US20050085676A1 - Methods for inhibiting hydrate blockage in oil and gas pipelines using betaines and amine oxides - Google Patents
Methods for inhibiting hydrate blockage in oil and gas pipelines using betaines and amine oxides Download PDFInfo
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- US20050085676A1 US20050085676A1 US10/918,210 US91821004A US2005085676A1 US 20050085676 A1 US20050085676 A1 US 20050085676A1 US 91821004 A US91821004 A US 91821004A US 2005085676 A1 US2005085676 A1 US 2005085676A1
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Definitions
- This invention relates to the prevention of gas hydrate blockage in oil and natural gas pipelines containing low-boiling hydrocarbons and water. More specifically, the invention relates to a method of controlling gas hydrate blockage through the addition of various chemical compositions.
- hydrocarbon gas molecules dissolve in water, the hydrogen-bonded network of water molecules encapsulates the gas molecules to form a cage-like structure or hydrate. Higher pressures and lower temperatures foster the formation of these structures. These hydrates grow by encapsulating more and more gaseous molecules to form a crystalline mass. The crystalline mass agglomerates to form a larger mass that can result in a plugged transmission line.
- the hydrocarbon gases that form the majority of the hydrates include methane, ethane, propane, n-butane, iso-butane, n-pentane, iso-pentane, and combinations of these gases.
- thermodynamic hydrate inhibitors such as methanol or one of the glycols
- methanol or one of the glycols have traditionally been used to prevent these hydrate formations.
- These thermodynamic inhibitors are effective at 5-30% (or higher) based on the amount of water.
- the total gas/oil/water productions are also increasing. The use of these thermodynamic inhibitors is not viable in these applications due to logistics.
- Kinetic hydrate inhibitors have been identified to prevent these hydrate formations so that the fluids can be pumped out before a catastrophic hydrate formation occurs.
- the kinetic inhibitors prevent or delay hydrate crystal nucleation and disrupt crystal growth.
- These kinetic hydrate inhibitors contain moieties similar to gas molecules previously mentioned. It is suspected that these kinetic inhibitors prevent hydrate crystal growth by becoming incorporated into the growing hydrate crystals, thereby disrupting further hydrate crystal growth.
- the growing hydrate crystals complete a cage by combining with the partial hydrate-like cages around the kinetic hydrate inhibitor moieties containing gas-like groups.
- These inhibitors are effective with or without the presence of a liquid hydrocarbon phase, but they are typically less effective in preventing the hydrate formation as the production pressure increases.
- kinetic hydrate inhibitors include poly(N-methylacrylamide), poly(N,N-dimethylacrylamide), poly(N-ethylacrylamide), poly(N,N-diethylacrylamide), poly(N-methyl-N-vinylacetamide), poly(2-ethyloxazoline), poly(N-vinylpyrrolidone), and poly(N-vinylcaprolactam).
- anti-agglomerate hydrate inhibitors are effective only in the presence of an oil phase. These inhibitors do not inhibit the formation of gas hydrates to the same level as kinetic inhibitors, rather their primary activity is in preventing the agglomeration of hydrate crystals.
- the oil phase provides a transport medium for the hydrates which are referred to as hydrate slurries so that the overall viscosity of the medium is kept low and can be transported along the pipeline. As such, the hydrate crystals formed in the water-droplets are prevented from agglomerating into a larger crystalline mass.
- Klomp U.S. Pat. No. 5,460,728 teaches the use of alkylated ammonium, phosphonium or sulphonium compounds having three or four alkyl groups in their molecule, at least three of which are independently chosen from the group of normal or branched alkyls having four to six carbon atoms.
- Klomp U.S. Pat. No. 5,648,575 teaches very similar compositions having three or four organic groups in their molecule, at least three of which have at least four carbon atoms, i.e., two normal or branched alkyl groups having at least four carbon atoms and with a further organic moiety containing a chain of at least four carbon atoms.
- Klomp U.S. Pat. No.
- Klug (U.S. Pat. No. 6,369,004 B1) teaches the kinetic inhibition of gas hydrate formation using polymers based on reacting maleic anhydride with one or more amines. These polymers can also be used together with various other substances, called synergists, including tetrabutylammonium salts, tetrapentylammonium salts, tributylamine oxide, tripentylamine oxide, zwitterionic compounds having at least one butyl or pentyl group on the quaternary ammonium nitrogen atom, such as as Bu 3 N + —CH 2 —COO—.
- synergists including tetrabutylammonium salts, tetrapentylammonium salts, tributylamine oxide, tripentylamine oxide, zwitterionic compounds having at least one butyl or pentyl group on the quaternary ammonium nitrogen atom, such as as Bu 3 N + —CH 2
- Rabeony (U.S. Pat. No. 6,015,929) teaches the use of zwitterionic compounds such as R(CH 3 ) 2 N + —(CH 2 ) 4 —SO 3 — as anti-agglomerate hydrate inhibitors.
- the synthesis of this product involves the use of butyl sultone.
- R 1 , R 2 , R 3 and R 4 are organic moieties, wherein R 1 is an alkyl having 4 or 5 carbon atoms, wherein R 2 is hydrogen or an alkyl having from 1 to 4 carbon atoms, and wherein R 3 has 2 to 20 carbon atoms.
- R 3 has an amide functionality.
- R 3 is —[(CH 2 —CHR 5 —O)] n —H, wherein R 5 is selected from a hydrogen, a methyl group, and an ethyl group, and n ranges from 1 to 3.
- R 4 is preferably a normal or branched alkyl group, such as where R 4 is selected from —(CH 2 ) n —, —[CH 2 —(CHR 5 ) n ]— and combinations thereof, n is an integer 1 or greater, and R 5 is an alkyl having from 1 to 3 carbon atoms.
- A is N or P; and m is an integer 0 or 1.
- the method may optionally include adding at least one amine salt to the mixture along with the at least one compound.
- Suitable amine salts include those previously described herein.
- Preferred betaines may be derived from an amine and an acid, wherein the amine is selected from dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, butyldicocoylanine, and mixtures thereof and the acid is selected from chloroacetic acid, acrylic acid, methacrylic acid, and mixtures thereof.
- suitable betaines include, without limitation,
- Suitable amine oxides include, without limitation, butylmethylhexadecylamine, butylmethyltetradecylamine, butylmethyloctadecylamine, butylethylhexadecylamine, butylethyltetradecylamine, butylethyloctadecylamine, dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, dibutylcocoylamine, butylpropylhexadecylamine, butylpropyltetradecylamine, butylpropyloctadecylamine, butylpropyloleoylamine, butyldicocoylamine, and mixtures thereof.
- R 3 is the amide group —[(R 5 —NH—(C ⁇ O)—R 6 )], wherein R 5 is selected from —(CH 2 ) t —, —[CH 2 —CHR 7 ) t ]—, —(CH 2 —CHR 7 O) u —(CH 2 ) t — and combinations thereof, t is an integer 2 to 4, u is 0 or an integer (1 or greater), R 7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R 6 is an organic moiety, such as an alkyl or alkenyl group having 4 to 20 carbon atoms. Most preferably, R 5 is —(CH 2 —CHR 7 O) u —(CH 2 ) t —.
- a preferred method comprises adding to the mixture an effective amount of at least one compound having a formula: (R 1 )(R 2 )(R 3 )A + -[R 4 —(C ⁇ O)] m —O ⁇
- A is N or P
- R 1 is an alkyl having 4 or 5 carbon atoms
- R 2 is hydrogen or an alkyl having from 1 to 4 carbon atoms
- R 3 is the amide group —[(R 5 —NH—(C ⁇ O)—R 6 )], wherein R 5 is selected from —(CH 2 ) t —, —[CH 2 —(CHR 7 ) t ]—, —(CH 2 —CHR 7 O) u —(CH 2 ) t — and combinations thereof, t is an integer 2 to 4, u is 0 or an integer (1 or greater), R 7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R 6 is an alkyl or alkenyl group having 4
- m is 1 and R 4 is —(CH 2 ) n —. While n is an integer 1 or greater, n is preferably an integer from 1 to 10, more preferably from 2 to 4, and most preferably 2.
- R 5 is preferably —(CH 2 —CHR 7 O) u —(CH 2 ) t —, and t is most preferably 3.
- R 1 and R 2 are butyl groups.
- FIG. 1 is a graph of a temperature and pressure profile used in FIGS. 3-17 .
- FIG. 2 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for an untreated mixture of hydrocarbon and water.
- FIG. 3 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% trimethylhexadecylammonium bromide.
- FIG. 4 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethylethylhexadecylammonium bromide
- FIG. 5 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethylbutylhexadecylammonium bromide.
- FIG. 6 is a graph of sensor activation time (a measure of hydrate formation and blockge) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethylbutyloctadecylammonium bromide.
- FIG. 7 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dipropylbutylhexadecylammonium bromide.
- FIG. 8 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dibutylpropylhexadecylammonium bromide.
- FIGS. 9 a and 9 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1% tributylhexadecylammonium bromide, respectively.
- FIG. 10 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethyldihexadecylammonium bromide.
- FIG. 11 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N-dibutyl-cocoamidopropyl carbomethoxy betaine.
- FIG. 12 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N-dibutylamino-cocoamidopropylamine oxide.
- FIG. 13 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N,N-tributyl-cocoamidopropylammonium bromide.
- FIG. 14 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N-dibutylhexadecyl-cocoamidopropylammonium bromide.
- FIGS. 15 a and 15 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1% N,N-dibutylhexadecyltriethoxyarnmonium bromide, respectively.
- FIGS. 16 a and 16 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1% tributylhexadecylphosphonium bromide, respectively.
- FIGS. 17 a and 17 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1%, respectively, of a blend of N,N-dibutyl-cocoamidopropyl carboethoxy betaine and amine salt.
- This invention relates a method and a composition used therein for inhibiting, retarding, mitigating, reducing, controlling and/or delaying formation of hydrocarbon hydrates or agglomerates of hydrates.
- the method may be applied to prevent or reduce or mitigate plugging of conduits, pipes, transfer lines, valves, and other places or equipment where hydrocarbon hydrate solids may form under the conditions.
- inhibitor is used herein in a broad and general sense to mean any improvement in preventing, controlling, delaying, reducing or mitigating the formation, growth and/or agglomeration of hydrocarbon hydrates, particularly light hydrocarbon gas hydrates in any manner, including, but not limited to kinetically, thermodynamically, by dissolution, by breaking up, other mechanisms, or any combinations thereof.
- formation or “forming” relating to hydrates is used herein in a broad and general manner to include, but are not limited to, any formation of hydrate solids from water and hydrocarbon(s) or hydrocarbon gas(es), growth of hydrocarbon hydrate solids, agglomeration of hydrocarbon hydrates, accumulation of hydrocarbon hydrates on surfaces, any deterioration of hydrate solids plugging or other problems in a system and combinations thereof.
- the present method is useful for inhibiting hydrate formation for many hydrocarbons and hydrocarbon mixtures.
- the method is particularly useful for lighter or low-boiling, C 1 -C 5 , hydrocarbon gases or gas mixtures at ambient conditions.
- low-boiling gases include methane, ethane, propane, n-butane, isobutane, isopentane and mixtures thereof.
- Other examples include various natural gas mixtures that are present in many gas and/or oil formations and natural gas liquids (NGL).
- NNL natural gas liquids
- the hydrates of all of these low-boiling hydrocarbons are also referred to as gas hydrates.
- the hydrocarbons may also comprise other compounds including, but not limited to CO 2 , hydrogen sulfide, and other compounds commonly found in gas/oil formations or processing plants, either naturally occurring or used in recovering/processing hydrocarbons from the formation or both, and mixtures thereof.
- the method of the present invention involves contacting a hydrocarbon and water mixture with a suitable compound or composition.
- a suitable compound or composition When an effective amount of the compound is used, hydrate blockage is prevented. In the absence of such effective amount, hydrate blockage is not prevented.
- the contacting may be achieved by a number ways, including mixing, blending with mechanical mixing equipment or devices, stationary mixing setup or equipment, magnetic mixing or other suitable methods, other equipment and means known to one skilled in the art and combinations thereof to provide adequate contact and/or dispersion of the composition in the mixture.
- the contacting can be made in-line or offline or both.
- the various components of the composition may be mixed prior to or during contact, or both.
- the composition or some of its components may be optionally removed or separated mechanically, chemically, or by other methods known to one skilled in the art, or by a combination of these methods after the hydrate formation conditions are no longer present.
- the pressure of the condition is usually at or greater than atmospheric pressure. (i.e. about 101 kPa), preferably greater than about 1 MPa, and more preferably greater than about 5 MPa.
- the pressure in certain formation or processing plants or units could be much higher, say greater than about 20 MPa.
- the present method can be used at any pressure that allows formation of hydrocarbon gas hydrates.
- the temperature of the condition for contacting is usually below, the same as, or not much higher than the ambient or room temperature. Lower temperatures tend to favor hydrate formation, thus requiring the treatment with the composition of the present invention. At much higher temperatures, however, hydrocarbon hydrates are less likely to form, thus obviating the need of carrying out any treatments.
- ammonium, phosphonium, and -sulphonium compounds of the present invention may also be connected through one of the organic side chains, such as represented by —R 4 , to become a pendent group of many oxygen-containing polymers.
- Such polymers include, but not limited to polyacrylate, polymethacrylate, copolymers of acrylate and methacrylate, polyacrylamide, polymethacrylamide, copolymers of acrylamide and methacrylamide, and polymers and copolymers of N-vinylcaprctam.
- ammonium, phosphonium, and sulphonium compounds of the present invention may also be connected through one of the organic side chains, such as represented by —R 4 , to become a pendent group of nitrogen containing polymers, where the nitrogen is on the polymer backbone.
- nitrogen containing polymers and copolymers can be obtained by the Michael addition reaction between polyethylenimine and acrylic or methacrylic acids.
- the copolymers may also include N-vinylcaprolactam, N,N-dimethylacrylamide, N-ethylacrylamide, N-isopropylacrylamide, N-butylacrylamide, or N-tert. butylacrylamide.
- the suitable onium compounds can be attached through the acid moiety using suitable diamino or aminoalcoholic chemicals followed by the salt forming reactions.
- the concentration of the onium compound in a solvent should be in the range from about 5 wt % to about 75 wt %, preferably from about 10 wt % to about 65 wt %.
- the composition may also include liquids.
- liquids are generally solvents for the virgin solid form of the compounds.
- solvents include, but are not limited to, water, simple alcohols like methanol, ethanol, iso-propanol, n-butanol, iso-butanol, 2-ethyl hexanol; glycols like ethylene glycol, 1,2-propylene glycols, 1,3-propylene glycol, and hexylene glycol; ether solvents like ethylene glycol mono butylether (butyl cellosolve), ethylene glycol dibutyl ether, and tetrahydrofuran; ketonic solvents like methylethylketone, diisobutylketone, N-methylpyrrolidone, cyclohexanone; armatic hydrocarbon solvents like xylene and toluene; and mixtures thereof.
- the selection of the suitable solvent or combination of solvents are important to maintain a stable solution of the compounds during storage and to provide stability and reduced viscosity for the inhibitor solutions when they are injected against a pressure of 200 to 25,000 psi.
- the solvent is present in the inhibitor composition in the range from 0 wt % to about 95 wt %, preferably from 20 wt % to about 95 wt %, more preferably from 50 wt % to about 95 wt % of the total composition, based on volume.
- the concentration of the active inhibitor compound is between about 0.01 wt % and about 5 wt % based on the water content in the hydrocarbons and water mixture. More preferably, the inhibitor compound concentration is between about 0.1 wt % and about 3 wt %.
- the present invention may also be used in combination with other means of hydrate inhibition such as the use of thermodynamic or kinetic inhibitors discussed in the background section.
- These other hydrate inhibitors may be of the same or different type of hydrate inhibitor used in the composition. If mixtures of hydrate inhibitors are used, the mixture may be added to the hydrocarbon and water containing process stream through a single port or multiple ports. Alternatively, individual hydrate inhibitors may be added at separate ports to the process stream.
- the present invention may also be used in combination with other oil field flow assurance compounds such as, but not limited to, corrosion inhibitors, scale inhibitors, paraffin inhibitors, and asphaltene inhibitors.
- the hydrate inhibitors may also be used in combination with emulsion breakers or water clarifiers.
- Certain simple quaternary ammonium and phosphonium compounds are suitable for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, by adding to the mixture an effective amount of at least one hydrate inhibitor compound.
- One preferred family of hydrate inhibitor compounds has the formula:
- R 1 is selected from hydrogen and normal or branched alkyls having from 1 to 3 carbon atoms.
- R 2 is selected from normal or branched alkyls having from 1 to 4 carbon atoms, preferably exactly 4 carbon atoms. It should be recognized that R 1 and R 2 may be the same or different, such as where R 1 and R 2 each have exactly one carbon atom.
- R 3 is an organic moiety having 4 or 5 carbon atoms.
- R 4 is an organic moiety having from 2 to 20 carbon atoms.
- R 4 may be selected from alkyl, alkenyl, aryl, arylalkyl, arylalkenyl, alkylaryl, alkenylaryl, glycol and combinations thereof.
- R 4 may include one or more heteroatoms selected from oxygen, nitrogen, sulfur and combinations thereof.
- R 4 may be chemically bound to a polymer.
- R 4 is —[(CH 2 —CHR 5 —O)] n —H
- R 5 is selected from a hydrogen, a methyl group, and an ethyl group, and n ranges from 1 to 3.
- A is a nitrogen atom (N) or a phosphorus atom (P).
- X ⁇ is an anion.
- X ⁇ may be selected from hydroxide, carboxylate, halide, sulfate, organic sulphonate, and combinations thereof.
- the X ⁇ anion may be a halide ion selected from bromide, chloride, and combinations thereof.
- the at least one compound is the product of a reaction between an organic halide having one of R 1 , R 2 , R 3 , and R 4 and an amine or phosphene having the other three of R 1 , R 2 , R 3 , and R 4 .
- the at least one compound may be the product of a reaction between butyl bromide and an N,N-dimethyl-alkylamine having between 10 and 20 carbon atoms.
- the N,N-dimethyl-alkylamine may be N,N-dimethyl-hexadecylamine.
- the method may be performed at any pressure, such as between 100 and 10,000 psi or even greater than 10,000 psi.
- the method may include adding at least one amine salt to the mixture along with the at least one compound.
- the amine salt may include a cation moiety that is an amine selected from ammonia, dimethylamine, diethylamine, di-n-propylamine, trimethylamine, triethylamine, tri-n-propylamine, tri-iso-propylamine, ethanolamine, diethylethanolamine, triethanolamine, methyl ethanolamine, ethyl ethanolamine, propyl ethanolamine, methyl diethanolamine, ethyl diethanolamine, dimethyl ethanolamine, diethanolamine, dibutylethanolamine, dipropylethanolamine, dibutylpropanolamine, dipropylpropanolamine, morpholine, N-methylmorpholine, N-ethylmorpholine, N-propylmorpholine, dibutylethanolamine, N,N-dibutyl-cocoamidopropylamine,
- the amine salt may include an anionic moiety that is an acid selected from carboxylic acids and inorganic acids.
- carboxylic acids include, with limitation, formic acid, acetic acid, propionic acid, butyric acid, glycolic acid, malonic acid, succinic acid, acrylic acid, methacrylic acid, trifluoroacetic acid, methane sulfonic acid and mixtures thereof.
- Suitable inorganic acids include, without limitation, nitric acid, hydrogen chloride, hydrogen bromide, and mixtures thereof.
- the at least one compound may, for example, include at least one of the following: dimethylbutylhexadecylammonium salt; dimethylbutyloctadecylammonium bromide, dimethylbutyldodecylammonium salt; at least one ammonium salt having an ammonium compound selected from trimethylhexadecylammonium, dimethylethylhexadecylammonium, dimethylbutyloctadecylammonium, dimethylbutylhexadecylammonium, dimethylbutyldodecylammonium, dimethylbutyltetradecylammonium, propyldibutylhexadecylammonium, dipropylbutylhexadecylammonium, and mixtures thereof; or at least one phosphonium salt having a phosphonium compound selected from trimethylhexadecylphosphonium, dimethyle
- the hydrate inhibitor compound is preferably mixed with a solvent, for example water, simple alcohols, glycols, ethers, ketonic liquids, aromatic hydrocarbons, and combinations thereof. More specifically, preferred solvents include water, methanol, ethanol, iso-propanol, n-butanol, iso-butanol, 2-ethyl hexanol, ethylene glycol, 1,2-prpylene glycols, 1,3-propylene glycol, hexylene glycol, ethylene glycol mono butylether (butyl cellosolve), ethylene glycol dibutyl ether, tetrahydrofuran, methylethylketone, methylisobutylketone, diisobutylketone, N-methylpyrrolidone, cyclohexanone, xylene, toluene, and combinations thereof.
- a solvent for example water, simple alcohols, glycols, ethers, ketonic liquids, aromatic
- R 1 , R 2 , R 3 and R 4 are organic moieties, wherein R 1 is an alkyl having 4 or 5 carbon atoms, and wherein R 2 is hydrogen or an alkyl having from 1 to 4 carbon atoms, and wherein R 3 has 2 to 20 carbon atoms.
- R 3 has an amide functionality.
- R 3 is —[(CH 2 —CHR 5 —O)] n —H, wherein R 5 is selected from a hydrogen, a methyl group, and an ethyl group, and n ranges from 1 to 3.
- R 4 is preferably a normal or branched alkyl group, such as where R 4 is selected from —(CH 2 ) n —, —[CH 2 —(CHR 5 ) n ]— and combinations thereof, n is an integer 1 or greater, and R 5 is an alkyl having from 1 to 3 carbon atoms.
- A is N or P; and m is an integer 0 or 1.
- the method may optionally include adding at least one amine salt to the mixture along with the at least one compound.
- Suitable amine salts include those previously described herein.
- Preferred betaines may be derived from an amine and an acid, wherein the amine is selected from dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, butyldicocoylamine, and mixtures thereof and the acid is selected from chloroacetic acid, acrylic acid, methacrylic acid, and mixtures thereof.
- suitable betaines include, without limitation,
- Suitable amine oxides include, without limitation, butylmethylhexadecylamine, butylmethyltetradecylamine, butylmethyloctadecylamine, butylethylhexadecylamine, butylethyltetradecylamine, butylethyloctadecylamine, dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, dibutylcocoylamine, butylpropylhexadecylamine, butylpropyltetradecylamine, butylpropyloctadecylamine, butylpropyloleoylamine, butyldicocoylamine, and mixtures thereof.
- R 1 , R 2 and R 3 is the amide group —[(R 5 —NH—(C ⁇ O)—R 6 )], R 5 is selected from —(CH 2 ) t —, —[CH 2 —(CHR 7 ) t ]—, —(CH 2 —CHR 7 O) u —(CH 2 ) t — and combinations thereof, t is an integer 2 to 4, u is 0 or an integer (1 or greater), R 7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R 6 is an organic moiety, such as an alkyl or alkenyl group, having 4 to 20 carbon atoms. Most preferably, R 5 is —(CH 2 —CHR 7 O) u —(CH 2 ) t —.
- a preferred method comprises adding to the mixture an effective amount of at least one compound having a formula: (R 1 )(R 2 )(R 3 )A + -[R 4 —(C ⁇ O)] m —O ⁇
- A is N or P
- R 1 is an alkyl having 4 or 5 carbon atoms
- R 2 is hydrogen or an alkyl having from 1 to 4 carbon atoms
- R 3 is the amide group —[(R 5 —NH—(C ⁇ O)—R 6 )], wherein R 5 is selected from —(CH 2 ) t —, —[CH 2 —(CHR 7 ) t ]—, —(CH 2 —CHR 7 O) u —(CH 2 ) t — and combinations thereof, t is an integer 2 to 4, u is 0 or an integer (1 or greater)
- R 7 is hydrogen or an alkyl having from 1 to 3 carbon atoms
- R 6 is an organic moiety, such as an alky
- m is 1 and R 4 is —(CH 2 ) n —. While n is an integer 1 or greater, n is preferably an integer from 1 to 10, more preferably from 2 to 4, and most preferably 2.
- R 5 is preferably —(CH 2 —CHR 7 O) u —(CH 2 ) t —, and R 7 is hydrogen, u is 0 or 1, and t is most preferably 3.
- R 1 and R 2 are butyl groups.
- the method may include adding to the mixture an effective amount of at least one amide compound having a formula: where: R 1 , R 2 , R 4 , and R 5 are organic moieties; R 1 is an alkyl having from 4 to 5 carbon atoms; R 2 is hydrogen or an alkyl having from 1 to 4 carbon atoms; R 4 is selected from —(CH 2 ) t —, —[CH 2 —(CHR 6 ) t ]—(CH 2 —CHR 6 O) u —(CH 2 ) t — and combinations thereof, t is an integer 2 to 4, u is 0 or an integer (1 or greater), R 6 is hydrogen or an alkyl having from 1 to 3 carbon atoms; R 5 is an organic moiety, such as alkyl or alkenyl group, having 4 to 20 carbon atoms; A is N or P; X ⁇ is an anion; and a is 0 or 1.
- R 3 is selected from —[(CH 2 )(CHR 7 ) b (C ⁇ O)] c —O ⁇ , —[(CH 2 CH 2 )—(SO 2 )]—O ⁇ , —[(CH 2 CH(OH)CH 2 )—(SO 2 )]—O ⁇ , —[(CH 2 ) n —(C ⁇ S)]—S ⁇ and combinations thereof, wherein b is 0 or 1, c is 0 or 1, n is 2 or 3, and R 7 is hydrogen or methyl group.
- R 3 is selected from hydrogen, organic moieties having from 1 to 20 carbon atoms, and combinations thereof.
- R 3 is the same as the group containing the amide functionality.
- the X anion is preferably selected from hydroxide, carboxylate, halide, sulphate, organic sulphonate, and combinations thereof.
- Suitable halide ions include, without limitation, bromide, chloride, and combinations thereof.
- R 3 is hydrogen, a is 1, and the anion X ⁇ is selected from hydroxide, carboxylate, halide, sulphate, organic sulphonate, and combinations thereof.
- the at least one amide compound is the reaction product of an N,N-dialkyl-aminoalkylamine with an ester or glyceride.
- the ester or glyceride is derived from a plant source or animal source selected from coconut oil, tallow oil, vegetable oil, and combinations thereof.
- the method may further comprise adding at least one amine salt to the mixture along with the at least one compound.
- Suitable amine salts include those previously described herein.
- the at least one compound may be mixed with the solvents previously described herein.
- the at least one compound includes a product prepared by the reaction of an amine selected from (3-dialkylamino)propylamine and (3-dialkylamino)ethylamine with vegetable oil or tallow oil followed by reacting with a reactant selected from an organic halide, such as an alkyl halide, having from 4 to 20 carbon atoms, hydrogen peroxide, and an acid, wherein the acid is selected from mineral acids, formic acid, acetic acid, chloroacetic acid, propionic acid, acrylic acid, and methacrylic acid, and wherein the dialkyl of the (3-dialkylamino)propylamine includes two alkyl groups independently selected from methyl, ethyl, propyl, butyl, morpholine, piperidine, and combinations thereof.
- an organic halide such as an alkyl halide, having from 4 to 20 carbon atoms, hydrogen peroxide
- the acid is selected from mineral acids, formic acid, acetic acid, chloroacetic acid
- the present invention provides yet another method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water.
- This method comprises adding to the mixture an effective amount of at least one compound having a formula: wherein: A is N or P; R 1 is a normal or branched alkyl group containing at least 4 carbon atoms; R 2 is hydrogen or an alkyl group containing from 1 to 4 carbon atoms; R 4 is selected from hydrogen, methyl and ethyl; R 5 is either H or an organic moiety, such as an alkyl chain, containing from 4 to 20 carbon atoms; (X ⁇ ) a is an anion; and a is 0 or 1; n is 1 to 3; and m is 0 or 1.
- R 3 is selected from —[(CH 2 )(CH) b (C ⁇ O)] c —O ⁇ , —[(CH 2 CH 2 )—(SO 2 )]—, —[(CH 2 CH(OH)CH 2 )—(SO 2 )]—O ⁇ , and combinations thereof; wherein b is 0 or 1; c is 0 or 1; and R 6 is selected from hydrogen, methyl, ethyl and combinations thereof.
- R 3 is selected from hydrogen, an organic moiety, such as an alkyl or alkenyl group, having from 1 to 20 carbon atoms, and combinations thereof.
- the X ⁇ anion is preferably selected from hydroxide, carboxylate, halide, sulphate, organic sulphonate, and combinations thereof.
- the preferred halide ions include, without limitation, bromide, chloride, and combinations thereof.
- the method may further comprise adding at least one amine salt to the mixture along with the at least one compound.
- Suitable amine salts include those previously described herein.
- the at least one compound may be mixed with the solvents previously described herein.
- the at least one compound includes a product of the reaction of N-alkylamine or N,N-dialkylamine with ethylene oxide, propylene oxide or combinations thereof, followed by reacting with at least one alkyl halide having from 1 to 20 carbon atoms.
- the method comprises introducing ester moieties by trans-esterfication of hydroxy terminals in the alkoxy chains using methyl esters of fatty acids.
- the present invention provides still another method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water.
- This method comprises adding to the mixture an effective amount of at least one compound having a formula: wherein: A is N or P; R 1 is an alkyl group containing at least 4 carbon atoms; R 2 is hydrogen or an alkyl group containing from 1 to 4 carbon atoms; R 4 is an organic moiety, such as an alkyl, alkenyl or aryl group, containing from 4 to 20 carbon atoms, most preferably 8 to 16 carbon atoms; (X) ⁇ is an anion selected from hydroxide, chloride, bromide, sulfate, sulfonate, or carboxylate; and a is 0 or 1.
- R 3 is selected from —[(CH 2 )(CH 6 ) b (C ⁇ O)] c —O ⁇ , —[(CH 2 CH 2 )—(SO 2 )]—O ⁇ , —[(CH 2 CH(OH)CH 2 )—(SO 2 )]—O ⁇ , and combinations thereof, wherein b is 0 or 1, c is 0 or 1, and R 6 is selected from hydrogen and methyl.
- R 3 is selected from hydrogen, an organic moiety, such as an alkyl or alkenyl group, having from 4 to 20 carbon atoms, and combinations thereof.
- the at least one compound includes a product of the Michael addition reaction of alkyl or N,N-dialkyl amine with an acrylate, followed by reacting with at least one organic halide, such as an alkyl halide, having from 1 to 20 carbon atoms.
- the at least one compound includes a product of the reaction of a tertiary amine containing the ester moiety with chloroacetic acid, acrylic acid or methacrylic acid.
- the at least one compound includes a product of the reaction of a tertiary amine containing the ester moiety with hydrogen peroxide.
- the “Rocking Arm” test apparatus used for these evaluations contains “pressure cells” made of sapphire tubing containing a stainless steel ball. The cells are placed in a rack, and the rack gently rocked forward, then back. The cells are charged with liquids prior to being placed in the rack and then immersed in an insulated tank containing water. Once the cells are immersed in the bath they can then be charged with gas and the experiment begun. Sensors are used to monitor ball movement within the cells, with one sensor placed near each end of the cell. The ball falling time is recorded. This data is referred to as Sensor Activation Time and they are noted as Sensor-1 and Sensor-2.
- the cells were charged with oil to brine ratios ranging from 10:1 to 1:10. A typical oil to brine ratio is about 2:1.
- the hydrate inhibitors were mixed with the solutions in the cells.
- the cells were purged with a synthetic natural gas blend, then charged with gas to the desired pressure and allowed to equilibrate at the pre-determined temperature.
- the bath was then cooled to a lower pre-determined temperature at specified rates.
- the following parameters were recorded: (1) bath temperature, (2) individual cell pressure, (3) sensor activation time, and (4) visual observations. Hydrate formation or blockage is indicated by either an increase in sensor activation time (SAT) or visual observation of hydrate particles sticking to the walls.
- SAT sensor activation time
- the results can indicate: (1) a viscosity increase due to the formation of hydrates, which can also be due in part to oil effects; (2) a partial blockage; and (3) a complete blockage.
- the inhibitor evaluations were conducted using a synthetic natural gas blend shown in Table 1.
- the composition of the synthetic salt water (brine) used for the inhibitor evaluations is presented in Table 2.
- a typical temperature-pressure profile is presented in FIG. 1 .
- a list of inhibitor compounds that were evaluated and the results of the evaluations are summarized in Table 3 and in FIGS. 2-17 .
- Each of these inhibitor compounds was tested as an inhibitor solution at a 3 volume % dosage rate.
- Each inhibitor solution was made up of 40 wt % inhibitor compound and 60 wt % solvent, wherein the solvent itself was a mixture of half xylene and half n-butanol.
- the terms “at least one” and “one or more” are used interchangeably.
- the term “one” or “single” shall be used to indicate that one and only one of something is intended. Similarly, other specific integer values, such as “two,” are used when a specific number of things is intended.
- the terms “preferably,” “preferred,” “prefer,” “optionally,” “may,” and similar terms are used to indicate that an item, condition or step being referred to is an optional (not required) feature of the invention.
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- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
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Abstract
A method and a betaine or amine oxide composition used therein for inhibiting, retarding, mitigating, reducing, controlling and/or delaying formation of hydrocarbon hydrates or agglomerates of hydrates. The method may be applied to prevent or reduce or mitigate plugging of conduits, pipes, transfer lines, valves, and other places or equipment where hydrocarbon hydrate solids may form under the conditions. At least one betaine or amine oxide compound is added into the process stream, where the compound may be mixed with another compound selected from amino alcohols, esters, quaternary ammonium, phosphonium or sulphonium salts, amides, simple amine salts, and combinations thereof.
Description
- This application claims priority of U.S. provisional patent application 60/513,311 filed on Oct. 21, 2003.
- 1. Field of the Invention
- This invention relates to the prevention of gas hydrate blockage in oil and natural gas pipelines containing low-boiling hydrocarbons and water. More specifically, the invention relates to a method of controlling gas hydrate blockage through the addition of various chemical compositions.
- 2. Background of the Related Art
- When hydrocarbon gas molecules dissolve in water, the hydrogen-bonded network of water molecules encapsulates the gas molecules to form a cage-like structure or hydrate. Higher pressures and lower temperatures foster the formation of these structures. These hydrates grow by encapsulating more and more gaseous molecules to form a crystalline mass. The crystalline mass agglomerates to form a larger mass that can result in a plugged transmission line. The hydrocarbon gases that form the majority of the hydrates include methane, ethane, propane, n-butane, iso-butane, n-pentane, iso-pentane, and combinations of these gases.
- Thermodynamic hydrate inhibitors, such as methanol or one of the glycols, have traditionally been used to prevent these hydrate formations. These thermodynamic inhibitors are effective at 5-30% (or higher) based on the amount of water. As oil companies are exploring new production in deep waters, the total gas/oil/water productions are also increasing. The use of these thermodynamic inhibitors is not viable in these applications due to logistics.
- Kinetic hydrate inhibitors have been identified to prevent these hydrate formations so that the fluids can be pumped out before a catastrophic hydrate formation occurs. The kinetic inhibitors prevent or delay hydrate crystal nucleation and disrupt crystal growth. These kinetic hydrate inhibitors contain moieties similar to gas molecules previously mentioned. It is suspected that these kinetic inhibitors prevent hydrate crystal growth by becoming incorporated into the growing hydrate crystals, thereby disrupting further hydrate crystal growth. The growing hydrate crystals complete a cage by combining with the partial hydrate-like cages around the kinetic hydrate inhibitor moieties containing gas-like groups. These inhibitors are effective with or without the presence of a liquid hydrocarbon phase, but they are typically less effective in preventing the hydrate formation as the production pressure increases. Examples of kinetic hydrate inhibitors include poly(N-methylacrylamide), poly(N,N-dimethylacrylamide), poly(N-ethylacrylamide), poly(N,N-diethylacrylamide), poly(N-methyl-N-vinylacetamide), poly(2-ethyloxazoline), poly(N-vinylpyrrolidone), and poly(N-vinylcaprolactam).
- Unlike the kinetic hydrate inhibitors, anti-agglomerate hydrate inhibitors are effective only in the presence of an oil phase. These inhibitors do not inhibit the formation of gas hydrates to the same level as kinetic inhibitors, rather their primary activity is in preventing the agglomeration of hydrate crystals. The oil phase provides a transport medium for the hydrates which are referred to as hydrate slurries so that the overall viscosity of the medium is kept low and can be transported along the pipeline. As such, the hydrate crystals formed in the water-droplets are prevented from agglomerating into a larger crystalline mass.
- Examples of several chemicals acting as anti-agglomerate hydrate inhibitors have been reported in U.S. Pat. Nos. 5,460,728; 5,648,575; 5,879,561; and 6,596,911. These patents teach the use of quaternary ammonium salts having at least three alkyl groups with four or five carbon atoms and a long chain hydrocarbon group containing 8-20 atoms. Exemplary compositions include tributylhexadecylphosphonium bromide and tributylhexadecylammonium bromide.
- More specifically, Klomp (U.S. Pat. No. 5,460,728) teaches the use of alkylated ammonium, phosphonium or sulphonium compounds having three or four alkyl groups in their molecule, at least three of which are independently chosen from the group of normal or branched alkyls having four to six carbon atoms. Klomp (U.S. Pat. No. 5,648,575) teaches very similar compositions having three or four organic groups in their molecule, at least three of which have at least four carbon atoms, i.e., two normal or branched alkyl groups having at least four carbon atoms and with a further organic moiety containing a chain of at least four carbon atoms. Klomp (U.S. Pat. No. 5,879,561) teaches the use of alkylated ammonium or phosphonium compounds having four alkyl groups, two of which are independently normal or branched alkyls having four or five carbon atoms and two more of which independently represent organic moieties having at least eight carbon atoms.
- Klug (U.S. Pat. No. 6,369,004 B1) teaches the kinetic inhibition of gas hydrate formation using polymers based on reacting maleic anhydride with one or more amines. These polymers can also be used together with various other substances, called synergists, including tetrabutylammonium salts, tetrapentylammonium salts, tributylamine oxide, tripentylamine oxide, zwitterionic compounds having at least one butyl or pentyl group on the quaternary ammonium nitrogen atom, such as as Bu3N+—CH2—COO—. However, kinetic inhibitors are not effective as the pipeline pressure increases.
- Rabeony (U.S. Pat. No. 6,015,929) teaches the use of zwitterionic compounds such as R(CH3)2N+—(CH2)4—SO3— as anti-agglomerate hydrate inhibitors. The synthesis of this product involves the use of butyl sultone.
- However, there remains a need for hydrate inhibitor compounds that effectively prevent agglomeration of hydrates in oil and gas transportation and handling processes. It would be desirable to identify hydrate inhibitor compounds that are effective at higher pressures and/or lower temperatures such as those encounter in deep water production. It would be even more desirable if the same compounds had increased biodegradability.
- Other quaternary ammonium and phosphonium compounds, known as betaines and amine oxides, have also been found to be suitable for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, by adding to the mixture an effective amount of at least one hydrate inhibitor compound having the formula:
(R1)(R2)(R3)A+-[R4—(C═O)]m—O− - In accordance with the invention, R1, R2, R3 and R4 are organic moieties, wherein R1 is an alkyl having 4 or 5 carbon atoms, wherein R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms, and wherein R3 has 2 to 20 carbon atoms. Optionally, R3 has an amide functionality. In one embodiment, R3 is —[(CH2—CHR5—O)]n—H, wherein R5 is selected from a hydrogen, a methyl group, and an ethyl group, and n ranges from 1 to 3. R4 is preferably a normal or branched alkyl group, such as where R4 is selected from —(CH2)n—, —[CH2—(CHR5)n]— and combinations thereof, n is an
integer 1 or greater, and R5 is an alkyl having from 1 to 3 carbon atoms. - A is N or P; and m is an
integer - The method may optionally include adding at least one amine salt to the mixture along with the at least one compound. Suitable amine salts include those previously described herein.
- Preferred betaines may be derived from an amine and an acid, wherein the amine is selected from dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, butyldicocoylanine, and mixtures thereof and the acid is selected from chloroacetic acid, acrylic acid, methacrylic acid, and mixtures thereof. Whether derived in this or a different manner, suitable betaines include, without limitation,
- dibutylhexadecylcarboxypropyl, dibutyltetradecylcarboxypropyl, dibutyloctadecylcarboxypropyl, dibutyloleylcarboxypropyl, butyldicocoylcarboxypropyl, dibutylhexadecylcarboxyethyl, dibutyltetradecylcarboxyethyl, dibutyloctadecylcarboxyethyl, dibutyloleylcarboxyethyl, butyldicocoylcarboxyethyl, dibutylhexadecylcarboxymethyl, dibutyltetradecylcarboxymethyl, dibutyloctadecylcarboxymethyl, dibutyloleylcarboxymethyl, butyldicocoylcarboxymethyl and mixtures thereof. Suitable amine oxides include, without limitation, butylmethylhexadecylamine, butylmethyltetradecylamine, butylmethyloctadecylamine, butylethylhexadecylamine, butylethyltetradecylamine, butylethyloctadecylamine, dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, dibutylcocoylamine, butylpropylhexadecylamine, butylpropyltetradecylamine, butylpropyloctadecylamine, butylpropyloleoylamine, butyldicocoylamine, and mixtures thereof.
- In one embodiment, R3 is the amide group —[(R5—NH—(C═O)—R6)], wherein R5 is selected from —(CH2)t—, —[CH2—CHR7)t]—, —(CH2—CHR7O)u—(CH2)t— and combinations thereof, t is an
integer 2 to 4, u is 0 or an integer (1 or greater), R7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R6 is an organic moiety, such as an alkyl or alkenyl group having 4 to 20 carbon atoms. Most preferably, R5 is —(CH2—CHR7O)u—(CH2)t—. - A preferred method comprises adding to the mixture an effective amount of at least one compound having a formula:
(R1)(R2)(R3)A+-[R4—(C═O)]m—O−
where: A is N or P; R1 is an alkyl having 4 or 5 carbon atoms; R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms; R3 is the amide group —[(R5—NH—(C═O)—R6)], wherein R5 is selected from —(CH2)t—, —[CH2—(CHR7)t]—, —(CH2—CHR7O)u—(CH2)t— and combinations thereof, t is aninteger 2 to 4, u is 0 or an integer (1 or greater), R7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R6 is an alkyl or alkenyl group having 4 to 20 carbon atoms; R4 is selected from —(CH2)n—, —[CH2—(CHR8)n]— and combinations thereof, wherein n is aninteger 1 or greater and R8 is an alkyl having from 1 to 3 carbon atoms; and m is aninteger integer 1 or greater, n is preferably an integer from 1 to 10, more preferably from 2 to 4, and most preferably 2. R5 is preferably —(CH2—CHR7O)u—(CH2)t—, and t is most preferably 3. In one embodiment, R1 and R2 are butyl groups. -
FIG. 1 is a graph of a temperature and pressure profile used inFIGS. 3-17 . -
FIG. 2 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for an untreated mixture of hydrocarbon and water. -
FIG. 3 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% trimethylhexadecylammonium bromide. -
FIG. 4 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethylethylhexadecylammonium bromide -
FIG. 5 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethylbutylhexadecylammonium bromide. -
FIG. 6 is a graph of sensor activation time (a measure of hydrate formation and blockge) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethylbutyloctadecylammonium bromide. -
FIG. 7 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dipropylbutylhexadecylammonium bromide. -
FIG. 8 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dibutylpropylhexadecylammonium bromide. -
FIGS. 9 a and 9 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1% tributylhexadecylammonium bromide, respectively. -
FIG. 10 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% dimethyldihexadecylammonium bromide. -
FIG. 11 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N-dibutyl-cocoamidopropyl carbomethoxy betaine. -
FIG. 12 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N-dibutylamino-cocoamidopropylamine oxide. -
FIG. 13 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N,N-tributyl-cocoamidopropylammonium bromide. -
FIG. 14 is a graph of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% N,N-dibutylhexadecyl-cocoamidopropylammonium bromide. -
FIGS. 15 a and 15 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1% N,N-dibutylhexadecyltriethoxyarnmonium bromide, respectively. -
FIGS. 16 a and 16 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1% tributylhexadecylphosphonium bromide, respectively. -
FIGS. 17 a and 17 b are graphs of sensor activation time (a measure of hydrate formation and blockage) as a function of time for a mixture of hydrocarbon and water treated with 3% and 1%, respectively, of a blend of N,N-dibutyl-cocoamidopropyl carboethoxy betaine and amine salt. - This invention relates a method and a composition used therein for inhibiting, retarding, mitigating, reducing, controlling and/or delaying formation of hydrocarbon hydrates or agglomerates of hydrates. The method may be applied to prevent or reduce or mitigate plugging of conduits, pipes, transfer lines, valves, and other places or equipment where hydrocarbon hydrate solids may form under the conditions.
- The term “inhibiting” is used herein in a broad and general sense to mean any improvement in preventing, controlling, delaying, reducing or mitigating the formation, growth and/or agglomeration of hydrocarbon hydrates, particularly light hydrocarbon gas hydrates in any manner, including, but not limited to kinetically, thermodynamically, by dissolution, by breaking up, other mechanisms, or any combinations thereof.
- The term “formation” or “forming” relating to hydrates is used herein in a broad and general manner to include, but are not limited to, any formation of hydrate solids from water and hydrocarbon(s) or hydrocarbon gas(es), growth of hydrocarbon hydrate solids, agglomeration of hydrocarbon hydrates, accumulation of hydrocarbon hydrates on surfaces, any deterioration of hydrate solids plugging or other problems in a system and combinations thereof.
- The present method is useful for inhibiting hydrate formation for many hydrocarbons and hydrocarbon mixtures. The method is particularly useful for lighter or low-boiling, C1-C5, hydrocarbon gases or gas mixtures at ambient conditions. Non-limiting examples of such “low-boiling” gases include methane, ethane, propane, n-butane, isobutane, isopentane and mixtures thereof. Other examples include various natural gas mixtures that are present in many gas and/or oil formations and natural gas liquids (NGL). The hydrates of all of these low-boiling hydrocarbons are also referred to as gas hydrates. The hydrocarbons may also comprise other compounds including, but not limited to CO2, hydrogen sulfide, and other compounds commonly found in gas/oil formations or processing plants, either naturally occurring or used in recovering/processing hydrocarbons from the formation or both, and mixtures thereof.
- The method of the present invention involves contacting a hydrocarbon and water mixture with a suitable compound or composition. When an effective amount of the compound is used, hydrate blockage is prevented. In the absence of such effective amount, hydrate blockage is not prevented.
- The contacting may be achieved by a number ways, including mixing, blending with mechanical mixing equipment or devices, stationary mixing setup or equipment, magnetic mixing or other suitable methods, other equipment and means known to one skilled in the art and combinations thereof to provide adequate contact and/or dispersion of the composition in the mixture. The contacting can be made in-line or offline or both. The various components of the composition may be mixed prior to or during contact, or both. As discussed, if needed or desired, the composition or some of its components may be optionally removed or separated mechanically, chemically, or by other methods known to one skilled in the art, or by a combination of these methods after the hydrate formation conditions are no longer present.
- Because the present invention is particularly suitable for lower boiling hydrocarbons or hydrocarbon gases at ambient conditions, the pressure of the condition is usually at or greater than atmospheric pressure. (i.e. about 101 kPa), preferably greater than about 1 MPa, and more preferably greater than about 5 MPa. The pressure in certain formation or processing plants or units could be much higher, say greater than about 20 MPa. There is no specific high-pressure limit. The present method can be used at any pressure that allows formation of hydrocarbon gas hydrates.
- The temperature of the condition for contacting is usually below, the same as, or not much higher than the ambient or room temperature. Lower temperatures tend to favor hydrate formation, thus requiring the treatment with the composition of the present invention. At much higher temperatures, however, hydrocarbon hydrates are less likely to form, thus obviating the need of carrying out any treatments.
- The ammonium, phosphonium, and -sulphonium compounds of the present invention may also be connected through one of the organic side chains, such as represented by —R4, to become a pendent group of many oxygen-containing polymers. Such polymers include, but not limited to polyacrylate, polymethacrylate, copolymers of acrylate and methacrylate, polyacrylamide, polymethacrylamide, copolymers of acrylamide and methacrylamide, and polymers and copolymers of N-vinylcaprctam.
- The ammonium, phosphonium, and sulphonium compounds of the present invention may also be connected through one of the organic side chains, such as represented by —R4, to become a pendent group of nitrogen containing polymers, where the nitrogen is on the polymer backbone. Such nitrogen containing polymers and copolymers can be obtained by the Michael addition reaction between polyethylenimine and acrylic or methacrylic acids. The copolymers may also include N-vinylcaprolactam, N,N-dimethylacrylamide, N-ethylacrylamide, N-isopropylacrylamide, N-butylacrylamide, or N-tert. butylacrylamide. The suitable onium compounds can be attached through the acid moiety using suitable diamino or aminoalcoholic chemicals followed by the salt forming reactions.
- Based on the total weight of the composition, the concentration of the onium compound in a solvent should be in the range from about 5 wt % to about 75 wt %, preferably from about 10 wt % to about 65 wt %.
- In addition to the ammonium, phosphonium and sulphonium compounds, the composition may also include liquids. These liquids are generally solvents for the virgin solid form of the compounds. Such solvents include, but are not limited to, water, simple alcohols like methanol, ethanol, iso-propanol, n-butanol, iso-butanol, 2-ethyl hexanol; glycols like ethylene glycol, 1,2-propylene glycols, 1,3-propylene glycol, and hexylene glycol; ether solvents like ethylene glycol mono butylether (butyl cellosolve), ethylene glycol dibutyl ether, and tetrahydrofuran; ketonic solvents like methylethylketone, diisobutylketone, N-methylpyrrolidone, cyclohexanone; armatic hydrocarbon solvents like xylene and toluene; and mixtures thereof. The selection of the suitable solvent or combination of solvents are important to maintain a stable solution of the compounds during storage and to provide stability and reduced viscosity for the inhibitor solutions when they are injected against a pressure of 200 to 25,000 psi. The solvent is present in the inhibitor composition in the range from 0 wt % to about 95 wt %, preferably from 20 wt % to about 95 wt %, more preferably from 50 wt % to about 95 wt % of the total composition, based on volume.
- When the compounds of the present invention are added into the mixture of hydrocarbons and water at any concentration effective to inhibit the formation of hydrates under the given conditions. Preferably, the concentration of the active inhibitor compound is between about 0.01 wt % and about 5 wt % based on the water content in the hydrocarbons and water mixture. More preferably, the inhibitor compound concentration is between about 0.1 wt % and about 3 wt %.
- The present invention may also be used in combination with other means of hydrate inhibition such as the use of thermodynamic or kinetic inhibitors discussed in the background section. These other hydrate inhibitors may be of the same or different type of hydrate inhibitor used in the composition. If mixtures of hydrate inhibitors are used, the mixture may be added to the hydrocarbon and water containing process stream through a single port or multiple ports. Alternatively, individual hydrate inhibitors may be added at separate ports to the process stream.
- The present invention may also be used in combination with other oil field flow assurance compounds such as, but not limited to, corrosion inhibitors, scale inhibitors, paraffin inhibitors, and asphaltene inhibitors. The hydrate inhibitors may also be used in combination with emulsion breakers or water clarifiers.
- Simple Quaternary Ammonium and Phosphonium Compounds
- Certain simple quaternary ammonium and phosphonium compounds are suitable for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, by adding to the mixture an effective amount of at least one hydrate inhibitor compound. One preferred family of hydrate inhibitor compounds has the formula:
- R1 is selected from hydrogen and normal or branched alkyls having from 1 to 3 carbon atoms.
- R2 is selected from normal or branched alkyls having from 1 to 4 carbon atoms, preferably exactly 4 carbon atoms. It should be recognized that R1 and R2 may be the same or different, such as where R1 and R2 each have exactly one carbon atom.
- R3 is an organic moiety having 4 or 5 carbon atoms.
- R4 is an organic moiety having from 2 to 20 carbon atoms. In certain embodiments, R4 may be selected from alkyl, alkenyl, aryl, arylalkyl, arylalkenyl, alkylaryl, alkenylaryl, glycol and combinations thereof. Alternatively, R4 may include one or more heteroatoms selected from oxygen, nitrogen, sulfur and combinations thereof. Still further, R4 may be chemically bound to a polymer. In one embodiment, R4 is —[(CH2—CHR5—O)]n—H, R5 is selected from a hydrogen, a methyl group, and an ethyl group, and n ranges from 1 to 3.
- A is a nitrogen atom (N) or a phosphorus atom (P).
- X− is an anion. For example, X− may be selected from hydroxide, carboxylate, halide, sulfate, organic sulphonate, and combinations thereof. Suitably, the X− anion may be a halide ion selected from bromide, chloride, and combinations thereof.
- In one preferred embodiment, the at least one compound is the product of a reaction between an organic halide having one of R1, R2, R3, and R4 and an amine or phosphene having the other three of R1, R2, R3, and R4. For example, the at least one compound may be the product of a reaction between butyl bromide and an N,N-dimethyl-alkylamine having between 10 and 20 carbon atoms. Suitably, the N,N-dimethyl-alkylamine may be N,N-dimethyl-hexadecylamine.
- The method may be performed at any pressure, such as between 100 and 10,000 psi or even greater than 10,000 psi.
- Independently, the method may include adding at least one amine salt to the mixture along with the at least one compound. For example, the amine salt may include a cation moiety that is an amine selected from ammonia, dimethylamine, diethylamine, di-n-propylamine, trimethylamine, triethylamine, tri-n-propylamine, tri-iso-propylamine, ethanolamine, diethylethanolamine, triethanolamine, methyl ethanolamine, ethyl ethanolamine, propyl ethanolamine, methyl diethanolamine, ethyl diethanolamine, dimethyl ethanolamine, diethanolamine, dibutylethanolamine, dipropylethanolamine, dibutylpropanolamine, dipropylpropanolamine, morpholine, N-methylmorpholine, N-ethylmorpholine, N-propylmorpholine, dibutylethanolamine, N,N-dibutyl-cocoamidopropylamine, and combinations thereof. Alternatively, the amine salt may include an anionic moiety that is an acid selected from carboxylic acids and inorganic acids. Suitable carboxylic acids include, with limitation, formic acid, acetic acid, propionic acid, butyric acid, glycolic acid, malonic acid, succinic acid, acrylic acid, methacrylic acid, trifluoroacetic acid, methane sulfonic acid and mixtures thereof. Suitable inorganic acids include, without limitation, nitric acid, hydrogen chloride, hydrogen bromide, and mixtures thereof.
- Accordingly, the at least one compound may, for example, include at least one of the following: dimethylbutylhexadecylammonium salt; dimethylbutyloctadecylammonium bromide, dimethylbutyldodecylammonium salt; at least one ammonium salt having an ammonium compound selected from trimethylhexadecylammonium, dimethylethylhexadecylammonium, dimethylbutyloctadecylammonium, dimethylbutylhexadecylammonium, dimethylbutyldodecylammonium, dimethylbutyltetradecylammonium, propyldibutylhexadecylammonium, dipropylbutylhexadecylammonium, and mixtures thereof; or at least one phosphonium salt having a phosphonium compound selected from trimethylhexadecylphosphonium, dimethylethylhexadecylphosphonium, dimethylbutyloctadecylphosphonium dimethylbutylhexadecylphosphonium, dimethylbutyldodecylphosphonium, dimethylbutyltetradecylphosphonium, propyldibutylhexadecylphosphonium, dipropylbutylhexadecylphosphonium, and mixtures thereof.
- The hydrate inhibitor compound is preferably mixed with a solvent, for example water, simple alcohols, glycols, ethers, ketonic liquids, aromatic hydrocarbons, and combinations thereof. More specifically, preferred solvents include water, methanol, ethanol, iso-propanol, n-butanol, iso-butanol, 2-ethyl hexanol, ethylene glycol, 1,2-prpylene glycols, 1,3-propylene glycol, hexylene glycol, ethylene glycol mono butylether (butyl cellosolve), ethylene glycol dibutyl ether, tetrahydrofuran, methylethylketone, methylisobutylketone, diisobutylketone, N-methylpyrrolidone, cyclohexanone, xylene, toluene, and combinations thereof.
- Betaines and Amine Oxides
- Other quaternary ammonium and phosphonium compounds, known as betaines and amine oxides, have also been found to be suitable for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, by adding to the mixture an effective amount of at least one hydrate inhibitor compound having the formula:
(R1)(R2)(R3)A+-[R4(C═O)]m—O− - In accordance with the invention, R1, R2, R3 and R4 are organic moieties, wherein R1 is an alkyl having 4 or 5 carbon atoms, and wherein R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms, and wherein R3 has 2 to 20 carbon atoms. Optionally, R3 has an amide functionality. In one embodiment, R3 is —[(CH2—CHR5—O)]n—H, wherein R5 is selected from a hydrogen, a methyl group, and an ethyl group, and n ranges from 1 to 3. R4 is preferably a normal or branched alkyl group, such as where R4 is selected from —(CH2)n—, —[CH2—(CHR5)n]— and combinations thereof, n is an
integer 1 or greater, and R5 is an alkyl having from 1 to 3 carbon atoms. - A is N or P; and m is an
integer - The method may optionally include adding at least one amine salt to the mixture along with the at least one compound. Suitable amine salts include those previously described herein.
- Preferred betaines may be derived from an amine and an acid, wherein the amine is selected from dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, butyldicocoylamine, and mixtures thereof and the acid is selected from chloroacetic acid, acrylic acid, methacrylic acid, and mixtures thereof. Whether derived in this or a different manner, suitable betaines include, without limitation,
- dibutylhexadecylcarboxypropyl, dibutyltetradecylcarboxypropyl, dibutyloctadecylcarboxypropyl, dibutyloleylcarboxypropyl, butyldicocoylcarboxypropyl, dibutylhexadecylcarboxyethyl, dibutyltetradecylcarboxyethyl, dibutyloctadecylcarboxyethyl, dibutyloleylcarboxyethyl, butyldicocoylcarboxyethyl, dibutylhexadecylcarboxymethyl, dibutyltetradecylcarboxymethyl, dibutyloctadecylcarboxymethyl, dibutyloleylcarboxymethyl, butyldicocoylcarboxymethyl and mixtures thereof. Suitable amine oxides include, without limitation, butylmethylhexadecylamine, butylmethyltetradecylamine, butylmethyloctadecylamine, butylethylhexadecylamine, butylethyltetradecylamine, butylethyloctadecylamine, dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, dibutylcocoylamine, butylpropylhexadecylamine, butylpropyltetradecylamine, butylpropyloctadecylamine, butylpropyloleoylamine, butyldicocoylamine, and mixtures thereof.
- In one embodiment, at least one of R1, R2 and R3 is the amide group —[(R5—NH—(C═O)—R6)], R5 is selected from —(CH2)t—, —[CH2—(CHR7)t]—, —(CH2—CHR7O)u—(CH2)t— and combinations thereof, t is an
integer 2 to 4, u is 0 or an integer (1 or greater), R7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R6 is an organic moiety, such as an alkyl or alkenyl group, having 4 to 20 carbon atoms. Most preferably, R5 is —(CH2—CHR7O)u—(CH2)t—. - A preferred method comprises adding to the mixture an effective amount of at least one compound having a formula:
(R1)(R2)(R3)A+-[R4—(C═O)]m—O−
where: A is N or P; R1 is an alkyl having 4 or 5 carbon atoms; R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms; R3 is the amide group —[(R5—NH—(C═O)—R6)], wherein R5 is selected from —(CH2)t—, —[CH2—(CHR7)t]—, —(CH2—CHR7O)u—(CH2)t— and combinations thereof, t is aninteger 2 to 4, u is 0 or an integer (1 or greater) R7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R6 is an organic moiety, such as an alkyl or alkenyl group, having 4 to 20 carbon atoms; R4 is selected from —(CH2)n—, —[CH2—CHR8)n]— and combinations thereof, wherein n is aninteger 1 or greater and R8 is an alkyl having from 1 to 3 carbon atoms; and m is aninteger integer 1 or greater, n is preferably an integer from 1 to 10, more preferably from 2 to 4, and most preferably 2. R5 is preferably —(CH2—CHR7O)u—(CH2)t—, and R7 is hydrogen, u is 0 or 1, and t is most preferably 3. In one embodiment, R1 and R2 are butyl groups. Other suitable betaines include (R1)(R2)(R3)A+-[(CH2CH2)—(SO2)]—O−, (R1)(R2)(R3)A+-[(CH2CH(OH)CH2)—(SO2)]—O−, and (R1)(R2)(R3)A+-[(CH2)n—(C═S)]—S−, wherein n is 1 or greater.
Amides - Further still, the method may include adding to the mixture an effective amount of at least one amide compound having a formula:
where: R1, R2, R4, and R5 are organic moieties; R1 is an alkyl having from 4 to 5 carbon atoms; R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms; R4 is selected from —(CH2)t—, —[CH2—(CHR6)t]—(CH2—CHR6O)u—(CH2)t— and combinations thereof, t is aninteger 2 to 4, u is 0 or an integer (1 or greater), R6 is hydrogen or an alkyl having from 1 to 3 carbon atoms; R5 is an organic moiety, such as alkyl or alkenyl group, having 4 to 20 carbon atoms; A is N or P; X− is an anion; and a is 0 or 1. When a is 0, then R3 is selected from —[(CH2)(CHR7)b(C═O)]c—O−, —[(CH2CH2)—(SO2)]—O−, —[(CH2CH(OH)CH2)—(SO2)]—O−, —[(CH2)n—(C═S)]—S− and combinations thereof, wherein b is 0 or 1, c is 0 or 1, n is 2 or 3, and R7 is hydrogen or methyl group. When a is 1, then R3 is selected from hydrogen, organic moieties having from 1 to 20 carbon atoms, and combinations thereof. Preferably, R3 is the same as the group containing the amide functionality. - The X anion is preferably selected from hydroxide, carboxylate, halide, sulphate, organic sulphonate, and combinations thereof. Suitable halide ions include, without limitation, bromide, chloride, and combinations thereof.
- In one embodiment, R3 is hydrogen, a is 1, and the anion X− is selected from hydroxide, carboxylate, halide, sulphate, organic sulphonate, and combinations thereof. In a still further embodiment, the at least one amide compound is the reaction product of an N,N-dialkyl-aminoalkylamine with an ester or glyceride. Preferably, the ester or glyceride is derived from a plant source or animal source selected from coconut oil, tallow oil, vegetable oil, and combinations thereof.
- The method may further comprise adding at least one amine salt to the mixture along with the at least one compound. Suitable amine salts include those previously described herein. Furthermore, the at least one compound may be mixed with the solvents previously described herein.
- In another embodiment, the at least one compound includes a product prepared by the reaction of an amine selected from (3-dialkylamino)propylamine and (3-dialkylamino)ethylamine with vegetable oil or tallow oil followed by reacting with a reactant selected from an organic halide, such as an alkyl halide, having from 4 to 20 carbon atoms, hydrogen peroxide, and an acid, wherein the acid is selected from mineral acids, formic acid, acetic acid, chloroacetic acid, propionic acid, acrylic acid, and methacrylic acid, and wherein the dialkyl of the (3-dialkylamino)propylamine includes two alkyl groups independently selected from methyl, ethyl, propyl, butyl, morpholine, piperidine, and combinations thereof.
- Amino Alcohols and Ester-1 Compounds
- The present invention provides yet another method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water. This method comprises adding to the mixture an effective amount of at least one compound having a formula:
wherein: A is N or P; R1 is a normal or branched alkyl group containing at least 4 carbon atoms; R2 is hydrogen or an alkyl group containing from 1 to 4 carbon atoms; R4 is selected from hydrogen, methyl and ethyl; R5 is either H or an organic moiety, such as an alkyl chain, containing from 4 to 20 carbon atoms; (X−)a is an anion; and a is 0 or 1; n is 1 to 3; and m is 0 or 1. When a is 0, then R3 is selected from —[(CH2)(CH)b(C═O)]c—O−, —[(CH2CH2)—(SO2)]—, —[(CH2CH(OH)CH2)—(SO2)]—O−, and combinations thereof; wherein b is 0 or 1; c is 0 or 1; and R6 is selected from hydrogen, methyl, ethyl and combinations thereof. When a is 1, then R3 is selected from hydrogen, an organic moiety, such as an alkyl or alkenyl group, having from 1 to 20 carbon atoms, and combinations thereof. The X− anion is preferably selected from hydroxide, carboxylate, halide, sulphate, organic sulphonate, and combinations thereof. The preferred halide ions include, without limitation, bromide, chloride, and combinations thereof. - The method may further comprise adding at least one amine salt to the mixture along with the at least one compound. Suitable amine salts include those previously described herein. Furthermore, the at least one compound may be mixed with the solvents previously described herein.
- In one embodiment, the at least one compound includes a product of the reaction of N-alkylamine or N,N-dialkylamine with ethylene oxide, propylene oxide or combinations thereof, followed by reacting with at least one alkyl halide having from 1 to 20 carbon atoms.
- In a further embodiment, the method comprises introducing ester moieties by trans-esterfication of hydroxy terminals in the alkoxy chains using methyl esters of fatty acids.
- Ester-2 Compounds
- The present invention provides still another method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water. This method comprises adding to the mixture an effective amount of at least one compound having a formula:
wherein: A is N or P; R1 is an alkyl group containing at least 4 carbon atoms; R2 is hydrogen or an alkyl group containing from 1 to 4 carbon atoms; R4 is an organic moiety, such as an alkyl, alkenyl or aryl group, containing from 4 to 20 carbon atoms, most preferably 8 to 16 carbon atoms; (X)− is an anion selected from hydroxide, chloride, bromide, sulfate, sulfonate, or carboxylate; and a is 0 or 1. When a is 0, then R3 is selected from —[(CH2)(CH6)b(C═O)]c—O−, —[(CH2CH2)—(SO2)]—O−, —[(CH2CH(OH)CH2)—(SO2)]—O−, and combinations thereof, wherein b is 0 or 1, c is 0 or 1, and R6 is selected from hydrogen and methyl. When a is 1, then R3 is selected from hydrogen, an organic moiety, such as an alkyl or alkenyl group, having from 4 to 20 carbon atoms, and combinations thereof. - In one embodiment, the at least one compound includes a product of the Michael addition reaction of alkyl or N,N-dialkyl amine with an acrylate, followed by reacting with at least one organic halide, such as an alkyl halide, having from 1 to 20 carbon atoms.
- Optionally, the at least one compound includes a product of the reaction of a tertiary amine containing the ester moiety with chloroacetic acid, acrylic acid or methacrylic acid. In accordance with a similar option, the at least one compound includes a product of the reaction of a tertiary amine containing the ester moiety with hydrogen peroxide.
- The “Rocking Arm” test apparatus used for these evaluations contains “pressure cells” made of sapphire tubing containing a stainless steel ball. The cells are placed in a rack, and the rack gently rocked forward, then back. The cells are charged with liquids prior to being placed in the rack and then immersed in an insulated tank containing water. Once the cells are immersed in the bath they can then be charged with gas and the experiment begun. Sensors are used to monitor ball movement within the cells, with one sensor placed near each end of the cell. The ball falling time is recorded. This data is referred to as Sensor Activation Time and they are noted as Sensor-1 and Sensor-2.
- In a typical experiment, the cells were charged with oil to brine ratios ranging from 10:1 to 1:10. A typical oil to brine ratio is about 2:1. The hydrate inhibitors were mixed with the solutions in the cells. The cells were purged with a synthetic natural gas blend, then charged with gas to the desired pressure and allowed to equilibrate at the pre-determined temperature. The bath was then cooled to a lower pre-determined temperature at specified rates. The following parameters were recorded: (1) bath temperature, (2) individual cell pressure, (3) sensor activation time, and (4) visual observations. Hydrate formation or blockage is indicated by either an increase in sensor activation time (SAT) or visual observation of hydrate particles sticking to the walls. When evaluating the sensor data the results can indicate: (1) a viscosity increase due to the formation of hydrates, which can also be due in part to oil effects; (2) a partial blockage; and (3) a complete blockage.
- The inhibitor evaluations were conducted using a synthetic natural gas blend shown in Table 1. The composition of the synthetic salt water (brine) used for the inhibitor evaluations is presented in Table 2. A typical temperature-pressure profile is presented in
FIG. 1 . A list of inhibitor compounds that were evaluated and the results of the evaluations are summarized in Table 3 and inFIGS. 2-17 . Each of these inhibitor compounds was tested as an inhibitor solution at a 3 volume % dosage rate. Each inhibitor solution was made up of 40 wt % inhibitor compound and 60 wt % solvent, wherein the solvent itself was a mixture of half xylene and half n-butanol.TABLE 1 Gas Composition Synthetic Blend Components Mol % Nitrogen 0.4 Methane 87.2 Ethane 7.6 Propane 3.1 i-Butane 0.5 n-Butane 0.8 i-Pentane 0.2 n-Pentane 0.2 -
TABLE 2 Composition of Synthetic brine Concentrations of Individual Ions Ions (mg/L) Sodium 24000 Potassium 250 Calcium 2800 Magnesium 990 Barium 14 Strontium 95 Chloride 45019 Bromide 2200 -
TABLE 3 Inhibitor Compounds Evaluated Inhibitor FIG. # Inhibitor Performance 2 None Complete hydrate blockage at 9° C. (48.2° F.). 3 Trimethylhexadecylammonium Partial hydrate blockage at 6° C. (42.8° F.). bromide Later on, the hydrate broke lose. 4 Dimethylethylhexadecylammonium Partial hydrate blockage at 4.4° C. (40° F.). bromide Later on, the hydrate broke lose. 5 Dimethylbutylhexadecylammonium No hydrate blockage at 4.4° C. (40° F.) in bromide 18 hours. 6 Dimethylbutyloctadecylammonium No hydrate blockage at 4.4° C. (40° F.) in bromide 13 hours. 7 Dipropylbutylhexadecylammonium No hydrate blockage at 4.4° C. (40° F.) in bromide 13 hours. 8 Dibutylpropylhexadecylammonium No hydrate blockage at 4.4° C. (40° F.) in bromide 13 hours. 9 a & b Tributylhexadecylammonium bromide No hydrate blockage at 4.4° C. (40° F.) in 13 hours with 3% inhibitor; complete hydrate blockage with 1% inhibitor. 10 Dimethyldihexadecylammonium Complete hydrate blockage at 11° C. bromide (51.8° F.). 11 N,N-Dibutyl-cocoamidopropyl No hydrate blockage at 4.4° C. (40° F.) in carbomethoxy betaine 13 hours. 12 N,N-Dibutylcocoamidopropylamine No hydrate blockage at 4.4° C. (40° F.) in oxide 13 hours. 13 N,N,N-Tributyl- No hydrate blockage at 4.4° C. (40° F.) in cocoamidopropylammonium bromide 13 hours. 14 N,N-Dibutylhexadecyl- No hydrate blockage at 4.4° C. (40° F.) in cocoamidopropylammonium bromide 13 hours. 15 a & b N,N- No hydrate blockage at 4.4° C. (40° F.) in Dibutyltriethoxyhexadecylammonium 13 hours with 1 and 3% inhibitor. bromide 16 a & b Tributylhexadecylphosphonium No hydrate blockage at 4.4° C. (40° F.) in Bromide 13 hours with 3% inhibitor; initial hydrate blockage with 1% inhibitor. 17 a & b Blend of N,N-Dibutyl- No hydrate blockage at 4.4° C. (40° F.) in cocoamidopropyl carboethoxy betaine 13 hours with 1 and 3% inhibitor. and amine salt - The above examples are intended to illustrate the performance of the new inhibitors. These examples are not intended and should not be interpreted to limit their applicabilities under any other conditions such,as pressure, gas composition, amount and type of oil, amount and type of water (salinity). Please also note that the performance ranking of the inhibitors noted here may be changed or reversed under a different set of conditions.
- The terms “comprising,” “including,” and “having,” as used in the claims and specification herein, shall be considered as indicating an open group that may include other elements not specified. The term “consisting essentially of,” as used in the claims and specification herein, shall be considered as indicating a partially open group that may include other elements not specified, so long as those other elements do not materially alter the basic and novel characteristics of the claimed invention. The terms “a,” “an,” and the singular forms of words shall be taken to include the plural form of the same words, such that the terms mean that one or more of something is provided. For example, the phrase “a solution comprising a phosphorus-containing compound” should be read to describe a solution having one or more phosphorus-containing compound. The terms “at least one” and “one or more” are used interchangeably. The term “one” or “single” shall be used to indicate that one and only one of something is intended. Similarly, other specific integer values, such as “two,” are used when a specific number of things is intended. The terms “preferably,” “preferred,” “prefer,” “optionally,” “may,” and similar terms are used to indicate that an item, condition or step being referred to is an optional (not required) feature of the invention.
- The disclosure of a range of values, such as a disclosure of a compound having an alkyl having from 6 to 20 carbon atoms, shall be construed as further specifically disclosing each and every individual value there between, such as 7, 8, 9, . . . 18, 19. Where an embodiment is disclosed as including more than one range, then the disclosure shall be construed as further specifically disclosing each and every possible combination of values within those ranges. Still further, the disclosure of lists of alternative components, conditions, steps, or aspects of the invention shall be construed as specifically disclosing each and every combination of those alternatives, unless the combination is specifically excluded or mutually exclusive.
- It should be understood from the foregoing description that various modifications and changes may be made in the preferred embodiments of the present invention without departing from its true spirit. It is intended that this foregoing description is for purposes of illustration only and should not be construed in a limiting sense. Only the language of the following claims should limit the scope of this invention.
Claims (31)
1. A method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, the method comprising:
(R1)(R2)(R3)A+-[R4—(C═O)]m—O−
adding to the mixture an effective amount of at least one compound having a formula:
(R1)(R2)(R3)A+-[R4—(C═O)]m—O−
where: R1, R2, R3 and R4 are organic moieties, wherein R1 is an alkyl having 4 or 5 carbon atoms, R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms and R3 has 2 to 20 carbon atoms;
A is N or P; and
m is an integer 0 or 1.
2. The method of claim 1 , wherein the at least one compound includes at least one betaine.
3. The method of claim 1 , wherein the at least one compound includes at least one amine oxide.
4. The method of claim 1 , wherein at least one of R1, R2 and R3 has an amide functionality.
5. The method of claim 1 , wherein at least one of R1, R2 and R3 is —[(CH2—CHR5—O)]n—H, R5 is selected from a hydrogen, a methyl group, and an ethyl group, and n ranges from 1 to 3.
6. The method of claim 1 , wherein R4 is a normal or branched alkyl group.
7. The method of claim 1 , wherein R4 is —[CH2—(CHR5)n]—, wherein n is 0 or 1, and R5 is hydrogen or an alkyl having from 1 to 3 carbon atoms.
8. The method of claim 1 , further comprising:
adding at least one amine salt to the mixture along with the at least one compound.
9. The method of claim 8 , wherein the amine salt includes a cation moiety that is an amine selected from ammonia, dimethylamine, diethylamine, di-n-propylamine, trimethylamine, triethylamine, tri-n-propylamine, tri-iso-propylamine, ethanolamine, diethylethanolamine, triethanolamine, methyl ethanolamine, ethyl ethanolamine, propyl ethanolamine, methyl diethanolamine, ethyl diethanolamine, dimethyl ethanolamine, diethanolamine, dibutylethanolamine, dipropylethanolamine, dibutylpropanolamine, dipropylpropanolamine, morpholine, N-methylmorpholine, N-ethylmorpholine, N-propylmorpholine, dibutylethanolamine, and combinations thereof.
10. The method of claim 8 , wherein the amine salt includes an anionic moiety that is an acid selected from carboxylic acids and inorganic acids.
11. The method of claim 8 , wherein the amine salt includes an anionic moiety that is a carboxylic acid selected from formic acid, acetic acid, propionic acid, butyric acid, glycolic acid, malonic acid, succinic acid, acrylic acid, methacrylic acid, trifluoroacetic acid, methane sulfonic acid and mixtures thereof.
12. The method of claim 8 , wherein the amine salt includes an anionic moiety that is an-inorganic acid selected from nitric acid, hydrogen chloride, hydrogen bromide, and mixtures thereof.
13. The method of claim 1 , wherein the at least one compound includes at least one betaine derived from an amine and an acid, wherein the amine is selected from dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, butyldicocoylamine, and mixtures thereof and the acid is selected from chloroacetic acid, acrylic acid, methacrylic acid, and mixtures thereof.
14. The method of claim 1 , wherein the at least one compound includes at least one betaine selected from dibutylhexadecylcarboxypropyl, dibutyltetradecylcarboxypropyl, dibutyloctadecylcarboxypropyl, dibutyloleylcarboxypropyl, butyldicocoylcarboxypropyl, dibutylhexadecylcarboxyethyl, dibutyltetradecylcarboxyethyl, dibutyloctadecylcarboxyethyl, dibutyloleylcarboxyethyl, butyldicocoylcarboxyethyl, dibutylhexadecylcarboxymethyl, dibutyltetradecylcarboxymethyl, dibutyloctadecylcarboxymethyl, dibutyloleylcarboxymethyl, butyldicocoylcarboxymethyl and mixtures thereof.
15. The method of claim 1 , wherein the at least one compound includes at least one amine oxide selected from butylmethylhexadecylamine, butylmethyltetradecylamine, butylmethyloctadecylamine, butylethylhexadecylamine, butylethyltetradecylamine, butylethyloctadecylamine, dibutylhexadecylamine, dibutyltetradecylamine, dibutyloctadecylamine, dibutyloleylamine, dibutylcocoylamine, butylpropylhexadecylamine, butylpropyltetradecylamine, butylpropyloctadecylamine, butylpropyloleoylamine, butyldicocoylamine, and mixtures thereof.
16. The method of claim 1 , wherein at least one of R1, R2 and R3 is the amide group —[(R5—NH—(C═O)—R6)], wherein R5 is selected from —(CH2)t—, —[CH2—(CHR7)t]—, —(CH2—CHR7O)u—(CH2)t— and combinations thereof, wherein t is an integer 2 to 4, u is 0 or an integer and R7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and wherein R6 is an alkyl or alkenyl group having 4 to 20 carbon atoms.
17. The method of claim 16 , wherein R5 is —(CH2—CHR7O)u—(CH2)t—.
18. A method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, the method comprising:
(R1)(R2)(R3)A+-[R4—(C═O)]m—O−
adding to the mixture an effective amount of at least one compound having a formula:
(R1)(R2)(R3)A+-[R4—(C═O)]m—O−
where: A is N or P;
R1 is an alkyl having 4 or 5 carbon atoms;
R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms;
R3 is the amide group —[(R5—NH—(C═O)—R6)], wherein R5 is selected from —(CH2)t—, —[CH2—(CHR7)t]—, —CH2—CHR7O)u—(CH2)t—) and combinations thereof, t is an integer 2 to 4, u is 0 or an integer, R7 is hydrogen or an alkyl having from 1 to 3 carbon atoms, and R6 is an alkyl or alkenyl group having 4 to 20 carbon atoms; and
R4 is —[CH2(CHR8)n]—, wherein n is 0 or 1, and R8 is hydrogen or an alkyl having from 1 to 3 carbon atoms.
19. The method of claim 1 , wherein m is 1.
20. The method of claim 19 , wherein R5 is —(CH2—CHR7O)u—(CH2)t—, and R7 is hydrogen, u is 0 or 1.
21. The method of claim 20 , wherein t is 3.
22. The method of claim 19 , wherein R1 and R2 are butyl groups.
23. The method of claim 19 , wherein R1 is butyl and R2 is hydrogen.
24. The method of claim 16 , wherein the amide functionality increases the biodegradability of the compound.
25. The method of claim 18 , wherein m is 0.
26. The method of claim 25 , wherein R5 is —(CH2—CHR7O)u—(CH2)t—, and R7 is hydrogen, u is 0 or 1.
27. The method of claim 26 , wherein t is 3.
28. The method of claim 25 , wherein R1 and R2 are butyl groups.
29. The method of claim 25 , wherein R1 is butyl and R2 is hydrogen.
30. A method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, the method comprising:
adding to the mixture an effective amount of at least one compound having a formula selected from (R1)(R2)(R3)A+-[(CH2CH2)—(SO2)]—O−, (R1)(R2)(R3)A+-[(CH2CH(OH)CH2)—(SO2)]—O−, and (R1)(R2)(R3)A+-[(CH2)n—(C═S)]—S−, wherein n is 1 or greater; R1, R2, and R3 are organic moieties, wherein R1 is an alkyl having 4 or 5 carbon atoms, R2 is hydrogen or an alkyl having from 1 to 4 carbon atoms and R3 has 2 to 20 carbon atoms; and A is N or P.
31. A method for inhibiting formation of gas hydrate plugs in conduits containing a mixture of hydrocarbons and water, the method comprising:
adding to the mixture an effective amount of an ammonium or phosphonium compound having a functionality selected from carboxylate betaine, sulfobetaine, amine oxide, and combinations thereof.
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CA2543426A CA2543426C (en) | 2003-10-21 | 2004-10-14 | Methods for inhibiting hydrate blockage in oil and gas pipelines using simple quaternary ammonium and phosphonium compounds |
AU2004285117A AU2004285117B2 (en) | 2003-10-21 | 2004-10-14 | Methods for inhibiting hydrate blockage in oil and gas pipelines using simple quaternary ammonium and phosphonium compounds |
GB0609874A GB2422840B (en) | 2003-10-21 | 2004-10-14 | Methods for inhibiting hydrate blockage in oil and gas pipelines using simple quaternary ammonium and phosphonium compounds |
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ARP040103800A AR046549A1 (en) | 2003-10-21 | 2004-10-20 | METHODS FOR THE INHIBITION OF THE FORMATION OF OBSTRUCTIONS OF GAS HYDRATION IN DUCTS THAT CONTAIN A MIXTURE OF HYDROCARBON AND WATER |
NO20062235A NO344577B1 (en) | 2003-10-21 | 2006-05-18 | Methods for inhibiting hydrate blockages in oil and gas pipelines using simple quaternary ammonium and phosphonium compounds |
ARP120100757A AR085630A2 (en) | 2003-10-21 | 2012-03-08 | A METHOD FOR THE INHIBITION OF THE FORMATION OF OBSTRUCTIONS OF GAS HYDRATION IN DUCTS CONTAINING A MIXTURE OF HYDROCARBONS AND WATER |
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US10/918,214 Active 2026-01-18 US7381689B2 (en) | 2003-10-21 | 2004-08-13 | Methods for inhibiting hydrate blockage in oil and gas pipelines using amide compounds |
US10/918,210 Abandoned US20050085676A1 (en) | 2003-10-21 | 2004-08-13 | Methods for inhibiting hydrate blockage in oil and gas pipelines using betaines and amine oxides |
US10/918,192 Abandoned US20050085675A1 (en) | 2003-10-21 | 2004-08-13 | Methods for inhibiting hydrate blockage in oil and gas pipelines using ester compounds |
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US10/918,213 Abandoned US20050085396A1 (en) | 2003-10-21 | 2004-08-13 | Methods for inhibiting hydrate blockage in oil and gas pipelines using amino alcohols and ester compounds |
US10/918,214 Active 2026-01-18 US7381689B2 (en) | 2003-10-21 | 2004-08-13 | Methods for inhibiting hydrate blockage in oil and gas pipelines using amide compounds |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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US20080064611A1 (en) * | 2004-11-04 | 2008-03-13 | Spratt Paul A | Ion pair amphiphiles as hydrate inhibitors |
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US7958939B2 (en) * | 2006-03-24 | 2011-06-14 | Exxonmobil Upstream Research Co. | Composition and method for producing a pumpable hydrocarbon hydrate slurry at high water-cut |
WO2008089262A1 (en) * | 2007-01-21 | 2008-07-24 | M-I Llc | Method and pill for remediating hydrate condensate blockage in pipelines |
AU2008305441B2 (en) | 2007-09-25 | 2014-02-13 | Exxonmobil Upstream Research Company | Method for managing hydrates in subsea production line |
US8047296B2 (en) * | 2008-07-25 | 2011-11-01 | Baker Hughes Incorporated | Method of transitioning to kinetic hydrate inhibitors in multiple tie-in well systems |
US8242287B2 (en) * | 2009-03-12 | 2012-08-14 | Nalco Company | Process for reacting an α, β-unsaturated dicarboxylic acid compound with an ethylenically unsaturated hydrocarbon |
KR101895614B1 (en) | 2009-05-15 | 2018-09-05 | 더루우브리졸코오포레이션 | Quaternary ammonium amide and/or ester salts |
DE102009059188A1 (en) * | 2009-12-17 | 2011-06-22 | Wirtgen GmbH, 53578 | Chisel holder and base part |
US8980798B2 (en) * | 2010-03-31 | 2015-03-17 | Baker Hughes Incorporated | Precipitation prevention in produced water containing hydrate inhibitors injected downhole |
US20120010112A1 (en) | 2010-07-06 | 2012-01-12 | Basf Se | Acid-free quaternized nitrogen compounds and use thereof as additives in fuels and lubricants |
US8146667B2 (en) * | 2010-07-19 | 2012-04-03 | Marc Moszkowski | Dual gradient pipeline evacuation method |
US8618025B2 (en) * | 2010-12-16 | 2013-12-31 | Nalco Company | Composition and method for reducing hydrate agglomeration |
US9505707B2 (en) * | 2010-12-22 | 2016-11-29 | Nalco Company | Composition and method for reducing hydrate agglomeration |
US10006128B2 (en) | 2012-09-28 | 2018-06-26 | Ecolab Usa Inc. | Quaternary and cationic ammonium surfactants as corrosion inhibitors |
GB2516862A (en) * | 2013-08-01 | 2015-02-11 | M I Drilling Fluids Uk Ltd | Quaternary ammonium compounds and gas hydrate inhibitor compositions |
US9410073B2 (en) | 2013-11-26 | 2016-08-09 | Ecolab Usa Inc. | Anti-agglomerants for controlling gas hydrates |
US9765254B2 (en) | 2014-10-30 | 2017-09-19 | Ecolab Usa Inc. | Cationic ammonium surfactants as low dosage hydrate inhibitors |
US9663666B2 (en) | 2015-01-22 | 2017-05-30 | Baker Hughes Incorporated | Use of hydroxyacid to reduce the localized corrosion potential of low dose hydrate inhibitors |
US9988568B2 (en) | 2015-01-30 | 2018-06-05 | Ecolab Usa Inc. | Use of anti-agglomerants in high gas to oil ratio formations |
WO2016161108A1 (en) * | 2015-04-01 | 2016-10-06 | Ecolab Usa Inc. | Fluorine-containing agents for enhancing hydrate inhibitors |
FR3044322B1 (en) | 2015-11-27 | 2020-08-14 | Ceca Sa | USE OF A SPECIFIC CARBOXYLIC AMINOACID TO LIMIT THE FORMATION AND / OR AGGLOMERATION OF GAS HYDRATES |
FR3044321B1 (en) | 2015-11-27 | 2020-08-07 | Ceca Sa | COMPOSITION TO LIMIT THE FORMATION AND / OR AGGLOMERATION OF GAS HYDRATES |
WO2017105507A1 (en) | 2015-12-18 | 2017-06-22 | Halliburton Energy Services, Inc. | High temperature hydrate inhibitors and methods of use |
EP3420055A4 (en) | 2016-02-26 | 2020-01-22 | Ecolab USA Inc. | Kinetic hydrate inhibitors for controlling gas hydrate formation in wet gas systems |
AU2016403731B2 (en) * | 2016-04-19 | 2020-11-05 | Halliburton Energy Services, Inc. | Hydrate inhibitors and methods of use |
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EP3452525A1 (en) | 2016-05-06 | 2019-03-13 | Saudi Arabian Oil Company | Acrylamide-based copolymers, terpolymers, and use as hydrate inhibitors |
KR102342913B1 (en) | 2016-05-06 | 2021-12-28 | 사우디 아라비안 오일 컴퍼니 | Use as succinimide-based copolymer and hydrate inhibitor |
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IT201600130571A1 (en) | 2016-12-23 | 2018-06-23 | Lamberti Spa | INHIBITORS OF GAS HYDRATES |
IT201600130556A1 (en) | 2016-12-23 | 2018-06-23 | Lamberti Spa | INHIBITORS OF GAS HYDRATES |
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US11236261B2 (en) | 2018-09-14 | 2022-02-01 | Halliburton Energy Services, Inc. | Polyaromatic hydrocarbon additives for hydrate inhibition |
WO2020068046A1 (en) | 2018-09-25 | 2020-04-02 | Multi-Chem Group, Llc | Anti-agglomerant hydrate inhibitors and method of use |
US11161804B2 (en) | 2018-10-09 | 2021-11-02 | Clariant International Ltd. | Unsymmetrically substituted dicarboxylic acid diamido ammonium salts and their use for gas hydrate anti-agglomeration |
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Citations (34)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3634235A (en) * | 1967-12-21 | 1972-01-11 | Oil Base | Drilling fluid and method of use |
US5135668A (en) * | 1990-02-09 | 1992-08-04 | Scandinavian Oilfield Chemicals A/S | Process for inhibiting corrosion in oil production fluids |
US5244878A (en) * | 1987-12-30 | 1993-09-14 | Institut Francais Du Petrole | Process for delaying the formation and/or reducing the agglomeration tendency of hydrates |
US5331105A (en) * | 1991-10-10 | 1994-07-19 | The British Petroleum Company P.L.C. | Method for inhibiting hydrate formation |
US5434323A (en) * | 1992-08-03 | 1995-07-18 | Institut Francais Du Petrole | Method for reducing the agglomeration tendency of hydrates in production effluents |
US5460728A (en) * | 1993-12-21 | 1995-10-24 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US5491269A (en) * | 1994-09-15 | 1996-02-13 | Exxon Production Research Company | Method for inhibiting hydrate formation |
US5639925A (en) * | 1992-11-20 | 1997-06-17 | Colorado School Of Mines | Additives and method for controlling clathrate hydrates in fluid systems |
US5648575A (en) * | 1995-01-10 | 1997-07-15 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US5741758A (en) * | 1995-10-13 | 1998-04-21 | Bj Services Company, U.S.A. | Method for controlling gas hydrates in fluid mixtures |
US5744665A (en) * | 1995-06-08 | 1998-04-28 | Exxon Production Research Company | Maleimide copolymers and method for inhibiting hydrate formation |
US5874660A (en) * | 1995-10-04 | 1999-02-23 | Exxon Production Research Company | Method for inhibiting hydrate formation |
US5879561A (en) * | 1995-04-25 | 1999-03-09 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US5958844A (en) * | 1997-07-25 | 1999-09-28 | Institut Francais Du Petrole | Method of transporting hydrates suspended in production effluents |
US6015929A (en) * | 1994-09-15 | 2000-01-18 | Exxon Research And Engineering Co. | Gas hydrate anti-agglomerates |
US6025302A (en) * | 1998-05-18 | 2000-02-15 | Bj Services Company | Quaternized polyether amines as gas hydrate inhibitors |
US6035933A (en) * | 1997-10-17 | 2000-03-14 | Petroleo Brasileiro S.A.-Petrobras | Process for the thermo-hydraulic control of gas hydrates |
US6063972A (en) * | 1994-05-08 | 2000-05-16 | Bp Exploration Operating Company Limited | Hydrate inhibition |
US6102986A (en) * | 1996-07-23 | 2000-08-15 | Clariant Gmbh | Method of inhibiting gas hydrate formation |
US6152993A (en) * | 1997-09-09 | 2000-11-28 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US6177497B1 (en) * | 1998-01-29 | 2001-01-23 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6180699B1 (en) * | 2000-02-02 | 2001-01-30 | Isp Investments Inc. | Blend for preventing or retarding the formation of gas hydrates |
US20020038063A1 (en) * | 2000-02-22 | 2002-03-28 | Przybylinski John L. | Composition and method for inhibition of formation of gas hydrates |
US6369004B1 (en) * | 1996-11-22 | 2002-04-09 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6379294B1 (en) * | 1999-07-29 | 2002-04-30 | Akzo Nobel N.V. | Process for preparing esterquats |
US6566309B1 (en) * | 1999-05-03 | 2003-05-20 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6620330B2 (en) * | 2001-12-18 | 2003-09-16 | Baker Hughes Incorporated | Detoxification of quaternary onium compounds with polycarboxylate-containing compound |
US20040163307A1 (en) * | 2003-02-24 | 2004-08-26 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
US20040164278A1 (en) * | 2003-02-24 | 2004-08-26 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
US20040167040A1 (en) * | 2003-02-24 | 2004-08-26 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
US6867262B1 (en) * | 1999-07-28 | 2005-03-15 | Basf Aktiengesellschaft | Grafted polymers as gas hydrate inhibitors |
US20050101495A1 (en) * | 2003-02-24 | 2005-05-12 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
US6894007B2 (en) * | 2001-03-24 | 2005-05-17 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6905605B2 (en) * | 2000-04-07 | 2005-06-14 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3054750A (en) * | 1957-06-07 | 1962-09-18 | Sun Oil Co | Method for inhibiting corrosion caused by oil well fluids |
US4856593A (en) | 1987-09-21 | 1989-08-15 | Conoco Inc. | Inhibition of hydrate formation |
WO1993025798A1 (en) | 1992-06-11 | 1993-12-23 | Shell Internationale Research Maatschappij B.V. | A method for inhibiting gas hydrate formation |
WO1994024413A1 (en) | 1993-04-08 | 1994-10-27 | Bp Chemicals Limited | Method for inhibiting solids formation and blends for use therein |
GB9400538D0 (en) | 1994-01-13 | 1994-03-09 | Bp Exploration Operating | Hydrate inhibition |
GB9505865D0 (en) | 1995-03-23 | 1995-05-10 | Bp Exploration Operating | Hydrate Inhibitors |
GB9505864D0 (en) * | 1995-03-23 | 1995-05-10 | Bp Exploration Operating | Hydrate Inhibition |
DE19624345B4 (en) * | 1996-06-19 | 2004-12-23 | Südzucker AG Mannheim/Ochsenfurt | Acylated carbohydrates with at least one carboxyalkyl group etherified with the carbohydrate, process for their preparation and their use in detergents |
JP4194162B2 (en) * | 1999-02-01 | 2008-12-10 | ステラケミファ株式会社 | Method for removing calcium from water containing a high concentration of calcium bicarbonate |
US6444852B1 (en) * | 1999-06-24 | 2002-09-03 | Goldschmidt Chemical Corporation | Amines useful in inhibiting gas hydrate formation |
DE10134224B4 (en) * | 2001-07-13 | 2012-12-20 | Clariant Produkte (Deutschland) Gmbh | Additives for inhibiting gas hydrate formation |
-
2004
- 2004-08-13 US US10/918,191 patent/US7264653B2/en active Active
- 2004-08-13 US US10/918,213 patent/US20050085396A1/en not_active Abandoned
- 2004-08-13 US US10/918,214 patent/US7381689B2/en active Active
- 2004-08-13 US US10/918,210 patent/US20050085676A1/en not_active Abandoned
- 2004-08-13 US US10/918,192 patent/US20050085675A1/en not_active Abandoned
- 2004-10-20 AR ARP040103800A patent/AR046549A1/en active IP Right Grant
-
2012
- 2012-03-08 AR ARP120100757A patent/AR085630A2/en active IP Right Grant
Patent Citations (39)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3634235A (en) * | 1967-12-21 | 1972-01-11 | Oil Base | Drilling fluid and method of use |
US5244878A (en) * | 1987-12-30 | 1993-09-14 | Institut Francais Du Petrole | Process for delaying the formation and/or reducing the agglomeration tendency of hydrates |
US5135668A (en) * | 1990-02-09 | 1992-08-04 | Scandinavian Oilfield Chemicals A/S | Process for inhibiting corrosion in oil production fluids |
US5331105A (en) * | 1991-10-10 | 1994-07-19 | The British Petroleum Company P.L.C. | Method for inhibiting hydrate formation |
US5434323A (en) * | 1992-08-03 | 1995-07-18 | Institut Francais Du Petrole | Method for reducing the agglomeration tendency of hydrates in production effluents |
US5639925A (en) * | 1992-11-20 | 1997-06-17 | Colorado School Of Mines | Additives and method for controlling clathrate hydrates in fluid systems |
US5460728A (en) * | 1993-12-21 | 1995-10-24 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US6063972A (en) * | 1994-05-08 | 2000-05-16 | Bp Exploration Operating Company Limited | Hydrate inhibition |
US6436877B1 (en) * | 1994-05-08 | 2002-08-20 | Bp Exploration Operating Co., Ltd. | Hydrate inhibition |
US5491269A (en) * | 1994-09-15 | 1996-02-13 | Exxon Production Research Company | Method for inhibiting hydrate formation |
US6015929A (en) * | 1994-09-15 | 2000-01-18 | Exxon Research And Engineering Co. | Gas hydrate anti-agglomerates |
US5648575A (en) * | 1995-01-10 | 1997-07-15 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US5879561A (en) * | 1995-04-25 | 1999-03-09 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US5744665A (en) * | 1995-06-08 | 1998-04-28 | Exxon Production Research Company | Maleimide copolymers and method for inhibiting hydrate formation |
US5874660A (en) * | 1995-10-04 | 1999-02-23 | Exxon Production Research Company | Method for inhibiting hydrate formation |
US5741758A (en) * | 1995-10-13 | 1998-04-21 | Bj Services Company, U.S.A. | Method for controlling gas hydrates in fluid mixtures |
US6331508B1 (en) * | 1995-10-13 | 2001-12-18 | Bj Service Company, U.S.A. | Method for controlling gas hydrates in fluid mixtures |
US6102986A (en) * | 1996-07-23 | 2000-08-15 | Clariant Gmbh | Method of inhibiting gas hydrate formation |
US6544932B2 (en) * | 1996-11-22 | 2003-04-08 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6369004B1 (en) * | 1996-11-22 | 2002-04-09 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US5958844A (en) * | 1997-07-25 | 1999-09-28 | Institut Francais Du Petrole | Method of transporting hydrates suspended in production effluents |
US6152993A (en) * | 1997-09-09 | 2000-11-28 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US6214091B1 (en) * | 1997-09-09 | 2001-04-10 | Shell Oil Company | Method and compound for inhibiting the plugging of conduits by gas hydrates |
US6035933A (en) * | 1997-10-17 | 2000-03-14 | Petroleo Brasileiro S.A.-Petrobras | Process for the thermo-hydraulic control of gas hydrates |
US6177497B1 (en) * | 1998-01-29 | 2001-01-23 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6025302A (en) * | 1998-05-18 | 2000-02-15 | Bj Services Company | Quaternized polyether amines as gas hydrate inhibitors |
US6566309B1 (en) * | 1999-05-03 | 2003-05-20 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6867262B1 (en) * | 1999-07-28 | 2005-03-15 | Basf Aktiengesellschaft | Grafted polymers as gas hydrate inhibitors |
US6379294B1 (en) * | 1999-07-29 | 2002-04-30 | Akzo Nobel N.V. | Process for preparing esterquats |
US6180699B1 (en) * | 2000-02-02 | 2001-01-30 | Isp Investments Inc. | Blend for preventing or retarding the formation of gas hydrates |
US6596911B2 (en) * | 2000-02-22 | 2003-07-22 | Baker Hughes Incorporation | Composition and method for inhibition of formation of gas hydrates |
US20020038063A1 (en) * | 2000-02-22 | 2002-03-28 | Przybylinski John L. | Composition and method for inhibition of formation of gas hydrates |
US6905605B2 (en) * | 2000-04-07 | 2005-06-14 | Shell Oil Company | Method for inhibiting the plugging of conduits by gas hydrates |
US6894007B2 (en) * | 2001-03-24 | 2005-05-17 | Clariant Gmbh | Additives for inhibiting gas hydrate formation |
US6620330B2 (en) * | 2001-12-18 | 2003-09-16 | Baker Hughes Incorporated | Detoxification of quaternary onium compounds with polycarboxylate-containing compound |
US20040163307A1 (en) * | 2003-02-24 | 2004-08-26 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
US20040164278A1 (en) * | 2003-02-24 | 2004-08-26 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
US20040167040A1 (en) * | 2003-02-24 | 2004-08-26 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
US20050101495A1 (en) * | 2003-02-24 | 2005-05-12 | Clariant Gmbh | Corrosion and gas hydrate inhibitors having improved water solubility and increased biodegradability |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080064611A1 (en) * | 2004-11-04 | 2008-03-13 | Spratt Paul A | Ion pair amphiphiles as hydrate inhibitors |
GB2453125A (en) * | 2007-09-25 | 2009-04-01 | Statoil Asa | Deadleg |
GB2453125B (en) * | 2007-09-25 | 2012-02-08 | Statoilhydro Asa | Deadleg |
US9297237B2 (en) | 2007-09-25 | 2016-03-29 | Statoil Petroleum As | Deadleg |
US8404895B2 (en) | 2011-01-24 | 2013-03-26 | Baker Hughes Incorporated | Tertiary amine salt additives for hydrate control |
US20140346117A1 (en) * | 2011-12-20 | 2014-11-27 | Ulfert Cornelis Klomp | Method for inhibitng the plugging of conduits by gas hydrates |
RU2569348C1 (en) * | 2014-11-18 | 2015-11-20 | Александр Филиппович Кардаш | Method for preparing hydrocarbon material with gaseous phase for transportation |
US11084970B2 (en) * | 2017-12-04 | 2021-08-10 | Multi-Chem Group, Llc | Additive to decrease the pour point of paraffin inhibitors |
US20240132791A1 (en) * | 2022-09-30 | 2024-04-25 | Afton Chemical Corporation | Fuel composition |
Also Published As
Publication number | Publication date |
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US20050085396A1 (en) | 2005-04-21 |
US7264653B2 (en) | 2007-09-04 |
US20050081432A1 (en) | 2005-04-21 |
US20050081714A1 (en) | 2005-04-21 |
AR085630A2 (en) | 2013-10-16 |
US20050085675A1 (en) | 2005-04-21 |
US7381689B2 (en) | 2008-06-03 |
AR046549A1 (en) | 2005-12-14 |
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