CN113501581A - Step steady flow type anaerobic reaction system - Google Patents
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Abstract
The invention provides a step steady flow type anaerobic reaction system, which comprises an anaerobic reactor and is characterized in that: anaerobic reactor be provided with two, two anaerobic reactors are anaerobic reactor and No. two anaerobic reactor respectively, anaerobic reactor with No. two anaerobic reactor series connection each other, anaerobic reactor with No. two anaerobic reactor all be connected with the stationary flow jar, anaerobic reactor and stationary flow jar link to each other, No. two anaerobic reactor and No. two stationary flow jar link to each other, anaerobic reactor's upper end be provided with a water outlet system, No. two anaerobic reactor's upper end also be provided with No. two water outlet systems, a water outlet system and No. two stationary flow jar link to each other. The first anaerobic reactor and the second anaerobic reactor in the design are arranged in a step mode, and the two-stage gradient flow stabilizing system enables the impact-resistant load of the reactors to be stronger and more stable.
Description
Technical Field
The invention relates to the technical field of organic wastewater treatment, in particular to a step steady flow type anaerobic reaction system.
Background
The anaerobic technology is commonly used for treating high-concentration high-organic wastewater and is also commonly used in projects for treating high-concentration refractory toxic organic chemical wastewater. The wastewater has certain biological toxicity besides high concentration, and the fluctuation of the water quality and the water quantity of the wastewater is large, so that the key for treating the high-concentration organic wastewater difficult to degrade is how to more efficiently and stably carry out the anaerobic reaction.
For high-concentration refractory organic wastewater, as the wastewater contains certain refractory bacteriostatic substances, most conventional anaerobic reactors are primary reactors, the treatment efficiency is normally 40-50%, the concentration of effluent pollutants is still high, the treatment pressure of a subsequent A/O system is high, the sludge production amount is high (the A/O sludge production coefficient is 0.6kg sludge/kgBOD, and the anaerobic sludge production coefficient is 0.1kg sludge/kgBOD), the produced sludge is hazardous waste, and the treatment cost is high.
Most of the existing anaerobic reactors adopt a forced internal circulation system to ensure the ascending flow velocity in the reactor so as to ensure the muddy water mixing effect in the reactor, but the high-concentration degradation-resistant organic wastewater mainly comes from chemical enterprises, the water quality and the water quantity of the chemical enterprises are greatly fluctuated, and the chemical wastewater water inflow is unstable, so that the ascending flow velocity in the reactor can be changed when the water inflow is changed, thereby causing the unstable operation of the reactor and the decline of the treatment effect, and therefore, the design of a step steady flow type anaerobic reaction system for solving the problems is particularly important.
Disclosure of Invention
The invention provides a step steady flow type anaerobic reaction system, wherein a first anaerobic reactor and a second anaerobic reactor are respectively connected with a steady flow tank, so that inflow water and backflow water are completely fed into the respective steady flow tanks, and then are pumped into the reactor through the steady flow tanks for water distribution, therefore, the rising flow speed in the reactor can be kept stable regardless of the inflow amount in the reactor, and the mud-water mixing effect is better. Besides, the second flow stabilizing tank can ensure the normal operation of the circulation system of the second anaerobic reactor, and simultaneously has the function of lifting the effluent of the first anaerobic reactor into the second-stage reactor.
In order to solve the technical problem, the invention provides a step steady flow type anaerobic reaction system, which comprises an anaerobic reactor and is characterized in that: the anaerobic reactor is provided with two anaerobic reactors, the two anaerobic reactors are respectively a first anaerobic reactor and a second anaerobic reactor, the first anaerobic reactor and the second anaerobic reactor are connected in series, the first anaerobic reactor and the second anaerobic reactor are both connected with a flow stabilizing tank, the first anaerobic reactor is connected with the first flow stabilizing tank, the second anaerobic reactor is connected with the second flow stabilizing tank, the first flow stabilizing tank is communicated with a first water distribution system in the lower end of the first anaerobic reactor through a first conveying pipeline, a first circulating pump is arranged on the first conveying pipeline, the second flow stabilizing tank is communicated with a second water distribution system in the lower end of the second anaerobic reactor through a second conveying pipeline, a second circulating pump is arranged on the second conveying pipeline, and a first water outlet system is arranged at the upper end of the first anaerobic reactor, the upper end of the second anaerobic reactor is also provided with a second water outlet system, and the first water outlet system is connected with a second flow stabilizing tank.
Further: the first flow stabilizing tank and the second flow stabilizing tank are internally provided with baffle plates, the baffle plates are in a circular ring shape and are fixed at the bottom in the flow stabilizing tank, the baffle plates separate the inner space of the flow stabilizing tank into an outer ring circulation channel and an inner ring circulation channel, the upper end of the inner ring circulation channel is communicated with the outer ring circulation channel, the first flow stabilizing tank and the second flow stabilizing tank are respectively provided with a water inlet, a backflow pipe interface and a backflow pump interface, the water inlet, the backflow pipe interface and the backflow pump interface are arranged in the tangential direction of the flow stabilizing tank body, the water inlet and the backflow pipe interface are communicated with the inner ring circulation channel, the backflow pump interface is communicated with the outer ring circulation channel, the first conveying pipeline is connected with the backflow pump interface of the first flow stabilizing tank, the first water outlet system is connected with the water inlet of the second flow stabilizing tank, and the second conveying pipeline is connected with a reflux pump interface of the second flow stabilization tank.
And further: and heating coils are arranged in the outer ring circulation channels of the first flow stabilization tank and the second flow stabilization tank.
And further: the anaerobic reactor is internally provided with a first circulating system, the first circulating system is connected with a backflow pipe interface of a first flow stabilizing tank, the first circulating system is positioned above the first water distribution system, the second anaerobic reactor is internally provided with a second circulating system, and the second circulating system is positioned above the second water distribution system and is connected with the backflow pipe interface of the second flow stabilizing tank.
And further: a three-phase separator is arranged in an anaerobic reactor between a circulating system and a water outlet system, the three-phase separator is connected with a water seal box fixed at the top of the anaerobic reactor, a second three-phase separator is also arranged in a second anaerobic reactor between a second circulating system and a second water outlet system, and the second three-phase separator is connected with a second water seal box fixed at the top of the second anaerobic reactor.
And further: a water distribution system below anaerobic reactor in be provided with anaerobic reactor mud discharging system, anaerobic reactor mud discharging system stretch out to an anaerobic reactor outside, No. two anaerobic reactors of water distribution system below also be provided with No. two anaerobic reactor mud discharging system in, No. two anaerobic reactor mud discharging system also stretch out to No. two anaerobic reactor outsides.
And further: the first anaerobic reactor and the second anaerobic reactor are arranged in a step mode, and the first anaerobic reactor is 50cm lower than the second anaerobic reactor.
And further: the first anaerobic reactor, the first flow stabilizing tank, the second anaerobic reactor and the second flow stabilizing tank are all provided with heat preservation layers outside.
After adopting the structure, the invention has the beneficial effects that:
1. this design makes anaerobic reactor and No. two anaerobic reactors be connected with a stationary flow jar respectively to make into water and the backward flow water all get into stationary flow jar separately, then cloth water in the steady flow jar pump income reactor, consequently, can realize that the rising velocity of flow in the reactor of no matter how big of inflow can all remain stable in the reactor, and muddy water mixes the effect better. Besides, the second flow stabilizing tank can ensure the normal operation of the circulation system of the second anaerobic reactor, and simultaneously has the function of lifting the effluent of the first anaerobic reactor into the second-stage reactor.
2. In the design, all water inlet and outlet pipeline connectors of the flow stabilizing tank are arranged in the tangential direction of the tank body, so that water flow in the flow stabilizing tank is always in a rotational flow state, and the mixing of water inlet and return water in the flow stabilizing tank is enhanced.
3. The first anaerobic reactor and the second anaerobic reactor in the design are arranged in a step mode, and the two-stage gradient flow stabilizing system enables the impact-resistant load of the reactors to be stronger and more stable.
Drawings
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
FIG. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic plan view of a ballast tank.
Detailed Description
The step flow stabilization type anaerobic reaction system shown in fig. 1 comprises two anaerobic reactors, wherein the two anaerobic reactors are respectively a first anaerobic reactor 1 and a second anaerobic reactor 2, the first anaerobic reactor and the second anaerobic reactor are connected in series, the first anaerobic reactor and the second anaerobic reactor are both connected with a flow stabilization tank, the first anaerobic reactor is connected with a first flow stabilization tank 3, the second anaerobic reactor is connected with a second flow stabilization tank 11, the first flow stabilization tank is communicated with a first water distribution system 5 in the lower end of the first anaerobic reactor through a first conveying pipeline, a first circulating pump 4 is installed on the first conveying pipeline, the second flow stabilization tank is communicated with a second water distribution system 13 in the lower end of the second anaerobic reactor through a second conveying pipeline, the second conveying pipeline is provided with a second circulating pump 12, the upper end of the first anaerobic reactor is provided with a first water outlet system 9, the upper end of the second anaerobic reactor is also provided with a second water outlet system 17, and the first water outlet system is connected with a second flow stabilizing tank. This design makes anaerobic reactor and No. two anaerobic reactors be connected with a stationary flow jar respectively to make into water and the backward flow water all get into stationary flow jar separately, then cloth water in the steady flow jar pump income reactor, consequently, can realize that the rising velocity of flow in the reactor of no matter how big of inflow can all remain stable in the reactor, and muddy water mixes the effect better. Besides, the second flow stabilizing tank can ensure the normal operation of the circulation system of the second anaerobic reactor, and simultaneously has the function of lifting the effluent of the first anaerobic reactor into the second-stage reactor.
As shown in fig. 1 and fig. 2, the first flow stabilization tank and the second flow stabilization tank are both provided with a baffle plate, the baffle plate is circular and fixed at the bottom of the flow stabilization tank, the baffle plate separates the inner space of the flow stabilization tank into an outer ring circulation channel 21 and an inner ring circulation channel 22, the upper end of the inner ring circulation channel is communicated with the outer ring circulation channel, the first flow stabilization tank and the second flow stabilization tank are both provided with a water inlet a, a backflow pipe interface B and a backflow pump interface C, the water inlet, the backflow pipe interface and the backflow pump interface are all arranged in the tangential direction of the flow stabilization tank body, the water inlet a and the backflow pipe interface B are both communicated with the inner ring circulation channel 22, the backflow pump interface C is communicated with the outer ring circulation channel 21, the first conveying pipeline is connected with the backflow pump interface of the first flow stabilization tank, the first water outlet system is connected with a water inlet of the second flow stabilization tank, and the second conveying pipeline is connected with a reflux pump interface of the second flow stabilization tank. All water inlet and outlet pipeline interfaces of the flow stabilizing tank are arranged in the tangential direction of the tank body in the design, so that water flow in the flow stabilizing tank is always in a rotational flow state, the mixing of water inlet and backflow water in the flow stabilizing tank is enhanced, the water inlet load is reduced, the impact resistance load of a system is improved, and the treatment effect is more stable.
As shown in fig. 1 and 2, a first circulation system 6 is arranged in the first anaerobic reactor, the first circulation system is connected with a return pipe interface of a first flow stabilization tank, the first circulation system is positioned above the first water distribution system, a second circulation system 14 is arranged in the second anaerobic reactor, and the second circulation system is positioned above the second water distribution system and connected with a return pipe interface of a second flow stabilization tank.
A first three-phase separator 7 is arranged in a first anaerobic reactor between a first circulating system and a first water outlet system shown in figure 1, the first three-phase separator is connected with a first water seal box 8 fixed at the top of the first anaerobic reactor, a second three-phase separator 15 is also arranged in a second anaerobic reactor between a second circulating system and a second water outlet system, and the second three-phase separator is connected with a second water seal box 16 fixed at the top of the second anaerobic reactor.
As shown in fig. 1, a first anaerobic reactor sludge discharge system 10 is arranged in a first anaerobic reactor below a first water distribution system, the first anaerobic reactor sludge discharge system extends out of the first anaerobic reactor, a second anaerobic reactor sludge discharge system 18 is also arranged in a second anaerobic reactor below a second water distribution system, and the second anaerobic reactor sludge discharge system also extends out of the second anaerobic reactor.
The first anaerobic reactor and the second anaerobic reactor are arranged in a step mode, and the first anaerobic reactor is 50cm lower than the second anaerobic reactor. After adopting above-mentioned structure, make things convenient for anaerobic reactor effluent to flow certainly to No. two anaerobic reactor stationary flow jar, the cascade degradation is realized in two reactors in proper order to system's influent water, and 2 reactors strain after the stable operation of acclimatization are more targeted, and the treatment effeciency is higher. Compared with an IC reactor, the reactor has the advantages of reduced height-diameter ratio, reduced flow rate of a reflux pump, normal sludge inoculation in a system, no need of granular sludge, and low investment and operation cost. Compared with other single-stage reactors, the reactor can realize cascade reaction, the treatment efficiency is higher, and the two-stage gradient current stabilization system enables the impact load resistance of the reactor to be stronger and more stable.
The anaerobic reactors are all connected with a flow stabilization tank, on one hand, an in-vitro reflux system is adopted, the flow stabilization tank of each reactor and the reactor form a communicating vessel, the liquid level in the two tanks is equal, and when the flow stabilization tank reflux pumps water in the flow stabilization tank, the water automatically reflows into the flow stabilization tank through a reflux system in the reactor. In operation, the relationship between a single reactor and respective ballast tanks is: the flow (Q) of the reflux pump is equal to the flow (Q1) of inlet water and the reflux flow (Q2) from the reflux system of the reactor to the steady flow tank, the ascending flow speed in the reactor is only related to the flow of the reflux pump, the flow of the reflux pump is kept unchanged, and the ascending flow speed in the reactor is always stabilized at 1.2m/h, so that the muddy water mixing effect is ensured, and the treatment efficiency is more stable. The flow Q2 from the reflux system in the reactor to the external steady flow tank can automatically change along with the change speed of the liquid level of the reactor. When Q1 is zero, Q2 is Q, the reactor and the steady flow tank circulate, and water does not flow out of the reactor; when Q1 becomes larger, Q2 automatically becomes smaller, and reactor effluent Q1 is the reactor influent. On the other hand, a flow guide system and a rotational flow system are arranged in the flow stabilizing tank, the water inlet of the backflow system and the water inlet enter the bottom of the inner ring of the flow stabilizing tank and then are deflected to the outer ring, and the outer ring of the flow stabilizing tank is communicated with the backflow pump.
When the water-saving device works, the total inlet water of the system enters the bottom of the inner ring of the first flow-stabilizing tank through the water inlet of the first flow-stabilizing tank. The return water of the return system of the anaerobic reactor I enters the bottom of the inner ring of the flow stabilizing tank I through the return pipe joint of the flow stabilizing tank I. The total system inlet water and the return water of the first anaerobic reactor return system overflow to the outer ring of the first flow stabilizing tank after being mixed in a rotational flow manner in the first flow stabilizing tank. The outer ring of the first flow stabilization tank is communicated with the inlet of the first circulating pump, the first circulating pump pumps water in the first flow stabilization tank to the first anaerobic reactor, the outlet of the first circulating pump is communicated with the first water distribution system, and uniform water distribution of the first anaerobic reactor is realized through the first water distribution system. Under the action of the first flow stabilization tank, stable rising flow velocity can be realized in the first anaerobic reactor. The system water inlet is degraded in a high concentration stage in the first anaerobic reactor. A first three-phase separator is arranged at the top of the first anaerobic reactor to realize separation of gas cement in the reactor, effluent of the first anaerobic reactor passes through a first effluent system to a second steady flow tank, mud automatically descends to a bottom sludge area of the first anaerobic reactor, and residual sludge is discharged to a sludge collection unit through a first sludge discharge system. Biogas generated by the first anaerobic reactor is sealed by the first water seal tank at the top and is discharged at high altitude after being purified. The water outlet of the first water outlet system enters the bottom of the inner ring of the second flow stabilizing tank through the water inlet of the second flow stabilizing tank. And the return water of the return system of the second anaerobic reactor enters the bottom of the inner ring of the second flow stabilizing tank through the return pipe joint of the second flow stabilizing tank. The effluent of the first anaerobic reactor and the return water of the return system of the second anaerobic reactor are mixed in a swirling flow manner in the second flow stabilizing tank and then overflow to the outer ring of the second flow stabilizing tank. The outer ring of the second flow stabilization tank is communicated with the inlet of a second circulating pump, the second circulating pump pumps water in the second flow stabilization tank to the first anaerobic reactor, the outlet of the second circulating pump is communicated with the second water distribution system, and uniform water distribution of the second anaerobic reactor is realized through the second water distribution system. Under the action of the second flow stabilization tank, stable rising flow velocity can be realized in the second anaerobic reactor. The effluent of the first anaerobic reactor is degraded in the second anaerobic reactor in a low concentration stage. A second three-phase separator is arranged at the top of the second anaerobic reactor to realize separation of gas cement in the reactor, effluent of the second anaerobic reactor flows to a subsequent treatment unit through a second effluent system, mud automatically descends to a bottom sludge area of the second anaerobic reactor, and residual sludge is discharged to a sludge collection unit through a second sludge discharge system. Biogas generated by the second anaerobic reactor is sealed by the second water seal tank at the top and is discharged at high altitude after being purified.
Example (b):
the main components of the medical intermediate wastewater comprise methanol and isopropanol, and also contain a large amount of toxic and non-degradable substances such as toluene, dichloroethane, nitrobenzene and the like. The whole engineering adopts a treatment process of materialization, anaerobism, two-stage A/O and mixed precipitation. The design scale is 500 t/d. The anaerobic section adopts the step steady flow anaerobic reaction system, the height of the tower body of the first-stage anaerobic reactor is 18.5m, and the diameter is 8.5 m; the height of the second-stage anaerobic reactor tower body is 18m, and the diameter is 8.5 m. The two-stage anaerobic reactors are respectively provided with a steady flow tank with the diameter of 4m and the height of 5 m. The organic loading of the influent was designed to be about 2.5kgCOD/m3. d.
The specific operation effect is as follows:
(1) after the system is debugged and stably operated, the water inflow of the anaerobic system fluctuates between 200 and 500t/d, and COD fluctuates at 12000mg/L of 8000 and 8000;
(2) the sludge concentration in the two anaerobic reactors is kept at about 10000mg/L, and the ascending flow rate is controlled at 1.2 m/h;
(3) the COD of the effluent of the first-stage anaerobic reactor is 4000-5500mg/L, the removal rate is about 50 percent, the COD of the effluent of the second-stage anaerobic reactor is 1000-2000mg/L, and the total removal rate of the step flow-stabilizing anaerobic system is stabilized above 80 percent.
(4) After the effluent of the anaerobic system is treated by the subsequent two-stage A/O and coagulating sedimentation process, the effluent can stably reach the connection standard of a sewage plant in a garden (COD is below 350 mg/L)
The above description is only a single embodiment of the present invention, and is not intended to limit the scope of the present invention. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention shall fall within the protection scope of the present invention.
Claims (8)
1. The utility model provides a step steady flow formula anaerobic reaction system, includes anaerobic reactor, its characterized in that: the anaerobic reactor is provided with two anaerobic reactors which are respectively a first anaerobic reactor (1) and a second anaerobic reactor (2), the first anaerobic reactor and the second anaerobic reactor are connected in series, the first anaerobic reactor and the second anaerobic reactor are both connected with a flow stabilizing tank, the first anaerobic reactor is connected with a flow stabilizing tank (3), the second anaerobic reactor is connected with a flow stabilizing tank (11), the first flow stabilizing tank is communicated with a first water distribution system (5) in the lower end of the first anaerobic reactor through a first conveying pipeline, a first circulating pump (4) is arranged on the first conveying pipeline, the second flow stabilizing tank is communicated with a second water distribution system (13) in the lower end of the second anaerobic reactor through a second conveying pipeline, and a second circulating pump (12) is arranged on the second conveying pipeline, a first water outlet system (9) is arranged at the upper end of the first anaerobic reactor, a second water outlet system (17) is also arranged at the upper end of the second anaerobic reactor, and the first water outlet system is connected with a second flow stabilizing tank.
2. The step steady flow anaerobic reaction system of claim 1, wherein: the first flow stabilization tank and the second flow stabilization tank are internally provided with baffle plates, the baffle plates are in a circular ring shape and are fixed at the bottom in the flow stabilization tank, the baffle plates separate the inner space of the flow stabilization tank into an outer ring circulation channel (21) and an inner ring circulation channel (22), the upper end of the inner ring circulation channel is communicated with the outer ring circulation channel, the first flow stabilization tank and the second flow stabilization tank are provided with a water inlet (A), a backflow pipe interface (B) and a backflow pump interface (C), the water inlet, the backflow pipe interface and the backflow pump interface are arranged in the tangential direction of the flow stabilization tank body, the water inlet (A) and the backflow pipe interface (B) are communicated with the inner ring circulation channel (22), and the backflow pump interface (C) is communicated with the outer ring circulation channel (21), the first conveying pipeline is connected with a reflux pump interface of the first flow stabilization tank, the first water outlet system is connected with a water inlet of the second flow stabilization tank, and the second conveying pipeline is connected with a reflux pump interface of the second flow stabilization tank.
3. The step steady flow anaerobic reaction system of claim 2, wherein: heating coils (19) are arranged in outer ring circulation channels of the first flow stabilizing tank and the second flow stabilizing tank.
4. The step steady flow anaerobic reaction system of claim 2, wherein: a first circulation system (6) is arranged in the first anaerobic reactor, the first circulation system is connected with a backflow pipe interface of a first flow stabilization tank, the first circulation system is located above the first water distribution system, a second circulation system (14) is arranged in the second anaerobic reactor, and the second circulation system is located above the second water distribution system and connected with the backflow pipe interface of the second flow stabilization tank.
5. The step steady flow anaerobic reaction system of claim 4, wherein: a three-phase separator (7) is arranged in an anaerobic reactor between a circulating system and a water outlet system, the three-phase separator is connected with a water seal box (8) fixed at the top of the anaerobic reactor, a second three-phase separator (15) is also arranged in a second anaerobic reactor between a second circulating system and a second water outlet system, and the second three-phase separator is connected with a second water seal box (16) fixed at the top of the second anaerobic reactor.
6. The step steady flow anaerobic reaction system of claim 1, wherein: a water distribution system below anaerobic reactor in be provided with anaerobic reactor mud discharging system (10) one number, anaerobic reactor mud discharging system stretch out to an anaerobic reactor outside, No. two anaerobic reactors of water distribution system below in also be provided with No. two anaerobic reactor mud discharging system (18), No. two anaerobic reactor mud discharging system also stretch out to No. two anaerobic reactor outsides.
7. The step steady flow anaerobic reaction system of claim 1, wherein: the first anaerobic reactor and the second anaerobic reactor are arranged in a step mode, and the first anaerobic reactor is 50cm lower than the second anaerobic reactor.
8. The step steady flow anaerobic reaction system of claim 1, wherein: the first anaerobic reactor, the first flow stabilizing tank, the second anaerobic reactor and the second flow stabilizing tank are all provided with heat preservation layers outside.
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Citations (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1002868A (en) * | 1962-11-16 | 1965-09-02 | Accum Ag | Hot-water boiler |
| JPH06182387A (en) * | 1991-02-22 | 1994-07-05 | Toto Ltd | Method and apparatus for treating waste water utilizing acetic acid assimilating methane bacterium |
| JP2001193236A (en) * | 2000-01-14 | 2001-07-17 | Sekisui Chem Co Ltd | Rainwater storing joint |
| JP2006241354A (en) * | 2005-03-04 | 2006-09-14 | Mitsui Eng & Shipbuild Co Ltd | Waste gasification unit |
| CN101250006A (en) * | 2007-12-18 | 2008-08-27 | 华南理工大学 | Aerobic-anaerobic cycling treatment fluidized bed reactor for landfill leachate |
| CN102604816A (en) * | 2011-01-24 | 2012-07-25 | 北京中源创能工程技术有限公司 | Integrated solid-material two-phase methane fermentation reactor and method for preparing methane by using same |
| WO2013053217A1 (en) * | 2011-10-12 | 2013-04-18 | Lin Changqing | Internally circulating fluidized bed bioreactor |
| CN204022486U (en) * | 2014-07-28 | 2014-12-17 | 长业环保集团有限公司 | A kind of adjustable metered distributing well of the Sewage treatment systems for parallel running |
| CN204079589U (en) * | 2014-09-17 | 2015-01-07 | 南京大学盐城环保技术与工程研究院 | A kind of chemical wastewater treatment system with anaerobism reflux |
| US20170050892A1 (en) * | 2015-08-19 | 2017-02-23 | Council Of Scientific & Industrial Research | Anaerobic column reactor for biodegradation of wastes and the process thereof |
| CN206660982U (en) * | 2017-03-14 | 2017-11-24 | 中石化上海工程有限公司 | A kind of solid-liquid mixing tank |
| CN207435144U (en) * | 2017-10-25 | 2018-06-01 | 北京北华中清环境工程技术有限公司 | A kind of efficient double-cycling anaerobic reactor |
| CN207891126U (en) * | 2018-01-26 | 2018-09-21 | 西纯环保科技（上海）有限公司 | A kind of jetting type IC anaerobic reactors |
| CN208120813U (en) * | 2017-12-21 | 2018-11-20 | 深圳市海川实业股份有限公司 | A kind of composite anaerobic digestion reactor |
| CN209554873U (en) * | 2018-11-15 | 2019-10-29 | 杨志刚 | A kind of interior reflux/water inlet regulation device of reactor |
| CN209597025U (en) * | 2019-02-28 | 2019-11-08 | 湖北三宁化工股份有限公司 | A kind of slurry mixing channel |
| CN211847350U (en) * | 2020-03-11 | 2020-11-03 | 宜宾学院 | Sequencing batch type continuous sewage discharge treater |
| CN213085582U (en) * | 2020-05-28 | 2021-04-30 | 山东立方环保设备有限公司 | Anaerobic jar mixer of intaking |
| CN216472454U (en) * | 2021-07-28 | 2022-05-10 | 江苏南大华兴环保科技股份公司 | Step steady flow type anaerobic reaction system |
-
2021
- 2021-07-28 CN CN202110855533.8A patent/CN113501581A/en active Pending
Patent Citations (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1002868A (en) * | 1962-11-16 | 1965-09-02 | Accum Ag | Hot-water boiler |
| JPH06182387A (en) * | 1991-02-22 | 1994-07-05 | Toto Ltd | Method and apparatus for treating waste water utilizing acetic acid assimilating methane bacterium |
| JP2001193236A (en) * | 2000-01-14 | 2001-07-17 | Sekisui Chem Co Ltd | Rainwater storing joint |
| JP2006241354A (en) * | 2005-03-04 | 2006-09-14 | Mitsui Eng & Shipbuild Co Ltd | Waste gasification unit |
| CN101250006A (en) * | 2007-12-18 | 2008-08-27 | 华南理工大学 | Aerobic-anaerobic cycling treatment fluidized bed reactor for landfill leachate |
| CN102604816A (en) * | 2011-01-24 | 2012-07-25 | 北京中源创能工程技术有限公司 | Integrated solid-material two-phase methane fermentation reactor and method for preparing methane by using same |
| WO2013053217A1 (en) * | 2011-10-12 | 2013-04-18 | Lin Changqing | Internally circulating fluidized bed bioreactor |
| CN204022486U (en) * | 2014-07-28 | 2014-12-17 | 长业环保集团有限公司 | A kind of adjustable metered distributing well of the Sewage treatment systems for parallel running |
| CN204079589U (en) * | 2014-09-17 | 2015-01-07 | 南京大学盐城环保技术与工程研究院 | A kind of chemical wastewater treatment system with anaerobism reflux |
| US20170050892A1 (en) * | 2015-08-19 | 2017-02-23 | Council Of Scientific & Industrial Research | Anaerobic column reactor for biodegradation of wastes and the process thereof |
| CN206660982U (en) * | 2017-03-14 | 2017-11-24 | 中石化上海工程有限公司 | A kind of solid-liquid mixing tank |
| CN207435144U (en) * | 2017-10-25 | 2018-06-01 | 北京北华中清环境工程技术有限公司 | A kind of efficient double-cycling anaerobic reactor |
| CN208120813U (en) * | 2017-12-21 | 2018-11-20 | 深圳市海川实业股份有限公司 | A kind of composite anaerobic digestion reactor |
| CN207891126U (en) * | 2018-01-26 | 2018-09-21 | 西纯环保科技（上海）有限公司 | A kind of jetting type IC anaerobic reactors |
| CN209554873U (en) * | 2018-11-15 | 2019-10-29 | 杨志刚 | A kind of interior reflux/water inlet regulation device of reactor |
| CN209597025U (en) * | 2019-02-28 | 2019-11-08 | 湖北三宁化工股份有限公司 | A kind of slurry mixing channel |
| CN211847350U (en) * | 2020-03-11 | 2020-11-03 | 宜宾学院 | Sequencing batch type continuous sewage discharge treater |
| CN213085582U (en) * | 2020-05-28 | 2021-04-30 | 山东立方环保设备有限公司 | Anaerobic jar mixer of intaking |
| CN216472454U (en) * | 2021-07-28 | 2022-05-10 | 江苏南大华兴环保科技股份公司 | Step steady flow type anaerobic reaction system |
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