2019
DOI: 10.1002/cssc.201802978
|View full text |Cite
|
Sign up to set email alerts
|

Oxidation‐Resistant, Cost‐Effective Epoxide‐Modified Polyamine Adsorbents for CO2 Capture from Various Sources Including Air

Abstract: CO2 adsorbents based on the reaction of pentaethylenehexamine (PEHA) or tetraethylenepentamine (TEPA) with propylene oxide (PO) were easily prepared in “one pot” by impregnation on a silica support in water. The starting materials were readily available and inexpensive, facilitating the production of the adsorbents on a large scale. The prepared polyamine/epoxide adsorbents were efficient in capturing CO2 and could be regenerated under mild conditions (50–85 °C). They displayed a much‐improved stability compar… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

4
59
0
1

Year Published

2019
2019
2023
2023

Publication Types

Select...
8

Relationship

2
6

Authors

Journals

citations
Cited by 71 publications
(64 citation statements)
references
References 83 publications
4
59
0
1
Order By: Relevance
“…The fluoroalkyl groups in F-PAA-C60 triple the DAC capacity of PAA-C60 at low temperature, in line with the fourfold increase of CO2 uptake observed in a pure CO2 stream. With a DAC capacity of 1.30 mmol g -1 (2.28 mmol CO2 per gram of PAA) at 30 °C, F-PAA-C60 compares well with other materials reported in the literature such as PEI loaded SBA-15 (1.10 mmol g -1 ), [27] PEHA or TEPA co-impregnated with PO on silica support (1.25 and 1.34 mmol g -1 , respectively), [23] and amine-based nanofibrillated cellulose (1.39 mmol g -1 ). [28] A comprehensive table with key features and performance of polyamine-based DAC sorbent materials is provided in the SI, Table S2.…”
Section: Carbon Dioxide Capturesupporting
confidence: 77%
See 1 more Smart Citation
“…The fluoroalkyl groups in F-PAA-C60 triple the DAC capacity of PAA-C60 at low temperature, in line with the fourfold increase of CO2 uptake observed in a pure CO2 stream. With a DAC capacity of 1.30 mmol g -1 (2.28 mmol CO2 per gram of PAA) at 30 °C, F-PAA-C60 compares well with other materials reported in the literature such as PEI loaded SBA-15 (1.10 mmol g -1 ), [27] PEHA or TEPA co-impregnated with PO on silica support (1.25 and 1.34 mmol g -1 , respectively), [23] and amine-based nanofibrillated cellulose (1.39 mmol g -1 ). [28] A comprehensive table with key features and performance of polyamine-based DAC sorbent materials is provided in the SI, Table S2.…”
Section: Carbon Dioxide Capturesupporting
confidence: 77%
“…Additives can also increase thermal stability of the sorbent, for example propylene oxide (PO) was added to pentaethylenehexamine (PEHA) and tetraethylenepentamine (TEPA) before impregnation onto silica support significantly improving the oxidative stability of the sorbent. [23] The direct air capture performance of these sorbents was tested at 25 °C, under 400 ppm CO2, and the uptakes were 1.25 and 1.34 mmol CO2 g -1 for the PEHA and TEPA based adsorbents, respectively. Driven by the above findings on the pivotal role of polymer conformation in the CO2 capture process, and the beneficial effect of hydrophobic features on amine accessibility, we present here the successful implementation of a strategy to improve the CO2 capture performance at ambient temperature of highly loaded poly(allylamine) (PAA) fullerene cross-linked sorbents.…”
Section: Introductionmentioning
confidence: 99%
“…Amine-modified sorbents can be categorized into three classes based on their preparation methods,examples of each are shown in Figure 4. [142] Class 1sorbents can be prepared by physically impregnating amines into porous materials, [87,[143][144][145][146][147][148][149][150][151][152][153][154][155][156][157][158][159] but amines with low molecular weights easily leach during sorption and regeneration processes. [146,160] Class 2s orbents are prepared by chemically grafting the amine functional group onto the support surface,t hereby stabilizing the sorbent during regeneration.…”
Section: Chemisorption:a Mine-modified Materialsmentioning
confidence: 99%
“…68 However, since the heat of adsorption represents the energy required to remove CO 2 to re-generate the adsorbent, 69 the lower heat of adsorption of secondary and tertiary amines would be advantageous in reducing regeneration energy. 58,70,71 More recent work by the Jones group, in which heats of adsorption were measured directly by calorimetry, found that the heats of adsorption of strongly basic primary and secondary amines were approximately equal, at around 90 kJ mol À1 . 72 Considering the CO 2 uptakes and heats of adsorption for a range of aminosilanes of varying steric constraints, the authors postulated that the higher CO 2 adsorption observed for primary amines under dilute conditions is more likely to be dependent on entropic rather than enthalpic factors.…”
Section: The Role Of Amine Functionality In Co 2 Capturementioning
confidence: 99%