Latest Downloads
-
Water Bath Indirect Heaters
Art Montemayor - Oct 12 2018 02:35 PM
-
Petroleum: A Primer for Kansas
Art Montemayor - Oct 12 2018 02:27 PM
-
Spray Tower for Flue Gas Scrubbing Design
ankur2061 - May 02 2018 02:31 PM
-
Selection of Vertical Tanks
ankur2061 - Apr 19 2018 07:42 AM
-
Pressure Drop Calculator for Strainers 1
ankur2061 - Mar 24 2017 02:04 PM
-
Horizontal Pig Trap System Design Guidelines
ankur2061 - Jan 14 2017 02:54 PM
-
Performance Prediction of 3-Stage Propane Refrigeration System
ankur2061 - Aug 08 2016 02:43 PM
-
Centrifugal Pump Troubleshooting Checklist
ankur2061 - Dec 17 2015 08:18 AM
-
Compressor Troubleshooting Checklist
ankur2061 - Sep 08 2015 11:43 AM
-
Amine Sweetening Unit Preliminary Design
ankur2061 - May 19 2015 09:35 AM
Popular Store Titles
Tank Jacket Calculator
Specification Sheet Collection
PIPESIZE
Relief Valve Sizing
Rupture Disc Sizing
Chemical and Process Engineering Resources
Submitted Chris Haslego, Nov 21 2011 11:21 AM | Last updated Nov 21 2011 01:29 PM
Category: | Refining |
Question: | What is a good source of information about catalyst cooler operation, reliability and design for fluidized catalytic crackers. |
Keywords: | fcc,catalyst,cooler,design,revamp |
Answer: | UOP, Kellogg Brown and Root (KBR) and Stone and Webster all have catalyst cooler designs that are in commercial operation (the Stone and Webster Design was actually developed by the Bejing Design Institute in China). Each can probably supply you with contacts at refineries using their designs. All three cooler designs use essentially the same basic principles, but the hardware differs from licensor to licensor. From this standpoint, each design has both positive and negative aspects, and these differences must be weighed against your particular unit and needs. All three designs remove heat from a dense bed of catalyst located in the cooler vessel. Heat removal is through the generation of steam in tubes submerged in the dense bed. Hot catalyst enters the cooler from the regenerator bed. In most designs, cooled catalyst is returned to the regenerator using a standpipe and possibly a lift line. UOP also offers a "backmixed" design that does not require catalyst return lines (catalyst circulation to and from the cooler is controlled by fluidization air). Compared to flow through coolers, back mixed coolers have lower heat transfer rates. These dense bed coolers are considerably more reliable than older dilute phase coolers where the catalyst is blown through the tubes using air. |
Forum Quick Links
Tech Q & A Category List
-
Bulk Solids
-
ChE Outside the Plant
-
Chemical Process Business
-
Chemistry Basics
-
Corrosion
-
Equipment Design
-
Experimentation and Testing
-
Fluid Dynamics
-
Heat Transfer Technology
-
Industrial Utilities
-
Mass Transfer
-
Physical Property Information
-
Plant Basics
-
Plant Economics
-
Preparing to Become an Engineer
-
Process Control
-
Reactions and Processes
-
Refining
-
Safety
-
Separation Technology
-
The Environment
-
Thermodynamics
0 Comments