石油学报(石油加工)
石油學報(石油加工)
석유학보(석유가공)
ACTA PETROLEI SINICA(PETROLEUM PROCESSING SECTION)
2009年
6期
861-867
,共7页
旋转填充床%搅拌鼓泡釜%微观混合%高碱值石油磺酸钙%清净剂%微乳状液%水量控制%纳米颗粒%气含率
鏇轉填充床%攪拌鼓泡釜%微觀混閤%高堿值石油磺痠鈣%清淨劑%微乳狀液%水量控製%納米顆粒%氣含率
선전전충상%교반고포부%미관혼합%고감치석유광산개%청정제%미유상액%수량공제%납미과립%기함솔
rotating packed bed (RPB)%stirred bubbling tank reactor%micro-mixing%high-TBN calcium petroleum sulfonate%detergent%microemulsion%moisture control%nanoparticle%gas hold-up
合成高碱值石油磺酸钙清净剂的搅拌鼓泡釜工艺需外加水;而旋转填充床工艺中只需反应牛成水参与反应,即可达到碱值的要求,简化了工艺和控制过程.分析了2种反应器的特性.结果表明,强化了微观混合和传质的旋转填充床能快速生成细小、均匀的W/O型微乳液体系;通过溶解一消耗一再溶解一再消耗模式,能有效利用w/O型微乳液体系中的水核,需水量少;同时,旋转填充床使物料系统的含CO_2气率较均匀,生成的纳米CaCO_3粒子粒径小、分布窄,产品质量高.也指明r搅拌鼓泡釜反应器在混合分散和传质均匀性方面的相对不足.
閤成高堿值石油磺痠鈣清淨劑的攪拌鼓泡釜工藝需外加水;而鏇轉填充床工藝中隻需反應牛成水參與反應,即可達到堿值的要求,簡化瞭工藝和控製過程.分析瞭2種反應器的特性.結果錶明,彊化瞭微觀混閤和傳質的鏇轉填充床能快速生成細小、均勻的W/O型微乳液體繫;通過溶解一消耗一再溶解一再消耗模式,能有效利用w/O型微乳液體繫中的水覈,需水量少;同時,鏇轉填充床使物料繫統的含CO_2氣率較均勻,生成的納米CaCO_3粒子粒徑小、分佈窄,產品質量高.也指明r攪拌鼓泡釜反應器在混閤分散和傳質均勻性方麵的相對不足.
합성고감치석유광산개청정제적교반고포부공예수외가수;이선전전충상공예중지수반응우성수삼여반응,즉가체도감치적요구,간화료공예화공제과정.분석료2충반응기적특성.결과표명,강화료미관혼합화전질적선전전충상능쾌속생성세소、균균적W/O형미유액체계;통과용해일소모일재용해일재소모모식,능유효이용w/O형미유액체계중적수핵,수수량소;동시,선전전충상사물료계통적함CO_2기솔교균균,생성적납미CaCO_3입자립경소、분포착,산품질량고.야지명r교반고포부반응기재혼합분산화전질균균성방면적상대불족.
High-TBN calcium sulfonate synthesis in stirred bubbling tank reactor needs more water to participate, while in rotating-packed bed (RPB) it needs only water formed in synthesis itself to reach TBN requirement, so that the process becomes simply and easily controlled, simultaneously.The characteristics of the two reactors were analyzed.The results showed that in RPB, micro-mixing and mass transfer were intensified, tiny and uniform W/O microemulsion was formed quickly; by the pattern of dissolve-deplete-redissolve-redeplete, the utilization of water core of W/O microemulsion was efficient, the amount of water needed in process was small; CO_2 was fairly well-distributed and approximately homogeneous in all RPB system, making diameter of the grown CaCO_3 nanoparticle smaller and uniform and the performance of detergent product better;in stirred bubbling tank reactor.The shortcoming in the micro-mixing and mass transfer uniformity of stirred bubbling tank process was also indicated