Corrosion protection system. Electrochemical protection - a reliable method in the fight against corrosion Unified system of corrosion protection

The paint and varnish and galvanic coatings currently used for corrosion protection have significant drawbacks. As for paint and varnish coatings, first of all, these are a low degree of reliability in case of mechanical damage, a low resource of single-layer coatings and the high cost of multi-layer coatings. Damage to the coating to the protected metal leads to the development of under-film corrosion. In this case, the aggressive environment gets under the insulating layer of paint and varnish, and corrosion of the base metal begins, which actively spreads under the paint layer, which leads to peeling of the protective layer.

As for electroplating, once the required properties are achieved, the electrolyte is sensitive to temperature fluctuations throughout the deposition process, which usually lasts several hours. Electroplating also involves the use of materials and chemicals, many of which are quite harmful. Metallization and paint and varnish coatings compete with paint and varnish, galvanic, as well as glass-enamel, bitumen, bitumen-rubber, polymer and epoxy coatings and electrochemical protection. Spramet™.

Spramet™- a set of combined metallization and paint coatings for protection against corrosion for up to 50 years, each of which has additional properties - heat resistance, fire retardant characteristics, heat insulating characteristics, etc.

Spramet™ systems are applied both in production conditions and in repair conditions - at the site of operation of the facility. Spramet's high resistance to mechanical damage, the absence of under-film corrosion and prices comparable to high-quality painting make this system an ideal choice for long-term corrosion protection of especially dangerous and unique objects.

Under the influence of the main operational aging factors (time, combined temperature and moisture, aggressive environments, differences in electrochemical potentials), the system Spramet protection does not change its original properties, withstands heating up to 650°C, has high mechanical characteristics: wear resistance, flexibility, and also actively resists corrosion. Spramet effectively protects welds and retains its protective and decorative properties throughout the entire period of operation.

In total, the operating costs of products protected with Spramet systems are 2-4 times less compared to paint and varnish or other coatings known today.

CJSC "Plakart" conducted large-scale tests and began using compositions Spramet™— protective corrosion protection systems based on metal matrices. These compositions consist of one or more layers. The basis of the composition is a metal matrix: sprayed aluminum, zinc or their alloys. To improve performance properties, an impregnating layer is applied to close the pores, then a protective or heat-insulating layer, as well as a tinting layer.

IN JSC "Plakart" A line of compositions has been developed to solve problems under various operating conditions:

  • Spramet-ANTIKOR
  • Spramet-TERMO
  • Spramet-NON-SLIP
  • Spramet-NANO

Benefits compositions by Spramet are:

  • higher hardness,
  • resistance to abrasive wear.

To increase the protective properties, metal coatings are impregnated with special compounds. Spramet protection systems guarantee a service life of objects from 15 to 50 years of service without corrosion.

The corrosion resistance of Spramet compositions is due to the following factors:

  • firstly, the base metallization layer of the Spramet system itself protects the surface well from corrosion;
  • secondly, impregnation of the porous structure of the metal matrix with special compounds enhances the anti-corrosion properties of the system in a wide range of aggressive environments and temperatures;
  • thirdly, if the Spramet composition is damaged before the protected material, another protection mechanism comes into play, namely a protector, which does not allow the development of under-film corrosion and delays local damage.

If the metal matrix is ​​damaged in an aggressive environment, the protected metal and the coating metal form a galvanic couple in the presence of water. The potential difference in such a circuit is determined by the location of the metals in the electrochemical voltage series. Since the material being protected is typically ferrous metals, the coating material begins to be consumed, protecting the base metal and sealing the damaged area. In this case, the corrosion rate is determined by the difference in the electrode potentials of the pair. In addition, if the damage to the coating is minor (scratches), it is filled with oxidation products of the coating material, and the corrosion process stops or slows down significantly. For example, in sea and fresh water, aluminum and zinc are consumed at a rate of 3-10 microns per year, providing at least 25 years of corrosion resistance at a layer thickness of 250 microns.

The advantages of product processing protective compositions Spramet include the following:

  • no restrictions on product sizes compared to hot-dip galvanizing and galvanizing;
  • the ability to protect welds after installation of the structure (in the case of welding galvanized products, the quality of the seam deteriorates due to zinc compounds entering the weld pool);
  • the possibility of applying Spramet protection in the field, which is not feasible either in the case of galvanizing or in the case of powder coating.

Some options for using the Spramet protection system

Spramet-ANTIKOR
  • Spramet-100 is a system that is resistant to corrosion and mechanical stress both under normal conditions and at temperatures up to 650°C.
  • Spramet-130 is used for protection against corrosion in fresh water; it has good resistance to the effects of water of various compositions and the mechanical effects of ice.
  • Spramet-150 is used for atmospheric corrosion, has good chemical resistance, and is used for storing petroleum products.
  • Spramet-300 is used for atmospheric corrosion, operating temperatures up to 400°C, and has high adhesion.
  • Spramet-310 is best used in heat and water supply facilities, and is resistant to inhibitors in water treatment systems.
  • Spramet-320 is used in wastewater treatment plants for housing and communal services: it has high resistance to the effects of liquids with variable pH.
  • Spramet-330 is used for atmospheric corrosion and corrosion in fresh water at operating temperatures up to 120°C; it is resistant to mechanical stress and has high adhesion.
  • Spramet-430 is used for protection against atmospheric corrosion in the presence of chlorides, is resistant to deicing agents and has a decorative effect.
  • Spramet-425 is best used for protection against corrosion in sea water, is resistant to mechanical stress, including ice, and has good resistance to chlorides.
Spramet-TERMO

Anti-corrosion high temperature system. Operating temperature - up to 650°C.

  • Spramet-100 is a corrosion-resistant system both under normal conditions and at temperatures up to 650°C.
  • Spramet-160. The metal matrix is ​​coated with a certified fire retardant compound that foams when exposed to high temperatures and provides fire resistance of up to 60 minutes.
Spramet-NON-SLIP Spramet-500 and 510 provide roughness of the treated surface, which prevents slipping of personnel and equipment. Applicable to metal walkways of offshore platforms, helipads, decks and other pedestrian metal walkways. Spramet-NANO In this case, the metal matrix is ​​a nanostructured coating. Such a coating has even lower porosity, much higher resistance to corrosion and erosive wear, and increased heat resistance, which significantly increases the service life of the protected product.

Due to the increased reliability and durability of the composition, Spramet is recommended for use when increased demands are placed on the protected object: a significant increase in the turnaround time or provision of anti-corrosion protection for the entire period of operation of metal structures, as well as in the absence of access to restore protective coatings.

Practical application (2011)

Specialists of ZAO Plakart have completed work on applying the system Spramet-100 for protection against corrosion of exhaust shafts of gas pumping units of the main gas pipeline system of OJSC Gazprom. The system is resistant to corrosion both under normal conditions and at temperatures up to 650°C, has an even white surface color, and is not afraid of mechanical damage, temperature changes and ultraviolet radiation.

Work on applying a corrosion-resistant system has been completed Spramet-300 on the crossbars of one of the cable-stayed bridges of the Alpika-Service Olympic route. Olympic venues operating in difficult climatic conditions require guaranteed long-term corrosion protection. System Spramet-ANTIKOR not only provides excellent protection against corrosion, but also serves as an excellent primer for paintwork.

Work on applying the protection system has been completed Spramet-150 on the internal surfaces of petroleum product storage tanks in the Astrakhan region. This anti-corrosion system was applied to tens of thousands of square meters of the internal surfaces of the tank and the pontoon floating in it.

From a standardization point of view "Spramet" system belongs to the group of combined metallization-paint and varnish coatings recommended for use on particularly dangerous and unique objects SNIP 2.03.11 “Protection of building structures from corrosion”, as well as many industry and ISO standards.

Quality system JSC "Plakart" certified according to ISO 9001. CJSC Plakart is a member of the self-regulatory organizations Zapaduralstroy and Sopkor. Trademark Spramet™ registered and owned by Plakart CJSC.

Electrochemical protection of metal structures from corrosion is based on the imposition of a negative potential on the protected product. High level It demonstrates effectiveness in cases where metal structures are subject to active electrochemical destruction.

1 The essence of anti-corrosion electrochemical protection

Any metal structure begins to deteriorate over time as a result of corrosion. For this reason, metal surfaces must be mandatory coated with special compounds consisting of various inorganic and organic elements. Such materials reliably protect the metal from oxidation (rusting) for a certain period. But after some time they need to be updated (new compounds applied).

Then, when the protective layer cannot be renewed, corrosion protection of pipelines, car bodies and other structures is carried out using electrochemical techniques. It is indispensable for protecting against rusting tanks and containers operating underground, the bottoms of sea ships, various underground communications, when the corrosion potential (it is called free) is in the zone of repassivation of the base metal of the product or its active dissolution.

The essence of electrochemical protection is that a direct electric current is connected from the outside to a metal structure, which forms cathode-type polarization of microgalvanic couple electrodes on the surface of the metal structure. As a result, the transformation of anodic regions into cathodic ones is observed on the metal surface. After such a transformation, the negative influence of the environment is perceived by the anode, and not the material itself from which the protected product is made.

Electrochemical protection can be either cathodic or anodic. With cathodic potential, the metal potential shifts to the negative side, and with anodic potential, it shifts to positive.

2 Cathodic electrical protection - how does it work?

The mechanism of the process, if you understand it, is quite simple. A metal immersed in an electrolytic solution is a system with a large number of electrons, which includes spatially separated cathode and anode zones, electrically closed to each other. This state of affairs is due to the heterogeneous electrochemical structure of metal products (for example, underground pipelines). Corrosion manifestations form on the anodic areas of the metal due to its ionization.

When a material with a high potential (negative) is added to the base metal located in the electrolyte, the formation of a common cathode is observed due to the process of polarization of the cathode and anodic zones. By high potential we mean a value that exceeds the potential of the anodic reaction. In the formed galvanic couple, a material with a low electrode potential dissolves, which leads to the suspension of corrosion (since the ions of the protected metal product cannot enter the solution).

The electric current required to protect the car body, underground tanks and pipelines, and the bottoms of ships can come from an external source, and not just from the functioning of a microgalvanic couple. In such a situation, the protected structure is connected to the “minus” of the electric current source. The anode, made of materials with a low degree of solubility, is connected to the “plus” of the system.

If the current is obtained only from galvanic couples, we speak of a process with sacrificial anodes. And when using current from an external source, we are talking about protecting pipelines, parts of vehicles and water vehicles with the help of superimposed current. The use of any of these schemes provides high-quality protection of the object from general corrosive decay and from a number of its special variants (selective, pitting, cracking, intergranular, contact types of corrosion).

3 How does the anodic technique work?

This electrochemical technique for protecting metals from corrosion is used for structures made of:

  • carbon steels;
  • passivating dissimilar materials;
  • highly alloyed and;
  • titanium alloys.

The anode scheme involves shifting the potential of the protected steel by positive side. Moreover, this process continues until the system enters a stable passive state. Such corrosion protection is possible in environments that are good conductors of electrical current. The advantage of the anodic technique is that it significantly slows down the rate of oxidation of the protected surfaces.

In addition, such protection can be carried out by saturating the corrosive environment with special oxidizing components (nitrates, dichromates and others). In this case, its mechanism is approximately identical to the traditional method of anodic polarization of metals. Oxidizers significantly increase the effect of the cathodic process on the steel surface, but they usually negatively affect the environment by releasing aggressive elements into it.

Anodic protection is used less frequently than cathodic protection, since many specific requirements are put forward for the protected object (for example, impeccable quality of welds of pipelines or a car body, constant presence of electrodes in the solution, etc.). In anode technology, cathodes are placed according to a strictly defined scheme, which takes into account all the features of the metal structure.

For the anodic technique, poorly soluble elements are used (cathodes are made from them) - platinum, nickel, stainless high-alloy alloys, lead, tantalum. The installation itself for such corrosion protection consists of the following components:

  • protected structure;
  • current source;
  • cathode;
  • special reference electrode.

It is allowed to use anodic protection for containers where mineral fertilizers, ammonia compounds, sulfuric acid are stored, for cylindrical installations and heat exchangers operated at chemical plants, for tanks in which chemical nickel plating is performed.

4 Features of tread protection for steel and metal

A fairly frequently used option for cathodic protection is the technology of using special protector materials. With this technique, an electronegative metal is connected to the structure. Over a given period of time, corrosion affects the protector, and not the protected object. After the protector is destroyed to a certain level, a new “defender” is installed in its place.

Protective electrochemical protection is recommended for treating objects located in soil, air, water (that is, in chemically neutral environments). Moreover, it will be effective only when there is some transition resistance between the medium and the protector material (its value varies, but in any case it is small).

In practice, protectors are used when it is economically infeasible or physically impossible to supply the required charge of electric current to an object made of steel or metal. It is worth separately noting the fact that protective materials are characterized by a certain radius over which their positive effect extends. For this reason, you should correctly calculate the distance to remove them from the metal structure.

Popular protectors:

  • Magnesium. They are used in environments with a pH of 9.5–10.5 units (soil, fresh and slightly salted water). They are made from magnesium-based alloys with additional alloying with aluminum (no more than 6–7%) and zinc (up to 5%). For the environment, such protectors that protect objects from corrosion are potentially unsafe due to the fact that they can cause cracking and hydrogen embrittlement of metal products.
  • Zinc. These “protectors” are indispensable for structures operating in water with a high salt content. There is no point in using them in other environments, since hydroxides and oxides appear on their surface in the form of a thick film. Zinc-based protectors contain minor (up to 0.5%) additives of iron, lead, cadmium, aluminum and some other chemical elements.
  • Aluminum. They are used in sea running water and at objects located on the coastal shelf. Aluminum protectors contain magnesium (about 5%) and zinc (about 8%), as well as very small amounts of thallium, cadmium, silicon, and indium.

In addition, iron protectors are sometimes used, which are made from iron without any additives or from ordinary carbon steels.

5 How is the cathode circuit performed?

Temperature changes and ultraviolet rays cause serious damage to all external components and components of vehicles. Protecting the car body and some of its other elements from corrosion by electrochemical methods is recognized as a very effective way to prolong the ideal appearance of the car.

The principle of operation of such protection is no different from the scheme described above. When protecting a car body from rusting, the function of an anode can be performed by almost any surface that is capable of efficiently conducting electric current (wet road surfaces, metal plates, steel structures). The cathode in this case is the vehicle body itself.

Elementary methods of electrochemical protection of a car body:

  1. We connect the body of the garage in which the car is parked through the mounting wire and an additional resistor to the battery positive. This protection against corrosion of the car body is especially effective in the summer, when the greenhouse effect is present in the garage. This effect precisely protects the external parts of the car from oxidation.
  2. We install a special grounding metalized rubber “tail” in the rear of the vehicle so that drops of moisture fall on it while driving in rainy weather. At high humidity, a potential difference is formed between the highway and the car body, which protects the outer parts of the vehicle from oxidation.

The car body is also protected using protectors. They are mounted on the thresholds of the car, on the bottom, under the wings. The protectors in this case are small plates made of platinum, magnetite, carboxyl, graphite (anodes that do not deteriorate over time), as well as aluminum and “stainless steel” (they should be replaced every few years).

6 Nuances of anti-corrosion protection of pipelines

Pipe systems are currently protected using drainage and cathodic electrochemical techniques. When protecting pipelines from corrosion using the cathodic scheme, the following are used:

  • External current sources. Their plus will be connected to the anode grounding, and the minus to the pipe itself.
  • Protective anodes using current from galvanic pairs.

The cathodic technique involves the polarization of the protected steel surface. In this case, underground pipelines are connected to the “minus” of the cathodic protection complex (in fact, it is a current source). “Plus” is connected to the additional external electrode using a special cable, which is made of conductive rubber or graphite. This circuit allows you to obtain a closed-type electrical circuit, which includes the following components:

  • electrode (external);
  • electrolyte located in the soil where the pipelines are laid;
  • pipes directly;
  • cable (cathode);
  • current source;
  • cable (anode).

For tread protection of pipelines, materials based on aluminum, magnesium and zinc are used, the efficiency of which is 90% when using protectors based on aluminum and zinc and 50% for protectors made of magnesium alloys and pure magnesium.

For drainage protection of pipe systems, technology is used to drain stray currents into the ground. There are four options for drainage piping - polarized, earthen, reinforced and straight. With direct and polarized drainage, jumpers are placed between the “minus” of stray currents and the pipe. For the earth protection circuit, it is necessary to make grounding using additional electrodes. And with increased drainage of pipe systems, a converter is added to the circuit, which is necessary to increase the magnitude of the drainage current.

Preface

The goals, basic principles and basic procedure for carrying out work on interstate standardization are established by GOST 1.0-92 “Interstate standardization system. Basic provisions" and GOST 1.2-97 "Interstate standardization system. Interstate standards, rules and recommendations for interstate standardization. Procedure for development, adoption, application, updating and cancellation"

Standard information

1. DEVELOPED by the Technical Committee for Standardization TC 214 “Protection of Products and Materials from Corrosion” (State Unitary Enterprise of the Order of the Red Banner of Labor Academy of Public Utilities named after K.D. Pamfilov, State Unitary Enterprise VNII of Railway Transport, FSUE “VNII Standard”)

2. INTRODUCED by the Federal Agency for Technical Regulation and Metrology

3. ADOPTED by the Interstate Council for Standardization, Metrology and Certification (Minutes No. 27 of June 22, 2005)

Short name of the country according to MK (ISO3166)004-97 Country code according to MK (ISO 3166) 004-97 Abbreviated name of the national standardization body
Azerbaijan AZ Azstandard
Armenia A.M. Ministry of Trade and Economic Development of the Republic of Armenia
Belarus BY State Standard of the Republic of Belarus
Kazakhstan KZ Gosstandart of the Republic of Kazakhstan
Kyrgyzstan KG Kyrgyzstandard
Moldova M.D. Moldova-Standard
Russian Federation RU Federal Agency for Technical Regulation and Metrology
Tajikistan T.J. Tajikstandard
Turkmenistan TM Main State Service "Turkmenstandartlary"
Uzbekistan UZ Uzstandard

4. This standard takes into account the main normative provisions of ISO/IEC Guide 21:1999 “Adoption of international standards as regional or national standards”.

(ISO/IEC Guide 21:1999 “Regional or national adoption of international standards deliverables”)

5. By Order of the Federal Agency for Technical Regulation and Metrology dated October 25, 2005 No. 262-st, the interstate standard GOST 9.602-2005 was put into effect directly as a national standard Russian Federation from January 1, 2007

6. INSTEAD GOST 9.602-89

Information on the entry into force (termination) of this standard and amendments to it is published in the “National Standards” index.



Information about changes to this standard is published in the “National Standards” index, and the text of the changes is published in the “National Standards” information indexes. In case of revision or cancellation of this standard, the relevant information will be published in the information index “National Standards”


Preface Information about the standard Introduction General requirements for corrosion protection 1. Scope of application 2. Normative references 3. General provisions 4. Corrosion hazard criteria 5 Selection of corrosion protection methods 6. Requirements for protective coatings and quality control methods 7. Requirements for electrochemical protection 8. Requirements for limiting leakage currents at sources of stray currents 9. Requirements for performing work on anti-corrosion protection Appendix A (informative ) Determination of the electrical resistivity of the soil Appendix B (informative) Determination of the average cathode current density Appendix B (informative) Determination of the biocorrosive aggressiveness of the soil Appendix D (informative) Determination of the dangerous influence of stray direct current Appendix E (reference) Determination of the presence of stray currents in the ground Appendix E (reference) Determination of the presence of current in underground communication structures Appendix G (reference) Determination of the dangerous influence of alternating current Appendix I (reference) Determination of the adhesion of protective coatings Appendix K (reference) Determination of coating adhesion to steel after exposure to water Appendix L (informative) Determination of the peeling area of ​​protective coatings during cathodic polarization Appendix M (informative) Determination of the transient electrical resistance of an insulating coating Appendix H (informative) Determination of indentation resistance Appendix P (informative) Coatings for protection against external corrosion of pipelines heating networks and conditions for their installation Appendix P (informative) Measurement of polarization potentials during electrochemical protection Appendix C (informative) Determination of the total potential of a structure under electrochemical protection Appendix T (informative) Measurement of the potential of a channel laying pipeline during electrochemical protection of pipelines with anode grounding located in channel Appendix U (informative) Determination of the minimum polarization protective potential of underground steel pipelines by displacement from the stationary potential Bibliography

Introduction



Underground metal pipelines, cables and other structures are one of the most capital-intensive industries in the economy. The livelihoods of cities and towns depend on their normal, uninterrupted functioning.

The greatest influence on the operating conditions and service life of underground metal structures is exerted by the corrosive and biocorrosive aggressiveness of the environment, as well as stray direct currents, the source of which is electrified rail transport, and alternating currents of industrial frequency.

The impact of each of these factors, and especially their combination, can reduce the service life of steel underground structures several times and lead to the need for premature relaying of obsolete pipelines and cables.

The only possible way to combat this negative phenomenon is the timely application of measures for anti-corrosion protection of steel underground structures.

This standard takes into account the latest scientific and technical developments and achievements in the practice of anti-corrosion protection accumulated by operational, construction and design organizations.

This standard establishes corrosion hazard criteria and methods for their determination; requirements for protective coatings, their quality standards for different operating conditions of underground structures (adhesion of insulation to the pipe surface, adhesion between layers of coatings, resistance to cracking, resistance to impact, resistance to UV radiation, etc.) and methods for assessing the quality of coatings; requirements for electrochemical protection are regulated, as well as methods for monitoring the effectiveness of anti-corrosion protection.

The implementation of this standard will increase the service life and operational reliability of underground metal structures, reduce the costs of their operation and major repairs.

INTERSTATE STANDARD
Unified system of corrosion and aging protection Underground structures General requirements for corrosion protection Unified system of corrosion and aging protection. Underground constructions. General requirements for corrosion protection

Date of introduction - 2007-01-01

Application area

This standard establishes general requirements for corrosion protection of the outer surface of underground metal structures (hereinafter referred to as structures): pipelines and tanks (including trench type) made of carbon and low-alloy steels, power cables with voltage up to 10 kV inclusive; communication and signaling cables in a metal sheath, steel structures of unattended reinforcement (NUP) and regeneration (NRP) points of communication lines, as well as requirements for objects that are sources of stray currents, including electrified rail transport, direct current transmission lines via the wire-ground system, industrial enterprises consuming direct current for technological purposes.

The standard does not apply to the following structures: communication cables with a hose-type protective cover; reinforced concrete and cast iron structures; communications laid in tunnels, buildings and sewers; piles, sheet piles, columns and other similar metal structures; main pipelines transporting natural gas, oil, petroleum products, and branches from them; pipelines of compressor, pumping and pumping stations, oil depots and head structures of oil and gas fields; installations for complex gas and oil treatment; heating network pipelines with polyurethane foam thermal insulation and a shell pipe made of rigid polyethylene (pipe-in-pipe design), having a functioning system for operational remote monitoring of the condition of pipeline insulation; metal structures located in permafrost soils.

GOST 9.048-89 Unified system of protection against corrosion and aging. Technical products. Laboratory test methods for resistance to mold fungi

GOST 9.049-91 Unified system of protection against corrosion and aging. Polymer materials and their components. Laboratory test methods for resistance to mold fungi

GOST 12.0.004-90 System of occupational safety standards. Organization of occupational safety training. General provisions

GOST 12.1.003-83 System of occupational safety standards. Noise. General safety requirements

GOST 12.1.005-88 System of occupational safety standards. General sanitary and hygienic requirements for the air in the working area

GOST 12.2.004-75 System of occupational safety standards. Special machines and mechanisms for pipeline construction. Safety requirements

GOST 12.3.005-75 System of occupational safety standards. Painting works. General safety requirements

GOST 12.3.008-75 System of occupational safety standards. Production of metallic and non-metallic inorganic coatings. General safety requirements

GOST 12.3.016-87 System of occupational safety standards. Construction. Anti-corrosion works. Safety requirements

GOST 12.4.026-76 1) System of occupational safety standards. Signal colors and safety signs

GOST 112-78 Meteorological glass thermometers. Specifications

GOST 411-77 Rubber and glue. Methods for determining the bond strength with metal during peeling

GOST 427-75 Metal measuring rulers. Specifications

GOST 1050-88 Calibrated rolled products with special surface finishing from high-quality carbon structural steel. General technical conditions

GOST 2583-92 Batteries made of cylindrical manganese-zinc cells with salt electrolyte. Specifications

GOST 2678-94 Rolled roofing and waterproofing materials. Test methods

GOST 2768-84 Technical acetone. Specifications

GOST 4166-76 Sodium sulfate. Specifications

GOST 4650-80 Plastics. Methods for determining water absorption

GOST 5180-84 Soils. Methods laboratory determination physical characteristics.

GOST 5378-88 Protractors with vernier. Specifications

GOST 6055-86 2) Water. Unit of hardness

GOST 6323-79 Wires with polyvinyl chloride insulation for electrical installations. Specifications

GOST 6456-82 Sanding paper. Specifications

GOST 6709-72 Distilled water. Technical conditions.

GOST 7006-72 Protective cable covers. Design and types, technical requirements and test methods

GOST 8711-93 (IEC51-2-84) Analogue indicating electrical measuring devices of direct action and auxiliary parts for them. Part 2. Special requirements for ammeters and voltmeters

GOST 9812-74 Petroleum insulating bitumens. Specifications

GOST 11262-80 Plastics. Tensile test method.

GOST 12026-76 Laboratory filter paper. Specifications

GOST 13518-68 Plastics. Method for determining the resistance of polyethylene to stress cracking.

GOST 14236-81 Polymer films. Tensile test method.

GOST 14261-77 Hydrochloric acid of special purity. Technical conditions.

GOST 15140-78 Paint and varnish materials. Methods for determining adhesion.

GOST 16337-77 High pressure polyethylene. Specifications

GOST 16783-71 Plastics. Method for determining the brittleness temperature when squeezing a sample folded in a loop

GOST 22261-94 Instruments for measuring electrical and magnetic quantities. General technical conditions

GOST 25812-83 3) Main steel pipelines. General requirements for corrosion protection

GOST 29227-91 (ISO 835-1-81) Laboratory glassware. Graduated pipettes. Part 1. General requirements.

Note: When using this standard, it is advisable to check the validity of the reference standards using the “National Standards” index, compiled as of January 1 of the current year, and according to the corresponding information indexes published in the current year. If the reference standard is replaced (changed), then when using this standard you should be guided by the replaced (changed) standard. If the reference standard is canceled without replacement, then the provision in which a reference is made to it is applied in the part that does not affect this reference.

1) In the Russian Federation, GOST R 12.4.026-2001 “System of occupational safety standards” is in force. Signal colors, safety signs and signal markings. Purpose and rules of use. General technical requirements and characteristics. Test methods".

2) In the Russian Federation, GOST R 52029-2003 “Water. Unit of hardness."

3) In the Russian Federation, GOST R 51164-98 “Main steel pipelines” is in force. General requirements for corrosion protection."

General provisions

3.1. The requirements of this standard are taken into account when designing, constructing, reconstructing, repairing, and operating underground structures, as well as objects that are sources of stray currents. This standard is the basis for the development regulatory documents(ND) on protection specific types underground metal structures and measures to limit stray currents (leakage currents).

3.2. Means of protection against corrosion (materials and design of coatings, cathodic protection stations, instruments for monitoring the quality of insulating coatings and determining the danger of corrosion and the effectiveness of anti-corrosion protection) are used only in accordance with the requirements of this standard and having a certificate of conformity.

3.3. When developing a project for the construction of structures, a project for protecting them from corrosion is simultaneously developed.

Note: For signaling, centralization and interlocking (SCB), power and communication cables used on the railway, when it is not possible to determine the parameters of electrochemical protection at the project development stage, working drawings of electrochemical protection can be developed after laying the cables based on measurement data and trial activation of protective devices within the time limits established by the ND.

3.4. Measures to protect against corrosion of structures under construction, operating and reconstructed are provided for in protection projects in accordance with the requirements of this standard.

In construction and reconstruction projects of structures that are sources of stray currents, measures are taken to limit leakage currents.

3.5. All types of corrosion protection provided for by the construction project are accepted for use before the structures are put into operation. During the construction process for underground steel gas pipelines and liquefied gas tanks, electrochemical protection is put into effect in zones of dangerous influence of stray currents no later than one month, and in other cases - no later than six months after laying the structure in the ground; for communication structures - no later than six months after they are laid in the ground.

It is not allowed to commission objects that are sources of stray currents until all the measures provided for by the project to limit these currents have been carried out.

3.6. The protection of structures from corrosion is carried out in such a way as not to impair protection from electromagnetic influences and lightning strikes.

3.7. During the operation of structures, the effectiveness of anti-corrosion protection and the risk of corrosion is systematically monitored, as well as the causes of corrosion damage are recorded and analyzed.

3.8. Work to repair failed electrochemical protection installations is classified as an emergency.

3.9. The structures are equipped with control and measuring points (CPS).

To monitor the corrosion state of communication cables laid in cable ducts, inspection devices (wells) are used.

Corrosion Hazard Criteria

4.1. The criteria for the danger of corrosion of structures are:

Corrosive aggressiveness of the environment (soil, ground and other waters) in relation to the metal of the structure (including biocorrosive aggressiveness of soils);

Dangerous effects of stray direct and alternating currents.

4.2. To assess the corrosive aggressiveness of the soil in relation to steel, determine the electrical resistivity of the soil, measured in field and laboratory conditions, and the average cathode current density at a potential displacement of 100 mV negative than the stationary potential of the steel in the soil (Table 1). If, when determining one of the indicators, a high corrosive aggressiveness of the soil is established (and for reclamation structures - average), then the other indicator is not determined.

Methods for determining soil electrical resistivity and average cathode current density are given in Appendices A and B, respectively.

Notes

1. If the electrical resistivity of the soil, measured in laboratory conditions, is equal to or more than 130 Ohm m, the corrosive aggressiveness of the soil is considered low and is not assessed based on the average cathode current density z K.

2. The corrosive aggressiveness of the soil in relation to the steel armor of communication cables and steel structures of the NUP is assessed only by the electrical resistivity of the soil, determined in the field (see Table 1).

3. The corrosive aggressiveness of the soil in relation to the steel of pipes of ductless heating networks is assessed by the electrical resistivity of the soil, determined in field and laboratory conditions (see Table 1).

4. For heating network pipelines laid in channels, thermal chambers, inspection wells, etc., the corrosion hazard criterion is the presence of water or soil in the channels (thermal chambers, inspection wells, etc.) when the water or soil reaches thermal insulation structure or pipeline surface.

Table 1

table 2

Table 3

Table 4

Table 5

Requirements for protective coatings and quality control methods

6.1. The designs of highly reinforced and reinforced types of protective coatings used to protect steel underground pipelines, except for heat pipelines, are given in Table 6; coating requirements are in tables 7 and 8, respectively.

It is allowed to use other designs of protective coatings that ensure compliance with the requirements of this standard.

6.2. During the construction of pipelines, welded pipe joints, shaped elements (hydraulic seals, condensate collectors, elbows, etc.) and places where the protective coating is damaged are insulated under route conditions with the same materials as the pipelines, or with others whose protective properties meet the requirements given in Table 7 , not inferior to the coating of the linear part of the pipe and having adhesion to the coating of the linear part of the pipeline.

6.3. When repairing operating pipelines, it is allowed to use coatings similar to those previously applied to the pipeline, as well as those based on heat-shrinkable materials, polymer-bitumen, polymer-asmol and adhesive polymer tapes, except for polyvinyl chloride.

Note: To insulate joints and repair damaged areas of pipelines with mastic bitumen coatings, the use of polyethylene tapes is not allowed.

6.4. For steel tanks installed in the ground or embanked with soil, very protective coatings are used. reinforced type designs No. 5 and 7 according to table 6.

Table 6

Table 7

Requirements for highly reinforced coatings

Indicator name 1) Meaning Test method Coverage number according to table 6
1. Adhesion to steel, not less than, at a temperature Appendix I, method A
20˚С, N/cm 70,0
50,0
35,0 1 (for pipelines with a diameter of up to 820 mm), 9
20,0 3, 4, 5, 6, 10
40˚С, N/cm 35,0
20,0 1, 9
10,0 3, 4, 10
20˚С, MPa (kg/cm 2) 0,5 (5,0) Appendix I, method B 7, 8
2. Adhesion in overlap at a temperature of 20˚C, N/cm, not less: Appendix I, method A
Tapes to Tape 7,0 3, 4, 5
35,0
20,0
Wrappers for tape 5,0
Extruded polyolefin layer to tape 15,0
3. Adhesion to steel after exposure to water for 1000 hours at a temperature of 20ºC, N/cm, not less 50,0 Appendix K 1 (for pipelines with a diameter of 820 mm or more)
35,0 1, 2 (for pipelines with a diameter of up to 820 mm)
30,0
15,0 3, 4
4. Impact strength, not less, at temperature: According to GOST 25812, Appendix 5
From minus 15ºС to minus 40ºС, J For all coatings (except 1, 2, 3.9), for pipelines with a diameter, mm, no more than:
5,0
7,0
9,0
20ºС, J/mm coating thickness 1, 2, 3, 9 for pipelines with diameter, mm:
4,25 Up to 159
5,0 Up to 530
6,0 St. 530
2 for pipelines with diameter, mm:
8,0 From 820 to 1020
10,0 From 1220 and more
5. Tensile strength, MPa, not less, at a temperature of 20º 2) 12,0 GOST 11262 1, 2, 9
10,0 GOST 14236 3, 8, 10
6. Area of ​​coating peeling during cathodic polarization, cm 2, no more, at temperature: Appendix L
20ºС 5,0 For all coatings
40ºС 8,0 1, 2, 9
7. Resistance to stress cracking at a temperature of 50ºС, h, not less According to GOST 13518 For coatings with a polyolefin layer thickness of at least 1 mm: 1, 2, 3, 8, 9, 10
8. Resistance to UV radiation in a flow of 600 kWh/m at a temperature of 50ºС, h, no less According to GOST 16337 1, 2, 3, 8
9. Brittleness temperature, ºС, not higher -50ºС According to GOST 16783 4, 9
10. Temperature of fragility of the mastic layer (flexibility on the rod)ºС, no more -15ºС According to GOST 2678-94 5, 6, 8, 10
11. Transition electrical resistance of the coating in a 3% solution of Na 2 SO 4 at a temperature of 20ºC, Ohm m 2, not less than: Appendix M
original 10 10 1, 2, 9
10 8 3, 4, 5, 6, 7, 8, 10
In 100 days. excerpts 10 9 1, 2, 9
10 7 3, 4, 5, 6, 7, 8, 10
12. Transient electrical resistance of the coating 3) on completed pipeline sections (in pits) at temperatures above 0˚C, Ohm m 2, not less 5 10 5 Appendix M 1, 2, 3, 8, 9, 10
2·10 5 4, 5, 6
5 10 4
13. Dielectric continuity (no breakdown at electric voltage), kV/mm 5,0 Spark flaw detector 1, 2, 3, 4, 5, 6, 8, 9, 10
4,0
14. Penetration (indentation) resistance, mm, no more, at temperature: Appendix H For all coatings
Up to 20˚С 0,2
Over 20˚С 0,3
15. Water saturation in 24 hours, %, no more 0,1 According to GOST 9812 5, 6, 7, 8, 10
16. Fungal resistance, points, no less According to GOST 9.048, GOST 9.049 For all types of highly reinforced coatings.
1) Property indicators are measured at 20˚С, unless other conditions are specified in the ND. 2) The tensile strength of combined coatings, tapes and protective wraps (in megapascals) is related only to the thickness of the supporting polymer base without taking into account the thickness of the mastic or rubber sublayer, while the tensile strength related to the total thickness of the tape must be at least 50 N/ cm width, and the protective wrapper is at least 80 N/cm width. 3) Extremely permissible value The transient electrical resistance of the coating on underground pipelines operated for a long time (more than 40 years) must be at least 50 Ohm m 2 - for polymer coatings.

Table 8

Requirements for reinforced coatings

Indicator name 1) Meaning Test method Coverage number according to table 6
1 Adhesion to steel at a temperature of 20 °C:
N/cm, no less 50,0 Appendix I, method A 11 (for pipelines with a diameter of 820 mm and more) -
35,0 11 (for pipelines with a diameter of up to 820 mm) -
20,0
MPa (kgf/cm 2), not less 0,5 (5,0) Appendix I, method B
Point, no more According to GOST 15140 14, 15
2 Adhesion in overlap at a temperature of 20 °C, N/cm, not less: Appendix I, method A
tape to tape 7,0
layer of extruded polyethylene to the tape 15,0
3 Adhesion to steel after exposure to water for 1000 hours at a temperature of 20 °C:
N/cm, no less 50,0 Appendix K 11 (for pipelines with a diameter of 820 mm or more)
35,0 11 (for pipelines with a diameter of up to 820 mm)
15,0
point, no more According to GOST 15140 14, 15
4 Impact strength, no less, at temperature: According to GOST 25812, Appendix 5
from minus 15 °C to plus 40 °C, J 2,0
6,0 13/H^
8,0 15,16
20 °C, J/mm coating thickness 11, 12 for pipelines with diameter:
4.25 up to 159 mm
5,0 up to 530 mm
6,0 St. 530 mm
5 Tensile strength, MPa, not less, at a temperature of 20 °C 2)
12,0 According to GOST 11262
10,0 According to GOST 14236
6 Area of ​​coating peeling during cathodic polarization, cm 2, no more, at temperature: Appendix L
20°C 4,0 14, 15, 16
5,0 11, 12, 13
40°С 8,0 11, 15, 16
7 Resistance to stress cracking at temperature According to GOST 13518 For coatings with a polyolefin layer thickness of at least 1 mm:
50°С, h, not less 11,12
8 Resistance to UV radiation in a flow of 600 kWh/m at a temperature of 50 °C, h, not less According to GOST 16337
11, 12
9 Transition electrical resistance of the coating in a 3% solution of Na 2 SO 4 at a temperature of 20 °C, Ohm-m 2, not less: Appendix M
original 10 10
10 8 12, 13, 15, 16
5 10 2
after 100 days of exposure 10 9
10 7 12,13,15,16
3 10 2
10 Transition electrical resistance of the coating 3) on the completed pipeline section (in pits) at temperatures above 0°C, Ohm m 2, not less 3·10 5 Appendix M 11, 12, 16
1·10 5
5 10 4
11 Dielectric continuity (no breakdown at electric voltage), kV/mm 5,0 Spark flaw detector 11, 12, 16
4,0
2,0
12. Water saturation in 24 hours, %, no more 0,1 According to GOST 9812
13. Mushroom resistance, point, no less According to GOST 9.048, GOST 9.049 For all reinforced coatings
1) Property indicators are measured at 20°C, unless other conditions are specified in the ND. 2) The tensile strength of the combined coating, tapes and protective wraps (in megapascals) is related only to the thickness of the supporting polymer base without taking into account the thickness of the mastic or rubber sublayer. In this case, the tensile strength related to the total thickness of the tape must be at least 50 N/cm of width, and of the protective wrap - at least 80 N/cm of width. 3) The maximum permissible value of the transient electrical resistance of the coating on underground pipelines operated for a long time (more than 40 years) must be at least 50 Ohm-m 2 for mastic bitumen coatings and at least 200 Ohm-m 2 for polymer coatings.

6.5. The thickness of protective coatings is controlled by non-destructive testing using thickness gauges and other measuring instruments:

In basic and factory conditions for two-layer and three-layer polymer coatings based on extruded polyethylene, polypropylene; combined based on polyethylene tape and extruded polyethylene; strip polymer and mastic coatings - on every tenth pipe of one batch at least in four points around the circumference of the pipe and in places that raise doubts;

In route conditions for mastic coatings - on 10% of welded joints of pipes, insulated manually, at four points around the circumference of the pipe;

On tanks for mastic coatings - at one point on each square meter of surface, and in places where insulating coatings are kinked - every 1 m circumference,

6.6. The adhesion of protective coatings to steel is controlled using adhesimeters:

In basic and factory conditions - every 100m or on every tenth pipe in a batch;

In route conditions - on 10% of welded joints of pipes insulated manually;

On tanks - at least two points around the circumference,

For mastic coatings, it is allowed to determine adhesion by cutting out an equilateral triangle with a side length of at least 4.0 cm, followed by peeling the coating from the top of the cut angle. Adhesion is considered satisfactory if, when new coatings are peeled off, more than 50% of the area of ​​the peeled mastic remains on the pipe metal. The coating damaged during the adhesion test is repaired in accordance with the ND.

6.7. The continuity of pipe coatings after completion of the insulation process in basic and factory conditions is controlled over the entire surface with a spark flaw detector at a voltage of 4.0 or 5.0 kV per 1 mm of coating thickness (depending on the coating material), and for silicate-enamel - 2 kV per 1 mm of thickness, as well as on the route before lowering the pipeline into the trench and after insulating the tanks.

6.8. Defective areas, as well as through damage to the protective coating, identified during testing of its quality, are corrected before backfilling the pipeline. During repairs, ensure uniformity, solidity and continuity of the protective coating; After correction, the repaired areas are subject to secondary inspection.

6.9. After backfilling the pipeline, the protective coating is checked for the absence of external damage that would cause direct electrical contact between the pipe metal and the ground, using instruments to detect locations of insulation damage.

6.10. To protect pipelines of heating networks from external corrosion, protective coatings are used, the designs and conditions of use of which are given in Appendix P.

Requirements for electrochemical protection

7.1. Requirements for electrochemical protection in the absence of the dangerous influence of direct stray and alternating currents

7.1.1. Cathodic polarization of structures (except for pipelines transporting media heated above 20 °C) is carried out in such a way that the polarization potentials of the metal relative to the saturated copper-sulfate reference electrode are between the minimum and maximum (in absolute value) values ​​in accordance with Table 9.

Polarization potentials are measured in accordance with Appendix P.

Table 9

Requirements for electrochemical protection in the presence of the dangerous influence of direct stray currents

7.2.1. Protection of structures from the dangerous influence of direct stray currents is carried out in such a way as to ensure the absence of anode and alternating zones on the structure.

The total duration of positive potential displacements relative to the stationary potential is allowed to be no more than 4 minutes per day.

Determination of potential displacements (the difference between the measured potential of the structure and the stationary potential) is carried out in accordance with Appendix D.

INTERSTATE STANDARD

Unified system of protection against corrosion and aging

METALS AND ALLOYS

Determination methods
corrosion indicators
and corrosion resistance

GOST 9.908-85

MOSCOW
IPC PUBLISHING HOUSE OF STANDARDS
1999

INTERSTATE STANDARD

Date of introduction 01.01.87

This standard establishes the main indicators of corrosion and corrosion resistance (chemical resistance) of metals and alloys for continuous, pitting, intergranular, exfoliating corrosion, spot corrosion, stress-corrosion cracking, corrosion fatigue and methods for their determination. Indicators of corrosion and corrosion resistance are used in corrosion research, testing, inspection of equipment and defect detection of products during production, operation, and storage.

1. INDICATORS OF CORROSION AND CORROSION RESISTANCE

1.1. Indicators of corrosion and corrosion resistance of metal are determined under given conditions, taking into account their dependence on chemical composition and the structure of the metal, the composition of the environment, temperature, hydro- and aerodynamic conditions, the type and magnitude of mechanical stresses, as well as the purpose and design of the product. 1.2. Indicators of corrosion resistance can be quantitative, semi-quantitative (scores) and qualitative. 1.3. Corrosion resistance should, as a rule, be characterized by quantitative indicators, the choice of which is determined by the type of corrosion and operational requirements. The basis of most of these indicators is the time it takes to achieve a given (acceptable) degree of corrosion damage to the metal under certain conditions. Indicators of corrosion resistance, primarily the time until the permissible depth of corrosion damage is reached, in many cases determine the service life, durability and storage of structures, equipment and products. 1.4. The main quantitative indicators of corrosion and corrosion resistance of the metal are given in the table. For a number of corrosion effects (integral corrosion indicators), the corresponding rate (differential) corrosion indicators are given.

Type of corrosion

Basic quantitative indicators of corrosion and corrosion resistance

Corrosion effect (integral corrosion indicator)

Speed ​​(differential) corrosion indicator

Corrosion resistance index

Complete corrosion Corrosion penetration depth Linear corrosion rate Time of penetration of corrosion to the permissible (specified) depth*
Mass loss per unit area Mass loss rate Time until the mass decreases by the permissible (specified) value*
Corrosion spots Degree of surface damage
Pitting corrosion Maximum pitting depth Maximum speed pitting penetration Minimum time for pitting to penetrate to the permissible (specified) depth*
Maximum diameter of pitting at the mouth Minimum time to achieve the permissible (specified) size of the pitting diameter at the mouth*
Degree of surface damage by pitting Time to reach the permissible (specified) degree of damage*
Intergranular corrosion Penetration time to permissible (specified) depth*
Decrease in mechanical properties (elongation, contraction, impact strength, tensile strength) Time required for mechanical properties to decrease to an acceptable (specified) level*
Corrosion cracking Depth (length) of cracks Crack growth rate Time until first crack appears**
Decrease in mechanical properties (relative elongation, narrowing) Time until sample failure** Safe stress level** (conditional limit of long-term corrosion strength**) Threshold stress intensity factor for corrosion cracking**
Corrosion fatigue Depth (length) of cracks Crack growth rate Number of cycles before sample failure** Conditional limit of corrosion fatigue** Threshold stress intensity factor for corrosion fatigue**
Exfoliation corrosion Degree of damage to the surface by delamination Total length of ends with cracks
Corrosion penetration depth Corrosion penetration rate
With a linear dependence of the corrosion effect on time, the corresponding speed indicator is found by the ratio of the change in the corrosion effect over a certain time interval to the value of this interval. If the corrosion effect has a nonlinear dependence on time, the corresponding corrosion rate indicator is found as the first derivative with respect to time graphically or analytically. 1.5. Corrosion resistance indicators, marked in the table with *, are determined from the time dependence of the corresponding integral corrosion indicator graphically, shown in the diagram, or analytically from its empirical time dependence at= f(t), finding for the permissible (specified) value at extra the corresponding value t add. Indicators of corrosion resistance when metal is exposed to mechanical factors, including residual stresses, marked in the table with **, are determined directly during corrosion tests.

Diagram of the dependence of the corrosion effect (integral indicator) at from time

1.6. It is allowed to use, along with the indicators given in the table, other quantitative indicators determined by operational requirements, the high sensitivity of experimental methods or the possibility of using them for remote monitoring of the corrosion process, with a preliminary establishment of the relationship between the main and applied indicators. As such indicators of corrosion, taking into account its type and mechanism, the following can be used: the amount of hydrogen released and (or) absorbed by the metal, the amount of reduced (absorbed) oxygen, an increase in the mass of the sample (while maintaining solid corrosion products on it), a change in the concentration of corrosion products in environment (with their complete or partial solubility), an increase in electrical resistance, a decrease in reflectivity, heat transfer coefficient, a change in acoustic emission, internal friction, etc. For electrochemical corrosion, the use of electrochemical indicators of corrosion and corrosion resistance is allowed. For crevice and contact corrosion, corrosion and corrosion resistance indicators are selected from the table in accordance with the type of corrosion (solid or pitting) in the crevice (gap) or contact area. 1.7. For one type of corrosion, it is possible to characterize the results of corrosion tests using several corrosion indicators. If there are two or more types of corrosion on one sample (product), each type of corrosion is characterized by its own indicators. Corrosion resistance in this case is assessed by an indicator that determines the performance of the system. 1.8. If it is impossible or impractical to determine quantitative indicators of corrosion resistance, it is allowed to use qualitative indicators, for example, changes in the appearance of the metal surface. In this case, the presence of tarnish is visually determined; corrosion damage, the presence and nature of the layer of corrosion products; the presence or absence of an undesirable change in the environment, etc. Based on the qualitative indicator of corrosion resistance, an assessment is made of the type: resistant - not resistant; pass - fail, etc. Changes in appearance can be assessed using conventional scales, for example, for electronic products according to GOST 27597. 1.9. Acceptable indicators of corrosion and corrosion resistance are established in the regulatory and technical documentation for the material, product, equipment.

2. DETERMINATION OF CORROSION INDICATORS

2.1. Complete corrosion 2.1.1. Mass loss per unit surface area D m, kg/m2, calculated by the formula

Where m 0 - mass of the sample before testing, kg; m 1 - mass of the sample after testing and removal of corrosion products, kg; S- surface area of ​​the sample, m2. 2.1.2. When hard-to-remove solid corrosion products are formed or their removal is impractical, a quantitative assessment of continuous corrosion is carried out by increasing mass. The increase in mass per unit surface area is calculated from the difference in mass of the sample before and after testing, per unit surface area of ​​the sample. To calculate the loss of metal mass from an increase in the mass of the sample, it is necessary to know the composition of the corrosion products. This indicator of metal corrosion in gases at high temperatures is determined according to GOST 6130. 2.1.3. Corrosion products are removed according to GOST 9.907. 2.1.4. The change in dimensions is determined by direct measurements of the difference between the dimensions of the sample before and after testing and removal of corrosion products. If necessary, change the dimensions according to mass loss taking into account the geometry of the sample, for example, change the thickness of a flat sample D L, m, is calculated using the formula

Where D m- mass loss per unit area, kg/m2; ρ - metal density, kg/m3. 2.2. Spot corrosion 2.2.1. The area of ​​each spot is determined with a planimeter. If such a measurement is not possible, the spot is outlined with a rectangle and its area is calculated. 2.2.2. The degree of damage to the metal surface by corrosion stains ( G) as a percentage is calculated using the formula

Where S i- square i-that spot, m 2; n - number of spots; S - surface area of ​​the sample, m2. In case of spot corrosion, it is allowed to determine the degree of surface damage by corrosion using a grid of squares. 2.3. Pitting corrosion 2.3.1. The maximum depth of penetration of pitting corrosion is determined by: measuring with a mechanical indicator with a movable needle probe the distance between the mouth plane and the bottom of the pit after removing corrosion products in cases where the dimensions of the pit allow free penetration of the needle probe to its bottom; microscopically, after removing corrosion products by measuring the distance between the mouth plane and the bottom of the pitting (double focusing method); microscopically on a transverse section with appropriate magnification; sequential mechanical removal of metal layers of a given thickness, for example, 0.01 mm at a time until the last pitting disappears. Pittings with an opening diameter of at least 10 µm are taken into account. The total working surface area must be at least 0.005 m2. 2.3.2. A thin section to measure the maximum depth of penetration of pitting corrosion is cut out from the area where the largest pittings are located on the working surface. The cutting line should pass through as many of these pittings as possible. 2.3.3. The maximum depth of penetration of pitting corrosion is found as the arithmetic mean of measurements of the deepest pittings depending on their number ( n) on the surface: at n < 10 измеряют 1-2 питтинга, при n < 20 - 3-4, при n> 20 - 5. 2.3.4. For penetrating pitting corrosion, the thickness of the sample is taken as the maximum penetration depth. 2.3.5. The maximum diameter of the pitting is determined using measuring instruments or optical means. 2.3.6. The degree of damage to a metal surface by pitting is expressed as the percentage of the surface area occupied by pitting. If there are a large number of pittings with a diameter of more than 1 mm, it is recommended to determine the degree of damage according to clause 2.2. 2.4. Intergranular corrosion 2.4.1. The depth of intergranular corrosion is determined by the metallographic method according to GOST 1778 on an etched section made in the transverse plane of the sample, at a distance from the edges of at least 5 mm with a magnification of 50 ´ or more. It is allowed to determine the penetration depth of corrosion of aluminum and aluminum alloys using unetched sections. The etching mode is in accordance with GOST 6032, GOST 9.021 and NTD. (Changed edition, Amendment No. 1). 2.4.2. Changes in mechanical properties during intergranular corrosion - tensile strength, relative elongation, impact strength - are determined by comparing the properties of metal samples that were and were not subject to corrosion. The mechanical properties of metal samples that have not been subjected to corrosion are taken as 100%. 2.4.3. Samples are prepared according to GOST 1497 and GOST 11701 when determining tensile strength and relative elongation, and according to GOST 9454 when determining impact strength. 2.4.4. It is allowed to use physical methods to control the depth of corrosion penetration in accordance with GOST 6032. 2.5. Stress-corrosion cracking and corrosion fatigue 2.5.1. In case of corrosion cracking and corrosion fatigue, cracks are detected visually or using optical or other flaw detection means. It is possible to use indirect measurement methods, for example, determining the increase in the electrical resistance of the sample. 2.5.2. The change in mechanical properties is determined according to clause 2.4.2. 2.6. Exfoliation corrosion 2.6.1. The degree of surface damage during exfoliating corrosion is expressed as a percentage of the area with peeling on each surface of the sample according to GOST 9.904. 2.6.2. The total length of the ends with cracks for each sample ( L) as a percentage is calculated using the formula

Where L i- length of the end section affected by cracks, m; P- sample perimeter, m. 2.6.3. It is allowed to use a conditional scale score according to GOST 9.904 as a generalized semi-quantitative (score) indicator of exfoliation corrosion.

3. DETERMINATION OF CORROSION RESISTANCE INDICATORS

3.1. Complete corrosion 3.1.1. The main quantitative indicators of corrosion resistance against continuous corrosion in the absence of special requirements, for example, regarding environmental pollution, are determined from the table. 3.1.2. When continuous corrosion occurs at a constant rate, corrosion resistance indicators are determined using the formulas:

Where tm- time until the mass per unit area decreases by the permissible value D m, year; v m- rate of mass loss, kg/m 2 ∙year; t 1 - time of penetration to the permissible (specified) depth ( l), year; v 1 - linear corrosion rate, m/year. 3.1.3. When continuous corrosion occurs at an unstable rate, corrosion resistance indicators are determined according to clause 1.5. 3.1.4. If there are special requirements for the optical, electrical and other properties of the metal, its corrosion resistance is assessed by the time it takes for these properties to change to an acceptable (specified) level. 3.2. Spot corrosion An indicator of corrosion resistance for spot corrosion is time (t n) achieving an acceptable degree of surface damage. t value n determined graphically according to clause 1.5. 3.3. Pitting corrosion 3.3.1. The main indicator of corrosion resistance against pitting corrosion is the absence of pitting or the minimum time (t pit) for pitting to penetrate to the permissible (specified) depth. t pit is determined graphically from the dependence of the maximum pitting depth l max from time. 3.3.2. An indicator of resistance to pitting corrosion can also be the time it takes to reach the permissible degree of damage to the surface by pitting. 3.4. Intergranular corrosion 3.4.1. Indicators of corrosion resistance against intergranular corrosion are generally determined graphically or analytically from the time dependence of the penetration depth or mechanical properties in accordance with clause 1.5. 3.4.2. A qualitative assessment of resistance to intergranular corrosion of the type of struts - not struts based on accelerated tests of corrosion-resistant alloys and steel is established according to GOST 6032, aluminum alloys - according to GOST 9.021. 3.5. Corrosion cracking 3.5.1. Quantitative indicators of resistance to corrosion cracking are determined for high-strength steels and alloys according to GOST 9.903, for aluminum and magnesium alloys - according to GOST 9.019, welded joints of steel, copper and titanium alloys - according to GOST 26294-84. 3.6. Exfoliation corrosion 3.6.1. Indicators of resistance to exfoliation corrosion for aluminum and its alloys are determined according to GOST 9.904, for other materials - according to NTD.

4. PROCESSING RESULTS

4.1. It is recommended to pre-process the results in order to identify abnormal (outlier) values. 4.2. The dependence of the corrosion effect (integral corrosion indicator) on time in the case of its monotonic change is recommended to be expressed graphically, using at least four indicator values ​​to construct. 4.3. It is recommended to express the results of calculation of corrosion and corrosion resistance indicators as a confidence interval of the numerical value of the indicator. 4.4. The regression equation, confidence intervals and analysis accuracy are determined according to GOST 20736, GOST 18321. 4.5. The metallographic method for assessing corrosion damage is given in Appendix 1. (Introduced additionally, Amendment No. 1).APPLICATION.(Deleted, Amendment No. 1).

ANNEX 1

Mandatory

METALLOGRAPHIC METHOD FOR ASSESSING CORROSION DAMAGES

1. Essence of the method

The method is based on determining the type of corrosion, the form of corrosion damage, the distribution of corrosion damage in metals, alloys and protective metal coatings (hereinafter referred to as materials) by comparison with the corresponding standard forms, as well as measuring the depth of corrosion damage on a metallographic section.

2. Samples

2.1. The location for taking samples from the test material is selected based on the results of a visual (with the naked eye or using a magnifying glass) inspection of the surface or non-destructive flaw detection. 2.2. Samples are cut from the following places of the material: 1) if only part of the surface of the material is affected by corrosion, samples are taken in three places: from the part affected by corrosion; from the part not affected by corrosion and in the area between them; 2) if there are areas of the surface of the material with different types of corrosion or with different depths of corrosion damage, samples are taken from all areas affected by corrosion; 3) if there is one type of corrosion damage on the surface of the material, samples are taken from at least three characteristic areas of the material under study. 2.3. If necessary, at least one sample is taken from at least five functionally necessary areas of the test material. The sample size is determined based on the size of the corrosion zone. 2.4. The samples are cut so that the plane of the section is perpendicular to the surface under study. The manufacturing method should not affect the structure of the material and destroy the surface layer and edges of the sample. For materials with protective coatings, damage to the coating and its separation from the base material is not allowed. 2.5. Sample marking - according to GOST 9.905. 2.6. When making a metallographic section, all traces of cutting, for example, burrs, are removed from the surface of the sample. 2.7. During grinding and polishing operations, it is necessary to ensure that the nature and size of the corrosion damage does not change. The edges of the polished section at the site of corrosion damage should not be rounded. Roundings are allowed that do not affect the accuracy of determining corrosion damage. To do this, it is recommended to pour the sample into the casting compound in such a way that the edge being examined is at a distance of at least 10 mm from the edge of the section. Polishing is carried out briefly using diamond pastes. 2.8. The section is assessed before and after etching. Etching makes it possible to distinguish between corrosion damage and the structure of the material. When etching, the nature and size of the corrosion lesion should not be changed.

3. Carrying out the test

3.1. Determination and assessment of the type of corrosion, the form of corrosion damage and its distribution in the material 3.1.1. When conducting the test, it is necessary to take into account the chemical composition of the material being tested, the method of its processing, as well as all corrosive factors. 3.1.2. The test is carried out on a metallographic section under a microscope at a magnification of 50, 100, 500 and 1000´. 3.1.3. When determining the type of corrosion, corrosion control is carried out along the entire length of the section. It is possible to determine several types of corrosion on one sample. 3.1.4. When testing protective coatings, the type of corrosion of the coating and the base material is determined separately. 3.1.5. If the material, in addition to the corrosive environment, is affected by other factors that influence the change in the structure of the material, for example, high temperature, mechanical stress, corrosion damage is determined by comparing the material with a specific sample exposed to similar factors, but protected from the effects of a corrosive environment. 3.1.6. Assessment of the form of corrosion damage and determination of the type of corrosion is carried out by comparison with typical schemes of corrosion damage according to Appendix 2, distribution of corrosion damage in the material - according to Appendix 3. 3.2. Measuring the depth of corrosion damage 3.2.1. The depth of corrosion damage is determined on a micrometallographic section using an ocular scale and a micrometer screw of a microscope. 3.2.2. The depth of corrosion damage is determined by the difference in the thickness of the metal of the corroded section of the surface of the polished section and the surface area without corrosion or by measuring the depth of damage from a surface that is not damaged or slightly damaged by corrosion. When testing a material with a protective coating, the results of measuring the depth of corrosion damage to the coating and the base metal are determined separately. 3.2.3. If the entire surface of the sample is affected by corrosion and the depth of corrosion damage in different areas of the surface does not differ noticeably, for example in the case of intergranular or transgranular corrosion, the depth of corrosion damage is measured in at least 10 areas of the surface. For large samples, measurements are taken in at least 10 areas for every 20 mm of the length of the controlled surface, taking into account the deepest lesions. 3.2.4. In case of local corrosion damage (for example, pitting corrosion or stain corrosion), measurements are carried out in the places of this corrosion damage, and the number of areas for measurements may differ from the requirements given in paragraph. 3.2.3. 3.2.5. To clarify the determination of the maximum depth of corrosion damage, after a metallographic assessment of the sections, they are re-polished: 1) for samples with local corrosion damage, for example, stain corrosion or pitting corrosion - to the maximum depth of corrosion damage, i.e. until the moment when the measured depth is less than the previous measurement result; 2) for samples with almost the same depth of corrosion damage in different areas of the surface, after evaluation, they are re-polished and a new metallographic section is made, on which the corrosion damage is again assessed. 3.2.6. The error in measuring the depth of corrosion damage is no more than ±10%.

4. Test report - according to GOST 9.905

ANNEX 1.(Introduced additionally, Amendment No. 1).

APPENDIX 2

Mandatory

TYPES OF CORROSION

Type of corrosion

Characteristics of the form of corrosion damage

Diagram of a typical type of corrosion damage

1. Continuous (uniform) corrosion Forms of corrosion damage 1a and 1b differ only in the roughness of the surface. By changing the shape of the surface before and after the corrosion test, the presence of corrosion is detected: it is determined by the change in the mass and size of the samples before and after the corrosion test

Form 1c can be transitional between continuous and selective corrosion, for example, 10c, 10g and 10e. The type of corrosion can be specified by changes in its shape depending on the time of exposure to the corrosive environment, as well as by the structure of the metal

2. Local (uneven) corrosion The form corresponds to continuous corrosion, but differs in that part of the surface is subject to corrosion or corrosion occurs at different rates in its individual areas
3. Corrosion spots Minor corrosion damage of irregular shape; the size of its area in case of slight magnification may exceed the size of the field of view

4. Corrosion ulcer Corrosion lesion with depth approximately equal to width

5. Pitting corrosion Corrosion damage is much deeper than it is wide

6. Subsurface corrosion Corrosion damage, characterized by the fact that it occupies a small area on the surface and is mainly concentrated under the surface of the metal

A form of corrosion damage in which individual zones are located below the surface and usually do not have a noticeable direct exit to the surface

7. Layer corrosion Corrosion damage, the internal layers of which include grains of various sizes, various phases, inclusions, secretions, etc.
8. Intergranular corrosion Corrosion damage is characterized by the presence of a corroded zone along the grain boundaries of the metal, and it can affect the boundaries of all grains or only individual grains

9. Transgranular corrosion Corrosion damage is characterized by the presence of a large number of transgranular cracks

10. Selective corrosion Corrosion damage to which a specific structural phase or component is subjected; if the phase is formed by eutectic, determine whether the entire eutectic or some of its components, for example, cementite, is corroded

Corrosion damage to which a certain phase of metal is subjected without direct contact with the corroded surface. In this case, it is determined whether the phases corrode along the grain boundaries or within the grains of the main structure. Next, it is determined whether the boundaries between the corroding phases differ from the other boundaries (presence of phases, cracks). From this it is concluded whether the corrosive medium penetrates along the grain boundaries or by diffusion throughout the entire grain volume
Corrosion damage to which only individual grains are subjected, the physical state of which has changed, for example due to deformation

Corrosion damage to which only the deformable parts of the grains are subjected, while the resulting zone of corrosion damage is narrower than one grain and passes through several grains. At the same time, it is determined whether the deformation has affected the change in the structure of the metal, for example, the transition of austenite to martensite

Corrosion damage in the form of a zone with rows of isolated inclusions; at the same time, possible changes in the structure in this zone are determined

Corrosion damage in the form of a wide zone along the grain boundary. This form may be temporary and cannot be classified as intergranular corrosion; It is characterized by the fact that it does not penetrate deep into the metal. It can be more accurately determined by changes in the form of corrosion damage depending on the time of corrosion exposure and by the release of structural particles in the corroding alloy
Corrosion damage, as a result of which a new phase of a metallic appearance is formed, which has the ability to reduce the resistance of the metal
Corrosion damage, as a result of which the chemical composition of the phase changes while maintaining its shape and location, for example, graphitization of cementite plates in cast iron, dezincification of brass, etc. In the zone of this change, other corrosion products, for example, oxides, can form

11. Corrosion in the form of rare cracks Corrosion damage, as a result of which a deep, slightly branched crack is formed, wide near the surface with a gradual transition to a slight width; the crack is filled with corrosion products

Corrosion damage in the form of a deep crack of insignificant width emanating from a corrosion ulcer on the surface; the crack may have a branched shape

Corrosion damage, as a result of which an intercrystalline crack of insignificant width is formed in the absence of corrosion products. Compared to intergranular corrosion, it looks like single (rare) cracks

Corrosion damage, as a result of which a transcrystalline crack of insignificant width with significant branching is formed. Compared to transgranular corrosion, it has the appearance of single (rare) cracks. Some cracks may have the type of partially transgranular and partially intergranular corrosion damage
Corrosion damage, as a result of which cracks of insignificant width are formed, having the appearance of threads, mainly parallel to the surface and creating a zone of a certain depth. They cannot be classified as similar cracks formed due to deformation or poor processing of the sample.

Corrosion damage in the form of small, predominantly short cracks inside individual grains. Cracks can form, for example, due to the action of molecular hydrogen, high stress, corrosion of a certain phase
APPENDIX E 2.(Introduced additionally, Amendment No. 1).

APPENDIX 3

Mandatory

DISTRIBUTION OF CORROSION

APPENDIX 3.(Introduced additionally, Amendment No. 1).

INFORMATION DATA

1. DEVELOPED AND INTRODUCED by the USSR State Committee for Product Quality Management and StandardsDEVELOPERSL.I. Topchiashvili, G.V. Kozlova, Ph.D. tech. sciences (topic leaders); V.A. Atanova, G.S. Fomin, Ph.D. chem. sciences, L.M. Samoilova, I.E. Trofimova 2. APPROVED AND ENTERED INTO EFFECT by Resolution of the USSR State Committee on Standards dated October 31, 1985 No. 3526 3. The standard fully complies with ST SEV 4815-84, ST SEV 6445-88 4. INTRODUCED FOR THE FIRST TIME 5. REFERENCE REGULATIVE AND TECHNICAL DOCUMENTS

Item number, application

Item number, application

GOST 9.019-74 3.5.1 GOST 6032-89 2.4.1; 2.4.4; 3.4.2
GOST 9.021-74 2.4.1; 3.4.2 GOST 6130-71 2.1.2
GOST 9.903-81 3.5.1 GOST 9454-78 2.4.3
GOST 9.904-82 2.6.1; 2.6.3; 3.6.1 GOST 11701-84 2.4.3
GOST 9.905-82 Annex 1 GOST 18321-73 4.4
GOST 9.907-83 2.1.3 GOST 20736-75 4.4
GOST 1497-84 2.4.3 GOST 26294-84 3.5.1
GOST 1778-70 2.4.1 GOST 27597-88 1.8
6. REISSUE with Change No. 1, approved in October 1989 (IUS 2-90)

    These methods can be divided into 2 groups. The first 2 methods are usually implemented before the start of production operation of the metal product (selection of structural materials and their combinations at the stage of design and manufacture of the product, application of protective coatings to it). The last 2 methods, on the contrary, can only be carried out during the operation of the metal product (passing current to achieve a protective potential, introducing special inhibitor additives into the process environment) and are not associated with any pre-treatment before use.

    The second group of methods allows, if necessary, to create new protection modes that ensure the least corrosion of the product. For example, in certain sections of the pipeline, depending on the aggressiveness of the soil, the cathode current density can be changed. Or use different inhibitors for different types of oil pumped through pipes.

    Question: How are corrosion inhibitors used?

    Answer: To combat metal corrosion, corrosion inhibitors are widely used, which are introduced in small quantities into an aggressive environment and create an adsorption film on the metal surface, inhibiting electrode processes and changing the electrochemical parameters of metals.

    Question: What are the ways to protect metals from corrosion using paints and varnishes?

    Answer: Depending on the composition of pigments and the film-forming base, paint and varnish coatings can serve as a barrier, passivator or protector.

    Barrier protection is the mechanical insulation of a surface. Violation of the integrity of the coating, even at the level of the appearance of microcracks, predetermines the penetration of an aggressive environment to the base and the occurrence of under-film corrosion.

    Passivation of a metal surface using paintwork is achieved through chemical interaction between the metal and the coating components. This group includes primers and enamels containing phosphoric acid (phosphating), as well as compositions with inhibitory pigments that slow down or prevent the corrosion process.

    Protective protection of metal is achieved by adding powdered metals to the coating material, creating donor electron pairs with the protected metal. For steel these are zinc, magnesium, aluminum. Under the influence of an aggressive environment, the additive powder gradually dissolves, and the base material is not subject to corrosion.

    Question: What determines the durability of metal protection against corrosion using paints and varnishes?

    Answer: Firstly, the durability of metal protection from corrosion depends on the type (and type) of paint and varnish coating used. Secondly, the thoroughness of preparing the metal surface for painting plays a decisive role. The most labor-intensive process in this case is the removal of previously formed corrosion products. Special compounds are applied that destroy rust, followed by mechanical removal with metal brushes.

    In some cases, rust removal is practically impossible, which requires the widespread use of materials that can be applied directly to surfaces damaged by corrosion - rust coating materials. This group includes some special primers and enamels used in multi-layer or independent coatings.

    Question: What are high-fill two-component systems?

    Answer: These are anti-corrosion paints and varnishes with a reduced solvent content (the percentage of volatile organic substances in them does not exceed 35%). The market for materials for home use mainly offers single-component materials. The main advantage of highly filled systems compared to conventional ones is significantly better corrosion resistance at a comparable layer thickness, lower material consumption and the possibility of applying a thicker layer, which ensures the required anti-corrosion protection in just 1-2 times.

    Question: How to protect the surface of galvanized steel from destruction?

    Answer: Anti-corrosion primer based on modified vinyl acrylic resins in the Galvaplast solvent is used for interior and exterior work on descaled ferrous metal substrates, galvanized steel, and galvanized iron. Solvent – ​​white spirit. Application – brush, roller, spray. Consumption 0.10-0.12 kg/sq.m; drying 24 hours.

    Question: What is patina?

    Answer: The word “patina” refers to a film of various shades that forms on the surface of copper and copper-containing alloys under the influence of atmospheric factors during natural or artificial aging. Sometimes patina refers to oxides on the surface of metals, as well as films that cause tarnish on the surface of stones, marble or wooden objects over time.

    The appearance of patina is not a sign of corrosion, but rather a natural protective layer on the copper surface.

    Question: Is it possible to artificially create a patina on the surface of copper products?

    Answer: Under natural conditions, a green patina forms on the surface of copper within 5-25 years, depending on climate and the chemical composition of the atmosphere and precipitation. At the same time, copper carbonates are formed from copper and its two main alloys - bronze and brass: bright green malachite Cu 2 (CO 3) (OH) 2 and azure blue azurite Cu 2 (CO 3) 2 (OH) 2. For zinc-containing brass, the formation of green-blue rosasite with the composition (Cu,Zn) 2 (CO 3)(OH) 2 is possible. Basic copper carbonates can be easily synthesized at home by adding an aqueous solution of soda ash to an aqueous solution of a copper salt, such as copper sulfate. At the same time, at the beginning of the process, when there is an excess of copper salt, a product is formed that is closer in composition to azurite, and at the end of the process (with an excess of soda) - to malachite.

    Saving coloring

    Question: How to protect metal or reinforced concrete structures from the influence of aggressive environments - salts, acids, alkalis, solvents?

    Answer: To create chemical-resistant coatings, there are several protective materials, each of which has its own area of ​​protection. The widest range of protection is provided by: enamels XC-759, “ELOCOR SB-022” varnish, FLC-2, primers, XC-010, etc. In each individual case, a specific painting scheme is selected, according to operating conditions. Tikkurilla Coatings Temabond, Temacoat and Temachlor paints.

    Question: What compositions can be used when painting the internal surfaces of tanks for kerosene and other petroleum products?

    Answer: Temaline LP is a two-component epoxy gloss paint with an amino adduct-based hardener. Application - brush, spray. Drying 7 hours.

    EP-0215 ​​– primer for corrosion protection of the internal surface of caisson tanks operating in a fuel environment with an admixture of water. It is applied to surfaces made of steel, magnesium, aluminum and titanium alloys operated in different climatic zones, at elevated temperatures and exposure to polluted environments.

    Suitable for use with BEP-0261 primer and BEP-610 enamel.

    Question: What compounds can be used for protective coating of metal surfaces in marine and industrial environments?

    Answer: Thick film paint based on chlorinated rubber is used for painting metal surfaces in marine and industrial environments exposed to moderate chemical exposure: bridges, cranes, conveyors, port equipment, tank exteriors.

    Temacoat CB is a two-component modified epoxy paint used for priming and painting metal surfaces exposed to atmospheric, mechanical and chemical influences. Application - brush, spray. Drying time: 4 hours.

    Question: What compositions should be used to coat difficult-to-clean metal surfaces, including those immersed in water?

    Answer: Temabond ST-200 is a two-component modified epoxy paint with aluminum pigmentation and low solvent content. Used for painting bridges, tanks, steel structures and equipment. Application - brush, spray. Drying – 6 hours.

    Temaline BL is a two-component epoxy coating that does not contain solvents. Used for painting steel surfaces exposed to wear, chemical and mechanical stress when immersed in water, containers for oil or gasoline, tanks and reservoirs, wastewater treatment plants. Application by airless spray.

    Temazinc is a one-component zinc-rich epoxy paint with a polyamide-based hardener. Used as a primer in epoxy, polyurethane, acrylic, chlorinated rubber paint systems for steel and cast iron surfaces exposed to strong atmospheric and chemical influences. Suitable for painting bridges, cranes, steel frames, steel structures and equipment. Drying 1 hour.

    Question: How to protect underground pipes from the formation of fistulas?

    Answer: There can be two reasons for any pipe burst: mechanical damage or corrosion. If the first reason is the result of accident and carelessness - the pipe is caught in something or the weld has come apart, then corrosion cannot be avoided; this is a natural phenomenon caused by soil moisture.

    In addition to the use of special coatings, there is protection that is widely used throughout the world - cathodic polarization. It is a direct current source providing a polar potential of min 0.85 V, max – 1.1 V. It consists only of a conventional transformer AC voltage and a diode rectifier.

    Question: How much does cathodic polarization cost?

    Answer: The cost of cathodic protection devices, depending on their design, ranges from 1000 to 14 thousand rubles. The repair team can easily check the polarization potential. Installing protection is also not expensive and does not involve labor-intensive excavation work.

    Protection of galvanized surfaces

    Question: Why can't galvanized metals be shot blasted?

    Answer: Such preparation disrupts the natural corrosion resistance metal Surfaces of this kind are treated with a special abrasive agent - round glass particles that do not destroy the protective layer of zinc on the surface. In most cases, it is enough to simply treat with an ammonia solution to remove grease stains and zinc corrosion products from the surface.

    Question: How to restore damaged zinc coating?

    Answer: Zinc-filled compositions ZincKOS, TsNK, “Vinikor-zinc”, etc., which are applied by cold galvanizing and provide anodic protection of the metal.

    Question: How is metal protected using ZNC (zinc-filled compositions)?

    Answer: Cold galvanizing technology using CNC guarantees absolute non-toxicity, fire safety, and heat resistance up to +800°C. Coating of metal with this composition is carried out by spraying, with a roller or even just with a brush and provides the product with, in fact, double protection: both cathodic and film. The validity period of such protection is 25-50 years.

    Question: What are the main advantages of the cold galvanizing method over hot galvanizing?

    Answer: This method has the following advantages:

    1. Maintainability.
    2. Possibility of application on a construction site.
    3. No restrictions on overall dimensions protected structures.

    Question: At what temperature is thermal diffusion coating applied?

    Answer: Thermal diffusion zinc coating is applied at temperatures from 400 to 500°C.

    Question: Are there any differences in the corrosion resistance of coatings obtained by thermal diffusion galvanizing compared to other types of zinc coatings?

    Answer: The corrosion resistance of thermal diffusion zinc coating is 3-5 times higher than galvanic coating and 1.5-2 times higher than the corrosion resistance of hot zinc coating.

    Question: What paint and varnish materials can be used for protective and decorative painting of galvanized iron?

    Answer: For this, you can use both water-based ones - G-3 primer, G-4 paint, and organo-thinned ones - EP-140, "ELOCOR SB-022", etc. Tikkurila Coatings protective systems can be used: 1 Temakout GPLS-Primer + Temadur, 2 Temaprime EE+Temalak, Temalak and Temadur are tinted according to RAL and TVT.

    Question: What paint can be used to paint galvanized drainage pipes?

    Answer: Sockelfarg is a water-based latex paint in black and white. Designed for application to both new and previously painted outdoor surfaces. Resistant to weather conditions. Solvent – ​​water. Drying 3 hours.

    Question: Why are water-based anti-corrosion agents rarely used?

    Answer: There are 2 main reasons: the increased price compared to conventional materials and the prevailing opinion in certain circles that water systems have worse protective properties. However, as environmental legislation becomes stricter, both in Europe and throughout the world, the popularity of water systems is growing. Experts who tested high-quality water-based materials were able to verify that their protective properties are no worse than those of traditional materials containing solvents.

    Question: What device is used to determine the thickness of the paint film on metal surfaces?

    Answer: The “Constant MK” device is the easiest to use - it measures the thickness of paintwork on ferromagnetic metals. Much more features performs the multifunctional thickness gauge "Constant K-5", which measures the thickness of conventional paintwork, galvanic and hot-dip galvanized coatings on both ferromagnetic and non-ferromagnetic metals (aluminum, its alloys, etc.), and also measures surface roughness, temperature and humidity, and etc.

    The rust is receding

    Question: How can I treat items that are heavily corroded by rust?

    Answer: First recipe: a mixture of 50 g of lactic acid and 100 ml of vaseline oil. The acid converts iron metahydroxide from rust into a salt soluble in petroleum jelly - iron lactate. Wipe the cleaned surface with a cloth moistened with petroleum jelly.

    Second recipe: a solution of 5 g of zinc chloride and 0.5 g of potassium hydrogen tartrate, dissolved in 100 ml of water. Zinc chloride in aqueous solution undergoes hydrolysis and creates an acidic environment. Iron metahydroxide dissolves due to the formation of soluble iron complexes with tartrate ions in an acidic environment.

    Question: How to unscrew a rusty nut using improvised means?

    Answer: A rusted nut can be moistened with kerosene, turpentine or oleic acid. After some time it is possible to unscrew it. If the nut “persists,” you can set fire to the kerosene or turpentine with which it was moistened. This is usually enough to separate the nut and bolt. The most radical method: apply a very heated soldering iron to the nut. The metal of the nut expands and the rust moves away from the thread; Now you can pour a few drops of kerosene, turpentine or oleic acid into the gap between the bolt and the nut. This time the nut will definitely come loose!

    There is another way to remove rusty nuts and bolts. A “cup” of wax or plasticine is made around the rusted nut, the edge of which is 3-4 mm higher than the level of the nut. Dilute sulfuric acid is poured into it and a piece of zinc is placed. After a day, the nut can be easily unscrewed with a wrench. The fact is that a cup with acid and zinc metal on an iron base is a miniature galvanic cell. The acid dissolves the rust, and the resulting iron cations are reduced to the surface of the zinc. And the metal of the nut and bolt will not dissolve in the acid as long as it is in contact with zinc, since zinc is a more reactive metal than iron.

    Question: What anti-rust compounds does our industry produce?

    Answer: Domestic solvent-borne compounds applied “on rust” include well-known materials: primer (some manufacturers produce it under the name “Inkor”) and primer-enamel “Gramirust”. These two-part epoxy paints (base + hardener) contain corrosion inhibitors and targeted additives to cover tough rust up to 100 microns thick. The advantages of these primers: curing at room temperature, the possibility of application to a partially corroded surface, high adhesion, good physical and mechanical properties and chemical resistance, providing long-term operation coverings.

    Question: How can you paint old rusty metal?

    Answer: For stubborn rust, it is possible to use several paints and varnishes containing rust converters:

  • primer G-1, primer-paint G-2 (water-borne materials) – at temperatures up to +5°;
  • primer-enamel XB-0278, primer-enamel AS-0332 – up to minus 5°;
  • primer-enamel “ELOCOR SB-022” (materials based on organic solvents) – up to minus 15°C.
  • Primer enamel Tikkurila Coatings, Temabond (tinted according to RAL and TVT)

Question: How to stop the rusting process of metal?

Answer: This can be done using stainless steel primer. The primer can be used both as an independent coating on steel, cast iron, aluminum, and in a coating system that includes 1 layer of primer and 2 layers of enamel. The product is also used for priming corroded surfaces.

“Nerzhamet-soil” works on the metal surface as a rust converter, binding it chemically, and the resulting polymer film reliably isolates the metal surface from atmospheric moisture. When using the composition, the total costs of repair and restoration work on repainting metal structures are reduced by 3-5 times. The primer is supplied ready for use. If necessary, it must be diluted to working viscosity with white spirit. The drug is applied to metal surfaces with remnants of tightly adhered rust and scale with a brush, roller, or spray gun. Drying time at a temperature of +20° is 24 hours.

Question: Roofing often fades. What paint can be used on galvanized roofs and gutters?

Answer: Stainless steel-cycron. The coating provides long-term protection from weather conditions, humidity, ultraviolet radiation, rain, snow, etc.

It has high hiding power and light fastness, does not fade. Significantly extends the service life of galvanized roofs. Also Tikkurila Coatings, Temadur and Temalak coatings.

Question: Can chlorinated rubber paints protect metal from rust?

Answer: These paints are made from chlorinated rubber dispersed in organic solvents. In terms of their composition, they are classified as volatile resin and have high water and chemical resistance. Therefore, it is possible to use them to protect metal and concrete surfaces, water pipes and tanks from corrosion. From Tikkuril Coatings materials, you can use the Temanil MS-Primer + Temachlor system.

Anticorrosive in the bathhouse, bathtub, pool

Question: What kind of coating can protect bath containers for cold drinking and hot wash water from corrosion?

Answer: For containers for cold drinking and washing water, we recommend paint KO-42; Epovin for hot water - compositions ZinkKOS and Teplokor PIGMA.

Question: What are enamel pipes?

Answer: In terms of chemical resistance, they are not inferior to copper, titanium and lead, and their cost is several times cheaper. The use of enameled carbon steel pipes instead of stainless steel pipes results in tenfold cost savings. The advantages of such products include greater mechanical strength, including in comparison with other types of coatings - epoxy, polyethylene, plastic, as well as higher abrasion resistance, which makes it possible to reduce the diameter of pipes without reducing their throughput.

Question: What are the features of re-enamelling bathtubs?

Answer: Enameling can be done by brush or spray with the participation of professionals, or by brushing yourself. Preliminary preparation of the bathtub surface involves removing old enamel and cleaning off rust. The whole process takes no more than 4-7 hours, another 48 hours for the bath to dry, and you can use it after 5-7 days.

Re-enamel bathtubs require special care. Such baths cannot be washed with powders such as Comet and Pemolux, or using products containing acid, such as Silit. It is unacceptable to get varnishes on the surface of the bathtub, including hair varnishes, or to use bleach when washing. Such bathtubs are usually cleaned with soap products: washing powders or dishwashing detergents applied to a sponge or soft rag.

Question: What paint materials can be used to re-enamel bathtubs?

Answer: The “Svetlana” composition includes enamel, oxalic acid, hardener, and tinting pastes. The bath is washed with water, etched with oxalic acid (stains, stones, dirt, rust are removed and a rough surface is created). Wash with washing powder. Chips are repaired in advance. Then the enamel should be applied within 25-30 minutes. When working with enamel and hardener, contact with water is not allowed. Solvent – ​​acetone. Bath consumption – 0.6 kg; drying – 24 hours. Fully gains properties after 7 days.

You can also use two-component epoxy-based paint Tikkurila “Reaflex-50”. When using glossy bathtub enamel (white, tinted), either washing powders or laundry soap are used for cleaning. Fully gains properties after 5 days. Bath consumption – 0.6 kg. Solvent – ​​industrial alcohol.

B-EP-5297V is used to restore the enamel coating of bathtubs. This paint is glossy, white, tinting is possible. The coating is smooth, even, durable. Do not use “Sanitary” type abrasive powders for cleaning. Fully gains properties after 7 days. Solvents – a mixture of alcohol and acetone; R-4, No. 646.

Question: How to ensure protection against breakage of steel reinforcement in the bowl of a swimming pool?

Answer: If the condition of the pool's ring drainage is unsatisfactory, softening and suffusion of the soil is possible. Penetration of water under the bottom of the tank can cause subsidence of the soil and the formation of cracks in concrete structures. In these cases, the reinforcement in the cracks can corrode to the point of breaking.

In such difficult cases, the reconstruction of damaged reinforced concrete tank structures should include the implementation of a protective sacrificial layer of shotcrete on the surfaces of reinforced concrete structures exposed to the leaching action of water.

Obstacles to biodegradation

Question: What external conditions determine the development of wood-decaying fungi?

Answer: The most favorable conditions for the development of wood-decaying fungi are considered to be: the presence of air nutrients, sufficient wood moisture and favorable temperature. The absence of any of these conditions will retard the development of the fungus, even if it is firmly established in the wood. Most mushrooms develop well only at high relative humidity (80-95%). When wood moisture content is below 18%, the development of fungi practically does not occur.

Question: What are the main sources of moisture in wood and what is their danger?

Answer: The main sources of wood moisture in the structures of various buildings and structures include ground (underground) and surface (storm and seasonal) water. They are especially dangerous for wooden elements of open structures located in the ground (poles, piles, power line and communication supports, sleepers, etc.). Atmospheric moisture in the form of rain and snow threatens the ground part of open structures, as well as the external wooden elements of buildings. Operating moisture in liquid or vapor form in residential premises is present in the form of household moisture released during cooking, washing, drying clothes, washing floors, etc.

A large amount of moisture is introduced into a building when laying raw wood, using masonry mortars, concreting, etc. For example, 1 sq.m of laid wood with a moisture content of up to 23% releases up to 10 liters of water when it dries to 10-12%.

The wood of buildings, which dries naturally, is at risk of rotting for a long time. If chemical protection measures have not been provided, it is usually affected by house fungus to such an extent that the structures become completely unusable.

Condensation moisture that occurs on the surface or in the thickness of structures is dangerous because it is detected, as a rule, already when irreversible changes have occurred in the enclosing wooden structure or its element, for example, internal rotting.

Question: Who are the “biological” enemies of the tree?

Answer: These are mold, algae, bacteria, fungi and antimycetes (this is a cross between fungi and algae). Almost all of them can be combated with antiseptics. The exception is fungi (saprophytes), since antiseptics only affect some of their species. But it is fungi that are the cause of such widespread rot, which is the most difficult to deal with. Professionals classify rot by color (red, white, gray, yellow, green and brown). Red rot affects coniferous wood, white and yellow rot affects oak and birch, green rot affects oak barrels, as well as wooden beams and cellar floors.

Question: Are there ways to neutralize porcini mushroom?

Answer: The white house mushroom is the most dangerous enemy of wooden structures. The speed at which wood is destroyed by porcini mushroom is such that in 1 month it completely “eats” a four-centimeter oak floor. Previously, in villages, if a hut was infected by this fungus, it was immediately burned to save all other buildings from infection. After that, the whole world built a new hut for the affected family in another place. Currently, in order to get rid of white house fungus, the affected area is dismantled and burned, and the rest is impregnated with 5% chromium (5% solution of potassium dichromate in 5% sulfuric acid), while it is recommended to treat the ground with 0.5 m depth.

Question: What are ways to protect wood from rotting in the early stages of this process?

Answer: If the rotting process has already begun, it can only be stopped by thoroughly drying and ventilating wooden structures. In the early stages, disinfectant solutions, for example, such as the “Wood Healer” antiseptic compositions, can help. They are available in three different versions.

Mark 1 is intended for the prevention of wooden materials immediately after their purchase or immediately after building a house. The composition protects against fungus and wood-boring beetles.

Brand 2 is used if fungus, mold or “blue stain” has already appeared on the walls of the house. This composition destroys existing diseases and protects against their future manifestations.

Mark 3 is the most powerful antiseptic; it completely stops the rotting process. More recently, a special composition (grade 4) was developed to combat insects - “anti-bug”.

SADOLIN Bio Clean is a disinfectant for surfaces contaminated with mold, moss, and algae, based on sodium hypochlorite.

DULUX WEATHERSHIELD FUNGICIDAL WASH is a highly effective neutralizer of mold, lichen and rot. These compositions are used both indoors and outdoors, but they are effective only in the early stages of combating rot. In case of serious damage to wooden structures, it is possible to stop rotting using special methods, but this is quite complex work, usually performed by professionals using restoration chemical compounds.

Question: What protective impregnations and preservative compounds available on the domestic market prevent biocorrosion?

Answer: Of the Russian antiseptic drugs, it is necessary to mention metacid (100% dry antiseptic) or polysept (25% solution of the same substance). Such preservative compositions as “BIOSEPT”, “KSD” and “KSDA” have proven themselves well. They protect the wood from damage by mold, fungi, bacteria, and the last two, in addition, make the wood difficult to ignite. Textured coatings “AQUATEX”, “SOTEX” and “BIOX” eliminate the occurrence of fungus, mold and wood blue stains. They are breathable and have a durability of over 5 years.

A good domestic material for protecting wood is the glazing impregnation GLIMS-LecSil. This is a ready-to-use aqueous dispersion based on styrene-acrylate latex and reactive silane with modifying additives. Moreover, the composition does not contain organic solvents or plasticizers. Glazing sharply reduces the water absorption of wood, as a result of which it can even be washed, including with soap and water, protects against washing out of fireproofing impregnation, and thanks to its antiseptic properties destroys fungi and mold and prevents their further formation.

Of the imported antiseptic compositions for protecting wood, antiseptics from TIKKURILA have proven themselves well. Pinjasol Color is an antiseptic that forms a continuous water-repellent and weather-resistant coating.

Question: What are insecticides and how are they used?

Answer: To combat beetles and their larvae, poisonous chemical substances– contact and intestinal insecticides. Sodium fluoride and sodium fluoride are approved by the Ministry of Health and have been used since the beginning of the last century; When using them, safety precautions must be observed. To prevent damage to wood by the beetle, preventive treatment with silicofluoride compounds or a 7-10% solution of table salt is used. During historical periods of widespread wood construction, all wood was processed at the harvesting stage. Aniline dyes were added to the protective solution, which changed the color of the wood. In old houses you can still find red beams.

The material was prepared by L. RUDNITSKY, A. ZHUKOV, E. ABISHEV

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