The Chlorate concentration at which the current efficiency starts to decline
is not fully agreed in the literature. There are a lot of variables that effect
the point at where the low Chlorate concentration effects current efficiency. I
have assumed that it is effected at about 100g/l Chlorate which is roughly where
it happens in a fairly typical cell.
1 Mole Na Chlorate = 106.45g (+16 grams for Na Perchlorate) |
Run time in minutes per gram of
NaClO3 for 50% and 80% current efficiency's (no Chloride present in the cell at start, additives used, F or Persulphate) | ||
---|---|---|
Amps | 50% current efficiency Chlorate level below about 5g/l (at the end of the run) |
80% current efficiency Chlorate levels above 100g/l (at the end of the run) |
2 | 30.19 | 16.23 |
4 | 15.09 | 8.11 |
8 | 7.54 | 4.05 |
10 | 6.03 | 3.24 |
15 | 4.02 | 2.16 |
20 | 3.01 | 1.62 |
30 | 2.01 | 1.08 |
50 | 1.20 | 0.649 |
75 | 0.805 | 0.432 |
100 | 0.603 | 0.324 |
150 | 0.402 | 0.216 |
To put the table into perspective, @ 80% current efficiency you will convert 1g of NaClO3 into 1.15 grams Perchlorate ever 32.5 minutes per amp. |
That's 106.5g(one mole) NaClO3 converted into 122.5g Perchlorate every 57.3 hours |
The table
above assumes that you have not used Chlorate solution to top up your cell if it
needed topping up, it assumes you used water. If you use Chlorate solution you
can take a similar approach to calculating run time as used in the Chlorate run
time section.
When the cell is run for a length of time shown in the 50%
coulomb there will be very little chlorate left in the cell.
The current
efficiency will be about 80% when the Chlorate levels are above about 100g/l but
as the Chlorate level drops below the 100g/l mark (as more and more Perchlorate
is formed) the current efficiency drops and you get an overall current
efficiency of 50% if you run your cell to the point where there is very little
Chlorate left (ie. the run time in the 50% coulomb). This saves labour and you
can take out nearly pure Perchlorate out of the cell by simply evaporating off
all the water. You may wish to destroy the small amount of Chlorate left in the
cell first by chemical means.
If you want to run your cell and stay in the
high current efficiency region (>100g/l Chlorate) then you can stop running
your cell at the recommended time in the 80% coulmb and take out a crop of
Perchlorate. You should be able to get a crop of Perchlorate out by evaporating
off some water and also by adding some highly concentrated solution of Chlorate
which will help to ppt out the Perchlorate. Adding a small amount of solid
Perchlorate might help to start precipitation of the Perchlorate load. This
method of extracting Perchlorate from a cell will be very difficult for the
amateur to do successfully. I would recommend running your cell for long enough
(50% coulomb) for to convert nearly all of the Chlorate into Perchlorate and then
destroying residual Chlorate by Chemicals.
All mother liquor should always be
returned to the cell as it will be rich in Chlorate and Perchlorate because of
their high solubility.
Note that Platinum Anodes will corrode if used to reduce the Chlorate concentration
to a low value.
You need Lead Dioxide if you wish to run a cell from Chloride to
Chlorate to Perchlorate to Low Chlorate concentration, without stopping and use an
additive to stop cathodic reduction (F or Persulphate).
HIT THE BACK BUTTON ON YOUR BROWSER