1992
DOI: 10.1016/0016-2361(92)90011-c
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Catalytic purification of tarry fuel gas with carbonate rocks and ferrous materials

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Cited by 145 publications
(85 citation statements)
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“…Delgado et al, 87,88 Sutton et al, 61 and Dayton 56 wrote reviews on gas conditioning with dolomite catalysts. Other researchers who have studied dolomite catalysts include Simell and coworkers [89][90][91] and Corella and co-workers. 92,93 The operating conditions for using dolomite catalyst are temperatures from 700 to 100°C and space times from 0.007 to 7 s. 56 Other nonmetallic oxide catalysts used for this reaction include MgO, 87 CaO, 87 and olivine (a magnesium aluminosilicate).…”
Section: Gas Conditioningmentioning
confidence: 99%
“…Delgado et al, 87,88 Sutton et al, 61 and Dayton 56 wrote reviews on gas conditioning with dolomite catalysts. Other researchers who have studied dolomite catalysts include Simell and coworkers [89][90][91] and Corella and co-workers. 92,93 The operating conditions for using dolomite catalyst are temperatures from 700 to 100°C and space times from 0.007 to 7 s. 56 Other nonmetallic oxide catalysts used for this reaction include MgO, 87 CaO, 87 and olivine (a magnesium aluminosilicate).…”
Section: Gas Conditioningmentioning
confidence: 99%
“…Iron oxide is active in cracking coal volatiles into methane, 38 which is the most stable hydrocarbon formed from the cracking of coal volatiles up to 1,030 ° C. 39 The reactions between Pittsburgh #8 coal volatiles/tar and the composite Fe 2 O 3 particles in a fi xed bed reveal that 87% of the volatiles either were cracked to methane or were oxidized to CO 2 /H 2 O by the composite particles within a gas residence time of 4.6 seconds at 850 ° C. Thus, if the composite particles are capable of oxidizing methane, then they will be able to oxidize coal volatiles. The methane conversion profi le in a given countercurrent moving -bed reactor is shown in Figure 4.27 of Chapter 4 .…”
Section: Experimental Testing Of Reducer Operationsmentioning
confidence: 99%
“…Extensive studies have been reported in the literature to show that iron is very efficient in reduction of hydrocarbon yield, since neutral iron containing minerals, such as dolomite (Ca(Mg x Fe y ) (CO 3 ) 2 ) [8,14,15] or olivine ((Mg x Fe y ) 2 SiO 4 ) [10,16,17] are known for tar cracking and reforming. Moreover, it has also been demonstrated in many studies that iron (III) is responsible for the tar cracking reactions [18,19]. Similarly, Ni-based catalysts have also shown high August, 2011 effectiveness in removing hydrocarbons and in improving product gas quality [20][21][22][23].…”
Section: Introductionmentioning
confidence: 96%