kbd
01/18/2004, 01:11 PM
Greetings from London, England.
I hope that you can help me. I have discovered that I have high silicates in my tapwater, I estimate between 10 and 15 ppm using the Salifert test kit (diluting my sample with proven silicate-free DI).
I estimate that my RO reduces these to around 2 ppm, my DI has little additional impact. I am happy with the RO performance, but not realising the severity of my input, I have clearly bought the wrong membrane. It does what it says it should do.....
I use a generic TFS membrane made by Filmtec (MM-TFF 45/75), have good domestic water pressure and (the way it is plugged-in) usually warmish water. I use intermittantly.
My DI comprises separate columns, two litres each of cation/anion resin, I do not know the specifications. At around this volume I thought that I was safe ! My resin is not saturated at present (at least, not generally ! ). The cation resin is colour changing (brown to red), I replenish myself (resin is horrendously expensive in the UK).
Set out below (together with a recap of SiO2) is the performance measured in conductivity:-
...............................microS/cm....................ppm SiO2
Source Tap...............675.............................10 - 15
RO Output..................55................................2
DI Output.................. 1...............................1.5 - 2.0
I can improve DI output by reducing flow, but at 1 uS/cm I am probably beyond the precision of my probe, a Tunze, and don't bother.
As an experiment, I ran a closed loop thru' my DI, passing a sample several hundred times and only succeeded in reducing silicates to around 1 ppm. Does DI simply become "saturated" wrt silicates specifically while remaining active for other ions ?
I would like to reduce my silicates to comfortably below 1 ppm, allowing for the fact that source water may vary. At UK prices, I would prefer to use additional DI only if I can replenish it myself, but if I need to bite the bullet, so be it. In which case, given the expected RO output, would like to know the number of gallons I could reasonably expect before exhaustion.
I almost certainly need to import the kit....in the UK a high silicate rejection membrane costs about USD 200, a Kent Silica exchange module about USD 80 ! I do not joke......I weep.
Hope this sets out the problem I face and the result I seek. If you think that I should call you to discuss, then please post a number. Please don't be on the West Coast.....
Many thanks in advance for your advice, sorry for length of post but I wanted to set out all the info.
:)
kim
I hope that you can help me. I have discovered that I have high silicates in my tapwater, I estimate between 10 and 15 ppm using the Salifert test kit (diluting my sample with proven silicate-free DI).
I estimate that my RO reduces these to around 2 ppm, my DI has little additional impact. I am happy with the RO performance, but not realising the severity of my input, I have clearly bought the wrong membrane. It does what it says it should do.....
I use a generic TFS membrane made by Filmtec (MM-TFF 45/75), have good domestic water pressure and (the way it is plugged-in) usually warmish water. I use intermittantly.
My DI comprises separate columns, two litres each of cation/anion resin, I do not know the specifications. At around this volume I thought that I was safe ! My resin is not saturated at present (at least, not generally ! ). The cation resin is colour changing (brown to red), I replenish myself (resin is horrendously expensive in the UK).
Set out below (together with a recap of SiO2) is the performance measured in conductivity:-
...............................microS/cm....................ppm SiO2
Source Tap...............675.............................10 - 15
RO Output..................55................................2
DI Output.................. 1...............................1.5 - 2.0
I can improve DI output by reducing flow, but at 1 uS/cm I am probably beyond the precision of my probe, a Tunze, and don't bother.
As an experiment, I ran a closed loop thru' my DI, passing a sample several hundred times and only succeeded in reducing silicates to around 1 ppm. Does DI simply become "saturated" wrt silicates specifically while remaining active for other ions ?
I would like to reduce my silicates to comfortably below 1 ppm, allowing for the fact that source water may vary. At UK prices, I would prefer to use additional DI only if I can replenish it myself, but if I need to bite the bullet, so be it. In which case, given the expected RO output, would like to know the number of gallons I could reasonably expect before exhaustion.
I almost certainly need to import the kit....in the UK a high silicate rejection membrane costs about USD 200, a Kent Silica exchange module about USD 80 ! I do not joke......I weep.
Hope this sets out the problem I face and the result I seek. If you think that I should call you to discuss, then please post a number. Please don't be on the West Coast.....
Many thanks in advance for your advice, sorry for length of post but I wanted to set out all the info.
:)
kim