CN117125862A - Comprehensive three-dimensional treatment device for medical wastewater and medical waste - Google Patents
Comprehensive three-dimensional treatment device for medical wastewater and medical waste Download PDFInfo
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- CN117125862A CN117125862A CN202311336571.8A CN202311336571A CN117125862A CN 117125862 A CN117125862 A CN 117125862A CN 202311336571 A CN202311336571 A CN 202311336571A CN 117125862 A CN117125862 A CN 117125862A
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Abstract
The invention discloses a comprehensive three-dimensional treatment device for medical wastewater and medical wastes, which comprises a wastewater treatment tank and a logic controller, wherein a waste treatment device is arranged at the outer side of the wastewater treatment tank, a high-pressure fan is arranged at the outer side of the waste treatment device, a high-pressure conditioning device is arranged outside the high-pressure fan, an ozone generating source is arranged at the outer side of the high-pressure conditioning device, a composite vacuum pump is arranged at the outer side of the ozone generating source, a sludge dewatering device is arranged at the outer side of the composite vacuum pump, the wastewater treatment tank comprises a pretreatment sedimentation tank and a pretreatment regulating tank, a regulating tank lifting device is arranged in the pretreatment regulating tank, a furnace body only has a single air inlet and an air outlet, the whole furnace body and a bottom biochemical reaction area are controlled to be in a micro negative pressure state by valves, all gases are discharged after being treated, no direct discharge channel is formed, and pathogens in the medical wastewater are effectively controlled to be spread through gas.
Description
Technical Field
The invention relates to a wastewater or waste treatment technology, in particular to a comprehensive three-dimensional treatment device for medical wastewater and medical waste.
Background
Medical waste is waste material produced by medical institutions such as hospitals and clinics, including hazardous waste, infectious waste, general waste, and other special waste. These wastes contain a large amount of pathogens and harmful substances, and if not properly treated, are liable to cause environmental pollution and public health safety risks. Meanwhile, the waste water discharged from hospitals also contains harmful substances such as microorganisms, residual medicines and the like, and can cause potential threats to the surrounding environment and human health. Thus, there are many benefits to disposing of medical waste together with hospital wastewater.
Pathogens such as viruses and bacteria can exist in wastes generated in hospitals, and the risk of cross infection can be effectively reduced by adopting common treatment measures. Through reasonable classification and treatment, the transmission degree of pathogens in the environment can be reduced, so that public health safety is ensured.
Secondly, in the aspect of germ control, the garbage and the wastewater are treated together, so that the cross infection or recontamination phenomenon caused by different treatment modes can be avoided. The hospital wastewater may contain residual medicinal substances, and if the hospital wastewater is discharged untreated at will, the hospital wastewater not only affects the system stability of sewage treatment facilities, but also can cause serious harm to the surrounding environment and ecological safety. Therefore, by adopting a complete treatment scheme and controlling related links such as dispersion, transfer, disposal and the like of medical waste and wastewater, cross infection can be prevented, and pollution of medical waste and wastewater to the environment is avoided.
In medical facilities, a large amount of medical waste water is generated, and a large amount of medical waste is also generated, so that the medical waste and the hospital waste water are treated together, which is an effective means for improving the public health management level of medical institutions, and is beneficial to pollution control and ecological protection.
Especially in the case of sudden public health events, it is of more importance to implement co-processing measures.
The following disadvantages mainly exist:
1. separate treatments increase transportation and handling costs. Because of the need to process in two different systems, hospitals require more time, labor and money to maintain these facilities, which can place more stress and burden on hospital management;
2. the separate treatment of medical waste and wastewater has hidden sanitary safety problems. A large amount of wastewater is discharged in the conventional medical waste treatment process, and pathogens or harmful elements of the wastewater can still exist when the wastewater is discharged into a sewage pipeline, so that the conventional downstream wastewater treatment process cannot be effectively treated, thereby not only increasing the complexity and cost of a downstream wastewater treatment system, but also having the risk of environmental pollution;
3. conventional separate disposal may also lead to repeated contamination of medical waste. In the process of transportation, due to improper operation, the medical waste is possibly mixed with other general household garbage, and even has the opportunity of being abandoned and poured into forbidden areas such as surrounding villages or rivers;
4. the supervision and management of medical wastes and wastewater are difficult. Because of the lack of integral planning and unified standards, the medical wastewater treatment station and the medical waste transfer station of the general medical institution respectively need special personnel to operate, which increases the environmental pollution and the cross infection risk to a certain extent;
5. the medical wastewater treatment station needs to clean and discharge the sludge periodically, and the waste codes in the part of sludge 'national hazardous waste directory' are 841-001-01, and the sludge needs to be transported and treated separately.
Therefore, to more scientifically and efficiently manage medical waste water and waste, a comprehensive treatment scheme can be adopted
Disclosure of Invention
The invention aims to provide a comprehensive three-dimensional treatment device for medical wastewater and medical waste, which aims to solve the problems in the background technology.
In order to achieve the above purpose, the present invention provides the following technical solutions:
the utility model provides a medical wastewater and medical waste's comprehensive three-dimensional processing apparatus, including sewage treatment pond and logic controller, the outside of sewage treatment pond is equipped with the waste treatment ware, the outside of waste treatment ware is equipped with high-pressure fan, high-pressure fan's peripheral hardware is equipped with high-pressure conditioning device, high-pressure conditioning device's outside is equipped with ozone generating source, ozone generating source's outside is equipped with the vacuum pump for the complex, the outside of vacuum pump for the complex is equipped with sludge dewatering device, the sewage treatment pond includes pretreatment sedimentation tank and pretreatment equalizing basin, be equipped with equalizing basin hoisting device in the pretreatment equalizing basin, the bottom of waste treatment ware is equipped with the catalytic reaction case, be equipped with the catalytic reaction pond in the catalytic reaction case, the inboard of catalytic reaction pond is equipped with the catalytic column bed, the below of catalytic column bed is equipped with oxidation aeration device, catalytic column bed's top is equipped with catalytic separation device, waste treatment ware's middle part is through hollow incineration division wall and is constituteed burning cavity and turbulent fog reaction case, medical waste burns in burning cavity, the air intake is controlled through logic controller, thereby control oxygen content in the stove temperature, with the turbulent flow temperature control is 850 degrees, the top of turbulent flow is equipped with the top surface of the biochemical reactor of the top surface of the biochemical reactor, the top surface of the waste treatment ware is equipped with the hollow air-circulating device.
As a further scheme of the invention: the catalytic reaction box is internally provided with two, four, six or eight grids according to the inner part of the treatment capacity, the vacuum pump for compounding is communicated with one grid through a pipeline, a valve is connected on the pipeline, and the pipeline is inserted into the corresponding grid and is fixedly connected with a sewage receiving disc.
As still further aspects of the invention: the front side of burning cavity is equipped with the feed inlet, and feed inlet department is equipped with rotatory feeding sealing door, and the below of feed inlet is equipped with puts the thing platform, and the top of feed inlet is equipped with the flue gas and collects the cover, and the flue gas is collected the cover and is passed through the top intercommunication of pipeline and waste disposer, is equipped with the valve on the pipeline.
As still further aspects of the invention: the high-pressure conditioning device is used for mixing and drying ozone and is internally provided with an ion generator.
As still further aspects of the invention: the sludge dewatering device is communicated with the gap between the air-flow biochemical bed and the air-flow oxidation bed through a pipeline, the sludge dewatering device is communicated with the composite vacuum pump through a pipeline, a valve is arranged on the pipeline, the composite vacuum pump is respectively communicated with the bottom of the pretreatment sedimentation tank and the two sides of the catalytic separation device through the pipeline, the valve is arranged on the pipeline, a short circuit pipeline is arranged on the outer side of the composite vacuum pump, the short circuit pipeline is respectively connected with the inlet and outlet of the composite vacuum pump, and the valve is arranged on the short circuit pipeline.
As still further aspects of the invention: the ozone generating source is communicated with the high-pressure conditioning device through a pipeline, a valve is arranged on the pipeline, an air inlet is formed in the high-pressure conditioning device, the valve is arranged on the air inlet, the high-pressure conditioning device is simultaneously communicated with the air flow biochemical bed and the high-pressure fan through the pipeline, the valve is arranged on the pipeline, the high-pressure fan is respectively communicated with the turbulent flow mist reaction box and the oxidation aeration device through the pipeline, and the valves are arranged on the pipeline.
As still further aspects of the invention: the circulating fan is communicated with the top of the waste processor through a pipeline, the circulating fan is communicated with an external smoke exhaust chimney through a pipeline, a valve is arranged on the pipeline, and the top end of the external smoke exhaust chimney is provided with the valve.
Compared with the prior art, the invention has the beneficial effects that:
the internal gas circulation mode is adopted to control the internal oxygen supply to control the consumption of incineration oxygen, thereby controlling the temperature.
The furnace body only has a single air inlet and an air outlet, the whole furnace body and the biochemical reaction area at the bottom are controlled to be in a micro negative pressure state by utilizing the valve, all gases are discharged after being treated, no direct discharge channel exists, and pathogens in medical wastewater are effectively controlled to be transmitted through the gas.
The incineration heat is utilized to increase the raw water temperature, so that the applicability of the equipment in alpine regions is improved.
The water is used for cooling the furnace body, so that the heat insulation material of the furnace body is reduced, the structure of the furnace body is simplified, and the temperature of the combustion environment can be controlled.
The device can simultaneously treat medical sewage and medical garbage, realize the up-to-standard discharge of flue gas and sewage simultaneously, can be used for emergency medical conditions, can also be used for remote small-scale medical facilities, and reduces the influence of medical sewage on the surrounding environment and the secondary diffusion of pollutants caused by long-distance transportation of medical wastes.
Drawings
Fig. 1 is a schematic structural view of an integrated three-dimensional treatment device for medical wastewater and medical waste.
FIG. 2-1 is a top perspective view of a single catalytic bed in an integrated stereoscopic treatment device for medical wastewater and medical waste.
Fig. 2-2 is a top perspective view of a single catalytic bed in an integrated stereoscopic treatment device for medical wastewater and medical waste.
FIG. 3 is a perspective schematic view of a hollow flow biochemical bed of a comprehensive three-dimensional treatment device for medical wastewater and medical waste.
In the figure: 1. pretreating a sedimentation tank; 2. pretreatment regulating tank; 3. an adjusting pool lifting device; 4. a catalytic reaction tank; 5. a catalytic bed; 6. an oxidation aeration device; 7. a catalytic separation device; 8. an incineration cavity; 9. a storage table; 10. rotating a feed seal door; 11. a fume collection hood; 12. an air flow biochemical bed; 13. an air flow oxidation bed; 14. a pneumatic atomizer; 15. turbulent mist-liquid reaction box; 16. a high-pressure fan; 17. a high pressure conditioning device; 18. an ozone generating source; 19. a vacuum pump for compounding; 20. a catalytic reaction box; 21. an exhaust chimney; 22. hollow incineration partition walls; 23. a circulating fan; 24. a logic controller; 25. a sludge dewatering device; 26. a sewage treatment tank; 27. a waste disposer; 28. a dirt receiving tray.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Referring to fig. 1-3, in the embodiment of the invention, a comprehensive three-dimensional treatment device for medical wastewater and medical waste comprises a wastewater treatment tank 26 and a logic controller 24, wherein a waste treatment device 27 is arranged at the outer side of the wastewater treatment tank 26, a high-pressure fan 16 is arranged at the outer side of the waste treatment device 27, a high-pressure conditioning device 17 is arranged outside the high-pressure fan 16, the high-pressure conditioning device 17 is used for mixing and drying ozone, an ion generator is arranged in the high-pressure conditioning device 17, an ozone generating source 18 is arranged at the outer side of the ozone generating source 18, a composite vacuum pump 19 is arranged at the outer side of the ozone generating source 18, a sludge dewatering device 25 is arranged at the outer side of the composite vacuum pump 19, the wastewater treatment tank 26 comprises a pretreatment sedimentation tank 1 and a pretreatment regulating tank 2, a regulating tank lifting device 3 is arranged in the pretreatment regulating tank 2, a catalytic reaction tank 20 is arranged at the bottom of the waste treatment device 27, a catalytic reaction tank 4 is arranged in the catalytic reaction tank 20, the inside of the catalytic reaction tank 4 is provided with a catalytic bed 5, an oxidation aeration device 6 is arranged below the catalytic bed 5, a catalytic separation device 7 is arranged above the catalytic bed 5, a liquid outlet is arranged above the catalytic separation device 7, the upper part of the catalytic separation device 7 is connected with a burner in the burning cavity 8 through a pipeline for cooling, the middle part of a waste processor 27 is divided into the burning cavity 8 and a turbulent mist reaction tank 15 through a hollow burning partition wall 22, medical waste is burned in the burning cavity 8, air inflow is controlled by a logic controller 24, so that oxygen content is controlled, the temperature in a furnace is controlled, the temperature of a reactor core is controlled at 850 ℃, the top of the turbulent mist reaction tank 15 is provided with an air flow oxidation bed 13, the middle part of the turbulent mist reaction tank 15 is provided with a pneumatic atomizer 14, the top of the waste processor 27 is provided with an air flow biochemical bed 12, the top surface of the waste disposer 27 is provided with an exhaust stack 21 and a circulation blower 23.
The catalytic reaction box 20 is internally provided with two, four, six or eight grids according to the inner part of the treatment capacity, the vacuum pump 19 for compounding is communicated with one grid through a pipeline, a valve is connected on the pipeline, and the pipeline is inserted into the corresponding grid and is fixedly connected with the sewage receiving disc 28.
The front side of burning cavity 8 is equipped with the feed inlet, and feed inlet department is equipped with rotatory feeding sealing door 10, and the below of feed inlet is equipped with puts thing platform 9, and the top of feed inlet is equipped with flue gas collection cover 11, and flue gas collection cover 11 passes through the top intercommunication of pipeline and waste disposer 27, is equipped with the valve on the pipeline.
The sludge dewatering device 25 is communicated with the gap between the air-flow biochemical bed 12 and the air-flow oxidation bed 13 through a pipeline, the sludge dewatering device 25 is communicated with the composite vacuum pump 19 through a pipeline, a valve is arranged on the pipeline, the composite vacuum pump 19 is respectively communicated with the bottom of the pretreatment sedimentation tank 1 and the two sides of the catalytic separation device 7 through the pipeline, the pipeline is provided with the valve, the outer side of the composite vacuum pump 19 is provided with a short circuit pipeline, the short circuit pipeline is respectively connected with the inlet and outlet of the composite vacuum pump 19, and the short circuit pipeline is provided with the valve. The ozone generating source 18 is communicated with the high-pressure conditioning device 17 through a pipeline, a valve is arranged on the pipeline, an air inlet is arranged on the high-pressure conditioning device 17, the valve is arranged on the air inlet, the high-pressure conditioning device 17 is simultaneously communicated with the air flow biochemical bed 12 and the high-pressure fan 16 through the pipeline, the valve is arranged on the pipeline, the high-pressure fan 16 is respectively communicated with the turbulent mist reaction box 15 and the oxidation aeration device 6 through the pipeline, and the valves are arranged on the pipeline. The circulating fan 23 is communicated with the top of the waste processor 27 through a pipeline, the circulating fan 23 is communicated with the exhaust chimney 21 through a pipeline, a valve is arranged on the pipeline, and the top end of the exhaust chimney 21 is provided with a valve.
The catalytic reaction box 20 and the incineration chamber 8 can be horizontally connected to form a waste processor 27, and can be placed on the ground or buried.
The working principle of the invention is as follows:
in the water treatment process, hospital sewage is collected to a septic tank for digestion and deslagging, flows to a pretreatment section at the front end of the equipment through a pipe network, and is subjected to pretreatment sedimentation tank 1, and suspended matters in the sewage are further removed through dosing or sludge reflux.
The pretreated sewage enters a pretreatment regulating tank 2, a regulating tank lifting device 3 is arranged in the pretreatment regulating tank 2, and the water inflow of the device is regulated according to the requirement.
The sewage pumped by the regulating reservoir lifting device 3 enters the catalytic reaction box 20 from the bottom of the waste processor 27, and the water distribution in the catalytic reaction box 20 is stopped after reaching a certain liquid level by controlling the water inlet and outlet of different grids through the logic controller 24 according to the two grids, four grids, six grids or eight grids of the inner part of the treatment capacity.
The sewage entering the catalytic reaction box 20 is uniformly distributed through the water distribution pipe in the catalytic bed 5, and the water passes through the oxidation catalytic filler in the catalytic bed 5, and meanwhile, the logic controller 24 controls the inlet valve of the high-pressure fan 16 to enable the oxidation aeration device 6 to be exposed to gas with a certain ozone concentration, and the dispersed ozone gas is subjected to oxidation reaction, so that COD (chemical oxygen demand) in the sewage and other reducing pollutants are effectively removed to generate water, carbon dioxide, oxygen and part of other harmless gases, and meanwhile, viruses and escherichia coli in the sewage are killed by utilizing the strong oxidizing property of the ozone. The catalytic packing in the catalytic bed 5 has the effects of increasing the reaction time for ozone interception and increasing the reactivity and physical filtration for different pollutants after the surface modification of the catalyst.
The sewage passing through the catalytic reaction box 20 gradually rises to the upper catalytic separation device 7, and the catalytic separation device 7 separates the gas and the liquid in the sewage by utilizing the difference of the gas and the liquid densities. Then, aeration is suspended, and the liquid-solid two phases in the sewage are separated according to the shallow precipitation theory. Finally, the water level is lifted through the water inlet at the bottom, the treated sewage reaching the standard is lifted and discharged to a municipal pipe network or recycled to the inside of the upper incineration cavity 8 for cooling, dedusting and carbon source supplementing.
Mud is discharged from the bottom of the catalytic separation device 7: the water inlet of a certain reaction lattice in the catalytic reaction box 20 is stopped, the valve is controlled by the logic controller 24 to pause aeration, the liquid-solid two phases are separated, the bottom sludge is pumped to the sludge dewatering device 25 through the composite vacuum pump 19, and the sludge is packed after being squeezed and sent to the incineration cavity 8 for incineration treatment.
Backwash of the catalytic bed 5: the water inlet of a certain reaction lattice in the catalytic reaction box 20 is stopped, the vacuum pump 19 for compounding and the front end valve are controlled by the logic controller 24 to suck the reaction lattice, and the water flow direction in the catalytic bed 5 flows reversely under pressure at the moment, so that internal trapped matters are removed.
The garbage treatment process comprises the following steps:
medical waste in hospitals is transported to the treatment device after being packed, is placed on the object placing table 9, and then the rotary feeding sealing door 10 is opened at regular time according to the treatment capacity, so that the medical waste is pulled into the incineration cavity 8, and meanwhile, the leakage of smoke can be effectively prevented. The sealing material can be selected from elastic thin steel plates and flexible flame-retardant materials; medical waste is combusted in the incineration cavity 8, and air inflow is controlled by the logic controller 24, so that the oxygen content is controlled, the temperature in the furnace is further controlled, and the temperature of the reactor core is controlled at 850 ℃.
The waste gas generated by combustion enters the turbulent mist reaction box 15 from the bottom of the flue, the high-pressure fan 16 sprayed by the fan pressure and the logic controller 24 are used for controlling the high-pressure conditioning device 17 to mix with ozone with a certain concentration, the gas-liquid mixture sprayed by the gas pressure (ozone + air + waste gas) generates turbulent flow to fully react, the turbulent flow state is formed at the lower part of the turbulent mist reaction box 15, and fly ash and particulate matters in the waste gas are removed after the upper part is stabilized by the folded plate to stabilize the flow, so that the temperature of the waste gas is reduced.
The reacted gas enters into the air flow oxidation bed 13, and further carries out catalytic reaction with the waste gas under the action of the catalyst carried by the bed body, and simultaneously further reduces the temperature of the gas.
The waste gas after temperature reduction enters the air flow biochemical bed 12, and a small amount of sewage is sprayed from the upper part on the reaction bed, so that a sufficient amount of carbon sources are provided for the reaction on the biochemical bed, and most of the air flow biochemical bed 12 has low oxygen content of the combustion waste gas, and the oxidation bed at the front end is externally added with excessive oxidation reaction, the chemical potential of the oxidation bed is high, and the reduction reaction is easy to occur, so that the microorganism in the air flow biochemical bed 12 and the nitrogen oxide compound in the waste gas perform denitrification reaction in the anaerobic environment, and the carrier of the air flow biochemical bed 12 serves as the biological bed to provide a sufficient reaction point. The reacted gas is partially discharged, and part of the gas is used as a gas source of the high-pressure fan 16 to be further mixed with ozone and air, and enters the catalytic reaction box 20 and the incineration cavity 8 for reaction.
Circulation fan 23 action: when the outlet gas is detected to be not up to standard, the circulating fan 23 can be started to dilute the inlet gas, so that the nitrogen load of the air flow biochemical bed 12 is reduced.
The incineration cavity 8 is made of carbon steel, a hollow structure is arranged inside the incineration cavity, sewage reaching the standard is filled into the bottom of the hollow structure by the composite vacuum pump 19, circulating water is used for cooling the box, and meanwhile, the circulating water can partially flow back into the box to heat raw water, so that the temperature in the catalytic reaction box 20 is increased.
Sludge generated by the catalytic reaction tank 20 and ash slag generated by the turbulent mist reaction tank 15 are deposited by the pretreatment deposition tank 1, and then are pumped to the sludge dewatering device 25 by the composite vacuum pump 19 under the control of the logic controller 24, and are packaged and sent to the incineration cavity 8 for incineration treatment.
Although the present invention has been described with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described, or equivalents may be substituted for elements thereof, and any modifications, equivalents, improvements and changes may be made without departing from the spirit and principles of the present invention.
Claims (7)
1. The utility model provides a medical wastewater and medical waste's comprehensive three-dimensional processing apparatus, includes sewage treatment pond (26) and logic controller (24), its characterized in that: the sewage treatment tank (26) is provided with a waste treatment device (27) on the outer side, the waste treatment device (27) is provided with a high-pressure fan (16) on the outer side, a high-pressure conditioning device (17) is arranged outside the high-pressure fan (16), an ozone generating source (18) is arranged on the outer side of the high-pressure conditioning device (17), a vacuum pump (19) for compounding is arranged on the outer side of the ozone generating source (18), a sludge dewatering device (25) is arranged on the outer side of the vacuum pump (19) for compounding, the sewage treatment tank (26) comprises a pretreatment sedimentation tank (1) and a pretreatment regulating tank (2), a regulating tank lifting device (3) is arranged in the pretreatment regulating tank (2), a catalytic reaction tank (20) is arranged at the bottom of the waste treatment device (27), a catalytic reaction tank (4) is arranged in the catalytic reaction tank (20), a catalytic column bed (5) is arranged on the inner side of the catalytic reaction tank (4), an oxidation aeration device (6) is arranged below the catalytic column bed (5), a catalytic separation device (7) is arranged above the catalytic column bed (5), the middle part of the waste treatment device (27) is divided into a cavity (8) through a hollow incineration separating wall (22) and a turbulent flow (13) by a turbulent flow (15), the middle part of turbulent fog liquid reaction box (15) is equipped with pneumatic atomizer (14), and the top of waste disposer (27) is equipped with empty biochemical bed (12), and the top surface of waste disposer (27) is equipped with outer chimney (21) and circulating fan (23).
2. The integrated three-dimensional treatment device for medical wastewater and medical waste according to claim 1, wherein: the catalytic reaction box (20) is internally provided with two, four, six or eight grids according to the inner part of the treatment capacity, the vacuum pump (19) for compounding is communicated with one grid through a pipeline, a valve is connected on the pipeline, and the pipeline is inserted into the corresponding grid and is fixedly connected with a sewage receiving disc (28).
3. The integrated three-dimensional treatment device for medical wastewater and medical waste according to claim 1, wherein: the front side of burning cavity (8) is equipped with the feed inlet, and feed inlet department is equipped with rotatory feeding sealing door (10), and the below of feed inlet is equipped with puts thing platform (9), and the top of feed inlet is equipped with flue gas collection cover (11), and flue gas collection cover (11) are through the top intercommunication of pipeline with waste treatment ware (27), are equipped with the valve on the pipeline.
4. The integrated three-dimensional treatment device for medical wastewater and medical waste according to claim 1, wherein: the high-pressure conditioning device (17) is used for mixing and drying ozone and is internally provided with an ion generator.
5. The integrated three-dimensional treatment device for medical wastewater and medical waste according to claim 1, wherein: the sludge dewatering device (25) is communicated with a clearance between the air flow biochemical bed (12) and the air flow oxidation bed (13) through a pipeline, the sludge dewatering device (25) is communicated with the vacuum pump (19) for compounding through a pipeline, a valve is arranged on the pipeline, the vacuum pump (19) for compounding is respectively communicated with the bottom of the pretreatment sedimentation tank (1) and the two sides of the catalytic separation device (7) through a pipeline, the valve is arranged on the pipeline, a short circuit pipeline is arranged on the outer side of the vacuum pump (19) for compounding, and the valve is arranged on the short circuit pipeline.
6. The integrated three-dimensional treatment device for medical wastewater and medical waste according to claim 1, wherein: the ozone generating source (18) is communicated with the high-pressure conditioning device (17) through a pipeline, a valve is arranged on the pipeline, an air inlet is formed in the high-pressure conditioning device (17), the valve is arranged on the air inlet, the high-pressure conditioning device (17) is simultaneously communicated with the air flow biochemical bed (12) and the high-pressure fan (16) through the pipeline, the valve is arranged on the pipeline, the high-pressure fan (16) is respectively communicated with the turbulent mist reaction box (15) and the oxidation aeration device (6) through the pipeline, and the valves are all arranged on the pipeline.
7. The integrated three-dimensional treatment device for medical wastewater and medical waste according to claim 1, wherein: the circulating fan (23) is communicated with the top of the waste processor (27) through a pipeline, the circulating fan (23) is communicated with the exhaust chimney (21) through a pipeline, a valve is arranged on the pipeline, and the top end of the exhaust chimney (21) is provided with a valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311336571.8A CN117125862A (en) | 2023-10-16 | 2023-10-16 | Comprehensive three-dimensional treatment device for medical wastewater and medical waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202311336571.8A CN117125862A (en) | 2023-10-16 | 2023-10-16 | Comprehensive three-dimensional treatment device for medical wastewater and medical waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN117125862A true CN117125862A (en) | 2023-11-28 |
Family
ID=88856628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202311336571.8A Pending CN117125862A (en) | 2023-10-16 | 2023-10-16 | Comprehensive three-dimensional treatment device for medical wastewater and medical waste |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN117125862A (en) |
-
2023
- 2023-10-16 CN CN202311336571.8A patent/CN117125862A/en active Pending
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