<a href=showthread.php?s=&postid=6929736#post6929736 target=_blank>Originally posted</a> by pjpeels
What are the benifits to the additional upgrades, besides performance and effeciency of the system, to the water quality. What if TDS allready 0?
Really a Typhoon is good enough for a reef but I am a technology nuts so I have to modify everything for full automation.
The cartridge sizes are all standard so if you buy the Typhoon you can always upgrade the cartridges once they are exhausted the only difference is that if you upgrade the carbon filter then you may not need the two that come from the Typhoon but you can use the left housing for an additional DI cartridge by just re-routing the connections.
The upgraded cartridges and some of the automation equipment you can get from
www.spectrapure.com although airwaterice can also provide you with a second membrane kit add on and additional housings if you like.
Here are the benefits of the upgrades:
Sediment filter, the better micron rating (look for absolute rating rather than median) the longer the life of the membrane, passed particles eventually get deposited in the membrane pores.
Carbon filter. The better the grade and capacity the lower the cost per gallon of water produced and the less likelihood that chlorine may pass into the membrane, chlorine can totally damage a TFC membrane in just a couple of uses. This is why Typhoon uses two filters for carbon.
Membranes. All standard membranes up to 75 gallons are rated for 98% rejection and the 100 gal for 90% rejection. The difference is that at the higher rejection the DI cartridge lasts up to three times longer but your production capacity will be 75 nominal instead of 100 gpd.
The membranes I use have still an even higher rejection. All 75 gal TFC membranes from Filmtec are produced exactly the same but as per specifications there is a range of acceptable rejection. When a new lot comes in the vendor tests the membranes for rejection and sets aside the ones with rates of 99%+ to sell them as ultra at slightly higher price than the standard.
When using dual membranes, besides the obvious advantage of increased production is that the waste water per gallon of produced water is half of what it would be other wise. The waste from the first membrane is fed as inlet to the second membrane, this way you get basically twice the product with the same waste. There is an insignificant increase 0.5 to 1 TDS in the product out of the membranes but worth the water savings.
Strong Anion DI resin is specified for removing specifically Silicates and Phosphates but in my case specially in the winter there is a lot of CO2 dissolved in the tap water, the CO2 shortens the life of the DI cartridge a lot but a cheaper Anion cartridge helps extend the life of the most expensive high grade resin cartridges.
If your water is treated with chloramines the carbon breaks it down but this action releases Ammonia. The Ammonia is not removed by the membrane but by the DI filter. A DI filter with resins specified for Ammonia removal will last a bit longer.
The last electronic grade resin cartridge is normally specified to produce water of near absolute purity (In the range of Parts per Billion TDS) This water is mostly used in the manufacturing of electronic chips were any minor impurities can spoil hundreds of units. This is just my fancy, I had the housing and because the previous two DI cartridges, this one lasts really long so why not to have it if I can produce such a pure water.
The pump you only need if your tap water is low.
Now about automation, most of it is for comfort but there is one piece that I consider really beneficial, the auto purge at start up.
When a system is shut off impurities permeate to the product side of the membrane so every time you start the system there will be impurities passed with about the first gallon or so. If you have a top off and the system turns on and off often this will allow a lot of impurities in the product water. The purge system trows away the product water for five minutes before switching the output to the storage or the sump.
When the sump is back to level and the storage is full the pressure in the output starts to rise. a pressure switch detects this increase in pressure and opens a solenoid that by passes the flow restrictor in the waste increasing the flow of waste water, this waste carries away any sediment or carbonate accumulation on the inlet side of the membrane to prevent it from being plugged (You can do the same with a manual by pass valve). After two minutes the solenoid shuts off and at the same time the pump also turns off.
When the top of system detects low water level it opens a solenoid in the output of the unit and the pressure drops, this drop is detected and the pump turns on as well as the auto purge starting the cycle again.
Here is the order:
a) Tap faucet
b) Pressure Gauge
c) Sediment Filter
d) Carbon filter
e) Booster pump
f) controller valve (which signals and times purge, flush and a DIY electric relay to start and shut off the pump)
g) TDS meter
h) First membrane housing (inlet)
i) Housing pressure gauge
j) Waste output from first membrane to second membrane housing (inlet)
k) Waste outlet of second membrane to restrictor and solenoid flush bypass and from there to the drain
l) Product outlet of both membranes joint to a single line
m) TDS meter
n) check valve
o) Strong Anion cartridge
p) Ammonia removal DI cartridge
q) Purity Monitor
r) Mixed bed electronic grade resin DI cartridge
s) Dual output solenoid (to purge) that diverts the product water either to the drain or to the top off and storage.
t) Surge Tank
u) Pressure gauge
v) Output pressure switch
w) product line split one to top off solenoid valve and the other to the storage (which has a float valve)
Again you do not need all this, I just did it just for the sake of it not because the reef needs it.
If I want to have a good unit without all the fancies this is what I would get:
a) 1 micron sediment
b) One high capacity carbon block filter 1 micron or two normal capacity carbon filters
c) one 75 gpd membrane with pressure gauge
d) Two standard DI mixed bed DI cartridges. If chloramines, have the first for Ammonia removal. Preferably non color indicating but TDS shall be checked routinely to detect exhaustion of the resin.
e) Dual TDS meter
f) ASOV valve (Shuts off the feed water when top off or float closes but is actuated by differential pressure not electrically.
g) Manual back flush
h) manual valve to shut off output
h) Low voltage auto top off
i) float valve (In case top off fails to close)
Some extra tubing and a couple of extra John Guest "T"s and valves to tap in between cartridges for water testing will also become handy.
By the way, regarding TDS being zero, they never are with the kind of meters we normally use, it is usually 1 to 2 parts as the meters are not sensitive enough.
Do we need absolute 0 TDS for our reefs? absolutely no. We add more impurities with the salt and the food in a week than what we would add with an standard RO/DI unit in a year of water changes and top offs.
A couple of extra John Guest "T"s and valves to tap in between cartridges for water testing.
Sorry it was so long but tried to be as specific as I could.