scholarly journals REMOVED: Report on Pilot Scale Testing and Further Development of a Facilitated Transport Membrane for CO2 Capture from Power Plants

2012 ◽  
Vol 44 ◽  
pp. 432-433 ◽  
Author(s):  
M.B. Hägg ◽  
M. Sandru ◽  
T.J. Kim ◽  
W. Capala ◽  
M. Huijbers
Keyword(s):  
Co2 Capture ◽  
Power Plants ◽  
Pilot Scale ◽  
Facilitated Transport ◽  
Further Development

scholarly journals Pilot testing of CO2 capture from a coal-fired power plant—Part 2: Results from 1-MWe pilot tests

Clean Energy ◽  
2020 ◽  
Vol 4 (1) ◽  
pp. 12-25 ◽  
Author(s):  
Sharon Sjostrom ◽  
Constance Senior
Keyword(s):  
Power Plant ◽  
Fluidized Bed ◽  
Co2 Capture ◽  
Pilot Plant ◽  
Power Plants ◽  
Ion Exchange Resin ◽  
Pilot Scale ◽  
Solid Sorbent ◽  
Pilot Testing ◽  
Handling Characteristics

Abstract Using a 1-MWe slipstream pilot plant, solid-sorbent-based post-combustion CO2 capture was tested at a coal-fired power plant. Results from pilot testing were used to develop a preliminary full-scale commercial design. The sorbent selected for pilot-scale evaluation during this project consisted of an ion-exchange resin that incorporated amines covalently bonded to the substrate. A unique temperature-swing-absorption (TSA) process was developed that incorporated a three-stage fluidized-bed adsorber integrated with a single-stage fluidized-bed regenerator. Overall, following start-up and commissioning challenges that are often associated with first-of-a-kind pilots, the pilot plant operated as designed and expected, with a few key exceptions. The two primary exceptions were associated with: (i) handling characteristics of the sorbent, which were sufficiently different at operating temperature than at ambient temperature when design specifications were established with lab-scale testing; and (ii) CO2 adsorption in the transport line between the regenerator and adsorber that preloaded the sorbent with CO2 prior to entering the adsorber. Results from the pilot programme demonstrate that solid-sorbent-based post-combustion capture can be utilized to achieve 90% CO2 capture from coal-fired power plants.

scholarly journals Field test of a pre-pilot scale hollow fiber facilitated transport membrane for CO2 capture

2019 ◽  
Vol 86 ◽  
pp. 191-200 ◽  
Author(s):  
Zhongde Dai ◽  
Santinelli Fabio ◽  
Nardelli Giuseppe Marino ◽  
Costi Riccardo ◽  
Liyuan Deng
Keyword(s):  
Field Test ◽  
Co2 Capture ◽  
Hollow Fiber ◽  
Pilot Scale ◽  
Facilitated Transport

scholarly journals Pilot Scale Testing of Polymeric Membranes for CO2 Capture from Coal Fired Power Plants

2013 ◽  
Vol 37 ◽  
pp. 6473-6480 ◽  
Author(s):  
Marius Sandru ◽  
Taek-Joong Kim ◽  
Wieslaw Capala ◽  
Martin Huijbers ◽  
May-Britt Hägg
Keyword(s):  
Co2 Capture ◽  
Power Plants ◽  
Pilot Scale ◽  
Polymeric Membranes

scholarly journals Applications of oxygen for NOx control and CO2 capture in coal-fired power plants

2006 ◽  
Vol 10 (3) ◽  
pp. 119-142 ◽  
Author(s):  
Fabienne Châtel-Pélage ◽  
Rajani Varagani ◽  
Pavol Pranda ◽  
Nicolas Perrin ◽  
Hamid Farzan ◽  
...  
Keyword(s):  
Co2 Capture ◽  
Power Plants ◽  
Nox Reduction ◽  
Cost Effective ◽  
Pilot Scale ◽  
Capital Requirements ◽  
Pure Oxygen ◽  
Gas Treatment ◽  
Nox Control ◽  
The Cost

Two promising combustion modification approaches applicable to pulverized coal fired boilers are presented: "Oxygen-Enriched Combustion" (OEC) for NOx control and "Oxy-Combustion" (PC-OC) for CO2 capture. Oxygen-enriched air rather than air is used as an oxidizer in the OEC technology. Unlike flue gas treatment technologies, OEC directly impacts the NOx formation process by significantly reducing the conversion of coal bound nitrogen to NOx. Pilot-scale and full-scale tests have shown 20 to 30% NOx reduction from an optimized staged-air baseline. In addition to the overall cost competitiveness and the reduced capital requirements, other significant advantages of the O2-enriched technology vs. existing low NOx technologies are presented. The PC-OC technology is shown as a cost-effective technology for CO2 capture from existing or new coal-fired power plants. Pure oxygen diluted in recycled flue gases is used as an oxidizer. The process has been successfully demonstrated and extensively characterized at pilot-scale level (1.5 MWt). The tests have shown substantial benefits of the PC-OC technology, in terms of NOx reduction (60-70% from air-baseline), overall plant efficiency, etc. The cost effectiveness of this capture technology compared to competitive amine scrubbing technology was investigated. The cost of CO2 avoided was around $36/ton for the new PC-OC cases, about $48/ton on a retrofit PC-OC case, which is about 25 to 40% cheaper than the amine scrubbing system. Those numbers were calculated for sub-critical units and include the cost of CO2 compression up to 80 bar. .

Pilot Scale Demonstration of Solid Sorbent CO2 Capture Technology at a Biomass Power Station

2019 ◽  
Author(s):  
Gerhard Schöny ◽  
Johannes Fuchs ◽  
Melina Infantino ◽  
Sander Van Paasen ◽  
Jolinde van de Graaf ◽  
...  
Keyword(s):  
Co2 Capture ◽  
Pilot Scale ◽  
Solid Sorbent ◽  
Power Station

Life cycle cost assessment of biomass co-firing power plants with CO2 capture and storage considering multiple incentives

2021 ◽  
Vol 96 ◽  
pp. 105173
Author(s):  
Bo Yang ◽  
Yi-Ming Wei ◽  
Lan-Cui Liu ◽  
Yun-Bing Hou ◽  
Kun Zhang ◽  
...  
Keyword(s):  
Life Cycle ◽  
Co2 Capture ◽  
Life Cycle Cost ◽  
Power Plants ◽  
Cost Assessment ◽  
Co2 Capture And Storage ◽  
And Storage

Experimental Study on Utilization FGD Byproducts in Building Bricks

2010 ◽  
Vol 150-151 ◽  
pp. 753-757 ◽  
Author(s):  
Xiong Hao Li ◽  
Yong Jie Xue ◽  
Min Zhou
Keyword(s):  
Experimental Study ◽  
Compressive Strength ◽  
Optimum Design ◽  
Power Plants ◽  
Pilot Scale ◽  
Mixture Composition ◽  
Technical Requirement ◽  
Do No Harm ◽  
Maximum Compressive Strength ◽  
Scale Experiment

This paper discussed the feasibility of unburned and non-autoclaved, steam cured bricks prepared by FGD byproducts from coal-fired power plants. The results show that FGD byproduct, aggregates, cementious materials and water could be used to prepare bricks during the process of stir and compaction under natural cure and steam cured condition. S4 and Z2 are the optimum design mixture composition. The maximum compressive strength and saturation coefficient are 28.7 MPa and 96.7%. FGD byproducts do no harm to environment and a pilot-scale experiment demonstrates that bricks made with FGDA can meet the MU10 level bricks technical requirement.

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