< 9. Transport phenomena 2 Problems > < Transport phenomena 2 by JD > P.297 Problem 1) A 0.2m wide plate, 0.8m long, is placed on the bottom of a shallow tank. The plate is heated and maintained at a constant surface temperature of 60โ. Liquid water 12cm deep flows over the flat plate with bulk volumetric flow rate of 2.4 × 10 ๐ /๐ ๐๐. The bulk liquid water temperature may be assumed to remain constant at 20โ as it flows along the length of the plate. 0.2m a) What are the values of ๐น๐๐ณ and ๐ท๐ for this convective heat transfer process? Is the flow laminar or turbulent at the end of the plate? ๐ ๐ = ๐๐๐ฟ 992.2 × 0.1 × 0.8 = = 120,632 ๐ 658 × 10 Laminar flow (๐ ๐ <200,000) ๐๐ = ๐๐ถ 658 × 10 × 4175 = = 4.14 ๐ 0.663 < Transport phenomena 2 by JD > P.297 Problem 1) A 0.2m wide plate, 0.8m long, is placed on the bottom of a shallow tank. The plate is heated and maintained at a constant surface temperature of 60โ. Liquid water 12cm deep flows over the flat plate with bulk volumetric flow rate of 2.4 × 10 ๐ /๐ ๐๐. The bulk liquid water temperature may be assumed to remain constant at 20โ as it flows along the length of the plate. 0.2m b) What is the local heat flux at a distance 0.5 m from the leading edge of the plate? Use the Blasius solution based Nusselt number equation. ๐ / โ = 0.332 ๐ ๐ ๐๐ / ๐ฅ 0.663 992.2 × 0.1 × 0.5 = 0.332 × × 0.5 658 × 10 ๐ =โ ๐ −๐ ๐ด / × 4.14 / = 194.1 = 194.1 × 40 = 7764๐/๐ < Transport phenomena 2 by JD > P.297 Problem 1) A 0.2m wide plate, 0.8m long, is placed on the bottom of a shallow tank. The plate is heated and maintained at a constant surface temperature of 60โ. Liquid water 12cm deep flows over the flat plate with bulk volumetric flow rate of 2.4 × 10 ๐ /๐ ๐๐. The bulk liquid water temperature may be assumed to remain constant at 20โ as it flows along the length of the plate. 0.2m c) What is the total heat flux rate from the surface? โ๐ฟ / = 0.664๐ ๐ ๐๐ / ๐ 992.2 × 0.1 × 0.8 = 0.664 × 658 × 10 ๐๐ข = โ = 370.3 × . . ๐ = โ๐ด ๐ − ๐ / × 4.14 / = 370.3 = 307 = 307 × 0.16 × 40 = 1965๐/๐ < Transport phenomena 2 by JD > Problem 2) From an experiment of fluid flow over a heated flat plate, it has been shown that the temperature profile within the TBL is given as below. (Here, flow velocity is assumed to depend only on y coordinate) ๐ฃ ๐ = 400โ ๐ฆ ๐ = 300โ ๐−๐ ๐ฃ = 1 − (0.7 + ๐ฆ) ๐ −๐ ๐ / ๐ฅ Q. If ๐ = 400โ, ๐ = 300โ, ๐ = 0.037 ๐/๐๐พ, and = 1000/๐, what is the heat flux and heat transfer coefficient on the surface? < Transport phenomena 2 by JD > Problem 2) From an experiment of fluid flow over a heated flat plate, it has been shown that the temperature profile within the TBL is given as below. (Here, flow velocity is assumed to depend only on y coordinate) ๐ฃ ๐ = 400โ ๐ฆ ๐ = 0.037๐/๐๐พ ๐−๐ ๐ฃ = 1 − (0.7 + ๐ฆ) ๐ −๐ ๐ ๐ = 300โ / ๐ฅ ๐๐ ๐๐ฆ =− 1 ๐ −๐ 7 ๐ = −๐ ๐๐ ๐๐ฆ ๐ฃ ๐ 0.7 + =โ ๐ −๐ ๐ฃ ๐ฆ ๐ =− = 3947๐/๐ 1 ๐ −๐ 7 ๐ฃ ๐ 0.7 + ๐ฃ ๐ฆ ๐ = −106,669๐พ/๐ โ = 39.5๐/๐ ๐พ < Transport phenomena 2 by JD > Problem 2) From an experiment of fluid flow over a heated flat plate, it has been shown that the temperature profile within the TBL is given as below. (Here, flow velocity is assumed to depend only on y coordinate) ๐ฃ ๐ = 400โ ๐ฆ ๐ = 300โ ๐ = 0.037๐/๐๐พ ๐−๐ ๐ฃ = 1 − (0.7 + ๐ฆ) ๐ −๐ ๐ / ๐ฅ Further discussion) What if, velocity is dependent both on ๐ and ๐ ?? Hint. Energy balance analysis with control volume integral (P.286~287) < Transport phenomena 2 by JD > Problem 3) Consider a human body as a cylinder with 40cm diameter and 1.8m height in still air. If the body temperature is 2 โ lower than that of the air, how much of energy will be required to maintain body temperature(37 โ)? Generally, a human intakes about 8400KJ (2000kcal)/day. Compare it with calculated value. 1) Vertical cylinder problem ๏ (๐บ๐ = 2) = . . = 0.222 ≥ = 1.16 × 10 × 2 × 1.8 = . = 0.182 = 191.8) < Churchill and Chu’s Experiments > 0.387 × 1.16 × 10 × 2 × 1.8 × 0.705 = 0.825 + / 1 + 0.492/0.705 / = 0.825 + 10.17 = 121 ๏ = โ = 121 × = 121 × . . = 1.82 / = 121 < Transport phenomena 2 by JD > Problem 3) Consider a human body as a cylinder with 40cm diameter and 1.8m height in still air. If the body temperature is 2 โ lower than that of the air, how much of energy will be required to maintain body temperature(37 โ)? Generally, a human intakes about 8400KJ (2000kcal)/day. Compare it with calculated value. 3) ๐ = โ๐ดโ๐ = 1.82 × 0.4 × ๐ × 1.8 × 2 = 8.23๐ Total heat loss = 8.23๐ × 3600 × 24 = 711072 711072 = 0.084 8400 × 1000 About 8% of energy is used to maintain body temperature, even in the very hot weather < Transport phenomena 2 by JD > Problem 4) Problem 4) Problem 4) ๐จ ODE to be solved Boundary conditions Problem 5) JD left a cup of coffee for two weeks in his office. Initially, height of coffee was 7cm. Estimate the height of coffee after two weeks. Temperature is 293K and diffusion coefficient (D) of coffee (water) is ๐ท = 2.5 × 10 ๐ /๐ ๐๐ and pressure is 2.34 × 10 ๐๐. z 1) Pseudo steady state assumption & Mass balance ๐๐ 8cm − ๐๐ ๐ = ๐ฆ (๐ =0 ๐ + ๐ ) − cD ๐๐ฆ = constant ๐z 7cm ๐ = = ๐ถ๐๐๐ ๐ก๐๐๐ก, ๐ cD 1−y ln( ) z -z 1−y =0 Problem 5) JD left a cup of coffee for two weeks in his office. Initially, height of coffee was 7cm. Estimate the height of coffee after two weeks. Temperature is 293K and diffusion coefficient (D) of coffee (water) is ๐ท = 2.5 × 10 ๐ /๐ ๐๐ and pressure is 2.34 × 10 ๐๐. z ๐ฆ = ๐ A= ๐d(z − z ) A Mdt ๐ 8cm = ๐ฆ =0 cD 1−y ๐d(z − z ) ln( )= z -z 1−y Mdt 7cm C= * z − z d(z − z ) = cMD 1 − y ln( )dt ๐ 1−y < Open position > Complex fluid and Soft matter physics lab ์ฐ๊ตฌ ๋ถ์ผ: 1) Rheology (๋ฌผ์ง์ ๋ณํ๊ณผ ํ๋ฆ ์ฐ๊ตฌ) 2) Soft matter (Colloid & Polymer) 3) Process modeling & analysis ์ง์ ์๊ฒฉ: ๋ํ์ ์งํ์ ๊ณ ๋ คํ๋ ์ฐฝ์์ ์ด๊ณ ์ ๊ทน์ ์ธ 3,4ํ๋ (Attitude is all!!) ๋ชจ์ง ์ธ์: 2๋ช Colloidal gel Colloidal glass ์งํ ์์ ์ฐ๊ตฌ: 1) Temperature-Responsive polymer์ ์ ๋ณ๋ฌผ์ฑ ์ ์ด๋ฅผ ํตํ ๋ฌผ์ง ์ ๋ฌ ์กฐ์ (Sun-screen ๋ฐ Drug & Cosmetics์์ ์์ฉ) 2) Li-ion battery paste์ rheological property์ ๋ฐ๋ฅธ ๊ณต์ ๋ฐ ์ฑ๋ฅ ๋ถ์ 3) Liquid metal์ ์ ๋ณํ์ ํน์ฑ ๋ถ์ ๋ฐ ์์ฉ 4) ์ํ์ ์ฌ์ฉ๋๋ Hydrocolloids์ ์ ๋ณํ ํน์ฑ ๋ถ์ 5) ์ด๋ก ์ ์ ๊ทผ (๋ชจ๋ธ๋ง ๋ฐ ์ ์ ์๋ฎฌ๋ ์ด์ )์ ์ด์ฉํ Colloid suspension์ ์ ๋ณํ ๊ฑฐ๋ ๋ถ์ 6) ์์นํด์์ ์ด์ฉํ ์ ๋ ๋ถ์ 7) ๊ธฐํ ๋ณธ์ธ์ด ํ๊ณ ์ถ์ ์ฐ๊ตฌ ์ ์ ์ผ๋ง๋ ์ง ํ์!! < Open position > Complex fluid and Soft matter physics lab ๊ทผ๋ฌด ์กฐ๊ฑด: ์ถํด๊ทผ ์์ , ์ฃผ1ํ ๊ฐ์ธ ๋ฏธํ , ์ฃผ1ํ ์ฐ๊ตฌ์ค ๋ฏธํ (Paper & Research presentation) ์ฐ๊ตฌ ๋ฐ ํ์ ์๋ง ์ง์คํ ์ ์๋ ์ธ๊ฑด๋น, ์์ ๋ก์ด & ํ๋ฌธ์ ์ธ ๋ถ์๊ธฐ (๊ณผ์ ๋ถ๋ด X) ์์ ์๊ธฐ: 2021.1์ ํน์ 3์ ~ ์ด๋ฐ ๋ถ์๊ฒ ์ถ์ฒ - ๋ฌผ๋ฆฌํํ, ๊ณตํ์ํ, ์ ๋ฌํ์ 1&2 ์ ํฅ๋ฏธ๋ฅผ ๋๋๋ค (ํํ ๋ณด๋ค๋ ๋ฌผ๋ฆฌ & ์ํ์ด์ง!) Colloidal gel Colloidal glass - ์คํ์ ๋ง์ด ํ๋๊ฒ ์ซ๋ค & ๋ชธ์ ์ ์ข์ ํํ์ฝํ์ ์ฐ๊ณ ์ถ์ง ์๋ค - ์ปดํจํฐ ์๋ฎฌ๋ ์ด์ ์ด๋ ์ด๋ก ์ด ์ข๋ค (๋๋ ์ ์์ ์ ๋น์๋ค) - ๊ถ๊ธํ ๊ฑด ๋ชป ์ฐธ์! ์ ๋๊น์ง ๊ณ ๋ฏผํ๋ค! - ์ด๋ ค์ด ๋ฌธ์ ๋ฅผ ํด๊ฒฐํ๋ ๊ฒ์์ ์ฌ๋ฏธ๋ฅผ ๋๋๋ค - ๋จ๋ค ๋คํ๋ ์๋์ง, ๋ฐ์ด์ค๋ ์์ํด!! - ENTJ ๋ ์ ๋ง๊ฒ ๋๋ฐ? ์ง์ ๋ฐฉ๋ฒ: jdpark@sookmyung.ac.kr ๋ก ๊ฐ๋จํ ์๊ธฐ์๊ฐ & ์ง์๋๊ธฐ ์ ์ด์ ๋ณด๋ด์ฃผ์ธ์~ (12์ 28์ผ ์์์ผ๊น์ง), ์ง์์ ์ ๊ถ๊ธํ์ ์ด ์๊ฑฐ๋ ์๋ด์ ์ํด๋ ์ฐ๋ฝ์ฃผ์ธ์~