簡易檢索 / 詳目顯示

研究生: 郭哲齊
Kuo, Che-Chi
論文名稱: 可供具彈性氫網路設計的改良數學模式
An Improved Mathematical Model for Flexible Hydrogen Network Designs
指導教授: 張珏庭
Chang, Chuei-Tin
學位類別: 碩士
Master
系所名稱: 工學院 - 化學工程學系
Department of Chemical Engineering
論文出版年: 2014
畢業學年度: 102
語文別: 中文
論文頁數: 105
中文關鍵詞: 氫網路蒸氣重組工廠多時期設計分時共享
外文關鍵詞: Hydrogen network, Steam reformer, Multi-period design, Timesharing schemes
相關次數: 點閱:100下載:2
分享至:
查詢本校圖書館目錄 查詢臺灣博碩士論文知識加值系統 勘誤回報
  • 在石油煉製工業中,利用氫氣資源整合技術來降低操作成本並減少空氣汙染的相關議題近年來相當受到重視。過去雖然已開發出不少可供設計最佳氫網路的數學規劃模式,但仍有進一步改善的空間。具體而言,目前既有方式的主要缺點為:(1)不合理的單元模式及(2) 不周全的設計考量。前者涉及用氫單元(如加氫脫硫或加氫裂解工廠)及產氫單元(如蒸氣重組工廠)的模式。在合理的質量平衡假設下,我們除了將用氫單元進出口端的流量及濃度視為設計 變數外,也提出適當的限制式來描述其間關聯性,使得氫網路的設計能更具彈性;此外,作為煉油廠中主要氫氣提供單元的蒸氣重組工廠也被納入數學規劃模式中,我們作法是將其內部既有的單元(如氫化單元及氣體純化裝置等)一同加入超結構中考量。在另一方面,針對前述第二項缺點,我們除了將所有常見的參數變動(如用氫單元流量、原料價格和電價等)都涵蓋在多時期設計的考慮內,也將壓縮機、氣體純化裝置(PSA)及燃料電池視為可能新添的設備。除了針對這些缺點發展出更實用更全面的混整數非線性數學規劃模式,也提出分時共享(timesharing)的演算法作為氫網路多時期設計的另一可行的選擇。最後,一系列的案例探討也用來展示本研究提出模式的可行性及實用性。

    Operating cost reduction and/or air pollution abatement via hydrogen integration is a research issue that has recently attracted considerable attention in the petroleum refining industries. Although a number of mathematical programming models have already been developed to generate the optimal hydrogen distribution schemes, there is still room for further improvements. More specifically, the conventional models of hydrogen users are usually formulated according to fixed throughputs and also constant feed and product concentrations. Based on the shortcut calculations proposed in this study, not only the inlet and outlet flow rates and concentrations of these units can be treated as decision variables but also their interactions characterized with proper material-balance constraints. In addition, since the steam reforming plant is traditionally the primary hydrogen producer in a refinery and, in the existing model, it is treated only as a simple source, the more rigorous models of its embedded units have been established and added to the improved mathematical programs. As a result of the aforementioned modifications, more and better design options can be identified accordingly. To ensure comprehensive design considerations, all often-encountered seasonal variations in model parameters and the options to add extra compressors, purifiers and fuel cells have also been incorporated in a multi-period model. Finally, as an alternative approach to solve the above multi-period model, a systematic timesharing algorithm has been devised to integrate the conventional single-period designs in different periods to form a less economical but more flexible network structure for operations in multiple periods. Extensive case studies have been carried out to test the proposed design methods.

    摘要 I Extended Abstract II 誌謝 VII 目錄 IX 表目錄 XIII 圖目錄 XV Nomenclature XVII 第一章 緒論 1 1.1 研究動機 1 1.2 文獻回顧 1 1.3研究目的 4 1.4組織章節 4 第二章 既有氫網路設計模式之改善 5 2.1 基本定義 5 2.2 超結構 6 2.2.1 不考慮新添設備 6 2.2.2 考慮新添設備 8 2.3 既有模式 11 2.3.1用氫單元 11 2.3.2壓縮機 12 2.3.3氫氣純化裝置 14 2.3.4燃料電池 15 2.3.5 燃氣系統 17 2.3.6 新添設備 18 2.3.7 新添管線 19 2.3.8 目標函數 20 2.4 改良模式 22 2.4.1超結構 22 2.4.2 用氫單元 24 2.4.3 蒸氣重組工廠 27 2.4.4 燃氣系統 30 2.4.5 目標函數 31 2.5 測試例題 32 2.5.1 既有模式最適化結果 42 2.5.2 改良模式最適化結果 44 2.5.3不同設計成本比較 46 第三章 氫網路之多時期設計 47 3.1 前言 47 3.2 氫網路多時期數學模式 50 3.2.1 多時期新添設備 50 3.2.2 多時期新添管線 51 3.2.3 多時期年總成本 51 3.3 分時共享(Timesharing)的多時期設計策略 53 3.4 測試例題 56 3.4.1單時期最適設計用於多時期操作之年總成本 60 3.4.2具分時共享機制的多時期設計 63 3.4.3多時期數學模式的最適解 67 3.5 成本分析 70 第四章 案例探討 73 4.1 案例描述 73 4.2 單時期最適設計用於多時期操作之年總成本 81 4.3 具分時共享機制的多時期設計 86 4.4多時期數學模式的最適解 91 4.5 成本分析 96 4.6 延伸討論 99 第五章 結論與展望 100 5.1 研究結論 100 5.2 未來展望 101 參考文獻 102

    Alves, J. J., and Towler, G. P., Analysis of refinery hydrogen distribution systems. Ind. Eng. Chem. Res., 41, 5759-5769 (2002).
    Ahmad, M. I., Zhang, N., and Jobson, M., Modelling and optimisation for design of hydrogen networks for multi-period operation. J. Clean. Prod., 18(9), 889–899 (2010).
    Chiang, Y. C., and Chang, C. T., Single-objective and multiobjective designs for hydrogen networks with fuel cells. Ind. Eng. Chem. Res., 53, 6006−6020 (2014).
    El-Halwagi, M. M., Gabriel, E., and Harell, D., Rigorous graphical targeting for resource conservation via material recycle/reuse networks. Ind. Eng. Chem. Res., 42, 4319–4328 (2003).
    El-Halwagi, M. M., Sustainable Design through Process Integration : Fundamentals and Applications to Industrial Pollution Prevention, Resource Conservation, and Profitability Enhancement, Butterworth-Heinemann/Elsevier, Oxford, England, (2012).
    Hallale, N., and Liu, F., Refinery hydrogen management for clean fuels production. Adv. Environ. Res., 6(1), 81–98 (2001).
    Hallale, N., Moore, I., and Vauk, D., Hydrogen: liability or asset?. Chemical Engineering Progress, 98, 66–75 (2002).
    Jiao, Y., Su, H., and Hou, W., Improved optimization methods for refinery hydrogen network and their applications. Control Eng. Practice., 20 (10) , 1075−1093 (2012).
    Jiang, D., and Chang, C. T., A new approach to generate flexible multiperiod heat exchanger network designs with timesharing mechanisms. Ind. Eng. Chem. Res., 52, 3794−3804 (2013).
    Jiang, D., and Chang, C. T., An algorithmic approach to generate timesharing schemes for multi-period HEN designs. Ind. Eng. Chem. Res., in press (2014).
    Khajehpour, M., Farhadi, F., and Pishvaie, M. R., Reduced superstructure solution of MINLP problem in refinery hydrogen management. Int. J. Hydrogen Energy, 34(22), 9233–9238 (2009).
    Kumar, A., Gautami, G., and Khanam, S., Hydrogen distribution in the refinery using mathematical modeling. Energy, 35(9), 3763–3772 (2010).
    Liu, F., and Zhang, N., Strategy of purifier selection and integration in hydrogen networks. Chem. Eng. Res. Des., 82(A10), 1315–1330 (2004).
    Liao, Z. W., Wang, J. D., Yang, Y. R., and Rong, G., Integrating purifiers in refinery hydrogen networks: a retrofit case study. J. Clean. Prod., 18(3), 233–241 (2010).
    Posada, A., and Manousiouthakis, V., Heat and power integration of methane reforming based hydrogen production. Ind. Eng. Chem. Res., 44(24), 9113–9119 (2005).
    Robinson, P. R., and Dolbear, G. E., Hydrotreating and hydrocracking: fundamentals, in: C.S. Hsu, P.R. Robinson (Eds.), Practical Advances in Petroleum Processing, vol. 1, Springer, New York, pp. 177–217. Chapter 7, (2006).
    Spath, P. L., and Mann, M. K., Life Cycle Assessment of Hydrogen Production via Natural Gas Steam Reforming, Technical Report NREL, NREL/TP-570-27637, (2001).
    Smith, R., Chemical process design and integration, John Wiley & Sons : New York (2005).
    Sorokes, J. M., Selecting a centrifugal compressor. Chem. Eng. Prog., 6, 44–51 (2013).
    Van den Heever, S. A., and Grossmann, I. E., A strategy for the integration of production planning and reactive scheduling in the optimization of a hydrogen supply network. Comput. Chem. Eng., 27(12) , 1813 – 1839 (2003).
    Verheyen, W., and Zhang, N., Design of flexible heat exchanger network for multi-period operation. Chem. Eng. Sci., 61,7730–7753 (2006).
    Wu, S., Liu, G., Yu, Z., Feng, X., Liu, Y., and Deng, C., Optimization of hydrogen networks with constraints on hydrogen concentration and pure hydrogen load considered. Chem. Eng. Res. Des., 90 (9),1208−1220 (2012).
    Wu, S., Yu, Z., Feng, X., Liu, G., Deng, C., and Chu, K. H., Optimization of refinery hydrogen distribution systems considering the number of compressors. Energy, 62, 185−195 (2013).
    Wang, Y., Jin, J., Feng, X., and Chu, K. H., Optimal operation of a refinery’s hydrogen network. Ind. Eng. Chem. Res., unpublished (2014).
    Zhang, Q., Feng, X., Liu, G. L., and Chu, K. H., A novel graphical method for the integration of hydrogen distribution systems with purification reuse. Chem. Eng. Sci., 66, 797–809 (2011).
    Zhang, Q., Feng, X., and Chu, K. H., Evolutionary graphical approach for simultaneous targeting and design of resource conservation networks with multiple contaminants. Ind. Eng. Chem. Res., 52 (3), 1309−1321 (2013).

    下載圖示 校內:2017-08-22公開
    校外:2017-08-22公開
    QR CODE