Is Rust a Problem? Screening of (Oxygenated) Hydrocarbon Reactivity Nick Gonzales, Marc Levin, and Hector Zamora Shell Global Solutions (US) Inc. Mary Kay O’Connor Process Safety Center Annual Symposium Fall 2007 Copyright 2005 by Shell Global Solutions (US) Inc. This document is made available subject to the condition that the recipient will neither use nor disclose the contents except as agreed in writing with the copyright owner.
Outline Background Experimental Description Experimental Results for Species with Rust Summary
Rust – normally iron(III) oxide - is commonly found in petrochemical processing equipment Fines/deposits can provide significant surface area Potential exists for rust to react with or catalyze reaction of process species Screening of reactivity with such contaminants can be easily overlooked Background
APTAC TM Automatic Pressure Tracking Adiabatic Calorimeter APTAC is a trademark of TIAX, LLC Sample Stirring Magnet Ceramic Insulation Pressure Vessel Pressure & Temperature Controlled Chamber Reaction Vessel Heaters Nitrogen TC Sample TC Controlled Vent Gas/Liquid Injection P Transducer
Experimental Details APTAC Air purged - Vacuum/N2 addition - N2 pressure/venting Nitrogen pad gas (except for ethylene tests) Iron(III) oxide (“rust”) - Loaded into basket (C 2 H 4 ;EO) - Poured into cell Titanium cell Teflon TM -coated stir bar sample TC
Systems Studied Ethylene (1-170 m -Fe 2 O 3 powder) Ethylene Oxide (1-170 m -Fe 2 O 3 powder) Cumene Hydroperoxide (< 5 m -Fe 2 O 3 ) Di-tert-Butyl Peroxide (< 5 m -Fe 2 O 3 ) Ethylene Glycol (< 5 m -Fe 2 O 3 ) Diethylene Glycol (< 5 m -Fe 2 O 3 ) Hydrogen Peroxide (< 5 m -Fe 2 O 3 ) (Diethyl Hydroxyl Amine – not yet tested) In some systems, reaction with other iron oxides (e.g., FeO) was also examined
Ethylene + Iron (III) Oxide, Iron(II) Oxide Temperature constant pressure
Ethylene + Iron (III) Oxide, Iron(II) Oxide Self-Heat constant pressure
Ethylene + Iron (III) Oxide, Iron(II) Oxide Comments: L. Britton (UCC): referred to exotherm onset temperature as low as 100°C (data not presented in ethylene paper). This was “occasionally” observed. At this point, it is not clear why lowering of the onset temperature did not occur in our tests.
Ethylene Oxide + Iron Oxides Temperature Histories
Ethylene Oxide + Iron Oxides Pressure Histories
Ethylene Oxide + Iron Oxides Self-Heat Rates
Ethylene Oxide + Iron Oxides Pressurization Rates
30%w CHP/cumene + Iron(III) Oxide Temperature Histories
30%w CHP/cumene + Iron(III) Oxide Pressure Histories
30%w CHP/cumene + Iron(III) Oxide Self-Heat Rates
30%w CHP/cumene + Iron(III) Oxide Pressurization Rates
30%w CHP/cumene + Iron(III) Oxide Time to Maximum Rate
20%w DTBP/Toluene + Iron(III) Oxide Temperature Histories
20%w DTBP/Toluene + Iron(III) Oxide Pressure Histories
20%w DTBP/Toluene + Iron(III) Oxide Self-Heat Rate
20%w DTBP/Toluene + Iron(III) Oxide Pressurization Rate
Ethylene Glycol + Iron(III) Oxide Temperature Histories
Ethylene Glycol + Iron(III) Oxide Pressure Histories
Ethylene Glycol + Iron(III) Oxide Self-Heat Rates
Ethylene Glycol + Iron(III) Oxide Pressurization Rates
Diethylene Glycol + Iron(III) Oxide Temperature Histories
Diethylene Glycol + Iron(III) Oxide Pressure Histories
Diethylene Glycol + Iron(III) Oxide Self-Heat Rates
Diethylene Glycol + Iron(III) Oxide Pressurization Rates
Hydrogen Peroxide + Iron(III) Oxide Temperature Histories
Hydrogen Peroxide + Iron(III) Oxide Pressure Histories
Hydrogen Peroxide + Iron(III) Oxide Self-Heat Rates
Hydrogen Peroxide + Iron(III) Oxide Pressurization Rates
Hydrogen Peroxide + Iron(III) Oxide Time to Maximum Rate
Summary Of the systems examined, iron(III) Oxide (“rust”) significantly affects only EO. Marginal impact seen for CHP Surprisingly, no significant effect on ethylene Large effect observed for H 2 O 2 Overall conclusion: rust enhances reaction for species that are known for instability or reactivity
Summary Future Interest Continued testing Additional species with -Fe 2 O 3 Species with FeO Species with high surface area Fe