CN213865833U

CN213865833U - Sewage treatment integrated device

Info

Publication number: CN213865833U
Application number: CN202022521538.0U
Authority: CN
Inventors: 刘学农; 刘国华
Original assignee: Shanghai Ruan Tuo Automation Equipment Co ltd
Current assignee: Shanghai Ruan Tuo Automation Equipment Co ltd
Priority date: 2020-11-04
Filing date: 2020-11-04
Publication date: 2021-08-03
Anticipated expiration: 2030-11-04

Abstract

The utility model discloses a sewage treatment integrated device belongs to sewage treatment technical field. It includes the device body, the device body includes the stirring pond that is linked together in proper order through a plurality of pipelines, pond is synthesized to pipe chute sedimentation tank and biochemical ozone, be connected with the feeder on the pipeline between stirring pond and the pipe chute sedimentation tank, the input of feeder is connected with the liquid medicine and mixes the pond in advance, stirring pond output pipeline stretches into to pipe chute sedimentation tank middle part, biochemical ozone is synthesized the pond and is included good oxygen pond, anaerobism pond and ozone pond, good oxygen pond, anaerobism pond and ozone pond are linked together in proper order and strong calandria is all installed to three's inner chamber bottom. The utility model discloses an add the sneak into liquid medicine in sewage treatment process to loop through good oxygen pond, anaerobism pond and ozone pond, realize sewage treatment's biochemical ozone treatment, and cooperate strong calandria, discharge the precipitate in each treatment pond fast, improve sewage treatment efficiency.

Description

Sewage treatment integrated device

Technical Field

The utility model relates to a sewage treatment integrated device belongs to sewage treatment technical field.

Background

Conventional sewage treatment adopts the disconnect-type mostly, needs concentrate collection and transportation to sewage, and is comparatively inconvenient, and conventional sewage treatment integrated device specification is less relatively, and sewage treatment efficiency is the degree of purifying limited and cause the jam easily promptly.

Disclosure of Invention

The utility model discloses the technical problem that will solve lies in: provides a sewage treatment integrated device, which solves the problem of low operation efficiency of sewage treatment equipment.

The utility model discloses the technical problem that will solve takes following technical scheme to realize:

the utility model provides a sewage treatment integrated device, includes the device body, the device body includes the stirring pond, pipe chute sedimentation tank and the biochemical ozone comprehensive pool that are linked together in proper order through a plurality of pipelines, be connected with the feeder on the pipeline between stirring pond and the pipe chute sedimentation tank, the input of feeder is connected with the liquid medicine and mixes the pond in advance, stirring pond output pipeline stretch into extremely pipe chute sedimentation tank middle part, biochemical ozone comprehensive pool is including good oxygen pond, anaerobism pond and ozone pond, good oxygen pond the anaerobism pond and strong calandria is all installed to ozone pond and the inner chamber bottom that is linked together in proper order and the three.

As a preferable example, the output pipeline of the stirring tank extends into the middle part of the inclined tube sedimentation tank and is communicated with a plurality of branch pipes, and a plurality of drainage holes are formed in the side wall of each branch pipe at equal intervals.

As a preferable example, the top end of the inner cavity of the inclined tube sedimentation tank is annularly provided with an overflow plate, the overflow plate and the side wall of the inner cavity of the inclined tube sedimentation tank surround to form an overflow groove, a water inlet at the communication part of the inclined tube sedimentation tank and the biochemical ozone comprehensive tank is positioned in the overflow groove, and the depth of the inner cavity of the overflow groove is 4-8 cm.

As a preferable example, the top parts of the anaerobic tank and the ozone tank are provided with exhaust valves.

As a preferable example, a one-way valve for preventing the backflow of ozone is arranged on a pipeline connected between the anaerobic tank and the ozone tank.

As a preferred example, the aerobic tank is provided with a water inlet pipe and a water outlet pipe, the aerobic tank is communicated with the inclined tube sedimentation tank through the water inlet pipe, the aerobic tank is communicated with the anaerobic tank through the water outlet pipe, the water inlet pipe extends into the inner cavity of the aerobic tank through the top of the side wall of the aerobic tank, the end of the water inlet pipe extends to be close to the bottom of the inner cavity of the aerobic tank, the end of the water outlet pipe is close to the top of the inner cavity of the aerobic tank, and the water outlet pipe extends from the bottom of the inner cavity of the aerobic tank and is communicated with the anaerobic tank.

As a preferable example, a water inlet and a water outlet are respectively formed in two sides of the inner cavity of the anaerobic tank, a plurality of partition plates are respectively and fixedly connected to the top and the bottom of the inner cavity of the anaerobic tank, and the partition plates at the top of the anaerobic tank and the partition plates at the bottom of the anaerobic tank are arranged in a staggered mode.

As a preferred example, the bottom slope ratio of the anaerobic tank and the ozone tank are both 1/10.

The utility model has the advantages that: the utility model discloses a biochemical ozone that sets up good oxygen pond, anaerobism pond and ozone pond and combine to use formation synthesizes the pond and carries out further decomposition with organic matter etc. in the sewage, improves the sewage treatment effect, and strong calandria is deuterogamied, and the precipitate that produces blocks up and reduces the space that biochemical ozone synthesizes the pond inner chamber among the sewage treatment process in the biochemical ozone synthesis pond of prevention, crisscross a plurality of baffle that is provided with in the anaerobism pond increases the sewage flow path in the anaerobism pond, has improved sewage conversion efficiency.

Drawings

Fig. 1 is a schematic structural diagram of the present invention (the exterior is a box structure);

FIG. 2 is a schematic structural view of a stirring tank and an inclined tube sedimentation tank in the device body of the utility model;

FIG. 3 is a schematic view of the structure of the inner cavity of the anaerobic tank of the utility model;

FIG. 4 is a vent valve at the top box of the anaerobic tank and the ozone tank of the utility model;

fig. 5 is the top structure schematic diagram of the inner cavity of the inclined tube sedimentation tank of the utility model.

In the figure: the device comprises a stirring tank 1, an inclined tube sedimentation tank 2, a liquid medicine premixing tank 3, an aerobic tank 4, an anaerobic tank 5, an ozone tank 6, a forced exhaust pipe 7, an overflow plate 8, an exhaust valve 9 and a partition plate 10.

Detailed Description

In order to make the technical means, the creation features, the achievement purposes and the functions of the present invention easy to understand and understand, the present invention is further explained by combining the following specific drawings.

As shown in fig. 1-5, a sewage treatment integrated device comprises a device body, the device body comprises a stirring tank 1 (a water storage container and a stirrer in the water storage container), an inclined tube sedimentation tank 2 and a biochemical ozone comprehensive tank which are sequentially communicated through a plurality of pipelines, a feeder (a pump, such as a water pump, pumps liquid medicine into the pipeline from a liquid medicine premixing tank 3) is connected on the pipeline between the stirring tank 1 and the inclined tube sedimentation tank 2, the input end of the feeder is connected with the liquid medicine premixing tank 3, the output pipeline of the stirring tank 1 extends into the middle part of the inclined tube sedimentation tank 2, the biochemical ozone comprehensive tank comprises an aerobic tank 4, the anaerobic tank 5 and the ozone tank 6 are communicated in sequence, the aerobic tank 4, the anaerobic tank 5 and the ozone tank 6 are all provided with a strong exhaust pipe 7 at the bottom of the inner cavities of the anaerobic tank, the anaerobic tank and the ozone tank 6 (the strong exhaust pipe 7 refers to a drain pipe for actively draining water, and the drain pipe is connected with a strong water pump).

It should be noted that, the assembly box is arranged outside the device body to cover the whole device body as much as possible, so as to reduce the water leakage and waste gas dissipation during the sewage treatment process, the whole device body is located in the box, the box provides support for the device body, so as to facilitate the transportation and disassembly and assembly of the whole device body, fig. 3 is a cross-sectional view of the inner cavity of the anaerobic tank 5, the circle in the figure is the water inlet of the anaerobic tank 5, the arrow in the figure is the flow direction of sewage, the partition boards on the bottom of the anaerobic tank 5 can separate sediment deposited at the bottom of the inner cavity of the anaerobic tank 5, although the flow path of sewage is increased, the deposited sediment can not be discharged through a single sewage discharge hole, the sewage discharge pipes (i.e. the forced discharge pipes 7) at the bottom in fig. 3 are respectively connected in parallel to the interval formed by each partition board 10 and the side wall or the bottom wall of the inner cavity of the anaerobic tank for complete suction and removal, the sewage pipes are connected to the lowermost portion of the interval formed by the partitions 10.

The inclined tube sedimentation tank 2 is an inclined tube sedimentation tank 2 which is provided with an inclined tube (also can be made of porous plates) in a sedimentation area, the assembly form is an inclined tube and a branch tube, the sedimentation area of the horizontal flow type or vertical flow type inclined tube sedimentation tank 2 is divided into a series of shallow sedimentation layers by utilizing inclined parallel tubes or parallel pipelines (sometimes honeycomb fillers can be utilized), and the treated and settled sludge moves and is separated in each sedimentation shallow layer.

The output pipeline of the stirring tank 1 extends into the middle part of the inclined tube sedimentation tank 2 and is communicated with a plurality of branch pipes, and a plurality of drain holes are formed in the side wall of each branch pipe at equal intervals (the branch pipes are arranged and the drain holes are formed in the branch pipes, so that the sewage can be relatively uniform when being discharged from the inclined tube sedimentation tank 2 in the stirring tank 1).

An overflow plate 8 is annularly arranged at the top end of an inner cavity of the inclined tube sedimentation tank 2, the overflow plate 8 and the side wall of the inner cavity of the inclined tube sedimentation tank 2 are encircled to form an overflow groove (the overflow plate 8 is fixed on the side wall of the inner cavity of the inclined tube sedimentation tank 2 in an encircling way, the formed overflow groove is annular), a water inlet at the communication part of the inclined tube sedimentation tank 2 and the biochemical ozone comprehensive tank is positioned in the overflow groove, the depth of the inner cavity of the overflow groove is 4-8cm, liquid level meters are fixedly arranged at the top of the inner cavity of each treatment tank (the treatment tanks in the position refer to a stirring tank 1, the inclined tube sedimentation tank 2, an anaerobic tank 5, an ozone tank 6 and an aerobic tank 4) in the whole device body and are used for measuring the sewage height in each treatment tank, the water level of each treatment tank is kept to be reduced in sequence along the sewage flowing direction (the sewage sequentially passes through the stirring tank 1, the inclined tube sedimentation tank, it means that the corresponding treatment tank and the adjacent treatment tank are blocked, and the forced exhaust pipe 7 needs to be opened.

The top parts of the anaerobic tank 5 and the ozone tank 6 are both provided with exhaust valves 9, biochemical reactions in the anaerobic tank 5 and the ozone tank 6 may generate certain gas, so that the gas needs to be collected and discharged in a centralized manner, and the exhaust valves 9 are sleeved with gas collecting pipes.

Be provided with on the pipeline that is connected between anaerobism pond 5 and the ozone pond 6 and be used for preventing the palirrhea check valve of ozone, in addition the utility model discloses the connecting tube of many places if (the feeder is carried to stirring 1 output pipeline in pond, has just adopted the check valve on the pipeline that the feeder is connected, prevents that the material from moving the in-process backward flow to pollute whole device body).

Good oxygen pond 4 is provided with inlet tube and outlet pipe, good oxygen pond 4 is linked together with pipe chute sedimentation tank 2 through the inlet tube, good oxygen pond 4 is linked together through outlet pipe and anaerobism pond 5, the inlet tube stretches into to good oxygen pond 4 inner chambers through 4 lateral walls tops in good oxygen pond, the tip of inlet tube extends to and is close 4 inner chamber bottoms in good oxygen pond, the tip of outlet pipe is close 4 inner chamber tops in good oxygen pond, the outlet pipe is stretched out and is linked together with anaerobism pond 5 by 4 inner chamber bottoms in good oxygen pond, the inlet tube of here and the setting of outlet pipe, change pond in the sewage rivers to, there is promotion to the stirring degree of sewage.

Water inlet and delivery port have been seted up respectively to the both sides in the 5 inner chambers in anaerobism pond, 5 inner chamber tops in anaerobism pond and bottom be fixedly connected with a plurality of baffle 10 respectively, a plurality of baffle 10 at 5 tops in anaerobism pond and the crisscross setting of a plurality of baffle 10 of 5 bottoms in anaerobism pond, setting up between water inlet and delivery port makes the rivers removal path of anaerobism district inner chamber be the S-shaped setting, increases sewage flow path, and the decontamination effect rises to some extent.

The bottom slope ratio of the anaerobic tank 5 and the ozone tank 6 is 1/10, the sediment at the bottom of the anaerobic tank 5 and the ozone tank 6 can be concentrated to one side due to the slope at the bottom, the bottom of the slope is also connected to the strong exhaust pipe 7, and the working strength of the strong exhaust pipe 7 for absorbing the sediment is reduced.

The working principle is as follows: the utility model discloses the sewage treatment integrated device mentioned carries out preliminary mixing to sewage earlier, carry out preliminary sediment after sneaking into the liquid medicine again, through overflow plate 8, everywhere water inlet, the delivery port, the inlet tube, the outlet pipe, baffle 10 etc. have improved the flow distance of sewage in whole device body, and cooperate corresponding level gauge, forced drainage pipe 7 etc. ensure the inside smoothness nature in each treatment pond, thereby improve the sewage treatment efficiency of sewage treatment integrated equipment, can let in outside sedimentation tank to 7 exhaust sewage of forced drainage pipe and carry out further processing.

The basic principles and the main features of the invention and the advantages of the invention have been shown and described above. It should be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that various changes and modifications may be made without departing from the spirit and scope of the invention, and such changes and modifications fall within the scope of the claimed invention. The scope of the invention is defined by the appended claims and equivalents thereof.

Claims

1. The utility model provides a sewage treatment integrated device, includes the device body, its characterized in that: the device body includes that the pond is synthesized to stirring pond (1), pipe chute sedimentation tank (2) and biochemical ozone that are linked together in proper order through a plurality of pipelines, be connected with the feeder on the pipeline between stirring pond (1) and pipe chute sedimentation tank (2), the input of feeder is connected with liquid medicine and mixes pond (3) in advance, stirring pond (1) output pipeline stretch into extremely pipe chute sedimentation tank (2) middle part, biochemical ozone synthesizes the pond including good oxygen pond (4), anaerobism pond (5) and ozone pond (6), good oxygen pond (4) anaerobism pond (5) and strong calandria (7) are all installed to ozone pond (6) be linked together in proper order and the inner chamber bottom of three.

2. The integrated sewage treatment device of claim 1, wherein: the output pipeline of the stirring tank (1) extends into the middle part of the inclined tube sedimentation tank (2) and is communicated with a plurality of branch pipes, and a plurality of drain holes are formed in the side wall of each branch pipe at equal intervals.

3. The integrated sewage treatment device of claim 1, wherein: an overflow plate (8) is annularly arranged at the top end of the inner cavity of the inclined tube sedimentation tank (2), the overflow plate (8) and the side wall of the inner cavity of the inclined tube sedimentation tank (2) are encircled to form an overflow groove, a water inlet at the communication part of the inclined tube sedimentation tank (2) and the biochemical ozone comprehensive tank is positioned in the overflow groove, and the depth of the inner cavity of the overflow groove is 4-8 cm.

4. The integrated sewage treatment device of claim 1, wherein: the top parts of the anaerobic tank (5) and the ozone tank (6) are provided with exhaust valves (9).

5. The integrated sewage treatment device of claim 1, wherein: and a one-way valve for preventing ozone from flowing backwards is arranged on a pipeline connected between the anaerobic tank (5) and the ozone tank (6).

6. The integrated sewage treatment device of claim 1, wherein: good oxygen pond (4) are provided with inlet tube and outlet pipe, good oxygen pond (4) are passed through the inlet tube with pipe chute sedimentation tank (2) are linked together, good oxygen pond (4) are passed through the outlet pipe with anaerobism pond (5) are linked together, the inlet tube warp good oxygen pond (4) lateral wall top stretches into extremely good oxygen pond (4) inner chamber, the tip of inlet tube extends to and is close good oxygen pond (4) inner chamber bottom, the tip of outlet pipe is close good oxygen pond (4) inner chamber top, the outlet pipe by good oxygen pond (4) inner chamber bottom stretch out and with anaerobism pond (5) are linked together.

7. The integrated sewage treatment device of claim 1, wherein: the water inlet and the delivery port have been seted up respectively to both sides in anaerobism pond (5) inner chamber, anaerobism pond (5) inner chamber top and bottom are a plurality of baffle (10) of fixedly connected with respectively, a plurality of baffle (10) at anaerobism pond (5) top with a plurality of baffle (10) of anaerobism pond (5) bottom are crisscross to be set up.

8. The integrated sewage treatment device of claim 1, wherein: the bottom slope ratio of the anaerobic tank (5) to the ozone tank (6) is 1/10.