Holdfast Training Services Trial Blog

This blog will focus on the installation of a sump pump in basement level 2 which I was involved with last week – another classic example of simple things taking time due to co-ordination (sump pump access is directly under the lay down point for a tower crane) and H&S constraints (confined space).

What was required?

The installation and connection of 3 no pumps into the sump pump chamber, drawing of power & data cables, installation of the control panel and connection of the control panel. Energisation and testing and commissioning of the system were outside the scope of the works at the moment as we’ve not bought beneficial use of the sump pump – yet.

How was I involved?

RAMS

A few weeks ago I was given the RAMS for the installation of the sump pump which had previously been reviewed by a Carillion MEP manager and returned as status C – works cannot commence. The plan was that I would just have to ensure the new RAMS has incorporated the comments on the old RAMS. Obviously this plan didn’t survive contact. The first box to tick on Carillion’s cover sheet when reviewing RAMS is, “have you reviewed phoenix for the appropriate documentation?” Phoenix is Carillion’s intranet which has policy and guidance documentation. Looking at the previous cover sheet returned by the other Carillion manager it was clear that this box hadn’t been ticked. So out of due diligence I completed a quick search for working in confined spaces, which for once returned a whole host of information (like the army intranet, Phoenix is particularly good at normally not allowing you to find what you want). The fallout from this was that the RAMS submitted by the subcontractor needed additional information adding and subsequently checking by other specifically qualified individuals. The subby wasn’t happy about the goal posts moving, but ultimately we got the safe system of work required in place. So what? The MEP manager that originally checked the RAMS has forgotten more about safe systems of work and MEP than I have learnt. The original RAMS were probably good enough, but if an incident had occurred without the correct procedures in place then Carillion would have been exposed. My involvement eliminated that exposure and it has reinforced to me the need to question and apply scrutiny.

EXECUTION

Getting works started

In order to get into the sump pump the trade contractor required the chamber to opened and vented, dry and free from sludge. I have now fully got into the mentality of site and understand that being overly proactive is wasted effort. Being proactive, but leaving something until it is fairly urgent seems to be the most efficient way to get works completed. Therefore the day before the works were due to commence I arranged for the   sump pump to be opened and pumped dry. Prior to doing this I walked the area again and noticed that the lid had effectively been fixed in place by a small concrete spill which hadn’t been reported. This was rectified quickly enough and the area was then pumped dry. Looking inside the sump there appeared to be about 5mm of sludge left, which I didn’t think would represent an issue – wrong! The next day the trade contractor refused to enter due to the thin layer of sludge. Not on any health and safety grounds, but because their contract is to enter a clean sump. The options available were for the trade contractor to leave site (abortive works costs), see if we could instruct the sump pump trade contractor to clear out the small amount of sludge (unwilling to do so), which left only one viable COA – instruct our ground works contractor to enter the sump pump and clear the sludge. Fortunately this final COA was achieved   by using pre-existing confined spaces RAMS, the groundworks contractor’s confined space trained personnel and the sump pump trade contractors equipment. A simple and effective plan which required detailed co-ordination to ensure all parties were aware of what was going on. The groundworks contractor was given all the certification associated with the equipment being used so the idea was that they owned the clearing out element of the works and all risks associated with that – making the delineation of responsibility and culpability clear if anything went wrong. In reality the sump pump trade contractor was still involved in monitoring confined spaces work (this wasn’t the plan) and so if something had gone wrong the water would have been muddied. As it was the  area was cleared in about 20 mins of physical work after about 2 hours of getting everything geared up. The lesson I’ve re-learnt is that subbies are there to do a specific job and rarely step outside of their lane – don’t give them wriggle room. I should have had a plan in place to get the sump made spotlessly clean on the morning works were due to take place, any sooner and rain water would likely wash sludge back into the sump. What would have been even better is if the sump had been bunged when it was installed.

CO-ORDINATION

 As mentioned in the opening paragraph the sump pump lies directly below a lay down point for one of the tower cranes. This issue was simply resolved by briefing into our daily 4Cs meeting that works would be being under taken in this area the following week for 2 days. As belt and braces I also had a conversation had with the Carillion construction manager for this area to fully de-conflict – no problems. What I didn’t do was speak to other MEP trades directly. The reason for this was that SRW have representatives at the 4Cs and as the contractor delivering the entire MEP package under “self delivery” it should be a safe assumption that different elements of the SRW package speak to each other. In fact it shouldn’t have required me to go to the 4Cs at all, SRW should be capable of doing this themselves. On day two of the installation this problem came home. SRW electrical package were trying to deliver stores whilst the installation of the sump pump was ongoing. As it was this was easily resolved by my involvement, but it is frustrating that I had to get involved. Carillion have bought “self delivery” from SRW and this should mean that the left hand talks to the right and they resolve these issues internally.

Pulling Cables

The final issue to resolve was the pulling of cables from the sump pump to the control panel location, a distance of 40m with a 90 degree bend. This is probably too far without an intermediate pulling pit. I was given a call to say the pulling cable was jammed prior to anything being connected. There are two pulling cables in this area, so I asked are you sure you are looking at the ends of the same cable? I was assured they were and that they’d reviewed the issued for construction drawings. A quick walk on site confirmed that they were trying to pull cord A whilst having undone the end of cord B. This was quickly resolved and also highlighted that the control panel had been installed in the wrong place. All simple stuff to resolve, but frustrating given that SRW are supposed to be managing the works and are far too quick to pass any problems up to CCL as quickly as possible. Luckily for me it allows for some additional CPR material so I don’t mind too much. Finally the length of cable pull and 90 degree bend proved too much for the thin diameter pulling cable that had been installed – the cables wouldn’t come through and there was a risk the line would snap. As expected SRW came running to CCL for thicker / stronger cordage in order to allow a winch to be used to pull the cables through. Having had to jump through hoops to get the works underway I took absolutely no delight in reminding SRW that they were the Design & Build MEP contractor, they had provided input into the design process with respect to the location of the duct and lack of a pulling pit and that as competent contractor with access to the for construction drawings they should have fore seen this problem. Strangely enough they got the problem sorted when it looked like they’d have to stump up for the abortive work costs.

The Wastewater Treatment Plant project I am working on has quite a lot of concrete tanks. Amongst these is the ‘Plant Water Vault (PWV)’ which for the first month I assumed was just another tank, but couldn’t place it in the treatment process. Turns out its not a tank, but a pump lift station. Confusion rectified it still looks like a tank and part of my role has been doing rebar inspections. In the grand scheme of things they are probably pretty simple as it is a box with a few, but not that many, penetrations.

Below shows the form work and rebar for the ceiling.

Rebar in the vault ceiling with the penetration for the service hatch.

And the ceiling is where the problem lies; it’s not meeting the design strength. The pours for the base and walls have been comfortably meeting the 4500psi strength in 28 days as one might expect. However, at 28 days the contractor had to do some rounding up of the percentage strength up in order to meet the 85% threshold for removing the formwork. Now at the 56 day point the last two breaks have come in at 4400 and 4320 psi.

So what… The short and simple answer is strip it out and try again it as it doesn’t meet the spec. At the 28 day point when we were looking down the barrel of this as a possibility that is exactly what my boss said cueing the squirming; not least from the concrete supplier who I believe will be footing any bill. However in reality all parties are aware that a compromise will probably be reached. The options on the table on Thursday were:

• Feasibility of replacing slab. This really is the last resort for all:
  • Quality: It will definitely meet the quality.
  • Cost: Nil for the Government; expensive for the contractor and concrete supplier.
  • Time: 2 weeks for breaking, 2 for forming, fixing and pouring, 4 for curing. The PWV isn’t on the critical path but the steel fixers have weeks of work in front of them and winter is coming fast.
• Destructive testing of cores. Will assess the difference between the cylinders and the real condition; they are as likely to be worse as better.
  • Quality: Difficult to find a gap in all the rebar to core.
  • Cost: Cheap for contractor
  • Time: Results back in a week before next decision is made.
• Structural Modifications. Adding more steel to bring to strength. This requires a design analysis of which element of the concrete requires to be 4500psi.
  • Quality: Unknown as we don’t know where steel will have to be placed. The PWV is hardly a work of art already so a bit of steel won’t hurt.
  • Cost: Less expensive than replacing the slab.
  • Time: Overall it would be concurrent activity so wouldn’t add to the programme.
• Analyse the slab to check the required strength. Apparently concrete is specified in 500psi increments so there is a chance that it is strong enough already. USACE could ask our design consultants to do it but that wold cost us money so we won’t. Instead the contractor can do it independently and our consultant can check it.
  • Quality: We wouldn’t get what we asked for, but we would get what we need if the calcs showed that the concrete was strong enough.
  • Cost: $500 – $1000 for a Professional Engineer for a day.
  • Time: A week or two and if all is good then no knock on to the programme time.

So we are going down the analysis option, which would be required for the structural modifications anyway. From there on we will see what happens.

The PMV in the background. The actual tanks are currently being poured and will keep the steel fixers busy until the end of November.

And finally…

This is now the second car crash I have seen in 6 months of being out here. The woman in the blue car turned in to get gas, but tried to go through another car to get there. I had been planning on using that pump but it was blocked when I had turned up. Fortunately no one was hurt but all of the blue car’s airbags deployed and her groceries met her in the front of the car.

I now put a couple of fuel pumps between me and the road.

PS. I don’t know what mix the concrete is Damo so don’t ask.

In the last few weeks we’ve had a few incidents where stuff has fallen from height.  The list of “stuff” includes a helmet, a 7 foot scaffold tube (which it a bloke’s arm), a screw jack, a sheet of plywood, reinforcement spacers, a length of rope, a section of edge protection barrier and a bolt.  The length of rope was actually thrown off the side of the 6th floor intentionally!

It could be worse, on McAlpine sites across London so far this year even more stuff has fallen including: a scaffold board, a drill bit, a washer, a mobile phone, a metal plate, a brick, a lifting strop, 225mm concrete core, scaffold spanner, sheet of insulation, a pallet truck (how?!) …  the list goes on.  95 objects in total.  And that doesn’t include the bloke who fell off a scaffold!

In an attempt to curb this we got everyone together and gave them a little presentation about how bad it is when stuff falls from height.  The presentation will be given to them again in their own language too, which will be a significant undertaking considering the number of languages spoken on this site.

When walking away from the presentation I hear one scaffolder turn to another and say: “The thing is though mate, their not  accounting for stupidity!”  But he is wrong.  These issues are not caused by stupidity.  Well not all of them anyway.  Some of it is an attitude problem.  I’m sure we’ve all been to places where the value applied to life is less than it is here.  Some of the people from that place have come here and now work in the construction industry and have brought that attitude with them.  They’ve done it that way wherever they’ve come from and that’s what they’re used to.  This is not to point a finger at migrants.  Some of the old and bold from the construction industry are just as bad.  Others do dangerous things because they are too lazy to do the right thing.  I saw a bloke climb over a barrier because he couldn’t be bothered to walk around it.  It’s not about nationality, or intellect, it’s about discipline!  I’ve said this before and I’m sure I’ll say it again: at least in the Army all the idiots do as their told!

One problem that we have is that there is so much construction work in London that there is a serious shortage of competent skilled labour.  We have forced our blockwork contractor to only use their own full time lads, not agency, in an attempt to ensure that the quality is maintained.  Other sub-contractors have not made the same commitment and so staff turn-over is high as workers move around to whichever site is paying the most that week.  This has a serious impact of things such as quality, but also safety as it takes time to indoctrinate the new workforce into the McAlpine way to doing it.

In others news: Our site now looks like a small child has got a sign making kit for his birthday and has just gone nuts!

Introduction

This blog follows on from my previously explained, Chilled Water (CHW) pipework flushing blog. It takes the discussion further, explaining the CHW system, commissioning and project wide examples of applications including problems faced.

The CHW System

Fig 1 shows the main plant: flow and return connection to CEP CHW, the mixing decoupler, flow meters, the pump sets in an N + 1 arrangement (n = 4 pumps duty), the four flow and return legs that feed various risers and the critical to life pump sets and flow and return legs.

Fig 1. Plantroom 10 (Basement) CHW Equipment Layout.

The total flow rate for all four legs is 605.1 l/s. Fig 2 shows the N +1 pump sets with 4 x duty pumps (rated at 125 l/s each) producing 500 l/s; the 105.1 l/s delta (17%) is for system diversity.

Fig 2. Plantroom 10 CHW Pump Sets.

The CEP design flow temp is 7 °C and return is 14 °C.

The following main equipment is fed by the CHW system:

Central Computer Room 2 (CCR2) – This is the main communications hub of the building and houses sensitive electronic equipment, such as the 67 x computer data racks, which requires constant cooling. At full operational load the data racks will push out 450 kW of heat load. The design incorporates in-row cooling with a ‘hot aisle’ containment system (see figs 3, 4 and 5) using distributed Computer Room Air-Conditioning (CRAC) Units (stand-alone Fan Coil and Condensing Units) integrated into a false floor. Humidity is controlled locally and there are also self-protection measures such as a pro-inert fire suppression gas deluge system with purge ventilation, anti-static flooring and an Uninterruptable Power Supply (UPS).

Fig 3. CCR2 Data Rack In-Row Cooling.

Fig 4. CCR2 Hot Aisle Data Racks.

Fig 5. In-Row Cooling System Control PLC.

Field Communications Rooms (FCR) – Data from CCR2 feeds each of 37 x FCRs via a combination of copper and fibre optic connections, which also requires constant cooling provided by dedicated CRAC Units; fed by CHW from CEP. The FCRs, like CCR2, are critical to building functionality managing items such as: Building Management System (BMS), security, fire protection, nurse call, lifts, CCTV, Automated Guided Vehicles (AGVs), medical gases and the Health Integrated Network systems.

UPS Rooms – There are 3 x UPS Rooms each with 2 x CRAC Units (duty and standby).

MRI Machines – The 2 x MRI machines are hydraulically separated by plate heat exchangers with the secondary circuit pumps located in PR 6, see fig 6.

Fig 6. MRI Plate Heat Exchanger and Pump Set.

AHUs – There are approx. 82 x AHUs across 9 x Plantrooms (PR). These use the CHW to run through the coils used for air-conditioning.

Increased System Volume Issues

In normal circumstances commissioning of a piped water system would occur once all installation is complete. However, on the PCH project that was not possible due to the Client’s requirement to energise and therefore provide cooling to CCR2. The CHW feed from CEP was opened but because the initial heating load was very small, keeping the CHW flow and return permanently open would mean the return temp to CEP being around 8°C; too low. This gave a very small ∆T (7°C flow and 8°C return) and the concern was this would cause the CEP BMS to reduce the cooling required by the chillers thinking it’s not required and potentially turn them off or reduce their cooling. This would adversely affect other areas of the QEII Medical Centre, whose heating loads are at normal operating capacity.

In order to avoid this the PCH site controls the volume of CHW through; enough to provide sufficient cooling for current heating loads via the CEP Isolation Valves (IV). The design intent is to permanently keep the CEP IVs open to allow the CHW to flow from CEP around the PCH site and back again, closing the loop.

The design intent cannot be achieved until PCH sees ‘normal operating’ heating loads to avoid the return CHW being too cold; it should be around 14°C to avoid the above issue. This heating load will not be seen until all external facades are in place, the building has been completely sealed to the outside elements and all heat generating equipment has been installed like: lighting, AHU fans running etc. Only then will the AHUs be demanding sufficient CHW in order to maintain comfortable working conditions. Until this time the CEP IVs will be left in a controlled open/closed when necessary state with the decoupler loop valve left in the open position to allow what CHW has been let through to circulate round the PCH CHW system.

Periodically, when the PCH CHW temp begins to rise, the CEP flow IV is opened (operated by temp sensors that control the motorised valve) for a brief period to allow a slug of 7°C CHW through and similarly the return IV opened to allow a slug of 10 – 14°C CHW back to CEP. This procedure is fine in theory but in practice the CEP IVs are not meant to be operated at such regular intervals as they are designed to be either open or closed and not to regulate flow.

At present, because the BMS is not yet fully operational, the basement services co-ordinator has to manually set the return flow trigger temp (set at 10°C) to allow a slug of CHW through from CEP. This trigger temp is set based on the cooling load required for the equipment from across the building; which at present is very low. However, there are certain critical areas that must stay cool but have been experiencing high temps lately. These are the FCRs and UPS rooms.

The issue currently seen is caused by the following factors:

Due to a number of plantrooms having completed their commissioning they were ready to open-up to CEP via the central services risers. As they were opened the CHW system volume increased and with that the system pressure dropped. This meant that the flow rate was too low and the CHW would have gained too much heat by time it reached the FCUs (even with lagged pipes). The knock-on effect was that the FCRs and UPS rooms were struggling to keep cool as the FCUs / CRAC units were unable to provide sufficient CHW due to the reduced system pressure. An additional reason why the FCRs were getting warmer was because the building fabric is now better sealed and climate conditions are changing; getting hotter outside.

Solution

The solution is easy and in order to increase the flow rate and thus increase the system pressure the mechanical pumps need to increase their speed. Currently there is only one pump running at 40 Hz. When it is manually increased to 50 Hz (its design maximum) and if the system still requires more velocity pressure, an additional pump will be run-up to maintain this; found from the equation derived from Bernoulli’s: P_v = ½ ρ c².

At present until the BMS is fully operational, where two pumps at a time will run simultaneously; a second pump will have to be run-up manually. This will allow commissioning works to continue; balancing of individual plantrooms and thus not hold-up subsequent integrated commissioning or the project as a whole. The fully operational BMS is around three weeks away and that is a lot of time to lose to wait for the perfect control solution. Therefore, the interim measure requires careful co-ordination of the requirement to increase pump speed matched to the increasing system volume (from opening subsequent plantrooms to CEP CHW) in order to maintain system pressure. It also requires a robust means of monitoring temp control.

Co-ordination Requirements

It was evident that from the questions I was being asked by the installation services co-ordinators, that there was no clear methodology or plan in place in which to open-up subsequent plantrooms to CEP CHW in a sufficient way that would not cause the system to ‘fall-over’. In particular, my concerns were that critical equipment reliant on a CHW supply could become damaged, costing huge sums of money to replace, such as: MRI machines, UPS and FCR equipment.

So what part did I play in co-ordinating the effort to resolve these current issues?

The thing that was most obviously about the CHW system was that there were many people involved who were working in their own little silos with little communication happening. The first thing I wanted to achieve was to establish the single point of truth and from a commissioning team perspective, understand the system and what issues we were facing. This was achieved through an initial mtg with all key players: design consultant, construction subcontractor, controls subcontractor and us the managing contractor.

The mtg was successful in a number of ways, most notably was a number of action points for the subcontractors to answer and allow us to co-ordinate accordingly thus ensuring the integrity of the system and that critical areas did not get too warm.

In practice the co-ordinated plan didn’t quite survive first contact. The plan was to open up PRs 4, 5, 6 East and 8 to CEP. The objective was to open them all but maintain the current flow rate knowing that critical equipment was stable in a ‘happy’ state. We started off by measuring the flow rate to one of the FCRs in PR 6 which was 0.375 l/s, 140% of design flow rate of 0.27 l/s. This was with 1 x pump running at 46 Hz.

We then ran up a further 2 x pumps and backed-off the first pump to match them.  This was an iterative process until we got to a comfortable flow rate in PR 6.  This was 86% of 0.375 l/s which equated to about 120% of design flow rate.  All 3 pumps were running at 40 Hz.

We then opened-up PR 4 and went back to PR 6 to measure the % drop. We were at 81% of 0.375 l/s and content with that flow rate. All 3 pumps still at 40 Hz.

However, PRs 5 and 8 remained closed-off to CEP as I felt the condensate drains and some un-lagged pipework not being complete could cause condensation issues.  Once these are complete these can be opened.

We also witnessed the CEP CHW IVs opening and shutting letting through CHW as required based on the return temp control.  Therefore, we were content if the temp rises then CEP will restore it.

All pumps were still only manually controlled and would require the same above process for energising the remaining PRs to CEP.

It was found that the flow temp was slightly higer than design and should FCRs, CCR2 or MRI temp increase then we should first look at this.  Currently with the mixing occurring through the decoupler we are seeing a flow temp of around 10 – 11 °C. This is more likely the reason why areas are getting too warm rather than pressure drops or reduced flow rates.

The position we want to be in is have PR 1 flushed and opened to CEP. This being the index run throughout the building means we can set the pumps to monitor the differential pressure at that point. This is so that no matter if we open-up additional PRs (increasing system volume) or if we close-off PRs (reducing system volume and thus potentially causing a pressure build-up in a closed head scenario) then the controls can adjust accordingly in dynamic fashion and remain stable.

What did I learn?

1. If you are at the point where speaking to different parties gives you the feeling that the right hand isn’t talking to the left then you need to set up a mtg sit everyone down and systematically run through what’s what, where you are currently at and where you want to get to.

2. Old school still works. I’m referring to the simple but very effective method of printing off A0 dwgs and physically highlighting the pipe runs using a different colour to distinguish its status: flushed and cleaned, opened to CEP CHW, proportionally balanced etc. It provides a dynamic way of statusing the progress of a system when dealing with a complex building with nine plantrooms over nine floors.

3. Condensation is a real concern as proved by a number of valves not being lagged before CEP CHW connection as shown in figs 7 and 8.

Fig 7. Condensation Formed Drops on Valves.

Fig 8. Condensation Formed Drops on Valves.

4. A slightly annoying learning point is that no matter how many repeated verbal and written communications are made, subcontractors still ‘do their own thing’. An example of this was where the condensate drains not being correctly installed before the AHU CHW coil IVs were opened, causing the inevitable ‘sweating’ (condensation) to drip off the coil into the condensate collection tray through the drain pipe then onto the plantroom floor. The subcontractor, Fredon, said the spill on the floor was from when the engineer replaced the clear plastic section in the drain pipe to copper, as per fig 9. But I wonder how much trouble it would have been to use a receptacle or even just tissue paper to mitigate getting the floor wet? And, how do they explain opening up to the coil with the obviously missing section of pipe that should continue to the tundish in fig 10? This leads on to valuation payment claims from the subcontractor being reduced.

Fig 9. Condensate Drain Replacement.

Fig 10. Spot the Obvious Issue?

5. Although I am a member of the commissioning team, I have come to realise that you can never truly get away from construction/installation issues. Sequentially, the installation must be complete prior to commissioning activity so inevitably it falls to us to drive construction completion in order to stay on track with our commissioning programme.

In Other News

The British Defence Advisor to Australia, Commodore R L Powell OBE MA MSc RN, was visiting Perth and requested the presence of those on military exchange programmes.

There were only three of us Brits meeting the 1-Star, a RN Officer working at Garden Island (a nearby Naval Base), a SBS Warrant Officer working as the UK LO to the Australian Special Forces based just up the road at Campbell Barracks, and then myself.

The visit was pretty low-key with the Attaché just asking us how we were all getting along on our respective programmes and if we had any issues in moving out here. He then spoke a bit about ongoing projects from a relationship with Australia perspective. This was all good background info and sounded quite interesting, especially the fact his post out here is a 4 year tenure – nice if you can get it, oh and have promoted to Brigadier – no biggy!

Part of our falsework system incorporates 7No, 21tn, 30m trusses. These are assemble on the ground and lifted into place.

On Tuesday one of these trusses fell over during construction and landed at the feet of one of the lads. The panel that fell weighs 380kg. This is the sixth truss built on site, no previous concerns had been raised.

The highlighted panel was vertical. Bottom cords 1 & 2 are in the correct position, 3 has rotated with the panel. This panel had no lateral bracing.

The cross bracing has pulled out of it’s alignment. NB, this was not bolted as the cords are left free to creep through construction. The construction method was instructed by the supplier.

The revised construction method includes ‘tube and fit’ bracing.

The bracing is also tied back to the hand rail which has been increase to deal with greater loads.

Installation of these trusses sits on the crit path so no time was wasted in assessing, reviewing and modifying the construction. This process was thorough and the new mitigations seem to be appropriate and full proof with regards to a repeat of this situation.

A happy truss!!!

A link for the E&Ms (Fran, you should suggest this for your hospital!!!)

https://www.youtube.com/watch?v=uPVQMZ4ikvM