scholarly journals Summary Report of the Reactive CO2 Capture: Process Integration for the New Carbon Economy Workshop, February 18-19, 2020

2021 ◽  
Author(s):  
Todd Deutsch ◽  
Sarah Baker ◽  
Peter Agbo ◽  
Douglas Kauffman ◽  
James Vickers ◽  
...  
Keyword(s):  
Co2 Capture ◽  
Process Integration ◽  
Summary Report ◽  
Capture Process ◽  
Carbon Economy

Shand Coal Fired Power Plant Integrating a Post Combustion CO2 Capture Process

2019 ◽  
Author(s):  
Wayuta Srisang ◽  
Teerawat Sanpasertparnich ◽  
Brent Jacobs ◽  
Stavroula Giannaris ◽  
Corwyn Bruce ◽  
...  
Keyword(s):  
Power Plant ◽  
Co2 Capture ◽  
Capture Process

scholarly journals Advances and emerging techniques for energy recovery during absorptive CO2 capture: A review of process and non-process integration-based strategies

2021 ◽  
Vol 147 ◽  
pp. 111241
Author(s):  
Kelvin O. Yoro ◽  
Michael O. Daramola ◽  
Patrick T. Sekoai ◽  
Edward K. Armah ◽  
Uwemedimo N. Wilson
Keyword(s):  
Co2 Capture ◽  
Energy Recovery ◽  
Process Integration

scholarly journals Design of a Low-cost CO2 Capture Process Based on Heat Integration Technology

2014 ◽  
Vol 61 ◽  
pp. 365-368 ◽  
Author(s):  
Chunfeng Song ◽  
Yasuki Kansha ◽  
Masanori Ishizuka ◽  
Qian Fu ◽  
Atsushi Tsutsumi
Keyword(s):  
Co2 Capture ◽  
Low Cost ◽  
Heat Integration ◽  
Capture Process ◽  
Integration Technology

Assessing the risk of corrosion in amine-based CO2 capture process

2016 ◽  
Vol 43 ◽  
pp. 189-197 ◽  
Author(s):  
Alicja Krzemień ◽  
Angelika Więckol-Ryk ◽  
Adam Smoliński ◽  
Aleksandra Koteras ◽  
Lucyna Więcław-Solny
Keyword(s):  
Co2 Capture ◽  
Capture Process

Application of Sequential Design of Experiments (SDoE) to Large Pilot-Scale Solvent-Based CO2 Capture Process at Technology Centre Mongstad (TCM)

2021 ◽  
Author(s):  
Joshua Morgan ◽  
Benjamin Omell ◽  
Michael Matuszewski ◽  
David Miller ◽  
Muhammad Ismail Shah ◽  
...  
Keyword(s):  
Design Of Experiments ◽  
Co2 Capture ◽  
Pilot Scale ◽  
Sequential Design ◽  
Capture Process

scholarly journals Evaluation on the Stability of Amine-Mesoporous Silica Adsorbents used for CO2 Capture

2020 ◽  
Vol 36 (1) ◽  
Author(s):  
Dang Viet Quang ◽  
Dao Van Duong ◽  
Vu Thi Hong Ha ◽  
Dao Sy Duc ◽  
Tran Thi Ngoc Dung ◽  
...  
Keyword(s):  
Mesoporous Silica ◽  
Co2 Capture ◽  
Capture Process ◽  
Silica Substrate ◽  
Humid Condition ◽  
Silica Adsorbents ◽  
Reduction Of Energy Consumption ◽  
The Stability ◽  
Co2 Adsorption Capacity ◽  
Co2 Capture Capacity

Amine-mesoporous silica has been considered as a promising CO2 adsorbent with high potential for the reduction of energy consumption and CO2 capture cost; however, its stability could greatly vary with synthetic method. In this study, adsorbents prepared by impregnating different amines including polyethylenimine (PEI) and 3-aminopropyltriethoxysilane (APTES) onto mesoporous silica were used to evaluate the effect of amines selection on the stability of adsorbents used in CO2 capture process. Results revealed that APTES impregnated mesoporous silica (APTES-MPS) is more stable than PEI-impregnated mesoporous silica (PEI-MPS); APTES-MPS was thermally decomposed at ≈280 oC, while PEI-MPS was thermally decomposed at ≈180 oC only. PEI-MPS was particularly less stable when operating under dry condition; its CO2 adsorption capacity reduced by 22.1% after 10 adsorption/regeneration cycles, however, the capacity can be significantly improved in humid condition. APTES-MPS showed a greater stability with no significant reduction in CO2 capture capacity after 10 adsorption/regeneration cycles. In general, APTES-MPS adsorbent possesses a higher stability compared to PEI-MPS thanks to the formation of chemical bonds between amino-functional groups and mesoporous silica substrate. Keywords: Mesoporous silica; CO2 capture; Adsorption; Regeneration; Emission.

CO2 Capture Using Calcium Oxide Applicable to In-Situ Separation of CO2 From H2 Production Processes

2013 ◽  
Author(s):  
Saeed Danaei Kenarsari ◽  
Yuan Zheng
Keyword(s):  
Calcium Oxide ◽  
Co2 Capture ◽  
Fixed Bed ◽  
H2 Production ◽  
Fixed Bed Reactor ◽  
Capture Process ◽  
Conversion Rates ◽  
In Situ Separation ◽  
Separation Of Co2

A lab-scale CO2 capture system is designed, fabricated, and tested for performing CO2 capture via carbonation of very fine calcium oxide (CaO) with particle size in micrometers. This system includes a fixed-bed reactor made of stainless steel (12.7 mm in diameter and 76.2 mm long) packed with calcium oxide particles dispersed in sand particles; heated and maintained at a certain temperature (500–550°C) during each experiment. The pressure along the reactor can be kept constant using a back pressure regulator. The conditions of the tests are relevant to separation of CO2 from combustion/gasification flue gases and in-situ CO2 capture process. The inlet flow, 1% CO2 and 99% N2, goes through the reactor at the flow rate of 150 mL/min (at standard conditions). The CO2 percentage of the outlet gas is monitored and recorded by a portable CO2 analyzer. Using the outlet composition, the conversion of calcium oxide is figured and employed to develop the kinetics model. The results indicate that the rates of carbonation reactions considerably increase with raising the temperature from 500°C to 550°C. The conversion rates of CaO-carbonation are well fitted to a shrinking core model which combines chemical reaction controlled and diffusion controlled models.

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