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Page 1 19. Calorimetry and Heat Tansfer Introductory Exercise 19.1. 1. As Heat gain = Heat loss Q Q Q 1 2 3 + = Þ 140 15 80 ´ ´ + ´ 0.53 m = ´ ´ 200 1 40 Þ m = - = 8000 1113 80 86 g is the mass of ice melt \ Mass of water = + = 200 86 286 g g g and mass of ice = - = 140 86 54 g g g while final temperature of mixture is 0°C. 2. ms ms A B ( ) ( ) 16 12 19 16 - = - Þ 4 3 s s A B = ms ms B C ( ) ( ) 23 19 28 23 - = - Þ 4 5 s s B C = \ ms ms A ( ) ( ) q q - = - 12 4 5 28 or 3 4 12 4 5 28 s s B B ( ) ( ) q q - = - or 15 12 16 28 ( ) ( ) q q - = - or 31 448 180 q = + Þ q = ° 20 26 . C 3. mL ms = Dq Þ 80 1 cal cal/ = °C (q - ° 0 C) Þ q = ° 80 C 4. As Heat gain = Heat loss Þ ( ) 100 529 80 - ´ = ´ m m \ 100 529 609 ´ = m Þ m = ´ = 100 529 609 g 86.86 g of ice will be formed. 5. P d dt d dt ms dm dt s = = = q q q ( ) D D Þ dm dt P s = Dq \ dm dt = ´ ° ´ ° 500 10 4200 10 6 J/s J/ kg C C = ´ 5 4 2 10 4 . kg/s = ´ 12 10 4 . kg/s ice –15°C ice 0°C water 0°C Q 1 Q 2 140 g 140 g m g water 0°C 200 g Q 3 water 40°C 200 g A 12°C B 19°C C 28°C 16°C 23°C 0°C Page 2 19. Calorimetry and Heat Tansfer Introductory Exercise 19.1. 1. As Heat gain = Heat loss Q Q Q 1 2 3 + = Þ 140 15 80 ´ ´ + ´ 0.53 m = ´ ´ 200 1 40 Þ m = - = 8000 1113 80 86 g is the mass of ice melt \ Mass of water = + = 200 86 286 g g g and mass of ice = - = 140 86 54 g g g while final temperature of mixture is 0°C. 2. ms ms A B ( ) ( ) 16 12 19 16 - = - Þ 4 3 s s A B = ms ms B C ( ) ( ) 23 19 28 23 - = - Þ 4 5 s s B C = \ ms ms A ( ) ( ) q q - = - 12 4 5 28 or 3 4 12 4 5 28 s s B B ( ) ( ) q q - = - or 15 12 16 28 ( ) ( ) q q - = - or 31 448 180 q = + Þ q = ° 20 26 . C 3. mL ms = Dq Þ 80 1 cal cal/ = °C (q - ° 0 C) Þ q = ° 80 C 4. As Heat gain = Heat loss Þ ( ) 100 529 80 - ´ = ´ m m \ 100 529 609 ´ = m Þ m = ´ = 100 529 609 g 86.86 g of ice will be formed. 5. P d dt d dt ms dm dt s = = = q q q ( ) D D Þ dm dt P s = Dq \ dm dt = ´ ° ´ ° 500 10 4200 10 6 J/s J/ kg C C = ´ 5 4 2 10 4 . kg/s = ´ 12 10 4 . kg/s ice –15°C ice 0°C water 0°C Q 1 Q 2 140 g 140 g m g water 0°C 200 g Q 3 water 40°C 200 g A 12°C B 19°C C 28°C 16°C 23°C 0°C Introductory Excersise 19.2 1. Rest of the liquid will be heated due to conduction and not convection. 2. dQ dt k r d dr = × - 4 2 p q ( ) \ dQ dt dr r k d × = - 2 4p q or dQ dt dr r k d a b T T 2 4 1 2 ò ò = - p q or dQ dt a b k T T 1 1 4 2 1 - æ è ç ö ø ÷ = - - p ( ) Þ dQ dt k T T a b kab T T b a = - - = - - 4 1 1 4 1 2 1 2 p p ( ) 3. d Q d t kA t = Dq Þ k dQ dt t A = × Dq \ Unit of k k = = watt m m - W/m - K 2 4. K A l K A l 1 1 1 2 2 2 D D q q = 001 19 3 5 10 2 . ( ) . ( ) - = + q q 0.08 or 2 19 28 10 ( ) ( ) - = + q q or 38 280 30 - = q or q = - = - ° 242 30 8.07 C dQ dt = ´ ´ + ´ - 0 . 0 1 8 .1 3.5 1 19 10 2 ( ) = 7.74 W / m 2 5. dQ dt dm dt L = × = ´ ´ 0.44 kg s 2.256 300 10 6 J/kg = 3308 J/s . 8 = = ´ ´ - ´ - kA t q q 50.2 0.15 1.2 ( ) 100 10 2 = - 627.5 ( ) q 100 Þ q - = = 100 3308.8 627.5 5.27 Þ q = ° 105.27 C 6. dQ dt kA y dm dt L = - - = × [ ( )] 0 q = × = × r r dV dt L A dy dt L Þ kA y AL dy dt q r = Þ dy dt k L y = q r (Proved) 7. dQ dt e AT = s 4 = ´ ´ ´ ´ - - 4 5.67 10 4 4 10 8 2 2 p ( ) ´ ( ) 3000 4 = ´ ´ ´ ´ 0 4 4 4 3 2 4 . p 5.67 J/s = ´ 3.7 10 4 watt 8. dQ dt R = Dq th Þ R d dt K W th KW = = = - Dq q 1 65 | Calorimetry and Heat Tansfer dy A y 19°C –10°C q 0.01 0.08 3.5 cm 2 cm r b a r+dr Page 3 19. Calorimetry and Heat Tansfer Introductory Exercise 19.1. 1. As Heat gain = Heat loss Q Q Q 1 2 3 + = Þ 140 15 80 ´ ´ + ´ 0.53 m = ´ ´ 200 1 40 Þ m = - = 8000 1113 80 86 g is the mass of ice melt \ Mass of water = + = 200 86 286 g g g and mass of ice = - = 140 86 54 g g g while final temperature of mixture is 0°C. 2. ms ms A B ( ) ( ) 16 12 19 16 - = - Þ 4 3 s s A B = ms ms B C ( ) ( ) 23 19 28 23 - = - Þ 4 5 s s B C = \ ms ms A ( ) ( ) q q - = - 12 4 5 28 or 3 4 12 4 5 28 s s B B ( ) ( ) q q - = - or 15 12 16 28 ( ) ( ) q q - = - or 31 448 180 q = + Þ q = ° 20 26 . C 3. mL ms = Dq Þ 80 1 cal cal/ = °C (q - ° 0 C) Þ q = ° 80 C 4. As Heat gain = Heat loss Þ ( ) 100 529 80 - ´ = ´ m m \ 100 529 609 ´ = m Þ m = ´ = 100 529 609 g 86.86 g of ice will be formed. 5. P d dt d dt ms dm dt s = = = q q q ( ) D D Þ dm dt P s = Dq \ dm dt = ´ ° ´ ° 500 10 4200 10 6 J/s J/ kg C C = ´ 5 4 2 10 4 . kg/s = ´ 12 10 4 . kg/s ice –15°C ice 0°C water 0°C Q 1 Q 2 140 g 140 g m g water 0°C 200 g Q 3 water 40°C 200 g A 12°C B 19°C C 28°C 16°C 23°C 0°C Introductory Excersise 19.2 1. Rest of the liquid will be heated due to conduction and not convection. 2. dQ dt k r d dr = × - 4 2 p q ( ) \ dQ dt dr r k d × = - 2 4p q or dQ dt dr r k d a b T T 2 4 1 2 ò ò = - p q or dQ dt a b k T T 1 1 4 2 1 - æ è ç ö ø ÷ = - - p ( ) Þ dQ dt k T T a b kab T T b a = - - = - - 4 1 1 4 1 2 1 2 p p ( ) 3. d Q d t kA t = Dq Þ k dQ dt t A = × Dq \ Unit of k k = = watt m m - W/m - K 2 4. K A l K A l 1 1 1 2 2 2 D D q q = 001 19 3 5 10 2 . ( ) . ( ) - = + q q 0.08 or 2 19 28 10 ( ) ( ) - = + q q or 38 280 30 - = q or q = - = - ° 242 30 8.07 C dQ dt = ´ ´ + ´ - 0 . 0 1 8 .1 3.5 1 19 10 2 ( ) = 7.74 W / m 2 5. dQ dt dm dt L = × = ´ ´ 0.44 kg s 2.256 300 10 6 J/kg = 3308 J/s . 8 = = ´ ´ - ´ - kA t q q 50.2 0.15 1.2 ( ) 100 10 2 = - 627.5 ( ) q 100 Þ q - = = 100 3308.8 627.5 5.27 Þ q = ° 105.27 C 6. dQ dt kA y dm dt L = - - = × [ ( )] 0 q = × = × r r dV dt L A dy dt L Þ kA y AL dy dt q r = Þ dy dt k L y = q r (Proved) 7. dQ dt e AT = s 4 = ´ ´ ´ ´ - - 4 5.67 10 4 4 10 8 2 2 p ( ) ´ ( ) 3000 4 = ´ ´ ´ ´ 0 4 4 4 3 2 4 . p 5.67 J/s = ´ 3.7 10 4 watt 8. dQ dt R = Dq th Þ R d dt K W th KW = = = - Dq q 1 65 | Calorimetry and Heat Tansfer dy A y 19°C –10°C q 0.01 0.08 3.5 cm 2 cm r b a r+dr AIEEE Corner ¢ Subjective Questions (Level-1) 1. ice Water Water steam 0 C 0 C 100 C 100 C ° ° ° ° ¾® ¾® ¾® Q Q Q 1 2 3 Q Q Q Q = + + 1 2 3 = + + mL ms mL f v Dq = + ´ + 10 80 1 100 540 [ ] = ´ 10 720 cal = 7200 cal 2. 10 g of wa ter at 40°C do not have suf fi cient heat en ergy to melt 15 g of ice at 0°C , so there will be a mix ture of ice-wa ter at 0°C. Let the mass of ice left is mg. \ ( ) 15 80 10 1 40 - ´ = ´ ´ m 15 5 - = m Þ m = 10 g \ Mass of ice = 10 g and mass of water = + = ( ) 10 5 15 g g 3. 4 60 55 1 55 50 ´ - = ´ ´ - s s P R ( ) ( ) Þ 4s s P R = 1 60 55 1 55 50 ´ - = ´ - s s P Q ( ) ( ) Þ s s P Q = 1 60 1 50 ´ - = ´ - s s Q R ( ) ( ) q q or s s P P ( ) ( ) 60 4 50 - = - q q 260 5 = q Þ q = = ° 260 5 52 C 4. dQ dt m = ´ ´ ´ 336 10 4 60 3 J/ kg s = 1400 J/ kg = 1400 m W / kg = × = ´ - ´ m s t m D q q 4 2 0 0 0 2 6 0 ( ) c s \ 1 4 00 2 60 4200 ´ ´ = q Þ q = ° 40 C 5. Q mv ms mL = ´ = + 1 2 1 2 2 Dq Þ v s L = + 4 ( ) Dq \ v = ´ + ´ 4 125 300 2 5 10 4 ( . ) = ´ + ´ 4 3 75 10 4 ( . ) 2.5 = ´ ´ 4 10 4 6.25 = 500 m/s 6. h q mg h ms D D = \ D D q h = = ´ ´ = ° g h s 0.4 0.5 400 C 10 800 1 = ´ ° - 2.5 C 10 3 7. K A l K A l 1 2 0 100 ( ) ( ) q q - = - Þ ( ) K K K 1 2 2 100 + = q \ q = + = ´ ´ = ° 100 100 46 390 46 1055 2 1 2 K K K . C 8. i i i CD AC CB = - KA l KA l KA l ( ) ( ) / ( ) / q q q - = - - - 25 100 2 0 2 or q q q - = - - 25 2 100 2 ( ) or 5 225 q = Þ q = ° 45 C \ i R CD = = - = Dq th 45 25 5 4 W 9. i i i A C D = + KA T l KA T l KA T l ( ) ( ) / ( ) / 1 3 2 3 2 3 2 - = - + - q q q Þ T T T 1 3 2 2 3 2 3 - = - + - q q q ( ) ( ) or T T T 1 2 3 2 3 1 4 3 + + = + æ è ç ö ø ÷ ( ) q Þ q = + + T T T 1 2 3 2 3 7 3 ( ) / = + + 3 2 7 1 2 3 T T T ( ) 10. K A l K A l ( ) ( ) 2 0 0 2 1 1 2 - = - q q q Calorimetry and Heat Tansfer | 66 T t 0°C q°C 5 1 7 Page 4 19. Calorimetry and Heat Tansfer Introductory Exercise 19.1. 1. As Heat gain = Heat loss Q Q Q 1 2 3 + = Þ 140 15 80 ´ ´ + ´ 0.53 m = ´ ´ 200 1 40 Þ m = - = 8000 1113 80 86 g is the mass of ice melt \ Mass of water = + = 200 86 286 g g g and mass of ice = - = 140 86 54 g g g while final temperature of mixture is 0°C. 2. ms ms A B ( ) ( ) 16 12 19 16 - = - Þ 4 3 s s A B = ms ms B C ( ) ( ) 23 19 28 23 - = - Þ 4 5 s s B C = \ ms ms A ( ) ( ) q q - = - 12 4 5 28 or 3 4 12 4 5 28 s s B B ( ) ( ) q q - = - or 15 12 16 28 ( ) ( ) q q - = - or 31 448 180 q = + Þ q = ° 20 26 . C 3. mL ms = Dq Þ 80 1 cal cal/ = °C (q - ° 0 C) Þ q = ° 80 C 4. As Heat gain = Heat loss Þ ( ) 100 529 80 - ´ = ´ m m \ 100 529 609 ´ = m Þ m = ´ = 100 529 609 g 86.86 g of ice will be formed. 5. P d dt d dt ms dm dt s = = = q q q ( ) D D Þ dm dt P s = Dq \ dm dt = ´ ° ´ ° 500 10 4200 10 6 J/s J/ kg C C = ´ 5 4 2 10 4 . kg/s = ´ 12 10 4 . kg/s ice –15°C ice 0°C water 0°C Q 1 Q 2 140 g 140 g m g water 0°C 200 g Q 3 water 40°C 200 g A 12°C B 19°C C 28°C 16°C 23°C 0°C Introductory Excersise 19.2 1. Rest of the liquid will be heated due to conduction and not convection. 2. dQ dt k r d dr = × - 4 2 p q ( ) \ dQ dt dr r k d × = - 2 4p q or dQ dt dr r k d a b T T 2 4 1 2 ò ò = - p q or dQ dt a b k T T 1 1 4 2 1 - æ è ç ö ø ÷ = - - p ( ) Þ dQ dt k T T a b kab T T b a = - - = - - 4 1 1 4 1 2 1 2 p p ( ) 3. d Q d t kA t = Dq Þ k dQ dt t A = × Dq \ Unit of k k = = watt m m - W/m - K 2 4. K A l K A l 1 1 1 2 2 2 D D q q = 001 19 3 5 10 2 . ( ) . ( ) - = + q q 0.08 or 2 19 28 10 ( ) ( ) - = + q q or 38 280 30 - = q or q = - = - ° 242 30 8.07 C dQ dt = ´ ´ + ´ - 0 . 0 1 8 .1 3.5 1 19 10 2 ( ) = 7.74 W / m 2 5. dQ dt dm dt L = × = ´ ´ 0.44 kg s 2.256 300 10 6 J/kg = 3308 J/s . 8 = = ´ ´ - ´ - kA t q q 50.2 0.15 1.2 ( ) 100 10 2 = - 627.5 ( ) q 100 Þ q - = = 100 3308.8 627.5 5.27 Þ q = ° 105.27 C 6. dQ dt kA y dm dt L = - - = × [ ( )] 0 q = × = × r r dV dt L A dy dt L Þ kA y AL dy dt q r = Þ dy dt k L y = q r (Proved) 7. dQ dt e AT = s 4 = ´ ´ ´ ´ - - 4 5.67 10 4 4 10 8 2 2 p ( ) ´ ( ) 3000 4 = ´ ´ ´ ´ 0 4 4 4 3 2 4 . p 5.67 J/s = ´ 3.7 10 4 watt 8. dQ dt R = Dq th Þ R d dt K W th KW = = = - Dq q 1 65 | Calorimetry and Heat Tansfer dy A y 19°C –10°C q 0.01 0.08 3.5 cm 2 cm r b a r+dr AIEEE Corner ¢ Subjective Questions (Level-1) 1. ice Water Water steam 0 C 0 C 100 C 100 C ° ° ° ° ¾® ¾® ¾® Q Q Q 1 2 3 Q Q Q Q = + + 1 2 3 = + + mL ms mL f v Dq = + ´ + 10 80 1 100 540 [ ] = ´ 10 720 cal = 7200 cal 2. 10 g of wa ter at 40°C do not have suf fi cient heat en ergy to melt 15 g of ice at 0°C , so there will be a mix ture of ice-wa ter at 0°C. Let the mass of ice left is mg. \ ( ) 15 80 10 1 40 - ´ = ´ ´ m 15 5 - = m Þ m = 10 g \ Mass of ice = 10 g and mass of water = + = ( ) 10 5 15 g g 3. 4 60 55 1 55 50 ´ - = ´ ´ - s s P R ( ) ( ) Þ 4s s P R = 1 60 55 1 55 50 ´ - = ´ - s s P Q ( ) ( ) Þ s s P Q = 1 60 1 50 ´ - = ´ - s s Q R ( ) ( ) q q or s s P P ( ) ( ) 60 4 50 - = - q q 260 5 = q Þ q = = ° 260 5 52 C 4. dQ dt m = ´ ´ ´ 336 10 4 60 3 J/ kg s = 1400 J/ kg = 1400 m W / kg = × = ´ - ´ m s t m D q q 4 2 0 0 0 2 6 0 ( ) c s \ 1 4 00 2 60 4200 ´ ´ = q Þ q = ° 40 C 5. Q mv ms mL = ´ = + 1 2 1 2 2 Dq Þ v s L = + 4 ( ) Dq \ v = ´ + ´ 4 125 300 2 5 10 4 ( . ) = ´ + ´ 4 3 75 10 4 ( . ) 2.5 = ´ ´ 4 10 4 6.25 = 500 m/s 6. h q mg h ms D D = \ D D q h = = ´ ´ = ° g h s 0.4 0.5 400 C 10 800 1 = ´ ° - 2.5 C 10 3 7. K A l K A l 1 2 0 100 ( ) ( ) q q - = - Þ ( ) K K K 1 2 2 100 + = q \ q = + = ´ ´ = ° 100 100 46 390 46 1055 2 1 2 K K K . C 8. i i i CD AC CB = - KA l KA l KA l ( ) ( ) / ( ) / q q q - = - - - 25 100 2 0 2 or q q q - = - - 25 2 100 2 ( ) or 5 225 q = Þ q = ° 45 C \ i R CD = = - = Dq th 45 25 5 4 W 9. i i i A C D = + KA T l KA T l KA T l ( ) ( ) / ( ) / 1 3 2 3 2 3 2 - = - + - q q q Þ T T T 1 3 2 2 3 2 3 - = - + - q q q ( ) ( ) or T T T 1 2 3 2 3 1 4 3 + + = + æ è ç ö ø ÷ ( ) q Þ q = + + T T T 1 2 3 2 3 7 3 ( ) / = + + 3 2 7 1 2 3 T T T ( ) 10. K A l K A l ( ) ( ) 2 0 0 2 1 1 2 - = - q q q Calorimetry and Heat Tansfer | 66 T t 0°C q°C 5 1 7 = - 3 100 2 KA l ( ) q \ 200 2 3 100 1 1 2 2 - = - = - q q q q ( ) ( ) Þ 3 2 200 1 2 q q - = q q q 1 2 2 3 500 11 1300 + = - = - Þ q 2 1300 11 118 2 = = ° . C q q 1 2 1 3 200 2 145 45 = + = ° [ ] . C 11. 25 400 10 100 12 4 = ´ - - ( ) / q + ´ - - 400 10 0 1 2 4 ( ) / q 25 8 10 100 2 = ´ - + - [ ] q q or 312.5 = - 2 100 q Þ q = = 412.5 2 206 25 . \ Dq 1 = 106.25 and Dq 2 206 25 = . \ D D q 1 1 2 l = ° = ° 106.25 C m 212.5 C/m / and D D q 2 1 2 l = ° = 206.25 C m 412.5 / °C/m 12. dQ dt e AT = = ´ ´ - s 4 8 10 0.6 5.67 ´ ´ ´ 2 1073 2 4 ( ) ( ) 0.1 = ´ ´ ´ ´ - 0.6 5.67 10.73 ( ) 4 2 10 2 = 902 W 13. dQ dt e AT æ è ç ö ø ÷ = 1 4 s and dQ dt AT æ è ç ö ø ÷ = 2 4 s Þ e dQ dt dQ dt = = = ( / ) ( / ) 1 2 210 700 0.3 14. ( ) 80 50 5 80 50 2 20 - = + - æ è ç ö ø ÷ c c Þ K = 6 45 ; ( ) 60 30 6 45 - = t 60 30 2 20 + - æ è ç ö ø ÷ Þ t = 9 min ¢ Objective Questions (Level-1) 1. 3 35 10 0 20 KA KA ( ) ( ) - = - q q Þ 6 35 ( ) - = q q Þ q = ´ = ° 6 35 7 30 C \ Dq A = - = ° 35 30 5 C 2. T T S N N S = = = l l 350 510 0.69 According to Wien’s law 3. dQ dt dQ dt K A l K l æ è ç ö ø ÷ æ è ç ö ø ÷ = × = 2 1 1 4 4 2 2 D D q q / Þ dm dt dm dt æ è ç ö ø ÷ = æ è ç ö ø ÷ 2 1 2 = 0.2 g/s 4. dQ dt K a a a a K a a a a = - - × = - - × 4 0 2 2 4 100 3 2 3 2 p q p q ( ) ( ) Þ 2 6 100 q q = - ( ) Þ q = ´ = ° 6 8 100 75 C 5. K A T T d K A T T d 1 2 1 2 3 2 3 ( ) ( ) - = - Þ K T T K T T 1 2 1 2 3 2 1 3 ( ) ( ) - = - Þ K K 1 2 1 3 = Þ K K 1 2 1 3 : : = 6. dQ dt dQ dt K A l KA l æ è ç ö ø ÷ æ è ç ö ø ÷ = × × é ë ê ù û ú é ë ê ù û ú 2 1 2 2 2 D D q q = 2 Þ d Q d t d Q d t æ è ç ö ø ÷ = æ è ç ö ø ÷ = 2 1 2 8 cal/s 7. 67 | Calorimetry and Heat Tansfer H 100°C 0°C S 1/2 m 1/2 m 25 W 0°C dx q, q, + dq x Page 5 19. Calorimetry and Heat Tansfer Introductory Exercise 19.1. 1. As Heat gain = Heat loss Q Q Q 1 2 3 + = Þ 140 15 80 ´ ´ + ´ 0.53 m = ´ ´ 200 1 40 Þ m = - = 8000 1113 80 86 g is the mass of ice melt \ Mass of water = + = 200 86 286 g g g and mass of ice = - = 140 86 54 g g g while final temperature of mixture is 0°C. 2. ms ms A B ( ) ( ) 16 12 19 16 - = - Þ 4 3 s s A B = ms ms B C ( ) ( ) 23 19 28 23 - = - Þ 4 5 s s B C = \ ms ms A ( ) ( ) q q - = - 12 4 5 28 or 3 4 12 4 5 28 s s B B ( ) ( ) q q - = - or 15 12 16 28 ( ) ( ) q q - = - or 31 448 180 q = + Þ q = ° 20 26 . C 3. mL ms = Dq Þ 80 1 cal cal/ = °C (q - ° 0 C) Þ q = ° 80 C 4. As Heat gain = Heat loss Þ ( ) 100 529 80 - ´ = ´ m m \ 100 529 609 ´ = m Þ m = ´ = 100 529 609 g 86.86 g of ice will be formed. 5. P d dt d dt ms dm dt s = = = q q q ( ) D D Þ dm dt P s = Dq \ dm dt = ´ ° ´ ° 500 10 4200 10 6 J/s J/ kg C C = ´ 5 4 2 10 4 . kg/s = ´ 12 10 4 . kg/s ice –15°C ice 0°C water 0°C Q 1 Q 2 140 g 140 g m g water 0°C 200 g Q 3 water 40°C 200 g A 12°C B 19°C C 28°C 16°C 23°C 0°C Introductory Excersise 19.2 1. Rest of the liquid will be heated due to conduction and not convection. 2. dQ dt k r d dr = × - 4 2 p q ( ) \ dQ dt dr r k d × = - 2 4p q or dQ dt dr r k d a b T T 2 4 1 2 ò ò = - p q or dQ dt a b k T T 1 1 4 2 1 - æ è ç ö ø ÷ = - - p ( ) Þ dQ dt k T T a b kab T T b a = - - = - - 4 1 1 4 1 2 1 2 p p ( ) 3. d Q d t kA t = Dq Þ k dQ dt t A = × Dq \ Unit of k k = = watt m m - W/m - K 2 4. K A l K A l 1 1 1 2 2 2 D D q q = 001 19 3 5 10 2 . ( ) . ( ) - = + q q 0.08 or 2 19 28 10 ( ) ( ) - = + q q or 38 280 30 - = q or q = - = - ° 242 30 8.07 C dQ dt = ´ ´ + ´ - 0 . 0 1 8 .1 3.5 1 19 10 2 ( ) = 7.74 W / m 2 5. dQ dt dm dt L = × = ´ ´ 0.44 kg s 2.256 300 10 6 J/kg = 3308 J/s . 8 = = ´ ´ - ´ - kA t q q 50.2 0.15 1.2 ( ) 100 10 2 = - 627.5 ( ) q 100 Þ q - = = 100 3308.8 627.5 5.27 Þ q = ° 105.27 C 6. dQ dt kA y dm dt L = - - = × [ ( )] 0 q = × = × r r dV dt L A dy dt L Þ kA y AL dy dt q r = Þ dy dt k L y = q r (Proved) 7. dQ dt e AT = s 4 = ´ ´ ´ ´ - - 4 5.67 10 4 4 10 8 2 2 p ( ) ´ ( ) 3000 4 = ´ ´ ´ ´ 0 4 4 4 3 2 4 . p 5.67 J/s = ´ 3.7 10 4 watt 8. dQ dt R = Dq th Þ R d dt K W th KW = = = - Dq q 1 65 | Calorimetry and Heat Tansfer dy A y 19°C –10°C q 0.01 0.08 3.5 cm 2 cm r b a r+dr AIEEE Corner ¢ Subjective Questions (Level-1) 1. ice Water Water steam 0 C 0 C 100 C 100 C ° ° ° ° ¾® ¾® ¾® Q Q Q 1 2 3 Q Q Q Q = + + 1 2 3 = + + mL ms mL f v Dq = + ´ + 10 80 1 100 540 [ ] = ´ 10 720 cal = 7200 cal 2. 10 g of wa ter at 40°C do not have suf fi cient heat en ergy to melt 15 g of ice at 0°C , so there will be a mix ture of ice-wa ter at 0°C. Let the mass of ice left is mg. \ ( ) 15 80 10 1 40 - ´ = ´ ´ m 15 5 - = m Þ m = 10 g \ Mass of ice = 10 g and mass of water = + = ( ) 10 5 15 g g 3. 4 60 55 1 55 50 ´ - = ´ ´ - s s P R ( ) ( ) Þ 4s s P R = 1 60 55 1 55 50 ´ - = ´ - s s P Q ( ) ( ) Þ s s P Q = 1 60 1 50 ´ - = ´ - s s Q R ( ) ( ) q q or s s P P ( ) ( ) 60 4 50 - = - q q 260 5 = q Þ q = = ° 260 5 52 C 4. dQ dt m = ´ ´ ´ 336 10 4 60 3 J/ kg s = 1400 J/ kg = 1400 m W / kg = × = ´ - ´ m s t m D q q 4 2 0 0 0 2 6 0 ( ) c s \ 1 4 00 2 60 4200 ´ ´ = q Þ q = ° 40 C 5. Q mv ms mL = ´ = + 1 2 1 2 2 Dq Þ v s L = + 4 ( ) Dq \ v = ´ + ´ 4 125 300 2 5 10 4 ( . ) = ´ + ´ 4 3 75 10 4 ( . ) 2.5 = ´ ´ 4 10 4 6.25 = 500 m/s 6. h q mg h ms D D = \ D D q h = = ´ ´ = ° g h s 0.4 0.5 400 C 10 800 1 = ´ ° - 2.5 C 10 3 7. K A l K A l 1 2 0 100 ( ) ( ) q q - = - Þ ( ) K K K 1 2 2 100 + = q \ q = + = ´ ´ = ° 100 100 46 390 46 1055 2 1 2 K K K . C 8. i i i CD AC CB = - KA l KA l KA l ( ) ( ) / ( ) / q q q - = - - - 25 100 2 0 2 or q q q - = - - 25 2 100 2 ( ) or 5 225 q = Þ q = ° 45 C \ i R CD = = - = Dq th 45 25 5 4 W 9. i i i A C D = + KA T l KA T l KA T l ( ) ( ) / ( ) / 1 3 2 3 2 3 2 - = - + - q q q Þ T T T 1 3 2 2 3 2 3 - = - + - q q q ( ) ( ) or T T T 1 2 3 2 3 1 4 3 + + = + æ è ç ö ø ÷ ( ) q Þ q = + + T T T 1 2 3 2 3 7 3 ( ) / = + + 3 2 7 1 2 3 T T T ( ) 10. K A l K A l ( ) ( ) 2 0 0 2 1 1 2 - = - q q q Calorimetry and Heat Tansfer | 66 T t 0°C q°C 5 1 7 = - 3 100 2 KA l ( ) q \ 200 2 3 100 1 1 2 2 - = - = - q q q q ( ) ( ) Þ 3 2 200 1 2 q q - = q q q 1 2 2 3 500 11 1300 + = - = - Þ q 2 1300 11 118 2 = = ° . C q q 1 2 1 3 200 2 145 45 = + = ° [ ] . C 11. 25 400 10 100 12 4 = ´ - - ( ) / q + ´ - - 400 10 0 1 2 4 ( ) / q 25 8 10 100 2 = ´ - + - [ ] q q or 312.5 = - 2 100 q Þ q = = 412.5 2 206 25 . \ Dq 1 = 106.25 and Dq 2 206 25 = . \ D D q 1 1 2 l = ° = ° 106.25 C m 212.5 C/m / and D D q 2 1 2 l = ° = 206.25 C m 412.5 / °C/m 12. dQ dt e AT = = ´ ´ - s 4 8 10 0.6 5.67 ´ ´ ´ 2 1073 2 4 ( ) ( ) 0.1 = ´ ´ ´ ´ - 0.6 5.67 10.73 ( ) 4 2 10 2 = 902 W 13. dQ dt e AT æ è ç ö ø ÷ = 1 4 s and dQ dt AT æ è ç ö ø ÷ = 2 4 s Þ e dQ dt dQ dt = = = ( / ) ( / ) 1 2 210 700 0.3 14. ( ) 80 50 5 80 50 2 20 - = + - æ è ç ö ø ÷ c c Þ K = 6 45 ; ( ) 60 30 6 45 - = t 60 30 2 20 + - æ è ç ö ø ÷ Þ t = 9 min ¢ Objective Questions (Level-1) 1. 3 35 10 0 20 KA KA ( ) ( ) - = - q q Þ 6 35 ( ) - = q q Þ q = ´ = ° 6 35 7 30 C \ Dq A = - = ° 35 30 5 C 2. T T S N N S = = = l l 350 510 0.69 According to Wien’s law 3. dQ dt dQ dt K A l K l æ è ç ö ø ÷ æ è ç ö ø ÷ = × = 2 1 1 4 4 2 2 D D q q / Þ dm dt dm dt æ è ç ö ø ÷ = æ è ç ö ø ÷ 2 1 2 = 0.2 g/s 4. dQ dt K a a a a K a a a a = - - × = - - × 4 0 2 2 4 100 3 2 3 2 p q p q ( ) ( ) Þ 2 6 100 q q = - ( ) Þ q = ´ = ° 6 8 100 75 C 5. K A T T d K A T T d 1 2 1 2 3 2 3 ( ) ( ) - = - Þ K T T K T T 1 2 1 2 3 2 1 3 ( ) ( ) - = - Þ K K 1 2 1 3 = Þ K K 1 2 1 3 : : = 6. dQ dt dQ dt K A l KA l æ è ç ö ø ÷ æ è ç ö ø ÷ = × × é ë ê ù û ú é ë ê ù û ú 2 1 2 2 2 D D q q = 2 Þ d Q d t d Q d t æ è ç ö ø ÷ = æ è ç ö ø ÷ = 2 1 2 8 cal/s 7. 67 | Calorimetry and Heat Tansfer H 100°C 0°C S 1/2 m 1/2 m 25 W 0°C dx q, q, + dq x P dQ dt K Ad dx K ax A d dx = = × = + q q 0 1 ( ) \ dx ax K A P d l 1 0 0 0 100 + = ò ò q 1 1 10 10 1 1 0 2 4 0 100 a ax l ln ( )| | + = ´ × = - q Þ ln ( ) ln 1 1 1 + - = al Þ ln ( ) ln 1 1 1 + - = al Þ ln ( ) 1 1 + = al or 1 1 + = al e or l a e e = - = - = 1 1 1 1 7 ( ) . m 8. l l 2 1 1 2 2 3 = = T T Þ l l 2 2 3 = m 9. Heat re quired to boil 1 g of ice is 180 cal while 1 g of steam can re lease 540 cal dur ing condenstion. So, temperture of the mix ture will be 100°C with 2/3 g steam and 4.3 g wa ter. 10. T T T 1 2 3 < < as temperature of a body de creases in rate of cool ing also de creases such that time in creases for equal temperature dif fer ence. 11. Con duc t ion is max i m um for which thermal re sis tance is min i m um, as R l r th µ 2 then for (a) 50 (b) 25 (c) 100 (d) 33.33, So option ‘b’ has minimum resistance. 12. Slope of temperature versus heat graph gives in crease of spe cific heat or heat ca pac ity and the por tion DE is the gas e ous state . 13. d Q m s d t = = maT dT 3 Þ Q m a T a a = = - = 4 4 16 1 15 4 4 1 2 | ( ) 14. Re sis tance be comes 1/4th in par al lel of that in se ries, so times taken will also be com e 1/4t h i e , 12/4 = 3 min. 15. ms ms 1 2 12 8 ´ = ´ Þ s s 1 2 2 3 : : = 16. KA T T l KA T T l c c ( ) ( ) - = - 2 2 Þ T T T T c c 2 2 2 + = + Þ 3 2 1 2 2 T T c = + Þ T T c = + 3 1 2 17. P = - = ( ) 1000 160 840 W W = ´ ´ 2 4200 50 t \ t = ´ = = 42 10 840 500 8 20 4 s s min 18. dQ dt KA T T x KA T T x = - = - ( ) ( ) 2 1 2 4 Þ T T T T 2 1 1 2 1 2 - = - Þ T T T 2 1 1 2 3 2 + = Þ T T T T T = + æ è ç ö ø ÷ = + 2 3 1 2 1 3 2 2 1 2 1 ( ) \ dQ dt KA x T T T = - + é ë ê ù û ú 2 2 1 1 3 2 ( ) = - - ´ KA x T T T [ ] 3 2 1 3 2 2 1 = - ´ KA x T T ( ) 2 1 1 3 Þ f = 1 3 19. Dq µ 1 K Þ D D q q A B B A K K = = 1 2 Þ D D q q A B = = ° 1 2 18 C ¢ More than One Correct Options 20. Amount of heat ra di ated or absorbed de pends upon. Sur face type, sur face area, sur face tem per a ture and tem p er a tu re of sur roun d ing, so (a) and (b) are correct. Calorimetry and Heat Tansfer | 68Read More
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2. What is the purpose of calorimetry in studying heat transfer? |
3. How does a calorimeter work in measuring heat transfer? |
4. What are the different methods of heat transfer studied in calorimetry? |
5. How can calorimetry be applied in real-world scenarios? |
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