella, adds chlorella seed liquor and carries out chlorella cultivation, carries out organic chlorella product that drying can obtain rich trace elements after results algae liquid.
2. organic chlorella production method of a kind of rich trace elements according to claim 1, it is characterized in that: the preparation of microbiological anaerobic fermention medium, utilize abandoned biomass for main raw material, prepare burden according to its nutrition composition, supplement the fertilizer such as nitrogen, phosphorus, potassium and regulate substratum various element balance, add zinc, chromium (Cr simultaneously 3+), the inorganic salt element such as selenium, iodine prepares burden as trace element; Pass into steam sterilizing after being pulverized by above-mentioned compound, add sterilized water and be deployed into anaerobically fermenting substratum; Described abandoned biomass, refer to the waste that all kinds of industrial and agricultural production produces and by product, the biomass of fermentable can be supplied, as fermentation waste water, brewing wastewater, vinasse, manioc waste, bagasse, dregs of beans, peanut meal, rice bran, wheat bran, agricultural stalk etc. containing protein, polysaccharide (being mainly starch and Mierocrystalline cellulose) etc.; Described nutrition composition, refers to the material such as protein and polysaccharide that can be utilized by microorganism in abandoned biomass; Described allotment, refer to according to the component content such as albumen, polysaccharide in different waste biomass materials, by a certain percentage proportioning raw material, and the supplementary of correspondence adds the fertilizer such as nitrogen, phosphorus, potassium, reach be suitable for fermentable growth needed for nutrition and element proportioning; The interpolation of described trace element, refers to the needs according to target chlorella product, and corresponding adds zinc, chromium (Cr 3+), the inorganic salt element of the trace such as selenium, iodine.
3. organic chlorella production method of a kind of rich trace elements according to claim 1, it is characterized in that: producing of fertilizer anaerobic fermented liquid, cellulose-decomposing bacterium and proteolysis bacterium bacterial classification will be added in microbiological anaerobic fermention medium, under anaerobic ferment, obtain containing organic fermented liquids such as monose, oligosaccharides, low first organic acid, total free aminoacids, protein peptide, thalline, in fermented liquid, be rich in zinc, chromium (Cr simultaneously 3+), the trace element such as selenium, iodine; Described fertilizer anaerobically fermenting, under referring to oxygen free condition, the process of cellulose-decomposing bacterium, amylolysis bacterium, steatolysis bacterium and proteolysis bacterium is cultivated in microbiological anaerobic fermention medium, its principle utilizes cellulose-decomposing bacterium, and in the process of amylolysis bacterium and steatolysis bacterium growth and breeding in the medium, the material such as Mierocrystalline cellulose, starch, fat decomposed in substratum becomes monose, oligosaccharides and the low first organic acid etc. that other mushrooms or chlorella can directly utilize; Utilize proteolysis bacterium, in the process of growth and breeding in the medium, decomposition of protein class material, if the material such as thalline, albumen is the process of the chlorella total free aminoacids that can directly utilize and protein small peptide;
Further, described cellulose-decomposing bacterium, is referred to and can under anaerobic, be produced and metabolism by thalline, Mierocrystalline cellulose in decomposing biomass is the bacterial classification of low first carbohydrate such as monose, oligosaccharides and formic acid, acetic acid, propionic acid, butyric acid, as each kind of strain of Clostridium;
Further, described amylolysis bacterium, is referred to and can under anaerobic, be produced and metabolism by thalline, starch in decomposing biomass is the bacterial classification of low first carbohydrate such as monose, oligosaccharides and formic acid, acetic acid, propionic acid, butyric acid, as some of Bacillus subtilus plant strain;
Further, described steatolysis bacterium, is referred to and can under anaerobic, be produced and metabolism by thalline, fat in decomposing biomass is the bacterial classification of low first carbohydrate such as monose, oligosaccharides and formic acid, acetic acid, propionic acid, butyric acid, as Clostridium and Bacillus subtilus;
Further, described protein decomposing bacteria, refer to and can under anaerobic, be produced and metabolism by thalline, the protein in decomposing biomass is the bacterial classification of total free aminoacids and protein small peptide, and in environment, most anerobe all has protelytic function.
4. organic chlorella production method of a kind of rich trace elements according to claim 1, it is characterized in that: organic chlorella produces, by the fermented liquid sterilizing of the rich trace elements of acquisition, after allotment, be added into chlorella Cultivation container, carry out chlorella cultivation; After chlorella has cultivated, centrifugally to gather, dry, namely obtain the organic chlorella product being enriched all kinds of trace element, can develop for follow-up further processing; Described chlorella cultivation, refer to and utilize the fermented liquid being rich in monose, oligosaccharides, low first organic acid, total free aminoacids, protein small peptide and each trace element obtained as substratum, as the raw material that chlorella is cultivated, in culture vessel, cultivate the process of chlorella; Further, what chlorella culture vessel referred to must be fermentor tank, Closed photobioreactor or open pond, and the series combination of above different vessels; Described centrifugally to gather, refer to the process utilizing the centrifugal chlorella of gathering of disc centrifuge to obtain chlorella underflow; Described drying, refers to and utilizes spray-drying tower dried pellet algae underflow, obtains the process of chlorella dry powder.
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105802853A (en) * 2016-05-20 2016-07-27 佛山市聚成生化技术研发有限公司 Method for promoting porphyridium growth by virtue of aquatic product processing wastewater
CN106701588A (en) * 2016-11-17 2017-05-24 中盐工程技术研究院有限公司 Culture method of selenium-enriched chlorella
CN108410920A (en) * 2018-05-10 2018-08-17 天津大学 The optimization method of polysaccharide and grease is produced using high concentration tofu wastewater culture chlorella L166
CN109897784A (en) * 2019-02-27 2019-06-18 天津大学 A kind of method that novel two stages autotrophy-Heterotrophic culture promotes microalgae lipid
CN110194567A (en) * 2019-06-19 2019-09-03 北京林业大学 A kind of processing method of sludge hydrolysis, acidification liquid
CN111320510A (en) * 2020-02-28 2020-06-23 广州市土根旺生物科技有限公司 Directional fermentation microbial fertilizer and preparation method thereof
CN112430161A (en) * 2020-12-01 2021-03-02 鹤山市新的生物制品有限公司 Organic fermented paste fertilizer and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102864188A (en) * 2011-07-07 2013-01-09 中国科学院青岛生物能源与过程研究所 Method for producing biodiesel from lignocellulose
CN103740794A (en) * 2014-01-06 2014-04-23 东莞市绿安奇生物工程有限公司 A kind of process method for large-scale and graded preparation of active components of chlorella

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102864188A (en) * 2011-07-07 2013-01-09 中国科学院青岛生物能源与过程研究所 Method for producing biodiesel from lignocellulose
CN103740794A (en) * 2014-01-06 2014-04-23 东莞市绿安奇生物工程有限公司 A kind of process method for large-scale and graded preparation of active components of chlorella

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
ATHURRAHMAN LANANAN ET AL.: "Symbiotic bioremediation of aquaculture wastewater in reducing ammonia and phosphorus utilizing effective microorganism(EM-1) and microalgae(Chlorella sp.)", 《INTERNATIONAL BIODETERIORATION&BIODEGRADATION》 *
吕蓉: "海洋微藻活性微量元素积累的研究", 《中国优秀硕士学位论文全文数据库基础科技辑》 *
陈小晨等: "光合细菌对铜绿微囊藻和小球藻生长的影响研究", 《安徽农学通报》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105802853A (en) * 2016-05-20 2016-07-27 佛山市聚成生化技术研发有限公司 Method for promoting porphyridium growth by virtue of aquatic product processing wastewater
CN106701588A (en) * 2016-11-17 2017-05-24 中盐工程技术研究院有限公司 Culture method of selenium-enriched chlorella
CN108410920A (en) * 2018-05-10 2018-08-17 天津大学 The optimization method of polysaccharide and grease is produced using high concentration tofu wastewater culture chlorella L166
CN109897784A (en) * 2019-02-27 2019-06-18 天津大学 A kind of method that novel two stages autotrophy-Heterotrophic culture promotes microalgae lipid
CN110194567A (en) * 2019-06-19 2019-09-03 北京林业大学 A kind of processing method of sludge hydrolysis, acidification liquid
CN111320510A (en) * 2020-02-28 2020-06-23 广州市土根旺生物科技有限公司 Directional fermentation microbial fertilizer and preparation method thereof
CN112430161A (en) * 2020-12-01 2021-03-02 鹤山市新的生物制品有限公司 Organic fermented paste fertilizer and preparation method thereof

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