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    • 3. 发明申请
    • Systems and Methods for Producing a Crude Product
    • 生产原油产品的系统和方法
    • US20090008290A1
    • 2009-01-08
    • US12233171
    • 2008-09-18
    • Goutam BiswasDarush Farshid
    • Goutam BiswasDarush Farshid
    • C10G45/22
    • C10G67/049
    • Systems and methods for hydroprocessing a heavy oil feedstock, the system employs a plurality of contacting zones and separation zones and an interstage solvent deasphalting unit. The contacting zones operate under hydrocracking conditions, employing a slurry catalyst for upgrading the heavy oil feedstock, forming upgraded products of lower boiling hydrocarbons. In the separation zones which operates at a temperature within 20° F. and a pressure within 10 psi of the pressure in the contacting zones, upgraded products are removed overhead and optionally, further treated in an in-line hydrotreater. At least a portion of the non-volatile fractions recovered from at least one of the separation zones is sent to the interstage solvent deasphalting unit, for separating unconverted heavy oil feedstock into deasphalted oil and asphaltenes. The deasphalted oil stream is sent to one of the contacting zones for further upgrade.
    • 用于加氢处理重油原料的系统和方法,该系统采用多个接触区和分离区以及级间溶剂脱沥青单元。 接触区在加氢裂化条件下运行,使用用于升级重油原料的浆料催化剂,形成较低沸点烃的升级产物。 在温度在20°F范围内工作的分离区和接触区压力在10 psi以内的压力,升级后的产物在顶部除去,任选地在直列式加氢处理机中进一步处理。 从至少一个分离区回收的至少一部分非挥发性馏分被送入级间溶剂脱沥青装置,用于将未转化的重油原料分离成脱沥青油和沥青质。 脱沥青油流被送到其中一个接触区域进一步升级。
    • 4. 发明授权
    • Systems and methods for producing a crude product
    • 用于生产粗产品的系统和方法
    • US08372266B2
    • 2013-02-12
    • US12233171
    • 2008-09-18
    • Goutam BiswasDarush Farshid
    • Goutam BiswasDarush Farshid
    • C10G67/04C10G65/10
    • C10G67/049
    • Systems and methods for hydroprocessing a heavy oil feedstock, the system employs a plurality of contacting zones and separation zones and an interstage solvent deasphalting unit. The contacting zones operate under hydrocracking conditions, employing a slurry catalyst for upgrading the heavy oil feedstock, forming upgraded products of lower boiling hydrocarbons. In the separation zones which operates at a temperature within 20° F. and a pressure within 10 psi of the pressure in the contacting zones, upgraded products are removed overhead and optionally, further treated in an in-line hydrotreater. At least a portion of the non-volatile fractions recovered from at least one of the separation zones is sent to the interstage solvent deasphalting unit, for separating unconverted heavy oil feedstock into deasphalted oil and asphaltenes. The deasphalted oil stream is sent to one of the contacting zones for further upgrade.
    • 用于加氢处理重油原料的系统和方法,该系统采用多个接触区和分离区以及级间溶剂脱沥青单元。 接触区在加氢裂化条件下运行,使用用于升级重油原料的浆料催化剂,形成较低沸点烃的升级产物。 在温度在20°F范围内工作的分离区和接触区压力在10 psi以内的压力,升级后的产物在顶部除去,任选地在直列式加氢处理机中进一步处理。 从至少一个分离区回收的至少一部分非挥发性馏分被送入级间溶剂脱沥青装置,用于将未转化的重油原料分离成脱沥青油和沥青质。 脱沥青油流被送到其中一个接触区域进一步升级。