scholarly journals Cyclic operation of a fixed-bed pressure and temperature swing process for CO2 capture: Experimental and statistical analysis

2013 ◽  
Vol 12 ◽  
pp. 35-43 ◽  
Author(s):  
S. García ◽  
M.V. Gil ◽  
J.J. Pis ◽  
F. Rubiera ◽  
C. Pevida
Author(s):  
Rafael Morales-Ospino ◽  
Vitória N. Santos ◽  
Antônio R. A. Lima ◽  
A. Eurico B. Torres ◽  
Enrique Vilarrasa-García ◽  
...  

2021 ◽  
Author(s):  
Pierre Hovington ◽  
Omid Ghaffari-Nik ◽  
Laurent Mariac ◽  
Andrew Liu ◽  
Brett Henkel ◽  
...  

2013 ◽  
Author(s):  
Saeed Danaei Kenarsari ◽  
Yuan Zheng

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.


2018 ◽  
Vol 185 ◽  
pp. 494-504 ◽  
Author(s):  
Ruikai Zhao ◽  
Li Zhao ◽  
Shengping Wang ◽  
Shuai Deng ◽  
Hailong Li ◽  
...  

Author(s):  
Hadi Ramin ◽  
Easwaran N Krishnan ◽  
Gurubalan Annadurai ◽  
Carey J. Simonson

Abstract Fixed-bed regenerators (FBRs) have high sensible effectiveness, making them an energy-efficient Air-to-Air Energy Recovery Exchanger (AAEE) to reduce the energy consumption for ventilation in buildings. FBRs operate by alternately storing and releasing heat in fixed bed exchangers, which results in outlet temperatures that vary with time during both heating and cooling periods. This variation in FBR's outlet temperature adds a new optimization variable that needs to be considered when designing FBRs. For example, in HVAC systems, Careful design is required to prevent large variations in FBR's outlet temperature (Temperature Swing (TS)), which might deteriorate occupant thermal comfort and introduce a variable load on the HVAC system. In this paper, a correlation for TS is developed as a function of FBR design parameters. FBRs optimization is performed considering TS as an additional objective to the traditional parameters of exchanger effectiveness, pressure drop, payback period, and mass. A selection procedure (decision making) is also integrated into the optimization process to select optimized FBRs from Pareto fronts. The results show that when TS is included as an additional objective to the optimization and selection process, the selected optimized FBRs have higher mass and effectiveness.


2020 ◽  
Vol 25 ◽  
pp. 154-167
Author(s):  
M.F.C. Silva Canuto ◽  
J. Morais Ferreira ◽  
S.W.C. Araújo Silva ◽  
Líbia de Sousa Conrado ◽  
Odelsia Leonor Sánchez Alsina ◽  
...  

In this chapter the adsorption fundamentals using biomass as adsorbents in the removal of metallic ions are presented. The research as shows the importance of many factors that affects the adsorption, such as the biomass superficial area, system temperature, pH, initial concentration of the metal, biomass amount and status (living or dead). The study was directed at the approach of two applications using Saccharomyces cerevisiae yeast in the adsorption of Cd2+ metal ions. In the first application it is discussed the influence of the pH of the medium and the biomass status (living or dead) in the adsorption of Cd2+, in batch. In the second application, it was studied the adsorption of Cd2+metallic ions through the Saccharomyces cerevisiae yeast immobilized in chitosan, in fixed bed, where the influence inlet mass flow rate and the initial effluent concentration on the adsorption capacity and percentage of Cd2+ ions removal are evaluated.The studies realized are supported by statistical analysis with 95% confidence intervals.


2019 ◽  
Vol 33 (8) ◽  
pp. 7534-7549 ◽  
Author(s):  
Goutham Kotamreddy ◽  
Ryan Hughes ◽  
Debangsu Bhattacharyya ◽  
Joshua Stolaroff ◽  
Katherine Hornbostel ◽  
...  

Author(s):  
Stephen J.A. DeWitt ◽  
Anshuman Sinha ◽  
Jayashree Kalyanaraman ◽  
Fengyi Zhang ◽  
Matthew J. Realff ◽  
...  

Recent advances in adsorptive gas separations have focused on the development of porous materials with high operating capacity and selectivity, useful parameters that provide early guidance during the development of new materials. Although this material-focused work is necessary to advance the state of the art in adsorption science and engineering, a substantial problem remains: how to integrate these materials into a fixed bed to efficiently utilize the separation. Structured sorbent contactors can help manage kinetic and engineering factors associated with the separation, including pressure drop, sorption enthalpy effects, and external heat integration (for temperature swing adsorption, or TSA). In this review, we discuss monoliths and fiber sorbents as the two main classes of structured sorbent contactors; recent developments in their manufacture; advantages and disadvantages of each structure relative to each other and to pellet packed beds; recent developments in system modeling; and finally, critical needs in this area of research.


2019 ◽  
Vol 17 (1) ◽  
pp. 9-13
Author(s):  
А. Zhumagaliyeva ◽  
V. Gargiulo ◽  
F. Raganat ◽  
Ye. Doszhanov ◽  
M. Alfe

Carbon capture and sequestration contains a group of technologies keeping thedifferentiation of CO2 from large industrial and energy related sources, transport toa storage location and long-term isolation from the atmosphere. Previous studiesof CO2 adsorption on low-cost iron metal oxide surfaces strongly encourage thepossible use of metal oxide as sorbents, but the tendency of magnetite particles toagglomerate causes a lowering of CO2 sorption capacity. This work investigates theadsorption behavior of CO2 on composite materials prepared coating a low-costcarbonized rice husk (cRH), commercial carbon black (CB) with magnetite fineparticles. The CO2 capture capacity of composites and based on rice husk materialswas evaluated the basis of the breakthrough times measured at atmosphericpressure and room temperature in a lab-scale fixed bed micro-reactor. To thisaim the reactor has been firstly operated for CO2 adsorption data with obtainedsamples.


2018 ◽  
Vol 16 (2) ◽  
pp. 115-119
Author(s):  
А. Zhumagaliyeva ◽  
V. Gargiulo ◽  
Ye. Doszhanov ◽  
M. Alfe

In this work carbonized rice husk  was used as carbon-based solid matrix in the preparation of composite materials modified with Fe3O4 particles. Aim of this study is to exploit the advantages and shortcomings of using a real biomass as starting material for the preparation of sorbents for CO2 capture applications. Sorption capacity of the obtained composite materials was tested on fixed-bed  microreactor.


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