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1.发明授权Hydrocarbon conversion process comprising once-through coking with hydrotreating and fluid catalytic cracking 失效包含通过加氢和流体催化裂化的一次加工的油气转化工艺
公开(公告)号：EP0308196B1
公开(公告)日：1992-07-15
申请号：EP88308492.3
申请日：1988-09-14
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2.发明公开Method of preparing a phosphomolybdic acid catalyst and hydroconversion process utilizing the catalyst 失效制备磷酰胆酸催化剂的方法和利用催化剂的氢化方法
公开(公告)号：EP0243143A3
公开(公告)日：1988-01-07
申请号：EP87303482
申请日：1987-04-21
发明人： Bearden, Roby Jr. , Aldridge, Clyde Lee , Lewis, William Ernest , Mayer, Francis Xavier , Taylor, James Howard Jr.
摘要： A phosphomolybdic acid catalyst is made by mixing an aqueous solution of phosphomolybdic acid with a hydrocarbonaceous oil, drying the mixture and contacting the dried mixture with H₂S to sulfide the dried mixture and then heating the sulfided mixture to convert same to a solid molybdenum-containing catalyst-containing material. The said material is useful for hydrocarbon hydroconversion processes.
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3.发明公开Method of preparing a phosphomolybdic acid catalyst and hydroconversion process utilizing the catalyst 失效一种制备用于通过该催化剂加氢转化磷钼酸和方法的组成的催化剂过程。
公开(公告)号：EP0243143A2
公开(公告)日：1987-10-28
申请号：EP87303482.1
申请日：1987-04-21
发明人： Bearden, Roby Jr. , Aldridge, Clyde Lee , Lewis, William Ernest , Mayer, Francis Xavier , Taylor, James Howard Jr.
摘要： A phosphomolybdic acid catalyst is made by mixing an aqueous solution of phosphomolybdic acid with a hydrocarbonaceous oil, drying the mixture and contacting the dried mixture with H₂S to sulfide the dried mixture and then heating the sulfided mixture to convert same to a solid molybdenum-containing catalyst-containing material. The said material is useful for hydrocarbon hydroconversion processes.
摘要翻译： 甲磷钼酸催化剂通过在与烃油的磷钼酸的wässrige溶液混合，干燥该混合物，并用H 2 S接触干燥的混合物以硫化所述干燥的混合物，然后加热硫化的混合物以相同转换成固体含钼催化剂制备 含材料。 所述材料为烃加氢转化过程中有用。
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5.发明公开Hydrocarbon conversion process comprising once-through coking with hydrotreating and fluid catalytic cracking 失效烃转化方法，包括在单次通过用氢气处理和流体催化裂化焦化。
公开(公告)号：EP0308196A1
公开(公告)日：1989-03-22
申请号：EP88308492.3
申请日：1988-09-14
摘要： Disclosed is a process for converting heavy hydrocarbonaceous feedstock to more valuable products. The feedstock is introduced into a coking unit (14) containing a coking zone (12) and a scrubbing zone (24). The bottoms fraction (28) from the scrubbing zone is passed through a microfiltration unit (30), thus removing fine coke particles which are recycled (32) to the coking zone (12). The substantially solids-free filtrate (36) is hydrotreated (48), then passed to a catalytic cracking unit (52).
摘要翻译： 公开了一种用于重烃原料转化成更有价值的产品的过程。 原料被引入到含有焦化区（12）和一个洗涤区（24），焦化单元（14）。 来自洗涤区的塔底馏分（28）通过微量过滤单元（30）从而去除哪些是再生细焦炭颗粒（32）至所述焦化区（12）通过。 基本上不含固体的滤液（36）进行加氢精制（48），然后传递到催化裂化装置（52）。
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6.发明公开Process for catalytic-slurry hydroconversion of hydrocarbons 失效Wasserstoffumwandlungsverfahren von Kohlenwasserstoffen mit suspendiertem Katalysator。
公开(公告)号：EP0244244A2
公开(公告)日：1987-11-04
申请号：EP87303868.1
申请日：1987-04-30
摘要： A slurry catalytic hydroconversion process comprising at least two hydroconversion zones is provided in which heavy hydrocarbonaceous fresh oil feed is added to more than one hydroconversion zone. Catalysts or catalyst precursors are added to the first hydroconversion zone and preferably also to subsequent hydroconversion zone(s) wherein said subsequent hydroconversion zone(s) are maintained at a temperature of at least 10°F (5.55°C) higher than an immediately preceding hydroconversion zone.
摘要翻译： 提供了包含至少两个加氢转化区的浆料催化加氢转化方法，其中将重质烃类新鲜油进料加入多于一个加氢转化区。 将催化剂或催化剂前体加入到第一加氢转化区，优选加入到随后的加氢转化区，其中所述随后的加氢转化区保持在比紧接着前一步高的至少10°F（5.55℃）的温度 加氢转化区。
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7.发明公开Process for hydroconversion of heavy hydrocarbonaceous feeds 失效Verfahren zur Hydroconversion von Rohmaterialien aus schweren Kohlenwasserstoffen。
公开(公告)号：EP0549257A1
公开(公告)日：1993-06-30
申请号：EP92311502.6
申请日：1992-12-16
摘要： A process for converting a heavy hydrocarbonaceous chargestock to lower boiling products, at hydroconversion conditions and in the presence of hydrogen, wherein a presulfided catalyst precursor concentrate is introduced with the chargestock into a hydroconversion zone. The hydroconversion is conducted at a temperature from about 425°C to 510°C and a hydrogen partial (gauge) pressure of from about 50 to 5,000 psig (0.345 to 34.475 MPa).
摘要翻译： 在加氢转化条件下和在氢的存在下，将重质含烃物质转化为较低沸点产物的方法，其中将预硫化的催化剂前体浓缩物与所述带电荷料导入加氢转化区。 加氢转化在约425℃至510℃的温度和约50至5,000psig（0.345至34.475MPa）的氢部分（表压）压力下进行。
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公开(公告)号：EP0308094B1
公开(公告)日：1992-11-25
申请号：EP88307879.2
申请日：1988-08-25
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公开(公告)号：EP0243142A1
公开(公告)日：1987-10-28
申请号：EP87303479.7
申请日：1987-04-21
CPC分类号： C10G49/12
摘要： A slurry hydroconversion process is provided in which a catalyst precursor concentrate comprising an aqueous solution of phosphomolybdic acid and a heavy oil is contacted with hot hydrogen to vaporize the water from the concentrate. The resulting catalyst precursor concentrate is introduced into a hydrocarbonaceous chargestock and the resulting mixture is heated in the presence of added hydrogen to convert the phosphomolybdic acid to a solid molybdenum-containing catalyst. The resulting slurry is subjected to hydroconversion conditions. The solid molybdenum-containing catalyst of the resulting hydroconverted products is separated and may be introduced into fresh hydrocarbonaceous chargestock.
摘要翻译： 提供了一种浆料加氢转化方法，其中包含磷钼酸和重油的水溶液的催化剂前体浓缩物与热氢接触以使来自浓缩物的水蒸发。 将所得催化剂前体浓缩物引入烃类带电荷的物料中，并将所得混合物在加入的氢气存在下加热，以将磷钼酸转化为固体含钼催化剂。 将所得浆液进行加氢转化条件。 得到的加氢转化产物的固体含钼催化剂被分离并且可以被引入到新鲜的含烃物料中。
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公开(公告)号：EP0244244B1
公开(公告)日：1992-01-08
申请号：EP87303868.1
申请日：1987-04-30
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