• Title/Summary/Keyword: Thermally Coupled Distillation Column

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Study on Control Efficiency of Fully Thermally Coupled Distillation Column for BTX Separation (BTX 분리용 열복합 증류탑의 제어성능에 관한 연구)

  • Kim, Mi Hee;Park, Chang Won;Lee, Ju-Yeong;Kim, Young Han;Hwang, Kyu Suk
    • Korean Chemical Engineering Research
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    • v.48 no.6
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    • pp.725-730
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    • 2010
  • The fully thermally coupled distillation columns(FTCDC) are thermodynamically more efficient than conventional columns. Despite these advantages, industry has been reluctant to use FTCDC. This can be largely attributed to the lack of established design procedures and column operability. In this study, the $3{\times}3$control structure was applied to control the FTCDC which was simulated using Aspen HYSYS on the possible control structure of 4 kinds and control performance was investigated. As the result of dynamic simulations, one of the proposed structures had better controllability of product compositions and control efficiency was evaluated.

Concentration of 2-Ethyl Hexanol Using an Energy-Efficient Distillation Column (에너지 절약형 증류탑을 이용한 2-에틸헥산올의 농축)

  • Kim, Dae-Hwan;Park, Jung-Woo;Kim, Young-Han
    • Clean Technology
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    • v.16 no.1
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    • pp.59-63
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    • 2010
  • The concentration process of 2-ethyl hexanol used for the intermediate material in the production of plasticizer is examined for the energy conservation of energy-efficient distillation system instead of the conventional two column system through numerical simulation. Some 41 % of energy conservation is expected from the proposed system, and its conservation principle is explained with column profiles. In addition, not only the operating cost but also investment cost can be reduced for the additional benefit of the column application when the thermally coupled distillation is implemented.

Design of Reformate Fractionation Process with Thermally Coupled Distillation Column (Reformate 분리공정에서의 열복합 증류탑 설계)

  • Lee, Ju-Yeong
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.12 no.5
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    • pp.2445-2450
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    • 2011
  • Design of reformate fractionation process using a fully thermally coupled distillation is conducted with commercial design software Aspen HYSYS. Detailed procedure of the design is explained, and the performance of the process is compared with that of a conventional system. The design outcome indicates that the procedure is simple and efficient. The performance of the new process indicates that an energy saving of 12.2% is obtained compared with the conventional process while total number of trays maintains at the same.

Application of An Energy-Efficient Distillation System using Three Columns to Hexane Process (3기의 증류탑을 이용한 에너지 절약형 증류탑의 헥산공정에의 응용)

  • Kim, Young-Han;Hwang, Kyu-Suk
    • Korean Chemical Engineering Research
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    • v.43 no.1
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    • pp.39-46
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    • 2005
  • Though a fully thermally coupled distillation column-an energy efficient distillation system-consumes less energy, it is not widely implemented in practice due to its operational difficulty. A 3-column distillation system having improved operability is proposed here, and its energy saving performance and application related issues are investigated from the implementation result to a practical hexane process. When an energy integration is employed, the proposed system requires 18% less energy than a conventional 2-column system, which is found from the HYSYS simulation. Though more control loops than the 2-column system are required, the proposed system has better controllability of product compositions and the pressure control of the system is easier.

A Study of Complex Distillation Arrangements Using Dividing Wall Columns for Improved Depropanizing, Debutanizing and Deisobutanizing Fractionation of NGL (천연가스액 중 프로판, 부탄, 이소-부탄의 개선된 분리회수를 위한 분리벽형 증류탑을 이용한 복합 증류배열에 관한 연구)

  • Nguyen, Van Duc Long;Jang, Sungkeun;Lee, Moonyong
    • Korean Chemical Engineering Research
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    • v.51 no.2
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    • pp.245-249
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    • 2013
  • The depropanizing, debutanizing and deisobutanizing fractionation steps of processing natural gas liquids were improved through studying complex distillation arrangements, including the double dividing wall column arrangement (DDWC), the sequence including a dividing wall column (DWC) and a bottom DWC (BDWC), and the sequence including a DWC and a BDWC with top vapor recompression heat pump. These arrangements offer benefits by decreasing reboiler and condenser power consumption. Reducing the number of columns and their diameters can potentially reduce construction costs. The result also showed that operating cost could be reduced most significantly through novel combinations of internal and external heat integration: bottom dividing wall columns employing a top vapor recompression heat pump.

The Study of Structure Design for Dividing Wall Distillation Column (분리벽형 증류탑의 구조 설계 및 분리 특성 연구)

  • Lee, Seung Hyun;Lee, Moon Yong
    • Korean Chemical Engineering Research
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    • v.45 no.1
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    • pp.39-45
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    • 2007
  • This paper proposed a shortcut method for the structure design of dividing wall column based on the Fen-ske-Underwood equation by applying it on three conventional simple column configuration. It is shown that the proposed shortcut method can design the column structure including the feed tray, dividing wall section, and side-stream tray in a simple and efficient way in the initial design stage. Simulation study using HYSYS to compare the energy saving performance between the conventional sequential two column system and the dividing wall column designed by the proposed method shows that the proposed dividing wall column system saves from 16% to 65% more over the condepends on the composition of intermediate component while the optimal energy consumption pattern to internal flow distribution on the dividing wall section is characterized by the ESI factor of the feed mixture.