CN211004760U - Automatic anaerobic three-phase separation system - Google Patents
Automatic anaerobic three-phase separation system Download PDFInfo
- Publication number
- CN211004760U CN211004760U CN201921838452.1U CN201921838452U CN211004760U CN 211004760 U CN211004760 U CN 211004760U CN 201921838452 U CN201921838452 U CN 201921838452U CN 211004760 U CN211004760 U CN 211004760U
- Authority
- CN
- China
- Prior art keywords
- gas collecting
- liquid level
- water seal
- level meter
- reactor
- 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.)
- Active
Links
Images
Abstract
The utility model relates to an automatic anaerobic three-phase separation system, which comprises a reactor, a three-phase separator arranged in the reactor, a water seal assembly arranged outside the reactor and a controller; the three-phase separator comprises a plurality of gas collecting hoods arranged in parallel, gas collecting pipes communicated with the upper ends of the gas collecting hoods, and a gas chamber liquid level meter arranged at the upper end of any one of the gas collecting hoods; the water seal assembly comprises a water seal tank, an air outlet pipe, an water inlet pipe, a water outlet pipe and a water seal liquid level meter, wherein the air outlet pipe, the water inlet pipe, the water outlet pipe and the water seal liquid level meter are arranged on the water seal tank; the controller is respectively electrically connected with the air chamber liquid level meter, the water seal liquid level meter, the first valve and the second valve. The utility model discloses a three-phase separation system that three-phase separator and water-sealed tank that adopts double-deck V type structure of invering constitute, through the coordinated control of controller, but automatically regulated air chamber pressure makes it and system operation phase-match.
Description
Technical Field
The utility model relates to the technical field of wastewater treatment, in particular to an automatic anaerobism three-phase separation system.
Background
Anaerobic digestion of wastewater treatment pollutants can be broadly divided into the following steps: 1) a hydrolysis acidification stage; 2) acid production and acetic acid production stages; 3) a methanogenesis stage. In the hydrolysis acidification stage, macromolecular refractory organic matters in water are subjected to ring opening and chain scission decomposition into degradable micromolecular organic matters under the action of hydrolysis acidification bacteria; in the acid and acetic acid producing stage, under the action of acetogenic bacteria, products in the hydrolysis acidification stage are further decomposed into volatile organic acids such as acetic acid and propionic acid; the methanogenesis stage is to reduce volatile organic acid generated in the acid production and acetic acid production stage or hydrogen and carbon dioxide generated in the acid production and acetic acid production stage into methane under the action of methane bacteria. In summary, the process of anaerobic treatment of wastewater is a process of decomposing organic matters in water into methane.
The anaerobic reactor corresponding to the anaerobic treatment of waste water is mainly composed of a water inlet system, a reaction zone and a three-phase separation system. The efficiency of the anaerobic reactor is determined by the anaerobic sludge concentration in the reactor to a great extent, so that the condition that the sludge is not lost is the central importance of the anaerobic system, but because the anaerobic system has the methane production phenomenon, the sludge slightly floats under the micro-bubble wrapping, the difficulty is increased for the sludge loss prevention, and therefore, a three-phase separation system is appeared, so that the gas, the liquid and the solid are well separated, the supernatant is discharged, the sludge flows back into the reactor through a backflow seam of the three-phase separator to ensure the sludge concentration, and the methane is directly discharged into the atmosphere after passing through a water-sealed tank or is recycled as energy, so the three-phase separation system is the core and the key components of the whole anaerobic reactor.
The prior art has the defects that the pressure of an air chamber in the three-phase separator is difficult to monitor in real time, adjust in time according to the operation condition and adjust to a reasonable level according to actual requirements. Because the pressure of the gas chamber needs to be adjusted according to the steam production strength in the reactor, and the steam production strength is difficult to stabilize due to the influence of many factors, if the pressure of the gas chamber cannot be adjusted timely according to the steam production strength, the pressure of the gas chamber is too high, and bubbles escape from the gas chamber to influence sludge sedimentation; or the air pressure of the air chamber is not enough, the three-phase separation is not ideal, and the three-phase mixed liquid enters the water-sealed tank along with the three-phase separator biogas collecting pipe; therefore, the utility model develops an automatic anaerobic three-phase separation system to solve the problems existing in the prior art, and the same or similar technical scheme of the utility model is not found through retrieval.
SUMMERY OF THE UTILITY MODEL
The utility model discloses the purpose is: provides an automatic anaerobic three-phase separation system, which solves the problem that the pressure of an air chamber in a three-phase separator is not easy to adjust in the prior art.
The technical scheme of the utility model is that: an automatic anaerobic three-phase separation system comprises a reactor, a three-phase separator arranged in the reactor, a water seal assembly arranged outside the reactor and a controller; the three-phase separator comprises a plurality of gas collecting hoods arranged in parallel, gas collecting pipes communicated with the upper ends of the gas collecting hoods, and a gas chamber liquid level meter arranged at the upper end of any one of the gas collecting hoods; the water seal assembly comprises a water seal tank, an air outlet pipe, an water inlet pipe, a water outlet pipe and a water seal liquid level meter, wherein the air outlet pipe, the water inlet pipe, the water outlet pipe and the water seal liquid level meter are arranged on the water seal tank; the controller is respectively electrically connected with the air chamber liquid level meter, the water seal liquid level meter, the first valve and the second valve.
Preferably, the gas collecting hoods are of an inverted V-shaped structure, two groups of gas collecting hoods are arranged up and down, the gas collecting hoods on the upper layer are sequentially arranged above the space between two adjacent gas collecting hoods on the lower layer at intervals, the width of the gas collecting hoods is larger than the distance between the lower ends of the two adjacent gas collecting hoods on the lower layer, and the lower ends of the gas collecting hoods on the two sides of the upper layer, which are close to the inner wall of the reactor, are respectively and fixedly connected with the inner wall of the reactor; a flow guide body is sequentially arranged below the space between two adjacent gas-collecting hoods on the lower layer.
Preferably, the air chamber liquid level meter is an ultrasonic liquid level meter and is arranged at the top end of any gas-collecting hood at the lower layer; the water seal liquid level meter is an ultrasonic liquid level meter and is fixedly installed at the top end of the water seal tank.
Preferably, the gas collecting pipe comprises a plurality of first branch pipes, a first header pipe, a plurality of second branch pipes and a second header pipe, the upper ends of the gas collecting hoods on the upper layer are respectively connected with the first branch pipes, the plurality of first branch pipes are communicated with the first header pipe, and the first header pipe extends into the water seal tank; and the upper ends of the gas collecting hoods on the lower layer are respectively connected with second branch pipes, the second branch pipes are communicated with a second header pipe, and the second header pipe extends into the water seal tank.
Preferably, the reactor is of a cuboid structure, two ends of the gas collecting channels are respectively fixed on a pair of parallel end face inner walls of the reactor, and overflow weirs are arranged at the upper ends of the pair of parallel end face inner walls of the reactor, which are perpendicular to the fixed ends of the gas collecting channels.
Compared with the prior art, the utility model has the advantages that:
(1) the utility model discloses an adopt the double-deck three-phase separator of inverting V type structure and the three-phase piece-rate system that water sealed tank constitutes, compare in traditional structure and add the air chamber level gauge, the during operation reactor is inside to be full of waste water, can separate through the three-phase separation, collect gas, gaseous gathering is in the gas collecting channel upper end to form the air chamber, the air chamber level gauge can the liquid level height of real-time supervision air chamber lower extreme, through the coordinated control of controller, but automatically regulated air chamber pressure makes it and system operation phase-match.
(2) Because the high degree of efficiency of anaerobic reactor is decided by the anaerobic sludge concentration in the reactor, therefore the real-time adjustment and balance of the air chamber pressure can effectively ensure the treatment efficiency, can avoid the over-high air chamber pressure, the gas flows out from the side edge of the gas-collecting hood, the settled sludge can float away under the action of the gas to influence the sludge concentration, and can also avoid the over-low air chamber pressure, and the sludge enters from the lower end of the gas-collecting hood to cause the blockage of the gas-collecting pipe.
Drawings
The invention will be further described with reference to the following drawings and examples:
fig. 1 is a front view of the structure of the present invention;
FIG. 2 is a top view of the gas collecting channel of the present invention with an air chamber liquid level meter installed;
fig. 3 is a control flow chart of the structure of the present invention.
Wherein: 1. the device comprises a reactor, 2, an overflow weir, 3, a gas collecting hood, 4, a flow guiding body, 5, a gas chamber, 6, a gas chamber liquid level meter, 7, a gas collecting pipe, 8, a first branch pipe, 9, a first main pipe, 10, a second branch pipe, 11, a second main pipe, 12, a water seal tank, 13, a water inlet pipe, 14, a first valve, 15, a water outlet pipe, 16, a second valve, 17, a gas outlet pipe, 18 and a water seal liquid level meter.
Detailed Description
The following detailed description is made in conjunction with specific embodiments of the present invention:
as shown in fig. 1 and 2, an automatic anaerobic three-phase separation system for realizing the treatment of wastewater and well separating gas, liquid and solid phases, discharging supernatant, and returning sludge into a reactor through a backflow seam of a three-phase separator to ensure the concentration of the sludge, and directly discharging biogas into the atmosphere after passing through a water-sealed tank or as energy recycling, mainly comprises a reactor 1, a three-phase separator arranged inside the reactor 1, a water seal assembly arranged outside the reactor 1 and a controller.
Reactor 1 is the cuboid structure, and a pair of parallel terminal surface inner wall upper end is provided with overflow weir 2, and this reactor 1 is inside to be used for holding waste water, and waste water up end and 2 upper ends of overflow weir are in same horizontal plane.
The three-phase separator comprises a plurality of gas-collecting hoods 3 arranged in parallel, a gas-collecting pipe 7 communicated with the upper ends of the gas-collecting hoods 3 and a gas-chamber liquid level meter 6 extending to the lower end of any one of the gas-collecting hoods 3; the gas collecting hoods 3 are immersed in the wastewater, biogas generated after three-phase separation can be gathered above the gas collecting hoods 3 to form a gas chamber 5, two ends of the gas collecting hoods 3 in the long axis direction are respectively fixed on the inner walls of a pair of parallel end faces of the reactor 1, which are perpendicular to the end face where the overflow weir 2 is located, the gas collecting hoods are in an inverted V-shaped structure along the section parallel to the fixed end faces, the two groups are arranged up and down, the gas collecting hoods 3 located on the upper layer are sequentially arranged above the space between two adjacent gas collecting hoods 3 on the lower layer at intervals, the width of each gas collecting hood 3 is larger than the distance between the lower ends of the two adjacent gas collecting hoods 3 on the lower layer, and the lower ends of the gas collecting hoods 3 on the two sides of; a flow guide body 4 is sequentially arranged below the space between two adjacent gas collecting hoods 3 on the lower layer, and the flow guide body 4 is of a rhombus structure which is asymmetric from top to bottom and symmetric from side to side along the section parallel to the fixed end surfaces of the gas collecting hoods 3 and is used for realizing the flow guide effect of wastewater; two through holes are formed in the upper end of the single gas collecting hood 3 connected with the gas chamber liquid level meter 6, one through hole is used for installing the gas chamber liquid level meter 6, the other through hole is used for connecting and installing the gas collecting pipe 7, and the through holes are formed in the upper ends of the remaining gas collecting hoods 3 and are used for connecting and installing the gas collecting pipe 7.
The gas collecting pipe 7 comprises a plurality of first branch pipes 8, a first main pipe 9, a plurality of second branch pipes 10 and a second main pipe 11, the upper ends of the upper layer of the plurality of gas collecting hoods 3 are respectively connected with the first branch pipes 8, the plurality of first branch pipes 8 are communicated with the first main pipe 9, and the first main pipe 9 extends into the water seal tank; the upper ends of a plurality of gas collecting hoods 3 on the lower layer are respectively connected with a plurality of second branch pipes 10, the plurality of second branch pipes 10 are communicated with a second main pipe 11, and the second main pipe 11 extends into a water seal tank.
The air chamber liquid level meter 6 selects an ultrasonic liquid level meter and is installed at the top end of any gas collecting hood 3 positioned at the lower layer, and the air chamber liquid level meter 6 is used for monitoring the liquid level height below the air chamber 5 in real time, so that the pressure of the air chamber 5 can be conveniently judged.
The water seal assembly comprises a water seal tank 12, an air outlet pipe 17, an water inlet pipe 13, an water outlet pipe 15 and a water seal liquid level meter 18 which are arranged on the water seal tank 12, liquid water is arranged in the water seal tank 12, and the end parts of the first main pipe 9 and the second main pipe 11 extend into the liquid water in the water seal tank 12; a first valve 14 is arranged on the water inlet pipe 13, and a second valve 16 is arranged on the water outlet pipe 15; the water seal liquid level meter 18 is also an ultrasonic liquid level meter and is fixedly installed at the upper end of the water seal tank 12 and used for monitoring the liquid level height of liquid water in the water seal tank 12 in real time.
The controller is respectively electrically connected with the air chamber liquid level meter 6, the water seal liquid level meter 18, the first valve 14 and the second valve 16, as shown in fig. 3, the control method is as follows:
(1) the method is characterized in that the controller is preset in such a way that wastewater is injected into the reactor 1, the upper end of the gas collecting hood 3 forms a gas chamber 5 through three-phase separation, the gas collecting hood 3 at the lower end of the gas chamber 5 has a liquid level, the controller sets the upper limit value and the lower limit value of the liquid level in the gas collecting hood 3 and records that the upper limit value is L1The lower limit value is L2；
(2) The liquid level in the gas collecting hood 3 is monitored in real time through the gas chamber liquid level meter 6, and the real-time liquid level is recorded as LQAnd the liquid level is transmitted to the controller, the liquid level in the water seal tank 12 is detected in real time through the water seal liquid level meter 18, and the liquid level is recorded as LsAnd transmitted to the controller;
(3) decision LQRelative to L1And L2And controlling the operation of the first valve 14 and the second valve 16, if L1＞LQ＞L2The first valve 14 and the second valve 16 are not operated, if LQ＞L1Then step (4) is executed, if LQ＜L2If yes, executing the step (5);
(4) if LQ＞L1The controller controls the first valve 14 to open, so that the liquid level in the water seal tank 12 rises, and the liquid level is monitored in real time through the water seal liquid level meter 18, wherein the required rising height of the liquid level is LQ-L1That is, the water seal level gauge 18 monitors the liquid level to Ls+(LQ-L1) When, the first valve 14 is closed;
(5) if LQ＜L2The controller controls the second valve 16 to open so that the liquid level in the water seal tank 12 is lowered, and detects the liquid level in real time through the water seal liquid level meter 18, wherein the liquid level needs to be lowered by L2-LQThat is, the water seal level gauge 18 monitors the liquid level to Ls-(L2-LQ) At this time, the second valve 16 is closed.
The air chamber liquid level meter 6 transmits signals to the controller in real time, and controls the opening of the first valve 14 and the second valve 16 through the comparison and analysis of the liquid level height, so as to adjust the height of the liquid level in the water seal tank 12; the water seal liquid level meter 18 sends signals to the controller in real time and monitors the rising and falling heights of the liquid level in the water seal tank 12, so that the first valve 14 and the second valve 16 are closed.
The during operation, the discharge that 1 lower extreme of reactor carried out waste water gets into, because the utility model relates to an automatic anaerobism three-phase piece-rate system, consequently do not do detailed description to the water intake system of 1 below of reactor, waste water realizes gas through the three-phase separator, liquid, solid three-phase well separation, final supernatant is discharged from overflow weir 2, mud passes through the three-phase separator backward flow and enters 1 assurance mud concentration of reactor, marsh gas gets into the 3 upper ends of gas collecting channel, and get into behind the water-sealed tank 12 or directly discharge into the atmosphere by outlet duct 17 through the discharge pipe 7, or as energy recycle, the air chamber level gauge 6 of addding, the liquid level height that can real-time supervision air chamber 5 lower extreme, coordination control through the controller, but automatically regulated air chamber 5 pressure, make it and system operation phase-match.
The above embodiments are only for illustrating the technical concept and features of the present invention, and the purpose of the embodiments is to enable those skilled in the art to understand the contents of the present invention and to implement the present invention, which cannot limit the protection scope of the present invention. It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof, and therefore, the present invention is considered to be exemplary and not restrictive in any way, since the scope of the present invention is defined by the appended claims, rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein, and therefore any reference signs in the claims are not intended to be construed as limiting the claims concerned.
Claims (5)
1. An automatic anaerobism three-phase separation system which characterized in that: comprises a reactor, a three-phase separator arranged inside the reactor, a water seal assembly arranged outside the reactor and a controller; the three-phase separator comprises a plurality of gas collecting hoods arranged in parallel, gas collecting pipes communicated with the upper ends of the gas collecting hoods, and a gas chamber liquid level meter arranged at the upper end of any one of the gas collecting hoods; the water seal assembly comprises a water seal tank, an air outlet pipe, an water inlet pipe, a water outlet pipe and a water seal liquid level meter, wherein the air outlet pipe, the water inlet pipe, the water outlet pipe and the water seal liquid level meter are arranged on the water seal tank; the controller is respectively electrically connected with the air chamber liquid level meter, the water seal liquid level meter, the first valve and the second valve.
2. An automated anaerobic three-phase separation system according to claim 1, wherein: the gas collecting hoods are of an inverted V-shaped structure, the upper and lower gas collecting hoods are arranged in two groups, the gas collecting hoods on the upper layer are sequentially arranged above the space between two adjacent gas collecting hoods on the lower layer at intervals, the width of the gas collecting hoods is larger than the distance between the lower end parts of the two adjacent gas collecting hoods on the lower layer, and the lower ends, close to the inner wall of the reactor, of the gas collecting hoods on the two sides of the upper layer are respectively and fixedly connected with the inner wall of the reactor; a flow guide body is sequentially arranged below the space between two adjacent gas-collecting hoods on the lower layer.
3. An automated anaerobic three-phase separation system according to claim 2, wherein: the air chamber liquid level meter is an ultrasonic liquid level meter and is arranged at the top end of any gas-collecting hood at the lower layer; the water seal liquid level meter is an ultrasonic liquid level meter and is fixedly installed at the top end of the water seal tank.
4. An automated anaerobic three-phase separation system according to claim 2, wherein: the gas collecting pipe comprises a plurality of first branch pipes, a first header pipe, a plurality of second branch pipes and a second header pipe, the upper ends of the gas collecting hoods on the upper layer are respectively connected with the first branch pipes, the first branch pipes are communicated with the first header pipe, and the first header pipe extends into the water seal tank; and the upper ends of the gas collecting hoods on the lower layer are respectively connected with second branch pipes, the second branch pipes are communicated with a second header pipe, and the second header pipe extends into the water seal tank.
5. An automated anaerobic three-phase separation system according to claim 1, wherein: the reactor is of a cuboid structure, two ends of the gas collecting hoods are respectively fixed on a pair of parallel end surface inner walls of the reactor, and overflow weirs are arranged at the upper ends of the pair of parallel end surface inner walls of the reactor, which are perpendicular to the fixed ends of the gas collecting hoods.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921838452.1U CN211004760U (en) | 2019-10-30 | 2019-10-30 | Automatic anaerobic three-phase separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921838452.1U CN211004760U (en) | 2019-10-30 | 2019-10-30 | Automatic anaerobic three-phase separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211004760U true CN211004760U (en) | 2020-07-14 |
Family
ID=71478877
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921838452.1U Active CN211004760U (en) | 2019-10-30 | 2019-10-30 | Automatic anaerobic three-phase separation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211004760U (en) |
-
2019
- 2019-10-30 CN CN201921838452.1U patent/CN211004760U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205346962U (en) | Novel anaerobic/Aerobic bioreactor | |
| CN110745942A (en) | Automatic anaerobic three-phase separation system and control method | |
| CN109761449A (en) | A kind of novel anaerobic reactor and processing system based on UASB | |
| CN211004760U (en) | Automatic anaerobic three-phase separation system | |
| CN219907230U (en) | IC anaerobic reactor for high concentration waste water treatment | |
| CN105907631A (en) | Channel-combined multifunctional anaerobic reactor | |
| CN205346964U (en) | Anaerobic/Aerobic bioreactor | |
| CN210915508U (en) | Pulse water distribution type UASB anaerobic reactor | |
| CN219324054U (en) | Multifunctional biogas purifying device | |
| CN108905599B (en) | Internal circulation biological desulfurization reactor and method | |
| CN212246402U (en) | IC tower for treating bean product wastewater | |
| CN212334745U (en) | Anaerobic bioreactor | |
| CN208717136U (en) | A kind of organic matter anaerobic reactor | |
| CN106542704A (en) | A kind of potato starch sewage disposal system | |
| WO2021118365A1 (en) | Reactor and method for the treatment of wet organic wastes such as black water from households, manure, sludge and slurries | |
| CN219839570U (en) | UASB anaerobic reaction device | |
| CN203781912U (en) | Gas-solid-liquid three-phase separation device in wastewater treatment process | |
| CN207016555U (en) | A kind of water inlet structure of anaerobic fermentation tank | |
| CN219526388U (en) | Novel high-load anaerobic reactor | |
| CN206783396U (en) | One kind drop flow type anaerobe reactor | |
| CN216972130U (en) | IC anaerobic treatment device for sulfate-containing wastewater | |
| CN216711714U (en) | Water distribution pipe system for treating UASB (upflow anaerobic sludge blanket) system in leachate | |
| CN204676036U (en) | The safety and environmental protection oil refining apparatus of a kind of continuously feeding, the waste and old organic cracking regeneration of deslagging | |
| CN213623711U (en) | Integrated device for comprehensive treatment of waste gas and waste water | |
| CN217838526U (en) | Three-phase separation device for oil-water-slag liquid mixture |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |