Amine Thermal Reclamation; Technology Development from Keywords: CO2 capture; amine; degradation; reclamation . amines during a reclaimer cycle. Amine reclaimer wastes (ARW) generated in CO2 capture processes demand suitable disposal means. Such wastes contain remaining amine, NH3 and other. Amine reclaimer wastes (ARW) generated in carbon capture and sequestration ( CCS) is categorized as a hazardous waste which needs proper disposal.

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Appendix D Thermal reclaiming of amine systems

The following reactions show how the possible HSS are formed. This facility has been performing CO 2 capture from flue gas since [28;38]. The most effective techniques used to purify reclaaimer solutions include distillation thermal reclaimingion exchange and electrodialysis.

The following model is reckaimer parametric model that aims to quantify the influence of gas impurities in the waste generated by the reclaimer unit. Corrosion products Fe contaminated the sulfinol solution causing erosion of carbon steel and stainless steel parts of the column and the associated overhead piping and elbows.

The following reaction rate has been derived experimentally:. JavaScript is disabled for your browser.

Appendix D Thermal reclaiming of amine systems | Global CCS Institute

Fraction of the lean stream reclaimed: Estimation of heat stable salts formation follows from the removal rates and stoichimetry of the reactions:. The energy associated with this reclaiming is 60MWth, approximately 0. The degradation products also interact with MEA molecules according to reactions 3 and 4. One of the problems related to the amine process is amine degradation, which leads to accumulation of degradation products.

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Corrosion in Amine Reclaimer System

Vapour containing H2S, CO2, and sulfinol leave the top of the column and oxosolidone in the liquid phase, which in turn leaves at the bottom outlet of the column. This study established the correlation between type of amine, type of flue gas, type of degradation products to be reclaimed, and type of reclaiming technology.

Some features of this site may not work without it. Login or Vote Anonymously. This paper describes the root cause failure analysis of severe corrosion and erosion in reclaimee reclaimer system including the overhead piping.

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Improvements of the model are suggested. To prevent these degradation products to accumulate, relcaimer to regain lost solvent, a reclaimer can be used reclaimfr purify the contaminated amine solution. Oxidative degradation rate depends on Temperature, oxygen concentration in the flue gas, MEA concentration, SO2 concentration in the flue gas and CO 2 loading [31].

Estimation of MEA loss is done trough the following equations: Nevertheless, in many thermal reclaimers the concentration of amine is still high, transforming the thermal reclaimer more into a feed and bleed system [27]. Concentration and temperature profiles were obtained. Reclaimeer the oxidative degradation is assumed to be 0. Amine reclaimer technologies Haaversen, Linn Christine Loe. The figure below show the results:. The fourth objective was to perform a lab distillation of a contaminated amine solvent.


The overall HSS formation rate is used for the mass balance over the reclaimer.

Output of the exchanger is sour water to the effluent treatment system. This reaction rate was used to estimated the MEA degradation rate at different O 2 concentrations in the Flue gas.

Metadata Show full item record. For case 4B the MEA degradation would be significantly larger 1.

Abstract Carbon dioxide CO2 capture in post-combustion by the use of amines is one of several technologies known to reduce the release of CO2 to the atmosphere when burning fossil fuels. Oxidative degradation is the main form of MEA loss in a capture process. Mass profiles, together with volume and temperature profiles within the reclaimer were found with respect of time.

An ordinary differential equation ODE solver was used to wmine the set of differential equations. This causes loss of valuable and expensive amine that has to be replaced together with reduced solvent performance. The table below shows the main performance characteristics of the capture plant and the lean solvent conditions for case 1B.

The oxidative pathways leads principally to the formation of carboxylic acids reactions 1 and 2 are an example of degradation reaction.

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