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1.发明授权公开(公告)号：US06346645B1
公开(公告)日：2002-02-12
申请号：US09551642
申请日：2000-04-18
Applicant: Santi Kulprathipanja , David W. House , Peter R. Pujado
Inventor： Santi Kulprathipanja , David W. House , Peter R. Pujado
IPC: C07C5112
Abstract: Carbonyl compounds (e.g. acetone and acetaldehyde) are often present as impurities in oxygenated organic liquids such as acetic acid made by the carbonylation of methanol or in phenol produced by the oxidation of cumene. These impurities can render petrochemical products unsuitable for long-term storage or otherwise adversely affect downstream processing operations. It has now been found that detrimental carbonyl impurities can be easily removed from oxygenated organic liquids by contact with resins having amine functional groups.
Abstract translation: 羰基化合物（例如丙酮和乙醛）通常作为杂质存在于氧化的有机液体中，例如通过羰基化甲醇或通过异丙苯的氧化产生的苯酚制得的乙酸。 这些杂质可能导致石化产品不适合长期储存或以其他方式不利地影响下游加工操作。 现在已经发现，通过与具有胺官能团的树脂接触，可以容易地从有氧氧化有机液体中除去有害的羰基杂质。
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公开(公告)号：US5672795A
公开(公告)日：1997-09-30
申请号：US533291
申请日：1995-09-25
Applicant: Bipin V. Vora , Tamotsu Imai , Peter R. Pujado
Inventor： Bipin V. Vora , Tamotsu Imai , Peter R. Pujado
Abstract: An etherification process combines an alkylation zone with a skeletal olefin isomerization zone in an arrangement that rejects isoalkanes and normal alkanes with only minor loss of valuable olefin isomers. The invention also provides a balanced feed to an alkylation zone for the production of high octane gasoline components. This invention can be used to provide ethers and gasoline boiling range alkylates from either C.sub.4 or C.sub.5 feedstocks. The invention fully utilizes all olefin isomers improve octane and vapor pressure charactristics of the gasoline components.
Abstract translation: 醚化方法将烷基化区与骨架烯烃异构化区结合在一起，其排斥异烷烃和正烷烃，只有少量有价值的烯烃异构体损失。 本发明还提供了用于生产高辛烷值汽油组分的烷基化区的平衡进料。 本发明可用于从C4或C5原料提供醚和汽油沸程烷基化物。 本发明充分利用所有烯烃异构体提高汽油组分的辛烷值和蒸气压特性。
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公开(公告)号：US5600052A
公开(公告)日：1997-02-04
申请号：US365622
申请日：1994-12-28
Applicant: Christine J. B. Girod , William W. Levy , Peter R. Pujado , Jacques J. L. Romatier , Dominique J. J. M. Sabin , Paul A. Sechrist
Inventor： Christine J. B. Girod , William W. Levy , Peter R. Pujado , Jacques J. L. Romatier , Dominique J. J. M. Sabin , Paul A. Sechrist
CPC classification number: F28F13/14 , B01J8/0207 , B01J8/0285 , B01J8/0403 , B01J8/0496 , B01J8/087 , B01J8/125 , F28D9/0006 , F28F3/04 , F28F9/0268 , B01J2208/00106 , B01J2208/0053 , B01J2208/022 , B01J2219/2453 , B01J2219/2459 , B01J2219/2464 , B01J2219/247 , B01J2219/2471 , B01J2219/2474 , B01J2219/2481 , B01J2219/2498 , Y02P20/582 , Y10S585/91 , Y10S585/911
Abstract: A reactor arrangement and process for indirectly contacting a reactant stream with a heat exchange stream uses an arrangement of heat exchange plates to control temperature conditions by varying the heat transfer factor in different portions of a continuous channel defined by the heat exchange plates. The reactor arrangement and process of this invention may be used to operate a reactor under isothermal or other controlled temperature conditions. The variation in the heat transfer factor within a single heat exchange section is highly useful in maintaining a desired temperature profile in an arrangement having a cross-flow of heat exchange medium relative to reactants. The corrugations arrangement eliminates or minimizes the typical step-wise approach to isothermal conditions.
Abstract translation: 用于间接地将反应物流与热交换流接触的反应器装置和方法使用热交换板的布置来通过改变由热交换板限定的连续通道的不同部分中的传热因子来控制温度条件。 本发明的反应器装置和方法可用于在等温或其它受控温度条件下操作反应器。 在单个热交换部分内的热传递因子的变化对于在具有相对于反应物的热交换介质的交叉流动的布置中维持期望的温度分布非常有用。 波纹布置消除或最小化了等温条件的典型逐步方法。
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公开(公告)号：US5559274A
公开(公告)日：1996-09-24
申请号：US427783
申请日：1995-04-25
Applicant: John I. Hammerman , Peter R. Pujado
Inventor： John I. Hammerman , Peter R. Pujado
IPC: C07C37/60
Abstract: Phenol is produced from a hydrocarbon feedstock using a process combination offering unexpected synergy. Benzene is produced from the hydrocarbon feedstock using a highly selective aromatization catalyst which provides substantial quantities of high-purity hydrogen. The hydrogen is converted to hydrogen peroxide, which in turn is used to convert the benzene to phenol in high yield.
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公开(公告)号：US4761504A
公开(公告)日：1988-08-02
申请号：US947009
申请日：1986-12-29
Applicant: Peter R. Pujado
Inventor： Peter R. Pujado
CPC classification number: C07C2/62 , C07C41/42 , C07C2527/1206 , Y02P20/125
Abstract: A process is disclosed for the simultaneous alkylation of light hydrocarbons to produce gasoline blending components and the etherification of an isoolefin to produce an ether. The etherification zone effluent stream contains normal olefins and isoparaffins consumed in an acid-catalyzed alkylation zone. The etherification zone effluent stream is separated in a fractionation column in a manner which provides a small amount of ether in the hydrocarbon-rich overhead stream. The presence of the ether in the acid-catalyst is beneficial to the alkylation reaction by providing a higher octane number product.
Abstract translation: 公开了一种用于同时烷基化轻质烃以产生汽油调和组分和异烯烃醚化生产醚的方法。 醚化区流出物流含有在酸催化的烷基化区消耗的正链烯烃和异链烷烃。 将醚化区流出物流在分馏塔中以在富含烃的塔顶馏出物流中提供少量醚的方式分离。 通过提供更高辛烷值的产物，在酸催化剂中存在醚有利于烷基化反应。
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Patent Agency Ranking6.发明授权Process for the recovery of phenol from a reaction mixture resulting from the acid cleavage of cumene hydroperoxide 失效从由氢过氧化枯烯的酸裂解产生的反应混合物中回收苯酚的方法
公开(公告)号：US4283568A
公开(公告)日：1981-08-11
申请号：US108736
申请日：1979-12-31
Applicant: Peter R. Pujado
Inventor： Peter R. Pujado
IPC: C07C27/00 , C07C27/26 , C07C29/132 , C07C37/08 , C07C37/68 , C07C37/72 , C07C37/74 , C07C39/04 , C07C45/53 , C07C67/00 , C07C37/86
CPC classification number: C07C45/53 , C07C37/08 , C07C37/685 , C07C37/72 , C07C37/74
Abstract: A process for the recovery of phenol from a reaction mixture resulting from the acid cleavage of cumene hydroperoxide is disclosed. Neutralization of the acidic reaction mixture is effected with sodium phenate--a product derived from the subsequent recovery of phenol and recycled to the neutralization process. Utilization of internal process recycle streams in this manner affords a reduced consumption of acid and caustic, and permits the elimination of certain vessels in the recovery scheme.
Abstract translation: 公开了从氢过氧化枯烯的酸裂解产生的反应混合物中回收苯酚的方法。 酸性反应混合物的中和通过苯酚钠 - 一种衍生自随后苯酚回收的产物再循环至中和过程进行。 以这种方式利用内部工艺循环料流减少了酸和苛性碱的消耗，并且允许在回收方案中消除某些容器。
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7.发明授权Process for the recovery of phenol from a reaction mixture resulting from the acid cleavage of cumene hydroperoxide 失效从由氢过氧化枯烯的酸裂解产生的反应混合物中回收苯酚的方法
公开(公告)号：US4262151A
公开(公告)日：1981-04-14
申请号：US108750
申请日：1979-12-31
Applicant: Peter R. Pujado
Inventor： Peter R. Pujado
CPC classification number: C07C37/685 , C07C37/72 , C07C37/74
Abstract: A process for the recovery of phenol from a reaction mixture resulting from the acid cleavage of cumene hydroperoxide is disclosed. Neutralization of the acidic reaction mixture is effected with sodium phenate--a product derived from the subsequent recovery of phenol and recycled to the neutralization process. The resulting mixture is further treated to effect an improved separation of the salt of neutralization therefrom.
Abstract translation: 公开了从氢过氧化枯烯的酸裂解产生的反应混合物中回收苯酚的方法。 酸性反应混合物的中和通过苯酚钠 - 一种衍生自随后苯酚回收的产物再循环至中和过程进行。 进一步处理所得混合物以实现中和盐的改进分离。
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8.发明授权公开(公告)号：US07998893B2
公开(公告)日：2011-08-16
申请号：US11681456
申请日：2007-03-02
Applicant: Peter R. Pujado
Inventor： Peter R. Pujado
IPC: B01J38/04
CPC classification number: B01J29/90 , B01J29/83 , B01J29/85 , B01J38/12 , C07C1/20 , C07C2529/85 , Y02P20/584 , Y10S502/516 , C07C11/02
Abstract: The invention relates to a conversion process for making olefin(s) using a molecular sieve catalyst composition. More specifically, the invention is directed to a process for converting a feedstock comprising an oxygenate in the presence of a molecular sieve catalyst composition, wherein the air feed to the catalyst regenerator is free of or substantially free of metal salts. The air feed is preferably purified by passage through a rotary adsorbent contactor or adsorbent wheel.
Abstract translation: 本发明涉及使用分子筛催化剂组合物制备烯烃的转化方法。 更具体地，本发明涉及在分子筛催化剂组合物存在下转化含有氧化合物的原料的方法，其中向催化剂再生器的空气进料不含或基本上不含金属盐。 空气进料优选通过通过旋转吸附剂接触器或吸附轮来净化。
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公开(公告)号：US07919660B2
公开(公告)日：2011-04-05
申请号：US12004843
申请日：2007-12-21
Applicant: Bipin V. Vora , Peter R. Pujado
Inventor： Bipin V. Vora , Peter R. Pujado
IPC: C07C1/00
CPC classification number: C07C1/20 , C07C7/11 , C07C11/06 , C07C11/08 , C07C41/01 , C07C41/09 , C07C2529/85 , Y02P20/52 , C07C43/043
Abstract: A method of converting methanol feedstock to olefins is provided and includes contacting the methanol feedstock in a first conversion zone with a catalyst at reaction conditions effective to produce a first reaction zone effluent comprising DME, unreacted methanol and water, and recycling at least a portion of an overhead vapor product to the first conversion zone and/or to the second conversion zone.
Abstract translation: 提供了将甲醇原料转化为烯烃的方法，包括在有效产生包含DME，未反应的甲醇和水的第一反应区流出物的反应条件下将第一转化区中的甲醇原料与催化剂接触，并将至少一部分 到第一转化区和/或第二转化区的塔顶蒸气产物。
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10.发明授权公开(公告)号：US07902100B2
公开(公告)日：2011-03-08
申请号：US11681380
申请日：2007-03-02
Applicant: Peter R. Pujado
Inventor： Peter R. Pujado
IPC: B01J38/12
CPC classification number: B01J29/90 , B01J38/12 , B01J38/42 , C07C1/20 , C07C2529/83 , C07C2529/85 , Y02P20/52 , Y02P20/584 , Y02P30/42 , Y10S502/514 , Y10S502/516 , C07C11/04 , C07C11/06
Abstract: The invention relates to a conversion process for making olefin(s) using a molecular sieve catalyst composition. More specifically, the invention is directed to a process for converting a feedstock comprising an oxygenate in the presence of a molecular sieve catalyst composition, wherein the air feed to the catalyst regenerator is free of or substantially free of metal salts.
Abstract translation: 本发明涉及使用分子筛催化剂组合物制备烯烃的转化方法。 更具体地，本发明涉及在分子筛催化剂组合物存在下转化含有氧化合物的原料的方法，其中向催化剂再生器的空气进料不含或基本上不含金属盐。
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