PDF Publication Title:
Text from PDF Page: 009
ISRN Chemical Engineering 9 [72] R. L. Bec, “Method for purifying hydrogen-based gas mix- tures using calcium X-zeolite,” U.S. patent 6, 849, 106, 2005. [73] P. Guerin de Montgareuil and D. Domine, “Process for separating a binary gaseous mixture by adsorption,” US patent 3, 155, 468, 1964. [74] N. H. Berlin, “Method for providing an oxygen-enriched environment,” U.S. Patent 3, 280, 536, 1966. [75] H. Ju ̈ntgen, K. Knoblauch, J. Reichenberger, and F. Tarnow, “Process for the recovery of nitrogen-rich gases from gases containing at least oxygen as other component,” U.S. patent 4, 264, 339, 1981. [76] D. M. Ruthven, N. S. Raghavan, and M. M. Hassan, “Adsorption and diffusion of nitrogen and oxygen in a carbon molecular sieve,” Chemical Engineering Science, vol. 41, no. 5, pp. 1325–1332, 1986. [77] C. G. Coe, J. F. Kirner, R. Pierantozzi, and T. R. White, “Nitrogen adsorption with Ca and or Sr exchanged lithium X-zeolites,” U.S. patent 5, 152, 813, 1992. [78] J. G. Jee, J. S. Lee, and C. H. Lee, “Air separation by a small-scale two-bed medical O2 pressure swing adsorption,” Industrial and Engineering Chemistry Research, vol. 40, no. 16, pp. 3647–3658, 2001. [79] Y. Lu ̈, S. J. Doong, and M. Bu ̈low, “Pressure-swing adsorption using layered adsorbent beds with different adsorption properties: II-experimental investigation,” Adsorption, vol. 10, no. 4, pp. 267–275, 2005. [80] J. C. Santos, A. F. Portugal, F. D. Magalha ̃es, and A. Mendes, “Optimization of medical PSA units for oxygen production,” Industrial and Engineering Chemistry Research, vol. 45, no. 3, pp. 1085–1096, 2006. [81] K. G. Teague and T. F. Edgar, “Predictive dynamic model of a small pressure swing adsorption air separation unit,” Industrial and Engineering Chemistry Research, vol. 38, no. 10, pp. 3761–3775, 1999. [82] K.T.Chue,J.N.Kim,Y.J.Yoo,S.H.Cho,andR.T. Yang, “Comparison of activated carbon and zeolite 13X for CO2 recovery from flue gas by pressure swing adsorption,” Industrial and Engineering Chemistry Research, vol. 34, no. 2, pp. 591–598, 1995. [83] J. H. Park, H. T. Beum, J. N. Kim, and S. H. Cho, “Numerical analysis on the power consumption of the PSA process for recovering CO2 from flue gas,” Industrial and Engineering Chemistry Research, vol. 41, no. 16, pp. 4122–4131, 2002. [84] A. L. Chaffee, G. P. Knowles, Z. Liang, J. Zhang, P. Xiao, and P. A. Webley, “CO2 capture by adsorption: materials and process development,” International Journal of Greenhouse Gas Control, vol. 1, no. 1, pp. 11–18, 2007. [85] J. S. D’amico, H. E. Reinhold III, and K. S. Knaebel, “Helium recovery,” U.S. patent, 5, 542, 966, 1996. [86] N. K. Das, H. Chaudhuri, R. K. Bhandari, D. Ghose, P. Sen, and B. Sinha, “Purification of helium from natural gas by pressure swing adsorption,” Current Science, vol. 95, no. 12, pp. 1684–1687, 2008. [87] A. P. G. Taveira and A. M. M. Mendes, “Xenon external recycling unit for recovery, purification and reuse of xenon in anesthesia circuits,” U.S. patent 7, 442, 236, 2008. [88] S. Sircar and W. R. Kock, “Adsorptive separation of methane and carbon dioxide gas mixtures,” European patent EP, 0193716, 1986. [89] S. Sircar, “High efficiency separation of methane and car- bon dioxide mixtures by adsorption: adsorption and ion exchange,” AIChE Symposium Series, vol. 84, pp. 70–72, 1988. [90] S. Sircar, R. Kumar, W. R. Koch, and J. Vansloun, “Recovery of methane from landfill gas,” United States patent 4, 770, 676, 1988. [91] M. M. Davis, R. L. J. Gray, and K. Patei, “Process for the purification of natural gas,” US patent, 5, 174, 796, 1992. [92] M. Mitariten, “Economic N2 removal,” Hydrocarbon Engi- neering, vol. 9, no. 7, pp. 53–57, 2004. [93] I. A. A. C. Esteves and J. P. B. Mota, “Simulation of a new hybrid membrane/pressure swing adsorption process for gas separation,” Desalination, vol. 148, no. 17–3, pp. 275–280, 2002. [94] K. S. Knaebel and H. E. Reinhold, “Landfill gas: from rubbish to resource,” Adsorption, vol. 9, no. 1, pp. 87–94, 2003. [95] C. A. Grande and A. E. Rodrigues, “Biogas to fuel by vacuum pressure swing adsorption I. Behavior of equilibrium and kinetic-based adsorbents,” Industrial and Engineering Chem- istry Research, vol. 46, no. 13, pp. 4595–4605, 2007. [96] C. A. Grande and R. Blom, “Utilization of Dual-PSA technology for natural gas upgrading and integrated CO2 capture,” Energy Procedia, vol. 26, pp. 2–14, 2012. [97] “Isosiv process operates commercially,” Chemical & Engineer- ing News, vol. 40, pp. 59–63, 1962. [98] T. C. Holcombe, “N-paraffin—isoparaffin separation pro- cess,” U.S. patent, 4, 176, 053, 1979. [99] J. A. C. Silva, Separation of n/iso—paraffins by adsorption pro- cess [Ph.D. dissertation], University of Porto, Porto, Portugal, 1998. [100] A. Mersmann, B. Fill, R. Hartmann, and S. Maurer, “The potential of energy saving by gas phase adsorption processes,” Chemical Engineering & Technology, vol. 23, pp. 937–944, 2000. [101] S. Sircar, “Pressure swing adsorption,” Industrial and Engi- neering Chemistry Research, vol. 41, no. 6, pp. 1389–1392, 2002. [102] C. Voss, “Applications of pressure swing adsorption technol- ogy,” Adsorption, vol. 11, no. 1, pp. 527–529, 2005. [103] K. Knaebel, “Adsorbent selection,” 2004, http://www.adsorp- tion.com/publications/AdsorbentSel1B.pdf. [104] N. Sundaram and R. T. Yang, “On the pseudomultiplicity of pressure swing adsorption periodic states,” Industrial and Engineering Chemistry Research, vol. 37, no. 1, pp. 154–158, 1998. [105] W. A. Patrick, B. F. Lovelace, and E. B. Miller, “Method and apparatus for separating vapors and gases,” U.S. patent 1, 335, 348, 1920. [106] A. B. Ray, “Process of recovering absorbable constituents from gas streams,” U.S. patent 1, 548, 280, 1925. [107] R. T. Yang and P. L. Cen, “Improved pressure swing adsorption processes for gas separation: by heat exchange between adsorbers and by high-heat-capacity inert addi- tives,” Industrial & Engineering Chemistry Process Design and Development, vol. 25, no. 1, pp. 54–59, 1986. [108] H. Ahn, C. H. A. Lee, B. Seo, J. Yang, and K. Baek, “Backfill cycle of a layered bed H2 PSA process,” Adsorption, vol. 5, no. 4, pp. 419–433, 1999. [109] W. D. Marsh, F. S. Pramuk, R. C. Hoke, and C. W. Skarstrom, “Pressure equalization depressurising in heatless adsorption,” U.S. patent no. 3, 142, 547, 1964. [110] T. M. Stark, “Gas separation by adsorption process,” U.S. patent 3, 252, 268, 1966. [111] M. P. S. Santos, C. A. Grande, and A. E. Rodrigues, “Pressure swing adsorption for biogas upgrading: effect of recyclingPDF Image | Advances in Pressure Swing Adsorption for Gas Separation
PDF Search Title:
Advances in Pressure Swing Adsorption for Gas SeparationOriginal File Name Searched:
982934.pdfDIY PDF Search: Google It | Yahoo | Bing
CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info
Heat Pumps CO2 ORC Heat Pump System Platform More Info
CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com | RSS | AMP |