28-01-2015 дата публикации
Номер: CN104311596A
Принадлежит:
The invention discloses a 2-phosphonobutane-1,2,4-tricarboxylic acid production hydrolysis continuous technology. In a pentaester hydrolysis process, 2-phosphonobutane-1,2,4-tricarboxylic acid pentaester obtained by esterification addition is sprayed into a hydrolysis tower by a sprayer at the top of the hydrolysis tower, vapor is input into the hydrolysis tower from the bottom of the hydrolysis tower, the atomized 2-phosphonobutane-1,2,4-tricarboxylic acid pentaester contacts with raising vapor between tower plates and is hydrolyzed to produce a 2-phosphonobutane-1,2,4-tricarboxylic acid aqueous solution, the 2-phosphonobutane-1,2,4-tricarboxylic acid aqueous solution is collected at the tower bottom and is fed into a material storage tank, and the produced methanol is gasified and then is condensed by a condenser, and the condensate is fed into a methanol rectification kettle. The 2-phosphonobutane-1,2,4-tricarboxylic acid production hydrolysis continuous technology realizes continuous ...
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