2015
DOI: 10.1016/j.ijggc.2015.09.015
|View full text |Cite
|
Sign up to set email alerts
|

Reclaiming of degraded MEA solutions by electrodialysis: Results of ED pilot campaign at post-combustion CO 2 capture pilot plant

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
4
1

Citation Types

0
20
0

Year Published

2016
2016
2024
2024

Publication Types

Select...
8
1

Relationship

1
8

Authors

Journals

citations
Cited by 30 publications
(20 citation statements)
references
References 27 publications
(26 reference statements)
0
20
0
Order By: Relevance
“…Similarly, ED can regenerate spent alkanolamine absorbents for CO 2 . Pilot-scale studies were conducted with a spent solution at 30 wt% monoethanolamine, showing stable performances during long-term operations [294]. The effect of CO 2 loading (from 0 to 0.2 mole/mole amine) on heat stable salts (48 meq/L) removal from monoethanolamine-based solvent (30 wt%) was studied by two-stage ED [295] ( Figure 17).…”
Section: Spent Solutions From Chemical Absorption Of Flue Gasesmentioning
confidence: 99%
“…Similarly, ED can regenerate spent alkanolamine absorbents for CO 2 . Pilot-scale studies were conducted with a spent solution at 30 wt% monoethanolamine, showing stable performances during long-term operations [294]. The effect of CO 2 loading (from 0 to 0.2 mole/mole amine) on heat stable salts (48 meq/L) removal from monoethanolamine-based solvent (30 wt%) was studied by two-stage ED [295] ( Figure 17).…”
Section: Spent Solutions From Chemical Absorption Of Flue Gasesmentioning
confidence: 99%
“…They found that ED is useful in removing anions and cations, but it can also cause absorbent losses during the process [ 21 ]. Bazhenov et al [ 22 ] studied the removal of HSS during the reclaiming of degraded monoethanolamine (MEA) solutions by ED in a pilot plant. They found that ED provides quite a uniform removal of HSS ions regardless of the nature of anions, but ED is unable to remove heavy metal.…”
Section: Introductionmentioning
confidence: 99%
“…The accumulation of HSS in the absorption system leads to such operational problems as the decrease of the absorbent CO 2 capacity and change in its physicochemical properties, increase in the corrosiveness and consequent clogging and equipment erosion [5]. HSS can be removed from the amine solvent by means of distillation (process by Gazprom VNIIGAZ [6] and CCR Technologies Ltd. [7]), ion exchange (process MPR CCAR™ and AmiPur ® –CCS by MPR Servises, Inc and Eco-Tec, correspondingly [8]) or electrodialysis [9,10,11,12,13,14,15,16]. The distillation process enables to remove all major impurities, but it is an energy-intensive process since HSS together with other non-volatile products of degradation (e.g., resins) are accumulated in the bottom residue, while the most of alkanolamine and water are evaporated.…”
Section: Introductionmentioning
confidence: 99%
“…The distillation process enables to remove all major impurities, but it is an energy-intensive process since HSS together with other non-volatile products of degradation (e.g., resins) are accumulated in the bottom residue, while the most of alkanolamine and water are evaporated. At the same time, the amine solvents can be reclaimed without phase change by ion-exchange [8,17,18,19] or electrodialysis (ED) [12,13,14,15,16]. Electrodialysis possesses several advantages typical for membrane processes: compactness, modularity, the flexibility of exploitation and easiness of upscaling [20,21].…”
Section: Introductionmentioning
confidence: 99%