Chemical Processing in High-Pressure Aqueous Environments. 2. Development of Catalysts for Gasification

Industrial and Engineering Chemistry Research

Volumn 32, Issue 8, 1993, Pages 1542-1548

  Elliott, Douglas C ^a   Sealock, L John ^a   Baker, Eddie G ^a  

^a PACIFIC NORTHWEST NATIONAL LABORATORY   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

ALUMINA; CARBON DIOXIDE; CATALYST SUPPORTS; FEEDSTOCKS; GASIFICATION; HIGH PRESSURE ENGINEERING; METHANE; NICKEL; PROCESSING; RHODIUM; RUTHENIUM;

ACTIVE METALS; CHEMICAL PROCESSING; HIGH PRESSURE AQUEOUS ENVIRONMENT; METAL CATALYSTS; THERMOCHEMICAL ENVIRONMENTAL ENERGY SYSTEM;

CATALYSTS;

EID: 0027641080     PISSN: 08885885     EISSN: 15205045     Source Type: Journal    
DOI: 10.1021/ie00020a002     Document Type: Article

References (24)

1. Agnelli, M.; Kolb, M.; Nicot, C.; Mirodatos, C. Sintering of a Ni-Based Catalyst During CO Hydrogenation: Kinetics and Modeling. Catalyst Deactivation; Bartholomew, C. H., Butt, J. B., Eds.; Elsevier: Amsterdam, 1991, pp 605–612.
2. Baker, E. G.; Sealock, L. J., Jr. Catalytic Destruction of Hazardous Organics in Aqueous Solutions; PNL-6491-2; Pacific Northwest Laboratory: Richland, WA, 1988.
3. Baker, E. G.; Butner, R. S.; Sealock, L. J., Jr.; Elliott, D. C.; Neuenschwander, G. G. Thermocatalytic Conversion of Food Processing Wastes: Topical Report FY 1988; PNL-6784; Pacific Northwest Laboratory: Richland, WA, 1989a.
4. Baker, E. G.; Sealock, L. J., Jr.; Butner, R. S.; Elliott, D. C.; Neuenschwander, G. G.; Banns, N. G. Catalytic Destruction of Hazardous Organics in Aqueous Wastes: Continuous Reactor System Experiments. Hazard. Waste Hazard. Mater. 1989b, 6 (1), 87–94.
5. Bartholomew, C. H.; Sorensen, W. L. Sintering Kinetics of Silica- and Alumina-Supported Nickel in Hydrogen Atmosphere. J. Catal. 1983, 81, 131–141.
6. Bartholomew, C. H.; Pannell, R. B.; Butler, J. L.; Mustard, D. G. Nickel-Support Interactions: Their Effects on Particle Morphology, Adsorption, and Activity Selectivity Properties. Ind. Eng. Chem. Prod. Res. Dev. 1981, 20, 296–300.
7. Butner, R. S.; Elliott, D. C.; Sealock, L. J., Jr. Effect of Catalyst Type and Concentration on Thermal Gasification of High-Moisture Biomass Feedstocks. Biotechnology and Bioengineering Symposium; Wiley: New York, 1987; No. 17, pp 169–177.
8. Chen, I.; Chen, F.-L. Effect of Initial pH Value on Coke Formation of Nickel-Alumina Catalysts in Catalytic Cracking of n-Hezane. Ind. Eng. Chem. Res. 1990, 29, 550–554.
9. Chick, L. A.; Pederson, L. R.; Maupin, G. D.; Bates, J. L.; Thomas, L. B.; Exarhos, G. J. Glycine-Nitrate Combustion Synthesis of Oxide Ceramic Powders. Mater. Lett. 1990, 10 (1–2), 6–12.
10. Cox, J. L.; Sealock, L. J., Jr.; Hoodmaker, F. C. Sulfur Problems in the Direct Catalytic Production of Methane from Coal-Steam Reactions. Energy Sources 1975, 2 (1), 83–100.
11. Dalla Betta, R. A.; Piken, A. G.; Shelef, M. Heterogeneous Methanation: Initial Rate of CO Hydrogenation on Supported Ruthenium and Nickel. J. Catal. 1974, 35, 54–60.
12. Elliott, D. C.; Sealock, L. J., Jr. Low Temperature Gasification of Biomass Under Pressure. In Fundamentals of Thermochemical Biomass Conversion; Overend, R. P., Milne, T. A., and Mudge, L. K., Eds.; Elsevier: London, 1985; pp 937–950.
13. Elliott, D. C.; Sealock, L. J., Jr.; Butner, R. S.; Baker, E. G.; Neuenschwander, G. G. Low-Temperature Conversion of High-Moisture Biomass: Continuous Reactor System Results; PNL-7126; Pacific Northwest Laboratory: Richland, WA, 1989.
14. Elliott, D. C.; Neuenschwander, G. G.; Baker, E. G.; Sealock, L. J., Jr.; Butner, R. S. Low-Temperature Catalytic Gasification of Wet Industrial Wastes, FY 1989–1990 Interim Report; PNL-7671; Pacific Northwest Laboratory: Richland, WA, 1991.
15. Elliott, D. C.; Sealock, L. J., Jr.; Baker, E. G. Chemical Processing in High-Pressure Aqueous Environments. 3. Evaluation of Feedstock Effects. Ind. Eng. Chem. Res. 1993a. Submitted for publication.
16. Elliott, D. C.; Phelps, M. R.; Sealock, L. J., Jr.; Baker, E. G. Chemical Processing in High-Pressure Aqueous Environments. 4. Results from Continuous-Feed Reactor Systems. Ind. Eng. Chem. Res. 1993b. Submitted for publication.
17. 2O. J. Geol. 1951, 59, 381–394.
18. Kelley, R. D.; Candela, G. A.; Madey, T. E.; Mewbury, D. E.; Schehl, R. R. Surface and Bulk Analysis of a Deactivated Raney Nickel Methanation Catalyst. J. Catal. 1983, 80, 235–248.
19. Mirodatos, C.; Praliaud, H.; Primet, M. Deactivation of Nickel-Based Catalysts during CO Methanation and Diproportionation. J. Catal. 1987, 107, 275–287.
20. Pearce, R.; Patterson, W. R. Catalysis and Chemical Processes; Wiley: New York, 1981; p 15.
21. Rostrup-Nielsen, J. R. Steam Reforming Catalysts; Danish Technical Press: Copenhagen, 1975.
22. Sealock, L. J., Jr.; Elliott, D. C.; Butner, R. S.; Neuenschwander, G. G. Low-Temperature Conversion of High-Moisture Biomass: Topical Report January 1984–January 1988; PNL-6726; Pacific Northwest Laboratory: Richland, WA, 1988.
23. 2/CO Mixtures over the Group VIII Metals: 1. The Specific Activities and Product Distributions of Supported Metals. J. Catal. 1975, 37, 449–461.
24. Varma, R. L.; Bakhshi, N. N.; Mathews, J. F. Selective Synthesis of Hydrocarbons from Syngas Using Nickel/ZSM-5 Catalysts. Ind. Eng. Chem. Res. 1990, 29, 1753–1757.