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LOSS OF CORROSION AND PREVENTION OF CORROSION GROUP 4 MD. AL FAHAD ID: 2161381002 MD. MASUM RANA ID: 2161381006 BATCH : 11 TH (REGULAR)

Loss of corrosion and prevention of corrosion

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Page 1: Loss of corrosion and prevention of corrosion

LOSS OF CORROSION AND PREVENTION OF CORROSION

GROUP 4MD. AL FAHAD

ID: 2161381002MD. MASUM RANA ID: 2161381006BATCH : 11TH (REGULAR)

Page 2: Loss of corrosion and prevention of corrosion

CORROSION CYCLE

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FACTS ABOUT CORROSION

Corrosion is a natural process. Corrosion is an electrochemical process. Corrosion leads to tremendous loss. It can’t be eliminated

completely. However, its extent can be minimized. Corrosion is exactly the reverse of extraction of metals and also

known as weeping of metals.

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LOSS OF CORROSION

Every year almost all country of the world face a large amount of economic loss due to corrosion .

The overall economic loss due to corrosion may be divided into two classes, Direct loss Indirect loss

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DIRECT LOSS

Cost of replacing corroded parts of the articles and machinery including labour cost.

Cost of repairing the structure, where prevention of rusting is prime object.

The capital cost involved in modifying the metal by alloy Cost of galvanizing or nicel plating of steel Cost of addition of corrosion inhibitors to water or any other

environment Use of dehumidifying storage room for metal, metallic apparatus,

equipment's etc.

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INDIRECT LOS DUE TO CORROSION Its can not be measured in term of cost of metal and materials Losses con not be replace by money A few example of indirect loss are,

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SHUTDOWN OF THE INDUSTRY

The replacement of corroded part in many industry may cost an appreciable amount of money or per year which considered as direct loss

During repairing , the industries are to be shutdown which may cost huge amount of money in production loss.

Replacement of corroded boiler or condenser tube of a power plant may require a lot of money per year for power purchased from interconnected electric system to supply customers while the boiler is down.

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LOSS OF PRODUCT

Oil gas water etc. may be leak out through corroded pipe system. Through a corroded radiator antifreeze liquid may also leak out

which may cause a serious accident. In addition to these the total production of an industry is reduce

due to corrosion of its machinery.

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LOSS OF EFFICIENCY

Boiler may occur by decreasing heat transfer capacity through the accumulation of corroder products.

The pipeline for water supply may also be clogged by the deposition of rust which required increase pumping capacity.

Internal combustion of automobile engine Loss of critical dimension of piston ring and cylinders

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CONTAMINATION OF THE PRODUCT

Corroded product do not have mechanical strength. The possibility of adulteration of the product with the substance

is very high. Example soap industry, copper salt mixed with raw materials

accelerates the rapidity of soap and shortens the time for which the soap is to be stored before sale. A small amount of copper picked up by corrosion of copper piping.

Load equipment is no recommended to use in pharmaceutical, food, beverage industry because of toxic property of lead and its corroded product

For the same reason lead pipe are not safe for transporting soft water for drinking purpose.

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OVER DESIGN

Over design is a common phenomenon that incurs huge amount of loss.

In the designing of unde ground pipeline, water tanks, reaction vessel, boiler, condenser tube, marine structure, etc.

the young engineers designer usually do many times heavier than that is required for normal operation pressure applied stress in order to ensure safety of life.

This is due to lack of information about the corrosion rate, name of environment quality of materials method of corrosion control etc.

Example :over design is always common in the under ground oil pipes.

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PREVENTION OF CORROSION THE HUGE ANNUAL LOSS DUE TO CORROSION IS A NATIONAL WASTE

AND SHOULD BE MINIMIZED

MATERIALS ALREADY EXIST WHICH, IF PROPERLY USED, CAN

ELIMINATE 80 % OF CORROSION LOSS

PROPER UNDERSTANDING OF THE BASICS OF CORROSION AND

INCORPORATION IN THE INITIAL DESIGN OF METALLIC STRUCTURES

IS ESSENTIAL

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Factors that affect the rate of corrosionTemperature Oxygen

Humidity Chemical Salts

Chemicals and airborne gases

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How to avoid (or control) Corrosion? Material Selection! Remember – environment key. Look at

potential pH diagrams!!! Eliminate any one of the 4 requirements for corrosion! Galvanic - Avoid using dissimilar metals.

Or close together as possible Or electrically isolate one from the other Or MAKE ANODE BIG!!!

Pitting/Crevice: Watch for stagnate water/ electrolyte. Use gaskets Use good welding practices

Intergranular – watch grain size, environment, temperature, etc.. Careful with Stainless Steels and AL.

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Methods To Control Corrosion

Design of structures

Material selection

Cathodic Protection

Reduce the activity of the cathode and or electrolyte. (Polarization)

Protection of the Anode. (Passivation)

Alteration of environment

Inhibitors

Protective Coatings

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DESIGN OF STRUCTURE Avoid sharp corners

Complete draining of vessels

Avoid sudden changes in section

Avoid contact between dissimilar metals

Weld rather than rivet

Easy replacement of vulnerable parts

Avoid excessive mechanical stress

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MATERIAL SELECTION

Metallic : [metal and alloy] Nonmetallic : [rubbers (natural and synthetic), plastics, ceramics, carbon

and graphite, and wood]

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IMPROVEMENTS OF MATERIALS

Purification of metals: Al , Zr Making more noble, e.g. Pt in Ti Passivating, e.g. Cr in steel Inhibiting, e.g. As & Sb in brass Scavenging, e.g. Ti & Nb in S.S Improving other properties

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Material Selection - Galvanic Series [Seawater at 77 F.]⁰

Magnesium Zinc Aluminum Mild Steel Cast Iron Copper Stainless Steel Gold Platinum

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CATHODIC PROTECTION Cathodic protection (CP) is a technique to control the corrosion of a metal surface by making it

work as a cathode of an electrochemical cell. This is achieved by placing in contact with the metal to be protected another more easily corroded metal to act as the anode of the electrochemical cell. Cathodic protection systems are most commonly used to protect steel, water or fuel pipelines and storage tanks, steel pier piles, ships, offshore oil platforms and onshore oil well casings.

Types of CP:

sacrificial anodes (zinc, magnesium or aluminum): The sacrificial anodes are more active (more negative potential) than the metal of the structure they’re designed to protect. The anode pushes the potential of the steel structure more negative and therefore the driving force for corrosion halts. The anode continues to corrode until it requires replacement,

Impressed current CP: done for large structures (pipes, offshore platforms, etc.) where a galvanic (or sacrificial) anode can not economically deliver enough current.

Galvanized steel (see previous slide): again, steel is coated with zinc and if the zinc coating is scratched and steel exposed, the surrounding areas of zinc coating form a galvanic cell with the exposed steel and protects in from corroding. The zinc coating acts as a sacrificial anode.

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POLARIZATION

This is an effect which reduces the actual chemical potential driving of the

cell. If the thermodynamic force driving the ion into solution is reduced, this

is polarization.

Easy example. By lowering the electrolyte temperature, we find that it is

usually less corrosive. Diffusion of ions is slowed.

Inhibitors are chemicals which slow corrosion. Some of them do this by

promoting the polarization of the cathode.

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PASSIVATION OF THE ANODE

We have two examples already. Stainless and aluminum.

A thin oxide layer forms on the surface and isolates the metal from the environment.

Zn, Mg, Cu and Ti are also capable of passivation under normal conditions of operation.

Steel will also passivate in the presence of an alkaline environment, such as rebar in

concrete.

Corrosion inhibitors. Some of these, such as the chromates, are capable of coating a steel

and passivating it.

Coatings, paints, etc.

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Environment factors affecting corrosion

Dust particles and man-made pollution – CO, NO, methane, etc.

Temperature – high T & high humidity accelerates corrosion.

Rainfall – excess washes corrosive materials and debris but scarce may leave

water droplets.

Proximity to sea

Air pollution – NaCl, SO2, sulfurous acid, etc.

Humidity – cause condensation

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INHIBITORS

Inhibitors are materials that may be injected into the system . They plate out on the surface and inhibit the formation of corrosion cells. They are commonly used in pipelines and other vessels that will contain materials that are corrosive.

Some metals, such as gold and platinum, corrode very slowly or not at all. Choosing a corrosion resistant material can reduce the rate of corrosion.

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THANK YOU