BrewingTechniques

Technical Communications

Republished from BrewingTechniques' September/October 1994.

Parti-Gyle Brewing

I am writing in reference to the article "Parti-Gyle Brewing" by Randy Mosher (BrewingTechniques 2 [2], 36-39 [1994]). The author states that the total extract will be split equally between the first third and the last two-thirds of the runoff volume, or split two-thirds/one-third between the first half and the second half of the runoff volume. It occurs to me that the distribution of extract between the early and late runnings from the mash will depend to a great extent upon the mash thickness and sparging rate used. If the author used a standard mash thickness and sparge-to-mash-water ratio to develop the extract split rules, it should have been provided in the article. A general relationship including the additional variables would have been even useful, as some brewers adjust the mash thickness, and possibly the sparge rate as well, to suit the specific recipe being brewed.

Martin Manning
Cincinnati, Ohio

I read Randy Mosher's "Parti-Gyle Brewing" article with interest, as I have been using a similar technique for about a year now. I approached the calculations from a different angle, which may be of interest.

I assumed that, at the end of the mash, a certain concentration of sugars will be dissolved in the liquor, in equilibrium with the sugars still in the grains. The equilibrium sugar concentration should depend only on the ratio of water to grain (for a given grain mix and set of mash conditions, anyway).

I have done some experiments that verify this hypothesis, within "homebrew precision." I offer the following table (Table I). The specific gravity column is rounded to the nearest 0.005 points; the extract efficiency column to the nearest point (0.001 SG).

As you can see, I also found that about 0.6 qt of water was absorbed per pound of grain. From the table, I can then calculate how much grain and water I need to make a first-runnings wort of a given gravity.

For example, to make 3 gal of barleywine at 1.100, I could take 4 gal at 1.075 and boil it down to 3 gal. From the chart, I would use a water/grain ratio of about 1.6 to give me 1 qt/lb out. Thus, to get 16 qt of wort, I would need 16 lb of grain and 16 X 1.6 = 25.6 qt of water in my mash.

I usually then sparge the grains normally to take a second, lower gravity wort. Continuing with the barleywine example, the first runnings took about 19 points extract/lb. Assuming my overall extract efficiency to be 30, about 180 points are left. If I sparge enough for a 5-gal batch, I should end up with a gravity of about 1.036 for a nice bitter.

If I want a heavier second wort, I can start with more grain and water, still in the 1.6 ratio, and take only 4 gal of first runnings before sparging normally for the second wort. To get 5 gal at 1.045, I would need an additional 9(5/30) = 1.5 lb of grain, and my mash liquor would increase to 28 qt.

How does this compare to Randy's tables? Let's consider the first line in his Table 1. Per gallon of first runnings, I would need 5 lb of grain to get a total batch gravity of l.050. I would mash with 8(5 X 1.6) qt of water, and take 1 gal at 1.075, removing half the potential extract (as he notes). I could then sparge an additional 2 gal with a specific gravity of 1.0375, as he indicates.

Spencer Thomas
Ann Arbor, Michigan

Mosher responds: Spencer Thomas has expanded on the idea of parti-gyle brewing in a sensible and useful way. I have taken the liberty of rearranging his table to make his ideas a little clearer (Table II). This will be a useful method to follow for those seeking complete predestination of their brews because it makes it easy to calculate the total strength and volume of any given

runoff. My usual (simpler) method is to run off first and second runnings as normal, then mix them to get the desired gravities, which may still be necessary with these calculations, especially if the two batches are intended to be close in gravity. This method, however, is indispensible for obtaining very high gravity worts.

I think the first three columns of Table II are pretty clear after you read Spencer's letter. The fourth column represents the amount of extract removed from the mash during the first runnings, at various dilutions. This table is based on mashes that get about 1.030 of extract/lb/gal of wort in the total batch. This number gives you an idea of the amount of extract remaining and available for collection during the second runnings.

Randy Mosher
Chicago, Illinois

Kegging ales


There are numerous methods for carbonating kegged homebrews, from priming to shaking, and just as many arguments over the pros and cons of each method. Here's a method that works well for me and resolves some of the problems presented by other methods.

The typical method for quick carbonation is to rack the cleared beer into a keg, purge the headspace with carbon dioxide, turn the carbon dioxide pressure up to 30 psi, and shake vigorously. Though this will give you a carbonated beer in half an hour, it has some drawbacks. First, if there is any oxygen left in the headspace, the vigorous shaking can lead to oxidation problems. Second, some brewers have reported that a beer's head retaining ability is diminished by excessive foaming.

After much consultation with other home brewers, I have settled on a method for ales that clears and carbonates the beer concurrently.

Once fermentation is effectively complete but the yeast is still in suspension, I rack the beer into a keg. I add finings (usually gelatin or isinglass), flush the air out, then fill the headspace with about 35 psi of carbon dioxide. I make sure the headspace pressure is topped up once or twice a day, and in four days at cellar temperature the beer is both clear and properly carbonated.

At that time I bleed off excess pressure, set the regulator for dispensing pressure (~10 psi), and enjoy the beer. To avoid yeast in the glass, I trim an inch off the end of the dip tube so that it sits just above the yeast sediment. One could use a full-length dip tube and bleed the yeast off the bottom, but I personally prefer to use the short tube method.

If you want to drink your beer immediately after kegging then by all means use another method. I use this method because it requires little effort, produces consistent results, and clearing is accelerated by finings and pressure, which means I can actually drink the beer sooner than if I let it clear in the carboy.

Ed Hitchcock
Dartmouth, Nova Scotia
Canada

Steam-Heat Injection Correction


A reader who contacted me via e-mail with some questions about my article, "Direct Injection of Steam for Mash Temperature Control" (BrewingTechniques 2 [4], 40-43 [1994]), was able to help me discover a minor error in the article. On page 42, at the top of the third column, I mention drilling an 11/16-in. hole which is to be tapped with 1/8-in. MPT threads. Unfortunately, 11/16 in. is the wrong size for these threads; it should read 11/32 in. (Most readers who set out to build such an apparatus would quickly notice the discrepancy once the required parts were in hand.) I apologize for this oversight.

Kelly Jones
Salt Lake City, Utah

More on the BruProbe

In "High-Tech Home Brewing" (BrewingTechniques 1 [2], 50-53 [1994]),the author described how to make a 3-ft brass probe with a temperature sensor at the end and how to build a circuit to display the temperature. He also mentions that you can buy the prefabricated wand and a PC board for the circuit from J.B. Distributing (Hollis, New Hampshire), What he didn't tell you is the following:
  • J.B. Distributing sells the wand for $20. The sensor alone costs $15.40 from Digi-Key.
  • The PC board is $25, or $35 for the wand and the PC board together. Shipping is $5.
  • The wand is thinner and better built than the one described in the article. The end is brazed shut before the sensor is mounted so it is hermetically sealed.
  • The output of the sensor is 10 mV/°F, and the circuit is basically a voltmeter. If you have a digital multimeter, you just need to connect a supply to the sensor (I used a 9-V battery with a 100-W resistor in series as per the circuit described in the BrewingTechniques article), connect it to your digital multimeter, and you're in business.
    I finally got to use it last weekend (it was a Father's Day present) and it works great!
    Usual disclaimer - no financial interest in J.B. Distributing, just a satisfied customer.

    Jim Grady
    North Andover, Massachusetts

    Closed-System Home Brewing

    Thanks for the great job you did on my article in last month's issue (Closed-System Home Brewing, BrewingTechniques 2 [4], 48-51 [1994]). The only error I detected was the "bottling" graphic which showed the hoses hooked up backwards, and some extra pieces of rigid tubing were attached to hoses where they weren't necessary. However, the basic concepts were clear, and I hope will prove useful to brewers.

    There are two things I should have included in the article. First, the concept of pushing beer from carboy to carboy was passed on to me by Deneb Williams, who is now the executive chef at the Medicine Bow Brewing Co. in Cheyenne, Wyoming.

    Second, if a brewer adopts the techniques described in my article, it is absolutely crucial that the cooled wort be sufficiently aerated before pitching the yeast. I recommend running the aeration setup for at least 45 min. If you don't, your fermentation will be sluggish and probably incomplete. Because you are racking into a carbon dioxide-purged carboy, the only oxygen in your wort is what you put there with your airstone. Don't cut corners on this important step.

    Again, thanks for the great job and fantastic publication. Fal Allen's article will be invaluable to any brewer with aspirations of becoming a pro.

    Bennett Dawson
    The Brew Lab
    St. Albans, Vermont

    Thanks for the update. The figure at top shows the graphic as it should have appeared.-Ed.

    RIMS Controversy

    Although the latest issue of BrewingTechniques contains the usual plethora of excellent articles and ideas (kudos to Fal Allen for his excellent article - I can't wait for parts II-IV!), Dave Miller's column (at page 22) contains a world-class airball.

    Contrary to his understanding, RIMS systems do clarify wort by recirculating it through a grain bed, and they do not pump the grain through the pump or heating element tube. Indeed, the false bottom and use of a well-developed filter bed are the real hallmarks and advantages of the RIMS system, as they promote quick and thorough conversion and a sparklingly clear wort.

    Nor is it that constant agitation produces excessive tannin extraction in RIMS systems - excessive tannin extraction is due almost always to (1) excessive sparging, (2) not keeping the pH of the mash/sparge water below 5.7, or (3) hot-side aeration (which is not a problem with a properly designed and used RIMS system). I've never had any problems with huskiness or astringency on any of my batches (I use a modified prototype of the Brew Magic RIMS from Sabco [Toledo, Ohio]).

    Louis K. Bonham
    Houston, Texas

    In the recent issue of BrewingTechniques, Dave Miller says, "As I understand it, the RIMS design does not clarify wort. It pumps the whole mash - grain and all - around and around through a tube."

    This is completely wrong. A RIMS system uses a false bottom and pumps wort out from under the grain and deposits it back at the top of the grain bed, having heated it as it passes through the tube. One of the great advantages of a RIMS system is that it produces brilliantly clear wort, usually by about halfway through the saccharification rest.

    Dave goes on to mention how the bad rap of excessive agitation in RIMS has been corrected by later systems. Thanks to him for dispelling this myth. Wort properly returned to the top of the grain bed through a manifold will not disturb the grain bed at all and causes no agitation of the grain at all throughout the entire mash. I cannot imagine any other system which could agitate the grain less.

    Miller says, "My own view of the RIMS approach is that it seems to be a solution in search of a problem. The system's claimed advantage is precise temperature control . . . impressive . . . but not really necessary."

    The advantage of a RIMS system is in its ease of use. I agree that 0.1 °F control is overkill, but still, it cannot hurt. The advantage is that I can do an upward step infusion mash with no more effort than turning the dial to the right temperature at the correct time. I never have to worry about scorching, raising temperature too quickly or too slowly, or overshooting a temperature for a particular conversion rest.

    In fact, I liked the idea of precise temperature control with no hassle so much, I waited to convert from extract recipes to all-grain until I had my RIMS system working. It is a delight to use and allows me to "relax, and have a homebrew" while I am brewing, not run around like crazy between stove and ice water bath trying to control the temperature of a mash.

    Dion Hollenbeck
    San Diego, California

    Just a note to correct Dave Miller's possible misunderstanding of RIMS designs and how they work. . . . He goes on to describe a "system" with ±0.1 °F precision temperature control. One might assume he's attempting to describe the very successful Brew Magic Brewing System, which uses the RIMS technology and is used both as a pilot system in commercial breweries and as a self- contained small-batch brewhouse for the advanced home user.

    With the Brew Magic, the whole mash, grain and all, does not get pumped around an around as he suggests. Only the wort is transported, very gently at that, through stainless tubing, at a regulated speed, past a microprocessor-controlled heating element and back to the top of a static mash filter bed. There is virtually no agitation whatsoever. Furthermore, hot-side aeration, caramelization, and frothing and foaming are negligible with this design. Yield efficiency is vastly improved with RIMS, and yet at the same time the variables inherent with the typical mash-mixing, air-pushing, hot-spot methods have all but been eliminated.

    Five years of development and brewing on this system have passed without any apparent fermentation difficulties resulting from an almost crystal clear wort. For large batch sizes (beyond this system's capacity), perfect temperature control becomes progressively more difficult, and minor changes in product appearance and flavor become less obvious. However, with decreased volume pilot recipe testing and smaller batch homebrew production, subtle changes in methodology, temperature, and equipment handling become more serious threats to accurate, repeatable brews.

    All in all, I feel that any technique, RIMS or otherwise, that improves consistency in brewing is a welcome "necessary" topic for major brewers, microbrewers, and home brewers alike.

    Bob Sulier
    Sabco Industries
    Toledo, Ohio

    As the person who wrote the question to Dave Miller regarding RIMS and lipids, I feel that I should address some inaccuracies in his reply. I think that he has a basic misunderstanding of the way in which RIMS works. In a RIMS system, only the wort is recirculated.

    Essentially, RIMS is a modified lauter tun. The wort is collected from underneath a false bottom and is recirculated with a pump. En route, it passes by an in-line heating element that maintains the wort at a specified temperature. Although not all brewers may heat the first runnings during recirculation, it is thus far the same procedure about which Mr. Miller was writing in the March/April issue ("Wort Recirculation Questioned," BrewingTechniques 2 [2], 14-16 [1994]).

    The differences between RIMS and a traditional vorlauf are that in RIMS the wort is recirculated during the actual mash, and the heating element and flow rate are used to maintain and adjust the temperature. As you can see, a well-designed RIMS system would call for minimal disturbance of the grain bed.

    This technique is attractive for three reasons: accurate temperature control within ±0.1 °F, a higher extract yield, and a brilliantly clear wort. The latter is achieved because the wort is continuously clarified by the natural filter bed that the grains create.

    What this all amounts to is a really long modified vorlauf of sorts. In his March/April article, Miller suggests that overzealous clarification might result in a lipid-poor wort which could contribute to fermentation problems. Given that assumption, it seems natural to me that a RIMS produced wort would, indeed, be deficient in lipids. Could you please re-address this question, and could you also explain how a RIMS system designed to minimize agitation of the grain could extract more tannins than a standard infusion mash? Does the mere action of the water flowing through the grain bed extract more tannins when taken to this extreme?

    Samuel Lloyd Kinsey
    New York, New York

    Miller responds: I am sorry for muddying this issue with old information. Some years ago, I saw a prototype RIMS system and talked about it with Rodney Morris, its inventor. Subject to his correction, my recollection of that conversation was that the prototype did circulate the mash - not just the wort. If that is the case, then the newer versions now on the market represent a fairly major redesign. Such a redesign would make the system less prone to tannin extraction. As for overclarifying the wort, I find it difficult to believe that this is possible for most small-scale brewers, regardless of how long it is recirculated.

    Dave Miller
    St. Louis, Missouri

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