石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2014年
3期
51-54
,共4页
催化重整%催化剂%铂%铼%硅%分子筛
催化重整%催化劑%鉑%錸%硅%分子篩
최화중정%최화제%박%래%규%분자사
catalytic reforming%catalyst%platinum%rhenium%silicon%molecular sieve
以不同方式引入硅,研究了不同硅源对重整催化剂性能的影响。结果表明:催化剂载体中引入含硅分子筛导致重整催化剂的裂解活性提高,选择性变差,积炭速率提高;重整载体制备过程中引入硅后导致催化剂的比表面积下降,选择性变差,积炭量增大;重整催化剂在反应过程中受到硅污染后,催化剂的持氯能力变差,活性降低。硅中毒是不可逆的,不能通过常规再生的方法恢复催化剂的活性。
以不同方式引入硅,研究瞭不同硅源對重整催化劑性能的影響。結果錶明:催化劑載體中引入含硅分子篩導緻重整催化劑的裂解活性提高,選擇性變差,積炭速率提高;重整載體製備過程中引入硅後導緻催化劑的比錶麵積下降,選擇性變差,積炭量增大;重整催化劑在反應過程中受到硅汙染後,催化劑的持氯能力變差,活性降低。硅中毒是不可逆的,不能通過常規再生的方法恢複催化劑的活性。
이불동방식인입규,연구료불동규원대중정최화제성능적영향。결과표명:최화제재체중인입함규분자사도치중정최화제적렬해활성제고,선택성변차,적탄속솔제고;중정재체제비과정중인입규후도치최화제적비표면적하강,선택성변차,적탄량증대;중정최화제재반응과정중수도규오염후,최화제적지록능력변차,활성강저。규중독시불가역적,불능통과상규재생적방법회복최화제적활성。
This paper described the influence of Si addition in different ways on the performance of reforming catalysts. Introduction of Si-containing molecular sieve in catalysts increases the cracking ac-tivity and coking rate,and lowers the selectivity. The experiment find that the addition of Si in carrier preparation leads to the reduction of specific surface area and selectivity of the catalysts and higher co-king rate and that after contaminated by Si during reforming reaction,the Cl-keeping capacity becomes poor and the catalyst activity is dropped as well. Si poisoning are irreversible and catalyst activity cannot be recovered through conventional regeneration method.