建議

1. 由於本研究中所使用之水蒸汽系統並無加壓幫浦之設計，故需加 以通入氮氣做為輔助之動力，然氮氣會使尾端 CO₂ 出流濃度降 低，故若能將水蒸汽產出系統加以設計，直接使用蒸汽鍋爐，則 不需要N₂載流氣體，因此能進一步提升尾端氣流濃度，更有利後 續碳儲存之減容需求。

2. 氧化鈣的應用可以嘗試藉由模板分散吸附劑或流體化床等方式，

控制吸附劑顆粒彼此間之距離，避免於反覆吸脫附的過程中，因 燒結影響其再利用率。

3. 本研究為模擬燃煤發電廠的煙道氣流，將進流氣體濃度調整為 15%CO₂、6%O₂與79%N₂，然煙道氣流中尚有其他氣體存在，例 如 SO_X、NO_X等，可能會產生競爭吸附或加速劣化等行為，如能 在實驗中亦將其考量，則可得到吸附劑應用後更確實的資訊。

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在文檔中 水合作用改質氧化鈣捕獲溫室二氧化碳氣體之循環再生能力研究 (頁 88-96)