CN210528710U

CN210528710U - Biochemical regulation and control reaction system

Info

Publication number: CN210528710U
Application number: CN201921113357.5U
Authority: CN
Inventors: 刘景峰
Original assignee: Shenyang Songliao Environmental Engineering Co Ltd
Current assignee: Shenyang Songliao Environmental Engineering Co Ltd
Priority date: 2019-07-16
Filing date: 2019-07-16
Publication date: 2020-05-15
Anticipated expiration: 2029-07-16

Abstract

The utility model discloses a biochemical regulation and control reaction system, which relates to the technical field of biochemical purification water source and solves the technical problem that the prior biochemical reaction tank can not regulate the water quality and purify impurities in water in a grading way through biochemical reaction so as to lead to the incomplete purification of the water source, comprising a biochemical reaction tank, wherein a conveyor belt is arranged on the biochemical reaction tank, two ends of the conveyor belt are respectively sheathed with a driving wheel, the utility model carries out biochemical treatment on waste water through a catalytic oxidation unit, catalyzes and oxidizes the impurities such as grease in the water source into fine suspended matters, and then sprays the waste water in a micro-bubble mode through a dissolved gas release device, the impurities with lighter quality float upwards along with the bubbles and are removed through a scraper, the impurities with larger quality are isolated through an isolation plate, the impurities such as silt are discharged through a mud discharge port, and the treated waste water can fluctuate to the liquid level through a water outlet regulation and control device, ensuring the smoothness of drainage.

Description

Biochemical regulation and control reaction system

Technical Field

The utility model relates to a biochemical water source that purifies technical field specifically is a biochemical regulation and control reaction system.

Background

Along with the development of society and the improvement of science and technology, the living standard of people is gradually improved, the water source is a more indispensable resource in life, the water consumption of people is increased every day, the generated waste water is increased, the waste water needs to be treated for cyclic utilization, for example, in the utility model with the name of an environment-friendly air floating machine for waste water treatment and the publication number of CN208394823U, a scraping net, a rotating shaft and a return spring are designed, the scraping net is driven by a chain to lead the scum on the upper layer of the waste water to enter the discharging groove, meanwhile, the scraping net rotates around the rotating shaft at one end of the scraping plate, the contact coincidence between the scraping net and the discharging groove surface is improved, the gap between the scraping net and the discharging groove is avoided, the scum removing efficiency is improved, when the scraping net is separated from the discharging groove, the scraping net and the scraping plate are in the same horizontal plane by the return spring, increase and scrape the continuity that the net passed the dross, the shower nozzle that the equidistant was placed is adopted, improve the equilibrium of gas distribution in waste water, improve waste water treatment's efficiency, reduce waste water treatment's time, adopt the spout, pressure-limiting valve and buffer lever, make waste water enter into inside the air supporting machine through the spout, improve waste water gas's scattered degree, avoid gaseous too big waste residue that causes not adsorb with the bubble, avoid simultaneously not enough through the water pressure that dissolves the gas jar inside, the waste water dissolved oxygen volume that causes is not enough air supporting machine, but because current biochemical regulation and control system does not have biochemical reaction regulation and control to the water source, the water source can not obtain optimal treatment, only clear up the suspended solid on upper strata through the scraper blade, the aquatic still has great impurity of quality and silt, can not obtain timely clearance, the purification efficiency of biochemical regulation and control system to waste water has been reduced from this.

SUMMERY OF THE UTILITY MODEL

Not enough to prior art, the utility model provides a biochemical regulation and control reaction system has solved current biochemical reaction pond and can not adjust quality of water and carry out the hierarchical formula to aquatic impurity and purify thereby leading to the water source to purify thorough technical problem inadequately through biochemical reaction.

In order to achieve the above purpose, the utility model discloses a following technical scheme realizes: a biochemical regulation and control reaction system comprises a biochemical reaction tank, wherein a conveyor belt is arranged on the biochemical reaction tank, driving wheels are sleeved at two ends of the conveyor belt respectively, a driving motor is arranged on one of the driving wheels, a scraper is arranged on the conveyor belt, a slag discharging groove is formed in one side of the conveyor belt in the biochemical reaction tank, a baffle is arranged on the side wall surface of the slag discharging groove, a liquid level regulation and control device is arranged between the baffle and the side wall surface of the biochemical reaction tank, a water outlet is formed in the side wall surface of the biochemical reaction tank and is connected with the liquid level regulation and control device, a guide plate is arranged on the side wall surface of the other side of the slag discharging groove in the biochemical reaction tank, a support frame is arranged between the guide plate and the slag discharging groove in the biochemical reaction tank, a partition plate is arranged on the, and a dissolved air water release device is arranged between the other side wall surface in the biochemical reaction tank and the guide plate, and the dissolved air water release device is connected with a catalytic oxidation unit.

Preferably, the liquid level regulation and control device comprises a water collecting tank, the water collecting tank is installed at the input end of the water outlet, a water service pipe is connected to the water collecting tank, a floater is installed at the port of the water service pipe, and a balance weight needle is installed on the floater.

Preferably, the dissolved air-water release device comprises two flow guide pipes with the same structure, wherein the two flow guide pipes are arranged between the other side wall surface and the flow guide plate in the biochemical reaction tank, one end of each flow guide pipe is provided with a dissolved air releaser, the other end of each flow guide pipe is provided with an adjusting valve, and the adjusting valves are connected through flange pipes.

Preferably, the catalytic oxidation unit includes the water pump, the inlet tube is installed to the water pump input, the water pump output has the host computer through the pipe connection, there is the ozone machine through the pipe connection between water pump and the host computer, the host computer output is connected with the catalytic oxidation reactor, the filling has the catalyst in the catalytic oxidation reactor.

Preferably, the output end of the catalytic oxidation reactor is fixedly connected with the flange pipe through a flange plate.

Preferably, a discharge port is formed in the slag discharge groove.

Preferably, the isolation plate is obliquely arranged on the support frame, and the isolation plate is of a corrugated structure.

Preferably, the height of the two side wall surfaces of the sludge discharge port is gradually reduced from outside to inside to form a concave structure.

Advantageous effects

The utility model provides a biochemical regulation and control reaction system has solved current biochemical reaction pond and can not adjust the water quality through biochemical reaction and carry out the hierarchical formula to impurity in water and purify and lead to the water source to purify thorough technical problem inadequately, the utility model discloses a catalytic oxidation unit carries out biochemical treatment with waste water, with impurity catalytic oxidation such as grease in the water source tiny suspended solid, rethread dissolved gas release device sprays away waste water with the tiny bubble mode, the impurity that the quality is lighter is along with the bubble come-up, the rethread scraper blade is clear away, the great impurity of quality passes through the division board and keeps apart, the impurity of a class of silt is discharged through row mud mouth, waste water after the processing can fluctuate and reciprocate the liquid level through delivery port discharge liquid level regulation and control device, guarantees the smoothness nature of drainage.

Drawings

Fig. 1 is a schematic view of a biochemical regulation and control reaction system according to the present invention.

Fig. 2 is a schematic structural view of a liquid level control device of a biochemical control reaction system according to the present invention.

In the figure: 1-biochemical reaction tank; 2-a conveyor belt; 3-a transmission wheel; 4-driving the motor; 5-a scraper; 6-slag discharge groove; 7-a baffle plate; 8-water outlet; 9-a deflector; 10-a support frame; 11-a separator plate; 12-a sludge discharge port; 13-a discharge outlet; 14-a water collecting tank; 15-water pipe; 16-floating; 17-a counter weight needle; 18-a draft tube; 19-dissolved air releaser; 20-adjusting the valve; 21-a flange tube; 22-a water pump; 23-a water inlet pipe; 24-a host; 25-an ozone machine; 26-a catalytic oxidation reactor; 27-catalyst.

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.

Referring to fig. 1-2, the present invention provides a technical solution: a biochemical regulation and control reaction system comprises a biochemical reaction tank 1, wherein a conveyor belt 2 is installed on the biochemical reaction tank 1, driving wheels 3 are respectively sleeved at two ends of the conveyor belt 2, a driving motor 4 is installed on one of the driving wheels 3, a scraper 5 is installed on the conveyor belt 2, a slag discharge groove 6 is formed in one side of the conveyor belt 2 in the biochemical reaction tank 1, a baffle 7 is installed on the side wall surface of the slag discharge groove 6, a liquid level regulation and control device is installed between the baffle 7 and the side wall surface of the biochemical reaction tank 1, a water outlet 8 is formed in the side wall surface of the biochemical reaction tank 1, the water outlet is connected with the liquid level regulation and control device, a guide plate 9 is installed on the other side wall surface of the slag discharge groove 6 in the biochemical reaction tank 1, a support frame 10 is installed between the guide plate 9 and the slag discharge groove 6 in the biochemical reaction tank 1, and a separation, a sludge discharge port 12 is formed in the biochemical reaction tank 1 below the support frame 10, a dissolved air-water releasing device is installed between another side wall surface and the guide plate 9 in the biochemical reaction tank 1, a catalytic oxidation unit is connected on the dissolved air-water releasing device, the liquid level regulating device comprises a water collecting tank 14, the water collecting tank 14 is installed at the input end of the water outlet 8, a water through pipe 15 is connected on the water collecting tank 14, a floater 16 is installed at the port of the water through pipe 15, a balance weight needle 17 is installed on the floater 16, the dissolved air-water releasing device comprises two guide pipes 18 with the same structure, the two guide pipes 18 are installed between the other side wall surface and the guide plate 9 in the biochemical reaction tank 1, one ends of the two guide pipes 18 are respectively provided with a dissolved air releasing device 19, the other ends of the two guide pipes 18 are respectively provided with a regulating valve 20, and the regulating valves, catalytic oxidation unit includes water pump 22, inlet tube 23 is installed to water pump 22 input, there is host computer 24 water pump 22 output through the pipe connection, there is ozone machine 25 through the pipe connection between water pump 22 and the host computer, host computer 24 output is connected with catalytic oxidation reactor 26, the filling has catalyst 27 in the catalytic oxidation reactor 26, catalytic oxidation reactor 26 output and flange pipe 21 pass through ring flange fixed connection, it has bin outlet 13 to seted up in the row's

cinder notch

6, 11 slope installations on support frame 10 of division board, be corrugated structure on the division board 11, it is concave type structure to highly reduce gradually in to arrange the mud outlet 12 both sides wall by outer.

All the electrical components in the present application are connected with the power supply adapted to the electrical components through the wires, and an appropriate controller should be selected according to actual conditions to meet the control requirements, and specific connection and control sequences should be obtained.

Example (b): in the above, the power input ends of the driving motor 4, the dissolved air releaser 19, the water pump 22, the host 24, the ozone machine 25 and the catalytic oxidation reactor 26 are electrically connected with an external power supply through a lead, as can be seen from the attached drawings 1-2 of the specification, when in use, wastewater passes through the water inlet pipe 23, the water pump 22 is started, the water pump 22 pumps the wastewater in the water inlet pipe 23 into the output end of the water pump 22 from the input end of the water pump 22, at this time, the ozone machine 25 is started, ozone is generated by the ozone machine 25 and is combined with the pumped wastewater to enter the host 24, the host 24 discharges the combined wastewater into the catalytic oxidation reactor 26, the wastewater generates chemical reaction under the action of the catalyst 27, the wastewater is primarily treated, the wastewater is discharged into the flange pipe 21 at this time, the regulating valve 20 is opened, the wastewater after the primary treatment flows into the draft tube 18 and is ejected through the dissolved, at the moment, a large amount of fine bubbles are generated in the wastewater in the biochemical reaction tank 1, a large amount of impurities are attached to the surfaces of the bubbles, the fine bubbles float upwards under the action of a guide plate 9, a driving motor 4 is started, the driving motor 4 drives a driving wheel 3 to rotate, meanwhile, a conveying belt 2 rotates along with the driving wheel, a scraper 5 sequentially conveys the floating bubbles into a slag discharging groove 6 and discharges the floating bubbles through a discharging opening 13, the wastewater after the other part of reaction flows downwards, the impurities with higher mass in the wastewater are reduced due to gravity, the impurities with higher mass are blocked by a partition plate 11 at the moment, the partition plate 11 is prevented from being blocked by a corrugated structure on the partition plate 11 due to excessive impurities, the partition plate 11 plays a role in flow choking, a worker regularly cleans the partition plate 11, some silt also sinks to a mud discharging opening 12 through the partition plate 11, and inclined planes are arranged on two sides of the mud discharging opening, therefore, silt can be better collected at the position of the silt discharging port 12, the treated wastewater passes through the baffle 7, enters the water collecting tank 14 through the water service pipe 15 and flows out through the water outlet 8, in the drainage process, due to fluctuation of the liquid level, the port of the water service pipe 15 floats upwards by the float 16 on the water service pipe 15, the port of the water service pipe 14 is pressed downwards by the balance weight needle 17, the port of the water service pipe 15 can be always positioned at the liquid level, and the smoothness of drainage is kept.

It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation. The use of the phrase "comprising one of the elements does not exclude the presence of other like elements in the process, method, article, or apparatus that comprises the element.

Claims

1. A biochemical regulation and control reaction system comprises a biochemical reaction tank (1), a conveyor belt (2) is installed on the biochemical reaction tank (1), driving wheels (3) are respectively sleeved at two ends of the conveyor belt (2), a driving motor (4) is installed on one of the driving wheels (3), a scraper (5) is installed on the conveyor belt (2), the biochemical regulation and control reaction system is characterized in that a slag discharge groove (6) is formed in one side of the conveyor belt (2) in the biochemical reaction tank (1), a baffle plate (7) is installed on the side wall surface of the slag discharge groove (6), a liquid level regulation and control device is installed between the baffle plate (7) and the side wall surface of the biochemical reaction tank (1), a water outlet (8) is formed in the side wall surface of the biochemical reaction tank (1), the water outlet is connected with the liquid level regulation and control device, a guide plate (9) is installed on the other side surface of the slag discharge groove (6), the biochemical reaction tank is characterized in that a support frame (10) is arranged between a guide plate (9) and a slag discharge groove (6) in the biochemical reaction tank (1), a separation plate (11) is installed on the support frame (10), a sludge discharge port (12) is formed in the biochemical reaction tank (1) and below the support frame (10), a dissolved gas-water release device is installed between another side wall surface and the guide plate (9) in the biochemical reaction tank (1), and a catalytic oxidation unit is connected to the dissolved gas-water release device.

2. The biochemical regulation and control reaction system according to claim 1, wherein the liquid level regulation and control device comprises a water collection tank (14), the water collection tank (14) is installed at the input end of the water outlet (8), a water pipe (15) is connected to the water collection tank (14), a float (16) is installed at the port of the water pipe (15), and a balance weight needle (17) is installed on the float (16).

3. The biochemical regulation and control reaction system according to claim 1, wherein the dissolved air water release device comprises two flow guide pipes (18) with the same structure, the two flow guide pipes (18) are installed between the other side wall surface and the flow guide plate (9) in the biochemical reaction tank (1), one end of each of the two flow guide pipes (18) is respectively provided with a dissolved air releaser (19), the other end of each of the two flow guide pipes (18) is respectively provided with a regulating valve (20), and the regulating valves (20) are connected through a flange pipe (21).

4. The biochemical regulation and control reaction system according to claim 1, wherein the catalytic oxidation unit comprises a water pump (22), an inlet pipe (23) is installed at an input end of the water pump (22), an output end of the water pump (22) is connected with a host (24) through a pipeline, an ozone machine (25) is connected between the water pump (22) and the host through a pipeline, an output end of the host (24) is connected with a catalytic oxidation reactor (26), and a catalyst (27) is filled in the catalytic oxidation reactor (26).

5. The biochemical regulation reaction system according to claim 4, wherein the output end of the catalytic oxidation reactor (26) is fixedly connected with the flange pipe (21) through a flange plate.

6. The biochemical regulation reaction system according to claim 1, wherein a discharge opening (13) is formed in the slag discharge groove (6).

7. The biochemical regulation and control reaction system according to claim 1, wherein the isolation plate (11) is obliquely installed on the support frame (10), and the isolation plate (11) has a corrugated structure.

8. The biochemical regulation and control reaction system according to claim 1, wherein the two side wall surfaces of the sludge discharge port (12) gradually decrease in height from outside to inside to form a concave structure.