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Revolutionary New Cooling Solution PROVIDING EXTRA COLD, SUPER CHILLED DRINKS
• Aspecialistliquidcoolantwithanaccurate rangeoffreezepointtemperaturesavailable (-2°C,-3°C,-4°C,etc).• Providesauniform,crystallineicestorewith excellentenergyreserves.• Superiorthermal&heattransferproperties.• Reducescoolerenergyconsumption.• Anon-toxic,non-corrosive,stableliquid.• Apre-mixed‘Bag-In-Box’solution.
Water
Advantages: •Lessviscous•Hasicebankreserve•Excellentthermalproperties
Disadvantages: •Freezesat0˚C
Glycol
Advantages:Canbesetatlowtemperatures
Disadvantages: •Lowtemperaturecanonlybeheldforashorttime. •Noicebankreserve•Expensive •Moreremotesareneededtocopewithdemanddueto low reserve •Heavydutypumpsrequiredduetohighviscosity•Difficulttocontrol •Shelldatasheetswarnagainst •Verylimitedshelflife •Extrememeasuresrequiredtopreventcontactwith airduetohighabsorptionrates •Unstablemixturepercentageleadstocorrosion •Requiresengineerwithspecialistequipmenttocheckandtopup•Highviscosity.(seenextslide)•Extremelycorrosive(seenextslide)•Inferiorthermalandheattransferproperties(partlyduetohighviscositybutalsolowspecificheatcapacity)
Viscosity&Corrosion
ViscosityTests
GlycolDisadvantages•Highviscosity•Lowflowrate•Lessheattransfer•Strongerpump•Morecost
Uninhibitedglycolscanformvariousacidswhichareextremelycorrosive.
Evenglycolswithinhibitorsareonlyprotectedto25%strength.
Absorptionofwaterandconstantuncontrolledtopupsleadstoanuncontrollable,unstablesystem.
Glycolmixturesoflessthan25%arevulnerabletohotspotcorrosionwhichcancorrodeasystemwithinweeks.
GlycolCorrosion&BiologicalGrowth
25
33% Glycol @ -8˚c Water @ 0˚c
Types of Coolant
Comparison of Coolant Viscosity
Flui
dity
2flow
20
15
10
5
0
Actualpumpremovedfromaglycolbaseddrinksdispensesystem.
AdvantagesOf2Flow
•Freezesat-2˚C(enablingtheformationofanicebankreserve)
•Morecosteffective •Icebankreservemeanspeaktradingdoesn’trequiremorecoolers •Usesexistingcoolers
•Doesn’tneedexpensiveheavydutypumps •Farlessviscousthanglycol(flowratesalmostmatchingthatofwater)
•Excellentthermalandheattransferproperties(partlyduetoflowrates)
•Canbetransferredintoallstandardcoolers •Nondisruptiveinstallation
•Noncorrosiveandisnotharmfulortoxictotheenvironment
•2Flowis20%moreefficientthandiluteglycol(Seenextslidefordetails)
Energy Levels
Water
2Flow
Glycol
ON
/ O
FF
Compressor Usage
CS
CR
CS
CR
CR
CS
1 54 107 160 213 266 319 372 425 478 531 584 637 690 743 796 849 902 955 1008 1061 1114 1167 1220 1273
Time
CS = Compressor Start UpCR = Compressor Running
Glycolmixturescutinfarmoreoftenthan2Flow&water,leadingtoanincreaseinpotentialmaintenanceproblemsandenergyusage.
Test Results
1 21 41 61 81 101 121 141 161 181 201 221
Glycol
2flow
Water
Number of drinks (240 = 1 hour)
10.0
8.0
6.0
4.0
2.0
0
-2.0
-4.0
Tem
pera
ture
[°C
]
TE 25 draw testTinlet = 12°C; Python 15m insulation 19mm; 1 drink = 1 pint; flow rate = 1 pint / 9,5
sec; 4 pint / minute. 2flow and water with 8kg ice bank, glycol without ice bank.
UpgradeProcedure
•2Flowcanbeusedinanycooler •Switchoffremotecooler
•Removeiceandwaterfromsystemincludingpythonrecirculationpipes
•Establishtemperaturecontrolmethod •Ifmechanicalthermostatthensimplyreplaceexistingwithanew mechanicalthermostat •Ifelectroniccontrolwithprobethensimplyadjustsetpoint. •Ificebankcontrollerthenasimplerewireintoanewmechanical thermostatorbespokeconversionkitwillberequired.
•Refillwith2flow
•Attachinformationstickerstoremotecooler
•Switchonremote
TradeTrialUK
•Averagedispensetempbefore2.24˚C•Averagedispensetempafter0.74˚C•34ccremotewithadditionalunder countercooling
• Cellartemp11˚C• Ambienttemp25˚C• Pythonlength12M• Pythoninsulation19mm• Tempstakenexpod
0
0 .5
1
1 .5
2
2 .5
3
1 4 7 10 13 16 19 22 25 28 31 34 37 40 43 46 49
Trade Trial
Number of Drinks
Before
After
Linear (After)
Linear (Before)
EuropeanTradeTrial
Purpose:TocomparethetemperatureperformanceofBrewfitt’s2flowagainstthetemperatureperformanceofaregularcooler.
Day 1 Waterbath Celsius -0.01 -1.70
Pint Standard 2flow differenceCelsius
1 2.50 1.00 1.50 2 2.30 0.50 1.80 3 1.80 0.50 1.30 4 1.80 0.50 1.30 5 2.00 0.30 1.70 6 1.70 0.20 1.50 7 1.70 0.00 1.70 8 1.60 0.00 1.60 9 1.60 0.00 1.60 10 1.90 0.00 1.90 11 1.70 0.00 1.70 12 1.70 0.00 1.70 13 1.60 -0.10 1.70Average 1.84 0.22 1.62
Day 2 Waterbath Celsius 0.50 -1.10
Pint Standard 2flow differenceCelsius
1 4.20 2.20 2.00 2 3.10 1.60 1.50 3 2.90 1.30 1.60 4 2.90 1.30 1.60 5 3.00 1.40 1.60 6 3.00 1.40 1.60 7 2.80 1.40 1.40 8 2.90 1.30 1.60 9 2.90 1.40 1.50 10 3.00 1.50 1.50 11 2.80 1.30 1.50 12 2.80 1.40 1.40 13 3.00 1.50 1.50 14 3.00 1.50 1.56 15 2.80 1.30 1.53 16 2.90 1.50 1.53 17 2.90 1.40 1.52Average 2.99 1.45 1.56
Method:TwoCalypso9coolersweresetupundercounteronewith2Flowinthewaterbathandtheotherwithwaterinthewaterbath.
The2Flowcoolerhadaspecialthermostatfitted.Eachcoolerwasallowed24hrstobuildice.Thetrialwasdoneonkegsfromacoldroomat6˚candfromastoreat25˚c.
Conclusion:• 2flowwillgiveonaverage1.5degreesofa temperaturereductionoverthestandardwaterbath.• Recommendontradetrials.
-0 .500.000.501.001.502.002.503.00
1 2 3 4 5 6 7 8 9 10 11 12 13 14
celci
us
2Flow Vs Standard Waterbath Coldroom Keg
Pint
Water 2Flow
0.00
1.00
2.00
3.00
4.00
5.00
1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17
2Flow Vs Standard Waterbath Store Keg
Pint
Water 2Flow
celci
us
Results:
EuropeanTradeTrial2
Data: Congelationpoint(3Flow)=-3ºCTemperatureset-point=-4ºC Beer : SuperBockBeer(Alc.(v/v)=4,8andCO2(g/l)=5,1)
Congelationpoint(Super-BockBeer)=-2,2and-2,5ºC
Temperatureambient(kegtemp.)=20ºC Beerflow=2,44Lts/min
Conclusions: Forcontinuoustaping,thebeertemperaturerangedbetween-2,2and5,4ºC. Fortapingwithstops(5min),thebeertemperaturerangedbetween-2,2and-1,6ºC. Forthesametemperatureandwhenwehaveacontinuoustapingbeerthe3flowefficiencydecreases.
Super-Bock Beer (Continuous taping) 3 Flow
Volume Taping (Liters) tt (min)
3 Flow Liquid Temperature
(ºC)
Beer Temperature
(ºC)
Ice-bank formed
0 -2.9 -2.2 Yes2.7 -0.3 0.3 Yes5.4 0.2 1.2 Yes8.1 2.5 1.4 Yes
10.8 2.8 1.8 Yes13.5 3.6 2 Yes16.2 4.2 2.3 Yes18.9 4.2 2.6 Yes21.6 4.2 5 Yes24.3 4.1 5.2 Yes27 4.1 5.3 Yes29 ~12 4.2 5.4 Yes
Super-Bock Beer (Taping after every 5 min) 3 Flow
Volume Taping (Liters) tt (min)
3 Flow Liquid Temperature
(ºC)
Beer Temperature
(ºC)
Ice-bank formed
0 0 -2.9 -2.2 Yes2 5 -2.8 -2.1 Yes4 10 -2.6 -2.0 Yes6 15 -2.5 -1.9 Yes8 20 -2.4 -1.9 Yes
10 25 -2.4 -1.8 Yes12 30 -2.5 -1.9 Yes14 35 -2.4 -1.8 Yes16 40 -2.3 -1.6 Yes18 45 -2.3 -1.6 Yes20 50 -2.3 -1.6 Yes22 55 -2.3 -1.6 Yes24 60 -2.3 -1.7 Yes26 65 -2.3 -1.6 Yes
Results:
South Africa
UAE
Indonesia
Singapore
Canada
USA
Mexico
Chile
UK
Ireland
France
Spain
Portugal
Italy
Netherlands
Poland
Greece
Cyprus
Croatia
Austria
Australia
New Zealand
China
Japan
Hong Kong
Pacific Islands
2Flow Presentation 2010
UK Patent No: GB2441836Worldwide: PCT/GB2008/050177
BrewfittLtd,InternationalHouse,PenistoneRoad,FenayBridge,Huddersfield,WestYorkshire,UnitedKingdom,HD80LETelephone+44(0)1484340800Fax+44(0)[email protected]