化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2010年
1期
187-191
,共5页
顾耀明%刘春平%程立泉%朱泽华
顧耀明%劉春平%程立泉%硃澤華
고요명%류춘평%정립천%주택화
环己酮肟%钛硅分子筛HTS-1%氨肟化%工业试验%膜分离
環己酮肟%鈦硅分子篩HTS-1%氨肟化%工業試驗%膜分離
배기동우%태규분자사HTS-1%안우화%공업시험%막분리
cyclohexanone-oxime%HTS-1%ammoximation%industrial tfial%membrane separation
通过工业试验,考察了钛硅分子筛HTS-1新剂和再生剂在环己酮氨肟化制备环己酮肟工艺中的工业试验性能,工业运行结果显示:环己酮转化率>99.6%,环己酮肟选择性>99.5%,催化剂单程寿命大于600 h.同时介绍了亚微米级HTS-1催化过程中的分离和粘壁问题及其工程解决措施,应用陶瓷膜微滤技术解决了催化剂和反应液的分离和循环使用问题,应用波纹管技术克服了催化剂粘壁现象,达到正常换热的效果,并通过优化使系统满足生产要求.
通過工業試驗,攷察瞭鈦硅分子篩HTS-1新劑和再生劑在環己酮氨肟化製備環己酮肟工藝中的工業試驗性能,工業運行結果顯示:環己酮轉化率>99.6%,環己酮肟選擇性>99.5%,催化劑單程壽命大于600 h.同時介紹瞭亞微米級HTS-1催化過程中的分離和粘壁問題及其工程解決措施,應用陶瓷膜微濾技術解決瞭催化劑和反應液的分離和循環使用問題,應用波紋管技術剋服瞭催化劑粘壁現象,達到正常換熱的效果,併通過優化使繫統滿足生產要求.
통과공업시험,고찰료태규분자사HTS-1신제화재생제재배기동안우화제비배기동우공예중적공업시험성능,공업운행결과현시:배기동전화솔>99.6%,배기동우선택성>99.5%,최화제단정수명대우600 h.동시개소료아미미급HTS-1최화과정중적분리화점벽문제급기공정해결조시,응용도자막미려기술해결료최화제화반응액적분리화순배사용문제,응용파문관기술극복료최화제점벽현상,체도정상환열적효과,병통과우화사계통만족생산요구.
Through industrial trials for cyclohexanone-oxime synthesis catalyzed with molecular sieves HTS-1, the activity and the life of fresh and regenerated HTS-1 catalysts have been investigated. The running results showed that the conversion of cyclohexanone was above 99.6%, and the selectivity for cyclohexanone oxime was above 99.5%, and the single circle life of HTS-1 was no less than 600 h. The separation and on-line recycle of HTS-1 catalyst were achived through ceramic microfiltration, and the wall-sticking problem of HTS-1 catalyst was resolved through a technology of corrugated tube heat exchange.