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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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摘要

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) 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气体脱水工艺是一种乙二醇增强工艺,它使用一种常用的烃类溶剂来逆流接触半贫乙二醇,从而使气-乙二醇接触器获得很高的乙二醇纯度。一种改进方法是在溶剂汽化之前用小型固体床干燥器干燥烃类液体溶剂,测定的重量比为99.999 wt。%。 %TEG乙二醇纯度,对于至少135 C(243 F)的可测量露点降低,一致的出口出水量为0.1 ppm或更低。这对应于+ 30C(86F)接触器温度和-108C(-162F)脱甲烷塔回流处理温度。 M.O.L.设计标准是16巴(232 Psig)时的-85C(-121F)的水露点和16巴(232 Psig)时的-108C(-162F)的脱甲烷气回流露点,涉及接触器介于0.1和0.16 ppm之间。该机组连续一年以恒定的出口水含量(低于设计值)运行。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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