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    • 2. 发明授权
    • Continuous in-situ combination process for upgrading heavy oil
    • 连续原位组合工艺提升重油
    • US5935421A
    • 1999-08-10
    • US734322
    • 1996-10-21
    • Glen BronsRonald D. MyersRoby Bearden
    • Glen BronsRonald D. MyersRoby Bearden
    • C10G29/04C10G67/02C10G19/02
    • C10G29/04C10G67/02
    • The invention relates to an integrated, continuous process for the removal of organically bound sulfur (e.g., mercaptans, sulfides and thiophenes) comprising the steps of contacting a heavy oil, sodium hydroxide, hydrogen and water at a temperature of from about 380.degree. C. to 450.degree. C. to partially desulfurize the heavy oil and to form sodium sulfide, contacting said sodium sulfide via steam stripping to convert the sodium sulfide to sodium hydroxide and the sulfur recovered as hydrogen sulfide. The sodium hydroxide is recirculated for reuse. The partially desulfurized, dewatered heavy oil is treated with sodium metal under desulfurizing conditions, typically at a temperature of from about 340.degree. C. to about 450.degree. C., under a hydrogen pressure of at least about 50 psi to essentially desulfurize the oil, and form sodium sulfide. Optionally, the sodium salt generated can be regenerated to sodium metal using regeneration technology. The process advantageously produces essentially sulfur-free product oils having reduced nitrogen, oxygen and metals contents and reduced viscosity, density, molecular weight and heavy ends.
    • 本发明涉及用于去除有机结合硫(例如硫醇,硫化物和噻吩)的一体化连续方法,包括以下步骤:在约380℃的温度下使重质油,氢氧化钠,氢气和水接触。 至450℃,以部分重硫脱硫并形成硫化钠,通过汽提将硫化钠接触,将硫化钠转化为氢氧化钠,硫作为硫化氢回收。 将氢氧化钠再循环以重新使用。 部分脱硫的脱水重油在脱硫条件下,通常在约340℃至约450℃的温度下,在至少约50psi的氢气压力下用金属钠处理以使油基本上脱硫, 并形成硫化钠。 任选地,所生成的钠盐可以使用再生技术再生成金属钠。 该方法有利地产生具有降低的氮,氧和金属含量以及降低的粘度,密度,分子量和重量的基本上无硫产品油。
    • 3. 发明授权
    • Process for reducing coke formation in heavy feed catalytic cracking
    • 重质进料催化裂化中焦炭形成减少的方法
    • US4372840A
    • 1983-02-08
    • US259830
    • 1981-05-04
    • Roby BeardenGordon F. Stuntz
    • Roby BeardenGordon F. Stuntz
    • B01J21/20B01J29/90C10G11/02C10G11/18C10G9/16
    • C10G11/02B01J21/20B01J29/90C10G11/187
    • A method for decreasing the amount of coke produced during the cracking of hydrocarbon feedstock to lower molecular weight products in a reaction zone is disclosed, where the feedstock contains at least one metal contaminant selected from the class consisting of nickel, vanadium and iron and where the contaminant becomes deposited on the catalyst such that at least 50 wt. % of the total of the metal contaminants comprises only one of the metal contaminants. The method comprises adding a hydrogen donor material to the reaction zone, monitoring the composition of the metal contaminant on the catalyst, adding an effective passivating amount of at least one of the metal contaminants which is not the major contaminant on the catalyst and passing the catalyst from the reaction zone through a reduction zone maintained at an elevated temperature.
    • 公开了一种在反应区中将烃原料裂解成较低分子量产物时产生的焦炭量减少的方法,其中原料含有至少一种选自镍,钒和铁的金属污染物, 污染物沉积在催化剂上,使得至少50wt。 金属污染物总量的百分比仅包括一种金属污染物。 该方法包括向反应区添加氢供体材料,监测催化剂上的金属污染物的组成,在催化剂上加入不是主要污染物的金属污染物中的至少一种的有效钝化量并使催化剂 从反应区通过保持在高温下的还原区。
    • 5. 发明授权
    • Process for reducing coke formation in heavy feed catalytic cracking
    • 重质进料催化裂化中焦炭形成减少的方法
    • US4370220A
    • 1983-01-25
    • US285817
    • 1981-07-22
    • Roby BeardenGordon F. Stuntz
    • Roby BeardenGordon F. Stuntz
    • B01J21/20B01J29/90C10G11/02C10G11/18C10G9/16
    • B01J29/90B01J21/20C10G11/02C10G11/187
    • A method for decreasing the amount of hydrogen and coke produced during the cracking of hydrocarbon feedstock to lower molecular weight products in a reaction zone is disclosed, where the feedstock contains at least one metal contaminant selected from the class consisting of nickel, vanadium and iron and where the contaminant becomes deposited on the catalyst such that at least 50 wt. % of the total of the metal contaminants comprises only one of the metal contaminants. The method comprises monitoring the composition of the metal contaminant on the catalyst, adding an effective passivating amount of at least one of the metal contaminants which is not the major contaminant on the catalyst and passing catalyst from the reaction zone through a regeneration zone operated under net reducing conditions and through a reduction zone maintained at an elevated temperature.
    • 公开了一种在反应区中将烃原料裂解成较低分子量产物时产生的氢和焦炭的量减少的方法,其中原料含有至少一种选自镍,钒和铁的金属污染物, 其中污染物沉积在催化剂上,使得至少50wt。 金属污染物总量的百分比仅包括一种金属污染物。 该方法包括监测催化剂上的金属污染物的组成,在催化剂上添加不是主要污染物的至少一种金属污染物的有效钝化量,并将催化剂从反应区通过在网下运行的再生区 并且通过保持在高温下的还原区。
    • 6. 发明授权
    • Passivation of cracking catalysts
    • 破裂催化剂钝化
    • US4280896A
    • 1981-07-28
    • US108396
    • 1979-12-31
    • Roby BeardenGordon F. Stuntz
    • Roby BeardenGordon F. Stuntz
    • B01J21/20B01J29/90C10G11/02C10G11/18C10G9/16
    • B01J29/90B01J21/20C10G11/02C10G11/187Y10S502/521
    • A method for passivating a catalyst used to crack hydrocarbon feedstock to lower molecular weight products in a reaction zone is disclosed where the feedstock contains at least one metal contaminant selected from the class consisting of nickel, vanadium and iron and where the contaminant becomes deposited on the catalyst such that at least a major portion of the total of said metal contaminant deposited on the catalyst comprises only one of the metal contaminants. The method comprises monitoring the composition of said metal contaminant on the catalyst, adding a predetermined amount of at least one of said metal contaminants not present as the major contaminant on the catalyst, and passing the catalyst from the reaction zone through a reduction zone maintained at an elevated temperature for a time sufficient to at least partially passivate said metal contaminant.CROSS-REFERENCE TO RELATED APPLICATIONSThis application is related to U.S. Patent Application, Ser. No. 108,395 filed on even date herewith.
    • 公开了一种用于钝化用于将烃原料裂解成反应区中较低分子量产物的催化剂的方法,其中原料含有至少一种选自镍,钒和铁的金属污染物,并且其中污染物沉积在 催化剂,使得沉积在催化剂上的所述金属杂质总量的至少大部分仅包含一种金属污染物。 该方法包括监测催化剂上所述金属污染物的组成,在催化剂上加入预定量的至少一种不作为主要污染物存在的所述金属污染物,并使催化剂从反应区通过保持在 升高的温度足以至少部分地钝化所述金属污染物的时间。
    • 9. 发明授权
    • Process for reducing total acid number of crude oil
    • 减少原油总酸值的方法
    • US5928502A
    • 1999-07-27
    • US72763
    • 1998-05-05
    • Roby BeardenSaul Charles BlumWilliam Neergaard Olmstead
    • Roby BeardenSaul Charles BlumWilliam Neergaard Olmstead
    • C10G29/06C10G17/00
    • C10G29/06
    • The invention comprises a method for reducing the amount of carboxylic acids in petroleum feeds comprising the steps of (a) adding to said petroleum feed a catalytic agent comprising an oil soluble or oil dispersible compound of a metal selected from the group consisting of Group VB, VIB, VIIB and VIII metals, wherein the amount of metal in said petroleum feed is at least about 5 wppm, (b) heating said petroleum feed with said catalytic agent in a reactor at a temperature of about 400 to about 800.degree. F. (about 204.44 to about 426.67.degree. C.) and a pressure of about atmospheric to about 1000 psig (about 6996.33 kPa) in the substantial absence of hydrogen, and (c) sweeping the reactor containing said petroleum feed and said catalytic agent with an inert gas to maintain the combined water and carbon dioxide partial pressure below about 50 psia (344.75 kPa).
    • 本发明包括一种减少石油原料中羧酸含量的方法,包括以下步骤:(a)向所述石油原料中加入一种催化剂,该催化剂包含选自由VB组成的组的油溶性或油分散性金属化合物, VIB,VIIB和VIII族金属,其中所述石油原料中金属的量为至少约5wppm,(b)在反应器中在约400至约800°F的温度下用所述催化剂加热所述石油进料( 约204.44至约426.67℃)和基本上不存在氢气的压力为约大气压至约1000psig(约6996.33kPa),和(c)用惰性气体吹扫含有所述石油进料和所述催化剂的反应器 以保持水分和二氧化碳的组合分压低于约50psia(344.75kPa)。