Webinar - Industrial Boiler Water Treatment and Chemistry - An Introduction

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Language: en

00:00:00.290
so welcome everybody to the webinar
00:00:03.980 00:00:03.990 today we've got a special guest with us
00:00:07.070 00:00:07.080 today David Addison from thermal
00:00:09.830 00:00:09.840 chemistry limited who's a local guy here
00:00:14.450 00:00:14.460 from the Waikato but travels the world
00:00:16.760 00:00:16.770 these days looking at all sorts of
00:00:18.980 00:00:18.990 things and in particular specialists in
00:00:20.810 00:00:20.820 industrial boiler water treatment in
00:00:23.779 00:00:23.789 chemistry and so we're privileged having
00:00:27.170 00:00:27.180 with us today to talk about some fairly
00:00:29.300 00:00:29.310 unique and and very important topics in
00:00:33.229 00:00:33.239 regards to not just the performance and
00:00:36.170 00:00:36.180 efficiency you boiler plant but also in
00:00:37.880 00:00:37.890 terms of its reliability and and
00:00:39.770 00:00:39.780 longevity so on that note I'll hand the
00:00:43.549 00:00:43.559 time over to David and just a reminder
00:00:45.200 00:00:45.210 for any of you that have questions
00:00:46.970 00:00:46.980 through the day today's webinar you feel
00:00:49.790 00:00:49.800 free to use the question portal and
00:00:51.709 00:00:51.719 we'll hopefully address them either
00:00:54.290 00:00:54.300 either at the end of the webinar or as
00:00:56.360 00:00:56.370 we go through if it's appropriate so on
00:00:58.729 00:00:58.739 that note welcome David great to have
00:01:00.830 00:01:00.840 you here and we'll we'll let you get
00:01:02.119 00:01:02.129 underway cool all right thanks James all
00:01:06.350 00:01:06.360 right so what we got here is a dusty old
00:01:09.320 00:01:09.330 boiler water treatment in chemistry and
00:01:11.450 00:01:11.460 it's a very brief introduction my
00:01:14.600 00:01:14.610 background is primarily in large fossil
00:01:16.550 00:01:16.560 plants I turned up at the Huntley power
00:01:19.999 00:01:20.009 station as a recent graduate speaking to
00:01:22.670 00:01:22.680 be there for a summer job and quite a
00:01:24.499 00:01:24.509 few years ago and took me about 11 years
00:01:26.810 00:01:26.820 to escape so I've been kicking around
00:01:28.580 00:01:28.590 boilers for quite a while but you know
00:01:30.530 00:01:30.540 what with cogent plants smaller
00:01:32.810 00:01:32.820 industrial boilers all the way from
00:01:34.490 00:01:34.500 little wee ones at what we call
00:01:37.100 00:01:37.110 supercritical units for large-scale
00:01:39.109 00:01:39.119 fossil plants so this is going to be let
00:01:45.139 00:01:45.149 me just get this thing to work all right
00:01:46.880 00:01:46.890 so what we're going to run through is
00:01:48.020 00:01:48.030 with a bit of an introduction over the
00:01:49.580 00:01:49.590 water cycle chemistry talk about water
00:01:51.770 00:01:51.780 tube and fire tube boilers which are the
00:01:54.740 00:01:54.750 most common industrial types a little
00:01:56.780 00:01:56.790 bit on what is corrosion what is
00:01:58.039 00:01:58.049 deposition chemistry guidelines there's
00:02:00.859 00:02:00.869 a number of guidelines that you can
00:02:02.840 00:02:02.850 operate clients to landis always
00:02:04.639 00:02:04.649 recommended that you run to a guideline
00:02:06.230 00:02:06.240 a little bit of our ayats which is the
00:02:08.540 00:02:08.550 International Association for the
00:02:09.949 00:02:09.959 properties water and steam which is a
00:02:11.479 00:02:11.489 free resource for cycle chemist
00:02:14.210 00:02:14.220 information and then we'll run through
00:02:16.220 00:02:16.230 each of the key aspects of industrial
00:02:17.840 00:02:17.850 boilers control just briefly touch on
00:02:20.690 00:02:20.700 each of those and then summary this is a
00:02:23.500 00:02:23.510 very brief introduction to the subject
00:02:25.880 00:02:25.890 and it is very complex and multifaceted
00:02:28.750 00:02:28.760 every plant is unique to some degree and
00:02:32.630 00:02:32.640 in every plants chemistry program is
00:02:34.760 00:02:34.770 customizable to a degree it might be
00:02:36.560 00:02:36.570 that you run all the time it might be
00:02:38.090 00:02:38.100 that you run once a week it might be
00:02:40.880 00:02:40.890 that you have to produce steam that has
00:02:42.980 00:02:42.990 a certain chemistry because you're
00:02:45.920 00:02:45.930 contacting food or you're going through
00:02:47.930 00:02:47.940 a certain type of turbine and there's a
00:02:50.540 00:02:50.550 variety advice out there available in an
00:02:52.760 00:02:52.770 industry and not all of it is correct
00:02:55.490 00:02:55.500 was a correct as it should be there's a
00:02:57.020 00:02:57.030 lot of people selling various chemical
00:02:58.940 00:02:58.950 treatments for industrial boilers and
00:03:00.830 00:03:00.840 power boilers as well if you you know
00:03:04.760 00:03:04.770 think about it you you may have a vested
00:03:06.890 00:03:06.900 interest and promoting a certain type of
00:03:08.840 00:03:08.850 chemistry if you're going to make a
00:03:10.070 00:03:10.080 bunch of money at someone buying a
00:03:11.600 00:03:11.610 certain product the work that I do I'm a
00:03:14.750 00:03:14.760 pure consultant we don't sell anything
00:03:16.970 00:03:16.980 don't sell any hardware don't sell any
00:03:18.410 00:03:18.420 chemicals so we try to offer on
00:03:20.750 00:03:20.760 impartial advice solve problems for
00:03:24.199 00:03:24.209 people the other thing is this is only
00:03:26.060 00:03:26.070 an hour through the reading will be
00:03:27.949 00:03:27.959 required for deep understanding and
00:03:29.720 00:03:29.730 we're not really going to go into any
00:03:31.759 00:03:31.769 great detail around corrosion mechanisms
00:03:33.830 00:03:33.840 and what we intend to do is do a
00:03:35.120 00:03:35.130 following webinar some point in the next
00:03:38.210 00:03:38.220 few months where what we do is we'll go
00:03:39.890 00:03:39.900 through sort of the key corrosion
00:03:42.229 00:03:42.239 failure type problems that can occur in
00:03:44.330 00:03:44.340 industrial plants and talk about what
00:03:46.280 00:03:46.290 they are how to identify them what the
00:03:48.590 00:03:48.600 mechanism is and what the root causes so
00:03:51.110 00:03:51.120 they perhaps in your own plants you can
00:03:53.060 00:03:53.070 maybe take some preemptive steps to stop
00:03:55.160 00:03:55.170 those types of problems from happening
00:03:56.800 00:03:56.810 so first up what a cycle chemistry it's
00:03:59.990 00:04:00.000 the chemical treatment of water and
00:04:01.880 00:04:01.890 steam within a boil or steam raising
00:04:03.740 00:04:03.750 plant and it encompasses the water
00:04:06.650 00:04:06.660 treatment the makeup water you've got to
00:04:08.509 00:04:08.519 put water into the boiler somehow so you
00:04:11.180 00:04:11.190 got to do normally do some kind of
00:04:12.500 00:04:12.510 treatment through that it's the chemical
00:04:14.960 00:04:14.970 treatment of feed water and the boiler
00:04:16.640 00:04:16.650 water and these two things are normally
00:04:18.590 00:04:18.600 addressed separately and then also
00:04:20.210 00:04:20.220 sampling and analysis for control you
00:04:23.060 00:04:23.070 know you you can't control what you
00:04:25.310 00:04:25.320 can't measure so one way or the other
00:04:27.170 00:04:27.180 you need to know
00:04:28.040 00:04:28.050 what's going on and this could be a fire
00:04:30.320 00:04:30.330 tube or water tube what we call a heat
00:04:32.749 00:04:32.759 recovery steam generator system so what
00:04:34.969 00:04:34.979 we'll talk about basically what those
00:04:36.890 00:04:36.900 are so and and you might have a boiler
00:04:39.529 00:04:39.539 that produces what we saturated steam so
00:04:41.839 00:04:41.849 it's its saturation temperature or as
00:04:44.749 00:04:44.759 perhaps superheated where additional
00:04:46.430 00:04:46.440 heat inputs been added and there's
00:04:48.830 00:04:48.840 different requirements and different
00:04:50.149 00:04:50.159 problems that occur from there and
00:04:51.619 00:04:51.629 basically all the industrial boiler
00:04:54.080 00:04:54.090 cycle chemistry information and
00:04:56.809 00:04:56.819 knowledge and guidance out there is
00:04:58.159 00:04:58.169 derived from the sides behind the power
00:05:00.770 00:05:00.780 boilers and the heat recovery steam
00:05:02.240 00:05:02.250 generator cycle chemistry so HR heat
00:05:05.209 00:05:05.219 recovery steam generator is what we put
00:05:06.499 00:05:06.509 behind large gas turbines if you're
00:05:08.510 00:05:08.520 driving on the motorway and all clean
00:05:11.029 00:05:11.039 you go passio - who do power station
00:05:12.800 00:05:12.810 that's what that is and that's it so
00:05:14.390 00:05:14.400 just just another type of boiler but we
00:05:16.339 00:05:16.349 don't really want to too much on that so
00:05:18.529 00:05:18.539 why cycle chemistry what we're what
00:05:20.839 00:05:20.849 we're trying to do is prevent corrosion
00:05:22.760 00:05:22.770 and deep position related failures and
00:05:25.070 00:05:25.080 of obviously if you're a boiler Springs
00:05:27.200 00:05:27.210 a big leak it's not gonna run so we call
00:05:29.240 00:05:29.250 that a forced outage of the feed system
00:05:31.820 00:05:31.830 the boiler HT and the steam path so all
00:05:34.580 00:05:34.590 these images here bad days in the office
00:05:37.129 00:05:37.139 this is a severe Pettine damage which is
00:05:39.559 00:05:39.569 actually caused the leak and a super
00:05:41.629 00:05:41.639 heater here's what we call a short-term
00:05:43.159 00:05:43.169 overheating failure and another plant
00:05:44.749 00:05:44.759 and this is a multi-colored turbine
00:05:47.029 00:05:47.039 because some of the chemical components
00:05:49.430 00:05:49.440 and the feedwater have ended up on a
00:05:51.320 00:05:51.330 turbine and it's not really great
00:05:53.809 00:05:53.819 because it significantly impacts on
00:05:56.029 00:05:56.039 performance of it steam turbine so
00:05:59.059 00:05:59.069 what's the most common industrial boiler
00:06:01.010 00:06:01.020 it's what we call the foster wheeler
00:06:02.330 00:06:02.340 d-type it's called the d-type because
00:06:05.450 00:06:05.460 when you look at it in the side profile
00:06:06.800 00:06:06.810 the the shape of the drum and the tubes
00:06:08.749 00:06:08.759 makes a d but basically you have a
00:06:11.059 00:06:11.069 cavity there'll be a flame going and
00:06:14.689 00:06:14.699 there might be gas or oil series of
00:06:18.230 00:06:18.240 tubes that pick up heat we have a steam
00:06:20.209 00:06:20.219 drum up here that assisting water
00:06:21.860 00:06:21.870 separation and there'll be a super
00:06:23.360 00:06:23.370 heater on the back here if it is one of
00:06:25.790 00:06:25.800 those and it's really the most common
00:06:27.409 00:06:27.419 type worldwide and you know they wear
00:06:30.260 00:06:30.270 says one that's all fully cleared and in
00:06:32.269 00:06:32.279 service and a plan and they they range
00:06:33.890 00:06:33.900 in size but you know from few tons are
00:06:36.529 00:06:36.539 now at tens of tons an hour and this is
00:06:39.589 00:06:39.599 what a lot like inside profile really
00:06:41.420 00:06:41.430 it's
00:06:41.830 00:06:41.840 it's you have a feedwater drum at the
00:06:43.900 00:06:43.910 bottom what it comes in Rises the heat
00:06:47.500 00:06:47.510 there starts to boil in these tubes
00:06:49.450 00:06:49.460 comes up into the steam drum with water
00:06:51.250 00:06:51.260 steam separation occurs steam will come
00:06:53.770 00:06:53.780 out go through the superheater
00:06:55.120 00:06:55.130 and how it goes and it may be an
00:06:56.560 00:06:56.570 economizer onto the back here as well
00:06:59.379 00:06:59.389 just depends on design but we call there
00:07:02.500 00:07:02.510 water to boiler the water is in the
00:07:05.050 00:07:05.060 tubes in the fire or the heat is in the
00:07:07.780 00:07:07.790 gas space around there the second most
00:07:10.330 00:07:10.340 common type particularly new zealand
00:07:12.070 00:07:12.080 frontier has a lot of these what we call
00:07:13.659 00:07:13.669 water-tube boilers and this is basically
00:07:16.180 00:07:16.190 directly evolved from the old steam
00:07:18.400 00:07:18.410 trains in here we have basically a tank
00:07:21.730 00:07:21.740 which is full of water with a sequence
00:07:23.230 00:07:23.240 of tubes running through it and the fire
00:07:25.060 00:07:25.070 is within the tubes okay so the owner at
00:07:28.930 00:07:28.940 one end and hot gases flows through
00:07:31.600 00:07:31.610 those tubes and the heat transfer occurs
00:07:33.490 00:07:33.500 and then it boils within this vessel and
00:07:36.129 00:07:36.139 there's some steam separation and off it
00:07:37.960 00:07:37.970 goes so water to boil is really only
00:07:39.700 00:07:39.710 produce my experience only produced
00:07:42.129 00:07:42.139 saturated steam where a fire tube sorry
00:07:47.560 00:07:47.570 I put water tube boiler on here when I
00:07:50.440 00:07:50.450 meant to put fire tube so there's a typo
00:07:52.090 00:07:52.100 on that slide so that's terrible of me
00:07:53.620 00:07:53.630 but a water tube boiler will produce
00:07:58.140 00:07:58.150 normally produced superheated steam
00:08:00.190 00:08:00.200 where a fire tube boilers normally only
00:08:02.140 00:08:02.150 saturated steam so it's correct on this
00:08:04.870 00:08:04.880 slide which is one also looking at one
00:08:06.580 00:08:06.590 on the outside and here we have the
00:08:07.930 00:08:07.940 burner and the in box here and then
00:08:10.240 00:08:10.250 there will be a sequence of tubes if
00:08:11.469 00:08:11.479 flames flow through there and and this
00:08:13.990 00:08:14.000 slide here just really shows a
00:08:15.430 00:08:15.440 difference so we have a water to boiler
00:08:17.290 00:08:17.300 it is to flame here and then the water
00:08:19.750 00:08:19.760 comes in as water at the bottom here and
00:08:21.879 00:08:21.889 there's it rises up it starts to form
00:08:23.469 00:08:23.479 steam and then there's a is a fraction a
00:08:25.330 00:08:25.340 steam that comes out and often the water
00:08:26.890 00:08:26.900 recycle don't come and then we have a
00:08:30.339 00:08:30.349 fire true boiler where water is from the
00:08:32.980 00:08:32.990 tank its surrounding the tubes and the
00:08:34.930 00:08:34.940 flame or the heat flows through there
00:08:36.699 00:08:36.709 okay so chemistry problems are different
00:08:40.120 00:08:40.130 similar in a lot of respects so what a
00:08:43.360 00:08:43.370 true saturated or superheated steam and
00:08:45.340 00:08:45.350 these can be low-pressure few bar timber
00:08:48.370 00:08:48.380 to up to 180 bar and that's about the
00:08:50.860 00:08:50.870 limit what we call subcritical boilers
00:08:53.579 00:08:53.589 anything higher than they
00:08:55.210 00:08:55.220 we pretty much get into supercritical
00:08:56.740 00:08:56.750 which is far beyond the realms of
00:08:58.629 00:08:58.639 industrial boilers but it's very very
00:09:00.280 00:09:00.290 interesting chemistry if they're
00:09:02.710 00:09:02.720 superheated steam and then we have to be
00:09:04.540 00:09:04.550 very concerned about superheated
00:09:06.160 00:09:06.170 corrosion and in the position control
00:09:08.199 00:09:08.209 because that's absolutely critical so
00:09:10.030 00:09:10.040 pretty much most industrial boilers that
00:09:12.280 00:09:12.290 have super heaters will end up having
00:09:13.869 00:09:13.879 some problem at some point in their
00:09:16.179 00:09:16.189 lives and the record that I've seen
00:09:19.600 00:09:19.610 complete destruction of super heaters
00:09:21.460 00:09:21.470 after a few years operation I've seen
00:09:23.679 00:09:23.689 complete destruction after 18 months and
00:09:25.869 00:09:25.879 I've seen complete structure enough for
00:09:27.220 00:09:27.230 about five days on this when they got
00:09:29.889 00:09:29.899 absolutely everything wrong fire tube
00:09:32.829 00:09:32.839 saturated steam only very normally only
00:09:35.350 00:09:35.360 around 10 bar pressure in in less
00:09:37.509 00:09:37.519 complex and water-tube boilers so much
00:09:39.579 00:09:39.589 simpler to operate so what does
00:09:42.009 00:09:42.019 corrosion corrosion is the wearing away
00:09:44.410 00:09:44.420 metals due to a chemical reaction so you
00:09:46.869 00:09:46.879 your bilge plant out of normally carbon
00:09:49.569 00:09:49.579 steel as the most common material and
00:09:51.309 00:09:51.319 corrosion is that carbon steel wanting
00:09:53.530 00:09:53.540 to turn back into a you know fall back
00:09:56.019 00:09:56.029 down the energy tree and go back into
00:09:58.420 00:09:58.430 the raw material that it was in the
00:10:00.040 00:10:00.050 ground before it got dug out and refined
00:10:01.929 00:10:01.939 and turned into a steel so it's it's the
00:10:04.990 00:10:05.000 disintegration of the material into its
00:10:07.590 00:10:07.600 Stewart atoms due to chemical reactions
00:10:10.150 00:10:10.160 or surroundings and it's it's basically
00:10:11.559 00:10:11.569 electrochemical oxidation process okay
00:10:13.900 00:10:13.910 and obviously if your tube is trying to
00:10:17.439 00:10:17.449 turn back into something else eventually
00:10:19.030 00:10:19.040 it'll start to leak or you have a
00:10:20.769 00:10:20.779 failure if it's holding some kind of
00:10:23.019 00:10:23.029 pressure so what is D position the
00:10:26.769 00:10:26.779 position is a transport of material onto
00:10:28.629 00:10:28.639 a surface so or in a boiler it's
00:10:31.480 00:10:31.490 normally receiver a suspended solid
00:10:35.670 00:10:35.680 which has been picked up from one
00:10:37.720 00:10:37.730 location so in the case of boilers often
00:10:39.879 00:10:39.889 this is you have corrosion in one
00:10:42.069 00:10:42.079 location so you've corrosion of carbon
00:10:43.840 00:10:43.850 steel you end up with an iron oxide
00:10:45.699 00:10:45.709 probably magnetite or hematite and then
00:10:48.939 00:10:48.949 that gets transported and deposited onto
00:10:50.949 00:10:50.959 another surface where that may cause you
00:10:52.749 00:10:52.759 some more problems might be heat
00:10:54.189 00:10:54.199 transfer or may become a location where
00:10:56.199 00:10:56.209 other corrosion can occur the other part
00:10:58.480 00:10:58.490 of the position is that if you have
00:10:59.799 00:10:59.809 something dissolved into the water like
00:11:01.629 00:11:01.639 in this image here showing silica
00:11:03.790 00:11:03.800 deposition and side of boiler so what's
00:11:06.069 00:11:06.079 happened is has been a bit too much
00:11:07.449 00:11:07.459 dissolved silica in there and is
00:11:09.040 00:11:09.050 temperatures of moved around that's
00:11:10.930 00:11:10.940 changed the solubility profile and
00:11:13.060 00:11:13.070 you've had silica precipitation on to
00:11:15.400 00:11:15.410 that surface it's a problem in boilers
00:11:18.430 00:11:18.440 because it affects heat transfer and it
00:11:20.079 00:11:20.089 can cause overheating and it's a major
00:11:21.639 00:11:21.649 problem and steam turbines because it
00:11:23.530 00:11:23.540 all cause normally efficiency or output
00:11:29.139 00:11:29.149 issues because you get a buildup on to
00:11:30.730 00:11:30.740 the blades it disrupts the lamina flow
00:11:32.500 00:11:32.510 on the turbine of the steam and then the
00:11:34.840 00:11:34.850 two-point efficiency falls right away we
00:11:37.540 00:11:37.550 don't want it
00:11:38.170 00:11:38.180 um terms of the plan itself it's the
00:11:42.430 00:11:42.440 bulk of the plants carbon steel already
00:11:44.199 00:11:44.209 mentioned there and and what good
00:11:46.660 00:11:46.670 chemistry does is it actually forms a
00:11:48.880 00:11:48.890 stable oxide but like your aluminium and
00:11:51.699 00:11:51.709 the aluminium oxide on you and the
00:11:53.259 00:11:53.269 aluminium beer cans okay and what we're
00:11:55.660 00:11:55.670 trying to form as a stable minger Titan
00:11:58.120 00:11:58.130 hematite oxide on the surface and what
00:12:00.250 00:12:00.260 the corrosion does is it disrupts those
00:12:02.410 00:12:02.420 protective oxide so listen any kind of
00:12:05.380 00:12:05.390 boiler plant we have particular oxides
00:12:07.360 00:12:07.370 which we get the reaction to go right is
00:12:10.720 00:12:10.730 a very quick very a self-limiting
00:12:13.870 00:12:13.880 reaction where you get a few microns of
00:12:15.819 00:12:15.829 oxide formed and it's since that you
00:12:17.829 00:12:17.839 grow and and it stays here
00:12:19.990 00:12:20.000 corrosion disrupt set or heavy
00:12:22.630 00:12:22.640 deposition will deposit more material on
00:12:24.639 00:12:24.649 top of it and then result more problem
00:12:26.319 00:12:26.329 so so that's basically what corrosion is
00:12:29.019 00:12:29.029 it's as disruption of those oxides
00:12:31.800 00:12:31.810 material gets lost from underneath the
00:12:34.090 00:12:34.100 oxide and then you're thinning and
00:12:35.590 00:12:35.600 failures and the type and location and
00:12:37.990 00:12:38.000 that corrosion depends on the design the
00:12:39.819 00:12:39.829 temperatures the pressures and and we'll
00:12:41.620 00:12:41.630 talk about that and follow-up webinar
00:12:44.500 00:12:44.510 that we'll do later on in the year in
00:12:46.319 00:12:46.329 terms of the position the biggest issue
00:12:49.750 00:12:49.760 in the industrial boilers as he keep
00:12:51.639 00:12:51.649 deposits on the heat transfer surfaces
00:12:53.710 00:12:53.720 so these can be the boiler tubes and
00:12:55.780 00:12:55.790 heating tubes and obviously things like
00:12:58.240 00:12:58.250 silica heavy silica deposits or calcium
00:13:01.600 00:13:01.610 magnesium deposits have quite
00:13:05.050 00:13:05.060 significant insulating effects and what
00:13:07.360 00:13:07.370 it means is that the tube is no longer
00:13:09.400 00:13:09.410 being cooled by the water or the steam
00:13:11.500 00:13:11.510 that's flowing through it and what
00:13:13.780 00:13:13.790 happens is basically the material will
00:13:16.150 00:13:16.160 approach the gas side temperature and
00:13:18.040 00:13:18.050 you'll get what call it creep failure
00:13:20.019 00:13:20.029 and this can happen quite quickly
00:13:22.489 00:13:22.499 particularly if the tube is blocked by
00:13:24.649 00:13:24.659 the depositor some maintenance debris
00:13:26.689 00:13:26.699 but creep failures predominantly in
00:13:29.689 00:13:29.699 super heaters but they can't happen and
00:13:31.189 00:13:31.199 natural boiler tubes and it's not a not
00:13:34.999 00:13:35.009 a good day in the office because
00:13:36.019 00:13:36.029 normally if one tube goes you've got a
00:13:37.579 00:13:37.589 bunch of them they're gonna go as well
00:13:39.309 00:13:39.319 alright so history cycle chemistry
00:13:42.289 00:13:42.299 wizard or come from originally came from
00:13:44.509 00:13:44.519 steam trains and this is a steam train
00:13:46.999 00:13:47.009 with a higher two boiler okay you can
00:13:50.869 00:13:50.879 see the troops here and he's having a
00:13:52.009 00:13:52.019 bit of a bad day in the office because
00:13:53.539 00:13:53.549 he's obviously had a catastrophic
00:13:54.559 00:13:54.569 failure of his boiler so next we're
00:13:57.769 00:13:57.779 basically boiler chemistry came out of
00:14:00.229 00:14:00.239 there was the Industrial Revolution
00:14:01.339 00:14:01.349 started boilers were invented and they
00:14:03.979 00:14:03.989 started running them and they started to
00:14:05.269 00:14:05.279 have all kinds of problems with boilers
00:14:06.919 00:14:06.929 exploding and killing people and steam
00:14:10.069 00:14:10.079 trains not run on time and the whole
00:14:12.229 00:14:12.239 area of boiler cycle chemistry science
00:14:15.049 00:14:15.059 was developed to try to improve the
00:14:16.969 00:14:16.979 reliability of these engines and then
00:14:18.679 00:14:18.689 stationary engines and factories and
00:14:20.599 00:14:20.609 that's where it's all kind of come from
00:14:22.129 00:14:22.139 so if you need some guidance there are
00:14:25.519 00:14:25.529 some guidelines out there rule boilers
00:14:27.679 00:14:27.689 as me in the US has a guideline that you
00:14:30.679 00:14:30.689 can purchase it's the consensus document
00:14:33.499 00:14:33.509 on operating practices that maybe a
00:14:36.799 00:14:36.809 couple of hundred bucks New Zealand for
00:14:38.719 00:14:38.729 their psi the British standards have
00:14:41.899 00:14:41.909 another one recommendations for the
00:14:44.389 00:14:44.399 treatment of for steam boilers and water
00:14:45.769 00:14:45.779 heaters this is quite old and quite out
00:14:47.659 00:14:47.669 of date you can purchase it as well so
00:14:49.339 00:14:49.349 AF Singh's it standards is really
00:14:51.619 00:14:51.629 nothing available and then there's also
00:14:54.109 00:14:54.119 these IX guidelines from the
00:14:55.789 00:14:55.799 International Association probably the
00:14:56.989 00:14:56.999 water and steam these are free these are
00:14:59.029 00:14:59.039 primarily focused on power plants but
00:15:00.979 00:15:00.989 they do have the replicability the
00:15:02.719 00:15:02.729 industrial boilers and there are some
00:15:04.389 00:15:04.399 discussion around whether I should
00:15:06.469 00:15:06.479 produce an industrial boiler guideline
00:15:08.569 00:15:08.579 as well so just quickly on their IEPs if
00:15:11.029 00:15:11.039 you've ever used the steam table you
00:15:13.339 00:15:13.349 would have you some I it's technology so
00:15:15.049 00:15:15.059 it's a non-profit association made up of
00:15:17.479 00:15:17.489 national organizations New Zealand's a
00:15:19.039 00:15:19.049 member I'm people involved in it and all
00:15:21.949 00:15:21.959 very interested in the thermo physical
00:15:23.329 00:15:23.339 properties of water and steam and
00:15:25.579 00:15:25.589 particularly for thermal power plants
00:15:28.309 00:15:28.319 and industrial applications and you go
00:15:30.919 00:15:30.929 to the website and you can find a bunch
00:15:32.449 00:15:32.459 of guidelines that were talked about
00:15:33.469 00:15:33.479 there's ones for measuring I think will
00:15:35.179 00:15:35.189 carry over
00:15:36.199 00:15:36.209 is volatile treatments for steam water
00:15:38.210 00:15:38.220 circuits a fossil a combined cycle
00:15:39.710 00:15:39.720 plants phosphate and caustic treatments
00:15:42.350 00:15:42.360 for mine cycle and fossil power plants
00:15:45.530 00:15:45.540 there's some instrumentation guideline
00:15:47.569 00:15:47.579 is some steam purity if you've got steam
00:15:49.639 00:15:49.649 turbine you want to know a bit more
00:15:51.019 00:15:51.029 about steam purity for your turbine
00:15:52.519 00:15:52.529 operation this stuff there there's
00:15:54.319 00:15:54.329 another one for corrosion product sound
00:15:56.389 00:15:56.399 analysis which is quite useful as well
00:15:59.329 00:15:59.339 and you can get all of these off the
00:16:01.069 00:16:01.079 iights website if you get better than I
00:16:03.350 00:16:03.360 it's not org and then click on technical
00:16:05.329 00:16:05.339 guidance documents it'll it'll take you
00:16:07.100 00:16:07.110 through to there and they're all free to
00:16:08.569 00:16:08.579 an available to download so what are the
00:16:11.419 00:16:11.429 key aspects of industrial boiler cycle
00:16:13.970 00:16:13.980 chemistry control obviously effective
00:16:15.859 00:16:15.869 makeup makeup water treatment and to
00:16:17.809 00:16:17.819 that we're going to go through each of
00:16:19.069 00:16:19.079 these feed water pH corrosion control
00:16:21.460 00:16:21.470 feed water dissolved gases control
00:16:24.340 00:16:24.350 boiler pH and corrosion control boiler
00:16:27.650 00:16:27.660 scale control boiler blow down control
00:16:30.699 00:16:30.709 saturated steam V position and corrosion
00:16:33.710 00:16:33.720 control superheated steam D position and
00:16:35.989 00:16:35.999 corrosion control steam turbine D
00:16:38.299 00:16:38.309 position and corrosion control if you
00:16:39.859 00:16:39.869 have a steam turbine not all plants do
00:16:42.639 00:16:42.649 condensate return purity control
00:16:45.549 00:16:45.559 sampling analysis layup and storage
00:16:48.619 00:16:48.629 protection that's that's basically what
00:16:53.150 00:16:53.160 we're going to what we're going to touch
00:16:54.169 00:16:54.179 on today as we go through so first one
00:16:57.350 00:16:57.360 effective make up water treatment so
00:16:59.739 00:16:59.749 water treatment is as the removal of
00:17:02.840 00:17:02.850 unwanted suspended and dissolved ions
00:17:04.669 00:17:04.679 prior to entering and boiler so if we
00:17:07.850 00:17:07.860 took the lovely Waikato River water and
00:17:10.610 00:17:10.620 we put that straight into a boiler it's
00:17:13.850 00:17:13.860 got both suspended material maybe maybe
00:17:16.939 00:17:16.949 the odds swimmer and things like that
00:17:18.289 00:17:18.299 still in there I'm in a whole lot of
00:17:20.120 00:17:20.130 dissolved material and as we start to
00:17:21.949 00:17:21.959 heat it up we changed some abilities and
00:17:24.199 00:17:24.209 we'll get an awful lot of deep position
00:17:25.370 00:17:25.380 and the water may actually be quite
00:17:26.779 00:17:26.789 corrosive as well
00:17:28.970 00:17:28.980 higher the pressure the boiler the more
00:17:31.039 00:17:31.049 critical the water treatment is and this
00:17:32.720 00:17:32.730 is because as you increase the pressure
00:17:34.820 00:17:34.830 operating pressure of a boiler your
00:17:37.100 00:17:37.110 tolerance because for cycle chemistry
00:17:40.669 00:17:40.679 problems goes down and down and down
00:17:42.529 00:17:42.539 currently there's higher the temperature
00:17:43.970 00:17:43.980 the faster the reaction rates
00:17:46.269 00:17:46.279 solubilities change with pressure and
00:17:48.289 00:17:48.299 temperature as well
00:17:49.860 00:17:49.870 so normally you know lesson 10 bath oil
00:17:53.220 00:17:53.230 is all around him you want potable water
00:17:55.500 00:17:55.510 potable waters had most of the suspended
00:17:58.769 00:17:58.779 solids removed should have you know
00:18:00.330 00:18:00.340 probably less than 0.3 in tea use of
00:18:02.730 00:18:02.740 stability in there and normally it'll go
00:18:05.490 00:18:05.500 through a water softener and in order
00:18:07.289 00:18:07.299 water softener deserts remove some metal
00:18:09.269 00:18:09.279 cations only so it takes out magnesium
00:18:11.549 00:18:11.559 and calcium and substitutes those with
00:18:14.070 00:18:14.080 sodium ions and less commonly fir say
00:18:17.330 00:18:17.340 firetube boiler and like Fonterra plant
00:18:20.039 00:18:20.049 or maybe at a small industrial plant
00:18:24.450 00:18:24.460 that is commonly the only treatment in
00:18:26.159 00:18:26.169 use and it it kind of works and kind of
00:18:29.549 00:18:29.559 dozen if you operating it more than kind
00:18:31.860 00:18:31.870 of dentin bar plus really you know my
00:18:34.710 00:18:34.720 recommendation is you really need to
00:18:36.029 00:18:36.039 consider what mineralize ER and this is
00:18:39.180 00:18:39.190 removes basically all of the dissolved
00:18:41.340 00:18:41.350 ions if you're taking raw water off in
00:18:44.130 00:18:44.140 their plant or have some kind of pre
00:18:45.600 00:18:45.610 treatment plant on there remove all the
00:18:47.940 00:18:47.950 suspended material and then it will go
00:18:50.310 00:18:50.320 through and take out all the dissolved
00:18:51.930 00:18:51.940 ions so basically the bitter the
00:18:54.990 00:18:55.000 dissolved iron removal the bit of the
00:18:56.549 00:18:56.559 boil and make up water in terms of
00:18:57.930 00:18:57.940 quality and because of that you'll get
00:18:59.909 00:18:59.919 love blowdown of the oilers will lower
00:19:02.730 00:19:02.740 your treatment chemical demands and it
00:19:05.250 00:19:05.260 lowers your operating costs so it's one
00:19:06.779 00:19:06.789 of these things that you spend a bit
00:19:08.100 00:19:08.110 more capex upfront and you build a plant
00:19:10.680 00:19:10.690 it's got a good water treatment plan
00:19:11.909 00:19:11.919 only your opposite operating expenses
00:19:14.430 00:19:14.440 will go down because you don't have to
00:19:17.330 00:19:17.340 deal with the problem and the boiler you
00:19:19.649 00:19:19.659 take the problem away before it goes in
00:19:21.769 00:19:21.779 and in water treatment plants like a
00:19:24.450 00:19:24.460 talking you know the bait most basic
00:19:26.010 00:19:26.020 there's a softener when they have to
00:19:27.630 00:19:27.640 potable water or you could have an ion
00:19:30.120 00:19:30.130 exchange plant you use cation cation
00:19:32.940 00:19:32.950 resin beard followed by an anion resin
00:19:34.860 00:19:34.870 beads cation
00:19:35.850 00:19:35.860 takes out all the positive charged ions
00:19:37.590 00:19:37.600 and ion removes the the negative charged
00:19:40.710 00:19:40.720 ions where you can enter cation and
00:19:42.299 00:19:42.309 anion in a mixed beard which improves
00:19:45.210 00:19:45.220 the performance even more you could use
00:19:47.610 00:19:47.620 reverse osmosis membranes or you could
00:19:49.919 00:19:49.929 use a reverse osmosis and a continuous
00:19:52.110 00:19:52.120 electrical deionization unit 101
00:19:56.159 00:19:56.169 different ways to skin the care on there
00:19:57.750 00:19:57.760 but basically at a water trip
00:20:00.720 00:20:00.730 plant you know this is these are sort of
00:20:02.460 00:20:02.470 the things that we want to see for
00:20:03.810 00:20:03.820 anything over about ten bar we want to
00:20:05.820 00:20:05.830 see water out of the plant
00:20:06.960 00:20:06.970 conductivity listen one microsiemens
00:20:08.789 00:20:08.799 centimeter for conductivity after cation
00:20:12.480 00:20:12.490 exchange less than 0.1 in silica less
00:20:15.270 00:20:15.280 than 10 ppb and that will pretty much
00:20:17.669 00:20:17.679 give you suitable quality water to avoid
00:20:19.950 00:20:19.960 a whole lot of problems but don't just
00:20:22.110 00:20:22.120 an equality we also need the right
00:20:23.640 00:20:23.650 quantity if your plant demand is say
00:20:27.419 00:20:27.429 five tons an hour of makeup water
00:20:29.580 00:20:29.590 because you're using some in your
00:20:30.870 00:20:30.880 process building a three-ton an hour
00:20:33.000 00:20:33.010 water treatment plan you're probably
00:20:34.710 00:20:34.720 going to have quite a few operational
00:20:36.120 00:20:36.130 problems the industry rule of thumb that
00:20:38.460 00:20:38.470 we use when designing water treatment
00:20:40.080 00:20:40.090 plants is normally 20% over what you
00:20:42.600 00:20:42.610 think your maximum demanders and you
00:20:44.789 00:20:44.799 should be about right in the problem of
00:20:47.400 00:20:47.410 poor quality makeup water as it's a
00:20:49.230 00:20:49.240 cumulative problem so you know i say to
00:20:52.200 00:20:52.210 many people it's you know you build new
00:20:54.480 00:20:54.490 boiler we can follow it up or whatever
00:20:56.640 00:20:56.650 water you want
00:20:57.480 00:20:57.490 failure won't have instantly it'll
00:20:59.340 00:20:59.350 happen over time and the further you
00:21:01.650 00:21:01.660 deviate from optimum water quality you
00:21:04.530 00:21:04.540 know that the shorter that time to
00:21:06.480 00:21:06.490 failure will be normally we find their
00:21:09.330 00:21:09.340 plants at a suboptimal and design you
00:21:12.060 00:21:12.070 know a few years down the track problems
00:21:13.919 00:21:13.929 start to happen so that's just something
00:21:16.590 00:21:16.600 to think about water treatment as a
00:21:18.360 00:21:18.370 long-term problem and normally when we
00:21:21.120 00:21:21.130 add in water into the plant it'll go
00:21:23.280 00:21:23.290 into the condenser hot well or gets made
00:21:25.680 00:21:25.690 up into the aerator so there'll be a
00:21:28.140 00:21:28.150 point in your plant whether with water
00:21:30.659 00:21:30.669 comes back in to replace water that's
00:21:32.820 00:21:32.830 lost so it might be lost because of oil
00:21:34.650 00:21:34.660 blowdown to be lost to the leakage and
00:21:36.990 00:21:37.000 the plant or it could be that you
00:21:38.909 00:21:38.919 produce in tons and hour of steam and in
00:21:42.060 00:21:42.070 your industrial process five tons an
00:21:44.610 00:21:44.620 hour of that steam is consumed by some
00:21:49.409 00:21:49.419 kind of he's hurt or rejection into the
00:21:51.840 00:21:51.850 process so you've got a replace set that
00:21:54.480 00:21:54.490 it fluid that's lost from system so
00:21:58.110 00:21:58.120 it'll it'll have to come back into your
00:21:59.940 00:21:59.950 plant somewhere along the line so the
00:22:02.640 00:22:02.650 next one is feed water pH corrosion
00:22:04.860 00:22:04.870 control and the simplest way that I can
00:22:07.169 00:22:07.179 kind of describe this as we have carbon
00:22:09.570 00:22:09.580 steel and carbon steel has a is a
00:22:12.270 00:22:12.280 corrosion rate so relative the tech here
00:22:14.680 00:22:14.690 that it depends on the pH we got pH
00:22:17.590 00:22:17.600 range of 1 to 14 so if we operate in a
00:22:20.620 00:22:20.630 pH of say you know one and a half to two
00:22:24.400 00:22:24.410 corrosion rates very high for carbon
00:22:26.530 00:22:26.540 steel and esri increases pH that
00:22:29.050 00:22:29.060 corrosion rate really comes down okay we
00:22:32.800 00:22:32.810 get we actually get down to a minimum
00:22:34.330 00:22:34.340 here it's about nine point eight to ten
00:22:36.460 00:22:36.470 is about the minimum for what we call
00:22:38.980 00:22:38.990 the ferrous ion solubility for carbon
00:22:40.990 00:22:41.000 steel what's it's it's basically wants
00:22:43.060 00:22:43.070 to be at that pH and then as we go over
00:22:45.430 00:22:45.440 that pH if we go up and the high
00:22:47.470 00:22:47.480 alkaline States the corrosion rate
00:22:49.540 00:22:49.550 starts to increase again so in in most
00:22:52.930 00:22:52.940 boilers and power plants you know we're
00:22:55.510 00:22:55.520 trying to get a pH it's alkaline you
00:22:58.810 00:22:58.820 know normally eight nine ten and the
00:23:01.780 00:23:01.790 feedwater and same for the boiler
00:23:03.700 00:23:03.710 because that's optimum for the materials
00:23:05.530 00:23:05.540 now whether you can obtain that pH
00:23:07.570 00:23:07.580 depends on your plant design and what
00:23:10.840 00:23:10.850 your steam and things like that have
00:23:14.350 00:23:14.360 been used for whether this hot water
00:23:15.940 00:23:15.950 being extracted from the boiler for
00:23:17.500 00:23:17.510 another process it may impact on other
00:23:19.180 00:23:19.190 materials in there but here is a bit of
00:23:22.390 00:23:22.400 a zoomin as we as we come in around the
00:23:24.580 00:23:24.590 difference between eight point eight
00:23:25.780 00:23:25.790 nine point six you can see here that
00:23:27.670 00:23:27.680 corrosion rate keeps coming down and and
00:23:30.850 00:23:30.860 most of the modern guidelines were
00:23:32.500 00:23:32.510 written in the our feedwater pH around
00:23:34.660 00:23:34.670 nine point eight these days for in the
00:23:37.660 00:23:37.670 optimum point between the cost of adding
00:23:41.170 00:23:41.180 something to to increase that pH versus
00:23:43.900 00:23:43.910 the pH where you get your best bang for
00:23:45.940 00:23:45.950 your buck so normally every plant you've
00:23:48.910 00:23:48.920 got to adjust the pH of your feed water
00:23:50.470 00:23:50.480 unless you're going to build your entire
00:23:51.910 00:23:51.920 feed water system here to say three one
00:23:54.460 00:23:54.470 six stainless steel or something like
00:23:56.140 00:23:56.150 that but you'll find that the cost of
00:23:58.540 00:23:58.550 adding building the plant out of a very
00:24:00.820 00:24:00.830 highly corrosion resistant material far
00:24:02.980 00:24:02.990 exceeds the cost of spending a little
00:24:05.080 00:24:05.090 bit of money on something like adding a
00:24:06.670 00:24:06.680 bidet yes ammonia and so um to increase
00:24:10.330 00:24:10.340 it pH so how do we do pH control
00:24:13.720 00:24:13.730 normally it's with a volatile aiming and
00:24:16.090 00:24:16.100 aqueous ammonia is the most common it's
00:24:18.670 00:24:18.680 cheap pretty easy to use you just dose a
00:24:20.710 00:24:20.720 little bit in with the dosing pump if
00:24:22.840 00:24:22.850 it's what we call a volatile a mean what
00:24:24.910 00:24:24.920 it means is it dissolves into the water
00:24:27.070 00:24:27.080 but then it all
00:24:28.090 00:24:28.100 so goes into the steam and all then when
00:24:30.549 00:24:30.559 steam condenses it's still present and
00:24:32.560 00:24:32.570 there so what it will do is will give
00:24:34.419 00:24:34.429 you a pH correction in the feed water
00:24:35.830 00:24:35.840 then it will give you a pH correction
00:24:37.630 00:24:37.640 and the condensate if you can't use a
00:24:40.510 00:24:40.520 volatile aiming so say your you've got
00:24:44.409 00:24:44.419 food contact with steam where if there's
00:24:46.510 00:24:46.520 any any ammonia prison and the steam
00:24:48.549 00:24:48.559 Nedim Exxon your product quality then
00:24:51.070 00:24:51.080 you have to use what we call a solid
00:24:52.539 00:24:52.549 alkali we've got to use something that's
00:24:53.950 00:24:53.960 not going to be volatile and the steam
00:24:55.690 00:24:55.700 and what we find the sodium hydroxide
00:24:57.960 00:24:57.970 injected into the feed water is the most
00:25:00.159 00:25:00.169 common solid alkali so it will give you
00:25:02.049 00:25:02.059 a pH shift and the feed water and then
00:25:04.450 00:25:04.460 it will go into the boiler and it stays
00:25:05.890 00:25:05.900 in the boiler and doesn't transport into
00:25:07.659 00:25:07.669 the steam so and that's and that's what
00:25:09.730 00:25:09.740 you want but again depends on your plant
00:25:12.190 00:25:12.200 Pinzon whether you got the right contact
00:25:14.409 00:25:14.419 if you've got non contact heat
00:25:16.120 00:25:16.130 exchangers so that you have the process
00:25:18.520 00:25:18.530 being heated on one side and the steam
00:25:20.529 00:25:20.539 condensing on the other then ammonia is
00:25:22.720 00:25:22.730 normally your best choice it's quite
00:25:24.850 00:25:24.860 well but it's easy and there's a lot of
00:25:27.460 00:25:27.470 science being done around its use for
00:25:30.640 00:25:30.650 dissolved gases it's a that's the next
00:25:32.409 00:25:32.419 one normally people use a deaerator okay
00:25:35.710 00:25:35.720 and here we use Henry's law so what we
00:25:37.720 00:25:37.730 have is we have a vessel and it's got a
00:25:40.600 00:25:40.610 the boiler feed water is sprayed in we
00:25:43.750 00:25:43.760 have some oxygen free steam that's
00:25:45.460 00:25:45.470 pushed them to the bottom here that
00:25:46.930 00:25:46.940 flows up by Henry's law we get gas
00:25:49.240 00:25:49.250 exchange net steam strips the oxygen
00:25:52.060 00:25:52.070 from the boiler feedwater and that'll be
00:25:53.560 00:25:53.570 ejected out in the event and then the
00:25:55.870 00:25:55.880 water falls down has picked up some heat
00:25:57.730 00:25:57.740 as well and then it will remain and what
00:26:00.130 00:26:00.140 we call the feed water storage tank and
00:26:01.750 00:26:01.760 it may have some steaming in there as
00:26:03.130 00:26:03.140 well and that's and that's fired now in
00:26:06.880 00:26:06.890 the girl days when we invented steam
00:26:09.970 00:26:09.980 trains the logic was that any oxygen is
00:26:13.120 00:26:13.130 bad so people went way out of their way
00:26:16.270 00:26:16.280 with deaerators and dosing chemical
00:26:19.120 00:26:19.130 oxygen scavengers to try to get the
00:26:20.680 00:26:20.690 oxygen to zero it was thought at any
00:26:23.200 00:26:23.210 oxygen is bad and any plant now we've
00:26:26.320 00:26:26.330 learnt a few mistakes around there and
00:26:28.630 00:26:28.640 we've discovered some of that logic if
00:26:30.909 00:26:30.919 the plant is constructed out of all
00:26:33.130 00:26:33.140 ferrous materials it's all carbon steel
00:26:35.230 00:26:35.240 actually having zero oxygen is bad and
00:26:37.990 00:26:38.000 we actually want a little bit of oxygen
00:26:39.520 00:26:39.530 present in the water
00:26:42.060 00:26:42.070 there's what we find is if we have
00:26:44.710 00:26:44.720 pretty good quality water its grafts a
00:26:47.619 00:26:47.629 little bit hard to understand but here's
00:26:48.970 00:26:48.980 our corrosion rate is there oxygen
00:26:51.009 00:26:51.019 content and this these numbers here 0.1
00:26:53.460 00:26:53.470 782 850 these relate to the conductivity
00:26:56.739 00:26:56.749 of the water in terms of its buildup of
00:26:59.409 00:26:59.419 corrosive ions so particularly chloride
00:27:01.720 00:27:01.730 that's in the water so the lower this
00:27:03.669 00:27:03.679 conductivity the cleaner the water is
00:27:05.289 00:27:05.299 and what we find is if we have pretty
00:27:07.060 00:27:07.070 clean water pretty good make up water if
00:27:09.460 00:27:09.470 we actually have no oxygen the corrosion
00:27:11.590 00:27:11.600 rate is higher than if we have a little
00:27:13.359 00:27:13.369 bit of oxygen present you see the
00:27:14.680 00:27:14.690 corrosion rate comes down however if we
00:27:17.109 00:27:17.119 have contamination in our water so we
00:27:19.210 00:27:19.220 have chlorides you learn fine you might
00:27:21.639 00:27:21.649 have to see water condenser or sea water
00:27:23.430 00:27:23.440 cooling system and then you get a
00:27:26.159 00:27:26.169 leakage and a heat exchanger and you get
00:27:28.389 00:27:28.399 some process contamination as that
00:27:30.669 00:27:30.679 conductivity goes up with that corrosive
00:27:33.669 00:27:33.679 material thats in there as they had
00:27:35.470 00:27:35.480 oxygen increases the corrosion rate
00:27:36.909 00:27:36.919 increases so oxygen is your friend in
00:27:38.830 00:27:38.840 your enemy but what we know is basically
00:27:42.220 00:27:42.230 if we've got 5 to 10 ppb of oxygen
00:27:44.859 00:27:44.869 that's about optimum we get actually
00:27:46.810 00:27:46.820 quite good corrosion protection from
00:27:49.180 00:27:49.190 that now what happens here is that if we
00:27:51.730 00:27:51.740 have a little bit of oxygen present in
00:27:53.499 00:27:53.509 the water and helps with that protective
00:27:56.080 00:27:56.090 oxide layer that wants to form we end up
00:27:58.149 00:27:58.159 with a little bit more hematite compared
00:28:00.460 00:28:00.470 to magnetite and that's a whole lot more
00:28:02.139 00:28:02.149 protective if you've got copper
00:28:06.450 00:28:06.460 materials in your plant then yes you do
00:28:09.430 00:28:09.440 have to dose an oxygen scavenger and
00:28:11.139 00:28:11.149 then oxygen scavenger is actually to
00:28:12.669 00:28:12.679 protect the copper oxides that form on
00:28:15.789 00:28:15.799 those copper materials so if you're all
00:28:17.799 00:28:17.809 ferrous if you look at your material
00:28:19.389 00:28:19.399 sheets and you say I've got all carbon
00:28:22.690 00:28:22.700 steel through my whole plant or I'm
00:28:24.159 00:28:24.169 stainless steel and you have a deaerator
00:28:26.230 00:28:26.240 and you're dosing an oxygen scavenger
00:28:28.629 00:28:28.639 I'll give you some advice which is you
00:28:30.639 00:28:30.649 don't need to dosey oxygen scavenger and
00:28:32.710 00:28:32.720 you actually want five options and you
00:28:35.169 00:28:35.179 don't want zero so it's it's quite a
00:28:38.289 00:28:38.299 common problem in industrial boilers
00:28:39.940 00:28:39.950 because you know again if I'm if I'm mr.
00:28:42.549 00:28:42.559 chemical vendor and I'm selling you an
00:28:44.019 00:28:44.029 oxygen scavenger they've got quite a
00:28:45.340 00:28:45.350 good margin on them they make a lot of
00:28:47.560 00:28:47.570 money selling them so you know there's a
00:28:49.720 00:28:49.730 vested interest and continuing with
00:28:52.239 00:28:52.249 their process but you don't really need
00:28:53.889 00:28:53.899 it the most
00:28:55.960 00:28:55.970 common oxygen scavenger we see an
00:28:58.240 00:28:58.250 industrial boilers a sodium sulphite
00:29:00.900 00:29:00.910 that gets added in and again this is
00:29:03.310 00:29:03.320 directly derived from old steam train
00:29:04.870 00:29:04.880 technology and if you do this wrong you
00:29:07.540 00:29:07.550 basically get this risk of sulfate
00:29:09.400 00:29:09.410 hissing especially if you transfer it
00:29:11.860 00:29:11.870 into your steam system and that's
00:29:13.210 00:29:13.220 probably the most corner the most common
00:29:14.770 00:29:14.780 failures that we see in industrial
00:29:16.360 00:29:16.370 boilers as sulfate as in in the steam
00:29:18.220 00:29:18.230 path because they've been dosing sodium
00:29:20.410 00:29:20.420 sulfite when they don't really need it
00:29:21.820 00:29:21.830 and it's and it's coming through now you
00:29:24.250 00:29:24.260 may have heard about has seen an oxygen
00:29:26.860 00:29:26.870 hissing yes that is a corrosion
00:29:29.590 00:29:29.600 mechanism that occurs but what you need
00:29:31.510 00:29:31.520 to understand is that actually only
00:29:33.040 00:29:33.050 happens when the plan is shut down okay
00:29:35.830 00:29:35.840 it's a it's a galvanic type process and
00:29:38.560 00:29:38.570 what it doesn't what it needs is like a
00:29:41.380 00:29:41.390 no flow condition it needs water sitting
00:29:43.720 00:29:43.730 there stagnant and very very high levels
00:29:46.060 00:29:46.070 of oxygen like approaching saturation so
00:29:48.340 00:29:48.350 sort of 9,000 BP so you know if you've
00:29:52.450 00:29:52.460 got pets in your plant and we'll talk
00:29:54.880 00:29:54.890 about this in the next webinar but a few
00:29:56.890 00:29:56.900 have seen pets that that are growing
00:29:59.230 00:29:59.240 what it's telling me straight away is
00:30:01.150 00:30:01.160 that you've got a layup and storage
00:30:02.680 00:30:02.690 issue your planners wit when it shut
00:30:04.570 00:30:04.580 down and you've gone oxygen saturated
00:30:06.880 00:30:06.890 and you've got no Flow oxygen pitting
00:30:09.130 00:30:09.140 doesn't happen when the plan isn't
00:30:10.750 00:30:10.760 service when you've got flow over the
00:30:13.000 00:30:13.010 surfaces you disrupt that galvanic
00:30:14.800 00:30:14.810 process and it doesn't occur but I'm
00:30:18.040 00:30:18.050 yeah that one's a commonly misunderstood
00:30:20.860 00:30:20.870 and in the industry so next one oil
00:30:24.070 00:30:24.080 earth pH corrosion control okay
00:30:26.680 00:30:26.690 basically this curve slope always here
00:30:28.630 00:30:28.640 we want you know we want to be elevated
00:30:30.940 00:30:30.950 alkaline pH and the boiler closer we get
00:30:33.670 00:30:33.680 to 10 the bitter that it is so how do we
00:30:36.730 00:30:36.740 do that normally there's some what we
00:30:38.800 00:30:38.810 call a solid alkalis directly injected
00:30:40.900 00:30:40.910 into the steam drum just to increase the
00:30:42.850 00:30:42.860 pH a bit more if we need to you can add
00:30:46.420 00:30:46.430 that in via the feed water but it's a
00:30:48.340 00:30:48.350 control loop it's a little bit harder
00:30:50.170 00:30:50.180 but most boilers are all designed for
00:30:52.290 00:30:52.300 direct injection of an additional
00:30:54.430 00:30:54.440 treatment chemical directly into the
00:30:55.900 00:30:55.910 drum it'll have a distribution line that
00:30:57.640 00:30:57.650 runs down and you know higher pressure
00:31:00.730 00:31:00.740 feed water pump the most common products
00:31:02.800 00:31:02.810 are sodium hydroxide or trisodium
00:31:04.930 00:31:04.940 phosphate
00:31:05.700 00:31:05.710 okay and you want to avoid what we call
00:31:08.680 00:31:08.690 mono advice
00:31:09.760 00:31:09.770 in phosphate blends and if you get this
00:31:12.130 00:31:12.140 wrong and you've got a high-pressure
00:31:13.630 00:31:13.640 boiler you can actually get a corrosion
00:31:15.310 00:31:15.320 mechanism called acid phosphate
00:31:16.600 00:31:16.610 corrosion which can be completely
00:31:18.790 00:31:18.800 avoided a few if your phosphate product
00:31:20.980 00:31:20.990 is trisodium phosphate and it's to do
00:31:22.780 00:31:22.790 with the ratio of sodium to phosphate in
00:31:26.320 00:31:26.330 terms of molar ratios and it's a whole
00:31:28.419 00:31:28.429 bunch of jiggery-pokery that goes on
00:31:31.419 00:31:31.429 when you get it wrong and you can end up
00:31:33.190 00:31:33.200 with um causing a corrosion problem by
00:31:35.890 00:31:35.900 correctly dosing the treatment but you
00:31:39.130 00:31:39.140 adding it in there for basically to
00:31:41.290 00:31:41.300 elevate the pH to minimize it ferrous
00:31:43.810 00:31:43.820 ion solubility and also for scale
00:31:46.240 00:31:46.250 control which will which will come to
00:31:48.100 00:31:48.110 next okay
00:31:49.540 00:31:49.550 so we want to we want to make sure we're
00:31:51.070 00:31:51.080 not getting scale forming inside the
00:31:53.080 00:31:53.090 boiler on our heat transfer surfaces so
00:31:55.690 00:31:55.700 what we what we find there's things like
00:31:58.570 00:31:58.580 you know silica the solubility of things
00:32:02.200 00:32:02.210 like silica as well as being changed by
00:32:05.080 00:32:05.090 temperature you can also there's a pH
00:32:06.850 00:32:06.860 influence so if you've got a certain
00:32:09.100 00:32:09.110 amount of silica our prison and your
00:32:10.450 00:32:10.460 boiler if we run at the right pH we
00:32:12.700 00:32:12.710 minimize the risk with it silica
00:32:14.620 00:32:14.630 starting to precipitate if anyone's ever
00:32:17.260 00:32:17.270 dealt with silica once it precipitates
00:32:19.360 00:32:19.370 it's very difficult to remove from a
00:32:21.940 00:32:21.950 surface because it basically it forms a
00:32:24.100 00:32:24.110 slight deposit and you've ever got to
00:32:26.830 00:32:26.840 mechanically remove it you can't
00:32:28.660 00:32:28.670 dissolve it off with most normal acids
00:32:31.870 00:32:31.880 you know hydrochloric acid won't touch
00:32:33.280 00:32:33.290 it citric acid won't touch it
00:32:35.290 00:32:35.300 the only acid that will pick it up is
00:32:36.730 00:32:36.740 hydrofluoric acid which has particular
00:32:40.360 00:32:40.370 health and safety handling
00:32:41.560 00:32:41.570 considerations and you really don't want
00:32:43.180 00:32:43.190 to be you know if you're not comfortable
00:32:44.890 00:32:44.900 with hydrofluoric acid you don't really
00:32:46.480 00:32:46.490 want to be using it and but so you want
00:32:49.000 00:32:49.010 to avoid silica precipitation if you can
00:32:51.040 00:32:51.050 the other thing that terms of scale
00:32:53.410 00:32:53.420 control one of the other things that we
00:32:55.330 00:32:55.340 can do with phosphate is that if we're
00:32:57.250 00:32:57.260 only using a water softener you know we
00:32:59.770 00:32:59.780 will have still some calcium magnesium
00:33:01.930 00:33:01.940 type products that get through into the
00:33:04.000 00:33:04.010 boiler and if we add a bit of phosphate
00:33:06.250 00:33:06.260 we can form calcium magnesium phosphates
00:33:08.799 00:33:08.809 and then these become insoluble but they
00:33:11.980 00:33:11.990 don't form a hard deposit they'll form a
00:33:13.750 00:33:13.760 sludge and it can form to the bottom of
00:33:15.549 00:33:15.559 the boiler and we can blow that out
00:33:16.990 00:33:17.000 using a bottom drain and that's the old
00:33:19.419 00:33:19.429 way that's a steam train way of doing it
00:33:21.310 00:33:21.320 you know they used to
00:33:23.450 00:33:23.460 take the river water from wherever and
00:33:25.460 00:33:25.470 you add the phosphate products in and
00:33:27.590 00:33:27.600 you would complex it up you'd form these
00:33:30.440 00:33:30.450 sludges and then as you're driving along
00:33:32.060 00:33:32.070 and you train you open up the bottom
00:33:33.560 00:33:33.570 drain and you blow that stuff out onto
00:33:35.870 00:33:35.880 the tracks and and it was how you
00:33:37.250 00:33:37.260 cleaned your water out the other way is
00:33:39.560 00:33:39.570 by controlling the boiler cycles so this
00:33:42.139 00:33:42.149 is the water goes into the boiler and
00:33:44.210 00:33:44.220 there's steam forms esteem is more pure
00:33:46.460 00:33:46.470 than the boiler water and these ions get
00:33:49.279 00:33:49.289 left behind in the boiler water and we
00:33:50.870 00:33:50.880 call that cycling up so one of the ways
00:33:53.240 00:33:53.250 that we can minimize that scale is by
00:33:55.430 00:33:55.440 controlling our cycles of concentration
00:33:57.769 00:33:57.779 and increase the amount of blowdown so
00:34:01.519 00:34:01.529 we we start to drain out portion of that
00:34:03.620 00:34:03.630 boiler water and we replace it with
00:34:05.840 00:34:05.850 fresh makeup water so that we're trying
00:34:07.580 00:34:07.590 to hold certain ions and certain
00:34:10.490 00:34:10.500 concentration rains the other way is you
00:34:13.339 00:34:13.349 can use sort of polymer type treatment
00:34:15.800 00:34:15.810 that some of these especially chemicals
00:34:17.570 00:34:17.580 and they operate similar to the
00:34:18.770 00:34:18.780 phosphate they form you know a soluble
00:34:21.919 00:34:21.929 complex that stops that the material
00:34:25.609 00:34:25.619 from from either precipitating or
00:34:27.589 00:34:27.599 forming any kind of posit and then in
00:34:31.099 00:34:31.109 that can be removed for the boiler
00:34:32.780 00:34:32.790 blowdown but these are very specialized
00:34:35.270 00:34:35.280 chemicals and you've got to buy these
00:34:36.500 00:34:36.510 from specialty chemical companies so
00:34:39.230 00:34:39.240 normally if you're getting supplied by
00:34:41.990 00:34:42.000 Elko Salinas or GE water or someone like
00:34:45.230 00:34:45.240 that they would be offering these types
00:34:47.000 00:34:47.010 product what a blow down control there's
00:34:50.899 00:34:50.909 a next one here so we know we
00:34:52.460 00:34:52.470 controlling blow down to try to keep
00:34:55.669 00:34:55.679 things and chicken the boiler and in the
00:34:57.890 00:34:57.900 most common way is there's a it's a
00:35:01.130 00:35:01.140 conductivity sensor which measures as a
00:35:04.940 00:35:04.950 reading as total dissolve solids it's
00:35:06.680 00:35:06.690 just an approximate measurement proper
00:35:08.210 00:35:08.220 total dissolve solids test involves a
00:35:10.160 00:35:10.170 test in the lab and what it does is that
00:35:12.290 00:35:12.300 that has a setpoint value that relates
00:35:14.420 00:35:14.430 to how many cycles you want to run which
00:35:16.160 00:35:16.170 will be calculated based on what make up
00:35:18.200 00:35:18.210 errors for sure you boiler and what your
00:35:21.290 00:35:21.300 what your risk of iron scaling is and
00:35:24.230 00:35:24.240 then that sends a signal to a blowdown
00:35:25.970 00:35:25.980 valve and to say their hits 100 and
00:35:28.160 00:35:28.170 that's it point is 99 then it flow down
00:35:30.079 00:35:30.089 vailable open a little bit and blow some
00:35:32.510 00:35:32.520 of that out and then takes it takes up
00:35:36.230 00:35:36.240 water out the boil
00:35:37.190 00:35:37.200 lowers the total dissolved solids in
00:35:38.839 00:35:38.849 there because it's been what it's been
00:35:40.460 00:35:40.470 replaced by fresh makeup water which is
00:35:43.010 00:35:43.020 hopefully got a lower total dissolved
00:35:44.870 00:35:44.880 solid and in this whole process is
00:35:47.030 00:35:47.040 normally fully automatic so like you
00:35:48.710 00:35:48.720 might buy unit like this from someone
00:35:50.809 00:35:50.819 like Saco or someone like that and it's
00:35:53.480 00:35:53.490 an all-in-one type unit so you it's
00:35:56.329 00:35:56.339 going to make sure that the valves are
00:35:58.430 00:35:58.440 getting blocked up and they're tedious
00:36:00.170 00:36:00.180 sensor is actually reading right and
00:36:01.670 00:36:01.680 that control logic is set correctly
00:36:05.049 00:36:05.059 terms of the next step which is we'll
00:36:07.789 00:36:07.799 just talk about steam so saturated and
00:36:10.039 00:36:10.049 superheated and steam turbine they're
00:36:11.510 00:36:11.520 all basically linked if you're getting
00:36:13.069 00:36:13.079 deep position and one you get into
00:36:14.480 00:36:14.490 position and all of them so what we got
00:36:17.690 00:36:17.700 a what we've got to be concerned with is
00:36:19.490 00:36:19.500 in the in the boiler we have a steam
00:36:22.579 00:36:22.589 drum and then their steam drum which is
00:36:24.380 00:36:24.390 a top of our foster wheel of D type or
00:36:26.480 00:36:26.490 any kind of boiler and it's the same for
00:36:29.210 00:36:29.220 if you can imagine this as your your
00:36:31.099 00:36:31.109 your firetube boiler you have water
00:36:33.829 00:36:33.839 boiling you know you've got a water
00:36:35.990 00:36:36.000 layer and we've got we steam being
00:36:38.030 00:36:38.040 formed here so here the the water steam
00:36:41.120 00:36:41.130 mixture comes in and it goes through a
00:36:42.890 00:36:42.900 scrubber cyclone scrubber which
00:36:44.660 00:36:44.670 separates the water from the steam and
00:36:46.730 00:36:46.740 then we have a secondary scrubber up
00:36:48.559 00:36:48.569 here and the idea of this is it's
00:36:50.630 00:36:50.640 saturated steam is as lower like it's
00:36:53.990 00:36:54.000 entrapped mooster content as possible
00:36:55.819 00:36:55.829 because x-team is quite pure and their
00:36:58.760 00:36:58.770 boiler water has dissolved ions in it so
00:37:01.190 00:37:01.200 if we are having what we call carryover
00:37:03.680 00:37:03.690 where water droplets are getting carried
00:37:06.230 00:37:06.240 through into the steam system as you
00:37:08.870 00:37:08.880 superheat their steam then those those
00:37:11.450 00:37:11.460 ions that are in those water droplets
00:37:13.039 00:37:13.049 will then form deposits very very
00:37:15.740 00:37:15.750 quickly so so the steam drum is a very
00:37:18.680 00:37:18.690 critical thing for a subcritical boiler
00:37:21.589 00:37:21.599 so two-stage separation and we're trying
00:37:24.440 00:37:24.450 to control carryover so if you can
00:37:25.789 00:37:25.799 imagine it's a the the operator gets the
00:37:28.039 00:37:28.049 drum level control wrong and that drum
00:37:30.380 00:37:30.390 level comes up and it actually touches
00:37:32.240 00:37:32.250 the scrubbers and water getting sucked
00:37:34.099 00:37:34.109 through or if these haven't been
00:37:36.440 00:37:36.450 attached properly into the boiler or
00:37:38.059 00:37:38.069 there's a hole or something like that in
00:37:39.770 00:37:39.780 you're going to get suboptimal steam
00:37:41.720 00:37:41.730 chemistry coming out the other side and
00:37:44.780 00:37:44.790 what you need to do here is you should
00:37:46.700 00:37:46.710 be doing periodic what people carry over
00:37:49.039 00:37:49.049 tests and if you go to their eye
00:37:50.990 00:37:51.000 website is actually a test protocol
00:37:53.000 00:37:53.010 available and and what you do is you
00:37:54.980 00:37:54.990 measure sodium and steam versus sodium
00:37:58.070 00:37:58.080 in the boiling water and you can
00:37:59.150 00:37:59.160 calculate the ratio of carryover and
00:38:01.340 00:38:01.350 determine whether you have problem or
00:38:02.810 00:38:02.820 not at your operating pressures so it's
00:38:07.310 00:38:07.320 pretty important because if you get it
00:38:08.900 00:38:08.910 wrong okay you get here here's
00:38:11.450 00:38:11.460 superheated tube and so obviously got a
00:38:13.340 00:38:13.350 bit of a nasty white deposit and this is
00:38:15.410 00:38:15.420 a sodium sulfate the dominant deposit
00:38:19.460 00:38:19.470 here because what was happening in this
00:38:20.900 00:38:20.910 particular plant is there steam drum
00:38:23.870 00:38:23.880 operating level was sick to high during
00:38:26.510 00:38:26.520 commissioning and there was a very high
00:38:29.780 00:38:29.790 level of background carryover where the
00:38:31.790 00:38:31.800 water was being carried over and it
00:38:33.410 00:38:33.420 posited on to those tubes there resulted
00:38:36.140 00:38:36.150 after 18 months operation and
00:38:38.650 00:38:38.660 superheated tube him in such a heavy
00:38:40.730 00:38:40.740 deposit that it overheated and then a
00:38:42.920 00:38:42.930 suffered and what we called a creep
00:38:44.390 00:38:44.400 failure here and that resulted in the
00:38:46.490 00:38:46.500 entire replacement of that super heater
00:38:48.530 00:38:48.540 after 18 months operation so was owner
00:38:51.380 00:38:51.390 wasn't a particularly good day in the
00:38:52.820 00:38:52.830 office
00:38:53.180 00:38:53.190 here's another plant again very heavy
00:38:57.230 00:38:57.240 deposits because a carry over and the
00:38:59.750 00:38:59.760 super heater and they have a small a
00:39:01.730 00:39:01.740 couple of megawatts steam turbine and
00:39:03.830 00:39:03.840 steam turbines are not meant to have
00:39:05.930 00:39:05.940 these white deposits on the middle
00:39:07.520 00:39:07.530 blades and this because of sodium
00:39:09.140 00:39:09.150 sulfate again transported through and
00:39:12.140 00:39:12.150 carried through that particular plant
00:39:14.620 00:39:14.630 came to me and said hey is it normal to
00:39:18.080 00:39:18.090 have these big white crystals coming out
00:39:19.760 00:39:19.770 of our super heater and I had to say to
00:39:21.170 00:39:21.180 them okay Dave I'm just gonna pause you
00:39:26.480 00:39:26.490 for a second here have you got sort of
00:39:29.330 00:39:29.340 some estimated sort of costs as a
00:39:31.730 00:39:31.740 consequence for these sorts of things so
00:39:33.530 00:39:33.540 dis you slide back the super heater you
00:39:36.350 00:39:36.360 know in saying okay they got the
00:39:37.730 00:39:37.740 chemistry wrong you know what sort of
00:39:39.800 00:39:39.810 dollar consequences you're talking about
00:39:41.450 00:39:41.460 thereafter on the eight months that
00:39:45.170 00:39:45.180 particular one the cost to replace it
00:39:47.600 00:39:47.610 super heater was I think in the order of
00:39:50.180 00:39:50.190 about 400 thousand when you took into
00:39:52.310 00:39:52.320 account the costs of the tubes plus it
00:39:56.870 00:39:56.880 cut the old one out well new one and in
00:39:59.510 00:39:59.520 the downtime so this doesn't this isn't
00:40:01.580 00:40:01.590 you know a couple of days this is a
00:40:03.290 00:40:03.300 couple of week outage
00:40:05.570 00:40:05.580 another one that I know of which was
00:40:07.760 00:40:07.770 after nine years of operation it was a
00:40:09.740 00:40:09.750 million dollars to replace the super
00:40:12.860 00:40:12.870 heater so these these things can be
00:40:14.660 00:40:14.670 pretty high cost for it could be avoided
00:40:18.350 00:40:18.360 by just some very simple and very low
00:40:21.020 00:40:21.030 cost operational activities to make sure
00:40:23.780 00:40:23.790 they're a your steam is the right purity
00:40:26.450 00:40:26.460 and you don't have the carryover
00:40:27.770 00:40:27.780 occurring so cost of failure is often
00:40:30.440 00:40:30.450 very very high yeah so so ballpark
00:40:33.260 00:40:33.270 figure you're saying saying 800 K to a
00:40:35.120 00:40:35.130 million in terms of the failure repair
00:40:37.040 00:40:37.050 bill versus the annual optics expense of
00:40:40.220 00:40:40.230 getting it right to avoid it you're
00:40:43.760 00:40:43.770 probably talking a few thousand dollars
00:40:45.110 00:40:45.120 yeah okay yep now great so you're just
00:40:48.740 00:40:48.750 trying to put this into perspective for
00:40:50.690 00:40:50.700 everyone so no great thank you for that
00:40:52.100 00:40:52.110 so you know it's it's it's good to sort
00:40:54.470 00:40:54.480 of recognize that yeah it's not even an
00:40:57.590 00:40:57.600 IRR calculation as what you're saying in
00:40:59.840 00:40:59.850 terms of getting your procedures right
00:41:04.270 00:41:04.280 yeah and the other one is if you've got
00:41:07.160 00:41:07.170 even a small steam turbine like steam
00:41:10.400 00:41:10.410 turbine Europe is a very expensive you
00:41:13.310 00:41:13.320 know it's um
00:41:14.240 00:41:14.250 you don't even even a one or two
00:41:15.830 00:41:15.840 megawatt pressure turbine often if
00:41:19.610 00:41:19.620 you've had a deposit and it's resulted
00:41:22.010 00:41:22.020 in some corrosion damage on that turbine
00:41:23.930 00:41:23.940 often they can't be repaired in New
00:41:25.850 00:41:25.860 Zealand they have to be shut off sure
00:41:27.530 00:41:27.540 bit to the turbine OEM for re machining
00:41:30.950 00:41:30.960 and blade replacements of things like
00:41:32.840 00:41:32.850 that so it's you've got the cost of
00:41:35.770 00:41:35.780 appear but then you've also got the lost
00:41:38.090 00:41:38.100 opportunity cost because you might have
00:41:39.620 00:41:39.630 been offset in your electricity bill by
00:41:42.530 00:41:42.540 running that turbine or you may have
00:41:44.090 00:41:44.100 actually been exporting to the grid
00:41:45.410 00:41:45.420 making a bit of money on the side as
00:41:47.180 00:41:47.190 well so that these you want to avoid
00:41:49.880 00:41:49.890 these types of problems if you know
00:41:51.680 00:41:51.690 that's great thanks very much all right
00:41:54.250 00:41:54.260 all right so the other one that's a big
00:41:57.170 00:41:57.180 problem in industrial plants is
00:41:58.640 00:41:58.650 condensate purity condensate return
00:42:01.310 00:42:01.320 purity control and and and this is this
00:42:04.010 00:42:04.020 is a real major one because say you're
00:42:06.020 00:42:06.030 producing steam for saying or a refinery
00:42:08.750 00:42:08.760 right in hydrocarbon return coming back
00:42:11.720 00:42:11.730 you're a dairy factory site like
00:42:14.240 00:42:14.250 Fonterra or some of the other ones you
00:42:15.590 00:42:15.600 get mobile products coming back if your
00:42:18.170 00:42:18.180 salt proceeds implant you know you may
00:42:20.810 00:42:20.820 get brine or something like that or
00:42:22.340 00:42:22.350 basically it could be anything so if
00:42:25.040 00:42:25.050 even if your some of your your steam is
00:42:27.170 00:42:27.180 consumed in your process you want to
00:42:29.390 00:42:29.400 make sure that whatever is coming back
00:42:31.490 00:42:31.500 then your condensate before you put it
00:42:33.410 00:42:33.420 back into the boiler that it's it's
00:42:35.000 00:42:35.010 meeting specification as you know you
00:42:40.100 00:42:40.110 want it to be you don't want to be
00:42:41.720 00:42:41.730 spending all this time and effort making
00:42:43.310 00:42:43.320 good quality makeup water to find that
00:42:45.500 00:42:45.510 your condensate is highly terminated
00:42:47.720 00:42:47.730 when it comes back so you know it could
00:42:49.940 00:42:49.950 be anything
00:42:50.540 00:42:50.550 milk salts hydrocarbons could be your
00:42:52.580 00:42:52.590 cooling water and normally what you have
00:42:55.010 00:42:55.020 to have as some means of contamination
00:42:57.080 00:42:57.090 detect and normally online so it might
00:42:59.870 00:42:59.880 be that you have a conductivity meter
00:43:01.460 00:43:01.470 and you know that if your condensate
00:43:03.830 00:43:03.840 it's clean that or have a conductivity
00:43:05.330 00:43:05.340 of X and you need a VA ssin of there is
00:43:09.620 00:43:09.630 telling you that it's problem you might
00:43:11.600 00:43:11.610 use a sodium or you could use your
00:43:13.130 00:43:13.140 silica and normally what we find is most
00:43:15.230 00:43:15.240 plants will normally have some kind of
00:43:17.090 00:43:17.100 automatic condensate dumping system that
00:43:19.790 00:43:19.800 it picks up the problem and says I'm
00:43:22.190 00:43:22.200 gonna dump that condensate it doesn't
00:43:24.140 00:43:24.150 not good enough to come back to the
00:43:25.520 00:43:25.530 boiler it may go to a holding tank will
00:43:27.290 00:43:27.300 be will be reprocessed somehow because
00:43:30.740 00:43:30.750 often if you're doing you're waiting for
00:43:32.840 00:43:32.850 the operator they may not pick it up and
00:43:35.060 00:43:35.070 the damage can be done very very quickly
00:43:36.740 00:43:36.750 so the other thing that may be required
00:43:39.170 00:43:39.180 is you may have to have a what they call
00:43:40.730 00:43:40.740 a condensate polisher which is it's a
00:43:43.160 00:43:43.170 condensate comes back to the plant to
00:43:45.230 00:43:45.240 the cogent plan or the boiler house it's
00:43:47.960 00:43:47.970 it goes through an additional water
00:43:50.090 00:43:50.100 treatment stick to remove any new
00:43:52.130 00:43:52.140 process contamination that as it goes
00:43:55.370 00:43:55.380 through so you know the big power plants
00:43:57.470 00:43:57.480 like Huntley units they all had
00:43:59.090 00:43:59.100 condensate polishes and that was to
00:44:00.530 00:44:00.540 protect the case primary heat exchangers
00:44:02.600 00:44:02.610 had a leak and we had white cat a river
00:44:05.060 00:44:05.070 water getting into the boiler feedwater
00:44:07.490 00:44:07.500 so we could protect boilers from there
00:44:09.590 00:44:09.600 and any systems often look like this you
00:44:12.620 00:44:12.630 you've got your condensate return coming
00:44:14.840 00:44:14.850 through here is a is a conductivity
00:44:18.170 00:44:18.180 sensor or some sensor of some type on a
00:44:20.930 00:44:20.940 bypass line here that's got a flow going
00:44:22.910 00:44:22.920 a drain it's got a controller and you've
00:44:25.160 00:44:25.170 got a you know you've got a valve here
00:44:27.830 00:44:27.840 that's either letting the condensate go
00:44:29.480 00:44:29.490 through or that valve
00:44:30.830 00:44:30.840 changes
00:44:31.760 00:44:31.770 rushon and it will dump it contaminated
00:44:33.920 00:44:33.930 on site to waste the often a lot of
00:44:36.650 00:44:36.660 plants will have some system where you
00:44:39.350 00:44:39.360 can perhaps through 100% condensate dump
00:44:42.110 00:44:42.120 in for a few hours because then you
00:44:44.570 00:44:44.580 start to run out of water because you
00:44:46.190 00:44:46.200 exceed in the make up capacity of your
00:44:48.380 00:44:48.390 water treatment plant and normally
00:44:50.270 00:44:50.280 that's enough to say identify we're in
00:44:52.460 00:44:52.470 your plant the process determined there
00:44:54.290 00:44:54.300 might be a heat exchanger or something's
00:44:55.820 00:44:55.830 gone wrong
00:44:56.510 00:44:56.520 it's to buy you time to go and fix the
00:44:58.670 00:44:58.680 problem or isolate that part of the
00:45:00.320 00:45:00.330 plant and then a condensate coming back
00:45:03.110 00:45:03.120 we're clean condensate coming back to
00:45:05.270 00:45:05.280 the plant going so pretty common to have
00:45:08.510 00:45:08.520 a condensate return dump type system
00:45:10.780 00:45:10.790 alright so the next one sampling and
00:45:14.210 00:45:14.220 analysis you know basically you can't
00:45:17.240 00:45:17.250 control what you can't measure and you
00:45:19.430 00:45:19.440 know I'm a I'm a I'm a big advocate of
00:45:23.090 00:45:23.100 versus their automatic online systems
00:45:25.640 00:45:25.650 food over manual grab sampling systems
00:45:28.010 00:45:28.020 but we do acknowledge that costs and
00:45:30.230 00:45:30.240 complexity is potentially very high for
00:45:32.420 00:45:32.430 small plants that the problem is is you
00:45:34.910 00:45:34.920 have a big thousand megawatt boiler you
00:45:38.120 00:45:38.130 got to put some online instruments on it
00:45:39.800 00:45:39.810 the cost is exactly the same for a one
00:45:42.620 00:45:42.630 megawatt boiler there's no you really
00:45:44.720 00:45:44.730 economy a scale here so I call this the
00:45:46.970 00:45:46.980 cursor cogent where you have all the
00:45:49.580 00:45:49.590 problems of the big plants but your
00:45:51.230 00:45:51.240 budgets are a lot smaller so you have to
00:45:53.390 00:45:53.400 be you know be pragmatic and say what
00:45:55.280 00:45:55.290 you absolutely need is it gonna generate
00:45:58.040 00:45:58.050 me some value is it gonna protect me
00:46:00.770 00:46:00.780 from a very high cost type problem or is
00:46:04.670 00:46:04.680 it just a nice to have so what we
00:46:07.520 00:46:07.530 normally find for industrial boilers
00:46:09.110 00:46:09.120 that there is no online some analysis
00:46:11.000 00:46:11.010 systems except for maybe boiler blowdown
00:46:12.920 00:46:12.930 control or maybe some kind of con and
00:46:15.530 00:46:15.540 say condensate dump look on a site you
00:46:19.010 00:46:19.020 know I say dumping system but what I can
00:46:21.500 00:46:21.510 point you to is you know there's an IX
00:46:23.150 00:46:23.160 guideline for instrumentation that you
00:46:25.040 00:46:25.050 can kind of use as your starting point
00:46:26.870 00:46:26.880 to say here's here's what we recommend
00:46:29.330 00:46:29.340 for the big plants and there's also
00:46:31.640 00:46:31.650 layers of redundancy built into there
00:46:33.470 00:46:33.480 can I can I kind of pick and mix out of
00:46:36.830 00:46:36.840 here is something that what's going to
00:46:38.330 00:46:38.340 give me my best bang for my buck and you
00:46:40.550 00:46:40.560 can go from there so just looking at
00:46:42.410 00:46:42.420 these slides here you know
00:46:44.539 00:46:44.549 on a second discharge would be equal
00:46:46.549 00:46:46.559 oven to condensate return and and we
00:46:48.769 00:46:48.779 would be measuring conductivity after
00:46:50.569 00:46:50.579 cation exchange which is a means of the
00:46:52.249 00:46:52.259 ticketing contamination could be
00:46:54.049 00:46:54.059 measuring dissolved oxygen or could be
00:46:55.549 00:46:55.559 measuring sodium and B cases gas
00:46:58.370 00:46:58.380 conductivity after cation exchange you
00:47:00.739 00:47:00.749 know and you might say look out of all
00:47:02.359 00:47:02.369 of those you know sodium is my biggest
00:47:04.789 00:47:04.799 risk that tells me a whole bunch of
00:47:06.289 00:47:06.299 information about if I've got a process
00:47:07.819 00:47:07.829 up C maybe I'll just put that in there
00:47:10.099 00:47:10.109 you know and we go through this list is
00:47:12.169 00:47:12.179 a whole I don't I'm not going to go
00:47:13.160 00:47:13.170 through it detailed it gives you some
00:47:14.900 00:47:14.910 some guidance around what what you could
00:47:17.749 00:47:17.759 do and then you know you go through a
00:47:19.789 00:47:19.799 risk basis cost based you know what's
00:47:23.449 00:47:23.459 practical and impossible and way that up
00:47:26.569 00:47:26.579 against you know if I take a sample once
00:47:28.579 00:47:28.589 a day the operator does a grab sample
00:47:30.499 00:47:30.509 and does a test is it going to provide
00:47:32.479 00:47:32.489 me adequate warning of a major major
00:47:34.999 00:47:35.009 process upset or a major plan upset the
00:47:38.359 00:47:38.369 problem that we find is that often if
00:47:40.130 00:47:40.140 people are doing you know one test shift
00:47:41.929 00:47:41.939 and you say to them take that test and
00:47:44.359 00:47:44.369 if it's out of spec what do you do and
00:47:46.189 00:47:46.199 normally they go or well I assume that
00:47:48.799 00:47:48.809 the test was wrong so I do it again
00:47:50.329 00:47:50.339 tomorrow and if it's the same tomorrow
00:47:52.579 00:47:52.589 then I assume there's something wrong
00:47:54.079 00:47:54.089 then and you're going like that's great
00:47:55.339 00:47:55.349 now you've been out of control for
00:47:56.719 00:47:56.729 perhaps two days okay where if you had
00:47:59.390 00:47:59.400 an on line instrument and you could see
00:48:00.859 00:48:00.869 a trend you could see there it's
00:48:02.449 00:48:02.459 starting to trend up and it's been like
00:48:05.329 00:48:05.339 that for a little while so you need to
00:48:07.249 00:48:07.259 do something about it right away so
00:48:09.009 00:48:09.019 there's this pros and cons to online and
00:48:12.579 00:48:12.589 offline analysis so again there's a
00:48:15.949 00:48:15.959 whole lot of stuff in those ayats
00:48:17.739 00:48:17.749 guidance documents so if you're thinking
00:48:19.759 00:48:19.769 about have you got the right
00:48:20.959 00:48:20.969 instrumentation from your plant on
00:48:22.549 00:48:22.559 encourage you to get the free download
00:48:24.620 00:48:24.630 every bit of a read and a thinkin and
00:48:26.900 00:48:26.910 then you know ask around and you know
00:48:29.569 00:48:29.579 get some advice on what you need all
00:48:32.929 00:48:32.939 right so
00:48:33.940 00:48:33.950 so today I'm gonna just pause you there
00:48:37.240 00:48:37.250 for a second obviously a key topic and
00:48:40.560 00:48:40.570 hopefully people will go and read but
00:48:43.240 00:48:43.250 for those that are just looking for the
00:48:45.670 00:48:45.680 helicopter view today in all your
00:48:48.760 00:48:48.770 experience is there one or two critical
00:48:51.370 00:48:51.380 things for a typical industrial process
00:48:53.620 00:48:53.630 heat boiler that you'd summarize and say
00:48:57.010 00:48:57.020 hey look these are the things that you
00:48:59.070 00:48:59.080 you should really look at so say for
00:49:01.240 00:49:01.250 example someone's seen the presentation
00:49:03.280 00:49:03.290 today grabs a few of the slides to scare
00:49:05.650 00:49:05.660 the bejeebies out of their boss to say
00:49:07.900 00:49:07.910 hey look holy cow we can't afford this
00:49:09.760 00:49:09.770 sort of expense and so maybe they can
00:49:11.710 00:49:11.720 get a little bit of money out of the
00:49:12.940 00:49:12.950 stone you know there's only so much
00:49:15.640 00:49:15.650 blood in the stone so you know could you
00:49:17.710 00:49:17.720 give any real I appreciate it sort of
00:49:20.050 00:49:20.060 all care and no responsibility because
00:49:21.880 00:49:21.890 it's very specific to each application
00:49:23.980 00:49:23.990 but in general terms even have it some
00:49:26.800 00:49:26.810 real simple basic aid that really good
00:49:29.020 00:49:29.030 pointers where to get started there's a
00:49:31.390 00:49:31.400 take home for everyone well first for
00:49:34.960 00:49:34.970 most of you if your you need something
00:49:38.530 00:49:38.540 on your condensate return for efforts
00:49:41.050 00:49:41.060 interacting with the process so and if
00:49:43.570 00:49:43.580 you've got a heat exchanger where the
00:49:46.859 00:49:46.869 the steam or the condensate then a lower
00:49:49.960 00:49:49.970 pressure than the process so if you
00:49:52.300 00:49:52.310 could leak back and that's milk or
00:49:55.540 00:49:55.550 hydrocarbon or sea water or something
00:49:58.780 00:49:58.790 like that in you need you need some kind
00:50:00.910 00:50:00.920 of condensate return contamination
00:50:03.250 00:50:03.260 detection and conductivity mean it would
00:50:04.870 00:50:04.880 probably be simple it's the most basic
00:50:07.060 00:50:07.070 one if you have a super heater on your
00:50:10.510 00:50:10.520 plant at a bare minimum you need a
00:50:13.480 00:50:13.490 sample point which has a sample cooler
00:50:16.090 00:50:16.100 so that you can at least get a grab
00:50:18.070 00:50:18.080 sample through the Cariocas and we've
00:50:20.620 00:50:20.630 seen a few plants built in New Zealand
00:50:22.630 00:50:22.640 where have super heaters but they never
00:50:25.570 00:50:25.580 actually had a sample point stall okay
00:50:28.930 00:50:28.940 so that they couldn't even do a
00:50:31.599 00:50:31.609 carryover test they wanted to you know
00:50:35.500 00:50:35.510 and that's resulted in all kinds of
00:50:37.090 00:50:37.100 problems and the boiler itself obviously
00:50:39.550 00:50:39.560 if you've got automatic blowdown
00:50:41.349 00:50:41.359 controlled will be a conductivity or a
00:50:43.510 00:50:43.520 TDS controller and their I would
00:50:46.390 00:50:46.400 recommend pH
00:50:47.720 00:50:47.730 on the boiler as well so but for ph
00:50:50.210 00:50:50.220 you've got to have a sample point which
00:50:52.010 00:50:52.020 has a sample caller to bring the
00:50:53.450 00:50:53.460 temperature down if you've got a dear
00:50:57.470 00:50:57.480 rater
00:50:57.920 00:50:57.930 you know having a dissolved oxygen
00:51:00.080 00:51:00.090 analyzer on the outlet of that as well
00:51:02.210 00:51:02.220 is quite useful and often a pH meter on
00:51:06.260 00:51:06.270 your feed water so again if you see an
00:51:08.150 00:51:08.160 ammonia or you're trying to get at pH
00:51:11.210 00:51:11.220 nine point eight to ten and your feed
00:51:12.920 00:51:12.930 water actually being able to verify that
00:51:14.750 00:51:14.760 with a two meter it's very helpful and
00:51:17.090 00:51:17.100 then it also means that you can set up
00:51:18.800 00:51:18.810 automatic control loops where you have a
00:51:20.750 00:51:20.760 pump controlling to a set point which
00:51:22.940 00:51:22.950 lowers your you know manual operator
00:51:25.220 00:51:25.230 intervention and things like that and
00:51:26.930 00:51:26.940 that would probably be would be my
00:51:29.210 00:51:29.220 minimum recommendation there all right
00:51:33.140 00:51:33.150 so the last one here on the list and
00:51:35.150 00:51:35.160 hopefully we're going to be on time
00:51:36.410 00:51:36.420 there's a layup and storage so say you
00:51:38.030 00:51:38.040 got everything absolutely perfect with
00:51:39.830 00:51:39.840 fuel and we find this actually out there
00:51:41.630 00:51:41.640 in the world people have all their
00:51:43.040 00:51:43.050 operating chemistry pretty spot-on and
00:51:45.710 00:51:45.720 and they plot they run their plants
00:51:47.090 00:51:47.100 really well but when they shut them down
00:51:49.720 00:51:49.730 everything corrodes and they have all
00:51:51.680 00:51:51.690 the problems start from the from that
00:51:53.150 00:51:53.160 from the offline environment and this is
00:51:54.800 00:51:54.810 quite Hooten that you know off
00:51:56.240 00:51:56.250 especially Fonterra plants or plants
00:51:58.250 00:51:58.260 that have a seasonal operational type
00:51:59.990 00:52:00.000 mode where they might be shut down for a
00:52:01.430 00:52:01.440 few months so what we get is loyalist
00:52:03.680 00:52:03.690 and by corrosion where we get unwanted
00:52:05.540 00:52:05.550 formation of non particular iron oxides
00:52:07.400 00:52:07.410 which is rust so here we have a boiler
00:52:10.099 00:52:10.109 heat recovery steam generator steam drum
00:52:12.170 00:52:12.180 and Australia it's been shut down for an
00:52:13.670 00:52:13.680 outage and they didn't get all the water
00:52:15.170 00:52:15.180 out and you can see here is a water
00:52:17.030 00:52:17.040 sitting here on the vessel and
00:52:18.500 00:52:18.510 straightaway you can see it's rusting
00:52:20.420 00:52:20.430 away and it's actually has in a way
00:52:21.920 00:52:21.930 under there because water is now a
00:52:23.960 00:52:23.970 hundred percent oxygen saturated and
00:52:26.750 00:52:26.760 over time you know the pH goes down and
00:52:29.540 00:52:29.550 away you go and this is me doing a
00:52:31.250 00:52:31.260 boiler inspection and we're marking out
00:52:33.020 00:52:33.030 things that we're finding and there
00:52:34.700 00:52:34.710 further for the plan owner taking photos
00:52:37.160 00:52:37.170 and going back to them and telling them
00:52:38.750 00:52:38.760 that it's it's not right and basically
00:52:40.940 00:52:40.950 if you've got an environment which is
00:52:42.800 00:52:42.810 you've got higher than thirty percent
00:52:44.120 00:52:44.130 relative humidity then you're going to
00:52:46.790 00:52:46.800 have offline corrosion and it's often
00:52:48.950 00:52:48.960 ignored in the gleek people just shut
00:52:50.599 00:52:50.609 their plants down and just turn it off
00:52:51.980 00:52:51.990 and say alright we're not running it for
00:52:53.480 00:52:53.490 a month we'll just walk away and and if
00:52:56.330 00:52:56.340 you in reserve all you're the backup
00:52:58.609 00:52:58.619 boiler or you're starting and shutting
00:53:00.800 00:53:00.810 down
00:53:01.120 00:53:01.130 a lot this is this is really where you
00:53:02.950 00:53:02.960 get a lot of problems and it's
00:53:04.059 00:53:04.069 absolutely critical for steam turbines
00:53:05.950 00:53:05.960 as well especially if you've got
00:53:07.329 00:53:07.339 seasonal operation on a little steam
00:53:09.039 00:53:09.049 turbine sit there the rest of the time
00:53:11.710 00:53:11.720 so we see problems like this and you can
00:53:14.019 00:53:14.029 see here where there was a puddle of
00:53:15.549 00:53:15.559 water and it's caused some corrosion and
00:53:17.589 00:53:17.599 then it's finally all evaporated away
00:53:19.120 00:53:19.130 but what happens is when that plant
00:53:20.799 00:53:20.809 starts up it oxide is NaN particular and
00:53:23.259 00:53:23.269 it just washes off and then it
00:53:24.880 00:53:24.890 transports through and will cause some
00:53:26.799 00:53:26.809 problems elsewhere in the plant so why
00:53:30.220 00:53:30.230 we wonder what are we interested in here
00:53:31.900 00:53:31.910 is his thing called the Vern on curve
00:53:33.759 00:53:33.769 it's from mr. Vernon back in 1935 and
00:53:36.609 00:53:36.619 this explains why things rust and the
00:53:38.650 00:53:38.660 jungle and is it so corrosion rate here
00:53:41.950 00:53:41.960 humidity B is for carbon steel where
00:53:44.049 00:53:44.059 100% humidity and the oxygen saturated
00:53:47.170 00:53:47.180 conditions we have very high corrosion
00:53:48.759 00:53:48.769 rates as we get drier and drier and
00:53:50.799 00:53:50.809 drier basically when we get down to less
00:53:53.259 00:53:53.269 than 30% the corrosion rate goes to zero
00:53:55.630 00:53:55.640 so if you've got a boiler and you say I
00:53:58.630 00:53:58.640 don't need to run it for six months or
00:54:00.460 00:54:00.470 I'm shutting it down we would recommend
00:54:02.349 00:54:02.359 that you you blow it on hot you get all
00:54:04.839 00:54:04.849 that water out and then you either use
00:54:06.789 00:54:06.799 something like instrument air or you get
00:54:08.740 00:54:08.750 a tuba or you get a dehumidification
00:54:10.809 00:54:10.819 system in there and you dry it out and
00:54:13.269 00:54:13.279 you try and get the internal environment
00:54:15.069 00:54:15.079 of all the water touch surfaces down
00:54:17.109 00:54:17.119 below 30 percent relative humidity and
00:54:19.539 00:54:19.549 basically you can say that boiler is now
00:54:21.609 00:54:21.619 in suspended animation then there should
00:54:23.349 00:54:23.359 be no corrosion occurring okay and a
00:54:26.099 00:54:26.109 dehumidifier is normally months as
00:54:29.470 00:54:29.480 dryers but they look like on the inside
00:54:31.269 00:54:31.279 you have a self-regenerating discont
00:54:33.730 00:54:33.740 wheel okay so we're we bring in you know
00:54:38.130 00:54:38.140 humid air comes in gets dried through
00:54:41.289 00:54:41.299 that desiccant comes out goes into the
00:54:43.359 00:54:43.369 process and then there's DISA can't we
00:54:45.400 00:54:45.410 or turns it's got an air heater it's
00:54:47.890 00:54:47.900 it's it's driving the moisture out of
00:54:49.960 00:54:49.970 the desiccant which has been ejected and
00:54:51.670 00:54:51.680 then it's been continuously regenerated
00:54:53.200 00:54:53.210 and continues to be dry and in a
00:54:56.049 00:54:56.059 properly sized unit will produce five
00:54:58.720 00:54:58.730 percent relative humidity and it's one
00:55:01.089 00:55:01.099 of these things that you you hook it up
00:55:02.740 00:55:02.750 to your boiler you know you drain the
00:55:05.319 00:55:05.329 boiler down you hook this up and you
00:55:06.789 00:55:06.799 know you're putting five percent
00:55:07.900 00:55:07.910 relative humidity at one end and you
00:55:09.789 00:55:09.799 boil through the boiler you have a flow
00:55:11.289 00:55:11.299 path set up and you measure the humidity
00:55:12.880 00:55:12.890 coming out the other end and if
00:55:15.010 00:55:15.020 it might be like 60% on day one and you
00:55:17.290 00:55:17.300 blow that here through and it might be
00:55:18.700 00:55:18.710 30% on day two and then it might be 2%
00:55:21.580 00:55:21.590 on day three and then you hand on your
00:55:23.860 00:55:23.870 heart and say you know it's weathers now
00:55:26.080 00:55:26.090 dry and it's in a particular state so
00:55:28.540 00:55:28.550 this is really a lot of problems I see
00:55:31.750 00:55:31.760 around the world is due to poor layup
00:55:34.120 00:55:34.130 and storage you know where people have
00:55:37.210 00:55:37.220 have initiated a whole bunch of
00:55:39.340 00:55:39.350 corrosion problems because of the way
00:55:41.020 00:55:41.030 they've stored the plant and things like
00:55:43.060 00:55:43.070 if you get pets in certain locations
00:55:45.730 00:55:45.740 they put you know eventually it'll cause
00:55:47.620 00:55:47.630 a through wall failure on its own and
00:55:50.020 00:55:50.030 it's a problem but the problem is is
00:55:51.550 00:55:51.560 you've created an irregularity in the
00:55:53.230 00:55:53.240 surface and there's a whole secondary
00:55:56.200 00:55:56.210 bunch of corrosion problems that occur
00:55:58.030 00:55:58.040 because you get cracks and been formed
00:56:00.820 00:56:00.830 from the pit when you put the plant in
00:56:02.530 00:56:02.540 service when you come up the temperature
00:56:04.600 00:56:04.610 and pressure their stress is applied to
00:56:06.190 00:56:06.200 the plant you can get these things with
00:56:08.170 00:56:08.180 stress corrosion cracking and in
00:56:11.110 00:56:11.120 corrosion fatigue particularly in
00:56:12.880 00:56:12.890 turbines and super heaters and you know
00:56:15.930 00:56:15.940 heat exchangers they've got some kind of
00:56:18.400 00:56:18.410 tensile stress on them so something need
00:56:21.430 00:56:21.440 to watch out for all right and no so
00:56:24.340 00:56:24.350 we've got to the we've pretty much got
00:56:26.140 00:56:26.150 to the end and I know there's been a bit
00:56:27.730 00:56:27.740 of a roller coaster ride and and we're
00:56:31.570 00:56:31.580 going to do some more on the corrosion
00:56:33.250 00:56:33.260 mechanisms and the next one but
00:56:34.900 00:56:34.910 basically the in summary the cycle
00:56:37.720 00:56:37.730 chemistry goal was minimize corrosion
00:56:39.400 00:56:39.410 and deep position and it's a very
00:56:41.020 00:56:41.030 complex area science and no I don't say
00:56:43.330 00:56:43.340 eliminate as we can never quite fully
00:56:45.490 00:56:45.500 eliminate it so we always try and
00:56:47.010 00:56:47.020 control it and bring it to a minimum
00:56:49.290 00:56:49.300 there's a lot of misinformation and
00:56:52.120 00:56:52.130 confusion out there and I blame the
00:56:53.710 00:56:53.720 steam train for there and also some of
00:56:55.390 00:56:55.400 it comes into what's right for one
00:56:58.420 00:56:58.430 design and pressure of oiler is not
00:57:00.490 00:57:00.500 necessarily right for another you know
00:57:03.160 00:57:03.170 so you've got to understand the cycle
00:57:04.600 00:57:04.610 and I recommend use a guideline and best
00:57:07.690 00:57:07.700 practice current you know take a free
00:57:09.730 00:57:09.740 one from my app so you can look at
00:57:11.320 00:57:11.330 purchasing here's me one and things like
00:57:12.970 00:57:12.980 that and and you need to consider the
00:57:15.190 00:57:15.200 whole cycle by doing one thing in one
00:57:17.290 00:57:17.300 location are you creating another
00:57:19.240 00:57:19.250 problem through the down the path you
00:57:20.980 00:57:20.990 know you might say hey I'm gonna dose
00:57:22.930 00:57:22.940 ammonia because I heard that's really
00:57:24.760 00:57:24.770 good for my feed water and it goes off
00:57:27.250 00:57:27.260 and you realize you've now contaminate
00:57:28.960 00:57:28.970 your your very expensive product you're
00:57:31.450 00:57:31.460 making and now you can't export that so
00:57:33.550 00:57:33.560 you've got any changes to your chemistry
00:57:36.190 00:57:36.200 especially for any plant that's
00:57:37.750 00:57:37.760 producing food or pharmaceuticals or
00:57:40.120 00:57:40.130 something like that you go through that
00:57:42.070 00:57:42.080 risk type analysis process through a
00:57:44.320 00:57:44.330 heads up and say am i by creating a
00:57:46.480 00:57:46.490 bigger problem by doing this or a zero
00:57:48.099 00:57:48.109 is there a better way of things like
00:57:50.170 00:57:50.180 that so there's a some additional
00:57:52.630 00:57:52.640 information I've pointed this one out
00:57:54.250 00:57:54.260 the IEPs - guidance document there is
00:57:56.680 00:57:56.690 actually a journal for power plant
00:57:58.690 00:57:58.700 chemistry which covers a lot of stuff
00:58:00.910 00:58:00.920 around industrial boilers so you know
00:58:02.890 00:58:02.900 that's got a chem net a cup an
00:58:06.460 00:58:06.470 electronic subscription and they have a
00:58:07.960 00:58:07.970 few papers and and things like that
00:58:09.880 00:58:09.890 available you can drop me a line as well
00:58:12.849 00:58:12.859 and I can probably send you a few bits
00:58:14.560 00:58:14.570 and pieces and then just James want to
00:58:18.040 00:58:18.050 do the last but here for what's coming
00:58:20.530 00:58:20.540 up next
00:58:21.130 00:58:21.140 okay so thanks very much Dave now just
00:58:24.760 00:58:24.770 before I get into this just a quick note
00:58:26.560 00:58:26.570 sort of that sort of concludes Dave's
00:58:28.270 00:58:28.280 presentation today and on behalf of
00:58:30.040 00:58:30.050 everyone thanks very much today was very
00:58:31.510 00:58:31.520 informative and obviously if you've got
00:58:34.630 00:58:34.640 the issues feel free to or questions you
00:58:36.400 00:58:36.410 can email them through we will stay on
00:58:38.440 00:58:38.450 the line for a few minutes now if anyone
00:58:40.750 00:58:40.760 wants to fire through questions through
00:58:42.430 00:58:42.440 the question portal you can just punch
00:58:45.460 00:58:45.470 in your question and if you have miked
00:58:47.109 00:58:47.119 up we'll we'll try and get you on line
00:58:50.710 00:58:50.720 otherwise we'll try and address your
00:58:52.210 00:58:52.220 question either way just as any of you
00:58:55.150 00:58:55.160 might be thinking about putting a
00:58:56.320 00:58:56.330 question in just a reminder here that
00:58:58.120 00:58:58.130 we've got some webinars coming up I do
00:59:01.000 00:59:01.010 apologize this seems to be a bit of
00:59:03.130 00:59:03.140 confusion but the next webinar actually
00:59:05.500 00:59:05.510 until which time is going to be on vs DS
00:59:07.210 00:59:07.220 it's with myself the week of the 30th of
00:59:10.450 00:59:10.460 March were actually having a break
00:59:12.820 00:59:12.830 around the Easter holiday period just in
00:59:16.300 00:59:16.310 recognition there's lots of people going
00:59:18.820 00:59:18.830 to and to-and-fro bit of time off etc so
00:59:21.970 00:59:21.980 there won't be a web another week of the
00:59:24.070 00:59:24.080 30th so the following webinar will be
00:59:25.930 00:59:25.940 the April the 6th on refrigeration
00:59:28.450 00:59:28.460 process calling and then April 20th on
00:59:32.710 00:59:32.720 mass and energy mapping for process heat
00:59:34.510 00:59:34.520 systems so getting into the meat and in
00:59:38.079 00:59:38.089 terms of how we need to address
00:59:41.500 00:59:41.510 getting optimization in our process
00:59:43.750 00:59:43.760 heating and cooling systems so yeah so
00:59:46.660 00:59:46.670 on that note really I guess that's the
00:59:49.630 00:59:49.640 webinars coming up and there's been a
00:59:51.370 00:59:51.380 couple of people commenting today are
00:59:54.520 00:59:54.530 asking questions and just to reaffirm
00:59:55.930 00:59:55.940 that the presentation today the audio in
00:59:58.960 00:59:58.970 slides will be available as per the
01:00:01.410 01:00:01.420 YouTube channel that Iike has set up
01:00:04.330 01:00:04.340 that can be accessed from their website
01:00:06.010 01:00:06.020 now for those that can't access YouTube
01:00:09.420 01:00:09.430 Iike has set up a Dropbox we're just
01:00:12.940 01:00:12.950 sort of working through the font of
01:00:13.990 01:00:14.000 details of that but if you're looking
01:00:16.060 01:00:16.070 for that information you can email me at
01:00:19.020 01:00:19.030 James in Waikato today cidade in Zedd
01:00:22.620 01:00:22.630 for more details if you need that so say
01:00:26.500 01:00:26.510 yes so just a reminder yes the slides
01:00:28.120 01:00:28.130 are available along with the slides and
01:00:31.540 01:00:31.550 presentations from the previous webinars
01:00:33.190 01:00:33.200 for review for yourselves or to be able
01:00:36.880 01:00:36.890 to share with your team or your boss to
01:00:38.650 01:00:38.660 say hey look we need to look at this you
01:00:41.370 01:00:41.380 know you might just be able to go to a
01:00:43.630 01:00:43.640 certain part and you can you can show
01:00:45.700 01:00:45.710 that so so yes so on that note we're
01:00:49.680 01:00:49.690 happy to carry on we've just had a
01:00:54.400 01:00:54.410 question Dave let's come through from /
01:00:57.490 01:00:57.500 mesh how common is online dissolved
01:01:00.760 01:01:00.770 oxygen monitoring and blowdown control
01:01:02.830 01:01:02.840 in the industry you mentioned it's
01:01:05.290 01:01:05.300 obviously useful automatic like
01:01:08.140 01:01:08.150 automatic blowdown control is extremely
01:01:09.580 01:01:09.590 common in fact I'm struggling to think
01:01:12.550 01:01:12.560 of any industrial boilers I've seen in
01:01:14.710 01:01:14.720 the last few years it didn't have an
01:01:17.380 01:01:17.390 automatic tds type controller on them
01:01:20.050 01:01:20.060 normally the reason for that is is that
01:01:22.470 01:01:22.480 when you buy an automatic blowdown
01:01:25.359 01:01:25.369 valves like say a spyrix psycho type
01:01:27.820 01:01:27.830 unit that comes with the conductivity
01:01:30.430 01:01:30.440 unit built into it right it's it's like
01:01:32.859 01:01:32.869 that's the module when the most of them
01:01:34.510 01:01:34.520 are supplied by a CR and things like
01:01:38.080 01:01:38.090 there there's other options and is less
01:01:40.780 01:01:40.790 common but it is still pretty common
01:01:44.580 01:01:44.590 either via a permanently installed
01:01:47.770 01:01:47.780 online meter or some sites might say
01:01:50.320 01:01:50.330 have multiple boilers they'll purchase a
01:01:52.210 01:01:52.220 portable unit that can be connected up
01:01:54.849 01:01:54.859 for
01:01:55.390 01:01:55.400 Yatta testing often you find that if
01:01:58.299 01:01:58.309 you're using a chemical vendor to
01:02:00.789 01:02:00.799 provide your boiler chemistry services
01:02:02.950 01:02:02.960 they will have them as well and if you
01:02:05.140 01:02:05.150 ask for some dissolved oxygen testing to
01:02:07.690 01:02:07.700 be carried out
01:02:08.620 01:02:08.630 I know Nalco and GE and things like that
01:02:11.109 01:02:11.119 have the equipment and they can come
01:02:13.089 01:02:13.099 into it all you gotta do is just connect
01:02:14.650 01:02:14.660 up like a three-quarter inch Swagelok
01:02:17.670 01:02:17.680 port and and you can run the instrument
01:02:21.309 01:02:21.319 and away you go I actually have one
01:02:23.260 01:02:23.270 myself as well for doing R&D work and
01:02:25.870 01:02:25.880 investigation work at client sites and
01:02:27.880 01:02:27.890 there may be $7,000 new zealand's for a
01:02:32.440 01:02:32.450 portable unit that lists for a
01:02:34.000 01:02:34.010 permanently installed one and they work
01:02:36.220 01:02:36.230 quite nicely yeah actually that answers
01:02:39.760 01:02:39.770 that question
01:02:40.890 01:02:40.900 premier sure you miked up no no it's
01:02:47.260 01:02:47.270 alright thank you from ish so well we'll
01:02:51.010 01:02:51.020 hang around for a minute or two more if
01:02:52.539 01:02:52.549 anyone else has got a question but
01:02:54.460 01:02:54.470 otherwise if there's no more questions
01:02:57.130 01:02:57.140 they feel free to carry on with your day
01:03:00.069 01:03:00.079 and just a reminder that the slides and
01:03:01.990 01:03:02.000 everything will be available and and
01:03:04.990 01:03:05.000 stay tuned for the invite that we sent
01:03:06.730 01:03:06.740 out for the the webinars coming up in
01:03:09.309 01:03:09.319 the future okay
01:03:30.580 01:03:30.590 okay hey yeah thanks very much to
01:03:33.260 01:03:33.270 everyone who's passing on their
01:03:35.300 01:03:35.310 appreciation but on that note in the
01:03:37.430 01:03:37.440 absence of any more fest questions we'll
01:03:39.620 01:03:39.630 will tidy up today and if you still have
01:03:43.340 01:03:43.350 questions that come to you by all means
01:03:45.440 01:03:45.450 feel free to send them through by email
01:03:47.060 01:03:47.070 and we'll do our best to assist where we
01:03:49.790 01:03:49.800 can so thank you very much and we'll see
01:03:52.610 01:03:52.620 you all in two weeks
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