How Plate Heat Exchanger Works

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Language: en

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00:00:04.630 00:00:04.640 hi welcome to 3d - knowledge comm today
00:00:08.629 00:00:08.639 we're going to be looking at heat
00:00:09.799 00:00:09.809 exchangers specifically the plate type
00:00:12.230 00:00:12.240 heat exchanger now heat exchangers have
00:00:14.959 00:00:14.969 a lot of applications you can see here
00:00:16.730 00:00:16.740 this one's a car radiator your cooling
00:00:18.920 00:00:18.930 down jacket water using air and this
00:00:21.290 00:00:21.300 prevents your engine from overheating
00:00:23.080 00:00:23.090 another good example here is a home
00:00:25.160 00:00:25.170 radiator and you'll be using a liquid
00:00:27.349 00:00:27.359 usually water to heat up air and keep
00:00:29.570 00:00:29.580 your home warm so these are both
00:00:32.420 00:00:32.430 different types of heat exchanger
00:00:34.450 00:00:34.460 but industrial world there's only two
00:00:36.889 00:00:36.899 types of heat exchanger a shell and tube
00:00:38.959 00:00:38.969 type and a plate type this is an image
00:00:43.250 00:00:43.260 of a plate type heat exchanger and we're
00:00:45.440 00:00:45.450 going to go now and have a look at the
00:00:46.580 00:00:46.590 model on the website and go through all
00:00:48.410 00:00:48.420 the parts and explain some of the
00:00:49.670 00:00:49.680 features
00:00:53.940 00:00:53.950 the design of the plate type heat
00:00:56.200 00:00:56.210 exchanger is actually rather simple the
00:00:58.570 00:00:58.580 heat exchanger consists of a series of
00:01:00.490 00:01:00.500 plates and these plates are stacked one
00:01:03.070 00:01:03.080 after the other between the plates
00:01:05.290 00:01:05.300 you'll have warm and cold fluids or at
00:01:07.780 00:01:07.790 least warmer and cooler fluids now
00:01:10.180 00:01:10.190 because the plates are relatively thin
00:01:11.980 00:01:11.990 and they have a large cross-sectional
00:01:13.600 00:01:13.610 area they have a very high heat transfer
00:01:15.640 00:01:15.650 rate and this heat will be transferred
00:01:18.010 00:01:18.020 through the plates
00:01:24.300 00:01:24.310 so I've gone to the website and I've
00:01:26.399 00:01:26.409 loaded the model and what we're going to
00:01:28.050 00:01:28.060 do now is talk through some of the main
00:01:29.430 00:01:29.440 components we zoom in here we can see
00:01:32.520 00:01:32.530 here this is an end plate the end plate
00:01:34.800 00:01:34.810 normally has four holes one two three
00:01:38.999 00:01:39.009 four and these will be Inlet and
00:01:41.490 00:01:41.500 discharge holes and the two others will
00:01:43.859 00:01:43.869 be for a cold fluid and Inlet and a
00:01:45.719 00:01:45.729 discharge you go further here we can see
00:01:48.690 00:01:48.700 a clamping bar
00:01:52.550 00:01:52.560 on the top view
00:01:54.300 00:01:54.310 Guide bar
00:01:56.350 00:01:56.360 further in we can see a black gasket is
00:01:58.660 00:01:58.670 such a man made of nitrile rubber
00:02:02.090 00:02:02.100 behind it we have a corrugated metal
00:02:04.610 00:02:04.620 plate and this is where the plate type
00:02:06.740 00:02:06.750 heat exchanger gets its name
00:02:09.430 00:02:09.440 further back we have more plates and
00:02:11.930 00:02:11.940 here this is a plate stack which is what
00:02:14.330 00:02:14.340 it looks like when all the plates are
00:02:15.590 00:02:15.600 pressed together
00:02:16.430 00:02:16.440 I have another end cover here which is
00:02:18.920 00:02:18.930 removable and as we can ascend all that
00:02:23.140 00:02:23.150 essentially everything will get pressed
00:02:25.670 00:02:25.680 together these clamping bars will screw
00:02:28.820 00:02:28.830 threads will go into the holes here on
00:02:31.430 00:02:31.440 the right-hand side and it'll all be
00:02:33.500 00:02:33.510 clamped together to a certain talk using
00:02:36.080 00:02:36.090 the torque wrench
00:02:37.250 00:02:37.260 so now let's have a look at how exactly
00:02:39.770 00:02:39.780 it works
00:02:45.510 00:02:45.520 here we can see the appearance of a
00:02:47.980 00:02:47.990 plate type heat exchanger when all the
00:02:49.690 00:02:49.700 plates are separated out now one of the
00:02:52.510 00:02:52.520 most interesting aspects of the plate
00:02:54.430 00:02:54.440 type heat exchanger is actually the
00:02:56.440 00:02:56.450 nitrile rubber gaskets that's these
00:02:59.320 00:02:59.330 black gaskets here that run around the
00:03:02.800 00:03:02.810 edges of the plate and the reason or
00:03:05.260 00:03:05.270 whether such a weird shape is because
00:03:07.450 00:03:07.460 they're directing flow in different
00:03:09.220 00:03:09.230 directions for each plate as we can see
00:03:13.240 00:03:13.250 here the gaskets they look similar they
00:03:15.100 00:03:15.110 each plate one after the other the
00:03:17.260 00:03:17.270 gaskets will be rotated 180 degrees and
00:03:19.960 00:03:19.970 this rotation changes the way the fluid
00:03:22.000 00:03:22.010 moves through the heat exchanger let's
00:03:26.050 00:03:26.060 imagine for a moment that the plate has
00:03:27.550 00:03:27.560 a fluid flowing through it and this
00:03:29.170 00:03:29.180 fluid is hot so it would be coming
00:03:31.540 00:03:31.550 through here and it would enter the
00:03:33.130 00:03:33.140 plate space now each of these plates are
00:03:35.440 00:03:35.450 pushed up tight against each other so
00:03:37.600 00:03:37.610 the fluid only ever be able to flow up
00:03:39.520 00:03:39.530 to the boundaries of the gasket and the
00:03:42.190 00:03:42.200 boundaries you can see here
00:03:45.420 00:03:45.430 and then once it's occupied the whole
00:03:47.880 00:03:47.890 space within the gasket area you will
00:03:52.649 00:03:52.659 exit through this hole here so we have
00:03:56.670 00:03:56.680 an inlet on the top for the hot fluid
00:03:58.229 00:03:58.239 and a discharge on the bottom now let's
00:04:01.289 00:04:01.299 imagine that we have a different flow
00:04:02.729 00:04:02.739 coming in and this time it's cold now
00:04:05.369 00:04:05.379 the cold fluid is going to come in here
00:04:07.229 00:04:07.239 and the same thing is going to occur
00:04:09.599 00:04:09.609 again it's going to flow out to the
00:04:11.099 00:04:11.109 edges of the gasket it's going to occupy
00:04:13.229 00:04:13.239 the whole area possible and then when
00:04:16.740 00:04:16.750 finished it's going to exit through this
00:04:20.819 00:04:20.829 hole here easily the discharge for the
00:04:23.640 00:04:23.650 cold fluid now you can notice that the
00:04:25.409 00:04:25.419 fluid in the bottom here the cold fluid
00:04:27.900 00:04:27.910 comes in the bottom and flows out the
00:04:29.339 00:04:29.349 top on the other plate the hot fluid
00:04:32.460 00:04:32.470 comes in at top and flows out of the
00:04:34.320 00:04:34.330 bottom this is known as contra flow or
00:04:36.510 00:04:36.520 counter flow it's the most efficient
00:04:38.580 00:04:38.590 means of heat transfer and that's why
00:04:40.620 00:04:40.630 most heat exchanges will have counter
00:04:42.870 00:04:42.880 flows or contra flows it raises the
00:04:45.480 00:04:45.490 efficiency of the heat exchanger now the
00:04:47.640 00:04:47.650 gaskets that are formed in the seal
00:04:49.200 00:04:49.210 these are not just ordinary gaskets they
00:04:51.810 00:04:51.820 manufacture from nitrile rubber they
00:04:54.089 00:04:54.099 have a very good coefficient of
00:04:55.620 00:04:55.630 elasticity that means they can be heated
00:04:57.839 00:04:57.849 up and cooled down without breaking this
00:05:00.060 00:05:00.070 is pretty useful if they're installed in
00:05:01.680 00:05:01.690 the heat exchanger they can also
00:05:03.210 00:05:03.220 withstand temperatures up to 100 degrees
00:05:05.100 00:05:05.110 this makes them suitable for a lot of
00:05:07.320 00:05:07.330 industrial applications
00:05:10.260 00:05:10.270 you may have noticed that the play isn't
00:05:12.579 00:05:12.589 flat it's actually corrugated the reason
00:05:15.219 00:05:15.229 for this is threefold the first reason
00:05:17.649 00:05:17.659 is that a corrugated plate gives it a
00:05:19.239 00:05:19.249 larger contact surface area and this
00:05:21.609 00:05:21.619 contact surface area increases the heat
00:05:23.619 00:05:23.629 transfer rate and makes the heat
00:05:24.999 00:05:25.009 exchange more efficient the second
00:05:26.889 00:05:26.899 reason is a corrugate your plate is
00:05:29.169 00:05:29.179 actually stiffer than a flat plate you
00:05:31.419 00:05:31.429 can manufacture a thinner plate and this
00:05:33.729 00:05:33.739 thinner plate as a higher heat transfer
00:05:35.109 00:05:35.119 rate than a thicker plate the third
00:05:37.540 00:05:37.550 reason is that the corrugated plate
00:05:39.609 00:05:39.619 creates turbulent flow the turbulent
00:05:43.899 00:05:43.909 flow prevents deposits forming on the
00:05:45.669 00:05:45.679 plate but it also has another function
00:05:47.999 00:05:48.009 it breaks down the boundary layer of
00:05:50.799 00:05:50.809 liquids that may form on a surface on
00:05:53.409 00:05:53.419 the left-hand side you can see linear
00:05:55.119 00:05:55.129 flow sometimes you'll get a boundary
00:05:57.399 00:05:57.409 layer of liquid on the heat exchanger
00:05:58.949 00:05:58.959 surface this inhibits heat transfer and
00:06:02.739 00:06:02.749 thus reduces the efficiency of the heat
00:06:04.869 00:06:04.879 exchanger on the right you can see we
00:06:07.600 00:06:07.610 have a turbulent flow this removes
00:06:09.909 00:06:09.919 deposits from the heat exchanger surface
00:06:11.829 00:06:11.839 and increases efficiency as no boundary
00:06:14.709 00:06:14.719 layer can form on the heat exchanger
00:06:16.029 00:06:16.039 surface the plates themselves can be
00:06:19.179 00:06:19.189 manufactured from a number of different
00:06:20.799 00:06:20.809 materials ranging from titanium to
00:06:23.589 00:06:23.599 different sorts of alloy as well as
00:06:25.239 00:06:25.249 plastics titanium would be chosen
00:06:28.359 00:06:28.369 whenever the environment is particularly
00:06:30.309 00:06:30.319 corrosive titanium has excellent
00:06:32.589 00:06:32.599 corrosion resistance characteristics but
00:06:35.139 00:06:35.149 unfortunate it's incredibly expensive
00:06:37.290 00:06:37.300 another disadvantage when using titanium
00:06:39.850 00:06:39.860 is there any metal connected to it will
00:06:42.189 00:06:42.199 normally act as an anode when two
00:06:44.379 00:06:44.389 dissimilar metals are connected together
00:06:45.999 00:06:46.009 one will be an anode and one will be a
00:06:47.709 00:06:47.719 cathode the anode will slowly wear away
00:06:50.139 00:06:50.149 due to galvanic action any metals
00:06:52.480 00:06:52.490 connected to titanium plates will need
00:06:54.759 00:06:54.769 to be protected and this can be achieved
00:06:56.769 00:06:56.779 by insulating the plate from the
00:06:58.209 00:06:58.219 dissimilar metal or by installing the
00:07:00.669 00:07:00.679 cathodic protection system other
00:07:02.549 00:07:02.559 chemical processes may not be able to
00:07:05.230 00:07:05.240 rely on metal alloys or titanium and in
00:07:08.619 00:07:08.629 these special instances the plate will
00:07:10.509 00:07:10.519 be constructed of plastic or a polymer
00:07:12.369 00:07:12.379 base material
00:07:18.320 00:07:18.330 the advantages with plate type heat
00:07:20.360 00:07:20.370 exchangers are that they are smaller and
00:07:22.219 00:07:22.229 lighter than to be exchanges they're
00:07:24.499 00:07:24.509 also more efficient when compared to 2p
00:07:26.749 00:07:26.759 exchanges of the same size they're easy
00:07:29.540 00:07:29.550 to dismantle and clean and they don't
00:07:31.610 00:07:31.620 need excess space dismantle tube type
00:07:34.909 00:07:34.919 heat exchangers do need a considerable
00:07:36.770 00:07:36.780 amount of spades in order that you can
00:07:38.629 00:07:38.639 clean them properly this is mainly
00:07:40.159 00:07:40.169 because you need to pull the tubes out
00:07:41.719 00:07:41.729 plate type heat exchangers don't have
00:07:43.909 00:07:43.919 this problem in addition to that the
00:07:46.879 00:07:46.889 turbulent flow in the plate type heat
00:07:48.830 00:07:48.840 exchanger helps keep the plate clean and
00:07:51.050 00:07:51.060 it also helps break down the boundary
00:07:53.450 00:07:53.460 layer of fluids that build up on the
00:07:55.189 00:07:55.199 plate surface in addition to that the
00:07:57.860 00:07:57.870 plates are relatively easy to replace
00:07:59.570 00:07:59.580 and you can actually increase or
00:08:01.580 00:08:01.590 decrease the heat transfer capacity of
00:08:03.680 00:08:03.690 the unit by adding or removing plates
00:08:06.640 00:08:06.650 the down size to plate up the exchanges
00:08:09.770 00:08:09.780 is simply that they're expensive or they
00:08:11.959 00:08:11.969 can be if using materials such as
00:08:14.180 00:08:14.190 titanium even nitrile rubber gaskets
00:08:16.999 00:08:17.009 themselves are quite expensive it's
00:08:19.159 00:08:19.169 difficult to find leaks because it's not
00:08:20.689 00:08:20.699 possible to pressurize each plate
00:08:22.399 00:08:22.409 individually normally you'll need to use
00:08:24.740 00:08:24.750 a non-destructive testing technique in
00:08:26.779 00:08:26.789 order to find a leak the nitrile rubber
00:08:29.540 00:08:29.550 gaskets themselves are also quite
00:08:32.389 00:08:32.399 difficult to replace they're adhered to
00:08:34.579 00:08:34.589 the plate and are quite difficult to
00:08:36.380 00:08:36.390 remove on land you could send the plate
00:08:38.899 00:08:38.909 away to a factory and they would use
00:08:40.579 00:08:40.589 liquid nitrogen to freeze the plate and
00:08:42.380 00:08:42.390 the gasket and then simply knock the
00:08:44.240 00:08:44.250 gasket off unfortunately if you're in
00:08:46.760 00:08:46.770 the middle of a desert or on a ship in
00:08:48.530 00:08:48.540 the Atlantic Ocean this is not really a
00:08:50.480 00:08:50.490 feasible option the only feasible option
00:08:52.699 00:08:52.709 is to carry spare place and replace the
00:08:54.710 00:08:54.720 plates in their entirety rather than
00:08:56.840 00:08:56.850 trying to exchange the gasket another
00:08:59.030 00:08:59.040 disadvantage is that if you're over
00:09:00.740 00:09:00.750 tighten the clamping bolts when
00:09:02.300 00:09:02.310 assembling will actually crush the
00:09:04.310 00:09:04.320 corrugated plates this can seriously
00:09:06.410 00:09:06.420 damage the plate and reduce the heat
00:09:08.329 00:09:08.339 transfer ray this reduction in heat
00:09:10.490 00:09:10.500 transfer rate also causes a reduction in
00:09:13.010 00:09:13.020 efficiency a solution to this is to use
00:09:15.259 00:09:15.269 a torque wrench when tightening the
00:09:16.639 00:09:16.649 clamping bolt in order that you don't
00:09:18.319 00:09:18.329 crush the plates if you get a chance to
00:09:21.079 00:09:21.089 go to the website load up the plate heat
00:09:23.269 00:09:23.279 exchanger model and then you can see it
00:09:25.850 00:09:25.860 being assembled and exploded you can
00:09:27.829 00:09:27.839 click on the annotations to find out a
00:09:30.019 00:09:30.029 bit more about what each component
00:09:32.110 00:09:32.120 does and then if you still need more
00:09:34.360 00:09:34.370 information go to the introduction page
00:09:36.730 00:09:36.740 and there there's some text and it will
00:09:38.860 00:09:38.870 tell you a bit more about the play type
00:09:40.960 00:09:40.970 heat exchanger so with the text the
00:09:43.420 00:09:43.430 model and the video you should really
00:09:45.130 00:09:45.140 has a firm grasp of what the plate type
00:09:47.500 00:09:47.510 heat exchanger does and how it does it
00:09:49.269 00:09:49.279 if you do like the video please do
00:09:51.340 00:09:51.350 subscribe it really helps us thank you
00:09:53.710 00:09:53.720 very much for your time
00:09:54.650 00:09:54.660
Office location
Engineering company LOTUS®
Russia, Ekaterinburg, Lunacharskogo street, 240/12

Phone: +7 343 216 77 75

E-mail: info@lotus1.ru

Sales phone

Russia: +7 343 216 77 75

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