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研究生: 蘇王尹
Su, Wang-Yin
論文名稱: 氫液化製程放大、經濟與㶲分析及最佳化探討
Scale-up, Techno-Economic and Exergy Analysis, and Optimization of Hydrogen Liquefaction Processes
指導教授: 吳煒
Wu, Wei
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: 2026
畢業學年度: 114
語文別: 中文
論文頁數: 133
中文關鍵詞: 氫液化正-仲氫轉換動力學遺傳演算法㶲分析AspenPlus技術經濟分析製程放大
外文關鍵詞: Hydrogen liquefaction, Aspen Plus, Ortho-para conversion kinetics, Genetic algorithm, Exergy analysis, Process scale-up, Techno-economic analysis
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  • 氫能因高質量能量密度與燃燒零碳排特性,被視為淨零轉型之關鍵能源載體,而液態氫(LH₂)為大規模氫能儲運之主要型態之一。然而現行氫液化製程之比能耗(SEC)普遍達10-15kWh/kgLH₂,遠高於理論值,且規模放大後之能耗與經濟性變化仍缺乏系統性評估。
    本研究以 Song 等人提出之LN₂預冷結合氦氣Joule-Brayton 深冷循環為基礎,使用Aspen Plus V14.0 搭配 REFPROP高精度狀態方程式重建基準製程(0.5 t/d),並導入Donaubauer一階動力學模型,以RPlug模組取代傳統平衡轉換假設,使五級正-仲氫轉換器之模擬具備物理意義。透過靈敏度分析篩選關鍵操作變數後,結合遺傳演算法(GA)進行多變數優化,使SEC由12.03降至8.72 kWh/kgLH₂,較 Song 等人之9.82 kWh/kgLH₂低約 11.2%,㶲效率則由29.1%提升至45.0%。
    進一步建立放大分析架構,產能由0.5 t/d放大至5、25及50 t/d,依文獻調整各規模之設備等熵效率與壓降,並於每一規模重新執行GA優化。結果顯示無壓降模型下SEC由8.72降至6.65 kWh/kgLH₂、㶲效率由45.0%提升至58.9%;加入壓降修正後SEC則由9.23降至6.79 kWh/kgLH₂。㶲破壞分布亦呈現結構性轉變,壓縮機佔比由47.5%降至34.6%,換熱器則由19.2%升至37.1%並於50 t/d規模超越壓縮機。最後建立初步技術經濟分析(TEA)模型,SLC由0.5 t/d之3.14 USD/kgLH₂降至50 t/d之 1.60 USD/kgLH₂,敏感度分析顯示外購LN₂價格為單位液化成本之主要制約因素。

    Liquid hydrogen is a leading carrier for large-scale hydrogen storage, yet current liquefiers consume 10–15 kWh/kg LH₂, and how this penalty and its cost evolve with plant scale has not been assessed consistently. This work rebuilds the LN₂-precooled helium Joule–Brayton process of Song et al. at 0.5 t/d in Aspen Plus V14.0 with REFPROP, optimizes it by genetic algorithm (GA), and scales it to 50 t/d.
    The five ortho–para converters are modeled as RPlug reactors driven by the first order kinetics of Donaubauer et al. rather than assumed to reach equilibrium; the model matches the reference data to 2.5% NRMSE, with all stages within 0.4 percentage points of equilibrium. A GA coupled to Aspen Plus then minimized SEC at four capacities under literature-based isentropic efficiencies and pressure drops.
    At 0.5 t/d the GA lowers SEC from 12.03 to 8.72 kWh/kg LH₂, 11.2% below the reference value, and raises exergy efficiency from 29.1% to 45.0%. At 50 t/d, SEC reaches 6.65 kWh/kg LH₂ (6.79 with pressure drop) and exergy efficiency 58.9%, 85% of the gain coming from equipment efficiency and re-optimization. The exergy bottleneck shifts from compression (47.5% to 34.6%) to cryogenic heat exchange (19.2% to 37.1%). Liquefaction cost falls from 3.14 to 1.60 USD/kg LH₂, of which purchased LN₂ is about 60% and the dominant sensitivity.

    摘要 II Extended Abstract III 目錄 XXVII 第一章 緒論 1 1.1研究背景 1 1.2研究動機與目標 2 1.3 論文架構 4 第二章 文獻回顧 5 2.1氫氣液化技術簡介 5 2.1.1氫氣的物理性質 5 2.1.2氫氣液化的技術瓶頸 7 2.2預冷與深冷循環技術 8 2.2.1預冷循環技術 8 2.2.2深冷循環技術 10 2.2.3 本研究之製程構型選擇依據 11 2.3正-仲氫轉換反應 12 2.3.1平衡轉換假設與動力學模型 13 2.4 㶲分析方法 13 2.5製程優化方法—遺傳演算法(GA) 14 2.6 氫液化製程之技術經濟分析 16 3.1 整體製程概述 17 3.2 模擬工具與方法 20 3.2.1 模擬工具選擇 20 3.2.2 熱力學模型選擇 21 3.2.3 Aspen Plus 與 Python 之整合 21 3.3 氫氣液化模組設計 22 3.3.1預冷循環模組設計與概念 22 3.3.2預冷循環流程 22 3.3.3深冷循環製程概述與設計邏輯 25 3.3.4 深冷循環流程 25 3.4 正-仲氫轉換反應器模組設計 26 3.4.1 動力學模型選擇 26 3.4.2 Aspen Plus RPlug 模組之模擬 27 3.4.3反應器操作模式——等溫與絕熱配置 28 3.4.4 反應器參數與模擬驗證 30 3.5 靈敏度分析 34 3.5.1 靈敏度分析之結果 36 3.6 製程優化方法—遺傳演算法(GA)38 3.6.1 GA之優化方法 39 3.6.2 優化結果分析 42 3.6.3能量與㶲分析結果 44 第四章 製程放大與經濟分析 48 4.1 放大製程與經濟分析架構 48 4.2 製程放大策略、假設與約束條件 49 4.2.1 放大模型假設與合理性檢核 49 4.2.2 設備等熵效率設定 51 4.2.3 壓降設定 52 4.2.4 放大參數設定 54 4.3 GA 再優化程序 54 4.3.1 GA 再優化結果 55 4.3.2 各規模 SEC 組成與變化趨勢 58 4.3.3 壓降修正後之 SEC 分析 60 4.3.4 SEC降幅來源拆解與壓降敏感度分析 61 4.4 放大規模之㶲分析對比 63 4.5 與文獻 SEC 比較 67 4.6經濟分析建模方法 70 4.6.1 經濟分析範圍與成本邊界 70 4.6.2 資本支出估算方法 71 4.6.3 營運支出估算方法 74 4.6.4 資本年化與單位液化成本定義 76 4.6.5 資本支出與單位液化成本分析 78 4.6.6 價格浮動分析 81 4.6.7 與文獻之單位液化成本比較 83 第五章 結論與未來展望 86 參考文獻 88 附錄A、正仲氫催化轉化反應動力學模型之建立與簡化 92 A.1原始速率表達式 92 A.2模型簡化 92 A.3拆解為正逆向不可逆反應 93 A.4擬合為 Power Law 形式 93 A.5模型驗證 94 A.5.1平衡組成驗證 94 A.5.2淨反應速率驗證 95

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