CN102976806A - Kiln fermentation process for producing bio-organic fertilize - Google Patents
Kiln fermentation process for producing bio-organic fertilize Download PDFInfo
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- CN102976806A CN102976806A CN2012104849742A CN201210484974A CN102976806A CN 102976806 A CN102976806 A CN 102976806A CN 2012104849742 A CN2012104849742 A CN 2012104849742A CN 201210484974 A CN201210484974 A CN 201210484974A CN 102976806 A CN102976806 A CN 102976806A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
The invention discloses a kiln fermentation process for producing a bio-organic fertilizer, comprising the following steps of: mixing animal manure, ground organic wastes, lignite and complex biological strains uniformly according to a proportion; adding the materials into a fermentation pool, and carrying out fully-enclosed anaerobic fermentation for 8-13 days after the fermentation pool is filled with the materials; after the temperature of the materials increases to 60-70 DEG C, ventilating the fermentation pool; after the temperature of the materials exceeds 70 DEG C, opening the discharge gate to move the materials out of the fermentation pool, carrying out the oxygen consumption fermentation for 2 days, and airing to obtain the bio-organic fertilizer which can be used. To overcome the defects of low putrescibility and long fermentation time of the existing stacking and opening type fermentation modes, the invention adopts the fully-enclosed kiln fermentation process. Due to the adoption of fully-enclosed kiln fermentation process, the putrescibility of the organic materials can be improved to be more than 90%, and the fermentation time can be shortened to 10-15 days, the fertility of the fertilizer can be improved, the time cost and the raw material loss can be reduced, and the wide application of the bio-organic fertilizer to agricultural production can be guaranteed significantly.
Description
Technical field
The present invention relates to the agricultural fertilizer field, be specifically related to the kiln formula zymotechnique that a kind of biological organic fertilizer is produced.
Background technology
Biological organic fertilizer refers to that microorganisms with specific functions and a class that mainly is composited through harmless treatment, the organic materials that becomes thoroughly decomposed for originating take plant and animal residues (such as feces of livestock and poultry, agricultural crop straw etc.) have the fertilizer of microbial fertilizer and fertilizer effect concurrently.Biological organic fertilizer has that nutritive element is complete, resistant to diseases and insects, the utilization that promotes chemical fertilizer that can improve soil, improve product quality, improve the rhizosphere microorganisms of crops group, improve plant, improve the characteristics such as chemical fertilizer utilization ratio and more and more be subject to people's attention.
The traditional biological fermentation technology for organic fertilizer mainly adopts pile formula and open type fermented technique at present, in the fermenting process, rapid heat dissipation, temperature is subjected to external influence large, and is uncontrollable a suitable scope, causes the organic rotten degree of biological organic fertilizer low, leavening temperature is crossed and low can't be killed the objectionable impuritiess such as intestinal bacteria in the fertilizer material, roundworm egg, the organic rotten degree of the biological organic fertilizer that dispatches from the factory is about about 70%, and fermentation time is also long, needs at least more than 20 days.
Summary of the invention
The present invention's " kiln formula zymotechnique that biological organic fertilizer is produced " is low for the organic rotten degree of traditional biological organic fertilizer production technique, yield poorly, the drawback that fermentation time is long, adopt totally enclosed ' kiln formula ' anaerobic ferment process, reduction time cost and material loss when promoting the fertility of fertilizer itself.For the large-scale production of biological organic fertilizer provides practicable production operation technique, promote biological organic fertilizer production to develop to qualitative leap.
Technical scheme of the present invention: feces of livestock and poultry, organic waste, brown coal, composite biological inoculum mixed in proportion knock down in the fermentation vat, after filling, fermentation materials carries out totally-enclosed anaerobically fermenting, through 8-13 days anaerobically fermentings, temperature of charge rises to 60 ℃-70 ℃, allow fermentation vat ventilate, when temperature of charge surpasses 70 ℃, material is shifted out fermentation vat, then carry out 2 days by a definite date oxygen consumption fermentation, after air-dry, just become spendable bio-organic fertilizer.
Further, described fermentation vat is that a kind of kiln formula can totally-enclosed anaerobically fermenting pond.
Further, described kiln formula fermenting tank structure comprises: three of fermentation vats are body of wall and the movable metope of one side, fermentation vat vault fixedly, is arranged on fermentation vat charging ventilation opening on the fermentation vat vault and the discharge port on the movable strong body of fermentation vat.
Further, described raw material weight per-cent is feces of livestock and poultry 30%-35%, organic waste 27%-35%, brown coal 30%-40%, composite biological inoculum 1%-2%.
Further, described raw material weight per-cent is feces of livestock and poultry 30%, organic waste 30%, brown coal 38.5%, composite biological inoculum 1.5%.
Further, described organic waste is husk, the stalk after pulverizing, a kind of or arbitrary combination of corn stalk.
Further, described composite biological inoculum is to be formed by subtilis, aspergillus niger, Phanerochaete chrysosporium, yeast saccharomyces cerevisiae, trichoderma pseudokiningii, white light gray streptomycete and biological enzyme balanced mix.
Further, described fermentation materials makes moisture account for the 40%-45% of weight percent by adding water.
Further, when described leavening temperature rises to 64 ℃-68 ℃, allow fermentation vat ventilate.
Technique effect of the present invention: " the kiln formula zymotechnique of biological organic fertilizer " solves the drawback that the organic rotten degree of traditional biological fertilizer technique is low, fermentation time is long; not only promote the fertility of fertilizer own; reduce simultaneously time cost and material loss; for the large-scale production of biological organic fertilizer provides practicable production operation technique, promote biological organic fertilizer production to develop to qualitative leap.
(1), the novel process organic rotten degree that makes biological organic fertilizer improves 20 percentage points from original 70%, reach more than 90%.
(2), the novel process leavening temperature namely can be raised to more than 70 ℃, kills harmful pathogenic agent such as intestinal bacteria, roundworm egg, is no more than again 80 ℃ simultaneously, guarantees the survival of biological probiotics.
(3), the novel process fermentation time reduces to 10-15 days from original more than 20 days, the raising of output is had obvious promoter action.
(4), novel process adopts top fed, without trampling, roll phenomenon, guarantees to ferment that matter is loose, fertilizer, biological organic fertilizer be effectively expanded.
(5), the charging ventilation opening of novel process fermentation vat vault, can seal and open according to fermentation is temperature required.
(6), novel process can carry out bio-organic fertilizer production according to demand in a large number, satisfies problem under-supply in the agriculture production.
Description of drawings
Fig. 1 is the used kiln formula fermenting tank structure figure of the present invention.
Shown in the accompanying drawing: 1, the fixing metope of three of fermentation vats, 2, fermentation vat charging ventilation opening, 3, the fermentation vat discharge port, 4, the fermentation vat vault.
Embodiment
For a better understanding of the present invention, be described further below in conjunction with accompanying drawing.
(1), organic waste, brown coal, composite biological inoculum after feces of livestock and poultry, the pulverizing are mixed by the weight of 300kg, 300kg, 385kg, 15kg, mix Hou Jiashui, make moisture content of material reach 40%, then from charging ventilation opening shown in Figure 13 material is knocked down the fermentation vat.
Organic waste is the mixture of stalk 90kg, husk 90kg and corn stalk 120kg; Each all is 2.14kg for the subtilis that comprises in the composite biological inoculum, aspergillus niger, Phanerochaete chrysosporium, yeast saccharomyces cerevisiae, trichoderma pseudokiningii, white light gray streptomycete and biological enzyme.
(2), material fills up fermentation vat rear enclosed charging ventilation opening and begins to carry out anaerobically fermenting, material was through fermentation in 8 days, the temperature required fermentation vat charging ventilation opening that passes through in the fermenting process is regulated, when the material internal temperature rises to 60 ℃, open charging ventilation opening 3, allow fermentation vat ventilate, when temperature surpasses 70 ℃, open the 4 beginning dischargings of discharge port gate.
(3), the consumption hair care ferment that the material that shifts out from fermentation vat carried out 2 days by a definite date can make the biological fermentation fertilizer of slaking rate more than 90%.
(4), after air-dry, just make the refined biometric fertilizer.
(1), organic waste, brown coal, composite biological inoculum after feces of livestock and poultry, the pulverizing are mixed by the weight of 330kg, 330kg, 330kg, 10kg, mix Hou Jiashui, make moisture content of material reach 43%, from charging ventilation opening shown in Figure 13 material is knocked down the fermentation vat.
Organic waste is the mixture of the corn stalk of the husk of 165kg and 165kg; Each all is 1.42kg for the subtilis that comprises in the composite biological inoculum, aspergillus niger, Phanerochaete chrysosporium, yeast saccharomyces cerevisiae, trichoderma pseudokiningii, white light gray streptomycete and biological enzyme.
(2), material fills up fermentation vat rear enclosed charging ventilation opening and begins to carry out anaerobically fermenting, material was through fermentation in 10 days, the temperature required fermentation vat charging ventilation opening that passes through in the fermenting process is regulated, when the material internal temperature rises to 65 ℃, open charging ventilation opening 3, allow fermentation vat ventilate, when the material internal temperature surpasses 70 ℃, open the 4 beginning dischargings of discharge port gate.
(3), the consumption hair care ferment that the material that shifts out from fermentation vat carried out 2 days by a definite date can make the biological fermentation material of slaking rate more than 90%.
(4), after air-dry, just make the refined biometric fertilizer.
(1), organic waste, brown coal, composite biological inoculum after feces of livestock and poultry, the pulverizing are mixed by the weight of 320kg, 300kg, 360kg, 20kg, mix Hou Jiashui, make moisture content of material reach 45%, knock down the fermentation vat from charging ventilation opening 3 shown in Figure 1.
Organic waste is the mixture of the corn stalk of the stalk of 150kg and 150kg, and each all is 2.86kg for the subtilis that comprises in the composite biological inoculum, aspergillus niger, Phanerochaete chrysosporium, yeast saccharomyces cerevisiae, trichoderma pseudokiningii, white light gray streptomycete and biological enzyme.
(2), material fills up fermentation vat rear enclosed charging ventilation opening and begins to carry out anaerobically fermenting, material was through fermentation in 13 days, the temperature required fermentation vat charging ventilation opening that passes through in the fermenting process is regulated, when the material internal temperature rises to 68 ℃, open charging ventilation opening 3, allow fermentation vat ventilate, when the material internal temperature surpasses 70 ℃, open the 4 beginning dischargings of discharge port gate.
(3), the consumption hair care ferment that the material that shifts out from fermentation vat carried out 2 days by a definite date can make the biological fermentation material of slaking rate more than 90%.
(4), after air-dry, just make the refined biometric fertilizer.
Employed subtilis, aspergillus niger, Phanerochaete chrysosporium, yeast saccharomyces cerevisiae, trichoderma pseudokiningii, white light gray streptomycete and biological enzyme in above-mentioned 3 embodiments, present in the decomposing agent product of Ministry of Agriculture's registration, the decomposing agent that bacterial classification quantity is maximum.Wherein subtilis is bacterium; Yeast saccharomyces cerevisiae is yeast; Aspergillus niger, trichoderma pseudokiningii are mould; Also contain simultaneously white light gray streptomycete and Phanerochaete chrysosporium, Phanerochaete chrysosporium is fungi, and white light gray streptomycete is actinomycetes; Aspergillus niger, trichoderma pseudokiningii, Phanerochaete chrysosporium can produce cellulase, Mierocrystalline cellulose in the decomposing and fermenting thing efficiently; Subtilis, yeast saccharomyces cerevisiae, white light gray streptomycete, aspergillus niger can produce hemicellulase, the hemicellulose in the decomposing and fermenting thing efficiently; Phanerochaete chrysosporium can produce lignoenzyme, and the xylogen in the decomposing and fermenting thing is conducive to the slaking of bio-organic fertilizer.
Claims (9)
1. the kiln formula zymotechnique produced of a biological organic fertilizer, it is characterized in that, may further comprise the steps: organic waste, brown coal, composite biological inoculum after feces of livestock and poultry, the pulverizing are knocked down in the fermentation vat after mixing in proportion, after filling, fermentation materials carries out totally-enclosed anaerobically fermenting, through 8-13 days anaerobically fermentings, when temperature of charge rises to 60 ℃-70 ℃, allow fermentation vat ventilate, when temperature of charge surpasses 70 ℃, material is shifted out fermentation vat, then carry out 2 days by a definite date oxygen consumption fermentation, after air-dry, become spendable bio-organic fertilizer.
2. the kiln formula zymotechnique produced of biological organic fertilizer according to claim 1, it is characterized in that: described fermentation vat is that a kind of kiln formula can totally-enclosed anaerobically fermenting pond.
3. the kiln formula zymotechnique produced of biological organic fertilizer according to claim 2, it is characterized in that: described kiln formula fermenting tank structure comprises: three of fermentation vats are body of wall and the movable metope of one side, fermentation vat vault fixedly, is arranged on fermentation vat charging ventilation opening on the fermentation vat vault and the discharge port on the movable strong body of fermentation vat.
4. the kiln formula zymotechnique produced of biological organic fertilizer according to claim 1, it is characterized in that: described raw material weight per-cent is feces of livestock and poultry 30%-35%, organic waste 27%-35%, brown coal 30%-40%, composite biological inoculum 1%-2%.
5. the kiln formula zymotechnique produced of biological organic fertilizer according to claim 4, it is characterized in that: described raw material weight per-cent is feces of livestock and poultry 30%, organic waste 30%, brown coal 38.5%, composite biological inoculum 1.5%.
6. the kiln formula zymotechnique produced of biological organic fertilizer according to claim 1 is characterized in that: described organic waste is husk, the stalk after pulverizing, a kind of or arbitrary combination of corn stalk.
7. the kiln formula zymotechnique produced of biological organic fertilizer according to claim 1, it is characterized in that: described composite biological inoculum is to be formed by subtilis, aspergillus niger, Phanerochaete chrysosporium, yeast saccharomyces cerevisiae, trichoderma pseudokiningii, white light gray streptomycete and biological enzyme balanced mix.
8. the kiln formula zymotechnique produced of biological organic fertilizer according to claim 1, it is characterized in that: described fermentation materials makes moisture account for the 40%-45% of total proportion by adding water.
9. the kiln formula zymotechnique of biological organic fertilizer production according to claim 1 is characterized in that: when described leavening temperature rises to 64 ℃-68 ℃, allow fermentation vat ventilate.
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| CN2012104849742A CN102976806A (en) | 2012-11-26 | 2012-11-26 | Kiln fermentation process for producing bio-organic fertilize |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857664A (en) * | 2017-12-28 | 2018-03-30 | 彭光简 | A kind of organic farm soils improvement microbial enzyme composite bacterial fertilizer and preparation method thereof |
| CN113716999A (en) * | 2021-08-23 | 2021-11-30 | 安徽坤健生物科技有限公司 | Biological treatment process for resource utilization of organic wastes |
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| US6423532B1 (en) * | 1997-02-24 | 2002-07-23 | Linde Brv Biowaste Technologies Ag | Refuse-treatment method and apparatus |
| CN1548405A (en) * | 2003-05-12 | 2004-11-24 | 武汉格瑞霖生物环保科技有限公司 | Method for producing efficient active biological organic fertilizer with excrement and organic garbage |
| CN1724486A (en) * | 2004-07-14 | 2006-01-25 | 农业部规划设计研究院 | Equipment for dry fermentation and its method |
| CN101565332A (en) * | 2009-04-10 | 2009-10-28 | 张山跃 | Biological organic fertilizer |
| CN101717284A (en) * | 2009-12-10 | 2010-06-02 | 四川农业大学 | Method for preparing organic compound fertilizer by treating chicken manure through biological fermentation technology |
| CN102040410A (en) * | 2009-10-16 | 2011-05-04 | 黄银宝 | Method for producing bio-organic fertilizer by utilizing livestock and poultry feces |
-
2012
- 2012-11-26 CN CN2012104849742A patent/CN102976806A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6423532B1 (en) * | 1997-02-24 | 2002-07-23 | Linde Brv Biowaste Technologies Ag | Refuse-treatment method and apparatus |
| CN1548405A (en) * | 2003-05-12 | 2004-11-24 | 武汉格瑞霖生物环保科技有限公司 | Method for producing efficient active biological organic fertilizer with excrement and organic garbage |
| CN1724486A (en) * | 2004-07-14 | 2006-01-25 | 农业部规划设计研究院 | Equipment for dry fermentation and its method |
| CN101565332A (en) * | 2009-04-10 | 2009-10-28 | 张山跃 | Biological organic fertilizer |
| CN102040410A (en) * | 2009-10-16 | 2011-05-04 | 黄银宝 | Method for producing bio-organic fertilizer by utilizing livestock and poultry feces |
| CN101717284A (en) * | 2009-12-10 | 2010-06-02 | 四川农业大学 | Method for preparing organic compound fertilizer by treating chicken manure through biological fermentation technology |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857664A (en) * | 2017-12-28 | 2018-03-30 | 彭光简 | A kind of organic farm soils improvement microbial enzyme composite bacterial fertilizer and preparation method thereof |
| CN113716999A (en) * | 2021-08-23 | 2021-11-30 | 安徽坤健生物科技有限公司 | Biological treatment process for resource utilization of organic wastes |
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Application publication date: 20130320 |