EP4656707A1 - Hydrogen sulphide and mercaptan scavenging composition comprising a particular triazine compound and a (poly)ethylene glycol - Google Patents

Hydrogen sulphide and mercaptan scavenging composition comprising a particular triazine compound and a (poly)ethylene glycol

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Publication number
EP4656707A1
EP4656707A1 EP24305854.2A EP24305854A EP4656707A1 EP 4656707 A1 EP4656707 A1 EP 4656707A1 EP 24305854 A EP24305854 A EP 24305854A EP 4656707 A1 EP4656707 A1 EP 4656707A1
Authority
EP
European Patent Office
Prior art keywords
compound
carbon atoms
composition
formula
weight
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.)
Pending
Application number
EP24305854.2A
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German (de)
French (fr)
Inventor
Hemant Sunanda Surendra MONDKAR
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TotalEnergies Onetech SAS
Original Assignee
TotalEnergies Onetech SAS
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Priority to EP24305854.2A priority Critical patent/EP4656707A1/en
Publication of EP4656707A1 publication Critical patent/EP4656707A1/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10Working-up natural gas or synthetic natural gas
    • C10L3/101Removal of contaminants
    • C10L3/102Removal of contaminants of acid contaminants
    • C10L3/103Sulfur containing contaminants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G29/00Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/20Organic compounds not containing metal atoms
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/201Impurities
    • C10G2300/202Heteroatoms content, i.e. S, N, O, P
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/54Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
    • C10L2290/545Washing, scrubbing, stripping, scavenging for separating fractions, components or impurities during preparation or upgrading of a fuel

Definitions

  • the present invention relates to a composition useful for scavenging hydrogen sulphide and organic compounds comprising at least one sulfhydryl group.
  • Said composition comprises a particular triazine compound and an additive chosen from mono- and poly-ethylene glycols.
  • the present invention also relates to the use of such composition for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • the invention also relates to the use of the (poly)ethylene glycol additive for improving the efficiency of triazine compounds in scavenging hydrogen sulphide and organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • the present invention also relates to a method for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group comprising contacting a hydrocarbon stream such as crude oil, fuel or natural gas with the composition of the invention.
  • Hydrogen sulphide is a colourless and fairly toxic, flammable and corrosive gas which has a characteristic odour at a very low concentration. Hydrogen sulphide dissolves in liquid and gaseous streams such as hydrocarbon and water streams and can also be present in the vapour phase above liquid streams as well as in hydrocarbon gas such as LPG and natural gas. The hydrogen sulphide emissions can be harmful to workers operating in the drilling, production, transport, storage, and processing of such streams. It would therefore be desirable for the workers' comfort and safety to reduce or even eliminate the hydrogen sulphide emissions during the handling of said products.
  • a variety of chemical scavengers are available to reduce the concentration of hydrogen sulphide and sulfhydryl-containing compounds in liquid and gaseous streams containing them, in particular aqueous streams and hydrocarbon streams such as gas, crude oils and refined products.
  • Some of the most common methods for treating hydrogen sulphide consist in contacting them with a chemical scavenger such as compounds containing a triazine group, glyoxal, as well as metal-based scavengers.
  • Glyoxal has been used extensively as hydrogen sulphide scavenger but suffers from a major drawback since aqueous glyoxal solutions are highly corrosive and cannot be used for a gas tower application.
  • Triazines have recently become more common chemical scavengers used for treating hydrogen sulphide from hydrocarbon streams.
  • the present invention relates to a composition useful for scavenging hydrogen sulphide and mercaptans in hydrocarbon streams, said composition comprising:
  • composition of the present invention allows achieving an improved scavenging of hydrogen sulphide and organic compounds comprising at least one sulfhydryl group in a short contact time.
  • the improvement can be seen when the remaining amount of sulphur compounds in the stream is reduced and/or when the speed of the scavenging of sulphur compounds is increased when contacting the composition according to the invention with said stream.
  • composition of the present invention allows a faster and more efficient scavenging, i.e. the amount of sulphur compounds is decreased more rapidly and in a greater amount than with prior art scavenging compositions.
  • the present invention also relates to the use of such a composition for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • the invention also relates to the use of a (poly)ethylene glycol of formula (II) as defined above for improving the efficiency of compounds of formula (I) in scavenging hydrogen sulphide and organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • the present invention also relates to a method for scavenging hydrogen sulphide and/or mercaptans comprising contacting a hydrocarbon stream such as crude oil, fuel or natural gas with the scavenging composition of the invention.
  • C N compound or group designates a compound or a group containing in its chemical structure N carbon atoms.
  • composition of the invention comprises at least one compound having the general formula (I): wherein:
  • R' represents CH 3 .
  • R is different from -CHOH-CH 3 .
  • R' represents CH 3 and R is different from -CHOH-CH 3 .
  • a “hydrocarbyl group” is a linear, branched or cyclic group that can be aliphatic or aromatic and when it is a cyclic group, the cycle(s) can be substituted by linear or branched groups.
  • the hydrocarbyl group comprises carbon atoms and hydrogen atoms and optionally heteroatoms selected from oxygen, sulfur, halogen, silicon, nitrogen, preferably selected from oxygen, sulfur, halogen, silicon.
  • R is selected from: R 1 -OH, R 1 -[O-R 2 ]p-OH, optionally substituted benzyl, R 1 -NR 3 R 4 , R 5 , R 1 -[N(H)-R 2 ] n -NR 3 R 4 , R 1 -[O-R 2 ] p -NR 3 R 4 , R 1 -Q, R 1 -[N(H)-R 2 ] n -Q, R 1 -[O-R 2 ] p -Q, R 1 -N(R 3 -Q)(R 4 -Q) wherein:
  • R is selected from: R 1 -OH, R 1 -O-R 2 -OH, optionally substituted benzyl, R 1 -NR 3 R 4 , R 5 , R 1 -N(H)-R 2 -NR 3 R 4 , R 1 -O-R 2 -O-R 2 -NR 3 R 4 , R 1 -Q, R 1 -N(H)-R 2 -Q, R 1 -O-R 2 -O-R 2 -Q, R 1 -N(R 3 -Q) 2 wherein:
  • R is selected from: R 1 -OH, R 1 -O-R 2 -OH, benzyl, R 1 -NR 3 R 4 , R 5 , R 1 -N(H)-R 2 -NR 3 R 4 , R 1 -O-R 2 -O-R 2 -NR 3 R 4 , R 1 -Q, R 1 -N(H)-R 2 -Q, R 1 -O-R 2 -O-R 2 -Q, R 1 -N(R 3 -Q) 2 wherein:
  • an alkyl group is a saturated group consisting in carbon atoms and hydrogen atoms, that can be linear, branched or cyclic.
  • an alkenyl group is an unsaturated group consisting in carbon atoms and hydrogen atoms, that can be linear, branched or cyclic.
  • the alkenyl group can be mono-unsaturated or poly-unsaturated.
  • R 3 is identical to R 4 .
  • the compound(s) of formula (I) is (are) chosen from the following compounds, and mixtures thereof:
  • preferred compound for use in the present invention are selected from compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof.
  • Compounds I-A, I-G, I-L and I-N are particularly preferred.
  • the compound(s) of formula (I) is (are) present in an amount ranging from 50 to 99% by weight, preferably from 60 to 90% by weight, more preferably from 70 to 80% by weight, relative to the total weight of the composition.
  • the compound(s) selected from compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof is (are) present in a total amount ranging from 50 to 99% by weight, preferably from 60 to 90% by weight, more preferably from 70 to 80% by weight, relative to the total weight of the composition.
  • the compound(s) selected from compounds I-A, I-G, I-L and I-N is (are) present in a total amount ranging from 50 to 99% by weight, preferably from 60 to 90% by weight, more preferably from 70 to 80% by weight, relative to the total weight of the composition
  • composition of the invention comprises at least one (poly)ethylene glycol chosen from compounds having the following formula (II): wherein n is an integer ranging from 1 to 30.
  • These compounds correspond to monoethylene glycol and polyethylene glycols containing up to 30 ethylene glycol units.
  • n ranges from 2 to 20, more preferably from 3 to 12.
  • PEG-600 is particularly preferred.
  • said (poly)ethylene glycol(s) is (are) present in a total amount ranging from 0.1 to 30% by weight, preferably from 1 to 20% by weight, more preferably from 5 to 10% by weight, relative to the total weight of the composition.
  • the composition contains at least one compound chosen from PEG-200, PEG-400, PEG-600 and mixtures thereof in a total amount ranging from 0.1 to 30% by weight, preferably from 1 to 20% by weight, more preferably from 2 to 10% by weight, relative to the total weight of the composition.
  • the composition contains PEG-600 in an amount ranging from 0.1 to 30% by weight, preferably from 1 to 20% by weight, more preferably from 2 to 10% by weight, relative to the total weight of the composition.
  • the weight ratio between the total content of compound(s) of formula (I) and the total amount of (poly)ethylene glycol(s) of formula (II) is comprised between 1 and 40, preferably between 10 and 30.
  • the weight ratio between the total content of compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof on one hand and the total amount of (poly)ethylene glycol(s) on the other hand is comprised between 1 and 40, preferably between 10 and 30.
  • the weight ratio between the total content of compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof and the total content of compound(s) chosen from PEG-200, PEG-400, PEG-600 and mixtures thereof on the other hand is comprised between 1 and 40, preferably between 10 and 30.
  • the weight ratio between the total content of compound(s) I-A, I-G, I-L and I-N and mixtures thereof and the total content of PEG-600 is comprised between 1 and 40, preferably between 10 and 30.
  • the composition of the invention further contains one or more liquid solvent(s).
  • liquid it is meant a solvent which is in liquid form at ambient temperature (20°C) and atmospheric pressure (1,013.10 5 Pa).
  • the solvent(s) is (are) selected from water and organic liquid solvents different from the (poly)ethylene glycols described above.
  • the solvent(s) is (are) selected from organic liquid solvents different from said (poly)ethylene glycols.
  • Such solvents may in particular be chosen from poly oxyalkyl ethers, aliphatic hydrocarbons such as alkanes, aromatic solvents such as aromatic hydrocarbons and aromatic hetero-compounds, naphtas, and mixtures thereof.
  • Preferred organic solvents are chosen from aromatic solvents, such as N-methylpyrrolidone, xylene, toluene, benzene; and poly oxyalkyl ethers such as butyl carbitol (diethylene glycol monobutyl ether); as well as mixtures thereof.
  • aromatic solvents such as N-methylpyrrolidone, xylene, toluene, benzene
  • poly oxyalkyl ethers such as butyl carbitol (diethylene glycol monobutyl ether); as well as mixtures thereof.
  • organic solvents include those derived from biomass, such as oils of vegetable origin.
  • a particularly preferred solvent is cashew nutshell liquid, also known as CSNL, which is a widely available vegetable oil derived from cashew nut shell.
  • CSNL cashew nutshell liquid
  • CNSL can be used as a mixture with any other solvent such as those described herein.
  • the choice of the solvent mainly depends on the final use of the composition.
  • water may be a solvent of choice.
  • an organic solvent will be preferred.
  • a solvent having a dual solubility i.e. a water solubility and a solubility in hydrocarbons
  • Poly alkyl ethers such as butyl carbitol are preferred solvents since they have such a dual solubility.
  • composition of the invention advantageously contains an amount of solvent ranging from 5 to 50% by weight, preferably from 10 to 40%wt, more preferably from 20 to 30%wt, relative to the total weight of the composition.
  • composition of the invention may further comprise art least one defoamer, preferably at least one silicone-based defoamer.
  • the defoamers are preferably chosen from polydimethylsiloxane polymers, more preferably from grafted polydimethylsiloxane polymers.
  • composition of the invention advantageously contains an amount of defoamer ranging from 0.1 to 2% by weight, relative to the total weight of the composition.
  • the present invention also encompasses the use of a composition as described above for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • the organic compounds comprising at least one sulfhydryl group are especially chosen from mercaptans, thiocarboxylic acids and dithiocarboxylic acids.
  • the liquid or gaseous stream may be a monophasic stream such as in particular an aqueous stream or an organic stream, or a multiphasic stream containing both water and hydrocarbons (such as for instance oil/water or oil/water/gas or gas/water).
  • the composition of the invention is used for scavenging hydrogen sulphide (H 2 S) and mercaptans (compounds of formula RSH) in a hydrocarbon containing stream.
  • the mercaptans which are eliminated are typically those of formula RSH wherein R is an alkyl or alkenyl group containing from 1 to 8, preferably from 1 to 6 and more preferably from 1 to 4 carbon atoms.
  • the hydrocarbon containing streams are typically selected from crude petroleum oils, hydrocarbon fractions and residues deriving from the distillation thereof, light petroleum gas (LPG) and natural gas, as well as mixtures thereof with aqueous phases such as brine.
  • LPG light petroleum gas
  • natural gas as well as mixtures thereof with aqueous phases such as brine.
  • Such streams contain H 2 S and/or mercaptans in total amounts which may range for example from 1 to 10 000 ppm by weight.
  • the present invention also concerns the use of (poly)ethylene glycol(s) of formula (II) as defined above for improving the efficiency of compound(s) of formula (I) for scavenging hydrogen sulphide (H 2 S) and/or mercaptans in hydrocarbon streams.
  • the present invention also relates to a method for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group such as mercaptans in a liquid or gaseous stream comprising contacting said stream with the composition of the invention.
  • the liquid or gaseous stream may be monophasic such as in particular an aqueous stream or an organic stream, or multiphasic such as a stream containing both water and hydrocarbons (such as for instance oil/water or oil/water/gas or gas/water).
  • the stream contains hydrocarbons.
  • the stream may be especially selected from crude petroleum oils, hydrocarbon fractions and residues deriving from the distillation thereof such as in particular fuel oils and heavy fuel oils, light petroleum gas (LPG) and natural gas, as well as mixtures thereof with aqueous compositions such as brine.
  • LPG light petroleum gas
  • the amount of composition used per amount of stream depends on the concentration of said compound(s) of formula (I) and of (poly)ethylene glycol(s) of formula (II) in the composition as well as the total content of hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in the liquid or gaseous stream, as explained above.
  • composition is contacted with the liquid or gaseous stream for a time sufficient to achieve an effective scavenging of hydrogen sulphide and of organic compounds comprising at least one sulfhydryl group.
  • compositions A1 to A24 (according to the invention) and C1 to C4 (comparative) were prepared by mixing the above ingredients in the amounts detailed Table (I) below: Table (I) I-A I-G I-L I-N PEG-200 PEG-400 PEG-600 Solvent A1 70 - - - 2.5 - - - - - 27.5 A2 70 - - - - 5.0 - - - - 25 A3 70 - - - - - - 2.5 - - - 27.5 A4 70 - - - - - - - - 5.0 - - 25 A5 70 - - - - - - - 2.5 - 27.5 A6 70 - - - - - - - - - 5.0 25 A7 - 70 - - 2.5 - - - - - - - - - - - 5.0 25 A7 - 70 -
  • the test was carried out at room temperature.
  • a 250 mL glass purger was charged with 100 mL of an inert solvent.
  • a gas consisting of N 2 containing H 2 S at a concentration of 50 ppm was released by a bubbling tube at a flow rate of 0.4 mL/min into the solvent contained in said purger.
  • the solvent was continuously agitated by using a magnetic stirrer.
  • the gas exiting the solvent and leaving the purger was conveyed to a H 2 S detector.
  • the gas H 2 S in N 2 at a concentration of 50 ppm
  • the H 2 S detector started recording the H 2 S concentration at the outlet of the purger.
  • the scavenging composition (1ml of said composition is mixed with 2ml of butyl carbitol to ensure proper injection into the reactor) to be tested was quickly injected into the purger.
  • the H 2 S concentration was recorded at every 5 sec time interval.
  • Table (II) Max scavenging obtained (in %) Time required to obtain max scavenging (in sec) Scavenging obtained at the end of test (1800 sec) (in %) A1 72 95 52 A2 70 95 50 A3 74 90 55 A4 76 90 56 A5 75 90 58 A6 77 85 60 A7 78 100 50 A8 80 95 56 A9 73 90 55 A10 75 90 54 A11 74 95 57 A12 76 95 60 A13 81 100 54 A14 79 95 56 A15 78 95 60 A16 82 90 63 A17 79 85 58 A18 78 85 58 A19 82 90 57 A20 84 90 58 A21 82 85 56 A22 80 90 58 A23 80 80 60 A24 85 80 62 C1 54 130 28 C2 60 120 24 C3 56 120 27 C4 62 105 23
  • compositions A1 to A24 according to the invention allow a faster and more efficient scavenging of hydrogen sulfide, than comparative compositions C1 to C4.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention relates to a composition useful for scavenging hydrogen sulphide and organic compounds comprising at least one sulfhydryl group, comprising a particular triazine compound and an additive chosen from (poly)ethylene glycols.
The invention also relates to the use of the composition of the invention for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.

Description

  • The present invention relates to a composition useful for scavenging hydrogen sulphide and organic compounds comprising at least one sulfhydryl group. Said composition comprises a particular triazine compound and an additive chosen from mono- and poly-ethylene glycols.
  • The present invention also relates to the use of such composition for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • The invention also relates to the use of the (poly)ethylene glycol additive for improving the efficiency of triazine compounds in scavenging hydrogen sulphide and organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • The present invention also relates to a method for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group comprising contacting a hydrocarbon stream such as crude oil, fuel or natural gas with the composition of the invention.
  • Hydrogen sulphide (H2S) is a colourless and fairly toxic, flammable and corrosive gas which has a characteristic odour at a very low concentration. Hydrogen sulphide dissolves in liquid and gaseous streams such as hydrocarbon and water streams and can also be present in the vapour phase above liquid streams as well as in hydrocarbon gas such as LPG and natural gas. The hydrogen sulphide emissions can be harmful to workers operating in the drilling, production, transport, storage, and processing of such streams. It would therefore be desirable for the workers' comfort and safety to reduce or even eliminate the hydrogen sulphide emissions during the handling of said products.
  • Legislation has been in place for years, imposing strict regulations on hydrogen sulphide levels of hydrocarbon streams in pipelines, in storage and shipping containers.
  • Similar problems arise with organic compounds comprising a sulfhydryl group (-SH) such as mercaptans R-SH, thiocarboxylic acids RC(O)SH, dithiocarboxylic acids RC(S)SH, with R denoting a hydrocarbon chain. Such sulfhydryl-containing compounds are very corrosive, and are likely to release hydrogen sulphide.
  • A variety of chemical scavengers are available to reduce the concentration of hydrogen sulphide and sulfhydryl-containing compounds in liquid and gaseous streams containing them, in particular aqueous streams and hydrocarbon streams such as gas, crude oils and refined products. Some of the most common methods for treating hydrogen sulphide consist in contacting them with a chemical scavenger such as compounds containing a triazine group, glyoxal, as well as metal-based scavengers. Glyoxal has been used extensively as hydrogen sulphide scavenger but suffers from a major drawback since aqueous glyoxal solutions are highly corrosive and cannot be used for a gas tower application. Triazines have recently become more common chemical scavengers used for treating hydrogen sulphide from hydrocarbon streams.
  • Conventional triazine derivatives, in particular those bearing identical substituants on the three nitrogen ring atoms such as MEA-triazine, have different drawbacks. Therefore, new triazine-based hydrogen sulphide scavengers have been developed recently to overcome these drawbacks.
  • However, the use of these triazine compounds often requires an important contact time in order to be efficient in sulphur removal and thus involves injection of higher doses.
  • There remains a continuous need for novel solutions for eliminating hydrogen sulphide and other compounds comprising a sulfhydryl group in an efficient, economic and safe manner.
  • The Applicant has now discovered that the combination of a particular triazine compound with a specific additive chosen from mono- and poly-ethylene glycols was particularly efficient for scavenging hydrogen sulphide and unwanted organic compounds comprising at least one sulfhydryl group.
  • Therefore, the present invention relates to a composition useful for scavenging hydrogen sulphide and mercaptans in hydrocarbon streams, said composition comprising:
    • at least one compound of formula (I): wherein R is a radical selected from a linear, branched or cyclic hydrocarbyl group optionally comprising one or more heteroatoms, such as oxygen, sulfur, halogen, silicon, nitrogen atoms and R' represents H or CH3, and
    • at least one (poly)ethylene glycol of formula (II): wherein n is an integer ranging from 1 to 30.
  • The composition of the present invention allows achieving an improved scavenging of hydrogen sulphide and organic compounds comprising at least one sulfhydryl group in a short contact time. The improvement can be seen when the remaining amount of sulphur compounds in the stream is reduced and/or when the speed of the scavenging of sulphur compounds is increased when contacting the composition according to the invention with said stream.
  • The composition of the present invention allows a faster and more efficient scavenging, i.e. the amount of sulphur compounds is decreased more rapidly and in a greater amount than with prior art scavenging compositions.
  • The present invention also relates to the use of such a composition for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • The invention also relates to the use of a (poly)ethylene glycol of formula (II) as defined above for improving the efficiency of compounds of formula (I) in scavenging hydrogen sulphide and organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • The present invention also relates to a method for scavenging hydrogen sulphide and/or mercaptans comprising contacting a hydrocarbon stream such as crude oil, fuel or natural gas with the scavenging composition of the invention.
  • In the following, and at least one other indication, the limits of a value range are included within this range, particularly in the expressions "between" and "ranging from ... to ...".
  • Moreover, the expressions "at least one" and "at least" used in the present description are respectively equivalent to the expressions "one or more" and "more than or equal to".
  • Finally, in a manner known per se, CN compound or group designates a compound or a group containing in its chemical structure N carbon atoms.
  • Within the meaning of the present invention:
    • the term "acyclic alkyl" refers to an alkyl group which does not form part of a cycle,
    • the term "acyclic alkenyl" refers to an alkenyl group which does not form part of a cycle,
    • the term "cyclic alkyl" refers to a saturated cycloalkyl group, wherein the cycle can be optionally substituted by one or more linear or branched alkyl or alkenyl groups. Preferably, the cycle comprises 5 or 6 carbon atoms and the substituent(s) if any comprise(s) from 1 to 6 carbon atoms, preferably from 1 to 3 carbon atoms,
    • the term "cyclic alkenyl" refers to an unsaturated cycloalkyl group, wherein the cycle comprising at least one unsaturation can be optionally substituted by one or more linear or branched alkyl or alkenyl groups. Preferably, the cycle comprises 5 or 6 carbon atoms and the substituent(s) if any comprise(s) from 1 to 6 carbon atoms, preferably from 1 to 3 carbon atoms.
    Compound of formula (I)
  • The composition of the invention comprises at least one compound having the general formula (I): wherein:
    • R is a radical selected from a linear, branched or cyclic hydrocarbyl group optionally comprising one or more heteroatoms, such as oxygen, sulfur, halogen, silicon and nitrogen atoms and
    • R' represents H or CH3.
  • According to a preferred embodiment, R' represents CH3.
  • According to a preferred embodiment, R is different from -CHOH-CH3.
  • According to a most preferred embodiment, R' represents CH3 and R is different from -CHOH-CH3.
  • Within the meaning of the present invention, a "hydrocarbyl group" is a linear, branched or cyclic group that can be aliphatic or aromatic and when it is a cyclic group, the cycle(s) can be substituted by linear or branched groups. The hydrocarbyl group comprises carbon atoms and hydrogen atoms and optionally heteroatoms selected from oxygen, sulfur, halogen, silicon, nitrogen, preferably selected from oxygen, sulfur, halogen, silicon.
  • According to an embodiment, R is selected from: R1-OH, R1-[O-R2]p-OH, optionally substituted benzyl, R1-NR3R4, R5, R1-[N(H)-R2]n-NR3R4, R1-[O-R2]p-NR3R4, R1-Q, R1-[N(H)-R2]n-Q, R1-[O-R2]p-Q, R1-N(R3-Q)(R4-Q) wherein:
    • R1 is selected from a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 24 carbon atoms, preferably from 1 to 16 carbon atoms, more preferably from 1 to 12 carbon atoms, even more preferably from 1 to 8 carbon atoms or from an aromatic radical optionally substituted by one or more substituent selected from C1-C6-alkyl, hydroxyl, C1-C6-alkoxy, or C1-C6-alkylamine, preferably a phenyl radical substituted by C1-C6-alkyl;
    • R2 is a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 24 carbon atoms, preferably from 1 to 16 carbon atoms, more preferably from 1 to 12 carbon atoms, even more preferably from 1 to 8 carbon atoms;
    • R3 and R4 are, independently to each other, a hydrogen atom or a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 16 carbon atoms, preferably from 1 to 12 carbon atoms, more preferably from 1 to 8 carbon atoms, even more preferably from 1 to 4 carbon atoms;
    • R5 is a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 30 carbon atoms, preferably from 1 to 24 carbon atoms, more preferably from 1 to 16 carbon atoms, even more preferably from 1 to 12 carbon atoms;
    • Q is a radical selected from morpholine, piperidine, piperazine, or the monovalent radical of formula:
    • the optionally substituted benzyl can be a benzyl substituted by one or more substituent selected from C1-C6-alkyl, hydroxyl, C1-C6-alkoxy, C1-C6-alkylamine;
    • n is an integer ranging from 1 to 10, preferably from 1 to 6, more preferably from 1 to 4, even more preferably from 1 to 2;
    • p is an integer ranging from 1 to 10, preferably from 1 to 6, more preferably from 1 to 4, even more preferably from 1 to 2.
  • According to a preferred embodiment, R is selected from: R1-OH, R1-O-R2-OH, optionally substituted benzyl, R1-NR3R4, R5, R1-N(H)-R2-NR3R4, R1-O-R2-O-R2-NR3R4, R1-Q, R1-N(H)-R2-Q, R1-O-R2-O-R2-Q, R1-N(R3-Q)2 wherein:
    • R1 is selected from a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 24 carbon atoms, preferably from 1 to 16 carbon atoms, more preferably from 1 to 12 carbon atoms, even more preferably from 1 to 8 carbon atoms or from a phenyl radical substituted by C1-C6-alkyl;
    • R2 is a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 24 carbon atoms, preferably from 1 to 16 carbon atoms, more preferably from 1 to 12 carbon atoms, even more preferably from 1 to 8 carbon atoms;
    • R3 and R4 are, independently to each other, a hydrogen atom or a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 16 carbon atoms, preferably from 1 to 12 carbon atoms, more preferably from 1 to 8 carbon atoms, even more preferably from 1 to 4 carbon atoms;
    • R5 is a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 30 carbon atoms, preferably from 1 to 24 carbon atoms, more preferably from 1 to 16 carbon atoms, even more preferably from 1 to 12 carbon atoms;
    • Q is a morpholine radical or the monovalent radical of formula:
    • the optionally substituted benzyl can be a benzyl substituted by one or more substituent selected from C1-C6-alkyl, hydroxyl, C1-C6-alkoxy, C1-C6-alkylamine.
  • According to a more preferred embodiment, R is selected from: R1-OH, R1-O-R2-OH, benzyl, R1-NR3R4, R5, R1-N(H)-R2-NR3R4, R1-O-R2-O-R2-NR3R4, R1-Q, R1-N(H)-R2-Q, R1-O-R2-O-R2-Q, R1-N(R3-Q)2 wherein:
    • R1 is selected from a linear or branched alkyl radical having from 1 to 16 carbon atoms, preferably from 1 to 12 carbon atoms, more preferably from 1 to 8 carbon atoms, even more preferably from 1 to 4 carbon atoms or from a phenyl radical substituted by C1-C6-alkyl;
    • R2 is a linear or branched alkyl radical having from 1 to 16 carbon atoms, preferably from 1 to 12 carbon atoms, more preferably from 1 to 8 carbon atoms, even more preferably from 1 to 4 carbon atoms;
    • R3 and R4 are, independently to each other, a hydrogen atom or a linear or branched alkyl radical having from 1 to 16 carbon atoms, preferably from 1 to 12 carbon atoms, more preferably from 1 to 8 carbon atoms, even more preferably from 1 to 4 carbon atoms;
    • R5 is a linear or branched alkyl radical having from 1 to 24 carbon atoms, preferably from 1 to 16 carbon atoms, more preferably from 1 to 12 carbon atoms, even more preferably from 1 to 8 carbon atoms;
    • Q is a morpholine radical or the monovalent radical of formula:
  • Within the meaning of the present invention, an alkyl group is a saturated group consisting in carbon atoms and hydrogen atoms, that can be linear, branched or cyclic.
  • Within the meaning of the present invention, an alkenyl group is an unsaturated group consisting in carbon atoms and hydrogen atoms, that can be linear, branched or cyclic. The alkenyl group can be mono-unsaturated or poly-unsaturated.
  • According to a preferred embodiment, R3 is identical to R4.
  • According to a most preferred embodiment, the compound(s) of formula (I) is (are) chosen from the following compounds, and mixtures thereof:
  • Among the compounds disclosed above, preferred compound for use in the present invention are selected from compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof. Compounds I-A, I-G, I-L and I-N are particularly preferred.
  • Preferably, the compound(s) of formula (I) is (are) present in an amount ranging from 50 to 99% by weight, preferably from 60 to 90% by weight, more preferably from 70 to 80% by weight, relative to the total weight of the composition.
  • In a preferred embodiment, the compound(s) selected from compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof is (are) present in a total amount ranging from 50 to 99% by weight, preferably from 60 to 90% by weight, more preferably from 70 to 80% by weight, relative to the total weight of the composition.
  • In a more preferred embodiment, the compound(s) selected from compounds I-A, I-G, I-L and I-N is (are) present in a total amount ranging from 50 to 99% by weight, preferably from 60 to 90% by weight, more preferably from 70 to 80% by weight, relative to the total weight of the composition
  • (Poly)Ethylene glycols
  • The composition of the invention comprises at least one (poly)ethylene glycol chosen from compounds having the following formula (II): wherein n is an integer ranging from 1 to 30.
  • These compounds correspond to monoethylene glycol and polyethylene glycols containing up to 30 ethylene glycol units.
  • Preferably, n ranges from 2 to 20, more preferably from 3 to 12.
  • Preferably, the (poly)ethylene glycol(s) is (are) chosen from PEG-200 (compound of formula (II) with n=4), PEG-400 (compound of formula (II) with n=8), PEG-600 (compound of formula (II) with n=12) and mixtures thereof. PEG-600 is particularly preferred.
  • Preferably, said (poly)ethylene glycol(s) is (are) present in a total amount ranging from 0.1 to 30% by weight, preferably from 1 to 20% by weight, more preferably from 5 to 10% by weight, relative to the total weight of the composition.
  • In a preferred embodiment, the composition contains at least one compound chosen from PEG-200, PEG-400, PEG-600 and mixtures thereof in a total amount ranging from 0.1 to 30% by weight, preferably from 1 to 20% by weight, more preferably from 2 to 10% by weight, relative to the total weight of the composition.
  • In a more preferred embodiment, the composition contains PEG-600 in an amount ranging from 0.1 to 30% by weight, preferably from 1 to 20% by weight, more preferably from 2 to 10% by weight, relative to the total weight of the composition.
  • Preferably, the weight ratio between the total content of compound(s) of formula (I) and the total amount of (poly)ethylene glycol(s) of formula (II) is comprised between 1 and 40, preferably between 10 and 30.
  • According to an embodiment, the weight ratio between the total content of compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof on one hand and the total amount of (poly)ethylene glycol(s) on the other hand is comprised between 1 and 40, preferably between 10 and 30.
  • According to another embodiment, the weight ratio between the total content of compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof and the total content of compound(s) chosen from PEG-200, PEG-400, PEG-600 and mixtures thereof on the other hand is comprised between 1 and 40, preferably between 10 and 30.
  • According to another embodiment, the weight ratio between the total content of compound(s) I-A, I-G, I-L and I-N and mixtures thereof and the total content of PEG-600 is comprised between 1 and 40, preferably between 10 and 30.
  • Liquid solvents
  • According to a preferred embodiment, the composition of the invention further contains one or more liquid solvent(s).
  • By liquid, it is meant a solvent which is in liquid form at ambient temperature (20°C) and atmospheric pressure (1,013.105 Pa).
  • According to a preferred embodiment, the solvent(s) is (are) selected from water and organic liquid solvents different from the (poly)ethylene glycols described above.
  • According to a preferred embodiment, the solvent(s) is (are) selected from organic liquid solvents different from said (poly)ethylene glycols.
  • Such solvents may in particular be chosen from poly oxyalkyl ethers, aliphatic hydrocarbons such as alkanes, aromatic solvents such as aromatic hydrocarbons and aromatic hetero-compounds, naphtas, and mixtures thereof.
  • Preferred organic solvents are chosen from aromatic solvents, such as N-methylpyrrolidone, xylene, toluene, benzene; and poly oxyalkyl ethers such as butyl carbitol (diethylene glycol monobutyl ether); as well as mixtures thereof.
  • Other preferred organic solvents include those derived from biomass, such as oils of vegetable origin. A particularly preferred solvent is cashew nutshell liquid, also known as CSNL, which is a widely available vegetable oil derived from cashew nut shell. CNSL can be used as a mixture with any other solvent such as those described herein.
  • The choice of the solvent mainly depends on the final use of the composition. When the composition is intended to be used for scavenging hydrogen sulphide and/or sulfhydryl-containing compounds in an aqueous stream, water may be a solvent of choice. When the composition is intended to be used for scavenging hydrogen sulphide and/or sulfhydryl-containing compounds in a hydrocarbon stream, an organic solvent will be preferred.
  • When the stream is a mixture of water and hydrocarbons (such as a mixture of crude oil and brine) a solvent having a dual solubility, i.e. a water solubility and a solubility in hydrocarbons, can be preferred. Poly alkyl ethers such as butyl carbitol are preferred solvents since they have such a dual solubility.
  • The composition of the invention advantageously contains an amount of solvent ranging from 5 to 50% by weight, preferably from 10 to 40%wt, more preferably from 20 to 30%wt, relative to the total weight of the composition.
  • Defoamer
  • The composition of the invention may further comprise art least one defoamer, preferably at least one silicone-based defoamer.
  • The defoamers are preferably chosen from polydimethylsiloxane polymers, more preferably from grafted polydimethylsiloxane polymers.
  • The composition of the invention advantageously contains an amount of defoamer ranging from 0.1 to 2% by weight, relative to the total weight of the composition.
  • Use
  • The present invention also encompasses the use of a composition as described above for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in a liquid or gaseous stream.
  • The organic compounds comprising at least one sulfhydryl group are especially chosen from mercaptans, thiocarboxylic acids and dithiocarboxylic acids.
  • The liquid or gaseous stream may be a monophasic stream such as in particular an aqueous stream or an organic stream, or a multiphasic stream containing both water and hydrocarbons (such as for instance oil/water or oil/water/gas or gas/water).
  • According to a preferred embodiment, the composition of the invention is used for scavenging hydrogen sulphide (H2S) and mercaptans (compounds of formula RSH) in a hydrocarbon containing stream.
  • The mercaptans which are eliminated are typically those of formula RSH wherein R is an alkyl or alkenyl group containing from 1 to 8, preferably from 1 to 6 and more preferably from 1 to 4 carbon atoms.
  • The hydrocarbon containing streams are typically selected from crude petroleum oils, hydrocarbon fractions and residues deriving from the distillation thereof, light petroleum gas (LPG) and natural gas, as well as mixtures thereof with aqueous phases such as brine.
  • Such streams contain H2S and/or mercaptans in total amounts which may range for example from 1 to 10 000 ppm by weight.
  • The present invention also concerns the use of (poly)ethylene glycol(s) of formula (II) as defined above for improving the efficiency of compound(s) of formula (I) for scavenging hydrogen sulphide (H2S) and/or mercaptans in hydrocarbon streams.
  • Method
  • The present invention also relates to a method for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group such as mercaptans in a liquid or gaseous stream comprising contacting said stream with the composition of the invention.
  • As described above, the liquid or gaseous stream may be monophasic such as in particular an aqueous stream or an organic stream, or multiphasic such as a stream containing both water and hydrocarbons (such as for instance oil/water or oil/water/gas or gas/water).
  • According to a preferred embodiment, the stream contains hydrocarbons. The stream may be especially selected from crude petroleum oils, hydrocarbon fractions and residues deriving from the distillation thereof such as in particular fuel oils and heavy fuel oils, light petroleum gas (LPG) and natural gas, as well as mixtures thereof with aqueous compositions such as brine.
  • The amount of composition used per amount of stream depends on the concentration of said compound(s) of formula (I) and of (poly)ethylene glycol(s) of formula (II) in the composition as well as the total content of hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group in the liquid or gaseous stream, as explained above.
  • The composition is contacted with the liquid or gaseous stream for a time sufficient to achieve an effective scavenging of hydrogen sulphide and of organic compounds comprising at least one sulfhydryl group.
  • The examples hereafter only aim at illustrating the present invention and shall not be interpreted so as to limit its scope.
  • Examples Preparation of compositions
  • The following ingredients were used:
    • as compounds of formula (I): compounds I-A, I-G, I-L and I-N as disclosed above;
    • as polyethylene glycols having the following formula (II): PEG-200, PEG-400 and PEG-600;
    • as solvent: butyl carbitol
  • Compositions A1 to A24 (according to the invention) and C1 to C4 (comparative) were prepared by mixing the above ingredients in the amounts detailed Table (I) below: Table (I)
    I-A I-G I-L I-N PEG-200 PEG-400 PEG-600 Solvent
    A1 70 - - - 2.5 - - - - - 27.5
    A2 70 - - - - 5.0 - - - - 25
    A3 70 - - - - - 2.5 - - - 27.5
    A4 70 - - - - - - 5.0 - - 25
    A5 70 - - - - - - - 2.5 - 27.5
    A6 70 - - - - - - - - 5.0 25
    A7 - 70 - - 2.5 - - - - - 27.5
    A8 - 70 - - - 5.0 - - - - 25
    A9 - 70 - - - - 2.5 - - - 27.5
    A10 - 70 - - - - - 5.0 - - 25
    A11 - 70 - - - - - - 2.5 - 27.5
    A12 - 70 - - - - - - - 5.0 25
    A13 - - 70 - 2.5 - - - - - 27.5
    A14 - - 70 - - 5.0 - - - - 25
    A15 - - 70 - - - 2.5 - - - 27.5
    A16 - - 70 - - - - 5.0 - - 25
    A17 - - 70 - - - - - 2.5 - 27.5
    A18 - - 70 - - - - - - 5.0 25
    A19 - - - 70 2.5 - - - - - 27.5
    A20 - - - 70 - 5.0 - - - - 25
    A21 - - - 70 - - 2.5 - - - 27.5
    A22 - - - 70 - - - 5.0 - - 25
    A23 - - - 70 - - - - 2.5 - 27.5
    A24 - - - 70 - - - - - 5.0 25
    C1 70 - - - - - - - - - 30
    C2 - 70 - - - - - - - - 30
    C3 - - 70 - - - - - - - 30
    C4 - - - 70 - - - - - - 30
  • Assessment of H2S scavenging ability
  • The performance of each composition for scavenging H2S was assessed by means of a H2S scavenging test carried out following the protocol detailed below.
  • The test was carried out at room temperature. A 250 mL glass purger was charged with 100 mL of an inert solvent. A gas consisting of N2 containing H2S at a concentration of 50 ppm was released by a bubbling tube at a flow rate of 0.4 mL/min into the solvent contained in said purger. The solvent was continuously agitated by using a magnetic stirrer. The gas exiting the solvent and leaving the purger was conveyed to a H2S detector.
  • At the beginning of each test, a setup was made as follows: the gas (H2S in N2 at a concentration of 50 ppm) was passed through the purger with a 0.4 mL/min flow rate, and the H2S detector started recording the H2S concentration at the outlet of the purger. Once the outlet H2S concentration remained stable (with a value of 50 ppm constant reading at the detector), the scavenging composition (1ml of said composition is mixed with 2ml of butyl carbitol to ensure proper injection into the reactor) to be tested was quickly injected into the purger. As the scavenging composition starts reacting with H2S which results in a reduction of the H2S concentration at the outlet, as recorded by the detector. The H2S concentration was recorded at every 5 sec time interval.
  • An interval of time of 30 min was respected between each test. In each test, once the H2S scavenger has been injected into the purger, the concentration of H2S recorded by the detector started decreasing from 50 ppm down towards 0 ppm, depending on the efficiency of the scavenging composition. The higher the H2S scavenging efficiency of the composition, the faster the H2S concentration recorded by the detector drops and the longer the rate of H2S concentration recorded by the detector remains low. It was also observed that, once the scavenging composition was consumed, the concentration of H2S recorded by the detector started increasing slowly back to 50 ppm.
  • Results
  • The results obtained are detailed in Table (II) below: Table (II)
    Max scavenging obtained (in %) Time required to obtain max scavenging (in sec) Scavenging obtained at the end of test (1800 sec) (in %)
    A1 72 95 52
    A2 70 95 50
    A3 74 90 55
    A4 76 90 56
    A5 75 90 58
    A6 77 85 60
    A7 78 100 50
    A8 80 95 56
    A9 73 90 55
    A10 75 90 54
    A11 74 95 57
    A12 76 95 60
    A13 81 100 54
    A14 79 95 56
    A15 78 95 60
    A16 82 90 63
    A17 79 85 58
    A18 78 85 58
    A19 82 90 57
    A20 84 90 58
    A21 82 85 56
    A22 80 90 58
    A23 80 80 60
    A24 85 80 62
    C1 54 130 28
    C2 60 120 24
    C3 56 120 27
    C4 62 105 23
  • The above results show that compositions A1 to A24 according to the invention allow a faster and more efficient scavenging of hydrogen sulfide, than comparative compositions C1 to C4.

Claims (15)

  1. A composition comprising:
    - least one compound of formula (I): wherein R is a radical selected from a linear, branched or cyclic hydrocarbyl group optionally comprising one or more heteroatoms, such as oxygen, sulfur, halogen, silicon, nitrogen atoms and R' represents H or CH3, and
    - at least (poly)ethylene glycol of formula (II): wherein n is an integer ranging from 1 to 30.
  2. A composition as defined in claim 1 wherein R' represents CH3.
  3. A composition as defined in any preceding claim, wherein in formula (I) R is selected from: R1-OH, R1-[O-R2]p-OH, optionally substituted benzyl, R1-NR3R4, R5,R1-[N(H)-R2]n-NR3R4, R1-[O-R2]p-NR3R4, R1-Q, R1-[N(H)-R2]n-Q, R1-[O-R2]p-Q, R1-N(R3-Q)(R4-Q) wherein:
    - R1 is selected from a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 24 carbon atoms, preferably from 1 to 16 carbon atoms, more preferably from 1 to 12 carbon atoms, even more preferably from 1 to 8 carbon atoms or from an aromatic radical optionally substituted by one or more substituent selected from C1-C6-alkyl, hydroxyl, C1-C6-alkoxy, or C1-C6-alkylamine, preferably a phenyl radical substituted by C1-C6-alkyl;
    - R2 is a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 24 carbon atoms, preferably from 1 to 16 carbon atoms, more preferably from 1 to 12 carbon atoms, even more preferably from 1 to 8 carbon atoms;
    - R3 and R4 are, independently to each other, a hydrogen atom or a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 16 carbon atoms, preferably from 1 to 12 carbon atoms, more preferably from 1 to 8 carbon atoms, even more preferably from 1 to 4 carbon atoms;
    - R5 is a linear, branched or cyclic alkyl or alkenyl radical having from 1 to 30 carbon atoms, preferably from 1 to 24 carbon atoms, more preferably from 1 to 16 carbon atoms, even more preferably from 1 to 12 carbon atoms;
    - Q is a radical selected from morpholine, piperidine, piperazine, or the monovalent radical of formula:
    - the optionally substituted benzyl can be a benzyl substituted by one or more substituent selected from C1-C6-alkyl, hydroxyl, C1-C6-alkoxy, C1-C6-alkylamine;
    - n is an integer ranging from 1 to 10, preferably from 1 to 6, more preferably from 1 to 4, even more preferably from 1 to 2;
    - p is an integer ranging from 1 to 10, preferably from 1 to 6, more preferably from 1 to 4, even more preferably from 1 to 2.
  4. A composition as defined in any preceding claim, wherein said compound of formula (I) is chosen from the following compounds, and mixtures thereof: preferably from compound I-A, compound I-B, compound I-C, compound I-D, compound I-E-, compound I-F, compound I-G, compound I-H, compound I-I, compound I-K, compound I-L, and mixture thereof; and more preferably from compounds I-A, I-G, I-L and I-N and mixtures thereof.
  5. A composition as defined in any preceding claim, wherein the compound(s) of formula (I) is (are) present in an amount ranging from 50 to 99% by weight, preferably from 60 to 90% by weight, more preferably from 70 to 80% by weight, relative to the total weight of the composition.
  6. A composition as defined in any preceding claim, wherein the (poly)ethylene glycols are chosen from compounds of formula (II) wherein n ranges from 2 to 20, preferably from 3 to 12.
  7. A composition as defined in any preceding claim, wherein the (poly)ethylene glycols are chosen from PEG-200, PEG-400, PEG-600 and mixtures thereof, and preferably PEG-600.
  8. A composition as defined in any preceding claim, wherein said (poly)ethylene glycol(s) is (are) present in a total amount ranging from 0.1 to 30% by weight, preferably from 1 to 20% by weight, more preferably from 2 to 10% by weight, relative to the total weight of the composition.
  9. A composition as defined in any preceding claim, wherein the weight ratio between the total amount of compound(s) of formula (I) and the total amount of (poly)ethylene glycol(s) of formula (II) is comprised between 1 and 40, preferably between 10 and 30.
  10. A composition as defined in any preceding claim further containing one or more liquid solvent(s).
  11. A composition as defined in claim 10, wherein the solvent(s) is (are) chosen from water and organic solvents different from (poly)ethylene glycol compounds of formula (II), preferably from aromatic solvents, poly oxyalkyl ethers, naphtas and organic solvents derived from biomass; more preferably from aromatic solvents, such as N-methylpyrrolidone, xylene, toluene, benzene; poly oxyalkyl ethers such as butyl carbitol ; and mixtures thereof.
  12. A composition as defined in anyone of claims 10 and 11, wherein the solvent(s) is (are) present in an amount ranging from 5 to 50% by weight, preferably from 10 to 40% by weight, more preferably from 20 to 30% by weight, relative to the total weight of the composition.
  13. Use of a composition as defined in anyone of claims 1 to 12 for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group such as mercaptans in a liquid or gaseous stream.
  14. Use of at least one (poly)ethylene glycol of formula (II) as defined in anyone of claims 1, 6 and 7 for improving the efficiency of compound(s) of formula (I) in scavenging hydrogen sulphide (H2S) and/or organic compounds comprising at least one sulfhydryl group such as mercaptans in a liquid or gaseous stream, preferably in a hydrocarbon stream.
  15. Method for scavenging hydrogen sulphide and/or organic compounds comprising at least one sulfhydryl group such as mercaptans in a liquid or gaseous stream, comprising contacting said stream with a composition as defined in anyone of claims 1 to 12.
EP24305854.2A 2024-05-30 2024-05-30 Hydrogen sulphide and mercaptan scavenging composition comprising a particular triazine compound and a (poly)ethylene glycol Pending EP4656707A1 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20210276917A1 (en) * 2020-03-06 2021-09-09 United States Gypsum Company Low shrinkage, fast drying spackling or joint compound
US20210389255A1 (en) * 2020-06-16 2021-12-16 Conocophillips Company Testing H2S Scavengers Polymerization Factors
CN115501731A (en) * 2021-06-07 2022-12-23 中国石油化工股份有限公司 For removing H from sulfur-containing gases 2 S absorption liquid, preparation method and application
WO2023036969A1 (en) * 2021-09-13 2023-03-16 Totalenergies Onetech Hydrogen sulphide and mercaptans scavengers

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20210276917A1 (en) * 2020-03-06 2021-09-09 United States Gypsum Company Low shrinkage, fast drying spackling or joint compound
US20210389255A1 (en) * 2020-06-16 2021-12-16 Conocophillips Company Testing H2S Scavengers Polymerization Factors
CN115501731A (en) * 2021-06-07 2022-12-23 中国石油化工股份有限公司 For removing H from sulfur-containing gases 2 S absorption liquid, preparation method and application
WO2023036969A1 (en) * 2021-09-13 2023-03-16 Totalenergies Onetech Hydrogen sulphide and mercaptans scavengers

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