Design and Operation of NHT Strippers to Protect Catalytic Reformers
•
0 j'aime•1,915 vues
Common Reformer Problems Purpose of NHT Stripper Typical Design Instrumentation of NHT Stripper Other Design Issues Indications of Problems in the NHT Response to Reformer Upsets
Recommandé
Recommandé
Contenu connexe
Tendances
Tendances (20)
En vedette
En vedette (15)
Similaire à Design and Operation of NHT Strippers to Protect Catalytic Reformers
Similaire à Design and Operation of NHT Strippers to Protect Catalytic Reformers (20)
Plus de Gerard B. Hawkins
Plus de Gerard B. Hawkins (20)
Dernier
Dernier (20)
Design and Operation of NHT Strippers to Protect Catalytic Reformers
- 1. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com GBHE Technical Bulletin CTB #55 Catalytic Reforming Design and Operation of NHT Strippers To Protect Catalytic Reformers Information contained in this publication or as otherwise supplied to Users is believed to be accurate and correct at time of going to press, and is given in good faith, but it is for the User to satisfy itself of the suitability of the information for its own particular purpose. GBHE gives no warranty as to the fitness of this information for any particular purpose and any implied warranty or condition (statutory or otherwise) is excluded except to the extent that exclusion is prevented by law. GBHE accepts no liability resulting from reliance on this information. Freedom under Patent, Copyright and Designs cannot be assumed.
- 2. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com Table of Contents Common Reformer Problems Purpose of NHT Stripper Typical Design Instrumentation of NHT Stripper Other Design Issues Indications of Problems in the NHT Response to Reformer Upsets
- 3. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com Common Reformer Problems • H2S in feed to reformer • Water in feed to reformer • Bad H2O:HCl control • Feed quality (High EP, low N+A) • Low H2:Oil • Organic Sulfur Compounds in feed to reformer Purpose of NHT Stripper • Remove the following to protect Reformer: – H2S – Light Ends – Water Typical Design • Number of Trays – 20-35 Trays • Reflux to Feed Ratio – 0.25 – 0.35 – More Reflux = More Reliability • Feed Tray Location – 5-10 trays from top of tower – More Rectifying Trays can be added if needed
- 4. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com Instrumentation of NHT Stripper Other Design Issues • Fired Reboiler vs. Heat Exchanger Reboiler – Better heat input control with Fired Reboiler • Overhead Pressure – Set by the vapor pressure of the liquid in the overhead receiver
- 5. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com Indications of Problems in the NHT • Sulfur in the feed to reformer – Organic Sulfur • Reactor Problem • F/E Exchanger Leak • Leaking Startup Bypass Line • Sulfur in the feed to reformer – H2S • Low heat input to column – High reflux temperature – Low reflux rate – Low feed temperature – Low feed rate – Sudden change in fuel gas composition – Sudden change in feed composition • Low heat input to column • Sudden change in flow rate to column • Water issues in the column • Water in the feed to reformer – Increase in the water analyzer on the recycle gas – HCl level decreases in the recycle gas – H2S in recycle gas – Free water in the feed to the stripper Should be removed in the water boot on the Product Separator – Sweet Naphtha from storage Should be fed to the NHT Stripper to remove water – Water refluxed back to stripper Usually due to manual level control on the boot Should be drained every 2-3 hours Blocked outlet piping on boot
- 6. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com Other Indicators in Reformer – Yield decreases – Recycle gas purity decreases – LPG make increases – Coke make increases Response to Reformer Upsets Cut Temperature on Reformer – ~900°F – Hold until H2S is back down Increase Chloride Injection – Double or Triple normal rates – Hold until H2S is back down
- 7. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com
- 8. Refinery Process Stream Purification Refinery Process Catalysts Troubleshooting Refinery Process Catalyst Start-Up / Shutdown Activation Reduction In-situ Ex-situ Sulfiding Specializing in Refinery Process Catalyst Performance Evaluation Heat & Mass Balance Analysis Catalyst Remaining Life Determination Catalyst Deactivation Assessment Catalyst Performance Characterization Refining & Gas Processing & Petrochemical Industries Catalysts / Process Technology - Hydrogen Catalysts / Process Technology – Ammonia Catalyst Process Technology - Methanol Catalysts / process Technology – Petrochemicals Specializing in the Development & Commercialization of New Technology in the Refining & Petrochemical Industries Web Site: www.GBHEnterprises.com