Ca基固体碱制备及其重油裂解气化性能

采用固相合成法制备Ca基固体碱催化剂，并利用N2吸附技术、XRD、FT IR及Hammett指示剂法对催化剂进行表征。采用双管反应器进行常压渣油催化裂解和气化再生实验，考察了反应温度、水/油质量比、剂/油质量比等对裂解产物中烯烃分布的影响，并考察了不同积炭量对待生剂气化性能的影响。结果表明，铝酸钙催化剂具有较强的碱强度和总碱量、较小的比表面积和孔容积。在反应温度750℃、水/油质量比10、剂/油质量比70时，催化裂解性能最优，乙烯质量产率达到214%，总烯烃质量产率为296%。积炭量对待生剂气化性能影响不明显。再生剂的总碱量略有减小，合成气以H2和CO2为主且含量达到89%（体积分数）。将催化裂解和气化再生整合，实现了热量耦合，达到综合利用重油的目标。

Preparation of Ca Based Solid Basic Catalyst and its Cracking Gasification Performance for Heavy Oil

Ca based solid base catalyst was prepared by the solid phase synthesis method. The prepared catalyst was characterized by N2 adsorption techniques, XRD, FT IR, the Hammett indicators methods. And atmospheric residue catalytic cracking and gasification reaction were carried out in the double pipe reactor to study the influences of reaction temperature, m(Water)/m(Oil) and m(Catalyst)/m(Oil) on the heavy oil cracking over solid base catalyst. Then the coke deposited gasification was also discussed. The results showed that calcium alumina catalyst had the stronger base strength and total base number, the lower specific surface area and pore volume compared with that of Al2O3. With calcium alumina as the catalyst and under the conditions of reaction temperature 750℃, m(Water)/m(Oil)=10 and m(Catalyst)/m(Oil)=70, the yields of ethylene and total olefins reached to 214% and 296%, respectively. The coke amount deposited on deactivated base catalyst had little influence to its gasification performance. Total base number of regenerated catalyst slightly reduced, and the volume fractions of H2 and CO2 in syngas could reach up to 89%. By integrating two reactions of catalytic cracking and gasification regeneration, the reaction heat coupling and comprehensive utilization for heavy oil were realized.