首页> 外文会议>World Engineers' Convention 2004 vol F-A: Resources and Energy; 20041102-06; Shanghai(CN) >Chemical Acid Removal Technique for High Naphthenic Acid Crude Oil
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Chemical Acid Removal Technique for High Naphthenic Acid Crude Oil

机译:高环烷酸原油的化学除酸技术

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According to the composing characteristics of the high-acid crude oil and on the basis of validating traditional distillate acid removal technique by test, the chemical acid removal is the development direction of the acid removal for high-acid crude oil. A series of acid removal agents are successfully developed by the chemical theory and they are the same with the crude oil with different qualities such as high freezing point and high viscosity oil , ordinary heavy oil, and extra-heavy oil. The corollary technologies of the acid removal for crude oil are completed and they include recycle and repetition use of the naphthenic acid and recycle and repetition use of the acid removal agents, and so on. The integrated new acid removal technique for crude oil is formed. The on-site operational process of the technique is simple and it can cooperate with the dehydration and salt removal technique for crude oil. It doesn't need to greatly reform existing technique. The middle-tests of Block 6 in Sudan show that the TAN (Total Acid Number) declines from 10mgKOH/g to less than 0.5 mg KOH/g after two grade acid removal treating; After the first crude oil treating of Block 3&7 is done, the TAN can decline from 5 mgKOH/g to 0. 5 mg KOH/g; After the second crude oil treating of super-heavy oil in Li-aohe, the TAN may decline from 10 mg KOH/g to less than 3 mg KOH/g. According to the middle-test, the operation parameters of different crude oil and different operation process are determined.
机译:根据高酸原油的组成特点,在通过试验验证传统馏分除酸技术的基础上,化学除酸是高酸原油除酸的发展方向。化学原理成功开发了一系列除酸剂,它们与高凝点,高粘度油,普通重油,超重油等不同品质的原油相同。原油除酸的相关技术已经完成,其中包括环烷酸的循环和重复使用以及除酸剂的循环和重复使用,等等。形成了用于原油的集成的新的除酸技术。该技术的现场操作过程简单,可与原油脱水脱盐技术配合使用。不需要对现有技术进行重大改革。苏丹第6区块的中期测试显示,经过两次除酸处理后,TAN(总酸值)从10mgKOH / g降至小于0.5mg KOH / g。在完成区块3&7的第一次原油处理后,TAN可以从5 mgKOH / g降至0. 5 mg KOH / g;在Li-aohe对超重油进行第二次原油处理后,TAN可能会从10 mg KOH / g降至3 mg KOH / g以下。根据中间测试,确定了不同原油,不同操作过程的操作参数。

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