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18th Annual Users Group Meeting Feedback
Process Safety Management
Our Approach
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Litigation Support
Compliance Auditing
Asset Integrity Management
Pipeline Safety Management
Battery Testing and Hazard Analysis
Quantitative Risk Assessment
Hazard Analysis
Ammonia Refrigeration Safety
Facility Siting
LOPA & SIS/SIL
Sustainability Reporting Support
Technology Transfer Package
Emergency Relief System Design
Our Approach
Emergency Relief Effluent Handling System Design
Pressure Relief & Flare System Design
Relief Header & Flare Analysis Systems
Process Simulation
LNG Risk Management
Our Approach
Enterprise Software
Our Approach
Process Safety Office®
SuperChems™
PSMPro™
Process Safety Enterprise®
Asset Integrity Workflow
Emergency Relief System Design Workflow
Incident Investigation Workflow
Management of Change Workflow
Managed Application Hosting
Process Safety Project Opportunity Marketplace
Software Request for Quote
Laboratory Testing
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Chemical Reactivity Testing
Flammability Testing
Physical Properties Measurement
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Case Studies
Adequacy of Hydrocracker Emergency Relief System Case Study
Adequacy of Hydrocracker Emergency Relief System Case Study
The Challenge
A refinery approached ioMosaic for the purposes of ensuring that pressure relief capacity was adequate for the loss of liquid seal scenario in a high-pressure separator (2,000 psig). They were also concerned about the pressure waves that would occur in the high-pressure separator’s outlet lines on rapid closing of the isolation valves and sought our expertise.
Our Approach
Using our
Process Safety Office
®
SuperChems™ software
, our team were able to
model the system
between the high-pressure separator and the down stream vessel. The system consisted of three parallel flow paths. In one path, there was a power recovery turbine that was modeled. The other two flow paths contained control valves. The fluid flowing in the piping was a mixture containing twelve compounds, which were also included in the modeling.
The Benefits
Using the SuperChems™ simulations we were able to show that the relief valves and piping were adequate for the flow of gas that would be encountered on loss of liquid seal, and that the downstream vessel would not be subject to a pressure greater than its MAWP. Lastly, an optimum valve closing time was determined that would not result in pressure waves that could cause failure of the upstream piping.
Learn More
Our mission is to help you protect your people, your plant, your stakeholder value and our planet. To learn more about how we can help you manage risk, call us at
1.844.ioMosaic
.