Heat Exchangers Example

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Language: en

00:00:00.030
so let's do this example 100 liter of
00:00:03.379 00:00:03.389 water per minute is to be cooled down
00:00:05.480 00:00:05.490 from 90 to 65 degrees Celsius using cold
00:00:09.320 00:00:09.330 water flux with an inner temperature of
00:00:11.720 00:00:11.730 20 degrees with an heat exchanger with
00:00:14.570 00:00:14.580 the area of 4 square meters and our task
00:00:17.810 00:00:17.820 is to calculate the cold water flux
00:00:19.310 00:00:19.320 needed if a counter current setup is
00:00:21.800 00:00:21.810 chosen and the K value has been
00:00:25.189 00:00:25.199 estimated to 1 kilo watt per square
00:00:27.589 00:00:27.599 meter in Kelvin we also get some numbers
00:00:30.019 00:00:30.029 here you could look this up in a
00:00:32.720 00:00:32.730 handbook so on the hot side we have 970
00:00:37.490 00:00:37.500 1 kilogram per cubic meter and 4190 1
00:00:40.639 00:00:40.649 euro per kilogram Kelvin as the heat
00:00:43.250 00:00:43.260 capacity and on the cold side well we
00:00:47.029 00:00:47.039 actually don't know the temperature so
00:00:49.700 00:00:49.710 you can't look that up but let's assume
00:00:53.360 00:00:53.370 that is 996 kilogram per cubic meter
00:00:56.810 00:00:56.820 density and 4175 as the heat capacity so
00:01:01.400 00:01:01.410 what you would need to do if you do it
00:01:03.200 00:01:03.210 is really really carefully is that you
00:01:05.420 00:01:05.430 assume something as you see I'm a
00:01:07.910 00:01:07.920 temperature range and then you look up
00:01:09.500 00:01:09.510 the density and the heat capacity for
00:01:11.870 00:01:11.880 that range and then you do your
00:01:14.480 00:01:14.490 calculation and see does my result is
00:01:18.070 00:01:18.080 that in coherent with the Assumption I
00:01:22.550 00:01:22.560 did okay so we make energy balances so
00:01:28.609 00:01:28.619 the energy that is being transferred and
00:01:32.060 00:01:32.070 taken up respectively is the mass flux
00:01:34.340 00:01:34.350 times the heat capacity times the
00:01:35.960 00:01:35.970 temperature change in the respective
00:01:38.120 00:01:38.130 flows and that must also be the same as
00:01:41.359 00:01:41.369 the temperature that goes this sorry the
00:01:43.490 00:01:43.500 heat flux that goes through the surface
00:01:45.980 00:01:45.990 so K times a times the logarithmic mean
00:01:48.319 00:01:48.329 temperature and not it's the logarithmic
00:01:51.139 00:01:51.149 mean temperature because we have no
00:01:54.109 00:01:54.119 phase changes so we have a nice study
00:01:56.889 00:01:56.899 increase and decrease respectively of
00:02:00.350 00:02:00.360 the temperature of the two mediums so
00:02:04.999 00:02:05.009 with the numbers we have we can see that
00:02:07.730 00:02:07.740 the hot medium is 100
00:02:10.300 00:02:10.310 a minute so that zero point one cubic
00:02:13.420 00:02:13.430 meter per minute times the density
00:02:15.400 00:02:15.410 divided by sixty translated to kilograms
00:02:18.309 00:02:18.319 per second and you have the change in
00:02:23.530 00:02:23.540 temperature for the hot flow is 90 minus
00:02:27.130 00:02:27.140 sixty five does twenty-five degrees
00:02:29.199 00:02:29.209 and from that you can calculate the
00:02:31.990 00:02:32.000 energy transferred so that's
00:02:34.240 00:02:34.250 approximately 170 kilo watts so
00:02:37.930 00:02:37.940 kilowatts per second when you do these
00:02:40.780 00:02:40.790 calculations I recommend you to check
00:02:42.789 00:02:42.799 the caf the unit's carefully because
00:02:46.000 00:02:46.010 it's easy to do mistakes now we know
00:02:49.750 00:02:49.760 everything now in the lost energy
00:02:54.460 00:02:54.470 balance there Q equals K times a times
00:02:56.890 00:02:56.900 Delta TL except the logarithmic mean
00:02:59.589 00:02:59.599 temperature so we can calculate the
00:03:01.240 00:03:01.250 logarithmic mean temperature as to Q
00:03:03.729 00:03:03.739 divided by the overall heat transfer
00:03:04.930 00:03:04.940 coefficient and area and we get that
00:03:08.620 00:03:08.630 forty two point 39 and we know the
00:03:12.190 00:03:12.200 formula for the log rating me
00:03:13.900 00:03:13.910 temperature delta T 2 minus delta T 1
00:03:16.420 00:03:16.430 divided by natural log of delta T 2
00:03:19.090 00:03:19.100 minus natural logarithm delta T 1 and
00:03:22.530 00:03:22.540 from that we get well first you have to
00:03:25.930 00:03:25.940 realize that delta T 2 and that's 65
00:03:29.800 00:03:29.810 minus 20 here it's it's important to
00:03:32.710 00:03:32.720 realize it's a counter current setup so
00:03:35.890 00:03:35.900 the coldest inflow and the coldest cold
00:03:39.729 00:03:39.739 medium in flow should meet the coldest
00:03:42.780 00:03:42.790 hot medium outflow so 65 minus 20 that's
00:03:48.250 00:03:48.260 45 degrees on one side and then you can
00:03:50.650 00:03:50.660 calculate the temperature difference on
00:03:52.720 00:03:52.730 the other side and that becomes thirty
00:03:54.699 00:03:54.709 nine point nine degrees Celsius we keep
00:03:56.949 00:03:56.959 some extra data here just in case so we
00:04:01.509 00:04:01.519 don't run into numerical problems and
00:04:05.580 00:04:05.590 delta T one so that the temperature
00:04:08.800 00:04:08.810 difference between the two flows on the
00:04:10.599 00:04:10.609 other side that's 90 for the hot flow
00:04:13.750 00:04:13.760 and the cold out we don't know so we
00:04:15.970 00:04:15.980 calculate that here delta T one was
00:04:18.820 00:04:18.830 thirty nine point nine so we get ninety
00:04:21.099 00:04:21.109 minus that nine point
00:04:22.069 00:04:22.079 and that's fifty point one degrees
00:04:24.379 00:04:24.389 Celsius so now we know the temperature
00:04:28.059 00:04:28.069 so we can calculate the the mass flux
00:04:33.140 00:04:33.150 now because now we also know how much
00:04:36.020 00:04:36.030 the temperature increased for the cold
00:04:37.909 00:04:37.919 medium so that's fifty point one minus
00:04:40.879 00:04:40.889 the inflow temperature that's twenty
00:04:42.920 00:04:42.930 that's thirty point one degrees Celsius
00:04:45.260 00:04:45.270 and let's check that things look right
00:04:49.399 00:04:49.409 here if you take the heat capacity of
00:04:53.540 00:04:53.550 the code medium times the temperature
00:04:56.360 00:04:56.370 change in that medium that's larger than
00:05:00.439 00:05:00.449 the heat capacity of the hot medium
00:05:02.480 00:05:02.490 times the temperature difference of the
00:05:04.399 00:05:04.409 hot medium and that should result in
00:05:07.040 00:05:07.050 mass flux W two that's less than W one
00:05:13.390 00:05:13.400 so let's put in the numbers there so W -
00:05:17.869 00:05:17.879 that must be Q divided by heat capacity
00:05:22.010 00:05:22.020 and the temperature change and we get
00:05:24.709 00:05:24.719 that as one point thirty five kilograms
00:05:27.830 00:05:27.840 per second which is less than one point
00:05:29.839 00:05:29.849 sixty two so it seems to be in good
00:05:32.600 00:05:32.610 order and if we want to we can
00:05:34.189 00:05:34.199 recalculate that as liters per minute so
00:05:37.249 00:05:37.259 one point thirty five kilograms per
00:05:38.899 00:05:38.909 second times sixty seconds divided by
00:05:42.409 00:05:42.419 the density and you get zero point zero
00:05:44.839 00:05:44.849 eighty one cubic meter per minute or
00:05:46.909 00:05:46.919 eighty one liter per minute okay when
00:05:53.480 00:05:53.490 you calculate heat exchangers the thing
00:05:58.129 00:05:58.139 is that you need to know how much heat
00:06:00.200 00:06:00.210 needs to be transferred what the for
00:06:02.180 00:06:02.190 temperature should be and what the flow
00:06:04.459 00:06:04.469 rate should be and the flow rate tells
00:06:10.369 00:06:10.379 you the overall heat transfer
00:06:11.540 00:06:11.550 coefficient and then you can calculate
00:06:13.670 00:06:13.680 the area needed and once you have
00:06:17.089 00:06:17.099 calculated area needed well then you
00:06:19.730 00:06:19.740 have to think if you want to do this all
00:06:22.790 00:06:22.800 the way okay if I know how big the area
00:06:26.540 00:06:26.550 should be how big should then the heat
00:06:29.749 00:06:29.759 exchanger be and that might influence
00:06:35.199 00:06:35.209 the transaction area which in turn will
00:06:40.219 00:06:40.229 influence the flow rate now the problem
00:06:44.420 00:06:44.430 is you you have to do it right in here
00:06:48.260 00:06:48.270 you have to guess a flow rate or you
00:06:51.139 00:06:51.149 just set a flow rate you would like to
00:06:53.360 00:06:53.370 have and then you do the calculations
00:06:55.279 00:06:55.289 and then you do this assign whatever you
00:06:57.499 00:06:57.509 do plate it a change here or whatever
00:07:00.260 00:07:00.270 and then when you've done all the design
00:07:04.189 00:07:04.199 choices you can calculate the flow rate
00:07:08.059 00:07:08.069 and if the flow rate is different than
00:07:11.570 00:07:11.580 the one you used before
00:07:12.709 00:07:12.719 then you need to redo your calculations
00:07:14.629 00:07:14.639 and continue and continue until it all
00:07:17.120 00:07:17.130 fits if you have boiling well it all
00:07:27.079 00:07:27.089 depends on how difficult equations are
00:07:29.659 00:07:29.669 used we will use the natural convection
00:07:31.309 00:07:31.319 boiling and then the first question we
00:07:34.370 00:07:34.380 need to ask yourself is how much heat is
00:07:36.980 00:07:36.990 need to be transferred and that is one
00:07:42.499 00:07:42.509 thing and then it's the second thing is
00:07:44.329 00:07:44.339 okay so how many watts per square meter
00:07:46.370 00:07:46.380 will that be but not we're going to try
00:07:50.629 00:07:50.639 to calculate the heat exchanger area and
00:07:52.760 00:07:52.770 we need to know how much energy is being
00:07:55.189 00:07:55.199 transferred per square meter hmm so
00:08:00.050 00:08:00.060 guess something you guess how many watts
00:08:03.170 00:08:03.180 per square meter you need to transfer
00:08:05.990 00:08:06.000 and then you calculate the heat transfer
00:08:09.230 00:08:09.240 coefficients using these equations and
00:08:11.449 00:08:11.459 then you calculate the overall heat
00:08:13.670 00:08:13.680 transfer coefficient and then you
00:08:15.170 00:08:15.180 calculate area needed and then you
00:08:18.680 00:08:18.690 calculate how many watts per square
00:08:19.909 00:08:19.919 meter
00:08:20.480 00:08:20.490 will that be and if you're lucky that is
00:08:23.779 00:08:23.789 the same number as you guessed before
00:08:25.309 00:08:25.319 and if you're unlucky just repeat and
00:08:28.279 00:08:28.289 repeat and repeat until you find a
00:08:31.070 00:08:31.080 solution
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