I'm in an area with moderately hard water, with a high ph and treated with chloramines.
(120-150 mg/l, 9.7-10 ph, 2.5 mg/l chloramines. No water softener.)
Current RO/DI setup is .5 micron sediment filter /.5 carbon block/chloramine block before the 90 gpd membrane.
I'm only getting around 250 or so gallons of finished water (4:1 ratio) before I have measurable chlorine after the first carbon block. I know that the chloramine block is catching what is getting through . But I'd like to get more life out of the first block. There's only so many things I could possibly do that I can think of, but I don't know if any of the options would have a measurable (or cost effective) impact. Here's what I think are the options, and I'd like everyone's opinions.
Sediment- switching from a .5 micron to a .35 micron sediment filter. How much gain?
1st carbon block- I already use a .5 micron, there's nothing smaller out there (that I know of). If I switched from the standard sized carbon (2.5 x 10) block to a larger block make a difference? Say, would switching from a 2.5 x 10 to a 2.5 x 20 get me double the life? More than double? Is the contact time/removal a linear relation?
At what level of chlorine breakthrough does damage to the membrane begin?
I've looked at the BRS Chloramine monster time and time again. But I just can't bring myself to pull the trigger. Not so much the price, but more the claims, and the fact that it is a 25 micron block.
Also, do carbon blocks need to , or benefit from "resting"- not having any water passing through them for a period of time?
Membrane- It would be easy enough for me to add another membrane to my system. I could plumb it in so both membranes were still on the system, but only use one at a time. If I added a lower production membrane to the system, that would increase contact time with the carbon block. Since the carbon block's capacity is a product of contact time, it seems the slower the flow the better. But exactly how much more capacity ? As far as decreased production, my normal water needs are about 70 gallons a week, so a smaller membrane wouldn't be an issue. If I needed more water for an emergency, I'd just run both membranes. (And I'd be sure to run some water though the 90gpd membrane on a weekly basis.) I've seen 35 gpd membranes, but do they make even lower production membranes? And do the lower production membranes have the same rejection rate as the more popular 75 gpd (or more) membranes? I really enjoy the DI Max Cap resin savings of my current Spectra Select 99% membrane. It would be kind of silly to save a few bucks on carbon blocks and have to turn around and spend those savings (probably more) on DI resin.
Tap water- Ok, let's go ahead and take this to the extreme.
It would be feasible for me to treat the tap water prior to running it through the system. Fill some barrels, treat them with Prime and do something to lower the ph ( muriatic acid? ), aerate the water for a period of time to blow off the elevated CO2 from treatment, then pump it through the system. It would be fairly easy to automate through my Apex. (Though not very cost-effective, I am sure.)
What exactly would/could the RO/DI system remove with such a setup? If the chlorine has been "removed", is the carbon block catching the "removal" by-products? And if the ammonia has been converted to another form, is the new form better caught by the membrane? And, what is this the effect of this new form of ammonia on the DI resin? Longer or shorter resin life?
Thanks in advance to all who take the time to respond.
OCD/Perfectionists members- please chime in!
(120-150 mg/l, 9.7-10 ph, 2.5 mg/l chloramines. No water softener.)
Current RO/DI setup is .5 micron sediment filter /.5 carbon block/chloramine block before the 90 gpd membrane.
I'm only getting around 250 or so gallons of finished water (4:1 ratio) before I have measurable chlorine after the first carbon block. I know that the chloramine block is catching what is getting through . But I'd like to get more life out of the first block. There's only so many things I could possibly do that I can think of, but I don't know if any of the options would have a measurable (or cost effective) impact. Here's what I think are the options, and I'd like everyone's opinions.
Sediment- switching from a .5 micron to a .35 micron sediment filter. How much gain?
1st carbon block- I already use a .5 micron, there's nothing smaller out there (that I know of). If I switched from the standard sized carbon (2.5 x 10) block to a larger block make a difference? Say, would switching from a 2.5 x 10 to a 2.5 x 20 get me double the life? More than double? Is the contact time/removal a linear relation?
At what level of chlorine breakthrough does damage to the membrane begin?
I've looked at the BRS Chloramine monster time and time again. But I just can't bring myself to pull the trigger. Not so much the price, but more the claims, and the fact that it is a 25 micron block.
Also, do carbon blocks need to , or benefit from "resting"- not having any water passing through them for a period of time?
Membrane- It would be easy enough for me to add another membrane to my system. I could plumb it in so both membranes were still on the system, but only use one at a time. If I added a lower production membrane to the system, that would increase contact time with the carbon block. Since the carbon block's capacity is a product of contact time, it seems the slower the flow the better. But exactly how much more capacity ? As far as decreased production, my normal water needs are about 70 gallons a week, so a smaller membrane wouldn't be an issue. If I needed more water for an emergency, I'd just run both membranes. (And I'd be sure to run some water though the 90gpd membrane on a weekly basis.) I've seen 35 gpd membranes, but do they make even lower production membranes? And do the lower production membranes have the same rejection rate as the more popular 75 gpd (or more) membranes? I really enjoy the DI Max Cap resin savings of my current Spectra Select 99% membrane. It would be kind of silly to save a few bucks on carbon blocks and have to turn around and spend those savings (probably more) on DI resin.
Tap water- Ok, let's go ahead and take this to the extreme.
It would be feasible for me to treat the tap water prior to running it through the system. Fill some barrels, treat them with Prime and do something to lower the ph ( muriatic acid? ), aerate the water for a period of time to blow off the elevated CO2 from treatment, then pump it through the system. It would be fairly easy to automate through my Apex. (Though not very cost-effective, I am sure.)
What exactly would/could the RO/DI system remove with such a setup? If the chlorine has been "removed", is the carbon block catching the "removal" by-products? And if the ammonia has been converted to another form, is the new form better caught by the membrane? And, what is this the effect of this new form of ammonia on the DI resin? Longer or shorter resin life?
Thanks in advance to all who take the time to respond.
OCD/Perfectionists members- please chime in!



