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How Shell and Tube Heat Exchangers Work (Engineering)
WEBVTT Kind: captions Language: en
00:00:01.120 --> 00:00:03.260 - [Narrator] Hi, John here and welcome 00:00:03.260 --> 00:00:05.711 to another exciting and interesting video 00:00:05.711 --> 00:00:08.860 on engineering machinery. 00:00:08.860 --> 00:00:10.470 Now, in this video we're gonna be talking 00:00:10.470 --> 00:00:13.510 about the shell and tube heat exchanger. 00:00:13.510 --> 00:00:15.360 Some of you might think you know a lot about 00:00:15.360 --> 00:00:16.830 shell and tube heat exchanges 00:00:16.830 --> 00:00:17.663 and that's fine. 00:00:17.663 --> 00:00:18.930 Then you can watch this video 00:00:18.930 --> 00:00:21.690 and it will just reinforce what you already know. 00:00:21.690 --> 00:00:22.930 Some of you might not know anything 00:00:22.930 --> 00:00:24.368 about shell and tube heat exchanges 00:00:24.368 --> 00:00:25.710 and that's also fine 00:00:25.710 --> 00:00:28.330 because you're going to learn a lot in this video. 00:00:28.330 --> 00:00:30.160 We're gonna look at all of the main components 00:00:30.160 --> 00:00:32.670 that make up a shell and tube heat exchanger. 00:00:32.670 --> 00:00:35.350 I'm gonna show you some of its design features, 00:00:35.350 --> 00:00:37.991 its advantages and disadvantages 00:00:37.991 --> 00:00:41.480 and I'm also gonna show you how it works. 00:00:41.480 --> 00:00:43.400 So, let's get started. 00:00:43.400 --> 00:00:45.920 Now, this is not how a shell and tube heat exchanger 00:00:45.920 --> 00:00:48.350 normally looks in the workplace. 00:00:48.350 --> 00:00:50.930 If it was, it would be a lot easier to understand 00:00:50.930 --> 00:00:52.500 how it works. 00:00:52.500 --> 00:00:55.750 So, let's reset the configurator tool for a moment 00:00:55.750 --> 00:00:59.230 and now you can see the shell and tube heat exchanger 00:00:59.230 --> 00:01:02.800 as it would normally be in the workplace. 00:01:02.800 --> 00:01:04.700 There are different designs of variations 00:01:04.700 --> 00:01:07.682 but this one here is quite standard. 00:01:07.682 --> 00:01:10.800 So, let's start by looking at the outside 00:01:10.800 --> 00:01:12.820 of the heat exchanger. 00:01:12.820 --> 00:01:17.150 We've got the shell, it's a pressure vessel 00:01:17.150 --> 00:01:20.040 which means it's gonna be pressurized 00:01:20.040 --> 00:01:22.960 to match the fluid or the system pressure 00:01:22.960 --> 00:01:24.480 that's flowing through it 00:01:24.480 --> 00:01:27.620 or specifically flowing through the shell. 00:01:27.620 --> 00:01:31.343 Sometimes people refer to the shell also as the housing. 00:01:32.280 --> 00:01:37.280 We've also got a front and a rear of the heat exchanger. 00:01:37.307 --> 00:01:40.740 Other than that, we've got four main connections 00:01:40.740 --> 00:01:42.370 to the heat exchanger. 00:01:42.370 --> 00:01:47.130 One, two, three and four. 00:01:47.130 --> 00:01:50.150 We have two inlets and two outlets 00:01:50.150 --> 00:01:53.238 because we have two fluids that are flowing into 00:01:53.238 --> 00:01:56.500 and out of the heat exchanger. 00:01:56.500 --> 00:01:57.920 This heat exchanger is called 00:01:57.920 --> 00:02:01.240 a shell and tube heat exchanger 00:02:01.240 --> 00:02:03.160 because it has a shell 00:02:03.160 --> 00:02:05.843 and because within the shell there are some tubes. 00:02:06.760 --> 00:02:08.110 Let's take a cross-section. 00:02:10.180 --> 00:02:11.870 And we can now see exactly what's happening 00:02:11.870 --> 00:02:14.410 inside the heat exchanger. 00:02:14.410 --> 00:02:17.120 So, we have a tube side fluid. 00:02:17.120 --> 00:02:21.863 The tube side fluid enters here and is discharged here. 00:02:22.720 --> 00:02:24.670 We have a shell side fluid 00:02:24.670 --> 00:02:27.950 which enters here and goes a long here 00:02:27.950 --> 00:02:29.293 and it's discharged here. 00:02:30.990 --> 00:02:34.160 The reason we call the tube side fluid the tube side fluid 00:02:34.160 --> 00:02:37.240 is because it flows through tubes. 00:02:37.240 --> 00:02:39.600 See it comes into the heat exchanger 00:02:39.600 --> 00:02:41.110 and once it enters this area, 00:02:41.110 --> 00:02:43.450 it has to flow through these tubes 00:02:43.450 --> 00:02:45.793 because it's the only place it can go. 00:02:46.920 --> 00:02:48.830 Once it flows through the tubes, 00:02:48.830 --> 00:02:50.990 it's gonna get to the other end of the tubes. 00:02:50.990 --> 00:02:53.523 These tubes are just straight tubes. 00:02:54.400 --> 00:02:57.110 The fluid comes out on the lower section here 00:02:58.380 --> 00:03:01.320 and re-enters in the top section here. 00:03:02.870 --> 00:03:05.010 When the tube side fluid re-enters 00:03:05.010 --> 00:03:08.160 through the top section of these tubes here, 00:03:08.160 --> 00:03:10.650 it's gonna flow again in a straight line 00:03:10.650 --> 00:03:12.770 to the opposite end of the heat exchanger 00:03:12.770 --> 00:03:16.190 and it's gonna come out here 00:03:16.190 --> 00:03:19.923 and then gonna be discharged or exit the heat exchanger 00:03:19.923 --> 00:03:22.060 through the outlet. 00:03:22.060 --> 00:03:26.050 That is the flow path of the tube side fluid. 00:03:26.050 --> 00:03:30.440 The shell side fluid enters the heat exchanger here 00:03:30.440 --> 00:03:32.510 and then it comes through 00:03:32.510 --> 00:03:35.740 and it'll pass through a series of baffles 00:03:35.740 --> 00:03:37.650 which we'll take a look at in a moment. 00:03:37.650 --> 00:03:39.810 And it's gonna be discharged 00:03:39.810 --> 00:03:43.950 through the shell side fluid outlet down here. 00:03:43.950 --> 00:03:47.720 So, tube side fluid in on the lower left, along here, 00:03:47.720 --> 00:03:52.720 straight flow, up, back the other way and then out. 00:03:52.850 --> 00:03:56.244 Shell side fluid down through here, 00:03:56.244 --> 00:03:59.790 passed all the baffles and then out 00:03:59.790 --> 00:04:01.443 on the lower right-hand side. 00:04:02.820 --> 00:04:07.200 Although, I refer to fluids in this video, 00:04:07.200 --> 00:04:08.750 sometimes it's a little bit easier 00:04:08.750 --> 00:04:11.680 to think of them as flowing mediums. 00:04:11.680 --> 00:04:13.520 I say that because doctors say, 00:04:13.520 --> 00:04:15.060 you should drink a lot of fluids 00:04:15.060 --> 00:04:17.743 but realistically a fluid can also be a gas. 00:04:18.700 --> 00:04:20.960 Let's have a look at the tube side flowing medium 00:04:20.960 --> 00:04:22.523 in a bit more detail. 00:04:23.790 --> 00:04:24.770 What I'm actually gonna do, 00:04:24.770 --> 00:04:26.920 I'm gonna remove everything but the tubes 00:04:26.920 --> 00:04:28.933 so that we can focus on those first. 00:04:30.550 --> 00:04:33.880 So, here are our tubes. 00:04:33.880 --> 00:04:37.440 The tubes are collectively known as a tube stack 00:04:37.440 --> 00:04:40.130 or a tube bundle. 00:04:40.130 --> 00:04:43.290 For example, the upper half of the tube bundle 00:04:43.290 --> 00:04:47.590 would be all of the tubes above this row here 00:04:47.590 --> 00:04:49.140 and the lower half of the tube bundle 00:04:49.140 --> 00:04:51.953 would be all of the tubes below this row here. 00:04:52.860 --> 00:04:56.750 So, that is our tube bundle or tube stack. 00:04:56.750 --> 00:04:59.590 In order to hold the tube bundle 00:04:59.590 --> 00:05:01.570 in the correct position, 00:05:01.570 --> 00:05:06.570 we're gonna use baffles, tube sheets and also tie rods. 00:05:06.920 --> 00:05:09.393 Let's add the tube sheets first. 00:05:11.110 --> 00:05:12.787 These are our tube sheets the tube sheets. 00:05:12.787 --> 00:05:16.090 The tube sheets are used to first, 00:05:16.090 --> 00:05:18.320 hold the tubes in position 00:05:18.320 --> 00:05:23.020 and secondly, to seal the inside of the shell 00:05:23.020 --> 00:05:27.720 so that the shell side fluid stays within this space 00:05:27.720 --> 00:05:30.090 between the two tube sheets. 00:05:30.090 --> 00:05:31.650 So, here's one tube sheet, 00:05:31.650 --> 00:05:33.427 sometimes known as the real tube sheet. 00:05:33.427 --> 00:05:35.480 Here's the front tube sheet 00:05:35.480 --> 00:05:40.480 and the shell side fluid is gonna remain in this space. 00:05:41.260 --> 00:05:44.493 So, that's the pressure boundary for the shell side fluid. 00:05:45.760 --> 00:05:48.040 We wanna fix the tubes in position 00:05:48.040 --> 00:05:50.240 using more than just two anchor points. 00:05:50.240 --> 00:05:52.433 So, we use baffles as well. 00:05:54.260 --> 00:05:57.330 And the baffles just add some extra support 00:05:57.330 --> 00:06:00.570 to help keep the tubes in alignment. 00:06:00.570 --> 00:06:02.980 You'll also sometimes see tie rods. 00:06:02.980 --> 00:06:05.680 And the tie rods are used to connect the tube sheets 00:06:05.680 --> 00:06:07.490 or the baffles together 00:06:07.490 --> 00:06:10.143 which again adds structural support to the tubes. 00:06:11.330 --> 00:06:12.800 Within the tubes, 00:06:12.800 --> 00:06:14.130 what you're actually going to have 00:06:14.130 --> 00:06:18.030 are turbulators or tube inserts. 00:06:18.030 --> 00:06:19.610 You'll push the tube inserts 00:06:19.610 --> 00:06:22.970 into every one of these tube holes. 00:06:22.970 --> 00:06:25.470 So, for example we'd push a tube insert in here 00:06:25.470 --> 00:06:26.380 or a turbulator. 00:06:26.380 --> 00:06:31.380 And that turbulator is gonna create turbulent flow. 00:06:31.570 --> 00:06:34.120 This turbulent flow helps increase 00:06:34.120 --> 00:06:37.780 the heat transfer capacity of the heat exchanger 00:06:37.780 --> 00:06:42.780 and also it helps us keep the inside of the tubes clean. 00:06:42.920 --> 00:06:44.660 We reduce the likelihood of deposits 00:06:44.660 --> 00:06:46.610 building up on the inside of the tubes 00:06:46.610 --> 00:06:48.130 because we have turbulent flow 00:06:48.130 --> 00:06:49.633 rather than laminar flow. 00:06:50.750 --> 00:06:53.923 So, that's everything related to the tube side fluid. 00:06:55.010 --> 00:06:56.530 Let's load up some parts now. 00:06:56.530 --> 00:06:58.880 So, we can have a look at the shell side fluid. 00:07:00.176 --> 00:07:03.400 Now, we've already discussed the tubes 00:07:03.400 --> 00:07:05.223 so I think we can remove those. 00:07:07.210 --> 00:07:09.140 And we can see now 00:07:09.140 --> 00:07:11.160 with the shell side fluid. 00:07:11.160 --> 00:07:13.630 The shell side fluid is entering through here. 00:07:13.630 --> 00:07:16.130 It's going round the baffles 00:07:16.130 --> 00:07:18.303 and then it is being discharged here. 00:07:19.300 --> 00:07:21.670 We can see that around the tubes 00:07:21.670 --> 00:07:23.560 there is space for the fluid to flow 00:07:23.560 --> 00:07:27.080 because the tubes are not all directly next to each other. 00:07:27.080 --> 00:07:29.700 There's a bit of a gap, you can see here. 00:07:29.700 --> 00:07:32.630 If I come across, all of these gaps 00:07:32.630 --> 00:07:33.970 where my mouse is going now 00:07:33.970 --> 00:07:36.760 is where the shell side fluid is going to flow 00:07:36.760 --> 00:07:37.953 around the tubes. 00:07:39.103 --> 00:07:41.310 We wanna have turbulent flow, 00:07:41.310 --> 00:07:43.340 the same as what we had in the tubes. 00:07:43.340 --> 00:07:46.490 And in order to get that we use the baffles. 00:07:46.490 --> 00:07:48.610 So, the shell side fluid comes in here, 00:07:48.610 --> 00:07:52.410 flows around the tubes because of the baffles. 00:07:52.410 --> 00:07:56.905 It will exchange heat with the fluid within the tubes 00:07:56.905 --> 00:07:58.450 and then it's gonna drop out 00:07:58.450 --> 00:08:00.863 of the shell side fluid outlet here. 00:08:01.780 --> 00:08:04.560 Once again this turbulent flow increases 00:08:04.560 --> 00:08:07.010 00:08:07.010 --> 00:08:08.550 which makes it more efficient 00:08:08.550 --> 00:08:11.380 but also helps us prevent or reduce 00:08:11.380 --> 00:08:13.470 the likelihood of deposits building up 00:08:13.470 --> 00:08:16.113 on the outside of the tubes. 00:08:17.580 --> 00:08:20.180 Let's load up another 3D model, 00:08:20.180 --> 00:08:23.000 so I can show you a slightly different design 00:08:23.000 --> 00:08:24.823 of a shell and tube heat exchanger. 00:08:26.450 --> 00:08:27.940 So, here is the first design 00:08:27.940 --> 00:08:28.930 that I wanna show you. 00:08:28.930 --> 00:08:31.760 It's slightly different from what we looked at before. 00:08:31.760 --> 00:08:35.287 You can see that externally it looks pretty much the same 00:08:35.287 --> 00:08:37.327 but if I show you the tubes 00:08:37.327 --> 00:08:39.470 and we reverse that around. 00:08:39.470 --> 00:08:41.820 You can see that the tubes themselves 00:08:41.820 --> 00:08:45.520 are no longer just straight. 00:08:45.520 --> 00:08:48.513 They're actually rounded into a u-shape. 00:08:49.500 --> 00:08:50.333 This is actually called 00:08:50.333 --> 00:08:52.810 a u-type shell and tube heat exchanger 00:08:52.810 --> 00:08:55.940 or a u-tube shell and tube heat exchanger 00:08:55.940 --> 00:08:57.400 which is slightly confusing. 00:08:57.400 --> 00:08:59.410 But anyway, you can see that the tubes 00:08:59.410 --> 00:09:01.423 have this u-shape. 00:09:02.330 --> 00:09:03.910 Let's load up a more simple design 00:09:03.910 --> 00:09:05.230 cause I just want to explain to you 00:09:05.230 --> 00:09:08.803 what a one pass and a multi pass heat exchanger is. 00:09:09.810 --> 00:09:11.280 So, here we have a heat exchanger 00:09:11.280 --> 00:09:13.700 without a header or a bonnet. 00:09:13.700 --> 00:09:15.297 And if we take away the shell, 00:09:15.297 --> 00:09:16.563 in fact what we can do we can actually 00:09:16.563 --> 00:09:18.930 just take a cross-section. 00:09:18.930 --> 00:09:22.600 Can see that this time the tube side fluid 00:09:22.600 --> 00:09:27.490 comes in here, flows through the tubes 00:09:27.490 --> 00:09:30.633 and exits on this side here. 00:09:30.633 --> 00:09:33.700 So, in on the right out on the left. 00:09:33.700 --> 00:09:37.210 And what's interesting about this particular heat exchanger 00:09:37.210 --> 00:09:38.960 is that the tube side fluid 00:09:38.960 --> 00:09:43.900 represents a single pass 00:09:43.900 --> 00:09:46.160 You'll often hear people referring to heat exchangers 00:09:46.160 --> 00:09:49.410 as either single or multi pass. 00:09:49.410 --> 00:09:53.000 The shell side fluid has a multi pass design. 00:09:53.000 --> 00:09:57.600 It's passing multiple times over the tubes. 00:09:57.600 --> 00:10:00.970 The tube side fluid does not have a multi pass design 00:10:00.970 --> 00:10:04.160 because it's traveling directly through the tubes 00:10:04.160 --> 00:10:06.060 and then out. 00:10:06.060 --> 00:10:08.650 If the tube side fluid was to come in from the right, 00:10:08.650 --> 00:10:11.170 come out on the left and then go back around 00:10:11.170 --> 00:10:13.140 and then exit on the right, 00:10:13.140 --> 00:10:15.390 then this would be a multi pass design. 00:10:15.390 --> 00:10:17.220 Because it too, would be passing through 00:10:17.220 --> 00:10:19.853 the heat exchanger multiple times. 00:10:20.740 --> 00:10:23.220 This heat exchanger would be described as a 00:10:23.220 --> 00:10:24.900 multi pass heat exchanger 00:10:24.900 --> 00:10:26.850 just because the shell side fluid 00:10:26.850 --> 00:10:29.400 or one of the fluids is passing multiple times 00:10:29.400 --> 00:10:30.821 over the other fluid. 00:10:30.821 --> 00:10:33.910 If the shell side fluid came in from the top 00:10:33.910 --> 00:10:37.410 and dropped out at the bottom with no baffles, 00:10:37.410 --> 00:10:38.530 then the shell side fluid 00:10:38.530 --> 00:10:40.560 would have a single pass design 00:10:40.560 --> 00:10:42.290 and so with the tube side fluid. 00:10:42.290 --> 00:10:46.440 And we would say, this is a single pass heat exchanger. 00:10:46.440 --> 00:10:47.830 That's actually quite rare though. 00:10:47.830 --> 00:10:49.220 You don't see that very often 00:10:49.220 --> 00:10:51.670 because it's not very efficient. 00:10:51.670 --> 00:10:53.750 If you have a look at steam condenses though, 00:10:53.750 --> 00:10:56.189 you will see that design. 00:10:56.189 --> 00:10:59.830 And generally, whenever you convert a vapor into a liquid 00:10:59.830 --> 00:11:03.240 or whenever you're changing the state of something, 00:11:03.240 --> 00:11:06.650 you'll often use a single pass design. 00:11:06.650 --> 00:11:09.680 People also talk about counter flow, cross flow 00:11:09.680 --> 00:11:11.340 and parallel flow. 00:11:11.340 --> 00:11:14.450 This particular design is a counter flow design 00:11:14.450 --> 00:11:17.210 because the tube side fluid enters on the right 00:11:17.210 --> 00:11:18.650 and exits on the left. 00:11:18.650 --> 00:11:20.947 And the shell side fluid enters on the left 00:11:20.947 --> 00:11:24.380 and is discharged on the right. 00:11:24.380 --> 00:11:28.260 So, they're flowing in opposite directions to one another, 00:11:28.260 --> 00:11:30.712 right to left and left to right. 00:11:30.712 --> 00:11:33.170 That is a counter flow design. 00:11:33.170 --> 00:11:36.890 It is the most efficient type of flow design 00:11:36.890 --> 00:11:39.630 you can have for a heat exchanger. 00:11:39.630 --> 00:11:42.020 came in on the right 00:11:42.020 --> 00:11:44.204 and exited on the left 00:11:44.204 --> 00:11:46.860 then we'd have a parallel flow design 00:11:46.860 --> 00:11:48.520 because both the tube side fluid 00:11:48.520 --> 00:11:50.010 and the shell side fluid 00:11:50.010 --> 00:11:53.015 are flowing from right to left. 00:11:53.015 --> 00:11:55.550 If the shell side fluid came in at the top 00:11:55.550 --> 00:11:57.610 and which discharged straight out of the bottom 00:11:57.610 --> 00:11:59.660 this would be a cross flow design 00:11:59.660 --> 00:12:02.980 because the fluids are flowing at a 90 degree angle 00:12:02.980 --> 00:12:04.413 relative to each other. 00:12:06.670 --> 00:12:08.340 So, different flow designs depend on 00:12:08.340 --> 00:12:10.993 what you wanna use the heat exchanger for. 00:12:12.070 --> 00:12:12.903 Let's have a talk now 00:12:12.903 --> 00:12:15.120 about some of the advantages and disadvantages 00:12:15.120 --> 00:12:17.873 associated with this type of heat exchanger. 00:12:20.050 --> 00:12:22.480 When we talk about 00:12:22.480 --> 00:12:25.340 associated with the shell and tube heat exchanger, 00:12:25.340 --> 00:12:28.570 we're often comparing it to the plate heat exchanger 00:12:28.570 --> 00:12:30.420 because in the industrial world 00:12:30.420 --> 00:12:32.640 we're either using plate heat exchangers 00:12:32.640 --> 00:12:34.780 or shell and tube heat exchangers. 00:12:34.780 --> 00:12:37.010 Normally, there are some other designs 00:12:37.010 --> 00:12:39.150 but those two are the most dominant 00:12:39.150 --> 00:12:42.080 within the industrial engineering world. 00:12:42.080 --> 00:12:46.000 Now, shell and tube heat exchangers are relatively cheap. 00:12:46.000 --> 00:12:47.310 They have a simple design 00:12:47.310 --> 00:12:49.800 and they're quite easy to maintain. 00:12:49.800 --> 00:12:52.930 They're also suitable for higher pressures and temperatures 00:12:52.930 --> 00:12:55.550 compared to plate heat exchangers. 00:12:55.550 --> 00:12:58.880 The pressure drop across 00:12:58.880 --> 00:13:02.710 is less than that of a plate heat exchanger. 00:13:02.710 --> 00:13:06.750 It's also easy to find and isolate leaks in the tubes 00:13:06.750 --> 00:13:09.130 compared to trying to find and isolated leak 00:13:09.130 --> 00:13:11.160 in a plate heat exchanger. 00:13:11.160 --> 00:13:13.067 Shell and tube heat exchangers also don't foul 00:13:13.067 --> 00:13:15.790 as easily as plate heat exchangers 00:13:15.790 --> 00:13:18.200 because they don't have the very fine clearances 00:13:18.200 --> 00:13:19.893 that a plate heat exchanger has. 00:13:21.230 --> 00:13:23.710 There are however some disadvantages. 00:13:23.710 --> 00:13:26.980 They're less efficient than plate heat exchangers. 00:13:26.980 --> 00:13:29.020 They also require more space to open 00:13:29.020 --> 00:13:31.110 and remove the tubes. 00:13:31.110 --> 00:13:33.620 And you can't increase the cooling capacity 00:13:33.620 --> 00:13:35.910 00:13:35.910 --> 00:13:37.310 With the plate heat exchanger, 00:13:37.310 --> 00:13:40.190 you can simply add more plates or remove plates 00:13:40.190 --> 00:13:42.500 in order to vary the cooling capacity. 00:13:42.500 --> 00:13:44.520 With the shell and tube type heat exchanger, 00:13:44.520 --> 00:13:45.823 this is not possible. 00:13:47.180 --> 00:13:50.040 If you wanna learn more about shell and tube heat exchangers 00:13:50.040 --> 00:13:52.090 then I suggest you go to the website. 00:13:52.090 --> 00:13:54.363 I'll put the link in the video description area 00:13:54.363 --> 00:13:57.920 and you can read through one of our articles 00:13:57.920 --> 00:13:59.540 which will tell you a little bit about 00:13:59.540 --> 00:14:01.360 00:14:01.360 --> 00:14:03.060 and discuss more of the topics 00:14:03.060 --> 00:14:04.923 that we've covered in this video. 00:14:05.890 --> 00:14:08.060 If you still wanna learn even more 00:14:08.060 --> 00:14:10.100 about heat exchangers after that, 00:14:10.100 --> 00:14:13.630 then you can check some of our other associated articles 00:14:13.630 --> 00:14:16.026 within our 3D encyclopedia. 00:14:16.026 --> 00:14:18.910 You can see here we have an associated article 00:14:18.910 --> 00:14:21.390 for a plate heat exchanger. 00:14:21.390 --> 00:14:25.750 If you want to access some free interactive 3D models, 00:14:25.750 --> 00:14:27.160 then go to the website 00:14:27.160 --> 00:14:31.690 and select any model from the 3D models menu 00:14:31.690 --> 00:14:33.223 those highlighted green. 00:14:34.190 --> 00:14:35.860 And if you wanna take your engineering knowledge 00:14:35.860 --> 00:14:36.900 to the next level, 00:14:36.900 --> 00:14:39.950 then check out some of that online video courses. 00:14:39.950 --> 00:14:44.490 We have over 30 hours of video courses, currently online. 00:14:44.490 --> 00:14:47.430 And they cover everything from valves to diesel engines 00:14:47.430 --> 00:14:49.640 to pumps to heat exchangers. 00:14:49.640 --> 00:14:53.240 I've pasted a discount coupon in the video description area 00:14:53.240 --> 00:14:55.370 so if you do decide to purchase any courses, 00:14:55.370 --> 00:14:58.320 then be sure to use that discount coupon. 00:14:58.320 --> 00:15:00.550 If you like this video then please do share it 00:15:00.550 --> 00:15:01.582 or like it on social media. 00:15:01.582 --> 00:15:04.789 It really does help us out and we really appreciate it. 00:15:04.789 --> 00:15:08.123 And don't forget to subscribe to our You Tube channel. 00:15:08.970 --> 00:15:10.670 Thank you very much for your time.
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