CN214141761U

CN214141761U - Sewage treatment GSB reactor

Info

Publication number: CN214141761U
Application number: CN202023128331.3U
Authority: CN
Inventors: 夏国庆
Original assignee: Changzhou Guojie Environmental Protection Technology Co ltd
Current assignee: Changzhou Guojie Environmental Protection Technology Co ltd
Priority date: 2020-12-23
Filing date: 2020-12-23
Publication date: 2021-09-07
Anticipated expiration: 2030-12-23

Abstract

The utility model discloses a sewage treatment GSB reactor, comprising a base plate, the top fixedly connected with reactor body of bottom plate, the supreme mixed area, inflation district and the smart district of handling including in proper order are down followed to the reactor body, supreme one-level three-phase separator and the second grade three-phase separator of being provided with respectively is down followed to the inner chamber of reactor body. The utility model discloses a waste water gets into behind the inner chamber of reactor body through the inlet tube, high hydraulic load makes the organic matter in the reactor body inner chamber abundant with the mud contact of reactor body inner chamber bottom with high yield gas load, mud is in abundant inflation state, make mass transfer rate obtain promoting, anaerobic reaction rate and organic load have been improved greatly, with mud through second grade three-phase separator and one-level three-phase separator, marsh gas separates with sewage, it is poor to have solved current GBS reactor mass transfer effect when using, biochemical reaction is inefficient, thereby be not convenient for the problem that people used.

Description

Sewage treatment GSB reactor

Technical Field

The utility model relates to a sewage treatment technical field specifically is a sewage treatment GSB reactor.

Background

Sewage treatment means that the sewage reaches the water quality requirement of discharging into a certain water body or reuse and purifies the process, sewage treatment is widely applied to various fields such as building, agriculture, traffic, energy, petrochemical industry, environmental protection, urban landscape, medical treatment and catering, and the GSB reactor is needed to be used in sewage treatment as well as the daily life of common people is increasingly gone into, but the mass transfer effect is poor when using current GBS reactor, and biochemical reaction efficiency is low, thereby not being convenient for people to use.

SUMMERY OF THE UTILITY MODEL

The utility model provides a not enough to prior art, the utility model provides a sewage treatment GSB reactor possesses the advantage that the treatment effeciency is high, and it is poor to have solved current GBS reactor mass transfer effect when using, and biochemical reaction is inefficient to the problem that people used not convenient for.

In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a sewage treatment GSB reactor, includes the bottom plate, the top fixedly connected with reactor body of bottom plate, the supreme mixed region, expansion zone and the smart processing area of including in proper order are down followed to the reactor body, supreme one-level triphase separator and the second grade triphase separator of being provided with respectively are down followed to the inner chamber of reactor body, there is the gas-liquid agitator at the top of reactor body inner chamber through bearing swing joint, and the gas-liquid agitator runs through one-level triphase separator and second grade triphase separator and extends to the mixed region, the top fixedly connected with collection chamber of reactor body, the bottom of inner chamber is provided with the water-locator.

Preferably, the left side and the right side at the top of the reactor body are both provided with gas outlets, the inner cavity of the gas collection chamber is provided with a reflection plate, the left side and the right side at the top of the gas collection chamber are both communicated with a gas-liquid separator, and the top of the gas-liquid separator is communicated with an exhaust pipe.

Preferably, the left bottom of reactor body communicates has the inlet tube, the left side intercommunication of inlet tube has the sewage pump, and the surface of inlet tube is provided with the solenoid valve, the left middle-end intercommunication of reactor body has circulating pipe, circulating pipe's bottom communicates in the top of inlet tube.

Preferably, the top on reactor body right side communicates has the outlet pipe, the surface of outlet pipe is provided with the solenoid valve, the right side intercommunication of outlet pipe has the suction pump.

Preferably, the bottom of the right side of the reactor body is communicated with a sewage discharge pipe, and the surface of the sewage discharge pipe is provided with an electromagnetic valve.

Compared with the prior art, the utility model provides a sewage treatment GSB reactor possesses following beneficial effect:

1. the utility model discloses a waste water gets into behind the inner chamber of reactor body through the inlet tube, high hydraulic load makes the organic matter in the reactor body inner chamber abundant with the mud contact of reactor body inner chamber bottom with high yield gas load, mud is in abundant inflation state, make mass transfer rate obtain promoting, anaerobic reaction rate and organic load have been improved greatly, with mud through second grade three-phase separator and one-level three-phase separator, marsh gas separates with sewage, it is poor to have solved current GBS reactor mass transfer effect when using, biochemical reaction is inefficient, thereby be not convenient for the problem that people used.

2. The utility model discloses a set up the reflecting plate, prevent effectively that marsh gas from passing through the collection chamber and overflowing.

3. The utility model discloses a set up the gas-liquid agitator, further promote the mixing efficiency of mud and organic matter.

Drawings

FIG. 1 is a schematic structural view of the present invention;

fig. 2 is a schematic view of the cross-sectional structure of the present invention.

In the figure: 1. a base plate; 2. a reactor body; 3. a water pump; 4. an electromagnetic valve; 5. a gas collection chamber; 6. a gas-liquid separator; 7. an exhaust pipe; 8. a sewage pump; 9. a water inlet pipe; 10. a circulating water pipe; 11. a reflective plate; 12. a secondary three-phase separator; 13. a gas-liquid stirrer; 14. an air outlet; 15. a water outlet pipe; 16. a mixing zone; 17. a fine processing area; 18. a first-stage three-phase separator; 19. an expansion zone; 20. a blow-off pipe; 21. a water distributor.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "front end", "rear end", "both ends", "one end", "the other end", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element to be referred must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.

In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted", "provided", "connected", and the like are to be construed broadly, such as "connected", which may be fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.

The utility model discloses a bottom plate 1, reactor body 2, suction pump 3, solenoid valve 4, collection chamber 5, vapour and liquid separator 6, blast pipe 7, sewage pump 8, inlet tube 9, circulating pipe 10, reflecting plate 11, second grade three phase separator 12, gas-liquid agitator 13, gas outlet 14, outlet pipe 15, mixing area 16, the smart district 17 that handles, one-level three phase separator 18, expansion zone 19, blow off pipe 20 and water-locator 21 part are the parts that general standard or technical personnel in the field know, its structure and principle all are that this technical personnel all can learn through the technical manual or learn through conventional experimental method.

Referring to fig. 1-2, a GSB reactor for sewage treatment comprises a bottom plate 1, a reactor body 2 is fixedly connected to the top of the bottom plate 1, gas outlets 14 are respectively formed on the left and right sides of the top of the reactor body 2, a reflecting plate 11 is arranged in an inner cavity of a gas collection chamber 5, biogas is effectively prevented from escaping through the gas collection chamber 5 by arranging the reflecting plate 11, the left and right sides of the top of the gas collection chamber 5 are respectively communicated with a gas-liquid separator 6, the top of the gas-liquid separator 6 is communicated with an exhaust pipe 7, the left bottom of the reactor body 2 is communicated with a water inlet pipe 9, the left side of the water inlet pipe 9 is communicated with a sewage pump 8, the surface of the water inlet pipe 9 is provided with an electromagnetic valve 4, the left middle end of the reactor body 2 is communicated with a circulating water pipe 10, the bottom of the circulating water pipe 10 is communicated with the top of the water inlet pipe 9, the top of the right side of the reactor body 2 is communicated with a water outlet pipe 15, the surface of the water outlet pipe 15 is provided with the electromagnetic valve 4, the right side intercommunication of outlet pipe 15 has suction pump 3, the bottom intercommunication on 2 right sides of reactor body has blow off pipe 20, and the surface of blow off pipe 20 is provided with solenoid valve 4, supreme mixing area 16 of including in proper order is followed to reactor body 2, inflation district 19 and smart processing area 17, supreme one-level three phase separator 18 and the second grade three phase separator 12 of being provided with respectively is followed to the inner chamber of reactor body 2, there is gas-liquid agitator 13 at the top of 2 inner chambers of reactor body through bearing swing joint, through setting up gas-liquid agitator 13, further promote mud and organic matter mixing efficiency, and gas-liquid agitator 13 runs through one-level three phase separator 18 and second grade three phase separator 12 and extends to mixing area 16, the top fixedly connected with collection chamber 5 of reactor body 2, the bottom of 2 inner chambers is provided with water-locator 21.

When using, waste water gets into the inner chamber of reactor body 2 through inlet tube 9 after, high hydraulic load makes the organic matter in the inner chamber of reactor body 2 abundant with the mud contact of reactor body 2 inner chamber bottom with high gas production load, mud is in abundant inflation state, make mass transfer rate obtain promoting, anaerobic reaction rate and organic load have been improved greatly, through second grade three-phase separator 12 and one-level three-phase separator 18 with mud, marsh gas and sewage separate, marsh gas rises to in the inner chamber of collection chamber 5, it is poor to have solved current GBS reactor mass transfer effect when using, biochemical reaction is inefficient, thereby be not convenient for the problem that people used (external controller is the PLC controller in this application, simultaneously, two of external controller are connected with power plug through the wire, and adopt the commercial power to supply power in this application).

While embodiments of the present invention have been shown and described, it will be apparent to those skilled in the art that various modifications and changes can be made in the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the scope of the claims of the present invention.

Claims

1. A sewage treatment GSB reactor, includes bottom plate (1), its characterized in that: the top fixed connection reactor body (2) of bottom plate (1), supreme mixing area (16), expansion region (19) and the fine processing district (17) of following in proper order are followed in reactor body (2), the inner chamber of reactor body (2) is followed supreme one-level triphase separator (18) and the second grade triphase separator (12) of being provided with respectively down, there are gas-liquid agitator (13) at the top of reactor body (2) inner chamber through bearing swing joint, and gas-liquid agitator (13) run through one-level triphase separator (18) and second grade triphase separator (12) and extend to mixing area (16), the top fixedly connected with collection chamber (5) of reactor body (2), the bottom of reactor body (2) inner chamber is provided with water-locator (21).

2. The wastewater treatment GSB reactor of claim 1, wherein: gas outlet (14) have all been seted up to the left and right sides at reactor body (2) top, the inner chamber of collection chamber (5) is provided with reflecting plate (11), the left and right sides at collection chamber (5) top all communicates vapour and liquid separator (6), and the top intercommunication of vapour and liquid separator (6) has blast pipe (7).

3. The wastewater treatment GSB reactor of claim 1, wherein: the left bottom intercommunication of reactor body (2) has inlet tube (9), the left side intercommunication of inlet tube (9) has sewage pump (8), and the surface of inlet tube (9) is provided with solenoid valve (4), the left middle-end intercommunication of reactor body (2) has circulating water pipe (10), the bottom of circulating water pipe (10) communicates in the top of inlet tube (9).

4. The wastewater treatment GSB reactor of claim 1, wherein: the reactor is characterized in that a water outlet pipe (15) is communicated with the top of the right side of the reactor body (2), an electromagnetic valve (4) is arranged on the surface of the water outlet pipe (15), and a water suction pump (3) is communicated with the right side of the water outlet pipe (15).

5. The wastewater treatment GSB reactor of claim 1, wherein: the bottom on the right side of the reactor body (2) is communicated with a sewage discharge pipe (20), and the surface of the sewage discharge pipe (20) is provided with an electromagnetic valve (4).