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A kind of anti-coking agent and preparation method thereof

A carbonation and modification technology, which is applied in chemical instruments and methods, natural water treatment, special compound water treatment, etc., can solve problems such as time-consuming and labor-intensive, affecting production progress, and reducing evaporator efficiency, so as to inhibit polymerization reaction, The effect of slowing down the speed of carbonization and easy water solubility

Active Publication Date: 2022-04-08
郑州卓而泰新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Wastewater contains a small amount of furfural and other organic paste-like by-products produced during the production of furfural. These substances are further polymerized and carbonized during the evaporation process of wastewater and adsorbed on the heat exchange tube wall inside the evaporator to gradually reduce the efficiency of the evaporator. After using for a period of time, clean up the carbon deposit on the evaporator, which is time-consuming and labor-intensive and affects the production progress
[0003] The problem of carbon formation in furfural wastewater evaporator is a common problem in the industry, and there is no solution in the market at present. Therefore, it is of great scientific significance and economic value to study the problem of anti-carbon formation in furfural wastewater evaporation.

Method used

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  • A kind of anti-coking agent and preparation method thereof
  • A kind of anti-coking agent and preparation method thereof
  • A kind of anti-coking agent and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] First prepare modified silicone oil according to the following steps:

[0033] a. Weigh a specified amount of allyl glycidyl ether into the reaction kettle, add platinum catalyst, the active ingredient of platinum catalyst is 0.002% of the mass of allyl glycidyl ether monomer, after stirring evenly, add hydrogen content of 1.5 %, hydrogen-containing silicone oil with a viscosity of 35mPa·s and cyclohexanone of equal mass, control the molar ratio of the Si-H bond of the hydrogen-containing silicone oil to the unsaturated double bond of the monomer to be 1:1, stir and heat to 60°C for 5h ;

[0034] b. Add a specified amount of diethanolamine to the reaction kettle, the molar ratio of the epoxy group to the diethanolamine molecule is 1:1.5, incubate at 80°C for 3 hours to remove unreacted diethanolamine and solvent cyclohexanone, That is, the modified silicone oil is obtained.

[0035] Finally, take the following components by weighing the following components relative t...

Embodiment 2

[0040] First prepare the modified silicone oil according to the following steps:

[0041] a. Weigh a specified amount of glycidyl acrylate and add it to the reaction kettle, add platinum catalyst, the active ingredient of platinum catalyst is 0.002% of the mass of glycidyl acrylate monomer, after stirring evenly, add hydrogen content of 1.3%, viscosity 100mPa s hydrogen-containing silicone oil and cyclohexanone of equal mass, control the molar ratio of the Si-H bond of the hydrogen-containing silicone oil to the unsaturated double bond of the monomer to be 1:1, stir and heat to 60°C for 5 hours;

[0042] b. Add a specified amount of diethanolamine to the reaction kettle, the molar ratio of the epoxy group to the diethanolamine molecule is 1:1.5, incubate at 80°C for 3 hours to remove unreacted diethanolamine and solvent cyclohexanone, That is, the modified silicone oil is obtained.

[0043] Finally, take the following components by weighing the following components relative t...

Embodiment 3

[0047] First prepare the modified silicone resin according to the following steps:

[0048] a. Weigh a specified amount of glycidyl methacrylate and add it to the reaction kettle, and add a platinum catalyst. The active ingredient of the platinum catalyst is 0.002% of the mass of glycidyl methacrylate monomer. After stirring evenly, add % Hydrogen-containing silicone oil with a viscosity of 20mPa·s and equal mass of cyclohexanone, control the molar ratio of the Si-H bond of the hydrogen-containing silicone oil to the unsaturated double bond of the monomer to be 1:1, stir and heat to 80°C for 5h.

[0049] b. Add a specified amount of diisopropanolamine to the reaction kettle, the molar ratio of epoxy groups to diisopropanolamine molecules is 1:1.5, and keep it at 80°C for 3 hours to remove unreacted diisopropanolamine by vacuum distillation. Propanolamine and solvent cyclohexanone are modified silicone oils.

[0050] Finally, take the following components by weighing the follo...

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Abstract

The invention belongs to the technical field of wastewater treatment produced by furfural production, and specifically provides an anti-coking agent, which is composed of the following content relative to the total mass percentage of the anti-coking agent: modified organic silicone oil 10-20%, 1-15% of organic acid, 1-5% of antioxidant, 1-3% of surfactant, and the balance of deionized water; the preparation method of this anti-coking agent is to weigh deionized water, organic acid, After the oxidizing agent is added into the reaction kettle A and stirred and dissolved evenly, the defoamer, surfactant and the prepared modified silicone oil are added in sequence, and after being stirred evenly, the anti-coking agent is obtained; the prepared anti-coking agent can obviously slow down The carbonation speed of the evaporator increases the cleaning cycle, and the carbonation is easier to soften and clean, which has obvious effects.

Description

technical field [0001] The invention belongs to the technical field of wastewater treatment produced by furfural production, and in particular relates to a preparation method of an anti-coking agent. Background technique [0002] As an important chemical raw material, furfural is widely used. Most of the current furfural production processes are prepared by dehydration after acid-catalyzed hydrolysis of pentosan-rich biomass (such as corncobs, bagasse) under high-temperature steam (160-180°C). After the furfural produced is discharged from the hydrolysis tank along with the high-temperature water vapor, the furfural product is obtained after distillation, concentration and purification. The waste water discharged from the distillation is heated and pressurized with high-temperature steam (180°C) in the evaporator, and then recycled. Because furfural has a certain solubility in water, and furfural is easy to thermally decompose and polymerize at high temperature. Wastewate...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08G77/388C02F1/04C02F5/12C02F5/10C02F103/36
CPCC02F1/042C02F5/12C02F5/10C08G77/388C02F2303/14C02F2305/04C02F2103/36
Inventor 李留帮蒋晓红丁宏卫冯俊波石耀杰
Owner 郑州卓而泰新材料科技有限公司