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71. 发明申请

US20160272908A1 Gas Purification Method 有权
标题翻译：气体净化方法
公开(公告)号：US20160272908A1
公开(公告)日：2016-09-22
申请号：US14777565
申请日：2014-03-18
申请人： OSAKA GAS CO., LTD.
发明人： Takahisa Utaki , Shota Kawashima , Kenji Seki , Yuhei Morita
IPC分类号： C10L3/10 , B01J20/20 , B01J20/28 , C01B31/08
CPC分类号： C10L3/101 , B01D53/047 , B01D2253/102 , B01D2253/108 , B01D2253/116 , B01D2256/245 , B01D2258/05 , B01J20/20 , B01J20/28004 , B01J20/28011 , B01J20/28069 , B01J20/28071 , B01J20/28078 , B01J20/2808 , B01J20/3416 , B01J20/3491 , C01B32/306 , C10L3/102 , C10L2290/12 , C10L2290/542
摘要： The rate of recovery of a purification target gas from a gas purification apparatus that uses a PSA device is improved, and both a high purity and a high recovery rate are achieved with good power efficiency. The present invention is directed to a gas purification method using the PSA method, in which a carbon molecular sieve having a pore volume, at a pore diameter of 0.38 nm or more, of not exceeding 0.05 cm3/g and a pore volume, at a pore diameter of 0.34 nm, of 0.15 cm3/g or more, in a pore diameter distribution measured by the MP method is used as an adsorbent, and, in an adsorption step, a miscellaneous gas is adsorbed from a source gas by bringing the source gas into contact with the adsorbent for 10 seconds or more and 6000 seconds or less so as to obtain a concentrated methane.
摘要翻译：来自使用PSA装置的气体净化装置的净化对象气体的回收率提高，并且以良好的功率效率实现高纯度和高回收率。本发明涉及一种使用PSA法的气体净化方法，其中在孔径为0.38nm以上的孔体积为0.1cm 3 / g以上的碳分子筛和孔体积为使用通过MP法测定的孔径分布中的0.34nm的孔径为0.34nm，为0.15cm 3 / g以上，作为吸附剂，在吸附工序中，通过使源极气体从源气体吸附杂质气体气体与吸附剂接触10秒以上6000秒以下，以获得浓缩的甲烷。

72. 发明授权

US09447335B2 Process for removing metals from hydrocarbons 有权
标题翻译：从碳氢化合物中除去金属的工艺
公开(公告)号：US09447335B2
公开(公告)日：2016-09-20
申请号：US13877706
申请日：2011-10-05
申请人： Mahpuzah Abai , Martin P. Atkins , Kuah Y. Cheun , John Holbrey , Peter Nockemann , Ken Seddon , Geetha Srinivasan , Yiran Zou
发明人： Mahpuzah Abai , Martin P. Atkins , Kuah Y. Cheun , John Holbrey , Peter Nockemann , Ken Seddon , Geetha Srinivasan , Yiran Zou
IPC分类号： C10G21/06 , C10G21/20 , C10G21/22 , C10G29/06 , C10G21/24 , C10L3/10
CPC分类号： C10G21/20 , B01D2252/30 , B01D2256/24 , B01D2257/602 , C10G21/06 , C10G21/22 , C10G21/24 , C10G25/003 , C10G29/06 , C10G2300/1025 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/205 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L3/101 , C10L2290/542
摘要： The present invention relates to a process for the removal of mercury from a mercury-containing hydrocarbon fluid feed using specifically selected ionic liquids comprising, contacting the mercury-containing hydrocarbon fluid feed with an ionic liquid having the formula [Cat+][M+][X−] and separating from the ionic liquid a hydrocarbon fluid product having a reduced mercury content compared to the mercury-containing fluid feed.
摘要翻译：本发明涉及一种使用特定选择的离子液体从含汞烃流体进料中除去汞的方法，该方法包括：使含汞烃流体进料与具有式[Cat +] [M +] [X - ]并与离子液体分离，与含汞流体进料相比，具有降低的汞含量的烃流体产物。

73. 发明申请

US20160243527A1 METHODS FOR REGENERATION OF AN ORGANOSILICA MEDIA 审中-公开
标题翻译：用于再生有机骨架介质的方法
公开(公告)号：US20160243527A1
公开(公告)日：2016-08-25
申请号：US15047171
申请日：2016-02-18
申请人： ProSep, Inc.
发明人： Michael GROSSMAN , Greg HALLAHAN , Caleb SMATHERS
IPC分类号： B01J20/34 , B01J20/22 , C10L3/10
CPC分类号： B01J20/34 , B01J20/22 , C10L3/06 , C10L3/101 , C10L2230/02 , C10L2290/06 , C10L2290/12 , C10L2290/542
摘要： Methods for regenerating a bed or organosilica particles and producing a treated gaseous stream are described herein. A method for regenerating a bed of organosilica particles includes introducing a heated regenerate stream to a bed of organosilica particles comprising captured C3+ hydrocarbons under conditions sufficient to remove at least a portion of the captured C3+ hydrocarbons from the organosilica particles; and introducing a cooled regenerate gaseous stream to the heated bed of organosilica particles. The regenerated organosilica particles are used to treat additional gaseous streams.
摘要翻译：本文描述了用于再生床或有机二氧化硅颗粒并产生经处理的气流的方法。用于再生床的有机二氧化硅颗粒的方法包括在足以从有机二氧化硅颗粒中去除至少一部分捕获的C3 +烃的条件下将加热的再生物流引入到包含捕获的C3 +烃的有机二氧化硅颗粒床中; 并将冷却的再生气流引入有机二氧化硅颗粒的加热床。再生的有机硅颗粒用于处理额外的气流。

74. 发明授权

US09404685B2 Water removal and heavy-hydrocarbon removal process in liquefied natural gas production from mixed gas rich in methane 有权
标题翻译：从富含甲烷的混合气体中生产液化天然气中的除水和重质烃清除工艺
公开(公告)号：US09404685B2
公开(公告)日：2016-08-02
申请号：US14345401
申请日：2012-09-13
申请人： Yonggen Xuan , Huazhou Xu
发明人： Yonggen Xuan , Huazhou Xu
IPC分类号： B01D53/02 , F25J3/06 , C10L3/10 , B01D53/04
CPC分类号： F25J3/0635 , B01D53/0423 , B01D53/0462 , B01D2256/245 , B01D2257/702 , B01D2257/80 , B01D2259/40001 , B01D2259/402 , B01D2259/406 , B01D2259/416 , C10L3/101 , C10L3/102 , C10L3/106 , C10L2290/08 , C10L2290/12 , C10L2290/541 , C10L2290/542 , C10L2290/543 , F25J3/061 , Y02C20/20
摘要： A process for dehydrating and removing heavy hydrocarbons in the production of liquefied natural gas from a methane-rich gas mixture is disclosed, wherein the methane-rich gas mixture subjected to deacidification treatment is divided into two streams, i.e. the first stream and the second stream, wherein the first stream used as a system process gas is introduced into a drying procedure, and the second stream used as regenerating gas is introduced into a regenerating procedure; the first stream is subjected to a drying treatment, and the moisture and the heavy hydrocarbons are simultaneously removed from the first stream in a composite adsorbent bed(s) of a drying tower, wherein the moisture is removed such that the dew point at normal pressure is ≦−76° C. and the heavy hydrocarbon components of C6 and higher are removed such that the content of these components is ≦217 ppm; and the second stream is used as a regenerating gas in the regenerating procedure of the above-mentioned drying tower, subjected to a regenerating process, and then returned as a part of the system process gas. Comparing to those conventional processes, the present invention can achieve good purifying effect, lower equipment investment and late-stage energy consumption of the system, increase utilization ratio of feed gas, and the operation target of each unit becomes more clear and easy to control. The present invention further relates to an apparatus for carrying out the process.
摘要翻译：公开了一种从富含甲烷的气体混合物中脱氢和除去液化天然气生产中的重质烃的方法，其中进行脱酸处理的富含甲烷的气体混合物被分成两股流，即第一流和第二流其中将用作系统工艺气体的第一料流引入干燥程序中，将用作再生气体的第二料流引入再生方法; 对第一流进行干燥处理，并且在干燥塔的复合吸附床中同时从第一流中除去水分和重质烃，其中去除水分使得常压下的露点 ≤-76℃，并且除去C6和更高的重质烃组分，使得这些组分的含量≤217ppm; 并且在上述干燥塔的再生过程中将第二流用作再生气体，进行再生过程，然后作为系统工艺气体的一部分返回。与传统方法相比，本发明可以实现良好的净化效果，较低的设备投入和系统的后期能耗，提高进料气的利用率，每个单元的运行目标变得更加清晰易控。本发明还涉及一种用于执行该过程的装置。

75. 发明授权

US09399607B2 Methods and apparatuses for reforming of hydrocarbons including recovery of products using a recovery zone, a pressure swing adsorption zone, and a membrane separation zone 有权
标题翻译：包括使用回收区回收产物的碳氢化合物的重整方法，变压吸附区和膜分离区
公开(公告)号：US09399607B2
公开(公告)日：2016-07-26
申请号：US14524301
申请日：2014-10-27
申请人： UOP LLC
发明人： Robert Edison Tsai , Xin X. Zhu , Bryan K. Glover , Eleftherios Adamopoulos , William Yanez
IPC分类号： B01D53/22 , B01D53/047 , C07C7/00 , C07C7/12 , C07C7/144 , C10L3/12 , C01B3/56
CPC分类号： C07C7/005 , B01D53/002 , B01D53/047 , B01D53/229 , B01D53/261 , B01D2053/221 , B01D2253/102 , B01D2253/104 , B01D2253/106 , B01D2253/108 , B01D2256/16 , B01D2256/24 , B01D2257/102 , B01D2257/108 , B01D2257/502 , B01D2257/7022 , B01D2257/7027 , B01D2257/80 , B01D2259/4146 , C01B3/34 , C01B3/501 , C01B3/56 , C01B2203/0405 , C01B2203/042 , C01B2203/043 , C01B2203/048 , C01B2203/1247 , C07C7/12 , C07C7/144 , C10L3/12 , C10L2290/542 , C10L2290/548
摘要： Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent into a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is separated for forming an H2-rich stream and a first intermediate liquid phase hydrocarbon stream. The H2-rich stream is contacted with an adsorbent to form an H2-ultra rich stream and a PSA tail gas stream. The PSA tail gas stream is contacted with an H2/hydrocarbon separation membrane to separate the PSA tail gas stream and form an H2-ultra rich permeate stream and a PSA tail gas hydrocarbon-containing non-permeate residue stream.
摘要翻译：提供了包括产物回收的烃类重整装置和方法的实施例。在一个实例中，一种方法包括将重整区流出物分离成净气相流和液相烃流。净气相流被分离以形成富H 2流和第一中间液相烃流。富H2流与吸附剂接触以形成富H2流和PSA尾气流。 PSA尾气流与H2 /烃分离膜接触以分离PSA尾气流并形成富H2的富含渗透物流和含PSA尾气烃的非渗透物残留物流。

76. 发明申请

US20160187057A1 LIQUEFIED NATURAL GAS FROM RICH NATURAL GAS 审中-公开
标题翻译：来自天然气的自然天然气
公开(公告)号：US20160187057A1
公开(公告)日：2016-06-30
申请号：US14977180
申请日：2015-12-21
申请人： Aspen Engineering Services, LLC
发明人： James M. Meyer
IPC分类号： F25J3/02 , C10L3/10
CPC分类号： F25J3/0209 , C10L3/101 , C10L3/106 , C10L2290/06 , C10L2290/08 , C10L2290/48 , C10L2290/541 , C10L2290/542 , C10L2290/543 , F25J1/0022 , F25J1/0052 , F25J1/023 , F25J1/0238 , F25J2220/62 , F25J2220/64
摘要： Rich natural gas is dried in a water scavenger unit, and then purified in a refluxed absorber. The refluxed stream for the absorber is a stream of predominantly methane condensed by cryogenic refrigeration. The refluxed absorber is operated below the critical point of methane, to allow condensation to occur. Liquefied natural gas is condensed in a cryogenic box, and then further cooled. Natural gas liquid from the refluxed absorber is stabilized for storage and transport.
摘要翻译：将丰富的天然气在除水单元中干燥，然后在回流吸收器中纯化。用于吸收器的回流物流是主要由低温制冷冷凝的甲烷流。回流的吸收器在甲烷的临界点以下操作，以使冷凝发生。液化天然气在低温箱中冷凝，然后进一步冷却。来自回流吸收器的天然气液体被稳定以用于储存和运输。

77. 发明申请

US20160167016A1 COATING METHODS USING ORGANOSILICA MATERIALS AND USES THEREOF 有权
标题翻译：使用有机硅材料的涂料方法及其用途
公开(公告)号：US20160167016A1
公开(公告)日：2016-06-16
申请号：US14966407
申请日：2015-12-11
申请人： Quanchang LI , Randall D. PARTRIDGE
发明人： Quanchang LI , Randall D. PARTRIDGE
IPC分类号： B01J20/32 , B01J20/18 , B01D53/04 , B01J20/28 , B01D53/02 , B01D53/047 , B01J20/26 , B01J20/10
CPC分类号： B01J20/223 , B01D15/00 , B01D53/02 , B01D53/04 , B01D53/0462 , B01D53/047 , B01D67/0088 , B01D69/10 , B01D71/70 , B01D2253/20 , B01D2253/25 , B01D2256/245 , B01D2257/302 , B01D2257/304 , B01D2257/40 , B01D2257/404 , B01D2257/504 , B01D2257/80 , B01J20/0229 , B01J20/0237 , B01J20/06 , B01J20/08 , B01J20/10 , B01J20/103 , B01J20/16 , B01J20/18 , B01J20/22 , B01J20/226 , B01J20/262 , B01J20/264 , B01J20/28011 , B01J20/28057 , B01J20/28061 , B01J20/28064 , B01J20/28066 , B01J20/28069 , B01J20/28071 , B01J20/28073 , B01J20/28076 , B01J20/28078 , B01J20/28083 , B01J20/286 , B01J20/3042 , B01J20/3204 , B01J20/3212 , B01J20/3236 , B01J20/3238 , B01J20/3272 , B01J23/42 , B01J23/44 , B01J29/0308 , B01J31/0274 , B01J31/125 , B01J31/127 , B01J35/1019 , B01J35/1023 , B01J35/1028 , B01J35/1061 , B01J37/0213 , B01J37/0236 , B01J37/036 , B01J2220/86 , B01J2231/641 , B01J2231/646 , C01B37/00 , C07C7/12 , C07F7/0807 , C07F7/081 , C07F7/0818 , C08F2/00 , C08F2/10 , C08F2/42 , C08F4/659 , C08F4/65912 , C08F4/65916 , C08F4/65925 , C08F4/65927 , C08F36/04 , C08F36/20 , C08G77/26 , C08G77/60 , C10G25/003 , C10G31/09 , C10G35/06 , C10G45/00 , C10G45/04 , C10G45/34 , C10G45/44 , C10G45/46 , C10G45/52 , C10G45/60 , C10G45/64 , C10G47/02 , C10G50/00 , C10K1/32 , C10L3/101 , C10L2290/542 , C10M101/02 , C23C16/56 , Y02C10/08 , Y02P20/152 , C07C9/04 , C08F210/02 , C08F4/64089 , C08F210/14 , C08F4/64048 , C08F4/64013 , C08F4/64189 , C08F4/64148 , C08F4/64193 , C08F4/027 , C08F4/64158
摘要： Methods for coating a substrate with a coating including an adsorbent material and a binder comprising an organosilica material which is a polymer comprising independent units of Formula [Z3Z4SiCH2]3 (I), wherein each Z3 represents a hydroxyl group, a C1-C4 alkoxy group or an oxygen atom bonded to a silicon atom of another unit or an active site on the substrate and each Z4 represents a hydroxyl group, a C1-C4 alkoxy group, a C1-C4 alkyl group, an oxygen atom bonded to a silicon atom of another unit or an active site on the substrate are provided. Methods of gas separation are also provided.
摘要翻译：用包含吸附剂材料和粘合剂的涂层涂覆基材的方法包括有机硅材料，其为包含式[Z 3 Z 4 SiCH 2] 3（I）的独立单元的聚合物，其中每个Z 3表示羟基，C 1 -C 4烷氧基或与基板上的另一单元或活性部位的硅原子键合的氧原子，各Z4表示羟基，C1-C4烷氧基，C1-C4烷基，与硅原子键合的氧原子提供了衬底上的另一单元或活性位点。还提供了气体分离方法。

78. 发明申请

US20160166983A1 PROCESS FOR CAPTURING A HEAVY METAL CONTAINED IN A MOIST GAS, INTEGRATING A HEAT PUMP TO HEAT THE GAS INTRODUCED INTO A CAPTURE MASS 有权
标题翻译：用于捕获在气体气体中包含的重金属的方法，整合热泵以将气体引入捕获质量
公开(公告)号：US20160166983A1
公开(公告)日：2016-06-16
申请号：US14908003
申请日：2014-06-17
申请人： IFP ENERGIES NOUVELLES
发明人： Florent GUILLOU , Fabien PORCHERON , Karin BARTHELET , Arnaud BAUDOT , Yann LEPINE , Clotilde JUBIN
IPC分类号： B01D53/64 , B01D53/34 , C10L3/10 , B01D53/00
CPC分类号： B01D53/64 , B01D53/005 , B01D53/343 , B01D2251/60 , B01D2251/602 , B01D2253/1124 , B01D2253/1128 , B01D2256/24 , B01D2257/60 , B01D2257/602 , B01D2259/655 , B01J20/06 , B01J20/3028 , B01J20/3204 , B01J20/3236 , C10L3/101 , C10L3/102 , C10L3/103 , C10L3/104 , C10L3/106 , C10L2290/06 , C10L2290/46 , C10L2290/48 , C10L2290/542
摘要： Capturing at least one heavy metal, from mercury and arsenic, contained in a moist gas comprising water vapour, by the following steps: a) heating the moist gas by heat exchange with a compressed heat transfer fluid obtained in step e) in order to obtain a condensed heat transfer fluid and a gas reheated to a temperature Tc; b) bringing the reheated gas into contact with a heavy metal capture mass in order to obtain a gas depleted in heavy metal; c) decompressing the cooled heat transfer fluid; d) cooling the gas depleted in heavy metal by heat exchange with the heat transfer fluid produced in step c) in order to obtain a cooled gas at a temperature Tf, the heat transfer fluid being vaporized; e) compressing the vaporized heat transfer fluid in a manner such as to obtain a compressed heat transfer fluid, the compressed heat transfer fluid being recycled.
摘要翻译：通过以下步骤捕获包含在包含水蒸气的潮湿气体中的至少一种重金属（来自汞和砷）：a）通过与在步骤e）中获得的压缩传热流体进行热交换来加热湿气体，以获得冷凝的传热流体和再加热到温度Tc的气体; b）使重新加热的气体与重金属捕集物体接触，以获得贫重的重金属的气体; c）减压冷却的传热流体; d）通过与步骤c）中产生的传热流体进行热交换来冷却贫金属的气体，以获得在Tf温度下的冷却气体，所述传热流体被蒸发; e）以这样的方式压缩蒸发的传热流体，以获得压缩的传热流体，所述压缩的传热流体被再循环。

79. 发明申请

US20160158770A1 GAS DISTRIBUTOR AND METHOD OF USE THEREOF 审中-公开
标题翻译：气体分配器及其使用方法
公开(公告)号：US20160158770A1
公开(公告)日：2016-06-09
申请号：US14560257
申请日：2014-12-04
申请人： Weldon Lee Ransbarger , Lee David Rhyne
发明人： Weldon Lee Ransbarger , Lee David Rhyne
IPC分类号： B05B1/00 , B01D53/04 , C10L3/10
CPC分类号： B05B1/005 , B01D53/04 , B01D53/0446 , B01D53/261 , B01D2253/108 , B01D2257/602 , C10L3/101 , C10L3/106 , C10L2290/542
摘要： A gas flow directing device to provide uniform gas flow into or out of a vessel having molecular sieve material contained therein and methods for treating a gas streams in the vessel using the gas flow directing device are described. The gas flow directing device includes a truncated cone having a cone base having an opening centered therein and a truncated top. The truncated cone further includes a gas permeable wall portion between the cone base and the truncated top having open sides to provide fluid communication between the opening in the cone base and space surrounding the gas permeable wall portion.
摘要翻译：描述了一种气流引导装置，用于提供均匀的气体流入或流出其中包含分子筛材料的容器，以及使用气体流动引导装置处理容器中的气流的方法。气体流动引导装置包括具有锥形基部的截头圆锥体，其具有以其为中心的开口和截顶。截锥体还包括在锥形基部和截顶部之间的透气壁部分，其具有开放侧面，以在锥形基部中的开口和围绕气体可透过壁部分的空间之间提供流体连通。

80. 发明申请

US20160145516A1 Process for Producing Biodiesel and Related Products 审中-公开
标题翻译：生物柴油及相关产品生产工艺
公开(公告)号：US20160145516A1
公开(公告)日：2016-05-26
申请号：US14897936
申请日：2014-06-19
申请人： Argent Energy Group Limited
发明人： Michael Scott
IPC分类号： C10L1/02 , C11C3/00 , C11B3/12 , C11B3/00 , C11C3/10 , C11B3/04
CPC分类号： C10L1/026 , B01D21/262 , B03D1/1431 , C07C67/03 , C07C67/08 , C07C67/58 , C10G3/00 , C10G3/40 , C10G33/00 , C10G2300/1003 , C10G2300/201 , C10G2400/04 , C10L2200/0446 , C10L2200/0476 , C10L2270/026 , C10L2270/04 , C10L2290/06 , C10L2290/18 , C10L2290/542 , C10L2290/543 , C10L2290/544 , C10L2290/547 , C11B3/001 , C11B3/006 , C11B3/008 , C11B3/04 , C11B3/12 , C11B3/16 , C11C3/003 , C11C3/10 , Y02E50/13 , Y02P30/20 , C07C69/24 , C07C69/52
摘要： There is described a process for producing biodiesel and related products from mixtures. There is also described a process for producing precursors and feedstock materials for producing biodiesel and related products. The processes use esterification and trans-esterification, separation and purification. Other process steps such as acidification and distillation can also be used.
摘要翻译：描述了从混合物生产生物柴油和相关产品的方法。还描述了生产生物柴油和相关产品的前体和原料的生产方法。该方法使用酯化和酯交换，分离和纯化。也可以使用其它的工艺步骤，例如酸化和蒸馏。

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