Globe valve spindle failure incident

 Are you maintaining your vent and drain valves?

 Read about a globe valve spindle failure incident in this link:

  https://www.oisd.gov.in/Image/GetSafetyAlertAttachmentByID?safetyAlertID=98

Guidance for Chemical Plants During Extreme Weather Events

 CSB guidance for Chemical Plants During Extreme Weather Events: Climate change is here...are your emergency response plans including the effects of climate change that can trigger emergencies?

Read the guidance in this link

https://www.csb.gov/assets/1/6/extreme_weather_-_final_w_links.pdf

The Dakar Ammonia Accident: Analysis of the Worst Incident at an Anhydrous Ammonia User

 The Dakar ammonia accident, in Senegal on March 24, 1992, is the worst ammonia industrial acci-dent ever. This anhydrous ammonia industrial catastrophe claimed 129 lives and injured another 1,150 workers and citizens.
The accident happened at a peanut oil processing facility where ammonia was used to detoxify the product. Anhydrous ammonia was stored in a portable tank commissioned in 1983 and repaired in 1991 before the incident. The weld repairs made were on cracks detected on the tank's surface. Fre-quent overfilling of the tank ("authorized" to hold 17.7 tonnes) was one of the primary causes noted in the reports. An overpressure inside the tank led to its catastrophic failure releasing 22 tonnes of pressurized ammonia. A heavy white cloud of ammonia aerosol plus vapor spread a significant dis-tance causing fatalities and injuries.
This paper presents an analysis of the incident and the resulting consequences.
Dharmavaram, S., Air Products, Allentown, PA, U.S.A.
Pattabathula, V., S.V.P. Chemical Plant Services, Brisbane, Australia

https://www.uvu.edu/es/docs/paper4a-dakar_accident_final.pdf

Failure analysis of a rubber hose in anhydrous ammonia service

 Interesting analysis of failure of ammonia hose:

Failure analysis of a rubber hose in anhydrous ammonia service
Michael K. Budinski *
National Transportation Safety Board, 490 L’Enfant Plaza East, SW, Washington, DC 20594, United States
 https://core.ac.uk/download/pdf/82491417.pdf

I AM BACK!!

 Dear Readers,

After a gap of more than a year or more, I am back with my blog due to popular demand. Follow me to get updates.

Thanks

Karthikeyan

Optimizing Flare Operation Through Proper Design - Chemical Engineering

Optimizing Flare Operation Through Proper Design - Chemical Engineering: Flares play a critical role in many CPI facilities, to manage hydrocarbon emissions. To improve operating safety, protect personnel and the environment, and avoid costly shutdowns, molecular seal systems must be properly designed, operated and maintained. Follow this guidance to get the job done right.

WORKER SERIOUSLY INJURED DUE TO RUPTURE OF AMMONIA HOSE

 https://www.dmp.wa.gov.au/Documents/Safety/MSH_SIR_228.pdf

Anhydrous Ammonia Hose Failure

Anhydrous Ammonia Hose Failure Good case study in ethics.

DNV greenlights SBM Offshore’s ammonia terminal

 https://www.offshore-energy.biz/dnv-greenlights-sbm-offshores-ammonia-terminal/

AMMONIA SHIP UNLOADING INCIDENT

 Summary of incident
On 21 July 2018, a major release of ammonia gas occurred at a Western Australian port.
As part of a standard operation, an ammonia tanker vessel was supplying anhydrous ammonia to a process plant. Following the completion of liquid ammonia unloading, purging of the loading arm and pipework was commenced with ammonia gas supplied by the ship via the onboard storage tank head space.
While the purging operation was underway, an operator inadvertently partially closed a line valve. As the line valve was no longer fully open, a control signal was sent to the plant emergency shut-down (ESD) valve to trip closed.
This resulted in increasing internal pressure and hydraulic hammer in the loading arm, creating significant forces against the loading arm quick connect/disconnect coupler which was not sufficiently tightened for the conditions. These forces caused the loading arm to decouple from the ship’s flange and release ammonia gas. Ammonia continued to flow from the ship manifold until the ship crew manually tripped the ship’s ESD system. The release was estimated to be 1200 kg over 24 seconds.
Five personnel present at the jetty were taken to the hospital for medical examination or assessed by ambulance services. All were released the same day.

 Direct factors
The loading arm quick connect/disconnect coupler disconnected from the ship due to internal pressure.
Contributory factors
The unloading of ammonia was completed without correct engagement of the coupler. This can be attributed to:
- insufficient written instruction provided
The standard operating procedure provided little detail on the correct process for the coupler engagement.
- the control panel provided ambiguous information
A green indicator lamp on the control panel indicated that process to engage the coupler was starting. This indicator can be misconstrued as meaning full engagement has been achieved.
- there was no procedural system to validate the coupler engagement prior to commencing ship unloading
There was no visual check to confirm that the two indicator lines aligned as per the manufacturer’s instructions.
- there was no interlock to prevent unloading unless the coupler was fully engaged.
The process relied on procedural controls.
There was full reliance on the coupler installation with no secondary back-up system.
At the flange connection, there was only one control measure to ensure continuity of attachment. As the coupler is an electric-hydraulic system, various faults in the system could result in a loss of connection.
Hazard identifications and risk assessments did not adequately identify all reasonable control measures for the interface between the ship and the plant.
Manual intervention by a third party was required to stop the flow of ammonia from the ship. There was no automated system to shut the supply of ammonia from the ship in the event of a plant emergency at the time of the incident.
Actions required
To ensure similar incidents do not happen, the following actions are recommended for all operations involving quick connect/disconnect couplers.
Ensure the quick connect/disconnect coupler is correctly engaged by:
- confirming the standard operating procedure provides adequate written instructions
- attending periodic refresher training from the vendor
- implementing checklist hold points to confirm critical systems are in place prior to unloading
- installing transducers on the coupler and interlock with the safety system.
Install a locking mechanism on the coupler to ensure it cannot be inadvertently decoupled.
Review and revise the hazard identification and risk assessments to ensure all reasonable control measures are in place at the interface with third parties. For ship transfers:
- install a ship to shore safety shutdown system to automatically close the ship manifold valve in the event of a plant ESD.
Revise competency and refresher training for all personnel working with couplers.

SOURCE: https://www.dmp.wa.gov.au/Documents/Dangerous-Goods/DGS_SIR_0119.pdf

Safety Alert - Failure to detect dangerous gas/vapour due to incorrect specification of sample tube

 https://www.hse.gov.uk/safetybulletins/failure-to-detect-dangerous-gas.htm?utm_source=govdelivery&utm_medium=email&utm_campaign=dangerous-gas-safety-alert&utm_term=main&utm_content=alert-bulletin-1609

A spotlight on IoT-enabled predictive maintenance

 Texmark Chemicals ushers in the Refinery of the Future 

A spotlight on IoT-enabled predictive maintenance

In an industry with a long history of reluctance to change, Texmark Chemicals, with the help of Deloitte, embraced digital innovations such as the industrial Internet of Things (IoT), a new technology in the chemical industry, to drive profitability and create a repeatable use case in predictive maintenance IoT.

 https://www2.deloitte.com/us/en/pages/strategy-operations/articles/iot-refinery-of-the-future-case-study.html

HAPPY NEW YEAR TO MY READERS!