中油101新進職員甄試試題-單操 - 考試
By Jacob
at 2013-10-18T10:57
at 2013-10-18T10:57
Table of Contents
題目101-7:http://i.imgur.com/rd9WQF9.jpg
包覆面積相同,熱量相等q=qa=qb
q=-kA(dT/dr) ,A=2πrL
題目為單位長通過得熱量
q ΔT
_ = _________________
L ln(r2/r1)÷2πk
各圓半徑
ro=200/2=100 mm = 0.1 m
ra=100+50=150 mm = 0.15 m
rb=150+25=175 mm = 0.175 m
阻抗R=ln(r2/r1)÷(2πk) , 總阻抗=各阻抗和
Rt=ln(0.15/0.1) ÷(2π0.09) +ln(0.175/0.15)÷(2π0.08)
Rt=0.717 + 0.307
=1.025
(1) q/L = (170-20)÷1.025=146 Kcal/hr m ℃
(2) qa = (T-Tab)÷Ra
146 = (170-Tab)÷0.717
Tab = 65 ℃
--------------------------------------------------------------------------
題目101-9:http://i.imgur.com/ReYbH0V.jpg
思考:氣體吸收熱量=管子放熱量
q=m Cp ΔT = UA'(LMTD) m= ρuA , A=πD^2÷4 ,A'=πDL(熱傳面積)
q=(0.0012)(20*100)(π1^2÷4)×0.23 × (90-30)
=(1.11e10^-3) ×(π*1*L) ×( [(105-30)-(105-90)]/ln[(105-30)/(105-90)] )
L=200 cm
-----------------------------------------------------------------------------
考題101-10:http://i.imgur.com/z3e76Of.jpg
思考
第一題:對數平均溫度差乘上修正因子
第二題:質量平衡
一、 ΔTlm=Fg ×(LMTD) =0.8 ×( [(120-60)-(40-20)]/ln[(120-60)/(40-20)] )
=29.13 ℃
二、 F = D + W , F*xf = D*xd + W*xw , 設各項出入料 x=苯
10000 = D + W , 1000*0.4 = D*0.97 + W*(1-0.98)
解聯立後 D=4000 Kg/hr , W=6000 Kg/hr
--------------------------------------------------------------------------
請幫忙訂正錯誤的地方,不吝賜教,謝謝。
※ 編輯: pj721911 來自: 118.163.37.8 (10/18 12:20)
推得人對不起,修改文章沒注意到推文刪到。
※ 編輯: pj721911 來自: 118.163.37.8 (10/18 12:28)
包覆面積相同,熱量相等q=qa=qb
q=-kA(dT/dr) ,A=2πrL
題目為單位長通過得熱量
q ΔT
_ = _________________
L ln(r2/r1)÷2πk
各圓半徑
ro=200/2=100 mm = 0.1 m
ra=100+50=150 mm = 0.15 m
rb=150+25=175 mm = 0.175 m
阻抗R=ln(r2/r1)÷(2πk) , 總阻抗=各阻抗和
Rt=ln(0.15/0.1) ÷(2π0.09) +ln(0.175/0.15)÷(2π0.08)
Rt=0.717 + 0.307
=1.025
(1) q/L = (170-20)÷1.025=146 Kcal/hr m ℃
(2) qa = (T-Tab)÷Ra
146 = (170-Tab)÷0.717
Tab = 65 ℃
--------------------------------------------------------------------------
題目101-9:http://i.imgur.com/ReYbH0V.jpg
思考:氣體吸收熱量=管子放熱量
q=m Cp ΔT = UA'(LMTD) m= ρuA , A=πD^2÷4 ,A'=πDL(熱傳面積)
q=(0.0012)(20*100)(π1^2÷4)×0.23 × (90-30)
=(1.11e10^-3) ×(π*1*L) ×( [(105-30)-(105-90)]/ln[(105-30)/(105-90)] )
L=200 cm
-----------------------------------------------------------------------------
考題101-10:http://i.imgur.com/z3e76Of.jpg
思考
第一題:對數平均溫度差乘上修正因子
第二題:質量平衡
一、 ΔTlm=Fg ×(LMTD) =0.8 ×( [(120-60)-(40-20)]/ln[(120-60)/(40-20)] )
=29.13 ℃
二、 F = D + W , F*xf = D*xd + W*xw , 設各項出入料 x=苯
10000 = D + W , 1000*0.4 = D*0.97 + W*(1-0.98)
解聯立後 D=4000 Kg/hr , W=6000 Kg/hr
--------------------------------------------------------------------------
請幫忙訂正錯誤的地方,不吝賜教,謝謝。
※ 編輯: pj721911 來自: 118.163.37.8 (10/18 12:20)
推得人對不起,修改文章沒注意到推文刪到。
※ 編輯: pj721911 來自: 118.163.37.8 (10/18 12:28)
→ MSNboy:這幾題去翻書就有了 10/18 13:24
※ pj721911:轉錄至看板 ChemEng 10/18 14:47 推 myemail:第二題不能這樣做。題目不是給總括熱傳係數。 10/18 15:18
→ pj721911:請問第二題的解題方向 10/18 16:49
→ pj721911:用無因次群解嗎? NU=hD/k 求k值後帶kA'ΔT/L嗎? 10/18 16:52
→ pj721911:上面的想法不對=.= 10/18 16:54
推 myemail:用殼層能量均衡,考慮軸向熱傳和徑向熱傳!參考3Wp291例題 10/18 17:08
推 terranbill:樓上說得對!!!這題要用Shell-Balance去解!! 10/18 22:33
→ kobe76724:請問一下 是不是會變的有點像散熱片那種解題觀念? 10/19 00:09
推 sundy2003:沒錯 散熱片也是用energy-balance去解題 10/19 09:08
→ sundy2003:原po手邊沒有林隆的教材嗎 第2題裡面有教= = 10/19 09:11
→ pj721911:我沒有,我只有買他的中油考試題本配大學買得DeWitt編著 10/19 10:52
→ pj721911:熱傳 10/19 10:52
→ pj721911:不過我在翻書後,發現我看到有管子熱交換的都執著再熱交 10/19 10:58
→ pj721911:器的計算,忘了overall energy balance這觀念 10/19 10:59
推 badiverson:也不用記哪種題型啦~反正就Energy Balacne 解天下 10/19 13:17
→ badiverson:剩下就是數學熟悉度 10/19 13:18
→ badiverson:反正輸送就是 分析系統 決定座標 Balance equation 10/19 13:19
→ badiverson:剩下就是簡單的ODE 10/19 13:20
→ pj721911:恩~謝謝你的指導 10/19 23:45
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