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100524e19920101dcu s| f1|||||eng|d |
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|a (TOE)ost7139320
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|a (TOE)7139320
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|a TOE
|c TOE
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|a GDWR
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|a 37
|2 edbsc
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|a E 1.99: conf-920951--57
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| 086 |
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|a E 1.99:doe/mc/26373-93/c0104
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|a E 1.99: conf-920951--57
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| 245 |
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|a Development of ceramic membrane reactors for high temperature gas cleanup
|h [electronic resource]
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| 260 |
|
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|a Washington, D.C. :
|b United States. Dept. of Defense ;
|a Oak Ridge, Tenn. :
|b distributed by the Office of Scientific and Technical Information, U.S. Dept. of Energy,
|c 1992.
|
| 300 |
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|a Pages: (8 p) :
|b digital, PDF file.
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| 336 |
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|a text
|b txt
|2 rdacontent.
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| 337 |
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|a computer
|b c
|2 rdamedia.
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| 338 |
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|a online resource
|b cr
|2 rdacarrier.
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| 500 |
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|a Published through the Information Bridge: DOE Scientific and Technical Information.
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| 500 |
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|a 01/01/1992.
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| 500 |
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|a "doe/mc/26373-93/c0104"
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| 500 |
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|a " conf-920951--57"
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| 500 |
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|a "DE93002824"
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| 500 |
|
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|a US Department of Energy contractors review meeting on gasification and gas stream cleanup systems, Morgantown, WV (United States), 15-17 Sep 1992.
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| 500 |
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|a Roberts, D.L.; Way, J.D.
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| 520 |
3 |
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|a The more difficult part of developing a membrane reactor was making a membrane with suitable permselectivity. Since both the ammonia and H[sub 2]S decomposition reactions produce H[sub 2], we want a membrane that selectively permeates hydrogen. We have taken the approach of coating a substrate that has fine pores (a microfilter or ultrafilter) with a completely dense layer and then (except for palladium coatings) malting super fine pores in the dense layer by leaching or pyrolysis. We used four different substrates (Norton 0.2 alumina monolith, Refractron alumina microfilters, Vycor glass, Alcoa ultrafilter) and five different coating materials (Poly N-methyl silazane, Aremco 617 alumina-based glaze, Polycyclohydridomethyl silazane, Aluminum phosphorus oxides, palladium). Only the palladium films on an alumina ultrafilter could be made regularly with a negligible defect population. The other approaches were plagued with cracks and poor reproducibility. We made palladium films on a tubular alumina ultrafilter (US Filter, Warrendale, PA) by electroless plating from a platinum amine complex solution in hydrazine (Rhoda, 1959). The best results were achieved with an ultrafilter pore size of 100 angstroms and with pretreatment of the surface in a stannic/stannous chloride solution. The films were about 5 microns thick and appeared defect free under electron microscopy. Because defect-free palladium films are infinitely selective to hydrogen with respect to the other components of gasifier product gas, we expect that the selectivity of our palladium films will exceed 1000 even with the inevitable defects that accompany real membranes. We have analyzed the performance and economics of membrane reactors for H[sub 2]S and NH[sub 3] decomposition using the reaction rates determined experimentally in our catalyst development work and using the permeation behavior of palladium films reported in the literature.
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| 536 |
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|b AC21-89MC26373.
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| 650 |
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7 |
|a Membranes.
|2 local.
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| 650 |
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7 |
|a Sulfides.
|2 local.
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| 650 |
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7 |
|a Palladium.
|2 local.
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| 650 |
|
7 |
|a Separation Processes.
|2 local.
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| 650 |
|
7 |
|a Ammonia.
|2 local.
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| 650 |
|
7 |
|a Testing.
|2 local.
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| 650 |
|
7 |
|a Sulfur Compounds.
|2 local.
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| 650 |
|
7 |
|a Hot Gas Cleanup.
|2 local.
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| 650 |
|
7 |
|a Nitrogen Hydrides.
|2 local.
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| 650 |
|
7 |
|a Oxygen Compounds.
|2 local.
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| 650 |
|
7 |
|a Hydrides.
|2 local.
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| 650 |
|
7 |
|a Platinum Metals.
|2 local.
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| 650 |
|
7 |
|a Fluids.
|2 local.
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| 650 |
|
7 |
|a Performance Testing.
|2 local.
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| 650 |
|
7 |
|a Permeability.
|2 local.
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| 650 |
|
7 |
|a Elements.
|2 local.
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| 650 |
|
7 |
|a Gases.
|2 local.
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| 650 |
|
7 |
|a Purification.
|2 local.
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| 650 |
|
7 |
|a Metals.
|2 local.
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| 650 |
|
7 |
|a Aluminium Compounds.
|2 local.
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| 650 |
|
7 |
|a Synthesis Gas.
|2 local.
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| 650 |
|
7 |
|a Nitrogen Compounds.
|2 local.
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| 650 |
|
7 |
|a Aluminium Oxides.
|2 local.
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| 650 |
|
7 |
|a Oxides.
|2 local.
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| 650 |
|
7 |
|a Transition Elements.
|2 local.
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| 650 |
|
7 |
|a Hydrogen Sulfides.
|2 local.
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| 650 |
|
7 |
|a Specificity.
|2 local.
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| 650 |
|
7 |
|a Hydrogen Compounds.
|2 local.
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| 650 |
|
7 |
|a Chalcogenides.
|2 local.
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| 650 |
|
7 |
|a Inorganic, Organic, Physical And Analytical Chemistry.
|2 edbsc.
|
| 710 |
2 |
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|a SRI International.
|4 res.
|
| 710 |
1 |
|
|a United States.
|b Department of Defense.
|4 spn.
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| 710 |
1 |
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|a United States.
|b Department of Energy.
|4 spn.
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| 710 |
2 |
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|a National Energy Technology Laboratory (U.S.).
|4 res.
|
| 710 |
1 |
|
|a United States.
|b Department of Energy.
|b Office of Scientific and Technical Information.
|4 dst.
|
| 856 |
4 |
0 |
|u http://www.osti.gov/servlets/purl/7139320-9hYgKL/
|z Online Access
|
| 907 |
|
|
|a .b59689900
|b 03-06-23
|c 05-26-10
|
| 998 |
|
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|a web
|b 05-26-10
|c f
|d m
|e p
|f eng
|g dcu
|h 0
|i 1
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| 956 |
|
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|a Information bridge
|
| 999 |
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|s b3054905-8c9f-5b71-a5d5-e016cb1fd100
|
| 952 |
f |
f |
|p Can circulate
|a University of Colorado Boulder
|b Online
|c Online
|d Online
|e E 1.99: conf-920951--57
|h Superintendent of Documents classification
|i web
|n 1
|
