I want to promote Scale Buildup in pipes and pumps
I want to promote Scale Buildup in pipes and pumps
(OP)
(Please excuse a newbies cross-posting. I first put this in Process Development, but I think this is a better forum.)
This probably sounds strange but I want to cause scale. I want to build a test bed to compare different pumps and their relative ability to tolerate scale that might occur in drinking water systems. While I would like to accelerate the rate of buildup; it would also be fairly important to have the areas of precipitation to be similar to real world systems. For example, would there be less scale in high flow areas and more in stagnate areas? I wouldn't want to precipitate free particles in the fluid stream (unless this too happens in real life).
I am a mechanical engineer with a fairly limited background in chemistry. So feel free to "talk-down" to me in the answer. What would the best salts to use? Should I start a little acidic and then adjust the PH higher over the test period?
This probably sounds strange but I want to cause scale. I want to build a test bed to compare different pumps and their relative ability to tolerate scale that might occur in drinking water systems. While I would like to accelerate the rate of buildup; it would also be fairly important to have the areas of precipitation to be similar to real world systems. For example, would there be less scale in high flow areas and more in stagnate areas? I wouldn't want to precipitate free particles in the fluid stream (unless this too happens in real life).
I am a mechanical engineer with a fairly limited background in chemistry. So feel free to "talk-down" to me in the answer. What would the best salts to use? Should I start a little acidic and then adjust the PH higher over the test period?





RE: I want to promote Scale Buildup in pipes and pumps
http://www.jaeger.com/1996foul.htm
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Calcium sulfate (CaSO4) or calcium carbonate (CaCO3) may be good salts to start (>1000 ppm). As for adjusting pH for these particular salts, say if you go from pH 4 to 9, scaling and fouling should increase with higher pH.
RE: I want to promote Scale Buildup in pipes and pumps
Two types of hardness are generally recognized: carbonate (sometimes referred to as temporary hardness) and non-carbonate hardness. Carbonate hardness, depending upon the nature of the water is composed of calcium or magnesium carbonates and bicarbonates. It is this form of hardness (calcium carbonate) that contributes most to scale formation. Non-carbonate hardness is normally a small component of the total hardness and is characterized by much higher solubility. As a result it's role in scale formation is generally negligibile.
Water hardness is classified according to a somewhat subjective criteria that varies from reference to reference. Table 1 provides a common interpretation. Scaling problems typically occur above levels of 100 ppm hardness.
http://geoheat.oit.edu/bulletin/bull21-1/art3.pdf
If you elevate the water pH above 10 to 11 pH units, your water will be scale forming (if the water hardness is above 35 mg/l of calcium carbonate hardness). From that point, the higher the hardness, the more scale that you will encounter.
RE: I want to promote Scale Buildup in pipes and pumps
As people have said here, you will have to elevate the pH of the water. I would suggest that for the pipe velocities you will typically encounter you will not able to prevent the scale from forming on the pipe wall.
RE: I want to promote Scale Buildup in pipes and pumps
Forgot to mention, if you elevate the temperature, the scaling will increase.
RE: I want to promote Scale Buildup in pipes and pumps
RE: I want to promote Scale Buildup in pipes and pumps
The CO32– reacts with Ca2+ or Mg2+ ions, to form insoluble calcium and magnesium carbonates which precipitate out. The key word there is INSOLUBLE.
Once material precipitates out of solution, the bulk of the material will not go back into solution unless you change the solution properties such as the addition of an acid.
Here is a picture of pipe scale. If what you are proposing is true, the material will not form the scale shown in the picture.
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RE: I want to promote Scale Buildup in pipes and pumps
In fouling applications in P&T systems I've seen, the pump efficiency is affected by the increased head from fouled pipes like the one in the picture you've shown. I suppose you could use anti-fouling pipes or cathodic protection to isolate the pump first.
RE: I want to promote Scale Buildup in pipes and pumps
However, if you are interested in the most common type of scale in potable water systems, then you should focus on the scale associated with water hardness.