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1. 发明授权

US5773381A Zeolite L preparation 失效
标题翻译：沸石L制备
公开(公告)号：US5773381A
公开(公告)日：1998-06-30
申请号：US458629
申请日：1995-06-02
申请人： Johannes Petrus Verduijn , Pieter Ernst Gellings
发明人： Johannes Petrus Verduijn , Pieter Ernst Gellings
IPC分类号： B01J29/50 , B01J29/60 , B01J29/62 , B01J29/70 , B01J29/80 , C01B39/06 , C01B39/32 , C07B61/00 , C07C1/00 , C07C5/22 , C07C5/393 , C07C5/41 , C07C67/00 , B01J21/00
CPC分类号： C07C5/415 , B01J29/60 , B01J29/62 , B01J29/7011 , B01J29/80 , C01B39/32 , C07C5/226 , B01J2229/26 , B01J2229/42 , B01J29/50 , B01J29/70 , C07C2529/61
摘要： Zeolite L containing caesium is prepared by a process in which said zeolite L is crystallised from a synthesis mixture with a molar composition (expressed as oxides) of: ______________________________________ K.sub.2 O/SiO.sub.2 0.15 to 0.40 K.sub.2 O/Cs.sub.2 O 3 to 10 H.sub.2 O/K.sub.2 O 40 to 100 and SiO.sub.2 /Al.sub.2 O.sub.3 7 to 13 ______________________________________ and containing 0.5 to 15 ppm (by weight) of divalent metal carbons, e.g. Mg ions. The zeolite L can form part of a dehydrocyclisation and/or isomerisation catalyst.
摘要翻译：含有铯的沸石L通过以下方法制备：其中所述沸石L以摩尔组成（表示为氧化物）： - K 2 O / SiO 2 0.15-0.40-K 2 O / Cs 2 O 3至10-H 2 O / K 2 O 40的合成混合物结晶至100-和SiO 2 / Al 2 O 3 7至13-并且含有0.5至15ppm（重量）的二价金属碳，例如 Mg离子沸石L可以形成脱氢环化和/或异构化催化剂的一部分。

2. 发明授权

US5466376A On-line analysis for continuous measurement of presence of carryunder in liquid-liquid extraction 失效
标题翻译：连续测量液 - 液萃取中残留物的在线分析
公开(公告)号：US5466376A
公开(公告)日：1995-11-14
申请号：US236906
申请日：1994-04-29
申请人： Joseph P. Boyle , Gordon C. Camano , Randall S. Lachine , Howard R. Lingley , Raymond W. Saunders
发明人： Joseph P. Boyle , Gordon C. Camano , Randall S. Lachine , Howard R. Lingley , Raymond W. Saunders
IPC分类号： B01D11/04 , G01N1/20 , G01N35/00
CPC分类号： G01N1/2035 , B01D11/0426 , G01N2035/00227
摘要： The presence of carryunder in the extract phase recovered from a solvent extraction tower is an indication of unsatisfactory performance. The continuous analysis of the extract phase using a turbidity analyzer to detect the presence of two phases, indicating carryunder permits corrective measures to be taken in tower operation to reduce or eliminate carryunder.
摘要翻译：从溶剂萃取塔回收的提取相中存在的残留物表现为不令人满意的性能。使用浊度分析仪对提取相进行连续分析，以检测两相的存在，指示进行塔架运行中采取的纠正措施，以减少或消除携带。

3. 发明授权

US5466364A Performance of contaminated wax isomerate oil and hydrocarbon synthesis liquid products by silica adsorption 失效
标题翻译：污染的蜡异构体油和烃合成液体产物通过二氧化硅吸附的性能
公开(公告)号：US5466364A
公开(公告)日：1995-11-14
申请号：US87309
申请日：1993-07-02
申请人： Bal K. Kaul , Craig Y. Sabottke , Rocco A. Fiato , Edward Niessen
发明人： Bal K. Kaul , Craig Y. Sabottke , Rocco A. Fiato , Edward Niessen
IPC分类号： C10G25/06 , C10G25/12 , C10G67/06 , C10M101/02 , C10M105/02 , C10G25/00
CPC分类号： C10G67/06
摘要： The daylight stability, foaming characteristics, color, engine performance test behavior, oxygenates content, and thermal stability of wax isomerate oils and/or hydrocarbon synthesis liquid products are improved by the process of contacting the aforesaid wax isomerate oil and/or hydrocarbon synthesis liquid products with a silica adsorbent, said silica adsorbent being characterized by possessing a pore size of at least about 100 .ANG., preferably at least about 125 .ANG., most preferably at least about 150 .ANG., an alkali/alkaline earth ion concentration, excluding sodium, of greater than about 125 ppm, an iron content of less than about 40 ppm and a zirconium content of less than about 130 ppm.
摘要翻译：通过使上述蜡异构体油和/或烃合成液体产物接触的方法提高了蜡异构体油和/或烃合成液体产品的日光稳定性，起泡特性，颜色，发动机性能测试行为，含氧化合物含量和热稳定性与二氧化硅吸附剂相比，所述二氧化硅吸附剂的特征在于具有至少约100安培的孔径，优选至少约125安培，最优选至少约150安培，不含钠的碱金属/碱土金属离子浓度较大约125ppm，铁含量小于约40ppm，锆含量小于约130ppm。

4. 发明授权

US5459122A Aromatic oil pesticide adjuvant 失效
标题翻译：芳香油农药助剂
公开(公告)号：US5459122A
公开(公告)日：1995-10-17
申请号：US233831
申请日：1994-04-26
申请人： Thomas J. Ford , Gilbert V. Chambers
发明人： Thomas J. Ford , Gilbert V. Chambers
IPC分类号： C10G45/02 , A01N25/02 , C10G65/04 , C10G65/08 , C10G67/04
CPC分类号： C10G65/08 , A01N25/02
摘要： An aromatic oil having an aniline point less than 120.degree. F., a mutagenicity index based on The Modified Ames Test of less than 2.0, a benzene, naphthalene and methyl substituted benzenes and naphthalenes individual component concentrations less than 100 wppm, and a clay gel aromatics fraction content of at least 50 weight % based on aromatic oil, said aromatics fraction characterized in that it has a naphthene-benzenes and dinaphthenebenzenes content of at least 50 volume % based on aromatics fraction. The invention also relates to a process for preparing the aromatic oil which comprises the steps of selective solvent extraction, selective distillation and two-stage hydrotreating with removal of hydrogen sulfide and/or ammonia. The aromatic oils are useful in agricultural formulations due to their low environmental impacts.
摘要翻译：苯胺点小于120°F的芳香油，基于改性Ames试验的致突变性指数小于2.0，苯，萘和甲基取代苯和萘单独成分浓度小于100wppm，粘土凝胶所述芳族化合物馏分的芳族化合物馏分含量至少为50重量％，所述芳族化合物部分的特征在于其基于芳族化合物部分具有至少50体积％的环烷 - 苯和苊萘含量。本发明还涉及一种制备芳香油的方法，包括选择性溶剂萃取，选择性蒸馏和两步加氢处理以除去硫化氢和/或氨的步骤。由于环境影响小，芳香油在农用配方中很有用。

5. 发明授权

US5455020A Gallium silicate having 12-ring pores (ECR-34) and a method for its preparation 失效
标题翻译：具有12环孔的硅酸镓（ECR-34）及其制备方法
公开(公告)号：US5455020A
公开(公告)日：1995-10-03
申请号：US265289
申请日：1994-06-24
申请人： David E. W. Vaughan , Karl G. Strohmaier
发明人： David E. W. Vaughan , Karl G. Strohmaier
IPC分类号： B01J29/87 , C01B39/06 , C01B39/08 , C01B39/04
CPC分类号： C01B39/065 , B01J29/87 , C01B39/082
摘要： A synthetic gallosilicate zeolite having a 12-ring pore structure and a process for preparing it.
摘要翻译：具有12环孔结构的合成硅酸盐沸石及其制备方法。

6. 发明授权

US5454842A Cetane improver compositions comprising nitrated fatty acid derivatives 失效
标题翻译：包含硝化脂肪酸衍生物的十六烷值改进剂组合物
公开(公告)号：US5454842A
公开(公告)日：1995-10-03
申请号：US348528
申请日：1994-12-02
申请人： Marc-Andre Poirier , David E. Steere , James A. Krogh
发明人： Marc-Andre Poirier , David E. Steere , James A. Krogh
IPC分类号： C07C203/04 , C10L1/23 , F02B3/06 , C10L1/22
CPC分类号： C10L1/231 , C07C203/04 , C10L10/12 , C10L2270/026 , F02B3/06
摘要： The present invention is directed to materials which improve the cetane number of diesel fusel when added in an amount in the range of 0.01 to 2 wt % to such fuel. The materials are the nitration product of alcohols obtained by the reduction of tall oil fatty acids, tall oil fatty acid esters, vegetable oils and mixtures thereof.
摘要翻译：本发明涉及当以0.01〜2重量％的量添加时，能够提高柴油装置的十六烷值的材料。这些材料是通过还原妥尔油脂肪酸，妥尔油脂肪酸酯，植物油及其混合物而获得的醇的硝化产物。

7. 发明授权

US5447622A Integrated catalytic cracking and olefin producing process using staged backflow regeneration 失效
标题翻译：综合催化裂化和烯烃生产过程使用分级回流再生
公开(公告)号：US5447622A
公开(公告)日：1995-09-05
申请号：US154828
申请日：1993-11-19
申请人： Michael C. Kerby , Roby Bearden, Jr. , Stephen M. Davis
发明人： Michael C. Kerby , Roby Bearden, Jr. , Stephen M. Davis
IPC分类号： C10G11/18 , C10G57/00 , C10G51/06 , C07C1/00
CPC分类号： C10G57/00 , C10G11/18
摘要： Disclosed is a method which combines catalytic cracking and olefin production using a coked catalytic cracking catalyst as a dehydrogenation catalyst to dehydrogenate an alkane feed stream and form an olefin rich product stream. The method uses a staged backmixed regeneration system to form the dehydrogenation catalyst and to fully reactivate deactivated cracking catalyst for reuse in the cracking reaction. The catalyst preferably comprises a crystalline tetrahedral framework oxide component.
摘要翻译：公开了一种使用焦化催化裂化催化剂作为脱氢催化剂将催化裂化和烯烃生产组合以使烷烃进料流脱氢并形成富烯烃产物流的方法。该方法使用分级回混再生系统形成脱氢催化剂，并在破裂反应中完全还原失活的裂化催化剂以供再利用。催化剂优选包含结晶四面体骨架氧化物组分。

8. 发明授权

US5435918A Solvent extraction process involving membrane separation of extract phase and/or intermediate zone phase 失效
标题翻译：涉及提取相和/或中间区相的膜分离的溶剂萃取过程
公开(公告)号：US5435918A
公开(公告)日：1995-07-25
申请号：US74573
申请日：1993-06-10
申请人： Adrianus Welmers , Laura E. Black
发明人： Adrianus Welmers , Laura E. Black
IPC分类号： B01D11/04 , B01D61/02 , B01D69/12 , B01D71/56 , C10G21/00 , C10G21/20 , C10G21/28 , C10G31/11 , C10G53/04 , B01D61/04
CPC分类号： B01D61/025 , B01D69/125 , C10G21/00 , C10G21/28 , C10G31/11
摘要： The solvent extraction of aromatics containing oil using a selective aromatics extraction solvent to produce an aromatics rich extract phase and an oil rich/aromatics lean raffinate is improved by the steps of subjecting the extract phase to a membrane separation step to produce a permeate phase and a retentate phase passing the retentate phase to a settling zone wherein the retentate phase spontaneously separates into two liquid phases, and recycling the upper phase to the extraction zone, either to the feed inlet or to the bottom of the extract reflux zone to thereby increase the raffinate oil recovered from the extraction tower. Alternatively or in addition to the above, a side stream can be taken from an intermediate zone of the extraction zone (e.g. extraction tower) and fed to a membrane separation to produce a solvent rich permeate and an oil rich retentate. The solvent rich permeate is recycled while the oil rich retentate is fed to a settling zone wherein it will spontaneously separate into an oil rich pseudo raffinate upper phase which is recovered and into a solvent rich pseudo extract bottoms phase which is recycled to the solvent extraction zone, preferably at a point below that at which the side stream was withdrawn. The membrane separation zone preferably employs interfacially polymerized membranes under reverse osmosis conditions.
摘要翻译：使用选择性芳族化合物萃取溶剂溶剂萃取含芳烃的油，以产生富含芳烃的萃取相和富油/芳族贫油萃取液，通过以下步骤进行改进：将提取相进行膜分离步骤以产生渗透相和滞留相通过滞留相进入沉降区，其中滞留相自发分离成两个液相，并将上相再循环到提取区，或者进入提取回流区的进料入口或底部，从而增加萃余液从提取塔回收的油。或者或除了上述之外，侧流可以从萃取区（例如萃取塔）的中间区取出，并进料到膜分离以产生富溶剂的渗透物和富含油的滞留物。富含溶剂的渗透物被再循环，同时将富油滞留物进料到沉降区，其中它将自发分离成富油的假提余液上相，并回收到富含溶剂的假萃取物底部相中，该相再循环到溶剂萃取区，优选在低于侧流被抽出的点的点以下。膜分离区优选在反渗透条件下使用界面聚合的膜。

9. 发明授权

US5416259A Feed pretreatment for pervaporation process 失效
标题翻译：进料预处理渗透蒸发过程
公开(公告)号：US5416259A
公开(公告)日：1995-05-16
申请号：US125044
申请日：1993-09-21
申请人： Charles P. Darnell , Tan J. Chen , Enrique F. Juarez
发明人： Charles P. Darnell , Tan J. Chen , Enrique F. Juarez
IPC分类号： C10G31/11 , C10G53/08 , C07C7/00 , C07C7/12 , C07C7/144
CPC分类号： C10G31/11 , C10G53/08
摘要： The pervaporative treatment of hydrocarbon feeds which have been exposed to air or oxygen and which contain mixtures of aromatic and non-aromatic hydrocarbons to selectively separate the feed into an aromatics rich stream and a non-aromatics rich stream is improved by the step of pretreating the hydrocarbon feed over an adsorbent such as attapulgite clay.
摘要翻译：已经暴露于空气或氧气并且含有芳烃和非芳烃的混合物的烃进料的蒸发处理以选择性地将进料分离成富含芳烃的物流和富含非芳烃的物流通过以下步骤来改进：烃类进料通过吸附剂如绿坡缕石粘土。

10. 发明授权

US5401383A Controlling chilling tower profile for dilution chilling dewaxing of 600N waxy oil 失效
标题翻译：控制600N蜡质油稀释冷冻脱蜡的冷却塔型材
公开(公告)号：US5401383A
公开(公告)日：1995-03-28
申请号：US119771
申请日：1993-09-10
申请人： Patrick C. Ewener
发明人： Patrick C. Ewener
IPC分类号： C10G73/06 , C10G73/32 , C10G43/08
CPC分类号： C10G73/32 , C10G73/06
摘要： The incremental solvent dilution chilling of 600N waxy oils in a staged agitated chilling tower using cold solvent injection is improved in terms of feed filter rate with respect to a 600N waxy oil having a final boiling point of >600.degree. C. and a mean boiling point of about 500.degree. C. when the solvent dewaxing process is practiced under conditions of cold solvent injection such that there is an equal chilling rate/stage profile as compared to an equal temperature drop/stage profile in the chilling tower and with respect to a 600N waxy oil having a final boiling point of 600.degree. C. and a mean boiling point of about 500.degree. C. when the solvent dewaxing process is practiced under conditions of cold solvent injection such that there is an equal temperature drop/stage profile as compared to an equal chilling rate/stage profile in the chilling tower.
摘要翻译：在使用冷溶剂注入的分级搅拌冷却塔中600N蜡质油的增量溶剂稀释冷却方面相对于终沸点> 600℃的600N蜡状油的平均沸点提高了进料过滤速率，当溶剂脱蜡过程在冷溶剂注入条件下进行时，与冷却塔中的相同温度下降/阶段曲线相比，与冷却塔相比，具有相同的冷却速率/阶段分布，并且相对于600N 当溶剂脱蜡过程在冷溶剂注入条件下进行时，具有终沸点为600℃，平均沸点为约500℃的蜡状油，使得与在寒冷的塔中平均冷却速度/阶段轮廓。

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