EFFECT OF COPPER AND COPPER OXIDE ON CORROSION OF BOILER STEEL

Similar documents
Corrosion of unalloyed steels in different alkaline solutions at high temperatures and under high pressures

Laboratory Experiments in Corrosion Engineering II

Corrosion Potential Measurements in Boiler Water: The Influence of Oxygen Content*

STRESS CORROSION CRACKING OF STAINLESS STEELS IN HIGH PRESSURE ALKALINE ELECTROLYSERS

1. Scaling. H.O.: H-5/21, KRISHNA NAGAR, DELHI Tel.: , Fax:

2. Wet Corrosion: Characteristics, Prevention and Corrosion Rate

The protection effectiveness of magnetite layers in relation to boiler corrosion

What happens if we connect Zn and Pt in HCl solution? Corrosion of platinum (Pt) in HCl. 1. If Zn and Pt are not connected

Corrosion Control and Cathodic Protection Data Sheet

The influence of Mg 17 Al 12 phase volume fraction on the corrosion behaviour of AZ91 magnesium alloy. Andrzej Kiełbus* and Grzegorz Moskal

A Case Study: Corrosion Failure of Tube Heat Exchanger

Characterization of Coatings on Grey Cast Iron Fabricated by Hot-dipping in Pure Al, AlSi11 and AlTi5 Alloys

Aluminum Alloys GOTChA Chart

Assignments. 1. Prepare Galvanic series for metals and alloys in flowing sea water. Compare this with the series available for stagnant sea water.

CORROSION PROPERTIES OF CERMET COATINGS SPRAYED BY HIGH-VELOCITY OXYGEN-FUEL. Dragos UŢU, Iosif HULKA, Viorel-Aurel ŞERBAN, Hannelore FILIPESCU

Galvanic corrosion evaluation of 6061 aluminum coupled to CVD coated stainless steel Elizabeth Sikora and Barbara Shaw 6/9/2016

Analysis of Nonmetallic Inclusions Distribution and Microstructure in Centrifugally Cast Steel Pipes Boris Katavić 1,a, Zoran Odanović 2,b

Steamate* technology. superior protection against condensate system corrosion. Water Technologies & Solutions technical bulletin

EVALUATION OF A CHEMICAL CLEANING FORMULATION FOR THE STEAM GENERATOR OF NUCLEAR POWER PLANTS

IN SITU MONITORING OF REINFORCEMENT CORROSION BY MEANS OF ELECTROCHEMICAL METHODS

The Effect of Preparation and Cleaning Techniques on Electrochemical Testing of Aluminium Anodes

FORMATION OF TiO 2 THIN FILM BY ION-BEAM-MIXING METHOD AND ITS APPLICATION AS THE CORROSION PROTECTING FILM

EMA4303/5305 Electrochemical Engineering Lecture 05 Applications (1)

Corrosion and Corrosion Protection

Experimental Simulation of Iron Oxide Formation on Low Alloy Steel Evaporator Tubes for Power Plant in the Presence of Iron Ions

Angle-resolved XPS study of carbon steel passivity and chloride-induced depassivation in simulated concrete pore solution

LASER SURFACE MELTING OF 17-4 PH PRECIPITATION-HARDENABLE STAINLESS STEEL Paper 1203

CORROSION BEHAVIOR OF AUSTENITIC AND FERRITIC STEELS IN SUPERCRITICAL WATER

Experiment E: Martensitic Transformations

Caustic Gouging. PPChem. PPChem 101 BOILER AND HRSG TUBE FAILURES LESSON 5: INTRODUCTION TYPICAL CHARACTERISTICS OF DAMAGE

DETECTION OF PITTING CORROSION OF ALUMINIUM ALLOYS BY ACOUSTIC EMISSION TECHNIQUE

MEASUREMENT OF THE OXYGEN POTENTIAL OF NON-FERROUS SLAGS WITH AN EX-SITU ELECTROCHEMICAL DEVICE

Sensitization & Corrosion Behaviour of Austenitic Stainless Steel 304 & 316

COMPREHENSIVE INVESTIGATION OF THE CORROSION STATE AND SURFACE PROPERTIES OF THE STAINLESS STEEL TUBES OF STEAM GENERATORS

Results are presented in Table 1. The tube was fabricated from a Type 347 and no unusual conditions were noted.

IRON CARBONATE SCALE GROWTH AND THE EFFECT OF INHIBITION IN CO 2 CORROSION OF MILD STEEL

Characteristics of centrifugally cast GX25CrNiSi18-9 steel

CORROSION of Metals CORROSION CORROSION. Outline ISSUES TO ADDRESS... Why does corrosion occur? What metals are most likely to corrode?

WF VAN DER VYVER

CORROSION PHENOMENA AN INTRODUCTION G P Rothwell

Experimental O 3. Results and discussion

Propagation of Localised Corrosion: FEM Approach

Effect of Anodizing Potential on the Surface Morphology and Corrosion Property of AZ31 Magnesium Alloy

Characteristics and Applications of High Corrosion Resistant Titanium Alloys

Tutorial Corrosion II. Electrochemical characterization with EC-Lab techniques

METAL FINISHING. (As per revised VTU syllabus: )

Localized Corrosion of a 7075 Aluminum Alloy Exposed to KCl

SurTec Technical Letter

NCERT solutions for Metals and Non Metals

Intergranular Corrosion (IGC)

Annex to the Accreditation Certificate D-PL according to DIN EN ISO/IEC 17025:2005

Combinations of alloys and environments subject to dealloying and elements preferentially removed

GENARAL INTRODUCTION TO METALLURGY :Std: XI-CHEMISTRY

Effect of Precorrosion and Temperature on the Formation Rate of Iron Carbonate Film

The Evaluation of Corrosion Behavior of AISI 347 Stainless Steel to ASTM A335 Low Alloy Steel Dissimilar Welds

Passivity Definitions and Influencing Parameters

Available online at ScienceDirect. Procedia Engineering 184 (2017 )

Distribution Review. Corrosion Control. Corrosion Control Vocabulary. American Water College 1. Corrosion Control Training Objectives

Corrosion and Protection of Metal in the Seawater Desalination

a: potential difference before direct current is applied b: potential difference after the application of current

Corrosion Rate Measurement on C-Steel

Effect of CO Gas Concentration on Reduction Rate of Major Mineral Phase in Sintered Iron Ore

A STUDY OF CASTING CHARACTERISTICS FOR DIE-CAST ALUMINUM ALLOY

ENERGY CARRIERS AND CONVERSION SYSTEMS Vol. II - Molten Carbonate Fuel Cells - Kouichi Takizawa

Metals I. Anne Mertens

Corrosion Mechanisms, Monitoring, and Service Life Enhancement of Reinforced Concrete Structures

Via Filling: Challenges for the Chemistry in the Plating Process

Investigation of Under Deposit Corrosion (UDC) in Halfdan Production Tubulars ABSTRACT

Semiconductor Technology

APPLICATIONS OF Fe-C PHASE DIAGRAM

PPS Outshines Stainless Steel in Chemically-Hostile Valve Applications

Experimental Investigation of the Galvanization. Effects on the Properties of. Low Carbon Alloy Steel

Heat Treating Basics-Steels

Methods of Corrosion Control. Corrosion Control or Corrosion Management?

CORROSION BEHAVIOR OF TITANIUM METAL IN PRESENCE OF INHIBITED SULFURIC ACID AT 50 o C 1

STRESS CORROSION CRACKING SUSCEPTIBILITY OF STEEL STRANDS IN CONCRETE CONTAMINATING SALT

DECOMPOSITION OF HYDRAZINE IN PRESERVED BOILERS 1

Biofilms And General Mechanisms In Biocorrosion

Problems and Prospects of Halogen Element Contained Dust Treatment in Recycling

85 Q.51 Which of the following carbonates would give the metal when heated with carbon? (1) MgCO 3 (2) PbCO 3 (3) K 2 CO 3 (4) CuCO 3

MATERIALS SCIENCE-44 Which point on the stress-strain curve shown gives the ultimate stress?

Why Does Rust Occur? 7.1 IN GENERAL

An Inexpensive Corrosion Laboratory Experiment - Suitable for All Ages.

ELECTROCHEMICAL SYNTHESIS OF POLYPYRROLE (PPy) and PPy METAL COMPOSITES ON COPPER and INVESTIGATION OF THEIR ANTICORROSIVE PROPERTIES

9707 Key West Avenue, Suite 100 Rockville, MD Phone: Fax:

CHEMISTRY 112 EXAM 3 JUNE 17, 2011 FORM A

not to be republished NCERT GENERAL PRINCIPLES AND PROCE ISOLATION ISOL ELEMENTS Unit I. Multiple Choice Questions (Type-I)

Iron is found in an oxidized state and is mined from the ground as an iron ore.

Sealing Mechanism of Anodic Porous Oxide Films Formed on Aluminum in Lithium Hydroxide Solution

CO forms CO 2. forms. (a) The coke reacts with the oxygen in the air to form carbon dioxide. C + O 2

Heat Treatment of Tubes for Condenser, Feedwater Heater, and Shell & Tube Heat Exchangers

The effect of electroplating of Cr and Sn on corrosion resistance of low carbon steel (CK15)

J = D C A C B x A x B + D C A C. = x A kg /m 2

Iron filings (Fe) 56g IRON + SULPHUR IRON SULPHIDE

An overview of nitrates-induced corrosion of reinforced concrete structures: case studies, laboratory investigations and corrosion mechanisms

Manufacturing of Fe-Cr-Al weld overlay coatings for high temperature applications

Corrosion Behavior of Steam Turbine Materials for Geothermal Power Plants

Electrolytic deposition of Zn-Mn-Mo alloys from a citrate bath

Oxidation and Reduction

Liquidus Surface of FeO-Fe 2 O 3 -SiO 2 -CaO Slags at Constant CO 2 /CO Ratios

Transcription:

06 koperoxide www.hbscc.nl - 1 - EFFECT OF COPPER AND COPPER OXIDE ON CORROSION OF BOILER STEEL W.M.M. HUIJBREGTS Mitteilungen der V.G.B., Vol. 51, No.3, pp. 229-235, June 1971 ABSTRACT Electrochemical measurements made on iron and copper have shown that rtain conditions copper and copper oxide promote corrosion in the magnetite coating of boiler pipes. 1. INTRODUCTION Suspended matter in boiler water is often deposited on the tu are the heat tran6fer is nigh. Relatively large amounts of the deposits. It is difficult to decide whether the copper is produced directly by coprecipitation of iron oxide and copper or by reduction of the copper oxide with simultaneous oxidation of the magnetite film on the tubes ( Refs. 1, 2). The deposits have led to a series of tube failures. In a investigation of the problem, polarisation measurements were made on c copper and iron and corrosion experiments were carried out on steel in alkaline containing suspended copper and copper oxide. 2. ELECTROCHEMICAL EXPERIMENTS The polarisation experiments were made in an autoclave at 2 5 0 a n d 4 2 k g / c m 2 p r e s s u r e, in alkaline solution. The autoclaves and the methods have already been described (Ref. 3). The polarisation curves at 250 and 42 kg/cm 2 pressure for chemically pure iron and for copper are shown in Figures 1-3. 2.1 Measurements in 0.0001 N NaOH It can be seen from Fig. 1 that the polarisation curves for iron show two current density maxima ( - 400 and - 100 W) which probably correspond to the oxidation of Fe 2+ and Fe +++ to Fe 3 O 4. At +230 W and higher potentials the current density fluctuates so that different, irregular current density maxima were measured. In our opinion, this phenomenon indicates oxidation of Fe3O4 to FeO42-, associated with pitting of the iron sample. At the rest potential ( - 475 m V iron is oxidised to Fe 3 O 4 according to the Schikorr reaction; Fe + 2 H 2 O Fe(OH) 2 + H2 3 Fe(OH) 2 Fe 3 O 4 + 2 H 2 0 + H 2 Other electrochemical reactions such as the formation of alpha Fe 2 0 3 by oxidation of Fe 3 O 4 are also thermodynamically possible. No reaction of this type however can be established from the polarisation measurements

06 koperoxide www.hbscc.nl - 2 - Figure 1: Polarisation curves, measured with iron in 1.10-4 n NaOH and 1. 10-2 n NaOH at 250 C. The curve for copper (Fig. 2) shows two current density maxima which can be attributed to the formation of Cu 2 0 and CuO. The polarization curve measured from cathodic to anodic show a rest potential of - 240 mv. At this potential the slope of the curve is small which suggests a small corrosion rate for copper. The anodic to cathodic scan shows a relatively high rest potential (+200 mv) at which CuO is converted into Cu 2 O which in turn is reduced to copper at a still lower potential.

06 koperoxide www.hbscc.nl - 3 - Fig 2. Polarisation curve for copper 0.001 n NaOH at 250 0 C. The reduction of copper oxide is scareely retarded by polarization resistance hence this reduction could be involved in the anodic corrosion reaction. The rest potential of iron can therefore be increased by the reduction of copper oxide and ferrous and ferric ions can be very easily oxidized in this way to finely powdered Fe 3 O 4. Further increase of the iron rest potential to the pitting potential by reduction of CuO to Cu2O must of course be very unfavourable with regard to the tendency to corrosion. 2.2 Measurements in 0.01 N NaOH The polarisation curve for iron measured in 0.01 N NaOH is also shown in Figure 1. There are two current density maxima; -290 mv and about 40 mv. The latter is split into two maxima at -69 and +20 mv. The first maximum at -290 mv is attributed to the formation of Fe 3 O 4 from FeO 2-2 ions and the second maximum at -40 mv to the formation of Fe 2 0 3 2- from HFeO2- of FeO 2 ions. The split of the secondd maximum may be due to the growth of alpha and gamma Fe 2 0 3 of of alpha Fe 2 0 3 in various modifications. The mechanism however is not yet adequately explained. According to Fig. 1 the Fe 2 0 3 formation in any case causes effective passivation. The production of oxygen occurs at +710 mv. At the restpotential Fe 3 O 4 is formed both 2- by the Schikorr reaction and by oxidation of FeO 2 ions. Fig. 3 shows the polarisation curve for copper in 0.01 N from cathodic to anodic and from anodic to cathodic potentials. It can be concluded from the anodic to cathodic potential curve that the CuO is

06 koperoxide www.hbscc.nl - 4 - very easily reduced at +290 mv to Cu20 and Cu20 is equally easily reduced to Cu at -20 mv. Copper oxides must therefore be regarded as very strong oxidising agents under these conditions. Fig 3. Polarisation curve for copper 0.01 n NaOH at 250 0 C. The rest potential of iron is increased by the reduction of CuO to Cu2O in situ at 290 mv so that the iron is passivated under formation of Fe 2 0 3. The reduction of Cu20 to Cu and hydrogen evolution on copper result in minor increases of the iron rest potential without giving rise of the formation of protective alpha- Fe 2 0 3. Whether the rate of corrosion in fact increases depends on the morphology and consistency of the oxide film which is formed. 3. LONG TERM EXPERIMENTS IN ALKALINE SOLUTIONS It should be possible to obtain a general view of the effect of copper oxide reduction on the morphology of the protective magnetite film and the rate of any corrosion reactions from long term experiments on steel in alkaline solution containing suspended copper and copper oxide. With this in mind long term experiments were carried out on mixtures of powdered Fe 3 O 4 and CuO and also on oxidised steel sheet. To avoid galvanic contact of the sample with the walls of the autoclave, the samples and the solution were contained in PTFE capsules. The experimental conditions are set out in Table 1 and the composition of the steel used is shown in Table 2.

06 koperoxide www.hbscc.nl - 5 - Table 1 Long term experiments with Fe 3 O 4 - CuO mixtures in powder form and pre-oxidispd steel sheet with copper and copper oxide coats. Temperature: 310 0 C Experimental time: two days. Samples Solution Solution Addition Tablets of Fe3O4 and CuO 0.1 1.10-5 none Preoxidised steel sheet 0.1 1.10 suspended CuO Preoxidised steel sheet 0.1 1.10 suspended Cu Preoxidised steel sheet 0.1 1.10 none Table 2 Chemical analysis of the steel sheet. C Mn Si S P Ni 0.16 1.08 0.40 0.025 0.023 0.15 3.1 Results with a mixture of Fe 3 O 4 - CuO powders A mixture of 2 mols Fe 3 O 4 and 1 mol CuO was compressed to form tablets and heated to 310 C in 0.1 N and 0.00001 N NaOH solution. X-ray analysis of the tablets at the end of the experiment showed the copper and red alpha Fe 2 0 3. Examination under the microscope established that copper was present in different crystalline forms. In 0.1 N NaOH the copper was in the form of platelets.. In 0.00001 N NaOH, it had grown in a spherical form. Both forms of copper have also been found in the iron oxide scales in boiler tubes. 3.2 Long term experiments with pre-oxidised steel sheet in alkaline solutions dosed with suspensions of CuO. To simulate the protective oxide film on tubes in operation, steel sheet was first placed for two days in a 0.5 N NaOH solution so that a passivating magnetite film could be obtained (Fig. 4). The oxidized samples were bent at one end and placed in PTFE capsules (Fig. 5). On the bent part of the sample 0.5 g of CuO was scattered. The samples were then heated at 310 C in alkaline solution for two days. Figure 4: Cross section of boiler steel corroded in 0.5 n NaOH at 310_C for 2 days in order to produce a protective magnetite coat.

06 koperoxide www.hbscc.nl - 6-3.2.1. Long term experiments in 0.1 n NaOH solution At the end of the experiments copper and Cu-0 were detected on the pre-oxidised steel samples. In Fig. 5 (position a) yellow copper and red-violet Cu2O can be seen on the bent part. Between the red coloured position c. and position a. there is a grey oxide lauer (position b.) The pos a-c are photomicrographs of cross sections at the individual positions. Figure 5: Pre-oxidised steel sample at the end of a long term experiment in 0.1 n NaOH at 310_C with the addition of 0.5 g CuO. Pos a: Cross section at the copper coated position a. Pos b: Cross section at the grey position b. above the copper coated zone a. Pos c: Cross section at the red upper part c. The grey oxide growth on the original magnetite film (position b.) is shown under the microscope in polarised light to be an optical anisotrope; this is also the case with the needle form of oxide on positions b and c. As the crystal structure Fe 3 O 4 and y Fe 2 0 3 are cubic, that is optical isotropes, the anisotrope oxide must be the trigonal alpha Fe 2 0 3. When the red oxide at position c. (Fig, 5) was illuminated by polarized light it shone with red internal reflection, indicating very finely grained alpha Fe 2 0 3. These phenomena can he explained by a drop in the stress in the oxide surface, produced by reduction of the copper oxide on the bent specimen (position a, Fig. 5) which allowed several

06 koperoxide www.hbscc.nl - 7 - oxidation types to be formed. In Fig. 6 the effect of resistance polarisation on the rest potential of the iron is represented in diagram form. At position a. where CuO is reduced to Cu 2 0 a high iron potential prevails so that good passivation associated with the formation of platelet alpha Fe 2 0 3 (Ref 3.) results. Because of the high electrical resistance of the magnetite film, the rest potential of iron in the upper part of the sample (position c) must be lower and insufficient for the formation of the platelet form of alpha Fe 2 0 3 (Fig 5 pos c). Figure 6: (Fig 9) Fig A; The electron transport with iron corrosion under the influence of copper oxide reduction. Fig B; Schematic representation of the influence of resistance polarization on the iron rest potential. 3.2.2. Long term experiments in 1.10-5 n NaOH. As mentioned before, in alkaline solution Fe 3 O 4 is oxidised to fine grained α-fe 2 0 3 by reduction of CuO. The protective magnetite film can therefore be destroyed in this way (Fig. 7).

06 koperoxide www.hbscc.nl - 8 - Figure 7: Cross section of a magnetite layer which has been destroyed by reduction of CuO after a long term experiment in 1.10-5 n NaOH. Fine grained α-fe 2 0 3 and copper can be recognized. It can be concluded from polarisation measurements that the reduction of CuO to Cu 2 O sets up a high iron rest potential if the electrical resistance of the magnetite is fairly small. At this high rest 2- potential (+230 mv) Fe 3 O 4 should dissolve with formation of FeO 4 ions and pitting of the steel should occur. This pitting was not however observed in long term experiments in 1.10-5 NaOH solutions. 3.3. Long term experiments on pre-oxidised steel sheet in alkaline solutions with Cu addition 0.5 g copper powder was scattered over the pre-oxidised steel sheet. After heating for two days to 310 0 C no great difference could be distinguished between the approximately 1.5 µm thick protective oxide film on samples with and without copper (Figs 8 and 9). The outer surfaces of the Fe 3 O 4 film is converted into α-fe 2 0 3 and this has clearly not affected the protective effect of the film. Figure 8 Left: The oxide layer after a long term experiment in 0.1 n NaOH without copper addition. Right: The oxide layer after a long term experiment in 0.1 n NaOH with copper addition. Platelets of α- Fe2O3 have grown between the copper particles. In long term experiments in 0.1 N NaOH solution, however, platelet crystals of α-fe 2 0 3 were formed at the places covered with copper, probably as a result of oxidation of FeO 2 2- ions (Ref.3 ) (Figs 8 right

06 koperoxide www.hbscc.nl - 9 - photo ). Copper is therefore to be regarded as a cathodic surface, and the presence of copper on the magnetite film stimulates oxide coating in strongly alkaline solutions (ph value greater than 11). Figure 9: The oxide layer after a long term experiment in 1.10-5 n NaOH with copper addition. A: without copper addition, B: With copper addition. 4. INVESTIGATION OF SOME COPPER CONTAINING OXIDE LAYERS ON SAMPLES TAKEN FROM OPERATION. An important objective of the investigation was the establishment of the extent of agreement between the results obtained from operation, samples and the laboratory tests. Figs 10 show photomicrographs of cross sections of oxide layers from boiler tubes. Where copper was present in the oxide layer, the magnetite layer was cracked in most instances. Layers of this type were found the decarburized as well as on the non-decarburised steel surfaces (Figs. 10). The cracking of the protective magnetite coat is therefore not connected with the steel structure. (ferrite-pearlite ratio). Cracked magnetite layers however were also found on the side away from the furnace, although in this position the coating contained only a small amount of copper or none at all. Copper was deposited with iron oxides on the side with high heat transfer. Occasionally pitting was found (Figs. 11A and 11B). Metallic copper was precipitated on the bottom of the pits.

06 koperoxide www.hbscc.nl - 10 - Figure 10: The oxide layer on an evaporator tube of a 170 kg/cm 2 absolute pressure boiler after 10500 operating hours.. Upper: A: unheated side, B: heated side Below: The oxide layer on a decarburated evaporator tube C: unheated side, D: heated side

06 koperoxide www.hbscc.nl - 11 - Figure 11: A: Pitting and copper in the pits of a steam receiver in a 73 kg=cm2 absolute pressure boiler (fig 20) B: Cross-section of an oxide coat on an evaporative tube of a 165 kg=cm2 absolute boiler. Under the amorphous copper-rich oxide a protective magnetite coat has grown. C and D: Homogenous unbroken oxide layers growing on an evaporator tube of a 150 kg=cm2 absolute boiler after 58000 operating hours. C: unheated position, D: heated position. E: Oxide layer on an evaporative tube of a 130 kg=cm2 absolute boiler. Figures 11C and 11D show an oxide layer from a boiler of the same type as that from which the magnetite layers in Figs. 10A - D were taken. There was no copper in the water in these boilers (Figs. 11C and 11D). The boiler tubes were not acid cleaned before commissioning. It is worth noting that a homogenous, continuous oxide layer was formed in these circumstances. A new protective coat can form under cracked, copper-coated magnetite layers provided copper oxides are no longer present in the water (Figs 11B and 11D). 5. CONCLUSIONS 1 Polarisation measurements on iron and copper have shown that copper oxides may affect the corrosion of iron and boiler steel can be derived. 2 Corrosion experiments on oxidised steel in galvanic contact with copper and copper oxide confirm the corrosion mechanism suggested by the electrochemical measurements.

06 koperoxide www.hbscc.nl - 12-3 In alkaline solutions parts of the magnetite layer are oxidized as a result of the reduction of copper oxide to copper. In general red α-fe 2 0 3 with a lower protective effect is produced. 4 However, in the immediate neighbourhood of areas in which copper oxide is reduced, in strongly alkaline solution, aggregates of platelets of α-fe 2 0 3 are formed which have a protective effect. In weakly alkaline solutions on the other hand, p ittin g can occur at such points, due to the oxidation of the magnetite to FeO 2-4. 5 Metallic copper has, in weakly alkaline solutions, no corrosive effect on the underlying magnetite layer. 6 2- In strongly alkaline solutions (ph greater than 11) FeO 2 ions are easily oxidized to Fe 2 0 3 on copper and thicker coatings can result. 7 Since relatively high local concentrations of alkali can occur in boiler tubes even with weak alkali operation, metallic copper cannot be disregarded as an agent which stimulates layer formation. 6. BIBLIOGRAPHY 1 Snel A. Electrotechniek 54, (1967), pp 51-55 2 Proceedings symposium internal corrosion in boilers Den Helder, 1968. 3 Huijbregts W.M.M., Osch G. van, Snel A.. 4th International Congress on metallic corrosion September 1969.