辽宁石油化工大学学报
遼寧石油化工大學學報
료녕석유화공대학학보
JOURNAL OF LIAONING UNIVERSITY OF PETROLEUM & CHEMICAL TECHNOLOGY
2014年
1期
34-38
,共5页
BASF 04-66催化剂%热点%温度%变化%预处理
BASF 04-66催化劑%熱點%溫度%變化%預處理
BASF 04-66최화제%열점%온도%변화%예처리
Catalyst of BASF 04-66%Hot spot%Temperature%Change%Pretreatment
通过对BASF 04-66型催化剂的填装、预处理以及进料后反应器热点温度位置的变化等进行分析研究,得出在催化剂预处理中,调节进入反应器的风量以及反应器温度可使催化剂活性最优;在反应刚开始进行时,热点温度位置主要集中在CL4催化剂层,随着反应的进行,热点温度位置逐渐转移至CL1催化剂层,即热点温度位置从3050 m m移动至650、550 m m处。热点的温度从410.5℃上升至431.5℃,热点温度提高了5.1%。
通過對BASF 04-66型催化劑的填裝、預處理以及進料後反應器熱點溫度位置的變化等進行分析研究,得齣在催化劑預處理中,調節進入反應器的風量以及反應器溫度可使催化劑活性最優;在反應剛開始進行時,熱點溫度位置主要集中在CL4催化劑層,隨著反應的進行,熱點溫度位置逐漸轉移至CL1催化劑層,即熱點溫度位置從3050 m m移動至650、550 m m處。熱點的溫度從410.5℃上升至431.5℃,熱點溫度提高瞭5.1%。
통과대BASF 04-66형최화제적전장、예처리이급진료후반응기열점온도위치적변화등진행분석연구,득출재최화제예처리중,조절진입반응기적풍량이급반응기온도가사최화제활성최우;재반응강개시진행시,열점온도위치주요집중재CL4최화제층,수착반응적진행,열점온도위치축점전이지CL1최화제층,즉열점온도위치종3050 m m이동지650、550 m m처。열점적온도종410.5℃상승지431.5℃,열점온도제고료5.1%。
The filling ,pretreatment of new catalyst of BASF 04-66 and the changing of hot spot temperature when the material entered the reactor were investigated .It was found that the activity of catalyst can be optimized by adjusting the air flowed into the reactor and the reactor temperature in pretreatment of the catalyst ;while the reaction has begun ,the hot spot temperature mainly focused on the catalyst layer of CL4 ,as the reaction proceeded , the hot spot temperature is gradually transferred to the position of the catalyst layer of CL1 .The hot spot temperature from 3 050 mm to move to the position of 650 nm and 550 mm .The hot spot temperature rises from 410 .5 ℃ to 431 .5 ℃ ,the hot spot temperature increase of 5 .1% .