IEK PROCESS HEAT TRANSFER [PEMINDAHAN HABA PROSES]

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1 UNIVERSII SAINS MALAYSIA Supplementary Semester Exaation Academic Session 200/20 June 20 IEK 22 - PROESS HEA RANSFER [PEMINDAHAN HABA PROSES] Duration: 3 hours Masa: [3 jam] Please check that this exaation paper consists of WELVE pages of printed material before you begin the exaation. [Sila pastikan bahawa kertas peperiksaan ini mengandungi DBELAS muka surat yang bercetak sebelum anda memulakan peperiksaan ini.] Instructions: Answer FIVE questions. You may answer the questions either in Bahasa Malaysia or in English. [Arahan: Jawab LIMA soalan. Anda dibenarkan menjawab soalan sama ada dalam Bahasa Malaysia atau Bahasa Inggeris.] In the event of any discrepancies, the English version shall be used. [Sekiranya terdapat sebarang percanggahan pada soalan peperiksaan, versi Bahasa Inggeris hendaklah diguna pakai.] 2/-

2 - 2 [IEK 22]. A furnace wall consisting of 0.30 m of fire clay brick (k =.56 W/m.K), 0.20 m of kaolin insulating brick (k 2 = 0.73 W/m.K) and a 0.0 m outer layer of masonry brick (k 3 = W/m.K) is exposed to furnace gas at 370 K with air at 300 K adjacent to the outer wall. he inside and outside convective heat transfer coefficients are 5 and 23 W/m 2.K, respectively. Detere the heat loss per square meter and the intermediate temperatures between walls.. (00 marks) 2. (a) Benzene condenses at atmospheric pressure on the outside of a 25-mm steel pipe and air at 5 o flows within at 6 m/s. he pipe wall is 3.5 mm thick. h i = 20 W/m 2. o. h o =,200 W/m 2. o. k m = 45 W/m. o. alculate the overall heat transfer coefficients based on both inside and outside areas. (30 marks) An organic liquid (c p = J/g. o ) flowing at 9,000 kg/h is to be cooled from 85 to 40 o using 3,500 kg/h of cooling water (c p = J/g. o ) at 20 o. he film coefficient for the organic liquid, outside the tubes, is,700 W/m 2. o. he wall resistance can be neglected. h i =,000 W/m 2. o. What area is needed if the flow is (i) countercurrent; (ii) parallel? (70 marks) 3. Water is flowing in a horizontal steel pipe of ID m and OD m at an average temperature of 65.6 o and a velocity of 2.44 m/s. It is being heated by condensing steam at 07.8 o on the outside of the pipe wall. he steam side coefficient has been estimated as h o = 0,500 W/m 2.K. (a) (c) alculate the convective coefficient h i for the water inside the pipe. alculate the overall coefficient U i based on the inside surface area. alculate the heat-transfer rate for m of pipe with the water at an average temperature of 65.6 o. For water at 65.6 o, Pr = 2.72, = 980 kg/m 3, k = W/m.K, = 4.32 x 0-4 kg/m.s (00 marks) 3/-

3 - 3 [IEK 22] 4. Water enters a 3.0-cm-diameter tube at 5.56 o and leaves at o. he mass flow rate is.0 kg/s. and the tube wall temperature is constant at 60 o. Detere the length of the tube. For water, c p = 4.8 J/kg. o, k =.0.64 W/m. o. (00 marks) 5. It is desired to use a double-pipe counter-current heat exchanger to cool 3 kg/s of oil (c p = 2. kj/kg.k) from 20 o. ooling water (c p = 4.2 kj/kg.k) at 20 o enters the heat exchanger at a rate of 0 kg/s. he overall heat transfer coefficient of the heat exchanger is 600 W/m 2.K and the heat transfer area is 6 m 2. alculate the exit temperature of oil and water. Given information: exp NU h h h h2 Or c c h h Hot fluid h2 c Hot fluid 2 A (00 marks) 4/-

4 - 4 - [IEK 22] 6. A single effect evaporator is to be used to concentrate a food solution containing 5% (by weight) dissolved solids to 50% solids. he feed stream enters the evaporator at 29 K with a feed rate of.0 kg/s. Steam of 0.07 bar is maintained in the evaporator at temperature 399K. Assug that the properties of the solution are the same as those of water, and taking the overall heat transfer coefficient to be 2.3 kwm -2 K -, calculate the rate of steam consumption and the necessary heat transfer surface area. alculate also the economy of the evaporator involved. Given information: λs = 285 kj/kg, h V = 2572 kj/kg, s = 399K, h L =63 kj/kg and L =32 K, h F = 75.5 kj/kg (00 marks) 5/-

5 - 5 - [IEK 22]. Satu dinding relau yang mengandungi selapisan bata tanah liat api tebalnya 0.30 m (k =.56 W/m.K), selapisan bata penebat kaolin tebalnya 0.20 m (k 2 = 0.73 W/m.K) dan selapisan luar bata batu tebalnya 0.0 m (k 3 = W/m.K) didedahkan kepada satu gas relau pada 370 K dan udara pada 300 K di luar dinding. Pekali pedahan haba perolakan dalaman dan luaran ialah masingmasing 5 dan 23 W/m 2.K. entukan kehilangan haba per meter persegi dan suhusuhu di antara lapisan-lapisan. (00 markah) 2. (a) Benzena mengkondensasi pada tekanan atmosfera di luar satu paip keluli yang berdiameter 25 mm dan udara pada 5 o mengalir di dalam paip pada 6 m/s. Ketebalan dinding paip ialah 3.5 mm. h i = 20 W/m 2. o. h o =,200 W/m 2. o. k m = 45 W/m. o. Hitungkan pekali pedahan haba keseluruhan berdasarkan kedua-dua luas dalaman dan luaran. (30 markah) Satu cecair organik (c p = J/g. o ) yang mengalir pada 9,000 kg/h akan disejukkan dar 85 hingga 40 o dengan menggunakan 3,500 kg/h air penyejuk (c p = J/g. o ) pada 20 o. Pekali pedahan haba bagi cecair organik tersebut, di luar tiub, ialah,700 W/m 2. o. Rintangan dinding tiub boleh diabaikan. h i =,000 W/m 2. o. Apakah luas diperlukan jika aliran ialah (i) aruslawan; (ii) selari. (70 markah) 3. Air mengalir di dalam satu paip keluli mendatar yang mempunyai ID m dan OD m pada suhu purata 65.6 o dan halaju 2.44 m/s. Air tersebut akan dipanaskan dengan stim yang mengkondensasi pada 07.8 o di luar dinding paip. Pekali pedahan sebelah stim ialah h o = 0,500 W/m 2.K. (a) (c) Hitungkan pekali pedahan haba perolakan h i bagi air di dalam paip. Hitungkan pekali pedahan haba keseluruhan U i berdasarkan luas permukaan dalaman. Hitungkan kadar pedahan haba bagi m (panjang) paip dengan air pada suhu purata 65.6 o. Bagi air pada 65.6 o, Pr = 2.72, = 4.32 x 0-4 kg/m.s = 980 kg/m 3, k = W/m.K, (00 markah) 6/-

6 - 6 - [IEK 22] 4. Air memasuki satu tiub yang berdiameter 3.0 cm pada 5.56 o dan keluar pada o. Kadar aliran jisim ialah.0 kg/s, dan suhu dinding tiub ialah malar pada 60 o. entukan panjang tiub tersebut. Bagi air, c p = 4.8 J/kg. o, k =.0.64 W/m. o. (00 markah) 5. Satu penukar haba paip berganda aliran berlawanan digunakan untuk menyejukkan 3 kg/s yak panas (c p = 2. kj/kg.k) bersuhu 20 o. Air penyejuk (c p = 4.2 kj/kg.k) pada suhu 20 o memasuki penukar haba pada kadar aliran 0 kg/s. Pemalar pedahan haba keseluruhan ialah 600 W/m 2.K dan luas permukaan penukaran haba ialah 6 m 2. Kira suhu akhir yak dan air yang keluar dari penukar haba. Maklumat diberi : exp NU h h h h2 or c c h h ecair panas h2 c ecair sejuk 2 A (00 markah) 7/-

7 - 7 - [IEK 22] 6. Satu penyejat kesan tunggal digunakan untuk memekatkan larutan makanan mengandungi 5% (berat) pepejal terlarut kepada 50% (berat) pepejal. Aliran suapan memasuki penyejat tunggal pada suhu 29 K dengan kadar aliran.0 kg/s. Stim yang dibekalkan pada tekanan 0.07 bar ke dalam penyejat bersuhu 399 K. Dengan mengandaikan sifat-sifat larutan makanan tersebut menyerupai sifat-sifat air dan pemalar pedahan haba keseluruhan ialah 2.3 kwm -2 K -, kirakan kadar penggunaan stim dan luas permukaan penukaran haba yang diperlukan. Kirakan juga ekonomi penyejat yang digunakkan. Maklumat yang diberi: λ S = 285 kj/kg, h V = 2572 kj/kg, h L =63 kj/kg and L =32 K, h F = 75.5 kj/kg (00 markah) 8/-

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