...
Overview
After the failure of the second experiment in which distilled water was used, the team decided that calcium carbonates were probably not the source of the problem. It was thought instead that reaction kinetics were the limiting factor and that lime/water contact area needed to increase. The idea for the third experiment was to dramatically increase the volume of the lime in the reactor in order to provide more solid lime surface area. With the same flow rate as was used in experiment two (120 ml/min), 200 grams were added instead of 20, a ten-fold increase. In an effort to determine what the failure mode would be if lime were continually added without cleaning the reactor in between, the team decided to add an additional 200 grams whenever the effluent pH dropped below saturation. Because it seemed to perform better than the original, particularly with large amounts of lime, only the large reactor was used in order to save water.
...
The 200 grams lime were mixed with distilled water and stirred to form a slurry. This was fed through the vertical column. The flow rate was 120ml/min. All the other procedures were the same as described on materials and methods.
Results and Discussion
A As can be seen in the graph from figure 1 below, the effluent pH remained at saturation for approximately six hours after lime was added each time. The second half of the second high-pH segment must be ignored due to problems with the experimental set-up. Because excess lime was not removed from the reactor before adding the next 200 grams, a total of 600 grams of lime had been added to the reactor by the beginning of the third segment seen in the graph. Despite the fact that the reactor was overloaded, it seemed to perform no better with the new addition of lime than it did with the first, when there was far less solid lime in suspension. This suggests that only the "new" lime is effective in saturating the effluent.
By observing A2 reactor, the team found at the end of the experiment the previous large particles suspending in the vertical column shifted to the slanting tube with a decreasing of particle size, and the whole apparatus became murky compared to the initial stage.
Possible failure modes could be:
- Because the smallest particles dissolve fastest and are most prone to being carried out with the effluent due to their low settling velocities, they do not persist in the reactor even though it appears to be filled with solids. Since they have the highest surface area to volume ratio, the small particles are the ones that dissolve most effectively, whereas the larger particles, which may remain for a very long time, do not dissolve well enough to saturate the effluent within the residence time of the reactor. See the hypotheses page.
- Preferential flow paths form over time in the densely-packed reactor, so that eventually clean water is allowed to pass through with very little contact time with solid lime.
- Although the results from experiment 2 suggest otherwise, chemical/physical interference by calcium carbonate precipitate may still be part of the problem. See the hypotheses section hypotheses.
Fig 1. Experiment 3
This experiment used only the large reactor to test overloading the apparatus with lime, adding 200 grams of lime initially and whenever the pH dropped.