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1. 发明申请

US20150307418A1 METHODS AND APPARATUSES FOR PRODUCING XYLENE FROM LIGNIN 审中-公开
标题翻译：从LIGNIN生产XYLENE的方法和装置
公开(公告)号：US20150307418A1
公开(公告)日：2015-10-29
申请号：US14260176
申请日：2014-04-23
申请人： UOP LLC
发明人： Stanley Joseph Frey , Joao Jorge da Silva Ferreira Alves
IPC分类号： C07C7/10 , C07C4/22 , C07C7/12 , C07C5/27 , C07C5/32 , C07C6/12
CPC分类号： C07C7/10 , C07C1/20 , C07C4/22 , C07C5/2702 , C07C5/277 , C07C5/321 , C07C5/373 , C07C6/12 , C07C6/126 , C07C7/12 , C10G1/002 , C10G1/02 , C10G1/08 , C10G45/58 , C10G69/02 , C10G2300/1014 , C10G2400/30 , C07C15/08 , C07C15/02
摘要： Methods and apparatuses are provided for producing a xylene product from a lignin supply. A method includes depolymerizing the lignin supply to produce a lignin aromatic stream, and isomerizing the lignin aromatic stream to produce an isomerized lignin stream. The desired xylene isomer is extracted from the isomerized lignin stream.
摘要翻译：提供了从木质素供应产生二甲苯产物的方法和装置。一种方法包括解聚木质素供应以产生木质素芳族物流，并使木质素芳族物流异构化以产生异构化的木质素流。从异构化的木质素流中提取所需的二甲苯异构体。

2. 发明申请

US20150232406A1 METATHESIS DEPOLYMERIZATION USING ACRYLATES 有权
标题翻译：使用丙烯酸酯的甲基脱氮化
公开(公告)号：US20150232406A1
公开(公告)日：2015-08-20
申请号：US14422740
申请日：2013-08-20
申请人： UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INC.
发明人： Kenneth Boone Wagener , Michael Schulz
IPC分类号： C07C51/60 , C08F236/02
CPC分类号： C07C51/60 , B01J31/2265 , B01J31/2273 , B01J31/2278 , B01J31/24 , B01J2231/54 , B01J2531/821 , C07C4/22 , C07C51/62 , C07C67/475 , C08F236/02 , C07C69/602 , C07C57/66 , C07C69/593
摘要： Olefin metathesis between an acrylate monomer and a polyene comprising molecule or polymer is employed as a method of cross-metathesizing or depolymerizing the molecule. The metathesis reaction forms a telechelic acrylate molecule that is a monomer, oligomer or polymer. The telechelic acrylate molecule can be employed as a monomer for condensation polymerization.
摘要翻译：使用丙烯酸酯单体和含多烯的分子或聚合物之间的烯烃复分解作为分子的交叉分解或解聚的方法。复分解反应形成作为单体，低聚物或聚合物的遥爪丙烯酸酯分子。丙烯酸遥爪分子可用作缩聚单体。

3. 发明申请

US20150175502A1 METHOD FOR MAKING HIGH PURITY DICYCLOPENTADIENE 审中-公开
标题翻译：制备高纯度二环戊二烯的方法
公开(公告)号：US20150175502A1
公开(公告)日：2015-06-25
申请号：US14471648
申请日：2014-08-28
申请人： CPC Corporation, Taiwan
发明人： Jyh-Haur HWANG , Wei-Bin SU , Chi-Yu CHEN , Karl Tze-Tang CHUANG , Cheng-Tsung HONG , Yung-Sheng HO
IPC分类号： C07C2/50 , C07C4/22
CPC分类号： C07C2/50 , C07C4/22 , C07C2601/10 , C07C2603/68 , C07C13/15 , C07C13/61
摘要： A method for making high purity dicyclopentadiene comprises the following steps: providing a dimer feedstock comprising dicyclopentadiene and methyl dicyclopentadiene; blending the dimer feedstock and a diluent to obtain a first blend; cracking the first blend in a vapor phase at 300° C. to 400° C. to obtain a cracked feedstock; separating the cracked feedstock into a second blend and a third blend; dimerizing the second blend at 50° C. to 120° C. to obtain a fourth blend; and separating the fourth blend to obtain a recycled diluent and high purity dicyclopentadiene. By using saturated C5 hydrocarbon, saturated C6 hydrocarbon, benzene and the mixture thereof as the diluent and the steps mentioned above, the clogging problem of cracker tubes is solved and the cost of makeup diluent usage is lowered.
摘要翻译：制备高纯度二环戊二烯的方法包括以下步骤：提供包含二环戊二烯和甲基二环戊二烯的二聚体原料; 将二聚体原料和稀释剂混合以获得第一共混物; 在300℃至400℃的气相中裂解第一共混物以获得裂化原料; 将裂化的原料分离成第二共混物和第三共混物; 将第二共混物在50℃-220℃下二聚，得到第四共混物; 并分离第四混合物以获得再循环稀释剂和高纯度二环戊二烯。通过使用饱和C 5烃，饱和C 6烃，苯及其混合物作为稀释剂和上述步骤，解决了裂解管的堵塞问题，降低了补充稀释剂使用的成本。

4. 发明申请

US20080097132A1 CRACKING OF DICYCLOPENTADIENE 审中-公开
标题翻译：二烯丙基二胺的裂解
公开(公告)号：US20080097132A1
公开(公告)日：2008-04-24
申请号：US11571413
申请日：2004-06-30
申请人： John C. Prindle Jr , Dru J. Manuel
发明人： John C. Prindle Jr , Dru J. Manuel
IPC分类号： C07C5/31
CPC分类号： C07C4/22 , C07C13/15
摘要： This invention provides a process for forming monomers from a dimer, wherein the dimer is dicyclopentadiene, di(methylcyclopentadiene), di(ethyleyclopentadiene), or a mixture of any two or more of these. The process comprises i) heating a liquid mixture comprising at least one dimer and at least one liquefying agent in a vaporization zone to at least the vaporization temperature of said mixture to form a vaporized mixture, wherein the vaporization zone consists essentially of a substantially straight conduit in which said liquid mixture occupies less than the entire cross sectional area of said conduit; and ii) introducing at least a portion of the vaporized mixture from i) into a cracking zone such that monomers are formed. This process is conducted at about atmospheric pressure.
摘要翻译：本发明提供了从二聚体形成单体的方法，其中二聚体是二环戊二烯，二（甲基环戊二烯），二（乙基环戊二烯）或其中任何两种或更多种的混合物。该方法包括：i）在蒸发区中将包含至少一种二聚体和至少一种液化剂的液体混合物加热至至少所述混合物的蒸发温度以形成蒸发的混合物，其中蒸发区基本上由基本上直的导管其中所述液体混合物占据小于所述导管的整个横截面面积; 和ii）将来自i）的蒸发混合物的至少一部分引入裂化区，从而形成单体。该过程在约大气压下进行。

5. 发明申请

US20010047120A1 Process for producing cyclopentadiene or derivatives thereof and apparatus for the same, and process for producing metallocenes or derivatives thereof 失效
标题翻译：生产环戊二烯或其衍生物的方法及其制备方法以及金属茂或其衍生物的制备方法
公开(公告)号：US20010047120A1
公开(公告)日：2001-11-29
申请号：US09822413
申请日：2001-04-02
申请人： Tanaka Kikinzoku Kogyo K.K.
发明人： Katsutsugu Kitada , Hiroaki Suzuki
IPC分类号： C07C013/15
CPC分类号： C07F17/00 , B01J19/0013 , B01J2219/00011 , B01J2219/00096 , B01J2219/00099 , B01J2219/00101 , B01J2219/00191 , C07C4/22 , C07C13/15 , C07C2601/10
摘要： The present invention provides a process for producing cyclopentadiene or a derivative thereof by heating a mixture containing at least one of dicyclopentadiene or a derivative thereof, the process comprising: a first step comprising heating the mixture into vapor; a second step comprising maintaining while heating the vapor at a temperature higher than the boiling point of the desired cyclopentadiene or derivative thereof to condense and remove high-boiling components and simultaneously collect residual vapor; and a third step comprising maintaining while heating the collected vapor at a temperature lower than the boiling point of the desired cyclopentadiene or derivative thereof to condense and collect the cyclopentadiene or derivative thereof. In the third step, the vapor may be contact with nitrogen gas to improve the yield of the cyclopentadiene or derivative thereof.
摘要翻译：本发明提供通过加热含有二环戊二烯或其衍生物中的至少一种的混合物来生产环戊二烯或其衍生物的方法，所述方法包括：第一步骤，包括将所述混合物加热成蒸气; 第二步骤包括在高于所需环戊二烯或其衍生物的沸点的温度下加热蒸气以冷凝和除去高沸点组分并同时收集残余蒸气; 并且第三步骤包括在低于所需环戊二烯或其衍生物的沸点的温度下加热所收集的蒸气，以冷凝和收集环戊二烯或其衍生物。在第三步骤中，蒸汽可以与氮气接触以提高环戊二烯或其衍生物的产率。

6. 发明授权

US6018085A Method of reclaiming styrene and other products from polystyrene based materials 有权
标题翻译：从聚苯乙烯基材料回收苯乙烯和其他产品的方法
公开(公告)号：US6018085A
公开(公告)日：2000-01-25
申请号：US150603
申请日：1998-09-10
申请人： Thomas E. Ponsford , Henry T. Ponsford
发明人： Thomas E. Ponsford , Henry T. Ponsford
IPC分类号： C07C4/22 , C07C1/00
CPC分类号： C07C4/22
摘要： A method of reclaiming styrene from polystyrene-containing materials contaminated with animal fats and/or vegetable oils. A solution of polystyrene from such materials in a solvent is heated in distillation equipment to depolymerize the polystyrene and produce a styrene fraction and a heavier fraction, the styrene fraction being separated from the heavier fraction. Prior to heating, an inert gas is used to purge the distillation equipment of oxygen. The method preferably is carried out at the lowest temperature which will achieve the desired rate of depolymerization.
摘要翻译：从含有动物脂肪和/或植物油污染的含聚苯乙烯材料回收苯乙烯的方法。将这种材料的聚苯乙烯在溶剂中的溶液在蒸馏设备中加热，使聚苯乙烯解聚，并产生苯乙烯部分和较重馏分，将苯乙烯部分与较重部分分离。在加热之前，使用惰性气体来吹扫氧气的蒸馏设备。该方法优选在将达到所需解聚速率的最低温度下进行。

7. 发明授权

US5877366A Dicyclopentadiene cracking process 失效
标题翻译：二环戊二烯裂解过程
公开(公告)号：US5877366A
公开(公告)日：1999-03-02
申请号：US861332
申请日：1992-03-25
申请人： John M. Birmingham
发明人： John M. Birmingham
IPC分类号： C07C4/22
CPC分类号： C07C4/22 , C07C2101/10
摘要： A process and a system for cracking dicyclopentadiene are disclosed pursuant to the process preheated dicyclopentadiene is introduced into a heated transfer fluid sufficiently below the transfer fluid surface to accomplish substantially complete conversion of said dicyclopentadiene to monomeric cyclopentadiene vapor.
摘要翻译：公开了一种用于裂解二环戊二烯的方法和系统，其中预热的二环戊二烯被引入到充分低于转移流体表面的加热的转移流体中，以实现所述二环戊二烯基本上完全转化为单环戊二烯蒸气。

8. 发明授权

US5799626A Methods for using styrene oil (as heat transfer fluid, hydraulic fluid, lubricant) 失效
标题翻译：使用苯乙烯油（作为传热液，液压油，润滑剂）
公开(公告)号：US5799626A
公开(公告)日：1998-09-01
申请号：US420236
申请日：1995-04-11
申请人： Thomas E. Ponsford , Henry T. Ponsford
发明人： Thomas E. Ponsford , Henry T. Ponsford
IPC分类号： A62D3/00 , C07C4/22 , C09K5/10 , C10G1/10 , C10L1/04 , C10M105/06 , C10M127/04 , C23F15/00 , G21D5/08 , F01P3/00 , C07C4/04
CPC分类号： G21D5/08 , C07C4/22 , C09K5/10 , C10G1/10 , C10L1/04 , C10M105/06 , C10M127/04 , C23F15/00 , C10M2203/06 , C10N2240/06 , C10N2240/08
摘要： Methods of using styrene oil, its fractions, and combinations thereof as working fluids, lubricants, fuels and solvents.
摘要翻译：使用苯乙烯油，其馏分及其组合作为工作流体，润滑剂，燃料和溶剂的方法。

9. 发明授权

US5672794A Recovery of styrene from waste polystyrene 失效
标题翻译：从废聚苯乙烯回收苯乙烯
公开(公告)号：US5672794A
公开(公告)日：1997-09-30
申请号：US697718
申请日：1996-08-29
申请人： Andreas Northemann
发明人： Andreas Northemann
IPC分类号： C07C4/22 , C07C1/00
CPC分类号： C07C4/22 , C07C2521/12 , C07C2521/14
摘要： Monomeric styrene is recovered from plastics waste containing styrene polymers by thermal depolymerization by a process in which the waste is transported in liquid or solid form into a fluidized bed of a solid heat transfer agent and is cracked or depolymerized in an average residence time of less than 60 seconds and styrene is obtained from the gaseous crack products. Preferably, magnesium aluminum silicate is used as a heat transfer agent and C.sub.1 -C.sub.6 -hydrocarbons formed as byproducts in the depolymerization are used as operating gas for maintaining the fluidized bed and are circulated.
摘要翻译：单体苯乙烯由包含苯乙烯聚合物的塑料废物通过热解聚反应回收，其中废物以液体或固体形式输送到固体传热剂的流化床中，并且在平均停留时间小于或等于 60秒，从气态裂纹产物得到苯乙烯。优选地，使用硅酸铝铝作为传热剂，并且在解聚中作为副产物形成的C 1 -C 6烃用作维持流化床并循环的操作气体。

10. 发明授权

US4522688A Process for recovery of cyclopentadienes 失效
标题翻译：回收环戊二烯的方法
公开(公告)号：US4522688A
公开(公告)日：1985-06-11
申请号：US545661
申请日：1983-10-26
申请人： Akira Yokogawa , Asao Takahashi , Isao Maruyama , Takao Hosaka
发明人： Akira Yokogawa , Asao Takahashi , Isao Maruyama , Takao Hosaka
IPC分类号： C07C1/00 , C07C4/22 , C07C7/04 , C07C13/15 , C07C67/00 , B01D3/14
CPC分类号： C07C13/15 , C07C4/22 , C07C7/04 , C07C2101/10
摘要： The process gives highly pure cyclopentadiene and methylcyclopentadiene from a cracked gasoline fraction. The merit of the process is that cyclopentadiene and methylcyclopentadiene are recovered by adding a simple distillation system to a conventional cracked gasoline treating plant without altering the plant and operating conditions thereof. An internal reflux stream is withdrawn from the stripping section of a BTX column of a conventional cracked gasoline treating plant, and is sent to a depolymerization-distillation column operated at a bottom temperature of 160.degree.-230.degree. C. The overhead stream of the column is sent to a cyclopentadiene column operated at a bottom temperature of 160.degree.-230.degree. C. Cyclopentadiene is recovered from the overhead of the column, and the bottom stream is sent to methylcyclopentadiene column operated at a bottom temperature of 170.degree.-210.degree. C. Methylcyclopentadiene is recovered from the overhead of the column.
摘要翻译：该方法从裂化汽油馏分中提供高度纯的环戊二烯和甲基环戊二烯。该方法的优点是通过向常规的裂化汽油处理装置添加简单的蒸馏系统而不改变其设备和操作条件来回收环戊二烯和甲基环戊二烯。将内部回流物流从常规裂化汽油处理装置的BTX柱的汽提段中取出，并送入在塔底温度为160°-230℃下操作的解聚 - 蒸馏塔。塔顶馏出物流送入在160°-230℃的底部温度下操作的环戊二烯塔。从塔顶塔顶回收环戊二烯，将塔底物流送入甲基环戊二烯塔，底部温度为170°-210℃ 从柱的顶部回收甲基环戊二烯。

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