Abstract

Traditionally, total sulfur content of a crude or condensate feedstock introduced to atmospheric distillation units in a refinery has been used as a measure to predict the high temperature corrosivity of these feeds. Such predictions were also utilized to decide on selection of materials of construction for refinery facilities processing condensate, and many chronic problems, sometimes leading to failure of materials have been reported. In reality, in addition to the total sulfur content, it is important to conduct a profiling of the distribution of the various types of sulfur components in the condensate or crude oil. A pilot plant, mimicking the thermal conditions in a condensate preheat train, was utilized to generate trends of H2S generation under various process conditions. The experimental variables included temperature, pressure, condensate feed rates, and sweep gas flow rates. Yields of H2S generation for the different conditions have been trended for the parametric studies. Such trends were compared for two different condensate feedstock, as a fundamental step towards understanding why different condensate feedstock exhibit significantly different pattern of H2S generation, and hence different corrosivity under similar high temperature processing conditions. Chromatograms of all sulfur containing species, as well as key types of sulfur-containing species have been presented to demonstrate why the H2S yield patterns can vary among different condensates.

Highlights

  • Condensates are relatively lighter than crude oil and are produced by separation from either crude oil or natural gas, after being released from the production well

  • In a typical oil refinery, crude oil or condensate streams are first heated in a preheat train and introduced to a distillation unit, where the crude/condensate is separated into several straight run fractions based on the boiling point ranges

  • Two condensate feedstock, codenamed as TR1 and TR2, were processed in a pilot plant to mimic the range of operating conditions, which is likely to be encountered in condensate processing in a refinery

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Summary

Introduction

Condensates are relatively lighter than crude oil and are produced by separation from either crude oil or natural gas, after being released from the production well. The term condensate refers broadly to any type of oil that ‘‘condenses’’ into a liquid after being released from high-pressure wells, where it pre-exists in gas form, or is physically separated from the gas. It has a low-density, high API gravity typically in the range of 50–80 degrees, and Reid Vapor Pressure (RVP) ranging from 2 to 14 psig [1]. In a typical oil refinery, crude oil or condensate streams are first heated in a preheat train and introduced to a distillation unit, where the crude/condensate is separated into several straight run fractions based on the boiling point ranges. Condensate feedstock, which can be from a single origin, or a blend of several condensate feedstock, is first heated up, recovering heat from several product

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