Process development for production of coal/sorbent pellets

final technical report
  • 26 Pages
  • 1.68 MB
  • 5413 Downloads
  • English
by
Illinois State Geological Survey , Champaign, Ill]
Separation (Technology), Coal, Sorbents, Desulfuriz
StatementIllinois State Geological Survey ; submitted to Illinois Dept. of Energy and Natural Resources and the Illinois Coal Industry Committee through the Center for Research on Sulfur in Coal
SeriesOpen file series (Illinois State Geological Survey) -- 1991-8, Open file series (Illinois State Geological Survey) -- 1991-8.
ContributionsBanerjee, D. D., 1930-, Illinois. Dept. of Energy and Natural Resources, Illinois State Geological Survey, Illinois Coal Industry Committee, Center for Research on Sulfur in Coal
The Physical Object
Pagination26 p. :
ID Numbers
Open LibraryOL25483971M
OCLC/WorldCa34004523

@article{osti_, title = {Process development for production of coal/sorbent agglomerates}, author = {Rapp, D.M.}, abstractNote = {The goal of this work was to develop a process flow diagram to economically produce a clean-burning fuel from fine Illinois coal. To accomplish this, the process of pelletizing fine coal with calcium hydroxide, a sulfur capturing Author: D.M.

Description Process development for production of coal/sorbent pellets EPUB

Rapp. Technical Report: Process development for production of coal/sorbent agglomerates. Final technical report, September 1, Aug EPA/ January ALTERNATIVES TO CALCIUM-BASED SO2 SORBENTS FOR FLUIDIZED-BED COMBUSTION: CONCEPTUAL EVALUATION by Richard A.

Newby and Dale L Keairns Westinghouse Research and Development Center Beulah Road Pittsburgh, Pennsylvania Contract No. Program Element No. EHEA EPA Project. Status of Development • Overall Process Development • Availability of Data 2.

Performance • SO2 Removal • Reliability 3. TABLE i ro SOLID WASTE PRODUCTION FOR THE LIMESTONE FGD PROCESS (Ash-Free Basis, 50 percent solids) Percent Boiler size and type removal g/s MWt(30xl06 Btu/hr) Underfeed Stoker 22 MWt(75xl05 Btu.

The fuels studied in this project are (a) three flotation slurry fuels beneficiated from coal fines at various stages of the cleaning process and (b) coal-sorbent pellets made from the flotation. The typical process concept for desulphurisation of natural gas and similar feedstock is a two-step process based on hydrogenation of organic S compounds (and Cl compounds if they are present) and subsequent adsorption/absorption of H 2 S (and HCl).

This process concept has been used industrially for decades and is well documented in the literature, see e.g. [12, 13, 14].Cited by: The effect of Process development for production of coal/sorbent pellets book dioxide partial pressure and fluidization velocity on activated carbons produced by carbon dioxide activation of scrap car tyre rubber in a fluidized bed has been studied.

There is an Open Access version for this licensed article that can be read free of charge and without license restrictions. The content of the Open Access version may differ from that of the licensed version. Full text of "Annual report to the Board of Natural Resources and Conservation" See other formats.

Please read our short guide how to send a book to Kindle. Save for later. Most frequently terms. bed fluidized combustion heat fluidized bed gas coal design particle particles temperature fuel sorbent boiler surface boilers erosion This banner text can have markup.

web; books; video; audio; software; images; Toggle navigation. Fluidized bed combustion of difficult fuels in a novel circofluid plant Further development of circulating fluidized-bed boiler plant for utilisation of different low-grade and waste fuels Circulating fluidized bed with optimal control of process parameters to achieve better environmental conditions and flexibility in operation.

Process development for production of coal/ sorbent agglomerates.

Details Process development for production of coal/sorbent pellets FB2

Final technical report, September 1, Aug SciTech Connect. Rapp, D.M. The goal of this work was to develop a process flow diagram to economically produce a clean-burning fuel from fine Illinois coal.

Development of Souvenir Production Transaction Processing System. NASA Astrophysics Data System (ADS) Rumambi, H.; Kaparang, R.; Lintong, J.

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This research aims to desi. The scale of this development, both in total capacity as well as in plant size, can be judged by the figures in Table Similar, if not quite so spectacular, developments took place in hydrogen and methanol production.

Table Development of ammonia production capacity – Year World ammonia production (MMt/y) Maximum converter. Combustion Engineering Issues for Solid Fuels TABLE United States Coal Production in by Region and State Coal-Producing Region and State Appalachia Total Alabama Kentucky, Eastern Maryland Ohio Pennsylvania Anthracite Bituminous Tennessee Virginia West Virginia Interior Total Arkansas Illinois Indiana Kansas Kentucky, Western.

This book gathers technical and scientific articles by leading experts from 15 countries and originally presented at the world’s most prestigious forum on coal preparation: the XVIII International Coal Preparation Congress.

Topics addressed include: the mineral resources basis of the coal industry; problems and prospects of development in the coal industry; crushing. fusion of gas into bulk and into grains of the solid feedstock control rate of interaction between gas and solid.

4 Also, since heat is transferred from crucible into the solid feed- stock, there is a temperature gradient within bulk of the solid feedstock; that is, temperature in the wall of the crucible is larger than temperature in its middle.

In addition, there is no means to enhance gas. Energy efficiency is important to LNG production as feed gas is consumed in order to carryout theliq uefaction process.

In this paper, two different types of natural gas liquefaction cycle with staged compression were designed and simulated for development of liquefaction process which is the core technology in the industry of natural gas.

The overall efficiency of such systems will be essentially reduced compared to direct or shorter conversion. The overall efficiency ηoverall is the product of the efficiencies of each step in the conversion process. 26 Applied Energy: An Introduction Hot reservoir K (°C) Heat J Engine system Useful work J Cold reservoir K.