| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 201 | AMINONAPHTHOQUINONE COMPOUNDS FOR TREATMENT AND/OR PREVENTION OF FIBROSIS DISEASES | US15776698 | 2016-11-16 | US20180325845A1 | 2018-11-15 | Yun YEN; Jing-ping LIOU; Chien Huang LIN |
| The invention relates to the use of a compound of Formula (I) as described herein and its effective dose in the prevention and/or treatment of fibrosis diseases. The compound can effectively prevent and/or treat a fibrosis disease without cytotoxicity or genotoxicity. | ||||||
| 202 | Production of aromatics from methane | US14967612 | 2015-12-14 | US10052617B2 | 2018-08-21 | Neeraj Sangar; Teng Xu; Larry L. Iaccino; Mobae Afeworki |
| A catalyst for the conversion of methane to higher hydrocarbons including aromatic hydrocarbons comprises molybdenum or a compound thereof dispersed on an aluminosilicate zeolite, wherein the amount of aluminum present as aluminum molybdate in the catalyst is less than 2700 ppm by weight. | ||||||
| 203 | SULFUR TERMINATED ORGANOSILICA MATERIALS AND USES THEREOF | US15802680 | 2017-11-03 | US20180142066A1 | 2018-05-24 | Joseph M. FALKOWSKI; Mobae AFEWORKI; David C. CALABRO; David A. GRIFFIN; Simon C. WESTON |
| Provided herein are compositions and methods for use of an organosilica material comprising a copolymer of at least one monomer of Formula [R1R2SiCH2]3 (I), wherein, R1 represents a C1-C4 alkoxy group; and R2 is a C1-C4 alkoxy group or a C1-C4 alkyl group; and at least one other monomer of Formula [(Z1O)xZ23-xSi—Z3—SZ4] (II), wherein, Z1 represents a hydrolysable functional group; Z2 represents a C1-C10 alkyl or aryl group; Z3 represents a C2-C11 cyclic or linear hydrocarbon; Z4 is either H or O3H; and x represents any one of integers 1, 2, and 3. The composition may be used as a support material to covalently attach transition metal cations, as a sorbent for olefin/paraffin separations, as a catalyst support for hydrogenation reactions, as a precursor for highly dispersed metal nanoparticles, or as a polar sorbent for crude feeds. | ||||||
| 204 | Method for the Production of Carbon Nanotube Structures | US15532649 | 2015-12-03 | US20170327378A1 | 2017-11-16 | Martin Pick; Fiona Ruth Smail; Adam Boies; Christian Hoecker |
| The present invention relates to a method for the production of carbon nanotube structures. | ||||||
| 205 | Production of aromatics from methanol and co-feeds | US15646889 | 2017-07-11 | US09809505B1 | 2017-11-07 | John S. Buchanan; Stephen H. Brown; Lorenzo C. DeCaul; Brett T. Loveless; Rohit Vijay; Stephen J. McCarthy; Michel Daage; Mayank Shekhar |
| Methods are provided for improving the yield of aromatics during conversion of oxygenate feeds. An oxygenate feed can contain a mixture of oxygenate compounds, including one or more compounds with a hydrogen index of less than 2, so that an effective hydrogen index of the mixture of oxygenates is between about 1.4 and 1.9. Methods are also provided for converting a mixture of oxygenates with an effective hydrogen index greater than about 1 with a pyrolysis oil co-feed. The difficulties in co-processing a pyrolysis oil can be reduced or minimized by staging the introduction of pyrolysis oil into a reaction system. This can allow varying mixtures of pyrolysis oil and methanol, or another oxygenate feed, to be introduced into a reaction system at various feed entry points. | ||||||
| 206 | Agent for the selective adjustment of blood lipids | US15094646 | 2016-04-08 | US09789134B2 | 2017-10-17 | Shamil′ D. Akhmedov; Sergej A. Afanasiev; Victor D. Filimonov; Pavel S. Postnikov; Marina E. Trusova; Rostislav S. Karpov |
| The invention relates to the medicine, namely to an agent for reducing the cholesterol and triglycerides in the blood plasma. The agent claimed comprises a nanocomposite that is a carbon-containing nanoparticles coated with the organic alkyl functional groups representing the residuals —C4H9, —C6H11, —C8H15, —C10H21, —C16H33, —C18H35. These groups are deposited by the covalent modification using diazonium salts of the general formula XC6H4N2+Y−, where X is the alkyl residual —C4H9, —C6H11, —C8H15, —C10H21, —C16H33, or C18H35, Y is the anion HSO4−, Cl−, BF4− or TsO−. The invention provides an effective reduction of cholesterol and triglyceride presented in the blood plasma. | ||||||
| 207 | Hydrocarbon Conversion | US15593984 | 2017-05-12 | US20170247300A1 | 2017-08-31 | Paul F. Keusenkothen; Juan D. Henao; Abhimanyu O. Patil; Guang Cao |
| This disclosure relates to the conversion of methane to higher molecular weight (C5+) hydrocarbon, including aromatic hydrocarbon, to materials and equipment useful in such conversion, and to the use of such conversion for, e.g., natural gas upgrading. | ||||||
| 208 | Hydrocarbon Conversion | US15593847 | 2017-05-12 | US20170247299A1 | 2017-08-31 | Juan D. Henao; Paul F. Keusenkothen; Abhimanyu O. Patil |
| This invention relates to the conversion of substantially-saturated hydrocarbon to higher-value hydrocarbon products such as aromatics and/or oligomers, to equipment and materials useful in such conversion, and to the use of such conversion for, e.g., natural gas upgrading. | ||||||
| 209 | Production of aromatics from methanol and co-feeds | US14829399 | 2015-08-18 | US09732013B2 | 2017-08-15 | John S. Buchanan; Stephen H. Brown; Lorenzo C. DeCaul; Brett T. Loveless; Rohit Vijay; Stephen J. McCarthy; Michel Daage; Mayank Shekhar |
| Methods are provided for improving the yield of aromatics during conversion of oxygenate feeds. An oxygenate feed can contain a mixture of oxygenate compounds, including one or more compounds with a hydrogen index of less than 2, so that an effective hydrogen index of the mixture of oxygenates is between about 1.4 and 1.9. Methods are also provided for converting a mixture of oxygenates with an effective hydrogen index greater than about 1 with a pyrolysis oil co-feed. The difficulties in co-processing a pyrolysis oil can be reduced or minimized by staging the introduction of pyrolysis oil into a reaction system. This can allow varying mixtures of pyrolysis oil and methanol, or another oxygenate feed, to be introduced into a reaction system at various feed entry points. | ||||||
| 210 | Production of aromatics from a methane conversion process | US13915113 | 2013-06-11 | US09327265B2 | 2016-05-03 | Jeffery C. Bricker; John Q. Chen; Peter K. Coughlin |
| Methods and systems are provided for converting methane in a feed stream to acetylene. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to a process stream having aromatic compounds. The acetylene stream can be reacted to generate larger hydrocarbon compounds, which are passed to a cyclization and aromatization reactor to generate aromatics. The method according to certain aspects includes controlling the level of carbon oxides in the hydrocarbon stream. | ||||||
| 211 | METHODS AND APPARATUSES FOR HYDROCARBON PRODUCTION | US14499663 | 2014-09-29 | US20160090335A1 | 2016-03-31 | Charles P. Luebke; Bart Dziabala; Belma Demirel |
| Methods and apparatuses are provided for producing hydrocarbons. A method for producing hydrocarbons may include two or more reactors having a distributed aromatic rich feed and hydrogen system. Using this configuration, the aromatic rich feed and hydrogen streams are split equally to all reactors wherein each reactor contains a catalyst. The outlet from the last reactor may include a recycle that may be injected into the inlet of the first reactor. | ||||||
| 212 | Process for the conversion of ethane to aromatic hydrocarbons | US14280914 | 2014-05-19 | US09144790B2 | 2015-09-29 | Ann Marie Lauritzen; Ajay Madhav Madgavkar |
| A process for producing aromatic hydrocarbons which comprises (a) contacting ethane with a dehyroaromatization aromatic catalyst which is comprised of about 0.005 to about 0.1 wt % platinum, an amount of gallium which is equal to or greater than the amount of the platinum, from about 10 to about 99.9 wt % of an aluminosilicate, and a binder, and (b) separating methane, hydrogen, and C2-5 hydrocarbons from the reaction products of step (a) to produce aromatic reaction products including benzene. | ||||||
| 213 | Process for the conversion of ethane to aromatic hydrocarbons | US14176875 | 2014-02-10 | US08946107B2 | 2015-02-03 | Ann Marie Lauritzen; Ajay Madhav Madgavkar |
| A process for producing aromatic hydrocarbons which comprises (a) contacting ethane with a dehydroaromatization aromatic catalyst which is comprised of 0.005 to 0.1% wt platinum, an amount of iron which is equal to or greater than the amount of the platinum, from 10 to 99.9% wt of an aluminosilicate, and a binder, and (b) separating methane, hydrogen, and C2-5 hydrocarbons from the reaction products of step (a) to produce aromatic reaction products including benzene. | ||||||
| 214 | SEPARATION OF HYDROCARBON FAMILIES OR OF INDIVIDUAL COMPONENTS BY CONSECUTIVE EXTRACTIVE DISTILLATIONS PERFORMED IN A SINGLE COLUMN | US14365739 | 2012-12-14 | US20140353216A1 | 2014-12-04 | Luciano Scibola; Stefano Favilli |
| A column for consecutive extractive distillations, in particular of crude hydrocarbon mixes comprising aromatic, naphthene and paraffin hydrocarbons. The invention also relates to methods for separating and recovering the components of a crude hydrocarbon mix comprising aromatic, naphthene and paraffin hydrocarbons by consecutive extractive distillations provided by means of the column for consecutive extractive distillations, to which the invention also relates. | ||||||
| 215 | Process for the conversion of mixed lower alkanes to aromatic hydrocarbons | US13505043 | 2010-10-29 | US08835706B2 | 2014-09-16 | Mahesh Venkataraman Iyer; Ann Marie Lauritzen; Ajay Madhav Madgavkar |
| A process for the conversion of mixed lower alkanes into aromatics which comprises first reacting a mixed lower alkane feed comprising at least propane and ethane in the presence of an aromatization catalyst under reaction conditions which maximize the conversion of propane into first stage aromatic reaction products, separating ethane from the first stage aromatic reaction products, reacting ethane in the presence of an aromatization catalyst under reaction conditions which maximize the conversion of ethane into second stage aromatic reaction products, and optionally separating ethane from the second stage aromatic reaction products. | ||||||
| 216 | PROCESS FOR THE CONVERSION OF ETHANE TO AROMATIC HYDROCARBONS | US14176875 | 2014-02-10 | US20140155258A1 | 2014-06-05 | Ann Marie LAURITZEN; Ajay Madhav MADGAVKAR |
| A process for producing aromatic hydrocarbons which comprises (a) contacting ethane with a dehydroaromatization aromatic catalyst which is comprised of 0.005 to 0.1% wt platinum, an amount of iron which is equal to or greater than the amount of the platinum, from 10 to 99.9% wt of an aluminosilicate, and a binder, and (b) separating methane, hydrogen, and C2-5 hydrocarbons from the reaction products of step (a) to produce aromatic reaction products including benzene. | ||||||
| 217 | Method for reacting natural gas to aromatics while electrochemically removing hydrogen and electrochemically reacting the hydrogen water | US13256536 | 2010-03-29 | US08575411B2 | 2013-11-05 | Joana Coelho Tsou; Alexander Panchenko; Annebart Engbert Wentink; Sebastian Ahrens; Thomas Heidemann |
| The invention relates to a process for converting aliphatic hydrocarbons having from 1 to 4 carbon atoms into aromatic hydrocarbons, which comprises the steps: a) reaction of a feed stream E comprising at least one aliphatic hydrocarbon having from 1 to 4 carbon atoms in the presence of a catalyst under nonoxidative conditions to give a product stream P comprising aromatic hydrocarbons and hydrogen and b) electrochemical removal of at least part of the hydrogen formed in the reaction from the product stream P by means of a gastight membrane-electrode assembly comprising at least one selectively proton-conducting membrane and at least one electrode catalyst on each side of the membrane, where at least part of the hydrogen is oxidized to protons over the anode catalyst on the retentate side of the membrane and the protons are, after passing through the membrane on the permeate side, reacted with oxygen to form water over the cathode catalyst, with the oxygen originating from an oxygen-comprising stream O which is brought into contact with the permeate side of the membrane. | ||||||
| 218 | Catalyst for aromatization of lower hydrocarbons and process for production of aromatic compounds | US12595924 | 2008-03-28 | US08558045B2 | 2013-10-15 | Shinichi Yamada; Tomohiro Yamada; Yuji Ogawa; Takuya Hatagishi; Yo Yamamoto; Yoshio Sugiyama |
| A catalyst for aromatizing a lower hydrocarbon, in order to increase the amount of production of useful aromatic compounds, such as benzene and toluene, by improving the methane conversion rate, the benzene formation rate, the naphthalene formation rate and the BTX formation rate (or a total formation rate of benzene, toluene and xylene) is such that molybdenum and silver are loaded on a metallosilicate as a substrate. It is more preferable to obtain the aromatizing catalyst by loading molybdenum and silver after modifying a zeolite formed of the metallosilicate with a silane compound that has a molecular diameter larger than a pore diameter of the zeolite and that has an amino group, which selectively reacts at a Bronsted acid point of the zeolite, and a straight-chain hydrocarbon group. | ||||||
| 219 | Renewable compositions | US13441468 | 2012-04-06 | US08546627B2 | 2013-10-01 | Patrick R. Gruber; Matthew W. Peters; Josefa M. Griffith; Yassin Al Obaidi; Leo E. Manzer; Joshua D. Taylor; David E. Henton |
| The present invention is directed to renewable compositions derived from fermentation of biomass, and integrated methods of preparing such compositions. | ||||||
| 220 | INITIAL HYDROTREATING OF NAPHTHENES WITH SUBSEQUENT HIGH TEMPERATURE REFORMING | US13327220 | 2011-12-15 | US20130158317A1 | 2013-06-20 | Mark D. Moser; David A. Wegerer; Manuela Serban; Kurt M. VandenBussche |
| A process for the production of aromatics through the reforming of a hydrocarbon stream is presented. The process utilizes the differences in properties of components within the hydrocarbon stream to increase the energy efficiency. The differences in the reactions of different hydrocarbon components in the conversion to aromatics allows for different treatments of the different components to reduce the energy used in reforming process. | ||||||
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