کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
4908756 | 1362583 | 2017 | 33 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Design of a rapid vacuum pressure swing adsorption (RVPSA) process for post-combustion CO2 capture from a biomass-fuelled CHP plant
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
مهندسی شیمی (عمومی)
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چکیده انگلیسی
It was aimed to design a novel RVPSA (Rapid Vacuum Pressure Swing Adsorption) unit for CO2 concentration and recovery in order to achieve the aggressive CO2 capture target, i.e. 95+% CO2 purity and 90+% CO2 recovery at the same time, applied to an existing 10 MWth biomass-fuelled CHP plant. Biomass-fuelled CHP plants are deemed carbon-neutral on the grounds of the net CO2 addition to the atmosphere as a result of its operation being practically zero, ignoring the CO2 emissions involved in the ancillary processes, such as soil enhancement, biomass transport and processing, etc. Furthermore, integrating the biomass-fuelled CHP plant with carbon capture, transport and storage enables carbon-negative energy generation, as its net effect is to recover some CO2 in the air and then store it underground through this plant operation. By the way, a RVPSA process features more efficient utilisation of the adsorbents in the column, leading to much higher bed productivity than a conventional adsorption process. Such a high bed productivity makes it easier to scale up this adsorption process for its application to industrial post-combustion capture. A two-stage, two-bed RVPSA unit was designed and simulated to capture CO2 from the biomass-fuelled CHP plant flue gas containing 13.3% CO2 mole fraction. Effects of operating conditions such as the Purge-to-Feed ratio (P/F) and desorption pressure on the specific power consumption were investigated in detail. It was found that the integrated two-stage RVPSA unit was capable of achieving the following overall performances: CO2 recovery of 90.9%, CO2 purity of 95.0%, bed productivity of 21.2Â molCO2/kg/h and power consumption of 822.9Â kJ/kgCO2. The productivity of the RVPSA unit designed in this study was 20-30 times higher than those of the conventional CO2 capture VPSA processes.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Journal of Environmental Chemical Engineering - Volume 5, Issue 4, August 2017, Pages 3973-3982
Journal: Journal of Environmental Chemical Engineering - Volume 5, Issue 4, August 2017, Pages 3973-3982
نویسندگان
Mauro Luberti, Gabriel David Oreggioni, Hyungwoong Ahn,