Model Based Optimization of Energy Consumption in Milk Evaporators

被引:2
作者
Tsochatzidi, Artemis [1 ]
Arvanitidis, Achilleas L. [1 ]
Georgiadis, Michael C. [1 ]
机构
[1] Aristotle Univ Thessaloniki, Dept Chem Engn, Thessaloniki 54124, Greece
关键词
milk industry; falling film evaporator; thermal vapor recompression; mechanical vapor recompression; dynamic optimization; global system analysis; FALLING-FILM EVAPORATORS; PERFORMANCE; DESIGN; DAIRY; SIMULATION;
D O I
10.3390/pr12010209
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work explores five falling film evaporator (FFE) simulation approaches combined with energy consumption minimization strategies, namely Mechanical Vapor Recompression and Thermal Vapor Recompression (MVR and TVR, respectively). Global system analysis and advanced dynamic optimization strategies are then investigated to minimize steam consumption, the cost of steam, and the total annualized cost and to maximize product yield. The results indicate that higher TVR discharge pressures, or MVR compression ratios, along with higher feed temperatures, enhance evaporation but increase operational costs. The most economical option includes three evaporator effects with TVR to achieve 50% product dry mass content. However, for a 35% dry mass content, MVR becomes cost-effective with an 11% reduction in unit electricity prices or a simultaneous 7% drop in electricity prices and a 5% increase in gas-based steam prices. Furthermore, switching from milk powder production to milk concentrates leads to an annual cost reduction ranging from 10.8 to 44%. Additionally, a forecasted 20% (or more) reduction in biomass-based steam cost can lead to lower annual expenditure compared with the nominal NG-based steam case. Regarding the total annualized cost, for a new plant design, optimization strategies lead to a 9-45% reduction in the total cost depending on the case under consideration.
引用
收藏
页数:28
相关论文
共 28 条
[1]  
[Anonymous], 1997, Siemens Process Systems Engineering gPROMS
[2]   Mathematical modelling and dynamic simulation of multi-effect falling-film evaporator for milk powder production [J].
Bojnourd, Fateme Medhat ;
Fanaei, Mohammad Ali ;
Zohreie, Hadi .
MATHEMATICAL AND COMPUTER MODELLING OF DYNAMICAL SYSTEMS, 2015, 21 (04) :336-358
[3]  
BOUMAN S, 1993, J SOC DAIRY TECHNOL, V46, P100, DOI 10.1111/j.1471-0307.1993.tb01256.x
[4]  
Choi Y., 1986, Transport Phenomena, VVolume 1, P99
[5]   Integrating environmental impact assessment into new product development and processing-technology selection: Milk concentrates as substitutes for milk powders [J].
Depping, Verena ;
Grunow, Martin ;
van Middelaar, Corina ;
Dumpler, Joseph .
JOURNAL OF CLEANER PRODUCTION, 2017, 149 :1-10
[6]   Analysis of the dynamic response of falling-film evaporators considering fouling [J].
Diaz-Ovalle, Christian O. ;
Gonzalez-Alatorre, Guillermo ;
Alvarado, Juan F. J. .
FOOD AND BIOPRODUCTS PROCESSING, 2017, 104 :124-136
[7]  
Eurostat, Natural Gas Price Statistics
[8]   Effect of thermo-compression on the design and performance of falling-film multi-effect evaporator [J].
Galvan-Angeles, Emmanuel ;
Diaz-Ovalle, Christian O. ;
Gonzalez-Alatorre, Guillermo ;
Omar Castrejon-Gonzalez, Edgar ;
Vazquez-Roman, Richart .
FOOD AND BIOPRODUCTS PROCESSING, 2015, 96 :65-77
[9]   Performance evaluation of falling film evaporators in the dairy industry [J].
Gourdon, Mathias ;
Mura, Ernesto .
FOOD AND BIOPRODUCTS PROCESSING, 2017, 101 :22-31
[10]  
Haasbroek A, 2013, 2013 IEEE INTERNATIONAL CONFERENCE ON INDUSTRIAL TECHNOLOGY (ICIT), P46, DOI 10.1109/ICIT.2013.6505646