发明名称 Process and system for blending synthetic and natural crude oils derived from offshore produced fluids
摘要 A process and system are described for the processing of gas associated with crude oil production, i.e. associated gas. A separation complex is used to separate produced fluids produced from a hydrocarbon reservoir into crude oil, liquefied petroleum gas, water, and natural gas. At least a portion of the natural gas is converted into synthesis gas in a synthesis gas generator. A combination of a synthesis gas conversion catalysts and hydroconversion catalysts are used in a synthesis gas reactor to convert the synthesis gas into a liquid effluent stream containing liquefied petroleum gas and a synthetic crude oil. The liquefied petroleum gas and synthetic crude oil from the synthesis gas reactor is sent to the separation complex. Liquefied petroleum gas is separated both from the synthetic crude oil and a natural crude oil obtained from the produced fluids. The system and process permits synthetic crude oil to be blended with the natural crude oil producing a blended stabilized crude oil having 2 wt % or more of the synthetic crude oil and with a pour point of 60° C. or less. Use of a common facility for separation operations on the natural crude oil and synthetic crude oil thus reduces capital costs and allows converted associated gases to be shipped with the natural crude oil on a conventional crude oil tanker.
申请公布号 US8753500(B2) 申请公布日期 2014.06.17
申请号 US201012974337 申请日期 2010.12.21
申请人 Chevron U.S.A. Inc. 发明人 Kibby Charles Leonard;O'Rear Dennis J.;Saxton Robert James;Das Tapan K.;Jothimurugesan Kandaswamy
分类号 C10B57/02 主分类号 C10B57/02
代理机构 代理人 DiDomenicis Karen R.;Schulte Richard J.
主权项 1. A process for producing a blended stabilized crude oil from a stream of produced fluids produced from a hydrocarbon containing subterranean reservoir, the process comprising: (a) separating, in a separation complex, natural gas from produced fluids produced from a hydrocarbon bearing reservoir; (b) converting the natural gas into synthesis gas; (c) converting the synthesis gas, in the presence of a synthesis gas conversion catalyst and a hydroconversion catalyst, into a tail gas and a liquid effluent stream including liquefied petroleum gas and synthetic crude oil containing less than 5 wt % C21+ normal paraffins; and (d) sending at least a portion of the liquid effluent stream to the separation complex and separating the liquefied petroleum gas from the synthetic crude oil and separating liquefied petroleum gas from natural crude oil obtained from the produced fluids and producing a blended stabilized crude oil containing natural crude oil and synthetic crude oil; wherein the blended stabilized crude oil has a pour point at or below 60° C. and comprises at least 2 wt % of the synthetic crude oil.
地址 San Ramon CA US