Sigurd Skogestad

Articles in Scholarly Journals [Incomplete List]

  1. L1/Q Approach for efficient computation of disturbance rejection measures for feedback control?
    Journal of Process Control, vol. 17, no. 6, pp. 501–508, 2007
  2. Application of plantwide control to the HDA process. I—steady-state optimization and self-optimizing control
    Control Engineering Practice, vol. 15, no. 10, pp. 1222–1237, 2007
  3. Control of fuel cell power output
    Journal of Process Control, vol. 17, no. 4, pp. 333–347, 2007
  4. Optimal operation of simple refrigeration cyclesPart I: Degrees of freedom and optimality of sub-cooling
    Computers & Chemical Engineering, vol. 31, no. 5-6, pp. 712–721, 2007
  5. Controllability analysis of two-phase pipeline-riser systems at riser slugging conditions
    Control Engineering Practice, vol. 15, no. 5, pp. 567–581, 2007
  6. Selection of Control Structure and Temperature Location for Two-product Distillation Columns
    Chemical Engineering Research and Design, vol. 85, no. A3, pp. 293–306, 2007
  7. Industrial & Engineering Chemistry Research, vol. 45, no. 26, pp. 9024–9032, 2006
  8. Industrial & Engineering Chemistry Research, vol. 45, no. 5, pp. 1751–1757, 2006
  9. Industrial & Engineering Chemistry Research, vol. 45, no. 23, pp. 7817–7822, 2006
  10. Control-oriented modelling and experimental study of the transient response of a high-temperature polymer fuel cell
    Journal of Power Sources, vol. 162, no. 1, pp. 215–227, 2006
  11. Feasible separations and entrainer selection rules for heteroazeotropic batch distillation
    Chemical Engineering Science, vol. 60, no. 11, pp. 2895–2909, 2005
  12. Minimum energy diagrams for multieffect distillation arrangements
    AIChE Journal, vol. 51, no. 6, pp. 1714–1725, 2005
  13. Analysis and control of heteroazeotropic batch distillation
    AIChE Journal, vol. 51, no. 4, pp. 1144–1157, 2005
  14. Achievable input performance of linear systems under feedback control
    International Journal of Control, vol. 78, no. 16, pp. 1327–1341, 2005
  15. Multi-effect distillation applied to an industrial case study
    Chemical Engineering and Processing, vol. 44, no. 8, pp. 819–826, 2005
  16. Controller design for serial processes
    Journal of Process Control, vol. 15, no. 3, pp. 259–271, 2005
  17. Industrial & Engineering Chemistry Research, vol. 44, no. 11, pp. 3966–3972, 2005
  18. Industrial & Engineering Chemistry Research, vol. 44, no. 7, pp. 2207–2217, 2005
  19. Industrial & Engineering Chemistry Research, vol. 44, no. 4, pp. 863–867, 2005
  20. Feedforward Control under the Presence of Uncertainty
    European Journal of Control, vol. 10, no. 1, pp. 30–46, 2004
  21. Corrections and comments from the author on the paper “Simple analytic rules for model reduction and PID controller tuning”, Journal of Process Control 13 (2003) 291–309
    Journal of Process Control, vol. 14, no. 4, p. 465, 2004
  22. Separation of ternary heteroazeotropic mixtures in a closed multivessel batch distillation–decanter hybrid
    Chemical Engineering and Processing, vol. 43, no. 3, pp. 291–304, 2004
  23. Industrial & Engineering Chemistry Research, vol. 43, no. 14, pp. 3994–3999, 2004
  24. Time requirements for heteroazeotropic distillation in batch columns
    Computers & Chemical Engineering, vol. 28, no. 9, pp. 1689–1700, 2004
  25. Time (energy) requirements in closed batch distillation arrangements
    Computers & Chemical Engineering, vol. 28, no. 5, pp. 829–837, 2004
  26. Selecting appropriate control variables for a heat-integrated distillation system with prefractionator
    Computers & Chemical Engineering, vol. 28, no. 5, pp. 683–691, 2004
  27. Near-optimal operation by self-optimizing control: from process control to marathon running and business systems
    Computers & Chemical Engineering, vol. 29, no. 1, pp. 127–137, 2004
  28. Control structure design for complete chemical plants
    Computers & Chemical Engineering, vol. 28, no. 1-2, pp. 219–234, 2004
  29. pH-neutralization: integrated process and control design
    Computers & Chemical Engineering, 2003
  30. Azeotropic phase equilibrium diagrams: a survey
    Chemical Engineering Science, vol. 58, no. 10, pp. 1903–1953, 2003
  31. Reactor/separator processes with recycles-2. Design for composition control
    Computers & Chemical Engineering, vol. 27, no. 3, pp. 401–421, 2003
  32. Simple analytic rules for model reduction and PID controller tuning
    Journal of Process Control, vol. 13, no. 4, pp. 291–309, 2003
  33. Industrial & Engineering Chemistry Research, vol. 42, no. 6, pp. 1225–1234, 2003
  34. Selection of variables for stabilizing control using pole vectors
    IEEE Transactions on Automatic Control, vol. 48, no. 8, pp. 1393–1398, 2003
  35. Implementation of Optimal Operation for Heat Integrated Distillation Columns
    Chemical Engineering Research and Design, vol. 81, no. A2, pp. 277–281, 2003
  36. Minimum Energy Consumption in Multicomponent Distillation. 1. Vmin Diagram for a Two-Product Column
    Industrial & Engineering Chemistry Research, vol. 42, no. 3, pp. 596–604, 2003
  37. Minimum Energy Consumption in Multicomponent Distillation. 2. Three-Product Petlyuk Arrangements
    Industrial & Engineering Chemistry Research, vol. 42, no. 3, pp. 605–615, 2003
  38. Minimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements
    Industrial & Engineering Chemistry Research, vol. 42, no. 3, pp. 616–629, 2003
  39. Industrial & Engineering Chemistry Research, vol. 42, no. 10, pp. 2198–2208, 2003
  40. Industrial & Engineering Chemistry Research, vol. 42, no. 14, pp. 3273–3284, 2003
  41. Achievable performance of multivariable systems with unstable zeros and poles
    International Journal of Control, vol. 74, no. 11, pp. 1131–1139, 2001
  42. Industrial & Engineering Chemistry Research, vol. 40, no. 22, pp. 4889–4901, 2001
  43. Self-optimizing control: the missing link between steady-state optimization and control
    Computers & Chemical Engineering, vol. 24, no. 2-7, pp. 569–575, 2000
  44. A systematic approach to the design of buffer tanks
    Computers & Chemical Engineering, vol. 24, no. 2-7, pp. 1395–1401, 2000
  45. Plantwide control: the search for the self-optimizing control structure
    Journal of Process Control, vol. 10, no. 5, pp. 487–507, 2000
  46. Closed operation of multivessel batch distillation: Experimental verification
    AIChE Journal, vol. 46, no. 6, pp. 1209–1217, 2000
  47. Optimal operation of Petlyuk distillation: steady-state behavior
    Journal of Process Control, vol. 9, no. 5, pp. 407–424, 1999
  48. Editorial
    Computers & Chemical Engineering, vol. 23, no. 4-5, p. 449, 1999
  49. Editorial
    Computers & Chemical Engineering, vol. 23, no. 4-5, pp. 451–455, 1999
  50. Optimal operation of heat exchanger networks
    Computers & Chemical Engineering, vol. 23, no. 4-5, pp. 509–522, 1999
  51. Two-degree-of-freedom controller design for an ill-conditioned distillation process using µ-synthesis
    IEEE Transactions on Control Systems Technology, vol. 7, no. 1, pp. 12–21, 1999
  52. Effect of RHP zeros and poles on the sensitivity functions in multivariable systems
    Journal of Process Control, vol. 8, no. 3, pp. 155–164, 1998
  53. Analysis of instability in an industrial ammonia reactor
    AIChE Journal, vol. 44, no. 4, pp. 888–895, 1998
  54. Multivessel batch distillation
    AIChE Journal, vol. 43, no. 4, pp. 971–978, 1997
  55. Complex distillation arrangements: Extending the petlyuk ideas
    Computers & Chemical Engineering, vol. 21, pp. S237–S242, 1997
  56. SVD controllers for H2-, H8- and µ-optimal control
    Automatica, vol. 33, no. 3, pp. 433–439, 1997
  57. Dynamics and Control of Distillation Columns: A Tutorial Introduction
    Chemical Engineering Research and Design, vol. 75, no. A6, pp. 539–562, 1997
  58. Industrial & Engineering Chemistry Research, vol. 36, no. 3, pp. 697–705, 1997
  59. Dynamic behaviour of integrated plants
    Journal of Process Control, vol. 6, no. 2-3, pp. 145–156, 1996
  60. Industrial & Engineering Chemistry Research, vol. 35, no. 2, pp. 475–484, 1996
  61. A procedure for SISO controllability analysis—With application to design of pH neutralization processes
    Computers & Chemical Engineering, vol. 20, no. 4, pp. 373–386, 1996
  62. The use of RGA and condition number as robustness measures
    Computers & Chemical Engineering, vol. 20, pp. S1005–S1010, 1996
  63. Total reflux operation of multivessel batch distillation
    Computers & Chemical Engineering, vol. 20, pp. S1041–S1046, 1996
  64. Optimal startup procedures for batch distillation
    Computers & Chemical Engineering, vol. 20, pp. S1257–S1262, 1996
  65. Loopshaping for robust performance
    International Journal of Robust and Nonlinear Control, vol. 6, no. 8, pp. 805–823, 1996
  66. Comparison of regular and inverted batch distillation
    Chemical Engineering Science, vol. 51, no. 22, pp. 4949–4962, 1996
  67. Limitations of dynamic matrix control
    Computers & Chemical Engineering, vol. 19, no. 4, pp. 409–421, 1995
  68. Industrial & Engineering Chemistry Research, vol. 34, no. 12, pp. 4395–4405, 1995
  69. Industrial & Engineering Chemistry Research, vol. 34, no. 6, pp. 2094–2103, 1995
  70. Control strategies for reactive batch distillation
    Journal of Process Control, vol. 4, no. 4, pp. 205–217, 1994
  71. Industrial & Engineering Chemistry Research, vol. 33, no. 3, pp. 631–640, 1994
  72. Sequential design of decentralized controllers,
    Automatica, vol. 30, no. 10, pp. 1601–1607, 1994
  73. Opitimal control and on-line operation of reactive batch distillation
    Computers & Chemical Engineering, vol. 18, pp. S391–S395, 1994
  74. Instability of distillation columns
    AIChE Journal, vol. 40, no. 9, pp. 1466–1478, 1994
  75. Effects of recycle on dynamics and control of chemical processing plants
    Computers & Chemical Engineering, vol. 18, pp. S529–S534, 1994
  76. Dynamic models for heat exchangers and heat exchanger networks
    Computers & Chemical Engineering, vol. 18, pp. S459–S463, 1994
  77. Industrial & Engineering Chemistry Research, vol. 33, no. 9, pp. 2134–2139, 1994
  78. Procedure for regulatory control structure selection with application to the FCC process
    AIChE Journal, vol. 39, no. 12, pp. 1938–1953, 1993
  79. Output estimation using multiple secondary measurements: High-purity distillation
    AIChE Journal, vol. 39, no. 10, pp. 1641–1653, 1993
  80. Simple frequency-dependent tools for control system analysis, structure selection and design
    Automatica, vol. 28, no. 5, pp. 989–996, 1992
  81. Multiple steady states in ideal two-product distillation
    AIChE Journal, vol. 37, no. 4, pp. 499–511, 1991
  82. Robust control of homogeneous azeotropic distillation columns
    AIChE Journal, vol. 37, no. 12, pp. 1810–1824, 1991
  83. Industrial & Engineering Chemistry Research, vol. 30, no. 12, pp. 2543–2555, 1991
  84. Industrial & Engineering Chemistry Research, vol. 30, no. 12, pp. 2555–2564, 1991
  85. Selecting the best distillation control configuration
    AIChE Journal, vol. 36, no. 5, pp. 753–764, 1990
  86. Mu-optimal LV-control of distillation columns
    Computers & Chemical Engineering, vol. 14, no. 4-5, pp. 401–413, 1990
  87. Industrial & Engineering Chemistry Research, vol. 29, no. 12, pp. 2339–2346, 1990
  88. Robust performance of decentralized control systems by independent designs
    Automatica, vol. 25, no. 1, pp. 119–125, 1989
  89. LV-Control of a high-purity distillation column
    Chemical Engineering Science, vol. 43, no. 1, pp. 33–48, 1988
  90. Understanding the dynamic behavior of distillation columns
    Industrial & Engineering Chemistry Research, vol. 27, no. 10, pp. 1848–1862, 1988
  91. Robust control of ill-conditioned plants: high-purity distillation
    IEEE Transactions on Automatic Control, vol. 33, no. 12, pp. 1092–1105, 1988
  92. Some new properties of the structured singular value
    IEEE Transactions on Automatic Control, vol. 33, no. 12, pp. 1151–1154, 1988
  93. Industrial & Engineering Chemistry Research, vol. 27, no. 5, pp. 898–898, 1988
  94. Industrial & Engineering Chemistry Research, vol. 26, no. 11, pp. 2323–2330, 1987
  95. Industrial & Engineering Chemistry Research, vol. 26, no. 10, pp. 2029–2035, 1987
  96. Control configuration selection for distillation columns
    AIChE Journal, vol. 33, no. 10, pp. 1620–1635, 1987
  97. Design of resilient processing plants-IX. Effect of model uncertainty on dynamic resilience
    Chemical Engineering Science, vol. 42, no. 7, pp. 1765–1780, 1987
  98. The dominant time constant for distillation columns
    Computers & Chemical Engineering, vol. 11, no. 6, pp. 607–617, 1987
  99. Internal model control: PID controller design
    Industrial & Engineering Chemistry Process Design and Development, vol. 25, no. 1, pp. 252–265, 1986
  100. Experience in Norsk Hydro with cubic equations of state
    Fluid Phase Equilibria, vol. 13, no. 1, pp. 179–188, 1983
  101. Prediction of VLE behavior in concentrated electrolyte solutions
    Fluid Phase Equilibria, vol. 13, no. 1, pp. 341–350, 1983