期刊文献+

结晶成核与生长两阶段的模型识别研究 被引量:4

The Study on Model Identification of Nucleation and Crystal Growth Stages
下载PDF
导出
摘要 针对溶液间歇结晶过程的特点 ,定义并关联了无因次变量K和K ,用于对结晶过程中成核和生长两阶段进行定量识别。对于添加晶种的KNO3 —H2 O间歇结晶过程 ,模拟分析的结果表明 :无因次变量K和K 的数值均随着晶核形成过程而减小 ,随着晶核生长过程而增大。由实验测定的动态透光率和溶液浓度 ,即可对结晶过程中的成核和生长两阶段进行定量识别。 Two new zero dimension variables,K and K *,concerning the stage identification of solution batch crystallization process were defined in this paper.For seeded crystallization of potassium nitrate in water,the results calculated showed the values of K and K * would be decreased with nucleation process and increased with crystal growth process.Based on the characteristics of the variables,coupled with the dynamic transmittance and concentration data,the nucleation and crystal growth stages could be identified.
出处 《化工时刊》 CAS 2004年第3期31-33,共3页 Chemical Industry Times
基金 中国药品大学青年基金
关键词 间歇结晶 硝酸钾 成核阶段 生长阶段 模型识别 制药 batch crystallization potassium nitrate nucleation stage crystal growth stage model identification
  • 相关文献

参考文献8

  • 1Tavare N S,Garsde J.Chem. Eng. Res. Des. 1986,64:109-118
  • 2伍川,黄培,时钧.KNO_3-H_2O溶液间歇结晶动力学[J].化工学报,2003,54(7):953-958. 被引量:20
  • 3Larson M A,Garside J.The Chemical Engineer,1973,274:318-327
  • 4Matthews H B,Miller S M,Rawlings J B.Powder Technology,1996,88:227~235
  • 5黄德春,刘巍,王志祥.添加晶种的间歇结晶器数学模型[J].化工时刊,2003,17(11):28-30. 被引量:3
  • 6Miller S M. Modelling and Quality Control Strategies for Batch Cooling Crystallizers. University of Texas at Austin,1993
  • 7Vekilov P G,Rosenberger F,Lin H .,et al. Journal of Crystal Growth,1999,196:261~275
  • 8王静康.化学工程手册--结晶.北京:化学工业出版社,1996

二级参考文献27

  • 1王静康.化学工程手册-结晶[M].北京:化学工业出版社,1996..
  • 2Rawings J B, Miller S M, Witkowski W R. Model Identification and Control of Solution Crystallization Process.Ind. Eng. Chem. Res. , 1993, 32: 1275-1296.
  • 3Monnier O, Fevotte G, Hoff C, Klein J P. Model Identification of Batch Cooling Crystallizations Through Calorimetry and Image Analysis. Chemical Engineering Science, 1997, 52(7): 1125--1139.
  • 4Akoglu K, Tavare N S, Garside J. Dynamic Simulation of a Non-isothermal MSMPR Crystallizer. Chemical Engineering Communication, 1984, 29:353--367.
  • 5Miller S M, Rawlings J B. Model Identification and Control Strategies for Batch Cooling Crystallizers. AIChE J., 1994,40 (8): 1312--1327.
  • 6Chung S H, Ma D L, Braatz R D. Optimal Model-based Experimental Design in Batch Crystallization. Chemometrics and Intelligent Laboratory Systems, 2000, 50:83--90.
  • 7Yan F Q, Rasmuson A C. Estimation of Crystallization Kinetics from Batch Cooling Experiments. AIChE J., 1994, 40 (5):799--812.
  • 8Hloznv L, Sato A, Kubota No. On-line Measurement of Supersaturation During Batch Cooling Crystallization of Ammonium Alum. Journal of Chemical Engineering of Japan, 1992, 25 (5): 604--606.
  • 9Singh B. Using a Crystal Size Distribution Sensor to Improve the Operation and Control of Batch Crystallizers. Analytical Proceedings, 1993, 30 (12): 495--496.
  • 10Fevotte G, Klein J P. Application of On-line Calorimetry to the Advanced Control of Batch Crystallizers. Chemical Engineering Science, 1994, 49 (9) : 1323--1336.

共引文献21

同被引文献49

引证文献4

二级引证文献11

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部