Secondary separation reflux device for anaerobic reactor
By designing a secondary separation and reflow device including a collection cover, oblique tube, spherical tube and condenser tube, the problem of gas impurity in the existing anaerobic reactor is solved, and the purification and cost reduction of gas are achieved.
Patent Information
- Application Number
- CN202422544049.5
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-10-22
- Publication Date
- 2025-08-29
- Estimated Expiration
- 2034-10-22
AI Technical Summary
In the gas separation and reflux device of the existing anaerobic reactor, the gas is not pure enough and requires secondary treatment, which increases production costs.
A secondary separation and reflux device including a collection cover, oblique tube, spherical tube, condensing tube and water filter plate is designed to remove liquid in the gas through multi-stage condensation and water filter plate to achieve gas purification.
Effectively removes liquids from the gas, improves gas purity and reduces production costs.
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Figure CN223280698U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the field of equipment related to anaerobic reactors, in particular to a secondary separation and reflux device for anaerobic reactors. Background Art
[0002] Anaerobic reactors are a highly efficient biofilm treatment method. They utilize large surface areas such as sand as a carrier. Anaerobic microorganisms form a membrane attached to the surface of the sand or other carrier, flowing through the wastewater. The microorganisms come into contact with organic matter in the wastewater, adsorbing and decomposing it, thereby achieving the desired treatment. During the anaerobic reaction, the microorganisms decompose the organic matter to produce methane, carbon dioxide, and new cellular substances.
[0003] The existing anaerobic reactor has only one separation and reflux device, but the gas after separation and reflux still contains liquid water droplets and steam, making the collected gas not pure enough and requiring secondary treatment, which increases production costs. Utility Model Content
[0004] The purpose of the utility model is to solve the shortcomings in the prior art and to propose a secondary separation and reflux device for an anaerobic reactor.
[0005] In order to achieve the above-mentioned purpose, the utility model adopts the following technical scheme: a secondary separation and reflux device for an anaerobic reactor, comprising a collecting hood, the upper end of the collecting hood is fixedly connected to a first oblique tube, the end of the first oblique tube away from the collecting hood is fixedly connected to a spherical tube, the lower end of the spherical tube is fixedly connected to a second oblique tube, the upper end of the spherical tube is fixedly connected to a first condensing tube, the upper end of the first condensing tube is fixedly connected to a first connecting tube, the upper end of the first connecting tube is fixedly connected to a second condensing tube, the upper end of the second condensing tube is fixedly connected to a second connecting tube, the upper end of the second connecting tube is fixedly connected to an exhaust pipe, the collecting hood, the first oblique tube, the spherical tube, the second oblique tube, the first condensing tube, the first connecting tube, the second condensing tube, the second connecting tube and the exhaust pipe are internally connected.
[0006] As a further description of the above technical solution:
[0007] One end of the first oblique tube close to the collection cover is fixedly connected to a solenoid valve.
[0008] As a further description of the above technical solution:
[0009] One end of the first oblique tube connected to the spherical tube is inserted and extended to the lower end of the interior of the spherical tube.
[0010] As a further description of the above technical solution:
[0011] An end of the second oblique tube close to the spherical tube is fixedly connected to a solenoid valve.
[0012] As a further description of the above technical solution:
[0013] A spiral condenser is provided in the middle of the first condenser, a water outlet pipe is provided at the upper end of the spiral condenser, a water inlet pipe is provided at the lower end of the spiral condenser, and the water outlet pipe and the water inlet pipe of the spiral condenser both pass through the first condenser and are connected to an external water pump.
[0014] As a further description of the above technical solution:
[0015] A water filter plate is provided at the upper end of the second condensing tube.
[0016] As a further description of the above technical solution:
[0017] A first collecting funnel and a second collecting funnel are provided in the middle of the second condenser, and the first collecting funnel is located at the lower end of the second collecting funnel. Air holes are provided on the first collecting funnel and the second collecting funnel, and a water flow hole is provided at the lower end of the middle of the first collecting funnel. Water troughs are provided inside the first collecting funnel and the second collecting funnel. One side of the first collecting funnel and the second collecting funnel is fixedly connected with a water inlet pipe, and the other side of the first collecting funnel and the second collecting funnel is fixedly connected with a water outlet pipe, and the water inlet pipe and the water outlet pipe are both connected to the water trough inside the first collecting funnel and the second collecting funnel, and the water outlet pipe and the water inlet pipe on both sides of the first collecting funnel and the second collecting funnel are both connected to the external water pump through the second condenser.
[0018] The utility model has the following beneficial effects:
[0019] In the utility model, first, gas enters the interior of the spherical tube from the collecting cover along the first oblique tube, and separated liquid accumulates inside the spherical tube. The gas enters the interior of the spherical tube from the first oblique tube, so that part of the liquid in the gas is dissolved in the liquid remaining in the spherical tube, increasing the liquid inside the spherical tube. Then, the gas enters the interior of the first condenser tube from the top of the spherical tube. After being cooled by the first condenser tube, the vapor is liquefied and falls into the interior of the spherical tube. Then, the gas enters the interior of the second condenser tube. When the gas touches the surfaces of the first collecting funnel and the second collecting funnel, the vapor in the gas will be liquefied, and gather into liquid droplets at the lower end of the second collecting funnel, and fall into the middle of the first collecting funnel, and fall into the middle of the spherical tube from the water flow hole in the middle of the first collecting funnel. Then, the gas continues to upward, passes through the water filter plate, and the water filter plate can aggregate the water mist, so that all the moisture in the gas is removed, thereby obtaining pure gas. BRIEF DESCRIPTION OF THE DRAWINGS
[0020] Figure 1 It is a three-dimensional diagram of the utility model;
[0021] Figure 2 This is a cross-sectional perspective view of the spherical tube of the present invention;
[0022] Figure 3 This is a cross-sectional three-dimensional structural diagram of the second condenser tube of the present invention.
[0023] Legend:
[0024] 1. Collection hood; 2. First oblique tube; 3. Spherical tube; 4. Second oblique tube; 5. First condenser tube; 6. First connecting tube; 7. Second condenser tube; 8. Second connecting tube; 9. Exhaust pipe; 10. Spiral condenser tube; 11. Water filter plate; 12. First collecting funnel; 13. Second collecting funnel. DETAILED DESCRIPTION
[0025] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the embodiments described are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative efforts are within the scope of protection of the present invention.
[0026] In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicating directions or positional relationships, are based on the directions or positional relationships shown in the accompanying drawings and are only for the convenience of describing the present invention and simplifying the description. They do not indicate or imply that the devices or components referred to must have a specific direction, be constructed and operate in a specific direction. Therefore, they should not be understood as limiting the present invention. The terms "first", "second", and "third" are used for descriptive purposes only and should not be understood as indicating or implying relative importance. In addition, unless otherwise expressly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense. For example, they can be fixed connections, detachable connections, or integral connections; they can be mechanical connections or electrical connections; they can be direct connections, indirect connections through an intermediate medium, or internal connections between two components. For those skilled in the art, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.
[0027] Reference Figure 1-3The utility model provides an embodiment: a secondary separation and reflux device for an anaerobic reactor, comprising a collecting hood 1, a first oblique tube 2 being fixedly connected to the upper end of the collecting hood 1, a spherical tube 3 being fixedly connected to the end of the first oblique tube 2 away from the collecting hood 1, a second oblique tube 4 being fixedly connected to the lower end of the spherical tube 3, a first condensing tube 5 being fixedly connected to the upper end of the first condensing tube 5, a first connecting tube 6 being fixedly connected to the upper end of the first connecting tube 6, a second condensing tube 7 being fixedly connected to the upper end of the second condensing tube 7, a second connecting tube 8 being fixedly connected to the upper end of the second connecting tube 8, an exhaust pipe 9 being fixedly connected to the upper end of the second connecting pipe 8, and the collecting hood 1, the first oblique tube 2, the spherical tube 3, the second oblique tube 4, the first condensing tube 5, the first connecting tube 6, the second condensing tube 7, the second connecting tube 8 and the exhaust pipe 9 being internally connected.
[0028] A first collecting funnel 12 and a second collecting funnel 13 are provided in the middle of the second condensing tube 7, and the first collecting funnel 12 is located at the lower end of the second collecting funnel 13, and air holes are provided on the first collecting funnel 12 and the second collecting funnel 13, and a water flow hole is provided at the lower end of the middle of the first collecting funnel 12, and a water trough is provided inside the first collecting funnel 12 and the second collecting funnel 13. One side of the first collecting funnel 12 and the second collecting funnel 13 is fixedly connected to a water inlet pipe, and the other side of the first collecting funnel 12 and the second collecting funnel 13 is fixedly connected to a water outlet pipe, and the water inlet pipe and the water outlet pipe are connected to the water trough inside the first collecting funnel 12 and the second collecting funnel 13, and are located The water outlet pipe and the water inlet pipe on both sides of the first collecting funnel 12 and the second collecting funnel 13 are connected to the external water pump through the second condenser 7, a water filter plate 11 is provided at the upper end of the second condenser 7, a spiral condenser 10 is provided in the middle of the first condenser 5, a water outlet pipe is provided at the upper end of the spiral condenser 10, and a water inlet pipe is provided at the lower end of the spiral condenser 10, and the water outlet pipe and the water inlet pipe of the spiral condenser 10 are connected to the external water pump through the first condenser 5, and the end of the second oblique tube 4 close to the spherical tube 3 is fixedly connected to the solenoid valve, and the end of the first oblique tube 2 connected to the spherical tube 3 is inserted into the lower end of the inside of the spherical tube 3, and the end of the first oblique tube 2 close to the collection cover 1 is fixedly connected to the solenoid valve.
[0029] Working principle: There is liquid that has not been discharged after separation in the middle of the spherical tube 3. Open the solenoid valve on the first oblique tube 2, and the mixed gas enters the lower end of the spherical tube 3 from the first oblique tube 2. The liquid and steam merge into the liquid, and the other gases and steam enter the inside of the first condenser tube 5. The external water pump injects cold water into the spiral condenser tube 10, the first collecting funnel 12 and the second collecting funnel 13 through the water inlet pipe, and finally flows out of the spiral condenser tube 10, the first collecting funnel 12 and the second collecting funnel 13 from the water outlet pipe to circulate the cold water, so as to avoid the cold water inside the spiral condenser tube 10, the first collecting funnel 12 and the second collecting funnel 13 becoming hot after absorbing heat for a long time. The steam is condensed after passing through the spiral condenser tube 10, and the water droplets gather on the spiral condenser tube 10 and finally fall into the middle of the spherical tube 3. The remaining steam continues to go up and passes through the first The steam condenses and converges on the surfaces of the first and second collecting funnels 12 and 13. The liquid droplets on the surface of the second collecting funnel 13 fall into the middle of the first collecting funnel 12 and fall into the middle of the spherical tube 3 from the water flow holes. The gas will flow upward through the air holes on the first and second collecting funnels 12 and 13, and finally pass through the water filter plate 11, so that the small water droplets brought out by the gas are separated by the water filter plate 11, gathered into large water droplets on the surface of the water filter plate 11, and fall into the middle of the spherical tube 3. The gas enters the middle of the outlet pipe 9 from the second connecting pipe 8 and flows into the collection device. When the liquid in the middle of the spherical tube 3 exceeds a certain volume, the solenoid valve on the second oblique pipe 4 is opened to allow part of the liquid to flow back to the anaerobic reactor along the second oblique pipe 4. Then the solenoid valve is closed to allow the device to continue working.
[0030] Finally, it should be noted that the above is only a preferred embodiment of the present invention and is not intended to limit the present invention. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art can still modify the technical solutions described in the aforementioned embodiments or make equivalent replacements for some of the technical features therein. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention should be included in the scope of protection of the present invention.
Claims
1. A secondary separation and reflux device for an anaerobic reactor, comprising a collecting hood (1), characterized in that: The upper end of the collecting hood (1) is fixedly connected to a first oblique tube (2), the end of the first oblique tube (2) away from the collecting hood (1) is fixedly connected to a spherical tube (3), the lower end of the spherical tube (3) is fixedly connected to a second oblique tube (4), the upper end of the spherical tube (3) is fixedly connected to a first condensing tube (5), the upper end of the first condensing tube (5) is fixedly connected to a first connecting tube (6), the upper end of the first connecting tube (6) is fixedly connected to a second condensing tube (7), the upper end of the second condensing tube (7) is fixedly connected to a second connecting tube (8), the upper end of the second connecting tube (8) is fixedly connected to an exhaust pipe (9), and the collecting hood (1), the first oblique tube (2), the spherical tube (3), the second oblique tube (4), the first condensing tube (5), the first connecting tube (6), the second condensing tube (7), the second connecting tube (8) and the exhaust pipe (9) are internally connected.
2. The secondary separation and reflux device for an anaerobic reactor according to claim 1, characterized in that: One end of the first oblique tube (2) close to the collection cover (1) is fixedly connected to a solenoid valve.
3. The secondary separation and reflux device for an anaerobic reactor according to claim 1, characterized in that: One end of the first oblique tube (2) connected to the spherical tube (3) is inserted and extended to the lower end inside the spherical tube (3).
4. The secondary separation and reflux device for an anaerobic reactor according to claim 1, characterized in that: One end of the second oblique tube (4) close to the spherical tube (3) is fixedly connected to a solenoid valve.
5. The secondary separation and reflux device for an anaerobic reactor according to claim 1, characterized in that: A spiral condenser tube (10) is provided in the middle of the first condenser tube (5), a water outlet pipe is provided at the upper end of the spiral condenser tube (10), and a water inlet pipe is provided at the lower end of the spiral condenser tube (10), and both the water outlet pipe and the water inlet pipe of the spiral condenser tube (10) pass through the first condenser tube (5) and are connected to an external water pump.
6. The secondary separation and reflux device for an anaerobic reactor according to claim 1, characterized in that: A water filter plate (11) is provided at the upper end of the second condenser tube (7).
7. The secondary separation and reflux device for an anaerobic reactor according to claim 1, characterized in that: A first collecting funnel (12) and a second collecting funnel (13) are provided in the middle of the second condensing tube (7), and the first collecting funnel (12) is located at the lower end of the second collecting funnel (13). Air holes are provided on the first collecting funnel (12) and the second collecting funnel (13). A water flow hole is provided at the lower end of the middle of the first collecting funnel (12). A water trough is provided inside the first collecting funnel (12) and the second collecting funnel (13). One side of the first collecting funnel (12) and the second collecting funnel (13) is fixedly connected to a water inlet pipe, and the other side of the first collecting funnel (12) and the second collecting funnel (13) is fixedly connected to a water outlet pipe, and the water inlet pipe and the water outlet pipe are both connected to the water trough inside the first collecting funnel (12) and the second collecting funnel (13), and the water outlet pipe and the water inlet pipe located on both sides of the first collecting funnel (12) and the second collecting funnel (13) pass through the second condensing tube (7) and are connected to an external water pump.