CN201949386U - Process pipeline structure of high-temperature high-pressure pulse sterilization system - Google Patents
Process pipeline structure of high-temperature high-pressure pulse sterilization system Download PDFInfo
- Publication number
- CN201949386U CN201949386U CN2010206778593U CN201020677859U CN201949386U CN 201949386 U CN201949386 U CN 201949386U CN 2010206778593 U CN2010206778593 U CN 2010206778593U CN 201020677859 U CN201020677859 U CN 201020677859U CN 201949386 U CN201949386 U CN 201949386U
- Authority
- CN
- China
- Prior art keywords
- valve
- condensed fluid
- temperature high
- pressure pulse
- pipe
- 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.)
- Expired - Lifetime
Links
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
The utility model relates to a process pipeline structure of a high-temperature high-pressure pulse sterilization system. The process pipeline structure comprises a high-temperature high-pressure pulse sterilizer, a secondary sterilization tank, a biofilter, a condensed fluid collection valve, a drain valve, an exhaust valve, a condensed fluid collection pipe, an exhaust pipe and a main pipe, wherein the lower part of the high-temperature high-pressure pulse sterilizer is connected with the condensed fluid collection pipe, the condensed fluid collection pipe is respectively connected with the main pipe and the drain valve through the condensed fluid collection valve, and the main pipe is connected with the lower part of the secondary sterilization tank; and the lower part of the secondary sterilization tank is connected with the exhaust pipe, and the exhaust pipe is connected with the exhaust valve through the biofilter. In the utility model, waste gas is adopted to heat waste liquor, clean energy is not used, or less clean energy is used, and the process pipeline structure is suitable for innoxious treatment of bacteria bearing condensed fluid generated during high-temperature high-pressure pulse sterilization process adopting a non-incineration mode of medical wastes. The process pipeline structure of the high-temperature high-pressure pulse sterilization system has the advantages of energy conservation and simple structure, and is environment-friendly; and the emission is reduced.
Description
Technical field
This utility model belongs to hazardous waste and handles non-incineration treatment technology field, the process pipeline structure that relates to a kind of High Temperature High Pressure pulsation disinfection system is particularly useful for the harmlessness disposing of the condensed fluid that carries disease germs that produces in the non-burning mode of the clinical waste High Temperature High Pressure pulsation sterilization disposal process.
Background technology
The non-incineration disposal of existing clinical waste field, the waste liquid that carries disease germs for the generation of MEDICAL WASTE TREATMENT process, domestic a kind of method is to adopt the discharging of venturi high temperature and high pressure steam system, and principle is to penetrate-flow-inhale-arrange, and contacts by high-temperature steam and waste liquid, waste gas moment and sterilizes, the method drawback is that power consumption is high, require steam supply boiler pressure height, operating noise is big, when beginning to discharge the initial stage, steam water content high-temperature is low, and sterilization is not thorough when sterilising temp is not high.
Another kind method is at first to collect the waste liquid that carries disease germs, focus in the pressure-vessel disinfection tank, when waste collection arrives high liquid level, by circulating pump circulation waste liquid, by the plate type heat exchanger heat temperature raising, when arriving uniform temperature and a period of time of insulation, reach the purpose of secondary waste collection jar inner condensat liquid sterilization, to consume a lot of cleaning steam during this.When the collection valve valve closing of pulsation vacuum sterilizer and two-stage sterilization jar, form one section blind pipe between valve and the two-stage sterilization jar, the sterilization that can't thoroughly circulate of the condensed fluid that carries disease germs in the blind pipe is easy to cause sterilization not thorough.The method is complex structure in design, after exchanger works long hours the inner power consumption of fouling easily bigger, heat loss is big.
Summary of the invention
Problem to be solved in the utility model is, overcomes the deficiencies in the prior art, and a kind of process pipeline structure of High Temperature High Pressure pulsation disinfection system is provided, and adopts waste gas to heat to waste liquid, does not use or use less clean energy resource.In the work process of pulsation disinfection system and in the two-stage sterilization jar collection discharging, the waste liquid that carries disease germs does not intersect, does not reverse, does not exist blind pipe to die for the sake of honour, the waste collection of carrying disease germs pipe and two-stage sterilization jar steam-heating pipe are with the pipe co-flow, unique reverse flow be arterial drainage, and the arterial drainage discharging time is the sterilized water after having sterilized.
This utility model solves its technical problem and takes following technical scheme to realize:
The process pipeline structure of a kind of High Temperature High Pressure pulsation disinfection system that provides according to this utility model, comprise High Temperature High Pressure pulsation steriliser, two-stage sterilization jar, biofilter, condensed fluid collection valve, drain valve, air bleeding valve, condensate collector tube, exhaustor and main, the bottom of described High Temperature High Pressure pulsation steriliser connects condensate collector tube, condensate collector tube is collected valve through condensed fluid and is connected main and drain valve respectively, and main connects the bottom of two-stage sterilization jar; The top of two-stage sterilization jar connects exhaustor, and exhaustor connects air bleeding valve through biofilter.
This utility model compared with prior art has significant advantage and beneficial effect:
Because utility model adopts waste gas to heat to waste liquid, does not use or use less clean energy resource.In the work process of pulsation disinfection system and in the two-stage sterilization jar collection discharging, the waste liquid that carries disease germs does not intersect, does not reverse, does not exist blind pipe to die for the sake of honour, the waste collection of carrying disease germs pipe and two-stage sterilization jar steam-heating pipe are with the pipe co-flow, unique reverse flow be arterial drainage, and the arterial drainage discharging time is the sterilized water after having sterilized, and has thoroughly solved the halfway problem of sterilization.
Also removed parts such as circulation line circulating pump and heat exchanger simultaneously, it is one that the waste collection pipe in past, discharging tube, steam-heating pipe close three, has reduced manufacturing cost and maintenance fund, and it is convenient that simplified overhauling is installed, and remedies the deficiencies in the prior art.When saving the energy, also accomplished to reduce the discharging of pollutant, reduced cost of investment, reduced fault rate, reduced maintenance cost, well solved the halfway problem of sterilization that the residual waste liquid that carries disease germs of blind pipe causes, obvious social benefit, the discharging that can save the energy and reduction pollutant greatly.
The specific embodiment of the present utility model is provided in detail by following examples and accompanying drawing thereof.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Wherein: 1, High Temperature High Pressure pulsation steriliser 2, condensed fluid are collected valve 3, condensate collector tube 4, main 5, drain valve 6, two-stage sterilization jar 7, biofilter 8, exhaustor 9, air bleeding valve
The specific embodiment
Below in conjunction with accompanying drawing and preferred embodiment, the specific embodiment, structure, feature and effect thereof that foundation this utility model is provided, describe in detail as after.
The process pipeline structure of a kind of High Temperature High Pressure pulsation disinfection system as shown in Figure 1, comprise High Temperature High Pressure pulsation steriliser, two-stage sterilization jar, biofilter, condensed fluid collection valve, drain valve, air bleeding valve, condensate collector tube, exhaustor and main, the bottom of High Temperature High Pressure pulsation steriliser 1 connects condensate collector tube 3, condensate collector tube is collected valve 2 through condensed fluid and is connected main 4 and drain valve 5 respectively, and main connects the bottom of two-stage sterilization jar 6; The top of two-stage sterilization jar connects exhaustor 8, and exhaustor connects air bleeding valve 9 through biofilter 7.
Operation principle: the bottom condensed fluid of High Temperature High Pressure pulsation steriliser 1 at first with pressure, collecting valve 2 by condensed fluid on bottom condensate collector tube 3 and the condensate collector tube opens, collect in the two-stage sterilization jar 6 by main 4, enter the condensed fluid in the two-stage sterilization jar, because condensate flow-rate is lowered in the reducing dilatation, condensed fluid will exist in the two-stage sterilization jar, upper gas is discharged through two-stage sterilization jar top exhaustor 8, through the filtration of biofilter 7, the air bleeding valve 9 on the process gas exhaust piping 8 is opened and is finished the aseptic discharging of gas.The drain valve 5 that is positioned at two-stage sterilization jar bottom is to be used for discharging waste liquid after the sterilization of two-stage sterilization jar, the aseptic condensed fluid in sterilization back is to finish the sterile liquid discharging through main 4 and the drain valve opened, and condensed fluid is collected valve 2 and closed when discharging aseptic waste liquid.
In the work process of pulsation disinfection system, vacuum---sterilization---drying is three main technique stages, when the work of pulsation disinfection system finishes to sterilizing, an aerofluxus blood pressure lowering process is arranged when wherein sterilization phase finishes to change drying stage over to, needing discharging high-temperature steam pressure is that the TVOC that this high-temperature steam of 0.2MP (temperature 132 degree) contains in the clinical waste is a waste vapour, this utility model is to give two-stage sterilization jar heat temperature raising with waste gas, improves by PLC control by pipeline and finishes.Code requirement is 125 degree insulation certain hours.When the sterilization of two-stage sterilization jar finished, aseptic waste water passed through main 4 and opens drain valve 5 drainings and finish.
Claims (1)
1. the process pipeline structure of High Temperature High Pressure pulsation disinfection system, comprise High Temperature High Pressure pulsation steriliser, two-stage sterilization jar, biofilter, condensed fluid collection valve, drain valve, air bleeding valve, condensate collector tube, exhaustor and main, it is characterized in that: the bottom of described High Temperature High Pressure pulsation steriliser (1) connects condensate collector tube (3), condensate collector tube is collected valve (2) through condensed fluid and is connected main (4) and drain valve (5) respectively, and main connects the bottom of two-stage sterilization jar (6); The top of two-stage sterilization jar connects exhaustor (8), and exhaustor connects air bleeding valve (9) through biofilter (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206778593U CN201949386U (en) | 2010-12-24 | 2010-12-24 | Process pipeline structure of high-temperature high-pressure pulse sterilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206778593U CN201949386U (en) | 2010-12-24 | 2010-12-24 | Process pipeline structure of high-temperature high-pressure pulse sterilization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201949386U true CN201949386U (en) | 2011-08-31 |
Family
ID=44493516
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206778593U Expired - Lifetime CN201949386U (en) | 2010-12-24 | 2010-12-24 | Process pipeline structure of high-temperature high-pressure pulse sterilization system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201949386U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113633792A (en) * | 2021-08-20 | 2021-11-12 | 冰山松洋生物科技(大连)有限公司 | Sterilizer exhaust treatment device with biological emission safety and working method thereof |
| CN113813435A (en) * | 2021-10-07 | 2021-12-21 | 海南金特尔环境科技有限公司 | Medical waste disinfection treatment system for ward department |
-
2010
- 2010-12-24 CN CN2010206778593U patent/CN201949386U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113633792A (en) * | 2021-08-20 | 2021-11-12 | 冰山松洋生物科技(大连)有限公司 | Sterilizer exhaust treatment device with biological emission safety and working method thereof |
| CN113813435A (en) * | 2021-10-07 | 2021-12-21 | 海南金特尔环境科技有限公司 | Medical waste disinfection treatment system for ward department |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101691247B (en) | Pathogenic microorganism waste liquor treatment system | |
| CN201814878U (en) | Steam intake and exhaust device of sterilizer | |
| CN105836940A (en) | Domestic solar water purifying device | |
| CN201320308Y (en) | Medical waste sterilizer | |
| CN201949386U (en) | Process pipeline structure of high-temperature high-pressure pulse sterilization system | |
| CN103330953A (en) | Biosafety type pulsation vacuum sterilizer | |
| CN203777372U (en) | Medical waste sterilizer pipeline system | |
| CN214415283U (en) | Steam-water mixing sterilizer of fermentation continuous sterilization system | |
| CN201190131Y (en) | Continuous waste water treatment system with active virus | |
| CN2642310Y (en) | Pollution-prevention high-pressure steam sterilizer | |
| CN214792616U (en) | Sterilization kettle pre-vacuum condensate water recycling system | |
| CN204352224U (en) | A kind of energy-saving high vacuum autoclave with pulsing system | |
| CN201558337U (en) | Full automatic horizontal autoclave sterilizer | |
| CN200998425Y (en) | Dual-purpose machine for boiling the medicinal herbs and disinfection | |
| CN203354935U (en) | Energy-saving biological safety type pulsation vacuum sterilizer | |
| CN204147298U (en) | A kind of waste liquid inactivating device utilizing flash steam | |
| CN214713611U (en) | Medical waste pre-vacuum type sterilization treatment system | |
| CN104208728B (en) | Utilize the waste liquid inactivating device of flash steam | |
| CN220116379U (en) | Energy-saving purified water pretreatment equipment degassing unit | |
| CN210150890U (en) | Community domestic wastewater treatment device | |
| CN213911467U (en) | Hospital pulsation vacuum sterilizer economizer system | |
| CN212902762U (en) | Volumetric heat exchange device with sterilization structure and high heat exchange efficiency | |
| CN210559881U (en) | Cosmetic production is with disinfection pure water jar | |
| CN213066548U (en) | Heat pump water heater with sterilization and water purification functions | |
| CN219603561U (en) | Bioreactor drainage device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110831 |