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    • 6. 发明申请
    • PROCESS FOR REDUCING CHLORIDE IN HYDROCARBON PRODUCTS USING AN IONIC LIQUID CATALYST
    • 使用离子液体催化剂在碳氢化合物产品中还原氯化物的方法
    • US20140171720A1
    • 2014-06-19
    • US13715873
    • 2012-12-14
    • Bi-Zeng ZhanHye Kyung Cho TimkenMichael Sean Driver
    • Bi-Zeng ZhanHye Kyung Cho TimkenMichael Sean Driver
    • C07C7/10
    • C07C7/10B01D3/009B01J31/0284B01J31/0288B01J31/0289B01J31/26B01J2231/64C10G29/16
    • We provide a process comprising: a. feeding a chlorinated-hydrocarbon and an ionic liquid catalyst to a treatment unit; b. operating the treatment unit at an elevated temperature to produce dechlorinated-hydrocarbon and HCl; and c. collecting the dechlorinated-hydrocarbon, wherein at least 90 wt % of the chlorides are removed. A second process comprises: a. creating an ionic liquid catalyst-rich zone in a distillation unit; b. passing chlorinated-hydrocarbon to the distillation unit; c. operating the unit under conditions causing removal of alkyl chloride to produce dechlorinated-hydrocarbon having a final boiling point close to a first final boiling point. A third process comprises: a. feeding alkylate gasoline blending component and ionic liquid catalyst to a treatment unit; b. operating the treatment unit; and c. collecting a dechlorinated-hydrocarbon, wherein at least 90 wt % of the chlorides have been removed and the dechlorinated-hydrocarbon has a second RON that is close to a first RON.
    • 我们提供一个过程,包括:a。 将氯代烃和离子液体催化剂供给到处理单元; b。 在升高的温度下操作处理单元以产生脱氯烃和HCl; 和c。 收集脱氯烃,其中除去至少90重量%的氯化物。 第二个过程包括:a。 在蒸馏单元中产生离子液体催化剂富集区; b。 将氯化烃通入蒸馏单元; C。 在引起去除烷基氯的条件下操作该单元以产生具有接近第一最终沸点的最终沸点的脱氯烃。 第三个过程包括:a。 将烷基化汽油调和组分和离子液体催化剂加入到处理单元中; b。 操作治疗单元; 和c。 收集脱氯烃,其中已除去至少90重量%的氯化物,脱氯烃具有接近第一RON的第二RON。
    • 7. 发明授权
    • Process for reducing chloride in hydrocarbon products using an ionic liquid catalyst
    • 使用离子液体催化剂还原烃产物中的氯化物的方法
    • US08969645B2
    • 2015-03-03
    • US13715873
    • 2012-12-14
    • Bi-Zeng ZhanHye Kyung Cho TimkenMichael Sean Driver
    • Bi-Zeng ZhanHye Kyung Cho TimkenMichael Sean Driver
    • C07C7/10B01J31/26
    • C07C7/10B01D3/009B01J31/0284B01J31/0288B01J31/0289B01J31/26B01J2231/64C10G29/16
    • We provide a process comprising: a. feeding a chlorinated-hydrocarbon and an ionic liquid catalyst to a treatment unit; b. operating the treatment unit at an elevated temperature to produce dechlorinated-hydrocarbon and HCl; and c. collecting the dechlorinated-hydrocarbon, wherein at least 90 wt % of the chlorides are removed. A second process comprises: a. creating an ionic liquid catalyst-rich zone in a distillation unit; b. passing chlorinated-hydrocarbon to the distillation unit; c. operating the unit under conditions causing removal of alkyl chloride to produce dechlorinated-hydrocarbon having a final boiling point close to a first final boiling point. A third process comprises: a. feeding alkylate gasoline blending component and ionic liquid catalyst to a treatment unit; b. operating the treatment unit; and c. collecting a dechlorinated-hydrocarbon, wherein at least 90 wt % of the chlorides have been removed and the dechlorinated-hydrocarbon has a second RON that is close to a first RON.
    • 我们提供一个过程,包括:a。 将氯代烃和离子液体催化剂供给到处理单元; b。 在升高的温度下操作处理单元以产生脱氯烃和HCl; 和c。 收集脱氯烃,其中除去至少90重量%的氯化物。 第二个过程包括:a。 在蒸馏单元中产生离子液体催化剂富集区; b。 将氯化烃通入蒸馏单元; C。 在引起去除烷基氯的条件下操作该单元以产生具有接近第一最终沸点的最终沸点的脱氯烃。 第三个过程包括:a。 将烷基化汽油调和组分和离子液体催化剂加入到处理单元中; b。 操作治疗单元; 和c。 收集脱氯烃,其中已除去至少90重量%的氯化物,脱氯烃具有接近第一RON的第二RON。