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TW201816098A - Composition for removing iron sulfide - Google Patents

Composition for removing iron sulfide Download PDF

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TW201816098A
TW201816098A TW106121359A TW106121359A TW201816098A TW 201816098 A TW201816098 A TW 201816098A TW 106121359 A TW106121359 A TW 106121359A TW 106121359 A TW106121359 A TW 106121359A TW 201816098 A TW201816098 A TW 201816098A
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iron sulfide
methyl
composition
carbon atoms
acrolein
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TW106121359A
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清水將貴
齊藤勇祐
靍田拓大
藤純市
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可樂麗股份有限公司
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    • CCHEMISTRY; METALLURGY
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    • C10G75/00Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general
    • C10G75/02Inhibiting corrosion or fouling in apparatus for treatment or conversion of hydrocarbon oils, in general by addition of corrosion inhibitors
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    • 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
    • C10G21/00Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
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    • C10G21/16Oxygen-containing compounds
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10G25/00Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
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    • 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
    • C10G29/22Organic compounds not containing metal atoms containing oxygen as the only hetero atom
    • C10G29/24Aldehydes or ketones
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    • 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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
    • C10G9/16Preventing or removing incrustation
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    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
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    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G5/00Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents
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    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G5/00Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents
    • C23G5/02Cleaning or de-greasing metallic material by other methods; Apparatus for cleaning or de-greasing metallic material with organic solvents using organic solvents

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
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Abstract

Provided is a composition for removing iron sulfide, the composition containing an [alpha], [beta]-unsaturated aldehyde represented by general formula (1) as an active ingredient (wherein: R1-R3 each independently represent a hydrogen atom, an alkyl group having 1-10 carbon atoms, an alkenyl group having 2-10 carbon atoms, or an aryl group having 6-12 carbon atoms; R1 may be bonded with R2 or R3 to form an alkylene group having 2-6 carbon atoms; and R1 and R2 would not simultaneously be hydrogen atoms).

Description

去除硫化鐵用之組成物    Composition for removing iron sulfide   

本發明係關於去除硫化鐵用之組成物、及使用其的硫化鐵之去除方法。 The present invention relates to a composition for removing iron sulfide and a method for removing iron sulfide using the same.

在天然氣、液化天然氣、酸氣、原油、石油腦、重質芳香族石油腦、汽油、煤油、柴油、輕油、重油、FCC漿料、柏油、油田濃縮物等的化石燃料或精製石油製品等的烴中常常存在的硫化氫,會腐蝕掘削設備等所使用的鐵而成為產生硫化鐵的原因。硫化鐵由於會在化石燃料或精製石油製品的製造設備內累積成為堆積物,而降低熱交換器、冷卻塔、反應容器、輸送管道或爐等的機器類之操作效率或妨礙用於設備保全的正確測定,所以最好將其去除。 Fossil fuels or refined petroleum products such as natural gas, liquefied natural gas, sour gas, crude oil, petroleum brain, heavy aromatic petroleum brain, gasoline, kerosene, diesel, light oil, heavy oil, FCC slurry, asphalt, oil field concentrates, etc. Hydrogen sulfide, which is often present in hydrocarbons, corrodes iron used in excavation equipment, etc., and causes iron sulfide. Iron sulfide accumulates as deposits in the manufacturing facilities of fossil fuels or refined petroleum products, reducing the operating efficiency of machinery such as heat exchangers, cooling towers, reaction vessels, pipelines, or furnaces, or preventing the use of equipment for equipment maintenance. Correct measurement, so it is best to remove it.

作為去除硫化鐵之方法,已知有使用丙烯醛以融化硫化鐵之方法,於2011年10月30日~11月2日在美國科羅拉多州丹佛所舉行的SPE Annual Technical Conference and Exhibition SPE 146080中,亦發表了關於以丙烯醛為有效成分的硫化鐵去除。但是,丙烯醛係毒性強,在勞動安全上及環境安全上嚴格規定其濃度的化合物,會有在處理上需要注意的問題。此外,丙烯醛係極為容易聚合,在欠缺熱安定性方面,或從欠缺pH 安定性,會因為使用之環境的pH而緩緩地減少存在量方面,在處理上也會成為問題。 As a method for removing iron sulfide, a method of using acrolein to melt iron sulfide is known. In the SPE Annual Technical Conference and Exhibition SPE 146080 held in Denver, Colorado, USA from October 30, 2011 to November 2, 2011, The removal of iron sulfide using acrolein as an active ingredient has also been published. However, acrolein is a highly toxic compound whose concentration is strictly regulated in terms of labor safety and environmental safety, and there are problems that require attention in handling. In addition, acrolein is extremely easy to polymerize. In terms of lack of thermal stability, or lack of pH stability, it gradually decreases the amount of presence due to the pH of the environment in which it is used, and it also becomes a problem in handling.

先前技術文獻Prior art literature 非專利文獻Non-patent literature

非專利文獻1 SPE Annual Technical Conference and Exhibition SPE 146080, 2011年;http://dx.doi.org/10.2118/146080-MS Non-Patent Literature 1 SPE Annual Technical Conference and Exhibition SPE 146080, 2011; http://dx.doi.org/10.2118/146080-MS

如上所述,以去除硫化鐵為目的而使用丙烯醛,會在安全性或熱安定性、及pH安定性方面有問題,而期望更安全且安定的化合物來代替。從而,本發明的目的在於提供具有熱安定性及pH安定性高的有效成分,而且能安全且效率良好地去除硫化鐵之組成物。 As described above, the use of acrolein for the purpose of removing iron sulfide has problems in terms of safety, thermal stability, and pH stability, and a safer and more stable compound is desired instead. Therefore, an object of the present invention is to provide a composition having an active ingredient having high thermal stability and high pH stability, and capable of removing iron sulfide safely and efficiently.

根據本發明,上述之目的可藉由下述[1]至[7]而達成。 According to the present invention, the above-mentioned objects can be achieved by the following [1] to [7].

[1]一種去除硫化鐵用之組成物,其含有下述通式(1)所示之α,β-不飽和醛(以下,稱為醛(1))為有效成分。 [1] A composition for removing iron sulfide, which contains an α, β-unsaturated aldehyde (hereinafter, referred to as an aldehyde (1)) as an active ingredient represented by the following general formula (1).

(R1~R3各自獨立表示氫原子、碳數1~10的烷基、碳數2~10的烯基或碳數6~12的芳基。其中,R1 可與R2或R3互相連結以構成碳數2~6的伸烷基,R1與R2不同時為氫原子。) (R 1 to R 3 each independently represent a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, an alkenyl group having 2 to 10 carbon atoms, or an aryl group having 6 to 12 carbon atoms. Among them, R 1 and R 2 or R 3 They are connected to each other to form an alkylene group having 2 to 6 carbon atoms, and R 1 and R 2 are not hydrogen atoms at the same time.)

[2]如[1]之組成物,其中R1~R3各自獨立為氫原子或碳數1~5的烷基。 [2] The composition according to [1], wherein R 1 to R 3 are each independently a hydrogen atom or an alkyl group having 1 to 5 carbon atoms.

[3]如[1]或[2]之組成物,其中R3為氫原子。 [3] The composition according to [1] or [2], wherein R 3 is a hydrogen atom.

[4]一種硫化鐵之去除方法,其特徵係使如[1]至[3]中任一項之組成物接觸硫化鐵。 [4] A method for removing iron sulfide, characterized in that the composition according to any one of [1] to [3] is brought into contact with iron sulfide.

[5]如[4]之方法,其中相對於硫化鐵1質量份,添加前述組成物中的醛(1)使其成為0.1~100質量份。 [5] The method according to [4], wherein the aldehyde (1) in the composition is added to 0.1 to 100 parts by mass based on 1 part by mass of iron sulfide.

[6]如[4]或[5]之方法,其係使該組成物中的醛(1)與硫化鐵在-30℃~150℃的範圍接觸。 [6] The method according to [4] or [5], wherein the aldehyde (1) in the composition is brought into contact with iron sulfide in a range of -30 ° C to 150 ° C.

[7]一種如[1]至[3]中任一項之組成物之用途,其係用於去除硫化鐵。 [7] Use of a composition according to any one of [1] to [3], which is for removing iron sulfide.

本發明的組成物係藉由含有醛(1),而硫化鐵的去除性能優異。 The composition of the present invention is excellent in the removal performance of iron sulfide by containing aldehyde (1).

尤其是與含有丙烯醛之以往的硫化鐵去除劑相比,本發明的組成物具有毒性極低,熱安定性及pH安定性高的優點。其理由雖未必清楚,但醛(1)由於在β位具有至少1個烷基、烯基或芳基,所以與在β位不具有取代基的丙烯醛相比,認為生物分子或生長鏈等的體積大的分子於β位不易引起加成反應為主要因素之一。另一方面,關於硫化鐵的去除,雖認為結合硫化鐵與在平衡狀態的硫化氫,藉此將其去除會促進硫化鐵的溶解,結果硫化鐵被去除,但認為即使在β位具有取代基,也並不 那麼妨礙來自一般小分子之硫化氫的攻撃,而硫化鐵去除性能受到保持。 In particular, compared with the conventional iron sulfide remover containing acrolein, the composition of the present invention has the advantages of extremely low toxicity, high thermal stability, and high pH stability. Although the reason may not be clear, since aldehyde (1) has at least one alkyl group, alkenyl group or aryl group at the β position, it is considered to be a biomolecule or a growing chain compared with acrolein having no substituent at the β position One of the main factors is that it is difficult for the large molecule to cause the addition reaction at the β position. On the other hand, regarding the removal of iron sulfide, it is thought that combining iron sulfide with hydrogen sulfide in equilibrium and removing it will promote the dissolution of iron sulfide. As a result, iron sulfide is removed. It also does not hinder the attack of hydrogen sulfide from ordinary small molecules, and the removal performance of iron sulfide is maintained.

圖1係顯示丁烯醛(SAL)的pH安定性之圖表。 FIG. 1 is a graph showing pH stability of butenal (SAL).

圖2係顯示丙烯醛的pH安定性之圖表。 Fig. 2 is a graph showing the pH stability of acrolein.

實施發明之形態Embodiment of the invention

本發明的組成物之特徵係含有醛(1)為有效成分。 The composition of the present invention is characterized by containing an aldehyde (1) as an active ingredient.

醛(1)中R1~R3各自獨立表示的碳數1~10之烷基可為直鏈狀或分支狀或環狀,可列舉例如甲基、乙基、n-丙基、異丙基、n-丁基、異丁基、t-丁基、n-戊基、n-己基、n-辛基、n-癸基、n-十二烷基、環戊基等。從硫化鐵的去除性能之觀點來看,其中較佳為甲基、乙基或n-丙基,更佳為甲基或乙基,進一步較佳為甲基。 In the aldehyde (1), R 1 to R 3 each independently represent an alkyl group having 1 to 10 carbon atoms, which may be linear, branched, or cyclic. Examples include methyl, ethyl, n-propyl, and isopropyl. Group, n-butyl, isobutyl, t-butyl, n-pentyl, n-hexyl, n-octyl, n-decyl, n-dodecyl, cyclopentyl and the like. From the viewpoint of the removal performance of iron sulfide, among them, methyl, ethyl or n-propyl is preferred, methyl or ethyl is more preferred, and methyl is more preferred.

R1~R3各自獨立表示之碳數2~10的烯基可為直鏈狀或分支狀或環狀,可列舉例如乙烯基、烯丙基、1-戊烯-1-基、4-甲基-3-戊烯-1-基、4-戊烯-1-基、1-己烯-1-基、1-辛烯-1-基、1-癸烯-1-基等。其中較佳為碳數1~8的烯基,更佳為碳數1~6的烯基。 The alkenyl group having 2 to 10 carbon atoms independently represented by R 1 to R 3 may be linear or branched or cyclic, and examples thereof include vinyl, allyl, 1-penten-1-yl, 4- Methyl-3-penten-1-yl, 4-penten-1-yl, 1-hexen-1-yl, 1-octen-1-yl, 1-decen-1-yl, and the like. Among them, alkenyl groups having 1 to 8 carbon atoms are preferred, and alkenyl groups having 1 to 6 carbon atoms are more preferred.

R1~R3各自獨立表示之碳數6~12的芳基,可列舉例如苯基、甲苯基、乙基苯基、二甲苯基、三甲基苯基、萘基、聯苯基等。其中較佳為碳數6~10的芳基。 R 1 to R 3 each independently represent an aryl group having 6 to 12 carbon atoms, and examples thereof include phenyl, tolyl, ethylphenyl, xylyl, trimethylphenyl, naphthyl, and biphenyl. Among them, an aryl group having 6 to 10 carbon atoms is preferred.

又,R1與R2或R3互相連結表示碳數2~6的伸烷基情形,就該伸烷基而言,可列舉例如伸乙基、n-伸丙基、n-丁烯基、n-伸戊基、n-伸己基、2-甲基伸乙基、1,2-二甲基伸乙基、2-甲基-n-伸丙基、2,2-二甲基-n-伸丙基、3-甲基-n-伸戊基等。 In addition, when R 1 and R 2 or R 3 are connected to each other to represent an alkylene group having 2 to 6 carbon atoms, examples of the alkylene group include ethylene, n-propyl, and n-butenyl. , N-pentyl, n-hexyl, 2-methylethylene, 1,2-dimethylethyl, 2-methyl-n-propyl, 2,2-dimethyl- n-propyl, 3-methyl-n-pentyl and the like.

R1~R3較佳係各自獨立為氫原子或碳數1~5的烷基。 R 1 to R 3 are each preferably a hydrogen atom or an alkyl group having 1 to 5 carbon atoms.

從具有硫化鐵的去除性能且確保熱安定性及pH安定性之觀點來看,較佳係R1、R2的至少一者為甲基,更佳係R1、R2均為甲基。 Having the iron sulfide removal performance from the standpoint of ensuring the thermal stability and pH stability of view and, based preferred R 1, R 2 is at least one of methyl, more preferably based R 1, R 2 are methyl.

又,從促進與硫化氫的反應、效率良好地去除硫化鐵之觀點來看,R3較佳為氫原子。 From the viewpoint of promoting the reaction with hydrogen sulfide and efficiently removing iron sulfide, R 3 is preferably a hydrogen atom.

就醛(1)而言,可列舉例如2-丁烯醛、2-戊烯醛、2-己烯醛、2-庚烯醛、2-辛烯醛、2-壬烯醛、2-癸烯醛、2-十一碳烯醛、2-十二碳烯醛、2-十三碳烯醛、4-甲基-2-戊烯醛、4-甲基-2-己烯醛、5-甲基-2-己烯醛、4,4-二甲基-2-戊烯醛、6-甲基-2-庚烯醛、4-乙基-2-己烯醛、2-甲基-2-丁烯醛、2-甲基-2-戊烯醛、2-甲基-2-己烯醛、2-甲基-2-庚烯醛、2-甲基-2-辛烯醛、4-甲基-2-丙基-2-己烯醛、2,4-二甲基-2-戊烯醛、2,4-二甲基-2-己烯醛、2,4-二甲基-2-庚烯醛、2,5-二甲基-2-己烯醛、2,6-二甲基-2-庚烯醛、2,4,4-三甲基-2-戊烯醛、2-乙基-2-丁烯醛、2-乙基-2-戊烯醛、2-乙基-2-己烯醛、2-乙基-2-庚烯醛、2-乙基-2-辛烯醛、2-乙基-4-甲基-2-戊烯醛、2-乙基-4-甲基-2-己烯醛、2-丙基-2-丁烯醛、2-丙基-2-戊烯醛、2- 丙基-2-己烯醛、2-丙基-2-庚烯醛、2-丙基-4-甲基-2-戊烯醛、2-丙基-5-甲基-2-己烯醛、2-異丙基-2-丁烯醛、2-異丙基-4-甲基-2-戊烯醛、2-異丙基-4-甲基-2-己烯醛、2-異丙基-5-甲基-2-己烯醛、2-丁基-2-丁烯醛、2-丁基-2-戊烯醛、2-丁基-2-己烯醛、2-丁基-2-庚烯醛、2-丁基-2-辛烯醛、2-異丁基-2-庚烯醛、2-異丁基-6-甲基-2-庚烯醛、2-戊基-2-丁烯醛、2-戊基-2-戊烯醛、2-戊基-2-己烯醛、2-戊基-2-庚烯醛、2-戊基-2-辛烯醛、3-甲基-2-丁烯醛、3-甲基-2-戊烯醛、3-甲基-2-己烯醛、3-甲基-2-庚烯醛、3-甲基-2-辛烯醛、3-甲基-2-壬烯醛、3-甲基-2-癸烯醛、3-甲基-2-十一碳烯醛、3-甲基-2-十二碳烯醛、3-甲基-2-十三碳烯醛、3-乙基-2-戊烯醛、3,4-二甲基-2-戊烯醛、3,4,4-三甲基-2-戊烯醛、3-異丙基-4-甲基-2-戊烯醛、3-乙基-2-己烯醛、3-丙基-2-己烯醛、3,5-二甲基-2-己烯醛、3-(t-丁基)-4,4-二甲基-2-戊烯醛、3-丁基-2-庚烯醛、2,3-二甲基-2-丁烯醛、2-乙基-3-甲基-2-丁烯醛、2-異丙基-3-甲基-2-丁烯醛、2,3-二甲基-2-戊烯醛、2,3,4-三甲基-2-己烯醛、2-異丁基-3-甲基-2-丁烯醛、3-甲基-2-戊基-2-戊烯醛、2,3-二乙基-2-庚烯醛、2-(1,1-二甲基丙基)-3-甲基-2-丁烯醛、3,5,5-三甲基-2-己烯醛、2,3,4-三甲基-2-戊烯醛、2-環亞丙基丙醛、2-環亞戊基丙醛、2-環亞戊基己醛、2-(3-甲基環亞戊基)丙醛、2-環亞己基丙醛、2-(2-甲基環亞己基)丙醛、2-環亞己基丁醛、2-環亞己基己醛、1-甲醯基環丁烯、1-甲醯基-3,3-二甲基環丁 烯、1-環丙基-2-甲醯基環丁烯、1-甲醯基環戊烯、5-乙基-1-甲醯基環戊烯、1-甲醯基-3-甲基環戊烯、1-甲醯基-4-甲基環戊烯、1-甲醯基-5-甲基環戊烯、1-甲醯基-3,3-二甲基環戊烯、1-甲醯基-4,5-二甲基環戊烯、1-甲醯基-2-甲基環戊烯、1-甲醯基-5-異丙基-2-甲基環戊烯、1-甲醯基-2,5,5-三甲基環戊烯、1-甲醯基環己烯、1-甲醯基-3-甲基環己烯、1-甲醯基-4-甲基環己烯、1-甲醯基-5-甲基環己烯、1-甲醯基-6-甲基環己烯、1-甲醯基-3,3-二甲基環己烯、1-甲醯基-5,5-二甲基環己烯、1-甲醯基-2甲基環己烯、1-甲醯基-2,5,6,6-四甲基環己烯、1-甲醯基-2,4,6,6-四甲基環己烯、1-甲醯基環庚烯、1-甲醯基-2-甲基環庚烯、1-甲醯基-3-甲基環庚烯、1-甲醯基環辛烯、2,4-戊二烯醛、2,4-己二烯醛、2,5-己二烯醛、5-甲基-2,4-己二烯醛、2,4-庚二烯醛、2,4-辛二烯醛、2,7-辛二烯醛、3,7-二甲基-2,6-辛二烯醛(檸檬醛)、2,4,6-辛三烯醛、7-甲基-2,4,6-辛三烯醛、2,4-壬二醛、2,6-壬二醛、4,8-二甲基-2,7-壬二醛、2,4-癸二醛、2,4-十一碳二烯醛、2,4-十二碳二烯醛、2,4-十三碳二烯醛、2,4,7-十三碳三烯醛、3-苯基丙烯醛、3-苯基-2-甲基丙烯醛、3-(o-甲苯基)丙烯醛、3-(p-甲苯基)丙烯醛、3-萘基丙烯醛等。其中,較佳為3-甲基-2-丁烯醛、3-甲基-2-戊烯醛、3-甲基-2-己烯醛、3-甲基-2-庚烯醛、3-甲基-2-辛烯醛、3,7-二甲基-2,6-辛二烯醛(檸檬醛)、3-乙基-2-戊烯醛、3-乙基-2-己烯醛、3-丙基-2-己烯醛,更佳為3-甲基-2-丁烯醛、3- 甲基-2-戊烯醛、3-乙基-2-戊烯醛,進一步較佳為3-甲基-2-丁烯醛(丁烯醛,以下僅稱為SAL)。 Examples of the aldehyde (1) include 2-butenal, 2-pentenal, 2-hexenal, 2-heptenal, 2-octenal, 2-nonenal, and 2-decane Enal, 2-undecenal, 2-dodecenal, 2-tridecenal, 4-methyl-2-pentenal, 4-methyl-2-hexenal, 5 -Methyl-2-hexenal, 4,4-dimethyl-2-pentenal, 6-methyl-2-heptenal, 4-ethyl-2-hexenal, 2-methyl 2-butenal, 2-methyl-2-pentenal, 2-methyl-2-hexenal, 2-methyl-2-heptenal, 2-methyl-2-octenal , 4-methyl-2-propyl-2-hexenal, 2,4-dimethyl-2-pentenal, 2,4-dimethyl-2-hexenal, 2,4-di Methyl-2-heptenal, 2,5-dimethyl-2-hexenal, 2,6-dimethyl-2-heptenal, 2,4,4-trimethyl-2-pentene Enal, 2-ethyl-2-butenal, 2-ethyl-2-pentenal, 2-ethyl-2-hexenal, 2-ethyl-2-heptenal, 2-ethyl 2-Octenal, 2-ethyl-4-methyl-2-pentenal, 2-ethyl-4-methyl-2-hexenal, 2-propyl-2-butenal , 2-propyl-2-pentenal, 2-propyl-2-hexenal, 2-propyl-2-heptenal, 2-propyl-4-methyl-2-pentenal, 2-propyl-5-methyl-2-hexenal, 2-isopropyl-2 -Butenal, 2-isopropyl-4-methyl-2-pentenal, 2-isopropyl-4-methyl-2-hexenal, 2-isopropyl-5-methyl- 2-hexenal, 2-butyl-2-butenal, 2-butyl-2-pentenal, 2-butyl-2-hexenal, 2-butyl-2-heptenal, 2-butyl-2-octenal, 2-isobutyl-2-heptenal, 2-isobutyl-6-methyl-2-heptenal, 2-pentyl-2-butenal , 2-pentyl-2-pentenal, 2-pentyl-2-hexenal, 2-pentyl-2-heptenal, 2-pentyl-2-octenal, 3-methyl- 2-butenal, 3-methyl-2-pentenal, 3-methyl-2-hexenal, 3-methyl-2-heptenal, 3-methyl-2-octenal, 3-methyl-2-nonenal, 3-methyl-2-decenal, 3-methyl-2-undecenal, 3-methyl-2-dodecenal, 3- Methyl-2-tridecenal, 3-ethyl-2-pentenal, 3,4-dimethyl-2-pentenal, 3,4,4-trimethyl-2-pentene Aldehyde, 3-isopropyl-4-methyl-2-pentenal, 3-ethyl-2-hexenal, 3-propyl-2-hexenal, 3,5-dimethyl-2 -Hexenal, 3- (t-butyl) -4,4-dimethyl-2-pentenal, 3-butyl-2-heptenal, 2,3-dimethyl-2-butan Enal, 2-ethyl-3-methyl-2-butenal, 2-isopropyl-3-methyl-2-butene Aldehyde, 2,3-dimethyl-2-pentenal, 2,3,4-trimethyl-2-hexenal, 2-isobutyl-3-methyl-2-butenal, 3 -Methyl-2-pentyl-2-pentenal, 2,3-diethyl-2-heptenal, 2- (1,1-dimethylpropyl) -3-methyl-2- Butenal, 3,5,5-trimethyl-2-hexenal, 2,3,4-trimethyl-2-pentenal, 2-cyclopropylenepropanal, 2-cyclopentene Propanal, 2-cyclopentylidenehexanal, 2- (3-methylcyclopentylidene) propanal, 2-cyclohexylenepropanal, 2- (2-methylcyclohexylene) propanal, 2-cyclohexylenebutyraldehyde, 2-cyclohexylenehexanaldehyde, 1-methylfluorenylcyclobutene, 1-methylfluorenyl-3,3-dimethylcyclobutene, 1-cyclopropyl-2- Formamylcyclobutene, 1-formamylcyclopentene, 5-ethyl-1-formamylcyclopentene, 1-formamyl-3-methylcyclopentene, 1-formamyl- 4-methylcyclopentene, 1-methylfluorenyl-5-methylcyclopentene, 1-methylfluorenyl-3,3-dimethylcyclopentene, 1-methylfluorenyl-4,5-di Methylcyclopentene, 1-methylfluorenyl-2-methylcyclopentene, 1-methylfluorenyl-5-isopropyl-2-methylcyclopentene, 1-methylfluorenyl-2,5, 5-trimethylcyclopentene, 1-methylfluorenylcyclohexene, 1-methylfluorenyl-3-methylcyclohexene, 1-methylfluorenyl-4-methylcyclohexene, 1-methyl Methyl-5-methylcyclohexene, 1-methylfluorenyl-6-methylcyclohexene, 1-methylfluorenyl-3,3-dimethylcyclohexene, 1-methylfluorenyl-5,5 -Dimethylcyclohexene, 1-methylfluorenyl-2 methylcyclohexene, 1-methylfluorenyl-2,5,6,6-tetramethylcyclohexene, 1-methylfluorenyl-2, 4,6,6-tetramethylcyclohexene, 1-methylfluorenylcycloheptene, 1-methylfluorenyl-2-methylcycloheptene, 1-methylfluorenyl-3-methylcycloheptene, 1-methylfluorenyl cyclooctene, 2,4-pentadienal, 2,4-hexadienal, 2,5-hexadienal, 5-methyl-2,4-hexadienal, 2,4-heptadienal, 2,4-octadienal, 2,7-octadienal, 3,7-dimethyl-2,6-octadial (citral), 2, 4,6-octatrienal, 7-methyl-2,4,6-octatrienal, 2,4-nonanedial, 2,6-nonedial, 4,8-dimethyl-2 , 7-nonanedialdehyde, 2,4-decanedial, 2,4-undecadienal, 2,4-dodecadienal, 2,4-tridecadienal, 2, 4,7-Thirteen carbon trienal, 3-phenyl acrolein, 3-phenyl-2-methacryl, 3- (o-tolyl) acrolein, 3- (p-tolyl) propylene Aldehyde, 3-naphthyl acrolein and the like. Among them, 3-methyl-2-butenal, 3-methyl-2-pentenal, 3-methyl-2-hexenal, 3-methyl-2-heptenal, 3 -Methyl-2-octenal, 3,7-dimethyl-2,6-octadial (citral), 3-ethyl-2-pentenal, 3-ethyl-2-hexan Enal, 3-propyl-2-hexenal, more preferably 3-methyl-2-butenal, 3-methyl-2-pentenal, 3-ethyl-2-pentenal, More preferred is 3-methyl-2-butenal (butenal, hereinafter simply referred to as SAL).

此外,針對具有trans體及cis體的化合物,可使用任一者,也可使用混合物。使用混合物的情形,可使用任意的混合比者。 For compounds having a trans form and a cis form, either one or a mixture may be used. When a mixture is used, an arbitrary mixing ratio may be used.

醛(1)可使用市售品,也可藉由對應的α,β-不飽和醇之氧化脫氫反應而合成(參照例如日本特開昭60-224652號公報)。 The aldehyde (1) may be a commercially available product, or may be synthesized by an oxidative dehydrogenation reaction of a corresponding α, β-unsaturated alcohol (see, for example, Japanese Patent Application Laid-Open No. 60-224652).

本發明之組成物中的有效成分之醛(1)的含有比例,可根據使用態樣而適當設定,通常為1~99.9質量%,從費用相對於效果之觀點來看,較佳為5~99.9質量%,更佳為5~95質量%。 The content ratio of the aldehyde (1) as the active ingredient in the composition of the present invention can be appropriately set according to the use situation, and is usually 1 to 99.9% by mass. From the viewpoint of cost and effect, it is preferably 5 to 99.9% by mass, more preferably 5 to 95% by mass.

本發明的組成物在不損及本發明效果之範圍內,可含有丙烯醛、肆(羥基甲基)膦或對應的鏻鹽、鹽酸、甲酸等的其他硫化鐵去除劑。 The composition of the present invention may contain other iron sulfide removing agents such as acrolein, methane (hydroxymethyl) phosphine or the corresponding sulfonium salt, hydrochloric acid, formic acid and the like within a range that does not impair the effects of the present invention.

又,本發明的組成物可含有環己烷、甲苯、二甲苯、重質芳香族石油腦、石油蒸餾物;甲醇、乙醇、乙二醇等的碳數1~10的單醇或二醇等的適當溶劑。 In addition, the composition of the present invention may contain cyclohexane, toluene, xylene, heavy aromatic petroleum naphtha, petroleum distillates, methanol, ethanol, ethylene glycol, and the like having a carbon number of 1 to 10, or a diol, and the like. Appropriate solvent.

本發明的組成物係除了醛(1)以外,只要不損及本發明效果,可含有界面活性劑、防腐劑、脫氧劑、鐵分控制劑、交聯劑、分解劑(breaker)、凝集劑、溫度安定劑、pH調整劑、脫水調整劑、膨潤防止劑、防垢劑、殺生物劑、摩擦減低劑、消泡劑、逸泥防止劑、潤滑劑、黏土分散劑、加重劑、凝膠化劑等的成分。 In addition to the aldehyde (1), the composition of the present invention may contain a surfactant, a preservative, a deoxidizing agent, an iron content control agent, a cross-linking agent, a breaker, and an aggregating agent as long as the effects of the present invention are not impaired 、 Temperature stabilizer, pH adjuster, dehydration adjuster, swelling preventer, antiscalant, biocide, friction reducing agent, defoamer, sludge preventer, lubricant, clay dispersant, weighting agent, gel Ingredients such as chemical agents.

本發明的組成物的製造方法並未特別限定,例如可藉由在醛(1)中添加混合前述其他的硫化鐵去除劑或溶劑等的任意成分等而製造。 The manufacturing method of the composition of this invention is not specifically limited, For example, it can manufacture by adding arbitrary components, such as the said other iron sulfide remover, a solvent, etc., to aldehyde (1).

本發明的組成物適宜為液狀,能根據為了去除硫化鐵使用的形態,而載持在適當載體等,且可為粉體、流體等的固體狀。 The composition of the present invention is preferably in a liquid state, can be supported on an appropriate carrier or the like depending on the form used for removing iron sulfide, and can be a solid state such as a powder or a fluid.

就本發明的較佳實施態樣之例而言,可列舉將足以去除硫化鐵的量之本發明的組成物,朝含有硫化鐵的液體添加而進行處理。在使用本發明之組成物的去除硫化鐵之方法中,本發明之組成物中含有的醛(1)的量,相對於硫化鐵1質量份,較佳係添加成0.1~100質量份,更佳係添加成2~100質量份。將本發明的組成物添加至含有硫化鐵的液體中使其接觸而進行處理時的溫度,較佳為0℃~150℃,更佳為20℃~130℃的範圍。 As an example of a preferred embodiment of the present invention, the composition of the present invention sufficient to remove iron sulfide may be added to a liquid containing iron sulfide for treatment. In the method for removing iron sulfide using the composition of the present invention, the amount of aldehyde (1) contained in the composition of the present invention is preferably 0.1 to 100 parts by mass relative to 1 part by mass of iron sulfide, and more The best line is added to 2 ~ 100 parts by mass. The temperature at which the composition of the present invention is added to a liquid containing iron sulfide and brought into contact for processing is preferably in a range of 0 ° C to 150 ° C, and more preferably in a range of 20 ° C to 130 ° C.

實施例Examples

以下,藉由實施例等來具體地說明本發明,但本發明並不因以下之例而受到任何限定。此外,實施例及比較例所使用的SAL、檸檬醛及丙烯醛為以下者。 Hereinafter, the present invention will be specifically described by way of examples, but the present invention is not limited to the following examples. The SAL, citral, and acrolein used in the examples and comparative examples are as follows.

SAL:按照日本特開昭60-224652號公報所記載的方法,由異戊烯醇(prenol)而合成者(純度98.1%) SAL: Synthesized from prenol according to the method described in Japanese Patent Laid-Open No. 60-224652 (purity 98.1%)

檸檬醛:Kuraray股份有限公司製(純度98.0%,trans:cis=51:49~57:43(莫耳比)) Citral: manufactured by Kuraray Co., Ltd. (purity 98.0%, trans: cis = 51: 49 ~ 57: 43 (molar ratio))

丙烯醛:東京化成工業股份有限公司製,作為安定劑且含有氫醌 Acrolein: manufactured by Tokyo Chemical Industry Co., Ltd. as a stabilizer and containing hydroquinone

<實施例1>硫化鐵去除試驗(SAL)     <Example 1> Iron sulfide removal test (SAL)    

在具備溫度計、攪拌機、冷卻管之1L的三口燒瓶中,加入500mL的蒸餾水、1mL的1mol/L鹽酸、120.0mg(0.5mmol)的硫化鈉.9水合物、138.2(0.5mmol)的硫酸鐵.7水合物,攪拌時硫化鐵生成為微細的黑色沉澱。於其中添加126.3mg(1.5mmol)的SAL,將反應液以500rpm一邊攪拌一邊升溫至50℃。將添加SAL的時間點設為0小時,觀察硫化鐵的樣子,結果在4小時後硫化鐵溶解,且反應液為無色透明。 In a 1 L three-necked flask equipped with a thermometer, a stirrer, and a cooling tube, 500 mL of distilled water, 1 mL of 1 mol / L hydrochloric acid, and 120.0 mg (0.5 mmol) of sodium sulfide were added. 9 hydrate, 138.2 (0.5 mmol) of iron sulfate. 7 hydrate, iron sulfide is formed into fine black precipitates when stirred. 126.3 mg (1.5 mmol) of SAL was added thereto, and the reaction liquid was heated to 500C while stirring at 500 rpm. The time point at which SAL was added was set to 0 hours, and the state of the iron sulfide was observed. As a result, the iron sulfide was dissolved after 4 hours, and the reaction solution was colorless and transparent.

<實施例2>硫化鐵去除試驗(檸檬醛)     <Example 2> Iron sulfide removal test (citral)    

除了取代SAL而使用檸檬醛以外,實施與實施例1同樣的試驗。7小時後硫化鐵溶解,且反應液為無色透明。 The same test as in Example 1 was performed except that citral was used instead of SAL. After 7 hours, the iron sulfide was dissolved, and the reaction solution was colorless and transparent.

<比較例1>硫化鐵去除試驗(丙烯醛)     <Comparative Example 1> Iron sulfide removal test (acrolein)    

除了取代SAL而使用丙烯醛以外,實施與實施例1同樣的試驗。4小時後硫化鐵溶解,且反應液為無色透明。 The same test as in Example 1 was performed except that acrolein was used instead of SAL. After 4 hours, the iron sulfide was dissolved, and the reaction solution was colorless and transparent.

<試驗例1>熱安定性試驗     <Test Example 1> Thermal stability test    

將SAL及丙烯醛分別放入50mL三口燒瓶,在氮環境下升溫至50℃,用使用內部標準之氣相層析法所得到的校正曲線法,觀察將升溫之後的SAL及丙烯醛的含量設為100%時之含有率的變化。將結果示於表1。 Put SAL and acrolein into 50mL three-necked flasks respectively, raise the temperature to 50 ° C under nitrogen environment, and use the calibration curve method obtained by internal standard gas chromatography to observe the SAL and acrolein content after heating up. Change in content at 100%. The results are shown in Table 1.

[氣相層析法分析]     [Gas chromatography analysis]    

分析機器:GC-14A(島津製作所股份有限公司製) Analysis equipment: GC-14A (manufactured by Shimadzu Corporation)

偵測器:FID(氫焰游離型偵測器(hydrogen flame ionization detector)) Detector: FID (hydrogen flame ionization detector)

使用管柱:DB-1701(長度:50m,膜厚1μm,內徑0.32mm)(Agilent Technologies股份有限公司製) Use column: DB-1701 (length: 50m, film thickness 1μm, inner diameter 0.32mm) (manufactured by Agilent Technologies)

分析條件:Inject.Temp.250℃,Detect.Temp.250℃ Analysis conditions: Inject.Temp.250 ℃, Detect.Temp.250 ℃

升溫條件:70℃→(以5℃/分鐘升溫)→250℃ Heating conditions: 70 ℃ → (heating at 5 ℃ / min) → 250 ℃

內部標準物質:二甘二甲醚(二乙二醇二甲基醚) Internal standard substance: Diglyme (diethylene glycol dimethyl ether)

10小時後,相對於SAL殘存99.9%,丙烯醛儘管含有作為安定劑之氫醌,仍損失了3.4%。從該結果,可知SAL的熱安定性遠高於丙烯醛。 After 10 hours, acrolein was lost by 3.4% relative to the remaining 99.9% of SAL despite the hydroquinone as a stabilizer. From this result, it is understood that the thermal stability of SAL is much higher than that of acrolein.

<試驗例2>pH安定性試驗     <Test Example 2> pH stability test    

使SAL及丙烯醛分別溶解於pH不同的0.5mol/L磷酸緩衝液中,而調製0.1wt%溶液。將該溶液50mL在氮環境下放入試樣瓶,在23±2℃下保管,用藉由高速液體滲透層析分析所得到的絕對校正曲線,觀察將調製時之SAL及丙烯醛的含量設為100%時的含有率之變化。將結果示於圖1及2。 SAL and acrolein were each dissolved in 0.5 mol / L phosphate buffer solution having different pHs to prepare a 0.1 wt% solution. Put 50 mL of this solution into a sample bottle under a nitrogen environment, store it at 23 ± 2 ° C, and use the absolute calibration curve obtained by high-speed liquid permeation chromatography analysis to observe the SAL and acrolein content at the time of preparation. Change in content at 100%. The results are shown in FIGS. 1 and 2.

從該結果,可知SAL的pH安定性遠高於丙烯醛。 From this result, it turns out that pH stability of SAL is much higher than acrolein.

[磷酸緩衝液的調製]     [Preparation of phosphate buffer]    

pH1.7:使4.9g的75%磷酸、7.8g的磷酸二氫鈉.2水合物溶解於200mL的蒸餾水中。 pH1.7: Make 4.9g of 75% phosphoric acid and 7.8g of sodium dihydrogen phosphate. The dihydrate was dissolved in 200 mL of distilled water.

pH6.2:使7.8g的磷酸二氫鈉.2水合物、7.1g的磷酸氫二鈉溶解於200mL的蒸餾水中。 pH6.2: Make 7.8g of sodium dihydrogen phosphate. Dihydrate, 7.1 g of disodium hydrogen phosphate were dissolved in 200 mL of distilled water.

pH8.1:使0.3g的磷酸二氫鈉.2水合物、13.9g的磷酸氫二鈉溶解於200mL的蒸餾水中。 pH8.1: Make 0.3g of sodium dihydrogen phosphate. Dihydrate and 13.9 g of disodium hydrogen phosphate were dissolved in 200 mL of distilled water.

[高速液體滲透層析分析]     [High-speed liquid permeation chromatography analysis]    

分析機器:Prominence系統(島津製作所股份有限公司製) Analysis equipment: Prominence system (manufactured by Shimadzu Corporation)

使用管柱:Cadenza CD-C18(長度:150m,內徑4.6mm) Use column: Cadenza CD-C18 (length: 150m, inner diameter 4.6mm)

展開液:H2O/MeOH=45/55vol比,H3PO4=1mol/L Developing solution: H 2 O / MeOH = 45 / 55vol ratio, H 3 PO 4 = 1mol / L

流速:1mL/min Flow rate: 1mL / min

<參考例>     <Reference example>    

SAL、檸檬醛及丙烯醛為現有的化合物,關於安全性的資訊已被揭示。將關於安全性的資訊當作參考示於表2。已知與丙烯醛相比,SAL或檸檬醛的毒性極低,且為安全的。 SAL, citral and acrolein are existing compounds, and information on safety has been revealed. Information on security is shown in Table 2 as a reference. Compared to acrolein, SAL or citral are known to be extremely low toxic and safe.

從以上的實施例、比較例、試驗例及參考例,可知SAL等的醛(1)具有與丙烯醛同等的硫化鐵去除能力,熱安定性及pH安定性比丙烯醛高,且為安全的。 From the above examples, comparative examples, test examples, and reference examples, it can be seen that aldehydes (1) such as SAL have the same iron sulfide removal ability as acrolein, higher thermal stability and pH stability than acrolein, and are safe. .

產業上的利用可能性Industrial availability

本發明之組成物的熱安定性及pH安定性高,在能安全且效率良好地去除硫化鐵這方面是有用的。 The composition of the present invention has high thermal stability and pH stability, and is useful in that iron sulfide can be safely and efficiently removed.

Claims (7)

一種去除硫化鐵用之組成物,其係含有下述通式(1)所示之α,β-不飽和醛為有效成分, (R 1~R 3各自獨立表示氫原子、碳數1~10的烷基、碳數2~10的烯基或碳數6~12的芳基;其中,R 1可與R 2或R 3互相連結以構成碳數2~6的伸烷基,R 1與R 2不同時為氫原子)。 A composition for removing iron sulfide, which contains an α, β-unsaturated aldehyde represented by the following general formula (1) as an active ingredient, (R 1 to R 3 each independently represent a hydrogen atom, an alkyl group having 1 to 10 carbon atoms, an alkenyl group having 2 to 10 carbon atoms, or an aryl group having 6 to 12 carbon atoms; wherein R 1 and R 2 or R 3 They are connected to each other to form an alkylene group having 2 to 6 carbon atoms, and R 1 and R 2 are not hydrogen atoms at the same time). 如請求項1之組成物,其中R 1~R 3各自獨立為氫原子或碳數1~5的烷基。 For example, the composition of claim 1, wherein R 1 to R 3 are each independently a hydrogen atom or an alkyl group having 1 to 5 carbon atoms. 如請求項1或2之組成物,其中R 3為氫原子。 The composition of claim 1 or 2, wherein R 3 is a hydrogen atom. 一種硫化鐵之去除方法,其特徵係使如請求項1至3中任一項之組成物接觸硫化鐵。     A method for removing iron sulfide, characterized in that the composition according to any one of claims 1 to 3 is contacted with iron sulfide.     如請求項4之方法,其中相對於硫化鐵1質量份,添加該組成物中的α,β-不飽和醛使其成為0.1~100質量份。     The method according to claim 4, wherein the α, β-unsaturated aldehyde in the composition is added to 1 to 100 parts by mass relative to 1 part by mass of iron sulfide.     如請求項4或5之方法,其係使該組成物中的α,β-不飽和醛與硫化鐵在-30℃~150℃的範圍接觸。     The method according to claim 4 or 5, which involves contacting the α, β-unsaturated aldehyde in the composition with iron sulfide in a range of -30 ° C to 150 ° C.     一種如請求項1至3中任一項之組成物之用途,其係用於去除硫化鐵。     A use according to any one of claims 1 to 3 for removing iron sulfide.    
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