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Preparation method of cellulose ether and cellulose ether obtained in same

A technology of cellulose ether and cellulose powder, applied in the field of cellulose ether, can solve the problems of poor light transmittance, low filtration loss reduction effect, low water retention rate, etc., and achieves high temperature stability and mildew resistance improvement, preparation method Simple and easy to implement, the effect of filtration reduction effect is improved

Active Publication Date: 2015-12-02
广东龙湖科技股份有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the production process of cellulose ether, due to equipment, process, operation and other reasons, it is very easy to have the problem of incomplete and uneven reaction of raw materials, and the incomplete and uneven reaction of raw materials will cause the product to contain raw fiber and hemicellulose ether , this part of raw fiber and hemicellulose ether will bring the following problems to the product: 1. After being dissolved in water, the solution will be turbid and the light transmittance will be poor; 2. The water retention rate is low, which will affect the workability and the full hydration of cement; 3. 1. Poor mildew resistance, easy to be corroded and deteriorated by mold; 4. High temperature resistance or high temperature stability is poor; 5. The product is fuzzy, fluffy, low specific gravity, and heavy dust, which makes it difficult for workers to pick up materials and pack them; 6. There are many tail air materials , not easy to handle, low product yield; 7, as a fluid loss control agent, the fluid loss control effect is low; 8, the excess lye in the system after the reaction is not effectively utilized; 9, the raw fiber and semi Cellulose ethers will put pressure on sewage treatment
In the existing cellulose ether preparation method, once the etherification reaction is completed, the product performance is basically determined, and the problematic products caused by incomplete and uneven reactions can only be added and diluted in a small amount in the subsequent mixing process. However, due to the continuity of chemical production, there will often be a backlog of a large number of unqualified products, coupled with more tailings, lower product yields, and pressure from sewage treatment, resulting in increased costs and difficult sales, which seriously affect the benefits of manufacturers.

Method used

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  • Preparation method of cellulose ether and cellulose ether obtained in same

Examples

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Effect test

Embodiment 1

[0019] (1) Preparation of lye: first prepare 7000L of mixed solvent, the mixed solvent is the mass ratio: isopropanol / (isopropanol+toluene)=0.13, add 5000L of mixed solvent, 450Kg For solid NaOH, heat up and stir until the solid alkali is completely dissolved, then cool down to 20±1°C;

[0020] (2) Crushing the refined cotton into cotton powder;

[0021] (3) Add 800Kg of cotton powder into the reaction kettle, spray with the remaining 2000L of mixed solvent while adding cotton powder, and stir for 1.5h at a temperature equal to or lower than 20°C after the addition is complete;

[0022] (4) Add 180Kg propylene oxide and 590Kg methyl chloride to the reactor, and keep warm for 90 minutes when the temperature is raised to 54°C and 87°C;

[0023] (5) Desolventize the material in the reactor for not less than 1.5 hours;

[0024] (6) Add 25Kg of analytically pure acrylic acid: acrylamide = 4:1 mixed solution, 0.025Kg of potassium persulfate, stir for 35min at a temperature not low...

Embodiment 2

[0029] (1) Preparation of lye: first prepare 8000L of mixed solvent, the mixed solvent is the mass ratio: isopropanol / (isopropanol+toluene)=0.19, add 7000L of mixed solvent, 850Kg For solid NaOH, heat up and stir until the solid alkali is completely dissolved, then cool down to 26±1°C;

[0030] (2) Crushing the refined cotton into cotton powder;

[0031] (3) Add 880Kg of cotton powder into the reaction kettle, spray with the remaining 1000L of mixed solvent while adding cotton powder, and stir for 2 hours at a temperature equal to or lower than 26°C after the feeding is completed;

[0032] (4) Add 310Kg propylene oxide and 1000Kg methyl chloride to the reactor, and keep warm for 2 hours when the temperature is raised to 54°C and 87°C;

[0033] (5) Desolventize the material in the reactor for not less than 1.5 hours;

[0034] (6) Add 20Kg of analytically pure acrylic acid: acrylamide = 6:1 mixed solution, 0.02Kg of potassium persulfate, stir for 40min at a temperature not low...

Embodiment 3

[0039] (1) Preparation of lye: first prepare 7500L of mixed solvent, the mixed solvent has a mass ratio of isopropanol / (isopropanol+toluene)=0.16, add 7000L of mixed solvent, 500Kg For solid NaOH, heat up and stir until the solid alkali is completely dissolved, then cool down to 24±1°C;

[0040] (2) Crushing the refined cotton into cotton powder;

[0041] (3) Add 850Kg cotton powder into the reaction kettle, and spray with the remaining 500L mixed solvent while adding cotton powder. After the feeding is completed, stir at a temperature equal to or lower than 24 for 2 hours;

[0042](4) Add 240Kg propylene oxide and 700Kg methyl chloride to the reactor, and keep warm for 90min and 2h when the temperature is raised to 54°C and 87°C respectively;

[0043] (5) Desolventize the material in the reactor for not less than 1.5 hours;

[0044] (6) Add analytically pure acrylic acid: acrylamide = 9:1 mixed solution 10Kg, ammonium persulfate 0.01Kg, stir at a temperature not lower than ...

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Abstract

The invention provides a preparation method capable of improving various performances and especially a water retention rate and light transmittance of cellulose ether. The method comprises an alkalization step, an etherification step, a desolvation step, an acid regulation step and a posttreatment step of cellulose powder, wherein the acid regulation step is as follows: adding an acrylic acid / acrylamide mixed solution accounting for 1.0 to 3.5 percent by weight of the cellulose powder and initiator accounting for 0.1 to 0.13 percent by weight of the mixed solution, stirring for 10 to 40 minutes under the condition that the temperature is not lower than 90 DEG C, determining the pH value to be 5.5 to 8.5, and then discharging the material, wherein the acrylic acid / acrylamide mixed solution consists of acrylic acid and acrylamide in a mass ratio of (3 to 9): 1, and the initiator is potassium persulfate or ammonium persulfate. The preparation method is simple and easy, the problem of poor reaction at the etherification period can be overcome by utilizing the step for systematically adjusting the pH value, the cellulose ether obtained in the method hardly contains fibers and semi-cellulose ether, so that the light transmittance, water retention property and filtration reduction effect are obviously improved. The invention also provides cellulose ether obtained by the preparation method.

Description

technical field [0001] The present invention relates to a method for preparing cellulose ether, in particular to a method for preparing cellulose ether by a solvent method, and more particularly to a preparation method capable of improving various properties of cellulose ether, especially water retention and light transmittance method. The present invention also relates to a cellulose ether obtained by the above method. Background technique [0002] Cellulose ether is the most commonly used additive in dry powder mortar. As a water retaining agent, it can prevent the moisture in the wet mortar from evaporating prematurely or being absorbed by the base layer, and ensure that the cement is fully hydrated, thereby ensuring the mechanical properties of the mortar. There are various production processes of cellulose ether, including solvent method and gas-solid method. Compared with the production of cellulose ether by gas-solid method, the production process of cellulose ether ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08B11/20C08B11/02C08B11/08C08B31/08C08F251/02C08F220/06C08F220/56C08F251/00
Inventor 刘晓清洪永顺
Owner 广东龙湖科技股份有限公司
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