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公开(公告)号:US20240071575A1
公开(公告)日:2024-02-29
申请号:US17899271
申请日:2022-08-30
Applicant: INTERNATIONAL BUSINESS MACHINES CORPORATION , EXXONMOBIL TECHNOLOGY AND ENGINEERING COMPANY
Inventor: Rodrigo Neumann Barros Ferreira , Ricardo Luis Ohta , Yogesh V. Joshi , Mathias B. Steiner , Tonia Elengikal , Binquan Luan , Ashish B. Mhadeshwar , Jayashree Kalyanaraman , Anantha Sundaram , Sumathy Raman
IPC: G16C20/30
CPC classification number: G16C20/30
Abstract: Ranking materials for post combustion carbon capture by characterizing sorbent materials with a molecular model workflow that generates microscopic figures of merit for materials by microscopic properties; and evaluating the materials from the molecular model workflow with a process model workflow that generates macroscopic figures of merit for process steps of a carbon recovery process. The materials for applicability as a sorbent material are ranked using a combined microscopic performance and macroscopic process feasibility generator that ranks the materials according to the microscopic figures of merit for materials and the macroscopic figures of merit for the process steps.
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公开(公告)号:US11634371B2
公开(公告)日:2023-04-25
申请号:US17457731
申请日:2021-12-06
Inventor: Changyub Paek , Randall D. Partridge , Yogesh V. Joshi , Jayashree Kalyanaraman , Joseph M. Falkowski
Abstract: A method for separating classes of hydrocarbon compounds from a feed stream including a hydrocarbon mixture is disclosed. The method includes the steps of passing a feed stream through a plurality of separation units arranged in a series in any order, wherein each separation unit has an adsorbent material; and separating classes of hydrocarbon compounds from the feed stream. When one of the plurality of separation units comprises an adsorbent material that is a metal organic framework selected from a zirconium, hafnium, cerium, or titanium-based metal organic framework, then another plurality of separation units includes an adsorption material that is different from the metal organic framework. The method is conducted in a liquid phase. The method can also use a single separation unit with a continuous cyclic bed apparatus. The method can be combined with refining and downstream processes.
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