Fractional distillation equipment for separating propargyl alcohol and method of equipment

A technology of propynyl alcohol and rectification tower, which is applied in the field of fractionation equipment for separating propynyl alcohol, can solve the problems of high energy consumption, achieve the effects of simplifying the separation process, improving product quality, and improving the separation capacity of the equipment

Active Publication Date: 2012-10-17
NORTHEAST PHARMA GRP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In the above process, butynediol needs to be over-concentrated at high temperature to remove low-boiling impurities such as propynyl alcohol and formaldehyde. At the same time, 90% of the water is distilled and cooled repeatedly, which consumes a lot of energy.

Method used

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  • Fractional distillation equipment for separating propargyl alcohol and method of equipment
  • Fractional distillation equipment for separating propargyl alcohol and method of equipment

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Embodiment Construction

[0010] With reference to the accompanying drawings, the following embodiments will help to understand the present invention, but these embodiments are only for illustrating the present invention, and the present invention is not limited to these contents.

[0011] A fractionation equipment for separating propynyl alcohol, comprising a double wall tower 1, a rectification tower stripping section 2, a rectification tower rectification section 3, a rectification tower condenser 4, a vacuum evaporator 5, and a rectification tower tail cooler 6 , a reflux tank 7, a heater 8, a vacuum evaporator cooler 9, a mixture feed port 10, a first pipeline 11, a second pipeline 12, and a third pipeline 13. The sandwiched wall tower 1 is composed of a stripping section. The top of the wall tower 1 is provided with a lye feed inlet; the rectification tower is composed of a rectification tower stripping section 2 and a rectification tower rectification section 3, between the rectification tower st...

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Abstract

The invention discloses fractional distillation equipment for separating propargyl alcohol and a method of the equipment, which are applied to the field of chemical separation. The fractional distillation equipment comprises a clamping wall tower, a rectifying tower stripping section, a rectifying tower rectifying section, a rectifying tower condenser, a vacuum evaporator, a rectifying tower tail cooler, a return tank, heaters and a vacuum evaporator cooler, wherein the clamping wall tower comprises stripping sections; an alkali liquor feeding hole is formed on the top of the clamping wall tower; the rectifying tower consists of the rectifying tower stripping section and the rectifying tower rectifying section; a mixture feeding hole and a demister are arranged between the rectifying tower stripping section and the rectifying tower rectifying section; the clamping wall tower is coupled to the rectifying tower; the clamping wall tower and the rectifying tower are connected with the heaters respectively; the rectifying tower is connected with the rectifying tower condenser; the rectifying tower condenser is connected with the rectifying tower tail cooler and the return tank; and the return tank is connected with the top of the rectifying tower through a first pipeline and is connected with a propargyl alcohol recovery pipeline. The concentration process is omitted, the concentration and propargyl alcohol concentration extraction are integrated, the process of separating the propargyl alcohol from butynediol is simplified, the production efficiency is improved, the multi-effect energy-saving technologies such as thermal coupling and thermal networking are adopted, and the product quality is improved.

Description

[0001] The present invention relates to a fractionation equipment and method for separating propynyl alcohol in the field of chemical separation. Background technique [0002] Propargyl alcohol is an important chemical raw material, mainly used in various industries such as pharmaceutical chemical industry, electroplating pesticide and oil drilling. At present, the industrialized production of propynyl alcohol basically adopts the Reppe method production process, which was first successfully developed by the German scholar Reppe and the country's IG company in 1937, using formaldehyde aqueous solution and acetylene as raw materials, and acetylene copper as a catalyst for joint production Proynyl alcohol and butynediol increase the partial pressure of acetylene in the reaction, and the production ratio of propynyl alcohol increases accordingly. Therefore, when the target product is propynyl alcohol, the acetylene pressure of 1.0-2.0MPa is generally used, and the propynyl alcohol...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D3/14B01D1/00C07C33/046C07C33/042C07C29/80C07C29/78
Inventor 汲涌张春玲刘宪成侯凤阳王远航吕栋英陈阳巴剑华高云生魏志君
Owner NORTHEAST PHARMA GRP
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