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BOILER WATER TREATMENT THE POLYAMINE SOLUTION

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Presentation on theme: "BOILER WATER TREATMENT THE POLYAMINE SOLUTION"— Presentation transcript:

1 BOILER WATER TREATMENT THE POLYAMINE SOLUTION

2 Water cycle in the boiler house
RAW WATER SOFTENER Superheater uses Water meter Deaerator FFEED TANK condenser BOILER BLOWDOWN Dosing tank CONDENSATE RETURN

3 MAIN PROBLEMS Scaling Corrosion Carry over

4 Raw water composition Including Suspended solids
Sand, mud, colloidal organic material, and so on, Organic material in solution Organic acid, vegetation rejection,… Dissolved salts Cations : Anions : Calcium Ca2+ Magnesium Mg2+ Sodium Na+ Potassium K+ etc... Bicarbonates HCO3- Chlorides Cl- Sulfates SO42- Nitrates NO3- etc... Dissolved gas Oxygen, carbonic gas, nitrogen Micro-organisms Algae, bacteria, fungi

5 Usual water analysis unit Observations pH - Acidity or basicity
Total Hardness ppm Calcium+Magnesium p Alkalinity OH and CO3 m Alkalinity OH, CO3 and HCO3 Chlorides mg/L Determination Rc T.D.S. Total dissolved salts Conductivity mS/cm Water quality

6 Feed water requirements
For P<20 bar According prEN and standards pH > 8.5 > 9.2 TH ppm CaCO3 < 3 < 2 Oxygen mg/L < 0,1 < 0.05 Oil and grease No < 1 mg/L Organic matters TOC < 1 mg/L < 0,2 if P>40b

7 Boiler water requirements
For P<20 bar General, from manufacturer According prEN and standards pH 10.5 to 11.5 10.5 to 12 p-Alk ppm CaCO3 - 50 to 750 m-Alk ppm CaCO3 < 1200 SiO2 in mg/L < 200 < 160 Conductivity µS/cm < 8000 PO4 in mg/L 30 à 100 < 30

8 Scale-forming salts mg/L CaSO ,2H O 2200 (gypsum) CaSO (anhydrite )
4 2 (gypsum) CaSO 4 (anhydrite ) CaSO ,1/2H O 4 2 (semi-hydrate) 300 CaCO 3 100 °C

9 SILICA SiO2 in steam in ppm SiO2 in boiler (mg/L) Pressure in bar

10 Basic corrosion process
Anodic reaction H O 2 Fe Fe 2+ + 2 OH - OH - + 2 e - OH - Fe(OH) 2 + H + Cathodic reaction - + 2H + 2 e H 2 2 e With dissolved oxygen : 4 e - + O + 2 H O 4 OH - 2 2

11 Local oxygen corrosion
Oxygen cannot reach the metal under the deposit, which creates an anodic area. O 2 O O 2 2 OH - Fe ++ OH - e - e - e - The cathodic reaction is taking place where oxygen can reach the metal. Metal : Iron

12 High temperature corrosion
3 Fe + 4 H2O  Fe3O4 + 4 H2 Shikorr reaction : This reaction is catalysed by dissolved oxygen.

13 CO2 production by softened water
BICARBONATES ARE DECOMPOSED IN CARBONATES BY HEAT WITH PRODUCTION OF CO2 CARBONATES ARE HYDROLYSED INTO CAUSTIC SODA WITH PRODUCTION OF CO2 THE REACTIONS : 2NaHCO3  Na2CO3 + CO2 + H2O Na2CO3 + H2O  2 NaOH + CO2

14 Bicarbonate decomposition
100 100 °C 90 °C 50 time mn REACTION 1 : 2NaHCO3  Na2CO3 + CO2 + H2O

15 Carbonate decomposition
% Hydrolysis 100 50 P in bars REACTION 2 : Na2CO3 + H2O  2 NaOH + CO2

16 PURPOSE OF BOILER WATER TREATMENT
pH control of feedwater and boiler water Avoid precipitation of scaling salts: calcium carbonate, silica, iron, copper Internal protection of boiler tubes and drums Protection of condensate return lines

17 TRADITIONAL TREATMENT
Phosphates Oxygen scavengers Dispersants, anti-scaling agents Neutralizing amines

18 Oxygen scavengers MAIN OXYGEN SCAVENGERS sulfites :
Na2SO3 + ½ O2 Na2SO4 hydrazine : N2H4 + O2 N2+H2O tanins

19 MAIN DISADVANTAGES Toxicity: hydrazine, morpholine
Corrosion of copper and copper alloys Extra salinity added: phosphates, sulfites Problems due to feedwater injection in steam

20 POLYAMINE ALTERNATIVE
A combination of 2 main actions pH control Filming protection

21 R-NH- CH2 3-n-NH2 FILMING POLYAMINES n = 0 to 7
example : octadecylamine  n = 0 R = straight carbon chain with C12 minimum and C18 predominant

22 VARIOUS ACTIONS ANTI-SCALING EFFECT ADSORPTION : FILMING EFFECT
PSEUDO-COMPLEX FORMATION WITH METALS DROP CONDENSATION

23 ADSORPTION 1. Adsorption 2. Ion - ion 3. Hydrophobic bond 3 3 2 2 1 1

24 PSEUDO-COMPLEX FORMATION
CH3 CH3 CH2 CH2 CH2 CH2 H H N N O O H H Fe Fe H H O O O O H H Fe Fe

25 THE POLYAMINE FILM Polyamines form a protective film on the metal surface. This film has been evidenced by means of electrochemical measurements of corrosion and particulary by electrochemical impedance diagrams.

26 INVESTIGATION OF THE FILM EXPERIMENTAL PROCEDURE
Potentiostat I mA mV E Auxiliary electrode (Pt) Reference electrode Rotating disc electrode (steel)

27 IMPEDANCE DIAGRAM - jG (.cm2) HF loop : film evidence R (.cm2) Re Rp
Cd CHF Cd Re Re RHF Rp Rp

28 Protection of boiler tubes
Polyamines stabilize the magnetite layer formation on the tubes of steam generators. The study of the effect of POLYAMINE products on the Shikorr reaction (magnetite production) proves the efficiency of polyamines against corrosion.

29 Emulsion water/steam 24 %
Magnetite production : experimental procedure Emulsion water/steam 24 % H2 Incondensable gases Expansion condensation cooling Boiler tube :  = 23 w/cm2 P = 100 bars T°C = 315 °C Make - up : demineralized water 3 Fe + 4 H2O  Fe3O4 + H2 Shikorr reaction

30 Stability of the magnetite layer
H2 as vpm (volume per million) Magnetite production POLYAMINE injection 10 2 vpm during 72 hours 2 time

31 HEAT EXCHANGE The polyamine film formed on metal surfaces does not affect the thermal exchange. Presence of polyamines increases the yield of condensers.

32 THERMAL EXCHANGE  in w/cm.°C

33 DROP CONDENSATION Dh (%) Film condensation ppm ODA Drop condensation 5
4 3 2 1 Film condensation ppm ODA Drop condensation

34 Toxicity vs inocuity Toxicity of hydrazine:
LD 50 = 60 mg / kg of weight Carcinogenic Inocuity of the polyamine: LD 50 > 2000 mg / kg Non carcinogenic

35 CONCLUSIONS Efficiency Simplicity Hydrazine free Non toxic
Reduction of blowdown Improvement of condenser yield Cost-effective


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