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1. 发明授权

EP0056009B1 Multiple stage hydrocarbon conversion with gravity flowing catalyst particles 失效
标题翻译：多级流态催化剂颗粒的多级碳氢化合物转化
公开(公告)号：EP0056009B1
公开(公告)日：1984-10-17
申请号：EP82300027.8
申请日：1982-01-05
申请人： UOP INC.
发明人： Peters, Kenneth David
IPC分类号： C10G35/12
CPC分类号： B01J8/12 , C10G35/12

2. 发明授权

EP0083762B1 Recovery of C3+hydrocarbon conversion products and net excess hydrogen in a catalytic reforming process 失效
标题翻译： C3 +碳氢转化产物和催化再生过程中过量氢的回收
公开(公告)号：EP0083762B1
公开(公告)日：1985-05-02
申请号：EP82111696.9
申请日：1982-12-16
申请人： UOP INC.
发明人： DeGraff, Richard Raymond , Peters, Kenneth David
IPC分类号： C10G35/04
CPC分类号： C10G35/04 , C10G49/22

3. 发明公开

EP0134335A1 A catalytic reforming process 失效
标题翻译： Verfahren zur katalytischen Reformierung。
公开(公告)号：EP0134335A1
公开(公告)日：1985-03-20
申请号：EP83304722.8
申请日：1983-08-15
申请人： UOP INC.
发明人： Peters, Kenneth David
IPC分类号： C10G35/04
CPC分类号： C10G35/04
摘要： Hydrocarbons are subjected to a catalytic reforming process in which they are preheated in a fired heater (4) prior to the reforming reactor (5,9,11) and the liquid portion of the reactor effluent is fractionated in a stabilizer column (16) to recover the product reformate (22). In order to dispense with a separate fired heater for the stabilizer column a predetermined amount of the reformate is reheated in indirect heat exchange (23a) in a convection heating section of the fired heater (4) for the reforming reactor (5, 9, 11) and then returned to the stabilizer column (16), and a further portion of the reformate is subjected to indirect heat exchange (15) with the reactor effluent and returned to the stabilizer column (16) to provide the remainder of its heat requirement.
摘要翻译：碳氢化合物进行催化重整过程，其中它们在重整反应器（5,9,11）之前在烧制加热器（4）中预热，并将反应器流出物的液体部分在稳定剂塔（16）中分馏至回收产品重组（22）。为了省略用于稳定剂塔的单独的燃烧加热器，在用于重整反应器（5,9,11）的燃烧加热器（4）的对流加热部分中，间接热交换（23a）中重新预定量的重整产物再加热），然后返回到稳定剂塔（16）中，并将另一部分重整产物与反应器流出物进行间接热交换（15）并返回到稳定塔（16），以提供剩余的热量需求。

4. 发明授权

EP0025352B1 Multiple stage hydrocarbon conversion process 失效
标题翻译：多级油气转化工艺
公开(公告)号：EP0025352B1
公开(公告)日：1983-05-18
申请号：EP80303136.8
申请日：1980-09-05
申请人： UOP INC.
发明人： Peters, Kenneth David
IPC分类号： C10G35/12
CPC分类号： B01J8/12 , C10G35/12

5. 发明公开

EP0025352A1 Multiple stage hydrocarbon conversion process 失效
标题翻译： Mehrstufiges Verfahren zur Umwandlung von Kohlenwasserstoffen。
公开(公告)号：EP0025352A1
公开(公告)日：1981-03-18
申请号：EP80303136.8
申请日：1980-09-05
申请人： UOP INC.
发明人： Peters, Kenneth David
IPC分类号： C10G35/12
CPC分类号： B01J8/12 , C10G35/12
摘要： When using a multiple stage hydrocarbon conversion (e.g. reforming) system wherein a hydrogen-hydrocarbonaceous feedstock reaction mixture (10) is processed serially through a plurality of reaction zones (I-IV), each of which contains a particulate catalyst movable downwardly through the reaction zone, catalyst being withdrawn (31) from the last zone (IV) and fresh or regenerated catalyst introduced (28) into the first zone (I), and the effluent (11, 14, 17) from each reaction zone except the last is reheated (12,15, 18) before passage (13, 16, 19) to the next reaction zone, pinning of the catalyst particles is substantially alleviated by the device of charging only a portion (40-80 mole %) of the total hydrogen (2, 8, 10) to the first reaction zone (I), and charging the balance of the total hydrogen (4, 7) to a subsequent reaction zone (IV).
摘要翻译：当使用多级烃转化（例如重整）系统时，其中氢 - 烃类原料反应混合物（10）被串联地加工通过多个反应区（I-IV），每个反应区含有可通过反应物向下移动的颗粒催化剂从第一区（IV）抽出催化剂（31），将引入的新鲜或再生的催化剂（28）引入第一区（I），并且除了最后一个区之外的每个反应区的流出物（11,14,17）在通过（13,16,19）之前再加热（12,15,18）到下一个反应区，催化剂颗粒的钉扎基本上被装入仅部分（40-80摩尔％）总氢（2,8,10）加入到第一反应区（I）中，并将总氢（4,7）的余量加入到次级反应区（IV）中。

6. 发明授权

EP0134335B1 A catalytic reforming process 失效
标题翻译：催化改性方法
公开(公告)号：EP0134335B1
公开(公告)日：1987-07-15
申请号：EP83304722.8
申请日：1983-08-15
申请人： UOP INC.
发明人： Peters, Kenneth David
IPC分类号： C10G35/04
CPC分类号： C10G35/04

7. 发明公开

EP0083762A1 Recovery of C3+hydrocarbon conversion products and net excess hydrogen in a catalytic reforming process 失效
标题翻译：的C3 +烃转化产物和净过量的氢气在催化重整过程中回收。
公开(公告)号：EP0083762A1
公开(公告)日：1983-07-20
申请号：EP82111696.9
申请日：1982-12-16
申请人： UOP INC.
发明人： DeGraff, Richard Raymond , Peters, Kenneth David
IPC分类号： C10G35/04
CPC分类号： C10G35/04 , C10G49/22
摘要： This invention relates to a hydrocarbon conversion process effected in the presence of hydrogen, especially a hydrogen-producing hydrocarbon conversion process. More particularly, this invention relates to the catalytic reforming of a naphtha feedstock, and is especially directed to an improved recovery of the net excess hydrogen, and to an improved recovery of a C 3 + normally gaseous hydrocarbon conversion product and a C 5 + hydrocarbon conversion product boiling in the gasoline range.

8. 发明公开

EP0056009A1 Multiple stage hydrocarbon conversion with gravity flowing catalyst particles 失效
标题翻译：多级烃转化与由重力催化剂颗粒流动。
公开(公告)号：EP0056009A1
公开(公告)日：1982-07-14
申请号：EP82300027.8
申请日：1982-01-05
申请人： UOP INC.
发明人： Peters, Kenneth David
IPC分类号： C10G35/12
CPC分类号： B01J8/12 , C10G35/12
摘要： A multiple stage catalytic conversion system is provided in which a hydrocarbonaceous charge stock and hydrogen flow serially through a plurality of catalytic reaction zones (I-IV), in each of which the catalyst particles are downwardly movable via gravity flow. At least four reaction zones are utilized, with the fresh feed and hydrogen reactant stream being split between the first and second reaction zones (I,II). The flow (10) of that portion introduced into the second zone is restricted (11). The effluent (12) from the first reaction zone (I) is also restricted (13) and then combined with the effluent (14) from the second reaction zone (II). One portion of the combined effluent (16) is introduced into the third reaction zone (III), and the remaining portion (17) is restricted in flow (18), combined with the effluent (19) from said third reaction zones (III), and introduced (21) into the fourth reaction zone (IV). This technique decreases the mass flow to the first three zones (I-III) and increases the pressure drop experienced within the entire conversion system, thus serving to alleviate the problems associated with the occurrence of stagnant catalyst areas as a result of catalyst particles being "pinned" within a reaction zone and thus unable to assume a downward gravity flow pattern. Restriction of the second zone feed (10) and first reaction zone effluent (12) ensures a higher pressure in the first zone (I).

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