CN214880455U - Integrated equipment for wastewater treatment - Google Patents
Integrated equipment for wastewater treatment Download PDFInfo
- Publication number
- CN214880455U CN214880455U CN202121213288.2U CN202121213288U CN214880455U CN 214880455 U CN214880455 U CN 214880455U CN 202121213288 U CN202121213288 U CN 202121213288U CN 214880455 U CN214880455 U CN 214880455U
- Authority
- CN
- China
- Prior art keywords
- wastewater
- waste water
- solidification
- treatment
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides an integrated device for wastewater treatment, which comprises a wastewater solidification device, a solid waste treatment device which can treat wastewater solidification bodies obtained after the wastewater solidification device adsorbs and solidifies wastewater, and a gas purification device which can treat gas generated by the solid waste treatment device; wherein, a combustion device capable of combusting the wastewater solidified body is arranged in the solid waste treatment device; the solid waste treatment device is provided with an airflow outlet and a waste residue port, and the airflow outlet is communicated with the gas purification device and the waste water solidification device so that gas enters the gas purification device to be treated and enters the waste water solidification device to dry waste water solidification bodies. Through this integration equipment, the utility model discloses retrieval and utilization technology is ripe, rate of equipment utilization is high, and investment and operation maintenance cost are low, and have higher waste water treatment effect to it is higher to have solved among the prior art waste water treatment equipment investment and operation maintenance cost, and lower and the tail gas that produces of efficiency to waste water treatment brings secondary environmental pollution's problem.
Description
Technical Field
The utility model relates to a waste water treatment technical field, concretely relates to an integrated equipment for waste water treatment.
Background
At present, for sewage which is difficult to treat, such as high-concentration organic wastewater, inorganic wastewater, wastewater with over-standard heavy metal content, high-salinity wastewater and the like, physicochemical treatment is usually adopted in combination with biochemical control, and equipment comprising concentration, evaporative crystallization or concentration and flue evaporation is commonly used in the market for treating the high-concentration wastewater.
For example, chinese patent 201310355878.2 discloses a method for wastewater treatment using a mechanical compression evaporative crystallizer system, the method comprising the steps of: (1) pretreatment: carrying out early-stage biochemical, physicochemical and membrane filtration treatment on the petroleum drilling wastewater; (2) evaporation and crystallization: pumping the pretreated wastewater into a storage tank in a mechanical compression evaporation crystallization system, buffering the wastewater by a balance tank, then entering a heat exchanger for heat exchange with condensed water, raising the temperature of the material to 5-8 ℃ after heat exchange, entering a heater of an evaporation separation crystallization device for heating, feeding the material after the temperature reaches the boiling point, carrying out evaporation crystallization under the negative pressure of 300-90 mbar and the temperature of 80-90 ℃, carrying out high-speed separation on crystal slurry in a centrifuge, returning the separated saturated solution to the evaporation crystallization system for evaporation, and packaging the separated solid particles.
Chinese patent 201420660503.7 discloses an evaporative crystallization salt manufacturing equipment for high salt organic wastewater treatment, including the flash tank, it has first circulating water inlet and is located the circulating water outlet below the first circulating water inlet, the circulating water outlet with first circulating water inlet is connected by the circulating line, be provided with heating device on the circulating line, its characterized in that, evaporative crystallization salt manufacturing equipment still include with the bottom of flash tank is connected and the salt washing leg that link up, the salt washing leg further includes: an upper water inlet positioned in the salt washing leg and downward in the water inlet direction; a middle water inlet below the upper water inlet, the middle water inlet configured to impart a swirling flow to wastewater within the salt washing leg and a salt drain below the middle water inlet.
Although the equipment and the process can treat high-concentration wastewater, the investment and operation maintenance cost is high, the wastewater treatment efficiency is low, and the generated tail gas can cause secondary environmental pollution.
SUMMERY OF THE UTILITY MODEL
In view of this, the utility model provides an integrated equipment for waste water treatment, through solid useless ration throwing of solid useless processing apparatus after high temperature treatment to waste water solidification device in as the curing agent retrieval and utilization, and a part high-temperature gas that produces is introduced into waste water solidification device, stoving, fast solidification waste water with higher speed, other high-temperature flue gas is introduced into gas purification device through the air current export and is purified, final gas is discharged up to standard; the equipment has the advantages of simple structure, low investment and operation cost and higher wastewater treatment effect, and further solves the problems of higher investment and operation maintenance cost, lower wastewater treatment efficiency and secondary environmental pollution caused by generated tail gas in the prior art.
In order to achieve the above object, the present invention provides an integrated apparatus for wastewater treatment, which comprises a wastewater solidification device capable of adsorbing and solidifying wastewater, a solid waste treatment device capable of treating a wastewater solidification body obtained after the wastewater solidification device adsorbs and solidifies the wastewater, and a gas purification device capable of treating gas generated by the solid waste treatment device; a combustion device capable of combusting the wastewater solidified body is arranged in the solid waste treatment device; and the solid waste treatment device is provided with an airflow outlet and a waste residue port, and the airflow outlet is communicated with the gas purification device and the waste water solidification device so that gas enters the gas purification device for treatment and enters the waste water solidification device for drying the waste water solidification body.
Further, the waste residue port is communicated with the waste water solidifying device.
Further, the waste water solidification device is provided with an agitating component so that waste water can be adsorbed and solidified in an accelerated or sufficient mode.
Further, a first pipeline for gas circulation is arranged between the wastewater solidification device and the solid waste treatment device.
Further, a blowing device is arranged on the first pipeline.
Further, the airflow outlet is connected with a second pipeline, and the second pipeline is connected with the gas purification device along one end far away from the airflow outlet.
Further, at least one absorption compartment for process gas is provided within the gas cleaning device.
Further, the gas purification device is provided with an exhaust port for exhausting gas.
Further, the solid waste treatment device is a combustion boiler, and the waste residue port is arranged at the lower part of the combustion boiler.
Further, the gas purification apparatus is provided with a cooling device.
The utility model has the advantages that:
the utility model discloses utilize solid useless processing apparatus to adsorb the waste water solidification body that obtains behind the solidification waste water with waste water solidification device through high temperature scorching heat and fully pulverize, the solid useless ration that the burning obtained is thrown into waste water solidification device and is used as the curing agent retrieval and utilization, the partial high-temperature gas that produces of burning is reused in waste water solidification device and is dried waste water solidification body with higher speed, this process greatly reduced the medicament cost, reduced solidification waste water treatment cost, simultaneously make full use of the heat that the firing produced, promote waste water treatment efficiency; in addition, other high-temperature flue gas is introduced into the gas purification device for step-by-step purification, and finally the flue gas is discharged after reaching the standard, so that the problem of secondary pollution of tail gas is solved; therefore, the utility model discloses retrieval and utilization technology is ripe, equipment utilization is high, and investment and operation maintenance cost are low, have higher waste water treatment effect, and then solved investment and operation maintenance cost among the prior art higher, lower and the tail gas that produces of waste water treatment's efficiency brings secondary environmental pollution's problem.
Drawings
The following drawings are included to provide a further understanding of the invention, are incorporated in and constitute a part of this application, and are provided for illustrative purposes only and are not intended to limit the scope of the invention. In the drawings:
FIG. 1 is a schematic front view of an integrated wastewater treatment plant according to an embodiment of the present application;
FIG. 2 is a schematic top view of an integrated wastewater treatment facility according to an embodiment of the present application.
Reference numerals:
1. a wastewater solidification device; 2. a gas purification device; 3. a combustion boiler; 4. a solid waste transport vehicle; 5. an equipment support frame; 6. a first blower device; 7. a cooling device; 10. a first conduit; 11. a feed inlet; 12. a discharge port; 13. a feed switch; 14. a discharging switch; 15. a blender motor; 16. a helical agitator; 21. a primary absorption compartment; 211. primary filter sieve plate holes; 22. a secondary absorption compartment; 23. a tertiary absorption compartment; 231. A third-stage filter sieve plate hole; 24. an exhaust port; 30. a second conduit; 31. a waste residue port.
Detailed Description
The following embodiments of the present invention will be disclosed with reference to the drawings, and will be described in detail, and a part of the drawings constituting the present application is provided to further understand the present invention, and the exemplary embodiments and descriptions of the present invention are provided to explain the present invention, and do not constitute the improper limitation of the present invention, and all other embodiments obtained by the ordinary skilled person without creative labor in the field belong to the protection scope of the present invention.
It should be noted that, unless the directions indicated are individually defined, the directions of up, down, left, right, horizontal, vertical, etc. referred to herein are based on the directions of up, down, left, right, horizontal, vertical, etc. shown in fig. 2 of the embodiment of the present application, and if the specific posture is changed, the directional indication is changed accordingly. The terms "plurality," "plurality," and "a number" mean two or more, and are used herein collectively to describe "first," "second," and the like, and do not denote any order, quantity, or importance, but rather are used to distinguish one element from another. Further, in the various embodiments of the present disclosure, the same or similar reference numerals denote the same or similar components.
In the present invention, the terms "connected" and "fixed" are to be understood broadly, unless otherwise specifically defined and limited, for example, "fixed" may be fixedly connected, detachably connected, or integrated, unless otherwise specifically defined. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.
In addition, the technical solutions between the embodiments of the present invention can be combined with each other, but it is necessary to be able to be realized by a person having ordinary skill in the art as a basis, and when the technical solutions are contradictory to each other or cannot be realized, the combination of such technical solutions should be considered to be absent, and is not within the scope of the present invention.
Example one
Referring to fig. 1 and 2, an integrated apparatus for wastewater treatment in this embodiment includes a wastewater solidification device 1 capable of adsorbing and solidifying wastewater, a solid waste treatment device capable of treating a wastewater solidification body obtained after the wastewater solidification device adsorbs and solidifies the wastewater, and a gas purification device 2 capable of treating gas generated by the solid waste treatment device, wherein a combustion device capable of combusting the wastewater solidification body is arranged in the solid waste treatment device; the solid waste treatment device is provided with an airflow outlet and a waste residue port, and the airflow outlet is communicated with the gas purification device and the waste water solidification device so that gas enters the gas purification device for treatment and enters the waste water solidification device for drying a waste water solidification body.
In the present embodiment, a wastewater solidification precursor is provided in the wastewater solidification apparatus, and the wastewater solidification precursor can adsorb and solidify wastewater to obtain a wastewater solidified body. The waste water solidification precursor can be solid waste residue obtained after combustible substances are combusted or other substances capable of adsorbing waste water, and the solid waste residue is low in cost and even free of cost, so that the solid waste residue is preferred. In practical application, some drying agents and/or initial curing agents and the like can be further added into the wastewater curing precursor, and the wastewater adsorption and curing capacity is stronger after the drying agents and/or the initial curing agents are added, and certainly, the drying agents and/or the initial curing agents can be added or not added and determined according to actual conditions. In addition, waste water in this application can include multiple water samples such as organic waste liquid, inorganic waste water, heavy metal waste water that exceeds standard, high salt waste water. Solid waste residue that this application will give up processing apparatus burning waste water solidification body back production flows through the waste residue mouth and recycles in waste water solidification equipment 1, uses as the curing agent that is used for adsorbing solidification waste water, greatly reduced the medicament cost, and then reduced solidification waste water treatment's cost. Moreover, part of high-temperature gas generated by combustion of the solid waste treatment device enters the waste water solidification device through the airflow outlet to be used for accelerating drying of waste water solidified bodies, so that the equipment utilization rate and the waste water treatment efficiency are improved; the rest flue gas enters the gas purification device through the airflow outlet to be purified and then is discharged to the atmosphere after reaching the standard, so that the problem of secondary environmental pollution caused by tail gas is solved.
Example two
In this embodiment, as a further preferable embodiment, the waste residue port in this embodiment is communicated with the waste water solidifying apparatus 1 in addition to the first embodiment.
It should be noted that, in the embodiment, the solid waste generated after the solid waste treatment device burns the waste water solidified body flows out through the waste residue port and is quantitatively fed into the waste water solidification device under the control of the automatic control system, or the waste water solidified body generated after the waste water solidification device adsorbs and solidifies can also enter the solid waste treatment device through the waste residue port, so that the circular automatic management of the integrated equipment is realized, the waste water treatment efficiency is further improved, and the operation cost is saved. Certainly, according to actual conditions, can select waste residue mouth and waste water solidification equipment not direct intercommunication, the solid useless transport vechicle of accessible carries out manual transportation operation.
EXAMPLE III
In this embodiment, as a further preferable embodiment, on the basis of the first embodiment, the waste water solidifying apparatus 1 in this embodiment is provided with a feeding port 11, a discharging port 12 and a first pipeline 10, the combustion boiler 3 is provided with a waste residue port 31 and a second pipeline 30, the first pipeline 10 is connected with the second pipeline 30, and the second pipeline 30 is connected with the gas purifying apparatus 2. A first-stage absorption compartment 21, a second-stage absorption compartment 22 and a third-stage absorption compartment 23 are sequentially arranged in the gas purification device 2 from bottom to top; further, an exhaust port 24 is opened at the top of the gas purification apparatus 2. Further, a stirring component is arranged in the wastewater solidification device 1 in the embodiment.
It should be noted that the external structure of the wastewater solidification device 1 in this embodiment is a cone structure with a large top and a small bottom, and the adopted material is preferably made of high-temperature resistant stainless steel, and the first pipeline 10 and the second pipeline 30 are also preferably made of high-temperature resistant stainless steel; the combustion boiler 3 (solid waste treatment device) and the gas purification device 2 are made of carbon steel preferably, high-temperature-resistant coatings are arranged inside the devices, the service life is long, and the devices are generally free of problems for 5-8 years, so that the equipment replacement cost is reduced, and the investment cost is saved.
By using the technical scheme of the embodiment, firstly, water samples such as high-concentration organic waste liquid, inorganic waste water, heavy metal overproof waste water, high-salinity waste water and the like are filled into the waste water curing device 1 containing the drying agent, the initial curing agent and the ash slag body through the feed inlet for curing. And moreover, the drying agent, the initial curing agent and the wastewater are fully contacted through the stirring of the stirring assembly, the wastewater is rapidly cured under the drying action of high-temperature gas to form a wastewater cured body, and when the temperature reaches the safe temperature of a temperature measuring point, a professional takes out the wastewater cured body through the discharge hole 12. Secondly, the solid waste is transported to a combustion boiler 3 by a solid waste transport vehicle 4 for incineration, a waste water solidified body is fully pulverized by high-temperature scorching heat of the combustion boiler 3, the solid waste obtained by combustion is quantitatively fed into a waste water solidification device 1 to be reused as a solidification agent, and part of high-temperature gas generated by combustion is reused in the waste water solidification device 1 through a first pipeline 10 to accelerate drying and solidification of waste water, so that the medicament cost is greatly reduced, the treatment cost of solidification waste water is reduced, and the heat generated by ignition is fully utilized; in addition, the gas in the wastewater solidification device may flow into the second pipe through the first pipe. Other high-temperature flue gas is guided into the multi-stage absorption compartments in the gas purification device through the second pipeline for step-by-step purification and is discharged through the exhaust port after reaching the standard, so that the problem of secondary pollution of tail gas is solved; therefore, the utility model discloses retrieval and utilization technology is ripe, equipment utilization is high, and investment and operation maintenance cost are low, and have higher waste water treatment effect, and then solved investment and operation maintenance cost among the prior art higher, lower and the tail gas that produces of waste water treatment's efficiency brings secondary environmental pollution's problem.
It should be further noted that the drying agent and the initial curing agent filled in the wastewater curing apparatus 1 of this example are LTS-SF drying agent and LTS-CA curing agent, and the curing time is about 30 minutes. The LTS-CA drying agent is mainly prepared by polymerizing various high molecular compounds, can quickly solidify organic wastewater, is non-toxic and harmless, cannot bring new burden to a water body, and has certain flammability. The LTS-SF curing agent is in the form of fine solid particles, is formed by cooling after heat absorption of a hot surface under the condition of suspension combustion, has flammability, can quickly dry waste water, and has the characteristic of being reusable. After two kinds of series of medicaments enter sewage, inorganic mineral compositions in the product can quickly adsorb COD in various existing forms in the sewage to the surface of a material, the material is quickly solidified and dried, the COD is completely oxidized by high-temperature burning, and byproducts after oxidation exist in a solid form and do not cause unnecessary influence on other parameters. The effective removal rate of COD is up to more than 99 percent, and the method also has obvious effect on removing TP and TN. The effective volume of the combustion boiler 3 is preferably 0.5m3But not limited to, the volume can be selected according to actual conditions, and the solidified water sample can be sufficiently pulverized through a high-temperature reaction of 1 hr.
As a specific implementation manner, the first pipeline 10 of the present embodiment is provided with a first air blowing device 6, the first air blowing device is preferably an air blower with corresponding power, one end of the first pipeline 10 is connected to the lower part of the wastewater solidification device 1, which is beneficial for drying the solidified wastewater by the high-temperature gas, and the other end is connected to the second pipeline 30; furthermore, a second blower is arranged on the second pipeline 30, one end of the second pipeline 30 is connected to the top of the solid waste treatment device 3, and the other end is connected to the primary absorption compartment 21 at the lower part of the gas purification device 2.
It should be noted that the flow rate and the strength of the air flow can be controlled by the air blowing device, the first air blowing device guides part of the high-temperature gas generated by the combustion boiler 3 into the wastewater solidification device, and the temperature is controlled to be 50-55 ℃ according to the measured value of the temperature measuring point, so that the drying is accelerated, and the wastewater solidification efficiency is improved. The second blowing device guides the high-temperature flue gas and the peculiar smell generated in the curing process into the second pipeline 30, and the flue gas enters the gas purification device 2 to be collected and purified.
As a specific implementation manner, the feeding port 11 and the discharging port 12 in this embodiment are respectively disposed at the top and the bottom of the wastewater solidification device 1, and correspondingly, the wastewater solidification device 1 is provided with a feeding switch 13, a discharging switch 14 and a first temperature detector, the feeding switch 13 controls the opening or closing of the closing cover of the feeding port, and the discharging switch 14 controls the opening or closing of the closing cover of the discharging port, so that the system is intelligent and high in safety.
As a specific embodiment, the wastewater solidification device 1 in this embodiment is fixedly installed on the equipment support frame 5, and a space of the solid wastewater transport vehicle 4 is reserved below the discharge port 12.
As a specific embodiment, the solid waste treatment apparatus in this embodiment is a combustion boiler, the combustion boiler is provided with an ignition controller and a waste residue port 31, and the waste residue port 31 is provided on a side surface of a lower portion of the combustion boiler.
It should be noted that, the solid waste water is ignited by the ignition device inside the combustion boiler 3, and heating is provided if necessary to ensure complete slagging of the solid waste water, so as to be used as a curing agent, thereby saving the cost of the agent. The solid waste in the combustion boiler 3 is put into and taken out through the waste residue port 31, the sealing performance of the waste residue port is high, the second temperature detector is arranged at the position, the waste residue is cooled to 50 ℃ after high-temperature combustion and then taken out, and the safety of operators is ensured.
As a specific implementation manner, the number of the absorption compartments in this embodiment is 3 levels, which are the primary absorption compartment 21, the secondary absorption compartment 22, and the tertiary absorption compartment 23, and the primary filter sieve plate hole 211, the secondary filter sieve plate hole, and the tertiary filter sieve plate hole 231 for pre-filtering large-particle smoke are respectively opened on each absorption compartment.
It should be noted that the number of the absorption compartments in this embodiment is 3 stages, but is not limited to 3 stages, and may be more integer stages such as 2 stages, 4 stages, 5 stages, etc. according to the actual situation, preferably, the absorption compartments are purification dust collectors, and the dust collectors with corresponding mesh number and precision are selected according to the requirement of the actual filtration precision. In the embodiment, the large-particle smoke dust is pre-filtered through the arranged filter sieve plate holes; active carbon and other fillers are contained in each absorption compartment to absorb a large amount of smoke and peculiar smell, the smoke enters from the first-stage absorption compartment 21 of the gas purification device, is purified step by step through the third-stage absorption compartments from bottom to top, and is finally discharged from the exhaust port 24 at the top after reaching the standard.
As a specific embodiment, the gas purification apparatus 3 of the present embodiment is provided with a cooling apparatus 7 and a third temperature detector on one side, at least one cooling pipe 71 is connected to the cooling apparatus 7, and the cooling pipe 71 is connected to the inside of the gas purification apparatus.
It should be noted that the number of the cooling pipes in this embodiment is 2, but is not limited to 2, and may be set to be plural according to actual situations. The cooling water is sprayed out through the spray head by the booster pump on the cooling device, and the high-temperature flue gas is cooled under the control of the third temperature measurer, so that the use is convenient, and the safety is high.
To sum up, the working process of the utility model is explained as follows, firstly, water samples such as drying agent, initial curing agent, ash slag body, high-concentration organic waste liquid, inorganic waste water, heavy metal standard-exceeding waste water, high-salinity waste water and the like are filled into the waste water curing device 1 through the feed inlet. The drying agent, the initial curing agent and the wastewater are fully contacted through the stirring of the stirring assembly, the wastewater is rapidly cured under the drying action of high-temperature gas, and when the safe temperature of a temperature measuring point is reached, a professional takes out a cured water sample through the discharge hole 12. Secondly, the solid waste is transported to a combustion boiler 3 by a solid waste transport vehicle 4 to be burned, the solidified waste water is fully pulverized by high-temperature scorching heat of the combustion boiler 3, the solid waste obtained by burning is quantitatively fed into a waste water solidification device 1 to be reused as a solidifying agent, and part of high-temperature gas generated by burning is reused in the waste water solidification device 1 through a first pipeline 10 to accelerate drying and solidifying of the waste water, so that the medicament cost is greatly reduced, the solidification waste water treatment cost is reduced, and meanwhile, the heat generated by burning is fully utilized; in addition, other high-temperature flue gas is guided into a multi-stage absorption compartment in the gas purification device through a second pipeline for step-by-step purification and is discharged through an exhaust port after reaching the standard, so that the problem of secondary pollution of tail gas is solved; therefore, the utility model discloses retrieval and utilization technology is ripe, equipment utilization is high, and investment and operation maintenance cost are low, and have higher waste water treatment effect, and then solved investment and operation maintenance cost among the prior art higher, lower and the tail gas that produces of waste water treatment's efficiency brings secondary environmental pollution's problem.
While the above description shows and describes the preferred embodiments of the application, it is to be understood, as noted above, that the application is not limited to the forms disclosed herein, but is not intended to be exhaustive of other embodiments, and is capable of use in various other combinations, modifications, and environments and is capable of changes within the scope of the subject matter disclosed above, as determined by the teachings or knowledge of the relevant art. And that modifications and variations may be effected by those skilled in the art without departing from the spirit and scope of the application, which is to be protected by the claims appended hereto.
Claims (10)
1. The integrated equipment for wastewater treatment is characterized by comprising a wastewater solidification device (1) capable of adsorbing and solidifying wastewater, a solid waste treatment device capable of treating a wastewater solidification body obtained after the wastewater solidification device (1) adsorbs and solidifies the wastewater, and a gas purification device (2) capable of treating gas generated by the solid waste treatment device;
a combustion device capable of combusting the wastewater solidified body is arranged in the solid waste treatment device; and an airflow outlet and a waste residue port are arranged on the solid waste treatment device, and the airflow outlet is communicated with the gas purification device (2) and the waste water solidification device (1) so that gas enters the gas purification device (2) for treatment and enters the waste water solidification device (1) for drying the waste water solidification body.
2. An integrated plant for wastewater treatment according to claim 1, characterized in that the waste residue port communicates with the wastewater solidification device (1).
3. The integrated wastewater treatment facility of claim 1, wherein the wastewater solidification device is provided with an agitation assembly to accelerate or sufficiently adsorb and solidify the wastewater.
4. An integrated plant for the treatment of waste water according to claim 1, characterized in that a first conduit (10) for the passage of gas is provided between the solidification means of waste water and the solid waste treatment means.
5. An integrated plant for wastewater treatment according to claim 4, characterized in that said first pipe (10) is provided with blowing means.
6. An integrated plant for the treatment of waste water according to claim 1, characterized in that a second pipe (30) is connected to the gas flow outlet, said second pipe (30) being connected to the gas cleaning device (2) along the end remote from the gas flow outlet.
7. An integrated plant for wastewater treatment according to claim 1, characterized in that at least one absorption compartment for process gas is provided in said gas cleaning device (2).
8. The integrated apparatus for wastewater treatment according to claim 1, wherein the gas purification device (2) is provided with a gas outlet (24) for discharging gas.
9. An integrated apparatus for wastewater treatment according to claim 1, characterized in that the solid waste treatment device is a combustion boiler (3), and the waste residue port (31) is provided at a lower portion of the combustion boiler (3).
10. An integrated plant for wastewater treatment according to claim 1, characterized in that the gas cleaning device (2) is provided with a cooling device (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121213288.2U CN214880455U (en) | 2021-06-01 | 2021-06-01 | Integrated equipment for wastewater treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121213288.2U CN214880455U (en) | 2021-06-01 | 2021-06-01 | Integrated equipment for wastewater treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214880455U true CN214880455U (en) | 2021-11-26 |
Family
ID=78902266
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121213288.2U Active CN214880455U (en) | 2021-06-01 | 2021-06-01 | Integrated equipment for wastewater treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214880455U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113511694A (en) * | 2021-05-21 | 2021-10-19 | 南京乐透思环保科技有限公司 | Composite sponge material, preparation method thereof and application of composite sponge material in treatment of high-salinity and high-calorific-value wastewater |
-
2021
- 2021-06-01 CN CN202121213288.2U patent/CN214880455U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113511694A (en) * | 2021-05-21 | 2021-10-19 | 南京乐透思环保科技有限公司 | Composite sponge material, preparation method thereof and application of composite sponge material in treatment of high-salinity and high-calorific-value wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208406422U (en) | A kind of spray paint dust-removing waste gas purification integrated machine | |
| CN100563783C (en) | A kind of bitumen flue gas purifying method | |
| CN207102169U (en) | A kind of purification of chemical waste gas pipeline with cooling function | |
| CN100571842C (en) | A kind of improvement method and device of fish powder waste gases | |
| CN108787713B (en) | Method for treating medical waste based on flotation combined microwave method | |
| CN110508057A (en) | Exhaust gas purifying method and system in a kind of lithium battery removal process | |
| CN103599695B (en) | A kind of integrated treating device of organic exhaust gas and method | |
| CN102489280B (en) | Silica gel regenerator and renovation process | |
| CN214880455U (en) | Integrated equipment for wastewater treatment | |
| CN104976625B (en) | A kind of processing system and processing method of the organic phosphorus waste liquid of high concentration | |
| CN111112296B (en) | Resource utilization treatment method for industrial waste salt | |
| JP4051415B2 (en) | Garbage incineration, dust collection, neutralization, and catalytic reaction treatment equipment after incineration, post-catalyst fertilizer plant and its structure | |
| CN110257090A (en) | Division solves garbage carbonized processing system | |
| CN107606623B (en) | Small garbage gas-carbon complementary carbonization combustion furnace | |
| CN106076114B (en) | A kind of smoke processing system and method | |
| CN203710909U (en) | Integrated treatment device of organic waste gas | |
| CN112892168A (en) | Waste gas purification treatment device for lost foam casting | |
| CN206121512U (en) | Exhaust gas treatment system | |
| CN106139840A (en) | Purifier and method containing low concentration VOC waste gas | |
| CN210045064U (en) | Device for efficiently treating mercury-containing polluted soil thermal desorption waste gas | |
| CN202803043U (en) | Boiler smoke purifying device | |
| CN214094494U (en) | Waste incineration system | |
| CN103877795B (en) | Sintering flue gas dioxin and particulate matter synergism purification equipment and method | |
| CN111964083B (en) | Treatment equipment for treating component-complicated waste gas | |
| CN213207883U (en) | Digital intelligent control organic waste gas treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: Building 4, Phase II, Innovation and Entrepreneurship Education Park, Nanda Science Park, Yuanhua Road, Xianlin University Town, Xianlin Street, Qixia District, Nanjing, Jiangsu Province, 210000 Patentee after: Nanjing Letousi High tech Materials Technology Co.,Ltd. Address before: 210000 Room 197, Building 8, Yuanhua Road, Xianlin University, Xianlin Street, Qixia District, Nanjing City, Jiangsu Province Patentee before: NANJING LOTUS ENVIRONMENTAL SCIENCE & TECHNOLOGY CO.,LTD. |