CN204569915U - Complete mixing Anaerobic reactor - Google Patents
Complete mixing Anaerobic reactor Download PDFInfo
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- CN204569915U CN204569915U CN201520090553.0U CN201520090553U CN204569915U CN 204569915 U CN204569915 U CN 204569915U CN 201520090553 U CN201520090553 U CN 201520090553U CN 204569915 U CN204569915 U CN 204569915U
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Abstract
The utility model relates to a kind of mixing anaerobic reactor completely, belong to methane engineering technology field, comprise housing, water distribution system, triphase separator and whipping appts is provided with in housing, described inner walls is provided with the wiper ring of annular, wiper ring upper end is connected with the second lifting motor with the first lifting motor being fixed on housing upper end respectively, and the first lifting motor and the second lifting motor are symmetrically distributed in both sides; Whipping appts comprises the agitator motor be fixed on housing, stir shaft and along stir shaft arrange on stir leaf and under stir leaf.This complete mixing anaerobic reactor, by arranging wiper ring, the first lifting motor and the second lifting motor, is cleared up inner walls, is avoided inwall impurity layer blocked up, improve biogas yield.
Description
Technical field
The utility model relates to a kind of mixing anaerobic reactor completely, belongs to methane engineering technology field.
Background technology
In biogas engineering, stalk, all kinds of feces of livestock and poultry and other mixture of organic substance are by sending into complete mixing anaerobic reactor, and through mechanical stirring, fully ferment, output biogas, therefore, complete mixing anaerobic reactor is one of key equipment.Existing complete mixing anaerobic reactor stirs when charging usually, for the high density stock liquid containing higher solids thing, its stirring is full and uniform not, in addition, firedamp gas equipment is in lengthy fermentation process, inner walls easily adheres to mixture, affects the output efficiency of biogas, causes biogas output low.
Utility model content
According to above the deficiencies in the prior art, technical problem to be solved in the utility model is: provide a kind of mixing anaerobic reactor completely, fermented liquid is mixed, regularly cleans inner walls, improve biogas yield.
Complete mixing anaerobic reactor described in the utility model, comprise housing, water distribution system, triphase separator and whipping appts is provided with in housing, described inner walls is provided with the wiper ring of annular, wiper ring upper end is connected with the second lifting motor with the first lifting motor being fixed on housing upper end respectively, and the first lifting motor and the second lifting motor are symmetrically distributed in both sides; Whipping appts comprises the agitator motor be fixed on housing, stir shaft and along stir shaft arrange on stir leaf and under stir leaf.
By arranging wiper ring, when after equipment use certain hour, the mixture impurity that inner walls is adhered to is thicker, wiper ring lifting is driven by the first lifting motor and the second lifting motor, inner walls is cleared up, avoids inwall impurity layer blocked up, affect biogas yield.By above stir leaf and under stir leaf and respectively the bottom of mixed solution and the middle part of rising stirred, make it fully mix with the zymophyte in mud, reach best biogas yield.
Be provided with slag-drip opening in the middle of described housing bottom, by slag-drip opening, natural pond slag discharged.
Triphase separator, comprise cone-shaped body, air chamber and air outlet is provided with in cone-shaped body, cone-shaped body bottom periphery sets gradually the first traverse baffle of connection downwards, second traverse baffle, 3rd traverse baffle and the 4th traverse baffle, the first flow deflector of connection is set gradually inside each traverse baffle, second flow deflector, 3rd flow deflector and the 4th flow deflector, first traverse baffle and the first flow deflector form first-class chamber, second traverse baffle and the second flow deflector form second chamber, 3rd traverse baffle and the 3rd flow deflector form second chamber, 4th traverse baffle and the 4th flow deflector form the 4th and flow chamber, baffle is provided with between two the 4th contiguous flow deflectors, be provided with to reflux between baffle and the 4th flow deflector and stitch.By arranging first-class chamber, second chamber, the 3rd stream chamber and the 4th stream chamber, make mixed solution when flowing through triphase separator, repeatedly baffling in multiple stream chamber, air pocket is wherein by thorough fragmentation, air pocket is avoided to carry mud, mud is continuous sedimentation in baffling process, and finally by the backflow of backflow seam, gas is discharged through air chamber and collected.Solid-liquid-gas three phase is separated completely, carries out effective throttling to mud, thus improves mud life cycle, avoids the microorganism in mud to run off, and improves biogas output.
Described first-class chamber, second chamber, the 3rd stream chamber, the 4th stream chamber sectional area increase successively, by four the stream chambeies increased successively, the flow velocity of mixed solution is progressively slowed down, is conducive to the deposition of mud.
The first described traverse baffle, the 3rd traverse baffle are vertically arranged, second traverse baffle, the 4th traverse baffle are diagonally arranged, the first flow deflector, the second flow deflector, the 3rd flow deflector and the 4th flow deflector are corresponding with the first traverse baffle, the second traverse baffle, the 3rd traverse baffle and the 4th traverse baffle respectively.
Described backflow gap is less than first-class cavity gap, and mixed solution is refluxed by first-class chamber, and mud is through the backflow of backflow seam.
Stalk, all kinds of feces of livestock and poultry and other organic mixed solution are sent into housing bottom through water-in, uniform by water distribution system, agitator motor drives stir shaft to rotate, by above stir leaf, under stir the common stirring of leaf, mixed solution is mixed with mud fully, and the gas-liquid-solid mixture of generation is separated through triphase separator, and biogas is discharged by effuser, venting port, solids is through the backflow of settling tank precipitation, and the water outlet of liquid through top is discharged.
Compared with prior art, the beneficial effect that the utility model has is:
This complete mixing anaerobic reactor, by arranging wiper ring, the first lifting motor and the second lifting motor, is cleared up inner walls, is avoided inwall impurity layer blocked up, improve biogas yield; By above stir leaf and under stir leaf and respectively the bottom of mixed solution and the middle part of rising stirred, make it fully mix with the zymophyte in mud, reach best biogas yield; By arranging first-class chamber, second chamber, the 3rd stream chamber and the 4th stream chamber, thoroughly eliminating the air pocket in mixed solution, making three phase separation complete, effectively improve mud life cycle, improve biogas quantum of output, improve processing efficiency.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
Fig. 2 is triphase separator structural representation.
In figure: 1, housing; 2, wiper ring; 3, the first lifting motor; 4, effuser; 5, triphase separator; 5.1, air chamber; 5.2, cone-shaped body; 5.3, the first flow deflector; 5.4, the second flow deflector; 5.5, the 3rd flow deflector; 5.6, the 4th flow deflector; 5.7, first-class chamber; 5.8, second chamber; 5.9, the 3rd stream chamber; 5.10, the 4th stream chamber; 5.11, the first traverse baffle; 5.12, the second traverse baffle; 5.13, the 3rd traverse baffle; 5.14, the 4th traverse baffle; 5.15, backflow seam; 5.16, baffle; 6, agitator motor; 7, the second lifting motor; 8, venting port; 9, stir shaft; 10, leaf is stirred on; 11, leaf is stirred under; 12, slag-drip opening; 13, water-in; 14, water distribution system.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described further.
As shown in Figure 1, this complete mixing anaerobic reactor comprises housing 1, water distribution system 14, triphase separator 5 and whipping appts is provided with in housing 1, housing 1 inwall is provided with the wiper ring 2 of annular, wiper ring 2 upper end is connected with the second lifting motor 7 with the first lifting motor 3 being fixed on housing 1 upper end respectively, and the first lifting motor 3 and the second lifting motor 7 are symmetrically distributed in both sides; Whipping appts comprises the agitator motor 6 being fixed on housing 1 top, and agitator motor 6 lower end connects stir shaft 9, is provided with down and stirs leaf 11, be provided with and stir leaf 10 in the middle part of it, thus stir fully the mixed solution in housing, mix bottom stir shaft.Be provided with slag-drip opening 12 in the middle of bottom housing 1, the natural pond slag of generation is discharged through slag-drip opening 12.
As shown in Figure 2, triphase separator comprises cone-shaped body 5.2, air chamber 5.1 and air outlet is provided with in cone-shaped body 5.2, cone-shaped body 5.2 bottom periphery sets gradually the first traverse baffle 5.11 of connection downwards, second traverse baffle 5.12, 3rd traverse baffle 5.13 and the 4th traverse baffle 5.14, the first flow deflector 5.3 of connection is set gradually inside each traverse baffle, second flow deflector 5.4, 3rd flow deflector 5.5 and the 4th flow deflector 5.6, first traverse baffle 5.11 and the first flow deflector 5.3 form first-class chamber 5.7, second traverse baffle 5.12 and the second flow deflector 5.4 form second chamber 5.8, 3rd traverse baffle 5.13 and the 3rd flow deflector 5.5 form second chamber 5.8, 4th traverse baffle 5.14 and the 4th flow deflector 5.6 form the 4th and flow chamber 5.10, first-class chamber 5.7, second chamber 5.8, 3rd stream chamber 5.9, 4th stream chamber 5.10 sectional area increases successively, mixed solution is in flow process, flow velocity progressively slows down, mud wherein is progressively precipitated, air pocket in mixed solution is broken in repeatedly baffling process.Baffle 5.16 is provided with between two the 4th contiguous flow deflectors 5.6, the seam 5.15 that refluxes is provided with between baffle 5.16 and the 4th flow deflector 5.6, backflow seam 5.15 gap is less than gap, first-class chamber 5.7, the mixed solution overwhelming majority is flowed along first-class chamber 5.7, ensures collection and the reflowing result of biogas.
First traverse baffle 5.11, the 3rd traverse baffle 5.13 are vertically arranged, second traverse baffle 5.12, the 4th traverse baffle 5.14 are diagonally arranged, the first flow deflector 5.3, second flow deflector 5.4, the 3rd flow deflector 5.5 and the 4th flow deflector 5.6 are corresponding with the first traverse baffle 5.11, second traverse baffle 5.12, the 3rd traverse baffle 5.13 and the 4th traverse baffle 5.14 respectively.
Working process:
Stalk, all kinds of feces of livestock and poultry and other organic mixed solution are sent into bottom housing 1 through water-in 13, uniform by water distribution system 14, agitator motor 6 drives stir shaft 9 to rotate, by above stir leaf 10, under stir the common stirring of leaf 11, mixed solution is mixed with mud fully, and the gas-liquid-solid mixture of generation is separated through triphase separator, and biogas is discharged by effuser 4, venting port 8, solids is through the backflow of settling tank precipitation, and the water outlet of liquid through top is discharged.
Claims (6)
1. a complete mixing anaerobic reactor, comprise housing (1), water distribution system (14), triphase separator (5) and whipping appts is provided with in housing (1), it is characterized in that: described housing (1) inwall is provided with the wiper ring (2) of annular, wiper ring (2) upper end is connected with the second lifting motor (7) with the first lifting motor (3) being fixed on housing (1) upper end respectively, and the first lifting motor (3) and the second lifting motor (7) are symmetrically distributed in both sides; Whipping appts comprises the agitator motor (6) be fixed on housing (1), stir shaft (9) and along stir shaft (9) arrange on stir leaf (10) and under stir leaf (11).
2. complete mixing anaerobic reactor according to claim 1, is characterized in that: be provided with slag-drip opening (12) in the middle of described housing (1) bottom.
3. complete mixing anaerobic reactor according to claim 1, it is characterized in that: described triphase separator comprises cone-shaped body (5.2), air chamber (5.1) and air outlet is provided with in cone-shaped body (5.2), cone-shaped body (5.2) bottom periphery sets gradually first traverse baffle (5.11) of connection downwards, second traverse baffle (5.12), 3rd traverse baffle (5.13) and the 4th traverse baffle (5.14), first flow deflector (5.3) of connection is set gradually inside each traverse baffle, second flow deflector (5.4), 3rd flow deflector (5.5) and the 4th flow deflector (5.6), first traverse baffle (5.11) and the first flow deflector (5.3) form first-class chamber (5.7), second traverse baffle (5.12) and the second flow deflector (5.4) form second chamber (5.8), 3rd traverse baffle (5.13) and the 3rd flow deflector (5.5) form second chamber (5.8), 4th traverse baffle (5.14) and the 4th flow deflector (5.6) form the 4th and flow chamber (5.10), baffle (5.16) is provided with between two the 4th contiguous flow deflectors (5.6), be provided with to reflux between baffle (5.16) and the 4th flow deflector (5.6) and stitch (5.15).
4. complete mixing anaerobic reactor according to claim 3, is characterized in that: described first-class chamber (5.7), second chamber (5.8), the 3rd stream chamber (5.9), the 4th stream chamber (5.10) sectional area increase successively.
5. the complete mixing anaerobic reactor according to claim 3 or 4, it is characterized in that: described the first traverse baffle (5.11), 3rd traverse baffle (5.13) is vertically arranged, second traverse baffle (5.12), 4th traverse baffle (5.14) is diagonally arranged, first flow deflector (5.3), second flow deflector (5.4), 3rd flow deflector (5.5) and the 4th flow deflector (5.6) respectively with the first traverse baffle (5.11), second traverse baffle (5.12), 3rd traverse baffle (5.13) and the 4th traverse baffle (5.14) corresponding.
6. complete mixing anaerobic reactor according to claim 3, is characterized in that: described backflow seam (5.15) gap is less than first-class chamber (5.7) gap.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520090553.0U CN204569915U (en) | 2015-02-09 | 2015-02-09 | Complete mixing Anaerobic reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520090553.0U CN204569915U (en) | 2015-02-09 | 2015-02-09 | Complete mixing Anaerobic reactor |
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| CN204569915U true CN204569915U (en) | 2015-08-19 |
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| CN201520090553.0U Active CN204569915U (en) | 2015-02-09 | 2015-02-09 | Complete mixing Anaerobic reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607776A (en) * | 2019-01-23 | 2019-04-12 | 成都市和谐环保工程技术有限公司 | One kind springing up high efficiency anaerobic reactor and anaerobic reaction technique |
| CN116768360A (en) * | 2023-08-14 | 2023-09-19 | 湖南化工设计院有限公司 | Pig farm wastewater treatment method |
-
2015
- 2015-02-09 CN CN201520090553.0U patent/CN204569915U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607776A (en) * | 2019-01-23 | 2019-04-12 | 成都市和谐环保工程技术有限公司 | One kind springing up high efficiency anaerobic reactor and anaerobic reaction technique |
| CN116768360A (en) * | 2023-08-14 | 2023-09-19 | 湖南化工设计院有限公司 | Pig farm wastewater treatment method |
| CN116768360B (en) * | 2023-08-14 | 2024-05-07 | 湖南化工设计院有限公司 | Pig farm wastewater treatment method |
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| GR01 | Patent grant |