i-1300 HT and LT Inert Coatings for Ethylene Cracking and Delayed Cokers


	- Highly inert to filamentous coke-make.
 
	- Substantial energy and emissions reductions.
 
	- Target high severity olefins production and refinery / upgrading operations.
 
i-1300 HT [Higher Severity]
	- Inert-1300 High Temperature coating.
 
	- World-first intrinsic inertness to filamentous coke-make.
 
	- Highest coating thermal stability achieved in sector to-date.
 
i-1300 LTpc [Medium Severity]
	- i-1300 Low Temperature Petrochemical coating.
 
	- Low-cost alumina-forming coating for olefins production.
 
	- Low oxide formation temperatures.
 
	- Converts Fe and Ni from base steel into highly thermally-stable inert phases.
 
i-1300 LTdc
	- i-1300 Low Temperature Delayed Coker coating.
 
	- Inert to surface based coke-make mechanisms.
 
	- Eliminates the formation of Fe-S-C coke layer.
 
	- Eliminates any filamentous coke-make.
 
	- Reduces feedstream “dropout” coke.
 
	- Piggable to a broad range of carbide appendages.
 
 
Engineered Properties

Surface and Coating Properties
	- Inert to surface filamentous coke make.
 
	- i-3000HT requires no surface oxide growth.
 
	- i-1300LTpc grows alumina surface at lower temperatures.
 
	- i-1300LTdc coating matrix is universally inert throughout entire coating matrix and piggable.
 
Degradation Resistance
	- Oxidation
 
	- Carburization
 
	- Sulfidation
 
	- Temperature Extremes/Upsets for (HT)
 
	- Piggable (i-1300 LTdc)
 
Key Mechanical Properties
	- CTE Matched
 
	- Ductile and Weldable
 
 
Multiple Industry Applications

How It Works

i-1300 HT
World-first INTRINSIC inertness (>95%) to filamentous coke-make in higher severity olefins production in the hottest part of the furnace coil without the need for the prior formation of a surface oxide barrier.
i-1300 LTpc
Low-cost inert alumina scale former for use in the cooler parts of olefins production furnace coils without any weldability challenges.
i-1300 LTdc
Low-temperature INTRINSIC inertness to all surface coke-make mechanisms and reduction in feedstream “dropout” coke collection for use in Delayed Coker furnace coils.  Intrinsic inertness requires no oxide growth and is piggable.
 
Targeted Field Performance
i-1300 HT & LTpc (Olefins Production)
	- 8-10% reduction in energy and GHG emissions
 
	- 1 year energy payback time
 
	- Up to 3-5X longer runtimes in ethane
 
	- Up to 2+X longer runtimes in naphtha
 
	- 17kT CO2e/yr reduction per installation
 
i-1300 LTdc (Delayed Coker / Refinery)
	- 4X decrease in pigging operations
 
	- 1.5X increase in coil lifetime
 
	- OPEX reduction via energy cost
 
	- 8kt CO2e/yr reduction per installation