Author: Publisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Corrosion and Corrosion Control in CO2 Absorption Process Using Aqueous Amine Solutions
Author: Post-combustion CO2 Capture Technology
Author: Helei LiuPublisher: Springer
ISBN: 303000922X
Category : Technology & Engineering
Languages : en
Pages : 55
Book Description
This book presents a comprehensive review of the latest information on all aspects of the post-combustion carbon capture process. It provides designers and operators of amine solvent-based CO2 capture plants with an in-depth understanding of the most up-to-date fundamental chemistry and physics of the CO2 absorption technologies using amine-based reactive solvents. Topics covered include the physical properties, chemical analysis, reaction kinetics, CO2 solubility, and innovative configurations of absorption and stripping columns as well as information on technology applications. This book also examines the post-build operational issues of corrosion prevention and control, solvent management, solvent stability, solvent recycling and reclaiming, intelligent monitoring and plant control including process automation. In addition, the authors discuss the recent insights into the theoretical basis of plant operation in terms of thermodynamics, transport phenomena, chemical reaction kinetics/engineering, interfacial phenomena, and materials. The insights provided help engineers, scientists, and decision makers working in academia, industry and government gain a better understanding of post-combustion carbon capture technologies.
Corrosion in CO2 Absorption Process Using Aqueous Monoethanolamine/piperazine Solution
Author: Manjula NainarPublisher:
ISBN:
Category : Amines
Languages : en
Pages : 312
Book Description
This work explores the promise of aqueous solutions of blended monoethanolamine (MEA) and piperazine (PZ) as a cost-effective solvent for carbon dioxide (CO2) capture from industrial flue gas streams with respect to addressing corrosion, which is regarded as one of the most severe operational problems in typical CO2 capture plants. Two types of corrosion experiments were carried out in bench-scale setups, electrochemical tests for short-term exposure and weight loss tests for long-term exposure. The results show that the blended MEA/PZ solutions are more corrosive than the MEA solutions. The corrosion rate of carbon steel increases with concentration of PZ, total amine concentration, CO2 loading of solution, solution temperature, the presence of heat stable salts, and the presence of the proprietary oxidative degradation inhibitor (Inhibitor A provided by the University of Texas at Austin). Among the tested heat-stable salts, formate is the most corrosive salt, followed by acetate, oxalate, and thiosulfate in the absence of oxygen (O2), while acetate is the most corrosive salt followed by formate, oxalate, and thiosulfate in the presence of O2. Based on the level of corrosion rate found in the MEA/PZ system, corrosion control is required during plant operation to suppress the corrosion rate of carbon steel to below an acceptable level. Sodium metavanadate (NaVO3) and copper carbonate (CuCO3) were proven to be effective corrosion inhibitors with inhibition performance of up to 94-98%. Dissolved O2 is required in the solution to maintain active Cu2 or V5+, which, thus, prevents the metallic copper (Cu) from plating out or the formation of other oxidative states of vanadate. The performance of these two inhibitors can be deteriorated by the presence of heat-stable salts in the solutions.
Corrosion of Stainless and Carbon Steel in Aqueous Amine for CO2 Capture
Author: Kent Billington FischerPublisher:
ISBN:
Category :
Languages : en
Pages : 448
Book Description
Post-combustion carbon capture and storage with amine absorbents is a key technology needed to provide low-cost decarbonized electricity. Improving understanding of corrosion by amines may reveal a solvent system compatible with carbon steel, which would reduce plant capital costs. Corrosion of stainless and carbon steel in aqueous monoethanolamine (MEA) and piperazine (PZ) has been measured. High temperature amine corrosion was measured in a bench-scale pressure vessel and iron solubility in amines was screened in stirred reactors. Corrosion was measured at two PZ pilot plants and one MEA pilot plant, using coupons and electrical resistance probes. Corrosion products were characterized by SEM and powder X-ray diffraction. Carbon steel (C1010) often performs well in 5 molal PZ up to 150 °C due to the formation of a passivating FeCO3 layer. This layer is promoted at high temperature, high CO2 loading, low solution velocity, and in amines with low Fe2+ solubility. FeCO3 formation is favorable at high temperature because Fe2+ solubility decreases and the kinetics of FeCO3 formation are faster. This also means that FeCO3 is not observed at low temperature. Despite this, carbon steel performs well at low temperature due to slower kinetics of metal oxidation. Depassivation and high corrosion of stainless steel (316L) can occur in amine solutions at high temperature (150 °C) when conditions are relatively anoxic and reducing. Performance of stainless at high temperature in PZ suggests that it can be pushed into and out of the passive state by small process changes, such as different flue gas O2 concentrations. However, stainless performs well in both MEA and PZ in pilot plants at ≈120 °C. Fe3+ corrosion products are generated in the absorber, then reduced to Fe2+ in the high temperature, anoxic conditions of the stripper. In this way, carried-over Fe3+ is responsible for oxidation of amine and corrosion at high temperature. Certain highly corrosive amines also have high Fe2+ solubility. Ethylamines like MEA are likely the correct chain length to form stable complexes with Fe2+ in solution. Stable Fe2+-amine complexes cause high Fe2+ solubility, which prevents FeCO3 formation and leads to high corrosion
Corrosion Evaluation for Absorption - Based CO2 Capture Process Using Single and Blended Amines
Author: Prakashpathi GunasekaranPublisher:
ISBN:
Category :
Languages : en
Pages :
Book Description
Environmentally-Friendly Corrosion Inhibitors for the Amine-Based CO2 Absorption Process
Author: Sureshkumar SrinivasanCorrosion Inhibition Performance of Copper Carbonate in CO2 Absorption Process Using Aqueous Solution of Monoethanolamine
Author: Immanuelraj SoosaiprakasamPublisher:
ISBN:
Category : Carbon dioxide mitigation
Languages : en
Pages : 292
Book Description
Corrosion is one of the most severe operational problems in CO2 absorption processes, which use aqueous solutions of alkanolamines, especially when carbon steel is used for plant construction. Corrosion inhibitors are widely applied used in this process to suppress severe corrosion to an acceptable level. However, currently available corrosion inhibitors are heavy metals, which are toxic to human health and the environment, making solvent handling and waste disposal more difficult and costly. This work evaluated a low-toxic corrosion inhibitor, copper carbonate (CuCO3), as a replacement for toxic corrosion inhibitors. An inhibition evaluation was performed on copper carbonate by examining its parametric effects on the corrosion rate and corrosion behavior of carbon steel.
Corrosion of Stainless and Carbon Steel in Aqueous Piperazine for CO2 Capture
Author: Ching-Ting LiuPublisher:
ISBN:
Category :
Languages : en
Pages : 0
Book Description
Current obstacles that prevent commercial implementation of amine-scrubbing CO2 capture are the high costs. Reducing capital costs by appropriate selection of construction materials, which requires knowledge of material corrosion performance for the process, will improve the economic feasibility of this technology. Corrosion was evaluated in three pilot plant campaigns using aqueous piperazine with the Advanced Stripper (PZAS). 316L stainless steel (SS) experienced higher corrosion than 304 SS and 2205 duplex SS, and the corrosion rate showed strong dependence on the temperature. 304 and 2205 performed well at all locations and should be good construction materials for PZAS. Degraded PZ exacerbated 316L corrosion, and removal of PZ degradation products using a carbon adsorption bed significantly reduced corrosion. Carbon steel (CS) corrosion showed a weak temperature effect because the corrosion was more dependent on the protective siderite film. The protectiveness of the films was related to fluid velocity. Ni-based alloys corroded in PZ, and the rate increased with temperature. Corrosion of C1010 CS and SS (304, 316L, 430) was measured at absorber and water wash conditions on the bench-scale. Corrosion rate decreases with increasing PZ. With more than 0.003 m PZ in solution, CS has acceptable corrosion performance. Corrosion of CS increases with increasing partial pressure of CO2, suggesting loading is another dominant parameter for carbon steel corrosion. Temperature has a less significant effect than PZ concentration and loading. CS corrosion increases with increasing flow velocity at both absorber and water wash conditions. SS had little corrosion at this lower temperature. Performance of siderite (FeCO3) protective films on CS was studied at representative stripper conditions on the bench-scale. Siderite films can deposit on the surface of CS in CO2-loaded PZ solution at temperatures >100 °C and protect CS from corrosion. The protection may fail in degraded PZ. Ethylenediamine (EDA) is one of the major contributors for the loss of film protectiveness or can be the surrogate for the effect of PZ degradation on siderite film protection. A link between protectiveness and the apparent density of siderite films was discovered. The apparent density of siderite films decreases with increasing flow velocity and decreasing CO2 loading, resulting in higher corrosion of CS
Screening and Evaluating Environmentally-Friendly Corrosion Inhibitors for Amine-Based CO2 Absorption Process
Author: Sureshkumar SrinivasanPublisher:
ISBN:
Category : Technology
Languages : en
Pages :
Book Description
This chapter evaluated the performance of environmentally friendly organic corrosion inhibitors on carbon steel in the amine-based carbon dioxide (CO2) absorption process. The evaluation was experimentally conducted using electrochemical techniques in 5.0 kmol/m3 monoethanolamine (MEA) solutions in the absence and presence of process contaminants, namely formate and chloride, at 80°C and 0.55 mol/mol CO2 loading. The results show, in the absence of process contaminants, that 2-aminobenzene sulfonic acid, 3-aminobenzene sulfonic acid, 4-aminobenzene sulfonic acid, sulfapyridine, and sulfolane yielded 85-92% corrosion inhibition efficiencies, while sulfanilamide yielded the lowest efficiency of 20-42%. Sulfolane was the only tested inhibitor whose performance could be maintained in chloride- and formate-containing MEA solutions. On the contrary, the performance of 3-aminobenzene sulfonic acid and sulfapyridine was decreased by chloride. The performance of all the tested aminobenzene sulfonic acids was compromised by formate.
Corrosion in CO2 Capture, Transportation, Geological Utilization and Storage
Author: Liwei ZhangPublisher: Springer Nature
ISBN: 9819923921
Category : Science
Languages : en
Pages : 136
Book Description
This book systematically discusses the operational stages with high risk of CO2-induced corrosion in CCUS projects, and related measures for corrosion control. CO2 capture, utilization, and storage (CCUS) is a key technology to mitigate climate change and substantially reduce greenhouse gas emissions from fossil fuels. CCUS deals with high concentration CO2, which is very corrosive in a humid environment. Therefore, it is very important to characterize, monitor, and mitigate CO2-induced corrosion in all processes of the CCUS operation chain. Some corrosion control techniques included in this book (e.g., CO2-resisting wellbore cement additives) are beneficial for corrosion control research and engineering practices. This book belongs to the field of corrosion science and engineering, and the expected readership is researchers and engineers working on CCUS.