Production method of vinyl acetate
A vinyl acetate and vinyl acetate technology, applied in the field of vinyl acetate production, can solve the problems of high energy consumption and low product yield
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2021-01-12
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Abstract
Description
technical field
[0001] The invention relates to a method and a device for producing vinyl acetate, in particular to a production method for vinyl acetate that improves product yield, reduces waste discharge, and reduces material and energy consumption. Background technique
[0002] Vinyl acetate (VAC), also known as vinyl acetate, is an important organic chemical raw material. Through self-polymerization or copolymerization with other monomers, vinyl acetate can produce polyvinyl alcohol (PVA), vinyl acetate-ethylene copolymer (EVA), polyvinyl acetate (PVAC), vinyl acetate-vinyl chloride copolymer (EVC) and other products . These products have a wide range of uses, and are generally used in adhesives, sizing agents for paper or fabrics, paints, inks, leather processing, emulsifiers, water-soluble films, soil conditioners, etc. In 2018, my country's vinyl acetate production capacity was about 3.318 million tons per year, accounting for about 40% of the global production cap...
Examples
Embodiment Construction
[0050] The method and device for removing ethyl acetate in the vinyl acetate production process proposed by the present invention mainly include an extractive distillation tower system and an ethyl acetate tower (405) system. The following is a description of the method and device of the present invention in conjunction with the accompanying drawings.
[0051] The present invention passes figure 1 , figure 2 , image 3 The method shown implements:
[0052] Specifically, fresh ethylene enters the lower part of the acetic acid evaporator (103) after being mixed with the circulating gas from the circulating gas compressor (101), and is mixed with the fresh acetic acid from the acetic acid tower (201) in the rectification section and the fresh acetic acid from the ethylene recovery tower (117). countercurrent contact. The mixed gas of ethylene and acetic acid obtained at the top of the acetic acid evaporator (103) is further mixed with fresh oxygen in the oxygen mixer (106) an...