CN218833202U - Energy-saving high-temperature high-pressure moist heat sterilizer - Google Patents
Energy-saving high-temperature high-pressure moist heat sterilizer Download PDFInfo
- Publication number
- CN218833202U CN218833202U CN202223082456.6U CN202223082456U CN218833202U CN 218833202 U CN218833202 U CN 218833202U CN 202223082456 U CN202223082456 U CN 202223082456U CN 218833202 U CN218833202 U CN 218833202U
- Authority
- CN
- China
- Prior art keywords
- water
- water tank
- bottom plate
- energy
- vacuum pump
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
The utility model belongs to the technical field of the steriliser, especially, an energy-saving high temperature high pressure moist heat steriliser, comprising a base plate, the mounting bracket, be provided with the sterilization boiler on the mounting bracket, be provided with the water softener on the bottom plate, it is provided with first water tank to be close to the water softener on the bottom plate, first water tank top is provided with the second water tank, be provided with steam boiler on the bottom plate, steam boiler one side is provided with heat exchanger, be provided with the vacuum pump on the bottom plate, it is provided with biofilter to be close to heat exchanger on the bottom plate, bottom plate one side is provided with the radiator, it is provided with circulating water pump to be close to the vacuum pump on the bottom plate, be provided with the gas-liquid separation jar on the bottom plate. The utility model discloses a steam boiler, sterilization boiler, biofilter, heat exchanger, water circulation vacuum pump, first water tank, second water tank, water pump, water filter, vapour and liquid separator, waste water and energy consumption that the reduction steriliser that can very big degree produced in the course of the work, the complete inner loop of water resource of system itself does not need additionally to add the water source again.
Description
Technical Field
The utility model relates to a sterilizer technical field specifically is an energy-saving high temperature high pressure damp and hot sterilizer.
Background
The non-incineration type high-temperature sterilizer commonly used in the market is mainly divided into a microwave high-temperature type and a high-temperature high-pressure damp-heat type. Among them, the autoclave has become an excellent sterilization technique recognized in the industry due to its excellent stability and broad spectrum. However, the traditional high-temperature and high-pressure sterilizer not only needs an external water source and generates a large amount of wastewater, but also needs a high-power steam generator and has extremely large energy consumption in the working process. The utility model discloses take the condition of water and take the electricity to the sterilizer and carry out redesign, be applicable to the sterilizer that adopts high temperature high pressure technique to disinfect.
SUMMERY OF THE UTILITY MODEL
The utility model provides a not enough to prior art, the utility model provides an energy-saving high temperature high pressure moist heat sterilizer has solved the traditional high temperature high pressure sterilizer that exists now and not only needs external water source in the course of the work, produces a large amount of waste water, needs powerful steam generator moreover, also very big problem to the consumption of the energy.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides an energy-saving high temperature high pressure moist heat sterilizer, includes bottom plate, mounting bracket, be provided with sterilization boiler on the mounting bracket, be provided with the water softener on the bottom plate, it is provided with first water tank to be close to the water softener on the bottom plate, first water tank top is provided with the second water tank, be provided with steam boiler on the bottom plate, steam boiler one side is provided with heat exchanger, be provided with the vacuum pump on the bottom plate, it is provided with biological filter to be close to heat exchanger on the bottom plate, bottom plate one side is provided with the radiator, it is provided with circulating water pump to be close to the vacuum pump on the bottom plate, be provided with the gas-liquid separation jar on the bottom plate, first water tank top is close to the second water tank and is provided with the active carbon and removes the flavor case, the active carbon removes the last negative-pressure fan that is provided with of flavor case, radiator one side is provided with the water pump, water filter is provided with to water pump one side.
As an optimal technical solution of the utility model: the mounting bracket is fixedly mounted on the bottom plate, and the sterilization boiler is fixedly mounted on the mounting bracket.
As an optimal technical solution of the utility model: the water softener is communicated with the second water tank through a pipeline, and the second water tank is fixedly mounted on the first water tank and communicated with the first water tank.
As an optimal technical solution of the utility model: the steam boiler is connected with the first water tank through corresponding pipelines, and the vacuum pump is connected with the second water tank.
As an optimal technical solution of the utility model: one end of the biological filter is connected with the sterilization boiler through a corresponding pipeline, and the heat exchanger is communicated with the biological filter.
As a preferred technical solution of the utility model: the heat exchanger is connected with the vacuum pump through corresponding pipelines, the radiator is communicated with the vacuum pump through a pipeline, the water pump is connected with the radiator, the output end of the water filter is communicated with the first water tank, and the input end of the water filter is connected with the output end of the water pump.
As a preferred technical solution of the utility model: the input end of the gas-liquid separation tank is communicated with the heat exchanger, the output end of the gas-liquid separation tank is communicated with the activated carbon odor removal box, the negative pressure fan is fixedly installed at the top of the activated carbon odor removal box, the input end of the negative pressure fan is communicated with the inside of the activated carbon odor removal box, the input end of the circulating water pump is communicated with the first water tank, and the output end of the circulating water pump is connected with the radiator through a corresponding pipeline.
Compared with the prior art, the utility model provides an energy-saving high temperature high pressure damp and hot sterilizer possesses following beneficial effect:
the energy-saving high-temperature high-pressure moist heat sterilizer is provided with a steam boiler, a sterilization boiler, a biological filter, a heat exchanger, a water circulation vacuum pump, a first water tank, a second water tank, a water pump, a water filter and a gas-liquid separator, wherein the first water tank and the second water tank are added to a water level line before use, clean water enters the steam boiler from the first water tank for pressurization and heating, and then enters the sterilization boiler for multiple times of pulse heating; after hot gas extracted in the pulsating heating process is filtered by the biological filter, residual heat is conveyed to the first water tank again through the heat exchanger. The water temperature in the first water tank can gradually rise along with repeated work of the sterilizer, so that the energy consumption required by the heating of the steam boiler is reduced. A water circulation vacuum pump for supporting pulsating heating, wherein a water source of the water circulation vacuum pump is provided by a second water tank (because the water temperature exceeds 45 ℃ and generates an air chamber in the vacuum pump to influence the work of the vacuum pump, the water source required by the water circulation vacuum pump cannot be consistent with the water source of a steam boiler); the water circulation vacuum pump can generate 20-40L of waste water after a complete sterilization process, the waste water generated by the water circulation vacuum pump and condensate generated after the sterilization process are subjected to gas-liquid separation by a gas-liquid separator, the separated waste water is filtered by a water filter and then is subjected to secondary filtration by a biological filter. The treated wastewater enters a water circulation cooler, is cooled by a fan for a sterilization period (about 45 minutes) to bring the temperature to room temperature, and is then re-injected into a second water tank by a water pump to be used by a water circulation vacuum pump. After a plurality of sterilization processes, the water in the second water tank exceeds the water level line of the second water tank, and redundant water enters the first water tank through the overflow port of the second water tank to supplement the water consumption generated by the condensate in the sterilization boiler.
Wherein the pulse heating is to pump out air in the sterilization boiler through a water circulation vacuum pump to form negative pressure. And opening a steam valve, and injecting high-temperature and high-pressure steam generated by the steam generator into the sterilization boiler to form a high-temperature and high-pressure environment in the sterilization boiler. Repeating the steps to achieve the effect of killing bacteria.
Through above scheme can be very big degree reduce waste water and the energy consumption that the sterilizer produced in the course of the work, the complete internal circulation of water resource of system itself does not need additionally to add the water source again.
Drawings
FIG. 1 is a schematic view of the overall structure of one side of the present invention;
FIG. 2 is a schematic view of the overall structure of the other side of the present invention;
FIG. 3 is a schematic top view of the present invention;
fig. 4 is a frame diagram of the operation flow of the present invention.
In the figure: 1. sterilizing the boiler; 2. a water softener; 3. a first water tank; 4. a second water tank; 5. a steam boiler; 6. a heat exchanger; 7. a vacuum pump; 8. a biological filter; 9. a heat sink; 10. a circulating water pump; 11. a gas-liquid separation tank; 12. an activated carbon odor removal box; 13. a negative pressure fan; 14. a water pump; 15. a water filter; 16. a base plate; 17. and (7) mounting frames.
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. 1-4, in the present embodiment: the utility model provides an energy-saving high temperature high pressure moist heat sterilizer, comprising a base plate 16, a mounting bracket 17, be provided with sterilization boiler 1 on the mounting bracket 17, be provided with water softener 2 on the bottom plate 16, be provided with first water tank 3 near water softener 2 on the bottom plate 16, first water tank 3 top is provided with second water tank 4, be provided with steam boiler 5 on the bottom plate 16, steam boiler 5 one side is provided with heat exchanger 6, be provided with vacuum pump 7 on the bottom plate 16, be provided with biofilter 8 near heat exchanger 6 on the bottom plate 16, bottom plate 16 one side is provided with radiator 9, be provided with circulating water pump 10 near vacuum pump 7 on the bottom plate 16, be provided with gas-liquid separation jar 11 on the bottom plate 16, it removes flavor case 12 to be provided with the active carbon near second water tank 4 above the first water tank 3, be provided with negative-pressure fan 13 on the active carbon removes flavor case 12, radiator 9 one side is provided with water pump 14, water filter 15 is provided with on one side of water pump 14.
In the embodiment, the mounting rack 17 is fixedly mounted on the bottom plate 16, the sterilizing boiler 1 is fixedly mounted on the mounting rack 17, and garbage needing to be sterilized can be conveniently placed through the sterilizing boiler 1; the water softener 2 is communicated with the second water tank 4 through a pipeline, the second water tank 4 is fixedly arranged on the first water tank 3 and is communicated with the first water tank 3, and purified water can be softened through the water softener 2; the steam boiler 5 is connected with the first water tank 3 through corresponding pipelines, the vacuum pump 7 is connected with the second water tank 4, and high-temperature steam can be generated through the steam boiler 5 to sterilize the garbage in the sterilization boiler 1; one end of the biological filter 8 is connected with the sterilizing boiler 1 through a corresponding pipeline, the heat exchanger 6 is communicated with the biological filter 8, filtering can be carried out through the biological filter 8, and heat exchange can be carried out through the heat exchanger 6; the heat exchanger 6 is connected with the vacuum pump 7 through a corresponding pipeline, the radiator 9 is communicated with the vacuum pump 7 through a pipeline, the water pump 14 is connected with the radiator 9, the output end of the water filter 15 is communicated with the first water tank 3, the input end of the water filter 15 is connected with the output end of the water pump 14, waste water generated by the vacuum pump 7 can be stored and radiated through the radiator 9, and the waste water in the radiator 9 can be filtered and then conveyed to the first water tank 3 through the water pump 14 and the water filter 15 to form circulation; the input end of a gas-liquid separation tank 11 is communicated with a heat exchanger 6, the output end of the gas-liquid separation tank 11 is communicated with an activated carbon odor removal tank 12, a negative pressure fan 13 is fixedly installed at the top of the activated carbon odor removal tank 12, the input end of the negative pressure fan 13 is communicated with the inside of the activated carbon odor removal tank 12, the input end of a circulating water pump 10 is communicated with a first water tank 3, the output end of the circulating water pump 10 is connected with a radiator 9 through a corresponding pipeline, waste water in condensate can be separated out through the gas-liquid separation tank 11, waste gas separated out by the gas-liquid separation tank 11 can be removed through the activated carbon odor removal tank 12, and the waste gas is discharged outwards through the negative pressure fan 13.
The utility model discloses a theory of operation and use flow: the operator operating steps are as follows:
1. injecting water from the outside into the water softener 2;
2. the water softened by the water softener 2 enters the second water tank 4;
3. after the water in the second water tank 4 reaches the upper limit of the liquid level, the water flows into the first water tank 3 through the overflow port;
4. the water in the first water tank 3 enters a steam boiler 5 to maintain the continuous operation of the steam boiler 5;
5. water in the second water tank 4 enters the vacuum pump 7 from the water outlet of the second water tank 4 to support the operation of the vacuum pump 7;
6. after introducing garbage into the sterilization boiler 1, the vacuum pump 7 is operated to pump the air pressure in the sterilization boiler 1 to minus 50-80 KPa, so as to realize primary vacuum. Air in the sterilizing boiler 1 enters a heat exchanger 6 after being blocked by bacteria through a biological filter 8;
7. the gas with heat energy replaced by the heat exchanger 6 enters a vacuum pump 7;
7.1, maintaining the waste water generated by the operation of the vacuum pump 7, and discharging the waste water into a radiator 9 through a corresponding water pipe for temporary storage and heat dissipation;
7.2 the water in the first water tank 3 enters a radiator 9 through a circulating water pump 10 to participate in the heat energy replacement in the step 7, and returns to the first water tank 3 after the replacement is finished;
8. the gas cooled by the heat exchanger 6 enters a gas-liquid separation tank 11 for gas-liquid separation;
9. the gas after being subjected to liquid removal by the gas-liquid separation tank 11 enters the activated carbon box for removing odor 12 and is discharged by the negative pressure fan 13;
10. exhausting air in the sterilization boiler 1, and after reaching a specified negative pressure, feeding high-temperature high-pressure steam in the steam boiler 5 into the sterilization boiler 1 for first high-temperature killing;
repeating the steps 6-10 for a plurality of times until the killing work is finished (the gas pumped in the step 7 in the subsequent repeated cycling work is high-temperature gas, and the heat energy of the gas is replaced to the first water tank 3 for the steam boiler 5 to work);
11. after the killing work is finished, the condensate is discharged and enters the gas-liquid separation tank 11;
12. the waste water separated by the gas-liquid separation tank 11 is discharged into the radiator 9;
13. the water cooled by the radiator 9 enters the water filter 15 through the water pump 14;
14. the water filtered by the water filter 15 returns to the second water tank 4 again;
the heat energy of the high-temperature steam exhausted after the sterilization of the sterilization boiler 1 is replaced to the first water tank 3 to the maximum extent, the water temperature in the first water tank 3 rises, and the energy required by the steam generated by the steam boiler 5 is reduced; the wastewater generated in the working process of the sterilization boiler 1 is fully recycled, no wastewater is discharged outside, and no external water source is needed in the working process.
Finally, it should be noted that: although the present invention has been described in detail 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 in the foregoing embodiments, or equivalents may be substituted for elements thereof. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (7)
1. An energy-saving high-temperature high-pressure moist heat sterilizer is characterized by comprising a bottom plate (16) and a mounting rack (17), a sterilization boiler (1) is arranged on the mounting rack (17), a water softener (2) is arranged on the bottom plate (16), a first water tank (3) is arranged on the bottom plate (16) and close to the water softener (2), a second water tank (4) is arranged above the first water tank (3), a steam boiler (5) is arranged on the bottom plate (16), a heat exchanger (6) is arranged on one side of the steam boiler (5), a vacuum pump (7) is arranged on the bottom plate (16), a biological filter (8) is arranged on the bottom plate (16) close to the heat exchanger (6), a radiator (9) is arranged on one side of the bottom plate (16), a circulating water pump (10) is arranged on the bottom plate (16) close to the vacuum pump (7), a gas-liquid separation tank (11) is arranged on the bottom plate (16), an active carbon deodorization box (12) is arranged above the first water tank (3) and close to the second water tank (4), a negative pressure fan (13) is arranged on the active carbon odor removing box (12), a water pump (14) is arranged on one side of the radiator (9), and a water filter (15) is arranged on one side of the water pump (14).
2. The energy-saving high-temperature high-pressure moist heat sterilizer of claim 1, wherein: the mounting frame (17) is fixedly mounted on the bottom plate (16), and the sterilizing boiler (1) is fixedly mounted on the mounting frame (17).
3. The energy-saving high-temperature high-pressure moist heat sterilizer of claim 1, wherein: the water softener (2) is communicated with the second water tank (4) through a pipeline, and the second water tank (4) is fixedly installed on the first water tank (3) and is communicated with the first water tank (3).
4. The energy-saving high-temperature high-pressure moist heat sterilizer as claimed in claim 1, wherein: the steam boiler (5) is connected with the first water tank (3) through corresponding pipelines, and the vacuum pump (7) is connected with the second water tank (4).
5. The energy-saving high-temperature high-pressure moist heat sterilizer of claim 1, wherein: one end of the biological filter (8) is connected with the sterilizing boiler (1) through a corresponding pipeline, and the heat exchanger (6) is communicated with the biological filter (8).
6. The energy-saving high-temperature high-pressure moist heat sterilizer of claim 1, wherein: the heat exchanger (6) is connected with the vacuum pump (7) through a corresponding pipeline, the radiator (9) is communicated with the vacuum pump (7) through a pipeline, the water pump (14) is connected with the radiator (9), the output end of the water filter (15) is communicated with the first water tank (3), and the input end of the water filter (15) is connected with the output end of the water pump (14).
7. The energy-saving high-temperature high-pressure moist heat sterilizer of claim 1, wherein: the input and the heat exchanger (6) of gas-liquid separation jar (11) are linked together, the output and the active carbon of gas-liquid separation jar (11) remove flavor case (12) and are linked together, negative pressure fan (13) fixed mounting removes flavor case (12) top at the active carbon, the input and the active carbon of negative pressure fan (13) remove flavor case (12) inside and communicate with each other, be linked together between the input of circulating water pump (10) and first water tank (3), link to each other through corresponding the pipeline between the output of circulating water pump (10) and radiator (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223082456.6U CN218833202U (en) | 2022-11-21 | 2022-11-21 | Energy-saving high-temperature high-pressure moist heat sterilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223082456.6U CN218833202U (en) | 2022-11-21 | 2022-11-21 | Energy-saving high-temperature high-pressure moist heat sterilizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218833202U true CN218833202U (en) | 2023-04-11 |
Family
ID=87301956
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223082456.6U Active CN218833202U (en) | 2022-11-21 | 2022-11-21 | Energy-saving high-temperature high-pressure moist heat sterilizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218833202U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117427190A (en) * | 2023-11-16 | 2024-01-23 | 北京市政中燕工程机械制造有限公司 | Intelligent high-temperature steam and microwave combined sterilization device |
-
2022
- 2022-11-21 CN CN202223082456.6U patent/CN218833202U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117427190A (en) * | 2023-11-16 | 2024-01-23 | 北京市政中燕工程机械制造有限公司 | Intelligent high-temperature steam and microwave combined sterilization device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN218833202U (en) | Energy-saving high-temperature high-pressure moist heat sterilizer | |
| CN201814878U (en) | Steam intake and exhaust device of sterilizer | |
| CN201814890U (en) | Water supply device for sterilizer vacuum pump | |
| EP2739317B1 (en) | Steam sterilizer | |
| CN204746017U (en) | Cooling deodorization tower | |
| CN2642310Y (en) | Pollution-prevention high-pressure steam sterilizer | |
| CN211886100U (en) | Negative pressure station room waste gas high temperature sterilization unit | |
| CN214713611U (en) | Medical waste pre-vacuum type sterilization treatment system | |
| CN213446346U (en) | Disinfection equipment | |
| CN211863412U (en) | Disinfection, sterilization and dust removal device of ventilation system of power plant | |
| CN213273839U (en) | Cooling tower with recycling function | |
| CN111084899A (en) | Disinfection, sterilization and dust removal device of ventilation system of power plant | |
| CN214018650U (en) | Medical waste disinfection device | |
| CN201949386U (en) | Process pipeline structure of high-temperature high-pressure pulse sterilization system | |
| CN212205259U (en) | Be arranged in egg liquid production process sterilization machine frozen water recovery unit | |
| CN216694556U (en) | Boiler condensate water recovery device | |
| CN209541271U (en) | High-efficiency vacuum cooler | |
| CN213099580U (en) | Steam sterilization pot cooling water retrieval and utilization device | |
| CN212409429U (en) | Device for cooling high-temperature steam discharged by medical waste cooking reaction kettle | |
| CN217636869U (en) | Novel large-capacity cooling tower | |
| KR101648929B1 (en) | Dual type heat exchanger for food waste disposer and food waste disposer comprising the same | |
| CN216061364U (en) | Steam sterilizer with ultraviolet sterilization function | |
| CN209299865U (en) | A kind of edible fungi culture medium sterilizer | |
| CN217377349U (en) | Low-temperature vacuum wastewater treatment system | |
| CN211724085U (en) | Steam type is inactivation mechanism in cabinet for sterilizer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |