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Emissions Estiation Expressions for Vessel Depressurization in Batch Chemical

机译:批量化学品中容器降压的排放估算表达式

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摘要

Emissions estimation expressions are presented for vessel depressurization in batch chemical operation where inert gas pressurizes a VOC-containing material. The expressions are compared to the procedure in EPA's Gideline Series. An obvious first improvement is the expressions presented here apply to a wider range of conditions - both initial VOC saturation and constant VOC saturation of depressurized gas and both uncontrolled and condenser-controlled emissions. A second improvement is EPA's procedure may over-estimate emissions by employing an average VOC composition during depressurization based on an assumed linear profile between initial and final compositions. The overestimate increases with increasing initial system pressure and VOC volatility, which itself increases with temperature. A third improvement is the capability to estimate, through the use of uncontrolled and controlled emissions estimation expressions, the control device efficiency and its sensitivity to operational flexibilties, like changes in temperature, pressure and product formulation. Industrial operations benefiting from these emissions estimation expressions include depressurization following closed-vessel filtration of VOC-containing material and depressurization of a VOC-containing reaction vessel blanketed by inert gas.
机译:给出了用于分批化学操作中容器减压的排放估算表达式,其中惰性气体对含VOC的材料加压。将表达式与EPA Gideline系列中的程序进行比较。一个明显的第一个改进是,此处介绍的表达式适用于范围更广的条件-减压气体的初始VOC饱和度和恒定VOC饱和度,以及不受控制和由冷凝器控制的排放。第二个改进是EPA的程序可能会根据初始和最终成分之间的线性关系,在减压过程中采用平均VOC成分,从而高估排放量。高估随着初始系统压​​力和VOC挥发性的增加而增加,VOC挥发性本身随温度而增加。第三个改进是通过使用不受控制和受控的排放估算表达式来估算控制设备效率及其对操作灵活性(如温度,压力和产品配方变化)的敏感性的能力。受益于这些排放量估算表达式的工业运营包括:对包含VOC的材料进行密闭容器过滤后的减压,以及对被惰性气体覆盖的VOC的反应容器的减压。

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