2009
DOI: 10.1016/j.egypro.2009.01.186
|View full text |Cite
|
Sign up to set email alerts
|

Chilled ammonia process for CO2 capture

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

1
42
0

Year Published

2011
2011
2019
2019

Publication Types

Select...
6
1
1

Relationship

0
8

Authors

Journals

citations
Cited by 112 publications
(49 citation statements)
references
References 0 publications
1
42
0
Order By: Relevance
“…Alstom and Powerspan are the two major players in this area. Alstom is developing a chilled NH 3 process, in which, as described in the open literature (Darde et al, 2009;Kozak et al, 2009;Valenti et al, 2009), CO 2 is absorbed in highly ammoniated solution at low temperatures (0-20 • C), producing a slurry containing ammonium bicarbonate. In the stripper, ammonium bicarbonate is converted to ammonium carbonate at temperatures above 100 • C and pressures of 20-40 bar.…”
Section: Introductionmentioning
confidence: 99%
“…Alstom and Powerspan are the two major players in this area. Alstom is developing a chilled NH 3 process, in which, as described in the open literature (Darde et al, 2009;Kozak et al, 2009;Valenti et al, 2009), CO 2 is absorbed in highly ammoniated solution at low temperatures (0-20 • C), producing a slurry containing ammonium bicarbonate. In the stripper, ammonium bicarbonate is converted to ammonium carbonate at temperatures above 100 • C and pressures of 20-40 bar.…”
Section: Introductionmentioning
confidence: 99%
“…In most traditional adsorption cases, the energy consumption of capturing CO 2 is 1-3 GJ ton À 1 CO 2 , as reported in the literature (Bounaceur et al, 2006;Kozak et al, 2009). Membrane separation technology effectively utilized the pressure of feed gas as the driving force.…”
Section: Energy and Cost Analysis For Membrane Processesmentioning
confidence: 95%
“…Given the composition and temperature, the NH 3 -WW product stream resembles the conditions found in the CO 2 -desorber rather than those found in the CO 2 -absorber. Hence, an addition to the CO 2 -desorber as suggested by Kozak et al (2009) and in one of the layouts presented by Valenti et al (2013) may also be a reasonable strategy -provided that both desorbers are operated at the same pressure.…”
Section: Nh 3 Water Wash Desorbermentioning
confidence: 97%
“…In the end, pilot tests revealed that handling solids in a packed column is hardly feasible due to equipment clogging and the resulting difficulties in plant operation and control. Accordingly, the current CAP implementations avoid solid formation by limiting the NH 3 and CO 2 concentrations as well as the chilling (Yu et al, 2011;Kozak et al, 2009). …”
Section: Introductionmentioning
confidence: 98%
See 1 more Smart Citation