CN206902141U - The waste material waste heat temperature-raising marsh pool system discharged using methane-generating pit - Google Patents
The waste material waste heat temperature-raising marsh pool system discharged using methane-generating pit Download PDFInfo
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- CN206902141U CN206902141U CN201720479531.2U CN201720479531U CN206902141U CN 206902141 U CN206902141 U CN 206902141U CN 201720479531 U CN201720479531 U CN 201720479531U CN 206902141 U CN206902141 U CN 206902141U
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- tank
- anaerobic fermentation
- tank body
- methane
- generating pit
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- Processing Of Solid Wastes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model proposes the waste material waste heat temperature-raising marsh pool system using methane-generating pit discharge, including one-level anaerobic fermentation gas production tank and B grade anaerobic fermentation aerogenesis tank, one-level anaerobic fermentation gas production tank and B grade anaerobic fermentation the aerogenesis tank is sequentially connected, the outside of the one-level anaerobic fermentation gas production tank is provided with the incubation cavity of closing, the B grade anaerobic fermentation aerogenesis tank connects with incubation cavity, by the way that the sewage of B grade anaerobic fermentation aerogenesis tank is imported in incubation cavity, burning boiler manufacture hot water is gone to heat without wasting the valuable energy in short supply again, reduce environmental pollution, reduce construction costs, reduce complicated labor intensity, reduce operating cost, reach innoxious operation, realize thorough energy-saving and emission-reduction.
Description
Technical field
The utility model belongs to field of renewable energy technology, particularly relates to heat using the waste material waste heat of methane-generating pit discharge
Methane tank system.
Background technology
The energy and environmental problem have become two big outstanding problem of today's society, non-renewable energy resources increasingly reduce and into
In the case of this is increasingly elevated, big-and-middle-sized biogas engineering is one of important means for solving the energy and environmental problem.Biogas fermentation
The temperature conditionss in pond are divided into:1. 10 DEG C~30 DEG C of normal temperature fermentation (also referred to as cold fermentation), under this temperature conditions, factor of created gase
Can be 0.15~0.3m3/m3d;2. 30 DEG C~45 DEG C of mesophilic digestion, under this temperature conditions, it is reachable that pond holds factor of created gase
1m3/m3d or so;3. 45 DEG C~60 DEG C of hot fermentation, under this temperature conditions, pond holds factor of created gase up to 2~2.5m3/
M3d or so, gas caused by temperature height is just more, particularly winter, it is necessary to which tank for sewage gas is heated.On the other hand, natural pond
The waste heat of waste material after fermenting tank for fermentation all lost in the form of heat, it is impossible to utilize well.
Utility model content
The utility model proposes the waste material waste heat temperature-raising marsh pool system using methane-generating pit discharge, solve in the prior art
The problem of using energy source of waste material waste heat is insufficient after biogas fermentation, while solve the problems, such as the defects of heat supply of march gas producing container.
What the technical solution of the utility model was realized in:
The waste material waste heat temperature-raising marsh pool system discharged using methane-generating pit, including one-level anaerobic fermentation gas production tank and two level are detested
Aerobe fermentation aerogenesis tank, one-level anaerobic fermentation gas production tank and B grade anaerobic fermentation the aerogenesis tank are sequentially connected, the one-level anaerobism
The outside of fermentation gas tank is provided with the incubation cavity of closing, and the B grade anaerobic fermentation aerogenesis tank connects with incubation cavity.
Further, the one-level anaerobic fermentation gas production tank includes the first tank body, and hyperboloid water conservancy diversion is provided with the first tank body
Cylinder, the outside of hyperboloid guide shell form a water outlet stabilizing feed well together with the first inner tank wall, the hyperboloid guide shell and the
The bottom of one tank body is connected, and by-pass filtration guard, the first tank body lower part are provided with the open top of the hyperboloid guide shell
Provided with water distributor, the water distributor is connected in hyperboloid guide shell, is provided with discharge pipeline in the hyperboloid guide shell, and first
The top of tank body is provided with the first biogas discharge pipe, is provided with the first delivery port in the water outlet stabilizing feed well side wall, described first goes out
The mouth of a river is connected with B grade anaerobic fermentation aerogenesis tank.
Further, the B grade anaerobic fermentation aerogenesis tank includes the second tank body, and second tank body is provided with and second
The consistent secondary filtration guard of tank body profile, a filtering buffering is formed between the secondary filtration guard and the second inner tank wall
Area, the second biogas discharge pipe is provided with above second tank body, mud discharging mouth is provided with below second tank body, it is described
Filter buffer connects with incubation cavity.
Further, second tank base is provided with twin-screw mixing plant, and the twin-screw mixing plant includes
Two opposite conveying augers of direction of rotation, two conveying augers and motor connection.
Further, it is provided with heat-insulation layer on the outer wall of the incubation cavity.
Further, suction pump is connected between the filter buffer and incubation cavity.
Further, the bottom of second tank body and first tank body is taper.
Further, the second delivery port is provided with incubation cavity.
In summary, the utility model has the advantage of:By the way that the sewage of B grade anaerobic fermentation aerogenesis tank is imported into insulation
In chamber, go burning boiler manufacture hot water to heat without wasting the valuable energy in short supply again, reduce environmental pollution, reduce construction costs, subtract
Few complicated labor intensity, reduces operating cost, reaches innoxious operation, realize thorough energy-saving and emission-reduction.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, drawings in the following description are only
It is some embodiments of the utility model, for those of ordinary skill in the art, before creative labor is not paid
Put, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the waste material waste heat temperature-raising marsh pool system structure diagram that the utility model utilizes methane-generating pit discharge.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
As shown in figure 1, the waste material waste heat temperature-raising marsh pool system discharged using methane-generating pit, including one-level anaerobic fermentation gas production
Tank 1 and B grade anaerobic fermentation aerogenesis tank 2, the one-level anaerobic fermentation gas production tank 1 and B grade anaerobic fermentation aerogenesis tank 2 connect successively
Connect, the outside of the one-level anaerobic fermentation gas production tank 1 is provided with the incubation cavity 3 of closing, the B grade anaerobic fermentation aerogenesis tank 2 with
Incubation cavity 3 connects, and the one-level anaerobic fermentation gas production tank 1 includes the first tank body, and hyperboloid guide shell 4 is provided with the first tank body,
The outside of hyperboloid guide shell 4 forms a water outlet stabilizing feed well 5, the hyperboloid guide shell 4 and together with the first inner tank wall
The bottom of one tank body is connected, and by-pass filtration guard 6, the first tank body lower part are provided with the open top of the hyperboloid guide shell
Provided with water distributor 7, the water distributor 7 is connected in hyperboloid guide shell 4, and discharge pipeline is provided with the hyperboloid guide shell 4
8, the top of the first tank body is provided with the first biogas discharge pipe 9, and the first delivery port 10, institute are provided with the water outlet stabilizing feed well side wall
State the first delivery port 10 to be connected with B grade anaerobic fermentation aerogenesis tank, the B grade anaerobic fermentation aerogenesis tank includes the second tank body, institute
State the second tank body and be provided with the secondary filtration guard 11 consistent with the second tank body profile, the tank of secondary filtration guard 11 and second
A filter buffer 12 is formed between internal wall, is provided with the second biogas discharge pipe 13 above second tank body, described the
Mud discharging mouth 14 is provided with below two tank bodies, the filter buffer 12 is connected with incubation cavity 3, and second tank base is set
There is twin-screw mixing plant, the twin-screw mixing plant includes two opposite conveying augers 15 of direction of rotation, two conveyings
Auger and motor connection, heat-insulation layer is provided with the outer wall of the incubation cavity, is connected between the filter buffer and incubation cavity
The bottom of suction pump 16, second tank body and first tank body is taper, and the second delivery port 17 is provided with incubation cavity.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements made etc., the utility model should be included in
Protection domain within.
Claims (7)
1. utilize the waste material waste heat temperature-raising marsh pool system of methane-generating pit discharge, it is characterised in that:Including one-level anaerobic fermentation gas production
Tank and B grade anaerobic fermentation aerogenesis tank, one-level anaerobic fermentation gas production tank and B grade anaerobic fermentation the aerogenesis tank are sequentially connected, institute
The outside for stating one-level anaerobic fermentation gas production tank is provided with the incubation cavity of closing, and the B grade anaerobic fermentation aerogenesis tank connects with incubation cavity
It is logical.
2. the waste material waste heat temperature-raising marsh pool system according to claim 1 discharged using methane-generating pit, it is characterised in that:Institute
Stating one-level anaerobic fermentation gas production tank includes the first tank body, is provided with hyperboloid guide shell in the first tank body, hyperboloid guide shell outside
Side forms a water outlet stabilizing feed well together with the first inner tank wall, and the hyperboloid guide shell is connected with the bottom of the first tank body, institute
State and by-pass filtration guard is provided with the open top of hyperboloid guide shell, the first tank body lower part is provided with water distributor, the water distribution
Pipe is connected in hyperboloid guide shell, and discharge pipeline is provided with the hyperboloid guide shell, and the top of the first tank body is provided with first
Biogas discharge pipe, the first delivery port, first delivery port and B grade anaerobic fermentation are provided with the water outlet stabilizing feed well side wall
Aerogenesis tank connects.
3. the waste material waste heat temperature-raising marsh pool system according to claim 1 discharged using methane-generating pit, it is characterised in that:Institute
Stating B grade anaerobic fermentation aerogenesis tank includes the second tank body, and second tank body is provided with the two level mistake consistent with the second tank body profile
Screen cover, a filter buffer, the top of second tank body are formed between the secondary filtration guard and the second inner tank wall
The second biogas discharge pipe is provided with, mud discharging mouth is provided with below second tank body, the filter buffer connects with incubation cavity
It is logical.
4. the waste material waste heat temperature-raising marsh pool system according to claim 3 discharged using methane-generating pit, it is characterised in that:Institute
State the second tank base and be provided with twin-screw mixing plant, the twin-screw mixing plant includes two opposite conveyings of direction of rotation
Auger, two conveying augers and motor connection.
5. the waste material waste heat temperature-raising marsh pool system according to claim 1 discharged using methane-generating pit, it is characterised in that:Institute
State and heat-insulation layer is provided with the outer wall of incubation cavity.
6. the waste material waste heat temperature-raising marsh pool system according to claim 3 discharged using methane-generating pit, it is characterised in that:Institute
State and suction pump is connected between filter buffer and incubation cavity.
7. the waste material waste heat temperature-raising marsh pool system according to claim 1 discharged using methane-generating pit, it is characterised in that:Protect
The second delivery port is provided with warm chamber.
Priority Applications (1)
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CN201720479531.2U CN206902141U (en) | 2017-05-02 | 2017-05-02 | The waste material waste heat temperature-raising marsh pool system discharged using methane-generating pit |
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CN201720479531.2U CN206902141U (en) | 2017-05-02 | 2017-05-02 | The waste material waste heat temperature-raising marsh pool system discharged using methane-generating pit |
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CN206902141U true CN206902141U (en) | 2018-01-19 |
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CN201720479531.2U Expired - Fee Related CN206902141U (en) | 2017-05-02 | 2017-05-02 | The waste material waste heat temperature-raising marsh pool system discharged using methane-generating pit |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109734252A (en) * | 2019-03-07 | 2019-05-10 | 四川舜瑞环境科技有限公司 | A kind of system and method handling pickle wastewater |
-
2017
- 2017-05-02 CN CN201720479531.2U patent/CN206902141U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109734252A (en) * | 2019-03-07 | 2019-05-10 | 四川舜瑞环境科技有限公司 | A kind of system and method handling pickle wastewater |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180119 Termination date: 20210502 |