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H2O SystemsInitial Prototype
Paulo JacobJennifer LiangJonathan TejadaAmi YamamotoJoy Yuan
Thursday April 6, 2006
Prototype Design Parameters
Biology
Water flow Electricity
Bacterial Culture PrepWater Sample PrepBacterial Quantification
Flow RateResidence Time
Breakdown of waterAnodizing TiCircuit Diagram
Prototype
Electrical Behavior• So far, we’ve shown that our proposed electric
field of 1-5 x 105 V/m is lower than the dielectricstrengths of water and air (100-300 x 105 and30 x 105 V/m respectively)
• Here we describe our efforts in preventingelectrolysis of water by insulating the electrodes.Also, we provide a comprehensive electricaldescription of our device through a circuit modelwhich guides our materials selection for thedevice.
Electrolysis of Water• Not to confuse with dielectric
breakdown potential of water,which pertains to the threshold atwhich “electron avalanches” occur.
Ref. Jones et. al. J. Appl. Phys. 77, 795, 1995• Electrolysis of water involves
electron transfer between watermolecules and electrically chargedmetal electrodes.
• Hydrogen and oxygen gas (thebubbles) are produced in thecathode (-) and anode (+)respectively. OH- and H+ are left inthe solution.
• GOAL: Prevent electrolysis ofwater
- +
+-
At the Cathode (-):2H2O + 2e- H2 +
2OH-
At the Anode (+)2OH- H2O + 1/2O2 + 2e-
Total Reaction:H2O H2 + 1/2O2
H2O +elecrolytes
Ti
Circuit Diagram
Wat
er
Ti
TiO2 or Polyester shimstock
Polyestershimstock
Ti
-
The device can be electrically represented by a circuit diagram in which one capacitoris in series with two other in parallel to oneanother.
Circuit Diagram• This treatment assumes the ideal
non-conducting behavior (noelectrolysis) and is useful toestimate the electric field andpotential in each component,especially in the water.
• κ is dielectric constant and ε ispermittivity, which are materialsproperties
• The values for the dielectricconstants are:
• TiO2; κ 1=14-170 or Polyester κ 1=κ 3 = 3.2
• H2O; κ 2= 80-
ε1, κ1ε3, κ3
ε2, κ2
Vapp
Ref. www.matweb.com
Solving the Circuit
-
C1
C3
C2
The equivalent capacitance for thiscircuit is:
Ceq=C1(C2 + C3)C1 + C2 + C3
Capacitance can be expressed as:
Ci = εiAd
, where ε0 = 8.854x10-12 C2 /Nm2 is the permittivityof free space, εi is permittivity of materialA is area and d distance
κi = εi / ε0
Q=CV
Vapp
Solving the Circuit
-
C1
C3
C2
Under these assumptions, thevoltage across each component is:
The electric field in each component canbe obtained through:
V1=
Vapp
Vapp (C2+C3)C1+C2+C3
V2= V3=VappC1
C1+C2+C3
But each capacitor modelsone material. The voltage dropcan be treated as linear
Ei=Vi/di
Solving the Circuit
-
C1
C3
C2
Therefore, the electric field acrosseach component can be expressedas:
E1=
Vapp
Vapp (C2+C3)(C1+C2+C3)d1
E2= E3=VappC1
(C1+C2+C3)d2,3
This enables us to predict theeffects of the insulating (electrolysisprotection) on the actual electricfield on water. As depicted earlier,capacitor 2 (or 3) stands for water. Ifthe capacitance of capacitor 1 is low(as in polymers) the field throughwater will decrease. Morequantitatively…
Quantitatively
1 cm
10 cm
5 cm
1 - Surface Area of insulating layer (TiO2 or polyester shimstock): 5x10-3 m2 , d~1x10-9 m forTiO2 or d= 12.5x10-6 m for shimstock.
2- Surface area of water layer: 3x10-3 m2 , d=127x10-6 m.
3- Surface area of shimstock window: 2x10-3 m2
d= 127x10-6 m.
Therefore, the capacitances are:1.1 - C1,TiO2 = 6.2x10-6 to 7.5x10-5 Fand C1,ST = 1.13x10-8 F
2.1 - C2,H2O = 2.8x10-8 F
3.1 - C3,ST= 1.12x10-9 F (Shimstock window)
Expected E-Fields• Therefore, the expected E-Field across the water (capacitor 2), for
the different insulating options under 25V are:– Using Shimstock: E2 = 359.23 V/m– Using TiO2: E2 = 1.9x105 to 23.8x105 V/m which falls in our targeted
range• There is a clear advantage in using anodized Ti under these
considerations, as it allows for lower voltages in order to obtain thelysing electric field. The changes in electrical field in each capacitoris caused by the distribution on potential between each capacitor,that in series must add to the total voltage. However, this distributiondepends on the dielectric constants, which can guide our materialsselection.
Insulating Attempts• As shown above, due to dielectric constraints, anodized Ti makes a
better suited insulator to minimize the electrolysis of water.
• Although the ohmeter measured TiO2 and polyester shimstockresistances cannot be resolved (too high), their calculatedresistances differ substantially. Through R=ρl/A, where ρ isresistivity, l length and A cross-secional area, we obtain:– TiO2 ρ=1011 to 1016 Ωm thus, RTiO2= 2MΩ to 2x105 MΩ– Polyester coating ρ=1013 Ωm thus R = 524.3 MΩ
• Therefore, anodized Ti provides both high resistance and gooddielectric properties. However, we observed poor prevention ofelectrolysis with anodized Ti when compared to polyester shimstockcovered electrodes.
Insulating the Electrodes:Anodized Ti
• Titanium anodization occurs byplacing a piece of titanium asthe anode in an electrolytic cell.TiO2 is formed on the surface ofthe sample, which providescorrosion resistance andelectrical insulation.
• Anodization took place with 30Vfor 1h. The current raised from~0.32A to 0.80A. The solutionemployed was 0.1M NaOH, withpH~13, as specified by SAEAMS 2488.
Color change observed in early stagesof anodization.
Insulating the Electrodes:Anodized Ti
• The resistances of theanodized layers andthe titanium weremeasured on thesurface by placing thevoltmeter probes onthe surface, separatedby 1cm
0.22Bare Ti
Resistance[Ω]Part
1013-1018 ΩcmResistivityof TiO2(anatase)
Not resolvedGrey region
50Blue layer
Ref. www.matweb.com
Insulating the Electrodes:Anodized Ti
Current Build Up in Anodized Ti Sample
-200
0
200
400
600
800
1000
1200
0 5 10 15 20 25
Applied Voltage (V)
Ob
served
Cu
rren
t (m
A)
The plot depicts the change in current as voltage was applied across the Ti electrodes, one of them anodized (the cathode in this case). Below we see the set up used.
A- +
- +
AnodizedElectrode
Water flow
TiO2 film thickness0nm ~200nm
Insulating the Electrodes:Anodized Ti
• Currently, we observe bubbles when running waterthrough the anodized device, which means electrontransfer occurs between water molecules and theelectrode plates.
• This can be due to the small films formed, because ofvoltage limitations
currentrange
Our Goal
Insulating the Electrodes:Anodized Ti
• Ideally, the sharp increase in current should beobserved at voltages higher than our targetoperating potential of 25V. This way electrolysisof water would be avoided.
• Power supply capable of higher voltages isnecessary, in order to assess the feasibility ofanodized titanium as means to preventelectrolysis of water.
• Possibility of TiO2 interacting with ions in water?
Insulating the Electrodes:Polyester Shimstock
• We also tested theperformance of theshimstock coating thesteel prototypeelectrodes underincreasing voltages.
• The shimstock proved tobe an efficient barrier forelectrolysis at thevoltages analysed:
• No bubbles wereobserved throughout theexperiment
Steel Coated with Polyester Shimstock
00.511.522.533.5
0 10 20 30 40
Voltage (V)
Cu
rren
t (
mA
)
Insulating the Electrodes:Summary
• As shown above, anodized Ti hasgreat potential as an insulating layer.However new attempts to createbetter films must be performed. Theuse of polyester shimstock has beenproven to be effective, however highervoltage supplies will be necessary inorder to create the target electric fieldthrough water.
Biology: Bacterial Culture
www.qiagen.com
Want bacteria to be inexponential growthphase duringexperiment
For every experimental run:1. Inoculate overnight culture day before2. Dilute o/n culture in fresh media
morning of run3. Prepare water sample from culture and
run experiment in afternoon
Biology: Water SampleTarget concentration ~ 272 cfu/ml
– Average E. coli concentration in Charles River– Concentration controlled by dilutions performed the
morning of the experiment
Stainless Steel system:– 40 ml total volume (20 ml/syringe)– prepare 45 ml sample = 9 ml culture + 36 ml water
Ti system:– 30 ml total volume– prepare 35 ml sample = 7 ml culture + 28 ml water
Biology: Bacterial Quantification
LB Amp plates1. Plate 100µL water sample
– Perform dilutionbeforehand if necessary
2. Allow 1 day to grow3. Count colonies
Spectrophotometer1. Transfer 1ml sample to
cuvette– Perform dilution
beforehand if necessary2. Measure OD6603. Calculate concentration by
Beer’s Law: A = εcl
• To be performed before and after each experimental run• 2 methods of bacterial concentration quantification:
– LB Amp plates– Spectrophotometer
• Decrease in bacterial concentration = indication of cell lysis
Experiment Set Up
Water In
Water Out
Power Supply
Weight
To control flow rate, will apply aconstant load » constant pressure
Water Flow: Controlling flow rateConstant Load
Constant PressureConstant Flow Rate
Flow Rate vs Applied Mass
y = 3.4586x - 2.9095R2 = 0.9593
0.00
1.00
2.00
3.00
4.00
5.00
6.00
0 0.5 1 1.5 2 2.5
Mass (kg)
Flo
w R
ate
(ml/s
)
Couette Flow
P = =3µLQ2Wd3Area
mg
Water Flow: Setting flow rate
Flow Rate [ml/s] = 3.46(Applied Mass [kg]) – 2.91Target Flow Rate = 1 liter/hour = 0.278 ml/s
Residence Time = Volumewater flow region / Flow RateTarget Residence Time >> 17 ms
Taking the target flow rate and required residencetime into consideration, we conclude that:
a ~1.5 kg weight will yield our desired results at a flowrate of ~2.3 ml/s and a residence time of ~134 ms
Initial PrototypeTesting procedure:1) Setup system design and attach
onto a stand.2) Prepare water sample for testing.3) Determine bacterial concentration
of pre-treatment water sample.4) Load water sample
(20mL/syringe in 2-syringe SSsystem; 30mL in 1-syringe Tisystem) into syringe(s) andremove air bubbles.
5) Clamp syringes onto stand tostabilize.
6) Set voltage at 25 V.7) Apply load onto syringe(s) and
allow entire volume of sample torun through system.
8) Determine bacterial concentrationof post-treatment water sample.
Gantt Chart
Modification
Testing
FinalPresentationPreparation
Construction
MaterialAcquisition
Design
Research
5/11-5/184/27-5/104/6-4/263/16-4/52/23-3/152/9-2/22
Questions?
Titanium Electrode Setup