Plumbing Africa September 2018 | Page 62

60 TECHNICAL Schematic diagram of RPZ cut away. b. a double check valve shall be incorporated as close as is practicable to the point of discharge; or c. a combined check valve and vacuum breaker shall be so installed that the vacuum breaker is at least 300 mm above the spill-over level of the receiving appliance. Look at section 7.4.3.3 above and think about Nikki spouts in baths. It clearly says here that for fittings that discharge into for example a bath, there must be a gap between the outlet and the spill-over level of the appliance (not the overflow outlet level — the spill-over level means the rim of the bath) with a certain vertical distance separating them. A Nikki spout does not have this gap, so we need to install either ‘b’ or ‘c’ as above. How many of us do this? As a side note, in Annexure D of SANS 10252-1 (D.1.6.1), it says that if the terminal water fitting already has a backflow prevention device incorporated within the fitting that is suitable for the hazard generated, we need not install additional backflow prevention. Given that a single check valve is not a suitable backflow prevention device, how many of us have actually installed Nikki spouts that comply? In essence, our role here is quite simple: we need to determine the hazard level and from that, we need to decide on the type of backflow preventer we need to install, if any. Note that a break tank with an air gap is also a suitable means of backflow prevention, but not September 2018 Volume 24 I Number 7 Figure 1: Typical backflow prevention set-up. easily employed. Note also that if there is no break tank, the two most common backflow prevention measures are given in table 12 — either an RPZ valve or a double- check valve. Not a single check valve, as this is not considered a backflow preventer. In many cases, it is not enough to simply install a backflow preventer on the main incoming supply — we need to prevent cross-contamination within the premises as well. That is to say a section or process within an installation that constitutes a hazard must be isolated from the rest of that installation, so the backflow preventer(s) must be installed immediately upstream of the process or area. Have a look at Figure 1. You will notice that all parts of the installation downstream of the backflow preventers are deemed to be non-potable (NP). Therefore, multiple backflow preventers are required in these cases. Backflow prevention devices must be tested and maintained according to manufacturer’s details, but these intervals shouldn’t be more than 12 months. In Annexure D of SANS 10252-1 (D.3.6.3), it states that if there is no such maintenance programme in place (again, this onus is on us as installers), that backflow preventer shall not be employed, and the standard air gap requirements shall apply, as this set-up is pretty much maintenance-free. www.plumbingafrica.co.za