CN203959857U - Low temperature continous way waste liquid inactivation system - Google Patents

Low temperature continous way waste liquid inactivation system Download PDF

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Publication number
CN203959857U
CN203959857U CN201420162309.6U CN201420162309U CN203959857U CN 203959857 U CN203959857 U CN 203959857U CN 201420162309 U CN201420162309 U CN 201420162309U CN 203959857 U CN203959857 U CN 203959857U
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CN
China
Prior art keywords
waste liquid
shell
entrance
tank
heat exchanger
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 - Fee Related
Application number
CN201420162309.6U
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Chinese (zh)
Inventor
冯亚科
徐炳坤
高风华
刘强
袁世斌
董营
樊光明
董帅
王珂
章植栋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANDONG XINHUA MEDICAL ENVIRONMENTAL EQUIPMENT CO Ltd
Original Assignee
SHANDONG XINHUA MEDICAL ENVIRONMENTAL EQUIPMENT CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SHANDONG XINHUA MEDICAL ENVIRONMENTAL EQUIPMENT CO Ltd filed Critical SHANDONG XINHUA MEDICAL ENVIRONMENTAL EQUIPMENT CO Ltd
Priority to CN201420162309.6U priority Critical patent/CN203959857U/en
Application granted granted Critical
Publication of CN203959857U publication Critical patent/CN203959857U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a kind of medical liquid waste treating apparatus, specifically a low temperature continous way waste liquid inactivation system, comprises temporary tank, it is characterized in that, the temporary outlet of tank and the entrance pipe of shell and tube heat exchanger are connected, and the outlet of shell and tube heat exchanger is connected with the entrance of double-pipe exchanger; Its beneficial effect is: 1) shell and tube heat exchanger replaces deactivation tank of the prior art, designs simplification, and floor space is little, the flow process of the biological waste liquid of increase that can be longer, inactivating efficacy is better; 2) electrification control is carried out to deactivation flow process in bus type valve island, and accurately, level of automation is high; 3) exit of double-pipe exchanger is connected to platinum resistance thermometer sensor, and under meter, can detect temperature out, reaches safety dumping; 4) basket filter, filters out larger impurity in waste liquid, avoids pipeline and interchanger to stop up.

Description

Low temperature continous way waste liquid inactivation system
Technical field
The utility model relates to a kind of medical liquid waste treating apparatus, specifically a kind of low temperature continous way waste liquid inactivation system.
Background technology
At present, in known high-temperature steam inactivation system, how to heat by deactivation tank, carry out biological waste liquid deactivation, publication number is CN202945119U, the Chinese patent of open day on 05 22nd, 2013, disclose the biological waste liquid inactivation system of a kind of telescoping, heat inactivation tank and double-pipe exchanger carry out bioinactivation, and the problem of existence is, deactivation tank cost is high, complex structure, and floor space is large.
Utility model content
The utility model provides that a kind of cost is low, simple in structure, floor space is little, the low temperature continous way waste liquid inactivation system that inactivating efficacy is good.
The concrete technical scheme adopting of the utility model is:
Low temperature continous way waste liquid inactivation system, comprise temporary tank, it is characterized in that, the temporary outlet of tank and the entrance pipe of shell and tube heat exchanger are connected, and the outlet of shell and tube heat exchanger is connected with the entrance of double-pipe exchanger, and tubular heat exchange carries out heat temperature raising to the waste liquid of flowing through, carry out preliminary sterilizing, double-pipe exchanger is composed in series, and increases waste liquid flow process, makes waste liquid have enough time to complete sterilization process.
Wherein, the entrance pipe of described temporary tank is provided with basket filter, basket filter is housed before temporary tank, filters out the larger impurity of volume in waste liquid, in order to avoid blocking pipeline or double-pipe exchanger.
Wherein, also comprise the Controlling System being arranged on pipeline, described Controlling System comprises bus type valve island, is arranged on the liquidometer in temporary tank, liquidometer is connected with bus type valve island, also comprise the water pump of being controlled by bus type valve island, the entrance of water pump is connected with temporary tank, and water pump outlet is connected with the entrance of shell and tube heat exchanger.
Wherein, described water pump is two, is connected in parallel on pipeline.
Wherein, on the connecting pipeline of each parts, be provided with manual valve and pneumavalve, pneumavalve and bus type valve island connection.
Wherein, the exit of described double-pipe exchanger is connected to platinum resistance thermometer sensor, and under meter, platinum resistance thermometer sensor,, under meter respectively with bus type valve island connection.
Compared with prior art, the utility model has the advantages that: 1) shell and tube heat exchanger replaces deactivation tank of the prior art, designs simplification, floor space is little, the flow process of the biological waste liquid of increase that can be longer, inactivating efficacy is better; 2) electrification control is carried out to deactivation flow process in bus type valve island, and accurately, level of automation is high; 3) exit of double-pipe exchanger is connected to platinum resistance thermometer sensor, and under meter, can detect temperature out, reaches safety dumping; 4) basket filter, filters out larger impurity in waste liquid, avoids pipeline and interchanger to stop up.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
In figure, 1, temporary tank, 2, water pump, 3, shell and tube heat exchanger, 4, double-pipe exchanger, 5, basket filter.
Embodiment
As shown in Figure 1, low temperature continous way waste liquid inactivation system mainly comprises temporary tank 1, shell and tube heat exchanger 3, double-pipe exchanger 4, the outlet of temporary tank 1 is connected with two water pumps 2 that are arranged on side by side on pipeline, the outlet of water pump 2 is connected with the entrance pipe of shell and tube heat exchanger 3, the outlet of shell and tube heat exchanger 3 is connected with the entrance of double-pipe exchanger 4, and the exit of double-pipe exchanger 4 is provided with platinum resistance thermometer sensor, and under meter; On the pipeline of the entrance of temporary tank 1, there is basket filter 5, in temporary tank 1, be provided with liquidometer; On pipeline Controlling System is also set, Controlling System comprises bus type valve island, and liquidometer is connected with bus type valve island, and water pump 2 is controlled by bus type valve island.
On the connecting pipeline of each parts, be provided with manual valve and pneumavalve, pneumavalve and bus type valve island connection, can realize manually and automatically controlling of pipeline.
The exit of double-pipe exchanger is connected to platinum resistance thermometer sensor, and under meter, platinum resistance thermometer sensor,, under meter respectively with bus type valve island connection, can detect temperature out.
All pipelines are weldprocedure, guarantee without leaking.
Every section of double-pipe exchanger is all provided with heat preservation protective layer, can save the energy, can prevent from again scalding.Working process
Sewage is collected through conduit, enter temporary tank by basket filter, in the time that temporary tank water level exceedes the water level of liquidometer setting, bus type valve island starts water pump, in tubular heat exchange, lead to steam simultaneously, waste liquid is raised to the temperature of sterilizing requirement through tubular heat exchange, waste liquid flows into double-pipe exchanger, in double-pipe exchanger, pass into steam simultaneously, make waste liquid keep the sterilising temp whole double-pipe exchanger group of flowing through, waste liquor stream is sterilization time through the time of double-pipe exchanger, the waste liquid reserving from double-pipe exchanger has met sterilizing requirement, double-pipe exchanger group tail end is connected to platinum resistance thermometer sensor, and under meter, in order to detect temperature out safety dumping.

Claims (6)

1. low temperature continous way waste liquid inactivation system, comprises temporary tank, it is characterized in that, the temporary outlet of tank and the entrance pipe of shell and tube heat exchanger are connected, and the outlet of shell and tube heat exchanger is connected with the entrance of double-pipe exchanger.
2. low temperature continous way waste liquid inactivation system according to claim 1, is characterized in that, the entrance pipe of described temporary tank is provided with basket filter.
3. the biological waste liquid inactivation system of a kind of telescoping according to claim 1, it is characterized in that, also comprise the Controlling System being arranged on pipeline, described Controlling System comprises bus type valve island, is arranged on the liquidometer in temporary tank, liquidometer is connected with bus type valve island, also comprise the water pump of being controlled by bus type valve island, the entrance of water pump is connected with temporary tank, and water pump outlet is connected with the entrance of shell and tube heat exchanger.
4. low temperature continous way waste liquid inactivation system according to claim 3, is characterized in that, described water pump is two, is connected in parallel on pipeline.
5. the biological waste liquid inactivation system of a kind of telescoping according to claim 4, is characterized in that, is provided with manual valve and pneumavalve, pneumavalve and bus type valve island connection on the connecting pipeline of each parts.
6. the biological waste liquid inactivation system of a kind of telescoping according to claim 4, is characterized in that, the exit of described double-pipe exchanger is connected to platinum resistance thermometer sensor, and under meter, platinum resistance thermometer sensor,, under meter respectively with bus type valve island connection.
CN201420162309.6U 2014-04-04 2014-04-04 Low temperature continous way waste liquid inactivation system Expired - Fee Related CN203959857U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420162309.6U CN203959857U (en) 2014-04-04 2014-04-04 Low temperature continous way waste liquid inactivation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420162309.6U CN203959857U (en) 2014-04-04 2014-04-04 Low temperature continous way waste liquid inactivation system

Publications (1)

Publication Number Publication Date
CN203959857U true CN203959857U (en) 2014-11-26

Family

ID=51920467

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420162309.6U Expired - Fee Related CN203959857U (en) 2014-04-04 2014-04-04 Low temperature continous way waste liquid inactivation system

Country Status (1)

Country Link
CN (1) CN203959857U (en)

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141126

Termination date: 20190404