中文论文文摘

    [1] 卢谦和．造纸原理与工程[M]．北京：中国轻工业出版社，2004：1-4，22-73．
[2] 隆言泉主编. 造纸原理与工程. 北京: 中国轻工业出版社，1994
[3] 制浆造纸手册编写组. 制浆造纸手册. 北京: 中国轻工业出版社，1991
[4] R.J. Kerekes. New Perspectives on Refining Intensity [C]. Third International Refining Conference & Exhibition, Atlanta,1995.
[5] D.M. Martinez and R.I. Kerekes. Forces on Fibres in Iow-Consisiency Refining [J]. TAPPI Journal.Vol 77, No. 12, 1994：119-123.
[6] S. Dharni, Estimation of the Number of Impacts Imparted to the pulp in a Disc Refiner [R]. Masters of Pulp & Paper Engineering, Project Report, DepI, of Chemical Engineering, Pulp & Paper Centre, Univ. of British Columhia. 1989.
[7] Jixian Dong, Jiangong Gu. CONSTRUCTION AND ANALYSES OF DYNAMIC AND ENERGY CONSUMPTION MODELS IN HIGH CONSISTENCY REFINING [C]. 3rd ISETPP. 2006,11:384-388.
[8] J. Lumianen, Refining performances with separated and mixed pulps for fine-paper production [J]. ATIP Journal.Vol 51, No. 3, 1997：99-108.
[9] D.M. Martinez and R.I. Kerekes. Forces on Fibres in Iow-Consisiency Refining [J]. TAPPI Journal.Vol 77, No. 12, 1994：119-123.
[10] R.J. Kerekes. New Perspectives on Refining Intensity [C]. Third International Refining Conference & Exhibition, Atlanta,1995. [11]EDSON ALEIXO. Triple-Cone Refiner Yields Energy Efficiency, Improved Paper Specs [J]. P&P 2004,(12): 45-50
[12] 葛培琪. 周以齐, 刘鸣, 孙家林, 刘延俊. 新型锥形磨浆机的性能分析. 纸和造纸, 2002,3:26-28
[13] 叶冠军. 高浓盘磨打浆和制浆. 湖北造纸, 1996,1:37-42
[14] 陈佩蓉等. 制浆造纸实验[M]．北京：中国轻工业出版社，1990：197-236，322-323
[15] 刘书钗. 制浆造纸分析与检测[M]．北京：化学工业出版社，2004：183-239
[16] Höglund H., Bäck R., Falk B., Jackson M.: ThermopulpTM – a new energy efficient ,mechanical pulping  process. International Mechanical Pulping Conference. Ottawa, Canada, 12-15 June 1995, pp. 213-225.
[17] Sabourin M. Xu E. Musselman R.: Evaluation of refiner disc speed, plate design and consistency on high  pressure / low residence (RTS)TMP pulps. International Mechanical Pulping Conference. Stockholm, Sweden, 9-13 June 1997, pp. 241-249
[18] Härkönen E., Ruottu S., Ruottu A., Johansson O.: A theoretical model for a TMP-refiner. International Mechanical Pulping Conference. Stockholm, Sweden, 9-13 June 1997, pp. 95-102.
[19] Miles K.B., May W.D.:The flow of pulp in chip refiners. Journal of Pulp and Paper Science, 16(1990):2, 63-71.
[20] Kure, K.-A., Dahlqvist, G. Development of structural fiber properties in high intensity refining. Pulp & Paper Canada 99 (7), T233-T237 (1998).
[21] Petteri Vuorio and Peter Bergquist Presented by Anders Hawén, NEW REFINER SEGMENTS TECHNOLOGY TO OPTIMIZE FIBER QUALITY AND ENERGY CONSUMPTION OF REFINER MECHANICAL PULP. TAPPSA. International Convention Centre, Durban, 8-11 October,2002.
[22] Alahautala T., Vattulainen J., Hernberg R.: Quantitative visualisation of pulp refining in a production line  refiner. International Mechanical Pulping Conference. Houston, TX, USA, 24-26 May 1999, pp. 87-95.
[23] Härkönen E., Huusari E., Raviala P.: Residence time of fiber in a single disc refiner. International Mechanical Pulping Conference. Houston, TX, USA, 24-26 May 1999, pp. 77-86.
[24] Hoglund, H., Tistad, G. Frequency and temperature in chip refining, Paperi ja Puu- Papper ochTra, No 3,1977.
[25] Sundholm, J., Heikkurinen, A. and Mannstrom, B., The role of rate of rotation and frequency in refiner mechanical pulping., IMPC, Vancouver, 1987.
[26] Jackson,M. and Akerlund, G.: Preheating and refiner housing pressure affects the quality of TMP and CTMP.  Tappi 67(1),1984, p54-58.
[27] Jackson, M., Danielsson, O., Falk B., Thermopulp- a new energy efficient mechanical pulping process, SPCI, Stockholm, 1996
[28] Kure, K.-A., Sabourin, M.J., Dahlqvist, G., Helle, T., Adjusting refining intensity by changing refiner plate design and rotational speed – effects on structural fibre properties
[29] Strand, B.C., Mokvist, A., Falk, B., Jackson, M., The effect of production rate on specific energy consumption in high consistency chip refining, IMPC, Oslo, 1993.
[30] Karnis, A. The mechanism of fibre development in mechanical pulping. Journal of Pulp and Paper Science 20 (10) J280-J288, 1994.
[31] Stationwala, M.I., Miles, K.B., Karnis, A. Effect of feed rate on refining. Journal of Pulp and Paper Science 20 (8), J236-J240 (1994).
[32] Reme, P.A., Helle, T., Johnsen, P.O. Fibre characteristics of various mechanical pulp grades. Proceedings 1997 International Mechanical Pulping Conference, 297-308, Stockholm, 1997.
[33] Miles, K.B. A simplified method for calculating the residence time and refining intensity in a chip refiner. Paperi ja Puu 73 (9), 852-857 (1991).
[34] Sundholm, J., Heikkurinen, A., Mannström, B. The role of rate of rotation and impact frequency in refiner mechanical pulping. Paper ja Puu 70 (5), 446-451 (1988).
[35] Sabourin, M., Xu, E., Musselman, R. Evaluation of refiner disc speed, plate design and consistency on high pressure/low residence (RTS) TMP pulps. Proceedings 1997 International Mechanical Pulping Conference, 241-249 Stockholm 1997.
[36] Fox, T. S. (1980).Inside a disk refiner. Preprints, Internation Symposium on Fundamenral Concepts of Refing,Appletion,281-313.
[37] 莫芳灿.制浆造纸工艺自动化. 北京:轻工业出版社. 1981
[38] Lewis, P.J.,Danforth,D.W.(1962). Stock preparation analysis. Tappi,45(3):185-188.
[39] Leider, P.J, Rihs, J.(1977a).Understanding the disk refiner. part 1. the hydrawlic behavior. Tappi, 60 (9) : 98-102.
[40] Leider, P. J. Nissan, A. H. (1977b). Understanding the disk refiner.  part 2. mechni cal  trea tmen t of the fibers. Tappi, 60 (10):85-89.
[41] Lumiainen, J. (1990).New theory can improve practice. PPI, 32 (8):46-54.
[42] Lumiainen, J. (1991).Refining intensity at low consistency-critical factors.  Paper Technology, 32(1I):22-26.
[43] Banks, A. (1967). Design considerations and characteristics of disk refiners. Paper Technology, 8(4):363-369.
[44] Hourani, M. J. (1988A). Fiber flocculation in pulp suspension flow, part1: theoretical results. Tappi, 71(6): 115-118.
[45] Hourani, M. J. (1988A). Fiber flocculation in pulp suspension flow, part2: experimental results. Tappi, 71(6): 186-189.
[46] 张政江．打浆过程的建模与先进控制研究[D]．浙江：浙江大学，2001．
[47] 张政江，皮道映，孙优贤. 高浓打浆过程的数学模型.中国造纸学报,2000,15:93-97
[48] Jixian Dong, Jiangong Gu. CONSTRUCTION AND ANALYSES OF DYNAMIC AND ENERGY CONSUMPTION MODELS IN HIGH CONSISTENCY REFINING. 3rd ISETPP. 2006,11:384-388
[49] Juha-Pekka Huhtanen 1 Reijo Karvinen,1 Kai Vikman2 and Petteri Vuorio3 Presented by Anders Hawen. Theoretical background of new energy saving refiner segments design. African Pulp and Paper Week 2004
[50] ARJAS, A.: Residence Time Distributions in Conical Refiners and Refining Systems, Preprints, Intl. Symposium on Fundamental Concepts of Refining, Appleton, WI, 1980, pp. 8-20.
[51] 刘初鹏，J.C.ROX，欧建志，G.CAUCA. 磨浆过程的流体力学分析. 造纸科学与技术, Vol. 20(3) J16-18, 2001.
[52] MILES, K.B., DANA, H.R.; MAY, W.D.: The Flow of Steam in Chip Refiners, Preprints, International Symposium on Fundamental Concepts of Refining, Appleton, WI, 1980, pp. 30-42.
[53] MILES. K.B.; MAY. W.D.: The Flow of Pulp in Chip Refiners, Journal of Pulp and Paper Science, Vol. 16(2) J63-72, March 1990.
[54] 李世扬.高浓磨区能耗解析. 轻工机械, 1996,2:16-19.
[55] Jixian DONG, Jiangong GU: The Formulation and Analysis of Dynamic and Energy Consumption Model in High Consistency Pulp-Refining, 3rd ISETPP. 2006,11: 384-388.
[56] 王忠厚. 制浆造纸工业计算手册. 中国轻工业出版社，1994
[57] Bethune, J.H., Mercier, E. Speciafic energy control of SCMP refiners at NBIP. Pulp & Paper Canada, 1982, 18: 307-314
[58] Arjas,A.(1980). Constant versus variable rotational during the refinering process and the adapt-set system. Preprints, Internation Symposium on Fundamental Concepts of Refing, Appletion, 264-265
[59] Owen J.et al. A practical approach to operator acceptance of advanced control with dual functionality: Proceeding Control System 98, Finland
[60] K. Miles.  A simplified method for caculating the residence time and refining intensity in a chip refiner: Paper ja Puu, 1991, 73(9):852-857
[61] Strand B.C. Effect of production rate on specific energy  consumption in high consistency chip refining: Proc.Intl.Mechanical Pulp Conf.，Oslo，1993
[62] 刘俊杰译. 精浆机的自动控制系统及其选择. 国外造纸，1983，12：44-45
[63] Ettaleb et al. Method of refining wood chips or pulp in a high consistency conical disc refiner: US, US 2006/0180684 A1[P]. 2006-8-17
[64] Ettaleb et al. Method of refining wood chips or pulp in a high consistency conical disc refiner: US, US 2006/0180684 A1[P]. 2006-8-17
[65] Murton K.D. Production rate effect on TMP pulp quality and energy consumption: J. Pulp Paper Sci., 1997, 23(8): 411-416
[66] K. Miles.  Refining intensity and pulp quality in high consistency refiner: Paper ja Puu, 1990, 72(5): 508-514
[67] K. Miles et al.  Predicting the performance of a chip refiner. A constitutive approach: J. Pulp Paper Sci., 1993, 19(6): 268-274
[68] 张政江．打浆过程的建模与先进控制研究[D]．浙江：浙江大学，2001
[69] 孙优贤. 打浆过程控制的现状和趋势. 中国造纸，2000,3：51-56
[70] 符曦. 系统最优化及控制. 北京: 机械工业出版社，1995
[71] 陈苏平，皮道映，郭爱莲.新编机械工程技术手册.经济日报出版社.1991

外文论文文摘

    [1] 卢谦和．造纸原理与工程[M]．北京：中国轻工业出版社，2004：1-4，22-73．
[2] 隆言泉主编. 造纸原理与工程. 北京: 中国轻工业出版社，1994
[3] 制浆造纸手册编写组. 制浆造纸手册. 北京: 中国轻工业出版社，1991
[4] R.J. Kerekes. New Perspectives on Refining Intensity [C]. Third International Refining Conference & Exhibition, Atlanta,1995.
[5] D.M. Martinez and R.I. Kerekes. Forces on Fibres in Iow-Consisiency Refining [J]. TAPPI Journal.Vol 77, No. 12, 1994：119-123.
[6] S. Dharni, Estimation of the Number of Impacts Imparted to the pulp in a Disc Refiner [R]. Masters of Pulp & Paper Engineering, Project Report, DepI, of Chemical Engineering, Pulp & Paper Centre, Univ. of British Columhia. 1989.
[7] Jixian Dong, Jiangong Gu. CONSTRUCTION AND ANALYSES OF DYNAMIC AND ENERGY CONSUMPTION MODELS IN HIGH CONSISTENCY REFINING [C]. 3rd ISETPP. 2006,11:384-388.
[8] J. Lumianen, Refining performances with separated and mixed pulps for fine-paper production [J]. ATIP Journal.Vol 51, No. 3, 1997：99-108.
[9] D.M. Martinez and R.I. Kerekes. Forces on Fibres in Iow-Consisiency Refining [J]. TAPPI Journal.Vol 77, No. 12, 1994：119-123.
[10] R.J. Kerekes. New Perspectives on Refining Intensity [C]. Third International Refining Conference & Exhibition, Atlanta,1995. [11]EDSON ALEIXO. Triple-Cone Refiner Yields Energy Efficiency, Improved Paper Specs [J]. P&P 2004,(12): 45-50
[12] 葛培琪. 周以齐, 刘鸣, 孙家林, 刘延俊. 新型锥形磨浆机的性能分析. 纸和造纸, 2002,3:26-28
[13] 叶冠军. 高浓盘磨打浆和制浆. 湖北造纸, 1996,1:37-42
[14] 陈佩蓉等. 制浆造纸实验[M]．北京：中国轻工业出版社，1990：197-236，322-323
[15] 刘书钗. 制浆造纸分析与检测[M]．北京：化学工业出版社，2004：183-239
[16] Höglund H., Bäck R., Falk B., Jackson M.: ThermopulpTM – a new energy efficient ,mechanical pulping  process. International Mechanical Pulping Conference. Ottawa, Canada, 12-15 June 1995, pp. 213-225.
[17] Sabourin M. Xu E. Musselman R.: Evaluation of refiner disc speed, plate design and consistency on high  pressure / low residence (RTS)TMP pulps. International Mechanical Pulping Conference. Stockholm, Sweden, 9-13 June 1997, pp. 241-249
[18] Härkönen E., Ruottu S., Ruottu A., Johansson O.: A theoretical model for a TMP-refiner. International Mechanical Pulping Conference. Stockholm, Sweden, 9-13 June 1997, pp. 95-102.
[19] Miles K.B., May W.D.:The flow of pulp in chip refiners. Journal of Pulp and Paper Science, 16(1990):2, 63-71.
[20] Kure, K.-A., Dahlqvist, G. Development of structural fiber properties in high intensity refining. Pulp & Paper Canada 99 (7), T233-T237 (1998).
[21] Petteri Vuorio and Peter Bergquist Presented by Anders Hawén, NEW REFINER SEGMENTS TECHNOLOGY TO OPTIMIZE FIBER QUALITY AND ENERGY CONSUMPTION OF REFINER MECHANICAL PULP. TAPPSA. International Convention Centre, Durban, 8-11 October,2002.
[22] Alahautala T., Vattulainen J., Hernberg R.: Quantitative visualisation of pulp refining in a production line  refiner. International Mechanical Pulping Conference. Houston, TX, USA, 24-26 May 1999, pp. 87-95.
[23] Härkönen E., Huusari E., Raviala P.: Residence time of fiber in a single disc refiner. International Mechanical Pulping Conference. Houston, TX, USA, 24-26 May 1999, pp. 77-86.
[24] Hoglund, H., Tistad, G. Frequency and temperature in chip refining, Paperi ja Puu- Papper ochTra, No 3,1977.
[25] Sundholm, J., Heikkurinen, A. and Mannstrom, B., The role of rate of rotation and frequency in refiner mechanical pulping., IMPC, Vancouver, 1987.
[26] Jackson,M. and Akerlund, G.: Preheating and refiner housing pressure affects the quality of TMP and CTMP.  Tappi 67(1),1984, p54-58.
[27] Jackson, M., Danielsson, O., Falk B., Thermopulp- a new energy efficient mechanical pulping process, SPCI, Stockholm, 1996
[28] Kure, K.-A., Sabourin, M.J., Dahlqvist, G., Helle, T., Adjusting refining intensity by changing refiner plate design and rotational speed – effects on structural fibre properties
[29] Strand, B.C., Mokvist, A., Falk, B., Jackson, M., The effect of production rate on specific energy consumption in high consistency chip refining, IMPC, Oslo, 1993.
[30] Karnis, A. The mechanism of fibre development in mechanical pulping. Journal of Pulp and Paper Science 20 (10) J280-J288, 1994.
[31] Stationwala, M.I., Miles, K.B., Karnis, A. Effect of feed rate on refining. Journal of Pulp and Paper Science 20 (8), J236-J240 (1994).
[32] Reme, P.A., Helle, T., Johnsen, P.O. Fibre characteristics of various mechanical pulp grades. Proceedings 1997 International Mechanical Pulping Conference, 297-308, Stockholm, 1997.
[33] Miles, K.B. A simplified method for calculating the residence time and refining intensity in a chip refiner. Paperi ja Puu 73 (9), 852-857 (1991).
[34] Sundholm, J., Heikkurinen, A., Mannström, B. The role of rate of rotation and impact frequency in refiner mechanical pulping. Paper ja Puu 70 (5), 446-451 (1988).
[35] Sabourin, M., Xu, E., Musselman, R. Evaluation of refiner disc speed, plate design and consistency on high pressure/low residence (RTS) TMP pulps. Proceedings 1997 International Mechanical Pulping Conference, 241-249 Stockholm 1997.
[36] Fox, T. S. (1980).Inside a disk refiner. Preprints, Internation Symposium on Fundamenral Concepts of Refing,Appletion,281-313.
[37] 莫芳灿.制浆造纸工艺自动化. 北京:轻工业出版社. 1981
[38] Lewis, P.J.,Danforth,D.W.(1962). Stock preparation analysis. Tappi,45(3):185-188.
[39] Leider, P.J, Rihs, J.(1977a).Understanding the disk refiner. part 1. the hydrawlic behavior. Tappi, 60 (9) : 98-102.
[40] Leider, P. J. Nissan, A. H. (1977b). Understanding the disk refiner.  part 2. mechni cal  trea tmen t of the fibers. Tappi, 60 (10):85-89.
[41] Lumiainen, J. (1990).New theory can improve practice. PPI, 32 (8):46-54.
[42] Lumiainen, J. (1991).Refining intensity at low consistency-critical factors.  Paper Technology, 32(1I):22-26.
[43] Banks, A. (1967). Design considerations and characteristics of disk refiners. Paper Technology, 8(4):363-369.
[44] Hourani, M. J. (1988A). Fiber flocculation in pulp suspension flow, part1: theoretical results. Tappi, 71(6): 115-118.
[45] Hourani, M. J. (1988A). Fiber flocculation in pulp suspension flow, part2: experimental results. Tappi, 71(6): 186-189.
[46] 张政江．打浆过程的建模与先进控制研究[D]．浙江：浙江大学，2001．
[47] 张政江，皮道映，孙优贤. 高浓打浆过程的数学模型.中国造纸学报,2000,15:93-97
[48] Jixian Dong, Jiangong Gu. CONSTRUCTION AND ANALYSES OF DYNAMIC AND ENERGY CONSUMPTION MODELS IN HIGH CONSISTENCY REFINING. 3rd ISETPP. 2006,11:384-388
[49] Juha-Pekka Huhtanen 1 Reijo Karvinen,1 Kai Vikman2 and Petteri Vuorio3 Presented by Anders Hawen. Theoretical background of new energy saving refiner segments design. African Pulp and Paper Week 2004
[50] ARJAS, A.: Residence Time Distributions in Conical Refiners and Refining Systems, Preprints, Intl. Symposium on Fundamental Concepts of Refining, Appleton, WI, 1980, pp. 8-20.
[51] 刘初鹏，J.C.ROX，欧建志，G.CAUCA. 磨浆过程的流体力学分析. 造纸科学与技术, Vol. 20(3) J16-18, 2001.
[52] MILES, K.B., DANA, H.R.; MAY, W.D.: The Flow of Steam in Chip Refiners, Preprints, International Symposium on Fundamental Concepts of Refining, Appleton, WI, 1980, pp. 30-42.
[53] MILES. K.B.; MAY. W.D.: The Flow of Pulp in Chip Refiners, Journal of Pulp and Paper Science, Vol. 16(2) J63-72, March 1990.
[54] 李世扬.高浓磨区能耗解析. 轻工机械, 1996,2:16-19.
[55] Jixian DONG, Jiangong GU: The Formulation and Analysis of Dynamic and Energy Consumption Model in High Consistency Pulp-Refining, 3rd ISETPP. 2006,11: 384-388.
[56] 王忠厚. 制浆造纸工业计算手册. 中国轻工业出版社，1994
[57] Bethune, J.H., Mercier, E. Speciafic energy control of SCMP refiners at NBIP. Pulp & Paper Canada, 1982, 18: 307-314
[58] Arjas,A.(1980). Constant versus variable rotational during the refinering process and the adapt-set system. Preprints, Internation Symposium on Fundamental Concepts of Refing, Appletion, 264-265
[59] Owen J.et al. A practical approach to operator acceptance of advanced control with dual functionality: Proceeding Control System 98, Finland
[60] K. Miles.  A simplified method for caculating the residence time and refining intensity in a chip refiner: Paper ja Puu, 1991, 73(9):852-857
[61] Strand B.C. Effect of production rate on specific energy  consumption in high consistency chip refining: Proc.Intl.Mechanical Pulp Conf.，Oslo，1993
[62] 刘俊杰译. 精浆机的自动控制系统及其选择. 国外造纸，1983，12：44-45
[63] Ettaleb et al. Method of refining wood chips or pulp in a high consistency conical disc refiner: US, US 2006/0180684 A1[P]. 2006-8-17
[64] Ettaleb et al. Method of refining wood chips or pulp in a high consistency conical disc refiner: US, US 2006/0180684 A1[P]. 2006-8-17
[65] Murton K.D. Production rate effect on TMP pulp quality and energy consumption: J. Pulp Paper Sci., 1997, 23(8): 411-416
[66] K. Miles.  Refining intensity and pulp quality in high consistency refiner: Paper ja Puu, 1990, 72(5): 508-514
[67] K. Miles et al.  Predicting the performance of a chip refiner. A constitutive approach: J. Pulp Paper Sci., 1993, 19(6): 268-274
[68] 张政江．打浆过程的建模与先进控制研究[D]．浙江：浙江大学，2001
[69] 孙优贤. 打浆过程控制的现状和趋势. 中国造纸，2000,3：51-56
[70] 符曦. 系统最优化及控制. 北京: 机械工业出版社，1995
[71] 陈苏平，皮道映，郭爱莲.新编机械工程技术手册.经济日报出版社.1991