专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US10030223B2 Apparatus and method for simultaneous operation of refining cellulosic biomass and mixing enzymes 有权
公开(公告)号：US10030223B2
公开(公告)日：2018-07-24
申请号：US14683053
申请日：2015-04-09
申请人： SK Innovation Co., LTD. , SK Energy Co., LTD.
发明人： Taewan Kim , Bonwook Koo , Minsu Koo
IPC分类号： C12M1/00 , C12M1/33 , C12P19/14 , C12P19/02 , D21D1/30 , C12P7/10
摘要： An apparatus comprises: a hopper for feeding biomass; a horizontal extruder comprising a cylindrical housing and a rotatable screw mounted in the housing, in which one side of the housing is connected to the hopper, and an outlet provided at the other side of the housing is connected to an inlet for feeding biomass into a refiner; and a refiner comprising a stator disc having a cooling water space formed on the outer peripheral surface thereof, one or more enzyme feeding holes provided in a refining region adjacent to the circumference of the stator disc, and a biomass inlet provided at the central portion thereof, and a refining disc which is disposed so as to form a gap with the inner surface of the stator disc and to have a refining region opposite to that of the stator disc and is rotated by a separate motor.

2. 发明授权

US09663738B2 Pneumatic conveying dryer for carbon fuel 有权
公开(公告)号：US09663738B2
公开(公告)日：2017-05-30
申请号：US14655628
申请日：2013-12-26
申请人： SK Innovation Co., Ltd. , SK Energy Co., Ltd.
发明人： Min Hoe Yi , Gyoo Tae Kim , Ju Hoe Kim , Jin Hwan Bang , Sung Kwang Lim , Ho Jun Song , Jae Wook Shin
IPC分类号： C10L9/00 , F26B17/10 , F23G5/04 , F23K1/00 , F23G5/027 , F15B1/00 , F16L57/06 , B65G53/42
CPC分类号： C10L9/00 , B65G53/42 , C10J2300/0909 , C10J2300/1653 , C10L2230/22 , C10L2290/06 , C10L2290/08 , C10L2290/143 , C10L2290/54 , C10L2290/56 , F15B1/00 , F16L57/06 , F23G5/027 , F23G5/04 , F23G2209/262 , F23K1/00 , F23K2201/30 , F23K2203/101 , F26B17/105 , Y02E20/18
摘要： Provided is a carbon fuel pneumatic dryer in which synthesis gas generated in a reactor is fed and cooled, including: a feeding part formed as a narrow pipe, via which synthesis gas and carbon fuel are fed; a drying part formed as a pipe having a larger diameter than the feeding part, in which the hot synthesis gas fed via the feeding part is cooled and the moisture content of the carbon fuel is lowered; and a conveying part formed as a pipe having a smaller diameter than the drying part such that the flow velocity of the synthesis gas and the carbon fuel having passed the drying part is increased, wherein the conveying part includes a bend so that the flow direction of the synthesis gas and the carbon fuel is changed.

3. 发明授权

US09556392B2 Gasification combined facility for carbon fuel including pneumatic conveying dryer 有权
标题翻译：包括气动输送干燥机在内的碳燃料气化联合设备
公开(公告)号：US09556392B2
公开(公告)日：2017-01-31
申请号：US14654883
申请日：2013-12-24
申请人： SK INNOVATION CO., LTD. , SK ENERGY CO., LTD.
发明人： Min Hoe Yi , In Kwon Bae , Gyoo Tae Kim , Jae Wook Shin
IPC分类号： C10J3/72 , C10K3/04 , C01B3/12 , F26B23/00 , C10J3/00
CPC分类号： C10J3/72 , C01B3/12 , C10J3/00 , C10J2200/09 , C10J2300/0909 , C10J2300/0916 , C10J2300/093 , C10J2300/0943 , C10J2300/1884 , C10K3/04 , F26B23/001 , Y02P20/145 , Y02P70/405
摘要： This invention relates to an integrated gasification apparatus for carbonaceous fuel, wherein high-pressure steam produced during a gasification process of carbonaceous fuel is directly used to dry the carbonaceous fuel, and steam obtained through the drying process is directly used in a water gas shift process.
摘要翻译：本发明涉及碳质燃料的一体化气化装置，其中直接用于碳质燃料的气化过程中产生的高压蒸汽干燥碳质燃料，通过干燥过程获得的蒸汽直接用于水煤气变换过程。

4. 发明授权

US09499753B2 Gasification process and system using dryer integrated with water-gas shift catalyst 有权
标题翻译：气化过程和系统使用与水煤气变换催化剂集成的干燥机
公开(公告)号：US09499753B2
公开(公告)日：2016-11-22
申请号：US14650997
申请日：2013-12-11
申请人： SK INNOVATION CO., LTD. , SK ENERGY CO., LTD.
发明人： Jong Sung Park , Ji Sung Park , Cheon Seong Lee , Gyoo Tae Kim , Jae Wook Shin , Yong Jeon Kim
IPC分类号： C01B3/38 , C10J3/06 , C01B3/16 , C10J3/12 , C10K3/04 , C10J3/20
CPC分类号： C10J3/06 , C01B3/16 , C01B2203/0288 , C01B2203/1023 , C01B2203/1047 , C01B2203/1076 , C10J3/12 , C10J3/20 , C10J2200/09 , C10J2300/0909 , C10J2300/0959 , C10J2300/0969 , C10J2300/1823 , C10K3/04 , Y02E20/18
摘要： The present invention relates to a gasification process and system, wherein a dryer integrated with a water-gas-shift catalyst is disposed in front of a gasifier.
摘要翻译：本发明涉及一种气化方法和系统，其中与气 - 气 - 变换催化剂结合的干燥器设置在气化器前面。

5. 发明授权

US09127215B2 Method for reducing the amount of organic acids in a hydrocarbon oil fraction 有权
$Method for reducing the amount of organic acids in a hydrocarbon oil fraction$
标题翻译：减少烃油馏分中有机酸含量的方法
公开(公告)号：US09127215B2
公开(公告)日：2015-09-08
申请号：US13979044
申请日：2012-01-04
申请人： Jin Kyu Choi , Cheol Woo Park , Tae Won Uhm , Il Yong Jeong , Ha Na Song , Do Woan Kim , Hee Jung Jeon , Gyung Rok Kim , Cheol Joong Kim , Do Hyoun Kim , Chang Woo Joo
发明人： Jin Kyu Choi , Cheol Woo Park , Tae Won Uhm , Il Yong Jeong , Ha Na Song , Do Woan Kim , Hee Jung Jeon , Gyung Rok Kim , Cheol Joong Kim , Do Hyoun Kim , Chang Woo Joo
IPC分类号： C10G45/02 , C10G45/22 , B01J23/883 , C10G3/00 , C10G67/02 , C10L1/02 , C10L1/04
CPC分类号： C10G45/22 , B01J23/883 , C10G3/42 , C10G3/50 , C10G45/02 , C10G67/02 , C10G2300/202 , C10G2300/203 , C10G2300/4075 , C10L1/02 , C10L1/04 , Y02P30/20
摘要： Provided is a method for reducing the amount of organic acids in a hydrocarbon oil fraction by hydrogenating the organic acids in the hydrocarbon oil fraction under mild conditions. Provided is a new method able to overcome the problem of organic-acid-induced corrosion during the process of distillation, by using hydrogen or a hydrogen-containing mixed gas and a hydrogenation catalyst to subject the organic acids in the hydrocarbon oil fraction to hydrogenation at an appropriate temperature and pressure, thereby converting the same to hydrocarbons and so reducing the amount of organic acids in the hydrocarbon oil fraction.
摘要翻译：提供一种通过在温和条件下氢化烃油馏分中的有机酸来减少烃油馏分中的有机酸的量的方法。提供了一种能够克服在蒸馏过程中有机酸诱导的腐蚀问题的新方法，通过使用氢气或含氢混合气体和氢化催化剂使烃油馏分中的有机酸在适当的温度和压力，从而将其转化为烃，从而减少烃油馏分中的有机酸的量。

6. 发明授权

US09029624B2 Treatment method for spent caustic soda 有权
标题翻译：用过的苛性钠的处理方法
公开(公告)号：US09029624B2
公开(公告)日：2015-05-12
申请号：US14129375
申请日：2012-06-26
申请人： Bang Un Song , Sung Ho Lee , Young Seek Yoon , Seung Hoon Oh
发明人： Bang Un Song , Sung Ho Lee , Young Seek Yoon , Seung Hoon Oh
IPC分类号： A62D3/38 , C01D1/36
CPC分类号： C01D1/36
摘要： An embodiment of the present invention relates to a method for treating spent caustic soda generated from an oil refinery process, a petrochemical process, etc. through a process in which a series of treatment steps are integrated, wherein the method can constitute a process under mild conditions excluding high temperature and/or high pressure conditions and can be advantageous to a post treatment process since the amount of by-products is small.
摘要翻译：本发明的一个实施方案涉及一种通过一系列处理步骤整合的方法来处理由炼油工艺，石化工艺等产生的废碱，其中该方法可以构成温和的过程条件不包括高温和/或高压条件，并且由于副产物的量少，因此可以有利于后处理过程。

7. 发明授权

US08980082B2 Method of simultaneously removing sulfur and mercury from hydrocarbon material using catalyst by means of hydrotreating reaction 有权
标题翻译：通过加氢处理反应，使用催化剂同时从烃类材料中除去硫和汞的方法
公开(公告)号：US08980082B2
公开(公告)日：2015-03-17
申请号：US13984412
申请日：2012-02-08
申请人： Do Kyoung Kim , Do Woan Kim , Sang Il Lee , Seung Hoon Oh , Woo Kyung Kim , Han Seung Pan , Woo Young Kim , Kyung Soo Jun , Sun Choi
发明人： Do Kyoung Kim , Do Woan Kim , Sang Il Lee , Seung Hoon Oh , Woo Kyung Kim , Han Seung Pan , Woo Young Kim , Kyung Soo Jun , Sun Choi
IPC分类号： C10G45/00 , C10G45/08 , B01J23/882 , B01J37/20 , C10L3/10 , C10G25/00 , C10G45/04 , B01J23/883 , C10G45/38 , C10G49/00 , C10G49/04 , C10G49/20 , C10G61/06 , B01J37/18 , B01J23/28 , B01J23/30 , B01J23/75 , B01J23/755 , B01J23/888 , B01J21/04 , B01J35/02 , B01J35/10
CPC分类号： C10G45/08 , B01J21/04 , B01J23/28 , B01J23/30 , B01J23/75 , B01J23/755 , B01J23/882 , B01J23/883 , B01J23/888 , B01J35/023 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J37/18 , B01J37/20 , C10G25/003 , C10G45/04 , C10G45/38 , C10G49/005 , C10G49/04 , C10G49/20 , C10G61/06 , C10G2300/1025 , C10G2300/1029 , C10G2300/104 , C10G2300/1044 , C10G2300/202 , C10G2300/205 , C10G2300/207 , C10G2300/4006 , C10L3/101 , C10L3/103
摘要： Disclosed herein is a method of simultaneously removing sulfur and mercury from a hydrocarbon material, including: hydrotreating the hydrocarbon material containing sulfur and mercury in the presence of a catalyst including a metal supported with a carrier to convert sulfur into hydrogen sulfide, and adsorb mercury on a metal active site or a carrier of the catalyst in the form of mercury sulfide.
摘要翻译：本文公开了一种同时从烃材料中除去硫和汞的方法，包括：在包含负载载体的金属的催化剂存在下加氢处理含硫和汞的烃材料，以将硫转化成硫化氢，并将汞吸附在金属活性部位或催化剂的载体，其形式为硫化汞。

8. 发明授权

US08657938B2 Air-supply system for breathing 有权
标题翻译：供气系统呼吸
公开(公告)号：US08657938B2
公开(公告)日：2014-02-25
申请号：US13056705
申请日：2009-07-27
申请人： Bum Su Kim , Hong Jun Kim
发明人： Bum Su Kim , Hong Jun Kim
IPC分类号： B01D46/46
CPC分类号： A62B15/00 , B01D46/0023
摘要： Disclosed is a system for supplying breathing air to a work space, which adopts a triple air-supply structure including a main air-supply unit for compressing, drying and filtering air supplied from the atmosphere so that breathing air is supplied to the work space, a plant air-supply unit for supplying industrial air used in a process plant to the work space, and an emergency air-supply unit for supplying breathing air to the work space in an emergency, wherein the operation of respective air-supply units is organically controlled, thus increasing the reliability of the air supply.
摘要翻译：公开了一种用于向工作空间供给呼吸空气的系统，该系统采用三重供气结构，其包括用于压缩，干燥和过滤从大气供应的空气的主供气单元，使得呼吸空气被供应到工作空间，用于向工作空间供应用于处理厂的工业空气的工厂供气单元，以及在紧急情况下向工作空间供应呼吸空气的紧急供气单元，其中各个供气单元的操作是有机地从而提高供气的可靠性。

9. 发明申请

US20130213793A1 SEPARATION OF OLEFINS FROM OLEFINS/PARAFFINS MIXED GAS 有权
标题翻译：来自烯烃/分散体混合气体的烯烃的分离
公开(公告)号：US20130213793A1
公开(公告)日：2013-08-22
申请号：US13855957
申请日：2013-04-03
申请人： KOREA INSTITUTE OF ENERGY RESEARCH , SK ENERGY CO., LTD.
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： C07C7/12
CPC分类号： C07C7/12 , C07C11/08
摘要： A method and 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. is provided. The apparatus includes 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 an 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 pressure equalization step, concurrent depressurization step, and accumulation pressure step to increase the yield and concentration of olefins depending on the operation pressure of the adsorption tower.
摘要翻译：用于从包括丁烯-1的C4烃混合气体中分离C4烯烃（丁烯-1，反式-2-丁烯，顺式-2-丁烯等）和C4链烷烃（正丁烷，异丁烷等）的方法和装置， 1，反式-2-丁烯，顺式-2-丁烯，正丁烷，异丁烷等。该装置包括装有吸附剂的几个吸附塔，该吸附剂选择性地吸附烯烃和两个用于分离烯烃/脱附剂和石蜡/脱附剂的混合气体的蒸馏塔。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，除去与C4烯烃一起吸附的少量C4链烷烃的C4烯烃漂洗步骤，以及通过以下步骤解吸C4烯烃的解吸步骤使用解吸剂，还包括压力平衡步骤，并行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。

10. 发明授权

US08431762B2 Production of high purity butene-1 from C4 olefins/paraffins mixed gas 有权
标题翻译：从C4烯烃/石蜡混合气体生产高纯度丁烯-1
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。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式