Search found 126 matches
- 14 May 2026, 18:39
- Forum: Inspection & Reliability Engineers
- Topic: Inspection Intervals - Multiple Storage Tanks
- Replies: 2
- Views: 65
Inspection Intervals - Multiple Storage Tanks
How would you prioritize inspection intervals across hundreds of tanks in a petrochemical complex?
- 08 May 2026, 09:47
- Forum: Process & Control Engineers
- Topic: Repetitive piping blockage - Line size increase
- Replies: 2
- Views: 179
Repetitive piping blockage - Line size increase
In one of our material handling unit, we have been facing issues of repetitive piping blockage. We believe that other than the heat tracing (installed to keep the material in melted form) effectiveness, smaller line size is also playing a role. However, would this be possible to just change the line ...
- 08 May 2026, 09:40
- Forum: Operation Engineers
- Topic: Management of O&M procedures
- Replies: 4
- Views: 3716
Re: Management of O&M procedures
Management of operating & maintenance procedures is of the key process safety management indicator, just to start with.
Typically, all procedures are required to be reviewed, and updated every 3 years, controlled by ISO.
Now coming to your query of modernizng them, sites have already been making ...
Typically, all procedures are required to be reviewed, and updated every 3 years, controlled by ISO.
Now coming to your query of modernizng them, sites have already been making ...
- 08 May 2026, 09:34
- Forum: Operation Engineers
- Topic: Frequent pitting corrosion failures of carbamate pump
- Replies: 3
- Views: 161
Re: Frequent pitting corrosion failures of carbamate pump
Even though 25-22-2 has good carbamate resistance, it is still vulnerable to localized pitting when chlorides contaminate the system.
Typical chloride sources:
Cooling water leakage
Steam condensate contamination
Hydrotest water
Improper flushing water
Contaminated passivation chemicals
Process ...
Typical chloride sources:
Cooling water leakage
Steam condensate contamination
Hydrotest water
Improper flushing water
Contaminated passivation chemicals
Process ...
- 03 May 2026, 11:59
- Forum: Process & Control Engineers
- Topic: Turbulent flow identification across a heat exchanger
- Replies: 3
- Views: 1611
Re: Turbulent flow identification across a heat exchanger
Reynolds number is the key here;
Once you calculate Re:
Re < 100 Laminar (very rare in shell side unless viscous fluid)
100 < Re < 1000 Transition
Re > 1000–2000 Turbulent crossflow
What is your intent?
Why are you worried about turbulence?
Once you calculate Re:
Re < 100 Laminar (very rare in shell side unless viscous fluid)
100 < Re < 1000 Transition
Re > 1000–2000 Turbulent crossflow
What is your intent?
Why are you worried about turbulence?
- 03 May 2026, 11:48
- Forum: Open Forum
- Topic: ClampOX - Temporary Repairs Engineering Software
- Replies: 17
- Views: 150874
Re: ClampOX - Temporary Repairs Engineering Software
Temporary repairs are in numbers before we approach any shutdown window to apply permanent nature of repairs. The management is important to address all those once that window is available. Currently at our site, maintenance teams are responsible to have them enlisted and make them part of the ...
- 19 Apr 2026, 09:45
- Forum: Process & Control Engineers
- Topic: SIS Master Register
- Replies: 3
- Views: 22937
Re: SIS Master Register
The interesting part here is that IEC 61511 doesn’t say to actually create an SIS Master Register.
What is does say is to track all SIFs, maintain lifecycle data, control changes, monitor performance, manage bypasses. And that all one cannot do without having a register in place.
What is does say is to track all SIFs, maintain lifecycle data, control changes, monitor performance, manage bypasses. And that all one cannot do without having a register in place.
- 19 Apr 2026, 09:42
- Forum: Process & Control Engineers
- Topic: Application of U-Tube Bundle
- Replies: 5
- Views: 5765
Application of U-Tube Bundle
What are the factors that a U-tube bundle is selected over fixed tube one?
I know about accommodating expansion during high temperature applications, bundle is removable, what else?
I know about accommodating expansion during high temperature applications, bundle is removable, what else?
- 15 Apr 2026, 04:37
- Forum: HSE Engineers
- Topic: Vacuum relief Activation - PRD Lift
- Replies: 3
- Views: 5270
Re: Vacuum relief Activation - PRD Lift
Definitely it is a case of Tier-3 API 754 KPI.
If there has been a demand for cauum relief to activate, it is required to be registered.
If there has been a demand for cauum relief to activate, it is required to be registered.
- 15 Apr 2026, 04:23
- Forum: Operation Engineers
- Topic: Pressure Vessels without Fireproofing
- Replies: 6
- Views: 5523
Re: Pressure Vessels without Fireproofing
This is the same observation we had at our site as well where we see some of the equipment with cleats provided to their skirt supports however with no fireproofing. I am not sure whether our HSE has already observed and evaluated that or not but all what I could say is that this is true with ...