Archive
Diffuser Selection
Initial task
As mentioned last week I’m currently being asked to look at two projects, a Biopharm for GlaxoSmith Kline (GSK) and the re-fit of some steam plant at the London School of Hygiene and Tropical Medicine. I get the impression that Bryden Wood were hoping to initially fill my time with the steam plant project, however, I won’t be able to get involved with this until Wed at the earliest. Therefore I’m having a bit of a slow start, which is no bad thing after the last few months on site. My task to date has been to look at possible diffuser solutions (air supply) in a number of rooms in the Biopharm facility, which will ultimately feed into the specification for the main contractor. I’ll start with a few paragraphs stolen from the GSK website:
Firstly what are Biopharmaceuticals?
Biopharmaceutical products are medicines engineered by scientists and manufactured by living organisms to treat specific ailments. Biopharmaceuticals often target specific cellular functions and tend to be more potent than chemically synthesised pharmaceuticals. Today, 16% of all pharmaceuticals are biologic in nature – treating a wide range of disease areas.
What does Biopharmaceutical Manufacturing involve?
All biopharmaceuticals are manufactured in the same way. Closed, controlled reactors cultivate cells or organisms to produce large quantities of the medicinal product. During cultivation, the reactors are fed with nutrients and its temperature, pH, and aeration are controlled.
Once enough of the product has been produced, the reactor contents are harvested.
Further processing isolates, purifies, and stabilizes the bulk product. It is frozen and stored until formulation and dispensing into its final dosage form used by our patients.
To keep production free from unintended contamination by naturally occurring microbes, manufacture is mostly executed in closed, clean, and sterile equipment. Cleanroom facilities and personnel gowning (similar to hospital operating theatres) provide additional assurance of product quality.

GMP classifications in terms of allowable particle numbers and size per metre cubed. See paragraph below.
What impact does this have on MEP?
It is this final paragraph leads to a requirement for varying levels of cleanliness in rooms depending on their use. The specification for cleanliness is via a standard called Good Manufacturing Practice (GMP).
The rooms I am looking at require a GMP classification of either C or D. This is achieved by increasing the number of air changes per hour (ACH) to a minimum of 10 for class D rooms and 20 for class C rooms. Additionally specific bag filters are use in the Air Handling Units (AHUs) and HEPA filters inserted into the system (see Fran’s blog on ductwork testing).
What’s the problem / why have I got involved?
The strategy for meeting the ventilation requirements in the class D rooms is for high level supply and extract. Unfortunately there doesn’t appear to be enough ceiling space to achieve this; the reactors that cultivate cells are fed by pipework from above, in addition the ceiling is up to 5m high in places and the lighting is being supplied with LEDs, which leads to large emitter arrays being required. The knock on of this is that there is little space for both supply diffusers and extract grilles in the ceiling. We are therefore looking to provide high level supply and low level extract.
My task has been firstly to look at what diffuser options meet our requirement. I approached this in the following manner:
- Identify what the air velocity requirements are for the clean rooms – .15 m/s to .45 m/s for class D rooms. (CIBSE guide B)
- Use the ACH values and room volumes to work out what the required room air flow rates were. The assumption was made that the GMP requirement would be in excess of the heating / cooling requirement.
- Use manufacturer’s data sheets to narrow down the number of products that meet our requirement (figure 1 and 2). The main driver for this was the “throw”. Where throw is the distance from a diffuser to where the velocity of the air jet drops to 0.5 m/s. The throw that is achievable for a given diffuser will predominantly depend on its design, its use (heating, cooling or ventilation) and the flow rate of air through it. Most manufacturer’s don’t give a distance for “throw” in their data sheets, but do give a distance to the 0.2 m/s isovel (line of constant velocity), which is actually more use in my circumstance.
- A secondary consideration was ensuring that the noise rating of the diffuser was acceptable along with the pressure drop across the diffuser.
This has allowed me to scope a couple of potential solutions. I am now in the process of approaching suppliers to confirm the type of diffuser and suggested layouts. We’ll then be able to put this back into our model to see how it impacts other services and eventually write it into the specification.

Figure 1. This figure is taken from a manufacturer’s guide and shows both the vertical and horizontal at a distance where the jet velocity has dropped to .2 m/s. The darker blue cloud indicates how the air jet would move when the diffuser is set up for isothermal or cooling conditions and the coanda effect is being utilised. The lighter colour bubbles indicate the blades in the diffuser being at a steeper angle to force warm air down into the occupied space. My room is 5m high and has 3m between diffusers, therefore ALv is 5m and ALh is 6.5m (the occupied zone is to the floor as the requirement is for cleanliness as opposed to the 1.8m indicated above for someone standing).

Figure 2. From figure 1 it is possible to calculate ALv and ALh. In my case ALv is 5m. I’ve used this with a blade angle of 45 degrees and a heating delta t of 5 degrees to calculate that one AX6 250 diffuser would need to be pushing through just over 1000 m cubed per hour to meet these conditions. This is then checked against the capability of the diffuser to see if it works, if it doesn’t either the blade angle can be changed or another diffuser has to be selected.
The next stage is to try and work out the low level return will work; part of the design brief is that GSK want the facility to conjure images of “ the Google of Pharmaceuticals” and for the process to be transparent. This is resulting in most of the internal walls being glass – not entirely sure how we’re going to turn glass walls into return plenum’s.
Leaky Pipes
The main fun last week was that the boilers in FtIG shutdown unexpectedly. The contractor has left site temporarily making things more difficult. The issue is not yet resolved so I will blog it when further progressed. In lieu of that excitement here is a thought on sustainability/serviceability.
After the shutdowns of the dual temperature distribution piping from my mechanical room in FtIG we noticed that significant quantities of make up water are required to return the system to pressure; this means that there is a leak somewhere. To do my bit for sustainability I mentioned this to the client and was met by little in the way of enthusiasm.
Replacing the pipe work had initially been part of the scope of the project but as there was no cost benefit attached to it this element was removed to improve the pay back period of the project. This is because the project was funded based on energy conservancy it had to have a 10 year pay back period. The client that the pipes were leaking however didn’t attach a cost to this.
The cost is inconsequential now but for the opportunity to exercise my calculator I have had a stab at it. I conducted a test on site to work out the leakage rate before plunging into a heat loss calculation.
I shut off the pumps and make up water valve and left the system to rest. The static pressure was initially 10psi. To get a representative flow rate for the make up water I used the local tap off to fill a 1 gallon jug, this took on average 8 seconds.
After 2 hours I opened the make up water valve again and timed how long it took to refill the system. By now there was plenty of air in the system from the leaks and so once the valve stopped gushing I restarted the pumps to cycle the system through the air separator with the make up water valve closed to remove the air and ensure the pressure rebuilt to 10 psi. I repeated this process 3 further times until the system balanced. The time on the stopwatch for the make up water valve being open was 8:20. So

This method is clearly riddled with errors, for a start:
- Water leaking whilst I was refilling the system.
- Stop watch error.
- A static condition is not the same as when the system is operating.
- How representative the local tap flow rate test was to the flow rate of the system when nearing 10psi.
- The exact cost of energy and water; I used some figures from Ft Drum. I did an initial calculation using my electricity cost, this came out at $5,400 a year!
However the discussion has to start somewhere and some data, even with a large error value, is better than none.
Either way, had this test been done a few years ago it might have added $11,000 to the budget (or $12,500 if accounting for 2.5% inflation), which might have brought the system within the payback period. I have tried chasing down some of the early paperwork but to no avail.
More pressingly, we are due to treat the system with chemical to preserve the inside of the pipework. The contract calls for testing and topping up the system every month At 31.25 gal/hr the lost water rate is 31.25 x 24 x 30 = 22,500 gallons a month. I don’t know the exact size of the system but assuming 2000′ of 4″ pipework it would be 1300 gallons, which is about 2 days work for our leak. Therefore the contractor will be paying to completely re treat the system each month, significant quantities of chemical will be released into the ground and the treatment of the system will be totally ineffective in preventing corrosion.
I continue to beat my head against the proverbial brick wall on this one…
Welcome to Phase 3
So after a nice period of leave (Iceland is a great holiday destination!) I am now in a design office.
I’ve been given two projects to get me started: designing a crossing point for quarry vehicles to get over a high pressure gas pipeline, and designing a drainage solution to a flooded National Grid site. Additionally I’m also getting pulled into a job designing a new facility for the Somalian SF next to Mogadishu airport, not too dissimilar to one I did for our SF in Lash just before it shut. So plenty to get stuck into.
Both of these jobs were sold to me as “nice simple ones to get started with”. Which it turns out is not true for either. The drainage job requires applying for a Section 50 licence to dig up a road and a discharge consent from the environment agency. The design itself is pretty straight forward but the hoops you need to just through are not.
The pipeline crossings job is more of a design headache as what I was told was gravel is in fact clay. Despite three different surveys being conducted, at no point did anyone do an SPT, or lab testing and so no Geo properties, ground water data or test results are available. So the first step is to get a “proper” site investigation done.
Additionally the company I am attached to (WYG – a fairly holistic medium sixed engineering consultancy) do the obvious structural, civil, mechanical and electrical design work, but they also do planning, transport, force protection, international development and aid work to name a few. So the plan seems to be for me to do about four months in the Civils/Structural design dept. (overuse of the work dept. – there are three of us in the London office) then a month in any three other depts. of my choice. I’m thinking International development, Project Management and Adjudication, but I’d be happy to get suggestions!