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1. 发明申请

WO2012148829A2 HIGH TEMPERATURE PLATFORMING PROCESS 审中-公开
标题翻译：高温平台过程
公开(公告)号：WO2012148829A2
公开(公告)日：2012-11-01
申请号：PCT/US2012/034605
申请日：2012-04-23
申请人： UOP LLC , MOSER, Mark D. , SADLER, Clayton C. , LAPINSKI, Mark P. , VANDEN BUSSCHE, Kurt M.
发明人： MOSER, Mark D. , SADLER, Clayton C. , LAPINSKI, Mark P. , VANDEN BUSSCHE, Kurt M.
IPC分类号： C10G61/02 , C10G59/02 , C10G35/04
CPC分类号： C10G35/04 , C07C4/06 , C10G35/06 , C10G61/04 , C10G2300/1044 , C10G2300/4018 , C10G2400/30 , Y02P20/584 , C07C15/02 , C07C15/067
摘要： A process for reforming a hydrocarbon stream is presented. The process involves increasing the processing temperatures in the reformers. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
摘要翻译：提出了一种重整烃流的方法。该方法涉及提高改性剂中的加工温度。改造者在不同的条件下运行，以利用平衡中的优点，但需要修改以防止增加热裂纹和防止焦化增加。该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。

2. 发明申请

WO1994002438A1 REFORMING PROCESS FOR PRODUCING HIGH-PURITY BENZENE 审中-公开
标题翻译：用于生产高纯度苯的改性方法
公开(公告)号：WO1994002438A1
公开(公告)日：1994-02-03
申请号：PCT/US1993006856
申请日：1993-07-23
申请人： CHEVRON RESEARCH AND TECHNOLOGY COMPANY
发明人： CHEVRON RESEARCH AND TECHNOLOGY COMPANY , MORRISON, Scott, G. , BROWN, Warren, E.
IPC分类号： C07C07/10
CPC分类号： C10G61/04
摘要： Provided is a reforming process for producing a high purity benzene product using a non-acidic zeolitic catalyst. The high purity benzene is extracted from a light fraction of reformate that has less than 500 ppm by weight toluene. Generally, a hydrocarbon feed is reformed in a reformer under reforming conditions in the presence of a non-acidic catalyst to produce a reformate. That reformate is separated into a light fraction and a heavy fraction. The extraction unit, preferably an extractive distillation unit, is then used to separate the light fraction into an aromatic extract stream and a nonaromatic raffinate stream.
摘要翻译：提供了使用非酸性沸石催化剂制造高纯度苯产物的重整方法。从具有少于500重量ppm的甲苯的轻馏分重整产物中提取高纯度苯。通常，在重整器中，在非酸性催化剂存在下，在重整器中重整碳氢化合物进料以产生重整产物。重整产物被分成轻馏分和重馏分。然后使用提取单元，优选萃取蒸馏单元将轻馏分分离成芳烃萃取物流和非芳族萃余液流。

3. 发明申请

WO2012099964A2 IMPROVED ORGANIC CHLORIDE ADSORBENT 审中-公开
标题翻译：改进的有机氯化物吸附剂
公开(公告)号：WO2012099964A2
公开(公告)日：2012-07-26
申请号：PCT/US2012021726
申请日：2012-01-18
申请人： BASF CORP , MAGLIO ALFONSE , MCCAFFREY RICHARD T
发明人： MAGLIO ALFONSE , MCCAFFREY RICHARD T
IPC分类号： B01D53/68 , B01D15/08 , B01J19/24 , B01J20/10 , B01J29/06
CPC分类号： B01D53/70 , B01D53/02 , B01D2253/108 , B01D2257/2064 , B01J20/18 , B01J23/42 , B01J23/96 , B01J38/18 , B01J38/44 , B01J2220/56 , C10G35/085 , C10G61/04 , C10G2300/104 , C10G2300/1044 , C10G2300/4081
摘要： Chemically combined chlorides are removed from intermediate and product streams of a hydrocarbon reforming process by contacting the streams with zeolite 13X, having a Si/AI ratio of less than 1.25.
摘要翻译：通过使物流与Si / Al比小于1.25的沸石13X接触，从烃重整过程的中间体和产物流中除去化学上合并的氯化物。

4. 发明申请

WO2006007034A1 NAPHTHA HYDROPROCESSING WITH MERCAPTAN REMOVAL 审中-公开
公开(公告)号：WO2006007034A1
公开(公告)日：2006-01-19
申请号：PCT/US2005/015123
申请日：2005-04-29
申请人： EXXONMOBIL RESEARCH AND ENGINEERING COMPANY , DAVIS, Timothy, J. , HILBERT, Timothy, L. , ELLIS, Edward, S. , GREELEY, John, P.
发明人： DAVIS, Timothy, J. , HILBERT, Timothy, L. , ELLIS, Edward, S. , GREELEY, John, P.
IPC分类号： C10G45/02
CPC分类号： C10G47/00 , C10G45/02 , C10G61/04 , C10G61/06 , C10G63/04 , C10G65/12 , C10G2400/02
摘要： This invention relates to the hydroprocessing of naphtha with removal of mercaptan from product. Naphtha feedstock is hydrotreated and hydrocracked. Sulfur-containing contaminants, notably C 5 + recombinant mercaptans, are then selectively removed from the hydrocracked naphtha by selective extraction or adsorption.
摘要翻译：本发明涉及从产物中除去硫醇的石脑油的加氢处理。石脑油原料被加氢处理和加氢裂化。然后通过选择性提取或吸附从加氢裂化石脑油中选择性除去含硫污染物，特别是C 5+重组硫醇。

5. 发明申请

WO1996010548A1 PROCESS FOR PRODUCING AROMATIC HYDROCARBON 审中-公开
标题翻译：生产芳香烃的方法
公开(公告)号：WO1996010548A1
公开(公告)日：1996-04-11
申请号：PCT/JP1995001059
申请日：1995-05-31
申请人： SANYO PETROCHEMICAL CO., LTD. , KIYAMA, Kazuyoshi , TSUNODA, Takashi , KAWASE, Masatsugu
发明人： SANYO PETROCHEMICAL CO., LTD.
IPC分类号： C07C15/02
CPC分类号： C10G69/08 , C07C2/00 , C07C2521/04 , C07C2523/06 , C07C2529/04 , C07C2529/06 , C07C2529/40 , C10G35/095 , C10G45/64 , C10G50/00 , C10G61/04 , C07C15/00
摘要： A process for producing aromatic hydrocarbon by bringing a low-boiling hydrocarbon feedstock containing olefin and/or paraffin into contact with a zeolite catalyst in a fixed-bed adiabatic reactor provided with a fixed catalyst bed containing a zeolite catalyst, characterized by conducting a catalytic cyclization under the following conditions: (1) the zeolite catalyst has an initial catalytic activity of at least 0.2 sec in terms of the initial first-order reaction rate constant of cracking of n-hexane therewith; (2) the temperature of the catalyst bed ranges from 450 to 650 DEG C; (3) the catalyst bed has a temperature distribution along the length thereof from the inlet to the outlet, and the distribution has at least one peak; and (4) the outlet temperature of the catalyst bed is in the range of the inlet temperature +/- 40 DEG C. The process permits aromatic hydrocarbon to be produced in a high yield and the operation to be conducted safely for long while avoiding the reduction in catalyst activity.
摘要翻译：一种通过在含有沸石催化剂的固定催化剂床的固定床绝热反应器中引入含有烯烃和/或石蜡的低沸点烃原料与沸石催化剂接触的方法，其特征在于进行催化环化在以下条件下：（1）沸石催化剂的初始催化活性以其正己烷裂解的初始一级反应速率常数为至少0.2秒-1; （2）催化剂床温度为450〜650℃; （3）催化剂床沿其长度从入口到出口具有温度分布，并且分布具有至少一个峰; 和（4）催化剂床的出口温度在入口温度+/- 40℃的范围内。该方法允许以高产率生产芳烃，并且操作长时间安全地进行，同时避免催化剂活性降低。

6. 发明申请

WO2014197205A1 NAPHTHA CRACKING 审中-公开
公开(公告)号：WO2014197205A1
公开(公告)日：2014-12-11
申请号：PCT/US2014/038870
申请日：2014-05-21
申请人： UOP LLC
发明人： FUNK, Gregory A. , WIER, Mary Jo
IPC分类号： C10G35/00
CPC分类号： C10G9/36 , C10G35/04 , C10G45/00 , C10G59/04 , C10G61/04 , C10G61/06 , C10G63/04 , C10G67/06 , C10G69/04 , C10G69/06 , C10G69/08
摘要： A process for increasing the yields of light olefins and the yields of aromatics from a hydrocarbon stream is presented. The process includes a first separation to direct the light components that are not reformable to a cracking unit, with the remainder passed to a second separation unit. The second separation unit extracts normal components from the hydrocarbon stream to pass to the cracking unit. The resulting hydrocarbon stream with reduced light ends and reduced normals is passed to a reforming unit.
摘要翻译：提出了一种从碳氢化合物流中提高轻质烯烃产率和芳族化合物收率的方法。该方法包括将不可重整的轻组分引导至裂化装置的第一分离，其余部分通入第二分离单元。第二分离单元从烃流中提取正常组分以通过裂解装置。所得到的具有减少的光端和减少的法线的烃流被传送到重整单元。

7. 发明申请

WO2012145740A2 PRODUCTION OF AROMATICS FROM NONCATALYTICALLY CRACKED FATTY ACID BASED OILS 审中-公开
标题翻译：从非糖化的基于脂肪酸的油中生产芳族化合物
公开(公告)号：WO2012145740A2
公开(公告)日：2012-10-26
申请号：PCT/US2012034648
申请日：2012-04-23
申请人： UNIV NORTH DAKOTA , SEAMES WAYNE , TANDE BRIAN
发明人： SEAMES WAYNE , TANDE BRIAN
IPC分类号： C07C15/04 , C07B61/00 , C07C15/06 , C07C15/08 , C07C15/085
CPC分类号： C10G3/49 , C10G3/00 , C10G47/20 , C10G51/04 , C10G55/04 , C10G57/005 , C10G61/04 , C10G63/04 , C10G2300/1014 , C10G2400/08 , Y02P30/20
摘要： A method for producing aromatic compounds from fatty acid oils including heating a fatty acid oil to a temperature between about 100° C to about 800° C at a pressure between about vacuum conditions and about 200 psia for a time sufficient to crack the oil and produce a cracked fatty acid oil; removing undesired materials, unreacted oil, heavy ends, and light ends from the cracked fatty acid oil; heating the resulting purified cracked fatty acid oil to a temperature between about 100° C to about 800° C at a pressure between about vacuum conditions and about 200 psia for a time sufficient to reform alkenes and alkanes in the cracked fatty acid oil into aromatic compounds and produce a reformed fatty acid oil; and extracting components from the reformed fatty acid oil to produce a mixture of chemical products containing between 5% and 90% aromatic compounds by weight.
摘要翻译：一种从脂肪酸油制备芳族化合物的方法，包括在约100℃至约800℃之间的温度下将脂肪酸油加热至大约真空条件和约200psia之间的压力足以裂解油并产生裂解脂肪酸油; 从破裂的脂肪酸油中除去不想要的物质，未反应的油，重的末端和轻馏分; 将所得纯化的裂解脂肪酸油在约100℃至约800℃之间的温度下在约真空条件和约200psia之间的压力下加热足够的时间，将裂解的脂肪酸油中的烯烃和烷烃重整成芳族化合物并生产改性脂肪酸油; 并从重整脂肪酸油中提取组分以产生含有5重量％至90重量％的芳族化合物的化学产品的混合物。

8. 发明申请

WO2010145193A1 一种多产芳烃的重整系统及其方法审中-公开
公开(公告)号：WO2010145193A1
公开(公告)日：2010-12-23
申请号：PCT/CN2010/000806
申请日：2010-06-09
申请人：北京金伟晖工程技术有限公司 , 丁冉峰
发明人：丁冉峰
IPC分类号： C10G59/02
CPC分类号： C10G61/04 , C10G2400/30

9. 发明申请

WO00034417A1 DEHYDROCYCLIZATION PROCESS WITH DOWNSTREAM DIMETHYLBUTANE REMOVAL 审中-公开
标题翻译：具有下游二甲基黄酮去除的脱氢方法
公开(公告)号：WO00034417A1
公开(公告)日：2000-06-15
申请号：PCT/US1998/026134
申请日：1998-12-09
IPC分类号： C10G35/085 , C10G35/095 , C10G61/02 , C10G61/04 , C10G61/06
CPC分类号： C10G61/02 , C10G35/085 , C10G35/095 , C10G61/04
摘要： In the present invention, dimethylbutanes are removed from the raffinate component of the feed to a dehydrocyclization process. Thus, according to a preferred embodiment, a process is provided for producing aromatics by the following steps: (a) contacting fresh paraffins rich feed hydrocarbons, containing 0.1 to 20.0 wt.% dimethylbutanes with a highly selective dehydrocyclization catalyst in a reaction zone, under dehydrocyclization reaction conditions, to convert paraffins to aromatics and obtain an aromatics rich effluent; (b) separating aromatics from the effluent to obtain an aromatics lean raffinate; (c) removing dimethylbutanes from the raffinate to obtain a raffinate of reduced dimethylbutane content; and (d) recycling the raffinate of reduced dimethylbutane content to the reaction zone. Preferably, the dehydrocyclization catalyst used is a nonacidic, monofunctional catalyst. Platinum on L zeolite is a particularly preferred highly selective dehydrocyclization catalyst for use in the process.
摘要翻译：在本发明中，将二甲基丁烷从进料的萃余液组分中除去脱氢环化过程。因此，根据优选的实施方案，提供了通过以下步骤生产芳族化合物的方法：（a）在反应区中将含有0.1至20.0重量％的二甲基丁烷的新鲜富含烯烃的原料烃与高选择性脱氢环化催化剂接触，脱氢环化反应条件，将石蜡转化为芳烃并获得富含芳烃的流出物; （b）从流出物中分离出芳族化合物以获得芳烃贫残余物; （c）从萃余液中除去二甲基丁烷以获得还原的二甲基丁烷含量的萃余液; 和（d）将还原的二甲基丁烷含量的残液回收到反应区。优选地，所用的脱氢环化催化剂是非酸性单官能催化剂。 L沸石上的铂是用于该方法的特别优选的高选择性脱氢环化催化剂。

10. 发明申请

WO2016003964A1 METHODS AND APPARATUSES FOR PRODUCING LINEAR ALKYLBENZENE FROM NATURAL OILS 审中-公开
标题翻译：从天然油生产线性烷基苯胺的方法和装置
公开(公告)号：WO2016003964A1
公开(公告)日：2016-01-07
申请号：PCT/US2015/038428
申请日：2015-06-30
申请人： UOP LLC
发明人： MAJUMDER, Debarshi , FICHTL, Geoffrey William
IPC分类号： C07C15/107 , C07C1/20 , C10G3/00 , C10G11/02 , C10G35/085 , C07C5/22 , C01B3/24 , C10G47/16
CPC分类号： C07C2/66 , C07C4/16 , C07C5/333 , C10G3/00 , C10G29/205 , C10G35/04 , C10G45/58 , C10G59/06 , C10G61/02 , C10G61/04 , C10G69/08 , C10G2300/1014 , C10G2300/1018 , C10G2400/30 , Y02P20/132 , Y02P30/20 , C07C15/107 , C07C11/02 , C07C15/04
摘要： Apparatuses and methods for producing linear alkylbenzene products from renewable oils are provided. An exemplary method includes deoxygenating the renewable oil in a deoxygenation zone to form paraffins. The method fractionates the paraffins to form first and second fractions. The method processes the first fraction of paraffins in a reforming zone to form a reformate stream and recovers a first hydrogen stream from the reforming zone. The method includes forming a LAB stream in a LAB production zone from the second fraction of paraffins and a portion of the reformate stream. Further, the method includes recovering a second hydrogen stream in the LAB production zone and recycling the first hydrogen stream from the reforming zone and the second hydrogen stream from the LAB production zone, wherein substantially all hydrogen recovered from the reforming zone and the LAB production zone is recycled.
摘要翻译：提供了从可再生油生产线性烷基苯产品的设备和方法。示例性的方法包括在脱氧区中对可再生油进行脱氧以形成链烷烃。该方法分馏石蜡以形成第一和第二馏分。该方法在重整区中处理第一级链烷烃以形成重整产物流并从重整区回收第一氢气流。该方法包括在第二部分石蜡和重整产物流的一部分的LAB生产区中形成LAB流。此外，该方法包括回收LAB生产区中的第二氢气流并将来自重整区的第一氢气流和来自LAB生产区的第二氢气流再循环，其中基本上从重整区和LAB生产区回收的所有氢被回收。

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