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    Fluid cat cracking with high olefins production
    1.
    发明授权
    Fluid cat cracking with high olefins production 有权
    流体催化裂化产生高烯烃

    公开(公告)号：US07261807B2

    公开(公告)日：2007-08-28

    申请号：US10131737

    申请日：2002-04-24

    申请人： B. Erik Henry ,  William A. Wachter ,  George A. Swan, III

    发明人： B. Erik Henry ,  William A. Wachter ,  George A. Swan, III

    IPC分类号： C10G11/00 ,  C10G11/14 ,  C10G11/02 ,  C10G11/04

    CPC分类号： C10G11/18 ,  C10G2400/20

    摘要： The propylene production of a fluid catalytic cracking unit employing a large pore zeolite cracking catalyst, produces more propylene by adding a naphtha cracking riser and a medium pore zeolite catalytic component to the unit, and recycling at least a portion of the naphtha crackate to the naphtha riser. The large pore size zeolite preferably comprises a USY zeolite and the medium pore size is preferably ZSM-5. Propylene production per unit of naphtha feed to the naphtha riser is maximized, by using the 60–300° F. naphtha crackate as the feed.

    摘要翻译： 使用大孔沸石裂化催化剂的流化催化裂化装置的丙烯生产通过向该装置中加入石脑油裂化提升管和中孔沸石催化组分产生更多的丙烯，并将至少一部分石脑油裂解物再循环至石脑油 冒口 大孔径沸石优选包含USY沸石，中等孔径优选为ZSM-5。 通过使用60-300°F的石脑油裂解液作为进料，使石脑油提升管的单位石脑油进料的丙烯产量最大化。

    Process for producing polypropylene from C3 olefins selectively produced by a two stage fluid catalytic cracking process
    2.
    发明授权
    Process for producing polypropylene from C3 olefins selectively produced by a two stage fluid catalytic cracking process 失效
    通过两阶段流化催化裂化方法选择性生产的C3烯烃生产聚丙烯的方法

    公开(公告)号：US06258257B1

    公开(公告)日：2001-07-10

    申请号：US09517551

    申请日：2000-03-02

    申请人： George A. Swan, III ,  Michael W. Bedell ,  Paul K. Ladwig ,  John E. Asplin ,  Gordon F. Stuntz ,  William A. Wachter ,  B. Erik Henry

    发明人： George A. Swan, III ,  Michael W. Bedell ,  Paul K. Ladwig ,  John E. Asplin ,  Gordon F. Stuntz ,  William A. Wachter ,  B. Erik Henry

    IPC分类号： C10G5102

    CPC分类号： C10G57/02 ,  C10G2400/20

    摘要： A process for producing polymers from olefins selectively produced by a two stage process for selectively producing C2 to C4 olefins from a gas oil or resid is disclosed herein. The gas oil or resid is reacted in a first stage comprising a fluid catalytic cracking unit wherein it is converted in the presence of conventional large pore zeolitic catalyst to reaction products, including a naphtha boiling range stream. The naphtha boiling range stream is introduced into a second stage comprising a process unit containing a reaction zone, a stripping zone, a catalyst regeneration zone, and a fractionation zone. The naphtha feed is contacted in the reaction zone with a catalyst containing from about 10 to 50 wt. % of a crystalline zeolite having an average pore diameter less than about 0.7 nanometers at reaction conditions which include temperatures ranging from about 500 to 650° C. and a hydrocarbon partial pressure from about 10 to 40 psia. Vapor products are collected overhead and the catalyst particles are passed through the stripping zone on the way to the catalyst regeneration zone. Volatiles are stripped with steam in the stripping zone and the catalyst particles are sent to the catalyst regeneration zone where coke is burned from the catalyst, which is then recycled to the reaction zone.

    摘要翻译： 本文公开了一种通过二级方法选择性制备聚合物的方法，用于从瓦斯油或渣油中选择性地生产C2至C4烯烃。 瓦斯油或渣油在包括流化催化裂化装置的第一阶段中反应，其中在常规大孔沸石催化剂存在下将其转化为包括石脑油沸程的反应产物。 将石脑油沸程流引入包含含有反应区，汽提区，催化剂再生区和分馏区的处理单元的第二阶段。 石脑油进料在反应区中与含有约10至50wt。 在包括约500至650℃的温度和约10至40psia的烃分压的反应条件下具有平均孔径小于约0.7纳米的结晶沸石的百分比。 蒸气产物被顶部收集，催化剂颗粒在通向催化剂再生区的途中通过汽提区。 挥发物在汽提区中用蒸汽汽提，并将催化剂颗粒送入催化剂再生区，其中焦炭从催化剂燃烧，然后再循环到反应区。

    FCC process using mesoporous catalyst
    5.
    发明授权
    FCC process using mesoporous catalyst 有权
    FCC工艺采用介孔催化剂

    公开(公告)号：US07504021B2

    公开(公告)日：2009-03-17

    申请号：US11106289

    申请日：2005-04-14

    申请人： William A. Wachter ,  Stephen J. McCarthy ,  Jeffrey S. Beck ,  David L. Stern

    发明人： William A. Wachter ,  Stephen J. McCarthy ,  Jeffrey S. Beck ,  David L. Stern

    IPC分类号： C10G11/05

    CPC分类号： C10G11/04 ,  C10G11/05

    摘要： This invention relates to a FCC process using a mesoporous catalytic cracking catalyst. The mesoporous fluidized catalytic cracking catalyst is selective for minimizing the production of coke and light gas. The catalyst comprises at least one amorphous, porous matrix, each matrix having pores ranging in diameter from about 1 Å to about 10 Å and pores ranging in diameter from about 40 Å to about 500 Å, wherein in the pore range from 50 Å to 250 Å, there is a single maximum in differential pore volume distribution over the 50 Å to 250 Å range.

    摘要翻译： 本发明涉及使用中孔催化裂化催化剂的FCC方法。 中孔流化催化裂化催化剂是选择性地使焦炭和轻质气体的生产最小化。 催化剂包含至少一种无定形多孔基质，每个基质的孔直径约为约至约10埃，孔径范围为约40至约500，其中孔径范围为50埃至250埃 Å，在50Å至250Å范围内，微分孔体积分布有单一最大值。

    Fluid catalytic cracking using catalysts containing monodispersed mesoporous matrices
    8.
    发明授权
    Fluid catalytic cracking using catalysts containing monodispersed mesoporous matrices 失效
    使用含有单分散介孔基质的催化剂进行流化催化裂化

    公开(公告)号：US4968405A

    公开(公告)日：1990-11-06

    申请号：US410563

    申请日：1989-09-21

    申请人： William A. Wachter

    发明人： William A. Wachter

    IPC分类号： B01J29/08 ,  C10G11/05

    CPC分类号： C10G11/05 ,  B01J29/084 ,  B01J2229/42

    摘要： Disclosed is a fluid catalytic cracking process employing a catalyst composition comprised of a monodispersed mesoporous aluminosilicate matrix material having pore diameters between about 100 and 500 Angstroms and alumina contents between about 5 and 40 wt. %, and a crystalline zeolite.

    摘要翻译： 公开了一种流化催化裂化方法，该方法采用催化剂组合物，该催化剂组合物包含孔径在约100-500埃之间的单分散中孔硅铝酸盐基质材料，氧化铝含量在约5-40重量％之间。 ％和结晶沸石。

    FCC catalyst
    10.
    发明授权
    FCC catalyst 有权
    FCC催化剂

    公开(公告)号：US07456123B2

    公开(公告)日：2008-11-25

    申请号：US11106297

    申请日：2005-04-14

    申请人： William A. Wachter

    发明人： William A. Wachter

    IPC分类号： B01J29/06

    CPC分类号： B01J29/084 ,  B01J21/12 ,  B01J21/16 ,  B01J29/7007 ,  B01J35/1061 ,  B01J35/1066 ,  B01J37/0232 ,  C10G11/02 ,  C10G11/05

    摘要： This invention relates to a mesoporous catalytic cracking catalyst, a process for the production of such catalysts, and a process utilizing such catalysts in cracking operations. The mesoporous fluidized catalytic cracking catalyst is selective for minimizing the production of coke and light gas. The catalyst comprises an amorphous, porous matrix having pores ranging in diameter from about 1 Å to about 10 Å and ranging in diameter from about 40 Å to about 500 Å, but substantially free of pores ranging in diameter from about 10 Å to about 40 Å.

    摘要翻译： 本发明涉及介孔催化裂化催化剂，制备这种催化剂的方法，以及在裂化操作中利用这种催化剂的方法。 中孔流化催化裂化催化剂是选择性地使焦炭和轻质气体的生产最小化。 该催化剂包括无定形多孔基体，其具有直径从大约至大约等于或约为范围内的孔的范围，但基本上不含直径从约至约为40埃的孔。 。