CN209352712U - A kind of organic wastewater with high concentration processing equipment - Google Patents
A kind of organic wastewater with high concentration processing equipment Download PDFInfo
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- CN209352712U CN209352712U CN201821686547.1U CN201821686547U CN209352712U CN 209352712 U CN209352712 U CN 209352712U CN 201821686547 U CN201821686547 U CN 201821686547U CN 209352712 U CN209352712 U CN 209352712U
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- precipitation tank
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Abstract
The utility model discloses a kind of organic wastewater with high concentration processing equipments, including physico-chemical precipitation tank and sludge filter press, the lower section of the physico-chemical precipitation tank is equipped with sludge filter press, the top of physico-chemical precipitation tank is equipped with leakage fluid dram, the right side of oily-water seperating equipment is equipped with triple effect evaporator, oily-water seperating equipment and triple effect evaporator pass through pipeline connection, the right side of triple effect evaporator is equipped with degreasing tank, the water outlet of triple effect evaporator is connected to degreasing tank, the right side of degreasing tank is equipped with biochemical slot, organic wastewater with high concentration is injected in materialization settling tank, organic wastewater with high concentration in physico-chemical precipitation tank is detected, the medicament in medicament storage tank is quantitatively imported in physico-chemical precipitation tank according to testing result, realize that the quantitative accurate of medicament is launched, made using triple effect evaporator crystallizable at analyzing in waste water, the grease in waste water is further removed using degreasing tank, it removes Waste water in oil groove enters in biochemical slot, solve the problems, such as existing sewage disposal device take up a large area, treatment effeciency it is low.
Description
Technical field
The utility model relates to a kind of sewage disposal device, specifically a kind of organic wastewater with high concentration processing equipment.
Background technique
In the industrial wastewaters such as sanitary sewage, food processing and papermaking, contain carbohydrate, protein, grease, wooden
The organic substances such as element.These substances can pass through the biological chemistry action of microorganism to suspend or dissolved state is present in sewage
And it decomposes.It needs to consume oxygen, thus referred to as oxygen consumption pollutant in its decomposable process.This pollutant can cause molten in water
It solves oxygen to reduce, influences the growth of fish He other aquatiles.After oxygen in water exhausts, organic matter carries out anaerobic digestion, produces
The bad smells such as raw hydrogen sulfide, ammonia and mercaptan, make water quality deterioration.
Often volume is larger for existing organic wastewater with high concentration processing equipment, takes up a large area, wastewater treatment efficiency is poor.
Utility model content
The purpose of this utility model is to provide a kind of organic wastewater with high concentration processing equipments, to solve in above-mentioned background technique
The problem of proposition.
To achieve the above object, the utility model provides the following technical solutions:
A kind of organic wastewater with high concentration processing equipment, including physico-chemical precipitation tank and sludge filter press, the physico-chemical precipitation tank
Lower section is equipped with sludge filter press, sludge filter press and sludge filter press by pipeline connection, and the top of physico-chemical precipitation tank is equipped with row
Liquid mouth, leakage fluid dram are connected to by pipeline with oily-water seperating equipment, and the right side of oily-water seperating equipment is equipped with triple effect evaporator, grease point
From device and triple effect evaporator by pipeline connection, the right side of triple effect evaporator is equipped with degreasing tank, the water outlet of triple effect evaporator
It is connected to degreasing tank, the right side of degreasing tank is equipped with biochemical slot, and degreasing tank is connected to biochemical slot.
As a further solution of the present invention: being equipped with stirring motor at the top of the physico-chemical precipitation tank, horse is stirred
The axle stretch end reached passes through to be protruded into physico-chemical precipitation tank at the top of physico-chemical precipitation tank, and the axle stretch end of stirring motor is equipped with paddle
Wheel.
The top of the physico-chemical precipitation tank is equipped with inlet as a further solution of the present invention,.
The physico-chemical precipitation tank is connected to medicament storage tank as a further solution of the present invention, in medicament storage tank
Compound pump is installed, the inside of physico-chemical precipitation tank is equipped with pH auto-controller, electric conductivity detector, fluid level controller, materialization
The outside of settling tank is equipped with control cabinet.
The bottom of the biochemical slot is placed with biochemical filler as a further solution of the present invention, biochemical slot
Inside holds oily strain liquid.
Compared with prior art, the utility model has the beneficial effects that organic wastewater with high concentration is injected in materialization settling tank,
Organic wastewater with high concentration in physico-chemical precipitation tank is detected, the medicament in medicament storage tank is quantitatively imported into object according to testing result
Change in settling tank, realizes that the quantitative accurate of medicament is launched, avoid excessive delivering medicament from generating waste, make to give up using triple effect evaporator
It is crystallizable at analyzing in water, the grease in waste water is further removed using degreasing tank, the waste water in degreasing tank enters biochemistry
In slot, waste water is handled using biochemical strain, sewage is carried out certainly using physico-chemical precipitation tank, triple effect evaporator, biochemical slot
Dynamicization processing, biochemical strain are German import, are aerobic and anaerobic type strain, do not need special anaerobic pond, the life of strain
Power is indomitable, and aerobic and anaerobic condition can survive, and biological flora time to live is long, solves existing sewage disposal device and accounts for
The problem that ground area is big, treatment effeciency is low.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of organic wastewater with high concentration processing equipment.
In figure: 1- physico-chemical precipitation tank；2- oily-water seperating equipment；3- triple effect evaporator；4- degreasing tank；5- biochemistry slot；6- is dirty
Mud filter press；7- medicament storage tank.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Embodiment 1
Referring to Fig. 1, in the utility model embodiment, a kind of organic wastewater with high concentration processing equipment, including physico-chemical precipitation tank 1
It is equipped with inlet with the top of sludge filter press 6, physico-chemical precipitation tank 1, organic wastewater with high concentration injects physico-chemical precipitation by inlet
In tank 1, physico-chemical precipitation tank 1 is connected to medicament storage tank 7, and compound pump, the inside peace of physico-chemical precipitation tank 1 are equipped in medicament storage tank 7
Equipped with pH auto-controller, electric conductivity detector, fluid level controller, the outside of physico-chemical precipitation tank 1 is equipped with control cabinet, utilizes pH
Auto-controller, electric conductivity detector detect the organic wastewater with high concentration in physico-chemical precipitation tank 1, and control cabinet controls compound pump
Start and stop, the medicament in medicament storage tank 7 is quantitatively imported in physico-chemical precipitation tank 1 according to testing result, realizes the quantitative essence of medicament
Standard is launched, and the lower section of physico-chemical precipitation tank 1 is equipped with sludge filter press 6, and sludge filter press 6 and physico-chemical precipitation tank 1 pass through pipeline connection,
The sludge of the bottom precipitation of physico-chemical precipitation tank 1 enters in sludge filter press 6, carries out filters pressing to sludge using sludge filter press 6, real
It is now separated by solid-liquid separation, the top of physico-chemical precipitation tank 1 is equipped with leakage fluid dram, and leakage fluid dram is connected to by pipeline with oily-water seperating equipment 2, passes through
The organic wastewater with high concentration of preliminary treatment is discharged by leakage fluid dram, into oily-water seperating equipment 2, by the oil in organic wastewater with high concentration
Dirt separation, the right side of oily-water seperating equipment 2 are equipped with triple effect evaporator 3, and oily-water seperating equipment 2 and triple effect evaporator 3 pass through pipeline
Connection, by oily-water seperating equipment 2 handle waste water enter in triple effect evaporator 3, using triple effect evaporator 3 make in waste water can
Crystallised component is precipitated, and the right side of triple effect evaporator 3 is equipped with degreasing tank 4, and the water outlet of triple effect evaporator 3 is connected to degreasing tank 4,
The grease in waste water is further removed using degreasing tank 4, the right side of degreasing tank 4 is equipped with biochemical slot 5, and degreasing tank 4 and biochemical slot 5 connect
Logical, the bottom of biochemical slot 5 is placed with biochemical filler, and the inside of biochemical slot 5 holds oily strain liquid, using biochemical strain to waste water
It is handled.
The working principle of the utility model is: organic wastewater with high concentration is injected in materialization settling tank 1, automatically controlled using pH
Instrument, electric conductivity detector detect the organic wastewater with high concentration in physico-chemical precipitation tank 1, and control cabinet controls the start and stop of compound pump,
The medicament in medicament storage tank 7 is quantitatively imported in physico-chemical precipitation tank 1 according to testing result, realizes that the quantitative accurate of medicament is launched,
Preliminary treatment is carried out to waste water, waste water after treatment enters in oily-water seperating equipment 2, the greasy dirt in waste water is separated, warp
Cross oily-water seperating equipment 2 processing waste water enter in triple effect evaporator 3, using triple effect evaporator 3 make in waste water it is crystallizable at
It analyzes, the grease in waste water is further removed using degreasing tank 4, the waste water in degreasing tank 4 enters in biochemical slot 5, utilizes life
Change strain to handle waste water.
Embodiment 2
On the basis of embodiment physico-chemical precipitation tank 1, the top of physico-chemical precipitation tank 1 is equipped with stirring motor, stirring motor
Axle stretch end pass through physico-chemical precipitation tank 1 top protrude into physico-chemical precipitation tank 1, the axle stretch end of stirring motor is equipped with paddle
Wheel, for stirring the organic wastewater with high concentration in materialization settling tank 1, is more fully mixed waste water with medicament.
It should be strongly noted that physico-chemical precipitation tank 1 and sludge filter press 6 are the application of the prior art, benefit in the application
The innovative point that automatic processing is the application is carried out to sewage with physico-chemical precipitation tank, triple effect evaporator, biochemical slot, is effectively solved
Existing sewage disposal device takes up a large area, treatment effeciency is low problem.
It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and
And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this is practical new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this is practical new
The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing for the equivalent requirements of the claims will be fallen in
All changes in justice and range are embraced therein.It should not treat any reference in the claims as limiting
Related claim.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (5)
1. a kind of organic wastewater with high concentration processing equipment, including physico-chemical precipitation tank (1) and sludge filter press (6), which is characterized in that institute
The lower section for stating physico-chemical precipitation tank (1) is equipped with sludge filter press (6), and sludge filter press (6) and physico-chemical precipitation tank (1) are connected by pipeline
Logical, the top of physico-chemical precipitation tank (1) is equipped with leakage fluid dram, and leakage fluid dram is connected to by pipeline with oily-water seperating equipment (2), water-oil separating
The right side of device (2) is equipped with triple effect evaporator (3), and oily-water seperating equipment (2) and triple effect evaporator (3) are by pipeline connection, and three
The right side for imitating evaporator (3) is equipped with degreasing tank (4), and the water outlet of triple effect evaporator (3) is connected to degreasing tank (4), degreasing tank (4)
Right side be equipped with biochemical slot (5), degreasing tank (4) is connected to biochemistry slot (5).
2. organic wastewater with high concentration processing equipment according to claim 1, which is characterized in that the physico-chemical precipitation tank (1)
Top is equipped with stirring motor, and the axle stretch end of stirring motor passes through and protrudes into physico-chemical precipitation tank (1) at the top of physico-chemical precipitation tank (1)
Interior, the axle stretch end of stirring motor is equipped with agitator arm.
3. organic wastewater with high concentration processing equipment according to claim 2, which is characterized in that the physico-chemical precipitation tank (1)
Top is equipped with inlet.
4. organic wastewater with high concentration processing equipment according to claim 3, which is characterized in that the physico-chemical precipitation tank (1) with
Medicament storage tank (7) connection, medicament storage tank (7) is interior to be equipped with compound pump, and the inside of physico-chemical precipitation tank (1) is equipped with pH automatic control
The outside of instrument, electric conductivity detector, fluid level controller, physico-chemical precipitation tank (1) is equipped with control cabinet.
5. organic wastewater with high concentration processing equipment according to claim 1 to 4, which is characterized in that the biochemistry slot (5)
Bottom be placed with biochemical filler, the inside of biochemical slot (5) holds oily strain liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821686547.1U CN209352712U (en) | 2018-10-18 | 2018-10-18 | A kind of organic wastewater with high concentration processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821686547.1U CN209352712U (en) | 2018-10-18 | 2018-10-18 | A kind of organic wastewater with high concentration processing equipment |
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| Publication Number | Publication Date |
|---|---|
| CN209352712U true CN209352712U (en) | 2019-09-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821686547.1U Active CN209352712U (en) | 2018-10-18 | 2018-10-18 | A kind of organic wastewater with high concentration processing equipment |
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| CN (1) | CN209352712U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114314978A (en) * | 2021-11-24 | 2022-04-12 | 山东钢铁股份有限公司 | Recycling treatment process for organic solid hazardous waste heat cracking wastewater in steel industry |
-
2018
- 2018-10-18 CN CN201821686547.1U patent/CN209352712U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114314978A (en) * | 2021-11-24 | 2022-04-12 | 山东钢铁股份有限公司 | Recycling treatment process for organic solid hazardous waste heat cracking wastewater in steel industry |
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