Catalytic conversion of 1,1,1,2-tetrafluoroethane (HFC-134a)
We examined the conversion of HFC-134a over five catalysts, Na 2 CO 3 , CaO, CaCO 3 , and two types of γ -Al 2 O 3 with different surface areas, between 300 and 600 °C. HFC-134a was barely converted via the non-catalytic reaction, even at the highest temperature (600 °C). The operating temperatures...
Gespeichert in:
Veröffentlicht in: | The Korean journal of chemical engineering 2018, 35(8), 221, pp.1611-1619 |
---|---|
Hauptverfasser: | , , , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
Zusammenfassung: | We examined the conversion of HFC-134a over five catalysts, Na
2
CO
3
, CaO, CaCO
3
, and two types of
γ
-Al
2
O
3
with different surface areas, between 300 and 600 °C. HFC-134a was barely converted via the non-catalytic reaction, even at the highest temperature (600 °C). The operating temperatures for the catalytic conversion of HFC-134a were reduced dramatically and its efficiency increased with increasing temperature. Among the catalysts used,
γ
-Al
2
O
3
with the larger surface area showed the highest conversion rate of HFC-134a, which was followed, in order, by
γ
-Al
2
O
3
with the smaller surface area, CaCO
3
, CaO, and Na
2
CO
3
. The conversion rate of
γ
-Al
2
O
3
decreased rapidly due to catalyst deactivation. The catalytic efficiency of
γ
-Al
2
O
3
was maintained for a longer period by water addition. Water acted as a hydrogen donor for the dehydrofluorination reaction. |
---|---|
ISSN: | 0256-1115 1975-7220 |
DOI: | 10.1007/s11814-018-0051-7 |