CN103007318A - Quick cooling and depressurizing system of sterilization feeding tank and sterilization stirring tank - Google Patents
Quick cooling and depressurizing system of sterilization feeding tank and sterilization stirring tank Download PDFInfo
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- CN103007318A CN103007318A CN2012105261210A CN201210526121A CN103007318A CN 103007318 A CN103007318 A CN 103007318A CN 2012105261210 A CN2012105261210 A CN 2012105261210A CN 201210526121 A CN201210526121 A CN 201210526121A CN 103007318 A CN103007318 A CN 103007318A
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- sterilization
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- agitator tank
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Abstract
The invention discloses a quick cooling and depressurizing system of a sterilization feeding tank and a sterilization stirring tank. The quick cooling and depressurizing system comprises a spray nozzle of the feeding tank, a spray nozzle of the sterilization stirring tank, a liquid-gas separation filter device, a drainage backlash tube, a high-pressure air pump and high-pressure water inlet pipes, wherein the sterilization feeding tank is positioned above the sterilization stirring tank; the spray nozzles are respectively arranged at the water inlets on the side walls of the sterilization feeding tank and the sterilization stirring tank; the spray nozzles are connected with a high-pressure water purifying device through high-pressure water inlet pipes; the high-pressure air pump is connected with the drainage backlash tube through a gas inlet pipe; the drainage backlash tube is provided with a gas inlet and a water outlet; the gas inlet is formed in the bottom in the sterilization stirring tank; the sterilization feeding tank is connected with a vent pipe; and the vent pipe is connected with the liquid-gas separation device. The quick cooling and depressurizing system is simple in structure, low in cost, can quickly cool and depressurize, and saves a lot of electrical energy.
Description
Technical field
The present invention relates to the fast cooling depressurizing system that a kind of Biohazard Waste and unclassified stores sterilization head tank and sterilization are used in the agitator tank.
The invention still further relates to the method for utilizing said system to carry out the fast cooling blood pressure lowering.
Background technology
Biohazard Waste or unclassified stores sterilization process tank are after the high-temp steam sterilizing process finishes, and the tank body temperature is very high, the steam of a large amount of High Temperature High Pressure is arranged in the tank body, and a large amount of high-temperature steams can not be discharged into directly in atmosphere or the sewer pipe.Therefore, the discharge process can not be opened the door of process tank discharge gate immediately, need to carry out the door that decrease temperature and pressure also just can be opened the whole liquefaction of steam discharge gate to head tank and sterilization agitator tank.Traditional method is to spray into a large amount of water for cooling blood pressure lowerings, but the cooled temperature of tank body can be too low after water gaging contacted with tank body greatly, and next sterilization cycle is warmed up to sterilising temp to be needed again for a long time, wastes a large amount of electric power energies.If the wait natural cooling then needs to cool off for a long time, work efficiency is very low again.
Summary of the invention
The object of the present invention is to provide the fast cooling compression system that adopts in a kind of Biohazard Waste or unclassified stores sterilization head tank and the sterilization agitator tank.
Another purpose of the present invention is to provide a kind of method of utilizing said system to carry out the fast cooling blood pressure lowering.
For achieving the above object, fast cooling depressurizing system in sterilization head tank provided by the invention and the sterilization agitator tank mainly comprises: the fluffy head of the water smoke of head tank, the fluffy head of sterilization agitator tank water smoke, liquid edema caused by disorder of QI are from defecator, blowdown recoil tube, high-pressure pump and high-pressure intake pipe; Wherein:
The sterilization head tank is positioned at the top of sterilization agitator tank;
On the water inlet in the sidewall of sterilization head tank and sterilization agitator tank the fluffy head of water smoke is installed respectively respectively;
The fluffy head of water smoke connects high pressure pure water device by high-pressure intake pipe;
High-pressure pump connects the blowdown recoil tube by air inlet pipe, and the blowdown recoil tube is provided with air inlet and outlet, and wherein air inlet is located at the bottom in the sterilization agitator tank;
Connect exhaustor on the sterilization head tank, exhaustor connecting fluid air separation 5.
Fast cooling depressurizing system in described sterilization head tank and the sterilization agitator tank wherein, is equipped with entering water electromagnetic valve on the water inlet pipe
Fast cooling depressurizing system in described sterilization head tank and the sterilization agitator tank, wherein, air inlet pipe is provided with air inlet electromagnetic valve.
Fast cooling depressurizing system in described sterilization head tank and the sterilization agitator tank, wherein, the outlet of blowdown recoil tube connects blowoff electromagnetic valve.
Fast cooling depressurizing system in described sterilization head tank and the sterilization agitator tank, wherein, gland steam exhauster is provided with the steam discharge electromagnetic valve.
Fast cooling depressurizing system in described sterilization head tank and the sterilization agitator tank, wherein, the fluffy head of water smoke of sterilization head tank and sterilization agitator tank is the fluffy head of lotus shape water smoke, is installed in the height point position of sterilization head tank and sterilization agitator tank.
The method of utilizing above-mentioned sterilization head tank and the interior fast cooling depressurizing system of sterilization agitator tank to carry out decrease temperature and pressure provided by the invention:
After sterilization process finished, the aqueous dispersion of the fluffy head ejection of water smoke of sterilization head tank and sterilization agitator tank became the water smoke shape, and water smoke makes the rapid condensation liquefaction of high-temperature steam with after high-temperature steam contacts, and pressure is rapidly reduction also;
After the water-atomization cooling blood pressure lowering, repeatedly be charged into pressure-air from the blowdown recoil tube to the sterilization head tank with in the sterilization agitator tank again, residue vapor in the tank and gas are further liquefied and filtration the temperature and pressure of opening to reach discharge gate repeatedly from filtration system through the liquid edema caused by disorder of QI.
Described decrease temperature and pressure method, when wherein reaching the temperature and pressure that discharge gate opens, temperature can make next On The Cycle Working Process be rapidly heated to the desired temperature of sterilization in the tank body of sterilization head tank and sterilization agitator tank.
The present invention is simple in structure, and is with low cost, and the fast cooling antihypertensive effect is obvious, saves the electric power energy of a large amount of intensification usefulness.
Description of drawings
Fig. 1 is overall structure sketch map of the present invention.
Primary clustering symbol description in the accompanying drawing:
1 sterilization head tank; 2 sterilization agitator tanks; The fluffy head of the water smoke of 3 head tanks; 4 sterilization agitator tank water atomization plants; 5 liquid edema caused by disorder of QI are from defecator; 6 high-pressure pumps; 7 high-pressure intake pipes; 8 blowdown recoil tubes; 9 air inlet electromagnetic valves; 10 entering water electromagnetic valves; 11 steam discharge electromagnetic valves; 12 blowoff electromagnetic valves; 13 high pressure pure water devices; 14 air inlet pipe; 15 gland steam exhausters.
The specific embodiment
The fast cooling compression system that adopts in Biohazard Waste provided by the invention or unclassified stores sterilization head tank and the sterilization agitator tank mainly comprises: the fluffy head of the water smoke of head tank, the fluffy head of sterilization agitator tank water smoke, the liquid edema caused by disorder of QI is from defecator, the blowdown recoil tube, high-pressure pump, high-pressure intake pipe.Air inlet, water inlet and exhaust outlet pipeline all be equipped with can gauge tap electromagnetic valve.
The fluffy head of the water smoke of lotus shape is installed in head tank and the height point position of the agitator tank of sterilizing, and is connected with the pure water pipe of high pressure.After the pure water pipe of solenoid control was opened, the water ejection namely was dispersed into the water smoke shape.The water smoke of low temperature is with after high-temperature steam fully contacts, and temperature moment reduces and makes the rapid condensation liquefaction of high-temperature steam, and pressure also reduces rapidly, reaches the fast cooling blood pressure lowering.
After the water atomization decrease temperature and pressure, repeatedly be charged into pressure-air in again from the blowdown recoil tube to tank, the residue vapor in the process tank and gas repeatedly through the further liquefaction and filtering of liquid vapour separating and filtering system.This two step just can be opened temperature, pressure and other conditions of requirement the temperature and pressure in the tank being reduced to rapidly the tank door.
Through after above-mentioned two fast cooling blood pressure lowering processes, tank body only contacts with a small amount of water that high steam mixes rear condensation with water smoke, the tank body temperature is still very high, and temperature and pressure has reduced rapidly in the tank, high-temperature steam is all liquefaction also, satisfies temperature, pressure and other conditional requests that discharge gate is opened.Because the tank body temperature is still very high, carry out the high temperature that next circulation time can be rapidly heated and require to sterilization, saved the electric power energy of a large amount of intensification usefulness.
Explain below in conjunction with accompanying drawing.
The present invention sees also Fig. 1, and fluffy 3 of installation high-voltage water smoke and 4 on the water inlet in the sidewall of sterilization head tank 1 and sterilization agitator tank 2, fluffy 3 of water smoke connect high pressure pure water devices 13 with being connected by high-pressure intake pipe 7, and entering water electromagnetic valve 10 is installed on the water inlet pipe 7; High-pressure pump 6 connects blowdown recoil tube 8 by air inlet pipe 14, and air inlet electromagnetic valve 9 is arranged on the air inlet pipe 14, and the outlet of blowdown recoil tube 8 connects blowoff electromagnetic valve 12; Connect exhaustor 15 on the head tank 1, exhaustor 15 connecting fluid air separations 5 are equipped with steam discharge electromagnetic valve 11 on the gland steam exhauster 15.
The present invention is after sterilization process finishes, the PLC controller directly drives into water solenoid valve 5 and opens, fluffy 4 of high-pressure water mist can fully contact with high-temperature steam by ejection water smoke, makes the rapid condensation liquefaction of high-temperature steam, and sterilization head tank 1 and sterilization agitator tank 2 be decrease temperature and pressure immediately.During to certain pressure, controller drives air inlet electromagnetic valve 9, in tank body 1 and 2, be filled with gases at high pressure by blowdown recoil tube 8, then steam discharge electromagnetic valve 11 is opened, after sterilization head tank 1 interior steam enters liquid vapour separating and filtering device 5 by electromagnetic valve 11, liquid vapour is filtered purification, then steam through the water in the device after steam liquefied, gas is discharged, until sterilization head tank 1 and sterilization agitator tank 2 internal and external pressure balances, in this way repeatedly several times after, temperature is reduced between the 80-100 degree, the tank internal and external pressure balance, steam is liquefied fully, then opens the discharge gate discharge.
Claims (8)
1. the fast cooling depressurizing system in a sterilization head tank and the sterilization agitator tank, mainly comprise: the fluffy head of the water smoke of head tank, the fluffy head of sterilization agitator tank water smoke, liquid edema caused by disorder of QI are from defecator, blowdown recoil tube, high-pressure pump and high-pressure intake pipe; Wherein:
The sterilization head tank is positioned at the top of sterilization agitator tank;
On the water inlet in the sidewall of sterilization head tank and sterilization agitator tank the fluffy head of water smoke is installed respectively respectively;
The fluffy head of water smoke connects high pressure pure water device by high-pressure intake pipe;
High-pressure pump connects the blowdown recoil tube by air inlet pipe, and the blowdown recoil tube is provided with air inlet and outlet, and wherein air inlet is located at the bottom in the sterilization agitator tank;
Connect exhaustor on the sterilization head tank, exhaustor connecting fluid air separation.
2. according to claim 1 described sterilization head tank and the fast cooling depressurizing system of sterilization in the agitator tank wherein, are equipped with entering water electromagnetic valve on the water inlet pipe
3. according to claim 1 described sterilization head tank and the fast cooling depressurizing system of sterilization in the agitator tank, wherein, air inlet pipe is provided with air inlet electromagnetic valve.
4. according to claim 1 described sterilization head tank and the fast cooling depressurizing system of sterilization in the agitator tank, wherein, the outlet of blowdown recoil tube connects blowoff electromagnetic valve.
5. according to claim 1 described sterilization head tank and the fast cooling depressurizing system of sterilization in the agitator tank, wherein, gland steam exhauster is provided with the steam discharge electromagnetic valve.
6. according to claim 1 described sterilization head tank and the fast cooling depressurizing system of sterilization in the agitator tank, wherein, the fluffy head of the water smoke of sterilization head tank and sterilization agitator tank is the fluffy head of lotus shape water smoke, is installed in the height point position of sterilization head tank and sterilization agitator tank.
7. method of utilizing the described sterilization head tank of claim 1 and the fast cooling depressurizing system of sterilization in the agitator tank to carry out decrease temperature and pressure:
After sterilization process finished, the aqueous dispersion of the fluffy head ejection of water smoke of sterilization head tank and sterilization agitator tank became the water smoke shape, and water smoke makes the rapid condensation liquefaction of high-temperature steam with after high-temperature steam contacts, and pressure is rapidly reduction also;
After the water-atomization cooling blood pressure lowering, repeatedly be charged into pressure-air from the blowdown recoil tube to the sterilization head tank with in the sterilization agitator tank again, residue vapor in the tank and gas are further liquefied and filtration the temperature and pressure of opening to reach discharge gate repeatedly from filtration system through the liquid edema caused by disorder of QI.
8. decrease temperature and pressure method according to claim 7, when reaching the temperature and pressure that discharge gate opens, temperature can make next On The Cycle Working Process be rapidly heated to the desired temperature of sterilization in the tank body of sterilization head tank and sterilization agitator tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105261210A CN103007318A (en) | 2012-12-07 | 2012-12-07 | Quick cooling and depressurizing system of sterilization feeding tank and sterilization stirring tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105261210A CN103007318A (en) | 2012-12-07 | 2012-12-07 | Quick cooling and depressurizing system of sterilization feeding tank and sterilization stirring tank |
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|---|---|
| CN103007318A true CN103007318A (en) | 2013-04-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012105261210A Pending CN103007318A (en) | 2012-12-07 | 2012-12-07 | Quick cooling and depressurizing system of sterilization feeding tank and sterilization stirring tank |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4576792A (en) * | 1983-09-23 | 1986-03-18 | Aktiebolaget Electrolux | Method for heat treatment of articles and arrangement for carrying out the method |
| CN201862007U (en) * | 2010-09-17 | 2011-06-15 | 山东新华医疗器械股份有限公司 | Fast cooling device for sterilizer |
| CN102743774A (en) * | 2012-06-14 | 2012-10-24 | 山东鼎泰盛食品工业装备股份有限公司 | Vertical sterilization kettle cold water cycle system |
| CN202950993U (en) * | 2012-12-07 | 2013-05-29 | 栖霞中泰环保设备有限公司 | Rapid temperature and pressure reducing system in sterilizing and feeding tank and sterilizing and stirring tank |
-
2012
- 2012-12-07 CN CN2012105261210A patent/CN103007318A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4576792A (en) * | 1983-09-23 | 1986-03-18 | Aktiebolaget Electrolux | Method for heat treatment of articles and arrangement for carrying out the method |
| CN201862007U (en) * | 2010-09-17 | 2011-06-15 | 山东新华医疗器械股份有限公司 | Fast cooling device for sterilizer |
| CN102743774A (en) * | 2012-06-14 | 2012-10-24 | 山东鼎泰盛食品工业装备股份有限公司 | Vertical sterilization kettle cold water cycle system |
| CN202950993U (en) * | 2012-12-07 | 2013-05-29 | 栖霞中泰环保设备有限公司 | Rapid temperature and pressure reducing system in sterilizing and feeding tank and sterilizing and stirring tank |
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Application publication date: 20130403 |