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Cooling Water
Watertreatment and chemical conditioning of
open and closed cooling systems
Dr. K. Nachstedt, Weidner Wassertechnik, Herten
Recirculation of process watervolume of utilization is increasingvolume of delivery is nearly constant
Rate of cooling water at direct wastewater disposal
Cooling Systems 1
Flow-through system
must be close to watersno recirculation of watervery large volume of water consumptionmarginal expenses for water treatmentecological problem: temperature rise of watersrare used at the present state of technology
Cooling Systems 2
closed/semi-closed circulation systemtypical useage: hydraulics, engine, injection mouldsneglectibal loss of water very strong corrosion inhibition possibleconnected to heat exchangers of secondary cooling systems (refrigerating machine / cooling tower
Cooling Systems 3
Open evaporating cooling systems mainly used system: cooling towertarget: high rate of recirculation (cycles of conc.)consumption of water: evaporaton + blowdownwatertreatment is always necessary
Cooling Systems 4Cooling towers
more than 80% of cooling capacity: evaporation
very high cooling capacity: use of latent heat of evaporation
consumption of water depends directly on water treatment
Problems to solve
Closed circuitshigh temperatures may cause scaling and corrosionlarge copper surfaces in heat exchangersdifferences in electrical potentials (e.g. target cooling)
Open circuits (cooling towers)high concentration of minerals in circulation water
deposits of calcium carbonate (scale formation)
biological growth (organic contamination, favorableenviroment for microorganism)
Priority tasks in cooling water treatment
avoidance of inorganic deposits (scale inhibition)
prevention / inhibition of corrosion
control of biological growth (fouling control)
Steps to take Cooling equipment:
Careful selection of materials and -combinationsFlow velocity within the range 1,5 – 2 m/slow temperature of water and materials < 45 °C (large surfaces of heat exchangers)
Water: Outer water treatment (Units and equipment)
filtration, softening, desalination
Internal water treatment (chemical products)Inhibitors for corrosion and scaling, antimicrobials
Closed / semi-closed systems (1) Usually easy to treat:
small systemvolume: typically < 200 m³no sunlight: suppression of biol. growth only small entry of pollutionneed only small amounts of makeup water(small costs of treatment products)
Makeup water:Town water / water from wells at T< 45 °Csoftening / desalination at T> 45 °C
Closed / semi-closed systems (2)Chemical treatment
in the past: chromates, nitrites, zinc, polyphosphatetoday: combinationproducts
dispergators (polycarbonic acids)corrosion inhibitors (molybdates, phosphonates, organic N-heterocyclic compounds)scaling inhibitors (phosphonates, polycarbonic acids)
Typical products & equipment necessary:dosing system: metering pump + water meter with impulse outputtreatment product: ca. 3-4 kg/m³ watercontroling: testkits / online-analysis / corrosion testsbiological contamination (well-water) : Biocides/ UV-burner
Closed / semi-closed systems (3)
Most common mistake of closed circuit treatmentLow concentration of corrosion inhibitor (Mo > 40 ppm)too large time – intervals between the control measurements
Closed / semi-closed systems (4)
Destructed surface of cast iron: 3 weeks after setting in operation with dangerous inhibitor concentration
Open evaporation cooling systems (1)
Water treatment can be very complicatedSystemvolume range 500 – 2000 m³
Makeup-water often above 100 m³/h
frequently large pre-destructed pipesystems. “historical material mix” (iron, steel, zinc-coatings, brass, copper, aluminium)
large amounts of dirt may enter the system
water is sometimes in direct contact with the product
seasonal large fluctuation of biological exposure.
Open evaporation cooling systems (2)
First priority: Prevention of depositsEconomical target: maximum of concentration cycles as possible ! (saving of makeup water):
Exceeding the limit of solubility of inorganic compounds:calciumcarbonate deposits (lime scale)
concentration of chloride content in the circulation water:promoting of corrosion (pitting at passive metals)
concentration of dirt in the circulation water:sludge-deposits can cause biological problems
Open evaporation cooling systems (3)
Target: cycle no. CN > 2,5Volume makeup (VM) = evaporation (VE) + blow down
VM = VE x (CN/(VN-1)) (Hyperbel)
CN = 2 = 100% VMCN = 3 = 75% -25%CN = 4 = 64% -11%
Even at small cooling towers:
enormous potential to save water and money !
Open evaporation cooling systems (4)
Practical Limits of concentration cycels:“carbonate-hardness” < 20° dH (tot. alkal. < 7 mmol/l) (better, if available: SI < 2,8)Chlorid concentration < 200 mg/l (danger of pitting)
Is it possible to operate an open cooling system without hardness-stabilizer?
15 mg/l = ca. 0,7 °dH
Deposits (1)Effects of deposits
Corrosion and microbiol. growth at and below depositsLoss of energy (flow resistance in pipes)Faulty flow (cavitation, erosion, promotion of corrosion)Poor heat transfer in heat exchangers (increas. tranf. coeff.)
Ablagerungen (2)
Plate of heat exchanger Pipe of coolingsystem
Products and methods of treatment (1)Basics of treatment products (state of the art)
phosphonic acids and phosphonatesscale inhibitioncorrosion protection
Polycarbonic acids / polycarbonatesdispersing agent / mobilisation of sludge scale inhibition
organic N-heterocyclic compounds (Triazoles)corrosion inhibition of yellow metals
additives for stabilisation of the formulation
Products and methods of treatment (2)Phosphonic acids: most effektive scale inhibitors
Threshold-inbitors (nonstoichiometric application)
Example: stoichiometric usage of known chelates
Products and methods of treatment (3)Phosphonic acids / Phosphonates
Threshold-inhibition (far below stoichiometric ratios)principle of operation: blocking of crystal growthunder-stoichoimetric ratio 1:<1000 underdosing: no hard deposits (easy to purge away)synergistic effect in combination with polycarbonic acidsusual concentration 5 - 10 g/m³ makeup water
Inhibition / prevention of corrosionamplification effect for other inhibitorsforming of protective membranes: anodic and cathodic corrosion inhibition
Products and methods of treatment (4)Phosphonic acids / phosphonates
Important difference: no polyphosphates ! (From the past!)
Easy hydrolysis !Degradation to ortho-phosphate !
Phosphonic acid are stable to hydrolysis in cooling water
Products and methods of treatment (5)Most effective phosphonic acid: PBTC
Products and methods of treatment (6)
Dipersing of sludges: anionic polymeres geringe Molmassen (1000 -4000)water soluble (highly negative charged)electrostatic effects mobilise sludge and slurry
R & D of formulationsTube-Blocking-Test / Scale inhibition test (NACE)
Practical application
Scale inhibitors / corrosion inhibitorsDosing proportional to addition of makeup watertypical dosing: 6-20 g/m³ makeup watercontrol of product concentration: total phosphate or special polymertest (if polymers are detectable)limit of scale stabilisation: 20 °dKH / 7mmol/l TAabove limit of stabilisation: dosing of mineral-acid (internal decarbonisation)Ion-exchange / reverse osmosis:decarbonisation / softening / desalination
Biological Control
Antimicrobials / biocidesNot oxidizing biocides
Isothiazolinones (CIT/MIT, deliv. 1,5%)DiBromNitriloPropionamid (DBNPA, deliv. 20%)
Oxidizing biozides Chlorine (sodium hypochlorite)Chlor/Brom-Hydantoin (halogen donor; tablettes)Bromine (Flow through reactor with chlorine)Chlordioxid (“one component”, production system)Ozon (AOX / CSB-reduction possible; expensive)
Applikation of antimicrobials
Nonoxidizing antimicrobials
always shockdosing (avoiding of resistence!)interval time after dosing: 7 - 14 daysnecessary concentration 0,1 kg / m³ circuit volumeuse with surfactant to combat biofilmsexpensive for large circuit volumes
Oxidizing antimicobials
continuous dosing possiblemay promote corrosionchlordioxide excellent for biofilms
Control of treatment success:
microbiological examination in regular intervals
Treatment of open circuits
Automatic system for open cooling circuits
Dosing of scale inhibitors Control of concentration cycles via conductivityPH-Control and pH-regulationTreatment with microbialsnonoxidizing: dosing at selectable timesoxidizing: dosing depends on continuously measurement (sensor, on-line analysis) Meeting WHG Anhang 31 (luminicence test)
Blocking of blow down / pre-blow-down
Automatic management system for cooling water
sensor for halogen
T
fluorescence
carboxylate
ortho - PO4
total- PO4
pH
total alkalinity
conductivity
Cooling tower
water circuit
Analytical Parameter Information
concentration cycles
concentration cycles
acid dosing / decarb.
Oxid. biozide content
cooling capicity
conc. treatment prod.
phosphonate x F =
conc. treatment prod.
KWMS 1: Coolingwater-Managementsystem
KWMS 1:
maximum of information formaximum of reliability
Keywords: External Water TreatmentIf no economical internal treatment is possible:
Softening of waterworks continuouslylarge consumption of regeneration salt(often more than 50.000 Kg/year in medium circuits)
Decarbonisation (partial desalination)internal decarbonisation (decreasing pH, acid dosing)external decarbonisation (weak acid ion exchanger)
DesalinationFull desalination (Ion-exchanger, anionic + cathionic)Reverse Osmosis (Costs of energy! 75% yield )
SummaryBasic schematics of open and closed circuits have been introduced.Targets of cooling water treatment in open and closed circuits were pointed out.Internal (chemical) and external (equipment based) treatment possibilities and limitations have been discussed. Problems of cooling systems and possible solutions of suitable water treatment have been shown.Modern treatment substances and their properties in formulated products have been listed and discussed.Automatic management systems or cooling water and projects of R & D have been introduced.
Further questions + informations
Dr. K. NachstedtTel. 0178/[email protected]
Weidner Wassertechnik GmbHZechenstrasse 2545699 Herten