scholarly journals Control of Solvent-Based Post-Combustion Carbon Capture Process with Optimal Operation Conditions

Processes ◽  
2019 ◽  
Vol 7 (6) ◽  
pp. 366 ◽  
Author(s):  
Yih-Hang Chen ◽  
Ming-Tien Shen ◽  
Hsuan Chang ◽  
Chii-Dong Ho

Solvent-based post-combustion carbon capture (PCC) is a mature and essential technology to solve the global warming problem. The high energy consuming issue and the flexible operation required by the power plants inquire about the development of effective control systems for PCC plants. This study proposes the optimal-based control approach that utilizes optimal set-point values for the quality controllers. The five optimal-based control schemes studied all employed L/G (liquid to gas ratio in absorber) as one quality control variable. Performance comparisons with a typical conventional control scheme are conducted employing a rate-based dynamic model for the MEA (monoethanolamine) solvent PCC process developed on a commercial process simulator. Compared to the typical control scheme, the optimal-based control schemes provide faster responses to the disturbance changes from the flue gas conditions and the set-point change of the CO2 capture efficiency, as well as better results in terms of IAEs (integral of absolute errors) of capture efficiency and reboiler heat duty during the stabilization period. LG-Tstr and LG-Tabs-Cascade are the best schemes. In addition to L/G, these two schemes employ the control of Tstr (the temperature of a stage of stripper) and a cascade control of Tabs (the temperature of a stage of absorber) (outer loop) and Tstr (inner loop), respectively.


2018 ◽  
Vol 2018 ◽  
pp. 1-9 ◽  
Author(s):  
M. Al-Dhaifallah ◽  
N. Kanagaraj ◽  
K. S. Nisar

This article presents a fuzzy fractional-order PID (FFOPID) controller scheme for a pneumatic pressure regulating system. The industrial pneumatic pressure systems are having strong dynamic and nonlinearity characteristics; further, these systems come across frequent load variations and external disturbances. Hence, for the smooth and trouble-free operation of the industrial pressure system, an effective control mechanism could be adopted. The objective of this work is to design an intelligent fuzzy-based fractional-order PID control scheme to ensure a robust performance with respect to load variation and external disturbances. A novel model of a pilot pressure regulating system is developed to validate the effectiveness of the proposed control scheme. Simulation studies are carried out in a delayed nonlinear pressure regulating system under different operating conditions using fractional-order PID (FOPID) controller with fuzzy online gain tuning mechanism. The results demonstrate the usefulness of the proposed strategy and confirm the performance improvement for the pneumatic pressure system. To highlight the advantages of the proposed scheme a comparative study with conventional PID and FOPID control schemes is made.



2021 ◽  
Author(s):  
Lisa Ann Brenskelle ◽  
Martin Bermudez Morles ◽  
Lauren Annette Flores

Abstract Slug flow in multiphase flowlines can cause operational instabilities which, when severe, lead to mechanical damage or even shutdown of processing facilities. While a number of control schemes to handle slugging have been published, many of them require subsea instrumentation or make use of calculated "pseudo-variables" for control, values which have no real physical meaning. Hydrodynamic slugging was anticipated during design of a new facility in Angola, and a simulation study demonstrated that a control scheme from the published literature could be applied effectively to control the slugging. However, that solution was rejected because of the use of a pseudo-variable as the principal control point. Therefore, a novel control scheme was developed and tested on simulation for both hydrodynamic slugging and severe riser-induced slugging and later patented.(1,2) The project implemented the novel active slugging control using a topsides control valve and topsides instrumentation. While a pseudo-variable, a pseudo-flow controller, was employed, it was part of a cascade scheme such that the principal control variable was a real topside pressure measurement. Upon commissioning, slugging at the facility was found to be more severe than anticipated during design, but the novel active slug control scheme was effective in controlling incoming slugs.



Author(s):  
Fengyong Sun ◽  
Chunsheng Ji ◽  
Tengfei Zhang

Under supersonic state, the aero-propulsion system exhibits different coupled characters in deceleration from that in acceleration. However, the deceleration control has not been fully studied. In order to solve the coupled problems, an integrated component-level model including inlet and turbofan engine was established. Based on the integrated model, the particularity of inlet adjustment during deceleration was analyzed. And the analyzed results showed that the inlet regulation is not necessary to keep the inlet and engine working in well-matched at any time under supersonic state. Due to the coupled relationship between inlet and turbofan engine, a new optimal integrated control scheme is proposed in this paper. The inlet ramp angle is taken as an optimal control variable as the same as main fuel mass flow and nozzle throat area. The simulation results indicate that inlet ramp angle regulation showed a more effective control quality in the rapid drop of aero-propulsion–installed thrust. Furthermore, the deceleration could be completed in a shorter control time.



2019 ◽  
Vol 93 ◽  
pp. 04002
Author(s):  
Shunxiang Xia ◽  
Enjelia Veony

As biocatalytic carbon capture has attracted wide attraction due to its high energy efficiency, the preference of carbon species of the reaction is concerned. The self-evolution between carbon species makes the determination of preference a changeling issue. In this study, by comparing the isocitrate dehydrogenase reaction rate profiles with pre-equilibrated and un-equilibrated HCO3--CO2 solutions, gas phase carbon dioxide was believed as the optimum substrate, as it can provide higher reaction rate. During the carbon capture process, the partial pressure of the carbon dioxide affected both the reaction equilibrium and kinetics, while the interfacial area can only determine the reaction rate.



2020 ◽  
Author(s):  
Linda Pastero ◽  
Alessandra Marengo ◽  
Davide Bernasconi ◽  
Guido Scarafia ◽  
Alessandro Pavese

<p>Carbon dioxide is a greenhouse gas and a natural component of the atmosphere, essential for plant life. Natural reservoirs (oceans, soils, etc.) regulate its geochemical cycle, but the anthropic activity disturbs this balance. In order to control the concentration of carbon dioxide in the atmosphere, many synergic CO<sub>2</sub> capture and sequestration methods (Aresta and Dibenedetto, 2007; Bachu, 2008; Baker et al., 2007; García-España et al., 2004; Lively et al., 2015; Rosa et al., 2018; Stenhouse et al., 2009)coupled with the reduction of carbon dioxide emissions in the atmosphere, have been proposed.</p><p>In an early paper (Pastero et al., 2019), we proposed the ascorbic acid (vitamin C) as a high-performance and green CO<sub>2</sub> scrubber. We hypothesized a red-ox reaction involving calcium ascorbate as the sacrificial reductant. As a result, the reduction of carbon from C(IV) to C(III) leads to the formation of oxalic acid and, in the presence of calcium as the counterion, to the precipitation of calcium oxalate. Calcium oxalate is an almost insoluble salt that doubles the capture efficiency with respect to calcium carbonate. The reaction’s performance in terms of carbon capture efficiency was evaluated under different experimental conditions. Depending on the experimental setup, the yield of the capture and sequestration reaction reaches very high values, up to 80%. The return of the system depends on the total surface exposed to the reaction, the CO<sub>2</sub>/vitamin C mixing mode, the presence of oxygen in the reaction vessel, and the stoichiometry of the solution.</p><p>The products of the reaction are limited to calcium oxalate dihydrate (weddellite), while no monohydrate (whewellite) or trihydrate (caoxite) oxalates were detected. The chemistry of the system was intentionally kept far from the stability field of the carbonates to avoid the co-precipitation of both calcium carbonate and oxalate and, accordingly, the competition between the two phases on the carbon capture process.</p><p>The technological finalization of a carbon capture system exploiting this reaction will trustfully increase further the effectiveness of the method, pointing towards the zero CO<sub>2</sub> emission.</p><p> </p><p>References</p><p>Aresta, M., Dibenedetto, A., 2007.  Dalt. Trans. 0, 2975. https://doi.org/10.1039/b700658f</p><p>Bachu, S., 2008.  Prog. Energy Combust. Sci. https://doi.org/10.1016/j.pecs.2007.10.001</p><p>Baker, J.M., Ochsner, T.E., Venterea, R.T., Griffis, T.J., 2007. Agric. Ecosyst. Environ. https://doi.org/10.1016/j.agee.2006.05.014</p><p>García-España, E., Gaviña, P., Latorre, J., Soriano, C., Verdejo, B., 2004.  J. Am. Chem. Soc. 126, 5082–5083. https://doi.org/10.1021/ja039577h</p><p>Lively, R.P., Sharma, P., Mccool, B.A., Beaudry-Losique, J., Luo, D., Thomas, V.M., Realff, M., Chance, R.R., 2015. Biofuels, Bioprod. Biorefining 9, 72–81. https://doi.org/10.1002/bbb.1505</p><p>Pastero, L., Curetti, N., Ortenzi, M.A., Schiavoni, M., Destefanis, E., Pavese, A., 2019. Sci. Total Environ. 666, 1232–1244. https://doi.org/10.1016/J.SCITOTENV.2019.02.114</p><p>Rosa, G.M. da, Morais, M.G. de, Costa, J.A.V., 2018. Bioresour. Technol. 261, 206–212. https://doi.org/10.1016/j.biortech.2018.04.007</p><p>Stenhouse, M., Arthur, R., Zhou, W., 2009. In: Energy Procedia. pp. 1895–1902. https://doi.org/10.1016/j.egypro.2009.01.247</p>



2017 ◽  
Vol 142 ◽  
pp. 3505-3510 ◽  
Author(s):  
Peizhi Liao ◽  
Yiguo Li ◽  
Meihong Wang ◽  
Xiao Wu ◽  
Jiong Shen


2012 ◽  
Vol 166-169 ◽  
pp. 2744-2750
Author(s):  
Chang Dong Li ◽  
Xin Li Hu ◽  
Liang Qing Wang ◽  
Qing Tao Liu

With the progressive proceeding of energy pipeline construction, long-distance petroleum and natural gas transmission pipelines were designed to pass through the mountain area of Midwest China, part of them have been threatened by severe landslide hazard. Therefore, the effective control scheme for the exiting pipelines across landslide area has been increasingly interested. A typical landslide in Western China area was taken as an example, from which the interaction model of landslide and pipeline was performed. On the base of the landslide characteristics analysis and numerical modeling, two kinds of typical control schemes, including anti-sliding piles and anchors supporting, were presented to carry out a comparative analysis and evaluation for landslide control. The results show that the scheme involving anti-sliding pile is the better scheme, whose cost and technical requirement are lower than that of anchors supporting scheme in the aspects of cost and the feasibility of construction. This study can provide a scientific basis for the optimal control scheme determination for the landslides with pipeline underground crossing in Western China.



Energies ◽  
2020 ◽  
Vol 14 (1) ◽  
pp. 55
Author(s):  
Nicholas Hawkins ◽  
Bhagyashri Bhagwat ◽  
Michael L. McIntyre

In this paper, a nonlinear controller is proposed to manage the rotational speed of a full-variable Squirrel Cage Induction Generator wind turbine. This control scheme improves upon tractional vector controllers by removing the need for a rotor flux observer. Additionally, the proposed controller manages the performance through turbulent wind conditions by accounting for unmeasurable wind torque dynamics. This model-based approach utilizes a current-based control in place of traditional voltage-mode control and is validated using a Lyapunov-based stability analysis. The proposed scheme is compared to a linear vector controller through simulation results. These results demonstrate that the proposed controller is far more robust to wind turbulence than traditional control schemes.



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