If corrosion is your problem – Cathodic Protection is our solution.

We offer Design, Supply, Installation, Testing and Commissioning, Monitoring of Cathodic Protection System for underground pipelines and structures.


Corr-Rad is a leading company specialized in giving corrosion protection for 44 years to
underground pipelines by providing Cathodic Protection System and Protective Anti-Corrosive
Coatings at major project sites all over the country. Corr-Rad has a team of highly qualified,
experienced and dedicated personnel and also has the latest equipments.
Corr-Rad is owned and managed by S. Somashekar who is a post graduate in Corrosion and has an
experience of over 48 years in the above fields of operations.
Corr-Rad is an ISO 9001:2015 accredited company and also approved by Engineers India Ltd. (EIL)


Cathodic Protection Systems
Design, Supply, Installation, Testing & Commissioning of Cathodic Protection Systems for
Underground Oil, Gas, Water pipe lines, Underground Storage Tanks, LPG Bullets, Steel Piles
of Jetties, Offshore platforms and CC Structures etc.
• Monitoring and Maintenance of CP Systems.

Anti – Corrosive Coatings
• Hot applied pipeline wrapping tape.
• Cold applied tape.
• Heat Shrink Sleeves for Welded Joints.

External Corrosion Direct Assessment (ECDA) Survey:

Close Interval Potential Survey (CIPS).
Current Attenuation Survey (CAT) with A-Frame.
Direct Current Voltage Gradient Survey (DCVG).
Soil Resistivity survey and Soil Chemical Analysis.
Current Drainage Survey.
Coating Integrity Test (CIT).

About us

Corr-Rad is owned and managed by S. Somashekar who is a post graduate in Corrosion and has an experience of Over 46 years in providing Protective Anticorrosive Coatings and Cathodic Protection Systems for Water, Oil & Gas Pipelines.

Key Personnel

P.M.Fanse Sr.Chartered Engineer with an experience of over 50 years in the pipeline industry with specialization in Cathodic Protection Systems and Pipeline Coatings and other activities related to oil and gas pipelines. 

Key Personnel


Cathodic Protection Systems


CATHODIC PROTECTION – SURVEY Preliminary Surveys required before design of Cathodic Protection System : To firm up a Cathodic Protection System Design certain data is

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CATHODIC PROTECTION – DESIGN: The cathodic protection system is generally designed to meet the following requirements: The pipe-to-soil potential will be between (-) 0.85 Volt

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Testing and Commissioning

CATHODIC PROTECTION – TESTING AND COMMISSIONING A) TEMPORARY CATHODIC PROTECTION SYSTEM Natural potential Anode potential Anode current PSP of entire pipeline Checking of Insulation joint.

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Monitoring and Maintainance

MONITORING AND MAINTENANCE The ICCP System shall have to be monitored by taking readings as mentioned below: MONITORING SCHEDULE: Transformer Rectifier Output Daily Individual Anode

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Anti-Corrosive Coatings

Supply and Application of Coatings

SUPPLY AND APPLICATION OF COATINGS Corr-Rad supplies and provides application services for hot and cold applied pipeline coatings. Corr-Rad is also marketing anti-corrosive tapes of the highest standards.

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PROTECTIVE COATING – INSPECTION HOLIDAY DETECTOR TEST This is a high voltage test carried out on underground M.S. pipelines coated with hot or cold applied

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Frequently Asked Questions

Cathodic protection is an use of an impressed current to prevent or to reduce the rate of corrosion of a metal in an electrolyteby making the metal the cathode for the impressed current.

The structure to soil potential of the structure to which Cathodic Protection is applied is made more negative than its natural potential. Usually –0.85 Volt to –1.5 Volt as measured with a special meter with respect to Cu-CuSO4 half-cell should be sufficient to prevent corrosion of the structure indefinitely.

There is no definite answer to this question. Each structure has its own current requirements, electrolyte resistivity maintenance schedule etc and hence each structure has to be considered individually. This also applies when selecting different metals for Sacrificial Anode system.

The source of electrical energy may be derived from a Transformer Rectifier unit or it may galvanic in origin as when iron and an active metal like zinc are connected to each other and are immersed in a common electrolyte, thereby protecting the iron at the expense of zinc.

Since a structure that has to be protected by Cathodic Protection must receive direct current from the electrolyte surrounding the structure and since air is poor conductor of electricity it is not possible to prevent atmospheric corrosion by Cathodic Protection.

Cathodic Protection is achieved if it is continuously and efficiently applied. It must be ‘ON’ all hours of the day and all of the year round. Occasional breakdown of power system is not dangerous if plate thickness is not just absolute minimum.

This can be applied on all structures when continuously immersed in water or permanently buried in soil. Oil, gas and water pipes, wharves, jetties, tanks, tankers, steel pilings, ships hull, heat exchangers, lead sheathed cables, etc are but a few cased in steel industry where cathodic protection has been used with large measure of success. Water and gas boards, oil industries, ports and sewage plants are large users of this system.

It is possible to protect the internal surfaces if the anodes are bonded inside the structure containing electrolyte.

Power Consumption is not very high when a good electrically insulating coating is applied on the structure to be protected.

The cost depends upon various factors like corrosive conditions of the environment, coating and its quality, and in case of pipelines on the thickness of the pipe shell. However against this direct cost, the cost of increased maintenance and repairs, increased depreciation, larger capital investment due to higher factor of safety, loss of revenue due to breakdowns and wastage, loss of public goodwill, damage suits etc is to be considered. Extra cost due to coating and cathodic protection is more than justified. As a rough measure, this cost comes to 5% to 10% of the cost of the structure.

Losses sustained by industry, defence forces and municipalities amount to many billions of dollars annually. Losses may be divided by direct and indirect losses. By direct losses meant cost of replacing corroded structures. Indirect losses are more difficult to assess. Examples of indirect losses are shut down, loss of product, loss of efficiency, contamination of product etc.



Our Associates

Contact Us

Contact us in case of project inquiry or any other query.

Gita, 92, Sion East, Mumbai 400 022. India.

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