Full metadata record
DC Field | Value | Language |
---|---|---|
dc.contributor.author | 김진국 | - |
dc.date.accessioned | 2017-12-11T02:02:32Z | - |
dc.date.available | 2017-12-11T02:02:32Z | - |
dc.date.issued | 2016-02 | - |
dc.identifier.citation | KOREAN JOURNAL OF CHEMICAL ENGINEERING, v. 33, NO 2, Page. 405-415 | en_US |
dc.identifier.issn | 0256-1115 | - |
dc.identifier.issn | 1975-7220 | - |
dc.identifier.uri | https://link.springer.com/article/10.1007%2Fs11814-015-0139-2 | - |
dc.identifier.uri | http://hdl.handle.net/20.500.11754/34046 | - |
dc.description.abstract | The separation of NGL (natural gas liquids) in gas processing is energy-intensive, requiring systematic process design and optimization to reduce energy consumption and to identify cost-effective solutions for the recovery valuable hydrocarbons. As NGL fractionation processes require a sequence of distillation columns to separate multi-component mixtures the determination of optimal energy-efficient distillation sequences and operating conditions is not a simple task. A design methodology is proposed in this study in which the process simulator Aspen HYSYSA (R) is linked with an optimization algorithm available in MATLAB(A (R)). The proposed methodology involves a procedure where in the first step possible distillation sequences are screened using a short-cut distillation column model. In the second step a few selected and promising candidate distillation sequences are further simulated and optimized, again using the same short-cut model. Finally, rigorous simulations are used to validate and confirm the feasibility of the optimal designs. A case study is presented to demonstrate the applicability of the proposed design framework for the design and optimization of NGL fractionation processes in practice. | en_US |
dc.description.sponsorship | This research was supported by a grant from the GAS Plant R&D Center funded by the Ministry of Land, Infrastructure and Transport (MOLIT) of the Korean government. | en_US |
dc.language.iso | en | en_US |
dc.publisher | KOREAN INSTITUTE CHEMICAL ENGINEERS | en_US |
dc.subject | Distillation Sequencing | en_US |
dc.subject | Optimization | en_US |
dc.subject | Energy Recovery | en_US |
dc.subject | Natural Gas Separation | en_US |
dc.title | A design procedure for heat-integrated distillation column sequencing of natural gas liquid fractionation processes | en_US |
dc.type | Article | en_US |
dc.relation.no | 2 | - |
dc.relation.volume | 33 | - |
dc.identifier.doi | 10.1007/s11814-015-0139-2 | - |
dc.relation.page | 405-415 | - |
dc.relation.journal | KOREAN JOURNAL OF CHEMICAL ENGINEERING | - |
dc.contributor.googleauthor | Yoo, Hanareum | - |
dc.contributor.googleauthor | Binns, Michael | - |
dc.contributor.googleauthor | Jang, Mun-Gi | - |
dc.contributor.googleauthor | Cho, Habin | - |
dc.contributor.googleauthor | Kim, Jin-Kuk | - |
dc.relation.code | 2016008246 | - |
dc.sector.campus | S | - |
dc.sector.daehak | COLLEGE OF ENGINEERING[S] | - |
dc.sector.department | DEPARTMENT OF CHEMICAL ENGINEERING | - |
dc.identifier.pid | jinkukkim | - |
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