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Journal articles on the topic 'Multiple Effect Evaporator'

Author: Grafiati

Published: 5 June 2025

Last updated: 16 July 2025

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1

Chantasiriwan, Somchart. "Increased Energy Efficiency of a Backward-Feed Multiple-Effect Evaporator Compared with a Forward-Feed Multiple-Effect Evaporator in the Cogeneration System of a Sugar Factory." Processes 8, no. 3 (2020): 342. http://dx.doi.org/10.3390/pr8030342.

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The cogeneration system of a sugar factory consists of boiler, steam turbine, and sugar juice evaporation process. The multiple-effect evaporator used for the conventional sugar juice evaporation process is the forward-feed multiple-effect evaporator, in which steam and sugar juice flow in the same direction. The main objective of this paper is to investigate the energy efficiency of the backward-feed multiple-effect evaporator, in which steam and sugar juice flow in opposite directions, compared with that of the forward-feed multiple-effect evaporator. Mathematical models are developed for bo

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2

B., K. Kempegowda. "ANALYSIS OF DRUG IN PHARMACEUTICAL WASTE WATER BY MULTIPLE EFFECT EVAPORATORS." Shanlax International Journal of Arts, Science and Humanities 6, S2 (2019): 141–49. https://doi.org/10.5281/zenodo.2580755.

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<em>Disposal of effluent from pharmaceutical industry is an increasing problem in India and worldwide. The bulk drug manufacturing process involves usage of more organic and inorganic salts, which is becoming major part of high chemical oxygen demand and total dissolved solids. Evaporation and cooling are the common techniques used to extract available salts and reusable water. The pharmaceutical industry of the study uses multiple effect falling and forced circulation evaporator to achieve zero liquid discharge process for pharmaceutical effluent. Multiple Effect Evaporator is a thermal evapo

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3

B.K., Kempegowda. "ANALYSIS OF DRUG IN PHARMACEUTICAL WASTE WATER BY MULTIPLE EFFECT EVAPORATOR." Shanlax International Journal of Arts, Science and Humanities 6, S2 (2019): 228–36. https://doi.org/10.5281/zenodo.2635077.

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<em>Disposal of effluent from pharmaceutical industry is an increasing problem in India and worldwide. The bulk drug manufacturing process involves usage of more organic and inorganic salts, which is becoming major part of high chemical oxygen demand and total dissolved solids. Evaporation and cooling are the common techniques used to extract available salts and reusable water. The pharmaceutical industry of the study uses multiple effect falling and forced circulation evaporator to achieve zero liquid discharge process for pharmaceutical effluent.  Multiple Effect Evaporator is a thermal

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4

Riadi, Indra, Zulfan Adi Putra, and Heri Cahyono. "Thermal integration analysis and improved configuration for multiple effect evaporator system based on pinch analysis." Reaktor 21, no. 2 (2021): 74–93. http://dx.doi.org/10.14710/reaktor.21.2.74-93.

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Pinch analysis for a sugar plant production capacity 4000 TCD has been carried out to reduce its energy consumptions. The plant has ten evaporators that can be configured to several multiple effect evaporators. It has been running with five-effect evaporator (quintuple) scheme. To maximize energy utilization within the plant, three multiple effect evaporator schemes were evaluated. They are triple effect evaporator, quadruple effect evaporator, and quintuple effect evaporator as the benchmark. The result shows that the quintuple effect evaporator yields the highest energy efficiency by about 1

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5

Tayseir, .M. Ahmed* &. Gurashi.A Gasmelseed. "DESIGN OF TRIPLE EFFECT EVAPORATORS BASED ON SOLAR DESALINATION OF RED SEA WATER." INTERNATIONAL JOURNAL OF ENGINEERING SCIENCES & RESEARCH TECHNOLOGY 6, no. 6 (2017): 165–70. https://doi.org/10.5281/zenodo.805407.

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Evaporation is the removal of solvent as vapor from a solution. It is the operation which is used for concentration of solution. There could be single effect evaporator or multiple effect evaporators. With addition of each effect steam economy of the system also increases. Evaporators are integral part of a number of a process industries like Pulp and Paper, Sugar, Caustic Soda, Pharmaceuticals, Desalination, Dairy and Food Processing etc. Caustic Soda Industry is of present interest. The system consists of quadruple effect having falling film evaporator as each effect. There is forward feed f

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6

Tayseir, .M. Ahmed*1 &. Gurashi.AGasmelseed2. "DESIGN OF TRIPLE EFFECT EVAPORATORS BASED ON SOLAR DESALINATION OF RED SEA WATER." INTERNATIONAL JOURNAL OF ENGINEERING SCIENCES & RESEARCH TECHNOLOGY 6, no. 7 (2017): 502–7. https://doi.org/10.5281/zenodo.829751.

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Evaporation is the removal of solvent as vapor from a solution. It is the operation which is used for concentration of solution. There could be single effect evaporator or multiple effect evaporators. With addition of each effect steam economy of the system also increases. Evaporators are integral part of a number of a process industries like Pulp and Paper, Sugar, Caustic Soda, Pharmaceuticals, Desalination, Dairy and Food Processing etc. The system consists of quadruple effect having falling film evaporator as each effect. There is forward feed flow. Designing of this system has been done. T

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7

Zavargo, Zoltan, Aleksandar Jokic, Bojana Prodanic, Jasna Grbic, and Rada Jeftic-Mucibabic. "Performance of falling film plate evaporators in reconstructed multiple-effect evaporation station in sugar factory." Thermal Science 10, no. 4 (2006): 55–61. http://dx.doi.org/10.2298/tsci0604055z.

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General trend of free trade in regional level as well as in the direction of European Union has motivated sugar factories located in Serbia to invest into technologies that are more efficient in order to make their products more competitive at the markets in Europe. The aim of this work was to evaluate effects of falling film plate evaporators on the energy consumption of evaporation plant, as well as to validate performance of this type of evaporators. It was found that this type of evaporator decreased energy requirements and in the same time evaporation process was more effective due to hig

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8

Sharan, Prashant, and Santanu Bandyopadhyay. "Solar assisted multiple-effect evaporator." Journal of Cleaner Production 142 (January 2017): 2340–51. http://dx.doi.org/10.1016/j.jclepro.2016.11.043.

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9

Veeravel, V., G. Sathish, R. Nishanthi, and S. V. Srinivasan. "Experimental Investigations on Accelerated Solar Evaporation for Management of Concentrated Saline Liquor." Journal of the American Leather Chemists Association 120, no. 01 (2025): 3–9. https://doi.org/10.34314/xad6dq57.

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Solar energy is an important energy sector that plays a crucial role in reducing greenhouse emission in different industrial sectors, including the leather sector, to control the pollution. Stringent environmental regulations of Zero Liquid Discharge (ZLD) in Indian tanneries are implemented as directed by regulatory authorities. The ZLD system resulted in the generation of saline rejected from membrane systems being evaporated by spending considerable energy. In this paper, the potential of solar energyfor evaporation of reject from ZLD in a closed accelerated solar dryer has been investigate

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10

KUNG, JASMINE, and NIKOLAI DEMARTINI. "Modeling the dynamics of evaporator wash cycles." TAPPI Journal 23, no. 7 (2024): 359–73. http://dx.doi.org/10.32964/tj23.7.359.

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Kraft pulping is a process that utilizes white liquor, composed of sodium sulfide (Na2S) and sodium hydroxide (NaOH), for wood delignification and pulp production. This process involves washing the dissolved organics and spent chemicals from the pulp, resulting in the generation of black liquor. Prior to its use as fuel in the recovery boiler, the black liquor is concentrated in multiple-effect evaporators. During the evaporation process, the inorganic salts present in the liquor become supersaturated and undergo crystallization. Fluctuations in sodium, carbonate, sulfate, and oxalate can give

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11

Chantasiriwan, Somchart. "Determination of Optimum Surface Distribution in Triple-Effect Evaporator." Applied Mechanics and Materials 598 (July 2014): 309–13. http://dx.doi.org/10.4028/www.scientific.net/amm.598.309.

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Subjected to fixed total heat transfer surface area, the distribution of surface in multiple-effect evaporator affects the performance of the evaporator. Previous studies have been concerned with optimization of surface distribution with the assumption that no fouling occurs. The present study considers a more realistic case when the last-effect vessel is subjected to fouling. It is shown that, in order to consume the minimum steam exergy to produce a given amount of evaporation, the area of the last-effect vessel must be increased as the rate of fouling increases.

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12

Lourentius, Suratno, and Aning Ayucitra. "Optimization of Heat Transfer Area and Steam Requirement in Multiple Effects Evaporator for Concentration of Juice in Sugar Factory." Equilibrium Journal of Chemical Engineering 7, no. 2 (2023): 123. http://dx.doi.org/10.20961/equilibrium.v7i2.73569.

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<strong>ABSTRACT.</strong> In maintaining the existence of sugar factories that exist and are still actively operating in Indonesia, efforts should be made to carry out intensification and extensification. In terms of the intensification of the process, it is necessary to periodically evaluate the performance of process tools, especially those that require utilities so that the process is effective and efficient. The process of making sugar passes through six stages, namely: milling, purification, evaporation (evaporation), cooking, screening, and packaging processes or the final s

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13

Lilik Suprianti, Nove Kartika Erliyanti, Soemargono Soemargono, Yehezkiel Hesed Providensia, and Stefanus Dady Waluyo. "Enhancing Seawater Salinity through Spray-Assisted Evaporation: Investigating the Effect of Nozzle Sprayer Diameter and Feed Flowrate on Evaporation Rate using Multiple Regression Analysis." Technium: Romanian Journal of Applied Sciences and Technology 16 (October 29, 2023): 430–35. http://dx.doi.org/10.47577/technium.v16i.10023.

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Salt production plays a vital role in life due to its essential minerals. Traditional salt production methods using direct solar rays are the most common in Indonesia. It needs a large area and several weeks extended to evaporate sea water into concentrated brine. It is very weather dependent. This study investigates the utilization of a spray-assisted evaporator to increase the salinity of seawater for salt production. The experimental setup consisted of a custom-designed spray evaporator that atomized seawater into fine droplets. A series of experiments were conducted to analyze the effect o

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14

Kitalekwa, Fredrick, Savinus Maronga, and Samwel Manyele. "Effect of vapor-bleeding and its configurations on multiple-effect sugarcane juice evaporator performance." International Journal of Engineering, Science and Technology 16, no. 3 (2024): 63–80. http://dx.doi.org/10.4314/ijest.v16i3.6.

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Improving process performance is always important in any processing industry with the aim of reducing operation costs and improving the profit.Vapor bleeding may be used in processing industries using multiple-effect evaporatorsto reduces steam consumption and increases steam economyThe effect of vapor bleeding on separation performance using multiple-effect sugarcane juice evaporator was analyzed. The effect of increasing percent of vapor bled and determination of the most effective bleeding configuration in terms of energy efficiency and operating costs. The performance factors assessed were

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15

Ye, Aiqian, Harjinder Singh, Michael W. Taylor, and Skelte G. Anema. "Interactions of fat globule surface proteins during concentration of whole milk in a pilot-scale multiple-effect evaporator." Journal of Dairy Research 71, no. 4 (2004): 471–79. http://dx.doi.org/10.1017/s0022029904000512.

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The changes in milk fat globules and fat globule surface proteins during concentration of whole milk using a pilot-scale multiple-effect evaporator were examined. The effects of heat treatment of milk at 95 °C for 20 s, prior to evaporation, on fat globule size and the milk fat globule membrane (MFGM) proteins were also determined. In both non-preheated and preheated whole milk, the size of milk fat globules decreased while the amount of total surface proteins at the fat globules increased as the milk passed through each effect of the evaporator. In non-preheated samples, the amount of caseins

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16

Jyoti, Ghoshna, and Shabina Khanam. "Simulation of heat integrated multiple effect evaporator system." International Journal of Thermal Sciences 76 (February 2014): 110–17. http://dx.doi.org/10.1016/j.ijthermalsci.2013.08.016.

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17

Khanam, Shabina, and Bikash Mohanty. "Energy reduction schemes for multiple effect evaporator systems." Applied Energy 87, no. 4 (2010): 1102–11. http://dx.doi.org/10.1016/j.apenergy.2009.05.003.

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18

Standiford, Ferris C. "Chapter 2.2 Control in multiple effect evaporator plants." Desalination 59 (August 1986): 263–92. http://dx.doi.org/10.1016/0011-9164(86)90032-9.

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19

Nishi, Yasuhide. "Improved Algorithm for Solving Multiple-Effect Evaporator Problems." KAGAKU KOGAKU RONBUNSHU 18, no. 2 (1992): 146–51. http://dx.doi.org/10.1252/kakoronbunshu.18.146.

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20

Han, Dong-Gu, and Jung-Myoung Lee. "Optimization of a Multiple-Effect Evaporator Process by Simulation." Journal of Korea Technical Association of the Pulp and Paper Industry 54, no. 3 (2022): 12–22. http://dx.doi.org/10.7584/jktappi.2022.06.54.3.12.

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21

Stefanov, Z., and K. A. Hoo. "Control of a Multiple-Effect Falling-Film Evaporator Plant." Industrial & Engineering Chemistry Research 44, no. 9 (2005): 3146–58. http://dx.doi.org/10.1021/ie049397w.

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22

Sharan, Prashant, and Santanu Bandyopadhyay. "Integration of thermo-vapor compressor with multiple-effect evaporator." Applied Energy 184 (December 2016): 560–73. http://dx.doi.org/10.1016/j.apenergy.2016.10.037.

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23

Gautami, G., and S. Khanam. "Selection of optimum configuration for multiple effect evaporator system." Desalination 288 (March 2012): 16–23. http://dx.doi.org/10.1016/j.desal.2011.12.005.

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24

Higa, M., A. J. Freitas, A. C. Bannwart, and R. J. Zemp. "Thermal integration of multiple effect evaporator in sugar plant." Applied Thermal Engineering 29, no. 2-3 (2009): 515–22. http://dx.doi.org/10.1016/j.applthermaleng.2008.03.009.

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25

MOREIRA, JÉSSICA, BRUNO LACERDA DE OLIVEIRA CAMPOS, ESLY FERREIRA DA COSTA JUNIOR, and ANDRÉA OLIVEIRA SOUZA DA COSTA. "Exergy and sensibility analysis of each individual effect in a kraft multiple effect evaporator." TAPPI Journal 18, no. 10 (2019): 607–18. http://dx.doi.org/10.32964/tj18.10.607.

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The multiple effect evaporator (MEE) is an energy intensive step in the kraft pulping process. The exergetic analysis can be useful for locating irreversibilities in the process and pointing out which equipment is less efficient, and it could also be the object of optimization studies. In the present work, each evaporator of a real kraft system has been individually described using mass balance and thermodynamics principles (the first and the second laws). Real data from a kraft MEE were collected from a Brazilian plant and were used for the estimation of heat transfer coefficients in a nonlin

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26

Chantasiriwan, Somchart. "Optimum surface area distribution in co-current multiple-effect evaporator." Journal of Food Engineering 161 (September 2015): 48–54. http://dx.doi.org/10.1016/j.jfoodeng.2015.03.030.

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27

Sharan, Prashant, and Santanu Bandyopadhyay. "Optimal Temperature Selection for Energy Integrated Multiple-Effect Evaporator System." Process Integration and Optimization for Sustainability 1, no. 3 (2017): 189–202. http://dx.doi.org/10.1007/s41660-017-0012-3.

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28

Khanam, Shabina, and Bikash Mohanty. "Placement of condensate flash tanks in multiple effect evaporator system." Desalination 262, no. 1-3 (2010): 64–71. http://dx.doi.org/10.1016/j.desal.2010.05.043.

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29

Khanam, S., and B. Mohanty. "Development of a new model for multiple effect evaporator system." Computers & Chemical Engineering 35, no. 10 (2011): 1983–93. http://dx.doi.org/10.1016/j.compchemeng.2010.11.001.

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30

Costa, Andréa O. S., and Enrique L. Lima. "Modelling and Control of an Industrial Multiple-Effect Evaporator System." Canadian Journal of Chemical Engineering 81, no. 5 (2008): 1032–40. http://dx.doi.org/10.1002/cjce.5450810514.

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31

Heluane, Humberto, Aníbal M. Blanco, María Rosa Hernández, and J. Alberto Bandoni. "Simultaneous re-design and scheduling of multiple effect evaporator systems." Computers & Operations Research 39, no. 5 (2012): 1173–86. http://dx.doi.org/10.1016/j.cor.2011.06.015.

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32

Riadi, Indra, and Dani Puji Utomo. "The Effect of Operating Condition on Low Pressure Steam (LPS) in Sugar Factory by Pinch Analysis." UNISTEK 9, no. 1 (2022): 68–82. http://dx.doi.org/10.33592/unistek.v9i1.1786.

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In the present work the sugar plant in Sragen, Central Java, Indonesia has ten evaporators that can be configured to five effect evaporators. The optimization ofenergy demand, finding optimum operating condition of LowPressure Steam (LPS), and choosing the best configuration of multiple effect evaporator (MEE) were performed by pinch analysis. In this paper, LPS at 0.4 kg/cm2.G – 1.1 kg/cm2.G were evaluated. The results show that the optimum operating condition of LPS was at 0.9 kg/cm2.G – 1.1 kg/cm2.G. This optimum operating condition enhances the energy saving by about 30% compared to that o

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33

Miranda, V., and R. Simpson. "Modelling and simulation of an industrial multiple effect evaporator: tomato concentrate." Journal of Food Engineering 66, no. 2 (2005): 203–10. http://dx.doi.org/10.1016/j.jfoodeng.2004.03.007.

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34

Stefanov, Z. I., and K. A. Hoo. "Distributed Parameter Model of Black Liquor Falling-Film Evaporators. 2. Modeling of a Multiple-Effect Evaporator Plant." Industrial & Engineering Chemistry Research 43, no. 25 (2004): 8117–32. http://dx.doi.org/10.1021/ie049611g.

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35

Bermingham, Sean K., Maurice Jonkers, Gert J. Kruizinga, Jos L. B. van Reisen, and Peter J. T. Verheijen. "Monitoring heat exchanger fouling for optimal operation of a multiple effect evaporator." Computers & Chemical Engineering 23 (June 1999): S771—S774. http://dx.doi.org/10.1016/s0098-1354(99)80189-6.

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36

Sharan, Prashant, and Santanu Bandyopadhyay. "Energy optimization in parallel/cross feed multiple-effect evaporator based desalination system." Energy 111 (September 2016): 756–67. http://dx.doi.org/10.1016/j.energy.2016.05.107.

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37

Sharan, Prashant, and Santanu Bandyopadhyay. "Energy integration of multiple-effect evaporator, thermo-vapor compressor, and background process." Journal of Cleaner Production 164 (October 2017): 1192–204. http://dx.doi.org/10.1016/j.jclepro.2017.07.041.

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38

Bhargava, R., S. Khanam, B. Mohanty, and A. K. Ray. "Selection of optimal feed flow sequence for a multiple effect evaporator system." Computers & Chemical Engineering 32, no. 10 (2008): 2203–16. http://dx.doi.org/10.1016/j.compchemeng.2007.10.012.

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39

Yanniotis, Stavros, and Peter A. Pilavachi. "Mathematical modeling and experimental validation of an absorption-driven multiple-effect evaporator." Chemical Engineering & Technology 19, no. 5 (1996): 448–55. http://dx.doi.org/10.1002/ceat.270190511.

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40

Ogosu, Wai, Biriye Danwi, Kenneth K. Dagde, Jackson G. Akpa, and ThankGod Oweifa Goodhead. "Computer Aided Simulation of Multiple Effect Evaporator for Concentration of Caustic Soda Solution." East African Scholars Journal of Engineering and Computer Sciences 3, no. 8 (2020): 146–56. http://dx.doi.org/10.36349/easjecs.2020.v03i08.001.

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41

Wang, Xiaojun, Chao Li, and Xisong Chen. "Disturbance rejection control for multiple-effect falling-film evaporator based on disturbance observer." Transactions of the Institute of Measurement and Control 38, no. 6 (2015): 773–83. http://dx.doi.org/10.1177/0142331215597296.

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42

Zain, Omer S., and Surendra Kumar. "Simulation of a Multiple Effect Evaporator for Concentrating Caustic Soda Solution-Computational Aspects." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 29, no. 5 (1996): 889–93. http://dx.doi.org/10.1252/jcej.29.889.

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43

Chen, Tianming, and Qi Ruan. "Modeling and energy reduction of multiple effect evaporator system with thermal vapor compression." Computers & Chemical Engineering 92 (September 2016): 204–15. http://dx.doi.org/10.1016/j.compchemeng.2016.05.011.

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44

Chantasiriwan, Somchart. "Effects of Cooling Water Flow Rate and Temperature on the Performance of a Multiple-Effect Evaporator." Chemical Engineering Communications 202, no. 5 (2014): 622–28. http://dx.doi.org/10.1080/00986445.2013.858040.

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45

Kim, Deukwon, and Sangmin Choi. "Design and Evaluation of Multiple Effect Evaporator Systems According to the Steam Ejector Position." Korean Journal of Air-Conditioning and Refrigeration Engineering 28, no. 11 (2016): 434–43. http://dx.doi.org/10.6110/kjacr.2016.28.11.434.

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46

Nafey, A. S., Mahmoud Abdelaal, Amaal Mohey Elden, and Rehab M. El-Maghraby. "Design and Performance Calculation using MATLAB for Multiple Effect Evaporator Desalination Process with Different Configurations." International Journal of Engineering Research and Technology 13, no. 10 (2020): 3029. http://dx.doi.org/10.37624/ijert/13.10.2020.3029-3042.

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47

Westerberg, A. W., and J. B. Hillenbrand. "The synthesis of multiple-effect evaporator systems using minimum utility insights—II. liquid flowpattern selection." Computers & Chemical Engineering 12, no. 7 (1988): 625–36. http://dx.doi.org/10.1016/0098-1354(88)80004-8.

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48

Wunder, Felix, Sabine Enders, and Raphael Semiat. "Numerical simulation of heat transfer in a horizontal falling film evaporator of multiple-effect distillation." Desalination 401 (January 2017): 206–29. http://dx.doi.org/10.1016/j.desal.2016.09.020.

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49

Verma, Om Prakash, Suryakant, and Gaurav Manik. "Solution of SNLAE model of backward feed multiple effect evaporator system using genetic algorithm approach." International Journal of System Assurance Engineering and Management 8, no. 1 (2016): 63–78. http://dx.doi.org/10.1007/s13198-016-0533-0.

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50

Aurellia, Amanda Novriza, Valentinus Satrio Adhi Laksono, Annas Wiguno, and Kuswandi Kuswandi. "Pra Desain Pabrik Garam Industri Dengan Proses Multiple Effect Evaporator Dari Air Konsentrat Reverse Osmosis." Journal of Fundamentals and Applications of Chemical Engineering (JFAChE) 3, no. 2 (2022): 38. http://dx.doi.org/10.12962/j2964710x.v3i2.18886.

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