US20120012506A1 - Method of removing hydrogen sulfide - Google Patents
Method of removing hydrogen sulfide Download PDFInfo
- Publication number
- US20120012506A1 US20120012506A1 US12/835,805 US83580510A US2012012506A1 US 20120012506 A1 US20120012506 A1 US 20120012506A1 US 83580510 A US83580510 A US 83580510A US 2012012506 A1 US2012012506 A1 US 2012012506A1
- Authority
- US
- United States
- Prior art keywords
- nitroxide
- scavenger
- promoter
- methyltriazine
- hydrogen sulfide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 229910000037 hydrogen sulfide Inorganic materials 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims abstract description 17
- 239000002516 radical scavenger Substances 0.000 claims abstract description 26
- AVXURJPOCDRRFD-UHFFFAOYSA-N Hydroxylamine Chemical class ON AVXURJPOCDRRFD-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 20
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 20
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 20
- 239000012530 fluid Substances 0.000 claims abstract description 17
- 150000004820 halides Chemical class 0.000 claims abstract description 4
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 12
- 230000002000 scavenging effect Effects 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 4
- FXKQPQOOZSXQAG-UHFFFAOYSA-N 4-methyltriazine Chemical compound CC1=CC=NN=N1 FXKQPQOOZSXQAG-UHFFFAOYSA-N 0.000 description 14
- -1 tri-substituted-hexahydro-s-triazines Chemical class 0.000 description 13
- 150000001875 compounds Chemical class 0.000 description 8
- 150000001299 aldehydes Chemical class 0.000 description 6
- 239000002904 solvent Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000009472 formulation Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000003350 kerosene Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- JYEUMXHLPRZUAT-UHFFFAOYSA-N 1,2,3-triazine Chemical compound C1=CN=NN=C1 JYEUMXHLPRZUAT-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 230000001172 regenerating effect Effects 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 0 [1*]N1CN([2*])CN([3*])C1 Chemical compound [1*]N1CN([2*])CN([3*])C1 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 125000001453 quaternary ammonium group Chemical group 0.000 description 2
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 150000003918 triazines Chemical class 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OYWRDHBGMCXGFY-UHFFFAOYSA-N 1,2,3-triazinane Chemical class C1CNNNC1 OYWRDHBGMCXGFY-UHFFFAOYSA-N 0.000 description 1
- BVOMRRWJQOJMPA-UHFFFAOYSA-N 1,2,3-trithiane Chemical compound C1CSSSC1 BVOMRRWJQOJMPA-UHFFFAOYSA-N 0.000 description 1
- HUHGPYXAVBJSJV-UHFFFAOYSA-N 2-[3,5-bis(2-hydroxyethyl)-1,3,5-triazinan-1-yl]ethanol Chemical compound OCCN1CN(CCO)CN(CCO)C1 HUHGPYXAVBJSJV-UHFFFAOYSA-N 0.000 description 1
- 125000000954 2-hydroxyethyl group Chemical group [H]C([*])([H])C([H])([H])O[H] 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 150000001923 cyclic compounds Chemical class 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000010747 number 6 fuel oil Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000012453 solvate Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 125000000547 substituted alkyl group Chemical group 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/20—Organic compounds not containing metal atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
- C07C7/152—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by forming adducts or complexes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/207—Acid gases, e.g. H2S, COS, SO2, HCN
Definitions
- This invention relates generally to the treatment of sour gas and liquid hydrocarbon to remove or reduce the levels of hydrogen sulfide therein.
- the toxicity of hydrogen sulfide in hydrocarbon streams is well known in the industry and considerable expense and efforts are expended annually to reduce its content to a safe level.
- a regenerative system for treating sour gas streams.
- These systems typically employ a compound used in an absorption tower to contact the produced fluids and selectively absorb the hydrogen sulfide and possibly other toxic materials such as carbon dioxide and mercaptans. The absorption compound is then regenerated and reused in the system.
- Typical hydrogen sulfide absorption materials include alkanolamines, PEG, hindered amines, and other species that can be regenerated.
- Nonregenerative scavengers for small plant hydrogen sulfide removal fall into four general categories: 1) aldehyde based, 2) metallic oxide based, 3) caustic based, and 4) other processes.
- the scavenger reacts with the hydrogen sulfide to form a nontoxic compound or a compound, which can be removed from the hydrocarbon.
- a chemical compound known as formthionals e.g., trithiane
- Prior Art aldehyde scavengers typically include low molecular weight aldehydes and ketones and adducts thereof.
- the low molecular weight aldehydes may also be combined with an alkyl or alkanolamine as disclosed in U.S. Pat. No. 4,748,011.
- Other aldehyde derived scavengers include the reaction product of low molecular weight alkanolamines and aldehydes as disclosed in U.S. Pat. No. 4,978,512.
- PCT Application WO 92/01481 discloses a method of reducing sulfides in a sewage gas using certain tri-substituted-hexahydro-s-triazines.
- German reference DE4027300 discloses a regenerative solvent for removing H 2 S and mercaptans.
- U.S. Pat. No. 5,347,004 discloses the use of 1,3,5 alkoxyalkylene hexahydro triazines.
- PCT Application WO 91 US 5232 discloses hydroxyalkyl triazine scavengers, specifically an N,N′,N′′-tris(2-hydroxyethyl)hexahydro-s-triazine.
- U.S. Pat. No. 5,774,024 discloses the combination of an alkyl triazine scavenger and quaternary ammonium salt, where the quaternary ammonium salt enhances the effectiveness of the alkyl-triazine.
- At least one embodiment of the invention is directed towards a method for removing hydrogen sulfide from a hydrocarbon fluid.
- the method comprises contacting the fluid with an effective amount of sulfide scavenger formulated with a nitroxide promoter.
- the amount of nitroxide promoter is sufficient to accelerate the scavenging action of the scavenger in comparison to the scavenging action of the scavenger in the absence of the nitroxide promoter.
- Alkyl-triazine means a molecule according to the formula:
- R 1 , R 2 , R 3 are Alkyl groups such as methyl, ethyl, propyl, isopropyl, t-butyl, etc. or are substituted alkyl groups such as CH 2 CH 2 OH, and R 1 , R 2 , R 3 can all be the same group or one or more different groups.
- Alkyl-triazines include but are not limited to the triazines disclosed in U.S. Pat. No. 5,744,024.
- Hydrocarbon fluid means a liquid or gas predominantly comprising organic material including but not limited to kerosene, crude oil, distillate fuels, fuel oil, heating oils, diesel fuel, gasoline, jet fuel, bunker fuel oils, and any combination thereof.
- Metaltriazine means an alkyl-triazine in which R 1 , R 2 , and R 3 are all methyl groups.
- Non-Regenerative Scavenger means a scavenger, which is consumed by the process of scavenging.
- Regenerative Scavenger means a scavenger, which is not consumed by the process of scavenging.
- Promoter means a composition of matter that in and of itself does not scavenge, but when combined with a known scavenger, significantly increases the effectiveness of the scavenger.
- Salt means a compound comprising an anion and a cation which usually ionizes in solution.
- “Scavenger” means a composition of matter, such as but not limited to alkyl triazines, useful in reducing the amount of some other composition of matter, such as but not limited to hydrogen sulfide, in a fluid medium.
- the amount of hydrogen sulfide in a hydrocarbon fluid is reduced by the introduction of an alkyl-triazine scavenger with a nitroxide promoter.
- the promoter increases the effectiveness of the alkyl-triazine scavenger.
- Nitroxide is superior to the prior art quarternay ammonium salt promoters because nitroxide is a single component and does not contain halides such as chloride.
- the effectiveness of a nitroxide as a promoter is unexpected because it is a single neutral compound.
- the promoter is from 1-25% of the scavenger-promoter containing composition.
- At least a portion of the triazines are synthesized according to the process described in U.S. Pat. No. 5,744,024.
- the ntiroxide is mixed with a solution of alkyl triazine where the solvent can be water and the nitroxide bearing solution is introduced into the hydrocarbon fluid.
- the nitroxide introduction is simultaneous to the alkyl-triazine introduction.
- nitroxide promoter with a scavenger over the prior art scavengers is that the nitroxide promoter is not a salt (it is not a combination of an anion and a cation) and therefore lacks halides and in particular lacks chloride.
- a scavenging formulation is used in a hydrocarbon stream.
- the formulation comprises a solvent, alkyl-triazine, and nitroxide.
- the solvent is selected from the list consisting of water, alcohol, aromatic solvent, a solvent that mutually solvates alkyl-triazine, and nitroxide and any combination thereof.
- the formulation can be introduced into the hydrocarbon stream by mechanical means including but not limited to injection pumps or any mechanism disclosed in U.S. Pat. Nos. 5,744,024 and 5,840,177.
- the gas may be passed through an absorption tower containing a scavenging formulation.
- the hydrocarbon fluid is in a liquid state. In at least one embodiment the hydrocarbon fluid is in a gaseous state.
- Samples of sour hydrocarbon streams (fuel oils) were tested to determine the efficiency of the triazine formulated with promoter versus the triazine formulated without a promoter.
- the samples were comparatively treated with various dosages of methyltriazine scavenger, methyltriazine scavenger with a promoter, and the amounts of residual H 2 S for the various samples were recorded.
- Table 1 compares the inventive composition at different concentrations
- Table 2 compares promoted scavenger with non-promoted scavenger
- table 3 compares methyltriazine with and without promoter over time.
- the vapor space hydrogen sulfide levels were measured according to the procedure described by ASTM D5705-03.
- the test procedure was modified for tables 2 and 3 by performing the test in kerosene at room temperature, which was approximately 22° C. instead of 60° C.
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention provides a method of removing hydrogen sulfide from hydrocarbon fluids. The method involves using a nitroxide molecule to promote a sulfide scavenger such as alkyl-triazine. The nitroxide effectively accelerates the scavenger's activity. This allows for the avoidance of the introduction of halides into the hydrocarbon stream.
Description
- None.
- Not Applicable.
- This invention relates generally to the treatment of sour gas and liquid hydrocarbon to remove or reduce the levels of hydrogen sulfide therein. The toxicity of hydrogen sulfide in hydrocarbon streams is well known in the industry and considerable expense and efforts are expended annually to reduce its content to a safe level.
- In large production facilities, it is generally more economical to install a regenerative system for treating sour gas streams. These systems typically employ a compound used in an absorption tower to contact the produced fluids and selectively absorb the hydrogen sulfide and possibly other toxic materials such as carbon dioxide and mercaptans. The absorption compound is then regenerated and reused in the system. Typical hydrogen sulfide absorption materials include alkanolamines, PEG, hindered amines, and other species that can be regenerated.
- Nonregenerative scavengers for small plant hydrogen sulfide removal fall into four general categories: 1) aldehyde based, 2) metallic oxide based, 3) caustic based, and 4) other processes. In the removal of hydrogen sulfide by nonregenerative compounds, the scavenger reacts with the hydrogen sulfide to form a nontoxic compound or a compound, which can be removed from the hydrocarbon. For example, when formaldehyde reacts with hydrogen sulfide, a chemical compound known as formthionals (e.g., trithiane) is formed.
- Prior Art aldehyde scavengers typically include low molecular weight aldehydes and ketones and adducts thereof. The low molecular weight aldehydes may also be combined with an alkyl or alkanolamine as disclosed in U.S. Pat. No. 4,748,011. Other aldehyde derived scavengers include the reaction product of low molecular weight alkanolamines and aldehydes as disclosed in U.S. Pat. No. 4,978,512. PCT Application WO 92/01481 discloses a method of reducing sulfides in a sewage gas using certain tri-substituted-hexahydro-s-triazines. German reference DE4027300 discloses a regenerative solvent for removing H2S and mercaptans. U.S. Pat. No. 5,347,004 discloses the use of 1,3,5 alkoxyalkylene hexahydro triazines. PCT Application WO 91 US 5232 discloses hydroxyalkyl triazine scavengers, specifically an N,N′,N″-tris(2-hydroxyethyl)hexahydro-s-triazine. U.S. Pat. No. 5,774,024 discloses the combination of an alkyl triazine scavenger and quaternary ammonium salt, where the quaternary ammonium salt enhances the effectiveness of the alkyl-triazine.
- Thus there is clear need and utility for an improved method of scavenging hydrogen sulfide from hydrocarbon fluids. The art described in this section is not intended to constitute an admission that any patent, publication or other information referred to herein is “prior art” with respect to this invention, unless specifically designated as such. In addition, this section should not be construed to mean that a search has been made or that no other pertinent information as defined in 37 CFR §1.56(a) exists.
- At least one embodiment of the invention is directed towards a method for removing hydrogen sulfide from a hydrocarbon fluid. The method comprises contacting the fluid with an effective amount of sulfide scavenger formulated with a nitroxide promoter. The amount of nitroxide promoter is sufficient to accelerate the scavenging action of the scavenger in comparison to the scavenging action of the scavenger in the absence of the nitroxide promoter.
- For purposes of this application the definition of these terms is as follows:
- “Alkyl-triazine” means a molecule according to the formula:
- Where R1, R2, R3 are Alkyl groups such as methyl, ethyl, propyl, isopropyl, t-butyl, etc. or are substituted alkyl groups such as CH2CH2OH, and R1, R2, R3 can all be the same group or one or more different groups. Alkyl-triazines include but are not limited to the triazines disclosed in U.S. Pat. No. 5,744,024.
- “Hydrocarbon fluid” means a liquid or gas predominantly comprising organic material including but not limited to kerosene, crude oil, distillate fuels, fuel oil, heating oils, diesel fuel, gasoline, jet fuel, bunker fuel oils, and any combination thereof.
- “Methyltriazine” means an alkyl-triazine in which R1, R2, and R3 are all methyl groups.
- “Nitroxide” means a composition of matter according to the formula:
- where R1 R2 and R3 are any alkyl group containing 1-30 carbon atoms and includes cyclic compounds. “Non-Regenerative Scavenger” means a scavenger, which is consumed by the process of scavenging.
- “Regenerative Scavenger” means a scavenger, which is not consumed by the process of scavenging.
- “Promoter” means a composition of matter that in and of itself does not scavenge, but when combined with a known scavenger, significantly increases the effectiveness of the scavenger.
- “Salt” means a compound comprising an anion and a cation which usually ionizes in solution.
- “Scavenger” means a composition of matter, such as but not limited to alkyl triazines, useful in reducing the amount of some other composition of matter, such as but not limited to hydrogen sulfide, in a fluid medium.
- In the event that the above definitions or a description stated elsewhere in this application is inconsistent with a meaning (explicit or implicit) which is commonly used, in a dictionary, or stated in a source incorporated by reference into this application, the application and the claim terms in particular are understood to be construed according to the definition or description in this application, and not according to the common definition, dictionary definition, or the definition that was incorporated by reference. In light of the above, in the event that a term can only be understood if it is construed by a dictionary, if the term is defined by the Kirk-Othmer Encyclopedia of Chemical Technology, 5th Edition, (2005), (Published by Wiley, John & Sons, Inc.) this definition shall control how the term is to be defined in the claims.
- In at least one embodiment, the amount of hydrogen sulfide in a hydrocarbon fluid is reduced by the introduction of an alkyl-triazine scavenger with a nitroxide promoter. The promoter increases the effectiveness of the alkyl-triazine scavenger. Nitroxide is superior to the prior art quarternay ammonium salt promoters because nitroxide is a single component and does not contain halides such as chloride.
- The effectiveness of a nitroxide as a promoter is unexpected because it is a single neutral compound. In at least one embodiment the promoter is from 1-25% of the scavenger-promoter containing composition.
- In at least one embodiment, at least a portion of the triazines are synthesized according to the process described in U.S. Pat. No. 5,744,024.
- In at least one embodiment the ntiroxide is mixed with a solution of alkyl triazine where the solvent can be water and the nitroxide bearing solution is introduced into the hydrocarbon fluid. In at least one embodiment the nitroxide introduction is simultaneous to the alkyl-triazine introduction. The properties of the ntiroxide promoter are such that it is highly effective in a number of different hydrocarbon fluids.
- One advantage of the use of the nitroxide promoter with a scavenger over the prior art scavengers is that the nitroxide promoter is not a salt (it is not a combination of an anion and a cation) and therefore lacks halides and in particular lacks chloride.
- In at least one embodiment a scavenging formulation is used in a hydrocarbon stream. The formulation comprises a solvent, alkyl-triazine, and nitroxide. The solvent is selected from the list consisting of water, alcohol, aromatic solvent, a solvent that mutually solvates alkyl-triazine, and nitroxide and any combination thereof. The formulation can be introduced into the hydrocarbon stream by mechanical means including but not limited to injection pumps or any mechanism disclosed in U.S. Pat. Nos. 5,744,024 and 5,840,177. In the context of gaseous hydrocarbon fluids, the gas may be passed through an absorption tower containing a scavenging formulation.
- In at least one embodiment the hydrocarbon fluid is in a liquid state. In at least one embodiment the hydrocarbon fluid is in a gaseous state.
- The foregoing may be better understood by reference to the following example, which is presented for purposes of illustration and is not intended to limit the scope of the invention.
- Samples of sour hydrocarbon streams (fuel oils) were tested to determine the efficiency of the triazine formulated with promoter versus the triazine formulated without a promoter. The samples were comparatively treated with various dosages of methyltriazine scavenger, methyltriazine scavenger with a promoter, and the amounts of residual H2S for the various samples were recorded. Table 1 compares the inventive composition at different concentrations, Table 2 compares promoted scavenger with non-promoted scavenger, and table 3 compares methyltriazine with and without promoter over time.
-
TABLE 1 Comparison of promoter at 3 different concentrations in vacuum gas oil for 2 hours at 60° C. Dose H2S Percent Dose Sample # Treatment (ppm) (ppm) Reduction Ratio Untreated 0 200 0 1 Methyltriazine + 60 100 50 0.3 2.5% nitroxide 2 Methyltriazine + 60 120 40 0.3 5% nitroxide 3 Methyltriazine + 60 130 35 0.3 10% nitroxide -
TABLE 2 Comparison of promoted and non-promoted triazine, in kerosene for 2 hours Dose H2S Percent Dose Sample # Treatment (ppm) (ppm) Reduction Ratio Untreated 0 1300 1 Methyltriazine + 260 70 95 0.2 5% Quaternary ammonium 2 Methyltriazine + 260 90 93 0.2 5% nitroxide 3 Methyltriazine 260 120 91 0.2 Untreated 0 950 1 Methyltriazine + 284 30 97 0.3 5% Quaternary ammonium 2 Methyltriazine + 284 70 93 0.3 5% nitroxide 3 Methyltriazine 284 80 92 0.3 -
TABLE 3 Comparison of alkyl-triazine with and without promoter over time in kerosene Sample Dose H2S Percent Dose Time # Treatment (ppm) (ppm) Reduction Ratio (min) Un- 0 1200 0 0 treated 1 Methyltriazine + 400 300 75 0.3 15 nitroxide 2 Methyltriazine + 400 200 83 0.3 30 nitroxide 3 Methyltriazine + 400 85 93 0.3 60 nitroxide 4 Methyltriazine + 400 75 94 0.3 90 nitroxide 5 Methyltriazine + 400 75 94 0.3 120 nitroxide Un- 0 600 0.3 0 treated 1 Methyltriazine 200 250 58 0.3 15 2 Methyltriazine 200 230 62 0.3 30 3 Methyltriazine 200 110 82 0.3 60 4 Methyltriazine 200 60 90 0.3 90 5 Methyltriazine 200 70 88 0.3 120 - The vapor space hydrogen sulfide levels were measured according to the procedure described by ASTM D5705-03. The test procedure was modified for tables 2 and 3 by performing the test in kerosene at room temperature, which was approximately 22° C. instead of 60° C.
- This data demonstrates that the presence of the nitroxide enables the methyltraizine scavenger to reduce the levels of H2S faster than methyltriazine does without the promoter.
- While this invention may be embodied in many different forms, there are shown in the drawings and described in detail herein specific preferred embodiments of the invention. The present disclosure is an exemplification of the principles of the invention and is not intended to limit the invention to the particular embodiments illustrated. All patents, patent applications, scientific papers, and any other referenced materials mentioned herein are incorporated by reference in their entirety. Furthermore, the invention encompasses any possible combination of some or all of the various embodiments described herein and incorporated herein.
- The above disclosure is intended to be illustrative and not exhaustive. This description will suggest many variations and alternatives to one of ordinary skill in this art. All these alternatives and variations are intended to be included within the scope of the claims where the term “comprising” means “including, but not limited to”. Those familiar with the art may recognize other equivalents to the specific embodiments described herein which equivalents are also intended to be encompassed by the claims.
- All ranges and parameters disclosed herein are understood to encompass any and all subranges subsumed therein, and every number between the endpoints. For example, a stated range of “1 to 10” should be considered to include any and all subranges between (and inclusive of) the minimum value of 1 and the maximum value of 10; that is, all subranges beginning with a minimum value of 1 or more, (e.g. 1 to 6.1), and ending with a maximum value of 10 or less, (e.g. 2.3 to 9.4, 3 to 8, 4 to 7), and finally to each number 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10 contained within the range.
- This completes the description of the preferred and alternate embodiments of the invention. Those skilled in the art may recognize other equivalents to the specific embodiment described herein which equivalents are intended to be encompassed by the claims attached hereto.
Claims (4)
1. A method of reducing the amount of hydrogen sulfide in a hydrocarbon fluid comprising contacting the fluid with an effective amount of a composition, the composition comprising a sulfide scavenger and a nitroxide promoter wherein the amount of nitroxide promoter is sufficient to accelerate the scavenging action of the scavenger in comparison to the scavenging action of the scavenger in the absence of the nitroxide promoter.
2. The method of claim 1 wherein the scavenger is an alkyl-triazine.
3. The method of claim 1 wherein the hydrocarbon fluid is liquid.
4. The method of claim 1 wherein the method results in no halides being added to the hydrocarbon fluid.
Priority Applications (12)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/835,805 US20120012506A1 (en) | 2010-07-14 | 2010-07-14 | Method of removing hydrogen sulfide |
EP11807421.0A EP2593534A4 (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulfide |
MX2013000511A MX2013000511A (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulfide. |
SG2013003025A SG187080A1 (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulfide |
BR112013000887A BR112013000887A2 (en) | 2010-07-14 | 2011-07-13 | method for reducing the amount of hydrogen sulfide in a hydrocarbon fluid |
CA2805402A CA2805402C (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulfide |
KR1020137003668A KR20130047738A (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulfide |
PCT/US2011/043780 WO2012009391A2 (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulfide |
ARP110102527A AR082847A1 (en) | 2010-07-14 | 2011-07-13 | IMPROVED METHOD OF ELIMINATION OF HYDROGEN SULFIDE |
JP2013519782A JP5815699B2 (en) | 2010-07-14 | 2011-07-13 | Improved method for removing hydrogen sulfide |
CN2011800347098A CN103003395A (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulfide |
RU2013102415/04A RU2562610C2 (en) | 2010-07-14 | 2011-07-13 | Improved method of removing hydrogen sulphide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/835,805 US20120012506A1 (en) | 2010-07-14 | 2010-07-14 | Method of removing hydrogen sulfide |
Publications (1)
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US20120012506A1 true US20120012506A1 (en) | 2012-01-19 |
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Family Applications (1)
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US12/835,805 Abandoned US20120012506A1 (en) | 2010-07-14 | 2010-07-14 | Method of removing hydrogen sulfide |
Country Status (12)
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US (1) | US20120012506A1 (en) |
EP (1) | EP2593534A4 (en) |
JP (1) | JP5815699B2 (en) |
KR (1) | KR20130047738A (en) |
CN (1) | CN103003395A (en) |
AR (1) | AR082847A1 (en) |
BR (1) | BR112013000887A2 (en) |
CA (1) | CA2805402C (en) |
MX (1) | MX2013000511A (en) |
RU (1) | RU2562610C2 (en) |
SG (1) | SG187080A1 (en) |
WO (1) | WO2012009391A2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9663390B2 (en) | 2013-05-10 | 2017-05-30 | Ecolab Usa Inc. | Reduction of hydrogen sulfide and/or malodor gassing from water via the addition of peroxyacetic acid/hydrogen peroxide product |
US11291947B2 (en) | 2016-06-28 | 2022-04-05 | Kuraray Co., Ltd. | Composition for removing sulfur-containing compound |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105056710B (en) * | 2015-08-21 | 2017-05-24 | 胜利油田胜利化工有限责任公司 | Liquid absorbent for removing hydrogen sulfide in oil gas |
CN107502329B (en) * | 2016-06-14 | 2020-07-10 | 中国石油大学(华东) | A kind of remover for removing the associated hydrogen sulfide gas in heavy oil thermal recovery |
JP7074754B2 (en) * | 2016-12-08 | 2022-05-24 | エコラブ ユーエスエイ インク | Hydrogen sulfide scavenger for polymer treated asphalt |
WO2024091459A1 (en) * | 2022-10-24 | 2024-05-02 | Cameron International Corporation | Sulfonyl azide composition for sulfur scavenging in oilfield operations |
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RU2080909C1 (en) * | 1988-12-23 | 1997-06-10 | Петролите Холдингз, Инк. | Method of selectively reducing hydrogen sulfide and/or organic sulfide content in gaseous and/or liquid streams |
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CA2148849A1 (en) * | 1994-06-23 | 1995-12-24 | Kishan Bhatia | Method of treating sour gas and liquid hydrocarbons |
US5744024A (en) * | 1995-10-12 | 1998-04-28 | Nalco/Exxon Energy Chemicals, L.P. | Method of treating sour gas and liquid hydrocarbon |
US5922794A (en) * | 1997-03-26 | 1999-07-13 | General Electric Company | Compositions stabilized with tertiary amine oxides |
JP2006522193A (en) * | 2003-03-31 | 2006-09-28 | チバ スペシャルティ ケミカルズ ホールディング インコーポレーテッド | Diesel fuel composition and method for improving the filterability of diesel fuel |
EP2288677A2 (en) * | 2008-04-18 | 2011-03-02 | M-i Swaco Norge As | Methods of predicting / optimizing hydrogen sulfide scavenging capacity and reduction of scale formation |
EP2267098A1 (en) * | 2009-06-26 | 2010-12-29 | M-i Swaco Norge As | Scavenger compositons and their use |
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2010
- 2010-07-14 US US12/835,805 patent/US20120012506A1/en not_active Abandoned
-
2011
- 2011-07-13 KR KR1020137003668A patent/KR20130047738A/en not_active Ceased
- 2011-07-13 EP EP11807421.0A patent/EP2593534A4/en not_active Withdrawn
- 2011-07-13 WO PCT/US2011/043780 patent/WO2012009391A2/en active Application Filing
- 2011-07-13 MX MX2013000511A patent/MX2013000511A/en active IP Right Grant
- 2011-07-13 AR ARP110102527A patent/AR082847A1/en active IP Right Grant
- 2011-07-13 CA CA2805402A patent/CA2805402C/en active Active
- 2011-07-13 JP JP2013519782A patent/JP5815699B2/en active Active
- 2011-07-13 RU RU2013102415/04A patent/RU2562610C2/en active
- 2011-07-13 SG SG2013003025A patent/SG187080A1/en unknown
- 2011-07-13 CN CN2011800347098A patent/CN103003395A/en active Pending
- 2011-07-13 BR BR112013000887A patent/BR112013000887A2/en not_active Application Discontinuation
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US5354453A (en) * | 1993-04-13 | 1994-10-11 | Exxon Chemical Patents Inc. | Removal of H2 S hydrocarbon liquid |
US5980733A (en) * | 1994-04-15 | 1999-11-09 | United Laboratories International | Method of removing sulfur compounds from hydrocarbon streams |
US6630435B1 (en) * | 1999-06-29 | 2003-10-07 | Procter & Gamble | Bleaching compositions |
US20050238556A1 (en) * | 2004-04-21 | 2005-10-27 | Pakulski Marek K | Method of scavenging hydrogen sulfide and/or mercaptans from fluid and gas streams |
Cited By (3)
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US9663390B2 (en) | 2013-05-10 | 2017-05-30 | Ecolab Usa Inc. | Reduction of hydrogen sulfide and/or malodor gassing from water via the addition of peroxyacetic acid/hydrogen peroxide product |
US10081561B2 (en) | 2013-05-10 | 2018-09-25 | Ecolab Usa Inc. | Reduction of hydrogen sulfide and/or malodor gassing from water via the addition of peroxyacetic acid/hydrogen peroxide product |
US11291947B2 (en) | 2016-06-28 | 2022-04-05 | Kuraray Co., Ltd. | Composition for removing sulfur-containing compound |
Also Published As
Publication number | Publication date |
---|---|
CA2805402C (en) | 2018-03-13 |
SG187080A1 (en) | 2013-03-28 |
WO2012009391A3 (en) | 2012-05-10 |
WO2012009391A2 (en) | 2012-01-19 |
KR20130047738A (en) | 2013-05-08 |
CA2805402A1 (en) | 2012-01-19 |
MX2013000511A (en) | 2013-02-27 |
BR112013000887A2 (en) | 2016-05-17 |
CN103003395A (en) | 2013-03-27 |
EP2593534A4 (en) | 2014-04-23 |
RU2562610C2 (en) | 2015-09-10 |
EP2593534A2 (en) | 2013-05-22 |
JP5815699B2 (en) | 2015-11-17 |
JP2013532735A (en) | 2013-08-19 |
RU2013102415A (en) | 2014-08-20 |
AR082847A1 (en) | 2013-01-16 |
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