CN212390704U - High-temperature silicone oil rapid cooling system - Google Patents

High-temperature silicone oil rapid cooling system Download PDF

Info

Publication number
CN212390704U
CN212390704U CN202020999501.6U CN202020999501U CN212390704U CN 212390704 U CN212390704 U CN 212390704U CN 202020999501 U CN202020999501 U CN 202020999501U CN 212390704 U CN212390704 U CN 212390704U
Authority
CN
China
Prior art keywords
temperature
rapid cooling
cooling system
water
liquid
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.)
Active
Application number
CN202020999501.6U
Other languages
Chinese (zh)
Inventor
宋林协
王建文
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.)
SHENZHEN WANCE TEST EQUIPMENT CO Ltd
Original Assignee
SHENZHEN WANCE TEST 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 SHENZHEN WANCE TEST EQUIPMENT CO Ltd filed Critical SHENZHEN WANCE TEST EQUIPMENT CO Ltd
Priority to CN202020999501.6U priority Critical patent/CN212390704U/en
Application granted granted Critical
Publication of CN212390704U publication Critical patent/CN212390704U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The utility model discloses a quick cooling system of high temperature silicon oil, include: the circulating cooling liquid exchanges heat with the low-temperature liquid in the heat exchanger firstly, and then flows into the oil tank to exchange heat with high-temperature silicon oil to realize rapid cooling. The utility model discloses cooling temperature wide range, cooling temperature is low, through cryogenic liquids to oil tank rapid cooling, and cooling rate is fast, and economical and energy-conserving.

Description

High-temperature silicone oil rapid cooling system
Technical Field
The utility model relates to a testing machine field, more specifically relate to a quick cooling system of silicone oil for heat altered shape vicat softening point testing machine.
Background
In the thermal deformation Vicat softening point testing machine, the testing temperature of the silicone oil in the oil tank is up to 300 ℃, and after the test is finished, the silicone oil flows out of the oil tank and is cooled to a normal temperature state, and a long time is needed to wait. This cooling can have a significant effect on the efficiency of the test for users who require large amounts of test data. The experimental equipment in the industry needs to recycle the silicone oil, so that the time is very important, and the time cannot be wasted in the process of waiting for cooling. Therefore, aiming at the prior art, a high-temperature silicone oil cooling system special for a thermal deformation vicat softening point testing machine is urgently needed to be developed, so that the silicone oil is efficiently and quickly cooled, and the experiment efficiency is improved.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that overcome above-mentioned prior art not enough, provide a quick cooling system of high temperature silicon oil.
The utility model provides a technical scheme that above-mentioned technical problem adopted is: a high-temperature silicone oil rapid cooling system comprises: the circulating cooling liquid exchanges heat with the low-temperature liquid in the heat exchanger firstly, and then flows into the oil tank to exchange heat with high-temperature silicon oil to realize rapid cooling.
Further comprising: the tap water source is connected with the cold liquid tank in parallel, the tap water source is also connected into the heat exchanger cavity, when the oil temperature is higher than 100 ℃, the tap water is firstly used for carrying out heat exchange cooling, and when the oil temperature is between 25 and 100 ℃, the low-temperature liquid is used for carrying out heat exchange.
And a first electromagnetic valve and a second electromagnetic valve are respectively arranged on parallel pipelines of the tap water source and the cold liquid tank connected to the heat exchanger, and the two electromagnetic valves are used for respectively controlling the on-off states of the two cold sources.
And a first one-way valve is arranged on a pipeline connected with a water inlet port of the heat exchanger.
And a second one-way valve is arranged on one side of the heat exchange tube along the circulation direction of the high-temperature pump.
And a water outlet port of the heat exchanger is connected with a waste water tank, and cooling water after heat exchange is discharged into the waste water tank.
The low-temperature liquid is low-temperature water or antifreeze liquid with the temperature lower than 25 ℃.
And a water cooler is connected and installed on the cold liquid tank, and the water in the cold liquid tank is cooled through the water cooler.
Compared with the prior art, the beneficial effects of the utility model are that:
1. the cooling temperature range is wide, the cooling temperature of conventional equipment on the market generally does not exceed 150 ℃, and the system can cool high-temperature silicone oil with the temperature as high as 300 ℃, and the temperature range capable of being processed is wider.
2. The cooling temperature is low, in south areas, the temperature of tap water in summer can reach about 30 ℃, conventional equipment can not cool high-temperature silicon oil to 25 ℃ required by the standard at all, and the system utilizes 4 ℃ low-temperature water to cool the oil tank, so that the enough temperature difference is kept, and the effect of quick cooling is realized.
3. The cooling rate is fast, and conventional equipment is when using the running water to cool off, and when the difference in temperature of oil temperature and running water was within 25 ℃, the cooling process was very slow, and the time can reach more than 1h, and this system cools down the water of cold liquid incasement in advance through the cold water machine, when waiting the heat exchange efficiency of running water to reduce, switches on low-temperature water again and cools down.
4. The scheme of the system is economical and energy-saving, and the system is cooled by tap water within the range of 100-300 ℃, so that the power consumption is very low.
Drawings
In order to more clearly illustrate the technical solution in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments will be briefly introduced, wherein:
fig. 1 is a schematic diagram of the connection principle of the preferred embodiment of the present invention.
Detailed Description
The present invention will be further described with reference to the accompanying drawings and the detailed description. In the preferred embodiments, the terms "upper", "lower", "left", "right", "middle" and "a" are used for the sake of clarity only, and are not intended to limit the scope of the invention, its relative relationship between the terms and their derivatives, and the scope of the invention should be understood as being limited by the claims.
Referring to fig. 1, a high-temperature silicone oil rapid cooling system according to a preferred embodiment of the present invention mainly includes: the heat exchange tube in the oil tank 11 is coiled in the liquid cooling box 2, the water pump 3 and the bending, and the low-temperature water of 4 ℃ or so is stored in the liquid cooling box 2, and other temperature values lower than 25 ℃ can be stored, and the low-temperature water in the liquid cooling box 2 is conveyed to the heat exchange tube through the water pump 3, so that heat exchange is rapidly carried out, and high-temperature silicon oil is rapidly cooled.
Further comprising: the heat exchanger 7 is a specific cavity of the heat exchanger, and the water inlet and outlet ports of the heat exchanger are respectively communicated with the cavity. One end of the heat exchange tube is also bent and coiled in the heat exchanger 7, circulating cooling liquid is filled in the heat exchange tube and can be dimethyl silicon oil, a high-temperature pump 8 is arranged on the heat exchange tube, the circulating cooling liquid is circulated between the heat exchanger 7 and the oil tank 11 through the high-temperature pump 8, low-temperature water flowing out through the water pump 3 is connected to a water inlet port of the heat exchanger 7, and a water outlet port of the heat exchanger 7 is connected with the waste water tank 9 through a pipeline. By additionally arranging the heat exchanger 7, low-temperature water does not directly flow into the heat exchange tube, the heat exchange tube is favorable for circulating work, and the low-temperature water used by the heat exchanger 7 is collected through the waste water tank 9.
Further comprising: the tap water source 1, the tap water source 1 and the cold liquid tank 2 are connected in parallel, and the tap water source 1 is also connected to the water inlet port of the heat exchanger 7 through a pipeline. The temperature of tap water is usually defined by the industry to be 25-30 ℃, when the oil temperature is higher than 100 ℃, the tap water can be used for heat exchange cooling, and because the temperature difference is large enough, the rapid cooling can be realized to take away the heat of silicon oil; when the oil temperature is 25-100 ℃, the cooling speed is reduced due to the reduction of the temperature difference with tap water, and at the moment, heat exchange is carried out through low-temperature water at 4 ℃ to keep the effect of rapid cooling.
A tap water source 1 and a cold liquid tank 2 are connected to a parallel pipeline of a heat exchanger 7, a first electromagnetic valve 4 and a second electromagnetic valve 5 are respectively arranged on the parallel pipeline, and the on-off states of two cold sources are respectively controlled by the two electromagnetic valves.
A first check valve 6 is arranged on a pipeline connected with a water inlet port of the heat exchanger 7 to prevent the cooling water entering the heat exchanger 7 from flowing reversely.
And a second one-way valve 10 is arranged on one side of the heat exchange pipe along the circulation direction of the high-temperature pump 8 to prevent the circulating cooling liquid from flowing reversely.
The cold liquid tank 2 is connected with a water cooler, and the water in the cold liquid tank 2 is cooled by the water cooler. Or the low-temperature water is directly replaced by the antifreeze.
For the convenience of understanding the scheme, a concrete implementation method is briefly described:
firstly, after the equipment is started, a water cooler on the equipment is automatically started to cool water in a cold liquid tank, wherein the cooling temperature is controlled to be about 4 ℃, and the cooling time is controlled to be within 15 min;
secondly, starting the test, and raising the temperature of the oil in the oil tank to a specified test temperature which can reach 300 ℃ at most until the test is finished;
and thirdly, after the test is finished, starting a high-temperature silicone oil rapid cooling process:
1. the current oil temperature is measured by a temperature sensor in the oil tank, when the oil temperature is higher than 100 ℃, a first electromagnetic valve P1 is opened, a second electromagnetic valve P2 is closed, tap water flows through the first electromagnetic valve P1 and a first one-way valve, enters a heat exchanger cavity, exchanges heat with circulating cooling liquid in the heat exchanger cavity, and is discharged into a waste water tank;
2. after the process is finished, the high-temperature pump is started, the circulating cooling liquid in the cavity of the heat exchanger is conveyed to the oil tank through the heat exchange tube, the circulating cooling liquid and the high-temperature silicone oil are subjected to heat exchange rapidly, then the circulating cooling liquid returns to the heat exchanger, and the circulating cooling process of tap water can be repeated for multiple times until the temperature of the oil is reduced to be below 100 ℃;
3. monitoring the oil temperature through a temperature sensor in the oil tank, when the oil temperature reaches 100 ℃ or below, opening a second electromagnetic valve 5, closing a first electromagnetic valve, starting a water pump, enabling low-temperature water in a cold liquid tank to flow into a heat exchanger through the water pump, the second electromagnetic valve and a first one-way valve, exchanging heat, and discharging the low-temperature water into a waste water tank; repeating the step 2, wherein the high-temperature pump keeps a starting state in the process, and similarly, the circulating cooling process of the low-temperature water can be repeated for many times until the oil temperature is reduced to the specified temperature;
4. when the oil temperature in the oil tank is cooled to the designated temperature, the high-temperature pump stops running, the two electromagnetic valves are closed, the cooling process is finished, and the next test can be restarted.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention in any way, and any person skilled in the art can make any simple modification, equivalent change and modification to the above embodiments according to the technical spirit of the present invention without departing from the scope of the present invention.

Claims (8)

1. A high temperature silicon oil rapid cooling system is characterized by comprising: the circulating cooling liquid exchanges heat with the low-temperature liquid in the heat exchanger firstly, and then flows into the oil tank to exchange heat with high-temperature silicon oil to realize rapid cooling.
2. The high-temperature silicone oil rapid cooling system according to claim 1, further comprising: the tap water source is connected with the cold liquid tank in parallel, the tap water source is also connected into the heat exchanger cavity, when the oil temperature is higher than 100 ℃, the tap water is firstly used for carrying out heat exchange cooling, and when the oil temperature is between 25 and 100 ℃, the low-temperature liquid is used for carrying out heat exchange.
3. The high-temperature silicone oil rapid cooling system as claimed in claim 2, wherein a first solenoid valve and a second solenoid valve are respectively arranged on parallel pipelines of the tap water source and the cold liquid tank connected to the heat exchanger, and the on-off states of the two cold sources are respectively controlled by the two solenoid valves.
4. The high-temperature silicon oil rapid cooling system as claimed in claim 1, 2 or 3, wherein a first one-way valve is arranged on a pipeline connected with a water inlet port of the heat exchanger.
5. A high-temperature silicon oil rapid cooling system as claimed in claim 1, 2 or 3, wherein a second one-way valve is arranged on the heat exchange pipe along one side of the circulation direction of the high-temperature pump.
6. A high-temperature silicon oil rapid cooling system as claimed in claim 1, 2 or 3, wherein the water outlet port of the heat exchanger is connected with a wastewater tank, and cooling water after heat exchange is discharged into the wastewater tank.
7. A high-temperature silicone oil rapid cooling system according to claim 1, 2 or 3, characterized in that the low-temperature liquid is low-temperature water or antifreeze liquid with a temperature below 25 ℃.
8. The high-temperature silicon oil rapid cooling system as claimed in claim 1, 2 or 3, wherein a water cooler is connected to the cold liquid tank, and the liquid in the cold liquid tank is cooled by the water cooler.
CN202020999501.6U 2020-06-03 2020-06-03 High-temperature silicone oil rapid cooling system Active CN212390704U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020999501.6U CN212390704U (en) 2020-06-03 2020-06-03 High-temperature silicone oil rapid cooling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202020999501.6U CN212390704U (en) 2020-06-03 2020-06-03 High-temperature silicone oil rapid cooling system

Publications (1)

Publication Number Publication Date
CN212390704U true CN212390704U (en) 2021-01-22

Family

ID=74252650

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202020999501.6U Active CN212390704U (en) 2020-06-03 2020-06-03 High-temperature silicone oil rapid cooling system

Country Status (1)

Country Link
CN (1) CN212390704U (en)

Similar Documents

Publication Publication Date Title
CN111816894B (en) Fuel cell heat management device and control method thereof
CN101078532B (en) Device for heating using residual heat of sulfuric acid production
CN212390704U (en) High-temperature silicone oil rapid cooling system
CN210799287U (en) Novel high-efficient scale control thermostatic type air compressor machine waste heat recovery system
CN105576943B (en) A kind of high voltage direct current converter valve heat recovery system and its implementation
CN111486661A (en) High-temperature silicone oil rapid cooling system
CN206803293U (en) A kind of heating plant that net backwater heat is extracted once using heat pump
CN108555261A (en) Continuous casting and rolling automatic production line cooling water recirculation system
CN204514133U (en) Plate-type heat exchange system
CN108679685B (en) Central heating system for cooling circulating water by multi-path backwater sectional cooling
CN112676549A (en) Control system of high-temperature die temperature machine special for die casting
CN105792622A (en) Natural cooling system and method for data center
CN212458011U (en) Energy-saving circulating cooling system
CN205135941U (en) Hydrothermal air compressor machine waste heat recovery system of exportable multiple temperature
CN104848593A (en) Printing and dyeing heat-treating machine and control method thereof
CN1280471C (en) Water out split flow equipment of exchanger for dyeing machine
CN211843379U (en) Segmented energy-saving cooling system of press
CN215337826U (en) Cooling device and coating test line thereof
CN203518712U (en) Heavy oil/heat transfer oil heat exchanger
CN104567491B (en) Plate-type heat exchange system
CN217900578U (en) Waste heat recovery system of air compressor
CN219907007U (en) Heat energy utilization system of polycrystalline silicon reduction furnace
CN211451530U (en) Water cooling system
CN217876460U (en) Multifunctional heat-conducting oil heating temperature control system
CN212688132U (en) Box quenching furnace circulative cooling system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant