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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.
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Outline Background Experimental Description Experimental Results for Species with Rust Summary
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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
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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
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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
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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
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Ethylene + Iron (III) Oxide, Iron(II) Oxide Temperature Histories @ constant pressure
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Ethylene + Iron (III) Oxide, Iron(II) Oxide Self-Heat Rates @ constant pressure
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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.
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Ethylene Oxide + Iron Oxides Temperature Histories
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Ethylene Oxide + Iron Oxides Pressure Histories
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Ethylene Oxide + Iron Oxides Self-Heat Rates
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Ethylene Oxide + Iron Oxides Pressurization Rates
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30%w CHP/cumene + Iron(III) Oxide Temperature Histories
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30%w CHP/cumene + Iron(III) Oxide Pressure Histories
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30%w CHP/cumene + Iron(III) Oxide Self-Heat Rates
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30%w CHP/cumene + Iron(III) Oxide Pressurization Rates
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30%w CHP/cumene + Iron(III) Oxide Time to Maximum Rate
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20%w DTBP/Toluene + Iron(III) Oxide Temperature Histories
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20%w DTBP/Toluene + Iron(III) Oxide Pressure Histories
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20%w DTBP/Toluene + Iron(III) Oxide Self-Heat Rate
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20%w DTBP/Toluene + Iron(III) Oxide Pressurization Rate
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Ethylene Glycol + Iron(III) Oxide Temperature Histories
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Ethylene Glycol + Iron(III) Oxide Pressure Histories
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Ethylene Glycol + Iron(III) Oxide Self-Heat Rates
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Ethylene Glycol + Iron(III) Oxide Pressurization Rates
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Diethylene Glycol + Iron(III) Oxide Temperature Histories
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Diethylene Glycol + Iron(III) Oxide Pressure Histories
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Diethylene Glycol + Iron(III) Oxide Self-Heat Rates
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Diethylene Glycol + Iron(III) Oxide Pressurization Rates
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Hydrogen Peroxide + Iron(III) Oxide Temperature Histories
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Hydrogen Peroxide + Iron(III) Oxide Pressure Histories
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Hydrogen Peroxide + Iron(III) Oxide Self-Heat Rates
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Hydrogen Peroxide + Iron(III) Oxide Pressurization Rates
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Hydrogen Peroxide + Iron(III) Oxide Time to Maximum Rate
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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
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Summary Future Interest Continued testing Additional species with -Fe 2 O 3 Species with FeO Species with high surface area Fe
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