CN1246260C - Process for producing organic biological composite fertilizer from biological wase material - Google Patents
Process for producing organic biological composite fertilizer from biological wase material Download PDFInfo
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- CN1246260C CN1246260C CNB021137560A CN02113756A CN1246260C CN 1246260 C CN1246260 C CN 1246260C CN B021137560 A CNB021137560 A CN B021137560A CN 02113756 A CN02113756 A CN 02113756A CN 1246260 C CN1246260 C CN 1246260C
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 75
- 238000000034 method Methods 0.000 title claims description 28
- 239000000463 material Substances 0.000 title claims description 8
- 239000002131 composite material Substances 0.000 title claims description 7
- 230000008569 process Effects 0.000 title claims description 5
- 238000000855 fermentation Methods 0.000 claims abstract description 51
- 230000004151 fermentation Effects 0.000 claims abstract description 51
- 150000001875 compounds Chemical class 0.000 claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 claims abstract description 32
- 239000002699 waste material Substances 0.000 claims abstract description 32
- 235000010469 Glycine max Nutrition 0.000 claims abstract description 30
- 244000068988 Glycine max Species 0.000 claims abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910019142 PO4 Inorganic materials 0.000 claims abstract description 10
- 239000010452 phosphate Substances 0.000 claims abstract description 10
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims abstract description 10
- 238000012545 processing Methods 0.000 claims abstract description 7
- 241000606125 Bacteroides Species 0.000 claims description 26
- 230000024121 nodulation Effects 0.000 claims description 26
- 239000007864 aqueous solution Substances 0.000 claims description 25
- 239000007788 liquid Substances 0.000 claims description 24
- 241000894006 Bacteria Species 0.000 claims description 14
- 239000002994 raw material Substances 0.000 claims description 14
- 230000001580 bacterial effect Effects 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims description 9
- 239000002054 inoculum Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 239000005416 organic matter Substances 0.000 claims description 7
- 238000010298 pulverizing process Methods 0.000 claims description 7
- 238000007789 sealing Methods 0.000 claims description 7
- 240000007594 Oryza sativa Species 0.000 claims description 6
- 235000007164 Oryza sativa Nutrition 0.000 claims description 6
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 6
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 6
- 239000004202 carbamide Substances 0.000 claims description 6
- 235000009566 rice Nutrition 0.000 claims description 6
- 244000046052 Phaseolus vulgaris Species 0.000 claims description 5
- 235000010627 Phaseolus vulgaris Nutrition 0.000 claims description 5
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 5
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 claims description 5
- 239000011591 potassium Substances 0.000 claims description 5
- 229910052700 potassium Inorganic materials 0.000 claims description 5
- 210000000582 semen Anatomy 0.000 claims description 5
- 239000012190 activator Substances 0.000 claims description 4
- 238000010907 mechanical stirring Methods 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- WFJIVOKAWHGMBH-UHFFFAOYSA-N 4-hexylbenzene-1,3-diol Chemical compound CCCCCCC1=CC=C(O)C=C1O WFJIVOKAWHGMBH-UHFFFAOYSA-N 0.000 claims description 3
- YMKIRWHSXOBLCF-UHFFFAOYSA-N [Mg].[P].[Ca] Chemical compound [Mg].[P].[Ca] YMKIRWHSXOBLCF-UHFFFAOYSA-N 0.000 claims description 3
- 235000013339 cereals Nutrition 0.000 claims description 3
- 235000013399 edible fruits Nutrition 0.000 claims description 3
- 238000000227 grinding Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000002002 slurry Substances 0.000 claims description 3
- 238000002791 soaking Methods 0.000 claims description 3
- 235000013311 vegetables Nutrition 0.000 claims description 3
- 230000004913 activation Effects 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- 230000008901 benefit Effects 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 3
- 239000011575 calcium Substances 0.000 abstract description 2
- 241000589151 Azotobacter Species 0.000 abstract 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 abstract 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 abstract 1
- 241000589180 Rhizobium Species 0.000 abstract 1
- 230000003213 activating effect Effects 0.000 abstract 1
- 229910052791 calcium Inorganic materials 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 229910052749 magnesium Inorganic materials 0.000 abstract 1
- 239000011777 magnesium Substances 0.000 abstract 1
- 238000004659 sterilization and disinfection Methods 0.000 abstract 1
- PCDQPRRSZKQHHS-CCXZUQQUSA-N Cytarabine Triphosphate Chemical compound O=C1N=C(N)C=CN1[C@H]1[C@@H](O)[C@H](O)[C@@H](COP(O)(=O)OP(O)(=O)OP(O)(O)=O)O1 PCDQPRRSZKQHHS-CCXZUQQUSA-N 0.000 description 19
- 238000009313 farming Methods 0.000 description 10
- 241000196324 Embryophyta Species 0.000 description 6
- 239000002689 soil Substances 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 235000007688 Lycopersicon esculentum Nutrition 0.000 description 4
- 240000003768 Solanum lycopersicum Species 0.000 description 4
- 238000001035 drying Methods 0.000 description 3
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 2
- 102000000584 Calmodulin Human genes 0.000 description 2
- 108010041952 Calmodulin Proteins 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 2
- 244000061176 Nicotiana tabacum Species 0.000 description 2
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 2
- 241000589194 Rhizobium leguminosarum Species 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- 238000005056 compaction Methods 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 229910001425 magnesium ion Inorganic materials 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000003248 secreting effect Effects 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 239000010455 vermiculite Substances 0.000 description 2
- 229910052902 vermiculite Inorganic materials 0.000 description 2
- 235000019354 vermiculite Nutrition 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 241000223782 Ciliophora Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 244000207740 Lemna minor Species 0.000 description 1
- 235000006439 Lemna minor Nutrition 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 235000001855 Portulaca oleracea Nutrition 0.000 description 1
- 210000003165 abomasum Anatomy 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000032823 cell division Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000037149 energy metabolism Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000008558 metabolic pathway by substance Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002688 soil aggregate Substances 0.000 description 1
- 239000002594 sorbent Substances 0.000 description 1
- 235000013555 soy sauce Nutrition 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Fertilizers (AREA)
Abstract
The present invention discloses a production technology for processing an organic biologic compound fertilizer richly containing azotobacter by various kinds of biologic waste. A water solution richly containing CTP is used for activating strain of soybean rhizobium bacteria; after two-stage fermentation is carried out, various kinds of biologic waste and a small number of calcium, magnesium and phosphate fertilizers are directly dried and crushed and are finally prepared with a small number of inorganic fertilizers to form an organic biologic compound fertilizer. The present invention has the advantages of little investment, simple device, no need of disinfection in a production process basically, low energy consumption, short fermentation period, low production cost, great price decrease, etc. Moreover, the organic biologic compound fertilizer has good use effect in agricultural and forestry production and can simultaneously and greatly recycle various kinds of biologic waste, and the economic benefits and the social benefits in the field of environmental protection of the organic biologic compound fertilizer are extremely obvious.
Description
The present invention relates to a kind of production technique of processing organic-biological compound fertilizer through two-stage fermentation, belong to the microbial fermentation field with bio-waste.
Utilize natural rhizobium leguminosarum to make bacterial classification, produce various microbial fertilizers, organic biofertilizer, organic-biological compound fertilizer, owing to can replenish the organic matter of soil effectively, simultaneously can replenish soil microorganisms, improve soil because the soil compaction situation that the life-time service inorganic fertilizer is caused, strengthen soil aggregate, thereby can be when increasing production significantly, improve the quality of farming, Forest products,, become the direction of farming in this century, the fertile production development of woods so especially be subjected to the attention of farming, forestry circle and family, forest products industry.
At present rhizobium leguminosarum is in, the application method in the forestry has two kinds, and first method is with after drying, pulverizes after the collection of natural fabaceous root nodule bacteroid, mixes root when the proportion of crop planting, sprays wine, the use of spreading manuer in holes as the azotogen powder.Though this method is simple, adopted by the producer easily, but because the long-term a large amount of inorganic fertilizers that use in most farmlands, soil compaction, organic matter descends significantly, has been not suitable for leguminous plants and nitrogen fixation flora generation symbiotic relationship, leguminous plants in most farmland is growth root nodule bacteroid on root system, even growth also is that quantity is few, the quality extreme difference, so this first method can't be promoted on a large scale, use; Second method is to make carrier with plant ash, or makes sorbent material with vermiculite, the root nodule bacterium appendix that will cultivate through three-class strain or be adsorbed on plant ash, the vermiculite, or fermented liquid is concentrated postlyophilization to be made.Though this method can obtain a large amount of root nodule bacterium goods, because equipment complexity, technical requirements height, one-time investment is big, is difficult in vast rural area, middle samll cities and towns apply.Simultaneously because the contained organic matter of this root nodule bacterium product all about 20%, does not even contain organic matter,, must cooperate with syrup, a large amount of inorganic fertilizer etc. or once more behind the heap fermentation, could use as organic bio-fertilizer in farming, when production of forestry person uses.Owing to cost an arm and a leg, use trouble, also be unfavorable for rhizobia fertilizer large-scale promotion, application.
The objective of the invention is to: provide a kind of extremely cheap bio-waste as main raw material, (the patent publication No.: that will " be rich in the CTP aqueous solution " CN1128800A) as the bio-stimulant of soybean nodulation bacteroid, directly with various bio-wastes and small amount of calcium magnesium-phosphorus fertilizer after two-stage fermentation, drying, pulverizing are mixed with organic-biological compound fertilizer with small amounts of inorganic fertilizer again.Because the organic content height of this fertilizer, the vinelandii in the root nodule flora also have high level, and biological activity is strong; Simultaneously the content of inorganic nitrogen, phosphorus, potassium is more reasonable, thereby farming, production of forestry person need not reprocessed, directly in the field, the forest land uses in a large number.Because the organic matter material of this fertilizer is very cheap, it is very abundant to originate, and production cost reduces significantly, can satisfy farming, the production of forestry heavy demand to the higher organic-biological compound fertilizer of vinelandii content.
The present invention is achieved in that it is to activate soybean nodulation bacteroid bacterial classification with " being rich in the CTP aqueous solution ", with various bio-wastes and small amount of calcium magnesium-phosphorus fertilizer mixture after two-stage fermentation, again through middle temperature is dried, pulverizing, at last again with a small amount of urea, Repone K, potassium primary phosphate, and the organic-biological compound fertilizer of a small amount of " being rich in the CTP aqueous solution " formulated different varieties;
One, preparatory process:
Handle the early stage of a, bio-waste: adopt the method for heap fermentation that various bio-wastes are tentatively decomposed, and as organic matter material, standby;
B, activation are also cultivated soybean nodulation bacteroid bacterial classification: exsiccant soybean nodulation bacteroid is cleaned up, need weigh up the soybean nodulation bacteroid with the ratio of 6.58 gram original strains in per hundred tons of organic-biological compound fertilizer finished products, use mechanical disintegration; Again in the ratio of 23.4 times of original strain amounts, be made into mixing raw material with accounting for the soyflour of solid medium material quantity 30%, 40% bean cake powder, 15.6% fine rice bran; Add " being rich in the aqueous solution of CTP ", 20% the aqua sterilisa of raw material consumption 5% again, make solid medium; Soybean nodulation bacteroid after pulverizing is evenly admixed in the substratum, and semitight was cultivated 120 hours under PH6-7,30 ℃ of-35 ℃ of conditions, made first class inoculum; Ratio and making method in above-mentioned bacterial classification, raw material, activator, water thresh twice again, make three-class strain, and be standby;
C, the making of producing bacterium liquid: the ratio in organic-biological compound fertilizer finished product planned production amount 0.256% weighs up soybean, adds 50 ℃-60 ℃ the warm water soaking two hours of 20 times of gross weights, makes the Semen sojae atricolor pulp of water content 9.5% with mechanical disintegration; Ratio in Semen sojae atricolor pulp 3.48% adds soybean nodulation bacteroid three-class strain again; Add " being rich in the aqueous solution of CTP " in the ratio of organic-biological compound fertilizer planned production amount 0.03% again, 30 ℃-10 ℃, the condition lower seal fermentation of PH6-7 3-15 days, it was stand-by to make bacterium liquid;
D, making organic liquid fertilizer: the ratio of occupying machine composite bio-fertilizer finished product planned production amount 6.3% in raw material, bio-wastes such as 95% decayed fruit vegetables, grain will wherein be accounted for, with account for bio-wastes such as 5% pluck, slough, add water to 10 times of gross weights, wear into pulpous state with machinery; Ratio in bio-waste slurry 3.06% adds prefabricated soybean nodulation bacteroid production bacterium liquid again; Add " being rich in the CTP aqueous solution " in the ratio of organic-biological compound fertilizer finished product planned production amount 0.03% again, at PH6-7,30 ℃ of-10 ℃ of condition bottom fermentations 10 days---30 days, make organic liquid fertilizer, stand-by;
Two, the preliminary making of organic-biological compound fertilizer:
A, one grade fermemtation will mix with the fused(calcium magnesium)phosphate of 30%--6.9% mutually through the various bio-wastes handled early stage respectively in the ratio of 57.5%--80.2%; The soybean nodulation bacteroid that adds organic-biological compound fertilizer finished product planned production amount 3.4% is then produced bacterium liquid, add again 0.07% " being rich in the aqueous solution of CTP ", even with mechanical stirring, make the one grade fermemtation blank, PH6--7,30 ℃--under 10 ℃ of conditions, semitight heap fermentation 7--15 days; Finish fermentation;
B, second order fermentation: earlier the one grade fermemtation blank that ferments is taken out, again with prefabricated organic liquid fertilizer; By measuring out of one grade fermemtation blank 49.98%, add " being rich in the aqueous solution of CTP " of occupying machine composite bio-fertilizer planned production output 0.07%, slowly, add dispersedly with in the one grade fermemtation blank in the pulverizer grinding and processing, make the second order fermentation blank of water content 64.9%, pack in the fermentation vat, PH6-7,30 ℃ of-10 ℃ of second sealing and fermenting of condition 5--12 days, treat black, the no foul smell of second order fermentation blank, and when the surface grows the canescence mycoderm of about 1 mm thick, can finish second order fermentation;
The processed of c, second order fermentation: the blank that will finish second order fermentation, placing 25 ℃--evaporation is 2--5 days under 50 ℃ of draughty conditions, when treating that the second order fermentation blank becomes water content 10% dried block, become the particulate of particle diameter 0.1---3 millimeter with mechanical disintegration, promptly become the organic-biological compound fertilizer work in-process, the pack warehouse-in is stand-by;
Three, total preparation of organic-biological compound fertilizer:
Press organic-biological compound fertilizer finished product planned production amount, the urea that adds 4.3%---13% respectively, the Repone K of 3%--11%, the potassium primary phosphate of 0--0.96%, and 0.3%---4.8% " being rich in the aqueous solution of CTP ", 19.7% liquid organic bio-fertilizer, even with mechanical stirring, promptly become the SOLID ORGANIC composite bio-fertilizer finished product of water content 30%, warehouse-in after packing.
The present invention compared with prior art owing to adopt " being rich in the aqueous solution of CTP " bio-stimulant, the mixture (Ca of wherein contained CTP (Cytidine triphosphate), magnesium ion and calcium ion and calmodulin as the soybean nodulation bacteroid
+ 2High-energy such as .CaM), the effect of high reactivity material, the root nodule flora is activated, its ability of decomposing various organic substances improves greatly, thereby it is little in investment, equipment is simple, equipment and raw material be not basically under the disinfectant state, can make bacterial classification by enough root nodule bacteroids, various bio-wastes and fused(calcium magnesium)phosphate fermentation are processed into organic-biological compound fertilizer, thereby reduced production cost widely, make organic bio-fertilizer can become cheap fertilizer, be vast farming, woods the producer accept, for containing the popularization of the organic-biological compound fertilizer that enriches vinelandii, use, favourable condition is provided, simultaneously because the ATP of trace, after magnesium ion, the mixture of calcium ion and calmodulin enter in the plant materials, can play and improve the plant energy metabolism, the substance metabolism ability, and the effect that strengthens cell division capacity, thereby through farmland experiment confirm, farming, the Forest products amount of increase in production is big, and quality obviously improves.Farming, woods crop disease-resistant, cold tolerance also strengthen to some extent; economic benefit to farming, the woods producer is extremely remarkable; simultaneously because this production technique can be processed into fertilizer in enormous quantities with various bio-wastes; turn waste into wealth; therefore can also aspect environment protection and city ecology construction, produce the huge social benefit.
Embodiments of the invention: (is example with the special-purpose fertilizer of tomato).
Bacterial classification: a, root nodule bacteroid original strain
B, saccharifying enzyme (including various mould mattress steamed stuffed buns)
The cud secretory product of c, ox (including a large amount of ciliates)
Raw material: a, various bio-waste;
B, fused(calcium magnesium)phosphate, urea, Repone K,
Substratum: soyflour, dregs of beans, rice bran,
Bacterial classification activator: " being rich in the aqueous solution of CTP ".
One, preparatory process:
1, handles the early stage of various bio-wastes: (carrying the first two months prepares)
1. natural heap fermentation: raw materials such as soy sauce is poor, poor duckweed of alcohol and various vinasse are piled up spontaneous fermentations and can be used to putrescing, and quantity is not limit.
2. add the mould heap fermentation: saccharifying enzyme is joined in the solid medium that 1 kilogram of starch, 6 kilograms of rice brans, 3 kg of water makes in 5% ratio,, make 10.5 kilograms of first class inoculums 30 ℃, PH5--6 condition bottom fermentation 96 hours; In 1: 30 ratio, use with quadrat method and make 310.5 kilograms of second class inoculums again; Use again with quadrat method and make 9310.5 kilograms of three-class strains, join among 279.3 tons of discard tobaccos, stir with platform-type stirrer, pile up in heaps, water the water of total amount 20% again, PH5--6,30 ℃--10 ℃ second sealing and fermenting of condition 10 days--30 days, to the stingless snuff leaf of discard tobacco smell, black and when putrescing, can be stand-by.
3. ox abomasum secretory product is taken out, ratio in 5% joins in the solid medium that 1 kilogram of starch, 6 kilograms of rice brans, 3 kg of water makes, PH5,30 ℃ of condition bottom fermentations 96 hours, make 10.5 kilograms of first class inoculums, in 1: 30 ratio, use with quadrat method and make 310.5 kilograms of second class inoculums again; Use again with quadrat method and make 9310.5 kilograms of three-class strains, add the discarded grass in 279.3 tons of lawns, in the poor and bright straw of the corn through pulverizing of vinegar, corn core, the Chinese medicine slag the like waste, stir with platform-type stirrer, pile up in heapsly, water the water that accounts for total amount 10%, PH5,30 ℃--10 ℃ of second sealing and fermenting 10 horizons of condition 0 day, to waste blackout, deliquescing, and when putrescing, can be stand-by.
2, activate and cultivate soybean nodulation bacteroid bacterial classification: (carrying the first two months prepares)
The soybean nodulation bacteroid is disposed surperficial silt, weigh up 6.58 grams, pulverize with micropulverizer, again 46.2 gram soyflours, 61.6 gram bean cake powders, 46.2 gram fine rice brans are made 154 gram mixing raw materials, add 7.65 grams " being rich in the CTP aqueous solution ", 30 gram aqua sterilisas again, stir, make solid medium, soybean nodulation bacteroid after will pulverizing is then evenly admixed in the substratum, PH6--7,30 ℃--35 ℃ of second sealing and fermenting of condition 120 hours, make 198 gram first class inoculums.Ratio and making method in above-mentioned bacterial classification, raw material, activator, water thresh twice again, make 179 kilograms of soybean nodulation bacteroid three-class strains, and be stand-by;
3, produce the making of bacterium liquid: (preparing in 45 days in advance)
With 256.1 kilograms of soybean, with 4865.9 kilograms 50 ℃--60 ℃ warm water soaking two hours, make 5122 kilograms of Semen sojae atricolor pulp with paste roller mill, add 178 kilograms of soybean nodulation bacteroid three-class strains again, add 30 kilograms " being rich in the CTP aqueous solution " again, PH6--7,30 ℃--10 ℃ of condition lower seals fermentations 3--15 days, make 5330 kilograms of soybean nodulation bacteroids and produce bacterial classifications, stand-by;
4, make organic liquid fertilizer: (preparing in 30 days in advance)
Bio-wastes (also available 600 kilograms of dregs of beans substitute) such as the pluck that bio-waste such as 6 tons of mashed vegetables, rotten fruit, mashed grain, pericarp, dish nation and 300 kilograms of slaughterhouse depleted frees from infection are polluted, slough add 42.2 tons of water, wear into 48.5 tons of slurries with paste roller mill; Add 1930 kilograms of soybean nodulation bacteroids again and produce bacterium liquid and 30 kilograms " being rich in the CTP aqueous solution ", PH6--7,30 ℃--10 ℃ of condition bottom fermentations 10--30 days, make 62.3 tons of organic liquid fertilizers, stand-by;
Two, the preliminary making of organic-biological compound fertilizer:
1, one grade fermemtation:
83.03 tons of processes are handled various bio-wastes and 8 tons of phosphorous (P of moisture 30% in earlier stage
2O
5) be not less than 16% fused(calcium magnesium)phosphate and mix, add 3400 kilograms of prefabricated soybean nodulation bacteroids again and produce bacterium liquid and 70 kilograms " being rich in the aqueous solution of CTP ", stir with platform-type stirrer, make 94.5 tons of organic-biological compound fertilizer one grade fermemtation blanks, PH6--7,30 ℃--10 ℃ of second sealing and fermenting of condition 7--15 days, finish fermentation;
2, second order fermentation:
Earlier the one grade fermemtation blank that ferments is taken out, add 47.23 tons of prefabricated organic liquid fertilizers, add 70 kilograms " being rich in the CTP aqueous solution " again, slowly, add dispersedly and using in the one grade fermemtation blank of bell chip pulverizer grinding and processing, make the organic-biological compound fertilizer second order fermentation blank of 141.8 tons of water contents 64.9%, pack in the fermentation vat, at PH6--7,30 ℃--10 ℃ of second sealing and fermenting of condition 5--12 days, treat that the second order fermentation blank is black, no foul smell, and when the surface grows the canescence mycoderm of about mm thick, can finish second order fermentation;
3, the processed of second order fermentation:
The blank of second order fermentation will be finished, placing 25 ℃--sun-exposed airing or 35 ℃-50 ℃ draughty drying rooms of 35 ℃ evaporated 2--5 days, when treating that the second order fermentation blank becomes water content 10% dried block, be ground into the particulate of particle diameter 2-3 millimeter again with fluted disc crusher, promptly become 63.95 tons of the special-purpose organic-biological compound fertilizer work in-process of tomato, the pack warehouse-in is stand-by;
Three, tomato total preparation of organic-biological compound fertilizer:
8.85 tons of urea, 7.2 tons of Repone K, 300 kilograms " being rich in the CTP aqueous solution ", 19.7 tons of organic liquid fertilizers will be added in 63.95 tons of work in-process, stir with platform-type stirrer, promptly obtain 100 tons of tomato organic-biological compound fertilizer finished products, warehouse-in after packing.
Claims (1)
1, a kind of production technique with bio-waste processing organic-biological compound fertilizer, it is to activate soybean nodulation bacteroid bacterial classification with " being rich in the CTP aqueous solution ", with various bio-wastes and small amount of calcium magnesium-phosphorus fertilizer mixture after the fermentation of the two poles of the earth, again through middle temperature is dried, pulverizing, at last again with a small amount of urea, Repone K, potassium primary phosphate, and the organic-biological compound fertilizer of a small amount of " being rich in the CTP aqueous solution " formulated different varieties, it is characterized in that:
(1), preparatory process:
Handle the early stage of a, bio-waste: adopt the method for heap fermentation that various bio-wastes are tentatively decomposed, and as organic matter material, standby;
B, activation are also cultivated soybean nodulation bacteroid bacterial classification: exsiccant soybean nodulation bacteroid is cleaned up, need weigh up the soybean nodulation bacteroid with the ratio of 6.58 gram original strains in per hundred tons of organic-biological compound fertilizer finished products, use mechanical disintegration; Again in the ratio of 23.4 times of original strain amounts, be made into mixing raw material with accounting for the soyflour of solid medium material quantity 30%, 40% bean cake powder, 15.6% fine rice bran; Add " being rich in the CTP aqueous solution ", 20% the aqua sterilisa of raw material consumption 5% again, make solid medium; Soybean nodulation bacteroid after pulverizing is evenly admixed in the substratum, and semitight was cultivated 120 hours under PH6-7,30 ℃ of-35 ℃ of conditions, made first class inoculum; Ratio and making method in above-mentioned bacterial classification, raw material, activator, water thresh twice again, make three-class strain, and be standby;
C, the making of producing bacterium liquid: the ratio in organic-biological compound fertilizer finished product planned production amount 0.256% weighs up soybean, adds 50 ℃-60 ℃ the warm water soaking two hours of 20 times of gross weights, makes the Semen sojae atricolor pulp of water content 9.5% with mechanical disintegration; Ratio in Semen sojae atricolor pulp 3.48% adds soybean nodulation bacteroid three-class strain again; 0.03% ratio in organic-biological compound fertilizer planned production amount adds " being rich in the CTP aqueous solution " again, and 30 ℃-10 ℃, the condition lower seal fermentation of PH6-7 3-15 days, it was stand-by to make bacterium liquid;
D, making organic liquid fertilizer: the ratio of occupying machine composite bio-fertilizer finished product planned production amount 6.3% in raw material, with decayed fruit vegetables, the grain bio-waste that wherein accounts for 95%, pluck, slough bio-waste with accounting for 5% add water to 10 times of gross weights, wear into pulpous state with machinery; Ratio in bio-waste slurry 3.06% adds prefabricated soybean nodulation bacteroid production bacterium liquid again; Add " being rich in the CTP aqueous solution " in the ratio of organic-biological compound fertilizer finished product planned production amount 0.03% again, at PH6-7,30 ℃ of-10 ℃ of condition bottom fermentations 10 days---30 days, make organic liquid fertilizer, stand-by;
(2), the preliminary making of organic-biological compound fertilizer:
A, one grade fermemtation will mix with the fused(calcium magnesium)phosphate of 30%--6.9% mutually through the various bio-wastes handled early stage respectively in the ratio of 57.5%--80.2%; The soybean nodulation bacteroid that adds organic-biological compound fertilizer finished product planned production amount 3.4% is then produced bacterium liquid, add 0.07% " being rich in the CTP aqueous solution " again, even with mechanical stirring, make the one grade fermemtation blank, PH6-7,30 ℃--under 10 ℃ of conditions, semitight heap fermentation 7-15 days; Finish fermentation;
B, second order fermentation: earlier the one grade fermemtation blank that ferments is taken out, again with prefabricated organic liquid fertilizer; By measuring out of one grade fermemtation blank 49.98%, add " being rich in the CTP aqueous solution " of occupying machine composite bio-fertilizer planned production output 0.07%, slowly, add dispersedly with in the one grade fermemtation blank in the pulverizer grinding and processing, make the second order fermentation blank that contains moisture 64.9%, pack in the fermentation vat, PH6-7,30 ℃ of-10 ℃ of second sealing and fermenting of condition 5--12 days, treat black, the no foul smell of second order fermentation blank, and when the surface grows the canescence mycoderm of about 1 mm thick, can finish second order fermentation;
The processed of c, second order fermentation: the blank that will finish second order fermentation, placing 25 ℃--evaporation is 2-5 days under 50 ℃ of draughty conditions, when treating that the second order fermentation blank becomes water content 10% dried block, become the particulate of particle diameter 0.1---3 millimeter with mechanical disintegration, promptly become the organic-biological compound fertilizer work in-process, the pack warehouse-in is stand-by;
(3), total preparation of organic-biological compound fertilizer;
Press organic-biological compound fertilizer finished product planned production amount, the urea that adds 4.3%---13% respectively, the Repone K of 3%--11%, the potassium primary phosphate of 0-0.96%, and 0.3%---4.8% " being rich in the CTP aqueous solution ", 19.7% liquid organic bio-fertilizer, even with mechanical stirring, promptly become the SOLID ORGANIC composite bio-fertilizer finished product of water content 30%, warehouse-in after packing.
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| CNB021137560A CN1246260C (en) | 2002-05-17 | 2002-05-17 | Process for producing organic biological composite fertilizer from biological wase material |
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| CN103265341B (en) * | 2013-06-14 | 2015-04-01 | 河北新世纪周天生物科技有限公司 | Preparation technology of microorganism-containing nitrogen manure |
| CN107759345A (en) * | 2017-11-22 | 2018-03-06 | 中国科学院地理科学与资源研究所 | Film-coated controlled release fertilizer and its production technology containing rhizobium |
| CN108753654A (en) * | 2018-06-14 | 2018-11-06 | 傅责中 | A kind of production technology of high activity rhizobium strain and its processing organic fertilizer rich in nitrogen-fixing bacteria |
| CN113402313A (en) * | 2021-06-24 | 2021-09-17 | 贵州鸿洋生物有机肥有限公司 | Cytidine triphosphate biological organic solid fertilizer formula and production method thereof |
| CN113416101A (en) * | 2021-06-24 | 2021-09-21 | 贵州鸿洋生物有机肥有限公司 | Cytidine triphosphate biological organic liquid fertilizer formula and production method thereof |
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