公开(公告)号：US09090522B2

公开(公告)日：2015-07-28

申请号：US13819021

申请日：2011-08-26

申请人： Jong Ho Park ,  Jong Nam Kim ,  Hee Tae Beum ,  Seong Jun Lee ,  Jang Jae Lee ,  Dong Wook Kim ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon Haeng Cho

发明人： Jong Ho Park ,  Jong Nam Kim ,  Hee Tae Beum ,  Seong Jun Lee ,  Jang Jae Lee ,  Dong Wook Kim ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon Haeng Cho

IPC分类号： C07C7/12 ,  B01D53/047 ,  C07C7/13 ,  C10G70/04

CPC分类号： C07C7/12 ,  B01D53/047 ,  B01D2253/108 ,  B01D2256/24 ,  B01D2257/7022 ,  B01D2259/40073 ,  B01D2259/4063 ,  C07C7/13 ,  C10G70/046 ,  C10G2300/107 ,  C10G2300/4081 ,  C10G2400/20 ,  Y02C20/20 ,  Y02P30/464 ,  C07C11/04

摘要： A method and apparatus for concentrating and recovering ethylene from the off-gas from an apparatus which produces gasoline, propylene and the like by fluidized catalytic cracking (FCC) of heavy oils such as atmospheric residue, generated in a crude oil refining process, is provided. The method and apparatus can reduce the amount of ethylene rinse in the subsequent ethylene displacement desorption process by increasing the ethylene purity of a raw material gas and reducing the concentration of weakly adsorbing components in the raw material gas and can reduce the loss of a desorbent during a distillation process for separating the desorbent from the weakly adsorbing components. Thus, ethylene can be recovered from the off-gas from fluidized catalytic cracking of heavy oils at high concentration and low cost.

摘要翻译： 提供了一种从废气中浓缩和回收乙烯的方法和装置，该装置通过在原油精炼过程中产生的重质油如大气残留物的流化催化裂化（FCC）产生汽油，丙烯等 。 该方法和装置可以通过提高原料气体的乙烯纯度和降低原料气体中弱吸附组分的浓度来减少后续乙烯取代脱附过程中的乙烯冲洗量，并可以减少脱附剂在 用于将解吸剂与弱吸附组分分离的蒸馏方法。 因此，可以从废气中以高浓度和低成本从重油的流化催化裂化中回收乙烯。

公开(公告)号：US20140148634A1

公开(公告)日：2014-05-29

申请号：US13819021

申请日：2011-08-26

申请人： Jong Ho Park ,  Jong Nam Kim ,  Hee Tae Beum ,  Seong Jun Lee ,  Jang Jae Lee ,  Dong Wook Kim ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon Haeng Cho

发明人： Jong Ho Park ,  Jong Nam Kim ,  Hee Tae Beum ,  Seong Jun Lee ,  Jang Jae Lee ,  Dong Wook Kim ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon Haeng Cho

IPC分类号： C07C7/12

CPC分类号： C07C7/12 ,  B01D53/047 ,  B01D2253/108 ,  B01D2256/24 ,  B01D2257/7022 ,  B01D2259/40073 ,  B01D2259/4063 ,  C07C7/13 ,  C10G70/046 ,  C10G2300/107 ,  C10G2300/4081 ,  C10G2400/20 ,  Y02C20/20 ,  Y02P30/464 ,  C07C11/04

摘要： A method and apparatus for concentrating and recovering ethylene from the off-gas from an apparatus which produces gasoline, propylene and the like by fluidized catalytic cracking (FCC) of heavy oils such as atmospheric residue, generated in a crude oil refining process, is provided. The method and apparatus can reduce the amount of ethylene rinse in the subsequent ethylene displacement desorption process by increasing the ethylene purity of a raw material gas and reducing the concentration of weakly adsorbing components in the raw material gas and can reduce the loss of a desorbent during a distillation process for separating the desorbent from the weakly adsorbing components. Thus, ethylene can be recovered from the off-gas from fluidized catalytic cracking of heavy oils at high concentration and low cost.

摘要翻译： 提供了一种从废气中浓缩和回收乙烯的方法和装置，该装置通过在原油精炼过程中产生的重质油如大气残留物的流化催化裂化（FCC）产生汽油，丙烯等 。 该方法和装置可以通过提高原料气体的乙烯纯度和降低原料气体中弱吸附组分的浓度来减少后续乙烯取代脱附过程中的乙烯冲洗量，并可以减少脱附剂在 用于将解吸剂与弱吸附组分分离的蒸馏方法。 因此，可以从废气中以高浓度和低成本从重油的流化催化裂化中回收乙烯。

公开(公告)号：US08377205B2

公开(公告)日：2013-02-19

申请号：US12605838

申请日：2009-10-26

申请人： Bo-Yun Jang ,  Chang-Hyun Ko ,  Jeong-Chul Lee ,  Joon-Soo Kim ,  Joo-Seok Park

发明人： Bo-Yun Jang ,  Chang-Hyun Ko ,  Jeong-Chul Lee ,  Joon-Soo Kim ,  Joo-Seok Park

IPC分类号： C30B21/04

CPC分类号： B01J19/088 ,  B01J2219/0883 ,  B01J2219/0894 ,  B82Y30/00 ,  B82Y40/00 ,  C01B33/027 ,  H05H1/46 ,  H05H2001/4667 ,  Y10T117/10 ,  Y10T117/1008 ,  Y10T428/2982

摘要： The present disclosure relates to an apparatus for producing silicon nanocrystals, which can minimize plasma diffusion by finely adjusting a plasma region created by an ICP coil. The apparatus includes a reactor having an ICP coil wound around an outer wall thereof and a tube inserted into the reactor, wherein a primary gas for forming silicon nanocrystals and a secondary gas for surface reaction of the silicon nanocrystals are separately supplied to the reactor through an inner side and an outer side of the tube, respectively.

摘要翻译： 本公开涉及一种用于制造硅纳米晶体的装置，其可以通过精细调节由ICP线圈产生的等离子体区域来最小化等离子体扩散。 该装置包括具有绕其外壁缠绕有ICP线圈的反应器和插入反应器中的管，其中用于形成硅纳米晶体的初级气体和用于硅纳米晶体的表面反应的二次气体通过 内侧和外侧。

公开(公告)号：US07007933B2

公开(公告)日：2006-03-07

申请号：US10431981

申请日：2003-05-08

申请人： Jai-Dong Lee ,  Ki-Hyun Hwang ,  Chang-Hyun Ko

发明人： Jai-Dong Lee ,  Ki-Hyun Hwang ,  Chang-Hyun Ko

IPC分类号： B01F3/04

CPC分类号： C23C16/4482 ,  Y10S261/65

摘要： A method for supplying a source gas to a processing chamber for forming a film on a substrate in the processing chamber includes: heating a carrier gas; bubbling the heated carrier gas in a liquid source disposed in a container to form a vapor source; and supplying a source gas including the vapor source and the heated carrier gas into the processing chamber for forming the film.

摘要翻译： 将源气体供给到处理室中的基板上形成膜的处理室的方法包括：对载气进行加热; 将加热的载气鼓泡在设置在容器中的液体源中以形成蒸气源; 以及将包括蒸气源和被加热的载气的源气体供应到用于形成膜的处理室中。

公开(公告)号：US20050032372A1

公开(公告)日：2005-02-10

申请号：US10814553

申请日：2004-03-31

申请人： Chang-Hyun Ko ,  Ki-Hyun Hwang ,  Hyo-Jung Kim

发明人： Chang-Hyun Ko ,  Ki-Hyun Hwang ,  Hyo-Jung Kim

IPC分类号： H01L21/20 ,  B05D5/00 ,  C23C16/40 ,  H01L21/302 ,  H01L21/314 ,  H01L21/461

CPC分类号： H01L21/02299 ,  C23C16/403 ,  C23C16/405 ,  C23C16/45525 ,  C23C16/45536 ,  H01L21/022 ,  H01L21/0228 ,  H01L21/3141 ,  H01L21/3142

摘要： Methods for forming a thin film on an integrated circuit device including providing energy to reactants in a deposition chamber to activate the reactants. The activated reactants are then deposited on the substrate to form a thin film on the substrate. The reactants selected may be selectively activated so that different thin films are formed in a single chamber thereby reducing processing time.

摘要翻译： 在集成电路装置上形成薄膜的方法，包括向沉积室中的反应物提供能量以激活反应物。 然后将活化的反应物沉积在基底上以在基底上形成薄膜。 选择的反应物可以被选择性地激活，使得在单个室中形成不同的薄膜，从而减少处理时间。

公开(公告)号：US09376354B2

公开(公告)日：2016-06-28

申请号：US13819007

申请日：2011-08-26

申请人： Jong Nam Kim ,  Jong Ho Park ,  Hee Tae Beum ,  Seong Jun Lee ,  Jang Jae Lee ,  Dong Wook Kim ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon Haeng Cho

发明人： Jong Nam Kim ,  Jong Ho Park ,  Hee Tae Beum ,  Seong Jun Lee ,  Jang Jae Lee ,  Dong Wook Kim ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon Haeng Cho

IPC分类号： B01D53/04 ,  C07C7/04 ,  C07C7/13 ,  C07C7/00

CPC分类号： C07C7/005 ,  B01D53/04 ,  B01D2253/108 ,  B01D2256/24 ,  B01D2257/7022 ,  B01D2259/40086 ,  B01D2259/404 ,  C07C7/04 ,  C07C7/13 ,  Y02P30/464 ,  C07C11/02 ,  C07C11/04 ,  C07C11/06

摘要： A process and apparatus for separating an olefin from mixed gases containing light olefins is provided. The process includes adsorbing the olefin of an olefin-containing mixed gas in an adsorption column packed with an adsorbent selectively adsorbing the olefin; discharging gases other than the olefin through the outlet of the adsorption column; desorbing the adsorbed olefin by displacement using a desorbent, and separating the olefin from the desorbent, thereby producing a high-purity olefin. The apparatus includes adsorption columns packed with an adsorbent selectively adsorbing an olefin, and at least two distillation columns for separating an olefin/desorbent mixture and an olefin poor stream/desorbent into their components. If the olefin concentration of the off-gas from an olefin rinse step is higher than that of a raw material gas, recovering the olefin from the off-gas is carried out before or after the adsorption step.

摘要翻译： 提供了一种用于从含有轻质烯烃的混合气体中分离烯烃的方法和装置。 该方法包括在填充有选择性吸附烯烃的吸附剂的吸附塔中吸附含烯烃混合气体的烯烃; 通过吸附塔的出口排出除烯烃以外的气体; 使用解吸剂通过置换解吸吸附的烯烃，并从解吸剂中分离烯烃，从而产生高纯度烯烃。 该装置包括填充有选择性吸附烯烃的吸附剂的吸附塔和用于将烯烃/脱附剂混合物和烯烃不良物流/解吸剂分离成其组分的至少两个蒸馏塔。 如果来自烯烃漂洗步骤的废气的烯烃浓度高于原料气体的烯烃浓度，则在吸附步骤之前或之后进行从废气中回收烯烃。

公开(公告)号：US08431762B2

公开(公告)日：2013-04-30

申请号：US12593252

申请日：2008-04-11

申请人： Jong-Ho Park ,  Jong-Nam Kim ,  Seong-Jun Lee ,  Min-Su Ko ,  Hee Tae Beum ,  Jongkee Park ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon-Haeng Cho

发明人： Jong-Ho Park ,  Jong-Nam Kim ,  Seong-Jun Lee ,  Min-Su Ko ,  Hee Tae Beum ,  Jongkee Park ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon-Haeng Cho

IPC分类号： C07C7/12

CPC分类号： C07C7/12 ,  B01D3/143 ,  B01D53/04 ,  B01D2253/108 ,  B01D2256/24 ,  B01D2257/7022 ,  B01D2259/40086 ,  B01D2259/403 ,  C07C7/005 ,  C07C7/04 ,  C07C7/13 ,  C07C11/08

摘要： The present invention relates to a hybrid process comprising an adsorption process and a distillation process for the separation of butene-1 from a C4 hydrocarbon mixture gas including butene-1, trans-2-butene, cis-2-butene, normal butane, isobutane, etc. The above hybrid process comprises introducing a gaseous C4 mixture into the adsorption tower loaded with adsorbents which adsorb olefins selectively to discharge C4 paraffins to the outlet of the tower, desorbing C4 olefins selectively adsorbed in the adsorption tower to produce high purity C4 olefins mixture gas in which isobutane and normal butane was removed, and separating the high C4 olefins mixture gas (a mixture of butene-1, trans-2-butene, cis-2-butene, and a trace amount of C4 paraffins) via distillation to obtain high purity butene-1 including a trace amount of isobutane in the top of the distillation tower and obtain a mixture gas including trans-2-butene, cis-2-butene and a trace amount of normal butane in the bottom of the tower.

摘要翻译： 本发明涉及一种混合方法，其包括吸附过程和用于从包含丁烯-1，反式-2-丁烯，顺式-2-丁烯，正丁烷，异丁烷的C 4烃混合气体中分离丁烯-1的蒸馏方法 等等。上述混合方法包括将气态C 4混合物引入到负载有吸附剂的吸附塔中，所述吸附剂选择性吸附烯烃以将C4链烷烃排出到塔的出口，解吸选择性吸附在吸附塔中的C4烯烃以产生高纯度C4烯烃 除去异丁烷和正丁烷的混合气体，通过蒸馏将高C4烯烃混合气体（丁烯-1，反式-2-丁烯，顺式-2-丁烯和痕量的C4链烷烃的混合物）分离成 在蒸馏塔顶部得到含有痕量异丁烷的高纯度丁烯-1，得到底部的反式-2-丁烯，顺式-2-丁烯和痕量正丁烷的混合气体 他塔。

公开(公告)号：US20120253091A1

公开(公告)日：2012-10-04

申请号：US13510403

申请日：2010-11-17

申请人： Chang-Hyun Ko ,  Jeong-Geol Na ,  Jong-Nam Kim ,  Kwang-Bok Yi ,  Sung-Youl Park ,  Jong-Ho Park ,  Hee-Tae Beum ,  Bo-Eun Yi

发明人： Chang-Hyun Ko ,  Jeong-Geol Na ,  Jong-Nam Kim ,  Kwang-Bok Yi ,  Sung-Youl Park ,  Jong-Ho Park ,  Hee-Tae Beum ,  Bo-Eun Yi

IPC分类号： C07C1/207

CPC分类号： B01J23/007 ,  B01J21/04 ,  B01J23/02 ,  B01J27/236 ,  C10G3/44 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2400/02 ,  C10G2400/04 ,  Y02E50/13 ,  Y02P30/20

摘要： The present invention relates to a method in which a catalytic reaction is used in order to produce hydrocarbons from renewable starting material derived from biological organisms such as vegetable lipids, animal lipids, and lipids extracted from macroalgae and microalgae, and more specifically relates to a method for selectively making a hydrocarbon, which is suitable for making gasoline or diesel, by removing the oxygen contained in the starting material without consuming hydrogen. In the present invention, the production takes place by bringing the starting material into contact with hydrotalcite, which constitutes a catalyst, thereby removing oxygen via a decarboxylation or decarbonylation reaction; and the starting material is one or more such material selected from triglycerides, fatty acids, and fatty acid derivatives obtained from a renewable source of supply originating from a biological organism.

摘要翻译： 本发明涉及一种方法，其中使用催化反应以从源自生物有机体（例如植物脂质，动物脂质和从大型藻类和微藻中提取的脂质）的可再生原料生产烃，更具体地涉及一种方法 用于通过除去原料中所含的氧而不消耗氢气来选择性制备适合于制备汽油或柴油的烃。 在本发明中，通过使起始材料与构成催化剂的水滑石接触而进行生产，从而通过脱羧或脱羰反应除去氧气; 并且起始材料是一种或多种这样的材料，其选自甘油三酸酯，脂肪酸和从源自生物体的可再生来源获得的脂肪酸衍生物。

公开(公告)号：US20120110902A1

公开(公告)日：2012-05-10

申请号：US13384230

申请日：2009-11-18

申请人： Kwang Bok Yi ,  Jong Nam Kim ,  Si Hyun Lee ,  Chang Hyun Ko ,  Hee Tae Beum ,  In Baek Kim

发明人： Kwang Bok Yi ,  Jong Nam Kim ,  Si Hyun Lee ,  Chang Hyun Ko ,  Hee Tae Beum ,  In Baek Kim

IPC分类号： C10L5/00 ,  C07D207/46 ,  C01F5/14 ,  C09K3/00 ,  C01B31/08 ,  C07C7/12 ,  C01F5/02

CPC分类号： B01D53/52 ,  B01D2251/402 ,  B01D2251/404 ,  B01D2253/102 ,  B01D2253/104 ,  B01J20/0225 ,  B01J20/041 ,  B01J20/08 ,  B01J20/3078 ,  B01J20/3204 ,  B01J20/3236 ,  C10G1/04 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2300/44

摘要： A sulfur compound adsorbent for solvent extraction of coal and methods using the same to adsorb sulfur compounds and refine coal are provided. The adsorbent for solvent extraction of coal serves to remove sulfur compounds from an organic solvent containing a coal's combustible component resulting from solvent extraction of low-grade coal and is composed of any one or a mixture of two or more selected from among alkali earth metal oxide, alkali earth metal hydroxide, aluminum oxide and activated carbon.

摘要翻译： 提供了一种用于溶剂萃取煤的硫化合物吸附剂及其使用的硫化合物和精炼煤的方法。 用于溶剂萃取的吸附剂用于从含有煤的可燃组分的有机溶剂中除去硫化合物，其由低等级煤的溶剂萃取产生，并且由选自碱土金属氧化物中的任何一种或两种或更多种的混合物组成 ，碱土金属氢氧化物，氧化铝和活性炭。

公开(公告)号：US20100048971A1

公开(公告)日：2010-02-25

申请号：US12593249

申请日：2008-03-28

申请人： Jong-Nam Kim ,  Jong-Ho Park ,  Seong-Jun Lee ,  Min-Su Ko ,  Hee Tae Beum ,  Jongkee Park ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon-Haeng Cho

发明人： Jong-Nam Kim ,  Jong-Ho Park ,  Seong-Jun Lee ,  Min-Su Ko ,  Hee Tae Beum ,  Jongkee Park ,  Chang Hyun Ko ,  Sang Sup Han ,  Soon-Haeng Cho

IPC分类号： C07C7/04 ,  C07C7/11

CPC分类号： B01D53/047 ,  B01D2256/24 ,  B01D2257/7022 ,  B01D2259/40054 ,  B01D2259/4006 ,  B01D2259/40062 ,  B01D2259/40067 ,  B01D2259/403 ,  C07C7/13 ,  C07C11/08

摘要： The present invention relates to a method and an apparatus for the separation of C4 olefins (butene-1, trans-2-butene, cis-2-butene, etc.) and C4 paraffins (normal butane, isobutane, etc.) from a C4 hydrocarbon mixed gas including butene-1, trans-2-butene, cis-2-butene, normal butane, isobutane, etc. The method of the present invention produces C4 olefins with high purity by introducing a gaseous C4 mixture into the adsorption tower loaded with adsorbent selectively adsorbing olefins to adsorb C4 olefins and to discharge C4 paraffins to the outlet of the tower, desorbing C4 olefins adsorbed on the adsorption tower with a desorbent (C5 hydrocarbon, C6 hydrocarbon, etc.), and then separating the C4 olefin and the desorbent by a distillation process. The apparatus of the present invention is composed of several adsorption towers loaded with an adsorbent which selectively adsorb olefins and two distillation towers for the separation of the mixture gases of olefins/desorbents and paraffins/desorbents respectively, The basic operating process of the adsorption tower comprises a adsorption step of selectively adsorbing C4 olefin from the feeding mixture, a C4 olefin rinse step of removing a small amount of C4 paraffins adsorbed together with C4 olefins, and a desorption step of desorbing C4 olefins by using a desorbent, and further comprises a pressure equalization step, a cocurrent depressurization step, and a accumulation pressure step in order to increase the yield and concentration of olefins depending on the operation pressure of the adsorption tower. The desorbent discharged from the process together with olefins or paraffins is separated in the distillation tower and then recycled.

摘要翻译： 本发明涉及一种用于分离C4烯烃（丁烯-1，反式-2-丁烯，顺-2-丁烯等）和C4链烷烃（正丁烷，异丁烷等）的方法和装置， 包括丁烯-1，反式-2-丁烯，顺式-2-丁烯，正丁烷，异丁烷等的C4烃混合气体。本发明的方法通过将气态C 4混合物引入吸附塔中来生产高纯度的C4烯烃 负载吸附剂选择性吸附烯烃以吸附C4烯烃并将C4链烷烃排出到塔的出口，用解吸剂（C5烃，C6烃等）解吸吸附在吸附塔上的C4烯烃，然后分离C4烯烃 和通过蒸馏方法的解吸剂。 本发明的装置由多个吸附塔组成，吸附塔分别选择性地吸附烯烃和两个蒸馏塔，用于分离烯烃/脱附剂和石蜡/脱附剂的混合气体。吸附塔的基本操作过程包括 从进料混合物中选择性吸附C4烯烃的吸附步骤，除去少量与C4烯烃一起吸附的C4链烷烃的C4烯烃漂洗步骤，以及通过使用脱附剂解吸C4烯烃的解吸步骤，还包括压力 平衡步骤，并流减压步骤和累积压力步骤，以根据吸附塔的操作压力提高烯烃的产率和浓度。 从该方法中排出的解吸剂与烯烃或链烷烃一起在蒸馏塔中分离，然后再循环。