Author: Richard J. WalkerPublisher:
ISBN:
Category : Flue gases
Languages : en
Pages :
Book Description
Evaluation of Advanced Separation Techniques for Application to Flue Gas Cleanup Processes for the Simultaneous Removal of Sulfur Dioxide and Nitrogen Oxides
Author: Richard J. WalkerPublisher:
ISBN:
Category : Flue gases
Languages : en
Pages :
Book Description
Energy Research Abstracts
Author: Energy Research Abstracts
Author: Flue Gas Desulfurization and Industrial Minerals
Author: M. Michael MillerPublisher:
ISBN:
Category : Flue gases
Languages : en
Pages : 720
Book Description
Contains 4,101 references on FGD [Flue Gas Desulfurization] ... primarily from 1982 through June 1993. Complements the "Flue Gas Desulfurization and Denitrification" bibliography published by the U.S. Dept. of Energy in Jan. 1985. References were located on the Energy, Science and Technology, Pollution Abstracts, and Environmental Bibliography databases. Primarily covers FGD and the use of industrial minerals in the desulfurization process or in by-product utilization and disposal. Emphasizes post-combustion removal of sulfur dioxide through processes such as in-duct injection and wet and dry scrubbing.
Fossil Energy Update
Author: ERDA Energy Research Abstracts
Author: Government Reports Annual Index
Author: Publisher:
ISBN:
Category : Research
Languages : en
Pages : 966
Book Description
Sections 1-2. Keyword Index.--Section 3. Personal author index.--Section 4. Corporate author index.-- Section 5. Contract/grant number index, NTIS order/report number index 1-E.--Section 6. NTIS order/report number index F-Z.
Coal Abstracts
Author: Membrane Technology and Applications
Author: Richard W. BakerPublisher: John Wiley & Sons
ISBN: 9780470854457
Category : Science
Languages : en
Pages : 556
Book Description
Table of Contents Preface Acknowledgments for the first edition Acknowledgments for the second edition 1 Overview of Membrane Science and Technology 1 2 Membrane Transport Theory 15 3 Membranes and Modules 89 4 Concentration Polarization 161 5 Reverse Osmosis 191 6 Ultrafiltration 237 7 Microfiltration 275 8 Gas Separation 301 9 Pervaporation 355 10 Ion Exchange Membrane Processes - Electrodialysis 393 11 Carrier Facilitated Transport 425 12 Medical Applications of Membranes 465 13 Other Membrane Processes 491 Appendix 523 Index 535.
Advanced Separation Technology for Flue Gas Cleanup. Topical Report
Author: Publisher:
ISBN:
Category :
Languages : en
Pages : 300
Book Description
The objective of this work is to develop a novel system for regenerable SO2 and NO(subscript x) scrubbing of flue gas that focuses on (1) a novel method for regenerating spent SO2 scrubbing liquor and (2) novel chemistry for reversible absorption of NO(subscript x). In addition, high efficiency hollow fiber contactors (HFC) are proposed as the devices for scrubbing the SO2 and NO(subscript x) from the flue gas. The system will be designed to remove more than 95% of the SO2 and more than 75% of the NO(subscript x) from flue gases typical of pulverized coal-fired power plants at a cost that is at least 20% less than combined wet limestone scrubbing of SO(subscript x) and selective catalytic reduction of NO(subscript x). The process will generate only marketable by-products. Our approach is to reduce the capital cost by using high-efficiency hollow fiber devices for absorbing and desorbing the SO2 and NO(subscript x). We will also introduce new process chemistry to minimize traditionally well-known problems with SO2 and NO(subscript x) absorption and desorption. Our novel chemistry for scrubbing NO(subscript x) will consist of water-soluble phthalocyanine compounds invented by SRI as well as polymeric forms of Fe{sup ++} complexes similar to traditional NO(subscript x) scrubbing media. The final novelty of our approach is the arrangement of the absorbers in cassette (stackable) form so that the NO(subscript x) absorber can be on top of the SO(subscript x) absorber. This arrangement is possible only because of the high efficiency of the hollow fiber scrubbing devices, as indicated by our preliminary laboratory data. This arrangement makes it possible for the SO2 and NO(subscript x) scrubbing chambers to be separate without incurring the large ducting and gas pressure drop costs necessary if a second conventional absorber vessel were used. Because we have separate scrubbers, we will have separate liquor loops and simplify the chemical complexity of simultaneous SO2/NO(subscript x) scrubbing.