CN115536442A - Fermentation equipment bacterial sprinkler - Google Patents
Fermentation equipment bacterial sprinkler Download PDFInfo
- Publication number
- CN115536442A CN115536442A CN202211345125.9A CN202211345125A CN115536442A CN 115536442 A CN115536442 A CN 115536442A CN 202211345125 A CN202211345125 A CN 202211345125A CN 115536442 A CN115536442 A CN 115536442A
- Authority
- CN
- China
- Prior art keywords
- sprinkler
- fermentation
- strain
- fermentation equipment
- level
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000855 fermentation Methods 0.000 title claims abstract description 43
- 230000004151 fermentation Effects 0.000 title claims abstract description 43
- 230000001580 bacterial effect Effects 0.000 title claims abstract description 12
- 238000005507 spraying Methods 0.000 claims abstract description 39
- 238000007599 discharging Methods 0.000 claims abstract description 26
- 239000007921 spray Substances 0.000 claims abstract description 24
- 238000010564 aerobic fermentation Methods 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims description 31
- 230000002572 peristaltic effect Effects 0.000 claims description 3
- 210000003608 fece Anatomy 0.000 abstract description 14
- 239000010871 livestock manure Substances 0.000 abstract description 14
- 239000003895 organic fertilizer Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 241001465754 Metazoa Species 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 34
- 241000894006 Bacteria Species 0.000 description 22
- 238000002955 isolation Methods 0.000 description 19
- 241000287828 Gallus gallus Species 0.000 description 9
- 238000002156 mixing Methods 0.000 description 6
- 230000008901 benefit Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 244000052616 bacterial pathogen Species 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000011550 stock solution Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- 235000019750 Crude protein Nutrition 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F3/00—Fertilisers from human or animal excrements, e.g. manure
- C05F3/06—Apparatus for the manufacture
-
- 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
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Fertilizers (AREA)
Abstract
The invention relates to a strain spraying device of fermentation equipment, and belongs to the technical field of animal manure organic fertilizer treatment projects. Fermentation equipment bacterial spraying machine sprays with the second grade including the one-level of connecting, and the second grade sprays the discharging pipe that the inlet pipe was sprayed with the one-level and is connected, the one-level sprays and is linked together with the discharging pipe of blendor, and the blendor sprays the feed to the one-level, the discharging pipe that the second grade sprayed is linked together with aerobic fermentation storehouse, to aerobic fermentation storehouse feed. Compared with the prior art, the invention has the following beneficial effects: according to the strain spraying device of the fermentation equipment, strain fermentation liquor is added into excrement and is uniformly mixed, so that the use requirement is met.
Description
Technical Field
The invention relates to a strain spraying device of fermentation equipment, and belongs to the technical field of animal manure organic fertilizer treatment projects.
Background
At present, all countries in the world pay attention to environmental protection and ecological recycling of waste resources due to environmental pollution, resource shortage and food safety.
The chicken manure contains rich nutrition, wherein 18.7 percent of crude protein, 2.5 percent of fat, 13 percent of ash, 11 percent of carbohydrate, 7 percent of fiber, 2.34 percent of nitrogen, 2.32 percent of phosphorus and 0.83 percent of potassium which are respectively 4.1 times, 5.1 times and 1.8 times of pig manure, the utilization value is very high, the chicken manure is fermented at low cost, and the chicken manure can be used as pig feed, cattle and sheep additive auxiliary materials and fish breeding feed. Therefore, the chicken manure is applied to crops after being subjected to harmless treatment and completely decomposed. The micro-ecological fermentation method is an economical and practical treatment method. Through the decomposition and fermentation of the beneficial fermentation microbial colonies, the culture wastes such as excrement and the like are quickly converted, and the effects of eliminating malodor and inhibiting pests and germs are achieved.
The most important step of the micro-ecological fermentation method is to add strain fermentation liquor into excrement and urine and mix the strain fermentation liquor uniformly, and the strain spraying device of the existing fermentation equipment cannot achieve the best effect due to the design problem.
Disclosure of Invention
According to the defects in the prior art, the technical problems to be solved by the invention are as follows: in order to solve one of the problems, the strain spraying device of the fermentation equipment is provided, and strain fermentation liquor is added into excrement and is uniformly mixed.
The invention relates to a strain spraying device of fermentation equipment, which is characterized in that: fermentation equipment bacterial spraying machine sprays with the second grade including the one-level of connecting, and the second grade sprays the discharging pipe that the inlet pipe was sprayed with the one-level and is connected, the one-level sprays and is linked together with the discharging pipe of blendor, and the blendor sprays the feed to the one-level, the discharging pipe that the second grade sprayed is linked together with aerobic fermentation storehouse, to aerobic fermentation storehouse feed.
Further, the one-level sprays including outer barrel, outer barrel cross-section is circular, the upper end cover is installed to the open-top of outer barrel, the bottom end cover is installed to the bottom opening of outer barrel, the inside coaxial isolation barrel A that is provided with of outer barrel, the barrel in the inside coaxial setting of isolation barrel A, the lower surface at the upper end cover is all fixed to the upper end of isolation barrel A and interior barrel, the bottom of isolation barrel A and interior barrel all links board fixed connection with the centre, the centre links the board and is the annular structure, and its major circle is connected with isolation barrel A, and its minor circle is connected with interior barrel, enclose synthetic stock solution chamber between interior barrel, isolation barrel A, upper end cover and the centre links the board, the punishment in advance clearance has between board and the lower end cover in the centre, the inlet of shower nozzle is linked together with the stock solution chamber, the internal main piston that has of inner tube, the center of upper end cover is installed the main hydraulic cylinder that the main piston of drive moved along inner tube length direction, be provided with the main piston valve that the discharging pipe upper end cover and the inlet pipe upper end cover move along the length direction of inlet pipe and the auxiliary gate valve that the inner tube was provided with the inlet pipe respectively.
Furthermore, the gap between the middle connecting plate and the lower end cover is set to be 1-3cm.
Furthermore, the middle connecting plate is of an annular structure, a plurality of groups of spray heads are distributed on the middle connecting plate at equal intervals, the plurality of groups of spray heads are all positioned on the same circle with the center of circle of the middle connecting plate, and a one-way valve is arranged at the inlet of each spray head.
Furthermore, the auxiliary hydraulic cylinders are provided with a plurality of groups, are all positioned on the same circle with the circle center of the end cover as the circle center, and simultaneously drive the annular piston to descend or ascend.
Furthermore, the inlet and the outlet of the bacteria liquid pump are respectively connected with the bacteria liquid storage tank and the liquid storage cavity, and the bacteria liquid pump is a peristaltic pump.
The invention also provides a fermentation equipment strain spraying system which is characterized by comprising a mixer, a fermentation equipment strain spraying device and an aerobic fermentation bin, wherein the fermentation equipment strain spraying device is used for spraying the fermentation equipment strain and comprises a first-stage spraying device and a second-stage spraying device which are connected, a second-stage spraying feeding pipe is connected with a discharging pipe of the first-stage spraying device, the first-stage spraying device is communicated with a discharging pipe of the mixer, the mixer sprays feed to the first stage, and the second-stage spraying discharging pipe is communicated with the aerobic fermentation bin and feeds to the aerobic fermentation bin.
Further, the working flow of the first-stage spraying is as follows,
s1: opening the gate valve B, simultaneously extending the main hydraulic cylinder and the auxiliary hydraulic cylinder, exhausting redundant air in the outer cylinder, and closing the gate valve B;
s2: opening the gate valve A, controlling the main piston to ascend through the main hydraulic cylinder, and sucking the semi-fluid material in the mixer into the inner cylinder under the action of negative pressure;
s3: closing the gate valve A, controlling the main piston to move downwards through the main hydraulic cylinder, driving the annular piston to move upwards through the auxiliary hydraulic cylinder, enabling the materials to flow between the isolation cylinder A and the outer cylinder from the inner cylinder through the material gap, starting the bacteria liquid pump, discharging the bacteria liquid through the spray head, mixing the bacteria liquid into the materials flowing in the material gap until the main piston is lowered to the lowest position, and lifting the annular piston to the highest position (the volume in the inner cylinder is equal to the volume between the outer cylinder and the isolation cylinder A);
s4: controlling the main piston to move upwards through the main hydraulic cylinder, driving the annular piston to move downwards through the auxiliary hydraulic cylinder, enabling the materials to flow back into the inner cylinder through the material gap again, starting the bacteria liquid pump, discharging the bacteria liquid through the spray head, mixing the bacteria liquid into the materials flowing in the material passing gap until the main piston is lifted to the highest position, lowering the annular piston to the lowest position, and closing the bacteria liquid pump;
s5: and opening the gate valve B, controlling the main piston to move upwards through the main hydraulic cylinder, and discharging the materials in the inner cylinder body into secondary spraying through the discharge pipe.
Furthermore, the structure of the first-stage spraying and the second-stage spraying is the same, only different bacteria liquid is sprayed in the preparation process, the mixer is used for mixing and fully mixing the manure through the mixer, water and biomass (powder of organic waste such as straw) according to a certain proportion, so that the material reaches the appropriate water content within 60 percent, and the mixture is ensured to have a semifluid structure to meet the requirements of composting; the first-stage spraying (3) is used for inoculating strains for the first time, and the second-stage spraying is used for inoculating strains for the second time; the aerobic fermentation chamber is used for fermentation, after the fermentation process is started, aerobic microorganisms are rapidly proliferated under the condition that an air feeder provides oxygen, the temperature of the chicken manure is rapidly raised, and the chicken manure enters a high-temperature period within 2-3 days.
The materials are maintained for 7-9 days at a high temperature of more than 60 ℃ by an automatic monitoring and automatic control system so as to fully kill pathogenic bacteria and weed seeds and realize the harmlessness and stabilization of the materials. After the high temperature period is finished, the internal uniform turnover device uniformly turns over the materials, so that the materials in the whole space are further uniformly mixed, and the quality of organic fertilizer products is improved.
Compared with the prior art, the invention has the following beneficial effects:
according to the strain spraying device of the fermentation equipment, strain fermentation liquor is added into excrement and is uniformly mixed, so that the use requirement is met;
the strain spraying system of the fermentation equipment changes the waste of the chicken manure into valuable, and generates better social benefit, ecological benefit and economic benefit.
Drawings
In order to more clearly illustrate the detailed description of the invention or the technical solutions in the prior art, the drawings that are needed in the detailed description of the invention or the prior art will be briefly described below. Throughout the drawings, like elements or portions are generally identified by like reference numerals. In the drawings, elements or portions are not necessarily drawn to scale.
FIG. 1 is a schematic view of the structure of the present invention;
FIG. 2 is a schematic view of the external structure of the first stage spray of the present invention;
in the figure: 1. the fermentation equipment comprises a mixer 2, a fermentation equipment strain spraying machine 3, a primary spraying device 3.1, an outer cylinder 3.2, an inner cylinder 3.3, an upper end cover 3.4, a lower end cover 3.5, an isolation cylinder A3.6, a middle connecting plate 3.7, a main piston 3.8, a main hydraulic cylinder 3.9, an annular piston 3.10, an auxiliary hydraulic cylinder 3.11, a spray head 3.12, a material passing gap 4, a secondary spraying device 5, an aerobic fermentation bin 6, a feed pipe 7, a discharge pipe 8, a gate valve A9, a gate valve B10, a bacterial liquid pump 11 and a bacterial liquid storage tank.
Detailed Description
The invention is further described below with reference to the accompanying drawings:
the present invention is further illustrated by the following examples, which are not intended to be limiting, and any modifications, equivalents, improvements, etc. which are within the spirit and principle of the present invention are intended to be included within the scope of the present invention.
Example one
As shown in fig. 1-2, a fermentation equipment strain sprinkler, fermentation equipment strain sprinkler and system machine 2 is including the one-level sprinkler 3 and the second grade sprinkler 4 of connecting, and the second grade sprinkler 4 inlet pipe is connected with the discharging pipe of one-level sprinkler 3, one-level sprinkler 3 is linked together with the discharging pipe of blendor 1, and blendor 1 supplies material to one-level sprinkler 3, the discharging pipe of second grade sprinkler 4 is linked together with aerobic fermentation storehouse 5, supplies material to aerobic fermentation storehouse 5.
Preferably, the primary spraying device 3 comprises an outer cylinder 3.1, the cross section of the outer cylinder 3.1 is circular, an upper end cover 3.3 is installed at the top opening of the outer cylinder 3.1, a lower end cover 3.4 is installed at the bottom opening of the outer cylinder 3.1, an isolation cylinder A3.5 is coaxially arranged inside the outer cylinder 3.1, an inner cylinder 3.2 is coaxially arranged inside the isolation cylinder A3.5, the upper ends of the isolation cylinder A3.5 and the inner cylinder 3.2 are both fixed on the lower surface of the upper end cover 3.3, the bottom ends of the isolation cylinder A3.5 and the inner cylinder 3.2 are both fixedly connected with a middle connecting plate 3.6, the middle connecting plate 3.6 is of an annular structure, the large circle of the middle connecting plate is connected with the isolation cylinder A3.5, the small circle of the middle connecting plate is connected with the inner cylinder 3.2, a liquid storage cavity is enclosed between the inner cylinder 3.2, the isolation cylinder A3.5, the upper end cover (3.3.3) and the middle connecting plate 3.6, intermediate even has punishment in advance clearance 3.12 between board 3.6 and the lower end cover 3.4, the lower surface mounting of intermediate even board 3.6 has shower nozzle 3.11, shower nozzle 3.11's inlet is linked together with the stock solution chamber, main piston 3.7 has in the interior barrel 3.2, main hydraulic cylinder 3.8 that drive main piston 3.7 removed along interior barrel 3.2 length direction is installed at the center of upper end cover 3.3, be provided with annular piston 3.9 between outer barrel 3.1 and the isolation barrel A3.5, upper end cover 3.3 upper surface has the auxiliary hydraulic cylinder 3.10 that drive annular piston 3.9 removed along the length direction of isolation barrel A3.5, the central point of lower end cover 3.4 puts and is provided with inlet pipe 6 and discharging pipe 7 that are linked together rather than the inner chamber respectively, be provided with gate valve A8 and gate valve B9 on inlet pipe 6 and the discharging pipe 7 respectively.
Preferably, the gap between the intermediate connecting plate 3.6 and the lower end cover 3.4 is set to be 1-3cm.
Preferably, the middle connecting plate 3.6 is of an annular structure, a plurality of groups of nozzles 3.11 are equidistantly distributed on the middle connecting plate 3.6, the plurality of groups of nozzles 3.11 are all positioned on the same circle with the center of the middle connecting plate 3.6, and an inlet of each nozzle 3.11 is provided with a one-way valve.
Preferably, the auxiliary hydraulic cylinders 3.10 are provided with multiple groups, all of which are located on the same circle with the circle center of the upper end cover 3.3 as the circle center, and simultaneously drive the annular piston 3.9 to descend or ascend.
Preferably, the inlet and the outlet of the bacteria liquid pump 10 are respectively connected with the bacteria liquid storage tank 11 and the liquid storage cavity, and the bacteria liquid pump is a peristaltic pump.
Example two
The utility model provides a fermentation equipment bacterial sprinkling system, includes that blendor 1, fermentation equipment bacterial spray 2, aerobic fermentation storehouse 5, the fermentation equipment bacterial sprays 2 and sprays 2 for above-mentioned fermentation equipment bacterial, including the one-level sprinkler 3 and the second grade sprinkler 4 of connecting, 4 inlet pipes of second grade sprinkler are connected with the discharging pipe of one-level sprinkler 3, one-level sprinkler 3 is linked together with the discharging pipe of blendor 1, and blendor 1 is linked together to 3 feeds of one-level sprinkler, the discharging pipe of second grade sprinkler 4 is linked together with aerobic fermentation storehouse 5, to 5 feeds in aerobic fermentation storehouse.
Preferably, the working flow of the primary spraying device 3 is as follows,
s1: opening the gate valve B9, simultaneously extending the main hydraulic cylinder 3.8 and the auxiliary hydraulic cylinder 3.10, exhausting redundant air in the outer cylinder body 3.1, and closing the gate valve B9;
s2: opening a gate valve A8, controlling a main piston 3.7 to ascend through a main hydraulic cylinder 3.8, and sucking semi-fluid materials in the mixer (1) into an inner cylinder body 3.2 under the action of negative pressure;
s3: closing a gate valve A8, controlling a main piston 3.7 to move downwards through a main hydraulic cylinder 3.8, simultaneously driving an annular piston 3.9 to move upwards through an auxiliary hydraulic cylinder 3.10, enabling materials to flow between an isolation cylinder A3.5 and an outer cylinder 3.1 from the inner cylinder 3.2 through a material gap 3.12, starting a bacteria liquid pump 10, and discharging bacteria liquid through a spray head 3.11, so that bacteria liquid is mixed in the materials flowing in the material passing gap 3.12 until the main piston 3.7 is lowered to the lowest position, and the annular piston 3.9 is raised to the highest position (the volume in the inner cylinder 3.2 is equal to the volume between the outer cylinder 3.1 and the isolation cylinder A3.5);
s4: the main piston 3.7 is controlled to move upwards through the main hydraulic cylinder 3.8, meanwhile, the annular piston 3.9 is driven to move downwards through the auxiliary hydraulic cylinder 3.10, the materials flow back into the inner cylinder 3.2 through the material gap 3.12 again, the bacteria liquid pump 10 is started, bacteria liquid is discharged through the spray head 3.11, so that the bacteria liquid is mixed into the materials flowing in the material passing gap 3.12 until the main piston 3.7 rises to the highest position, the annular piston 3.9 falls to the lowest position, and the bacteria liquid pump 10 is closed;
s5: and opening a gate valve B9, controlling a main piston 3.7 to move upwards through a main hydraulic cylinder 3.8, and discharging the material in the inner cylinder 3.2 into the secondary spraying device 4 through a discharge pipe 7.
S6: and repeating the step S2 to the step S5.
Preferably, the first-stage spraying device 3 and the second-stage spraying device 4 are identical in structure and only spray different bacteria liquids, and the mixer 1 is used for mixing and fully mixing manure through a mixer, water and biomass (powder of organic waste such as straw) according to a certain proportion, so that the material reaches a proper water content within 60%, and the mixture is guaranteed to have a semifluid structure to meet the requirements of composting; the first-stage spraying device 3 is used for inoculating strains for the first time, and the second-stage spraying device 4 is used for inoculating strains for the second time; the aerobic fermentation chamber 5 is used for fermentation, after the fermentation process is started, aerobic microorganisms are rapidly proliferated under the condition that an air feeder provides oxygen, the temperature of the chicken manure is rapidly increased, and the chicken manure enters a high-temperature period within 2-3 days. The materials are maintained for 7-9 days at a high temperature of more than 60 ℃ by an automatic monitoring and automatic control system so as to fully kill pathogenic bacteria and weed seeds and realize the harmlessness and stabilization of the materials. After the high temperature period is finished, the internal uniform turnover device uniformly turns over the materials, so that the materials in the whole space are further uniformly mixed, and the quality of organic fertilizer products is improved.
The foregoing shows and describes the general principles, principal features, and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.
The details of the present invention are not described in detail, but are known to those skilled in the art.
Claims (5)
1. The utility model provides a fermentation equipment bacterial sprinkler which characterized in that: fermentation equipment bacterial sprinkler and system machine are connected including the one-level sprinkler and the second grade sprinkler of connecting, and the second grade sprinkler inlet pipe is connected with the discharging pipe of one-level sprinkler, the discharging pipe of one-level sprinkler and blendor is linked together, and the blendor is to the one-level sprinkler feed, the discharging pipe and the aerobic fermentation storehouse of second grade sprinkler are linked together, to the feed of aerobic fermentation storehouse.
2. The fermentation device strain spray apparatus of claim 1, wherein the gap between the middle connecting plate and the lower end cap is set to 1-3cm.
3. The fermentation equipment strain spraying device of claim 2, wherein the intermediate connecting plate is of an annular structure, a plurality of groups of nozzles are equidistantly distributed on the intermediate connecting plate, the plurality of groups of nozzles are all positioned on the same circle by using the center of the intermediate connecting plate, and the inlet of each nozzle is provided with a one-way valve.
4. The fermentation equipment strain spraying device of claim 3, wherein the auxiliary hydraulic cylinders are provided with a plurality of groups, all of which are positioned on the same circle with the circle center of the upper end cover as the circle center, and simultaneously drive the annular piston to descend or ascend.
5. The fermentation equipment strain spraying device of claim 4, wherein an inlet and an outlet of the strain liquid pump are respectively connected with the strain liquid storage tank and the liquid storage cavity, and the strain liquid pump is a peristaltic pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211345125.9A CN115536442B (en) | 2022-10-31 | 2022-10-31 | Strain spraying device of fermentation equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211345125.9A CN115536442B (en) | 2022-10-31 | 2022-10-31 | Strain spraying device of fermentation equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115536442A true CN115536442A (en) | 2022-12-30 |
CN115536442B CN115536442B (en) | 2024-02-06 |
Family
ID=84717871
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211345125.9A Active CN115536442B (en) | 2022-10-31 | 2022-10-31 | Strain spraying device of fermentation equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115536442B (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT13602B (en) * | 1902-12-24 | 1903-10-10 | Bory & Co A | |
ES1013374U (en) * | 1990-03-28 | 1990-12-01 | Villegas Delgado Ignacio | Mixing apparatus and dosed liquid spray fungicides. (Machine-translation by Google Translate, not legally binding) |
CN2811304Y (en) * | 2005-06-30 | 2006-08-30 | 江苏大学 | Automatic seed-receiving device for fermentation system |
CN101759467A (en) * | 2008-12-24 | 2010-06-30 | 中国环境科学研究院 | Rural solid waste mixed aerobic composting method |
US20170058247A1 (en) * | 2015-08-26 | 2017-03-02 | Tze-Ming KAO | Anaerobic fermentation with venturi stirring equipment |
KR101920162B1 (en) * | 2017-07-26 | 2018-11-19 | 농업회사법인 청운표고 주식회사 | Automatic inoculaiton apparatus for liquid mushroom spawn |
CN114085746A (en) * | 2021-11-11 | 2022-02-25 | 海南大学 | Automatic fermentation system of trichoderma |
-
2022
- 2022-10-31 CN CN202211345125.9A patent/CN115536442B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT13602B (en) * | 1902-12-24 | 1903-10-10 | Bory & Co A | |
ES1013374U (en) * | 1990-03-28 | 1990-12-01 | Villegas Delgado Ignacio | Mixing apparatus and dosed liquid spray fungicides. (Machine-translation by Google Translate, not legally binding) |
CN2811304Y (en) * | 2005-06-30 | 2006-08-30 | 江苏大学 | Automatic seed-receiving device for fermentation system |
CN101759467A (en) * | 2008-12-24 | 2010-06-30 | 中国环境科学研究院 | Rural solid waste mixed aerobic composting method |
US20170058247A1 (en) * | 2015-08-26 | 2017-03-02 | Tze-Ming KAO | Anaerobic fermentation with venturi stirring equipment |
KR101920162B1 (en) * | 2017-07-26 | 2018-11-19 | 농업회사법인 청운표고 주식회사 | Automatic inoculaiton apparatus for liquid mushroom spawn |
CN114085746A (en) * | 2021-11-11 | 2022-02-25 | 海南大学 | Automatic fermentation system of trichoderma |
Also Published As
Publication number | Publication date |
---|---|
CN115536442B (en) | 2024-02-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107759254B (en) | Livestock and poultry farm pollution ecological treatment system and method based on cultivation and breeding combination | |
CN108129170B (en) | Environment-friendly livestock and poultry manure high-temperature aerobic fermentation chamber | |
CN107986830A (en) | The processing method of kitchen garbage and its organic fertilizer of preparation | |
CN107129953B (en) | Microbial additive for treating cattle manure and preparation method and application thereof | |
CN106591199B (en) | High-efficiency leavening agent for livestock and poultry manure and leavening method thereof | |
CN106007815A (en) | Production device and preparation method of livestock manure organic fertilizer | |
CN111996217A (en) | Straw bed-lying padding and livestock and poultry manure combined anaerobic fermentation method | |
CN103430906A (en) | Method for resource integrated utilization of agricultural wastes | |
CN104543514A (en) | Cellaring pot ale daily ration for efficient fattening of high-grade beef cattle and preparation method for cellaring pot ale daily ration | |
CN104987214A (en) | Efficient biology leavening agent capable of decreasing pollution gas emission in urine immersing manure technology | |
SE450769B (en) | PROCEDURE AND PLANT FOR USE OF WASTE PRODUCTS FROM WASTE | |
CN114568393A (en) | Method for recycling pig manure garbage by utilizing hermetia illucens | |
CN107986589B (en) | Three-section type cattle farm manure aerobic fermentation device and fermentation method thereof | |
CN115536442B (en) | Strain spraying device of fermentation equipment | |
CN108315232B (en) | Biogas generating device capable of rapidly fermenting and decomposing straw and application method thereof | |
CN111548220A (en) | Biological organic fertilizer | |
CN116874316A (en) | Method for high-value conversion of agricultural waste by cooperation of hermetia illucens and microorganisms | |
CN207193143U (en) | Turner | |
CN110526530A (en) | A method of utilizing microorganism, maggot composite system harmless treatment cyanobacteria | |
CN205624395U (en) | Biological feed continuous production equipment | |
CN201116297Y (en) | Variable pressure temperature-controlling stalk decomposition device | |
CN107950469B (en) | Method for feeding ecological pigs by utilizing separate separation and circulation fermentation tank for residues, liquid and gas | |
CN111849727A (en) | Edible fungus strain fermentation tank for black fungus | |
KR20090112839A (en) | Method of making composts using food wastes | |
CN213060681U (en) | Fermenting installation is used in production of portable fertilizer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |