CN202950993U - Rapid temperature and pressure reducing system in sterilizing and feeding tank and sterilizing and stirring tank - Google Patents
Rapid temperature and pressure reducing system in sterilizing and feeding tank and sterilizing and stirring tank Download PDFInfo
- Publication number
- CN202950993U CN202950993U CN 201220674566 CN201220674566U CN202950993U CN 202950993 U CN202950993 U CN 202950993U CN 201220674566 CN201220674566 CN 201220674566 CN 201220674566 U CN201220674566 U CN 201220674566U CN 202950993 U CN202950993 U CN 202950993U
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- China
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- sterilizing
- tank
- pressure
- agitator tank
- water
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Abstract
The utility model discloses a rapid temperature and pressure reducing system in a sterilizing and feeding tank and a sterilizing and stirring tank. The rapid temperature and pressure reducing system mainly comprises a water spray nozzle of the feeding tank, a water spray nozzle of the sterilizing and stirring tank, a liquid-gas separating and filtering device, a draining and backflushing pipe, a high-pressure gas pump and a high-pressure water inlet pipe; the sterilizing and feeding tank is located above the sterilizing and stirring tank; water inlets in side walls of the sterilizing and feeding tank and the sterilizing and stirring tank are respectively provided with the water spray nozzle; the water spray nozzles are connected with a high-pressure purified water device through the high-pressure water inlet pipe; the high-pressure gas pump is connected with the draining and backflushing pipe through an air inlet pipe, and the draining and backflushing pipe is provided with an air inlet and a water outlet, wherein the air inlet is arranged at the bottom inside the sterilizing and stirring tank; and the sterilizing and feeding tank is connected with an exhaust pipe which is connected with a liquid-gas separation device. The rapid temperature and pressure reducing system is simple in structure, low in cost and capable of rapidly reducing the temperature and the pressure and saving a great deal of electrical energy.
Description
Technical field
This utility model relates to the fast cooling depressurizing system of using in a kind of Biohazard Waste and unclassified stores sterilization head tank and sterilizing agitator tank.
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 tank body, and a large amount of high-temperature steams can not directly be discharged in atmosphere or sewer pipe.Therefore, the discharge process can not be opened the door of process tank discharge gate immediately, need to head tank and sterilizing agitator tank carry out decrease temperature and pressure and the whole liquefaction of steam just can open discharge gate.Traditional method is to spray into a large amount of water for cooling blood pressure lowerings, but large water gaging contacts with tank body that the cooled temperature of tank body can be too low afterwards, 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, need coolingly for a long time, work efficiency is very low again.
The utility model content
The purpose of this utility model is to provide the fast cooling compression system adopted in a kind of Biohazard Waste or unclassified stores sterilization head tank and sterilizing agitator tank.
For achieving the above object, fast cooling depressurizing system in the sterilization head tank that this utility model provides and sterilizing agitator tank mainly comprises: the fluffy head of the water smoke of head tank, the fluffy head of sterilizing 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 sterilizing agitator tank;
On water inlet in the sidewall of sterilization head tank and sterilizing agitator tank, the fluffy head of water smoke respectively is installed 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 sterilizing 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 sterilizing agitator tank, wherein, be equipped with entering water electromagnetic valve on water inlet pipe
Fast cooling depressurizing system in described sterilization head tank and sterilizing agitator tank, wherein, air inlet pipe is provided with air inlet electromagnetic valve.
Fast cooling depressurizing system in described sterilization head tank and sterilizing agitator tank, wherein, the outlet of blowdown recoil tube connects blowoff electromagnetic valve.
Fast cooling depressurizing system in described sterilization head tank and sterilizing agitator tank, wherein, exhaustor is provided with exhaust solenoid valve.
Fast cooling depressurizing system in described sterilization head tank and sterilizing agitator tank, wherein, the fluffy head of the water smoke of sterilization head tank and sterilizing agitator tank is the fluffy head of lotus shape water smoke, is arranged on the height point position of sterilization head tank and sterilizing agitator tank.
This utility model is simple in structure, with low cost, and the fast cooling antihypertensive effect is obvious, saves the electric power energy of a large amount of intensification use.
The accompanying drawing explanation
Fig. 1 is overall structure schematic diagram of the present utility model.
Primary clustering symbol description in accompanying drawing:
1 sterilization head tank; 2 sterilizing agitator tanks; The fluffy head of the water smoke of 3 head tanks; 4 sterilizing 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 exhaust solenoid valves; 12 blowoff electromagnetic valves; 13 high pressure pure water devices; 14 air inlet pipe; 15 exhaustors.
The specific embodiment
The fast cooling compression system adopted in the Biohazard Waste that this utility model provides or unclassified stores sterilization head tank and sterilizing agitator tank, mainly comprise: the fluffy head of the water smoke of head tank, the fluffy head of sterilizing 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 are equipped with electromagnetic valve that can gauge tap.
The fluffy head of the water smoke of lotus shape, be arranged on the height point position of head tank and sterilizing agitator tank, with the pure water pipe of high pressure, is connected.After the pure water pipe of solenoid control is opened, the water ejection is 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, more repeatedly be charged into pressure-air in from the blowdown recoil tube to tank, the residue vapor in process tank and gas are repeatedly further liquefied and filter through liquid vapour separating and filtering system.This two step just can be reduced to rapidly temperature, pressure and other conditions that the tank door is opened requirement to the temperature and pressure in tank.
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 in tank, temperature and pressure has reduced rapidly, high-temperature steam is all liquefaction also, meets temperature, pressure and other conditional requests that discharge gate is opened.Because the tank body temperature is still very high, carry out next circulation time and can be rapidly heated to the high temperature of sterilizing requirement, saved the electric power energy of a large amount of intensification use.
Below in conjunction with accompanying drawing, explain.
This utility model refers to Fig. 1, fluffy 3 of installation high-voltage water smoke and 4 on water inlet in the sidewall of sterilization head tank 1 and sterilizing agitator tank 2, fluffy 3 of water smoke is connected high pressure pure water device 13 with 4 by high-pressure intake pipe 7, and entering water electromagnetic valve 10 is installed on 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 air inlet pipe 14, and the outlet of blowdown recoil tube 8 connects blowoff electromagnetic valve 12; Connect exhaustor 15 on head tank 1, exhaustor 15 connecting fluid air separations 5, be equipped with exhaust solenoid valve 11 on exhaustor 15.
This utility model 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 sterilizing agitator tank 2 be decrease temperature and pressure immediately.During to certain pressure, controller drives air inlet electromagnetic valve 9, be filled with gases at high pressure by blowdown recoil tube 8 in tank body 1 and 2, then exhaust solenoid valve 11 is opened, after the interior steam of sterilization head tank 1 enters liquid vapour separating and filtering device 5 by electromagnetic valve 11, liquid vapour is filtered purification, then steam steam liquefied after the water in installing, gas is discharged, until sterilization head tank 1 and sterilizing 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 open the discharge gate discharge.
Claims (6)
1. the fast cooling depressurizing system in a sterilization head tank and sterilizing agitator tank, it is characterized in that, mainly comprise: the fluffy head of the water smoke of head tank, the fluffy head of sterilizing 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 sterilizing agitator tank;
On water inlet in the sidewall of sterilization head tank and sterilizing agitator tank, the fluffy head of water smoke respectively is installed 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 sterilizing agitator tank;
Connect exhaustor on the sterilization head tank, exhaustor connecting fluid air separation.
2. the fast cooling depressurizing system in sterilization head tank and sterilizing agitator tank according to claim 1, is characterized in that, entering water electromagnetic valve is installed on water inlet pipe
3. the fast cooling depressurizing system in sterilization head tank and sterilizing agitator tank according to claim 1, is characterized in that, air inlet pipe is provided with air inlet electromagnetic valve.
4. the fast cooling depressurizing system in sterilization head tank and sterilizing agitator tank according to claim 1, is characterized in that, the outlet of blowdown recoil tube connects blowoff electromagnetic valve.
5. the fast cooling depressurizing system in sterilization head tank and sterilizing agitator tank according to claim 1, is characterized in that, exhaustor is provided with exhaust solenoid valve.
6. the fast cooling depressurizing system in sterilization head tank and sterilizing agitator tank according to claim 1, it is characterized in that, the fluffy head of the water smoke of sterilization head tank and sterilizing agitator tank is the fluffy head of lotus shape water smoke, is arranged on the height point position of sterilization head tank and sterilizing agitator tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220674566 CN202950993U (en) | 2012-12-07 | 2012-12-07 | Rapid temperature and pressure reducing system in sterilizing and feeding tank and sterilizing and stirring tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220674566 CN202950993U (en) | 2012-12-07 | 2012-12-07 | Rapid temperature and pressure reducing system in sterilizing and feeding tank and sterilizing and stirring tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202950993U true CN202950993U (en) | 2013-05-29 |
Family
ID=48456591
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220674566 Expired - Lifetime CN202950993U (en) | 2012-12-07 | 2012-12-07 | Rapid temperature and pressure reducing system in sterilizing and feeding tank and sterilizing and stirring tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202950993U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103007318A (en) * | 2012-12-07 | 2013-04-03 | 栖霞中泰环保设备有限公司 | Quick cooling and depressurizing system of sterilization feeding tank and sterilization stirring tank |
| CN104567467A (en) * | 2014-12-24 | 2015-04-29 | 无锡市南长区科技创业服务中心 | Heat exchanger with relatively high efficiency |
-
2012
- 2012-12-07 CN CN 201220674566 patent/CN202950993U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103007318A (en) * | 2012-12-07 | 2013-04-03 | 栖霞中泰环保设备有限公司 | Quick cooling and depressurizing system of sterilization feeding tank and sterilization stirring tank |
| CN104567467A (en) * | 2014-12-24 | 2015-04-29 | 无锡市南长区科技创业服务中心 | Heat exchanger with relatively high efficiency |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190610 Address after: 100038 Building 8E, Yuyuantan South Road, Haidian District, Beijing Patentee after: Lin Zhongxuan Address before: 265300 Songshan Science and Technology Industrial Park, Qixia City, Yantai City, Shandong Province Patentee before: QIXIA SINOTEC Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210208 Address after: 100032 room 1003, 10 / F, building 1, 66 nanlishi Road, Xicheng District, Beijing Patentee after: Beijing Great White Shark Environmental Protection Technology Co.,Ltd. Address before: 100038 Building 8E, Yuyuantan South Road, Haidian District, Beijing Patentee before: Lin Zhongxuan |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130529 |
|
| CX01 | Expiry of patent term |