CN207567133U - Energy saving fermentation system - Google Patents
Energy saving fermentation system Download PDFInfo
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- CN207567133U CN207567133U CN201721515278.8U CN201721515278U CN207567133U CN 207567133 U CN207567133 U CN 207567133U CN 201721515278 U CN201721515278 U CN 201721515278U CN 207567133 U CN207567133 U CN 207567133U
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- 238000000855 fermentation Methods 0.000 title claims abstract description 120
- 230000004151 fermentation Effects 0.000 title claims abstract description 118
- 230000007306 turnover Effects 0.000 claims abstract description 50
- 238000000034 method Methods 0.000 claims abstract description 31
- 230000008569 process Effects 0.000 claims abstract description 23
- 238000004321 preservation Methods 0.000 claims abstract description 14
- 238000005192 partition Methods 0.000 claims abstract description 10
- 238000007599 discharging Methods 0.000 claims description 19
- 239000000463 material Substances 0.000 claims description 18
- 239000002918 waste heat Substances 0.000 claims description 8
- 239000003814 drug Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 239000010815 organic waste Substances 0.000 abstract description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Fertilizers (AREA)
Abstract
The utility model discloses a kind of energy saving fermentation systems, and including roof insulating body, the roof insulating body is divided into high fermentation area and heat-preservation transport area of lower floor；Solar thermal collector is equipped at the top of the high fermentation area, high fermentation area Peng Ti lower parts are equipped with air inlet, and canopy body top is equipped with air outlet and exhaust fan；The high fermentation area is divided into fermentation zone and turnover area by partition board, and annular processes area is equipped in the fermentation zone, turner is equipped in the annular processes area；The turnover area is set as charging turnover area and the turnover area that discharges；Lower floor's heat-preservation transport area side is equipped with the feed belt communicated with feeding turnover area in high fermentation area, and opposite side is equipped with the discharge bucket communicated with the turnover area that discharges in high fermentation area, transhipment belt is equipped with below the discharge bucket.Energy saving fermentation system in the utility model can not only securely achieve the fermentation of organic waste, and efficient, high degree of automation, cost saved artificial use.
Description
Technical field
The utility model belongs to dry fermentation arts, and in particular to a kind of energy-efficient fermentation system.
Background technology
Plant residue, aquaculture fowl and animal excrement, grocery trade or Agricultural Output organic waste value is cheap, volume
Huge not readily transportable and discarding, and pollution is easily generated, it is a great problem that above-mentioned industry practitioner is difficult to avoid that.It removes
The methods of traditional burning, landfill, more preferably processing method are the condition in certain humidity, carbon-nitrogen ratio and oxygen content
Under, organic waste rubbish is converted by the fermentation of microorganism by the high-quality biological organic fertilizer with practicability.
The process of fermentation is to carry out the pipe fitting technical process of organic waste harmless treatment, how to promote the craftwork of fermentation process
Matter, how to reduce production cost and do not generate secondary pollution be the most important thing in fermentation of organic wastes technique.
The fermentation technique of early stage mostly using static fermentation, i.e., ferments organic waste standing, the work of static fermentation
For skill process usually due to being converted to anaerobic fermentation for hypoxgia, can not only generate the foul smell such as a large amount of hydrogen sulfide increases operating personnel
Poisoning and the risk of environment explosion, and fermentation efficiency is very low, can not large-scale promoted.Existing fermentation technique is more
Dynamic fermentation is realized using the instrument of modernization, such as organic waste is carried out using the layering vertical structure of tower Zymolysis Equipment
Fermentation, makes organic waste rapid dehydration and fermentation period is short, but tower Zymolysis Equipment efficiency is low, equipment investment is larger.Make
For the improvement of fermentation process in the prior art, the producer of many organic waste treatments is realized using standing for fermentation with reference to throwing is turned over
Effective fermentation of large-scale, specially：Organic waste is spread in fermentation place and is left to ferment, after standing certain time length
Organic waste raw material is carried out using artificial or turner to turn over throwing, organic waste raw material is made effectively to be in contact with air,
Ensure that fermentation process has sufficient oxygen sources, this zymotechnique has reached its maturity at present, becomes large-scale organic waste
The preferred technique of processing item.
Above-mentioned standing combines the technique for turning over throwing although skillful, and solution many is still needed in actual application and is asked
Topic：1st, the problem of how promoting confined space utilization rate 2, the problem of how further saving the required energy in fermentation process 3, such as
What realizes the problem of full-automatic production.In the prior art, although being proposed there are also technical solution for certain a kind of problem
Corresponding solution, but still can not achieve automatic energy-saving production.
Invention content
In order to solve the deficiencies in the prior art, the utility model provides a kind of novel energy saving fermentation system, should
Energy saving fermentation system can not only securely achieve the fermentation of organic waste, and efficient, high degree of automation, greatly
Save artificial use.Meanwhile designed by Space Rationalization, the utilization rate of the confined space is improved, further, is passed through
The utilization of solar energy and waste heat largely saves required heat in fermentation process, reduces cost in fermentation process.
The utility model institute technique effect to be achieved is realized by following scheme：
A kind of energy saving fermentation system provided in the utility model, including roof insulating body, the roof insulating body is divided into
Floor fermentation zone and heat-preservation transport area of lower floor；
Solar thermal collector is equipped at the top of the high fermentation area, high fermentation area Peng Ti lower parts are equipped with air inlet, canopy body
Top is equipped with air outlet and exhaust fan；The high fermentation area is divided into fermentation zone and turnover area, the fermentation zone by partition board
It is interior to be equipped with annular processes area, it is equipped with turner in the annular processes area；The turnover area is set as charging turnover area and discharging week
Turn area；
Lower floor's heat-preservation transport area side is equipped with the feed belt communicated with feeding turnover area in high fermentation area, another
Side is equipped with the discharge bucket communicated with the turnover area that discharges in high fermentation area, and transhipment belt is equipped with below the discharge bucket；
Lower floor heat preservation zone bottom is equipped with waste heat heat collector, and the waste heat heat collector is tubular type collector.
Further, the solar thermal collector is tubular type collector.
Further, the inlet and outlet communicated with charging turnover area and the turnover area that discharges are respectively equipped on the partition board.
Further, 1.5-2 times that width is discharging turnover area inlet and outlet width is imported and exported at the charging turnover area.
Further, the discharging turnover area is equipped with blanking port, the blanking port and the discharge bucket in heat-preservation transport area of lower floor
Connect.
Further, assisted fermentation area is equipped in the middle part of the turnover area, the charging turnover area and discharging turnover area are set on
Assisted fermentation area both sides.
Further, the assisted fermentation area is set as the region of only one side open, and open sides are set on opposite with partition board
Side.
Further, the height between the bottom of the discharge bucket and transhipment belt is 0.8-1.5m.
Further, charging zone is equipped in the middle part of the annular processes area, the medicament of required addition is equipped in the charging zone
With drying material.
The utility model has the following advantages：Energy saving fermentation system in the utility model can not only securely achieve
The fermentation of machine waste, and efficient, high degree of automation, cost saved artificial use.Meanwhile pass through rationalization
Spatial design improves the utilization rate of the confined space, further, by the utilization of solar energy and waste heat, largely saves hair
Required heat during ferment, reduces cost in fermentation process.
Description of the drawings
Fig. 1 is the overall structure diagram of energy saving fermentation system in the utility model；
Fig. 2 is the structure diagram in energy saving fermentation system high fermentation area in the utility model.
Specific embodiment
The present invention will be described in detail with reference to the accompanying drawings and examples.
The overall structure of energy saving fermentation system embodiment is as shown in Figure 1 in the utility model.Energy saving fermentation in embodiment
System is divided into 2 two layers of high fermentation area 1 and heat-preservation transport area of lower floor, is separated by wall 3, is double-layer structure, two layers
In the roof insulating body of relative closure.In existing fermentation system, one is used other than fermentation tower has multilayered structure more
The structure of layer, the utilization rate of solid space is very low, and since the laying of fermentation place is excessive, to raw material transhipment and tunning
Transhipment bring very big challenge, often raw material area and product transit zone need to occupy very big space, at the same in order to
Distinguish the two, it is also necessary to be situated between and set up the isolated area of blank out, further reduced space availability ratio.This reality
It applies in example and main fermentation area is located at upper strata, its underpart is set as heat-preservation transport area, is not only effectively utilized solid space, but also utilize
Gravity makes discharging process energy consumption reduce by more than 80%, there are no must manually discharge, and by the setting of feed belt make into
Material process full automation further saves artificial.Fermentation zone also brings just the ventilation of fermentation process set on upper strata
Sharp condition, the ventilation effect for making fermentation zone are better.
Further to promote energy utilization rate so as to energy saving, high fermentation area top is equipped with solar thermal collector 101,
The solar thermal collector preferably using tubular type collector, heats roof insulating body using heat-conducting medium in heat collector pipe,
Maintain fermentation temperature.High fermentation area Peng Ti lower parts are equipped with air inlet 102, and canopy body top is equipped with air outlet and exhaust fan 103, into
Air port must be set on canopy body lower part, and air outlet and exhaust fan must be set on canopy body top, could form effective air pair in this way
Stream, makes air stream effectively by treating fermented organic waste in fermentation zone, realize the conveying of oxygen.
Heat-preservation transport area of lower floor side is equipped with the feed belt 202 communicated with feeding turnover area in high fermentation area, another
Side is equipped with the discharge bucket 203 communicated with the turnover area that discharges in high fermentation area, and 203 lower section of discharge bucket is equipped with what is set up in contrast
Belt 204 is transported, belt falls at the uniform velocity to discharge to the outside of roof insulating body with the material that fermentation is completed.
In many breeding enterprises or agriculture relevant enterprise, often equipped with the large-scale heating equipment such as boiler, these equipment
UTILIZATION OF VESIDUAL HEAT IN can effectively be adapted with the energy saving fermentation system in the utility model and be used.In the present embodiment, lower floor is protected
Warm area bottom is equipped with waste heat heat collector 201, it is preferable to use tubular type collector, and recirculated water use in tube heater as heating Jie
The aluminothermy of boiler plant is used for the heating and heat preservation of energy saving fermentation system by matter.
Embodiment fermentation zone structure diagram at the middle and upper levels, as shown in Figure 2.High fermentation area is divided by partition board 113
Fermentation zone 111 and turnover area 112 are equipped with annular processes area 105 in fermentation zone, turner 104 are equipped in annular processes area 105,
Turner continues dynamic during the fermentation to be treated fermentation materials and carries out turning over throwings, makes the oxygen in Matter Transfer to be fermented and air
Contact avoids anaerobic fermentation from generating toxic gas.Turnover area is set as charging turnover area 114 and the turnover area 115 that discharges.Partition board 113
On be respectively equipped with and charging turnover area and the inlet and outlet 109 and 110 that communicate of discharging turnover area.In view of what is used in fill process
It is belt self-feeding, and the step of the process of discharging uses direct blanking, discharge process efficiency higher, both to make speed
Fermentation system in the present embodiment is set as the organic circulation system that constant-quality measures into constant mass by matching, therefore it is preferred that will be into
Inlet and outlet width be that the turnover area that discharges imports and exports 1.5-2 times of width at material turnover area, can active balance input and output material technique speed
Degree, avoids windrow or batch mixing.The blanking port of at one or many places can be set at discharging turnover area 115, blanking port is kept the temperature with lower floor
The discharge bucket in transit zone connects, and realizes automatic blanking, discharging.
It treats that fermentation materials are sent by entrance 109 to annular by feeding belt 107 it can be seen from the structure in high fermentation area to send out
In ferment area 105, turner persistently treats fermentation materials and carries out turning over throwing, while ventilation device starts to work and ensures normal air stream
It is dynamic that oxygen is maintained to need.Material after fermentation is sent by outlet 110 to discharging turnover area 115, is opened and is fallen after confirmation discharging
Material mouth（It is not indicated in figure, which can be set on any position of discharging turnover area as needed）, material after fermentation
It is dropped down onto in discharge bucket 203 by blanking port discharging, then is dropped down onto on transhipment belt 204 by discharge bucket 203, transhipment belt 204 will ferment
Material after the completion is sent to outside, it is achieved thereby that automation feeding, blanking, the process fermented.
Overall structure is further improved, assisted fermentation area 108 is equipped in the middle part of turnover area for sending out special material
Ferment either carries out special process fermentation or for pre- spice etc. for certain raw materials to ferment that are difficult to, and feeds 114 He of turnover area
The turnover area 115 that discharges is set on assisted fermentation area both sides, by setting up for assisted fermentation area, not only by original charging and discharging every
Effective utilization has been carried out from band, and has efficiently separated charging and discharging process, has avoided batch mixing.To optimize the mistake of assisted fermentation
Journey, assisted fermentation area is set as the region of only one side open, and open sides are set on the opposite side with partition board as shown in Figure 2, avoid
With the material batch mixing in fermentation zone.
Further, to avoid the materials from spattering in blanking operation and falling, between the bottom of discharge bucket and transhipment belt
Highly preferred be set as 0.8-1.5m.Meanwhile added for the ease of medicament, it is equipped with charging zone at 105 middle part of annular processes area
106, charging zone 106 interior medicament and drying material equipped with required addition, for the cyclically charging during throwing is turned over.
As can be seen from the above-described embodiment, the energy saving fermentation system in the utility model can not only securely achieve organic
The fermentation of waste, and efficient, high degree of automation, cost saved artificial use.It is meanwhile empty by rationalizing
Between design, improve the utilization rate of the confined space, further, by the utilization of solar energy and waste heat, largely save fermentation
Required heat in the process reduces cost in fermentation process.
It is last it should be noted that above example is only to illustrate the technical solution of the utility model embodiment rather than right
It is limited, although the utility model embodiment is described in detail with reference to preferred embodiment, this field it is common
Technical staff should understand that still be modified or replaced equivalently the technical solution of the utility model embodiment, and this
A little ranges changed or equivalent replacement cannot also make modified technical solution be detached from the utility model embodiment technical solution.
Claims (9)
1. a kind of energy saving fermentation system, it is characterised in that：
Including roof insulating body, the roof insulating body is divided into high fermentation area and heat-preservation transport area of lower floor；
Solar thermal collector is equipped at the top of the high fermentation area, high fermentation area Peng Ti lower parts are equipped with air inlet, canopy body top
Equipped with air outlet and exhaust fan；The high fermentation area is divided into fermentation zone and turnover area by partition board, is set in the fermentation zone
There is annular processes area, turner is equipped in the annular processes area；The turnover area is set as charging turnover area and the turnover area that discharges；
Lower floor's heat-preservation transport area side is equipped with the feed belt communicated with feeding turnover area in high fermentation area, and opposite side is set
There is the discharge bucket communicated with the turnover area that discharges in high fermentation area, transhipment belt is equipped with below the discharge bucket；
Lower floor's heat-preservation transport area bottom is equipped with waste heat heat collector, and the waste heat heat collector is tubular type collector.
2. energy saving fermentation system as described in claim 1, it is characterised in that：The solar thermal collector is tubular type collector.
3. energy saving fermentation system as described in claim 1, it is characterised in that：Be respectively equipped on the partition board with charging turnover area and
The inlet and outlet that discharging turnover area communicates.
4. energy saving fermentation system as claimed in claim 3, it is characterised in that：Inlet and outlet width is discharging at the charging turnover area
1.5-2 times of turnover area inlet and outlet width.
5. energy saving fermentation system as claimed in claim 3, it is characterised in that：The discharging turnover area is equipped with blanking port, described to fall
Material mouth connects with the discharge bucket in heat-preservation transport area of lower floor.
6. energy saving fermentation system as described in claim 1, it is characterised in that：Assisted fermentation area, institute are equipped in the middle part of the turnover area
It states charging turnover area and discharging turnover area is set on assisted fermentation area both sides.
7. energy saving fermentation system as claimed in claim 6, it is characterised in that：The assisted fermentation area is set as the area of only one side open
Domain, and open sides are set on the opposite side with partition board.
8. energy saving fermentation system as described in claim 1, it is characterised in that：Between the bottom of the discharge bucket and transhipment belt
Highly it is 0.8-1.5m.
9. energy saving fermentation system as described in claim 1, it is characterised in that：Charging zone, institute are equipped in the middle part of the annular processes area
State medicament and drying material equipped with required addition in charging zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721515278.8U CN207567133U (en) | 2017-11-14 | 2017-11-14 | Energy saving fermentation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721515278.8U CN207567133U (en) | 2017-11-14 | 2017-11-14 | Energy saving fermentation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207567133U true CN207567133U (en) | 2018-07-03 |
Family
ID=62693355
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721515278.8U Active CN207567133U (en) | 2017-11-14 | 2017-11-14 | Energy saving fermentation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207567133U (en) |
-
2017
- 2017-11-14 CN CN201721515278.8U patent/CN207567133U/en active Active
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