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METHOD FOR PRODUCTION AND AUTOMATION OF CONTROL SYSTEM FOR N,N-DIMETHYLACETAMIDE PRODUCTION PROCESSES

机译:N,N-二甲基乙酰胺生产过程的控制系统的生产和自动化方法

摘要

FIELD: chemistry.;SUBSTANCE: method includes feeding gaseous dimethylamine and acetic acid into a tubular catalytic reactor, in the inter-tubular space of which a high-temperature heat carrier is fed in at least two points at different heights; reaction products are fed into a first fractionation column for distillation of unreacted dimethylamine, the vapour of which is returned into the reactor from the top of the column. The distillate from the first column is fed into the bottom of a second fractionation column for separating the aqueous-amine fraction, and the still residue is fed into a third fractionation column. The second fractionation column operates in periodic mode and its operating cycle consists of a dimethylamine distillation step, a technical acetone distillation step, a water-acetone fraction distillation step and a bottom residue discharge step. Technical dimethylacetamide in distillate form is fed from the third fractionation column into a fourth fractionation column where low-boiling fractions are distilled from dimethylacetamide. The bottom residue from the fourth fractionation column is fed into a fifth fractionation column where commercial-grade N,N-dimethylacetamide is distilled in distillate form, and the bottom residue is returned to the third fractionation column. An automated control system for the process of producing N,N-dimethylacetamide comprises three subsystems: a subsystem for automated adjustment of the ratio of the flow rates of acetic acid and dimethylamine fed into the reactor, a subsystem for automated control of the reactor and a subsystem for automated control of second fractionation column.;EFFECT: method enables to obtain N,N-dimethylacetamide with high output and a reduced amount of wastes.;2 cl, 1 dwg, 1 ex
机译:技术领域:方法:包括将气态二甲胺和乙酸进料到管式催化反应器中,在管间空间中,在至少两个点处以不同的高度进料高温载热体。将反应产物进料到第一分馏塔中以蒸馏未反应的二甲胺,其蒸气从塔顶返回到反应器中。将来自第一塔的馏出物进料到第二分馏塔的底部以分离胺水部分,并且将残余物进料到第三分馏塔。第二分馏塔以周期性模式操作,并且其操作周期包括二甲胺蒸馏步骤,工业丙酮蒸馏步骤,水-丙酮馏分蒸馏步骤和底部残留物排出步骤。将馏出物形式的工业二甲基乙酰胺从第三分馏塔供入第四分馏塔,在第四分馏塔中从二甲基乙酰胺蒸馏出低沸点馏分。将来自第四分馏塔的底部残余物进料至第五分馏塔,在其中以馏出物形式蒸馏工业级的N,N-二甲基乙酰胺,并将底部残余物返回至第三分馏塔。用于生产N,N-二甲基乙酰胺的过程的自动控制系统包括三个子系统:一个用于自动调节进料到反应器中的乙酸和二甲胺流速比的子系统,一个用于自动控制反应器的子系统和一个子系统:用于第二个分馏塔自动控制的子系统。效果:该方法能够获得高产量,减少废物量的N,N-二甲基乙酰胺。2cl,1 dwg,1 ex

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