CN101684049A - Method for preparing biological fertilizer and the biological fertilizer by the method - Google Patents
Method for preparing biological fertilizer and the biological fertilizer by the method Download PDFInfo
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- CN101684049A CN101684049A CN200810072959A CN200810072959A CN101684049A CN 101684049 A CN101684049 A CN 101684049A CN 200810072959 A CN200810072959 A CN 200810072959A CN 200810072959 A CN200810072959 A CN 200810072959A CN 101684049 A CN101684049 A CN 101684049A
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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
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Abstract
The invention discloses a method for preparing a fertilizer by utilizing plant waste slag and the biological fertilizer prepared by the method, wherein the biological fertilizer is prepared by uniformly mixing the plant waste slag, organic wastes, salts, carbamide, thermophilic aerobic biological bacteria, adding the mixture into a fermentation tank for dehydrating and crushing after thermophilicfermentation. Compared with prior art, the method using thermophilic aerobic bacteria as production strains, overcomes long deodorization process in current traditional biofertilizer production and control difficulty in technique, and has the advantages of simple industrial process, short preparation time and low cost. The method is especially suitable for recycling the waste slag in Chinese medicine production, decreases pollution on environment, and achieves the purpose for turning rubbish into treasure. The prepared fertilizer is quick release and slow release, contains more than 60% of organic matters, and riches in nitrogen, phosphorus, potassium, crude protein, pure protein, amino acid, kinds of vitamins and trace elements.
Description
Technical field
The present invention relates to a kind of biological organic fertilizer that utilizes method that waste plant dregs prepares fertilizer and this method to produce, particularly be to utilize microbial process that the method for organic fertilizer and the biological organic fertilizer that this method is produced are made in the waste plant dregs fermentation.
Background technology
In recent years, people's environmental protection consciousness strengthens, and gets down to the consumption that reduces chemical fertilizer, and the development Organic farming is set up green food safety technique system.Application of organic fertilizers is traditional experience that Chinese agriculture is produced, and up to 50～sixties of 20th century, China's manure resources overwhelming majority still relies on organic fertilizer.After the sixties, particularly carry out after the contract and responsibility system in the rural area, and fertilizer amount increases sharply, and the proportion of fertilizer just descends to some extent, but from the nutrient content meter, still accounts for more than 1/3 of China's fertilizer amount.As far back as nineteen eighty-three, people such as Zhang Fudao use situation to 33 years (1949～1981 years) fertilizer of China and carry out statistical study, and the result shows, no matter pass by, the present and the future, organic fertilizer all plays an important role to China's agriculture production, particularly potassium in the organic fertilizer and phosphorus.The fact shows, the simple nitrogenous fertilizer that uses, owing to reasons such as volatilization, leaching loss, denitrification, runoffs, the utilization ratio of nitrogenous fertilizer has only 30%～50%, and cause phreatic pollution, and the way that adopts biological organic fertilizer and inorganic fertilizer to use with can improve the utilization ratio of nitrogenous fertilizer greatly; Equally, because inorganic phosphorus is easy to generate insoluble compound in being manured into soil, therefore, the utilization ratio of phosphorus is very low, and after using bio-organic fertilizer, organic acid can form stable complex compound with metallic elements such as calcium, magnesium, iron, aluminium, thereby reduces the utilization ratio that phosphorus fixation can obviously improve phosphorus.
Present organic nutriment in a fertilizer two big classes, the i.e. farm manure of peasant oneself accumulation and the commercial fertilizer of producing by fertiliser production enterprise.Farm manure contains large number of biological material, plant and animal residues and some organic wastes etc. usually.The formed organic fertilizer of spontaneous fermentation is by anaerobically fermenting substantially, and the fertilizer stink is denseer, so can't commercialization.And commercial fertilizer is meant and utilizes straw, feces of livestock and poultry and multiple organic materials, the fertilizer that forms by the artificial fermentation, all needing to carry out deodorizing in the present production process handles, mainly be in raw material, to add the purpose microorganism, utilize the microbiological degradation organic matter, macromolecular substance is become small molecules, reach deodorizing then, become thoroughly decomposed, dehydration, exsiccant purpose, because deodorisation process is very long and technology is wayward, thereby the application of bio-feritlizer is affected.
Simultaneously, along with pharmacy industry Chinese materia medica pharmacy flourish particularly, particularly extract in the production and inevitably will produce a large amount of waste residues in Chinese medicinal plant, if it freely is put in the environment, will certainly cause severe contamination to environment, the waste residue that produces after the extraction as Radix Glycyrrhizae etc. is exactly wherein a kind of, as not adding processing, not only cause the wasting of resources but also cause environmental pollution, to its appropriate processing, imperative.
But at present its effective processing of carrying out is not seen that as yet report is arranged, main research is maximum is to utilize edible mushrooms such as glycyrrhiza residue fermentative preparation flat mushroom, but the utilization again of the waste residue that is produced thereafter is difficulty quite, also there is report to be used for preparing the dressing of pill, still is difficult to solve root problem but consumption is less.
Summary of the invention
The purpose of this invention is to provide a kind of technological process simple, without the production method of the biological organic fertilizer of deodorisation process and the biological organic fertilizer that this method is produced, particularly a kind ofly utilize the waste residue after waste plant dregs behind the herbal pharmaceutical such as Radix Glycyrrhizae are extracted to make the method for biological organic fertilizer and the biological organic fertilizer that this method is produced.
The technical solution used in the present invention is: described method comprises following technological process:
Batching: get 45～60 parts of waste plant dregs, 15～30 parts of organic wastes by weight, 10～30 parts of 2～15 parts of calcium salts, 1～5 part of nitrogen salt, sylvite mix with 50～70 parts of water, and add growth temperature simultaneously at the thermophilic aerobic bacteria more than 45 ℃: Thermus (Thermus), sulfolobus solfataricus belong at least a 5～15 parts in (Sulfolobus), Thermoplasma (Thermoplasma) or the bacstearothermophilus (Bacillus stearothermophilus).
Thermophilic fermentation: the material that proportioning is good is put into fermentation vat and is fermented, and overturning in per 6～24 hours once and is tested temperature in the fermentation vat at any time, overturning several times when temperature arrives more than 75 ℃, and temperature is reduced to below 65 ℃, when occurring temperature once more more than 75 ℃ the time, the artificial hypothermia is to normal temperature.
Dehydrate afterwards to water content≤15%, crushing packing gets final product.
Also can first granulation, be dried to packing after water content≤15% again.
Above-mentioned waste plant dregs is preferably the medicine waste residue that is produced in the Chinese medicine production, especially the medicine waste residue after Radix Glycyrrhizae is extracted, or kendir, hawthorn, chrysanthemum, Spica Prunellae, yncaria stem with hooks, Asian puccoon, Chinese ephedra, safflower, saussurea involucrata, rue greatly, the waste residue after the bulb of fritillary, Herba Cistanches, rhizoma alismatis or the root of bidentate achyranthes extracting and processing Chinese medicinal materials, can also be the mixing of above-mentioned waste residue.
Above-mentioned calcium salt is at least a as in calcium sulfate, calcium superphosphate, lime carbonate, lemon acid calcium, calcium lactate, the calglucon of at least a in inorganic calcium salt or the organic calcium salt, ammonium salt is at least a in bicarbonate of ammonia, ammonium chloride, ammonium nitrate, ammonium phosphate (primary ammonium phosphate), Secondary ammonium phosphate, saltpetre or the urea, and sylvite is at least a in vitriolate of tartar, Repone K or the plant ash.
It is characterized in that described above-mentioned organic waste is one or more in the skin slag, human and animal excreta, beer slag, liquor slag, citric acid waste, black rice schlempe, animal bone powder, ocean class animal powder in plant oil cake slag, the grain processing.
Compared with prior art, the present invention had both overcome the weak point of traditional compost, especially utilize thermophilic aerobic bacteria as producing bacterial strain, it is long to have overcome in the present traditional biological fertiliser production deodorisation process, the unmanageable deficiency of technology has that technological process is simple, preparation time is short, production cost is in the advantage for reducing.Particularly can the waste residue that Chinese materia medica production is produced be utilized again, minimizing is to the pollution of environment, reach the purpose that turns waste into wealth, prepared fertilizer combines many-sided advantage and functions such as fertilizer, chemical fertilizer, bacterial manure, quick-acting, slow has both, and wherein contains organic matter more than 60%, and is rich in nitrogen, phosphorus, potassium, crude protein, true protein, amino acid, multivitamin and trace element, every gram contains probiotics more than 400,000,000, and nutritive element is complete.
Embodiment:
Embodiment 1:
After getting the ratio of 14 parts of 1 part in 5 parts in 20 parts of 50 parts of licorice slags, soya-bean cakes, calcium sulfate, urea, plant ash after air-dry, 10 parts of bacstearothermophiluses and 65 parts of water by weight and mixing, insert in the fermentation vat of high 15cm, thermophilic fermentation 7 days, every overturning in 24 hours once, continuous overturning several times when rising to 75 ℃, temperature is reduced to below 65 ℃, dehydration and be dried to water content≤15% behind the normal temperature when occurring second 75 ℃ below the artificial hypothermia to 35 ℃, be crushed to the particle of 3～6mm, enter packet assembler afterwards.
Embodiment 2:
Get by weight and air-dryly be lower than 60 parts of 10% licorice slags to moisture, 15 parts of wheat brans, 10 parts of calcium superphosphate, 5 parts in bicarbonate of ammonia, 5 parts of vitriolate of tartar, after sulfolobus solfataricus belongs to the ratio of 10 parts on bacterium and 55 parts of water and mixes, put into fermentation vat, thermophilic fermentation 10 days, every overturning in 24 hours once, continuous overturning several times when rising to 75 ℃, make temperature reduce to 60 ℃, continue fermentation and once every overturning in 18 hours, normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 30 ℃, dehydration also is dried to water content≤8%, be crushed to the particle of 3～6mm, enter packet assembler afterwards.
Embodiment 3:
Get and air-dryly be lower than 45 parts of 7% licorice slags to moisture, 15 parts of rape cakes, 15 parts in lime carbonate, 5 parts of ammonium chlorides, 10 parts in Repone K, after the ratio that the Thermoplasma bacterium is 6 parts and 70 parts of water mix, put into fermentation vat, thermophilic fermentation 20 days, every overturning in 12 hours once, continuous overturning several times when rising to 75 ℃, make temperature reduce to 55 ℃, continue fermentation and once every overturning in 10 hours, normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 40 ℃, dehydration also is dried to water content≤12%, be crushed to the particle of 3～6mm, enter packet assembler afterwards.
Embodiment 4:
To prepare the capsular kendir of kendir pressure-reducing, hawthorn, extractions such as chrysanthemum backs also air-dryly is lower than 10% the dregs of a decoction and cooperates by arbitrary proportion to moisture content, get 50 parts in above-mentioned blended waste residue by weight, 20 parts of black rice schlempes, 10 parts of lemon acid calcium, 3 parts in ammonium nitrate, 15 parts in Repone K, after sulfolobus solfataricus belongs to the ratio of 12 parts on bacterium and 50 parts of water and mixes, put into fermentation vat, thermophilic fermentation 15 days, every overturning in 24 hours once, continuous overturning several times when rising to 75 ℃, make temperature reduce to 62 ℃, continue fermentation and once every overturning in 10 hours, normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 30 ℃, dehydration also is dried to water content≤8%, be crushed to the particle of 3～6mm, enter packet assembler afterwards.
Embodiment 5:
Getting the capsular kendir of preparation kendir pressure-reducing by weight extracts the back and air-dryly is lower than 50 parts of 15% the dregs of a decoction to moisture content, 15 parts of black rice schlempes, 12 parts in lime carbonate, 5 parts of Secondary ammonium phosphates, 12 parts in Repone K, after sulfolobus solfataricus belongs to the ratio of 15 parts on bacterium and 55 parts of water and mixes, put into fermentation vat, thermophilic fermentation 5 days, every overturning in 24 hours once, continuous overturning several times when rising to 75 ℃, make temperature reduce to 62 ℃, continue fermentation and once every overturning in 10 hours, normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 30 ℃, dehydration also is dried to water content≤5%, be crushed to the particle of 3～6mm, enter packet assembler afterwards.
Embodiment 6:
Getting hawthorn by weight extracts the back and air-dryly is lower than 20 parts of 13% the dregs of a decoction to moisture content, air-dryly be lower than 30 parts of 10% licorice slags to moisture, 20 parts of black rice schlempes, 10 parts in lime carbonate, 3 parts in ammonium phosphate (primary ammonium phosphate), 13 parts in Repone K, hot Pseudomonas, sulfolobus solfataricus belongs to, sulfolobus solfataricus belongs to three kinds by getting 12 parts after 1: 1: 1 the mixed, getting 70 parts of water mixes, put into fermentation vat, thermophilic fermentation 12 days, every overturning in 15 hours once, continuous overturning several times when rising to 75 ℃, make temperature reduce to 60 ℃, continue fermentation and once every overturning in 10 hours, normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 25 ℃, dehydration also is dried to water content≤6%, is crushed to the particle of 3～6mm, enters packet assembler afterwards.
Embodiment 7:
Getting safflower by weight extracts the back and air-dryly is lower than 20 parts of 13% the dregs of a decoction to moisture content, air-dryly be lower than 30 parts of 10% licorice slags to moisture, 20 parts of black rice schlempes, 10 parts in lime carbonate, 3 parts of ammonium chlorides, 14 parts in Repone K, three kinds of Thermoplasma and bacstearothermophiluses are by getting 15 parts after 2: 1 the mixed, getting 65 parts of water mixes, put into fermentation vat, thermophilic fermentation 6 days, every overturning in 24 hours once, continuous overturning several times when rising to 75 ℃, make temperature reduce to 65 ℃, continue fermentation and once every overturning in 24 hours, normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 25 ℃, dehydration also is dried to water content≤7%, is crushed to the particle of 3～6mm, enters packet assembler afterwards.
Embodiment 8:
Getting saussurea involucrata by weight extracts the back and air-dryly is lower than 20 parts of 13% the dregs of a decoction to moisture content, air-dryly be lower than 30 parts of 10% licorice slags to moisture, 20 parts of black rice schlempes, 10 parts of calcium superphosphate, 3 parts of ammonium chlorides, 11 parts in Repone K, three kinds of Thermoplasma and bacstearothermophiluses are by getting 15 parts after 2: 1 the mixed, getting 70 parts of water mixes, put into fermentation vat, thermophilic fermentation 6 days, every overturning in 24 hours once, continuous overturning several times when rising to 75 ℃, make temperature reduce to 65 ℃, continue fermentation and once every overturning in 24 hours, normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 25 ℃, dehydration also is dried to water content≤7%, is crushed to the particle of 3～6mm, enters packet assembler afterwards.
Embodiment 9:
Get and air-dryly be lower than 40 parts of 7% licorice slags to moisture; 18 parts of rape cakes; 10 parts in lime carbonate; 3 parts of ammonium chlorides; 10 parts in Repone K; after the ratio that the Thermoplasma bacterium is 6 parts and 60 parts of water mix; put into fermentation vat; thermophilic fermentation 20 days; every overturning in 15 hours once; continuous overturning several times when rising to 75 ℃; make temperature reduce to 55 ℃; continue fermentation and once every overturning in 10 hours; normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 40 ℃; dehydration also is dried to water content≤30%; insert tablets press again and be processed into the particle of 4～6mm, enter packet assembler afterwards.
Embodiment 10:
Getting the capsular kendir of preparation kendir pressure-reducing by weight extracts the back and air-dryly is lower than 45 parts of 15% the dregs of a decoction to moisture content; 25 parts of black rice schlempes; 8 parts of calcium superphosphate; 2 parts of ammonium chlorides; 10 parts in Repone K; after sulfolobus solfataricus belongs to the ratio of 15 parts on bacterium and 55 parts of water and mixes; put into fermentation vat; thermophilic fermentation 8 days; every overturning in 24 hours once; continuous overturning several times when rising to 75 ℃; make temperature reduce to 62 ℃; continue fermentation and once every overturning in 10 hours; normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 30 ℃; dehydration also is dried to water content≤25%; insert tablets press again and be processed into the particle of 3～5mm, dewater and be dried to water content≤5%.
Embodiment 11:
Getting Herba Cistanches by weight extracts the back and air-dryly is lower than 15 parts of 13% the dregs of a decoction to moisture content; air-dryly be lower than 25 parts of 10% licorice slags to moisture; 30 parts of black rice schlempes; 5 parts of calglucons; 3 parts in urea; 4 parts in Repone K; 8 parts of plant ash; hot Pseudomonas; sulfolobus solfataricus belongs to; sulfolobus solfataricus belongs to three kinds by getting 15 parts after 1: 2: 1 the mixed; getting 70 parts of water mixes; put into fermentation vat; thermophilic fermentation 16 days; every overturning in 10 hours once; continuous overturning several times when rising to 75 ℃; make temperature reduce to 55 ℃; continue fermentation and once every overturning in 8 hours; normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 25 ℃ dewaters and is dried to water content≤20%, inserts the particle that tablets press is processed into 2～4mm again; dehydration also is dried to water content≤6%, enters packet assembler afterwards.
Embodiment 12:
Getting hawthorn by weight extracts the back and air-dryly is lower than 25 parts of 13% the dregs of a decoction to moisture content; air-dryly be lower than 35 parts of 10% licorice slags to moisture; 20 parts of soya-bean cake slags; 4 parts in lime carbonate; 3 parts of volatile salts; 10 parts of vitriolate of tartar; three kinds of Thermoplasma and bacstearothermophiluses are by getting 15 parts after 1: 3 the mixed; getting 70 parts of water mixes; put into fermentation vat; thermophilic fermentation and once every overturning in 12 hours; continuous overturning several times when rising to 75 ℃; make temperature reduce to 65 ℃; continue fermentation and once every overturning in 6 hours; normal temperature when reaching 75 ℃ once more below the artificial hypothermia to 25 ℃; dehydration also is dried to water content≤35%; insert tablets press again and be processed into the particle of 3～4mm, dewater and be dried to water content≤7%, enter packet assembler afterwards.
Embodiment 13:
Get Spica Prunellae by weight respectively; 25 parts and 35 parts in waste residue after Chinese ephedra is extracted; 10 parts of citric acid wastes; 10 parts of animal bone powders; 15 parts in calcium sulfate; 1 part in urea; 30 parts of vitriolate of tartar; mix with 60 parts of water; add Thermus simultaneously by 2: 1: 1 mixing match; sulfolobus solfataricus belongs to; 12 parts of Thermoplasmas; the material that said ratio is good is put into fermentation vat; ferment overturning in per 12 hours once; and test temperature in the fermentation vat at any time; continuous overturning several times when temperature arrives more than 75 ℃; and temperature is reduced to below 65 ℃; when occurring temperature once more more than 75 ℃ the time; below the artificial hypothermia to 30 ℃; dehydration also is dried to water content≤30%; insert tablets press again and be processed into the particle of 4～8mm, dewater and be dried to water content≤10%, enter packet assembler afterwards.
Embodiment 14:
Get Asian puccoon by weight respectively; 15 parts in waste residue after the bulb of fritillary and the extraction that rues greatly; 15 parts and 15 parts; 10 parts of liquor slags; 10 parts in ocean fish powder; 6 parts in calcium sulfate; 5 parts in urea; 20 parts of plant ash; mix with 65 parts of water; add Thermus simultaneously by 2: 1: 2 mixing match; sulfolobus solfataricus belongs to; 15 parts of Thermoplasmas; the material that said ratio is good is put into fermentation vat; ferment overturning in per 24 hours once; and test temperature in the fermentation vat at any time; continuous overturning several times when temperature arrives more than 75 ℃; and temperature is reduced to below 60 ℃; when occurring temperature once more more than 75 ℃ the time; below the artificial hypothermia to 30 ℃; dehydration also is dried to water content≤25%; insert tablets press again and be processed into the particle of 3～4mm, dewater and be dried to water content≤8%, enter packet assembler afterwards.
Embodiment 15:
35 parts in medicine waste residue after extracting liquorice extracts respectively by weight; 10 parts of 25 parts of liquor slags of waste residue after kendir is extracted; 10 parts of human and animal excretas; 8 parts of calcium lactates; 5 parts of ammonium chlorides; 30 parts of plant ash; mix with 50 parts of water; add Thermus simultaneously by 1: 1: 2 mixing match; sulfolobus solfataricus belongs to; 12 parts of Thermoplasmas; the material that said ratio is good is put into fermentation vat; ferment overturning in per 12 hours once; and test temperature in the fermentation vat at any time; continuous overturning several times when temperature arrives more than 75 ℃; and temperature is reduced to below 60 ℃; when occurring temperature once more more than 75 ℃ the time; below the artificial hypothermia to 30 ℃; dehydration also is dried to water content≤25%; insert tablets press again and be processed into the particle of 2～4mm, dewater and be dried to water content≤8%, enter packet assembler afterwards.
Embodiment 16:
Get Asian puccoon by weight respectively; each 16 parts in waste residue after the bulb of fritillary and the extraction that rues greatly; 12 parts of liquor slags; 8 parts in ocean fish powder; 6 parts in calcium sulfate; 5 parts in urea; 20 parts of plant ash; mix with 65 parts of water; add Thermus simultaneously by 1: 2: 3 mixing match; sulfolobus solfataricus belongs to; 15 parts of Thermoplasmas; the material that said ratio is good is put into fermentation vat; ferment overturning in per 24 hours once; and test temperature in the fermentation vat at any time; continuous overturning several times when temperature arrives more than 75 ℃; and temperature is reduced to below 60 ℃; when occurring temperature once more more than 75 ℃ the time; below the artificial hypothermia to 40 ℃; dehydration also is dried to water content≤20%; insert tablets press again and be processed into the particle of 2～4mm, dewater and be dried to water content≤10%, enter packet assembler afterwards.
Embodiment 16:
20 parts in medicine waste residue after extracting liquorice extracts respectively by weight; 40 parts in waste residue after kendir is extracted; 5 parts of citric acid wastes; 5 parts of black rice schlempes; 10 parts of animal bone powders; 8 parts of calcium lactates; 5 parts in urea; 10 parts in Repone K; 20 parts of plant ash; mix with 70 parts of water; add Thermus simultaneously by 1: 2 mixing match; 15 parts of Thermoplasmas; the material that said ratio is good is put into fermentation vat; ferment overturning in per 12 hours once; and test temperature in the fermentation vat at any time; continuous overturning several times when temperature arrives more than 75 ℃; and temperature is reduced to below 60 ℃; overturning in per afterwards 6 hours once; when occurring temperature once more more than 75 ℃ the time; below the artificial hypothermia to 30 ℃; dehydration also is dried to water content≤25%; insert tablets press again and be processed into the particle of 2～4mm; dehydration also is dried to water content≤8%, enters packet assembler afterwards.
Claims (7)
1. the production method of a biological organic fertilizer is characterized in that mainly comprising following technological process:
Batching: get 45～60 parts of waste plant dregs, 15～30 parts of organic wastes by weight, 10～30 parts of 2～15 parts of calcium salts, 1～5 part of nitrogen salt, sylvite mix with 50～70 parts of water, add growth temperature simultaneously at the thermophilic aerobic bacteria more than 45 ℃: in Thermus, sulfolobus solfataricus genus, Thermoplasma or the bacstearothermophilus at least a 5～15 parts;
Thermophilic fermentation: the material that proportioning is good is put into fermentation vat and is fermented, and overturning in per 6～24 hours once and is tested temperature in the fermentation vat at any time, continuous overturning several times when temperature arrives more than 75 ℃, and temperature is reduced to below 65 ℃, when occurring temperature once more more than 75 ℃ the time, the artificial hypothermia;
Enter afterwards dehydrate, pulverizing or granulation, packaging process.
2. according to the production method of the described biological organic fertilizer of claim 1, it is characterized in that described waste plant dregs is the medicine waste residue that is produced in the Chinese medicine production.
3. according to the production method of the described biological organic fertilizer of claim 2, it is characterized in that described plant amedica waste residue be Radix Glycyrrhizae, kendir, hawthorn, chrysanthemum, Spica Prunellae, yncaria stem with hooks, Asian puccoon, Chinese ephedra, safflower, saussurea involucrata, rue greatly, at least a in the waste residue after the bulb of fritillary, Herba Cistanches, rhizoma alismatis or the Radix Acanthopanacis Bidentatae extraction processing.
4. according to the production method of claim 1,2 or 3 described biological organic fertilizers, it is characterized in that described calcium salt is at least a as in calcium sulfate, calcium superphosphate, lime carbonate, lemon acid calcium, calcium lactate, the calglucon of at least a in inorganic calcium salt or the organic calcium salt, ammonium salt is at least a in bicarbonate of ammonia, ammonium chloride, ammonium nitrate, ammonium phosphate, primary ammonium phosphate, Secondary ammonium phosphate, saltpetre or the urea, and sylvite is at least a in vitriolate of tartar, Repone K or the plant ash.
5. according to the production method of claim 1,2 or 3 described biological organic fertilizers, it is characterized in that described above-mentioned organic waste is one or more in the skin slag, human and animal excreta, beer slag, liquor slag, citric acid waste, black rice schlempe, animal bone powder, ocean class animal powder in plant oil cake slag, the grain processing.
6. according to the production method of the described biological organic fertilizer of claim 4, it is characterized in that described above-mentioned organic waste is one or more in the skin slag, human and animal excreta, beer slag, liquor slag, citric acid waste, black rice schlempe, animal bone powder, ocean class animal powder in plant oil cake slag, the grain processing.
7. a biological organic fertilizer is characterized in that producing according to the method for each described claim of claim 1～6.
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