CN118064265A - Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function - Google Patents
Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function Download PDFInfo
- Publication number
- CN118064265A CN118064265A CN202410460012.6A CN202410460012A CN118064265A CN 118064265 A CN118064265 A CN 118064265A CN 202410460012 A CN202410460012 A CN 202410460012A CN 118064265 A CN118064265 A CN 118064265A
- Authority
- CN
- China
- Prior art keywords
- wall
- biogas slurry
- tank
- fixedly connected
- displacement
- 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
- 239000002002 slurry Substances 0.000 title claims abstract description 99
- 238000006460 hydrolysis reaction Methods 0.000 title claims abstract description 46
- 230000007062 hydrolysis Effects 0.000 title claims abstract description 45
- 238000006073 displacement reaction Methods 0.000 claims abstract description 53
- 239000007921 spray Substances 0.000 claims abstract description 33
- 230000007246 mechanism Effects 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims description 36
- 238000003756 stirring Methods 0.000 claims description 29
- 238000000354 decomposition reaction Methods 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 claims 1
- 230000009471 action Effects 0.000 abstract description 8
- 230000005540 biological transmission Effects 0.000 abstract description 5
- 238000013459 approach Methods 0.000 abstract description 4
- 230000008859 change Effects 0.000 abstract description 4
- 239000010410 layer Substances 0.000 description 8
- 244000005700 microbiome Species 0.000 description 6
- 230000003301 hydrolyzing effect Effects 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 239000000110 cooling liquid Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000004891 communication Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000011229 interlayer Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 210000001503 joint Anatomy 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a biogas slurry hydrolysis tank with a double-pump temperature-regulating self-circulation function, and particularly relates to the technical field of hydrolysis tanks, which mainly comprises a tank body, a frame plate and a gear motor, wherein the frame plate is fixed on the inner wall of the tank body, the gear motor is fixedly arranged on the inner wall of the frame plate, and an output end of the gear motor is provided with an accurate displacement mechanism; the precise displacement mechanism comprises a screw fixedly arranged at the output end of the speed reducing motor, and the speed reducing motor is used for driving the screw to rotate. According to the invention, an accurate displacement mechanism is adopted, the screw rod carrying sleeve block approaches to the displacement distance sensor under the action of a screw transmission force, the two toothed plates can synchronously move and displace to the sensing distance position of the displacement distance sensor, after the two inclined spray pipes can synchronously change the azimuth, the displacement blades can rotate clockwise by anticlockwise displacement under the action of two pressurized biogas slurries, and the temperature uniformity of the biogas slurries in the hydrolysis tank can be rapidly realized.
Description
Technical Field
The invention relates to the technical field of hydrolysis tanks, in particular to a biogas slurry hydrolysis tank with a double-pump temperature-regulating self-circulation function.
Background
The biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function can eliminate the temperature gradient by circulating the biogas slurry, so that the hydrolysis reaction is carried out under the relatively consistent temperature condition, the hydrolysis efficiency is improved, meanwhile, the uniform temperature distribution is also beneficial to preventing the local overheating or supercooling phenomenon, the activity of microorganisms is protected, the stability of the hydrolysis process is ensured, and the function also promotes the uniform distribution of the microorganisms in the biogas slurry.
In the prior art, patent number CN205164715U discloses a hydrolysis tank, and the hydrolysis tank is wrapped with a heat exchange interlayer containing circulating cooling liquid through the outside of the tank, and the heat exchange interlayer is provided with a cooling liquid inlet and a cooling liquid outlet; the annular pipeline through which the gaseous cooling medium flows is arranged at the bottom of the inner cavity of the tank body, so that the technical problems of how to reduce the running resistance and maintenance difficulty of the hydrolysis tank are effectively solved, the cooling speed is increased, the running energy consumption of equipment is further reduced, and the hydrolysis tank is energy-saving and environment-friendly. However, the hydrolysis tank has the following problems when in use;
When the biogas slurry is hydrolyzed in the hydrolysis tank, although the biogas slurry can be uniformly mixed by stirring, the upper layer of the biogas slurry in the hydrolysis tank is uniformly mixed in the upper layer in the stirring process, and the lower layer of the biogas slurry in the hydrolysis tank is uniformly mixed in the lower layer, so that the whole equilibrium temperature of the upper layer and the lower layer of the biogas slurry in the hydrolysis tank is difficult to realize, and the biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function is needed.
Disclosure of Invention
In order to overcome the defects in the prior art, the invention provides the biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function.
In order to achieve the above purpose, the present invention provides the following technical solutions: the biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function comprises a tank body, a frame plate and a gear motor, wherein the frame plate is fixed on the inner wall of the tank body, the gear motor is fixedly arranged on the inner wall of the frame plate, and an accurate displacement mechanism is arranged at the output end of the gear motor; the precise displacement mechanism comprises a screw fixedly arranged at the output end of a speed reducing motor, and the speed reducing motor is used for driving the screw to rotate; the accurate displacement mechanism further comprises a sleeve block, a linkage bar, two toothed plates, a distance sensor and a displacement distance sensor; the sleeve block is in threaded connection with the outer wall of the screw rod, the linkage bar is welded at the top end of the sleeve block, and the two toothed plates are respectively fixed at the two end parts of the linkage bar; the distance sensor is positioned in front of the linkage bar, the displacement distance sensor is positioned behind the linkage bar, and the bottom ends of the distance sensor and the displacement distance sensor are fixedly connected with the top end of the frame plate; and one side of each toothed plate is provided with a deflection temperature equalizing component.
Preferably, the outer wall of the sleeve block is in sliding connection with the inner wall of the frame plate, and the outer wall of the sleeve block and the inner wall of the frame plate are polished; the frame plate and the sleeve block are made of stainless steel, the cross section of each toothed plate is L-shaped, the two toothed plates are sequentially arranged from right to left, the top end of the tank body is fixedly connected with a controller, and one side of the controller is provided with a rotating shaft which is rotationally connected with the tank body; a decomposing exhaust pipe communicated with the tank body is arranged on one side of the rotating shaft, a feeding pipe is communicated with one side of the decomposing exhaust pipe, and a feeding hopper is communicated with the top end of the feeding pipe; the feed hopper and the tank body are fixedly connected with the feed pipe, the bottom end of the rotating shaft is welded with a deflection blade, the bottom end of the deflection blade is fixedly connected with a stirring shaft, and the stirring shaft is used for stirring biogas slurry.
According to the technical scheme, when the device is used, the speed reducing motor is started through the controller, the speed reducing motor drives the screw rod to rotate, the sleeve block approaches to the deflection distance sensor under the action of the screw drive force, the linkage bar can drive the two toothed plates to move simultaneously, the deflection distance sensor can sense the movement distance of the linkage bar, and the two toothed plates can synchronously move and deflect.
Preferably, each group of the deflection temperature equalizing components comprises a toothed ring, a rotating rod, a sleeve plate, a bearing ring, a supporting frame, two slip rings, a rotating ring, an inclined spray pipe, a linkage shaft and a pressure sensor; the gear ring is meshed and connected to one side of the gear plate in a transmission manner, the rotating rod is fixed on the inner wall of the gear ring, the sleeve plate is fixed at the bottom end of the gear ring, the bearing ring is rotationally connected to the outer wall of the rotating rod and positioned below the sleeve plate, the supporting frame is welded on the outer wall of the bearing ring, the two slip rings are positioned below the sleeve plate, the linkage shaft is fixed on the inner wall of the sleeve plate and positioned on one side of the gear ring, and the inner walls of the two slip rings are fixedly connected with the outer wall of the linkage shaft; the rotating ring is welded at the bottom end of the linkage shaft, and the inclined spray pipe is fixedly connected to the inner wall of the rotating ring; the bottom end of the slip ring is fixedly connected with a supporting sleeve plate, and the outer wall of the supporting sleeve plate is fixedly connected with the inner wall of the tank body; the two pressure sensors are fixedly connected to the top end of one of the support frames, and are symmetrically arranged about the rotating rod; the circulating supercharging assembly is installed at one end of each inclined spray pipe, the outer wall of the linkage shaft is in sliding connection with the inside of the supporting frame, the sliding rings are in sliding connection with the supporting frame, the sliding rings are symmetrically arranged about the supporting frame, the bottom end face of the toothed ring is higher than the top end face of the linkage shaft, and the center point of the rotating rod and the center point of the bearing ring are in the same vertical line.
According to the technical scheme, when the device is used, the two toothed plates respectively drive the two toothed rings to rotate, the toothed rings carry the rotating rods to rotate, the rotating rods rotate inside the bearing rings, the supporting sleeve plate provides supporting force for the supporting frame, the toothed rings carry the sleeve plate to rotate, the sleeve plate drives the linkage shaft to realize stable rotation, the linkage shaft drives the two sliding rings to move, the two sliding rings slide with the supporting frame, the rotating rings drive the inclined spray pipes to realize rotation operation, the rotating rings extrude on the pressure sensor in front of the toothed rings, meanwhile, when the distance sensed by the displacement distance sensor and the linkage bar is the distance set by the controller, and when the distance sensed by the distance sensor and the linkage bar is the distance set by the controller, the speed reducing motor is turned off by the controller, the two inclined spray pipes can rotate to another direction, two biogas fluids are sprayed on the displacement blades, the displacement blades rotate anticlockwise to realize clockwise rotation on the inner wall of the tank body by the stirring shaft.
Preferably, each circulating pressurizing assembly comprises a deflection hose, a liquid outlet electric valve, a supply pipe, a heat exchange pipe, a circulating pump, a liquid inlet electric valve, a suction pipe, a solar panel, a storage battery and an inverter; the displacement hose is fixedly communicated with one end part of the inclined spray pipe, the liquid outlet electric valve is fixedly communicated with one end part of the displacement hose, the outer wall of the displacement hose is fixedly connected with the inner wall of the tank body, and the supply pipe is fixedly connected with one end part of the liquid outlet electric valve and communicated with the one end part of the liquid outlet electric valve;
The utility model discloses a solar energy heat exchange device, including heat exchange tube, circulating pump machine, suction pipe, inverter, temperature sensor, battery, discharge valve, tank body, temperature sensor, battery, inverter, battery bottom, discharge valve is installed to the below of suction pipe, discharge valve's one end and tank body outer wall fixed communication, two temperature sensor are installed to the below of shifting the hose, temperature sensor is located circulating pump machine input and fixed intercommunication at a liquid feed electric valve tip, solar cell panel is located circulating pump machine one side, the battery is fixed in solar cell panel bottom, dc-to-ac converter fixed connection is in the battery bottom, discharge valve is installed to the below of suction pipe, discharge valve's one end and tank body outer wall fixed communication.
According to the technical scheme, when the biogas tank is used, the controller closes the outer discharge valve, opens the two liquid outlet electric valves and the two liquid inlet electric valves, starts the two circulating pump machines, the two suction pipes suck biogas slurry in the tank body into the two liquid inlet electric valves, the heat exchange pipe is conveyed into the supply pipe, the supply pipe is used for pouring the biogas slurry into the liquid outlet electric valves, the liquid outlet electric valves convey the biogas slurry through the deflection hose, the deflection hose conveys the biogas slurry into the inclined spray pipes, the two inclined spray pipes can be used for obliquely spraying the biogas slurry on the deflection blades, the deflection blades are used for anticlockwise rotating under the action of the two pressurized biogas slurry, and the stirring shaft is used for stirring the biogas slurry in reverse time, so that the biogas slurry circulation below the tank body can be mixed with the biogas slurry above the tank body.
The invention has the technical effects and advantages that:
according to the invention, an accurate displacement mechanism is adopted, the screw is driven to rotate by a reducing motor, the screw carries the sleeve block to approach to the displacement distance sensor under the action of a thread transmission force, the linkage bar can drive the two toothed plates to move at the same time, the displacement distance sensor can sense the moving distance of the linkage bar, the two toothed plates can synchronously move and displace to the sensing distance position of the displacement distance sensor, after the two inclined spray pipes can synchronously change the azimuth, the two inclined spray pipes can boost and spray biogas slurry on the displacement blades, the displacement blades are changed into clockwise rotation from anticlockwise under the action of two pressurized biogas slurries, so that the temperature of the biogas slurry can be circularly regulated from bottom to top, the clockwise rotation of the biogas slurry can be realized by utilizing the circulating impact force of the biogas slurry, the biogas slurry in the upper layer and the lower layer of the hydrolysis tank can be rapidly balanced in a displacement mode, and the temperature of the biogas slurry in the hydrolysis tank can be rapidly uniform;
According to the invention, through the deflection temperature equalizing assembly, the two toothed plates respectively drive the two toothed rings to rotate, the toothed rings carry the rotating rods to rotate, the toothed rings carry the sleeve plates to rotate, the two slip rings slide with the support frame, the linkage shaft drives the rotating rings to rotate, the two inclined spray pipes can rotate to another direction, and two biogas slurry are sprayed on the deflection blades, so that the deflection blades rotate anticlockwise to rotate clockwise, the spraying direction of the two inclined spray pipes is changed, meanwhile, the stirring shaft on the deflection blades can also change anticlockwise to stir clockwise, and the biogas slurry hydrolysis temperature can be rapidly and uniformly realized;
According to the invention, a circulating pressurizing assembly is adopted, an outer discharge valve is closed through a controller, two liquid outlet electric valves and two liquid inlet electric valves are opened, two circulating pump machines enable two suction pipes to suck biogas slurry in a tank body into the two liquid inlet electric valves respectively, the biogas slurry is conveyed into a supply pipe through a heat exchange pipe, the supply pipe is used for filling the biogas slurry into the liquid outlet electric valves, a deflection hose is used for conveying the biogas slurry into an inclined spray pipe, the two inclined spray pipes can be used for obliquely pressurizing and spraying the biogas slurry on deflection blades, the biogas slurry in the tank body can be circulated up and down, the anticlockwise rotation stirring of a stirring shaft can be realized by utilizing the biogas slurry spraying, and the temperature of the biogas slurry can be rapidly and uniformly realized;
Through the mutual influence of a plurality of effects, firstly, the counter-clockwise rotation stirring of the stirring shaft can be realized by utilizing biogas slurry injection, secondly, the two toothed plates can synchronously move and shift to the sensing distance position of the shifting distance sensor, and then the two inclined spray pipes can rotate to another direction, the stirring shaft can also change anticlockwise into clockwise stirring, so that the biogas slurry can be circularly regulated from bottom to top to the sum, and the biogas slurry circulation impulsive force can be utilized to realize anticlockwise rotation of the biogas slurry and then clockwise rotation shifting of the biogas slurry, and the biogas slurry in the hydrolysis tank can rapidly realize uniform temperature.
Drawings
Fig. 1 is a schematic diagram of a main view structure of a biogas slurry hydrolysis tank with a double-pump temperature-regulating self-circulation function.
Fig. 2 is a schematic view of a partial structure of a vertical section of a can body according to the present invention.
Fig. 3 is a schematic view of a partial structure of a cross section of a can body according to the present invention.
Fig. 4 is a schematic view of a cross-sectional cut-away partial structure of the connection of the tank body and the frame plate according to the present invention.
Fig. 5 is an enlarged schematic view of the structure of fig. 4 a according to the present invention.
FIG. 6 is a schematic view of a vertical section cut-off partial structure of the connection of the tank and the deflection hose of the present invention.
Fig. 7 is a schematic diagram of a front view of a circulating booster assembly according to the present invention.
Fig. 8 is a schematic view showing a bottom partial structure of a junction between a solar panel and a storage battery according to the present invention.
The reference numerals are: 1.a tank body; 2. a frame plate; 3. a speed reducing motor; 4. sleeving blocks; 5. a screw; 6. a linkage bar; 7. a toothed plate; 8. a distance sensor; 9. a displacement distance sensor; 10. a feed hopper; 11. a controller; 12. a rotating shaft; 13. decomposing the exhaust pipe; 14. a feed pipe; 15. a deflection blade; 16. a stirring shaft; 17. a toothed ring; 18. a rotating rod; 19. a sleeve plate; 20. a bearing ring; 21. a frame is supported; 22. supporting the sleeve plate; 23. a slip ring; 24. a swivel; 25. tilting the nozzle; 26. a deflection hose; 27. a liquid outlet electric valve; 28. a supply pipe; 29. a heat exchange tube; 30. a circulating pump; 31. a liquid inlet electric valve; 32. a suction pipe; 33. an outer discharge valve; 34. a temperature sensor; 35. a linkage shaft; 36. a solar cell panel; 37. a storage battery; 38. an inverter; 39. a pressure sensor.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
1-8, The biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function is provided with an accurate position-changing mechanism, a position-changing temperature-equalizing component and a circulating pressurizing component, the temperature of the biogas slurry can be regulated circularly from bottom to top by the arrangement of the mechanisms and the components, the clockwise rotation position-changing can be carried out after the counterclockwise rotation of the biogas slurry is realized by utilizing the circulating impulsive force of the biogas slurry, the temperature uniformity can be rapidly realized by the biogas slurry in the hydrolysis tank, and the specific structures of the mechanisms and the components are as follows:
In the technical scheme, as shown in figures 1-5, the accurate displacement mechanism comprises a screw 5 fixedly arranged at the output end of a speed reducing motor 3, and the speed reducing motor 3 is used for driving the screw 5 to rotate; the accurate displacement mechanism further comprises a sleeve block 4, a linkage bar 6, two toothed plates 7, a distance sensor 8 and a displacement distance sensor 9; the sleeve block 4 is in threaded connection with the outer wall of the screw 5, the linkage bar 6 is welded at the top end of the sleeve block 4, and the two toothed plates 7 are respectively fixed at the two ends of the linkage bar 6; the distance sensor 8 is positioned in front of the linkage bar 6, the displacement distance sensor 9 is positioned behind the linkage bar 6, and the bottom ends of the distance sensor 8 and the displacement distance sensor 9 are fixedly connected with the top end of the frame plate 2; and one side of each toothed plate 7 is provided with a deflection temperature equalizing component.
In the technical scheme, as shown in figures 1-4, the top end of a tank body 1 is fixedly connected with a controller 11, and one side of the controller 11 is provided with a rotating shaft 12 which is rotationally connected with the tank body 1;
A decomposing exhaust pipe 13 communicated with the tank body 1 is arranged on one side of the rotating shaft 12, a feeding pipe 14 is communicated on one side of the decomposing exhaust pipe 13, and a feeding hopper 10 is communicated at the top end of the feeding pipe 14; the feed hopper 10 and the tank body 1 are fixedly connected with the feed pipe 14, so that biogas slurry and hydrolytic microorganisms are filled into the feed hopper 10, the feed hopper 10 is filled into the feed pipe 14, the feed pipe 14 is used for filling the biogas slurry and hydrolytic microorganisms into the tank body 1, the controller 11 is used for closing the outer discharge valve 33, the bottom end of the rotating shaft 12 is welded with the deflection blade 15, the bottom end fixedly connected with stirring shaft 16 of the deflection blade 15, and the stirring shaft 16 is used for stirring the biogas slurry, so that the deflection blade 15 drives the stirring shaft 16 to stir the biogas slurry in reverse time, the two inclined spray pipes 25 can be used for mixing the biogas slurry circulation below the inner part of the tank body 1 with the biogas slurry above the inner part of the tank body 1, and anticlockwise stirring operation is realized on the biogas slurry inside the tank body 1.
In the technical scheme, as shown in fig. 5-6, each group of deflection temperature equalizing components comprises a toothed ring 17, a rotating rod 18, a sleeve plate 19, a bearing ring 20, a support frame 21, two slip rings 23, a rotating ring 24, an inclined spray pipe 25 and a linkage shaft 35; the toothed ring 17 is meshed and connected to one side of the toothed plate 7 in a transmission way, the rotating rod 18 is fixed on the inner wall of the toothed ring 17, the sleeve plate 19 is fixed at the bottom end of the toothed ring 17, the bearing ring 20 is rotatably connected to the outer wall of the rotating rod 18 and positioned below the sleeve plate 19, the supporting frame 21 is welded on the outer wall of the bearing ring 20, the two slip rings 23 are positioned below the sleeve plate 19, the linkage shaft 35 is fixed on the inner wall of the sleeve plate 19 and positioned on one side of the toothed ring 17, and the inner walls of the two slip rings 23 are fixedly connected with the outer wall of the linkage shaft 35; the swivel 24 is welded at the bottom end of the linkage shaft 35, and the inclined spray pipe 25 is fixedly connected to the inner wall of the swivel 24; the bottom end of the slip ring 23 is fixedly connected with a supporting sleeve plate 22, the outer wall of the supporting sleeve plate 22 is fixedly connected with the inner wall of the tank body 1, two pressure sensors 39 are fixedly connected to the top end of one of the support frames 21, and two heat exchange tubes 29 are symmetrically arranged about the rotating rod 18; the circulation pressurizing assembly is installed at one end of each inclined spray pipe 25, the outer wall of the linkage shaft 35 is in sliding connection with the inside of the supporting frame 21, the two sliding rings 23 are in sliding connection with the supporting frame 21, the two sliding rings 23 are symmetrically arranged relative to the supporting frame 21, the bottom end surface of the toothed ring 17 is higher than the top end surface of the linkage shaft 35, and the center point of the rotating rod 18 and the center point of the bearing ring 20 are in the same vertical line.
In this technical solution, as shown in fig. 6-8, each circulating booster component includes a displacement hose 26, a liquid outlet electric valve 27, a supply pipe 28, a heat exchange pipe 29, a circulating pump 30, a liquid inlet electric valve 31, a suction pipe 32, a solar panel 36, a storage battery 37 and an inverter 38; the deflection hose 26 is fixedly communicated with one end part of the inclined spray pipe 25, the liquid outlet electric valve 27 is fixedly communicated with one end part of the deflection hose 26, the outer wall of the deflection hose 26 is fixedly connected with the inner wall of the tank body 1, and the supply pipe 28 is fixedly connected with one end part of the liquid outlet electric valve 27 and communicated with the same; the heat exchange tube 29 is located the feed tube 28 bottom and fixed intercommunication, circulation pump machine 30 output fixed intercommunication is in heat exchange tube 29 bottom, and circulation pump machine 30 is used for the pressurization circulation natural pond liquid, feed liquor electric valve 31 is located circulation pump machine 30 input and fixed intercommunication, suction tube 32 fixed mounting is in feed liquor electric valve 31 one end, solar cell panel 36 is located circulation pump machine 30 one side, battery 37 is fixed in solar cell panel 36 bottom, dc-to-ac converter 38 fixed connection is in battery 37 bottom, outer row valve 33 is installed to suction tube 32's below, outer row valve 33's one end and jar body 1 outer wall fixed intercommunication, two temperature sensor 34 are installed to the below of shifting hose 26, two temperature sensor 34 all are with jar body 1 inner wall fixed connection.
The invention relates to a biogas slurry hydrolysis tank with a double-pump temperature-regulating self-circulation function, which is based on the following application principle:
When the biogas slurry and hydrolytic microorganism are ready to be used, the biogas slurry and hydrolytic microorganism are filled into the feed hopper 10, enter the feed pipe 14 through the feed hopper 10, are filled into the tank body 1 through the feed pipe 14, can contact the bottom end of the deflection blade 15, are in butt joint with the top end of the decomposition exhaust pipe 13, are arranged outdoors through the two solar panels 36, and can be respectively inverted through the two inverters 38 to store electric energy into the two storage batteries 37, and are inverted through the two storage batteries 37 through the two inverters 38 to supply electricity for the biogas slurry hydrolysis tank equipment;
In the two-pump circulation temperature adjustment of the invention, the controller 11 is used for closing the external discharge valve 33, opening the two liquid outlet electric valves 27 and the two liquid inlet electric valves 31, the controller 11 is used for starting the two circulating pump machines 30, the two circulating pump machines 30 respectively enable the two suction pipes 32 to suck the biogas slurry in the tank body 1 into the two liquid inlet electric valves 31, the liquid inlet electric valves 31 are used for filling the biogas slurry into the heat exchange pipes 29, the biogas slurry is conveyed into the supply pipes 28 through the heat exchange pipes 29, the supply pipes 28 are used for filling the biogas slurry into the liquid outlet electric valves 27, the liquid outlet electric valves 27 are used for conveying the biogas slurry through the displacement hose 26, the displacement hose 26 is used for conveying the biogas slurry into the inclined spray pipes 25, the two inclined spray pipes 25 can be used for obliquely jetting the biogas slurry onto the displacement blades 15, the two displacement blades 15 are used for anticlockwise rotating under the action of the two pressurized biogas slurry, and the two displacement blades 15 simultaneously drive the stirring shafts 16 to stir the biogas slurry, and simultaneously realize anticlockwise stirring of the biogas slurry in the tank body 1 by using the two inclined spray pipes 25 to circulate the biogas slurry below the inner part of the tank body 1 and the biogas slurry above the tank body 1;
Step three, when the invention is precisely shifted, the speed reducing motor 3 is started by the controller 11, the speed reducing motor 3 drives the screw rod 5 to rotate, the screw rod 5 carries the sleeve block 4 to approach to the shifting distance sensor 9 under the action of the screw transmission force, the sleeve block 4 carries the linkage bar 6 to move, the linkage bar 6 can drive the two toothed plates 7 to move at the same time, the shifting distance sensor 9 can sense the moving distance of the linkage bar 6, the distance sensor 8 can sense the distance of the linkage bar 6, and the two toothed plates 7 can synchronously move and shift;
in the fourth step, when the invention carries out deflection temperature equalization, the two toothed plates 7 respectively drive the two toothed rings 17 to rotate, the two toothed rings 17 synchronously rotate, the toothed rings 17 carry the rotating rods 18 to rotate, the rotating rods 18 rotate in the bearing rings 20, meanwhile, the supporting sleeve plate 22 provides supporting force for the supporting frame 21, the supporting frame 21 provides supporting force for the bearing rings 20, the toothed rings 17 carry the sleeve plate 19 to rotate, the sleeve plate 19 drives the linkage shaft 35 to realize stable rotation, the linkage shaft 35 drives the two sliding rings 23 to move, the two sliding rings 23 slide with the supporting frame 21, the linkage shaft 35 drives the rotating ring 24 to rotate, the rotating ring 24 drives the inclined spray pipes 25 to realize rotation operation, when the rotating ring 24 is extruded on the pressure sensor 39 in front of the toothed rings 17, meanwhile, when the distance sensed by the displacement distance sensor 9 and the linkage bar 6 is the distance set by the controller 11, and when the distance sensed by the distance sensor 8 on the linkage bar 6 is the distance set by the controller 11, the gear motor 3 is closed by the controller 11, the two inclined spray pipes 25 can rotate to another direction, the two inclined spray pipes 25 continue to spray biogas slurry, and the two biogas slurries are sprayed on the displacement blades 15, so that the displacement blades 15 rotate anticlockwise to rotate clockwise, the displacement blades 15 drive the stirring shaft 16 to rotate, the stirring shaft 16 rotates clockwise on the biogas slurry on the inner wall of the tank body 1, and after the displacement direction, the biogas slurry in the tank body 1 can flow and displace in an up-down circulating manner, and meanwhile, the rotation displacement on the biogas slurry can be realized;
And fifthly, when the temperature is shifted, the temperature sensing of the biogas slurry in the tank body 1 can be realized through the two temperature sensors 34, when the temperatures sensed by the two temperature sensors 34 are the same, the two circulating pump 30 are closed through the controller 11, and meanwhile, the discharge valve 33 is opened to discharge the biogas slurry in the tank body 1.
The details not described in detail in the specification belong to the prior art known to those skilled in the art, and model parameters of each electric appliance are not specifically limited, and conventional equipment is used.
The foregoing description of the preferred embodiments of the invention is not intended to limit the invention to the precise form disclosed, and any such modifications, equivalents, and alternatives falling within the spirit and principles of the invention are intended to be included within the scope of the invention.
Claims (10)
1. The utility model provides a natural pond liquid hydrolysis tank with self-loopa function adjusts temperature by two pumps, includes jar body (1), frame board (2) and gear motor (3), frame board (2) are fixed at jar body (1) inner wall, gear motor (3) fixed mounting is at frame board (2) inner wall, its characterized in that: an output end of the speed reducing motor (3) is provided with an accurate displacement mechanism;
The precise displacement mechanism comprises a screw rod (5) fixedly arranged at the output end of the speed reducing motor (3), and the speed reducing motor (3) is used for driving the screw rod (5) to rotate;
The precise displacement mechanism further comprises a sleeve block (4), a linkage bar (6), two toothed plates (7), a distance sensor (8) and a displacement distance sensor (9);
the sleeve block (4) is in threaded connection with the outer wall of the screw rod (5), the linkage bar (6) is welded at the top end of the sleeve block (4), and the two toothed plates (7) are respectively fixed at the two ends of the linkage bar (6);
the distance sensor (8) is positioned in front of the linkage bar (6), the displacement distance sensor (9) is positioned behind the linkage bar (6), and the bottom ends of the distance sensor (8) and the displacement distance sensor (9) are fixedly connected with the top end of the frame plate (2);
One side of each toothed plate (7) is provided with a deflection temperature equalizing component.
2. The biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function according to claim 1, wherein the tank is characterized in that: the outer wall of the sleeve block (4) is in sliding connection with the inner wall of the frame plate (2), and the outer wall of the sleeve block (4) and the inner wall of the frame plate (2) are polished;
the frame plate (2) and the sleeve block (4) are both made of stainless steel materials.
3. The biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function according to claim 1, wherein the tank is characterized in that: the cross section shape of the two toothed plates (7) is L-shaped, and the two toothed plates (7) are sequentially arranged from right to left.
4. The biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function according to claim 1, wherein the tank is characterized in that: the top end of the tank body (1) is fixedly connected with a controller (11), and one side of the controller (11) is provided with a rotating shaft (12) which is rotationally connected with the tank body (1);
A decomposition exhaust pipe (13) communicated with the tank body (1) is arranged on one side of the rotating shaft (12), a feed pipe (14) is communicated on one side of the decomposition exhaust pipe (13), and a feed hopper (10) is communicated at the top end of the feed pipe (14);
The feed hopper (10) and the tank body (1) are fixedly connected with the feed pipe (14).
5. The biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function according to claim 4, wherein the biogas slurry hydrolysis tank is characterized in that: the bottom of pivot (12) is welded with and is shifted blade (15), the bottom fixedly connected with (16) of blade (15) shifts, just (16) are used for stirring the natural pond liquid.
6. The biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function according to claim 1, wherein the tank is characterized in that: each group of deflection temperature equalization components comprises a toothed ring (17), a rotating rod (18), a sleeve plate (19), a bearing ring (20), a support frame (21), two slip rings (23), a rotating ring (24), an inclined spray pipe (25), a linkage shaft (35) and a pressure sensor (39);
The gear ring (17) is meshed and connected to one side of the gear plate (7), the rotating rod (18) is fixed on the inner wall of the gear ring (17), the sleeve plate (19) is fixed at the bottom end of the gear ring (17), the bearing ring (20) is rotationally connected to the outer wall of the rotating rod (18) and located below the sleeve plate (19), the support frame (21) is welded on the outer wall of the bearing ring (20), two sliding rings (23) are located below the sleeve plate (19), the linkage shaft (35) is fixed on the inner wall of the sleeve plate (19) and located on one side of the gear ring (17), and the inner walls of the two sliding rings (23) are fixedly connected with the outer wall of the linkage shaft (35);
The swivel (24) is welded at the bottom end of the linkage shaft (35), and the inclined spray pipe (25) is fixedly connected to the inner wall of the swivel (24);
the bottom end of the slip ring (23) is fixedly connected with a support sleeve plate (22), and the outer wall of the support sleeve plate (22) is fixedly connected with the inner wall of the tank body (1);
the two pressure sensors (39) are fixedly connected to the top end of one of the support frames (21), and the two pressure sensors (39) are symmetrically arranged about the rotating rod (18);
a circulating and pressurizing assembly is arranged at one end part of each inclined spray pipe (25).
7. The biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function according to claim 6, wherein the biogas slurry hydrolysis tank is characterized in that: the outer wall of the linkage shaft (35) is in sliding connection with the inside of the support frame (21), the two slip rings (23) are in sliding connection with the support frame (21), and the two slip rings (23) are symmetrically arranged relative to the support frame (21).
8. The biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function according to claim 6, wherein the biogas slurry hydrolysis tank is characterized in that: the bottom end surface of the toothed ring (17) is higher than the top end surface of the linkage shaft (35), and the center point of the rotating rod (18) and the center point of the bearing ring (20) are positioned in the same vertical line.
9. The biogas slurry hydrolysis tank with the double-pump temperature-regulating self-circulation function according to claim 6, wherein the biogas slurry hydrolysis tank is characterized in that: each circulating pressurizing assembly comprises a deflection hose (26), a liquid outlet electric valve (27), a supply pipe (28), a heat exchange pipe (29), a circulating pump (30), a liquid inlet electric valve (31), a suction pipe (32), a solar cell panel (36), a storage battery (37) and an inverter (38);
The displacement hose (26) is fixedly communicated with one end part of the inclined spray pipe (25), the liquid outlet electric valve (27) is fixedly communicated with one end part of the displacement hose (26), the outer wall of the displacement hose (26) is fixedly connected with the inner wall of the tank body (1), and the supply pipe (28) is fixedly connected with one end part of the liquid outlet electric valve (27) and communicated with the other end part of the liquid outlet electric valve;
The utility model provides a solar energy heat pump, including heat exchange tube (29), circulating pump machine (30), battery (37), dc-to-ac converter, battery (37) are located supply tube (28) bottom and fixed intercommunication, circulating pump machine (30) output fixed intercommunication is in heat exchange tube (29) bottom, just circulating pump machine (30) are used for the pressurization cycle natural pond liquid, feed liquor electric valve (31) are located circulating pump machine (30) input and fixed intercommunication, suction tube (32) fixed mounting is in feed liquor electric valve (31) one end, solar cell panel (36) are located circulating pump machine (30) one side, battery (37) are fixed in solar cell panel (36) bottom, dc-to-ac converter (38) fixed connection is in battery (37) bottom.
10. The biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function according to claim 9, wherein the tank is characterized in that: an outer valve (33) is arranged below the suction pipe (32), one end of the outer valve (33) is fixedly communicated with the outer wall of the tank body (1), two temperature sensors (34) are arranged below the deflection hose (26), and the two temperature sensors (34) are fixedly connected with the inner wall of the tank body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202410460012.6A CN118064265B (en) | 2024-04-17 | Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202410460012.6A CN118064265B (en) | 2024-04-17 | Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN118064265A true CN118064265A (en) | 2024-05-24 |
| CN118064265B CN118064265B (en) | 2024-07-02 |
Family
ID=
Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201924008U (en) * | 2010-12-13 | 2011-08-10 | 萧县爱得葡萄深加工研发有限公司 | Automatic vinegar brewing equipment |
| CN202322828U (en) * | 2011-11-17 | 2012-07-11 | 西安建筑科技大学 | Energy-saving anaerobic fermentation device |
| CN103391808A (en) * | 2011-02-17 | 2013-11-13 | 新东工业株式会社 | Tank apparatus, circulating-type dispersion system, and dispersion method |
| CN205188301U (en) * | 2015-12-03 | 2016-04-27 | 丰城黑五类食品有限公司 | Biodiasmin is with automatic fermentation cylinder that has feed arrangement |
| CN206014920U (en) * | 2016-09-20 | 2017-03-15 | 济宁学院 | Biomass ferment consersion unit |
| CN106701546A (en) * | 2017-02-11 | 2017-05-24 | 曲阜七星沼气科技发展有限公司 | Solar vacuum constant-temperature marsh gas reaction tank |
| CN206872693U (en) * | 2017-06-28 | 2018-01-12 | 山西玉衡同创环境技术有限公司 | Biogas slurry organic fertilizer preparation system |
| EP3336168A1 (en) * | 2009-05-20 | 2018-06-20 | Xyleco, Inc. | Processing biomass |
| CN109107359A (en) * | 2018-11-02 | 2019-01-01 | 山西资环科技股份有限公司 | A kind of methane bio-desulfurization system |
| CN209997478U (en) * | 2019-03-22 | 2020-01-31 | 新疆美克化工股份有限公司 | Formaldehyde solution self-loopa stirring hinders and gathers device |
| DE202020105739U1 (en) * | 2020-10-07 | 2021-01-14 | Tongji University | System device for decarbonisation and synchronous recovery of nitrogen and phosphorus from negative pressure biogas slurry |
| CN214571820U (en) * | 2021-02-24 | 2021-11-02 | 上海宝鼎酿造有限公司 | Solid-state fermentation tank convenient to reduce product temperature |
| CN216764885U (en) * | 2021-06-29 | 2022-06-17 | 四川大学 | Biogas fermentation tank and biogas system |
| CN218026061U (en) * | 2022-04-29 | 2022-12-13 | 内蒙古华蒙科创环保科技工程有限公司 | Accurate temperature regulating device for biogas fermentation tank |
Patent Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3336168A1 (en) * | 2009-05-20 | 2018-06-20 | Xyleco, Inc. | Processing biomass |
| CN201924008U (en) * | 2010-12-13 | 2011-08-10 | 萧县爱得葡萄深加工研发有限公司 | Automatic vinegar brewing equipment |
| CN103391808A (en) * | 2011-02-17 | 2013-11-13 | 新东工业株式会社 | Tank apparatus, circulating-type dispersion system, and dispersion method |
| CN202322828U (en) * | 2011-11-17 | 2012-07-11 | 西安建筑科技大学 | Energy-saving anaerobic fermentation device |
| CN205188301U (en) * | 2015-12-03 | 2016-04-27 | 丰城黑五类食品有限公司 | Biodiasmin is with automatic fermentation cylinder that has feed arrangement |
| CN206014920U (en) * | 2016-09-20 | 2017-03-15 | 济宁学院 | Biomass ferment consersion unit |
| CN106701546A (en) * | 2017-02-11 | 2017-05-24 | 曲阜七星沼气科技发展有限公司 | Solar vacuum constant-temperature marsh gas reaction tank |
| CN206872693U (en) * | 2017-06-28 | 2018-01-12 | 山西玉衡同创环境技术有限公司 | Biogas slurry organic fertilizer preparation system |
| CN109107359A (en) * | 2018-11-02 | 2019-01-01 | 山西资环科技股份有限公司 | A kind of methane bio-desulfurization system |
| CN209997478U (en) * | 2019-03-22 | 2020-01-31 | 新疆美克化工股份有限公司 | Formaldehyde solution self-loopa stirring hinders and gathers device |
| DE202020105739U1 (en) * | 2020-10-07 | 2021-01-14 | Tongji University | System device for decarbonisation and synchronous recovery of nitrogen and phosphorus from negative pressure biogas slurry |
| CN214571820U (en) * | 2021-02-24 | 2021-11-02 | 上海宝鼎酿造有限公司 | Solid-state fermentation tank convenient to reduce product temperature |
| CN216764885U (en) * | 2021-06-29 | 2022-06-17 | 四川大学 | Biogas fermentation tank and biogas system |
| CN218026061U (en) * | 2022-04-29 | 2022-12-13 | 内蒙古华蒙科创环保科技工程有限公司 | Accurate temperature regulating device for biogas fermentation tank |
Non-Patent Citations (1)
| Title |
|---|
| 禹言芳等: "新型循环射流混合器湍流特性分析", 《过程工程学报》, vol. 11, no. 01, 28 February 2011 (2011-02-28), pages 1 - 8 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN118064265B (en) | Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function | |
| CN118064265A (en) | Biogas slurry hydrolysis tank with double-pump temperature-regulating self-circulation function | |
| CN212669689U (en) | Anaerobic fermentation biogas fermentation equipment | |
| CN207811717U (en) | A kind of wine brewing material blending device | |
| CN108854744A (en) | A kind of energy-saving production device of emulsified pitch | |
| CN206143202U (en) | High -efficient dry -type anaerobic fermentation tank of modular | |
| CN213369063U (en) | Liquid strain fermentation device for edible mushroom inoculation | |
| CN214863575U (en) | Device for reducing energy consumption in iron oxide red processing production | |
| CN104263639A (en) | Dry fermentation system and fermentation method thereof | |
| CN210974663U (en) | Culture apparatus for biological fermentation | |
| CN204097478U (en) | A kind of dry method fermentation system | |
| CN113680261A (en) | Raw materials mixes and preprocessing device for emulsion processing | |
| CN112619589A (en) | Combined device for preparing mixed fatty acid methyl ester | |
| CN207973760U (en) | A kind of environment-friendly type fermentation tank | |
| CN111603957A (en) | Novel powder stirring device | |
| CN218222450U (en) | Yellow phosphorus refining storage tank | |
| CN201389433Y (en) | Rotary nozzle type stirrer | |
| CN213229989U (en) | Store up thick liquid bucket with heating function | |
| CN218404253U (en) | Temperature-controlled fermentation device | |
| CN216826104U (en) | Laboratory high-pressure batch autoclave | |
| CN217677441U (en) | Microbial fermentation is even reaction unit for traditional chinese medicine | |
| CN219849054U (en) | Batching production jar of antiseized structure | |
| CN220737380U (en) | Dissolving device | |
| CN220835534U (en) | Polyester resin reaction kettle with uniform heating | |
| CN219091844U (en) | Homogenizer is used in shower gel production |
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 |