Zobrazeno 1 - 10
of 13
pro vyhledávání: '"Mahesh V. Iyer"'
Publikováno v:
Industrial & Engineering Chemistry Research. 50:1716-1729
Enhancement in the production of high purity hydrogen (H2) from fuel gas, obtained from coal gasification, is limited by thermodynamics of the water gas shift reaction. However, this constraint can...
Autor:
Bartev B. Sakadjian, Robert M. Statnick, Mahesh V. Iyer, Songgeng Li, Shwetha Ramkumar, Liang-Shih Fan, William S.-Y. Wang, Danny S. Wong
Publikováno v:
Industrial & Engineering Chemistry Research. 49:5094-5101
Increasing concerns over growing CO2 levels in the atmosphere have led to a worldwide demand for efficient, cost-effective, and clean carbon capture technologies. One of these technologies is the Carbonation−Calcination Reaction (CCR) process, whic
Autor:
Tarunjit S. Butalia, Harold W. Walker, Ah-Hyung Alissa Park, Liang-Shih Fan, Rajeev Agnihotri, Himanshu Gupta, Theodore J. Thomas, Mahesh V. Iyer, Linda K. Weavers, Raja A. Jadhav, Puneet Gupta
Publikováno v:
Industrial & Engineering Chemistry Research. 46:5051-5060
A pilot-scale study of the Ohio State Carbonation Ash Reactivation (OSCAR) process was performed to demonstrate the reactivity of two novel calcium-based sorbents toward sulfur and trace heavy metal (arsenic, selenium, and mercury) capture in the fur
Publikováno v:
Industrial & Engineering Chemistry Research. 46:35-42
The influence of several process parameters on the calcination of a naturally occurring limestone and a precipitated mesoporous calcium carbonate (CaCO3) sorbent structure to calcium oxide (CaO) is detailed in this study. CaCO3 calcination is an inte
Autor:
Alex Punnoose, Dady B. Dadyburjor, Mohindar S. Seehra, Mahesh V. Iyer, Edwin L. Kugler, Lawrence P. Norcio
Publikováno v:
Topics in Catalysis. 29:197-200
Cobalt–tungsten η-carbide [Co6W6C] is the precursor for a novel stable and active catalyst for “dry” reforming of methane with carbon dioxide to produce synthesis gas. Once the catalyst is pretreated, the catalyst activity is unchanged after 1
Publikováno v:
Industrial & Engineering Chemistry Research. 43:3939-3947
Micron-sized CaO, obtained by calcination of mesoporous CaCO3, attained 36 wt % CO2 sorption capacity after 100 cycles of carbonation and calcination reactions at 700 °C. The extent of simultaneous carbonation (XCO2) and sulfation (XSO2) of CaO at 7
Publikováno v:
Industrial & Engineering Chemistry Research. 42:2712-2721
A cobalt−tungsten η-carbide material [Co6W6C] was investigated as a precursor for a stable and active catalyst for the dry reforming of methane to produce synthesis gas. The kinetics of CH4/CO2 reforming were studied under differential conditions
Hydrogen production by the water gas shift reaction (WGSR) is equilibrium limited due to thermodynamic constrains. However, this can be overcome by continuously removing the product CO{sub 2}, thereby driving the WGSR in the forward direction to enha
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::c05f64cdee1585a2c412e75ac1fd1b77
https://doi.org/10.2172/838225
https://doi.org/10.2172/838225
Publikováno v:
International Journal of Environmental Technology and Management. 4:3
Calcium oxide powder derived by the calcination of mesoporous calcium carbonate provides a higher conversion towards carbonation compared to calcium oxide derived from naturally occurring limestone and hydrated lime. Compaction of this high reactivit
Autor:
Himanshu Gupta, Theodore J. Thomas, Ah-Hyung A. Park, Mahesh V. Iyer, Puneet Gupta, Rajeev Agnihotri, Raja A. Jadhav, Harold W. Walker, Linda K. Weavers, Tarunjit Butalia, Liang-Shih Fan
Publikováno v:
Industrial & Engineering Chemistry Research; Jul2007, Vol. 46 Issue 14, p5051-5060, 10p