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DRIZO UNIT COMPETES WITH SOLID BED DESICCANT DEHYDRATION

机译:DRIZO装置与固体床干燥剂脱水竞争

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The patented Drizo Gas Dehydration process is a glycol enhancement process using a commonly available hydrocarbon solvent to counter current contact semi-lean glycol to affect a very high glycol purity to the gas-glycol contactor. An improvement, drying the hydrocarbon liquid solvent with a small solid bed dryer prior to solvent vaporization, has permitted a measured 99.999 wt. % TEG glycol purity, with consistent exit water outlet content of 0.1 ppm or less for a measurable dew point depression of at least 135 C (243 F). This corresponds to a +30C (86F) contactor temperature with a -108C (-162F)* demethanizer reflux processing temperature. The M.O.L. design criteria was a water dew point of -85C (-121F) at 16 Barg (232 Psig) 7,8 and demethanizer reflux flow dew point of -108C (-162F) at 16 Barg (232 Psig), relating to an exit water content of the contactor between 0.1 and 0.16 ppm. The unit has been running at a consistent outlet water content of less than design values on a continuous basis for over a year. This paper will relate the site experience of this singular unit at the M.O.L. Szeged Gas Treating facility.
机译:获得专利的Drizo气体脱水工艺是乙二醇增强工艺 使用常用的碳氢化合物溶剂来逆流接触半 贫乙二醇会影响气-乙二醇接触器的乙二醇纯度。一个 改进,用小型固体床干燥机干燥烃类液体溶剂 在溶剂汽化之前,已允许测得99.999 wt。 %TEG乙二醇 纯度高,对于一口水,出口的出水水含量始终不超过0.1 ppm 可测量的露点压降至少为135 C(243 F)。这对应于一个 + 30C(86F)接触器温度,-108C(-162F)*脱甲烷塔回流 处理温度。 M.O.L.设计标准的水露点为- 85巴(-121F)在16巴(232 Psig)7,8和脱甲烷塔回流露点为- 108 C(-162F)在16 Barg(232 Psig)下,与 接触器介于0.1和0.16 ppm之间。该单元一直以一致的速度运行 连续超过一个小于设计值的出口水含量 年。本文将介绍该单个单元在M.O.L.的现场体验。 塞格德气体处理厂。

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