“…The use of lab-conditions for new materials is quite common and some studies only reported the performance of MgO sorbents under pure CO 2 stream. Although highly stable capture performance of CO 2 sorbents over cycles were reported, their testing conditions have been criticized to be "unrealistic" or "too mild" [14,33,34]. Thus, use of harsh conditions, especially in the calcination stage is highly suggested.…”
A series of mesoporous MgO samples with different morphologies were synthesized through a simple hydrothermal treatment and NaNO 3 /NaNO 2 were used as promoters to enhance CO 2 capture capacity at an intermediate temperature range (200-400 °C). The effects of hydrothermal solution pH and content of promoters were examined to determine the optimal synthesis conditions. The influence of operational temperatures, CO 2 partial pressure, and performance over repeated cycles was investigated and the reaction mechanism was discussed. The mesoporous MgO promoted by NaNO 3 /NaNO 2 exhibited a CO 2 capture capacity as high as 19.8 mmol•g-1 at 350 °C in the presence of 0.85 bar of CO 2 within only 50 min. A "three-stage" reaction process was proposed based on a detailed sorption kinetics study, namely Stage I: initiating interactions between CO 2 and exposed MgO; Stage II: generation and accumulation of Mg 2+ and CO 3 2-; and Stage III: fast carbonation. Gradual deterioration of sorbents was found over the first 5 cycles followed by stable regenerability in the 5-15 th cycles. A kinetic study of the 15 th cycle suggests that the deactivation of sorbents inhibited the accumulation of Mg 2+ and CO 3 2in Stage II and suppressed the carbonation in Stage III. A range of characterizations were undertaken revealing the morphology and structure of both fresh and regenerated sorbents. The results confirmed that, other than the sintering effect due to phase transition, the transformation of MgO skeleton is also an important contributor to the gradual deactivation of the sorbents over the first 5 cycles. More severe sintering effect under harsh decarbonation conditions suppressed the stability of the sorbents over cycles.
“…The use of lab-conditions for new materials is quite common and some studies only reported the performance of MgO sorbents under pure CO 2 stream. Although highly stable capture performance of CO 2 sorbents over cycles were reported, their testing conditions have been criticized to be "unrealistic" or "too mild" [14,33,34]. Thus, use of harsh conditions, especially in the calcination stage is highly suggested.…”
A series of mesoporous MgO samples with different morphologies were synthesized through a simple hydrothermal treatment and NaNO 3 /NaNO 2 were used as promoters to enhance CO 2 capture capacity at an intermediate temperature range (200-400 °C). The effects of hydrothermal solution pH and content of promoters were examined to determine the optimal synthesis conditions. The influence of operational temperatures, CO 2 partial pressure, and performance over repeated cycles was investigated and the reaction mechanism was discussed. The mesoporous MgO promoted by NaNO 3 /NaNO 2 exhibited a CO 2 capture capacity as high as 19.8 mmol•g-1 at 350 °C in the presence of 0.85 bar of CO 2 within only 50 min. A "three-stage" reaction process was proposed based on a detailed sorption kinetics study, namely Stage I: initiating interactions between CO 2 and exposed MgO; Stage II: generation and accumulation of Mg 2+ and CO 3 2-; and Stage III: fast carbonation. Gradual deterioration of sorbents was found over the first 5 cycles followed by stable regenerability in the 5-15 th cycles. A kinetic study of the 15 th cycle suggests that the deactivation of sorbents inhibited the accumulation of Mg 2+ and CO 3 2in Stage II and suppressed the carbonation in Stage III. A range of characterizations were undertaken revealing the morphology and structure of both fresh and regenerated sorbents. The results confirmed that, other than the sintering effect due to phase transition, the transformation of MgO skeleton is also an important contributor to the gradual deactivation of the sorbents over the first 5 cycles. More severe sintering effect under harsh decarbonation conditions suppressed the stability of the sorbents over cycles.
“…The EtOH/water pre-treated sorbents were assessed for their ability to resist sintering degradation over multiple calcium looping cycles. This cycling was conducted within an atmospheric pressure TGA (TA Instruments Q5000IR) and utilised industrially representative post-combustion calcination conditions, which has been shown to be vital in determining the actual potential of a sorbents carrying capacity [25].…”
Section: Sorbent Analysismentioning
confidence: 99%
“…The temperature was ramped at 50 °C/min and the CO 2 concentration was ramped up at a rate such that the sample remained slightly above the equilibrium position (until about 890 °C at which point a partial pressure greater than 1 bar was required to prevent calcination). A detailed explanation of this temperature linked CO 2 partial pressure ramping system is given by Clough et al [25]. A constant flow rate of 110 cm 3 /min was utilised throughout these runs.…”
Section: Sorbent Analysismentioning
confidence: 99%
“…Conducted within an atmospheric TGA, carbonation performed at 650 °C for 20 minutes and calcination at 950 °C for 1 minute. The CO 2 partial pressure was ramped between the carbonation and calcination conditions to prevent undesired early calcination[25].…”
The application of an ethanol pre-treatment step on biomass templated calcium looping sorbents resulting in an improved pore structure for cyclic CO 2 capture was investigated. Three ethanol solutions of varying concentrations were used and an improved pore and particle structure, and thermogravimetric analyser CO 2 carrying capacity arising with the 70 vol.% ethanol solution. The extent of attrition of these sorbents was tested within a fluidised bed reactor and compared against an untreated sorbent and a limestone base case. It found that despite the ethanol treated sorbents displaying an admirable CO 2 carrying capacity within the thermogravimetric analyser even under realistic post-combustion conditions, this was not translated equivalently in the fluidised bed. Attrition and elutriation of the biomass templated sorbents was a significant issue and the ethanol pre-treatment step appeared to worsen the situation due to the roughened surface and mechanically weaker structure.
This paper reviews the advances of enhanced thermo-chemical processes applying H2-selective membrane reactors and in situ CO2 capture for selective H2 production.
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