CN205403152U - Chemical engineering liquid raw materials heat preservation device - Google Patents

Chemical engineering liquid raw materials heat preservation device Download PDF

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Publication number
CN205403152U
CN205403152U CN201620182202.7U CN201620182202U CN205403152U CN 205403152 U CN205403152 U CN 205403152U CN 201620182202 U CN201620182202 U CN 201620182202U CN 205403152 U CN205403152 U CN 205403152U
Authority
CN
China
Prior art keywords
liquid
heat
oil
heat exchange
shower nozzle
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
CN201620182202.7U
Other languages
Chinese (zh)
Inventor
于宗杰
李春信
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 Longxin Chemical Coltd
Original Assignee
Shandong Xinhua Longxin Chemical Coltd
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 Longxin Chemical Coltd filed Critical Shandong Xinhua Longxin Chemical Coltd
Priority to CN201620182202.7U priority Critical patent/CN205403152U/en
Application granted granted Critical
Publication of CN205403152U publication Critical patent/CN205403152U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model provides a chemical engineering liquid raw materials heat preservation device, includes: an oil tank for storing the conduction oil, inside is equipped with the sealed heat transfer case that holds the chamber, set up in the sealed helical shape heat exchange tube that holds the intracavity, set up in sealed appearance intracavity and the shower nozzle directly over being located the heat exchange tube, set up the electric heater in the oil tank and be used for the stock solution bucket of storing liquid raw materials, the heat -conducting oil of electric heater in with the oil tank, conduction oil after the oil pump will heat passes through the shower nozzle and sprays on the heat exchange tube in the heat transfer case, going into in the heat exchange tube liquid feedstock pump in the stock solution bucket also through the feed liquor pipe about the pump, shower nozzle spun conduction oil carries out the heat transfer, thereby the mesh of heating fluid body raw materials has been realized, because liquid charging stock and heat source be direct contact not, consequently, effectively avoided the heat source high temperature to lead to the rotten condition of liquid charging stock to take place, and improves the production efficiency.

Description

Chemical liquid raw material attemperator
Technical field
This utility model relates to a kind of chemical liquid raw material attemperator.
Background technology
In chemical products production process, a lot of liquid charging stocks add in reactor after needing insulation uniform temperature, existing conventional liquid charging stock heat preserving mode is to be inserted into electric heater at the storage container of liquid charging stock to heat, but the temperature around electric heater is high, outer liquid temperature volume, uneven in temperature even, will also result in spoilage problems near the liquid charging stock of electric heater because temperature is too high simultaneously.
Summary of the invention
This utility model is in order to overcome the deficiency of above technology, it is provided that one guarantees stay-in-grade chemical liquid raw material insulation dress when chemical liquid raw material is incubated.
This utility model overcomes its technical problem be the technical scheme is that
A kind of chemical liquid raw material attemperator, including: for storing the fuel tank of conduction oil, inside is provided with the heat exchange box of sealed volume, it is arranged at the spiral heat exchanger tube in sealed volume, it is arranged in sealed volume and is positioned at the shower nozzle directly over heat exchanger tube, it is arranged at the electric heater in fuel tank and for storing the liquid storing barrel of liquid charging stock, it is provided with leakage fluid dram bottom described liquid storing barrel, described leakage fluid dram is provided with valve, described shower nozzle is connected with tank bottoms through oil pump by flowline, it is connected with fuel tank upper end by oil return pipe bottom described heat exchange box, described liquid storing barrel one end is connected with the inlet of heat exchanger tube through pump by feed tube, its other end is connected with the liquid outlet of heat exchanger tube by liquid back pipe.
In order to make the liquid charging stock homogeneous temperature in liquid storing barrel, also include support, described liquid storing barrel two ends rotate respectively through hollow axle and are installed on support, and described feed tube is connected with the hollow axle of homonymy respectively through swivel joint with liquid back pipe, and the hollow axle of one end is connected with motor-driven.
The beneficial effects of the utility model are: electric heater is by the heat-conducting oil heating in fuel tank, conduction oil after heating is ejected on the heat exchanger tube in heat exchange box by oil pump by shower nozzle, by feed tube, the liquid charging stock in liquid storing barrel is pumped into the conduction oil that in heat exchanger tube, also shower nozzle sprays about pump and carry out heat exchange, it is achieved thereby that the purpose of heating liquid charging stock, owing to liquid charging stock and thermal source are not directly contacted with, therefore effectively prevent the too high situation causing liquid charging stock rotten of heat source temperature to occur, improve production efficiency.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure, 1. fuel tank 2. electric heater 3. heat exchange box 4. oil return pipe 5. oil pump 6. flowline 7. shower nozzle 8. heat exchanger tube 9. feed tube 10. pump 11. liquid back pipe 12. support 13. hollow axle 14. swivel joint 15. motor 16. liquid storing barrel 17. leakage fluid dram 18. valve.
Detailed description of the invention
Below in conjunction with accompanying drawing 1, this utility model is described further.
A kind of chemical liquid raw material attemperator, including: for storing the fuel tank 1 of conduction oil, inside is provided with the heat exchange box 3 of sealed volume, it is arranged at the spiral heat exchanger tube 8 in sealed volume, it is arranged in sealed volume and is positioned at the shower nozzle 7 directly over heat exchanger tube 8, it is arranged at the electric heater 2 in fuel tank 1 and for storing the liquid storing barrel 16 of liquid charging stock, leakage fluid dram 17 it is provided with bottom liquid storing barrel 16, leakage fluid dram 17 is provided with valve 18, shower nozzle 7 is connected with bottom fuel tank 1 through oil pump 5 by flowline 6, it is connected with fuel tank 1 upper end by oil return pipe 4 bottom heat exchange box 3, liquid storing barrel 16 one end is connected through the inlet of pump 10 with heat exchanger tube 8 by feed tube 9, its other end is connected with the liquid outlet of heat exchanger tube 8 by liquid back pipe 11.Electric heater 2 is by the heat-conducting oil heating in fuel tank 1, conduction oil after heating is ejected on the heat exchanger tube 8 in heat exchange box 3 by oil pump 5 by shower nozzle 7, liquid charging stock in liquid storing barrel 16 is pumped into the conduction oil that in heat exchanger tube 8, also shower nozzle 7 sprays by feed tube 9 and carries out heat exchange by pump about 10, it is achieved thereby that the purpose of heating liquid charging stock, owing to liquid charging stock and thermal source are not directly contacted with, therefore effectively prevent the too high situation causing liquid charging stock rotten of heat source temperature to occur, improve production efficiency.Conduction oil after heat exchange returns fuel tank 1 by oil return pipe 4, and the liquid charging stock after heat exchange returns liquid storing barrel 16 by liquid back pipe 11, it is achieved that circulation.The liquid charging stock of insulation in liquid storing barrel 16 can be discharged use by leakage fluid dram 17 by Open valve 18, simple to operation.
Further, also including support 12, liquid storing barrel 16 two ends rotate respectively through hollow axle 13 and are installed on support 12, and feed tube 9 is connected with the hollow axle of homonymy respectively through swivel joint 14 with liquid back pipe 11, and hollow axle 13 and the motor 15 of one end are in transmission connection.Motor 15 rotates and drives liquid storing barrel 16 to rotate, liquid in liquid storing barrel 16 enters in feed tube 9 by swivel joint 14, will not leakage, and the liquid of liquid back pipe 11 enters in liquid storing barrel 16 by swivel joint 14, owing to liquid storing barrel 16 rotates always, therefore its internal liquid charging stock can remain stirring, and the temperature making liquid is more uniform, it is to avoid the problem generation that liquid charging stock is uneven in temperature.

Claims (2)

  1. null1. a chemical liquid raw material attemperator,It is characterized in that,Including: for storing the fuel tank (1) of conduction oil、Inside is provided with the heat exchange box (3) of sealed volume、It is arranged at the spiral heat exchanger tube (8) in sealed volume、It is arranged in sealed volume and is positioned at the shower nozzle (7) directly over heat exchanger tube (8)、It is arranged at the electric heater (2) in fuel tank (1) and for storing the liquid storing barrel (16) of liquid charging stock,Described liquid storing barrel (16) bottom is provided with leakage fluid dram (17),Described leakage fluid dram (17) is provided with valve (18),Described shower nozzle (7) is connected with fuel tank (1) bottom through oil pump (5) by flowline (6),Described heat exchange box (3) bottom is connected with fuel tank (1) upper end by oil return pipe (4),Described liquid storing barrel (16) one end is connected through the inlet of pump (10) with heat exchanger tube (8) by feed tube (9),Its other end is connected with the liquid outlet of heat exchanger tube (8) by liquid back pipe (11).
  2. 2. chemical liquid raw material attemperator according to claim 1, it is characterized in that: also include support (12), described liquid storing barrel (16) two ends rotate respectively through hollow axle (13) and are installed on support (12), described feed tube (9) is connected with the hollow axle of homonymy respectively through swivel joint (14) with liquid back pipe (11), and the hollow axle (13) of one end and motor (15) are in transmission connection.
CN201620182202.7U 2016-03-10 2016-03-10 Chemical engineering liquid raw materials heat preservation device Expired - Fee Related CN205403152U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620182202.7U CN205403152U (en) 2016-03-10 2016-03-10 Chemical engineering liquid raw materials heat preservation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620182202.7U CN205403152U (en) 2016-03-10 2016-03-10 Chemical engineering liquid raw materials heat preservation device

Publications (1)

Publication Number Publication Date
CN205403152U true CN205403152U (en) 2016-07-27

Family

ID=56440482

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620182202.7U Expired - Fee Related CN205403152U (en) 2016-03-10 2016-03-10 Chemical engineering liquid raw materials heat preservation device

Country Status (1)

Country Link
CN (1) CN205403152U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111720997A (en) * 2020-05-20 2020-09-29 广州文冲船厂有限责任公司 Heating device is washed to boats and ships pipeline cluster

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111720997A (en) * 2020-05-20 2020-09-29 广州文冲船厂有限责任公司 Heating device is washed to boats and ships pipeline cluster

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Legal Events

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

Granted publication date: 20160727

Termination date: 20190310

CF01 Termination of patent right due to non-payment of annual fee