PIPING MANTRA - _ SHELL & TUBE HEAT EXCHANGER PIPING LAYOUT _ PART - 3

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Kind: captions
Language: en

00:00:01.040
hi guys welcome to channel piping mantra
00:00:04.519 00:00:04.529 this is the continuation to part two I
00:00:06.950 00:00:06.960 will link part two of this video in
00:00:09.560 00:00:09.570 description box below n the link must
00:00:11.990 00:00:12.000 also be appearing in the solution box
00:00:13.999 00:00:14.009 I will link the part one of the same
00:00:15.650 00:00:15.660 video as well so please do watch those
00:00:18.050 00:00:18.060 as well so forth out further ado let's
00:00:20.689 00:00:20.699 get started on part three
00:00:22.160 00:00:22.170 after all the required information has
00:00:24.800 00:00:24.810 been collected for the piping design of
00:00:27.170 00:00:27.180 the heat exchanger the first step is to
00:00:29.359 00:00:29.369 outline clearance in working space in
00:00:31.400 00:00:31.410 front and around both ends of the
00:00:33.170 00:00:33.180 exchanger these working space should be
00:00:35.870 00:00:35.880 kept clear of any piping and accessories
00:00:38.959 00:00:38.969 to facilitate channel shall cover into
00:00:42.020 00:00:42.030 bundle removal as well as maintenance
00:00:44.150 00:00:44.160 and cleaning piping associated with heat
00:00:47.450 00:00:47.460 exchangers should be routed as per
00:00:49.819 00:00:49.829 general guidelines for layout you can
00:00:51.680 00:00:51.690 refer our video the link is appearing on
00:00:53.930 00:00:53.940 your screen moreover I'll link the video
00:00:56.270 00:00:56.280 in the description box below the free
00:00:58.400 00:00:58.410 space at the side of horizontal shell
00:01:00.410 00:01:00.420 can be used for placement of control
00:01:02.750 00:01:02.760 stations the piping is elevated from
00:01:05.690 00:01:05.700 great to have a clearance of 300 mm from
00:01:08.390 00:01:08.400 the grade level removable spools should
00:01:10.640 00:01:10.650 be provided on the lines connected with
00:01:13.100 00:01:13.110 the removable part of the exchangers for
00:01:15.260 00:01:15.270 ease of maintenance locally mounted
00:01:18.320 00:01:18.330 pressure and temperature indicators on
00:01:20.300 00:01:20.310 exchanger nozzles on the shelf for
00:01:23.060 00:01:23.070 channel lines should be visible from
00:01:25.010 00:01:25.020 grade or access platform the steam lines
00:01:28.010 00:01:28.020 connected to a header in the yard can be
00:01:30.380 00:01:30.390 arranged on either side of the exchanger
00:01:32.210 00:01:32.220 centerline without increasing the pipe
00:01:34.130 00:01:34.140 length pulling water lines if
00:01:39.109 00:01:39.119 underground should run right under the
00:01:41.240 00:01:41.250 lined up channel nozzles of all coolers
00:01:45.580 00:01:45.590 for stacked exchangers the nozzles
00:01:48.260 00:01:48.270 between the exchangers shall be
00:01:50.300 00:01:50.310 connected by exchanger vendor for other
00:01:52.700 00:01:52.710 nozzles connected with external piping
00:01:55.130 00:01:55.140 elbow nozzles can be proposed to reduce
00:01:56.990 00:01:57.000 the height of the stack some of the
00:01:59.899 00:01:59.909 typical piping arrangements are
00:02:01.539 00:02:01.549 horizontal reboilers and for vertical
00:02:05.719 00:02:05.729 tea boilers as you can see
00:02:07.610 00:02:07.620 nice crease now let's talk about support
00:02:15.770 00:02:15.780 location and the flexibility requirement
00:02:17.990 00:02:18.000 for heat exchangers general points
00:02:20.390 00:02:20.400 should be taken care of
00:02:22.010 00:02:22.020 while deciding the support rotation
00:02:23.720 00:02:23.730 angles play a large role in determining
00:02:25.880 00:02:25.890 the piping configuration for exchanges
00:02:28.220 00:02:28.230 it should be considered that in many
00:02:30.680 00:02:30.690 cases the location of anchors can be
00:02:33.170 00:02:33.180 adjusted to accommodate a better piping
00:02:35.240 00:02:35.250 design this is applicable to both pipe
00:02:37.610 00:02:37.620 anchors and exchange support anchors
00:02:39.830 00:02:39.840 stress group recommendations should be
00:02:41.870 00:02:41.880 followed to ensure minimum piping loads
00:02:44.360 00:02:44.370 on nozzles of heat exchangers allow the
00:02:47.660 00:02:47.670 muscle groups as well as standard margin
00:02:50.090 00:02:50.100 roads of equipments allowable nozzle
00:02:52.280 00:02:52.290 know it should be provided to mechanical
00:02:53.960 00:02:53.970 Department at inquiry in position stage
00:02:56.270 00:02:56.280 of air coolers piping supports on vendor
00:02:59.180 00:02:59.190 provided structure should be avoided if
00:03:01.370 00:03:01.380 any of the Clank specification mentions
00:03:04.430 00:03:04.440 for free flange displacement criteria
00:03:06.500 00:03:06.510 when supporting methodology shall be
00:03:08.930 00:03:08.940 finalized accordingly ignition stage of
00:03:11.630 00:03:11.640 project in setting vertical reboilers a
00:03:14.270 00:03:14.280 number of options for method of support
00:03:16.640 00:03:16.650 are possible as shown in the figure
00:03:18.140 00:03:18.150 below the best place for any given
00:03:20.690 00:03:20.700 application will depend on the process
00:03:23.240 00:03:23.250 requirement as well as the availability
00:03:24.830 00:03:24.840 of space type and weight of the
00:03:27.050 00:03:27.060 equipments being used and the
00:03:28.970 00:03:28.980 maintenance requirements for reboilers
00:03:32.690 00:03:32.700 generally pipe supports at Challen tube
00:03:35.550 00:03:35.560 exchanges can be incorporated with the
00:03:37.619 00:03:37.629 exchanger support foundation and can be
00:03:40.020 00:03:40.030 set up on the same foundation this can
00:03:42.600 00:03:42.610 save the expense of separate support
00:03:44.309 00:03:44.319 foundations anchors sat on such supports
00:03:48.059 00:03:48.069 allow the pipe to grow with the
00:03:49.710 00:03:49.720 exchanger instead of against it
00:03:51.420 00:03:51.430 however stress recommendations project
00:03:54.569 00:03:54.579 specification shall go on this criteria
00:03:57.589 00:03:57.599 flexibility requirement for high
00:03:59.699 00:03:59.709 temperature and high pressure lines as
00:04:02.490 00:04:02.500 shown in the page there can be two
00:04:04.199 00:04:04.209 arrangements possible to ensure
00:04:06.649 00:04:06.659 00:04:10.050 00:04:10.060 pressure and temperature lines first is
00:04:12.599 00:04:12.609 to provide loops in the piping layout as
00:04:14.729 00:04:14.739 shown in alternative a and other is to
00:04:17.370 00:04:17.380 provide spring support on the central
00:04:19.289 00:04:19.299 exchanger as shown on the alternative B
00:04:21.529 00:04:21.539 so that is it guys I hope you liked the
00:04:24.870 00:04:24.880 video if you did please hit the like
00:04:27.000 00:04:27.010 button for so more such useful content
00:04:29.370 00:04:29.380 please hit the subscribe button this
00:04:31.500 00:04:31.510 will keep us motivated and also will
00:04:33.779 00:04:33.789 notify you every time we post you thank
00:04:36.120 00:04:36.130 you so much please keep on watching bye
00:04:38.279 00:04:38.289 bye
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