-
公开(公告)号：US20170141421A1
公开(公告)日：2017-05-18
申请号：US15339983
申请日：2016-11-01
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN , Franklin F. MITTRICKER , Loren STARCHER
IPC: H01M8/0662 , H01M8/04089 , H01M8/0612
CPC classification number: H01M8/0662 , B01D53/047 , B01D53/265 , B01D2256/16 , B01D2256/22 , B01D2259/40056 , B01D2259/403 , B01D2259/404 , C01B3/34 , H01M8/04097 , H01M8/0618 , H01M8/0668 , H01M2008/147 , Y02C10/08 , Y02E60/526 , Y02P20/152
Abstract: Systems and methods are provided for combined cycle power generation while reducing or mitigating emissions during power generation. Recycled exhaust gas from a molten carbonate fuel cell power generation reaction can be separated by using a swing adsorption process so as to generate a high purity CO2 stream while reducing or minimizing the energy required for the separation and without having to reduce the temperature of the exhaust gas. A high temperature adsorption reactor adsorbs the CO2 and recovers H2 from an exhaust gas of a first molten carbonate fuel cell at a high temperature and at a low pressure. The reactor passes along the adsorbed CO2 to a cathode and the recovered H2 to an anode of a second molten carbonate fuel cell for further power generation. This can allow for improved energy recovery while also generating high purity streams of CO2 and H2.
-
公开(公告)号：US20180036670A1
公开(公告)日：2018-02-08
申请号：US15653806
申请日：2017-07-19
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN
CPC classification number: B01D53/047 , B01D53/0407 , B01D53/62 , B01D2253/108 , B01D2253/112 , B01D2253/1124 , B01D2256/10 , B01D2256/16 , B01D2256/22 , B01D2257/102 , B01D2257/504 , B01D2259/40056 , B01D2259/4006 , B01D2259/402 , C01B3/56 , C01B21/0466 , C01B32/50 , C01B2203/042 , C01B2203/043 , C01B2203/0465 , C01B2203/0475 , C01B2203/146 , F01N3/0842 , F01N3/0857 , F01N3/0871 , Y02C10/08
Abstract: Methods are provided for the production of nitrogen, hydrogen, and carbon dioxide from an exhaust gas. Exhaust gas from combustion in a fuel rich (or reducing) atmosphere is primarily composed of CO2, CO, N2, H2O, and H2. CO may be converted to CO2 and H2 via the water gas shift reaction. Carbon dioxide may then be effectively separated from nitrogen and hydrogen to produce a carbon dioxide stream and a nitrogen/hydrogen stream. The nitrogen/hydrogen stream may then be effectively separated to produce a high purity nitrogen stream and a high purity hydrogen stream. The process may be done in any order, such as separating the nitrogen first or the carbon dioxide first.
-
公开(公告)号：US20170136402A1
公开(公告)日：2017-05-18
申请号：US15339997
申请日：2016-11-01
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN , Edward W. CORCORAN, JR.
IPC: B01D53/04 , B01D53/047
CPC classification number: B01D53/0423 , B01D53/0462 , B01D53/047 , B01D2253/102 , B01D2253/104 , B01D2253/108 , B01D2253/1124 , B01D2253/116 , B01D2253/204 , B01D2256/10 , B01D2256/20 , B01D2256/245 , B01D2257/102 , B01D2257/104 , B01D2257/40 , B01D2257/504 , B01D2257/7022 , B01D2257/7025 , B01D2259/40015 , B01D2259/40022 , B01D2259/40033 , B01D2259/40045 , B01D2259/40052 , B01D2259/40066 , B01D2259/404 , B01D2259/414 , Y02C10/08 , Y02C20/20
Abstract: A staged complementary pressure swing adsorption system and method for low energy fractionation of a mixed fluid. Two beds in a four-column PSA system are selective for component A, and another two columns are selective for component B. The cycle creates an intermittent A and B product, using the purge effluent from the complementary product fed at an intermediate pressure. This intermittent product is used as purge gas for low-pressure purged elsewhere in the cycle using appropriate storage tanks. The use of an intermediate pressure in this cycle enables continuous production of purified component A and B without the use of compressors. Columns may also be configured to enable pressure to equalize between complementary columns.
-
4.发明申请公开(公告)号：US20170138222A1
公开(公告)日：2017-05-18
申请号：US15339987
申请日：2016-11-01
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN , Franklin F. MITTRICKER , Loren STARCHER
CPC classification number: F01K23/10 , B01D53/047 , B01D2256/10 , B01D2256/245 , B01D2257/504 , C10L3/104 , C10L2290/02 , C10L2290/10 , C10L2290/12 , C10L2290/543 , E21B41/0064 , E21B43/164 , F01K7/16 , F02C3/00 , F05D2220/32 , Y02C10/08 , Y02E20/16
Abstract: Systems and methods are provided for combined cycle power generation and enhanced hydrocarbon production where emission gases during power generation are separated by adsorption and applied to facilitate extraction of hydrocarbons from a reservoir. A power generation plant passes exhaust gas to a first swing adsorption reactor. The first swing adsorption reactor adsorbs the CO2 from the exhaust gas. An adsorption cycle of the first swing adsorption reactor is variable. An injection well injects the CO2 adsorbed by the first swing adsorption reactor in a hydrocarbon reservoir. A production well that is in communication with the injection well produces a mixture of hydrocarbons and CO2. A second swing adsorption reactor purifies the produced hydrocarbons by adsorbing the produced CO2 from the production well.The purified hydrocarbons are fed back to the power generation plant where combustion occurs and power is generated.
-
公开(公告)号：US20170087503A1
公开(公告)日：2017-03-30
申请号：US15258076
申请日：2016-09-07
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN
IPC: B01D53/04
CPC classification number: B01D53/0462 , B01D53/0407 , B01D53/0431 , B01D53/0446 , B01D2253/204 , B01D2253/25 , B01D2257/504 , B01D2259/4009 , B01D2259/414 , B01J20/04 , B01J20/226 , B01J20/3425 , B01J20/3458 , Y02C10/08
Abstract: In various aspects, apparatuses, systems, and methods are provided for performing two stage separation of CO2 from a gaseous stream. The first stage adsorbent can be comprised of a plurality of cylindrical or substantially cylindrical rings. The first stage adsorbent can be comprised of a metal organic framework. The second stage adsorbent can be subject to a displacement desorption process. The second stage adsorbent can be comprised of a support and a metal compound selected from the group consisting of alkali or alkaline earth. The first and second stage adsorbent can be arranged concentrically for space and efficiency considerations.
-
Patent Agency Ranking
6.发明申请公开(公告)号：US20180036672A1
公开(公告)日：2018-02-08
申请号：US15653822
申请日：2017-07-19
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN , David C. CALABRO , Frank MITTRICKER
IPC: B01D53/04 , B01D53/047
CPC classification number: B01D53/0423 , B01D53/0446 , B01D53/047 , B01D53/0473 , B01D2251/302 , B01D2251/304 , B01D2251/306 , B01D2251/402 , B01D2251/404 , B01D2253/104 , B01D2253/108 , B01D2253/1124 , B01D2253/116 , B01D2256/10 , B01D2256/16 , B01D2256/22 , B01D2257/102 , B01D2257/504 , B01D2259/40005 , B01D2259/414 , Y02C10/08
Abstract: An adsorption module and associated processes for conducting advanced separations processes such as sorption enhanced water-gas shift (SEWGS). The adsorption module contains at least one angled baffle to create at least two tapered adsorbent beds within the adsorption module. The taper is such that the adsorbent beds' cross-sections within the adsorption module decrease in the direction of feed flow, thereby taking advantage of increased product purity and process efficiency provided by tapered adsorption beds.
-
7.发明申请公开(公告)号：US20170136400A1
公开(公告)日：2017-05-18
申请号：US15339972
申请日：2016-11-01
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN , Edward W. CORCORAN, JR.
IPC: B01D53/047 , B01D53/04
CPC classification number: B01D53/047 , B01D53/0423 , B01D2253/108 , B01D2253/1124 , B01D2256/10 , B01D2256/22 , B01D2257/102 , B01D2257/504 , B01D2259/40028 , B01D2259/40043 , Y02C10/08
Abstract: Systems and methods are provided for combined cycle power generation while reducing or mitigating emissions during power generation. Recycled exhaust gas from a power generation combustion reaction can be separated using a staged complementary swing adsorption process so as to generate a high purity CO2 stream while reducing/minimizing the energy required for the separation and without having to reduce the temperature of the exhaust gas. This can allow for improved energy recovery while also generating high purity streams of carbon dioxide and nitrogen.
-
公开(公告)号：US20170087504A1
公开(公告)日：2017-03-30
申请号：US15258097
申请日：2016-09-07
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN
IPC: B01D53/04 , B01J20/34 , B01D53/047
CPC classification number: B01D53/0462 , B01D53/0407 , B01D53/047 , B01D2259/40011 , B01D2259/40083 , B01J20/34 , B01J20/3441
Abstract: Systems and methods are provided for performing a swing adsorption process, such as a temperature swing adsorption process. During portions of a swing cycle where one or more components are being desorbed, a vibration or other perturbation can be induced in the adsorbent and/or in the adsorbent structure to assist with desorption. Inducing a vibration or other perturbation in the adsorbent structure can provide a way to introduce additional energy into the adsorbent system without having to increase the temperature of the adsorbent structure.
-
公开(公告)号：US20180036688A1
公开(公告)日：2018-02-08
申请号：US15653853
申请日：2017-07-19
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , David C. CALABRO , Hans THOMANN , Randall D. PARTRIDGE
CPC classification number: B01D69/147 , B01D53/0407 , B01D53/229 , B01D71/022 , B01D71/06 , B01D2251/30 , B01D2251/302 , B01D2251/304 , B01D2251/306 , B01D2251/40 , B01D2251/402 , B01D2251/404 , B01D2251/406 , B01D2251/408 , B01D2251/606 , B01D2253/102 , B01D2253/106 , B01D2253/108 , B01D2253/204 , B01D2256/16 , B01D2256/245 , B01D2257/102 , B01D2257/302 , B01D2257/304 , B01D2257/504 , B01D2258/0283 , B01D2311/2626 , B01D2325/08 , B01D2325/12 , Y02C10/08 , Y02C10/10
Abstract: Gas separation modules and methods for use including an integrated adsorbent and membrane. In certain refining applications, it is paramount to obtain high purity product gases. Adsorbent beds are effective at removing certain contaminants, such as CO2, from gas streams containing product and contaminant constituents to form a product-rich stream. The integrated membrane permits a further separation of products from any unadsorbed contaminant to produce a high purity product, such as hydrogen, stream. The gas separation modules described herein include stacked, radial, and spiral arrangements. Each modules includes a configuration of feed and cross-flow channels for the collection of contaminant gases and/or high purity product gases.
-
10.发明申请公开(公告)号：US20180036674A1
公开(公告)日：2018-02-08
申请号：US15653833
申请日：2017-07-19
Applicant: ExxonMobil Research and Engineering Company
Inventor： Narasimhan SUNDARAM , Hans THOMANN , David C. CALABRO , Frank MITTRICKER
IPC: B01D53/053
CPC classification number: B01D53/053 , B01D53/047 , B01D2253/1122 , B01D2253/1124 , B01D2256/16 , B01D2256/20 , B01D2257/108 , B01D2257/504 , B01D2259/4003 , B01D2259/40035 , B01D2259/40043 , B01D2259/40079 , B01D2259/40081 , B01D2259/403 , B01D2259/404 , C01B3/56 , C01B32/50 , C01B2203/043 , C01B2203/0465 , C01B2203/0475 , Y02C10/08 , Y02P20/152 , Y02P30/30
Abstract: In various aspects, methods are provided for hydrogen production while reducing and/or mitigating emissions during various refinery processes that produce syngas, such as power generation. Syngas can be effectively separated to generate high purity carbon dioxide and hydrogen streams, while reducing and/or minimizing the energy required for the separation, and without needing to reduce the temperature of the flue gas. In various aspects, the operating conditions, such as high temperature, mixed metal oxide adsorbents, and cycle variations, for a pressure swing adsorption reactor can be selected to minimize energy penalties while still effectively capturing the CO2 present in syngas.
-
-
-
-
-
-
-
-
-
Search Results
14
records
(took 0.022 seconds)
