CN204058282U - The vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer - Google Patents
The vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer Download PDFInfo
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- CN204058282U CN204058282U CN201420000935.5U CN201420000935U CN204058282U CN 204058282 U CN204058282 U CN 204058282U CN 201420000935 U CN201420000935 U CN 201420000935U CN 204058282 U CN204058282 U CN 204058282U
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- 241000255789 Bombyx mori Species 0.000 title claims abstract description 85
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 28
- 239000003895 organic fertilizer Substances 0.000 title claims description 25
- 239000002131 composite material Substances 0.000 title claims description 23
- 238000000855 fermentation Methods 0.000 claims abstract description 36
- 230000004151 fermentation Effects 0.000 claims abstract description 35
- 238000002156 mixing Methods 0.000 claims abstract description 35
- 238000010563 solid-state fermentation Methods 0.000 claims abstract description 33
- 239000000463 material Substances 0.000 claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 239000000843 powder Substances 0.000 claims abstract description 13
- 239000003337 fertilizer Substances 0.000 claims abstract description 12
- 239000011343 solid material Substances 0.000 claims abstract description 10
- 239000000523 sample Substances 0.000 claims description 10
- 238000007790 scraping Methods 0.000 claims description 9
- 230000005540 biological transmission Effects 0.000 claims description 7
- 239000003595 mist Substances 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- 230000008901 benefit Effects 0.000 abstract description 8
- 210000003608 fece Anatomy 0.000 abstract description 4
- 150000001875 compounds Chemical class 0.000 abstract description 3
- 230000007306 turnover Effects 0.000 abstract description 2
- 239000010871 livestock manure Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 15
- 241000894006 Bacteria Species 0.000 description 6
- 239000004567 concrete Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000009366 sericulture Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 241000272165 Charadriidae Species 0.000 description 2
- 240000000249 Morus alba Species 0.000 description 2
- 235000008708 Morus alba Nutrition 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000002068 microbial inoculum Substances 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000186361 Actinobacteria <class> Species 0.000 description 1
- 241000255783 Bombycidae Species 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000000680 avirulence Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 125000000837 carbohydrate group Chemical group 0.000 description 1
- 239000011083 cement mortar Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229930002875 chlorophyll Natural products 0.000 description 1
- 235000019804 chlorophyll Nutrition 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000002921 fermentation waste Substances 0.000 description 1
- 238000012262 fermentative production Methods 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002918 waste heat 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Fertilizers (AREA)
Abstract
The utility model provides a kind of silkworm excrement compound manure vertical continuous solid-state production equipment, solid material mixing machine A, continuous solid-state fermentation device, wrapping machine, powder delivery pump are set and admittedly expect mixing machine B, admittedly expect mixing machine A, continuous solid-state fermentation device, wrapping machine, powder delivery pump and admittedly expect that mixing machine B is connected successively; The continuous solid-state fermentation device that described continuous solid-state fermentation device adopts the applicant to apply on the same day, this device is set to vertical square structure, tower body arranges solid-liquid mixed cell, fermentation unit and drying unit, solid-liquid mixed cell is located at tower body epimere, fermentation unit is located at tower body stage casing, and drying unit is located at tower body hypomere.The turnover of this device material is smooth and easy, effective use of energy sources, shortens the fermentation time of fertilizer, improves solid state fermentation efficiency, this apparatus structure is simple, easily operates, constant product quality, facility investment is few, can realize suitability for industrialized production, has good economic benefit, social benefit and ecological benefits.
Description
Invention field
The present invention relates to fertilizer processing units, particularly relate to the vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer, belong to field of mechanical technique.
Background technology
Silkworm excrement (silkworm fece) is also known as silkworm faeces, silkworm dung, and ancient times claims late silkworm excrement, two silkworm excrements, silkworm excrement, for Bombycidae insect silkworm (Bombyx mori L.) larva ingests the movement after mulberry leaf.The major ingredient of silkworm excrement is carbohydrate, robust fibre, is a kind of weakly alkaline fertilizer.Dry silkworm excrement, in short cylindrical shape, two ends are slightly smooth, long 2-5 millimeter, diameter 1.5-3 millimeter.Furvous, surface irregularity, having 6 shallow lines significantly indulging rib and 3-4 bar transverse direction, is six prismatic.Matter is hard and crisp, easily fragmentary after wet is wet.Micro-have green grass gas.The provinces and regions such as main product Guangxi, Jiangsu, Zhejiang, Sichuan, Chongqing, Guangdong, Shandong, Anhui, Yunnan, Henan, Hunan, Hubei.Nowadays, the maximum producing region of Guangxi Yi Shi China silk industry, silk is produced throughout counties and cities of the whole district 65%, relate to the livelihood of nearly 880,000 peasant household 3,500,000 population common people, year sericulture more than 450 ten thousand kinds, produce cocoon 200,000 tons per year, account for 1/4 of national total amount, year, silkworm waste elimination-silkworm excrement amount was about more than 1,500,000 tons.Existing silkworm excrement treatment process is except minority is as fermentation and biogas production, and for peasant household, oneself makes fuel and silkworm excrement production bio-fertilizer.Therefore, silkworm excrement is still stacked in a large number everywhere in silkworm producing region.Along with development and the popularization of mulberry sericulture are planted by China, silkworm excrement is not treated directly to be stacked everywhere, equally with other domestic refuse become new source of pollution, become the biggest factor of the diffusion of various flacherie cause of disease and the main contributor spread and environmental pollution, become the maximum bottleneck problem hindering the Sustainable development of Sericultural production high and stable yields high-quality.Specialty utilizes silkworm excrement to be the important means solving the waste of current sericulture there waste, environmental pollution and stop the diffusion of residual pathogenic bacteria.Silkworm excrement fermentation fertilizer is recycled, not only can extenuate because of a large amount of discarded silkworm excrement pollution on the environment, widen the raw material channel of fertilizer, and can soil acidity be regulated, increase soil fertility and protect function, there is good economy, ecology and social benefit.
The number of applying for a patent CN201110274990.4, the method for the fertilizer utilizing silkworm excrement fermentative production facility cultivation special.The method comprises: silkworm excrement mixes with microbial bacteria, carries out thermophilic fermentation after stirring.Fermentation initial adjustment water ratio is 55-60%, C/N ratio is about 25-30/1, and carry out turning ventilation, turning after temperature rises to 60 DEG C, stirred once every 24 hours.When heap temperature is down to envrionment temperature, fermentation completes substantially, altogether takes 12-16 days.Carry out drying, granulation again, sieving forms.Described silkworm excrement comprises directly to be collected next mixing silkworm excrement from peasant household or has extracted the discarded silkworm excrement after chlorophyll; Microbial bacteria comprises bud pole bacterium, actinomycetes, vinelandii, milk-acid bacteria, avirulence Bacterium lacticum or its mixed strains.
The number of applying for a patent CN201210304737.3, silkworm excrement innocent treatment method.By silkworm raiser by building described silkworm excrement room in units of family, build the outlying lower air port place from river of village in.Described silkworm excrement room is made up of top cover and three face walls, and the ground of described silkworm excrement indoor and outdoor ground intersection form interior low outer high step.Described silkworm excrement room wide be 2-4 rice, long be 3-6 rice.The method step: A, after matured silkworm is all put on an arrow silkworm excrement cleaning before, be watered the 70-100 kilogram of diluent formed with often liter of VT-1000 microbial inoculum or compound bud pole bacteria microorganism microbial inoculum and evenly spray silkworm excrement, make often liter of microbiobacterial agent spray the silkworm excrement of 360-450 kilogram, water content control is within the scope of 50-55%; B, the silkworm excrement spraying described diluent transported to silkworm excrement indoor and rick and advance row pile fermentation, described silkworm excrement room has the top cover of rain cover and the port with ft connection; C, silkworm excrement became thoroughly decomposed after pile fermentation completely through 10-20 days, back to the field to use in case of need, if wouldn't need go back to field, the new silkworm excrement produced is added in described silkworm excrement room after processing of step A, is deposited on the silkworm excrement buttress heap that ferments or fermented and carries out pile fermentation.
The number of applying for a patent CN200720004350.0, a kind of pool for processing silkworm excrement.This treating pond comprises material storing room, opening for feed, discharge port, and material storing room is arranged on above level land or below level land; Body of wall is brick or slabstone or cement concrete structure, and bottom surface is cement concrete, and end face is reinforced cement concrete, and indoor wall is that cement mortar is floating; Opening for feed is arranged on material storing room's end face, and surrounding slightly exceeds end face, for one or more; Discharge port is arranged on the side of material storing room; Opening for feed and discharge port can be opened also can hold one's breath and seal.This patent is intended to adopt the mode improving pool for processing silkworm excrement, and unified process silkworm excrement in airtight environment, be a kind of anaerobic fermentation method, airtight environment plays the effect of isolated silkworm excrement contaminate environment.Its by concrete implementation step by the construction simplification of pool for processing silkworm excrement, standardization.
The number of applying for a patent CN201210338974.1, plants the innoxious aerobic static composting treatment process of silkworm excrement.The method comprises the following steps: the bottom built for the treatment of pond is formed Stilt layer by (1); (2) tile one deck amendment on frame; (3) conditioning oxidant layer on pour the mixture of silkworm excrement and amendment into after pave, or pour silkworm excrement in turn into, amendment formed multiple composite bed accumulation; (4) finally one deck amendment is covered again on the top layer for the treatment of pond stores.Described built on stilts floor height 8-11cm; The amendment thickness that frame tiles is 5-10cm.In described silkworm excrement amendment mixture, the weight ratio of silkworm excrement and amendment is 7-9: 1-3, and piling height is 80-90cm, and the carbon-nitrogen ratio (C/N) adopting silkworm excrement is 10-30: 1.Described silkworm excrement amendment composite bed is pressed silkworm excrement-amendment-silkworm excrement compound successively and is piled up, and the weight ratio of layering silkworm excrement and amendment is 8: 2; Total piling height is 80-90cm, and the carbon-nitrogen ratio (C/N) adopting silkworm excrement is 10-30: 1.It is 5-10cm that described top layer finally covers one deck amendment thickness.Described amendment selects wooden chaff or husk.
The above number of applying for a patent CN201210338974.1 method small scale, floor space is large, and labour intensity is high, and fermentation time is long, and production efficiency is low, the technical problem of unstable product quality.The above other apply for a patent method and belong to Traditional compost method, also there is scale less, labour intensity is large, and fermentation time is long, and production efficiency is low, the technical problem of unstable product quality.At present, there is no vertical continuous solid-state fermentation device process silkworm excrement.
Summary of the invention
Object of the present invention is overcome the deficiency that oneself has silkworm excrement fertilizer processing technology, and provide a kind of larger, labour intensity is low, and fermentation time is short, and production efficiency is high, the vertical continuous solid-state production equipment of silkworm excrement composite organic fertilizer of constant product quality.
The present invention is achieved in that
The vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer, solid material mixing machine A, vertical continuous solid-state fermentation device, wrapping machine, powder delivery pump are set and admittedly expect mixing machine B, admittedly expect mixing machine A, vertical continuous solid-state fermentation device, wrapping machine, powder delivery pump and admittedly expect that mixing machine B is connected successively; The vertical continuous solid-state fermentation device that described vertical continuous solid-state fermentation device adopts the applicant to apply on the same day.
Described solid material mixing machine A arranges opening for feed, discharge port and agitator; Described discharge port is provided with switch.
Described solid material mixing machine B arranges opening for feed, discharge port and agitator; Described discharge port is provided with switch.
Described agitator is trilateral vertical plate type stirring rake, and in rotating shaft, correspondence arranges size each 1 piece or each 2 pieces of the size that is crisscross arranged.
Described vertical continuous solid-state fermentation device is vertical square structure, and tower body arranges solid-liquid mixed cell, fermentation unit and drying unit, and solid-liquid mixed cell is located at tower body epimere, and fermentation unit is located at tower body stage casing, and drying unit is located at tower body hypomere; Described fermentation unit is provided with stock supporting plate, recirculation blower, mist pipe, blowpipe, warm and humid probe; Described recirculation blower is connected with the blast inlet of fermentation unit and air outlet being located at tower body; Described solid-liquid mixed cell sets gradually material storing room, solid-liquid mixing section, sparge pipe, transmission rig A, material scraping plate A; Described drying unit is provided with stock supporting plate, material scraping plate B, transmission rig B, discharge port, backwind tube, blowpipe, temperature probe, and drying unit is separately provided with powdered fertilizer charging opening, and charging opening is successively with powder delivery pump with admittedly expect that mixing machine B is connected.
Advantage of the present invention and positively effect:
1, the vertical continuous solid-state production equipment of silkworm excrement composite organic fertilizer of the present invention, the solid-liquid mixed cell of vertical continuous solid-state fermentation device, fermentation unit and drying unit are set, solid-liquid mixed cell is located at tower body epimere, and fermentation unit is located at tower body stage casing, and drying unit is located at tower body hypomere; Effectively utilize silkworm excrement to process organic fertilizer, realize vertical serialization solid state fermentation.
2, the vertical continuous solid-state production equipment of this silkworm excrement composite organic fertilizer, the vertical continuous solid-state fermentation device of setting is provided with the oblique stock supporting plate of uniform small pores, material scraping plate A and material scraping plate B, and material turnover is smooth and easy.
3, the vertical continuous solid-state production equipment of this silkworm excrement composite organic fertilizer, the vertical continuous solid-state fermentation device arranged is provided with well heater, blower fan, recirculation blower, warm and humid probe, ensure condition that is dry and fermentation, effective use of energy sources, shorten the fermentation time of silkworm excrement organic fertilizer, improve solid state fermentation efficiency.
4, the vertical continuous solid-state production equipment of this silkworm excrement composite organic fertilizer, the vertical continuous solid-state fermentation device of setting is provided with solid-liquid mixing section and sparge pipe, can ensure zymogenicly to add and mix.
5, the vertical continuous solid-state production equipment of this silkworm excrement composite organic fertilizer, the vertical continuous solid-state fermentation device arranged is provided with powder delivery pump and admittedly expects mixing machine B, can ensure evenly adding and mixing with silkworm excrement organic fertilizer of solid state organic fertilizer, Solid inorganic fertilizer and trace element.
6, the vertical continuous solid-state production equipment of this silkworm excrement composite organic fertilizer, the vertical continuous solid-state fermentation device of setting is provided with drying unit can make full use of the dry silkworm excrement composite organic fertilizer of waste heat, and provides thermal source for solid state fermentation.
7, the vertical continuous solid-state production equipment of this silkworm excrement composite organic fertilizer, the vertical continuous solid-state fermentation device of setting is provided with recirculation blower, can ensure that fermentation unit is to organic fermentations such as silkworm excrements, makes full use of fermentation waste heat.
8, this silkworm excrement composite organic fertilizer vertical continuous solid-state production equipment structure is simple, and easily operate, constant product quality, facility investment is few, can realize industrialization solid state fermentation, has good economic benefit, social benefit and ecological benefits.
Accompanying drawing explanation
Fig. 1: be silkworm excrement composite organic fertilizer vertical continuous solid-state production equipment schematic diagram;
Identify in figure: 1-expects mixing machine A admittedly; 2-agitator 2; The vertical continuous solid-state fermentation device of 3-; 4-wrapping machine; 5-powder delivery pump; 6-expects mixing machine B admittedly.
Embodiment
The following examples further illustrate of the present invention.
Embodiment 1
The vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer, solid material mixing machine A1, vertical continuous solid-state fermentation device 3, wrapping machine 4, powder delivery pump 5 are set and admittedly expect mixing machine B6, admittedly expect mixing machine A1, vertical continuous solid-state fermentation device 3, wrapping machine 4, powder delivery pump 5 and admittedly expect that mixing machine B6 is connected successively; The vertical continuous solid-state fermentation device that described vertical continuous solid-state fermentation device 3 adopts the applicant to apply on the same day.
Described solid material mixing machine A1 arranges opening for feed, discharge port and agitator 2; Described discharge port is provided with switch.
Described solid material mixing machine B6 arranges opening for feed, discharge port and agitator 2; Described discharge port is provided with switch.
Described agitator 2 is trilateral vertical plate type stirring rake, and in rotating shaft, correspondence arranges size each 1 piece or each 2 pieces of the size that is crisscross arranged.
Described vertical continuous solid-state fermentation device 3 is vertical square structure, and tower body arranges solid-liquid mixed cell, fermentation unit and drying unit, and solid-liquid mixed cell is located at tower body epimere, and fermentation unit is located at tower body stage casing, and drying unit is located at tower body hypomere; Described fermentation unit is provided with stock supporting plate, recirculation blower, mist pipe, blowpipe, warm and humid probe; Described recirculation blower is connected with the blast inlet of fermentation unit and air outlet being located at tower body; Described solid-liquid mixed cell sets gradually material storing room, solid-liquid mixing section, sparge pipe, transmission rig A, material scraping plate A; Described drying unit is provided with stock supporting plate, material scraping plate B, transmission rig B, discharge port, backwind tube, blowpipe, temperature probe.The length of described stock supporting plate is identical with the length in tower body, and the width of stock supporting plate is less than the width in tower body, is evenly alternately located at the corresponding surface of tower body, forms " S " material channel; The stock supporting plate being staggered in tower body welds bottom high one side and arranges mist pipe, blowpipe, warm and humid probe respectively, and mist pipe, blowpipe are connected with water-main, blast main respectively by valve, and warm and humid probe is connected with warm and humid controller.
Described recirculation blower is connected with the blast inlet of fermentation unit and air outlet being located at tower body, blast inlet is located at fermentation unit epimere stock supporting plate and welds on the tower body bottom high one side, the fermentation unit hypomere stock supporting plate that air outlet is located at tower body weld high bottom tower body on.
Described solid-liquid mixed cell sets gradually material storing room, solid-liquid mixing section, sparge pipe, transmission rig A, material scraping plate A; The same plane of described sparge pipe evenly arranges jet hole, and upwards, sparge pipe is connected with the liquid-inlet pipe being provided with valve and under meter jet hole.
Described drying unit is provided with the backwind tube being located at discharge port, conventional cyclonic separator, well heater, blower fan, blast main and blowpipe, and connects successively; Warm and humid probe is connected with temperature control instrument; Drying unit is separately provided with powdered fertilizer charging opening, and charging opening is successively with powder delivery pump 5 with admittedly expect that mixing machine B6 is connected.
Claims (5)
1. the vertical continuous solid-state production equipment of silkworm excrement composite organic fertilizer, it is characterized in that: solid material mixing machine A (1), vertical continuous solid-state fermentation device (3), wrapping machine (4), powder delivery pump (5) are set and admittedly expect mixing machine B (6), admittedly expect mixing machine A (1), vertical continuous solid-state fermentation device (3), wrapping machine (4), powder delivery pump (5) and admittedly expect that mixing machine B (6) is connected successively; The vertical continuous solid-state fermentation device that described vertical continuous solid-state fermentation device (3) adopts the applicant to apply on the same day.
2. the vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer according to claim 1, is characterized in that: described solid material mixing machine A (1) arranges opening for feed, discharge port and agitator (2); Described discharge port is provided with switch.
3. the vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer according to claim 1, is characterized in that: described solid material mixing machine B (6) arranges opening for feed, discharge port and agitator (2); Described discharge port is provided with switch.
4. the vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer according to Claims 2 or 3, it is characterized in that: described agitator (2) is trilateral vertical plate type stirring rake, in rotating shaft, correspondence arranges size each 1 piece or each 2 pieces of the size that is crisscross arranged.
5. the vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer according to claim 1, it is characterized in that: described vertical continuous solid-state fermentation device (3) is vertical square structure, tower body arranges solid-liquid mixed cell, fermentation unit and drying unit, solid-liquid mixed cell is located at tower body epimere, fermentation unit is located at tower body stage casing, and drying unit is located at tower body hypomere; Described fermentation unit is provided with stock supporting plate, recirculation blower, mist pipe, blowpipe, warm and humid probe; Described recirculation blower is connected with the blast inlet of fermentation unit and air outlet being located at tower body; Described solid-liquid mixed cell sets gradually material storing room, solid-liquid mixing section, sparge pipe, transmission rig A, material scraping plate A; Described drying unit is provided with stock supporting plate, material scraping plate B, transmission rig B, discharge port, backwind tube, blowpipe, temperature probe, drying unit is separately provided with powdered fertilizer charging opening, and charging opening is successively with powder delivery pump (5) with admittedly expect that mixing machine B (6) is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420000935.5U CN204058282U (en) | 2014-01-02 | 2014-01-02 | The vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420000935.5U CN204058282U (en) | 2014-01-02 | 2014-01-02 | The vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer |
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| CN204058282U true CN204058282U (en) | 2014-12-31 |
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| CN201420000935.5U Expired - Fee Related CN204058282U (en) | 2014-01-02 | 2014-01-02 | The vertical continuous solid-state production equipment of a kind of silkworm excrement composite organic fertilizer |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103804046A (en) * | 2014-02-19 | 2014-05-21 | 广西三堡农业科技有限公司 | Vertical continuous solid state production device of silkworm excrement compound organic fertilizer |
| CN106396983A (en) * | 2016-11-30 | 2017-02-15 | 广西壮族自治区药用植物园 | Water-retention and growth-promoting fertilizer for planting gynostemma pentaphylla as well as preparation method and use method of fertilizer |
-
2014
- 2014-01-02 CN CN201420000935.5U patent/CN204058282U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103804046A (en) * | 2014-02-19 | 2014-05-21 | 广西三堡农业科技有限公司 | Vertical continuous solid state production device of silkworm excrement compound organic fertilizer |
| CN106396983A (en) * | 2016-11-30 | 2017-02-15 | 广西壮族自治区药用植物园 | Water-retention and growth-promoting fertilizer for planting gynostemma pentaphylla as well as preparation method and use method of fertilizer |
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