CN220334953U - High-temperature anaerobic reaction tank - Google Patents
High-temperature anaerobic reaction tank Download PDFInfo
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- CN220334953U CN220334953U CN202321560589.1U CN202321560589U CN220334953U CN 220334953 U CN220334953 U CN 220334953U CN 202321560589 U CN202321560589 U CN 202321560589U CN 220334953 U CN220334953 U CN 220334953U
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 130
- 239000010865 sewage Substances 0.000 claims abstract description 68
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 44
- 230000023556 desulfurization Effects 0.000 claims abstract description 44
- 230000007246 mechanism Effects 0.000 claims abstract description 32
- 238000002156 mixing Methods 0.000 claims abstract description 30
- 230000006837 decompression Effects 0.000 claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 171
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 90
- 238000002485 combustion reaction Methods 0.000 claims description 28
- 239000007921 spray Substances 0.000 claims description 25
- 239000007788 liquid Substances 0.000 claims description 14
- 239000002274 desiccant Substances 0.000 claims description 10
- 238000012544 monitoring process Methods 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 3
- 239000012153 distilled water Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 18
- 238000000855 fermentation Methods 0.000 abstract description 6
- 230000004151 fermentation Effects 0.000 abstract description 6
- 230000009471 action Effects 0.000 description 7
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 6
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 6
- 239000010802 sludge Substances 0.000 description 5
- 230000003009 desulfurizing effect Effects 0.000 description 4
- KAEAMHPPLLJBKF-UHFFFAOYSA-N iron(3+) sulfide Chemical compound [S-2].[S-2].[S-2].[Fe+3].[Fe+3] KAEAMHPPLLJBKF-UHFFFAOYSA-N 0.000 description 4
- JGIATAMCQXIDNZ-UHFFFAOYSA-N calcium sulfide Chemical compound [Ca]=S JGIATAMCQXIDNZ-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 230000001603 reducing effect Effects 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Treating Waste Gases (AREA)
Abstract
The utility model relates to the technical field of sewage treatment, in particular to a high-temperature anaerobic reaction tank, which comprises a reaction tank body, wherein a sewage mixing mechanism is arranged on the surface of the reaction tank body, a rapid decompression mechanism is arranged on the surface of the reaction tank body, and a drying and desulfurization treatment mechanism is arranged in a treatment tank. According to the utility model, when the reaction tank is used, sewage below the reaction tank can be conveyed to the upper end of the reaction tank, the effect of uniformly mixing the sewage is achieved from top to bottom, the fermentation effect is more comprehensive, the danger caused by overlarge biogas pressure in the reaction tank body can be prevented when the reaction tank is used, the integral safety performance of the reaction tank is improved, the problem of biogas treatment can be more comprehensively solved when the reaction tank is used, the reaction tank is more practical and convenient to use, and the use requirement of the reaction tank can be met.
Description
Technical Field
The utility model relates to the technical field of sewage treatment, in particular to a high-temperature anaerobic reaction tank.
Background
A large amount of sludge and sewage is produced in farms every day, and a large amount of sewage is discharged into rivers and lakes every year, so that a high-temperature anaerobic reaction tank is needed.
Firstly, after sewage enters the reaction tank, substances which react with the sewage need to be added to cause chemical reaction, and the existing reaction tank is inconvenient to mix the sewage uniformly when in use, so that the sewage below the reaction tank cannot be conveyed to the upper end of the reaction tank when in use, and the fermentation effect is not comprehensive enough; secondly, the internal pressure of the reaction tank can be increased when the reaction tank is used, if the internal pressure of the reaction tank is not timely reduced, the explosion risk is easy to occur, the pressure reducing effect of the existing reaction tank in the use process is not good enough, and the overall safety performance of the reaction tank is greatly reduced when the reaction tank is used; thirdly, after sewage is treated by the reaction tank, methane can be generated, sulfide and moisture are contained in the methane, so that the sulfide and the moisture in the methane are required to be treated, the existing reaction tank cannot dry the methane and desulfurize the methane when in use, the problem of methane treatment cannot be more comprehensively solved when the reaction tank is in use, and the reaction tank is not practical and convenient to use.
Disclosure of Invention
The utility model aims to provide a high-temperature anaerobic reaction tank, which solves the problems that the reaction tank is inconvenient to mix sewage uniformly when in use, the pressure reducing effect is not good enough in the use process, and methane cannot be dried and desulfurized.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a high temperature anaerobic reaction tank, includes the retort body, the surface mounting of retort body has control button, the internally mounted of retort body has fixed inner tank, the surface mounting of retort body has the treatment box, the surface mounting of retort body has a water inlet tube, the one end of water inlet tube runs through the inside of retort body and fixed inner tank and extension to fixed inner tank, the surface mounting of retort body has the blast pipe, the one end of blast pipe runs through the inside of retort body and fixed inner tank and extension to fixed inner tank, the surface mounting of retort body has the air duct, the one end of air duct runs through the inside of retort body and extends to the retort body, the surface of retort body is provided with sewage mixing mechanism, sewage mixing mechanism's inside contains water suction pipe, water suction pump and sewage mixing portion, the surface of retort body is provided with quick decompression mechanism, quick decompression mechanism's inside contains liquid level monitor, water tank body and quick portion, the inside of treatment box is provided with drying mechanism and drying mechanism, drying mechanism and drying mechanism.
Preferably, the surface mounting of fixed inner tank has driving motor, driving motor's input and control button's output electric connection, driving motor's output has the pivot through the shaft coupling, the one end of pivot runs through the inside of fixed inner tank and extends to fixed inner tank, the inside of fixed inner tank is provided with the blender, the inner wall mutually rotates the cooperation of blender and fixed inner tank, the surface of blender top position processing is fixed with the surface of pivot, equidistant puddler is all installed on the surface of blender, the orifice plate is installed to the inner wall of fixed inner tank, baffle body is installed to the inner wall of retort body, fixed through-hole has all been seted up on baffle body's surface, the surface mounting of retort body has the pressure detector who is used for carrying out the monitoring to the pressure of retort body inside, pressure detector is linked together with the inside of retort body, the other end of air duct runs through the inside of processing case and extends to the processing case, the drain pipe is installed to the bottom of retort body, the drain pipe's one end runs through the fixed inner tank and the surface of a fixed valve and the inner tank and the inner wall of a fixed surface of a fixed valve body is installed to the inner tank, and the inner valve door is connected with the first electric connection of the inner tank, the drain door is installed with the first surface of the fixed valve.
Preferably, the sewage mixing part is arranged on the surface of the reaction tank body and the fixed inner tank, the sewage mixing part is composed of a water diversion pipe and a first spray head, a water suction pump is arranged on the surface of the top position of the fixed inner tank, the input end of the water suction pump is electrically connected with the output end of the control button, the water suction pipe is arranged at the output end of the water suction pump, and one end of the water suction pipe penetrates through the reaction tank body and the fixed inner tank and extends to the inside of the fixed inner tank.
Preferably, the water diversion pipe is installed to the output of water suction pump, the one end of water diversion pipe runs through the retort body and extends to the inside of retort body, the inside of retort body is provided with the first shower nozzle that is used for the water spray, the surface of first shower nozzle is linked together with the water diversion pipe.
Preferably, the quick decompression portion is arranged in the reaction tank body and on the surface of the reaction tank body, the quick decompression portion is composed of a connecting pipe and a second spray head, a water tank body is arranged on the surface of the top of the reaction tank body, a connecting pipe is arranged in the water tank body, one end of the connecting pipe penetrates through the reaction tank body and extends to the inside of the reaction tank body, a second valve is sleeved on the surface of the connecting pipe, and the input end of the second valve is electrically connected with the output end of the control button.
Preferably, the inner wall of the reaction tank body is provided with a water pipe, the water pipe is communicated with the connecting pipe, the inside of the reaction tank body is provided with a second spray head for spraying water, the second spray head is communicated with the inside of the water pipe, the inner wall of the water tank body is provided with a liquid level monitor for monitoring the liquid level inside the liquid level monitor, the surface mounting at the top of the water tank body is provided with a pipe body for water inflow, and one end of the pipe body penetrates through the water tank body and extends to the inside of the water tank body.
Preferably, the desulfurization box is installed to the inner wall of handling the case, equidistant marsh gas desulfurization drier is all installed to the inside of desulfurization box, the internally mounted of handling the case has the siphunculus body, the one end of siphunculus body runs through the desulfurization box and extends to the inside of desulfurization box, the combustion chamber is installed to the inner wall of handling the case, the other end of siphunculus body runs through the combustion chamber and extends to the inside of combustion chamber, the combustion chamber is located the below of desulfurization box.
Preferably, the inner wall of the treatment tank is provided with a water storage tank for collecting distilled water, the water storage tank is located below the combustion chamber and is communicated with the combustion chamber, the surface of the water storage tank is provided with a water outlet pipe, one end of the water outlet pipe penetrates through the water storage tank, the treatment tank and extends to the outer side of the treatment tank, the surface of the water outlet pipe is sleeved with a third valve, and meanwhile, the input end of the third valve is electrically connected with the output end of the control button.
Compared with the prior art, the utility model has the beneficial effects that: the warm anaerobic reaction tank not only can convey sewage below the reaction tank to the upper end of the reaction tank when the reaction tank is used, but also plays a role of uniformly mixing the sewage from top to bottom, and the interval time can uniformly mix the sewage, so that the fermentation effect is more comprehensive, the danger caused by overlarge biogas pressure in the reaction tank body can be prevented when the reaction tank is used, the integral safety performance of the reaction tank is improved, the problem of biogas treatment can be more comprehensively solved when the reaction tank is used, the reaction tank is more practical and convenient to use, and the use requirement of the reaction tank can be met;
1. through being provided with sewage mixing mechanism, control the work of water suction pump, the effect of water suction pipe is through inhaling the sewage of retort body lower extreme to the inside of leading water pipe under the effect of water suction pump, afterwards, sewage rethread leading water pipe gets into the inside of first shower nozzle, spray sewage under the effect of first shower nozzle, thereby mix sewage, the time mixing sewage like this can be safer, the function of retort mixing sewage has been realized, thereby can carry the sewage below the retort to the retort upper end when making the retort use, from top to bottom the effect of mixing sewage, this kind of time mixing sewage can make fermentation effect more comprehensive;
2. through being provided with quick decompression mechanism, marsh gas pressure in the retort body is too big and can produce danger, at this moment, the inside leading-in water of body to the water tank through the body, at this moment, monitor the water yield in the water tank body under the effect of liquid level monitor, afterwards, the second shower nozzle on control water pipe surface works, the inside leading-in inside of connecting pipe of water tank body through the connecting pipe, the second valve work on control connecting pipe surface again, make water get into the inside of water pipe through the connecting pipe, at this moment, the control button is operated again, make control button control second shower nozzle work, spray water under the effect of second shower nozzle, can play the effect of decompression to the inside of retort body, thereby can prevent the dangerous that the marsh gas pressure is too big in the jar body, realized the quick decompression function of retort, thereby can prevent the danger that marsh gas pressure is too big in the retort body when making the retort use, holistic security performance when having improved the retort use.
3. Through being provided with drying and desulfurization treatment facility, marsh gas gets into the inside of desulfurization case through the treatment box, when hydrogen sulfide and other harmful gas in the marsh gas passes through from the surface of marsh gas desulfurization drier, produce chemical reaction and physical adsorption, hydrogen sulfide in the marsh gas generates ferric sulfide and calcium sulfide, adsorb on the surface of marsh gas desulfurization drier, pure marsh gas gets into the inside of combustion chamber through the siphunculus body, burn in the inside of combustion chamber, vapor is adsorbed in the inside of marsh gas desulfurization drier, the vapor condenses into water after, the comdenstion water falls into the aqua storage tank, the third valve work on the water outlet pipe surface is controlled again, the comdenstion water can be discharged from the outlet pipe afterwards, realized the retort and to marsh gas drying and desulfurization treatment's function, thereby the processing problem of marsh gas can be more comprehensive solved when making the retort use, make the retort use more practical convenient, the user demand when more can satisfy the use.
Drawings
FIG. 1 is a schematic three-dimensional perspective view of the present utility model;
FIG. 2 is a schematic view of a front cross-sectional structure of the present utility model;
FIG. 3 is an enlarged schematic view of the sewage mixing mechanism of FIG. 2 according to the present utility model;
FIG. 4 is an enlarged schematic view of the quick decompression mechanism of FIG. 2 according to the present utility model;
FIG. 5 is an enlarged schematic view of the drying and desulfurizing treatment mechanism of the present utility model.
In the figure: 1. a reaction tank body; 101. a control button; 102. fixing the inner tank; 103. a treatment box; 104. a water inlet cylinder; 105. an exhaust pipe; 106. a driving motor; 107. a rotating shaft; 108. a pressure detector; 109. an air duct; 110. a fixing through hole; 111. a baffle body; 112. a blow-down pipe; 113. a stirring rod; 114. a mixer; 115. an orifice plate; 2. a sewage mixing mechanism; 201. a water suction pipe; 202. a water suction pump; 203. a sewage mixing part; 2031. a water conduit; 2032. a first nozzle; 3. a rapid decompression mechanism; 301. a liquid level monitor; 302. a water tank body; 303. a rapid decompression section; 3031. a connecting pipe; 3032. a second nozzle; 4. a drying and desulfurizing treatment mechanism; 401. a water storage tank; 402. a biogas desulfurization drying agent; 403. a desulfurization tank; 404. a tube body; 405. a combustion chamber.
Detailed Description
The following description of the embodiments of the present utility model 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 utility model, but not all embodiments.
The structure of the high-temperature anaerobic reaction tank provided by the utility model is shown in figures 1 and 2, the high-temperature anaerobic reaction tank comprises a reaction tank body 1, a control button 101 is arranged on the surface of the reaction tank body 1, the model of the control button 101 can be LA series, a fixed inner tank 102 is arranged in the reaction tank body 1, a treatment box 103 is arranged on the surface of the reaction tank body 1, a driving motor 106 is arranged on the surface of the fixed inner tank 102, the model of the driving motor 106 can be JO series, the input end of the driving motor 106 is electrically connected with the output end of the control button 101, a rotating shaft 107 is arranged at the output end of the driving motor 106 through a coupler, one end of the rotating shaft 107 penetrates through the fixed inner tank 102 and extends into the fixed inner tank 102, a mixer 114 is arranged in the fixed inner tank 102, the mixer 114 is in mutual rotation fit with the inner wall of the fixed inner tank 102, the surface at the top position of the mixer 114 is fixed with the surface of the rotating shaft 107, the surface of the mixer 114 is provided with equidistant stirring rods 113, the inner wall of the fixed inner tank 102 is provided with a pore plate 115, the surface of the reaction tank body 1 is provided with a water inlet cylinder 104, one end of the water inlet cylinder 104 penetrates through the reaction tank body 1 and the fixed inner tank 102 and extends to the inside of the fixed inner tank 102, the surface of the reaction tank body 1 is provided with an exhaust pipe 105, one end of the exhaust pipe 105 penetrates through the reaction tank body 1 and the fixed inner tank 102 and extends to the inside of the fixed inner tank 102, the inner wall of the reaction tank body 1 is provided with a baffle body 111, the surface of the baffle body 111 is provided with a fixed through hole 110, the surface of the reaction tank body 1 is provided with a pressure detector 108 for monitoring the pressure inside the reaction tank body 1, the pressure detector 108 is communicated with the inside of the reaction tank body 1, the surface of the reaction tank body 1 is provided with an air duct 109, one end of the air duct 109 penetrates the reaction tank body 1 and extends to the inside of the reaction tank body 1, the other end of the air duct 109 penetrates the treatment box 103 and extends to the inside of the treatment box 103, a drain pipe 112 is installed at the bottom of the reaction tank body 1, one end of the drain pipe 112 penetrates the reaction tank body 1, the fixed inner tank 102 and extends to the inside of the fixed inner tank 102, a first valve is sleeved on the surface of the drain pipe 112, the type of the first valve is a TM series, the input end of the first valve is electrically connected with the output end of the control button 101, a door body is arranged on the surface of the treatment box 103, and the door body is in mutual running fit with the surface of the treatment box 103.
Further, as shown in fig. 2 and 3, the surface of the reaction tank body 1 is provided with a sewage mixing mechanism 2, the interior of the sewage mixing mechanism 2 includes a water suction pipe 201, a water suction pump 202 and a sewage mixing portion 203, the sewage mixing portion 203 is disposed on the surface of the reaction tank body 1 and the fixed inner tank 102, the sewage mixing portion 203 is composed of a water suction pipe 2031 and a first spray head 2032, the surface of the top of the fixed inner tank 102 is provided with the water suction pump 202, the type of the water suction pump 202 is selected from SLA series, the input end of the water suction pump 202 is electrically connected with the output end of the control button 101, the output end of the water suction pump 202 is provided with the water suction pipe 201, one end of the water suction pipe 201 penetrates through the reaction tank body 1 and the fixed inner tank 102 and extends to the interior of the fixed inner tank 102, the output end of the water suction pump 202 is provided with the water suction pipe 2031, one end of the water suction pipe 2031 penetrates through the reaction tank body 1 and extends to the interior of the reaction tank body 1, the interior of the reaction tank body 1 is provided with the first spray head 2032 for spraying water, and the surface of the first spray head 2032 is communicated with the water suction pipe 2031.
When the sewage treatment device is implemented, the water suction pump 202 is controlled to work, sewage at the lower end of the reaction tank body 1 is sucked into the water guide pipe 2031 through the water suction pipe 201 under the action of the water suction pump 202, then the sewage enters the first spray head 2032 through the water guide pipe 2031, and the sewage is sprayed under the action of the first spray head 2032, so that the sewage is mixed at intervals, the sewage is safer, and the function of uniformly mixing the sewage in the reaction tank is realized.
Further, as shown in fig. 2 and 4, the surface of the reaction tank body 1 is provided with a rapid decompression mechanism 3, the interior of the rapid decompression mechanism 3 comprises a liquid level monitor 301, a water tank body 302 and a rapid decompression portion 303, the rapid decompression portion 303 is arranged on the interior of the reaction tank body 1 and the surface of the reaction tank body 1, the rapid decompression portion 303 is composed of a connecting pipe 3031 and a second spray head 3032, the surface of the top position of the reaction tank body 1 is provided with the water tank body 302, the interior of the water tank body 302 is provided with the connecting pipe 3031, one end of the connecting pipe 3031 penetrates through the reaction tank body 1 and extends to the interior of the reaction tank body 1, the surface of the connecting pipe 3031 is sleeved with a second valve, the model of the second valve is selected from a TM series, the input end of the second valve is electrically connected with the output end of the control button 101, the inner wall of the reaction tank body 1 is provided with a water pipe, the water pipe is communicated with the connecting pipe 3031, the interior of the reaction tank body 1 is provided with a second spray head 3032 for communicating with the interior of the water pipe, the inner wall 302 is provided with the water pipe 302, the liquid level monitor 301 is arranged on the inner wall of the water tank body 302, and the water tank body 302 is used for monitoring the liquid level monitor 302, and the liquid level of the water tank body is connected to the water tank body 302, and the water tank body 302 is connected to the water tank body 302.
During implementation, water is introduced into the water tank body 302 through the pipe body, at this time, the water quantity in the water tank body 302 is monitored under the action of the liquid level monitor 301, then, the second spray head 3032 on the surface of the water through pipe is controlled to work, the water in the water tank body 302 is introduced into the interior of the connecting pipe 3031 through the connecting pipe 3031, the second valve on the surface of the connecting pipe 3031 is controlled to work, the water enters the interior of the water through the connecting pipe 3031, at this time, the control button 101 is operated, the control button 101 controls the second spray head 3032 to work, the water is sprayed under the action of the second spray head 3032, the pressure reduction effect is achieved on the interior of the reaction tank body 1, and accordingly, the danger caused by overlarge biogas pressure in the tank body can be prevented, and the function of quickly reducing the pressure of the reaction tank is achieved.
Further, as shown in fig. 2 and 5, the drying and desulfurizing mechanism 4 is disposed inside the treatment tank 103, the drying and desulfurizing mechanism 4 includes a water storage tank 401, a biogas desulfurization desiccant 402, a desulfurization tank 403, a through pipe body 404 and a combustion chamber 405 inside the treatment tank 103, the desulfurization tank 403 is mounted on the inner wall of the treatment tank 103, the equidistant biogas desulfurization desiccant 402 is mounted inside the desulfurization tank 403, the through pipe body 404 is mounted inside the treatment tank 103, one end of the through pipe body 404 penetrates the desulfurization tank 403 and extends to the inside of the desulfurization tank 403, the combustion chamber 405 is mounted on the inner wall of the treatment tank 103, the other end of the through pipe body 404 penetrates the combustion chamber 405 and extends to the inside of the combustion chamber 405, the combustion chamber 405 is located below the desulfurization tank 403, the water storage tank 401 is located below the combustion chamber 405, the water storage tank 401 is communicated with the combustion chamber 405, a water outlet pipe is mounted on the surface of the water storage tank 401, one end of the water outlet pipe penetrates the water storage tank 401 and the treatment tank 103 and extends to the outside of the treatment tank 103, and a third valve is sleeved on the surface of the water outlet pipe, and a third valve is electrically connected with a third series of input end of valves, and a third button is electrically connected to the output end 101.
When the method is implemented, methane enters the desulfurization tank 403 through the treatment tank 103, when hydrogen sulfide and other harmful gases in the methane pass through the surface of the methane desulfurization drying agent 402, chemical reaction and physical adsorption are generated, the hydrogen sulfide in the methane generates ferric sulfide and calcium sulfide which are adsorbed on the surface of the methane desulfurization drying agent 402, pure methane enters the combustion chamber 405 through the pipe body 404 and is combusted in the combustion chamber 405, water vapor is adsorbed in the methane desulfurization drying agent 402, after the water vapor is condensed into water, the condensed water falls into the water storage tank 401, a third valve on the surface of a water outlet pipe is controlled to work, then the condensed water is discharged from a water outlet pipe, and sludge enters the bottom of the fixed inner tank 102 through the pore plate 115, and at the moment, the sewage and the sludge are discharged from the sewage discharge pipe 112 so as to realize the functions of the reaction tank on methane drying and desulfurization treatment.
Working principle: when the reactor is used, the reactor body 1 is placed at a designated position, sewage discharged from farms and the like enters the reactor body 1 from the water inlet barrel 104, then methane-generating bacteria are added into the reactor body 1 to perform fermentation treatment, at the moment, a user operates the control button 101 to control the driving motor 106 to work, when the driving motor 106 works, the driving motor 106 drives the rotating shaft 107 to rotate in the fixed inner tank 102, when the rotating shaft 107 rotates, the rotating shaft 107 drives the mixer 114 to rotate in the inner wall of the fixed inner tank 102, and the sewage and the methane-generating bacteria in the fixed inner tank 102 are stirred and mixed under the action of the stirring rod 113.
After the sewage inside the fixed inner tank 102 is fermented and treated for a period of time, at this moment, the user operates the control button 101 again, so that the control button 101 controls the water suction pump 202 to work, the sewage at the lower end of the reaction tank body 1 is sucked into the water conduit 2031 through the water suction pipe 201 under the action of the water suction pump 202, then, the sewage passes through the water conduit 2031 to enter the first spray head 2032, and the sewage is sprayed under the action of the first spray head 2032, so that the sewage is mixed at intervals, the sewage mixing function of the reaction tank is safer, the sewage below the reaction tank can be conveyed to the upper end of the reaction tank when the reaction tank is used, the sewage mixing function is realized from top to bottom, and the fermentation effect can be more comprehensive through the interval time of sewage mixing.
After enough marsh gas is generated in the inside of the reaction tank body 1, marsh gas can concentrate in the upper portion of the reaction tank body 1 through the fixed through hole 110 on the surface of the baffle body 111, at this moment, detect the inside pressure of the reaction tank body 1 under the effect of the pressure detector 108, when the blast pipe 105 is blocked, marsh gas is not discharged out of the inside of the reaction tank body 1, marsh gas pressure is too big and can produce danger in the reaction tank body 1, at this moment, lead in water to the inside of the water tank body 302 through the body, at this moment, monitor the water yield in the inside of the water tank body 302 under the effect of the liquid level monitor 301, then, control the second shower nozzle 3032 on the surface of the water pipe, lead in the inside of the water tank body 302 into the inside of the connecting pipe 3031 through the connecting pipe 3031, then control the second valve on the surface of the connecting pipe 3031, make water get into the inside of the water pipe through the connecting pipe 3031, at this moment, operate the control button 101 again, make the second shower nozzle 3032 work, spray water under the effect of second shower nozzle 3032, can play the effect of decompression to the inside the reaction tank body 1, thereby can prevent the marsh gas from being used in the whole, the dangerous performance is fast when the reaction tank is used, can be prevented from being greatly leading up in the dangerous marsh gas, the inside the reaction tank can be realized, and the high performance can be realized when the pressure can be greatly used in the whole, and the reaction tank can be safely used.
Then, the control button 101 is operated again, the first valve on the surface of the air duct 109 is controlled to work by the control button 101, methane is sucked into the treatment tank 103 through the air duct 109, methane enters the treatment tank 403 through the treatment tank 103, when hydrogen sulfide and other harmful gases in the methane pass through the surface of the methane desulfurization drying agent 402, chemical reaction and physical adsorption function are generated, hydrogen sulfide in the methane generates ferric sulfide and calcium sulfide, the ferric sulfide is adsorbed on the surface of the methane desulfurization drying agent 402, pure methane enters the combustion chamber 405 through the through pipe body 404, combustion is carried out in the combustion chamber 405, water vapor is adsorbed in the methane desulfurization drying agent 402, after the water vapor is condensed into water, the condensed water falls into the water storage tank 401, then the third valve on the surface of the water outlet pipe is controlled to work, then the condensed water is discharged from the water outlet pipe, the sludge enters the bottom of the fixed inner tank 102 through the pore plate 115, at this time, the sewage and the sludge are discharged from the blow-down pipe 112, the functions of the methane drying and the desulfurization treatment are realized, so that the methane can be more comprehensively treated when the reaction tank is used, the reaction tank is more convenient to use, and the final use requirement of the reaction tank can be met.
It will be evident to those skilled in the art that the utility model is not limited to the details of the foregoing illustrative embodiments, and that the present utility model may be embodied in other specific forms without departing from the spirit or essential characteristics thereof.
Claims (8)
1. The utility model provides a high temperature anaerobic reaction jar, includes retort body (1), its characterized in that: the surface mounting of retort body (1) has control button (101), the internally mounted of retort body (1) has fixed inner tank (102), the surface mounting of retort body (1) has treatment box (103), the surface mounting of retort body (1) has a water inlet tube (104), the one end of water inlet tube (104) runs through the inside of retort body (1) and fixed inner tank (102) and extension to fixed inner tank (102), the surface mounting of retort body (1) has blast pipe (105), the one end of blast pipe (105) runs through the inside of retort body (1) and fixed inner tank (102) and extension to fixed inner tank (102), the surface mounting of retort body (1) has air duct (109), the one end of air duct (109) runs through the inside of retort body (1) and extension to retort body (1), the surface of retort body (1) is provided with sewage mixing mechanism (2), sewage mixing mechanism (2) inside, sewage mixing mechanism (202) contain the inside of inhaling water pump (203) and quick-release mechanism (203) contain water pump (301) and quick-release mechanism (3) are contained in the surface of reactor (1) and the inside of monitoring (203) The novel biogas desulfurization and desulfurization device comprises a water tank body (302) and a rapid decompression part (303), wherein a drying and desulfurization treatment mechanism (4) is arranged in a treatment tank (103), and a water storage tank (401), a biogas desulfurization drying agent (402), a desulfurization tank (403), a through pipe body (404) and a combustion chamber (405) are arranged in the drying and desulfurization treatment mechanism (4).
2. A thermophilic anaerobic reactor according to claim 1, wherein: the surface mounting of the fixed inner tank (102) is provided with a driving motor (106), the input end of the driving motor (106) is electrically connected with the output end of the control button (101), the output end of the driving motor (106) is provided with a rotating shaft (107) through a coupler, one end of the rotating shaft (107) penetrates through the fixed inner tank (102) and extends to the inside of the fixed inner tank (102), the inside of the fixed inner tank (102) is provided with a mixer (114), the mixer (114) is in mutual rotation fit with the inner wall of the fixed inner tank (102), the surface of the top position of the mixer (114) is fixed with the surface of the rotating shaft (107), the surface of the mixer (114) is provided with an equidistant stirring rod (113), the inner wall of the fixed inner tank (102) is provided with a baffle body (111), the surface of the baffle body (111) is provided with a fixing through hole (110), the surface mounting of the reaction tank body (1) is provided with a mixer (103) for monitoring the pressure inside the reaction tank (1) and the pressure detector (103) is communicated with the inner part (103) of the reaction tank (103) and the other end of the reaction tank (103) is communicated with the inner part (109), the sewage draining pipe (112) is installed at the bottom of the reaction tank body (1), one end of the sewage draining pipe (112) penetrates through the reaction tank body (1) and the fixed inner tank (102) and extends to the inside of the fixed inner tank (102), a first valve is sleeved on the surface of the sewage draining pipe (112), the input end of the first valve is electrically connected with the output end of the control button (101), a door body is arranged on the surface of the treatment tank (103), and the door body is in mutual rotation fit with the surface of the treatment tank (103).
3. A thermophilic anaerobic reactor according to claim 1, wherein: the sewage mixing part (203) is arranged on the surfaces of the reaction tank body (1) and the fixed inner tank (102), the sewage mixing part (203) is composed of a water diversion pipe (2031) and a first spray head (2032), a water suction pump (202) is arranged on the surface of the top of the fixed inner tank (102), the input end of the water suction pump (202) is electrically connected with the output end of the control button (101), a water suction pipe (201) is arranged at the output end of the water suction pump (202), and one end of the water suction pipe (201) penetrates through the reaction tank body (1) and the fixed inner tank (102) and extends to the inside of the fixed inner tank (102).
4. A thermophilic anaerobic reactor according to claim 3, wherein: the water suction pump is characterized in that a water guide pipe (2031) is arranged at the output end of the water suction pump (202), one end of the water guide pipe (2031) penetrates through the reaction tank body (1) and extends to the inside of the reaction tank body (1), a first spray head (2032) for spraying water is arranged in the reaction tank body (1), and the surface of the first spray head (2032) is communicated with the water guide pipe (2031).
5. A thermophilic anaerobic reactor according to claim 1, wherein: the quick decompression portion (303) is arranged on the inner portion of the reaction tank body (1) and the surface of the reaction tank body (1), the quick decompression portion (303) is composed of a connecting pipe (3031) and a second spray head (3032), a water tank body (302) is arranged on the surface of the top of the reaction tank body (1), a connecting pipe (3031) is arranged in the water tank body (302), one end of the connecting pipe (3031) penetrates through the reaction tank body (1) and extends to the inner portion of the reaction tank body (1), a second valve is sleeved on the surface of the connecting pipe (3031), and the input end of the second valve is electrically connected with the output end of the control button (101).
6. A thermophilic anaerobic reactor according to claim 1, wherein: the inner wall of retort body (1) is installed and is led to the water pipe, and leads to the water pipe and be linked together with connecting pipe (3031), the inside of retort body (1) all is provided with second shower nozzle (3032) that are used for the water spray, second shower nozzle (3032) are linked together with the inside of leading to the water pipe, liquid level monitor (301) that are used for carrying out monitoring to the liquid level monitor (301) inside are installed to the inner wall of water tank body (302), the surface mounting of water tank body (302) top position department has the body that is used for intaking, and the one end of body runs through water tank body (302) and extends to the inside of water tank body (302).
7. A thermophilic anaerobic reactor according to claim 1, wherein: the inner wall of treatment box (103) is installed desulfurization case (403), equidistant marsh gas desulfurization drier (402) are all installed to the inside of desulfurization case (403), the internally mounted of treatment box (103) has siphunculus body (404), the one end of siphunculus body (404) runs through desulfurization case (403) and extends to the inside of desulfurization case (403), combustion chamber (405) are installed to the inner wall of treatment box (103), the other end of siphunculus body (404) runs through combustion chamber (405) and extends to the inside of combustion chamber (405), combustion chamber (405) are located the below of desulfurization case (403).
8. A thermophilic anaerobic reactor according to claim 1, wherein: the inner wall of processing case (103) is installed and is used for collecting tank (401) of distilled water, tank (401) are located the below of combustion chamber (405), tank (401) are linked together with combustion chamber (405), the surface mounting of tank (401) has the outlet pipe, and the one end of outlet pipe runs through tank (401) and processing case (103) and extends to the outside of processing case (103) to the surface cover of outlet pipe is equipped with the third valve, simultaneously, the input and the output electric connection of control button (101) of third valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321560589.1U CN220334953U (en) | 2023-06-19 | 2023-06-19 | High-temperature anaerobic reaction tank |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321560589.1U CN220334953U (en) | 2023-06-19 | 2023-06-19 | High-temperature anaerobic reaction tank |
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| CN220334953U true CN220334953U (en) | 2024-01-12 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202321560589.1U Active CN220334953U (en) | 2023-06-19 | 2023-06-19 | High-temperature anaerobic reaction tank |
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| CN (1) | CN220334953U (en) |
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