Literatura científica selecionada sobre o tema "Absorption chimique du CO2"
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Artigos de revistas sobre o assunto "Absorption chimique du CO2"
Joly, Lilian, Olivier Coopmann, Vincent Guidard, Thomas Decarpenterie, Nicolas Dumelié, Julien Cousin, Jérémie Burgalat et al. "The development of the Atmospheric Measurements by Ultra-Light Spectrometer (AMULSE) greenhouse gas profiling system and application for satellite retrieval validation". Atmospheric Measurement Techniques 13, n.º 6 (12 de junho de 2020): 3099–118. http://dx.doi.org/10.5194/amt-13-3099-2020.
Texto completo da fonteFriedmann, G., Y. Guilbert e J. M. Catala. "Modification chimique de polymères en milieu CO2 supercritique". European Polymer Journal 36, n.º 1 (janeiro de 2000): 13–20. http://dx.doi.org/10.1016/s0014-3057(99)00011-7.
Texto completo da fonteFdil, F., J. J. Aaron, N. Oturan, A. Chaouch e M. A. Oturan. "Dégradation photochimique d'herbicides chlorophenoxyalcanoïques en milieux aqueux". Revue des sciences de l'eau 16, n.º 1 (12 de abril de 2005): 123–42. http://dx.doi.org/10.7202/705501ar.
Texto completo da fonteYan, Shuiping, Qingyao He, Wenchao Wang e Shefeng Li. "CO2 Absorption Using Biogas Slurry: CO2 Absorption Enhancement Induced by Biomass Ash". Energy Procedia 114 (julho de 2017): 890–97. http://dx.doi.org/10.1016/j.egypro.2017.03.1232.
Texto completo da fonteVilleret, Murielle. "Optical-absorption spectrum ofCdGa2Se4:Co2+". Physical Review B 39, n.º 14 (15 de maio de 1989): 10236–38. http://dx.doi.org/10.1103/physrevb.39.10236.
Texto completo da fonteKim, Hyung-Gon, e Wha-Tek Kim. "Optical absorption ofZnGa2S4andZnGa2S4:Co2+crystals". Physical Review B 41, n.º 12 (15 de abril de 1990): 8541–44. http://dx.doi.org/10.1103/physrevb.41.8541.
Texto completo da fonteNagano, Yatsuhisa, Tetsu Kiyobayashi e Tomoshige Nitta. "CO2 absorption in C60 solid". Chemical Physics Letters 217, n.º 3 (janeiro de 1994): 186–90. http://dx.doi.org/10.1016/0009-2614(94)80005-7.
Texto completo da fonteThamsiriprideeporn, Chanakarn, e Suekane Tetsuya. "Development of CO2 Absorption Using Blended Alkanolamine Absorbents for Multicycle Integrated Absorption–Mineralization". Minerals 13, n.º 4 (30 de março de 2023): 487. http://dx.doi.org/10.3390/min13040487.
Texto completo da fonteLiu, Lili, Yongsheng Ji, Zhanguo Ma, Furong Gao e Zhishan Xu. "Study on the Effects of Ultrasonic Agitation on CO2 Adsorption Efficiency Improvement of Cement Paste". Applied Sciences 11, n.º 15 (26 de julho de 2021): 6877. http://dx.doi.org/10.3390/app11156877.
Texto completo da fonteJin, Mei, Li Yan Zhou, Ping Lu, Jin Huang Wang e Guo Xian Yu. "Performance of MDEA-PZ-TETA for Absorption and Desorption of CO2". Advanced Materials Research 864-867 (dezembro de 2013): 1721–24. http://dx.doi.org/10.4028/www.scientific.net/amr.864-867.1721.
Texto completo da fonteTeses / dissertações sobre o assunto "Absorption chimique du CO2"
Neveux, Thibaut. "Modélisation et optimisation des procédés de captage de CO2 par absorption chimique". Thesis, Université de Lorraine, 2013. http://www.theses.fr/2013LORR0266/document.
Texto completo da fonteCO2 capture processes by chemical absorption lead to a large energy penalty on efficiency of coal-fired power plants, establishing one of the main bottleneck to its industrial deployment. The objective of this thesis is the development and validation of a global methodology, allowing the precise evaluation of the potential of a given amine capture process. Characteristic phenomena of chemical absorption have been thoroughly studied and represented with state-of-the-art models. The e-UNIQUAC model has been used to describe vapor-liquid and chemical equilibria of electrolyte solutions and the model parameters have been identified for four solvents. A rate-based formulation has been adopted for the representation of chemically enhanced heat and mass transfer in columns. The absorption and stripping models have been successfully validated against experimental data from an industrial and a laboratory pilot plants. The influence of the numerous phenomena has been investigated in order to highlight the most limiting ones. A methodology has been proposed to evaluate the total energy penalty resulting from the implementation of a capture process on an advanced supercritical coal-fired power plant, including thermal and electric consumptions. Then, the simulation and process evaluation environments have been coupled with a non-linear optimization algorithm in order to find optimal operating and design parameters with respect to energetic and economic performances
Hasib-ur-Rahman, Muhammad. "CO2 CAPTURE USING ALKANOLAMINE/ROOM-TEMPERATURE IONIC LIQUID BLENDS . Absorption, Regeneration, and Corrosion Aspects". Thesis, Université Laval, 2013. http://www.theses.ulaval.ca/2013/30062/30062.pdf.
Texto completo da fonteGlobal warming, largely resulting from anthropogenic emissions of carbon dioxide, continues to remain a matter of great concern. Carbon capture and storage (CCS) is a viable solution to ensure a prevised fall in CO2 emissions from large point sources involving fossil fuel combustion. In this context, aqueous alkanolamine systems offer a promising near-term solution for CO2 capture from power generation facilities. However, these face several operational hitches such as equilibrium limitations, high regeneration energy requirement, solvent loss, and soaring corrosion occurrence. The main culprit in this respect is water and, accordingly, one feasible practice may be the replacement of aqueous phase with some stable solvent. Room-temperature ionic liquids (RTILs), with high thermal stability and practically no volatility, are emerging as promising aspirants. Moreover, owing to the tunable nature of ionic liquids, RTIL phase can be adapted in accordance with the process requirements. Replacing aqueous phase with RTIL in case of alkanolamine based processes provided a potential opportunity for efficient CO2 capture. The most striking aspect of these schemes was the crystallization of CO2-captured product (carbamate) inside the RTIL phase that not only helped evade equilibrium constraints but also rendered a worthy opportunity of product separation. Since there is little information available in the literature about the viability of amine-RTIL systems, the proposed research was aimed at better understanding CO2 separation proficiency of these fluids through a more systematic approach. Imidazolium RTILs ([Cnmim][Tf2N], [Cnmim][BF4], [Cnmim][Otf]) were chosen for this purpose. Two alkanolamines, 2-amino-2-methyl-1-propanol (AMP) and diethanolamine (DEA) were examined in detail to explore CO2 capture and regeneration capabilities of amine-RTIL systems. The results revealed the superiority of DEA-RTIL combination as this scheme could help significantly narrow the gap between absorption and regeneration temperatures thus promising a sparkling prospect of attenuating energy needs. Furthermore, ionic liquids were scrutinized in reference to their hydrophobic/hydrophilic nature to study the corrosion behaviour of carbon steel in amine-RTIL media. Though hydrophilic ionic liquids helped decrease corrosion occurrence up to 72%, hydrophobic RTIL appeared to be the most effective in this regard, virtually negating the corrosion phenomenon under CO2 rich environment. In case of immiscible blends like DEA-[hmim][Tf2N], continual agitation appeared to be a necessity to ensure a prolonged dispersion of amine in the RTIL phase and, thereby, to attain an optimal capture rate.
Boucif, Noureddine. "Modélisation et simulation de contacteurs membranaires pour les procédés d'absorption de gaz acides par solvant chimique". Thesis, Université de Lorraine, 2012. http://www.theses.fr/2012LORR0280/document.
Texto completo da fonteThe overarching objective of this thesis is the research of mathematical models which are better to describe the process of gas-liquid absorption in a membrane contactor with porous or dense hollow fibers. The geometric configuration of these contactors, combined with their low energy consumption and their compactness, allows them to gradually replace conventional processes such as packing towers and absorption columns. Our goal is to study the performance of these innovative processes by developing more rigorous mathematical models. In this scope, we studied several cases where the hydrodynamics of fluid flow, the nature of the solute or solvent have been changed. First, only the hydrodynamics of the fibre side compartment has been taken into account for two types of an absorption process with and without chemical reaction. Subsequently, the hydrodynamics of fluid flow in both the fiber side as shell side were taken into consideration. Models have been developed for classical carbon dioxide absorption in monoéthanolamine solutions (liquid absorption of reference) where the flow fluid in the shell were is assumed to obey a plug-flow in a first case, described by the surface free model known as "Happel model" in a second case, and finally characterized by the momentum Navier-Stokes equations in a third case. The comparison of the numerically simulated results collected from the three models showed that those of the third case matched very closely with the laboratory experimental results
Cheng, Hao. "Etude d'absorption chimique du dioxyde de carbone : transfert de masse en écoulement diphasique dans un minicanal et conception d'un nouvel absorbeur multicanaux". Electronic Thesis or Diss., Nantes Université, 2024. http://www.theses.fr/2024NANU4030.
Texto completo da fonteMicro/minichannel devices show great interests for their potential in efficient CO2 chemical absorption in the context of the carbon capture. This PhD these aims to characterize and investigate the transport mechanisms involved in chemical reactionaccompanied two-phase mass transfer in minichannel, and to design and develop novel miniaturized CO2 absorbers featuring intensified structures and optimized absorption performances. Firstly, bubble dynamics within a T-junction straight minichannel were optically observed, showing that the chemical reaction tends to suppress bubble breakup while promoting its shrinkage. Then, the velocity field and CO2 concentration field in the liquid slug were determined using PTV and pH-sensitive colorimetry, respectively, permitting the development of a modified unit-cell mass transfer model that incorporates the effects of flow recirculation and chemical reaction. Further enhancement was achieved by embedding a spiral distributed baffle structure into the minichannel, leading to a significant increase in mass transfer coefficient with only a minor rise in pressure drop. Finally, building on this intensification measure, a novel design for an integrated multichannel CO2 absorber was proposed, featuring paralleling units of conjugated double-helix cross minichannels (Codohec). A lab-scale module of this design was realized, and its absorption performance was comprehensively evaluated, highlighting various advantages including a high mass transfer coefficient, acceptable energy consumption, high remove rate, and large CO2 treatment capacity. These findings may provide new insights into the underlying transport mechanisms of chemical reaction-accompanied gas-liquid mass transfer and contribute to the design and optimization of highly efficient miniaturized CO2 absorbers for industry applications
Lacroix, Olivier. "CO2 Capture using immobilized carbonic anhydrase in Robinson-Mahoney basket and packed absorption column reactors". Thesis, Université Laval, 2008. http://www.theses.ulaval.ca/2008/25183/25183.pdf.
Texto completo da fonteServia, Alberto. "Étude cinétique des phénomènes d'activation pour l'absorption de CO2 par des mélanges d'amines". Thesis, Université de Lorraine, 2013. http://www.theses.fr/2013LORR0071.
Texto completo da fonteProcesses based on chemical absorption are widely used for removing CO2 contained in natural gas, hydrogen or flue gas. Mixtures of amines can be used as a solvent for these applications in order to accelerate CO2 mass transfer towards the liquid phase, while keeping a low energy consumption to be regenerated. A methodology has been developed in the framework of this PhD to understand the kinetics of the absorption of CO2 into mixtures of amines. Experimental data provided by a wetted wall column apparatus have been interpreted by a rigorous model taking into account all phenomena occurring within the reactor. This work was firstly dedicated to study the kinetics of the absorption of CO2 by aqueous piperazine solutions. The extrapolation of PZ / CO2 kinetics given by the literature has been validated in a wide range of operating conditions. The kinetics of the absorption of CO2 by mixtures of N-methyldiethanolamine and piperazine has then been assessed. The synergy between both amines at low loading allowing the CO2 mass transfer to be accelerated as well as the impact of the CO2 loading on the absorption kinetics have been quantified. This methodology will be used at IFP Energies nouvelles in order to study the kinetics of the absorption of CO2 by mixtures of amines, in the framework of CO2 postcombustion capture and natural gas treatment processes development. The knowledge of the kinetics of the CO2 absorption by mixtures of amines will allow to enhance the reliability of the absorption column design
Hajj, Ali. "Coupling microwaves with a CO2 desorption process from amine solvent : experimental and modeling approaches". Electronic Thesis or Diss., Ecole nationale supérieure Mines-Télécom Atlantique Bretagne Pays de la Loire, 2024. http://www.theses.fr/2024IMTA0412.
Texto completo da fonteAs global energy needs will continue to be met by fossil-fuel based sources, a viable solution to reduce CO2 emissions would be to implement carbon capture technologies. CO2 capture by absorption in amine solvents ranks among the most advanced technologies to be implemented on post combustion units. Still, its application is remains constrained large point sources with small sources remaining difficult to decarbonize. Recently, microwave heating has gained in popularity due to its characteristics of selectiveness, volumetric nature, and ease of control; on the other hand, membrane contactors are promising gas-liquid contactors due to their compacity, operational flexibility, and ease scalability in comparison to packed columns. In this work we explore the operation of chemical desorption when a hollow fiber membrane contactor by microwave heating.A comprehensive understanding of the interactions of microwave fields and transfer phenomena is essential for the correct design, operation, and optimization of an industrial scale equipment. Hence CO2 desorption rates were experimentally studied at the local scale of a single millimetric fiber, placed in a mono-mode microwave cavity. Numerical modeling of the fiber allowed the visualization of the temperature gradients formed inside the solvent, and the corresponding local desorption rates. In parallel, a prototype-scale unit was designed for the desorption of CO2 at the scale of a hollow fiber module under microwave fields. To this end we designed a custom-design cavity was made to house a membrane module in such a manner that CO2 desorption would take place simultaneously with electromagnetic heating
Elayadi, Houda. "Comparaison physico-chimique et sites catalytiques entre les solides Au/CeO2 préparés par deux méthodes différentes : déposition-précipitation et imprégnation". Littoral, 2010. http://www.theses.fr/2010DUNK0269.
Texto completo da fonteTwo 4%Au/CeO2 catalysts have been prepared by two different methods : deposition-precipitation (DP) and impregnation (Imp). From the XRD, SEM and TEM study, nanoparticles of gold have been evidenced in the DP catalyst and agglomerates nearby nanoparticles in the Imp solid. Compared to the Imp solid, the DP catalyst showed a better catalytic activity in the CO oxidation reaction, the total oxidation of propene and the combustion of carbon black (soots). This difference in the activity is related to the presence of well-dispersed gold nanoparticles on the DP solid surface and a significant quantity of Aun+ located nearby the metallic gold and the O2- ions of the ceria lattice. The weak activity of the Imp catalyst is correlated to the presence on the surface of gold agglomerates and an important amount of chloride ions. These latter species are known as inhibitor in calatysis. In order to elucidate the redox properties of both DP and Imp catalysts, the solids have been degassed and treated under vacuum at 400°C for 1h before the absorption of air. Therefore, the two catalysts have been studied with the EPR technique. Two signals completely different have been evidenced : the first one with g- < g// on DP and the other one, denoted M, with g- > g// on the Imp catalyst. The DP signal has been attributed to O2- species whereas, the attribution of M signal has needed of more detailed study. In fact, the adsorption of air on x%Au/CeO2 (Imp) solids, where 0 <(or egal) x <(or egal) 4, has shown using the EPR technique, the appearance of a new P signal nearby of the M signal for Au contents less than x = 2. 5. From EPR results obtained after absorption, on x%Au/CeO2 (Imp) solids, O2, N2, O2+N2 or air, O2 before N2 ; N2 before O2, NO, N2O and NO2, the P signal has been attributed to O2- , NO2 2- or NO3 2- and M signal M to NO, O- or N2O-. The Nox formed can be considered as intermediate or final products. From these results mechanisms corresponding to all the formed products have been proposed
Rascol, Eva. "Modélisation des transferts entre phases en présence de réactions chimiques : application à l'absorption réactive de CO2 et H2S par des mélanges d'alkanolamines". Toulouse, INPT, 1997. http://www.theses.fr/1997INPT043G.
Texto completo da fonteRadfarnia, Hamid Reza. "High-temperature CO2 sorbents and application in the sorption enhanced steam reforming for hydrogen production". Thesis, Université Laval, 2013. http://www.theses.ulaval.ca/2013/30465/30465.pdf.
Texto completo da fonteSorption-enhanced steam reforming (SESR) is a forefront technology to produce H2 clean fuel, which integrates both CO2 capture and H2 production in a single process. The main objective of this work is to develop novel high-temperature CO2 sorbents and to investigate their application in SESR operation. Special attention was given to lithium zirconate (Li2ZrO3), sodium zirconate (Na2ZrO3) and calcium oxide (CaO)-based materials, as most famous high temperature CO2 sorbents, by applying two novel synthesis techniques. The application of Li2ZrO3 in CO2 capture sorption showed an increase in activity of the material prepared by surfactant template/sonication method compared to Li2ZrO3 prepared by simple surfactant template method (without sonication) or conventional wet-mixing route. Nevertheless, porous Li2ZrO3 still suffered from slow kinetics of CO2 sorption at low CO2 partial pressure (below 0.75 bar), which can limit its application for SESMR operation. Taking into consideration the improvement of Li2ZrO3 sorption properties, the same surfactant template/sonication technique was then applied to develop porous Na2ZrO3. The behavior of the new developed Na2ZrO3 was unexpected. The samples prepared by surfactant template/sonication technique were found to be less active than the conventional Na2ZrO3 during cyclic operation, due to the low resistivity of the pore structure at the very high temperature treatment required for calcination. The same surfactant template/sonication was also applied to develop Zr-stabilized CaO sorbents. An optimum Zr/Ca ratio of 0.303 was found to maximize the stability and CO2 capture activity of the proposed Zr-stabilized CaO sorbent. The results generally showed a better CO2 capture ability of Zr-stabilized CaO sorbent in comparison with pure CaO in severe cyclic operating conditions. With the purpose of reducing the cost of sorbent production, a cheaper source of CaO (natural limestone) was also considered and a novel synthesis technique (limestone acidification by citric acid followed by two-step calcination (in Ar and air atmospheres)) was applied in order to prepare highly porous CaO structure with unique CO2 capture ability. The results revealed a much better stability and CO2 sorption activity of the developed sorbent compared to natural limestone. The same technique was employed to develop a number of metal oxide (Al, Zr, Mg and Y)-stabilized CaO sorbents in order to enhance sorbent stability in severe operating conditions, i.e., high temperature regeneration in the presence of CO2. Al and Zr-stabilized CaO showed the best activity during both mild and severe operating conditions. The performance of the developed CO2 sorbents providing the best performance in CO2 capture (Zr-stabilized and Al-stabilized CaO) were then investigated experimentally in the sorption enhanced steam methane reforming (SESMR) using a fixed-bed reactor. To minimize the diffusional limitations, a hybrid catalyst-sorbent was developed for both sorbents. The application of Zr-stabilized CaO-nickel hybrid catalyst with 20.5 wt% NiO loading, prepared by surfactant-template/sonication method, resulted in 92% H2 production efficiency for the initial SESMR cycle, which is remarkably higher than traditional steam methane reforming (SMR) equilibrium H2 yield (70 %). The second developed hybrid sorbent-catalyst (Al-stabilized CaO-NiO) was prepared using limestone acidification coupled with two-step calcination technique. The long-term application of the hybrid catalyst containing 25 wt% NiO led to an average H2 production efficiency of 97.3%, proving its high efficiency in the SESMR process. In summary, the results of this thesis show that the SESR process is as an efficient alternative of traditional steam reforming for production of highly pure H2. The Al-stabilized CaO-NiO hybrid sorbent-catalyst showed an excellent activity over long-term operation, thus confirming its very high potential for use in the SESMR process.
Livros sobre o assunto "Absorption chimique du CO2"
Madeddu, Claudio, Massimiliano Errico e Roberto Baratti. CO2 Capture by Reactive Absorption-Stripping. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-04579-1.
Texto completo da fonteBudzianowski, Wojciech M., ed. Energy Efficient Solvents for CO2 Capture by Gas-Liquid Absorption. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/978-3-319-47262-1.
Texto completo da fonteMadeddu, Claudio, Massimiliano Errico e Roberto Baratti. CO2 Capture by Reactive Absorption-Stripping: Modeling, Analysis and Design. Springer, 2019.
Encontre o texto completo da fonteNakao, Shin-ichi, Katsunori Yogo, Kazuya Goto, Teruhiko Kai e Hidetaka Yamada. Advanced CO2 Capture Technologies: Absorption, Adsorption, and Membrane Separation Methods. Springer, 2019.
Encontre o texto completo da fonteBudzianowski, Wojciech M. Energy Efficient Solvents for CO2 Capture by Gas-Liquid Absorption: Compounds, Blends and Advanced Solvent Systems. Springer, 2018.
Encontre o texto completo da fonteBudzianowski, Wojciech M. Energy Efficient Solvents for CO2 Capture by Gas-Liquid Absorption: Compounds, Blends and Advanced Solvent Systems. Springer, 2016.
Encontre o texto completo da fonteBudzianowski, Wojciech M. Energy Efficient Solvents for CO2 Capture by Gas-Liquid Absorption: Compounds, Blends and Advanced Solvent Systems. Springer, 2017.
Encontre o texto completo da fonteAdsorption Analysis: Equilibria and Kinetics (Chemical Engineer Series, Volume 2). Imperial College Press, 1998.
Encontre o texto completo da fonteAdsorption Analysis: Equilibria and Kinetics. Imperial College Pr, 1998.
Encontre o texto completo da fonteAdsorption Analysis: Equilibria and Kinetics (Series on Chemical Engineering, Vol 2). World Scientific Publishing Company, 1998.
Encontre o texto completo da fonteCapítulos de livros sobre o assunto "Absorption chimique du CO2"
Vega, Fernando, Luz Marina Gallego-Fernández, David Abad-Correa e Francisco Manuel Baena-Moreno. "Advanced Fluids in Chemical Absorption of CO2". In Advanced Materials for a Sustainable Environment, 271–91. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/9781003206385-12.
Texto completo da fonteYu, W., T. Wang, M. X. Fang, H. Hei e Z. Y. Luo. "CO2 Absorption/Desorption Enhanced by Nanoparticles in Post-combustion CO2 Capture". In Clean Coal Technology and Sustainable Development, 591–96. Singapore: Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-10-2023-0_80.
Texto completo da fontePantoleontos, G., S. P. Kaldis, D. Koutsonikolas, P. Grammelis e G. P. Sakellaropoulos. "CO2 Absorption in a Mini-module Membrane Contactor". In Global Warming, 307–13. Boston, MA: Springer US, 2009. http://dx.doi.org/10.1007/978-1-4419-1017-2_18.
Texto completo da fontePuxty, Graeme, Marcel Maeder e Robert Bennett. "Reactive Chemical Absorption of CO2 by Organic Molecules". In Sustainable Carbon Capture, 29–71. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/9781003162780-2.
Texto completo da fonteSonawane, Shriram S., e Parag P. Thakur. "Applications of Nanofluids for the CO2 Absorption Process". In Nanofluids, 93–117. Boca Raton: CRC Press, 2024. http://dx.doi.org/10.1201/9781003404767-5.
Texto completo da fonteOrhan, Ozge Yuksel, Cyril Sunday Ume e Erdogan Alper. "The Absorption Kinetics of CO2 into Ionic Liquid—CO2 Binding Organic Liquid and Hybrid Solvents". In Green Energy and Technology, 241–61. Cham: Springer International Publishing, 2016. http://dx.doi.org/10.1007/978-3-319-47262-1_11.
Texto completo da fonteIsa, Faezah, Haslinda Zabiri, Salvinder Kaur Marik Singh e Azmi M. Shariff. "Dynamic Modelling for High Pressure CO2 Absorption from Natural Gas". In Communications in Computer and Information Science, 261–71. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-6502-6_23.
Texto completo da fonteNoroozi, Javad, William R. Smith, William R. Smith, William R. Smith e William R. Smith. "Molecular Simulation of pK Values and CO2 Reactive Absorption Prediction". In The Three Sisters, 185–91. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2019. http://dx.doi.org/10.1002/9781119510079.ch9.
Texto completo da fonteVishal Reddy, P., e Praveen Kumar Ghodke. "Design and Modeling of CO2 Absorption Column for Carbon Sequestration". In Lecture Notes in Mechanical Engineering, 25–34. Singapore: Springer Nature Singapore, 2024. http://dx.doi.org/10.1007/978-981-99-5990-7_3.
Texto completo da fonteSrinivasan, K., e M. C. Sashikkumar. "Behavioural Study on Concrete with Organic Materials for CO2 Absorption". In Proceedings of International Conference on Innovative Technologies for Clean and Sustainable Development (ICITCSD – 2021), 201–15. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-030-93936-6_17.
Texto completo da fonteTrabalhos de conferências sobre o assunto "Absorption chimique du CO2"
Zhu, Dongdong, Neng Guo, Xueyong Kou, Shuaipeng Li, Shengwen Chen e Zhiguo Sun. "CO2 absorption by diethanolamine mixed with sodium humate". In Fifth International Conference on Green Energy, Environment, and Sustainable Development, editado por Mohammadreza Aghaei, Hongyu Ren e Xiaoshuan Zhang, 76. SPIE, 2024. http://dx.doi.org/10.1117/12.3044497.
Texto completo da fonteGuo, Neng, Dongdong Zhu, Xueyong Kou, Shuaipeng Li, Shengwen Chen e Zhiguo Sun. "Improvement CO2 absorption of calcium-based by zirconia/alumina". In Fifth International Conference on Green Energy, Environment, and Sustainable Development, editado por Mohammadreza Aghaei, Hongyu Ren e Xiaoshuan Zhang, 57. SPIE, 2024. http://dx.doi.org/10.1117/12.3044455.
Texto completo da fontezhang, fengrui, jun ma e lei wang. "SVMD-based denoising methods for differential absorption lidar retrieval of CO2 concentration profiles". In Fourth International Conference on Optics and Communication Technology (ICOCT 2024), editado por Yang Zhao e Yongjun Xu, 29. SPIE, 2024. http://dx.doi.org/10.1117/12.3049764.
Texto completo da fonteEckel, Hans-Albert. "CO2 Laser Absorption in Ablation Plasmas". In BEAMED ENERGY PROPULSION: Fourth International Symposium on Beamed Energy Propulsion. AIP, 2006. http://dx.doi.org/10.1063/1.2203270.
Texto completo da fonteKang, Yong Tae, e Seonggon Kim. "CO2 ABSORPTION/REGENERATION PERFORMANCE ENHANCEMENT BY NANOABSORBENTS". In International Heat Transfer Conference 16. Connecticut: Begellhouse, 2018. http://dx.doi.org/10.1615/ihtc16.kn.000019.
Texto completo da fonteHao Zhiwu, Li Fangqin, Li Henan e Li Yanchao. "Progress of absorption CO2 by membrane contactor". In Environment (ICMREE). IEEE, 2011. http://dx.doi.org/10.1109/icmree.2011.5930614.
Texto completo da fonteVasil'ev, B. I., e O. M. Mannoun. "Differential absorption lidar using NH3-CO2 laser". In 2006 Conference on Lasers and Electro-Optics and 2006 Quantum Electronics and Laser Science Conference. IEEE, 2006. http://dx.doi.org/10.1109/cleo.2006.4628086.
Texto completo da fonte"Studies on CO2 absorption using humic substances". In Seventh International Conference on Humic Innovative Technologies "Humic substances and technologies for resilience" (HIT – 2022). NP CBR "Humus Sapiens", 2022. http://dx.doi.org/10.36291/hit.2022.002.
Texto completo da fonteQi, Na, Zhenting Wang e Tianhao Zhang. "A high stability infrared absorption CO2 sensor". In 6th International Conference on Mechatronics and Intelligent Robotics, editado por Srikanta Patnaik e Tao Shen. SPIE, 2022. http://dx.doi.org/10.1117/12.2644524.
Texto completo da fonteKarali, Dimitra, Konstantina Peloriadi, Nikolaos Margaritis e Panagiotis Grammelis. "CO2 Absorption Using Potassium Carbonate as Solvent". In ASEC 2022. Basel Switzerland: MDPI, 2022. http://dx.doi.org/10.3390/asec2022-13824.
Texto completo da fonteRelatórios de organizações sobre o assunto "Absorption chimique du CO2"
Jiang, C., e X. Zhang. Direct lithium extraction from raw and CO2-mineralization treated oilfield brine using an electrochemically assisted lithium-ion sieve: a preliminary feasibility study. Natural Resources Canada/CMSS/Information Management, 2024. https://doi.org/10.4095/pwwq3wrg5m.
Texto completo da fonteGary T. Rochelle, Andrew Sexton, Jason Davis, Marcus Hilliard, Qing Xu, David Van Wagener e Jorge M. Plaza. CO2 Capture by Absorption with Potassium Carbonate. Office of Scientific and Technical Information (OSTI), março de 2007. http://dx.doi.org/10.2172/907880.
Texto completo da fonteGary T. Rochelle, Eric Chen, Babatunde Oyenekan, Andrew Sexton, Jason Davis, Marcus Hilliard e Amornvadee Veawab. CO2 Capture by Absorption with Potassium Carbonate. Office of Scientific and Technical Information (OSTI), setembro de 2006. http://dx.doi.org/10.2172/895539.
Texto completo da fonteGary T. Rochelle, Eric Chen, Babatunde Oyenekan, Andrew Sexton, Jason Davis, Marus Hiilliard, Qing Xu, David Van Wagener e Jorge M. Plaza. CO2 Capture by Absorption with Potassium Carbonate. US: University Of Texas At Austin, dezembro de 2006. http://dx.doi.org/10.2172/899120.
Texto completo da fonteGary T. Rochelle, Eric Chen, Babatunde Oyenekan, Andrew Sexton e Amorvadee Veawab. CO2 Capture by Absorption with Potassium Carbonate. Office of Scientific and Technical Information (OSTI), abril de 2006. http://dx.doi.org/10.2172/882401.
Texto completo da fonteGary T. Rochelle, Eric Chen, Babatunde Oyenekan, Andrew Sexton, Jason Davis, Marcus Hilliard e Amorvadee Veawab. CO2 Capture by Absorption with Potassium Carbonate. Office of Scientific and Technical Information (OSTI), julho de 2006. http://dx.doi.org/10.2172/889472.
Texto completo da fonteRochelle, Gary T., Frank Seibert, Fred Closmann, Tim Cullinane, Jason Davis, George Goff, Marcus Hilliard et al. CO2 Capture by Absorption with Potassium Carbonate. Office of Scientific and Technical Information (OSTI), agosto de 2007. http://dx.doi.org/10.2172/922797.
Texto completo da fonteGary T. Rochelle, Eric Chen, Jennifer Lu, Babatunde Oyenekan e Ross Dugas. CO2 CAPTURE BY ABSORPTION WITH POTASSIUM CARBONATE. Office of Scientific and Technical Information (OSTI), novembro de 2004. http://dx.doi.org/10.2172/835452.
Texto completo da fonteGary T. Rochelle, Eric Chen, J.Tim Cullinane, Marcus Hilliard, Jennifer Lu, Babatunde Oyenekan e Ross Dugas. CO2 CAPTURE BY ABSORPTION WITH POTASSIUM CARBONATE. Office of Scientific and Technical Information (OSTI), julho de 2004. http://dx.doi.org/10.2172/829575.
Texto completo da fonteGary T. Rochelle, Eric Chen, Jennifer Lu, Babatunde Oyenekan e Ross Dugas. CO2 CAPTURE BY ABSORPTION WITH POTASSIUM CARBONATE. Office of Scientific and Technical Information (OSTI), abril de 2005. http://dx.doi.org/10.2172/840473.
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