Advancing Adsorption and Membrane-Separation Processes for the Gigaton Carbon Capture Challenge
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Membrane Seperation Processes, Supp. A
I PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California 94025 Abstract Process Economics Program Report No. 190A MEMBRANE GAS SEPARATION PROCESSES (January 1990) Advances in membrane technology in areas such as reverse osmosis and ultrafiltration have led to the development and commercial introduction of membranes for large-scale in- dustrial gas separations. This report studies four major applications--nitrogen production from air, oxygen-enriched air, hydrogen recovery from ammonia purge gas, and carbon dioxide separation from methane. Process economics for each application is presented, based on a preliminary process design. Competing separation operations are reviewed and competitive economics are evaluated for air separation by pressure swing adsorption. A technical review presents the essential criteria for designing on-site systems and membrane system attributes that affect economic competitiveness. Process design features required for the different industrial gas separations are also summarized, and the types of procedures employed to determine membrane area requirements are briefly described. a Finally, gas membrane system development activity by major world regions is presented, along with a review of the main market segments and a listing of current and potential applica- tions for gas membrane separation technology. Also, a look at the major supplier’s technology and market position is presented along with an SRI estimate of the number of currently installed units. Report No. 190A MEMBRANE GAS SEPARATION PROCESSES SUPPLEMENT A by RONALD SMITH - I I February 1990 cl a - A private report by the PROCESS ECONOMICS PROGRAM m a- Menlo Park, California 94025 a For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. -
MEMS Technology for Physiologically Integrated Devices
A BioMEMS Review: MEMS Technology for Physiologically Integrated Devices AMY C. RICHARDS GRAYSON, REBECCA S. SHAWGO, AUDREY M. JOHNSON, NOLAN T. FLYNN, YAWEN LI, MICHAEL J. CIMA, AND ROBERT LANGER Invited Paper MEMS devices are manufactured using similar microfabrica- I. INTRODUCTION tion techniques as those used to create integrated circuits. They often, however, have moving components that allow physical Microelectromechanical systems (MEMS) devices are or analytical functions to be performed by the device. Although manufactured using similar microfabrication techniques as MEMS can be aseptically fabricated and hermetically sealed, those used to create integrated circuits. They often have biocompatibility of the component materials is a key issue for moving components that allow a physical or analytical MEMS used in vivo. Interest in MEMS for biological applications function to be performed by the device in addition to (BioMEMS) is growing rapidly, with opportunities in areas such as biosensors, pacemakers, immunoisolation capsules, and drug their electrical functions. Microfabrication of silicon-based delivery. The key to many of these applications lies in the lever- structures is usually achieved by repeating sequences of aging of features unique to MEMS (for example, analyte sensitivity, photolithography, etching, and deposition steps in order to electrical responsiveness, temporal control, and feature sizes produce the desired configuration of features, such as traces similar to cells and organelles) for maximum impact. In this paper, (thin metal wires), vias (interlayer connections), reservoirs, we focus on how the biological integration of MEMS and other valves, or membranes, in a layer-by-layer fashion. The implantable devices can be improved through the application of microfabrication technology and concepts. -
A Density Functional Theory Study of Hydrogen Adsorption in MOF-5
17974 J. Phys. Chem. B 2005, 109, 17974-17983 A Density Functional Theory Study of Hydrogen Adsorption in MOF-5 Tim Mueller and Gerbrand Ceder* Department of Materials Science and Engineering, Massachusetts Institute of Technology, Building 13-5056, 77 Massachusetts AVenue, Cambridge, Massachusetts 02139 ReceiVed: March 8, 2005; In Final Form: August 3, 2005 Ab initio molecular dynamics in the generalized gradient approximation to density functional theory and ground-state relaxations are used to study the interaction between molecular hydrogen and the metal-organic framework with formula unit Zn4O(O2C-C6H4-CO2)3. Five symmetrically unique adsorption sites are identified, and calculations indicate that the sites with the strongest interaction with hydrogen are located near the Zn4O clusters. Twenty total adsorption sites are found around each Zn4O cluster, but after 16 of these are populated, the interaction energy at the remaining four sites falls off significantly. The adsorption of hydrogen on the pore walls creates an attractive potential well for hydrogen in the center of the pore. The effect of the framework on the physical structure and electronic structure of the organic linker is calculated, suggesting ways by which the interaction between the framework and hydrogen could be modified. Introduction ogies can be synthesized using a variety of organic linkers, One of the major obstacles to the widespread adoption of providing the ability to tailor the nature and size of the pores. hydrogen as a fuel is the lack of a way to store hydrogen with Several frameworks have been experimentally investigated for sufficient gravimetric and volumetric densities to be economi- their abilities to store hydrogen, but to date none are able to do cally practical. -
Membrane Technologies for CO2 Separation A
Journal of Membrane Science 359 (2010) 115–125 Contents lists available at ScienceDirect Journal of Membrane Science journal homepage: www.elsevier.com/locate/memsci Membrane technologies for CO2 separation A. Brunetti a, F. Scura a, G. Barbieri a,∗, E. Drioli a,b a National Research Council, Institute for Membrane Technology (ITM–CNR), Via Pietro BUCCI, c/o The University of Calabria, Cubo 17C, 87030 Rende CS, Italy1 b The University of Calabria, Department of Chemical Engineering and Materials, Cubo 44A, Via Pietro BUCCI, 87030 Rende CS, Italy article info abstract Article history: Today, all the existing coal-fired power plants present over the world emit about 2 billion tons of CO2 per Received 21 July 2009 year. The identification of a capture process which would fit the needs of target separation performances, Received in revised form 6 October 2009 together with a minimal energy penalty, is a key issue. Because of their fundamental engineering and Accepted 17 November 2009 economic advantages over competing separation technologies, membrane operations are, now, being Available online 26 November 2009 explored for CO2 capture from power plant emissions.The aim of this work is to provide people interested in the use of membranes in CO2 capture a general overview of the actual situation both in terms of Keywords: materials studies and global strategy to follow in the choice of the membrane gas separation with respect Membrane systems to the other separation technologies. Firstly, an overview on the polymeric membranes currently studied CO2 separation Flue gas for their use in CO2 capture and of their transport properties is proposed. -
Surface Science 675 (2018) 26–35
Surface Science 675 (2018) 26–35 Contents lists available at ScienceDirect Surface Science journal homepage: www.elsevier.com/locate/susc Molecular and dissociative adsorption of DMMP, Sarin and Soman on dry T and wet TiO2(110) using density functional theory ⁎ Yenny Cardona Quintero, Ramanathan Nagarajan Natick Soldier Research, Development & Engineering Center, 15 General Greene Avenue, Natick, MA 01760, United States ARTICLE INFO ABSTRACT Keywords: Titania, among the metal oxides, has shown promising characteristics for the adsorption and decontamination of Adsorption of nerve agents on TiO2 chemical warfare nerve agents, due to its high stability and rapid decomposition rates. In this study, the ad- Molecular and dissociative adsorption sorption energy and geometry of the nerve agents Sarin and Soman, and their simulant dimethyl methyl Dry and hydrated TiO2 phosphonate (DMMP) on TiO2 rutile (110) surface were calculated using density functional theory. The mole- Slab model of TiO 2 cular and dissociative adsorption of the agents and simulant on dry as well as wet metal oxide surfaces were DFT calculations of adsorption energy considered. For the wet system, computations were done for the cases of both molecularly adsorbed water Nerve agent dissociation mechanisms Nerve agent and simulant comparison (hydrated conformation) and dissociatively adsorbed water (hydroxylated conformation). DFT calculations show that dissociative adsorption of the agents and simulant is preferred over molecular adsorption for both dry and wet TiO2. The dissociative adsorption on hydrated TiO2 shows higher stability among the different configura- tions considered. The dissociative structure of DMMP on hydrated TiO2 (the most stable one) was identified as the dissociation of a methyl group and its adsorption on the TiO2 surface. -
30 Years of Membrane Technology for Gas Separation Paola Bernardo, Gabriele Clarizia*
1999 A publication of CHEMICAL ENGINEERING TRANSACTIONS The Italian Association VOL. 32, 2013 of Chemical Engineering Online at: www.aidic.it/cet Chief Editors: Sauro Pierucci, Jiří J. Klemeš Copyright © 2013, AIDIC Servizi S.r.l., ISBN 978-88-95608-23-5; ISSN 1974-9791 30 Years of Membrane Technology for Gas Separation Paola Bernardo, Gabriele Clarizia* Istituto di Ricerca per la Tecnologia delle Membrane, ITM-CNR, Via P. Bucci, cubo 17/C, 87030 Arcavacata di Rende, CS, Italy [email protected] Membrane technology applied to the separation of gaseous mixtures competes with conventional unit operations (e.g., distillation, absorption, adsorption) on the basis of overall economics, safety, environmental and technical aspects. Since the first industrial installations for hydrogen separation in the early eighties, significant improvements in membrane quality have been achieved in air separation as well as in CO2 separation. However, beside the improvement in the materials as well as in membrane module design, an important point is represented by a correct engineering of these separation processes. The recovery of high value co-products from different industrial streams (e.g. organic vapours from off-gas streams, helium from natural gas) is an interesting application, which created a new market for gas separation membranes, coupling environmental and economic benefits. The opportunity to integrate membrane operations in ongoing production cycles for taking advantage from their peculiar characteristics has been proved as a viable approach. In this ambit, membrane systems in appropriate ranges of operating conditions meet the main requirements such as purity, productivity, energy demand of specific industrial processes. -
Adsorption and Desorption Performance and Mechanism Of
molecules Article Adsorption and Desorption Performance and Mechanism of Tetracycline Hydrochloride by Activated Carbon-Based Adsorbents Derived from Sugar Cane Bagasse Activated with ZnCl2 Yixin Cai 1,2, Liming Liu 1,2, Huafeng Tian 1,*, Zhennai Yang 1,* and Xiaogang Luo 1,2,3,* 1 Beijing Advanced Innovation Center for Food Nutrition and Human Health, Beijing Technology & Business University (BTBU), Beijing 100048, China; [email protected] (Y.C.); [email protected] (L.L.) 2 School of Chemical Engineering and Pharmacy, Wuhan Institute of Technology, LiuFang Campus, No.206, Guanggu 1st road, Donghu New & High Technology Development Zone, Wuhan 430205, Hubei Province, China 3 School of Materials Science and Engineering, Zhengzhou University, No.100 Science Avenue, Zhengzhou 450001, Henan Province, China * Correspondence: [email protected] (H.T.); [email protected] (Z.Y.); [email protected] or [email protected] (X.L.); Tel.: +86-139-8627-0668 (X.L.) Received: 4 November 2019; Accepted: 9 December 2019; Published: 11 December 2019 Abstract: Adsorption and desorption behaviors of tetracycline hydrochloride by activated carbon-based adsorbents derived from sugar cane bagasse modified with ZnCl2 were investigated. The activated carbon was tested by SEM, EDX, BET, XRD, FTIR, and XPS. This activated carbon 2 1 exhibited a high BET surface area of 831 m g− with the average pore diameter and pore volume 3 1 reaching 2.52 nm and 0.45 m g− , respectively. The batch experimental results can be described by Freundlich equation, pseudo-second-order kinetics, and the intraparticle diffusion model, 1 while the maximum adsorption capacity reached 239.6 mg g− under 318 K. -
Engineered Transport in Microporous Materials and Membranes for Clean Energy Technologies
Lawrence Berkeley National Laboratory Recent Work Title Engineered Transport in Microporous Materials and Membranes for Clean Energy Technologies. Permalink https://escholarship.org/uc/item/1nb0c4hb Journal Advanced materials (Deerfield Beach, Fla.), 30(8) ISSN 0935-9648 Authors Li, Changyi Meckler, Stephen M Smith, Zachary P et al. Publication Date 2018-02-01 DOI 10.1002/adma.201704953 License https://creativecommons.org/licenses/by-nc-nd/4.0/ 4.0 Peer reviewed eScholarship.org Powered by the California Digital Library University of California REVIEW Microporous Materials www.advmat.de Engineered Transport in Microporous Materials and Membranes for Clean Energy Technologies Changyi Li, Stephen M. Meckler, Zachary P. Smith, Jonathan E. Bachman, Lorenzo Maserati, Jeffrey R. Long, and Brett A. Helms* 1. Introduction Many forward-looking clean-energy technologies hinge on the development of scalable and efficient membrane-based separations. Ongoing investment Improving the efficiency of membrane- in the basic research of microporous materials is beginning to pay dividends based separations is critical to the advance- in membrane technology maturation. Specifically, improvements in mem- ment of many clean-energy technologies, including gas and chemical separations, brane selectivity, permeability, and durability are being leveraged for more carbon capture and sequestration (CCS), efficient carbon capture, desalination, and energy storage, and the market water desalination, dehumidification, adoption of membranes in those areas appears to be on the horizon. Herein, fuel-cell technology, and electrochemical an overview of the microporous materials chemistry driving advanced energy storage (EES). Schemes to engineer membrane development, the clean-energy separations employing them, and highly selective species transport across microporous membranes have progressed the theoretical underpinnings tying membrane performance to membrane considerably in the past decade due to the structure across multiple length scales is provided. -
Simulation of Dynamic Pressure- Swing Gas Sorption in Polymers
ABSTRACT Title: SIMULATION OF DYNAMIC PRESSURE- SWING GAS SORPTION IN POLYMERS Heather Jane St. Pierre, Master of Science, 2005 Directed By: Professor Timothy A. Barbari Department of Chemical Engineering A transport model was developed to simulate a dynamic pressure-swing sorption process that separates binary gas mixtures using a packed bed of non-porous spherical polymer particles. The model was solved numerically using eigenfunction expansion, and its accuracy verified by the analytical solution for mass uptake from a finite volume. Results show the process has a strong dependence on gas solubility. The magnitudes and differences in gas diffusivities have the greatest effect on determining an optimal particle radius, time to attain steady-state operation, and overall cycle time. Sorption and transport parameters for three different polyimides and one copolyimide were used to determine the degree of separation for CO2/CH4 and O2/N2 binary gas mixtures. The separation results for this process compare favorably to those for membrane separation using the same polymer, and significantly improved performance when a second stage is added to the pressure-swing process. SIMULATION OF DYNAMIC PRESSURE-SWING GAS SORPTION IN POLYMERS by Heather Jane St. Pierre Thesis submitted to the Faculty of the Graduate School of the University of Maryland, College Park, in partial fulfillment of the requirements for the degree of Master of Science 2005 Advisory Committee: Professor Timothy A. Barbari, Chair Associate Professor Raymond A. Adomaitis Associate Professor Peter Kofinas © Copyright by Heather Jane St. Pierre 2005 Acknowledgements I would like to thank my advisor, Professor Barbari, for all of his help and guidance during the course of this research. -
Nanoparticle Size Effect on Water Vapour Adsorption by Hydroxyapatite
nanomaterials Article Nanoparticle Size Effect on Water Vapour Adsorption by Hydroxyapatite Urszula Szałaj 1,2,*, Anna Swiderska-´ Sroda´ 1, Agnieszka Chodara 1,2, Stanisław Gierlotka 1 and Witold Łojkowski 1 1 Institute of High Pressure Physics, Polish Academy of Sciences, Sokołowska 29/37, 01-142 Warsaw, Poland 2 Faculty of Materials Engineering, Warsaw University of Technology, Wołoska 41, 02-507 Warsaw, Poland * Correspondence: [email protected]; Tel.: +48-22-876-04-31 Received: 12 June 2019; Accepted: 10 July 2019; Published: 12 July 2019 Abstract: Handling and properties of nanoparticles strongly depend on processes that take place on their surface. Specific surface area and adsorption capacity strongly increase as the nanoparticle size decreases. A crucial factor is adsorption of water from ambient atmosphere. Considering the ever-growing number of hydroxyapatite nanoparticles applications, we decided to investigate how the size of nanoparticles and the changes in relative air humidity affect adsorption of water on their surface. Hydroxyapatite nanoparticles of two sizes: 10 and 40 nm, were tested. It was found that the nanoparticle size has a strong effect on the kinetics and efficiency of water adsorption. For the same value of water activity, the quantity of water adsorbed on the surface of 10 nm nano-hydroxyapatite was five times greater than that adsorbed on the 40 nm. Based on the adsorption isotherm fitting method, it was found that a multilayer physical adsorption mechanism was active. The number of adsorbed water layers at constant humidity strongly depends on particles size and reaches even 23 layers for the 10 nm particles. The amount of water adsorbed on these particles was surprisingly high, comparable to the amount of water absorbed by the commonly used moisture-sorbent silica gel. -
Membrane Separations
MEMBRANE SEPARATIONS RATE CONTROLLED SEPARATION PROCESSES ETH ZURICH — HS 2016 Department of Mechanical and Process Engineering Prof. Dr. Marco Mazzotti Dr. Matteo Gazzani Federico Milella Paolo Gabrielli October 7, 2016 Note for students — HS 2016 For the preparation of the exam the following parts of the script are of less impor- tance: section 1.3; eqs. (1.11), (1.12) and (1.16); chapter 2. The analysis of section 3.3 and 3.4 should be limited to what has been done during the lecture. Contents 1 Membranes theory 1 1.1 Introduction 2 1.2 Mass Balances Over A Membrane Module 3 1.3 Description of mass transfer across selectively permeable membranes 5 1.4 Models For Mass Transfer Through Membranes 10 1.4.1 Pore-flow (hydrodynamic) Model 11 1.4.2 Solution-Diffusion Model 11 1.5 Reverse Osmosis 16 1.5.1 An Application: Water Desalination 21 1.6 Gas Separation 26 1.7 Pervaporation 29 1.8 Unified View Of The Solution Diffusion Model 32 References 33 2 From ideal to real: losses mechanisms in membranes 35 2.1 Concentration Polarization In Liquid Separation Processes 37 iii iv CONTENTS 2.1.1 Osmotic Effect 38 2.2 Concentration Polarization In Gas Separation Processes 39 References 39 3 Design of Gas Separation Modules 41 3.1 Introduction 41 3.2 Gas Separation Module with Perfect Mixing 44 3.3 Gas Separation Module with Cross-plug flow 47 3.4 Gas Separation Module with Counter-current Flow 53 3.5 Design Considerations 56 3.5.1 Membrane Technology 56 3.5.2 Operating Variables 59 References 63 4 Membrane Modules and Processes 65 4.1 Membrane Modules -
The Viable Fabrication of Gas Separation Membrane Used by Reclaimed Rubber from Waste Tires
polymers Article The Viable Fabrication of Gas Separation Membrane Used by Reclaimed Rubber from Waste Tires Yu-Ting Lin 1, Guo-Liang Zhuang 1, Ming-Yen Wey 1,* and Hui-Hsin Tseng 2,3,* 1 Department of Environmental Engineering, National Chung Hsing University, Taichung 402, Taiwan; [email protected] (Y.-T.L.); [email protected] (G.-L.Z.) 2 Department of Occupational Safety and Health, Chung Shan Medical University, Taichung 402, Taiwan 3 Department of Occupational Medicine, Chung Shan Medical University Hospital, Taichung 402, Taiwan * Correspondence: [email protected] (M.-Y.W.); [email protected] (H.-H.T.); Tel.: +886-4-22840441 (ext. 533) (M.-Y.W.); +886-4-24730022 (ext. 12115) (H.-H.T.) Received: 14 September 2020; Accepted: 28 October 2020; Published: 30 October 2020 Abstract: Improper disposal and storage of waste tires poses a serious threat to the environment and human health. In light of the drawbacks of the current disposal methods for waste tires, the transformation of waste material into valuable membranes has received significant attention from industries and the academic field. This study proposes an efficient and sustainable method to utilize reclaimed rubber from waste tires after devulcanization, as a precursor for thermally rearranged (TR) membranes. The reclaimed rubber collected from local markets was characterized by thermogravimetric analyzer (TGA) and Fourier transfer infrared spectroscopy (FT-IR) analysis. The results revealed that the useable rubber in the as-received sample amounted to 57% and was classified as styrene–butadiene rubber, a type of synthetic rubber. Moreover, the gas separation measurements showed that the C7-P2.8-T250 membrane with the highest H2/CO2 selectivity of 4.0 and sufficient hydrogen permeance of 1124.61 GPU exhibited the Knudsen diffusion mechanism and crossed the Robeson trade-off limit.