Hi I am a newbie at this game. To date I have only completed 2 Turbo washes. Currently underway I have a TPW and a DWWG. I have been lurking around the Forums reading many interesting articles and posts. I really would appreciate any and all help.
I have a few questions the first are from an excellent article on High ABV Sugar Washes on www.homedistiller.org a site commonly referenced from this forum.
!). I note that the wash should remain aerobic for the first 48 hours and that the yeast should remain in suspension for the entirety of fermentation. To this end I thought a small submersible pump could assist. Has anyone tried this and if so what sort of pump did they use. My thought was to use a pump from the aquarium world.
2). I need some confirmation or correction of my perception of brix. As I understand it an initial SG of 1000 means zero sugar zero ethanol and zero brix (ie pure water). Whilst an initial SG of 1040 for a sugar wash prior to yeast addition represents a wash very near a brix of 10. Therefore to keep the brix sub 20 the initial wash should remain below SG 1080. Now as the wash ferments and ethanol is produced the SG falls. At about SG 1000 the mash should contain approximately 10.5% ABV. A pure water ethanol mix of 10.5% should produce a SG of slightly less than 980. Therefore the mash at SG 1000 should have a brix of 5. Now the article refers to maintaining the brix between 4 and 6 brix so when the SG drops to 996 some sugar could be added to bring the wash to 6 brix. Overall the remaining sugar to create the additional rise in ABV of 5% should be added in 2 brix increments or an SG increase of 8 keeping in mind the fact, that as one approaches 15% ABV a pure water ethanol mix would have an approximate SG of 970 and the SG of a 4 brix wash will drop to 986.
In summation, one starts by adding sufficient sugar to bring the sugar water mash to 1080. At SG 996 one adds 10% of the original sugar volume (inverted of course) which should raise SG to 1004 now when the SG drops to 994 one adds another 10% and allows the SG to drop to 992 and so on until the total amount of additional sugar reaches 50%. One then allows the fermentation to proceed to completion hoping for an SG of 970 but in reality somewhere between this reading and 980.
To my mind practically all this could be achieved simply through the dissolving of the total amount of sugar with an invertase in 4.5 litres of water. For a total wash of 23 litres, 3 litres of this could be added to 17.5 litres of water containing the tomato paste the yeast is then activated at the same temperature as the water (80F) in a further 1 litre of water and added to the water sugar wash. A fish tank heater could be set to keep the wash at this slightly elevated initial temperature and the temp lowered after 48 hours when the wash goes into its’ anaerobic stage through the addition of the fermenter lid and airlock. The additional sugar could then be introduced through 5x300ml additions of the left over sugar mix at the appropriate SG readings.
I note that most suggest keeping the ABV sub 10% is this because of taste or the extra rise is seen as too much trouble? In my naivety I see the pump for continual circulation as being highly beneficial. It is my intention to apply this methodology to my next TPW unless, of course, someone notes serious errors in my thought process.
The next question arises from an article on the commercial distillation of Scotch Whisky.
3). A reference is made to new yeast not being able to put up with the rigours of high ABV. The remedy for the commercial Scotch whisky makers is to add “brewers yeast” from the top of a fermenting beer. Referring to Scotch this would be UK based info and as they mainly consume ale rather than lager – Does anyone know if there is a difference? Has this been tried? I can find no general reference.
The next question arises from general forum lurking and refers furfurals
4). It would appear that high temperatures when distilling either at the immersed element/wash interface or the bottom of the boiler/wash interface when heating with propane can burn suspended solids creating unpleasant flavours from the resultant furfurals. My question is, has anyone here tried heating the fermented wash in the still with recirculated water through a coil in the bottom of the still tank. And if so what sort of pump did they use to circulate the near boiling fluid? I note that the recirculated fluid could have its’ boiling point raised by adding salt to the fluid. Further I note that most commercial breweries use this method to heat the wash in their stills.
5). Oh and one last question – Has anyone tried the addition of salt to the fermented TPW wash prior to distilling so as to raise the boiling point of the water and create a greater temperature differential between water and ethanol. If so was it successful or did it introduce new problems?
Regards