CN101779724A - Biological cycle process - Google Patents
Biological cycle process Download PDFInfo
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- CN101779724A CN101779724A CN200910003622A CN200910003622A CN101779724A CN 101779724 A CN101779724 A CN 101779724A CN 200910003622 A CN200910003622 A CN 200910003622A CN 200910003622 A CN200910003622 A CN 200910003622A CN 101779724 A CN101779724 A CN 101779724A
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Abstract
The invention discloses a method for producing basic rations, fine fodders and all-material feeds required by animals (pigs, bulls, sheep or poultry and fisheries) by utilizing forage plants and ordinary plant straws by a mildew method or an ammonization method, and a cultivation supporting process. The forage plants and the ordinary plants (straws) contain rich carbohydrates, vitamins and mineral composition required by the animals, the poultry and the fisheries; through the special function of the peculiar ammonization of mildews, the palatability of the produced feed is improved, nutrient substances of the feed are effectively replaced, and the feed is easily digested and absorbed by animals. In order to rich the nutrient substances, the complex bacteria (enzyme) method and the ammonization method are adopted and simultaneously bone meal and pine needle meal are rationally added, which makes the nutrition of the produced feed more sufficient and rational and have higher value in use. By producing a marsh gas by using garbage (animal excrements) and utilizing the marsh gas, a biological cycle process is formed so as to fulfill a plurality of aims of the comprehensive utilization of waste materials and environmental protection.
Description
Technical field:
The invention belongs to a kind of biological cycle.The biological cycle process of a kind of specifically waste utilization and integrated culture.
Background technology:
Existing agricultural crop straw all acts as a fuel and the usefulness of assorted feed rear cattle, sheep or extensive ground compost generally speaking.Its value is extremely low, and the waste resource do not say, contaminated environment also can not reach and economizes on resources and protect environment and produce the more purpose of large economy benefit.
Summary of the invention:
The object of the present invention is to provide a kind of composite technology of twice laid, and then reach the economic aim of the comprehensive organism circulation that improves environment, energy-conservation, synergy.
Purpose of the present invention is achieved by following technical proposals: biological cycle process comprises enzyme bacterium method and two kinds of processing and treating methods of ammoniation process, produces alcohol and feed; Feed is cultured and to be comprised moving, fowl, aquatic product; Animal excrements are used to produce biogas, and biogas is used for generating, and generating is used for production of fodder and processing; The natural pond slag is used for the vegetable material of farming and animal husbandry is exchanged; The plant regeneration that is exchanged produces feed can carry out the i.e. 100 kilograms of plant exchange 30-40 kilogram feeds of residual quantity exchange with peasant household again.And 100 kilograms of plants can produce feed more than 90 kilograms, and last residual quantity feed is used further to own aquaculture development and cultures.The plant of farming and animal husbandry can be cobalt blue pigment, wet feed and siccative.At first carry out virus and harmful bacterium and detect, respectively raw material are pulled an oar again and pulverize, slurry or powder are gone into jar to add an amount of water then, carry out the processing of ammonification or enzyme bacterium method again.Temperature in making jar reaches between 5～30 ℃, after the ammonification or fermentation through cycle in 8～1 weeks, filters out many moisture content (ammoniacal liquor or bacterium liquid) by vacuum tank again, and the mother liquor under the filter can recycle, and its value is higher.It is that centrifugal drying is baked and banked up with earth that residue filter thing enters next technology, detects qualified granulation again, packing listing.According to actual conditions, in enzyme bacterium method or ammoniation process early stage, can add earlier in addition after the alcohol yeast fermentation extracts alcohol, enter into jar again with alcohol trough and carry out ammonification or enzyme bacterium processing.
Enzyme bacterium of the present invention comprises: protease, zymase, ammonification microorganism and six fermentoids after alcohol yeast, saccharomyces cerevisiae, Lactobacillus acidophilus, streptococcus fecalis, hay bacillus, acetic acid bacteria, lichenin bacillus, saccharification wine yeast, lactic acid bacteria, S. cervisiae, lactobacillus, streptococcus lactis, lactobacterium bacteria, protease, amylase and the activation: oxidoreducing enzyme, hydrolase, lyase, isomerase, ligase, transferase.Methionine etc. utilize the specificity of bacterium, fungi and the height selectivity of enzyme, and the plant of being rich in vitamin, amino acid, protein, carbohydrate, fiber and trace element and mineral matter is cemented out by above-mentioned enzyme bacterium method.When improving the palatability of feed, improved the utilization of nutriment biglyyer and digested and assimilated.The effect each other of enzyme bacterium itself adds the cracking synthesis to plant, makes useless plant become the higher required feed of various animal bodies of value.
Ammoniation process of the present invention is included in the jar directly logical ammonia, ammoniacal liquor and urea water the plant slurry or the powder of required processing is carried out the ammonification in 1～8 week, and temperature should be between 5～30 ℃, and making a jar interior temperature most is between 24～26 ℃.By the feed after the ammonification, palatability is better, and nutriment is abundanter and be more conducive to be digested and absorbed by animal body.That the thing of raising increases income is bigger (refer to meat productivity, laying rate, the rate of giving milk, produce hair rate etc.).Tradition is given birth to and is used or the more superiority of unprocessed feed tool.
Advantage of the present invention is:
1, production selectivity is big, utilizes local method also can produce, and also can utilize modern automation and mechanization production, and it is adjustable arbitrarily that scale is changeable.Assembling is produced easily.
2, all raw material are that agriculture and animal husbandry crop discarded object is non-grain class, and traditional using method is burning, the direct rear cattle of coarse fodder, sheep or compost, and waste is big, and contaminated environment.Adopt the present invention can overcome above-mentioned shortcoming fully, and produce bigger economic worth.
3, a cover technology, two kinds of production methods need not unnecessary input, have equaled two production lines.Design science is reasonable, and configuration is calculated, and economic benefit and social benefit tool are good.
4, cost is low, and the cycle is short, instant effect, and technology is grasped easily, implements rapidly and efficiently.Meet national industrial policies, belong to and vigorously support industry, benefit the nation and the people.
Description of drawings:
Fig. 1: fen and colony house schematic diagram.
Fig. 2: dehydration (drying) conveyer schematic diagram.
Fig. 3: enzyme bacterium method and ammoniation process recycle (vacuum filtration and feeding figure).
Fig. 4: biological cycle retort artwork.
Fig. 5: biological cycle production distribution figure.
Fig. 6: biological cycle flow chart.
Be illustrated with regard to accompanying drawing respectively below:
Fig. 1: 1,2,3 be respectively marsh-gas fermentation tank.4,5,6 be respectively marsh-gas fermentation tank discharging (liquid and slag) valve and charging (animal excrements) valve.7,8,9 be respectively charging and discharging by-pass valve control.10,11,12, be respectively the biogas discharge valve.13,14,15 be respectively interim charging and discharging opening (lid).16,17,18 be respectively interim charging of marsh-gas fermentation tank and discharging opening.19 is the biogas conveyance conduit.20 is animal (colony house) excreta pipeline.21 and 22 are respectively biogas control gas valve.23 is above-ground route.Proof biogas jar is lower than colony house physical features.24 are the marsh gas power generation appliance arrangement, can supply 380V, 220V AC power.25 is the colony house passage.26 is colony house.
Fig. 2: 1 is motor.2 is speed change system.3 is the material transport tape.4 is fan-shaped driving gear.5 are centrifugal dehydration equipment peripheral seal bucket.6 are sealing bucket fixed support.7 is centrifugal refuse receptacle valve.8 is centrifuge storage filter cloth.9 is exactly 6.10 and 14 are all sector shaft.15 is centrifugal refuse receptacle.11 for fluid with go out the siccative valve.12 is liquid valve.13 for going out the siccative valve.
Fig. 3: 1 is motor.2 is vavuum pump.3 is exhaust tube.4 is blast pipe.5 is extraction valve.6 is vacuum tank.7 are the liquid valve of bleeding.8 is fermentation tank or ammonification jar.9 is fermentation tank or ammonification jar piston valve.10 is liquid valve.11 recycle pump for the liquid material.12 is the mother liquor carrier pipe.13 is feed duct.14 are the charging delivery pump.15 is feed hopper.16 is fermentation tank or ammonification jar bleeder valve.17 is discharge pipe.18 is dehydrogenation drying equipment.
Fig. 4: 1 is motor.2 is drive.3 is the material transport tape.4 is fermentation tank or ammonification jar charging aperture.5 is the piston type sealed valve.6 is tank body.7 bleeder valves for band filter cloth device.8 is the tank body cylindrical stent.9 is handle type discharging or fluid valve.10 are discharging or filtrate pipeline.
Fig. 5: biological cycle production distribution figure.The endless form of production distribution among Fig. 5 is seen in its explanation.Explanatory note is seen the literal of indicating in the square frame.The flow process mode is seen line and arrow points.Design has 5 enzyme bacterium jars and two kinds of production models of 5 ammonification jars among the figure.
Fig. 6: biological cycle flow chart.Explanatory note in the process blocks is seen among Fig. 6 in its detailed description, and production order and technology are seen line and arrow points among the figure.
The specific embodiment:
Below in conjunction with description of drawings the specific embodiment of the present invention is further described.
Among Fig. 5, Fig. 6, the plant siccative of agriculture and animal husbandry crop is through pulverizing, and cobalt blue pigment or wet feed be through making beating, pulverize and making beating before to carry out virus and the detection of harmful bacterium, the step process of being allowed for access down after qualified.The fineness of its slurry or powder can be formulated specification (screen cloth) according to the needs that reality is raised thing.Allow as situation, can carry out alcoholic fermentation, the vinasse behind the extraction alcohol enter enzyme bacterium jar or ammonification jar.Also can not extract alcohol directly enters slurry or powder in enzyme bacterium jar or the ammonification jar.Multiple bacterium is arranged in the enzyme bacterium jar and activated after enzyme.Available ventilation or stuffiness dual mode carry out.The interior temperature of tank body is controlled at 5～30 ℃ and is advisable.Need to get final product through the fermentation of 8～1 time-of-weeks, humidity is controlled at about 40%.Through venomous injurant detect and nutritive index qualified after, next step technology of being allowed for access is the centrifugal drying granulation transaction of can raising and go on the market.Ammoniation process too, early stage, to extract alcohol identical, later stage humidity also should be controlled at about 40% and be advisable, temperature also will be controlled between 5～30 ℃, approximately the cycle is between 8～1 weeks.Detection method is with enzyme bacterium method.The optimal temperature of enzyme bacterium method and ammoniation process is 24～26 ℃.Ammoniation process later stage flow process is with enzyme bacterium method.
Use repeatedly capable of circulation of the mother liquor of enzyme bacterium method of the present invention and value are higher, and mother liquor nutrition is abundanter.The mother liquor of ammoniation process equally can recycle, and its nutriment is also abundanter.
The feed that enzyme bacterium method of the present invention or ammoniation process are produced, can carry out the residual quantity transaction promptly with the plant exchange of farming and animal husbandry, exchange capacity is the 100 kilograms of commutative feed 30-40 of plant kilograms, annotating cobalt blue pigment and wet feed should have than big difference with siccative.100 kilograms of plants can produce feed more than 90 kilograms.The feed of residual quantity can be used for aquaculture on one's own account, and animal excrements can be used for producing biogas, and marsh gas power generation can be used for producing the required of feed, and the natural pond slag can be used for exchanging plant regeneration product feed with peasant household.The production technology of a biological cycle is formed in circulation so successively.
Enforcement of the present invention is used, and is the utility of benefiting the nation and the people and benefiting the society, and also is to improve environment, solves the optimal economic pattern of the employment of starting an undertaking, and still turns waste into wealth the effective way that economizes on resources.The present invention is reasonable in design, and technical difficulty is little, transforms easily, implements simple.
Claims (10)
1. to be made up of three parts be that enzyme bacterium method or ammoniation process and non-grain plant and aquaculture constitute jointly biological cycle process in the present invention.
2. biological cycle process according to claim 1 is characterized in that: described enzyme bacterium comprises: the protease after alcohol yeast, saccharomyces cerevisiae, Lactobacillus acidophilus, streptococcus fecalis, hay bacillus, acetic acid bacteria, lichenin bacillus, saccharification wine yeast, lactic acid bacteria, S. cervisiae, shaft-like lactobacillus, streptococcus lactis, zymase, lactobacterium bacteria, protease, amylase and the activation thereof, methionine and six big fermentoids: oxidoreducing enzyme, transferase, hydrolase, lyase and structure enzyme and ligase.And beneficial bacterium, enzyme such as ammonification microorganism.Utilize the specificity of bacterium and fungi and the height selectivity of enzyme, the nutriment that makes plant and bone meal class as: vitamin, protein, fat, amino acid and sugar are displaced well with mineral mass-energy, and improve the palatability of feed simultaneously and more help digesting and assimilating of animal body.
3. biological cycle process according to claim 2 is characterized in that: described enzyme bacterium method through adding bone meal and pine needle meal, can further produce daily ration base grain, concentrated feed and complete feed feed and mixed feed.Thickness according to pulverizing or making beating thing is that fiber length is as granulation or mash feed, as the of the right age feed of ox, pig, sheep, bird or aquatic product animal.It is fast that animal body is absorbed, and increases weight, gives milk, lays eggs etc.
4. the biological cycle process of ammoniation process according to claim 1 is characterized in that: described ammoniation process, can directly feed ammonia or ammoniacal liquor, and urea water is carried out non-grain plant sealing and is soaked reaction, discharges unnecessary ammoniacal liquor after the reaction again.Temperature can become grog through time in 1～8 week between 30-5 ℃.
5. according to claim 2,3,4 described biological cycle process, it is characterized in that: the feed that described enzyme bacterium method and ammoniation process are produced, needing to do further processing handles, be that the enzyme mother bacterial liquid utilizes and mother liquor from amination is recycled, centrifuge dewatering then, drying is cured granulation, detects the packing listing of the qualified back of harmful bacterium and venomous injurant.The mother liquor value of its recovery is higher.
6. biological cycle process according to claim 1 is characterized in that: described non-grain plant is virus-free, the non-grain plant of all of remains of pesticide and cereal crops tangerine stalk and herbage.Especially be optimum vegetable material with cornstalk, jowar stalk, potato rattan, bagasse, vinasse, shell etc.Above-mentioned vegetable material can be cobalt blue pigment, wet feed and siccative, do not exceed standard but all must detect harmful bacterium and Toxic, and then through making beating or pulverizing, its granularity is a fiber length, can be different and different according to animal species of raising thing and growth period, can select 30 orders, 50 orders, 80 orders and 120 mesh sieves.Can extract alcohol through distillery yeast fermentation, or not extract that alcohol directly enters enzyme bacterium method or ammonification is handled.The described processing of the same claim 5 of aftermentioned technology.
7. biological cycle process according to claim 1 is characterized in that: described material culture can be pig, ox, sheep, bird, aquatic product.Animal excrements except that aquatic product, row is produced biogas again.The biogas of being produced can generate electricity for electric energy needs required in the described biological cycle process of aforementioned claim.The natural pond slag can be used as that fertilizer is sold or needs straw with the peasant household clearing house.The product of raising can sell or process sale.
8. the feed that is produced according to the described biological cycle process of aforementioned claim, natural pond slag or raising thing exchange plant straw etc. with peasant household by barter system, again the biological cycle of row processing feed.
9. according to the described biological cycle process of aforementioned claim, it is characterized in that: described enzyme bacterium method and the required environment temperature of ammoniation process are strict controlled between 5～30 ℃, and optimum temperature should be 24～26 ℃.Enzyme bacterium method can adopt ventilation and stuffiness method.Ammoniation process must seal.
10. according to the described biological cycle process of aforementioned claim, it is characterized in that: described raw material in early stage (referring to plant) and its pellet of back, all must can produce and go on the market through virus and harmful bacterium sterilization processing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910003622A CN101779724A (en) | 2009-01-16 | 2009-01-16 | Biological cycle process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910003622A CN101779724A (en) | 2009-01-16 | 2009-01-16 | Biological cycle process |
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| CN101779724A true CN101779724A (en) | 2010-07-21 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102232469A (en) * | 2011-08-09 | 2011-11-09 | 陈聚恒 | Method for processing herbal straws into forage through hot spraying and microbial fermentation |
| CN102246913A (en) * | 2011-07-25 | 2011-11-23 | 上海牧农生物科技有限公司 | Biologically fermented straw feed prepared through anaerobic or facultative fermentation |
| CN103641571A (en) * | 2013-12-13 | 2014-03-19 | 汝州市九龙牧业有限公司 | Organic fertilizer for tuber type vegetables and production process of organic fertilizer |
| CN105766668A (en) * | 2016-03-14 | 2016-07-20 | 四川省地宸农业有限责任公司 | Exhaust gas recycling system for pig farm |
| CN107047986A (en) * | 2017-03-29 | 2017-08-18 | 安徽省微科生物科技有限公司 | A kind of wool sheep feed addictive |
-
2009
- 2009-01-16 CN CN200910003622A patent/CN101779724A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102246913A (en) * | 2011-07-25 | 2011-11-23 | 上海牧农生物科技有限公司 | Biologically fermented straw feed prepared through anaerobic or facultative fermentation |
| CN102232469A (en) * | 2011-08-09 | 2011-11-09 | 陈聚恒 | Method for processing herbal straws into forage through hot spraying and microbial fermentation |
| CN103641571A (en) * | 2013-12-13 | 2014-03-19 | 汝州市九龙牧业有限公司 | Organic fertilizer for tuber type vegetables and production process of organic fertilizer |
| CN103641571B (en) * | 2013-12-13 | 2016-01-20 | 汝州市九龙牧业有限公司 | A kind of rhizome vegetable fertilizer and production technique thereof |
| CN105766668A (en) * | 2016-03-14 | 2016-07-20 | 四川省地宸农业有限责任公司 | Exhaust gas recycling system for pig farm |
| CN107047986A (en) * | 2017-03-29 | 2017-08-18 | 安徽省微科生物科技有限公司 | A kind of wool sheep feed addictive |
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Application publication date: 20100721 |