An optimal multivariable controller for trans critical CO2 refrigeration cycle with an adjustable ejector

被引:39
作者
He Yang [1 ]
Deng Jianqiang [1 ]
Yang Fusheng [1 ]
Zhang Zaoxiao [1 ]
机构
[1] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
Transcritical CO2 refrigeration; Adjustable ejector; Dynamic model; Multivariable controller; HEAT-EXCHANGER; HIGH-PRESSURE; SYSTEM; MODEL; PERFORMANCE;
D O I
10.1016/j.enconman.2017.03.070
中图分类号
O414.1 [热力学];
学科分类号
摘要
The fixed ejector has to work under a restricted operating condition to keep its positive effectiveness on the transcritical CO2 refrigeration cycle, and a controllable ejector will be helpful. In this paper, an optimal multivariable controller based on the dynamic model is proposed to improve transcritical CO2 refrigeration cycle with an adjustable ejector (TCRAE). A nonlinear dynamic model is first developed to model the dynamic characteristic of TCRAE. The corresponding model linearization is carried out and the simulation results reproduce transient behavior of the nonlinear model very well. Based on the developed model, an optimal multivariable controller with a tracker based linear quadratic state feedback algorithm and a predictor using steepest descent method is designed. The controller is finally applied on the experimental apparatus and the performance is verified. Using the tracker only, the gas cooler pressure and chilled water outlet temperature (cooling capacity) are well tracked rejecting the disturbances from each other. Furthermore, by the predictor, the optimal gas cooler pressure for a constant cooling capacity is actually approached on the experimental apparatus with a settling time about 700 s. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:466 / 476
页数:11
相关论文
共 15 条
[1]   A general model for evaluation of vapor ejectors performance for application in refrigeration [J].
Cardemil, Jose M. ;
Colle, Sergio .
ENERGY CONVERSION AND MANAGEMENT, 2012, 64 :79-86
[2]   A real-time algorithm for the determination of R744 systems optimal high pressure [J].
Cecchinato, Luca ;
Corradi, Marco ;
Cosi, Giovanni ;
Minetto, Silvia ;
Rampazzo, Mirco .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2012, 35 (04) :817-826
[3]   The optimum high pressure for CO2 transcritical refrigeration systems with internal heat exchangers [J].
Chen, Y ;
Gu, JJ .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2005, 28 (08) :1238-1249
[4]   Performance evaluation and optimal design of supermarket refrigeration systems with supermarket model "SuperSim". Part II: Model applications [J].
Ge, Y. T. ;
Tassou, S. A. .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2011, 34 (02) :540-549
[5]  
GNIELINSKI V, 1976, INT CHEM ENG, V16, P359
[6]   RECENT TRENDS IN LINEAR OPTIMAL QUADRATIC MULTIVARIABLE CONTROL-SYSTEM DESIGN [J].
JOHNSON, MA ;
GRIMBLE, MJ .
IEE PROCEEDINGS-D CONTROL THEORY AND APPLICATIONS, 1987, 134 (01) :53-71
[7]   Development of a microchannel evaporator model for a CO2 air-conditioning system [J].
Kim, MH ;
Bullard, CW .
ENERGY, 2001, 26 (10) :931-948
[8]   A study on the real time optimal control method for heat rejection pressure of a CO2 refrigeration system with an internal heat exchanger [J].
Kim, Mo Se ;
Shin, Chang Soo ;
Kim, Min Soo .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2014, 48 :87-99
[9]   Experimental investigation on the effect of mixing length on the performance of two-phase ejector for CO2 refrigeration cycle with and without heat exchanger [J].
Nakagawa, M. ;
Marasigan, A. R. ;
Matsukawa, T. ;
Kurashina, A. .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2011, 34 (07) :1604-1613
[10]   Multivariable control-oriented modeling of a direct expansion (DX) air conditioning (A/C) system [J].
Qi, Qi ;
Deng, Shiming .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2008, 31 (05) :841-849