化学反应工程与工艺
化學反應工程與工藝
화학반응공정여공예
CHEMICAL REACTION ENGINEERING AND TECHNOLOGY
2014年
4期
329-335
,共7页
甲苯歧化%烷基转移%重芳烃利用%萘
甲苯歧化%烷基轉移%重芳烴利用%萘
갑분기화%완기전이%중방경이용%내
toluene disproportionation%transalkylation%heavy aromatics%naphthalene
研究了原料中萘含量对非贵金属改性催化剂上甲苯与重芳烃歧化和烷基转移反应的影响。结果表明:随着原料中萘含量的增加,甲苯与重芳烃歧化和烷基转移反应受到的抑制效果增加,需以提高反应温度来补偿催化剂活性的损失;撤掉原料中的萘后,甲苯歧化反应不能完全恢复,重芳烃烷基转移反应能够恢复。萘系物在反应过程中存在一平衡值:原料中不含萘时,甲苯与重芳烃歧化与烷基转移反应副产少量萘系物;原料中萘含量低于平衡值时,萘主要发生烷基转移反应,生成烷基萘;原料中萘含量高于平衡值时,萘除了发生烷基转移反应外,还发生了加氢裂解反应。
研究瞭原料中萘含量對非貴金屬改性催化劑上甲苯與重芳烴歧化和烷基轉移反應的影響。結果錶明:隨著原料中萘含量的增加,甲苯與重芳烴歧化和烷基轉移反應受到的抑製效果增加,需以提高反應溫度來補償催化劑活性的損失;撤掉原料中的萘後,甲苯歧化反應不能完全恢複,重芳烴烷基轉移反應能夠恢複。萘繫物在反應過程中存在一平衡值:原料中不含萘時,甲苯與重芳烴歧化與烷基轉移反應副產少量萘繫物;原料中萘含量低于平衡值時,萘主要髮生烷基轉移反應,生成烷基萘;原料中萘含量高于平衡值時,萘除瞭髮生烷基轉移反應外,還髮生瞭加氫裂解反應。
연구료원료중내함량대비귀금속개성최화제상갑분여중방경기화화완기전이반응적영향。결과표명:수착원료중내함량적증가,갑분여중방경기화화완기전이반응수도적억제효과증가,수이제고반응온도래보상최화제활성적손실;철도원료중적내후,갑분기화반응불능완전회복,중방경완기전이반응능구회복。내계물재반응과정중존재일평형치:원료중불함내시,갑분여중방경기화여완기전이반응부산소량내계물;원료중내함량저우평형치시,내주요발생완기전이반응,생성완기내;원료중내함량고우평형치시,내제료발생완기전이반응외,환발생료가경렬해반응。
In order to make full use of C10 aromatic (C10A) resources, the effects of naphthalene content in feedstock on the disproportionation and transalkylation of toluene with C9 and C10 aromatics over non-noble metal modified catalyst were investigated. The results indicated that with the increase of naphthalene content in feedstock, the catalytic activity of disproportionation and transalkylation of toluene with C9 and C10 aromatics transalkylation decreased, and the reaction temperature should be raised to improve catalyst activity. After withdrawing naphthalene, the transalkylation of C9 and C10 aromatics was recovered, while toluene disproportionation was not. Naphthalene derivatives had an equilibrium composition in the reaction system. When there was no naphthalene in the feedstock, naphthalene derivatives were produced as the by-products of the disproportionation and transalkylation of toluene with C9 and C10 aromatics. When naphthalene content was lower than the equilibrium value, naphthalene was mainly converted to alkylnaphthalenes through transalkylation. When naphthalene content was higher than the equilibrium value, while naphthalene was mainly converted to alkylnaphthalene and light aromatics through both transalkylation and hydrocracking.