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| 1 | Biomass gasification technology:The state of the art overview显示文摘In the last decades the interest in the biomass gasification process has increased due to the growing attention to the use of sustainable energy. Biomass is a renewable energy source and represents a valid alternative to fossil fuels. Gasification is the thermochemical conversion of an organic material into a valuable gaseous product, called syngas, and a solid product, called char. The biomass gasification represents an efficient process for the production of power and heat and the production of hydrogen and second-generation biofuels.This paper deals with the state of the art biomass gasification technologies, evaluating advantages and disadvantages, the potential use of the syngas and the application of the biomass gasification. Syngas cleaning though fundamental to evaluate any gasification technology is not included in this paper since; in the authors' opinion, a dedicated review is necessary. | Antonio Molino Simeone Chianese Dino Musmarra | 2016 | Journal of Energy Chemistry2016，25，1： | 28 |
| 2 | Silver impregnated carbon for adsorption and desorption of elemental mercury vapors显示文摘The Hg 0 vapor adsorption experimental results on a novel sorbent obtained by impregnating a commercially available activated carbon (Darco G60 from BDH) with silver nitrate were reported.The study was performed by using a fundamental approach,in an apparatus at laboratory scale in which a synthetic flue gas,formed by Hg 0 vapors in a nitrogen gas stream,at a given temperature and mercury concentration,was flowed through a fixed bed of adsorbent material.Breakthrough curves and adsorption isotherms were obtained for bed temperatures of 90,120 and 150°C and for Hg 0 concentrations in the gas varying in the range of 0.8–5.0 mg/m 3 .The experimental gas-solid equilibrium data were used to evaluate the Langmuir parameters and the heat of adsorption.The experimental results showed that silver impregnated carbon was very effective to capture elemental mercury and the amount of mercury adsorbed by the carbon decreased as the bed temperature increased.In addition,to evaluate the possibility of adsorbent recovery,desorption was also studied.Desorption runs showed that both the adsorbing material and the mercury could be easily recovered,since at the end of desorption the residue on solid was almost negligible.The material balance on mercury and the constitutive equations of the adsorption phenomenon were integrated,leading to the evaluation of only one kinetic parameter which fits well both the experimentally determined breakthrough and desorption curves. | Despina Karatza Marina Prisciandaro Amedeo Lancia Dino Musmarra | 2011 | Journal of Environmental Sciences2011，23，9： | 3 |
| 3 | Uncatalyzed heterogeneous oxidation of calcium bisulfite显示文摘 | Amedeo Lancia Dino Musmarra Francesco P | 1996 | Chem Eng Sci1996，51，16： | 2 |
| 4 | Uncatalyzed heterogeneous oxidation of calcium bisulfate显示文摘 | LANCIA A MUSMARRA D PEPE F | 1996 | Chem Eng Sci1996，，16： | 1 |
| 5 | Evaluation of the jet penetration depth in gas-fluidized beds by pressure signals analysis 显示文摘 | Vaccaro S Musmarra D Petrecca M | 1997 | International Journal of Multiphase Flow1997，23，4： | 1 |
| 6 | A technique for measurement of the jet penetration height in fluidized bed by pressure signal analysis 显示文摘 | Vaccaro S Musmarra D Petrecca M | 1997 | Powder Technology1997，92，2： | 1 |
| 7 | Model of oxygen absorption into calcium sulfite solutions 显示文摘 | Lancia A Musmarra D Pepe F | 1997 | Chem Eng J1997，66，2： | 1 |
| 8 | Measuring induction period for calcium sulfate dihydrate precipitation 显示文摘 | Lancia A Musmarra D | 1999 | AXChE 31999，45，2： | 1 |
| 9 | Catalytic oxidation of calcium bisulfite in the wet limestone-gypsum flue gas desulfurization process显示文摘 | AMEDEO LANCIA DINO MUSMARRA MARINA PRISCIANDARO | 1999 | Chemical Engineering Science1999，54，1516： | 1 |
| 10 | Study of mercury absorption and desorption on sulfur impregnated carbon 显示文摘 | Karatza D Lancia A Musmarra D | 2000 | Experimental Thermal and Fluid Science2000，21，123： | 1 |
| 11 | Uncatalyzed heterogeneous oxidation of calcium bisulfite 显示文摘 | Lancia A Musmarra D Pepe F | 1996 | Chem Eng Sci1996，51，16： | 1 |
| 12 | Measuring Induction Period for Calcium Sulfate Dihydrat Precipitation 显示文摘 | Lancia A Musmarra D Risciandaro M | 1999 | AIChE Journal1999，45，2： | 1 |
| 13 | Measure induction period for calcium sulfate dehydrate precipition显示文摘 | A Lancia D Musmarra | 1999 | A I Ch E J1999，45，： | 1 |
| 14 | Measuring induction period for calcium sulfate dihydrate precipitation显示文摘 | Lancia A Musmarra D Prisciandaro M | 1999 | AIChE J1999，45，2： | 1 |
| 15 | Removal of Mercuric Chloride ti'om Flue Gas by Sulfur Impregnated Activated Carbon显示文摘 | Karatza D Lancia A Musmarra D | 1996 | Hazard Waste Haz- ard Mater1996，13，1： | 1 |
| 16 | Uncatalyzed heterogeneous oxidation of calcium bisulfite 显示文摘 | LANCIA A MUSMARRA D PEPE F | 1996 | Chem Eng Sci1996，，16： | 1 |
| 17 | Catalytic oxidation of calcium bisulfite in the wet limestone-gypsum flue gas desulfurization process显示文摘 | MUSMARRA D | 1999 | Chemical Engineering Science1999，54，4： | 1 |
| 18 | Adsorption of mercuric Chloride Vapor from incinerator flue gases on calcium hydroxide particles 显示文摘 | LANCIA A MUSMARRA D PEPE F | 1993 | Combustion Science and Technology1993，93，： | 1 |
| 19 | A technique for measurement of the jet penetration height in fluidized beds by pressure signal analysis 显示文摘 | Vaccaro S Musmarra D Petrecca M | 1997 | Powder Technology1997，92，3： | 1 |
| 20 | Measuring induction period for calcium sulfate dihydrate precipitation显示文摘 | Lancia A Musmarra D Prisciandaro M | 1999 | AICHE Journal1999，45，2： | 1 |
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