A kind of preparation method of high temperature synthetic heat conduction oil

A heat-conducting oil and high-temperature technology, which is applied in the field of high-temperature synthetic heat-conducting oil preparation, can solve problems such as high operating temperature, inability to produce, and low saturated steam pressure, and achieve the effects of less reaction steps, low cost, and high flash point

Active Publication Date: 2021-09-07
SHE COUNTY JINDONG ECONOMIC & TRADE CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, there are still many kinds of synthetic heat transfer oil that cannot be produced domestically and can only be imported. Dowtherm RP produced by Dow Chemical in the United States belongs to this category, which is 1,2,3,4-tetrahydro-1-(1 -Isomer mixture of -phenethyl)naphthalene and 1,2,3,4-tetrahydro-5-(1-phenethyl)naphthalene
It has the advantages of high operating temperature, low saturated steam pressure, and good thermal stability. At present, there is no domestic production, and customers can only rely on imports.

Method used

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  • A kind of preparation method of high temperature synthetic heat conduction oil
  • A kind of preparation method of high temperature synthetic heat conduction oil
  • A kind of preparation method of high temperature synthetic heat conduction oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1 4

[0028] The synthesis of embodiment 1 tetrahydronaphthalene

[0029]

[0030] Put naphthalene into the autoclave, add 3.1% Raney nickel, after gas replacement, raise the temperature to 180°C and stir, then introduce hydrogen, the pressure is 3.0Mpa, after the reaction is completed, cool down to room temperature, remove Raney nickel, and rectify and separate of tetrahydronaphthalene.

Embodiment 2

[0031] Example 2 Synthesis of heat transfer oil

[0032]

[0033]

[0034] Add 400g tetrahydronaphthalene in the reactor, add 1600g of carbon tetrachloride, add 12g of aluminum trichloride, stir, then dropwise add 226g of styrene, the dropping temperature is the reflux temperature of carbon tetrachloride, after the dropwise addition Heat preservation reaction for 3 hours, add 36g of water, then stand to separate layers, separate the water layer, and rectify and separate to obtain the finished product, which is analyzed by gas chromatography: 1,2,3,4-tetrahydro-1-(1-phenylethyl ) naphthalene and 1,2,3,4-tetrahydro-5-(1-phenylethyl)naphthalene ratio is 8:2, kinematic viscosity is 15mm 2 / S, the boiling point is 338°C under standard conditions, and the flash point (opening) is 196°C.

Embodiment 3

[0035] Example 3 Synthesis of heat transfer oil

[0036]

[0037]

[0038] Add 400g of tetrahydronaphthalene in the reactor, add 2400g of dichloroethane, add 20g of sulfuric acid, stir, then dropwise add 226g of styrene, the dropping temperature is the reflux temperature of carbon tetrachloride, after the dropping, keep warm for 3 hour, add 100g of water, then let stand to separate layers, separate the water layer, and rectify and separate to obtain the finished product, which is analyzed by gas chromatography: 1,2,3,4-tetrahydro-1-(1-phenylethyl)naphthalene and The ratio of 1,2,3,4-tetrahydro-5-(1-phenylethyl)naphthalene is 8:2, and the kinematic viscosity is 15mm 2 / S, the boiling point is 338°C under standard conditions, and the flash point (opening) is 196°C.

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Abstract

The invention relates to a preparation method of high-temperature synthetic heat transfer oil, which comprises: putting naphthalene into an autoclave, adding 2.5%~3.8% catalyst, after gas replacement, raising the temperature to 150~300°C for stirring, feeding in hydrogen, and the pressure is 3.2~4.0Mpa, after the reaction, cool down, remove the catalyst, and rectify the separated tetralin; put the tetralin into the reaction kettle, add the solvent, then add 1%~5% acid catalyst, stir, and then drop Styrene, the molar ratio of styrene and tetrahydronaphthalene is 0.7~0.9:1, and the dropping temperature is 75~85℃. The water layer is separated by rectification to obtain finished products. The method provided by the invention has low raw materials, mild conditions, energy saving and consumption reduction, and is environmentally friendly. It is suitable for industrial mass production, effectively breaking the technical blockade of developed countries such as Europe and the United States on my country, and filling the domestic gap. .

Description

technical field [0001] The invention relates to the technical field of conductor heat flow, in particular to a preparation method of high-temperature synthetic heat-conducting oil. Background technique [0002] Heat transfer oil is an organic heat carrier, which is divided into synthetic type and mineral type. Mineral heat transfer oil is refined by adding additives to the distillate oil formed in the process of high temperature cracking or catalytic cracking of petroleum. The main component is hydrocarbon mixture; synthetic heat transfer oil is produced by chemical synthesis. Chemical structure and definite chemical name, the main feature is that the molecular structure contains aromatic hydrocarbon or cycloalkane structure, and most of them are bicyclic or tricyclic aromatic hydrocarbon compounds. [0003] Synthetic heat transfer oil has a wider temperature range and can be used at low, medium and high temperatures, while mineral heat transfer oil can only be used at low ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C09K5/10C07C2/68C07C2/72C07C7/04C07C15/12C07C5/11C07C13/48
CPCC07C2/68C07C2/72C07C5/11C07C7/04C07C2525/02C07C2527/126C09K5/10C07C2602/10C07C13/48C07C15/12
Inventor 詹石玉高双庆刘东东南彦冬
Owner SHE COUNTY JINDONG ECONOMIC & TRADE CO LTD
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