Emerson Exchange 365
Search
Sign-In / Register
Site
Search
Sign-In/Register
Services
Products
Control & Safety Systems
Asset Management
Measurement Instrumentation
Valves, Actuators & Regulators
Fluid Control & Pneumatics
Electrical Components & Lighting
Welding, Assembly & Cleaning
IIoT & Digital Transformation
Industries
Chemical
Food and Beverage
Industrial Energy
Life Sciences
Oil & Gas
Power
Refining
Other Industries
Women in STEM
Events
Düsseldorf 2024
Immerse - Anaheim 2023
Grapevine 2022
Nashville 2019
San Antonio 2018
The Hague 2018
World
China
South Korea
Russia
More
Cancel
Services
Tips for New Process Automation Folks
Compressor Surge and Stall Detection and Prevention Tips
Services Forum
Blogs
Library/Resources
Members
Tags
More
Cancel
Create New Post
Comment or Question? Become a member of this Emerson Exchange 365 group. Click here to join.
Gregory K McMillan
23 May 2014
Options
Subscribe by email
RSS
More
Cancel
Related
Recommended
Share
Tips for New Process Automation Folks
Compressor Surge and Stall Detection and Prevention Tips
A compressor going into stall is like jumping off a cliff with a bungee cord. If the bungee cord has no losses to dampen the oscillation, we have something akin to surge. A 0.5% drop in efficiency can occur for each surge cycle. Several surge cycles can occur due to delays and lags in high temperature, thrust, and vibration shutdown systems. In some compressors the damage is so severe after multiple surge cycles that rotors and seals need to be replaced. The cost of process downtime can be significant particularly when a compressor feeds parallel trains of equipment. The restart of exothermic fluidized bed reactors in the petrochemical industry may be the most hazardous mode of operation.
Read the full text.