Evaluating the Performance of a Newly Developed Carbon Capture Device for Mobile Emission Sources

2017 ◽  
Vol 139 (6) ◽  
Author(s):  
Samer F. Ahmed ◽  
Mert Atilhan

In the present study, a new carbon capture device that can be carried on-board vehicles has been developed and tested. The developed device uses absorption and adsorption methods of postcombustion CO2 capture. Sodium hydroxide (NaOH) pellets and calcium hydroxide Ca(OH)2 have been used as solvents and sorbents in the device. The CO2 capture efficiency has been evaluated at a wide range of operating conditions. The results showed that the higher the concentration of the solvent, the higher the capture efficiency, i.e., w 100% capture efficiency, being obtained at full saturation of NaOH. In addition, the increase in the solution temperature increases the capture efficiency up to 50 °C. Design of the gas distributer in the device has also a notable effect on CO2 capture. It was found that solvent prepared with seawater can provide high capture efficiency over a wide range of operation, but in general, it has a lower capture efficiency than that prepared by tap water. Moreover, solvents prepared by NaOH have a superior CO2 capture efficiency over those prepared by Ca(OH)2. For the adsorption technique, a 50% NaOH and 50% Ca(OH) mixture by mass has provided the highest capture efficiency compared with each sorbent when used alone.

Energies ◽  
2020 ◽  
Vol 13 (5) ◽  
pp. 1171 ◽  
Author(s):  
Christopher Otto ◽  
Thomas Kempka

Underground coal gasification (UCG) is an in situ conversion technique that enables the production of high-calorific synthesis gas from resources that are economically not minable by conventional methods. A broad range of end-use options is available for the synthesis gas, including fuels and chemical feedstock production. Furthermore, UCG also offers a high potential for integration with Carbon Capture and Storage (CCS) to mitigate greenhouse gas emissions. In the present study, a stoichiometric equilibrium model, based on minimization of the Gibbs function has been used to estimate the equilibrium composition of the synthesis gas. Thereto, we further developed and applied a proven thermodynamic equilibrium model to simulate the relevant thermochemical coal conversion processes (pyrolysis and gasification). Our modeling approach has been validated against thermodynamic models, laboratory gasification experiments and UCG field trial data reported in the literature. The synthesis gas compositions have been found to be in good agreement under a wide range of different operating conditions. Consequently, the presented modeling approach enables an efficient quantification of synthesis gas quality resulting from UCG, considering varying coal and oxidizer compositions at deposit-specific pressures and temperatures.


Clean Energy ◽  
2021 ◽  
Vol 5 (4) ◽  
pp. 742-755
Author(s):  
Qian Cui ◽  
Baodeng Wang ◽  
Xinglei Zhao ◽  
Guoping Zhang ◽  
Zhendong He ◽  
...  

Abstract Membrane-based separation technologies have the potential to lower the cost of post-combustion CO2 capture from power-plant flue gases through reduced energy and capital costs relative to conventional solvent approaches. Studies have shown promise under controlled conditions, but there is a need for data on performance and reliability under field conditions. Coal-fired power plants in China operate in a dynamic manner, with increases and decreases in output causing changes in flue-gas composition. In this paper, we describe the first field test of a membrane-based post-combustion CO2-capture system connected to a dynamically operating power plant in China. We report the performance of a Membrane Technology Research, Inc. (MTR) PolarisTM membrane-based capture system over a range of plant operating loads ranging from 54% to 84% and conducted an operational stability test over a 168-h period during which the power plant was operating at an average load of 55%, but ramped as high as 79% and as low as 55%. Our results confirm the ability of a membrane capture system to operate effectively over a wide range of host-plant operating conditions, but also identity several issues related to plant integration, system control and resilience in the face of host-plant upsets that require attention as membrane separation systems move towards commercial use.


2021 ◽  
Author(s):  
Amélie Cécile Martin ◽  
François Lacouture ◽  
Philip Llewellyn ◽  
Laurent Mariac

Abstract To curtail the global warming increase to less than 2°C by 2050, the IPCC highlights Carbon Capture Utilization and Storage (CCUS) as a vital approach. TotalEnergies, following its ambition to become a responsible energy major, invests 10% of its R&D budget in CCUS to reduce the global process cost and help decarbonize our activities. TotalEnergies is both working to decarbonize its own assets and developing a transport and storage infrastructure in Europe, with notably Northern Lights an example of note. It is equally of interest how this transport/storage infrastructure can be of use for other sectors and as such how various full CCUS chains may emerge. This explains the interest to develop techno-economic tools to evaluate CO2 capture processes applied to a wide range of industries. CO2 that is an integral part of the manufacturing process, is particularly difficult to abate in any future scenario, and one particular industry, which is facing such a challenge is the cement sector. CCUS has been identified as a potential solution to help with this issue. The present paper outlines the outcomes of a techno-economic study evaluating CO2 capture technologies based on cement factory retrofitting. A literature review aimed at identifying the main characteristics of a typical European cement plant (capacity, process mode, pollutant composition in the flue gas…) was carried out. In this paper, a base case scenario of 90% absorption-based CO2 capture with monoethanolamine (MEA) is compared with four alternative CO2 capture approaches: –An absorption technology based on non-amine solvent.–An adsorption technology based on a Concentration Swing Adsorption process.–An oxyfuel technology derived from the R&D works performed during the CEMCAP project (European CO2 capture project).–A Calcium Looping technology with tail-end process configuration. For each of these approaches, the whole carbon capture chain has been considered: this includes flue gas pretreatment, CO2 conditioning (including compression), steam generation, and utilities. Using process simulations, engineering studies have been carried out and have provided Key Performance Indicators (KPIs) such as Capital Costs, Operation Costs and Global Warming Potential (primary energy consumption per ton of CO2 avoided). It enabled mapping the technologies with regards to the cost and volume of CO2 avoided, as well as providing for each of the technologies the break-even point for an eventual CO2 tax. Based on these KPIs, several facts have been highlighted: –The need to consider the whole process (including utilities, compression…) and not only the capture unit.–The development of new materials for adsorption and contactor design is already driving down costs.–The availability of waste heat can be a game-changer to implement a CO2 capture technology.–Technology comparisons are location and site-specific and cannot be taken as a basis for concept selection. TotalEnergies approach to CCUS is collaborative. With these full-scale techno-economical assessments, generated via quotations from industrial equipment providers and using Engineering, Procurement and Construction standards, this not only gives a basis for comparison, but also assists our discussions with partners to identify key technological development pathways.


2020 ◽  
Author(s):  
Kasturi Nagesh Pai ◽  
Vinay Prasad ◽  
Arvind Rajendran

Practically achievable limits for pressure-vacuum swing adsorption (PVSA)-based post-combustion carbon capture are evaluated. The adsorption isotherms of CO2 and N2 are described by competitive Langmuir isotherms. Two low-energy process cycles are considered and a machine learning surrogate-model is trained with inputs from an experimentally-validated detailed PVSA model. Several case studies are considered to evaluate two critical performance indicators, namely, minimum energy and maximum productivity. For each case study, the genetic algorithm optimizer that is coupled to the machine learning surrogate model, searches tens of thousands of combinations of isotherms and process operating conditions. The framework pairs the optimum material properties with the optimum operating conditions, hence providing the limits of achievable performance. The results indicate that very low pressures ( <~0.2 bar) may be required to achieve process constraints for low feeds with low feed compositions ($<0.15$ mol fraction), indicating that PVSA may not be favourable. At higher CO2 feed compositions, PVSA can be attractive and can be operated at practically achievable vacuum levels. Further, the gap between the energy consumption of available adsorbents and the achievable limits with a hypothetical -best adsorbent varies between 20% to 2.5% as the CO2 feed composition changes between 0.05 to 0.4. This indicates a limited potential for development of new adsorbents of PVSA-based CO2 capture. Future work for PVSA should focus on flue gas streams with high CO2 compositions


2020 ◽  
Author(s):  
Kasturi Nagesh Pai ◽  
Vinay Prasad ◽  
Arvind Rajendran

Practically achievable limits for pressure-vacuum swing adsorption (PVSA)-based post-combustion carbon capture are evaluated. The adsorption isotherms of CO2 and N2 are described by competitive Langmuir isotherms. Two low-energy process cycles are considered and a machine learning surrogate-model is trained with inputs from an experimentally-validated detailed PVSA model. Several case studies are considered to evaluate two critical performance indicators, namely, minimum energy and maximum productivity. For each case study, the genetic algorithm optimizer that is coupled to the machine learning surrogate model, searches tens of thousands of combinations of isotherms and process operating conditions. The framework pairs the optimum material properties with the optimum operating conditions, hence providing the limits of achievable performance. The results indicate that very low pressures ( <~0.2 bar) may be required to achieve process constraints for low feeds with low feed compositions ($<0.15$ mol fraction), indicating that PVSA may not be favourable. At higher CO2 feed compositions, PVSA can be attractive and can be operated at practically achievable vacuum levels. Further, the gap between the energy consumption of available adsorbents and the achievable limits with a hypothetical -best adsorbent varies between 20% to 2.5% as the CO2 feed composition changes between 0.05 to 0.4. This indicates a limited potential for development of new adsorbents of PVSA-based CO2 capture. Future work for PVSA should focus on flue gas streams with high CO2 compositions


2020 ◽  
Vol 8 (3) ◽  
pp. 1-7
Author(s):  
Aya Ayad Hussein ◽  
Rajaaaldeen Abd Khalid

Global warming due to greenhouse gases has become a serious global issue. Extensive efforts are being made to fighting this phenomenon through carbon capture as carbon dioxide (CO2) is its major contributor. This study focused on CO2 capture in packed bed column reactor using Poly-(D) glucosamine under the various process parameters such as temperature, feed flow rate and mass of the adsorbent. Statistical design of experiments was carried out in order to analysis the effect process parameters on the capacity of CO2 capture in packed bed column. The obtained results show that feed flow rate has the significant affect compared to others. The maximum of 956 mg of CO2 is captured under the following operating conditions; temperature of 40oC, feed flow rate of 30 ml/min and 0.25 g of the Poly-(D) glucosamine. The ability of Poly-(D) glucosamine to capture the CO2 in packed bed column is confirmed.


2016 ◽  
Vol 192 ◽  
pp. 459-477 ◽  
Author(s):  
Yue Zhang ◽  
Brice Freeman ◽  
Pingjiao Hao ◽  
Gary T. Rochelle

A hybrid system combining amine scrubbing with membrane technology for carbon capture from natural gas combined cycle (NGCC) power plants is proposed in this paper. In this process, the CO2 in the flue gas can be enriched from 4% to 18% by the membrane, and the amine scrubbing system will have lower capture costs. Aqueous piperazine (PZ) is chosen as the solvent. Different direct contact cooler (DCC) options, multiple absorber operating conditions, optimal intercooling designs, and different cooling options have been evaluated across a wide range of inlet CO2. Amine scrubbing without DCC is a superior design for NGCC carbon capture. Pump-around cooling at the bottom of the absorber can effectively manage the temperature of the hot flue gas, and still be effective for CO2 absorption. The absorber gas inlet must be designed to avoid excessive localized temperature and solvent evaporation. When the inlet CO2 increases from 4% to 18%, total absorber CAPEX decreases by 60%; another 10% of the total absorber CAPEX can be saved by eliminating the DCC. In-and-out intercooling works well for high CO2, while pump-around intercooling is more effective for low CO2. Dry cooling requires more packing and energy but appears to be technically and economically feasible if cooling water availability is limited.


2021 ◽  
Vol 11 (13) ◽  
pp. 6021
Author(s):  
Shinje Lee ◽  
Hyun Seung Kim ◽  
Junhyung Park ◽  
Boo Min Kang ◽  
Churl-Hee Cho ◽  
...  

Steam methane reforming (SMR) process is regarded as a viable option to satisfy the growing demand for hydrogen, mainly because of its capability for the mass production of hydrogen and the maturity of the technology. In this study, an economically optimal process configuration of SMR is proposed by investigating six scenarios with different design and operating conditions, including CO2 emission permits and CO2 capture and sale. Of the six scenarios, the process configuration involving CO2 capture and sale is the most economical, with an H2 production cost of $1.80/kg-H2. A wide range of economic analyses is performed to identify the tradeoffs and cost drivers of the SMR process in the economically optimal scenario. Depending on the CO2 selling price and the CO2 capture cost, the economic feasibility of the SMR-based H2 production process can be further improved.


Author(s):  
David A. Ansley

The coherence of the electron flux of a transmission electron microscope (TEM) limits the direct application of deconvolution techniques which have been used successfully on unmanned spacecraft programs. The theory assumes noncoherent illumination. Deconvolution of a TEM micrograph will, therefore, in general produce spurious detail rather than improved resolution.A primary goal of our research is to study the performance of several types of linear spatial filters as a function of specimen contrast, phase, and coherence. We have, therefore, developed a one-dimensional analysis and plotting program to simulate a wide 'range of operating conditions of the TEM, including adjustment of the:(1) Specimen amplitude, phase, and separation(2) Illumination wavelength, half-angle, and tilt(3) Objective lens focal length and aperture width(4) Spherical aberration, defocus, and chromatic aberration focus shift(5) Detector gamma, additive, and multiplicative noise constants(6) Type of spatial filter: linear cosine, linear sine, or deterministic


2020 ◽  
Author(s):  
Nayyereh hatefi ◽  
William Smith

<div>Ideal{gas thermochemical properties (enthalpy, entropy, Gibbs energy, and heat capacity, Cp) of 49 alkanolamines potentially suitable for CO2 capture applications and their carbamate and protonated forms were calculated using two high{order electronic structure methods, G4 and G3B3 (or G3//B3LYP). We also calculate for comparison results from the commonly used B3LYP/aug-cc-pVTZ method. This data is useful for the construction of molecular{based thermodynamic models of CO2 capture processes involving these species. The Cp data for each species over the temperature range 200 K{1500 K is presented as functions of temperature in the form of NASA seven-term polynomial expressions, permitting the set of thermochemical properties to be calculated over this temperature range. The accuracy of the G3B3 and G4 results is estimated to be 1 kcal/mol and the B3LYP/aug-cc-pVTZ results are of nferior quality..</div>


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