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Method for bio-oxidative desulfurization of liquid hydrocarbon fuels and product thereof

a technology of liquid hydrocarbon fuel and desulfurization method, which is applied in the field of hydrocarbon fuel, can solve the problems of corroding parts of internal combustion engines and refinery equipment, lowering the required reactor volume and operating cost, and sulfur in fuels poisoning catalytic converters. and other problems, to achieve the effect of high effectiveness

Inactive Publication Date: 2009-09-03
INDIAN OIL CORPORATION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The present invention provides a method for producing ultra-low-sulfur fuel oils using bio-oxidative desulfurization of fossil fuel using a selective catalyst, lipase enzyme. The method selectively removes sulfur content from the fuel by oxidizing thiophenes and organosulfides to their respective sulfoxides and sulfones, without apparently changing non-sulfur-bearing components of the fuel. The method is pH independent and does not require water or co-factors for reactivity. The invention also provides a method for producing ultra-low-sulfur fuel oils using controlled and incremental amounts of hydrogen peroxide and carboxylic acid to oxidize thiophenes and organosulfides to their respective sulfoxides and sulfones, and a microbial source enzyme that is recoverable and reusable. The method is effective in removing even the most refractory organic sulfur compounds, such as dibenzothiophene and related sulfur-bearing organic sulfides. The invention also provides an industrial and environmental friendly hydrocarbon fuel with ultra-low-sulfur content.

Problems solved by technology

Sulfur in fuels poisons catalytic converters, corrodes the parts of internal combustion engines and refinery equipment because of the formation of oxy-acids of sulfur.
However, more active catalysts and recent developments in fixed bed hydro treating technology have reduced the time spent in the reactor, thus lowering the required reactor volume and operating costs but it is limited in treating benzothiophene and dibenzothiophene especially DBTs having alkyl substitutions on their 4 and / or 6 positions.
The 4,6 disubstituted compounds do not adsorb on the active sites of the catalyst due to steric limitations.
But the usage of such oxidants is known to be very non-selective and slow.
The use of large amount of hydrogen peroxide make it environment reactive and moreover, safety-related issues are also an area of concern.
Chemical oxidation route as described above are known to be very non-selective and slow.
The use of large amount of hydrogen peroxide makes it environment reactive and moreover, safety-related issues are also an area of concern.
Although this process is effective, it is energy-intensive and requires aqueous medium for reaction.
Microbial desulfurization, however, requires a vast amount of water during the desulfurization process to sustain microbial activity (intrinsic mass transfer issue).
Beside this, microorganisms for desulfurization also degrade some aliphatic or aromatic fractions of fuels causing the decrease of fuel yield.
The method reported in prior art for biocatalytic oxidation of organosulfur compounds require considerable amount of water in diesel mixture for reaction leading to stable emulsion formation and poor recovery of water soluble products.
Moreover, some of the enzyme requires costly co-factors (co-enzymes) and are pH sensitive.
The major drawback of these co-factor dependent enzymatic desulfurization reactions is that co-factors are gradually destroyed due to undesired side reactions.
These co-factors (co-enzymes) are very expensive.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

Biocatalytic Oxidation of Model Organosulfur Compounds

[0041]Myristic acid (0.5 mM) and dibenzothiophene DBT (2 mM) were dissolved in n-hexane (10 ml) in presence of Lipase NOVOZYM™ 435 and NOVOZYM™ LC (210 mg). To this, 0.8 ml hydrogen peroxide (50%) was added in six equal increments, over 4.5 hours. The reaction mixture was agitated with magnetic stirring at room temperature for 24 h. Reactions were also carried out for oxidation of benzothiophene (BT), phenyl sulfide (PS), 4,6 dimethyl benzothiophene (DMDBT). Oxidation was also attempted in combination, i.e., DBT+46 DMDBT, DBT+BT.

[0042]To study the effect of acid chain length on oxidation of organosulfur compounds, Myristic acid (0.5 mM) was replaced with 0.5 mM of either Behanic acid, Palmitic acid, Valeric acid, propionic acid, or decanoic acid. TABLE 1 depicts the effect of chain length on extent of oxidation.

TABLE 1Extent of conversion of organosulfurcompound (DBT and 4.6.6 DMDBTto corresponding sulfoxides / sulfonesAcid Chain l...

example 2

Biocatalytic Oxidations of Diesel

[0046]Biocatalytic oxidations of diesel containing 6400 ppm to 100 ppm sulfur were carried out in 20 ml reaction volume containing 114 mg myristic acid and 210 mg of lipase NOVOZYM™ LC. Reaction was started by adding H2O2 (50% w / v, 1.0 ml). H2O2 was added in increments over 4.5 hrs. Reaction mixture was incubated at room temperature. At the end of reaction 10 ml dichloromethane (DCM) was added to the reaction mixture and filtered through Whatman NO. 41 paper to separate enzyme. The filtrate was then passed through anhydrous Na2SO4. Solvents were evaporated under nitrogen atmosphere.

[0047]Solvent extraction of sulfoxide and sulfones from oxidized diesel was carried out by several solvents like DMF, DMSO, Methanol, NMP, Furfural and Acetonitrile. The tables 2a and 2b below show the extent of desulfurization of diesel before and after bio-oxidation process when extracted with furfural and DMF solvents.

TABLE 2aSulfur content after extraction atambient te...

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Abstract

Disclosed herein is a method for producing ultra-low-sulfur content hydrocarbon fuel and product thereof. The method comprises selective biocatalytic oxidation of sulfur containing compounds present in the fuels employing enzyme lipase as biocatalyst in presence of controlled and incremental amount of hydrogen peroxide and carboxylic acid without using water or any co-factor for the reactivity of said enzymes.

Description

FIELD OF THE INVENTION[0001]This invention, in general, relates to the field of hydrocarbon fuel, in particular to the method for desulfurization of the liquid hydrocarbon fuel and product thereof. More specifically but without restriction to the particular embodiments hereinafter described in accordance with the best mode of practice, this invention provides a method for selective biocatalytic oxidation of sulfur containing compounds present in fossil fuels employing enzyme lipase as a biocatalyst.BACKGROUND OF THE INVENTION[0002]Sulfur compounds are widely distributed in petroleum distillates of all boiling ranges. In gasoline, the principal sulfur compounds are mercaptans, aliphatic sulfides, disulfides, five and six membered ring cyclic sulfides, while diesel fuel is rich in benzothiophenes and alkyl substituted benzothiophenes. The removal of sulfur from fuels is necessary for both industrial and environmental reasons. Sulfur in fuels poisons catalytic converters, corrodes the ...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10L1/18C10G32/00
CPCC10G53/14C10G27/04C10G2400/06C10G2400/04C10G2400/02C10G21/16C10G53/04C10G32/00C10G27/12
Inventor SINGH, MAHENDRA PRATAPKUMAR, MANOJKALSI, WADHAVA RAMPULIKOTTIL, ALEX CHERUSARIN, RAKESHTULI, DEEPAK KUMARMALHOTRA, RAVINDER KUMARVERMA, RAM PRAKASHBANSAL, BRIJ MOHAN
Owner INDIAN OIL CORPORATION
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