摘要
用不同浓度的HF溶液对β沸石催化剂进行处理,当HF浓度较低时,催化剂的晶格外物种和不稳定的骨架铝被溶解,桥形羟基被F取代,孔体积和比表面积增加,总酸量减少。随着HF浓度的继续增加,强B酸变化不明显,强L酸量增加,这是因为强B酸主要来源于缺陷处硅羟基,强L酸是由AlF3或其它铝物种的形成。深度氟化的催化剂孔体积和比表面积均减少,此时β沸石被溶解。催化剂寿命主要取决于催化剂的比表面积和孔体积,而不是酸量。当氟质量分数为0 5%时,催化剂的孔体积和比表面积最大,此时催化剂寿命提高约30%。
The effects of fluorination on β zeolite and alkylation of benzene with long-chain olefins were investigated by means of XRD, BET measurements,FTIR,TPD,elemental analysis and catalyst testing.When β zeolite was impregnated with low concentration HF solutions,the extra-lattice species were dissolved,bridging hydroxyl groups (3605 cm -1 ) were substituted by fluorine and unstable lattice aluminum (3782 cm -1 ) was removed, so the specific area and pore volume increased and total amount of acid decreased gradually.With increasing HF concentration,decrease in strong Brnsted acid sites was less than that in weak Brnsted acid sites because the hydroxyl groups bonded to Si (3730 cm -1 and 3745 cm -1 ) were more stable and strong.Lewis acid sites increased owing to the formation of AlF 3 or other fluorinated compounds.When both β zeolite and the extra-lattice species dissolved,the specific area and pore volume decreased.The lifetime of the catalysts depended on the surface area and pore volume instead of acidity.When the fluorine content was 0 5%,keeping the catalyst at maximum specific surface area and pore volume the lifetime could be improved by 30%.
出处
《石油化工》
CAS
CSCD
北大核心
2003年第2期96-99,共4页
Petrochemical Technology