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姓名 謝明憲(Ming-Xian Xei )  查詢紙本館藏   畢業系所 機械工程研究所
論文名稱 轉注成型充填過程中邊界效應之數值模擬
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摘要(中) 在樹脂轉注射出成型充填過程中,樹脂於纖維束內、外的流動模式,直接影響氣泡之生成及位置,亦即影響了產品的品質。本文應用纖維蓆編織的特性,即纖維絲多集中於纖維束內,而纖維束與束之間隙則為無纖維區。因此,在無纖維區(纖維束與束之間隙)可使用Stokes方程式來描述樹脂的流動;而纖維束內,目前國內外研究多使用達西定律(Darcy’s Law),然而從文獻可知︰由於達西定律缺乏黏滯的剪應力項,因此會與Stokes方程式交界面產生速度不連續情形。因此,本文在纖維束內改使用Brinkman方程式來解決流場速度不連續問題,這是本文與目前國內外研究最大不同。在使用Brinkman方程式和Stokes方程式來求解流場時,由於纖維束內、外樹脂的流速不同,會使流場交界面產生一類似邊界層現象。因此,本文除了將完整模擬纖維束內、外流場運動外,也對樹脂在纖維束內流場形成的邊界層厚度及展開情形做一探討。藉由數值模擬的結果,將可使吾人更深入的了解在轉注成型充填階段,樹脂流動的詳細物理特性及其對成品品質的影響性。
摘要(英) Inside the fiber mats, the gaps between the fiber tows are the fiber free zones. The resin flow through the gap is assumed to obey the Stokes equation. Inside the fiber tows, large of literatures are found to be studied by Darcy’s law, while such a treatment would result in the discontinuity condition in simulated velocity on the interface which were against the gap and the fiber tow. Due to the difference of the velocity inside and outside fiber tows, the interface of the flow field would cause a quasi boundary layer phenomenon. Therefore, we use Brinkman equation instead of Darcy’s law in this study. The method not only simulate the motion inside and outside the fiber tows but discuss the development and formulation of the boundary layer thickness. The results of numerical simulation are convenient and effective in realizing the defect of filling process of Resin Transfer Molding. The physical meanings for such a resin motion and their influences on the quality of product are also discussed.
關鍵字(中) ★ Brinkman方程式
★  stokes方程式
★  樹脂轉注成型
關鍵字(英) ★ Brinkman equation
★  Resin Transfer Molding
論文目次 摘要 Ⅰ
英文摘要 Ⅱ
目錄 Ⅲ
表目錄 Ⅴ
圖目錄 Ⅵ
符號說明 Ⅷ
第一章、緒論 1
1-1 前言 1
1-2 文獻回顧 3
1-3 研究方向 13
第二章、理論模式 14
2-1 纖維束內流場 14
2-2 纖維束外流場 15
2-3 空孔度 16
2-4 滲透度 16
2-5 毛細數 17
2-6 無因此分析 18
第三章、數值方法 20
3-1 數值模擬 20
3-2 數值計算步驟 21
3-3 流動面的收斂 22
第四章、結果與討論 25
第五章、結論 30
第六章、參考文獻 32
表 43
圖 44
附錄 70
附錄A 70
表 目 錄
表1纖維蓆空孔度與滲透度對照表 43
圖 目 錄
圖1-1纖維束編織示意圖 44
圖2-1纖維束內、外流場交互作用情形 45
圖2-2交界面移動元素路徑示意圖 46
圖2-3樹脂為牛頓流體假設之合理性 47
圖2-4物理定義域示意圖 48
圖2-5邊界條件示意圖 49
圖3-1(a)主要程式流程圖 50
圖3-1(b)Simpler程式流程圖 51
圖3-2流場格點座標分佈情形 52
圖3-3流動面擷取方法示意圖 53
圖4-1(a)(b)利用非交錯格點所模擬壓力場示意圖 54
圖4-2交錯隔點配置示意圖 55
圖4-3縫隙與纖維束平均入口壓力隨時間變化圖 56
圖4-4(a)當纖維束滲透度為 時,流動面隨時間變化情形 57
圖4-4(b)當纖維束滲透度為 時,流動面隨時間變化情形 58
圖4-4(c)當纖維束滲透度為 時,流動面隨時間變化情形 59
圖4-5邊界層厚度隨纖維束滲透度增減之變化圖 60
圖4-6(a)當縫隙大小 為8時,流動面隨時間變化情形 61
圖4-6(b)當縫隙大小 為10時,流動面隨時間變化情形 62
圖4-6(c)當縫隙大小 為12時,流動面隨時間變化情形 63
圖4-7邊界層厚度隨縫隙大小增減之變化 64
圖4-8(a)(b) 當縫隙大小 分別為1,6時,流場壓力分佈情形 65
圖4-8(c)(d) 當縫隙大小 分別為10,16時,流場壓力分佈情形 66
圖4-9(a)縫隙平均入口壓力與縫隙大小關係圖 67
圖4-9(b)纖維束平均入口壓力與縫隙大小關係圖 68
圖4-10文獻[66]所模擬之流動面隨時間變化圖 69
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指導教授 洪勵吾(Lih-Wu Hourng) 審核日期 2001-7-18
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