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Dimethyl Sulfide (DMS) and TBPS 454 from Chevron Phillips Chemical are sulfiding agents that are used by refiners to transform metal oxide species to a metallic sulfide crystalline phase in situ for hydrotreating catalysts.
Sulfur is a naturally occurring substance in petroleum fuels. However, in an effort to reduce harmful SOx and NOx emissions, the United States E.P.A (Environmental Protection Agency) began mandating the use of low-sulfur fuel. The main process refineries use to remove sulfur compounds from gasoline, diesel and jet fuel is called hydrotreatment or hydrodesulfurization.
Catalytic hydrotreating is a catalytic refining process widely used to remove sulfur, unsaturated hydrocarbons, and nitrogen from petroleum products such as naphtha, gasoline, diesel fuel*, kerosene, and fuel oil.
It is also referred to as hydroprocessing or hydrodesulfurization, commonly occurs at multiple locations in a refinery.
Hydrodesulfurization processes typically include facilities for the capture and removal of the resulting hydrogen sulfide (H2S) gas, which is subsequently converted into elemental sulfur or sulfuric acid, as byproducts.
The processes are used to ensure that petroleum products meet performance specifications and involve a number of chemical conversions.
During hydrotreatment, catalysts inside the reactor, typically CoMo (Cobalt Molybdenum) or NiMo (Nickel Molybdenum) convert unwanted sulfur and nitrogen compounds into H2S (hydrogen sulfide) and NH3, which is then removed in downstream processing. In order to activate catalytic activity, the hydrotreating catalysts go through a process called "sulfiding" or "presulfiding" where metal oxides are reacted with H2S in the presence of hydrogen. Sulfiding agents are used to readily decompose sulfur compounds into the H2S required to complete the sulfiding reactions. Two of the most common sulfiding agents are TBPS 454 and DMS. Below are the advantages of each grade:
Dimethyl Disulfide (DMDS)
Property | DMDS
|
TBPS 454
|
DMS
|
---|---|---|---|
Sulfur %(wt) | 68
|
54
|
52
|
Density (lbs/gal) | 8.9
|
9.0
|
7.11
|
Freezing Point (°F) | -121
|
-54
|
-145
|
Boiling Point (°F) | 229
|
N/A
|
99
|
Flash Point | 59
|
217
|
-36
|
Vapor Pressure at 70°F (PSI) | 0.45
|
<0.1
|
8.1
|
Decomposition Temperature* (°F) | 392
|
320
|
482
|
Auto Ignition Temperature (°F) | 575
|
437
|
403
|
Viscosity at 70(°F) (mPa.s) | 0.62
|
12.8
|
.285
|
*In the presence of H2 and Catalysts
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