A kind of production method of acetone continuous dehydration

A production method and technology of acetone, applied in the field of continuous dehydration of acetone, can solve problems such as danger

Active Publication Date: 2016-02-24
SUZHOU JIMCEL ELECTRONICS NEW MATERIAL
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Molecular sieve will also adsorb a small amount of organic matter when it adsorbs moisture in organic matter. Therefore, if the molecular sieve is directly taken out for regeneration, there is a certain risk. After the regeneration of the molecular sieve is completed, the molecular sieve needs to be cooled and refilled.

Method used

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  • A kind of production method of acetone continuous dehydration

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Embodiment Construction

[0019] The present invention will be further described below in conjunction with embodiment.

[0020] figure 1 It is a process flow diagram of a production method of acetone continuous dehydration of the present invention, and its concrete process steps are:

[0021] Step 1), put the acetone stock solution in the acetone stock solution storage tank 1 into the first molecular sieve dehydrator 2 through the circulation pump 7, and flow back to the acetone stock solution storage tank 1 to continue the cycle dehydration, and put the dehydrated acetone into the middle of the acetone Tank 4, carry out the further purification of acetone by distillation system;

[0022] Step 2), when the molecular sieve in the first molecular sieve dehydrator 2 is saturated and adsorbed, close the acetone inlet and outlet valves of the first molecular sieve dehydrator 2, and pump the acetone to be dehydrated into the second molecular sieve dehydrator 3 through the circulation pump 7 , and flow back...

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Abstract

The invention discloses a production method of continuous acetone dehydration, belonging to the technical field of continuous acetone dehydration. The production method comprises the following concrete steps: (1) feeding acetone stock solution into a first molecular sieve dehydrator, enabling the acetone stock solution to flow back to an acetone stock solution storage tank for continuous dehydration; and after the acetone dehydration is finished, feeding dehydrated acetone into a middle tank and further purifying through a distillation system; (2) after a molecular sieve in the first molecular sieve dehydrator is in a saturation adsorption state, feeding acetone to be dehydrated into a second molecular sieve dehydrator, enabling acetone to flow back to the acetone stock solution storage tank for continuous dehydration, and regenerating the molecular sieve in the first molecular sieve dehydrator; (3) after a molecular sieve in the second molecular sieve dehydrator is in a saturation adsorption state, switching acetone to be dehydrated into the first molecular sieve dehydrator (in which molecular sieve regeneration is finished) for continuous dehydration, and regenerating the molecular sieve in the second molecular sieve dehydrator, thus forming a circle. According to the production method, the continuous acetone dehydration can be ensured and the dehydration and regeneration of the molecular sieves can be continuously carried out.

Description

technical field [0001] The invention belongs to the technical field of continuous dehydration of acetone, and in particular relates to a production method of continuous dehydration of acetone. Background technique [0002] During the reflux reaction carried out by acetone as a solvent, due to the moisture generated during the reaction and the moisture contained in the raw materials, if the water content in the reaction system exceeds a certain amount, the reaction will be difficult to carry out, affecting the yield and quality of the product. The acetone after the reaction needs to be dehydrated, usually by using a molecular sieve dehydrating agent. [0003] Although the molecular sieve dehydration process has a stable and efficient dehydration effect, the molecular sieve needs to be regenerated after saturated adsorption, and the existing technology is to take out the molecular sieve dehydrating agent separately for regeneration. Molecular sieves will also adsorb a small a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C49/08C07C45/79
CPCC07C45/79C07C49/08
Inventor 刘鸣于楼云刘利娟孙宇亮
Owner SUZHOU JIMCEL ELECTRONICS NEW MATERIAL
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