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US20090242461A1 - Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt - Google Patents

Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt Download PDF

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Publication number
US20090242461A1
US20090242461A1 US12/058,091 US5809108A US2009242461A1 US 20090242461 A1 US20090242461 A1 US 20090242461A1 US 5809108 A US5809108 A US 5809108A US 2009242461 A1 US2009242461 A1 US 2009242461A1
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US
United States
Prior art keywords
hydrogen sulfide
weight
scavenger composition
catalyst
asphalt
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Abandoned
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US12/058,091
Inventor
Sherif Eldin
Lawrence John KARAS
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General Electric Co
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Individual
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Publication date
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Priority to US12/058,091 priority Critical patent/US20090242461A1/en
Assigned to GENERAL ELECTRIC COMPANY reassignment GENERAL ELECTRIC COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ELDIN, SHERIF, KARAS, LAWRENCE JOHN
Priority to JP2011501855A priority patent/JP2011515560A/en
Priority to SG2013023239A priority patent/SG189715A1/en
Priority to AU2009229113A priority patent/AU2009229113A1/en
Priority to MX2010010509A priority patent/MX2010010509A/en
Priority to PCT/US2009/033995 priority patent/WO2009120419A1/en
Priority to CA 2718758 priority patent/CA2718758A1/en
Priority to KR20107024154A priority patent/KR20100127302A/en
Priority to BRPI0906328-5A priority patent/BRPI0906328A2/en
Priority to CN200980112488.4A priority patent/CN101981107B/en
Priority to PL09724916T priority patent/PL2262856T3/en
Priority to DK09724916.3T priority patent/DK2262856T3/en
Priority to RU2010135833/05A priority patent/RU2489456C2/en
Priority to EP20090724916 priority patent/EP2262856B1/en
Priority to ES09724916.3T priority patent/ES2537813T3/en
Priority to TW098107741A priority patent/TWI475106B/en
Priority to ARP090100953 priority patent/AR072660A1/en
Publication of US20090242461A1 publication Critical patent/US20090242461A1/en
Priority to CL2010000917A priority patent/CL2010000917A1/en
Abandoned legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G29/00Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/20Organic compounds not containing metal atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/17Amines; Quaternary ammonium compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/201Impurities
    • C10G2300/207Acid gases, e.g. H2S, COS, SO2, HCN

Definitions

  • This invention relates generally to hydrogen sulfide scavengers and more particularly, to hydrogen sulfide scavengers for asphalt.
  • asphalt products or heavy oil are produced as the residue from crude oil distillation.
  • Asphalt products are black, viscous materials, which can be upgraded to higher-valued gasoline or diesel by further refining.
  • asphalt products often contain hydrogen sulfide and upgrading the asphalt products increases the risk of hydrogen sulfide exposure. Since hydrogen sulfide is corrosive in the presence of water and poisonous in very small concentrations, it must be removed before the asphalt products can be upgraded.
  • Asphalt has a high temperature range and current commercial technology employs the use of water-based triazines as hydrogen sulfide scavengers.
  • these water-based triazine materials can cause foaming, spitting and possible spillovers.
  • Commercially available organic based scavengers are expensive and can contain metal ions. The introduction of additional metal ions can create incompatibility with up-grader catalyst beds.
  • a method for reducing hydrogen sulfide in asphalt comprises adding a hydrogen sulfide scavenger composition to the asphalt, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having the formula I:
  • R is an aliphatic radical and n is from about 0 to about 15.
  • a method for treating asphalt comprises adding a hydrogen sulfide scavenger composition to the asphalt products, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having the formula I:
  • R is an aliphatic radical and n is from about 0 to about 15.
  • a hydrogen sulfide scavenger composition comprises a polyaliphatic amine and a catalyst, said polyaliphatic amine having the formula I:
  • R is an aliphatic radical and n is from about 0 to about 15.
  • the various embodiments provide an organic-based hydrogen sulfide scavenger for asphalt and for an improved method of removing hydrogen sulfide from asphalt products.
  • FIG. 1 is a bar graph showing the amount of hydrogen sulfide in ppm in asphalt samples versus time in minutes.
  • FIG. 2 is a bar graph showing the amount of hydrogen sulfide in ppm in asphalt samples versus time in minutes.
  • a method for reducing hydrogen sulfide in asphalt comprises adding a hydrogen sulfide scavenger composition to the asphalt, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having formula I:
  • R is an aliphatic radical and n is from about 0 to about 15.
  • Asphalt products often contain hydrogen sulfide, which is corrosive and poisonous and must be removed before the asphalt products can be upgraded to higher value products, such as gasoline and diesel.
  • Asphalt is any type of crude oil residuum or heavy oil that is produced from the distillation of crude oil. It is a heavy intermediate or finished product having a boiling point in a temperature range from about 500° F. to about 1100° F.
  • the asphalt can have a range of hydrogen sulfide content and any level of hydrogen sulfide can be treated.
  • the hydrogen sulfide scavenger controls and removes hydrogen sulfide from asphalt. It is an organic-based composition comprising a polyaliphatic amine.
  • the polyaliphatic amine has the formula I:
  • R is an aliphatic radical and n is from about 0 to about 15.
  • n is from about 0 to about 10. In another embodiment, n is from about 1 to about 5.
  • the aliphatic radical may be alkyl, alkenyl or alkoxy.
  • the aliphatic radical may be a straight or branched chain and may be substituted or unsubstituted.
  • the aliphatic group is substituted with one or more organic or inorganic radicals, such as halogen, alkyloxy, alkoxy, amino, hydroxyl, cyano and mercapto groups.
  • the halogen group may be chloro, bromo or iodo.
  • the aliphatic group is a C 1 -C 30 alkyl group, a C 2 -C 30 alkenyl group or a C 1 -C 30 alkoxy group
  • the alkyl group may be methyl, ethyl, n-butyl, t-butyl, isopropyl, pentyl or hexyl.
  • the alkoxy group is methoxy, ethoxy or isopropoxy.
  • the alkenyl group may be ethylene, methylethylene, trimethylene, phenylethylene or propylene.
  • the polyaliphatic amine is a polyalkyleneamine.
  • the polyalkyleneamine may be ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine or N-tallow propylenediamine.
  • the scavenger composition is added to the asphalt in any conventional manner.
  • the scavenger composition is injected into the asphalt, such as via a metering pump system.
  • the scavenger composition can be added to the asphalt in a continuous manner or can be added in one or more batch modes and repeated additions may be made.
  • the scavenger composition is added to the asphalt in any amount sufficient to reduce the levels of hydrogen sulfide in the asphalt. In one embodiment, the scavenger composition is added in an amount of from about 50 ppm to about 3000 ppm by weight, based on the weight of the asphalt. In another embodiment, the scavenger composition is added in an amount of from about 50 ppm by weight to about 1000 ppm by weight, based on the weight of the asphalt.
  • the scavenger composition significantly reduces the hydrogen sulfide levels contained in the asphalt.
  • the actual amount of residual hydrogen sulfide will vary depending on the starting amount.
  • the hydrogen sulfide levels are reduced to 10 ppm by weight or less, based on the weight of the asphalt.
  • the hydrogen sulfide levels are reduced to 2 ppm by weight or less, based on the weight of the asphalt.
  • the hydrogen sulfide levels are reduced to less than 1 ppm by weight, based on the weight of the asphalt.
  • the hydrogen sulfide scavenger composition may optionally include a solvent.
  • the solvent aids the scavenger composition in dispersing with the asphalt products.
  • the solvent may be any solvent that is miscible with polyaliphatic amines and that has a high flashpoint. In one embodiment, the solvent has a flashpoint of at least 200° F.
  • the solvent includes, but is not limited to, propylene glycol, 1,4-butanediol, ethylene carbonate or propylene carbonate.
  • the solvent may be added in an amount of from about 0 to about 300 percent by weight based on the weight of the polyaliphatic amine. In another embodiment, the solvent is added in an amount of from about 0 to about 150 percent by weight based on the weight of the polyaliphatic amine. In another embodiment, the solvent is added in an amount of from about 0 to about 80 percent by weight, based on the weight of the polyaliphatic amine.
  • the hydrogen sulfide scavenger is a composition comprising a polyaliphatic amine and a catalyst.
  • the catalyst improves the efficacy of the scavenger composition and enhances removal of hydrogen sulfide.
  • the catalyst may be any suitable quaternary ammonium salt.
  • the catalyst has formula II:
  • R 1 , R 2 , R 3 and R 4 are each independently alkyl groups having from 1 to 30 carbon atoms, hydroxyalkyl groups having from 1 to 30 carbon atoms or an aryl group having from 6 to 30 carbon atoms; and X is a halide or methyl sulfate.
  • the halide may be chloride, bromide or iodide.
  • the catalyst is alkyl benzyl ammonium chloride or benzyl cocoalkyl dimethyl quaternary ammonium chloride.
  • the catalyst includes, but is not limited to dicocodimethylammonium chloride, ditallowedimethylammonium chloride, di(hydrogenated tallow alkyl) dimethyl quaternary ammonium methyl chloride, methyl bis(2-hydroxyethyl cocoalkyl quaternary ammonium chloride, dimethyl(2-ethyl) tallow ammonium methyl sulfate or hydrogenated tallow alkyl (2-ethylhyexyl) dimethyl quaternary ammonium methylsulfate.
  • a scavenger composition comprises from about 20 to about 98 percent by weight polyaliphatic amine, from about 2 to about 20 percent by weight catalyst and from 0 to about 78 percent by weight of a solvent, based on the weight of the composition. In another embodiment, the scavenger composition comprises from about 50 to about 97 percent by weight polyaliphatic amine, from about 3 to about 10 percent by weight catalyst and from 0 to about 47 percent by weight of a solvent, based on the weight of the composition.
  • the scavenger composition may optionally contain other compounds, such as amine dispersants, corrosion inhibitors, surfactants and the like.
  • the surfactants include anionic surfactants, nonionic surfactants or combinations thereof.
  • the scavenger composition may be added to the asphalt as one formulation or the polyaliphatic amine and other components may be added separately to the asphalt.
  • Optional components, such as the catalyst, solvent or other additives may be added separately, may be combined into one formulation with the polyaliphatic amine or may be preblended with other components before adding to the asphalt.
  • the components in the scavenger composition are blended together before adding to the asphalt.
  • a method for treating asphalt comprises adding a hydrogen sulfide scavenger composition to the asphalt products, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having formula I:
  • R is an aliphatic radical and n is from about 0 to about 15.
  • n is from about 0 to about 10. In another embodiment, n is from about 1 to about 5.
  • the aliphatic radical may be alkyl, alkenyl or alkoxy.
  • the aliphatic radical may be a straight or branched chain and may be substituted or unsubstituted.
  • the aliphatic group is substituted with one or more organic or inorganic radicals, such as halogen, alkyloxy, alkoxy, amino, hydroxyl, cyano and mercapto groups.
  • the halogen group may be chloro, bromo or iodo.
  • the aliphatic group is a C 1 -C 30 alkyl group, a C 2 -C 30 alkenyl group or a C 1 -C 30 alkoxy group.
  • the alkyl group may be methyl, ethyl, n-butyl, t-butyl, isopropyl, pentyl or hexyl.
  • the alkoxy group is methoxy, ethoxy or isopropoxy.
  • the alkenyl group may be ethylene, methylethylene, trimethylene, phenylethylene or propylene.
  • the polyaliphatic amine is a polyalkyleneamine.
  • the polyalkyleneamine may be ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine or N-tallow propylenediamine.
  • the hydrogen sulfide scavenger composition may optionally include a catalyst, solvent or other additive as explained above.
  • a hydrogen sulfide scavenger composition comprises a polyaliphatic amine and a catalyst, said polyaliphatic amine having the formula I:
  • R is an aliphatic radical and n is from about 0 to about 15.
  • n is from about 0 to about 10. In another embodiment, n is from about 1 to about 5.
  • the aliphatic radical may be alkyl, alkenyl or alkoxy.
  • the aliphatic radical may be a straight or branched chain and may be substituted or unsubstituted.
  • the aliphatic group is substituted with one or more organic or inorganic radicals, such as halogen, alkyloxy, alkoxy, amino, hydroxyl, cyano and mercapto groups.
  • the halogen group may be chloro, bromo or iodo.
  • the aliphatic group is a C 1 -C 30 alkyl group, a C 2 -C 30 alkenyl group or a C 1 -C 30 alkoxy group.
  • the alkyl group may be methyl, ethyl, n-butyl, t-butyl, isopropyl, pentyl or hexyl.
  • the alkoxy group is methoxy, ethoxy or isopropoxy.
  • the alkenyl group may be ethylene, methylethylene, trimethylene, phenylethylene or propylene.
  • the polyaliphatic amine is a polyalkyleneamine.
  • the polyalkyleneamine may be ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine or N-tallow propylenediamine.
  • Sample 1 was prepared by dispersing 51 mg of diethylenetriamine in 34 mg propylene glycol.
  • Sample 2 was prepared by dispersing 51 mg of diethylenetriamine and 3 mg of alkyl benzyl ammonium chloride (ARQUAD DMCB-80 from Akzo-Nobel) in 34 mg propylene glycol.
  • Sample 1 was added to 578 g of an asphalt (from Conoco Phillips, West Lake, La. refinery) containing over 350 ppm hydrogen sulfide.
  • Sample 2 was added to 821 g of the asphalt.
  • the concentration of the hydrogen sulfide in the vapor phase was determined at frequent intervals as shown in FIG. 1 .
  • the data scatter can be attributed to a +/ ⁇ 15% error in determining H 2 S vapor concentrations.
  • FIG. 1 shows that samples 1 and 2 reduce and control the hydrogen sulfide content in the asphalt.
  • the addition of the catalyst (alkyl benzyl ammonium chloride) significantly increases the efficacy of the scavenger composition.
  • Sample 2 effectively controls the hydrogen sulfide level in 42% more asphalt.
  • a control sample A was prepared by dispersing 51 mg of 1,3,5-trimethylhexahydro-1,3,5-triazine in 34 mg propylene glycol.
  • a control sample B was prepared by dispersing 51 mg of MA-triazine and 3 mg of alkyl benzyl ammonium chloride (ARQUAD DMCB-80 from Akzo-Nobel) in 34 mg propylene glycol.
  • Control sample A was added to 578 g of an asphalt (from Conoco Phillips, West Lake, La. refinery) containing over 350 ppm hydrogen sulfide.
  • Control sample B was added to 821 g of the asphalt.
  • the concentration of the hydrogen sulfide in the vapor phase was determined at frequent intervals as shown in FIG. 2 .
  • the data scatter can be attributed to a +/ ⁇ 15% error in determining H 2 S vapor concentrations.
  • FIG. 2 shows that the catalyst (ARQUAD DMCB-80) has no impact on the efficacy of hydrogen sulfide scavenging when using an organic-based MA-Triazine.
  • the data in FIG. 2 also shows that the overall scavenging of the control samples is not as effective as the scavenging for samples 1 and 2 in FIG. 1 .

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Abstract

A method for reducing hydrogen sulfide in asphalt includes adding a hydrogen scavenger composition to the asphalt. The hydrogen sulfide scavenger includes a polyaliphatic amine having the formula I:

H2NRNH—(RNH)n—H  I
R is an aliphatic radical and n is from about 0 to about 15. A method for treating asphalt and a hydrogen sulfide scavenger are also provided.

Description

    FIELD OF THE INVENTION
  • This invention relates generally to hydrogen sulfide scavengers and more particularly, to hydrogen sulfide scavengers for asphalt.
  • BACKGROUND OF THE INVENTION
  • During the refining of crude oil, asphalt products or heavy oil are produced as the residue from crude oil distillation. Asphalt products are black, viscous materials, which can be upgraded to higher-valued gasoline or diesel by further refining. However, asphalt products often contain hydrogen sulfide and upgrading the asphalt products increases the risk of hydrogen sulfide exposure. Since hydrogen sulfide is corrosive in the presence of water and poisonous in very small concentrations, it must be removed before the asphalt products can be upgraded.
  • Asphalt has a high temperature range and current commercial technology employs the use of water-based triazines as hydrogen sulfide scavengers. However, these water-based triazine materials can cause foaming, spitting and possible spillovers. Commercially available organic based scavengers are expensive and can contain metal ions. The introduction of additional metal ions can create incompatibility with up-grader catalyst beds.
  • What is needed is an improved organic based scavenger for removing hydrogen sulfide from asphalt.
  • BRIEF DESCRIPTION OF THE INVENTION
  • In one embodiment, a method for reducing hydrogen sulfide in asphalt, comprises adding a hydrogen sulfide scavenger composition to the asphalt, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having the formula I:

  • H2NRNH—(RNH)n—H  I
  • wherein R is an aliphatic radical and n is from about 0 to about 15.
  • In another embodiment, a method for treating asphalt comprises adding a hydrogen sulfide scavenger composition to the asphalt products, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having the formula I:

  • H2NRNH—(RNH)n—H  I
  • wherein R is an aliphatic radical and n is from about 0 to about 15.
  • In another embodiment, a hydrogen sulfide scavenger composition comprises a polyaliphatic amine and a catalyst, said polyaliphatic amine having the formula I:

  • H2NRNH—(RNH)n—H  I
  • wherein R is an aliphatic radical and n is from about 0 to about 15.
  • The various embodiments provide an organic-based hydrogen sulfide scavenger for asphalt and for an improved method of removing hydrogen sulfide from asphalt products.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • FIG. 1 is a bar graph showing the amount of hydrogen sulfide in ppm in asphalt samples versus time in minutes.
  • FIG. 2 is a bar graph showing the amount of hydrogen sulfide in ppm in asphalt samples versus time in minutes.
  • DETAILED DESCRIPTION OF THE INVENTION
  • The singular forms “a,” “an” and “the” include plural referents unless the context clearly dictates otherwise. The endpoints of all ranges reciting the same characteristic are independently combinable and inclusive of the recited endpoint. All references are incorporated herein by reference.
  • The modifier “about” used in connection with a quantity is inclusive of the stated value and has the meaning dictated by the context (e.g., includes the tolerance ranges associated with measurement of the particular quantity).
  • “Optional” or “optionally” means that the subsequently described event or circumstance may or may not occur, or that the subsequently identified material may or may not be present, and that the description includes instances where the event or circumstance occurs or where the material is present, and instances where the event or circumstance does not occur or the material is not present.
  • In one embodiment, a method for reducing hydrogen sulfide in asphalt, comprises adding a hydrogen sulfide scavenger composition to the asphalt, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having formula I:

  • H2NRNH—(RNH)n—H  I
  • wherein R is an aliphatic radical and n is from about 0 to about 15.
  • Asphalt products often contain hydrogen sulfide, which is corrosive and poisonous and must be removed before the asphalt products can be upgraded to higher value products, such as gasoline and diesel. Asphalt is any type of crude oil residuum or heavy oil that is produced from the distillation of crude oil. It is a heavy intermediate or finished product having a boiling point in a temperature range from about 500° F. to about 1100° F. The asphalt can have a range of hydrogen sulfide content and any level of hydrogen sulfide can be treated.
  • The hydrogen sulfide scavenger controls and removes hydrogen sulfide from asphalt. It is an organic-based composition comprising a polyaliphatic amine. The polyaliphatic amine has the formula I:

  • H2NRNH—(RNH)n—H  I
  • wherein R is an aliphatic radical and n is from about 0 to about 15.
  • In one embodiment, n is from about 0 to about 10. In another embodiment, n is from about 1 to about 5.
  • In one embodiment, the aliphatic radical may be alkyl, alkenyl or alkoxy. The aliphatic radical may be a straight or branched chain and may be substituted or unsubstituted. In one embodiment, the aliphatic group is substituted with one or more organic or inorganic radicals, such as halogen, alkyloxy, alkoxy, amino, hydroxyl, cyano and mercapto groups. In one embodiment, the halogen group may be chloro, bromo or iodo.
  • In another embodiment, the aliphatic group is a C1-C30 alkyl group, a C2-C30 alkenyl group or a C1-C30 alkoxy group, In one embodiment, the alkyl group may be methyl, ethyl, n-butyl, t-butyl, isopropyl, pentyl or hexyl. In another embodiment, the alkoxy group is methoxy, ethoxy or isopropoxy. In another embodiment, the alkenyl group may be ethylene, methylethylene, trimethylene, phenylethylene or propylene.
  • In one embodiment, the polyaliphatic amine is a polyalkyleneamine. In another embodiment, the polyalkyleneamine may be ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine or N-tallow propylenediamine.
  • The scavenger composition is added to the asphalt in any conventional manner. In one embodiment, the scavenger composition is injected into the asphalt, such as via a metering pump system. The scavenger composition can be added to the asphalt in a continuous manner or can be added in one or more batch modes and repeated additions may be made.
  • The scavenger composition is added to the asphalt in any amount sufficient to reduce the levels of hydrogen sulfide in the asphalt. In one embodiment, the scavenger composition is added in an amount of from about 50 ppm to about 3000 ppm by weight, based on the weight of the asphalt. In another embodiment, the scavenger composition is added in an amount of from about 50 ppm by weight to about 1000 ppm by weight, based on the weight of the asphalt.
  • The scavenger composition significantly reduces the hydrogen sulfide levels contained in the asphalt. The actual amount of residual hydrogen sulfide will vary depending on the starting amount. In one embodiment, the hydrogen sulfide levels are reduced to 10 ppm by weight or less, based on the weight of the asphalt. In another embodiment, the hydrogen sulfide levels are reduced to 2 ppm by weight or less, based on the weight of the asphalt. In another embodiment, the hydrogen sulfide levels are reduced to less than 1 ppm by weight, based on the weight of the asphalt.
  • The hydrogen sulfide scavenger composition may optionally include a solvent. The solvent aids the scavenger composition in dispersing with the asphalt products. The solvent may be any solvent that is miscible with polyaliphatic amines and that has a high flashpoint. In one embodiment, the solvent has a flashpoint of at least 200° F. In one embodiment, the solvent includes, but is not limited to, propylene glycol, 1,4-butanediol, ethylene carbonate or propylene carbonate.
  • In one embodiment, the solvent may be added in an amount of from about 0 to about 300 percent by weight based on the weight of the polyaliphatic amine. In another embodiment, the solvent is added in an amount of from about 0 to about 150 percent by weight based on the weight of the polyaliphatic amine. In another embodiment, the solvent is added in an amount of from about 0 to about 80 percent by weight, based on the weight of the polyaliphatic amine.
  • In another embodiment, the hydrogen sulfide scavenger is a composition comprising a polyaliphatic amine and a catalyst. The catalyst improves the efficacy of the scavenger composition and enhances removal of hydrogen sulfide. The catalyst may be any suitable quaternary ammonium salt. In one embodiment, the catalyst has formula II:

  • R1R2R3R4N+X  II
  • wherein R1, R2, R3 and R4 are each independently alkyl groups having from 1 to 30 carbon atoms, hydroxyalkyl groups having from 1 to 30 carbon atoms or an aryl group having from 6 to 30 carbon atoms; and X is a halide or methyl sulfate. In one embodiment, the halide may be chloride, bromide or iodide. In another embodiment, the catalyst is alkyl benzyl ammonium chloride or benzyl cocoalkyl dimethyl quaternary ammonium chloride. In another embodiment, the catalyst includes, but is not limited to dicocodimethylammonium chloride, ditallowedimethylammonium chloride, di(hydrogenated tallow alkyl) dimethyl quaternary ammonium methyl chloride, methyl bis(2-hydroxyethyl cocoalkyl quaternary ammonium chloride, dimethyl(2-ethyl) tallow ammonium methyl sulfate or hydrogenated tallow alkyl (2-ethylhyexyl) dimethyl quaternary ammonium methylsulfate.
  • In one embodiment, a scavenger composition comprises from about 20 to about 98 percent by weight polyaliphatic amine, from about 2 to about 20 percent by weight catalyst and from 0 to about 78 percent by weight of a solvent, based on the weight of the composition. In another embodiment, the scavenger composition comprises from about 50 to about 97 percent by weight polyaliphatic amine, from about 3 to about 10 percent by weight catalyst and from 0 to about 47 percent by weight of a solvent, based on the weight of the composition.
  • The scavenger composition may optionally contain other compounds, such as amine dispersants, corrosion inhibitors, surfactants and the like. In one embodiment, the surfactants include anionic surfactants, nonionic surfactants or combinations thereof.
  • The scavenger composition may be added to the asphalt as one formulation or the polyaliphatic amine and other components may be added separately to the asphalt. Optional components, such as the catalyst, solvent or other additives may be added separately, may be combined into one formulation with the polyaliphatic amine or may be preblended with other components before adding to the asphalt. In one embodiment, the components in the scavenger composition are blended together before adding to the asphalt.
  • In another embodiment, a method for treating asphalt comprises adding a hydrogen sulfide scavenger composition to the asphalt products, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having formula I:

  • H2NRNH—(RNH)n—H  I
  • wherein R is an aliphatic radical and n is from about 0 to about 15.
  • In one embodiment, n is from about 0 to about 10. In another embodiment, n is from about 1 to about 5.
  • In one embodiment, the aliphatic radical may be alkyl, alkenyl or alkoxy. The aliphatic radical may be a straight or branched chain and may be substituted or unsubstituted. In one embodiment, the aliphatic group is substituted with one or more organic or inorganic radicals, such as halogen, alkyloxy, alkoxy, amino, hydroxyl, cyano and mercapto groups. In one embodiment, the halogen group may be chloro, bromo or iodo.
  • In another embodiment, the aliphatic group is a C1-C30 alkyl group, a C2-C30 alkenyl group or a C1-C30 alkoxy group. In one embodiment, the alkyl group may be methyl, ethyl, n-butyl, t-butyl, isopropyl, pentyl or hexyl. In another embodiment, the alkoxy group is methoxy, ethoxy or isopropoxy. In another embodiment, the alkenyl group may be ethylene, methylethylene, trimethylene, phenylethylene or propylene.
  • In one embodiment, the polyaliphatic amine is a polyalkyleneamine. In another embodiment, the polyalkyleneamine may be ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine or N-tallow propylenediamine.
  • The hydrogen sulfide scavenger composition may optionally include a catalyst, solvent or other additive as explained above.
  • In another embodiment, a hydrogen sulfide scavenger composition comprises a polyaliphatic amine and a catalyst, said polyaliphatic amine having the formula I:

  • H2NRNH—(RNH)n—H  I
  • wherein R is an aliphatic radical and n is from about 0 to about 15.
  • In one embodiment, n is from about 0 to about 10. In another embodiment, n is from about 1 to about 5.
  • In one embodiment, the aliphatic radical may be alkyl, alkenyl or alkoxy. The aliphatic radical may be a straight or branched chain and may be substituted or unsubstituted. In one embodiment, the aliphatic group is substituted with one or more organic or inorganic radicals, such as halogen, alkyloxy, alkoxy, amino, hydroxyl, cyano and mercapto groups. In one embodiment, the halogen group may be chloro, bromo or iodo.
  • In another embodiment, the aliphatic group is a C1-C30 alkyl group, a C2-C30 alkenyl group or a C1-C30 alkoxy group. In one embodiment, the alkyl group may be methyl, ethyl, n-butyl, t-butyl, isopropyl, pentyl or hexyl. In another embodiment, the alkoxy group is methoxy, ethoxy or isopropoxy. In another embodiment, the alkenyl group may be ethylene, methylethylene, trimethylene, phenylethylene or propylene.
  • In one embodiment, the polyaliphatic amine is a polyalkyleneamine. In another embodiment, the polyalkyleneamine may be ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine or N-tallow propylenediamine.
  • In order that those skilled in the art will be better able to practice the present disclosure, the following examples are given by way of illustration and not by way of limitation.
  • EXAMPLES Example 1
  • Sample 1 was prepared by dispersing 51 mg of diethylenetriamine in 34 mg propylene glycol. Sample 2 was prepared by dispersing 51 mg of diethylenetriamine and 3 mg of alkyl benzyl ammonium chloride (ARQUAD DMCB-80 from Akzo-Nobel) in 34 mg propylene glycol. Sample 1 was added to 578 g of an asphalt (from Conoco Phillips, West Lake, La. refinery) containing over 350 ppm hydrogen sulfide. Sample 2 was added to 821 g of the asphalt. The concentration of the hydrogen sulfide in the vapor phase was determined at frequent intervals as shown in FIG. 1. The data scatter can be attributed to a +/−15% error in determining H2S vapor concentrations.
  • FIG. 1 shows that samples 1 and 2 reduce and control the hydrogen sulfide content in the asphalt. The addition of the catalyst (alkyl benzyl ammonium chloride) significantly increases the efficacy of the scavenger composition. Sample 2 effectively controls the hydrogen sulfide level in 42% more asphalt.
  • Example 2
  • A control sample A was prepared by dispersing 51 mg of 1,3,5-trimethylhexahydro-1,3,5-triazine in 34 mg propylene glycol. A control sample B was prepared by dispersing 51 mg of MA-triazine and 3 mg of alkyl benzyl ammonium chloride (ARQUAD DMCB-80 from Akzo-Nobel) in 34 mg propylene glycol. Control sample A was added to 578 g of an asphalt (from Conoco Phillips, West Lake, La. refinery) containing over 350 ppm hydrogen sulfide. Control sample B was added to 821 g of the asphalt. The concentration of the hydrogen sulfide in the vapor phase was determined at frequent intervals as shown in FIG. 2. The data scatter can be attributed to a +/−15% error in determining H2S vapor concentrations.
  • FIG. 2 shows that the catalyst (ARQUAD DMCB-80) has no impact on the efficacy of hydrogen sulfide scavenging when using an organic-based MA-Triazine. The data in FIG. 2 also shows that the overall scavenging of the control samples is not as effective as the scavenging for samples 1 and 2 in FIG. 1.
  • While typical embodiments have been set forth for the purpose of illustration, the foregoing descriptions should not be deemed to be a limitation on the scope herein. Accordingly, various modifications, adaptations and alternatives may occur to one skilled in the art without departing from the spirit and scope herein.

Claims (30)

1. A method for reducing hydrogen sulfide in asphalt, comprising adding a hydrogen sulfide scavenger composition to the asphalt, wherein the hydrogen sulfide scavenger comprises a polyaliphatic amine having formula I:

H2NRNH—(RNH)n—H  I
wherein R is an aliphatic radical and n is from about 0 to about 15.
2. The method of claim 1, wherein the aliphatic radical is a C1-C30 alkyl, C2-C30 alkenyl or C1-C30 alkoxy.
3. The method of claim 1, wherein the polyaliphatic amine is a polyalkyleneamine.
4. The method of claim 3, wherein the polyalkyleneamine is selected from the group consisting of ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine and N-tallow propylenediamine.
5. The method of claim 1, wherein the scavenger composition is added in an amount of from about 50 ppm to about 3000 ppm by weight, based on the weight of the asphalt.
6. The method of claim 1, wherein the hydrogen sulfide scavenger composition further comprises a solvent.
7. The method of claim 1, wherein the hydrogen sulfide scavenger composition further comprises a catalyst.
8. The method of claim 7, wherein the catalyst has formula II:

R1R2R3R4N+X  II
wherein R1, R2, R3 and R4 are each independently alkyl groups having from 1 to 20 carbon atoms, hydroxyalkyl groups having from 1 to 20 carbon atoms or an aryl group having from 6 to 20 carbon atoms; and X is a halide or methyl sulfate.
9. The method of claim 8, wherein the catalyst is selected from the group consisting of dicocodimethylammonium chloride, ditallowedimethylammonium chloride, di(hydrogenated tallow alkyl) dimethyl quaternary ammonium methyl chloride, methyl bis(2-hydroxyethyl cocoalkyl quaternary ammonium chloride, dimethyl(2-ethyl) tallow ammonium methyl sulfate and hydrogenated tallow alkyl (2-ethylhyexyl) dimethyl quaternary ammonium methylsulfate.
10. The method of claim 7, wherein the scavenger composition comprises from about 20 to about 98 percent by weight polyaliphatic amine, from about 2 to about 20 percent by weight catalyst and from 0 to about 78 percent by weight of a solvent, based on the weight of the composition.
11. A method for treating asphalt comprising adding a hydrogen sulfide scavenger composition to the asphalt products, wherein the hydrogen sulfide scavenger composition comprises a polyaliphatic amine having the formula I:

H2NRNH—(RNH)n—H  I
wherein R is an aliphatic radical and n is from about 0 to about 15.
12. The method of claim 11, wherein the aliphatic radical is a C1-C30 alkyl, C2-C30 alkenyl or C1-C30 alkoxy.
13. The method of claim 11, wherein the polyaliphatic amine is a polyalkyleneamine.
14. The method of claim 13, wherein the polyalkyleneamine is selected from the group consisting of ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine and N-tallow propylenediamine.
15. The method of claim 11, wherein the scavenger composition is added in an amount of from about 50 ppm to about 3000 ppm by weight, based on the weight of the asphalt.
16. The method of claim 11, wherein the hydrogen sulfide scavenger composition further comprises a solvent.
17. The method of claim 11, wherein the hydrogen sulfide scavenger composition further comprises a catalyst.
18. The method of claim 17, wherein the catalyst has formula II:

R1R2R3R4N+X  II
wherein R1, R2, R3 and R4 are each independently alkyl groups having from 1 to 30 carbon atoms, hydroxyalkyl groups having from 1 to 30 carbon atoms or an aryl group having from 6 to 30 carbon atoms; and X is a halide or methyl sulfate.
19. The method of claim 18, wherein the catalyst is selected from the group consisting of dicocodimethylammonium chloride, ditallowedimethylammonium chloride, di(hydrogenated tallow alkyl) dimethyl quaternary ammonium methyl chloride, methyl bis(2-hydroxyethyl cocoalkyl quaternary ammonium chloride, dimethyl(2-ethyl) tallow ammonium methyl sulfate and hydrogenated tallow alkyl (2-ethylhyexyl) dimethyl quaternary ammonium methylsulfate.
20. The method of claim 17, wherein the scavenger composition comprises from about 20 to about 98 percent by weight polyaliphatic amine, from about 2 to about 20 percent by weight catalyst and from 0 to about 78 percent by weight of a solvent, based on the weight of the composition.
21. A hydrogen sulfide scavenger composition comprising a polyaliphatic amine and a catalyst, said polyaliphatic amine having the formula I:

H2NRNH—(RNH)n—H  I
wherein R is an aliphatic radical and n is from about 0 to about 15.
22. The scavenger composition of claim 21, wherein the aliphatic radical is a C1-C30 alkyl, C2-C30 alkenyl or C1-C30 alkoxy.
23. The scavenger composition of claim 21, wherein the polyaliphatic amine is a polyalkyleneamine.
24. The scavenger composition of claim 23, wherein the polyalkyleneamine is selected from the group consisting of ethylenediamine, diethylenetriamine, triethylenetetraamine, tetraethylenepentamine, propylethylenediamine, tetrabutylenepentamine, hexaethyleneheptamine, hexapentyleneheptamine, heptaethyleneoctamine, octaethylenenonamine, nonaethylenedecamine, decaethyleneundecamine, decahexyleneundecamine, undecaethylenedodecamine, dodecaethylenetridecamine, tridecaethylenedodecamine, dodecaethylenetriamine, tridecaethylenetetradecamine and N-tallow propylenediamine.
25. The scavenger composition of claim 21, wherein the catalyst has formula TI:

R1R2R3R4N+X  II
wherein R1, R2, R3 and R4 are each independently alkyl groups having from 1 to 30 carbon atoms, hydroxyalkyl groups having from 1 to 30 carbon atoms or an aryl group having from 6 to 30 carbon atoms; and X is a halide or methyl sulfate.
26. The scavenger composition of claim 25, wherein the catalyst is selected from the group consisting of dicocodimethylammonium chloride, ditallowedimethylammonium chloride, di(hydrogenated tallow alkyl) dimethyl quaternary ammonium methyl chloride, methyl bis(2-hydroxyethyl cocalkyl quaternary ammonium chloride, dimethyl(2-ethyl) tallow ammonium methyl sulfate and hydrogenated tallow alkyl (2-ethylhyexyl) dimethyl quaternary ammonium methylsulfate.
27. The scavenger composition of claim 21, wherein the composition further comprises a solvent.
28. The scavenger composition of claim 27, wherein the scavenger composition comprises from about 20 to about 98 percent by weight polyaliphatic amine, from about 2 to about 20 percent by weight catalyst and from 0 to about 78 percent by weight of a solvent, based on the weight of the composition.
29. The method of claim 7 wherein the polyaliphatic amine is diethylene triamine and the catalyst is alkyl benzyl ammonium chloride.
30. The method of claim 29 wherein the scavenger composition further comprises a solvent having a flashpoint of at least about 200° F.
US12/058,091 2008-03-28 2008-03-28 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt Abandoned US20090242461A1 (en)

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ES09724916.3T ES2537813T3 (en) 2008-03-28 2009-02-13 Hydrogen sulphide scrubbers and procedures for the removal of hydrogen sulphide from asphalt
BRPI0906328-5A BRPI0906328A2 (en) 2008-03-28 2009-02-13 "method for reducing hydrogen sulfide in asphalt, method for treating asphalt and hydrogen sulfide sequestering composition"
PL09724916T PL2262856T3 (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt
AU2009229113A AU2009229113A1 (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt
MX2010010509A MX2010010509A (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt.
PCT/US2009/033995 WO2009120419A1 (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt
CA 2718758 CA2718758A1 (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt
KR20107024154A KR20100127302A (en) 2008-03-28 2009-02-13 How to remove hydrogen sulfide from hydrogen sulfide scavenger and asphalt
JP2011501855A JP2011515560A (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavenger and method for removing hydrogen sulfide from asphalt
CN200980112488.4A CN101981107B (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from bitumen
SG2013023239A SG189715A1 (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers and methods for removing hydrogen sulfide from asphalt
DK09724916.3T DK2262856T3 (en) 2008-03-28 2009-02-13 Hydrogen sulfide scavengers AND APPROACHES TO REMOVE hydrogen sulfide from ASPHALT
RU2010135833/05A RU2489456C2 (en) 2008-03-28 2009-02-13 Hydrogen sulphide scavengers and methods of removing hydrogen sulphide from asphalt
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ARP090100953 AR072660A1 (en) 2008-03-28 2009-03-17 HYDROGEN SULFIDE CLEANERS AND METHODS TO REMOVE ASPHALT HYDROGEN SULFIDE
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014209722A1 (en) * 2013-06-26 2014-12-31 Halliburton Energy Services, Inc. Catalyzed polyamine sulfide scavengers and methods of use in subterranean treatment fluids
US9150707B2 (en) 2011-12-20 2015-10-06 Total Marketing Services Process for producing a cross-linked bitumen/polymer composition with a reduction in H2S emissions
US9663390B2 (en) 2013-05-10 2017-05-30 Ecolab Usa Inc. Reduction of hydrogen sulfide and/or malodor gassing from water via the addition of peroxyacetic acid/hydrogen peroxide product
US9783728B2 (en) 2016-01-12 2017-10-10 King Fahd University Of Petroleum And Minerals Method for removing iron sulfide scale
WO2019099120A1 (en) * 2017-11-15 2019-05-23 Baker Hughes, A Ge Company, Llc Ionic liquid-based hydrogen sulfide and mercaptan scavengers
US10995280B2 (en) * 2016-01-08 2021-05-04 Innophos, Inc. Scavenger compositions for sulfur species
WO2022008754A1 (en) 2020-07-10 2022-01-13 Basf Se A method for reducing hydrogen sulfide emissions during production of asphalt composition

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130298799A1 (en) * 2010-12-21 2013-11-14 Sunil Ashtekar Bituminous composition with reduced emission of hydrogen sulfide
BR112014029665A2 (en) * 2012-05-31 2017-12-19 Huntsman Petrochemical absorption composition
US9981889B2 (en) * 2013-08-22 2018-05-29 General Electric Company Use of diethylenetriamine as a CS2 scavenger in isoprene production
CA2971078C (en) * 2014-12-19 2023-01-10 Shell Internationale Research Maatschappij B.V. Process for preparing a sulphur-containing soil improver
KR101949245B1 (en) * 2016-07-15 2019-02-18 가톨릭관동대학교산학협력단 Sulfur dye adsorbent having methyl-esterified eggshell membrane, manufacturing method of the same and method for adsorption of sulfur dye using the same
JP7074754B2 (en) * 2016-12-08 2022-05-24 エコラブ ユーエスエイ インク Hydrogen sulfide scavenger for polymer treated asphalt
CA3064549C (en) 2017-05-24 2023-06-20 Poet Research Inc. Enhanced alkyl ester containing oil compositions and methods of making and using the same
US12157822B2 (en) 2017-05-24 2024-12-03 Poet Research, Inc. Methods of producing vegetable oils with low minerals, metals, or other contaminants
WO2019241269A1 (en) 2018-06-11 2019-12-19 Poet Research, Inc. Methods of refining a grain oil composition feedstock, and related systems, compositions and uses
WO2020176604A1 (en) * 2019-02-28 2020-09-03 Ecolab Usa Inc. Hydrogen sulfide scavengers for asphalt
US10774040B1 (en) 2019-04-29 2020-09-15 Chevron Phillips Chemical Company Lp Processes for removing carbon disulfide from symmetrical and asymmetrical sulfide product streams
US12139657B1 (en) 2020-03-10 2024-11-12 Poet Research, Inc. Emulsifiers and emulsions as by-products of fermentation, compositions comprising same, and methods of use thereof
BR112023001818A2 (en) 2020-08-06 2023-02-23 Poet Res Inc ENDOGENOUS LIPASE FOR METAL REDUCTION IN CORN DISTILLERY OIL
EP4277967B1 (en) 2021-01-13 2024-09-25 Ecolab Usa Inc. Hydrogen sulfide scavengers

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2238201A (en) * 1937-09-18 1941-04-15 Carbide & Carbon Chem Corp Purification of hydrocarbon liquids
US6267938B1 (en) * 1996-11-04 2001-07-31 Stanchem, Inc. Scavengers for use in reducing sulfide impurities
US6444117B1 (en) * 2000-08-16 2002-09-03 Texaco, Inc. Sweetening of sour crudes
US20050238556A1 (en) * 2004-04-21 2005-10-27 Pakulski Marek K Method of scavenging hydrogen sulfide and/or mercaptans from fluid and gas streams

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5856583B2 (en) * 1980-08-28 1983-12-15 花王株式会社 asphalt emulsion
CA2017047C (en) * 1989-08-01 1999-08-17 Jerry J. Weers Method of scavenging hydrogen sulfide from hydrocarbons
US5744024A (en) * 1995-10-12 1998-04-28 Nalco/Exxon Energy Chemicals, L.P. Method of treating sour gas and liquid hydrocarbon
JP3704077B2 (en) * 2001-01-24 2005-10-05 花王株式会社 Asphalt emulsion composition
CN1215149C (en) * 2003-03-05 2005-08-17 扬子石油化工股份有限公司 Sulfide eliminating process and desulfurizer for high-sulfur raw oil
AR046755A1 (en) * 2003-12-10 2005-12-21 Shell Int Research SULFUR PELLET INCLUDING A H2S SUPPRESSOR
US20050145137A1 (en) * 2003-12-31 2005-07-07 Buras Paul J. Process for preparing bitumen compositions with reduced hydrogen sulfide emission
RU2279465C1 (en) * 2005-01-31 2006-07-10 Государственное унитарное предприятие "Институт нефтехимпереработки Республики Башкортостан" (ГУП "ИНХП РБ") Petroleum residue dewaxing process

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2238201A (en) * 1937-09-18 1941-04-15 Carbide & Carbon Chem Corp Purification of hydrocarbon liquids
US6267938B1 (en) * 1996-11-04 2001-07-31 Stanchem, Inc. Scavengers for use in reducing sulfide impurities
US6444117B1 (en) * 2000-08-16 2002-09-03 Texaco, Inc. Sweetening of sour crudes
US20050238556A1 (en) * 2004-04-21 2005-10-27 Pakulski Marek K Method of scavenging hydrogen sulfide and/or mercaptans from fluid and gas streams

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9150707B2 (en) 2011-12-20 2015-10-06 Total Marketing Services Process for producing a cross-linked bitumen/polymer composition with a reduction in H2S emissions
US9663390B2 (en) 2013-05-10 2017-05-30 Ecolab Usa Inc. Reduction of hydrogen sulfide and/or malodor gassing from water via the addition of peroxyacetic acid/hydrogen peroxide product
US10081561B2 (en) 2013-05-10 2018-09-25 Ecolab Usa Inc. Reduction of hydrogen sulfide and/or malodor gassing from water via the addition of peroxyacetic acid/hydrogen peroxide product
WO2014209722A1 (en) * 2013-06-26 2014-12-31 Halliburton Energy Services, Inc. Catalyzed polyamine sulfide scavengers and methods of use in subterranean treatment fluids
GB2529948A (en) * 2013-06-26 2016-03-09 Halliburton Energy Services Inc Catalyzed polyamine sulfide scavengers and methods of use in subterranean treatment fluids
US9340723B2 (en) 2013-06-26 2016-05-17 Halliburton Energy Services, Inc. Catalyzed polyamine sulfide scavengers and methods of use in subterranean treatment fluids
AU2014302914B2 (en) * 2013-06-26 2016-08-11 Halliburton Energy Services, Inc. Catalyzed polyamine sulfide scavengers and methods of use in subterranean treatment fluids
US10995280B2 (en) * 2016-01-08 2021-05-04 Innophos, Inc. Scavenger compositions for sulfur species
US9783728B2 (en) 2016-01-12 2017-10-10 King Fahd University Of Petroleum And Minerals Method for removing iron sulfide scale
US10323173B2 (en) 2016-01-12 2019-06-18 King Fahd University Of Petroleum And Minerals Method for removing iron sulfide scale from oil well equipment
WO2019099120A1 (en) * 2017-11-15 2019-05-23 Baker Hughes, A Ge Company, Llc Ionic liquid-based hydrogen sulfide and mercaptan scavengers
WO2022008754A1 (en) 2020-07-10 2022-01-13 Basf Se A method for reducing hydrogen sulfide emissions during production of asphalt composition

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