CN207259391U - Bio-fertilizer process units - Google Patents
Bio-fertilizer process units Download PDFInfo
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- CN207259391U CN207259391U CN201721068847.9U CN201721068847U CN207259391U CN 207259391 U CN207259391 U CN 207259391U CN 201721068847 U CN201721068847 U CN 201721068847U CN 207259391 U CN207259391 U CN 207259391U
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- bio
- fermentation cabin
- process units
- exhaust gas
- collecting hood
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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
- 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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Abstract
This application discloses a kind of bio-fertilizer process units, it is characterised in that including fermentation cabin, V-type collecting hood, dehydrater, air blower and heater；The V-type collecting hood is installed on above the fermentation cabin, and the tip of V-type collecting hood points up, and two sides bottom is equipped with catch basin on V-type collecting hood, and the extraneous drainpipe of connection is connected on catch basin；Gas outlet and air inlet are provided with fermentation cabin, the dehydrater is connected with the air outlet pipe, and the air blower is connected with dehydrater, air inlet lines are connected on air blower, regulating valve is equipped with the air inlet lines, the heater is connected with air blower, and the air inlet pipe is connected with heater；Ozone machine and exhaust gas treating device are further included, is connected between the V-type collecting hood and the exhaust gas treating device by exhaust duct；The ozone machine connects with exhaust gas treating device, and delivery pipe is provided with exhaust gas treating device.The utility model can discharge the vapor produced in fermentation process in time and the tail gas of discharge is not smelly.
Description
Technical field
It the utility model is related to agricultural equipment field, more particularly to a kind of bio-fertilizer process units.
Background technology
Modern society can all produce the kitchen and domestic organic garbage of flood tide daily, in order to make full use of these kitchens and life
Organic waste living, people's utility model utilize kitchen and the method for domestic organic garbage fermentation manufacture bio-fertilizer.Use at present
Production method be the fermenting and producing bio-fertilizer under conditions of 60 DEG C~70 DEG C, but this method can produce largely in process of production
Vapor, and Zymolysis Equipment is that to prevent that the heat in installation for fermenting scatters and disappears too fast, and the exhausting-gas hole that installation for fermenting is opened is very small
, this, which allows for substantial amounts of vapor, to discharge in time, cause obtained bio-fertilizer water content high, simultaneously because this method
It is excessive that bio-fertilizer water content is made, producer is usually taken and sends out for a long time to enable obtained bio-fertilizer to be up to state standards
The measure of ferment, this just also make it that the content of organic matter that bio-fertilizer is made is relatively low, therefore excludes in time in generating process in installation for fermenting
Vapor be production high-quality biological fertilizer must solve the problems, such as.
Utility model content
The utility model is in view of the above-mentioned problems, propose a kind of bio-fertilizer process units.
The technical solution that the utility model is taken is as follows：
A kind of bio-fertilizer process units, including fermentation cabin, V-type collecting hood, dehydrater, air blower and heater；The V-type
Collecting hood is installed on above the fermentation cabin, and the tip of V-type collecting hood points up, and two sides bottom is set on V-type collecting hood
There is catch basin, the extraneous drainpipe of connection is connected on catch basin；Be provided with gas outlet and air inlet in fermentation cabin, the dehydrater with
The air outlet pipe is connected, and the air blower is connected with dehydrater, is connected to air inlet lines on air blower, on the air inlet lines
Equipped with regulating valve, the heater is connected with air blower, and the air inlet pipe is connected with heater.
Can constantly there is vapor generation in fermentation process, the vapor positioned at fermentation cabin silo roof vicinity runs into V-type collection
After cover, can small water droplet is condensed on V-type collecting hood, small water droplet can be slided into catch basin along siding, and by drainpipe from
Opener sink enters external environment.Due to needing constantly to blast fresh air in fermentation process, fresh air is blasted in air blower
During so that the air pressure increase in fermentation cabin so that the original gas in fermentation cabin enters dehydrater by gas outlet,
And this portion gas temperature is still higher, if being directly discharged to atmospheric environment, wasted it will cause great, therefore still by this portion
Air is divided to blast fermentation cabin by air blower, the effect of heater is that the gas that all air blowers bloat is heated to needed for fermentation
Fermentation cabin is blasted again after the temperature wanted.
Optionally, ozone machine and exhaust gas treating device are further included, is passed through between the V-type collecting hood and the exhaust gas treating device
Exhaust duct is connected；The ozone machine connects with exhaust gas treating device, and delivery pipe is provided with exhaust gas treating device.
Tail gas after fermentation is smelly be because contain substantial amounts of sulfide in tail gas, and ozone has strong oxidizing property, can general
Sulfide oxidation Cheng Shui and acid, thus tail gas in exhaust gas treating device with will not be smelly again after ozone reaction, through discharged
To during environment sense of discomfort will not be caused to human body.
Optionally, the fermentation cabin on the outside of reverse V-shaped collecting hood with posting heat insulating block.
The effect of heat insulating block is so that the heat in installation for fermenting is more difficult and scatters and disappears, more energy saving.
Optionally, puddle support and motor are further included, the puddle support is installed in fermentation cabin, and the motor is installed on fermentation
Outside storehouse, the motor connects with puddle support.
Fermentation efficiency can be effectively improved by being stirred continuously during the fermentation.
Optionally, temperature and humidity detector are equipped with the fermentation cabin.
Optionally, heating tube and heat transfer medium are equipped with the bulkhead of the fermentation cabin.
Heating tube and heat transfer medium can be heated to fermentation cabin, ensure the stabilization of fermentation temperature.
Optionally, some baffles and liquid-leaking nozzle are equipped with the exhaust gas treating device, the baffle separates exhaust gas treating device
Into the separate space of several mutual unicom.
Since exhaust gas treating device is obstructed into the space of several independent communications by baffle, tail gas and ozone are left from entering
Time it is elongated, therefore the time of contact of tail gas and ozone is elongated, and so tail gas can be caused more to be filled with ozone reaction
Point.At the same time will necessarily be with some vapor in tail gas, this part vapor can condense out to be formed on exhaust gas treating device
Droplet, and this part droplet can leave exhaust gas treating device from liquid-leaking nozzle.
Optionally, it is provided with door in the fermentation cabin.
Door is used to fetch and deliver material.
Optionally, the height of the gas outlet is higher than the height of air inlet.
Optionally, bearing is further included, the fermentation cabin is installed on the bearing.
The beneficial effects of the utility model are：
1st, the vapor produced in fermentation process can be discharged in time；
2nd, the tail gas of discharge is not smelly；
3rd, high insulating effect, energy consumption are low.
Brief description of the drawings：
Fig. 1 is each component connection relationship diagram of the bio-fertilizer process units；
Fig. 2 is fermentation cabin, V-type collecting hood connection diagram；
Fig. 3 is schematic diagram at A in Fig. 2；
Fig. 4 is exhaust gas treating device structure diagram.
Each reference numeral is in figure：1st, fermentation cabin, 11, air inlet, 12, gas outlet, 13, puddle support, 14, motor, 15 temperature
Spend humidity detector, 16, door, 17, heating tube and heat transfer medium, 2, V-type collecting hood, 21, catch basin, 22, drainpipe, 3,
Dehydrater, 4, air blower, 41, air inlet lines, 42, regulating valve, 5, heater, 6, exhaust gas treating device, 61, baffle, 62, discharge
Pipe, 63, liquid-leaking nozzle, 7, heat insulating block, 9, exhaust duct, 10, bearing.
Embodiment：
With reference to each attached drawing, the utility model is described in detail.
As shown in attached drawing 1, attached drawing 2 and attached drawing 3, a kind of bio-fertilizer process units, including fermentation cabin 1, V-type collecting hood 2,
Dehydrater 3, air blower 4 and heater 5；V-type collecting hood 2 is installed on the top of fermentation cabin 1, and the tip of V-type collecting hood 2 is directed toward
Square, two sides bottom is equipped with catch basin 21 on V-type collecting hood 2, and the extraneous drainpipe 22 of connection is connected on catch basin 21；Fermentation cabin
Gas outlet 12 and air inlet 11 are provided with 1, dehydrater 3 is connected with air outlet pipe, and air blower 4 is connected with dehydrater 3, air blower
Air inlet lines 41 are connected on 4, regulating valve 42 is equipped with air inlet lines 41, heater 5 is connected with air blower 4, and air inlet pipe is with adding
Hot device 5 is connected.
Can constantly there is vapor generation in fermentation process, the vapor positioned at 1 silo roof vicinity of fermentation cabin runs into V-type collection
After cover 2, small water droplet can be condensed on V-type collecting hood 2, small water droplet can slide into catch basin 21 along siding, and pass through draining
Pipe 22 leaves catch basin 21 and enters external environment.Due to needing constantly to blast fresh air in fermentation process, blasted in air blower 4
During fresh air so that the air pressure increase in fermentation cabin 1 so that the original gas in fermentation cabin 1 passes through gas outlet
12 enter dehydrater 3, and this portion gas temperature is still higher, if being directly discharged to atmospheric environment, it will cause great wave
Take, therefore this partial air is still blasted into fermentation cabin 1 by air blower 4, the effect of heater 5 is to bloat all air blowers 4
Gas be heated to fermenting after required temperature and blast fermentation cabin 1 again.
As shown in Figure 2, ozone machine and exhaust gas treating device 6 are further included, is passed through between V-type collecting hood 2 and exhaust gas treating device 6
Exhaust duct 9 is connected；Ozone machine connects with exhaust gas treating device 6, and delivery pipe 62 is provided with exhaust gas treating device 6.
Tail gas after fermentation is smelly be because contain substantial amounts of sulfide in tail gas, and ozone has strong oxidizing property, can general
Sulfide oxidation Cheng Shui and acid, thus tail gas in exhaust gas treating device 6 with will not be smelly again after ozone reaction, discharged through delivery pipe 62
To during environment sense of discomfort will not be caused to human body.
As shown in Figure 2, heat insulating block 7 is posted in fermentation cabin 1 and the outside of reverse V-shaped collecting hood 2.
The effect of heat insulating block 7 is so that the heat in installation for fermenting is more difficult and scatters and disappears, more energy saving.
As shown in Figure 2, puddle support 13 and motor 14 are further included, puddle support 13 is installed in fermentation cabin 1, and motor 14 is pacified
Outside loaded on fermentation cabin 1, motor 14 connects with puddle support 13.
Fermentation efficiency can be effectively improved by being stirred continuously during the fermentation.
As shown in Figure 2, temperature and humidity detector 15 are equipped with fermentation cabin 1.
As shown in Figure 2, heating tube and heat transfer medium 17 are equipped with the bulkhead of fermentation cabin 1.
Heating tube and heat transfer medium 17 can be heated to fermentation cabin 1, ensure the stabilization of fermentation temperature.
As shown in Figure 4, some baffles 61 and liquid-leaking nozzle 63 are equipped with exhaust gas treating device 6, baffle 61 is by exhaust gas treating device
6 are separated into the separate space of several mutual unicom.
Since exhaust gas treating device 6 is obstructed into by baffle 61 space of several independent communications, tail gas and ozone are from entering
The time left is elongated, therefore the time of contact of tail gas and ozone is elongated, and can so cause tail gas with ozone reaction more
Add fully.At the same time will necessarily be with some vapor in tail gas, this part vapor can condense out on exhaust gas treating device 6
Droplet is formed, and this part droplet can leave exhaust gas treating device 6 from liquid-leaking nozzle 63.
As shown in Figure 2, door 16 is provided with fermentation cabin 1.
Door 16 is used to fetch and deliver material.
As shown in Figure 1, the height of gas outlet 12 is higher than the height of air inlet 11.
As shown in Figure 1, bearing 10 is further included, fermentation cabin 1 is installed on bearing 10.
The above is only the preferred embodiment of the present invention, not thereby limits the patent protection of the utility model
Scope, every equivalent structure transformation made with the utility model specification and accompanying drawing content, is directly or indirectly used in it
His relevant technical field, similarly includes within the protection scope of the present utility model.
Claims (10)
1. a kind of bio-fertilizer process units, it is characterised in that including fermentation cabin, V-type collecting hood, dehydrater, air blower and heating
Device；The V-type collecting hood is installed on above the fermentation cabin, and the tip of V-type collecting hood points up, two on V-type collecting hood
Side bottom is equipped with catch basin, and the extraneous drainpipe of connection is connected on catch basin；Gas outlet and air inlet are provided with fermentation cabin, institute
State dehydrater with the air outlet pipe to be connected, the air blower is connected with dehydrater, and air inlet lines are connected on air blower, described
Regulating valve is equipped with air inlet lines, the heater is connected with air blower, and the air inlet pipe is connected with heater.
2. bio-fertilizer process units as claimed in claim 1, it is characterised in that further include ozone machine and exhaust gas treating device, institute
State and be connected between V-type collecting hood and the exhaust gas treating device by exhaust duct；The ozone machine connects with exhaust gas treating device,
Delivery pipe is provided with exhaust gas treating device.
3. bio-fertilizer process units as claimed in claim 1, it is characterised in that the fermentation cabin is outer with reverse V-shaped collecting hood
Post heat insulating block in side.
4. bio-fertilizer process units as claimed in claim 1, it is characterised in that further include puddle support and motor, the stirring
Frame is installed in fermentation cabin, and the motor is installed on outside fermentation cabin, and the motor connects with puddle support.
5. bio-fertilizer process units as claimed in claim 1, it is characterised in that temperature is equipped with the fermentation cabin and is examined with humidity
Survey device.
6. bio-fertilizer process units as claimed in claim 1, it is characterised in that be equipped with heating tube in the bulkhead of the fermentation cabin
And heat transfer medium.
7. bio-fertilizer process units as claimed in claim 2, it is characterised in that be equipped with some baffles in the exhaust gas treating device
And exhaust gas treating device is separated into the separate space of several mutual unicom by liquid-leaking nozzle, the baffle.
8. bio-fertilizer process units as claimed in claim 1, it is characterised in that be provided with door in the fermentation cabin.
9. bio-fertilizer process units as claimed in claim 1, it is characterised in that the height of the gas outlet is higher than air inlet
Highly.
10. bio-fertilizer process units as claimed in claim 1, it is characterised in that further include bearing, the fermentation cabin is installed on
On the bearing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721068847.9U CN207259391U (en) | 2017-08-24 | 2017-08-24 | Bio-fertilizer process units |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721068847.9U CN207259391U (en) | 2017-08-24 | 2017-08-24 | Bio-fertilizer process units |
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| Publication Number | Publication Date |
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| CN207259391U true CN207259391U (en) | 2018-04-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721068847.9U Active CN207259391U (en) | 2017-08-24 | 2017-08-24 | Bio-fertilizer process units |
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| CN (1) | CN207259391U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107324853A (en) * | 2017-08-24 | 2017-11-07 | 杭州洁洁环保科技有限公司 | Bio-fertilizer process units |
-
2017
- 2017-08-24 CN CN201721068847.9U patent/CN207259391U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107324853A (en) * | 2017-08-24 | 2017-11-07 | 杭州洁洁环保科技有限公司 | Bio-fertilizer process units |
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