CN111875195A - A kind of pig manure biological treatment process and utilization method - Google Patents
A kind of pig manure biological treatment process and utilization method Download PDFInfo
- Publication number
- CN111875195A CN111875195A CN202010670434.8A CN202010670434A CN111875195A CN 111875195 A CN111875195 A CN 111875195A CN 202010670434 A CN202010670434 A CN 202010670434A CN 111875195 A CN111875195 A CN 111875195A
- Authority
- CN
- China
- Prior art keywords
- pig manure
- tank
- parts
- weight
- manure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 210000003608 fece Anatomy 0.000 title claims abstract description 106
- 239000010871 livestock manure Substances 0.000 title claims abstract description 104
- 238000000034 method Methods 0.000 title claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 73
- 239000003337 fertilizer Substances 0.000 claims abstract description 52
- 238000000746 purification Methods 0.000 claims abstract description 22
- 230000001580 bacterial effect Effects 0.000 claims abstract description 20
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 20
- 239000003607 modifier Substances 0.000 claims abstract description 20
- 150000001875 compounds Chemical class 0.000 claims abstract description 16
- 238000003860 storage Methods 0.000 claims abstract description 16
- 239000007787 solid Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000012535 impurity Substances 0.000 claims abstract description 6
- 239000000126 substance Substances 0.000 claims abstract description 6
- 238000000855 fermentation Methods 0.000 claims description 36
- 230000004151 fermentation Effects 0.000 claims description 36
- 239000001913 cellulose Substances 0.000 claims description 15
- 229920002678 cellulose Polymers 0.000 claims description 15
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 15
- AXKBOWBNOCUNJL-UHFFFAOYSA-M sodium;2-nitrophenolate Chemical compound [Na+].[O-]C1=CC=CC=C1[N+]([O-])=O AXKBOWBNOCUNJL-UHFFFAOYSA-M 0.000 claims description 15
- DCUJJWWUNKIJPH-UHFFFAOYSA-N nitrapyrin Chemical compound ClC1=CC=CC(C(Cl)(Cl)Cl)=N1 DCUJJWWUNKIJPH-UHFFFAOYSA-N 0.000 claims description 13
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 10
- 239000000047 product Substances 0.000 claims description 9
- 244000063299 Bacillus subtilis Species 0.000 claims description 7
- 235000014469 Bacillus subtilis Nutrition 0.000 claims description 7
- 241000193385 Geobacillus stearothermophilus Species 0.000 claims description 7
- 241000187654 Nocardia Species 0.000 claims description 7
- 241000933812 Streptomyces flaveus Species 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 229910000402 monopotassium phosphate Inorganic materials 0.000 claims description 7
- 235000019796 monopotassium phosphate Nutrition 0.000 claims description 7
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 claims description 7
- LWIHDJKSTIGBAC-UHFFFAOYSA-K potassium phosphate Substances [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 claims description 7
- 241000894006 Bacteria Species 0.000 claims description 6
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 5
- 239000004202 carbamide Substances 0.000 claims description 5
- 239000002781 deodorant agent Substances 0.000 claims description 5
- 239000001103 potassium chloride Substances 0.000 claims description 5
- 235000011164 potassium chloride Nutrition 0.000 claims description 5
- 239000002244 precipitate Substances 0.000 claims description 5
- 239000002131 composite material Substances 0.000 claims description 4
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims 2
- 238000009395 breeding Methods 0.000 abstract description 5
- 230000001488 breeding effect Effects 0.000 abstract description 5
- 238000011161 development Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 description 11
- 244000025254 Cannabis sativa Species 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 10
- 239000002689 soil Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 6
- 239000010865 sewage Substances 0.000 description 6
- 210000002700 urine Anatomy 0.000 description 6
- 241001481656 Stratiomyidae Species 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 5
- 230000001965 increasing effect Effects 0.000 description 5
- 241000282887 Suidae Species 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000238631 Hexapoda Species 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 210000004013 groin Anatomy 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 244000144977 poultry Species 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- KAQJMEHRXVENSF-UHFFFAOYSA-N 2-(trichloromethyl)pyridine Chemical compound ClC(Cl)(Cl)C1=CC=CC=N1 KAQJMEHRXVENSF-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 235000019739 Dicalciumphosphate Nutrition 0.000 description 1
- 240000005979 Hordeum vulgare Species 0.000 description 1
- 235000007340 Hordeum vulgare Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 1
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- 241000233805 Phoenix Species 0.000 description 1
- 241000254109 Tenebrio molitor Species 0.000 description 1
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 235000021120 animal protein Nutrition 0.000 description 1
- 230000008485 antagonism Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229960001701 chloroform Drugs 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 210000000805 cytoplasm Anatomy 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- NEFBYIFKOOEVPA-UHFFFAOYSA-K dicalcium phosphate Chemical compound [Ca+2].[Ca+2].[O-]P([O-])([O-])=O NEFBYIFKOOEVPA-UHFFFAOYSA-K 0.000 description 1
- 229910000390 dicalcium phosphate Inorganic materials 0.000 description 1
- 229940038472 dicalcium phosphate Drugs 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000021191 food habits Nutrition 0.000 description 1
- 229910052588 hydroxylapatite Inorganic materials 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000618 nitrogen fertilizer Substances 0.000 description 1
- 229910000392 octacalcium phosphate Inorganic materials 0.000 description 1
- 235000019629 palatability Nutrition 0.000 description 1
- XYJRXVWERLGGKC-UHFFFAOYSA-D pentacalcium;hydroxide;triphosphate Chemical compound [OH-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O XYJRXVWERLGGKC-UHFFFAOYSA-D 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 239000012047 saturated solution Substances 0.000 description 1
- NESLWCLHZZISNB-UHFFFAOYSA-M sodium phenolate Chemical compound [Na+].[O-]C1=CC=CC=C1 NESLWCLHZZISNB-UHFFFAOYSA-M 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- YIGWVOWKHUSYER-UHFFFAOYSA-F tetracalcium;hydrogen phosphate;diphosphate Chemical compound [Ca+2].[Ca+2].[Ca+2].[Ca+2].OP([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O YIGWVOWKHUSYER-UHFFFAOYSA-F 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B7/00—Fertilisers based essentially on alkali or ammonium orthophosphates
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/10—Solid or semi-solid fertilisers, e.g. powders
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/20—Liquid fertilisers
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Pest Control & Pesticides (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Mechanical Engineering (AREA)
- Fertilizers (AREA)
Abstract
本发明公开了一种猪粪生物处理工艺及利用方法,属于粪便处理领域。本发明的处理方法包括以下步骤:将猪粪放入粪便处理池,经过杂物格栅滤去大块杂物后进入粪便集中池中沉淀杂质,从储存罐加入重量为猪粪重量0.1‑0.4%的复合菌剂、猪粪重量2‑4%的改性剂和猪粪重量6‑11%的外加剂,打开搅拌器搅拌2‑5h混合均匀,然后在25‑29℃下发酵48‑72h,保持发酵物的含水量在50‑70%,每12h对发酵物搅拌30‑60min;再在28‑35℃下发酵60‑96h,发酵过的猪粪进入净化池,去除有害物质之后进入固液分离机,液体肥通过液体肥输送管进入液体肥收集池,得到液体、固体发酵猪粪肥料。本发明的猪粪处理工艺,可以大大减少养殖场所产生的污染,并结合固液两肥的运用使得猪粪可以得到循环利用,符合环保发展的理念。
The invention discloses a pig manure biological treatment process and a utilization method, and belongs to the field of manure treatment. The treatment method of the present invention comprises the following steps: put the pig manure into the manure treatment tank, filter out the large debris through the sundry grille, and then enter the manure concentration tank to precipitate impurities, and add the pig manure from the storage tank in a weight of 0.1-0.4 of the weight of the pig manure. % of the compound bacterial agent, 2-4% of the pig manure weight modifier and 6-11% of the pig manure weight of the admixture, turn on the stirrer and stir for 2-5h to mix well, then ferment at 25-29°C for 48-72h , keep the water content of the fermented product at 50-70%, stir the fermented product for 30-60min every 12h; then ferment it at 28-35 ℃ for 60-96h, the fermented pig manure enters the purification tank, removes harmful substances and enters the solid state Liquid separator, the liquid fertilizer enters the liquid fertilizer collection tank through the liquid fertilizer conveying pipe, and obtains liquid and solid fermented pig manure fertilizer. The pig manure treatment process of the invention can greatly reduce the pollution generated by the breeding site, and combined with the application of solid-liquid two fertilizers, the pig manure can be recycled, which conforms to the concept of environmental protection development.
Description
技术领域technical field
本发明涉及粪便处理领域,特别是涉及一种猪粪生物处理工艺及利用方法。The invention relates to the field of manure treatment, in particular to a pig manure biological treatment process and a utilization method.
背景技术Background technique
近年来我国规模化、集约化畜禽养殖业蓬勃发展,现代化封闭型的规模化养殖技术促进了我国城市的畜禽养殖业向优质高效发展,随之而来的畜禽养殖粪便排放量也呈现逐年增加趋势,给地区造成了严重的土壤、水源和空气等环境污染污染。In recent years, my country's large-scale and intensive livestock and poultry breeding industry has developed vigorously. The modern closed-type large-scale breeding technology has promoted the high-quality and efficient development of the livestock and poultry breeding industry in my country's cities. The trend of increasing year by year has caused serious environmental pollution such as soil, water and air pollution to the region.
黑水虻,腐生性的水虻科昆虫,能够取食禽畜粪便和生活垃圾,生产高价值的动物蛋白饲料,因其繁殖迅速,生物量大,食性广泛、吸收转化率高,容易管理、饲养成本低,动物适口性好等特点,从而进行资源化利用,其幼虫被称为“凤凰虫”,成为与蝇蛆、黄粉虫、大麦虫等齐名的资源昆虫,在全世界范围内得到推广。Black soldier flies, saprophytic soldier flies, can feed on livestock manure and domestic waste to produce high-value animal protein feed. Because of its rapid reproduction, large biomass, wide food habit, high absorption and transformation rate, it is easy to manage, It has the characteristics of low feeding cost and good animal palatability, so it can be used for resource utilization. Its larvae are called "Phoenix worms", which have become as famous resource insects as fly maggots, Tenebrio molitors, barley worms, etc., and are popularized all over the world. .
饲养猪只的食量大、粪尿多,粪尿污水浓度高。一个存栏6000头的猪场,每天消耗饲料约12吨,约产生猪粪12吨、猪尿19吨、污水约70吨~150吨,排放量很大。一个万头猪场的排污量相当于2.5万人的排污量。此外,猪粪尿污水cod浓度很高,猪粪约为21000mg/l,猪尿约为18000mg/l,污水约为12000mg/l。许多政府主管部门和养猪户对养猪场粪尿污水排放量之大和污染之严重缺乏足够的认识,以致只管养猪不管排污,先污染后治理,这对环境的污染可想而知。同时,猪粪处理技术一直是粪便处理的大难题。而新型资源型昆虫黑水虻,通过生物处理法处理猪粪,是最为理想的处理方式。Feeding pigs has a large amount of food, a lot of feces and urine, and the concentration of feces and urine is high. A pig farm with 6,000 pigs consumes about 12 tons of feed every day, produces about 12 tons of pig manure, 19 tons of pig urine, and about 70 to 150 tons of sewage. The amount of sewage discharged from a 10,000-head pig farm is equivalent to that of 25,000 people. In addition, the cod concentration of pig manure and urine sewage is very high, pig manure is about 21000mg/l, pig urine is about 18000mg/l, and sewage is about 12000mg/l. Many government departments and pig farmers lack sufficient understanding of the large amount of manure, urine and sewage from pig farms and the seriousness of pollution. As a result, they only focus on raising pigs regardless of sewage discharge, and treat pollution first. The pollution to the environment can be imagined. At the same time, pig manure treatment technology has always been a big problem in manure treatment. For the new resource-type insect black soldier flies, biological treatment of pig manure is the most ideal treatment method.
发明内容SUMMARY OF THE INVENTION
本发明目的在于提供一种猪粪生物处理工艺及利用方法,以解决现有技术存在的猪粪无法得到充分处理的技术问题。The purpose of the present invention is to provide a pig manure biological treatment process and utilization method, so as to solve the technical problem that pig manure cannot be fully treated in the prior art.
为此,本发明提出以下方案:For this reason, the present invention proposes the following scheme:
一种猪粪生物处理工艺,包括以下步骤:S1:将猪粪放入粪便处理池,猪粪先经过杂物格栅滤去大块杂物,然后进入粪便集中池中进一步沉淀杂质,当发酵池满时从储存罐加入重量为猪粪重量0.1-0.4%的复合菌剂、猪粪重量2-4%的改性剂和猪粪重量6-11%的外加剂,打开搅拌器搅拌2-5h混合均匀,然后在25-29℃下发酵48-72h,保持发酵物的含水量在50-70%,每12h对发酵物搅拌30-60min;提高温度,在28-35℃下发酵60-96h,发酵过的猪粪进入净化池,去除有害物质之后进入固液分离机,液体肥通过液体肥输送管进入液体肥收集池,得到液体、固体发酵猪粪肥料;A pig manure biological treatment process includes the following steps: S1: put the pig manure into a manure treatment tank, the pig manure first passes through a sundries grid to filter out large debris, and then enters the excrement concentration tank to further precipitate impurities, when the fermentation tank is used. When it is full, add the compound bacterial agent with the weight of 0.1-0.4% of the weight of pig manure, the modifier of 2-4% of the weight of pig manure and the admixture of 6-11% of the weight of pig manure from the storage tank, turn on the mixer and stir for 2-5h Mix well, then ferment at 25-29°C for 48-72h, keep the water content of the fermented product at 50-70%, and stir the fermented product for 30-60min every 12h; increase the temperature and ferment at 28-35°C for 60-96h The fermented pig manure enters the purification tank, removes harmful substances and enters the solid-liquid separator, and the liquid fertilizer enters the liquid fertilizer collection tank through the liquid fertilizer conveying pipe to obtain liquid and solid fermented pig manure fertilizer;
所述粪便处理池由杂物格栅、粪便集中池、发酵池、净化池、液体肥收集池、储存罐、搅拌器、固液分离机、液体肥输送管组成;其中,杂物格栅与粪便集中池连接;粪便集中池与发酵池连接,发酵池顶部设置有储存罐,发酵池内部有搅拌器,发酵池与净化池连接;净化池与固液分离机连接,固液分离机通过液体肥输送管与液体肥收集池连接。The manure treatment tank is composed of a sundries grill, a manure concentration pool, a fermentation pool, a purification pool, a liquid fertilizer collection pool, a storage tank, a mixer, a solid-liquid separator, and a liquid fertilizer conveying pipe; The excrement concentration tank is connected; the excrement concentration tank is connected with the fermentation tank, a storage tank is arranged on the top of the fermentation tank, there is a stirrer inside the fermentation tank, and the fermentation tank is connected with the purification tank; the purification tank is connected with the solid-liquid separator, and the solid-liquid separator passes through the liquid The fertilizer conveying pipe is connected with the liquid fertilizer collecting tank.
优选地,所述步骤S1中,加入重量为猪粪重量0.36%的复合菌剂混合。Preferably, in the step S1, a composite bacterial agent with a weight of 0.36% by weight of pig manure is added and mixed.
优选地,所述步骤S1中,拌匀后在27℃下发酵62h,保持发酵物的含水量在63%。Preferably, in the step S1, after mixing well, the fermentation is carried out at 27° C. for 62 hours, and the water content of the fermented product is kept at 63%.
优选地,所述复合菌剂由嗜热脂肪芽孢杆菌、黄链霉菌、沟诺卡氏菌、枯草芽孢杆菌按质量比3.1-4.0∶1.4-1.9∶0.7-1.6∶1.1-2.0的混合而得。Preferably, the compound bacterial agent is obtained by mixing Bacillus stearothermophilus, Streptomyces flavus, Nocardia dulcis and Bacillus subtilis in a mass ratio of 3.1-4.0:1.4-1.9:0.7-1.6:1.1-2.0 .
优选地,所述复合菌剂由嗜热脂肪芽孢杆菌、黄链霉菌、沟诺卡氏菌、枯草芽孢杆菌按质量比3.6∶1.7∶1.2∶1.6的混合而得。Preferably, the compound bacterial agent is obtained by mixing Bacillus stearothermophilus, Streptomyces flavus, Nocardia dulcis and Bacillus subtilis in a mass ratio of 3.6:1.7:1.2:1.6.
优选地,所述复合菌剂中有效活菌数7.0-11.0亿/g。Preferably, the number of effective viable bacteria in the composite bacterial agent is 700-1.10 billion/g.
优选地,所述改性剂以重量份为单位,包括以下组分:磷酸一钾24-37份、2-甲基-2-丙烯酸-18-19份、2-氯-6-三氯甲基吡啶5-8份、复硝酚钠1-4份、纤维素羟乙基醚2-5份。Preferably, the modifier is in parts by weight, and includes the following components: 24-37 parts of monopotassium phosphate, 18-19 parts of 2-methyl-2-acrylic acid, 2-chloro-6-trichloromethane 5-8 parts of pyridine, 1-4 parts of sodium nitrophenolate, 2-5 parts of cellulose hydroxyethyl ether.
优选地,所述改性剂以重量份为单位,包括以下组分:磷酸一钾28份、2-甲基-2-丙烯酸-114份、2-氯-6-三氯甲基吡啶6份、复硝酚钠3份、纤维素羟乙基醚3份。Preferably, the modifier is in parts by weight and includes the following components: 28 parts of monopotassium phosphate, 114 parts of 2-methyl-2-acrylic acid-114 parts, and 6 parts of 2-chloro-6-trichloromethylpyridine , 3 parts of sodium nitrophenolate, 3 parts of cellulose hydroxyethyl ether.
优选地,所述外加剂以重量份为单位,包括以下组分:尿素18-30份、氯化钾38-62份、除臭剂7-10份。Preferably, the admixture is in parts by weight and includes the following components: 18-30 parts of urea, 38-62 parts of potassium chloride, and 7-10 parts of deodorant.
一种猪粪利用方法,其特征在于,所述猪粪处理后在固体肥、液体肥的应用。A method for utilizing pig manure, characterized in that the pig manure is used in solid fertilizer and liquid fertilizer after being processed.
本发明与现有技术对比的有益效果包括:The beneficial effects of the present invention compared with the prior art include:
1.从表1数据中可以看到,添加完整组分的改性剂可以有效促进王草的生长,其中,在株高、平均单株重量、分蘖数上最优的实施例3分别比对比例4提高了26.0%、10.4%、49.3%,说明复硝酚钠、2-氯-6-三氯甲基吡啶和纤维素羟乙基醚起到了相应的协同作用,可以更好的促进王草的生长。1. As can be seen from the data in Table 1, the modifier adding the complete component can effectively promote the growth of King grass, wherein, the
2.本发明的猪粪处理工艺,可以大大减少养殖场所产生的污染,处理后得到的液体肥可还田种植作物,固体肥可养殖黑水虻,可再使用黑水虻做成饲料饲养生猪,以达到循环经济的目的。2. The pig manure treatment process of the present invention can greatly reduce the pollution produced by the breeding site, the liquid fertilizer obtained after the treatment can be returned to the field for planting crops, the solid fertilizer can be used to breed black soldier flies, and the black soldier flies can be used to make feed for raising live pigs. , in order to achieve the purpose of circular economy.
3.本发明的粪便处理池结构设计合理,适合推广应用到各地养殖场,使养殖户在减少养殖场维护成本的同时获得更高的经济效益。3. The manure treatment tank of the present invention has a reasonable structure design and is suitable for promotion and application to various farms, so that farmers can obtain higher economic benefits while reducing the maintenance cost of the farm.
附图说明Description of drawings
图1为本发明粪便处理池的结构示意图;Fig. 1 is the structural representation of the feces treatment tank of the present invention;
图2为本发明猪粪生物处理后利用方法示意图。Fig. 2 is a schematic diagram of the utilization method of pig manure after biological treatment of the present invention.
其中,1为杂物格栅、2为粪便集中池、3为发酵池、4为净化池、5为液体肥收集池、6为储存罐、7为搅拌器、8为固液分离机、9为液体肥输送管。Among them, 1 is the sundries grid, 2 is the excrement concentration pool, 3 is the fermentation pool, 4 is the purification pool, 5 is the liquid fertilizer collection pool, 6 is the storage tank, 7 is the mixer, 8 is the solid-liquid separator, 9 is the Conveying pipe for liquid fertilizer.
具体实施方式Detailed ways
下面结合具体实施方式对本发明作进一步详细说明。应该强调的是,下述说明仅仅是示例性的,而不是为了限制本发明的范围及其应用。The present invention will be further described in detail below in conjunction with specific embodiments. It should be emphasized that the following description is exemplary only, and is not intended to limit the scope of the invention and its application.
实施例1Example 1
一种猪粪生物处理工艺,包括以下步骤:A pig manure biological treatment process, comprising the following steps:
S1:将猪粪放入粪便处理池,猪粪先经过杂物格栅1滤去大块杂物,然后进入粪便集中池2中进一步沉淀杂质,当发酵池3满时从储存罐6加入重量为猪粪重量0.1%的复合菌剂、猪粪重量2%的改性剂和猪粪重量6%的外加剂,打开搅拌器7搅拌2h混合均匀,然后在25℃下发酵48h,保持发酵物的含水量在50%,每12h对发酵物搅拌30min;提高温度,在28℃下发酵60h,发酵过的猪粪进入净化池4,去除有害物质之后进入固液分离机8,液体肥通过液体肥输送管9进入液体肥收集池5,得到液体、固体发酵猪粪肥料;S1: Put the pig manure into the manure treatment tank. The pig manure first filters out the large debris through the
所述粪便处理池由杂物格栅1、粪便集中池2、发酵池3、净化池4、液体肥收集池5、储存罐6、搅拌器7、固液分离机8、液体肥输送管9组成;其中,杂物格栅1与粪便集中池2连接;粪便集中池2与发酵池3连接,发酵池3顶部设置有储存罐6,发酵池3内部有搅拌器7,发酵池3与净化池4连接;净化池4与固液分离机8连接,固液分离机8通过液体肥输送管9与液体肥收集池5连接。The manure treatment tank is composed of a
所述复合菌剂由嗜热脂肪芽孢杆菌、黄链霉菌、沟诺卡氏菌、枯草芽孢杆菌按质量比3.1∶1.4∶0.7∶1.1的混合而得。The compound bacterial agent is obtained by mixing Bacillus stearothermophilus, Streptomyces flavus, Nocardia dulcis and Bacillus subtilis in a mass ratio of 3.1:1.4:0.7:1.1.
所述复合菌剂中有效活菌数7.0亿/g。The number of effective viable bacteria in the compound bacterial agent is 700 million/g.
所述外加剂以重量份为单位,包括以下组分:尿素18份、氯化钾38份、除臭剂7份。The admixture is in parts by weight and includes the following components: 18 parts of urea, 38 parts of potassium chloride, and 7 parts of deodorant.
所述改性剂以重量份为单位,包括以下组分:磷酸一钾24-37份、2-甲基-2-丙烯酸-18份、2-氯-6-三氯甲基吡啶5份、复硝酚钠1份、纤维素羟乙基醚2份。The modifier is in parts by weight and includes the following components: 24-37 parts of monopotassium phosphate, 18 parts of 2-methyl-2-acrylic acid-18 parts, 5 parts of 2-chloro-6-trichloromethylpyridine, 1 part of sodium nitrophenolate, 2 parts of cellulose hydroxyethyl ether.
实施例2Example 2
一种猪粪生物处理工艺,包括以下步骤:A pig manure biological treatment process, comprising the following steps:
S1:将猪粪放入粪便处理池,猪粪先经过杂物格栅1滤去大块杂物,然后进入粪便集中池2中进一步沉淀杂质,当发酵池3满时从储存罐6加入重量为猪粪重量0.4%的复合菌剂、猪粪重量4%的改性剂和猪粪重量11%的外加剂,打开搅拌器7搅拌5h混合均匀,然后在29℃下发酵72h,保持发酵物的含水量在70%,每12h对发酵物搅拌60min;提高温度,在35℃下发酵96h,发酵过的猪粪进入净化池4,去除有害物质之后进入固液分离机8,液体肥通过液体肥输送管9进入液体肥收集池5,得到液体、固体发酵猪粪肥料;S1: Put the pig manure into the manure treatment tank. The pig manure first filters out the large debris through the
所述粪便处理池由杂物格栅1、粪便集中池2、发酵池3、净化池4、液体肥收集池5、储存罐6、搅拌器7、固液分离机8、液体肥输送管9组成;其中,杂物格栅1与粪便集中池2连接;粪便集中池2与发酵池3连接,发酵池3顶部设置有储存罐6,发酵池3内部有搅拌器7,发酵池3与净化池4连接;净化池4与固液分离机8连接,固液分离机8通过液体肥输送管9与液体肥收集池5连接。The manure treatment tank is composed of a
所述复合菌剂由嗜热脂肪芽孢杆菌、黄链霉菌、沟诺卡氏菌、枯草芽孢杆菌按质量比4.0∶1.9∶1.6∶2.0的混合而得。The compound bacterial agent is obtained by mixing Bacillus stearothermophilus, Streptomyces flavus, Nocardia groin and Bacillus subtilis in a mass ratio of 4.0:1.9:1.6:2.0.
所述复合菌剂中有效活菌数11.0亿/g。The number of effective viable bacteria in the compound bacterial agent was 1.10 billion/g.
所述改性剂以重量份为单位,包括以下组分:磷酸一钾37份、2-甲基-2-丙烯酸-119份、2-氯-6-三氯甲基吡啶8份、复硝酚钠4份、纤维素羟乙基醚5份。The modifier is in parts by weight and includes the following components: 37 parts of monopotassium phosphate, 119 parts of 2-methyl-2-acrylic acid-119 parts, 8 parts of 2-chloro-6-trichloromethylpyridine, 4 parts of sodium phenolate, 5 parts of cellulose hydroxyethyl ether.
所述外加剂以重量份为单位,包括以下组分:尿素30份、氯化钾62份、除臭剂10份。The admixture is in parts by weight and includes the following components: 30 parts of urea, 62 parts of potassium chloride, and 10 parts of deodorant.
实施例3Example 3
一种猪粪生物处理工艺,包括以下步骤:A pig manure biological treatment process, comprising the following steps:
S1:将猪粪放入粪便处理池,猪粪先经过杂物格栅1滤去大块杂物,然后进入粪便集中池2中进一步沉淀杂质,当发酵池3满时从储存罐6加入重量为猪粪重量0.36%的复合菌剂、猪粪重量3.2%的改性剂和猪粪重量8%的外加剂,打开搅拌器7搅拌3h混合均匀,然后在27℃下发酵62h,保持发酵物的含水量在63%,每12h对发酵物搅拌45min;提高温度,在33℃下发酵72h,发酵过的猪粪进入净化池4,去除有害物质之后进入固液分离机8,液体肥通过液体肥输送管9进入液体肥收集池5,得到液体、固体发酵猪粪肥料;S1: Put the pig manure into the manure treatment tank. The pig manure first filters out the large debris through the
所述粪便处理池由杂物格栅1、粪便集中池2、发酵池3、净化池4、液体肥收集池5、储存罐6、搅拌器7、固液分离机8、液体肥输送管9组成;其中,杂物格栅1与粪便集中池2连接;粪便集中池2与发酵池3连接,发酵池3顶部设置有储存罐6,发酵池3内部有搅拌器7,发酵池3与净化池4连接;净化池4与固液分离机8连接,固液分离机8通过液体肥输送管9与液体肥收集池5连接。The manure treatment tank is composed of a
所述复合菌剂由嗜热脂肪芽孢杆菌、黄链霉菌、沟诺卡氏菌、枯草芽孢杆菌按质量比3.6∶1.7∶1.2∶1.6的混合而得。The compound bacterial agent is obtained by mixing Bacillus stearothermophilus, Streptomyces flavus, Nocardia groin and Bacillus subtilis in a mass ratio of 3.6:1.7:1.2:1.6.
所述复合菌剂中有效活菌数9.0亿/g。The number of effective viable bacteria in the composite bacterial agent was 900 million/g.
优选地,所述改性剂以重量份为单位,包括以下组分:磷酸一钾28份、2-甲基-2-丙烯酸-114份、2-氯-6-三氯甲基吡啶6份、复硝酚钠3份、纤维素羟乙基醚3份。Preferably, the modifier is in parts by weight and includes the following components: 28 parts of monopotassium phosphate, 114 parts of 2-methyl-2-acrylic acid-114 parts, and 6 parts of 2-chloro-6-trichloromethylpyridine , 3 parts of sodium nitrophenolate, 3 parts of cellulose hydroxyethyl ether.
所述外加剂以重量份为单位,包括以下组分:尿素25份、氯化钾51份、除臭剂9份。The admixture is in parts by weight and includes the following components: 25 parts of urea, 51 parts of potassium chloride, and 9 parts of deodorant.
对比例1Comparative Example 1
猪粪生物处理工艺与实施例3基本相同,唯有不同的是改性剂中未加入2-氯-6-三氯甲基吡啶。The pig manure biological treatment process is basically the same as that of Example 3, except that 2-chloro-6-trichloromethylpyridine is not added to the modifier.
对比例2Comparative Example 2
猪粪生物处理工艺与实施例3基本相同,唯有不同的是改性剂中未加入复硝酚钠。The pig manure biological treatment process is basically the same as that of Example 3, except that sodium nitrophenolate is not added to the modifier.
对比例3Comparative Example 3
猪粪生物处理工艺与实施例3基本相同,唯有不同的是改性剂中未加入纤维素羟乙基醚。The biological treatment process of pig manure is basically the same as that of Example 3, the only difference is that cellulose hydroxyethyl ether is not added to the modifier.
对比例4Comparative Example 4
猪粪生物处理工艺与实施例3基本相同,唯有不同的是改性剂中未加入2-氯-6-三氯甲基吡啶、复硝酚钠、纤维素羟乙基醚。The pig manure biological treatment process is basically the same as that in Example 3, except that 2-chloro-6-trichloromethylpyridine, sodium nitrophenolate and cellulose hydroxyethyl ether are not added to the modifier.
将王草种植地平均分成7组,每组0.5亩,分别使用实施例1-3、对比例1-4所处理的猪粪液体肥进行浇灌,从2018年4月至2019年4月进行为期一年的种植,其中,每组每15天浇灌一次,每次按250kg/亩的量施用。每组王草在定植3个月后进行第一次刈割,留茬5cm,第一次刈割之后每隔45天进行刈割,到2019年4月份结束,共刈割7次。2019年4月25日从每组随机选20株进行测量,分蘖数为全年的总和,株高为全年的平均值,平均单株重为全年的平均值。具体数据如表1所示。The king grass planting land is divided into 7 groups on average, and each group is 0.5 mu, and the pig manure liquid fertilizers processed by Example 1-3 and Comparative Example 1-4 are used for watering, and the period from April 2018 to April 2019 is carried out for a period of time. One year of planting, in which, each group was irrigated once every 15 days, and the amount of 250kg/mu was applied each time. Each group of king grass was mowed for the first time after 3 months of planting, leaving a stubble of 5 cm. After the first mow, it was mowed every 45 days. By the end of April 2019, a total of 7 times were mowed. On April 25, 2019, 20 plants were randomly selected from each group for measurement. The number of tillers was the total of the whole year, the plant height was the average of the whole year, and the average weight per plant was the average of the whole year. The specific data are shown in Table 1.
表1王草1年种植情况Table 1 Planting situation of king grass in 1 year
从表1数据中可以看到,添加完整组分的改性剂可以有效促进王草的生长,其中,在株高、平均单株重量、分蘖数上最优的实施例3分别比对比例4提高了26.0%、10.4%、49.3%,可见在猪粪处理工艺中,2-氯-6-三氯甲基吡啶、复硝酚钠、纤维素羟乙基醚对王草的生长起到重要的促进作用,这可能是:From the data in Table 1, it can be seen that the modifier adding complete components can effectively promote the growth of king grass. Among them, the best example 3 in terms of plant height, average weight per plant and number of tillers is compared with comparative example 4. The increase of 26.0%, 10.4% and 49.3% shows that in the pig manure treatment process, 2-chloro-6-trichloromethylpyridine, sodium nitrophenolate and cellulose hydroxyethyl ether play an important role in the growth of king grass facilitation, which may be:
在添加改性剂所含的复硝酚钠、2-氯-6-三氯甲基吡啶和纤维素羟乙基醚中;复硝酚钠具有促进细胞原生质流动、加速植株生长发育和增强抗逆的能力,并可以解除在多元微量元素肥料中个元之间的拮抗作用,提高植物的吸收率;可促进植物生产更多ATP能量子,促进植物ATP的合成,增强植物对2-氯-6-三氯甲基吡啶的吸收;2-氯-6-三氯甲基吡啶,其作用在于抑制土壤中亚硝化细菌活动,从而抑制土壤中铵态氮的硝化作用,使施入土壤中的铵态氮肥能较长时间地以铵根离子的形式被胶体吸附,防止硝态氮的淋失和反硝化作用,减少氮素非生产性损失,起到提高王草对N的吸收率的作用,N的含量增大则会影响王草对复硝酚钠的吸收;纤维素羟乙基醚是一种天然高分子,每一个纤维基环上含有三个羟基基团,在施肥处,其微域土壤范围内饱和溶液的pH可达1-1.5,纤维素羟乙基醚中的羟基和土壤中的Ca离子与磷酸根离子作用,生成磷酸二钙和磷酸八钙,最后大部分形成稳定的羟基磷灰石,对土壤pH的稳定起到极大的作用,从而使得土壤中的复硝酚钠稳定性得到加强。以上说明复硝酚钠、2-氯-6-三氯甲基吡啶和纤维素羟乙基醚起到了相应的协同作用,可以更好的促进王草的生长。In the sodium nitrophenolate, 2-chloro-6-trichloromethylpyridine and cellulose hydroxyethyl ether contained in the additive modifier; sodium nitrophenolate can promote the flow of cell protoplasm, accelerate the growth and development of plants and enhance the It can also relieve the antagonism between the elements in the multi-trace element fertilizer and improve the absorption rate of plants; it can promote the production of more ATP energy by the plants, promote the synthesis of The absorption of 6-trichloromethylpyridine; 2-chloro-6-trichloromethylpyridine, its function is to inhibit the activity of nitrosating bacteria in the soil, thereby inhibiting the nitrification of ammonium nitrogen in the soil, and making the ammonium nitrogen applied in the soil. Ammonium nitrogen fertilizer can be adsorbed by colloid in the form of ammonium ion for a long time, preventing the leaching and denitrification of nitrate nitrogen, reducing the non-productive loss of nitrogen, and improving the absorption rate of king grass to N , the increase of N content will affect the absorption of sodium nitrophenolate by king grass; cellulose hydroxyethyl ether is a natural polymer, and each fiber base ring contains three hydroxyl groups. The pH of the saturated solution in the micro-domain soil range can reach 1-1.5. The hydroxyl groups in cellulose hydroxyethyl ether and the Ca ions in the soil interact with phosphate ions to generate dicalcium phosphate and octacalcium phosphate, and finally most of them are stable. The hydroxyapatite has a great effect on the stability of soil pH, thereby enhancing the stability of sodium nitrophenolate in the soil. The above shows that sodium nitrophenolate, 2-chloro-6-trichloromethylpyridine and cellulose hydroxyethyl ether play a corresponding synergistic effect, which can better promote the growth of king grass.
以上内容是结合具体的实施方式对本发明所作的进一步详细说明,不能认定本发明的具体实施只局限于这些说明。对于本发明所属技术领域的普通技术人员来说,在不脱离本发明构思的前提下,其还可以对这些已描述的实施例做出若干替代或变型,而这些替代或变型方式都应当视为属于本发明的保护范围。The above content is a further detailed description of the present invention in conjunction with specific embodiments, and it cannot be considered that the specific implementation of the present invention is limited to these descriptions. For those of ordinary skill in the technical field of the present invention, without departing from the concept of the present invention, they can also make several substitutions or modifications to the described embodiments, and these substitutions or modifications should be regarded as It belongs to the protection scope of the present invention.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010670434.8A CN111875195A (en) | 2020-07-13 | 2020-07-13 | A kind of pig manure biological treatment process and utilization method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010670434.8A CN111875195A (en) | 2020-07-13 | 2020-07-13 | A kind of pig manure biological treatment process and utilization method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111875195A true CN111875195A (en) | 2020-11-03 |
Family
ID=73150897
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010670434.8A Pending CN111875195A (en) | 2020-07-13 | 2020-07-13 | A kind of pig manure biological treatment process and utilization method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111875195A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113087550A (en) * | 2021-04-16 | 2021-07-09 | 菏泽学院 | Equipment for preparing plant liquid fertilizer by deep treatment of cow dung and using method thereof |
| ES2933285A1 (en) * | 2021-08-03 | 2023-02-03 | Sanchez Victor Manuel Marchena | Biological purification procedure for liquid waste with a high polluting load and/or high toxicity, especially slurry and vegetable water in the containment pond itself (Machine-translation by Google Translate, not legally binding) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1980001922A1 (en) * | 1979-03-14 | 1980-09-18 | Saf Soc Agricole Fonciere | Process for treating manures |
| JP2002003286A (en) * | 2000-06-20 | 2002-01-09 | Takashi Hirai | Method and system for producing fermentated fertilizer method |
| CN104496567A (en) * | 2014-12-17 | 2015-04-08 | 山东翔露农牧科技有限公司 | System and method for producing biogas manure from pig excrement and urine as chemical fertilizer |
| CN106316485A (en) * | 2016-08-20 | 2017-01-11 | 裕龙农牧科技股份有限公司 | New method for harmless treatment of livestock feces |
| CN107117786A (en) * | 2017-06-29 | 2017-09-01 | 重庆市万源禽蛋食品有限公司 | Plant's dejecta treatment method and system |
| CN107857451A (en) * | 2017-12-20 | 2018-03-30 | 山东绿福地生物科技有限公司 | A kind of technique for producing biogas using livestock and poultry solid manure |
| CN110436988A (en) * | 2019-06-27 | 2019-11-12 | 广西壮族自治区林业科学研究院 | A kind of bacteria fermentation type high phosphorus masson pine fertilizer, preparation method and its application method |
-
2020
- 2020-07-13 CN CN202010670434.8A patent/CN111875195A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1980001922A1 (en) * | 1979-03-14 | 1980-09-18 | Saf Soc Agricole Fonciere | Process for treating manures |
| JP2002003286A (en) * | 2000-06-20 | 2002-01-09 | Takashi Hirai | Method and system for producing fermentated fertilizer method |
| CN104496567A (en) * | 2014-12-17 | 2015-04-08 | 山东翔露农牧科技有限公司 | System and method for producing biogas manure from pig excrement and urine as chemical fertilizer |
| CN106316485A (en) * | 2016-08-20 | 2017-01-11 | 裕龙农牧科技股份有限公司 | New method for harmless treatment of livestock feces |
| CN107117786A (en) * | 2017-06-29 | 2017-09-01 | 重庆市万源禽蛋食品有限公司 | Plant's dejecta treatment method and system |
| CN107857451A (en) * | 2017-12-20 | 2018-03-30 | 山东绿福地生物科技有限公司 | A kind of technique for producing biogas using livestock and poultry solid manure |
| CN110436988A (en) * | 2019-06-27 | 2019-11-12 | 广西壮族自治区林业科学研究院 | A kind of bacteria fermentation type high phosphorus masson pine fertilizer, preparation method and its application method |
Non-Patent Citations (2)
| Title |
|---|
| 孙淑东: "猪场粪便环保处理方案", 《中国畜禽种业》 * |
| 毛小云主编: "《废弃物农用功能化理论与技术》", 31 July 2017, 华南理工大学出版社 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113087550A (en) * | 2021-04-16 | 2021-07-09 | 菏泽学院 | Equipment for preparing plant liquid fertilizer by deep treatment of cow dung and using method thereof |
| ES2933285A1 (en) * | 2021-08-03 | 2023-02-03 | Sanchez Victor Manuel Marchena | Biological purification procedure for liquid waste with a high polluting load and/or high toxicity, especially slurry and vegetable water in the containment pond itself (Machine-translation by Google Translate, not legally binding) |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1830917B (en) | Method. for preparing quick-acting compound organic fertilizer | |
| CN103274774B (en) | A high-efficiency biological liquid fertilizer using livestock and poultry manure as raw material and its preparation method | |
| CN106986720A (en) | The method for producing soil conditioner using the waste residue for handling livestock breeding wastewater generation | |
| CN101486609A (en) | Ecological organic fertilizer containing organic, inorganic and beneficial microorganism | |
| CN101811776B (en) | Method for processing aquaculture wastewater containing antibiotics by utilizing plant floating bed | |
| CN106106372A (en) | A kind of solid waste biologic treating technique based on vermiculture | |
| CN106754461A (en) | A kind of biological flocculation and its preparation method and application | |
| CN106946630A (en) | A kind of organic fungi-manure using sludge as raw material and preparation method thereof | |
| CN107384426A (en) | A kind of renovation agent of cation heavy-metal contaminated soil and preparation method thereof | |
| CN101531436A (en) | Treatment method of wastewater anaerobic digestive fluid in pig farm | |
| CN104365490B (en) | Pigsty cleaning-free and flushing-free method | |
| CN115806449A (en) | Full resource utilization method of livestock and poultry manure | |
| KR101156650B1 (en) | Manufacturing method of liquid manure using humic acid | |
| CN102100215A (en) | Integrated ecological breeding method comprising livestock waste composting, earthworm raising and poultry raising | |
| JP2018030777A (en) | Process for producing fully fertilizer with high humic acid content | |
| CN106947490A (en) | Soil conditioner and preparation method thereof | |
| CN109133516A (en) | A kind of breeding wastewater resource utilization utilizes method | |
| CN101274861B (en) | Heavy metal-passivated organic fertilizer and composting method | |
| CN111875195A (en) | A kind of pig manure biological treatment process and utilization method | |
| CN111072244A (en) | Comprehensive utilization method of large-scale dairy farm waste | |
| CN108794189A (en) | A kind of preparation method of NEW TYPE OF COMPOSITE bio-feritlizer | |
| CN116548360A (en) | Fish, lumbrous greenfeed and rice coupling planting and breeding system and planting and breeding method | |
| CN104557227A (en) | Yield-increase organic fertilizer for improving soil | |
| CN108727098A (en) | Method for preparing fertilizer from swine breeding wastewater | |
| CN107162699A (en) | A kind of special concentration organic Fertilizer water paste of biogas slurry of aquaculture and preparation method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20201103 |