[go: up one dir, main page]

US20120012505A1 - Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons - Google Patents

Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons Download PDF

Info

Publication number
US20120012505A1
US20120012505A1 US12/835,881 US83588110A US2012012505A1 US 20120012505 A1 US20120012505 A1 US 20120012505A1 US 83588110 A US83588110 A US 83588110A US 2012012505 A1 US2012012505 A1 US 2012012505A1
Authority
US
United States
Prior art keywords
bis
methylene
mercaptans
alpha
oxybis
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US12/835,881
Inventor
Dennis R. Compton
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ChampionX LLC
Original Assignee
Nalco Co LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nalco Co LLC filed Critical Nalco Co LLC
Priority to US12/835,881 priority Critical patent/US20120012505A1/en
Assigned to NALCO COMPANY reassignment NALCO COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: COMPTON, DENNIS R.
Priority to MX2013000509A priority patent/MX2013000509A/en
Priority to PL11807420.2T priority patent/PL2593533T3/en
Priority to BR112013000892-0A priority patent/BR112013000892B1/en
Priority to EP11807420.2A priority patent/EP2593533B1/en
Priority to ARP110102516A priority patent/AR082166A1/en
Priority to HUE11807420A priority patent/HUE030422T2/en
Priority to SG2013003009A priority patent/SG187079A1/en
Priority to RU2013102416/04A priority patent/RU2557545C2/en
Priority to ES11807420.2T priority patent/ES2593462T3/en
Priority to CA2805489A priority patent/CA2805489C/en
Priority to KR1020137003669A priority patent/KR20130141438A/en
Priority to PT118074202T priority patent/PT2593533T/en
Priority to JP2013519781A priority patent/JP5889296B2/en
Priority to PCT/US2011/043778 priority patent/WO2012009390A2/en
Publication of US20120012505A1 publication Critical patent/US20120012505A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • 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
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/148Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/152Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by forming adducts or complexes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/20Use of additives, e.g. for stabilisation
    • 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
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/104Light gasoline having a boiling range of about 20 - 100 °C
    • 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
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1044Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1048Middle distillates
    • C10G2300/1051Kerosene having a boiling range of about 180 - 230 °C
    • 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
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1048Middle distillates
    • C10G2300/1055Diesel having a boiling range of about 230 - 330 °C
    • 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
    • C10G2300/202Heteroatoms content, i.e. S, N, O, P

Definitions

  • the present invention relates to the scavenging of mercaptans in hydrocarbon fluids and more particularly to the use of alpha-amino ethers as mercaptan scavengers.
  • Hydrocarbon fluids such as crude oil, crude oil emulsions, oilfield condensate, petroleum residua and refined fuels such as naphtha, kerosene, gasoline, and other purified petroleum products often contain a variety of mercaptans, including mercaptans of relatively low molecular weight.
  • choline or choline hydroxide has been found to alleviate hydrogen sulfide evolution and to scavenge mercaptans as show in U.S. Pat. Nos. 4,594,147, 4,867,865, and 5,183,560.
  • choline and choline hydroxide are not well suited for many uses and media, such as in crude oil.
  • choline and choline hydroxide might scavenge mercaptans in such media, they also form a volatile and malodorous by-product with the sulfur compounds indigenous to such media.
  • choline and choline hydroxide to control odors associated with light weight mercaptans is self-defeating in media such as crude oil.
  • European Patent Application 0 538 819 A3 describes the use of oil-soluble quaternary ammonium compounds to scavenge mercaptans from certain oils, especially high boiling, heavy residual fuels.
  • U.S. Pat. No. 5,840,177 describes using quaternary ammonium hydroxides to scavenge mercaptans from certain hydrocarbon fluids.
  • At least one embodiment of the invention is directed towards a method of reducing the amount of mercaptans in a hydrocarbon fluid.
  • the method comprises contacting the fluid with an effective amount of alpha-amino ether sufficient to convert the mercaptan into a non-volatile species.
  • the hydrocarbon fluid can be a liquid.
  • the hydrocarbon fluid can be selected from the list consisting of but not limited to diesel fuel, kerosene, and gasoline.
  • the alpha-amino ether can be selected from the list consisting of:
  • the mercaptans can be present in the hydrocarbon fluid in amounts in excess of 500 ppm.
  • the ratio of alpha-amino ether molecules to mercaptan molecules can be within the range of 1:1000 to 1000:1.
  • FIG. 1 illustrates compositions of matter useful as a mercaptan scavenger.
  • Alpha-amino ether means a molecule according to the formula:
  • R 1 , R 2 , R 3 , R 4 are carbon containing side chains containing 1-20 carbon atoms and includes cyclic and acyclic compounds.
  • the cyclic compounds can be aromatic or non-aromatic. Examples include but are not limited to, methyl, ethyl, propyl, tert-butyl, cyclopentyl, cyclohexyl, morpholino, and phenyl, and they all can be the same group or one or more different groups.
  • B is an ether group, which is either an oxygen atom or a group having an oxygen atom at both ends (such as —OCH 2 O— or —OC 2 H 4 O—).
  • Hydrocarbon fluid means a liquid or gas predominantly comprising organic material including but not limited to kerosene, crude oil, crude oil emulsions, oilfield condensate, petroleum residua, refined fuels, distillate fuels, fuel oil, heating oils, diesel fuel, gasoline, jet fuel, bunker fuel oils, and any combination thereof.
  • “Mercaptan” means a sulfur-containing organic compound with the general formula RSH where R is any alkyl, aromatic or cyclic group.
  • Examples of common mercaptans are methylmercaptan CH 3 SH, ethylmercaptan CH 3 CH 2 SH, propylmercaptan CH 3 (CH 2 ) 2 SH, isopropylmercaptan (CH 3 ) 2 CHSH, Phenylmercaptan C 5 H S SH.
  • “Scavenger” means a composition of matter, such as but not limited to alpha-amino ethers, useful in reducing the amount of or mitigating the effects of some other composition of matter, such as but not limited to mercaptans, in a fluid medium.
  • Formaldehyde equivalent means a composition of matter containing at least one group according to the formula: (CH 2 O) n in which n is an integer greater than or equal to 1, and/or a composition of matter including formaldehyde or related molecules such as paraformaldehyde, and/or s-trioxane.
  • the amount of mercaptans in a hydrocarbon fluid is reduced by the introduction of an alpha-amino ether into the fluid.
  • the alpha-amino ether scavenges mercaptan by forming stable non-volatile compounds
  • the new sulfur containing compounds are higher molecular weight and lower volatility mitigating the odor associated with volatile mercaptans.
  • the mercaptan scavenger is produced by reacting a secondary amine with formaldehyde or other formaldehyde equivalents such as paraformaldehyde or s-trioxane.
  • formaldehyde or other formaldehyde equivalents such as paraformaldehyde or s-trioxane.
  • the reaction product also comprises 10-25% double amine that is non-reactive to the mercaptans.
  • any of the R groups correspond to any of the R 1 , R 2 , R 3 , and R 4 , groups described in the definition of “alpha-amino ether”.
  • reaction is performed without solvent.
  • This reaction can be performed with solvents such as aromatic 150, aromatic 100, etc. to create a diluted product.
  • a scavenging formulation is used in a hydrocarbon fluid.
  • the formulation can but is not required to contain a solvent and at least one alpha-amino ether, the alpha-amino ether can be used without solvent.
  • the solvent is selected from the list consisting of water, alcohol, aromatic solvent, non-aromatic solvent and a solvent that solvates alpha-amino ethers, and any combination thereof.
  • the formulation can be introduced into the hydrocarbon fluid by mechanical means including but not limited to injection pumps or any other mechanism known in the art including but not limited to those methods described in U.S. Pat. No. 5,840,177.
  • Table 1 shows the ppm wt of sulfur in the form of sec-butyl mercaptan and n-butyl mercaptan in the untreated sample.
  • Tables 2 and 3 show the reduction in mercaptans when treated with alpha-amino ethers derived from butyl amine and morpholine respectively. The loss of n-butyl mercaptan and increase in unidentified volatile sulfur compounds indicates that the mercaptan has formed a stable compound that did not match a known standard.
  • a complex mercaptan solution of nine different mercaptans was prepared and a series of alpha amino ethers was tested for their ability to reduce the mercaptans. 1000 ppm (v/v) was added to a solution of kerosene. The kerosene was then treated with 3000 ppm (v/v) of the specified samples.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention provides a method of removing mercaptans from hydrocarbon fluids. The method involves using an alpha-amino ether to scavenge the mercaptans. The scavenging reaction converts the mercaptans into a hydrocarbon soluble compound that mitigates the odor of the mercaptans.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • None.
  • STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT
  • Not Applicable.
  • BACKGROUND OF THE INVENTION
  • The present invention relates to the scavenging of mercaptans in hydrocarbon fluids and more particularly to the use of alpha-amino ethers as mercaptan scavengers. Hydrocarbon fluids, such as crude oil, crude oil emulsions, oilfield condensate, petroleum residua and refined fuels such as naphtha, kerosene, gasoline, and other purified petroleum products often contain a variety of mercaptans, including mercaptans of relatively low molecular weight. Because of the volatility of these low molecular weight mercaptans (for example, methyl mercaptan, CH3SH, ethyl mercaptan, CH3CH2SH, and propyl mercaptan, CH3CH2CH2SH), they tend to evolve into vapor spaces, where their offensive odors create problems in and around storage areas and throughout pipelines and shipping systems used for transporting the hydrocarbon.
  • Various additives have been employed in efforts to alleviate these problems. For example, choline or choline hydroxide has been found to alleviate hydrogen sulfide evolution and to scavenge mercaptans as show in U.S. Pat. Nos. 4,594,147, 4,867,865, and 5,183,560. However, choline and choline hydroxide are not well suited for many uses and media, such as in crude oil. Although choline and choline hydroxide might scavenge mercaptans in such media, they also form a volatile and malodorous by-product with the sulfur compounds indigenous to such media. Accordingly, the use of choline and choline hydroxide to control odors associated with light weight mercaptans is self-defeating in media such as crude oil. European Patent Application 0 538 819 A3 describes the use of oil-soluble quaternary ammonium compounds to scavenge mercaptans from certain oils, especially high boiling, heavy residual fuels. U.S. Pat. No. 5,840,177 describes using quaternary ammonium hydroxides to scavenge mercaptans from certain hydrocarbon fluids.
  • Despite these attempts however there is still a need for compositions that are produced in high yields and low cost, and that reduce mercaptan concentrations more effectively than the prior art. Thus there is clear need and utility for compositions and methods for scavenging molecular weight mercaptans more effectively and more efficiently. The art described in this section is not intended to constitute an admission that any patent, publication or other information referred to herein is “prior art” with respect to this invention, unless specifically designated as such. In addition, this section should not be construed to mean that a search has been made or that no other pertinent information as defined in 37 CFR §1.56(a) exists.
  • BRIEF SUMMARY OF THE INVENTION
  • At least one embodiment of the invention is directed towards a method of reducing the amount of mercaptans in a hydrocarbon fluid. The method comprises contacting the fluid with an effective amount of alpha-amino ether sufficient to convert the mercaptan into a non-volatile species.
  • The hydrocarbon fluid can be a liquid. The hydrocarbon fluid can be selected from the list consisting of but not limited to diesel fuel, kerosene, and gasoline. The alpha-amino ether can be selected from the list consisting of:
    • N,N′-oxybis(methylene)bis(N,N-dibutylamine),
    • N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-dibutylamine),
    • 4,4′-oxybis(methylene)dimorpholine,
    • bis(morpholinomethoxy)methane,
    • 1,1′-oxybis(methylene)dipiperidine,
    • bis(piperidinomethoxy)methane,
    • N,N′-oxybis(methylene)bis(N,N-dipropylamine),
    • N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-dipropylamine),
    • 1,1′-oxybis(methylene)dipyrrolidine,
    • bis(pyrrolldinomethoxy)methane,
    • N,N′-oxybis(methylene)bis(N,N-diethylamine),
    • N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-diethylamine),
  • and any combination thereof.
  • The mercaptans can be present in the hydrocarbon fluid in amounts in excess of 500 ppm. The ratio of alpha-amino ether molecules to mercaptan molecules can be within the range of 1:1000 to 1000:1.
  • DESCRIPTION OF THE DRAWINGS
  • FIG. 1 illustrates compositions of matter useful as a mercaptan scavenger.
  • DETAILED DESCRIPTION OF THE INVENTION
  • For purposes of this application the definition of these terms is as follows:
  • “Alpha-amino ether” means a molecule according to the formula:
  • Figure US20120012505A1-20120119-C00001
  • Where: R1, R2, R3, R4, are carbon containing side chains containing 1-20 carbon atoms and includes cyclic and acyclic compounds. The cyclic compounds can be aromatic or non-aromatic. Examples include but are not limited to, methyl, ethyl, propyl, tert-butyl, cyclopentyl, cyclohexyl, morpholino, and phenyl, and they all can be the same group or one or more different groups. B is an ether group, which is either an oxygen atom or a group having an oxygen atom at both ends (such as —OCH2O— or —OC2H4O—).
  • “Hydrocarbon fluid” means a liquid or gas predominantly comprising organic material including but not limited to kerosene, crude oil, crude oil emulsions, oilfield condensate, petroleum residua, refined fuels, distillate fuels, fuel oil, heating oils, diesel fuel, gasoline, jet fuel, bunker fuel oils, and any combination thereof.
  • “Mercaptan” means a sulfur-containing organic compound with the general formula RSH where R is any alkyl, aromatic or cyclic group. Examples of common mercaptans are methylmercaptan CH3SH, ethylmercaptan CH3CH2SH, propylmercaptan CH3(CH2)2SH, isopropylmercaptan (CH3)2CHSH, Phenylmercaptan C5HSSH.
  • “Scavenger” means a composition of matter, such as but not limited to alpha-amino ethers, useful in reducing the amount of or mitigating the effects of some other composition of matter, such as but not limited to mercaptans, in a fluid medium.
  • “Formaldehyde equivalent” means a composition of matter containing at least one group according to the formula: (CH2O)n in which n is an integer greater than or equal to 1, and/or a composition of matter including formaldehyde or related molecules such as paraformaldehyde, and/or s-trioxane.
  • In the event that the above definitions or a description stated elsewhere in this application is inconsistent with a meaning (explicit or implicit) which is commonly used, in a dictionary, or stated in a source incorporated by reference into this application, the application and the claim terms in particular are understood to be construed according to the definition or description in this application, and not according to the common definition, dictionary definition, or the definition that was incorporated by reference. In light of the above, in the event that a term can only be understood if it is construed by a dictionary, if the term is defined by the Kirk-Othmer Encyclopedia of Chemical Technology, 5th Edition, (2005), (Published by Wiley, John & Sons, Inc.) this definition shall control how the term is to be defined in the claims.
  • In at least one embodiment, the amount of mercaptans in a hydrocarbon fluid is reduced by the introduction of an alpha-amino ether into the fluid. The alpha-amino ether scavenges mercaptan by forming stable non-volatile compounds The new sulfur containing compounds are higher molecular weight and lower volatility mitigating the odor associated with volatile mercaptans.
  • As illustrated in FIG. 1, in at least one embodiment the mercaptan scavenger is produced by reacting a secondary amine with formaldehyde or other formaldehyde equivalents such as paraformaldehyde or s-trioxane. This produces a composition of matter that predominantly comprises two forms of alpha-amino ethers. 10%-25% of the composition is a single oxygen ether and 50%-80% of the composition is a double oxygen ether with a single carbon atom between the ether oxygen atoms. The reaction product also comprises 10-25% double amine that is non-reactive to the mercaptans. In FIG. 1, any of the R groups correspond to any of the R1, R2, R3, and R4, groups described in the definition of “alpha-amino ether”.
  • In at least one embodiment the reaction is performed without solvent. This reaction can be performed with solvents such as aromatic 150, aromatic 100, etc. to create a diluted product.
  • In at least one embodiment a scavenging formulation is used in a hydrocarbon fluid. The formulation can but is not required to contain a solvent and at least one alpha-amino ether, the alpha-amino ether can be used without solvent. The solvent is selected from the list consisting of water, alcohol, aromatic solvent, non-aromatic solvent and a solvent that solvates alpha-amino ethers, and any combination thereof. The formulation can be introduced into the hydrocarbon fluid by mechanical means including but not limited to injection pumps or any other mechanism known in the art including but not limited to those methods described in U.S. Pat. No. 5,840,177.
  • EXAMPLES
  • The foregoing may be better understood by reference to the following example, which is presented for purposes of illustration and is not intended to limit the scope of the invention.
  • Samples of kerosene were treated with known amounts of mercaptans and were tested according to ASTM D5623-94. In the test procedure described by ASTM D5623-94 the oven temperature increases from 10° C. (50° F.) to 250° C. (482° F.) at a rate of 10° C./min. Any sulfur containing compound that passes through the GC column up to the endpoint and does not have a retention time calibrated to a known structure is listed as an unidentified volatile compound.
  • Table 1 shows the ppm wt of sulfur in the form of sec-butyl mercaptan and n-butyl mercaptan in the untreated sample. Tables 2 and 3 show the reduction in mercaptans when treated with alpha-amino ethers derived from butyl amine and morpholine respectively. The loss of n-butyl mercaptan and increase in unidentified volatile sulfur compounds indicates that the mercaptan has formed a stable compound that did not match a known standard.
  • Untreated Sample Sulfur Speciation ASTM D-5623
  • TABLE 1
    ppm wt
    Mercaptan Sulfur
    sec-Butyl Mercaptan 1.5
    n-Butyl Mercaptan 396
  • N,N′-oxybis(methylene)bis(N,N-dibuyylamine) and N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-dibutylamine) Sulfur Speciation ASTM D-5623
  • TABLE 2
    ppm wt Sulfur
    Mercaptan Sulfur Reduction % Reduction
    sec-Butyl Mercaptan <0.2 >1.3 >87
    n-Butyl Mercaptan 6.8 389.2 98.3
    Unidentified Volatile 388
    Sulfur
  • 4,4′-oxybis(methylene)dimorphollne and bis(morpholinomethoxy)methane Sulfur Speciation ASTM D-5623
  • TABLE 3
    ppm wt Sulfer
    Mercaptan Sulfur Reduction % Reduction
    sec-Butyl Mercaptan 0.4 1.1 73
    n-Butyl Mercaptan 45 351 88.6
    Unidentified Volatile 343
    Sulfur

    To further illustrate the effectiveness of alpha-amino ethers as mercaptan scavengers, 9 different mercaptans were mixed together (Tables 4 and 5). The mercaptan mixture (1000 ppm v/v) was added to kerosene and then the ppm wt of the sulfur species was measured according to ASTM D5623-94. Various alpha-amino ethers (Tables 6-10) were used to treat the mercaptans by adding 3000 ppm v/v of various alpha-amino ethers. The decrease in the individual mercaptan components and the corresponding increase in unidentified volatile sulfur species demonstrates that the mercaptans reacted with the alpha-amino ethers to from stable compounds of lower volatility.
  • A complex mercaptan solution of nine different mercaptans was prepared and a series of alpha amino ethers was tested for their ability to reduce the mercaptans. 1000 ppm (v/v) was added to a solution of kerosene. The kerosene was then treated with 3000 ppm (v/v) of the specified samples.
  • TABLES 4 and 5
    Mercaptan Mass % Mole %
    Ethyl 11.1 15.7
    Isopropyl 11.1 12.8
    tert-Butyl 11.1 10.8
    n-Propyl 11.1 12.8
    Isobutyl 11.1 10.8
    n-Butyl 11.1 10.8
    Phenyl 11.1 8.9
    Benzyl 11.1 7.9
    n-Amyl 11.1 9.5
    Untreated Sample
    Sulfur Speciation ASTM D-5623
    ppm wt
    Mercaptan Sulfur
    Ethyl 57
    Isopropyl 48
    tert-Butyl 45
    N-Propyl 49
    Isobutyl 42
    N-Butyl 43
    Phenyl 35
    Benzyl 33
    Unidentified (n-Amyl) 40
  • N,N′-oxybis(methylene)bis(N,N-dibutylamine) and N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-dibutylamine) Sulfur Speciation ASTM D-5623
  • TABLE 6
    ppm wt Sulfur
    Mercaptan Sulfur Reduction % Reduction
    Ethyl 0.4 56.6 99.3
    Isopropyl 0.4 47.6 99.2
    tert-Butyl 1.0 44.0 97.8
    N-Propyl 0.3 48.7 99.4
    Isobutyl 0.4 41.6 99.0
    N-Butyl 0.4 42.6 99.1
    Phenyl 0.8 34.2 97.7
    Benzyl 0.6 32.4 98.2
    Unidentified 416
  • 1,1′-oxybis(methylene)dipiperidine and bis(piperidinomethoxy)methane Sulfur Speciation ASTM D-5623
  • TABLE 7
    ppm wt Sulfur
    Mercaptan Sulfur Reduction % Reduction
    Ethyl 0.2 56.8 99.6
    Isopropyl <0.2 >47.8 >99.6
    tert-Butyl 0.3 44.7 99.3
    N-Propyl 0.2 48.8 99.6
    Isobutyl <0.2 >41.8 >99.6
    N-Butyl <0.2 >42.8 >99.6
    Phenyl 0.3 34.7 99.1
    Benzyl 0.4 32.6 98.8
    Unidentified 431
  • 4,4′-oxybis(methylene)dimorpholine and bis(morpholinomethoxy)methane Sulfur Speciation ASTM D-5623
  • TABLE 8
    ppm wt Sulfur
    Mercaptan Sulfur Reduction % Reduction
    Ethyl <0.2 >56.8 >99.6
    Isopropyl <0.2 >47.8 >99.6
    tert-Butyl 0.2 44.8 99.6
    N-Propyl <0.2 >48.8 >99.6
    Isobutyl 0.3 41.7 99.3
    N-Butyl 0.2 42.8 99.5
    Phenyl 0.4 34.6 98.9
    Benzyl 1.5 31.5 95.5
    Unidentified 437
  • 1,1′-oxybis(methylene)dipyrrolidine and bis(pyrrolidinomethoxy)methane Sulfur Speciation ASTM D-5623
  • TABLE 9
    ppm wt Sulfur
    Mercaptan Sulfur Reduction % Reduction
    Ethyl 0.2 56.8 99.6
    Isopropyl <0.2 >47.8 >99.6
    tert-Butyl 0.2 44.8 99.6
    N-Propyl 0.2 48.8 99.6
    Isobutyl 0.2 41.8 99.5
    N-Butyl 0.2 42.8 99.5
    Phenyl 0.4 34.6 98.9
    Benzyl <0.2 >32.8 >99.4
    Unidentified 411
  • N,N′-oxybis(methylene)bis(N,N-diethylamine) and N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-diethylamine) Sulfur Speciation ASTM D-5623
  • TABLE 10
    ppm wt Sulfur
    Mercaptan Sulfur Reduction % Reduction
    Ethyl 0.2 56.8 99.6
    Isopropyl 0.2 47.8 99.6
    tert-Butyl 0.3 44.7 99.3
    N-Propyl 0.2 48.8 99.6
    Isobutyl <0.2 >41.8 >99.5
    N-Butyl 0.2 42.8 99.5
    Phenyl <0.2 >34.8 >99.4
    Benzyl <0.2 >32.8 >99.4
    Unidentified 436

    The previous data makes clear that the addition of an alpha-amino ether to a hydrocarbon fluid reduces the mercaptan to a non-volatile sulfur species and thereby scavenges mercaptans from the hydrocarbon fluid.
  • While this invention may be embodied in many different forms, there are shown in the drawings and described in detail herein specific preferred embodiments of the invention. The present disclosure is an exemplification of the principles of the invention and is not intended to limit the invention to the particular embodiments illustrated. All patents, patent applications, scientific papers, and any other referenced materials mentioned herein are incorporated by reference in their entirety. Furthermore, the invention encompasses any possible combination of some or all of the various embodiments described herein and incorporated herein.
  • The above disclosure is intended to be illustrative and not exhaustive. This description will suggest many variations and alternatives to one of ordinary skill in this art. All these alternatives and variations are intended to be included within the scope of the claims where the term “comprising” means “including, but not limited to”. Those familiar with the art may recognize other equivalents to the specific embodiments described herein which equivalents, are also intended to be encompassed by the claims.
  • All ranges and parameters disclosed herein are understood to encompass any and all subranges subsumed therein, and every number between the endpoints. For example, a stated range of “1 to 10” should be considered to include any and all subranges between (and inclusive of) the minimum value of 1 and the maximum value of 10; that is, all subranges beginning with a minimum value of 1 or more, (e.g. 1 to 6.1), and ending with a maximum value of 10 or less, (e.g. 2.3 to 9.4, 3 to 8, 4 to 7), and finally to each number 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10 contained within the range.
  • This completes the description of the preferred and alternate embodiments of the invention. Those skilled in the art may recognize other equivalents to the specific embodiment described herein which equivalents are intended to be encompassed by the claims attached hereto.

Claims (6)

1. A method of reducing the amount of mercaptans in a hydrocarbon fluid comprising contacting the fluid with an effective amount of alpha-amino ether sufficient to convert the mercaptan into a non-volatile species and facilitating the removal of the volatile species from the hydrocarbon liquid thereby reducing the amount of mercaptans released into the vapor phase
2. The method of claim 1 wherein the hydrocarbon fluid is liquid.
3. The method of claim 1 wherein the hydrocarbon fluid is selected from the list consisting of products produced from crude oils such as but not limited to kerosene, diesel fuel, gasoline, naphtha and heavy aromatic naphtha.
4. The method of claim 1 wherein there are different kinds of mercaptans in the hydrocarbon fluid.
5. The method of claim 1 wherein the alpha-amino ether is selected from the list consisting of:
N,N′-oxybis(methylene)bis(N,N-dibutylamine),
N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-dibutylamine),
4,4′-oxybis(methylene)dimorpholine,
bis(morpholinomethoxy)methane,
1,1′-oxybis(methylene)dipiperidine,
bis(piperidinomethoxy)methane,
N,N′-oxybis(methylene)bis(N,N-dipropylamine),
N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-dipropylamine),
1,1′-oxybis(methylene)dipyrrolidine,
bis(pyrrolldinomethoxy)methane,
N,N′-oxybis(methylene)bis(N,N-diethylamine),
N,N′-(methylenebis(oxy)bis(methylene))bis(N,N-diethylamine),
and any combination thereof.
6. The method of claim 1 wherein the ratio of alpha-amino ether molecules to mercaptan molecules is within the range of 1:1000 to 1000:1.
US12/835,881 2010-07-14 2010-07-14 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons Abandoned US20120012505A1 (en)

Priority Applications (15)

Application Number Priority Date Filing Date Title
US12/835,881 US20120012505A1 (en) 2010-07-14 2010-07-14 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
PCT/US2011/043778 WO2012009390A2 (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
HUE11807420A HUE030422T2 (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
RU2013102416/04A RU2557545C2 (en) 2010-07-14 2011-07-13 Application of alpha-aminoethers for removal of mercaptans from hydrocarbons
BR112013000892-0A BR112013000892B1 (en) 2010-07-14 2011-07-13 method to reduce the amount of mercaptans in a hydrocarbon fluid
EP11807420.2A EP2593533B1 (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
ARP110102516A AR082166A1 (en) 2010-07-14 2011-07-13 USE OF A-AMINO ETERES TO ELIMINATE HYDROCARBON MERCAPTANS
MX2013000509A MX2013000509A (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons.
SG2013003009A SG187079A1 (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
PL11807420.2T PL2593533T3 (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
ES11807420.2T ES2593462T3 (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the elimination of hydrocarbon mercaptans
CA2805489A CA2805489C (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
KR1020137003669A KR20130141438A (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
PT118074202T PT2593533T (en) 2010-07-14 2011-07-13 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
JP2013519781A JP5889296B2 (en) 2010-07-14 2011-07-13 Use of alpha amino ethers to remove mercaptans from hydrocarbons

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US12/835,881 US20120012505A1 (en) 2010-07-14 2010-07-14 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons

Publications (1)

Publication Number Publication Date
US20120012505A1 true US20120012505A1 (en) 2012-01-19

Family

ID=45466086

Family Applications (1)

Application Number Title Priority Date Filing Date
US12/835,881 Abandoned US20120012505A1 (en) 2010-07-14 2010-07-14 Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons

Country Status (15)

Country Link
US (1) US20120012505A1 (en)
EP (1) EP2593533B1 (en)
JP (1) JP5889296B2 (en)
KR (1) KR20130141438A (en)
AR (1) AR082166A1 (en)
BR (1) BR112013000892B1 (en)
CA (1) CA2805489C (en)
ES (1) ES2593462T3 (en)
HU (1) HUE030422T2 (en)
MX (1) MX2013000509A (en)
PL (1) PL2593533T3 (en)
PT (1) PT2593533T (en)
RU (1) RU2557545C2 (en)
SG (1) SG187079A1 (en)
WO (1) WO2012009390A2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130245204A1 (en) * 2010-11-30 2013-09-19 Connora Technologies, Inc. Novel agents for reworkable epoxy resins
US10214479B2 (en) 2012-06-05 2019-02-26 Connora Technologies, Inc. Synthesis of and compositions containing diaminoacetals and diaminoketals
US10919839B2 (en) 2017-07-11 2021-02-16 Aditya Birla Chemicals (Usa) Llc Silicon-containing compositions and their methods of use
CN114159946A (en) * 2022-02-11 2022-03-11 河北精致科技有限公司 Absorbent for removing sulfur dioxide in flue gas and application thereof
US20240110091A1 (en) * 2022-09-21 2024-04-04 Championx Usa Inc. Compositions and methods for scavenging sulfur-containing compounds

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5284576A (en) * 1989-08-01 1994-02-08 Petrolite Corporation Method of scavenging hydrogen sulfide from hydrocarbons
EP0882778A2 (en) * 1997-06-04 1998-12-09 Nalco/Exxon Energy Chemicals, L.P. Composition and method for sweetening gaseous or liquid hydrocarbons, aqueous systems and mixtures thereof

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2186398A (en) * 1939-02-07 1940-01-09 Shell Dev Process for removing acid components from hydrocarbon distillates
US3408287A (en) * 1966-04-20 1968-10-29 Universal Oil Prod Co Oxidation of mercaptans
US4405582A (en) * 1982-01-18 1983-09-20 Exxon Research And Engineering Co. Process for selective removal of H2 S from mixtures containing H22 using diaminoether solutions
US4556546A (en) * 1983-05-04 1985-12-03 Air Products And Chemicals, Inc. Bis tertiary amino alkyl derivatives as solvents for acid gas removal from gas streams
ATE179088T1 (en) * 1993-11-09 1999-05-15 Union Carbide Chem Plastic ABSORPTION OF MERCAPTANS
CA2148849A1 (en) * 1994-06-23 1995-12-24 Kishan Bhatia Method of treating sour gas and liquid hydrocarbons
US5698171A (en) * 1996-01-10 1997-12-16 Quaker Chemical Corporation Regenerative method for removing sulfides from gas streams
WO2007021462A2 (en) * 2005-08-09 2007-02-22 Exxonmobil Research And Engineering Company Alkylamino alkyloxy (alcohol) monoalkyl ether for acid gas scrubbing process
RU2349627C2 (en) * 2005-10-27 2009-03-20 Ахматфаиль Магсумович Фахриев Hydrogen sulphide and/or low-molecular mercaptan remover and method of using it
MX2011002377A (en) * 2008-09-02 2011-09-21 Gen Electric Process for removing hydrogen sulfide in crude oil.
US9394396B2 (en) * 2011-06-21 2016-07-19 Baker Hughes Incorporated Hydrogen sulfide scavenger for use in hydrocarbons

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5284576A (en) * 1989-08-01 1994-02-08 Petrolite Corporation Method of scavenging hydrogen sulfide from hydrocarbons
EP0882778A2 (en) * 1997-06-04 1998-12-09 Nalco/Exxon Energy Chemicals, L.P. Composition and method for sweetening gaseous or liquid hydrocarbons, aqueous systems and mixtures thereof

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130245204A1 (en) * 2010-11-30 2013-09-19 Connora Technologies, Inc. Novel agents for reworkable epoxy resins
US9631049B2 (en) * 2010-11-30 2017-04-25 Connora Technologies, Inc. Agents for reworkable epoxy resins
US10214479B2 (en) 2012-06-05 2019-02-26 Connora Technologies, Inc. Synthesis of and compositions containing diaminoacetals and diaminoketals
US11542224B2 (en) 2012-06-05 2023-01-03 Aditya Birla Chemicals (Usa), Inc. Synthesis of and compositions containing diaminoacetals and diaminoketals
US10919839B2 (en) 2017-07-11 2021-02-16 Aditya Birla Chemicals (Usa) Llc Silicon-containing compositions and their methods of use
US11124473B2 (en) 2017-07-11 2021-09-21 Aditya Birla Chemicals (Usa) Llc Salts of diaminoacetals and diaminoketals and their synthesis, and their transformations to diaminoacetals and diaminoketals
US11731932B2 (en) 2017-07-11 2023-08-22 Aditya Birla Chemicals (Usa), Inc. Silicon-containing compositions and their methods of use
US11905228B2 (en) 2017-07-11 2024-02-20 Aditya Birla Chemicals (Usa), Inc. Salts of diaminoacetals and diaminoketals and their synthesis, and their transformations to diaminoacetals and diaminoketals
CN114159946A (en) * 2022-02-11 2022-03-11 河北精致科技有限公司 Absorbent for removing sulfur dioxide in flue gas and application thereof
US20240110091A1 (en) * 2022-09-21 2024-04-04 Championx Usa Inc. Compositions and methods for scavenging sulfur-containing compounds

Also Published As

Publication number Publication date
BR112013000892A2 (en) 2016-05-17
PT2593533T (en) 2016-07-29
HUE030422T2 (en) 2017-05-29
CA2805489C (en) 2018-05-08
RU2557545C2 (en) 2015-07-27
MX2013000509A (en) 2013-02-27
JP5889296B2 (en) 2016-03-22
EP2593533A4 (en) 2014-04-23
AR082166A1 (en) 2012-11-14
BR112013000892B1 (en) 2020-10-20
KR20130141438A (en) 2013-12-26
ES2593462T3 (en) 2016-12-09
WO2012009390A2 (en) 2012-01-19
PL2593533T3 (en) 2016-12-30
EP2593533B1 (en) 2016-07-06
JP2013535530A (en) 2013-09-12
SG187079A1 (en) 2013-02-28
EP2593533A2 (en) 2013-05-22
RU2013102416A (en) 2014-08-20
WO2012009390A3 (en) 2012-04-19
CA2805489A1 (en) 2012-01-19

Similar Documents

Publication Publication Date Title
US20120012507A1 (en) Use of alpha-amino ethers for the removal of hydrogen sulfide from hydrocarbons
US20120012505A1 (en) Use of alpha-amino ethers for the removal of mercaptans from hydrocarbons
US20120152857A1 (en) Non-Nitrogen Sulfide Sweeteners
PH12014501483B1 (en) Sulfide scavengers, methods for making and methods for using them
JP2576952B2 (en) Quaternary ammonium hydroxides as mercaptan scavengers
RU2018145753A (en) COMPOSITION FOR REMOVING SULFUR CONTAINING COMPOUNDS
US20170044444A1 (en) Process for scavenging hydrogen sulfide present in a fluid stream
US8048175B2 (en) Quick removal of mercaptans from hydrocarbons
CA2805402C (en) Improved method of removing hydrogen sulfide
US20230365873A1 (en) Nitrogen-free hydrogen sulphide and mercaptans scavengers
US20240110091A1 (en) Compositions and methods for scavenging sulfur-containing compounds
EP3530775A1 (en) Metal corrosion suppressing method
US11053232B2 (en) 1,3,5-dioxazine derivatives, method of preparation and application thereof as sulfide scavenger

Legal Events

Date Code Title Description
AS Assignment

Owner name: NALCO COMPANY, ILLINOIS

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:COMPTON, DENNIS R.;REEL/FRAME:024681/0661

Effective date: 20100709

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION