FREE WEBINAR on CORROSION!

Are you someone who really needs to talk about their corrosion issues with a third person to get a fresh perspective?

Would you like to know -

How the researchers look at corrosion
How the industry looks at corrosion
How can they help each other
How to apply corrosion fundamentals
How one can learn corrosion anytime anywhere

Well, here's your chance!

I am excited to announce a webinar on corrosion - absolutely free!

Titled "Corrosion - What art thou?", this webinar is my attempt to get in touch with my connections and communicate my learnings about corrosion.

Details of the event are as below -

Date: 21st October 2021

Timing: 14:00 to 16:00 hours INDIAN STANDARD TIME

Venue: Live stream on my YouTube channel!

It will be livestreamed on my Youtube channel CORROSPECTIVE! Click on the link below to see the recording -

If you have any questions to discuss, feel free to get in touch with me before 20th October!

Something important...Will you get a certificate of attendance?

YES!

All the participants who send me a screenshot of them attending the webinar will get a certificate of attendance!

Hoping to see all of you there!

Website: https://corrospective.com
YouTube: https://lnkd.in/g_BfrXzy
Whatsapp: https://lnkd.in/gsvHAUp
Telegram: https://t.me/corrospective
Instagram: https://lnkd.in/gnGdiRYV
Blog: https://lnkd.in/geMbMeAe
Linkedin: https://www.linkedin.com/in/dr-shyama-ranade/

Comments

Corrosion risk planning - 2 - Above ground storage tanks - oil and gas- PART 1

Above ground storage tanks 1. Inner walls Coating degradation Corrosion due to water/dissolved oxygen insufficient/damaged cathodic protection system dissolved sacrificial anodes 2. Outer walls/roof Atmospheric corrosion coating degradation due to moisture + UV radiation + temperature Erosion and wear due to wind and dust particles biological growth at the bottom areas near soil soil corrosion near the bottom 3. Pipes Atmospheric corrosion Coating degradation mechanical failure internal corrosion due to water/dissolved oxygen crevice corrosion in areas facing away from atmosphere corrosion at welds and joints microbial corrosion at 6 o' clock positions erosion corrosion at bends 4. Railing Coating degradation Wrong coating selection based on pure aesthetics coating damage at joints and bends corrosion at welds in the railing crevice corrosion at fixtures pitting corrosion 5. Breather valve uniform corrosion/pitting depending on whether it is made up of carbon steel/stainless steel...

Corrosion risk planning - 1 - Lead acid battery

Corrosion is a quality, environment, and safety issue. Hence, it has to come under the cope of integrated management system audits However at the moment, it is more or less considered a quality issue. As such, the general tendency is to solve corrosion issues as they come. Especially in new inventions, the foresight to look for potential corrosion risk gets lost in the attempt to focus and highlight the amazing qualities of the said inventions. Hence, I have initiated this series, where I will take a component and point out the potential corrosion and damage risk areas. Here goes the first one - lead acid battery cell. (Source:https://opentextbc.ca/chemistry/chapter/17-5-batteries-and-fuel-cells/) Protective casing - effect of temperature + electrolyte + contamination in electrolyte on the polymer crevice corrosion at fixtures mechanical damage during handling leading to voids for moisture ingress and oxygen/electrolyte leakage Positive terminal - corrosion of the mate...

Corrosion in fertilizer industry - 1.2 Elemental sulphur attack

WATCH THE VIDEO HERE OR READ ON BELOW! Elemental sulphur attack is NOT sulphidation or hydrogen sulphide corrosion. It is an aqueous corrosion phenomenon. It considers two modes - acidification of sulphur - formation of sulphuric acid 2. direct cathodic reduction of sulphur with anodic dissolution of iron The lowering of pH is the main source of corrosion in both the methods. The phenomenon is temperature dependent. It increases with increase in temperature and becomes particularly severe above the melting point of sulphur (~112.8 degree Celsius). Hydrogen sulphide present in the petroleum may aggravate the sulphur attack by enhancing uniform pitting corrosion. Monoethylene glycol is used to prevent condensate formation ans may be present in traces in the feedstock petroleum. This enhances the sulphur attack in the form of uniform corrosion, and crevice corrosion. References: Fang, Haitao, Brown, Bruce, Young, David, and Srdjan Nešic. "Investigation...

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