AERATORS

AERATION

General theory for the oxygen transfer

As mentioned before the MO need the dissolved oxygen for the oxydation:Biochemical oxydation of carbohydrates: glucose C6H12O6 + 6O2 6CO2 + 6H2O Biochemical oxydation of ammonia (Nitrification) 2NH4+ + 3O2 2NO2- + 2H2O + 2H+ 2NO2- + O2 2NO3+ + 2H2O + 2H+General theory

General theory

General theoryWHAT AFFECTS THE AERATION EFFICENCY:

Oxygen transfer from the air bubble to the liquidGeneral theory

Volume VVolume 100% 100% 100%Surface 100% 126% 159%General theoryInfluence of bubble size

As a result the smaller the air bubbles are:

the larger is the bubble surface and by this, a larger contact layer air/water is obtained the longer the retention time will be Due to this facts more oxygen can be dissolvedGeneral theory

General theoryInfluence of the temperature

General theoryInfluence of the temperature

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Diagramm4

14.23

12.8

11.33

10.15

9.17

8.38

7.63

7.1

6.6

6.1

5.6

mg/l

Oxygen Saturation Values

Saturation value

A

Tabelle1

TemperatureSaturation value

1 C14.23

5 C12.8

10 C11.33

15 C10.15

20 C9.17

25 C8.38

30C7.63

35C7.1

40C6.6

45 C6.1

50C5.6

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As a result the cooler the water: the higher the oxygen saturation value and due to this the higher the O2 transfer Oxygen transfer tests should be made between +5C and +35C General theory

the higher the ambient pressure and due to this the higher the O2 concentration / contact layer

the longer the retention time will beAs a result the deeper the immersion depth:Due to this facts more oxygen can be dissolvedGeneral theory

General theoryCorrection factor of the altitude

Influence of the altitude of the plantAnother important point is the altitude of the plant, as the oxygen proportion of air decreases with increasing altitude.

(until 200 m above sea level is not relevant)General theory

General theoryThe main tasks of the aeration systems in activated sludge basins

The requirement to the aeration systemsGeneral theory

For the oxygen transfer of waste watersGeneral theory

ALPHA AND BETA VALUEGeneral theory

Alpha factorKla (sewage)

Kla (clean water) Type of aeration equipment Sludge age Conc. of surface active agents Type of waste water Intensity of mixing Type of process Location in the aeration basin Bubble size and velocity

Betaratio between the oxygen saturation in process water and in clean water.

_941021455.unknown

The value of depends onthe amounts of suspended mattersoluble organic compounds dissolved mineral salts

General influences on the oxygen transfer

1. Oxygen Transfer

Oxygen TransferComposition of air1 m3 air

Definitions of the American Standard ASCEOTR [kgO2/h] Oxygen Transfer RateSOTR [kgO2/h] Standard Oxygen Transfer Rate

Mass of oxygen per unit time dissolved in a volume of clean water by an oxygen transfer system operating under standard conditions:

Dissolved Oxygen (DO) = 0 mg/lWater temperature = 20CBarometric pressure = 1013 hPa sea level

Definitions of the American Standard ASCEAAE [kg O2/kWh] Actual Aeration Efficiency OTR per unit total power inputSAE [kgO2/kWh] Standard Aeration Efficiency

SOTR per unit total power input

Definitions of the preliminary European StandardOC [kgO2/h] Oxygen Transfer Capacity

OC is the mass [kg] of oxygen transfered by an aeration installation in one hour in a tank of certain size filled with clean water at:

Dissolved Oxygen (DO) = 0 mg/lWater temperature = 20CBarometric pressure = 1013 hPaaOC [kgO2/h] Oxygen Transfer Capacity in mixed liquor

Definitions of the preliminary European StandardaOP20 [kgO2/kWh] Aeration Efficiency in mixed liquor aOC per unit total power inputOP20 [kgO2/kWh] Aeration Efficiency in clean water under standard conditions

OC per unit total power input

Definitions of the American Standard ASCE

AOR[kgO2/h] Actual Oxygen Requirement

SOR [kgO2/h] Standard Oxygen Requirement

Conversionof SOR in AOR and vice versa

7

up to 1,5

1,2 4,5 0,95Fine BubblesSystemSurface AeratorsABS SubmersiblesTA OKI

0,65

4,5

0,75

max. 1,2

1,1 4SAE in clean water[kg O2/kWh]a-Valuesdepends on waste waterAs a resultAAE in waste water[kg O2/kWh]General theory

TO MAKE AN OFFER:1. SOTR and used -value2. AOR3. Process data:BOD5 inBOD5 outN inN total outNH4 outFlow amountTank dimensions and WLAltitudeDe nitrification involved?SBR process?

Waste Water CharacteristicsBOD, Biological Oxygen DemandCOD, Chemical Oxygen DemandNitrogenPhosphoruspHSuspended Solids

Typical Municipal Waste Water

BOD

mg/l

110 - 400

COD

mg/l

250 1000

Nitrogen

mg/l

20 85

Phosphorus

mg/l

4 15

Suspended Solids, SS

mg/l

100 - 350

1.) Clean water must be made oxygen-free before measuring --> addition of Na2SO3 or N2

2.) Switching on the aerator and measure the increase of DO from c = 0 mg/l up to the saturation (3 probes)

3.) The increase of the dissolved oxygen concentration proceeds very quickly until it runs asymptotically to the saturation value.

4.) Inclination of the curve= kLaStandard Oxygen Transfer Testvery short test descripiton

How to test it1 = Aerator2 = Air pipe3 = Thermometer4 = Oxygen probes 5 = Air flow meter6 = Power measuring7 = Test tank

Standard Oxygen Transfer Test

ABS / NOPOL AERATION SYSTEMS

Dissolved Oxygen level< 1 mg/l may limit the growth of micro-organisms2 mg/l safe value> 2 mg/l efficiency of aeration decreases

Other parameters

Aeration time in SBR something else than 24 hours

Aeration parametersStandard Oxygen Transfer Efficiency SOTE, (%)SOTE = SOTR / Air flow * 0,28Specific Oxygen Tranfer Efficiency SpOTE, (%/m)SpOTE = SOTE/submerged depthOxygen absorption, (g O2/Nm3*m)SOE = SOTR / Air flow * submerged depthStandard Aeration Efficiency, SAE (kg O2/kWh)SAE = SOTR / Power

ABS / NOPOL AERATION SYSTEMS

PIK 300 SOTE curve

Design of the aeration systemLoading to WWTPBOD-load (Kg/d)Nitrification / DenitrificationCalculation of AORMany alternatives, simple 0,8 - 1,2 Kg O2/ BOD-load (Kg BOD5 /d)

Design of aeration systemCalculation of SOTREstimates for alpha (0,4 - 0,9) , beta (0,95-1,0)Operating parameters, temperature, oxygen level, water depthSOTR = 1/a x C*/(b x C*-CL) x q(20-T) x AORLayout designNegative/positive effects of the basin dimensionsMixing requirements (1,2 - 2,0 m3/m2)Number of diffusers, air flows (min, average, max)

Fine bubble aerationThe most efficient way to aerate wastewaterExcellent control of the aeration processFlexible designTank dimensions not limitingCan be adjusted to match the loadDisc or membrane not suitable for all applications

Investment cost of the WWTP

Energy use in activated sludge WWTP

Factors Affecting Standard Aeration Efficiency Bubble sizeBubble rising velocityHead loss of the aeration systemCompression efficiency

Examples of Diffuser LayoutsHigh efficiencyLower efficiency

KKI 215 Diffuser SOTE

Spiral Flows in Aeration Tank

Bubble SizeAffected by: Surface properties of the membrane or disc Pore sizeAir velocity in the poreOptimum bubble size 1- 3 mmSmaller bubble size: requires higher headloss results lower process efficiency

Head loss of the Aeration SystemHead loss is generated by:Piping (1 - 3 kPa)Valves, filters, silencers (2 - 4 kPa)Diffuser (2 - 6 kPa)Fouling (0 - 4 kPa)Hydrostatic pressure(30 - 80 kPa)To minimize headloss:Low air velocities, low air flow/diffuserCleaning air filters, diffusers

Bubble velocityDepending on: bubble sizediffuser density (spiral flows)diffuser layout (spiral flows)uncovered areas (spiral flows)Velocity of the single bubble 0,2 - 0,3 m/sActual vertical velocity 0,3 - 0,4 m/s

ABS / NOPOL AERATION SYSTEMSNOPOL DISC DIFFUSER SYSTEMS

The experience gained over 25 years together with easily installable and long lasting parts as well as reliable and tailored solutions explain the worldwide success of the NOPOL DDS aeration systems

NOPOL O.K.I AERATOR/MIXEREfficient mixing, non-clogging, operational flexibility and easy installation are the key features of the NOPOL O.K.I. Aerator/mixer. Due to this it is the premium choice for all demanding aeration applications. ABS self aspirating aeratorsEfficient mixing, non-clogging, operational flexibility and easy installation are the key features of the ABS TA Aerator/mixer. Due to this it is the premium choice for all demanding aeration applications. For small need of oxygen.

AeratorsSystem Frings TAVenturi-JetOKI NOPOL DDS

TASELF ASPIRATING

Submersible Aerators

Non-torquing water tight encapsulated cable entry with strain reliefReplaceable bushingWater tight encapsulated squirrel cage NEMA B three phase motor, class F insulation, 155C, thermal sensors in each winding phaseMajor ComponentsAerator TA

Function of the TASelfaspirating AirWater

Working side pushes liquidBack side creates vacuum and aspirates airHydraulic PartsAerator TAStandard Material: 304on request: Chrome layer or 316ti

ImpellerChannel RingDistance of Gap between ImpellerTip and Channel Ring Tip --->0.75 mm

Impeller ScrewHydraulic PartsAerator TAStandard Material: 304on request: Chrome layer or 316ti

Hex. ScrewSpring WasherKeyMotor SupportImpellerImpeller WasherImpeller ScrewChannel RingBushingAll parts except bushing

Standard material: Stainless steel AISI 304Chrome layer on request

On request:Stainless steel AISI 316ti

Bushing

Standard material: bronzehardfibre on requestHydraulic PartsAerator TA

TA 1200M220/4 + M300/4max. w.d. 6.5 m SOTR= 30 kgO2/h

TA 2400M550/4 + M750/4max. w.d. 7.5 m SOTR= 70 kgO2/hTA 1800M370/4 - M550/4max. w.d. 9 m SOTR= 46 kgO2/h

Weight= 130 kgWeight= 90 kgWeight= 235 kgWeight= 360 kgWeight= 465 kgWeight= 785 kgWeight= 915 kgProduct Range Aerator TA/TAK 50 HTAK beginning at 601 improves the oxygen transfer performance up to 25 %TA 901M185/4 + M220/4max. w.d. 8,0 mSOTR= 21 kgO2/hTA 601M110/4 +M150/4max.w.d. 7,0 mSOTR= 14 kgO2/hTA 301M60/4 + M90/4) max. w.d. 6,0 m SOTR=7,5 kgO2/hTA 151M30/4 + M40/4max. w.d. 5,0 mSOTR=4 kgO2/h

Submersible Aerator TAFlow Pattern in Selfaspirating Operation (radial 360 Discharge)

TA 601 Starting Phase

Submersible Aerator TAKwith Channel Extension 1.5 m long

Cable ClampsCableCableCrane hook eyeletSubmersible Aerator TAInstallation Example

Minimum Distance from the Wall for TARound TankA/2A/2Diameter A

MixerA/2Examples for Positioning of AeratorsDonough Shape TankA/2

Maximum Mixing Zone BExamples for Positioning of AeratorsRectangular TankA/2A/2

Luft

0000000

60128248370411615930

55.5114247358417599909

51100239340413585.2888

4789228320402567866

4378211300388550838

3768196280368.2530809

3358178260350509777

5.548157.6237.3330487743

66138212310467705

6.56.56.56.56.56.56.5

&L&"ABSNeu,Regular Fett"&20A

H [m]

V [Nm3/h]

TA 2400

TA 1800

TA 1200

TA 901

TA 601

TA 301

TA 151

Submersible Aerators TA Selfaspirating

Performance Data 50 Hz Basin Diameter B Air Volume

Tauchbelfter TAselbstansaugend

Leistungsdaten 50 HzBeckendurchmesser BLuftmenge

TA 76/151

TA 301

TA 601

TA 901

TA 1200

TA 1800

TA 2400

P1 kw

0000000

34.7913.315.825.439

3.35.310.11518.928.643.6

3.65.911.216.72231.848.2

3.86.3911.91824.734.952.8

46.8712.619.0726.9837.757

4.27.2513.22029.0540.361

4.37.6413.620.730.5142.864.55

5.57.81421.331.6644.868.08

6614.321.832.746.571.5

6.56.56.56.56.56.56.5


P1[kW]

H (m)

TA 2400

TA 1800

TA 1200

TA 901

TA 601

TA 301

TA 151

Submersible Aerators TA Selfaspirating

Performance Data 50 Hz Basin Diameter B Power Consumption

Tauchbelfter TAselbstansaugend

Leistungsdaten 50 HzBeckendurchmesser BLeistungsaufnahme

TA 76/151

TA 301

TA 601

TA 901

TA 1200

TA 1800

TA 2400

OCB

0000000

2.95.31014.916.624.837

3.36.111.616.719.628.242.8

3.76.813.218.522.631.648.5

3.97.31419.62535.153.2

4.17.614.220.1926.73857.5

4.17.714.320.6128.140.161.5

3.97.614.120.628.994264.4

5.57.313.720.629.6543.7366.83

6613.220.1929.8645.469

6.56.56.56.56.56.56.5


OC/SOTR(KgO2/h)

H (m)

TA 2400

TA 1800

TA 1200

TA 901

TA 601

TA 301

TA 151

Submersible Aerators TA Performance Data 50 Hz (Basin Diameter B) Standard Oxygen Transfer Rate / Water Depth

TA 76/151

TA 301

TA 601

TA 901

TA 1200

TA 1800

TA 2400

Tabelle1

Luftleistung Tauchbelfter TA50 Hz

TypWassertiefe

022.533.544.555.566.5

TA 76/1516055.55147433733

TA 3011281141008978685848

TA 601248247239228211196178157.6138

TA 901370358340320300280260237.3212

TA 1200411417413402388368.2350330310

TA 1800615599585.2567550530509487467

TA 2400930909888866838809777743705

P (kW) Tauchbelfter TA50 Hz

TypWassertiefe

022.533.544.555.566.5

TA 76/15133.33.63.844.24.3

TA 3014.75.35.96.396.877.257.647.8

TA 601910.111.211.912.613.213.61414.3

TA 90113.31516.71819.072020.721.321.8

TA 120015.818.92224.726.9829.0530.5131.6632.7

TA 180025.428.631.834.937.740.342.844.846.5

TA 24003943.648.252.8576164.5568.0871.5

OC10 (kgO2/h)50 Hz

TypWassertiefe

022.533.544.555.566.5

TA 76/1512.93.33.73.94.14.13.9

TA 3015.36.16.87.37.67.77.67.3

TA 6011011.613.21414.214.314.113.713.2

TA 90114.916.718.519.620.1920.6120.620.620.19

TA 120016.619.622.62526.728.128.9929.6529.86

TA 180024.828.231.635.13840.14243.7345.4

TA 24003742.848.553.257.561.564.466.8369

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01020304050607080022,533,544,555,566,5P1 at duty point[kW]H [m]TA 2400TA 1800TA 1200TA 901TA 601TA 301TA 151 Submersible Aerator TAPerformance Data 50 Hz, Power Consumption / Water Depth

Submersible Aerator TA 151 A40-4 CRStainless Steel AeratorFor example oxydation of iron in water works

Submersible Aerator TA 601, 6 unitsSBR - Reactors:Industrial WWTP Fruitjuice Factory Krings-Fruchtsaft / Germany

Submersible Aerator TA 601, 1 unitMixing & Equalization Basin:Industrial WWTP Fruitjuice Factory Bscher Fruchtsfte / Germany

Submersible Aerator TA 901, 30 unitsMixing & Equalization Basin:Industrial WWTP Pharmaceutical Industry Schering / Germany

Submersible AeratorTA 2400, 1 unitAdditional Aeration in Existing Systems:Municipal WWTP / Germany

DDS

NOPOL

DISC DIFFUSER SYSTEM

DDS BASIC

SAE 4-5 kgO2/hLimitation hard water, CaCO3 must be less then 200 mg/l

NOPOL HKL 215Porous discContinuos operationFine bubblesNon-return valveQuick connectionCheap4 m3/h /diffusor

NOPOL KKI 215Membrane discIntermittent operationFine bubblesNon-return valveQuick connection4 m3/h /diffusor

NOPOL PIK 300Membrane discIntermittent operationFine bubblesNon-return valve ball typeQuick connectionMost cost effective solution8 m3/h /diffusor

Porous disc KKI HKLEPDM membraneNon return valve rubber, ball SS less pressurePolypropylen PIK 300 body, high temperature 10m3/hPVC HKL KKI body 4m3/hBlue ring self lubricating mtrl, if membrane cloggedpressure increases and membrane goes of and is not brokenWhen stretched normal the membranes are brokenNOPON clean, formic acid 20 mbarimmersed in acid to clean the membranePRK 300, strong bode on KKI 215, old non return valvehigher pressure dropFoot brackets, easy to install fully horizontally1,0 -1,2 m3/m2 to avoid settling

Quick and easy installationPossible to release the membrane and reinstall, not gluedTested unit from factory2 meters between the bottom bracketsWater drainage system, air lift small hole in the top3x density, water level, air flow

NOPOL PRK 300Membrane discIntermittent operationFine bubblesNon-return valveQuick connectionCost effective solutionRetrofit of KKI and HKLStronger version for industrial applications

NOPOL DDS SYSTEMS AND DIFFUSERS

HKL 215, MKL 215, KKI 215 and PRK 300 diffuser components for 90 mm piping

Parts of PIK 300 for 90 pipe

NOPOL CLEAN

NOPOL CLEANSHOULD START WHEN PRESSURE DROPS 20 mbar

1.Blower station6.Bottom mounting bracket HPK 21011.Water collection pipe2.Air supply header7.Connection sleeve HSY 90-9012.Purge hose / pipe3.Dropleg8.Diffuser element13.Pipe support4. Zone header 9.Diffuser (here KKI 215)14.Expansion joint5.Bottom mounting bracket TPK 15010.Drainage coupling VPL 90 Typical bottom-mounted fine-bubble aeration systemZone headerDiffuserBottom bracketDrainage couplingConnecting sleeveWater collection pipeDiffuser element

HPK 210

1.StrapHPA 2102.Pipe holderHKI 2103.Extension sleeveHJA 2104.FootHTU 2105.Hex screwM10 x 206.WasherKL 11/287.Drop-in anchorLAH 10TPK 125350

1.Threaded rodM122.Hex nutM123.Holder1253504.WasherM125.Drop-in anchorLAH 12

HPA 210Strap

HKI 210Pipe holder

HJA 210Extension sleeve

M10 x 20Hex screw

KL 11/28Washer

HTU 210Foot

LAH 10Drop-in anchor

WEDGE ATTACHMENT

1. Lock ringLUR 902. GasketHLT 903. BodyHSY 90R4. Screw3,5 x 35 Connecting sleeve

CONDENSATE REMOVAL Due to the pressure in the air main, moisture in the air and the cooling effect of the effluent, condensation will form in the pipe work

Drain this water back into the basin by opening the relevant valve

Drainage can vary from every day to once per month. Monitor the collection of water over the initial operating period

The water should be crystal clear

Dirty water means a problem with the system installation

Helsinki Viikinmaki Central Treatment Plant, Finland. 20,000 KKI 215 membrane disc diffusers. Population equivalent 750,000. Water depth 12m

EFFECT OF DIFFUSER DENSITY ON SOTE AND ENERGY CONSUMPTION3.6kgO2/kWh4.4kgO2/kWh

AIRFLOW CONTROL Air main is tapered so that the correct amounts of air go to the relevant zone

The air taper should deliver the correct amount of oxygen to each zone without valve control

Pressure losses over the diffuser membrane should be the same therefore no throttling will be required

Over time some variation in the pressure loss may occur thus resulting in the need for throttling

Throttle if the zone looks inactive

IS THIS OK?

GENERAL TIPS BE GENTLE!

GENERAL TIPSMONITOR THE BUBBLE PATTERN

INSTALLATION EXAMPLES

Optimal installation?

NOPOL AERATOR MIXER

OKI

WHY OKI AERATORS???

Demanding installationsMixer and aeratorNon cloggingDeep tanksEasy to installCheap to installAPLHA value 30% more then DDS, slightly smaller SOTE them DDSSAE 3,5-4,5kgO2/h

NOPOL O.K.I SUBMERGED AERATOR MIXER

Back pressure to blower typically 1m water head lower compared to fine bubble disc or tube systems

Typical industrial applications- Pulp and paper mills- Tanneries- Dairy waste water- Refineries- Chemical waste water- Textile industry

NOPOL O.K.I. 1000 SUMERGEDAERATOR MIXER

PRODUCT RANGE FOR NOPOL O.K.I. 1000

NOPOL O.K.I. 1000 SUBMERGED AERATOR MIXERSUBMERSIBLE MOTOR AND GEAR BOXSTATORROTORFRAME

NOPOL O.K.I AERATOR MIXER WORKING PRINCIPLE2 different type OKI 100 & 1000

WHERE TO INSTALL OKI?

IN THE CENTER OF THE TANK

NOPOL O.K.I AERATOR MIXER INSTALLATION PRINCIPLE

NOPOL O.K.I INSTALLATION

Cavendish Farms Inc., Canada. Food Industry equipped with 10 NOPOL O.K.I. aerator mixers

Enso Oyj, Imatra, Finland, pulp and paper mill with 42 NOPOL O.K.I. Aerator mixers

Prague Central WWTP, Czech Republic Return Sludge aeration in 14m water depth with 18 NOPOL O.K.I. Aerator mixers.

Phoenix Pulp & Paper, Thailand, equipped with 10 NOPOL O.K.I aerator mixer units

NOPOL AERATION SYSTEMS

QM Aeration dimensioning

HST HIGH SPEED TECHNOLOGY

HST Integral Turbo-CompressorComplete design: compressor, frequency converter and local control all in oneMagnetic bearings: no lubrication, no mechanical touch, total vibration free operationBuilt-in variable speed controlIntegrated turbo-rotor-cooling fan is the only rotating partNoise Enclosure as standard

High Speed Technology

_1030530066.doc

INU

AMB

High Speed TechnologySingle stage radial turbo-compressorContact-less and lubrication free magnetic bearing system, no friction lossesMassive rotor induction motorVariable rotation speed controlIntegrated frequency converter with control software

Minimize civil engineering costsSmall footprintLight weightLow noise - no special insulation neededNo vibration - no foundation base-plate requiredNo need for crane, fork-lift truck is sufficientInstallation in 60 minutes (HST record!)Ready assembled and tested complete unit

Minimize operation costsLow energy consumptionNo maintenance costsInbuilt self diagnostic protection and monitoring systemNo lubrication needed, no external cooling, no cooling water neededOptimization of operation at all timesSoft start function as standard

Superior TechnologyRotation speed control: no mechanical control organs as variable diffusers or inlet guide vanes, no risk of components being blockedRotation speed control: keeps high efficiency even by partial loadOnly one rotating componentNo auxiliary motors/equipmentAutomatic operation control50% lighter and smaller size than competitorsParallel operation always at optimum power

Rotation speed control p

Standard ProductTraditional way: every machine is specified to one single process impeller height, diameter and blade angledesign of spiral housinggear box transmission ratioHST way: every machine is a standard unitevery unit is factory tested and ready for installation50% shorter delivery timestandard spare parts, if needed

Exceptional ConditionsClogging of diffuser membranes by calcium in slots (independent of manufacturer)Excessive pressure ratio or intake temperatureTraditional compressors: no operation possible, break-down of treatment processHST Integral: automatic adjustment to new conditions by higher rotation speed - guaranteed air delivery

Principle of Magnetic Bearings

Dimensions

Sheet1

S2500S6000S9000

Length L (cm)142178-199204

Width W (cm)93135135

Height H (cm)189189200

Weight (kg)7501350-15001700

Principle of Magnetic BearingsActive magnetic bearing ( AMB ) consist of two attracting electromagnets, a position sensor and a controller. The electromagnets introduce forces acting on a ferromagnetic rotor pulling it to the opposite directions. Deviating the rotor from the central position towards one magnet increases the force pulling the rotor towards the deviation. Thus the rotor position is measured and the controller decreases the current in the magnet causing the pulling force in the direction of deviation and increases the current in the opposite electromagnet. In an actual AMB system, to levitate a rotor a five axis bearing system is used. Each axis, or channel, has its two electromagnets and a position sensor. Position controller takes care of all the channels keeping the rotor fully levitating.

HST ReferencesMB Joutseno Pulp, Finland 199610 x 6000-2-H-6, 60000 m3/hEspoo City, Finland 19977 x 6000-1-L-4, 48000 m3/hVsters City, Sweden 19984 x S6000-1-L-4, 25000 m3/hYoungjong Airport, South Korea 19994 x S6000-1-H-4, 25000 m3/hStockholm City, Sweden 20006 x S9000-1-L-4, 56000 m3/hKirin Beer, Japan 20004 x S6000-1-L-4, 26500 m3/h Baden City, Switzerland 20004 x S6000-1-L-4, 25000 m3/h

HST InstallationVsters, Sweden

HST Installation Lingen, Germany

Operation Range S2500-12500-1-Hca. 1300-3100 m3/h < 8 m2500-1-Lca. 1100-3200 m3/h < 6 m

2500-1

46

57

68

68

68

68

57

46

46

46

2500-1-L

2500-1-H

Flow[m/h]

Pressure Rise [mH2O]

2500-2

810

911

1012

1012

1012

1012

911

810

810

90010

2500-2-L

2500-2-H

Flow[m/h]


Flow Rate Area

Sheet1

2500-1-L2500-1-H

456678

min89010531208120813001400

max336835403250374534603220

456678

89010531208120813001400

6688

1208325014003220

654876

325035403368322034603745

4466

336889037451208

2500-2-L2500-2-H

8910101112

min9009501037103711401255

max248024302355255025452480

8910101112

9009501037103711401255

10101212

1037235512552480

1098121110

235524302480248025452550

881010

248090025501037


2500-1

46

57

68

68

68

68

57

46

46

46

2500-1-L

2500-1-H

Flow[m/h]


Flow Rate Area

2500-2

810

911

1012

1012

1012

1012

911

810

810

90010

2500-2-L

2500-2-H

Flow[m/h]


Sheet1

2500-1-L2500-1-H

456678

min89010531208120813001400

max336835403250374534603220

456678

89010531208120813001400

6688

1208325014003220

654876

325035403368322034603745

4466

336889037451208

2500-2-L2500-2-H

8910101112

min9009501037103711401255

max248024302355255025452480

8910101112

9009501037103711401255

10101212

1037235512552480

1098121110

235524302480248025452550

881010

248090025501037


6000-1

46

57

68

68

68

68

57

46

46

46

6000-1-L

6000-1-H

Flow[m/h]


6000-2

810

911

1012

1012

1012

1012

911

810

810

294010

6000-2-L

6000-2-H

Flow[m/h]


Flow Rate Area

Sheet1

6000-1-L6000-1-H

456678

min230026102850223026002910

max670070357055661568156600

456678

230026102850223026002910

6688

2850705529106600

654876

705570356700660068156615

4466

6700230066152230

60900-2-L6000-2-H

8910101112

min294031903410341036403850

max689069656950695066006320

8910101112

294031903410341036403850

10101212

3410695038506320

1098121110

695069656890632066006950

881010

6890294069503410


6000-1

46

57

68

68

68

68

57

46

46

46

6000-1-L

6000-1-H

Flow[m/h]


Flow Rate Area

6000-2

810

911

1012

1012

1012

1012

911

810

810

294010

6000-2-L

6000-2-H

Flow[m/h]


Sheet1

6000-1-L6000-1-H

456678

min230026102850223026002910

max670070357055661568156600

456678

230026102850223026002910

6688

2850705529106600

654876

705570356700660068156615

4466

6700230066152230

60900-2-L6000-2-H

8910101112

min294031903410341036403850

max689069656950695066006320

8910101112

294031903410341036403850

10101212

3410695038506320

1098121110

695069656890632066006950

881010

6890294069503410


9000-1

46

57

68

68

68

68

57

46

46

46

9000-1-L

9000-1-H

Flow[m/h]


Sheet1

9000-1-L9000-1-H

456678

min360037003800380040004250

max920094008900990093008800

456678

360037003800380040004250

6688

3800890042508800

654876

890094009200880093009900

4466

9200360099003800

AERATORS

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Transcript of AERATORS