CN118344511A - Mannich base and preparation method and application thereof - Google Patents

Mannich base and preparation method and application thereof Download PDF

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Publication number
CN118344511A
CN118344511A CN202310066511.2A CN202310066511A CN118344511A CN 118344511 A CN118344511 A CN 118344511A CN 202310066511 A CN202310066511 A CN 202310066511A CN 118344511 A CN118344511 A CN 118344511A
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formula
compound represented
mannich base
branched alkyl
phenylenediamine
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张浴阳
辛世豪
张建荣
黄作鑫
么佳耀
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Sinopec Petrochemical Research Institute Co ltd
China Petroleum and Chemical Corp
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Sinopec Petrochemical Research Institute Co ltd
China Petroleum and Chemical Corp
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    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1822Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/30Introducing nitrogen atoms or nitrogen-containing groups
    • C08F8/32Introducing nitrogen atoms or nitrogen-containing groups by reaction with amines
    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond

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

Abstract

The invention provides a Mannich base and a preparation method and application thereof. The structure of the Mannich base is shown as a formula (I): In formula (I), R 0 is selected from the group consisting of linear or branched alkylene of C 1~8; each R 1, equal to or different from each other, is independently selected from the group consisting of linear or branched alkyl groups of H, C 1~4; each R 1' is independently selected from the group consisting of linear or branched alkyl and phenyl of H, C 1~4; r 2 is selected from hydrocarbon groups with the number average molecular weight Mn of 300-3000; r 3 is selected from the group consisting of linear or branched alkyl of C 1~6. The Mannich base disclosed by the invention can be applied to gasoline, and has very excellent cleaning performance, deposit formation inhibition performance and rust prevention performance.

Description

一种曼尼希碱及其制备方法、用途A Mannich base and its preparation method and use

技术领域Technical Field

本发明涉及一种汽油清净剂,尤其涉及一种具有苯二胺结构的曼尼希碱清净剂。The invention relates to a gasoline detergent, in particular to a Mannich base detergent with a phenylenediamine structure.

背景技术Background technique

汽油燃料中含有较多不饱和烃类以及硫、氮化合物,在储存和使用过程中易与空气接触而被氧化成胶质,直接导致燃料燃烧过程中在电喷嘴、进气阀和燃烧室易生成积碳和沉积物,从而引起供油不畅,空燃比失调,燃烧不完全,浪费燃料,降低发动机效率等问题,并且排出大量的有害气体,同时也增大了运动部件之间的摩擦和磨损。Gasoline fuel contains a large amount of unsaturated hydrocarbons and sulfur and nitrogen compounds. During storage and use, it is easy to come into contact with air and be oxidized into gum, which directly leads to the formation of carbon deposits and sediments in the electric nozzle, intake valve and combustion chamber during the fuel combustion process, causing problems such as poor fuel supply, air-fuel ratio imbalance, incomplete combustion, fuel waste, reduced engine efficiency, etc., and a large amount of harmful gases are emitted, which also increases the friction and wear between moving parts.

为解决上述汽油在燃烧过程中存在的诸多问题,通常在现有汽油燃料中加入一种或多种多效复合添加剂,利用不同添加剂之间的性能起到改善汽油性能的作用,同时增加汽油的清净性和抗氧化性。目前最新一代清净剂主剂多使用曼尼希碱,能够有效去除进气阀沉积物。In order to solve the above-mentioned problems in the combustion process of gasoline, one or more multi-effect composite additives are usually added to the existing gasoline fuel to improve the performance of gasoline by utilizing the performance of different additives, while increasing the cleanliness and anti-oxidation properties of gasoline. Currently, the latest generation of detergents mainly use Mannich bases, which can effectively remove intake valve deposits.

US 20160289584A1中报道了一种曼尼希碱性清净剂的混合物,包括衍生自二胺或多胺的第一曼尼希碱性清净剂组分和衍生自单胺的第二曼尼希碱性清净剂组分,但其所报道的二胺型胺化物的合成方式和清净性能并未在实施例中披露。US 20160289584A1 reports a mixture of Mannich alkaline detergents, including a first Mannich alkaline detergent component derived from a diamine or a polyamine and a second Mannich alkaline detergent component derived from a monoamine, but the synthesis method and cleaning performance of the diamine-type amine reported therein are not disclosed in the examples.

US 8557003B2中报道了一种由含有伯氨基的多胺、羟基芳族化合物和醛制备的的曼尼希碱,对去除进气阀沉积物有较好的效果。US 8557003B2 reports a Mannich base prepared from a polyamine containing primary amino groups, a hydroxy aromatic compound and an aldehyde, which has a good effect on removing intake valve deposits.

US 7384434B2中报道了一种曼尼希碱,其由六氢三嗪与羟基芳族化合物反应制成,其反应产物与使用N,N-二甲基-1,3-丙二胺合成的结构类似,副产物多且清净效果有待改进。US 7384434B2 reports a Mannich base prepared by the reaction of hexahydrotriazine and a hydroxy aromatic compound. The reaction product has a similar structure to that synthesized using N,N-dimethyl-1,3-propylenediamine, but has many by-products and its purification effect needs to be improved.

GB 19592-2019对汽油的清净性提出了更高的要求,现有技术仍需要一种具有更好清净性能、抑制沉积物生成性能及防锈性能的曼尼希碱清净剂。GB 19592-2019 puts forward higher requirements on the cleanliness of gasoline. The existing technology still requires a Mannich base detergent with better cleaning performance, deposit formation inhibition performance and rust prevention performance.

发明内容Summary of the invention

本发明提出了一种曼尼希碱及其制备方法、用途。The invention provides a Mannich base and a preparation method and application thereof.

本发明包括以下方面的内容。The present invention includes the following aspects.

第一方面,本发明提出了一种曼尼希碱。In a first aspect, the present invention provides a Mannich base.

本发明的曼尼希碱,其结构如式(I)所示:The Mannich base of the present invention has a structure as shown in formula (I):

在式(I)中,R0选自C1~8的直链或支链亚烷基;各个R1彼此相同或不同,各自独立地选自H、C1~4的直链或支链烷基;各个R1’各自独立地选自H、C1~4的直链或支链烷基和苯基;R2选自数均分子量Mn为300~3000的烃基;R3选自C1~6的直链或支链烷基。In formula (I), R 0 is selected from a C 1-8 straight chain or branched alkylene group; each R 1 is the same as or different from each other and is independently selected from H, a C 1-4 straight chain or branched alkyl group; each R 1 ' is independently selected from H, a C 1-4 straight chain or branched alkyl group and a phenyl group; R 2 is selected from a hydrocarbon group with a number average molecular weight Mn of 300 to 3000; R 3 is selected from a C 1-6 straight chain or branched alkyl group.

根据本发明,优选地,R0选自C1~4的直链或支链亚烷基,各个R1各自独立地选自H或甲基,各个R1’各自独立地选自H、甲基,R2选自数均分子量Mn为500~2500的聚异丁烯基;R3选自C1~4的直链或支链烷基。According to the present invention, preferably, R 0 is selected from a C 1-4 straight or branched alkylene group, each R 1 is independently selected from H or methyl, each R 1 ' is independently selected from H, methyl, R 2 is selected from a polyisobutylene group with a number average molecular weight Mn of 500-2500; R 3 is selected from a C 1-4 straight or branched alkyl group.

第二方面,本发明提出了一种曼尼希碱的制备方法。In a second aspect, the present invention provides a method for preparing a Mannich base.

本发明的曼尼希碱的制备方法,包括使式(X)所示化合物、脂肪醛、式(Y)所示化合物发生反应,收集产物;The preparation method of the Mannich base of the present invention comprises reacting a compound represented by formula (X), a fatty aldehyde, and a compound represented by formula (Y), and collecting the product;

在式(X)中,R2选自数均分子量Mn为300~3000的烃基;R3选自C1~6的直链或支链烷基;In formula (X), R 2 is selected from a hydrocarbon group having a number average molecular weight Mn of 300 to 3000; R 3 is selected from a C 1 to 6 straight chain or branched alkyl group;

所述脂肪醛的碳数为1~8;The carbon number of the fatty aldehyde is 1 to 8;

在式(Y)中,各个R1彼此相同或不同,各自独立地选自H、C1~4的直链或支链烷基;各个R1’各自独立地选自H、C1~4的直链或支链烷基和苯基。In formula (Y), each R 1 is the same as or different from each other and is independently selected from H, a C 1-4 straight chain or branched alkyl group; each R 1 ′ is independently selected from H, a C 1-4 straight chain or branched alkyl group and a phenyl group.

根据本发明,优选地,在式(X)中,R2选自数均分子量Mn为500~2500的聚异丁烯基,R3选自C1~4的直链或支链烷基;所述脂肪醛的碳数为1~4;在式(Y)中,各个R1各自独立地选自H或甲基,各个R1’各自独立地选自H、甲基。According to the present invention, preferably, in formula (X), R 2 is selected from a polyisobutylene group having a number average molecular weight Mn of 500 to 2500, R 3 is selected from a C 1 to 4 straight chain or branched alkyl group; the carbon number of the fatty aldehyde is 1 to 4; in formula (Y), each R 1 is independently selected from H or methyl, and each R 1 ' is independently selected from H or methyl.

根据本发明,式(X)所示化合物可以通过苯酚和/或单邻位C1~6烷基酚与聚烯烃发生烷基化反应制备得到。所述烷基化反应可以参照CN103664655A中提出的烷基化反应方法。According to the present invention, the compound represented by formula (X) can be prepared by alkylation reaction of phenol and/or mono-ortho-C 1-6 alkylphenol with polyolefin. The alkylation reaction can refer to the alkylation reaction method proposed in CN103664655A.

根据本发明,所述脂肪醛优选甲醛或乙醛,更优选甲醛,所述的甲醛可以为甲醛水溶液、多聚甲醛或低聚甲醛。According to the present invention, the fatty aldehyde is preferably formaldehyde or acetaldehyde, more preferably formaldehyde, and the formaldehyde can be formaldehyde solution, paraformaldehyde or oligoformaldehyde.

根据本发明,式(Y)所示化合物可以选用对苯二胺、2-甲基对苯二胺、四甲基对苯二胺、N,N-二甲基-1,4-苯二胺、N-乙基对苯二胺、N,N-二乙基对苯二胺和N,N-二乙基-3-甲基对苯二胺中的一种或多种。According to the present invention, the compound represented by formula (Y) can be selected from one or more of p-phenylenediamine, 2-methyl-p-phenylenediamine, tetramethyl-p-phenylenediamine, N,N-dimethyl-1,4-phenylenediamine, N-ethyl-p-phenylenediamine, N,N-diethyl-p-phenylenediamine and N,N-diethyl-3-methyl-p-phenylenediamine.

根据本发明,所述式(X)所示化合物、脂肪醛、式(Y)所示化合物之间的摩尔比优选为1:0.1~3.5:0.3~3。According to the present invention, the molar ratio of the compound represented by formula (X), the fatty aldehyde, and the compound represented by formula (Y) is preferably 1:0.1-3.5:0.3-3.

根据本发明,所述式(X)所示化合物、脂肪醛、式(Y)所示化合物之间发生反应的温度为50℃~200℃,优选80℃~180℃,最优选90℃~160℃。According to the present invention, the temperature for the reaction between the compound represented by formula (X), the fatty aldehyde and the compound represented by formula (Y) is 50°C to 200°C, preferably 80°C to 180°C, and most preferably 90°C to 160°C.

根据本发明,所述式(X)所示化合物、脂肪醛、式(Y)所示化合物之间发生反应的时间通常越长越好,一般可以为1h~10h,优选2h~8h,最优选3h~6h。According to the present invention, the reaction time between the compound represented by formula (X), the fatty aldehyde and the compound represented by formula (Y) is generally as long as possible, generally 1h to 10h, preferably 2h to 8h, and most preferably 3h to 6h.

根据本发明,在所述式(X)所示化合物、脂肪醛、式(Y)所示化合物的反应中可以加入溶剂,所述溶剂选自沸点在100℃~160℃之间的烃类,例如甲苯、二甲苯、150号溶剂汽油,所述溶剂的加入量可以为式(X)所示化合物质量的2%~80%,优选10%~70%。所述溶剂可以在反应结束之后通过本领域公知的方法除去,例如减压蒸馏方法。According to the present invention, a solvent may be added during the reaction of the compound represented by formula (X), the fatty aldehyde, and the compound represented by formula (Y), and the solvent is selected from hydrocarbons with a boiling point between 100°C and 160°C, such as toluene, xylene, and No. 150 solvent gasoline, and the amount of the solvent added may be 2% to 80% of the mass of the compound represented by formula (X), preferably 10% to 70%. The solvent may be removed by a method known in the art after the reaction is completed, such as a vacuum distillation method.

根据本发明,在所述式(X)所示化合物、脂肪醛、式(Y)所示化合物的反应中可以加入稀释剂,所述稀释剂可以为矿物润滑油、聚烯烃和聚醚中的一种或多种。所述矿物润滑油可以选用API I、II、III类矿物润滑油,优选40℃粘度为20~120厘斯、粘度指数在50以上的矿物润滑油;所述聚烯烃是由乙烯、丙烯、α-烯烃单独聚合或共同聚合而得到的聚烯烃,所述α-烯烃包括正丁烯、异丁烯、正戊烯、正己烯、正辛烯和正癸烯中的一种或多种,优选100℃粘度为2~25厘斯的聚α-烯烃;所述聚醚是由醇与环氧化物反应所生成的聚合物,所述醇为乙二醇和/或1,3-丙二醇,所述的环氧化物为环氧乙烷和/或环氧丙烷,所述聚醚的数均分子量为500~3000,优选700~3000。在所述式(X)所示化合物、脂肪醛、式(Y)所示化合物的反应结束之后,可以将稀释剂分离除去,也可以将稀释剂保留在反应产物中,此时反应产物为包含了曼尼希碱和稀释剂的组合物,可以作为清净剂浓缩物加入到汽油中使用。所述清净剂浓缩物也可以通过制备得到的曼尼希碱产物与稀释剂在20℃~60℃混合1h~6h得到。According to the present invention, a diluent may be added to the reaction of the compound represented by formula (X), the fatty aldehyde, and the compound represented by formula (Y), and the diluent may be one or more of a mineral lubricant, a polyolefin, and a polyether. The mineral lubricant may be selected from API I, II, and III mineral lubricants, preferably mineral lubricants with a viscosity of 20 to 120 centistokes at 40°C and a viscosity index of more than 50; the polyolefin is a polyolefin obtained by polymerizing ethylene, propylene, and α-olefins alone or in combination, and the α-olefin includes one or more of n-butene, isobutylene, n-pentene, n-hexene, n-octene, and n-decene, preferably a poly-α-olefin with a viscosity of 2 to 25 centistokes at 100°C; the polyether is a polymer generated by the reaction of an alcohol and an epoxide, the alcohol is ethylene glycol and/or 1,3-propylene glycol, the epoxide is ethylene oxide and/or propylene oxide, and the number average molecular weight of the polyether is 500 to 3000, preferably 700 to 3000. After the reaction of the compound represented by formula (X), the fatty aldehyde, and the compound represented by formula (Y) is completed, the diluent can be separated and removed, or the diluent can be retained in the reaction product. In this case, the reaction product is a composition comprising a Mannich base and a diluent, which can be added to gasoline for use as a detergent concentrate. The detergent concentrate can also be obtained by mixing the prepared Mannich base product with a diluent at 20° C. to 60° C. for 1 h to 6 h.

第一方面所提出的曼尼希碱或按照第二方面方法所制得的曼尼希碱能够应用在汽油中,具有非常优异的清净性能、抑制沉积物生成性能和防锈性能。The Mannich base proposed in the first aspect or the Mannich base prepared according to the method of the second aspect can be used in gasoline and has very excellent cleaning performance, deposit generation inhibition performance and rust prevention performance.

第三方面,本发明提出了第一方面所提出的曼尼希碱的用途和按照第二方面方法所制得的曼尼希碱的用途。In a third aspect, the present invention proposes the use of the Mannich base proposed in the first aspect and the use of the Mannich base prepared according to the method of the second aspect.

所述曼尼希碱可以用作汽油清净剂。The Mannich base can be used as a gasoline detergent.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

图1是实施例1中高活性聚异丁烯原料与聚异丁烯基邻甲基苯酚产物的对比红外谱图,其中的上图(1)为高活性聚异丁烯的红外谱图,下图(2)为聚异丁烯基邻甲基苯酚产物的红外谱图。FIG1 is a comparative infrared spectra of the high-activity polyisobutylene raw material and the polyisobutylene-based o-methylphenol product in Example 1, wherein the upper figure (1) is the infrared spectrum of the high-activity polyisobutylene, and the lower figure (2) is the infrared spectrum of the polyisobutylene-based o-methylphenol product.

图2是实施例1中聚异丁烯基邻甲基苯酚产物的核磁共振氢谱(1H NMR)高场部分。FIG. 2 is a high-field portion of the nuclear magnetic resonance hydrogen spectrum (1H NMR) of the polyisobutylene-o-methylphenol product in Example 1.

图3是实施例1中聚异丁烯基邻甲基苯酚产物的核磁共振氢谱(1H NMR)低场部分。FIG. 3 is a low-field portion of the nuclear magnetic resonance hydrogen spectrum (1H NMR) of the polyisobutylene-o-methylphenol product in Example 1.

图4是实施例2产物的红外谱图。FIG. 4 is an infrared spectrum of the product of Example 2.

图5是实施例2产物的核磁共振氢谱。FIG5 is a hydrogen nuclear magnetic resonance spectrum of the product of Example 2.

图6是对比例1产物的红外谱图。FIG6 is an infrared spectrum of the product of Comparative Example 1.

图7是对比例1产物的核磁共振氢谱。FIG. 7 is a hydrogen nuclear magnetic resonance spectrum of the product of Comparative Example 1.

具体实施方式Detailed ways

下面通过实施例对本发明做进一步说明,但并非构成对本发明的限制。The present invention is further described below by way of examples, but they are not intended to limit the present invention.

对比例均采取目前专利文献中报道的合成曼尼希碱的主要方法。The comparative examples all adopt the main method for synthesizing Mannich bases reported in current patent literature.

所用主要原料如下:邻甲酚,AR,上海阿拉丁生化科技股份有限公司产品;高活性聚异丁烯(HRPIB,Mn≈1000),扬子石化-巴斯夫有限责任公司产品;正己烷,GC,北京伊诺凯科技有限公司产品;甲苯,AR,北京伊诺凯科技有限公司;二甲苯,AR,天津市富宇精细化工有限公司产品;商用汽油清净剂6416,雅富顿公司;无水甲醇,AR,天津市大茂化学试剂厂产品;甲醛水溶液,37%,赛默飞世尔科技(中国)有限公司产品;三氟化硼乙醚,北京伊诺凯科技有限公司;对苯二胺,N,N-二甲基-1,4-苯二胺,GC,上海阿拉丁生化科技股份有限公司;乙二胺,AR,北京伊诺凯科技有限公司;S150芳烃溶剂,聚醚,北京兴普精细化工技术开发有限公司;N,N-二甲基-1,3-丙二胺,AR,北京伊诺凯科技有限公司;1,3,5-三(二甲基胺丙基)-1,3,5-六氢化三嗪,AR,北京伊诺凯科技有限公司。The main raw materials used are as follows: o-cresol, AR, a product of Shanghai Aladdin Biochemical Technology Co., Ltd.; high-activity polyisobutylene (HRPIB, Mn≈1000), a product of Yangzi Petrochemical-BASF Co., Ltd.; n-hexane, GC, a product of Beijing Inokai Technology Co., Ltd.; toluene, AR, a product of Beijing Inokai Technology Co., Ltd.; xylene, AR, a product of Tianjin Fuyu Fine Chemical Co., Ltd.; commercial gasoline detergent 6416, Afton Chemical Corporation; anhydrous methanol, AR, a product of Tianjin Damao Chemical Reagent Factory; formaldehyde aqueous solution, 37%, Thermo Fisher Scientific Products of Beijing Inokai Technology Co., Ltd. (China); boron trifluoride etherate, Beijing Inokai Technology Co., Ltd.; p-phenylenediamine, N,N-dimethyl-1,4-phenylenediamine, GC, Shanghai Aladdin Biochemical Technology Co., Ltd.; ethylenediamine, AR, Beijing Inokai Technology Co., Ltd.; S150 aromatic solvent, polyether, Beijing Xingpu Fine Chemical Technology Development Co., Ltd.; N,N-dimethyl-1,3-propylenediamine, AR, Beijing Inokai Technology Co., Ltd.; 1,3,5-tris(dimethylaminopropyl)-1,3,5-hexahydrotriazine, AR, Beijing Inokai Technology Co., Ltd.

实施例1合成聚异丁烯基邻甲基苯酚Example 1 Synthesis of polyisobutylene o-methylphenol

在装有搅拌器、N2通入管、热电偶温度计、球形冷凝管和进料泵的1L反应釜中,加入64.96g(0.601mol)邻甲酚、12.88g(0.091mol)三氟化硼乙醚催化剂、215.03g正己烷溶剂和300.91g(0.300mol)聚异丁烯(Mn=1000)在30℃反应6h。反应结束后,加入去离子水64ml,转移至1L分液漏斗中,再加入160ml甲醇,振荡后静置1h分层,分出下层液体后再重复两次,上层液体减压蒸馏后得到淡黄色聚异丁烯基邻甲基苯酚产物。通过元素分析得到产物中F含量小于1ppm,GC-MS分析得到邻甲酚含量小于0.006%,氧元素含量分析得到聚异丁烯基邻甲基苯酚收率为99%。In a 1L reactor equipped with a stirrer, N2 inlet tube, thermocouple thermometer, spherical condenser and feed pump, 64.96g (0.601mol) o-cresol, 12.88g (0.091mol) boron trifluoride ether catalyst, 215.03g n-hexane solvent and 300.91g (0.300mol) polyisobutylene (Mn = 1000) were added and reacted at 30°C for 6h. After the reaction, 64ml of deionized water was added, transferred to a 1L separatory funnel, and then 160ml of methanol was added. After shaking, the mixture was allowed to stand for 1h to separate the layers. After separating the lower layer of liquid, the mixture was repeated twice. The upper layer of liquid was distilled under reduced pressure to obtain a light yellow polyisobutylene o-cresol product. The F content in the product was less than 1ppm by elemental analysis, the o-cresol content was less than 0.006% by GC-MS analysis, and the yield of polyisobutylene o-cresol was 99% by oxygen element content analysis.

图1是实施例1中高活性聚异丁烯原料与聚异丁烯基邻甲基苯酚产物的对比红外谱图,其中的上图(1)为高活性聚异丁烯的红外谱图,下图(2)为聚异丁烯基邻甲基苯酚产物的红外谱图。FIG1 is a comparative infrared spectra of the high-activity polyisobutylene raw material and the polyisobutylene-based o-methylphenol product in Example 1, wherein the upper figure (1) is the infrared spectrum of the high-activity polyisobutylene, and the lower figure (2) is the infrared spectrum of the polyisobutylene-based o-methylphenol product.

由图1可知,在烷基化反应结束后,高活性聚异丁烯(HRPIB)消失的特征峰有:3070cm-1(末端α-烯烃C-H键的不对称伸缩振动)、1640cm-1(末端α-亚甲基C=C双键的伸缩振动)。合成的聚异丁烯基邻甲基苯酚的特征吸收峰有:3620cm-1(无缔合剂自由酚羟基O-H的伸缩振动峰,峰形尖锐)、3500-3200cm-1(分子间氢键缔合后的酚羟基的O-H伸缩振动,为宽的吸收峰)、1605cm-1和1505cm-1(单核芳烃C=C双键的骨架振动的两个吸收带)、1262cm-1(苯环上Ar-O的伸缩振动吸收峰)以及818cm-1(苯环产生1,2,4取代时,苯环上C-H的面外弯曲振动)。As shown in Figure 1, after the alkylation reaction, the characteristic peaks of the highly active polyisobutylene (HRPIB) that disappear are: 3070 cm -1 (asymmetric stretching vibration of the terminal α-olefin CH bond) and 1640 cm -1 (stretching vibration of the terminal α-methylene C=C double bond). The characteristic absorption peaks of the synthesized polyisobutylene o-methylphenol are: 3620 cm -1 (stretching vibration peak of the free phenolic hydroxyl group OH without an associating agent, with a sharp peak shape), 3500-3200 cm -1 (stretching vibration of the phenolic hydroxyl group OH after intermolecular hydrogen bonding, which is a broad absorption peak), 1605 cm -1 and 1505 cm -1 (two absorption bands of skeleton vibration of mononuclear aromatic C=C double bond), 1262 cm -1 (stretching vibration absorption peak of Ar-O on the benzene ring) and 818 cm -1 (out-of-plane bending vibration of CH on the benzene ring when the benzene ring is 1,2,4 substituted).

图2是实施例1中聚异丁烯基邻甲基苯酚产物的核磁共振氢谱(1H NMR)高场部分。图3是实施例1中聚异丁烯基邻甲基苯酚产物的核磁共振氢谱(1HNMR)低场部分。Figure 2 is the high field portion of the nuclear magnetic resonance hydrogen spectrum (1H NMR) of the polyisobutenyl o-methylphenol product in Example 1. Figure 3 is the low field portion of the nuclear magnetic resonance hydrogen spectrum (1H NMR) of the polyisobutenyl o-methylphenol product in Example 1.

由图2和图3可知,在化学位移2.261处,存在聚异丁烯基邻甲基苯酚苯环上甲基氢的特征峰;在化学位移4.561处,存在聚异丁烯基邻甲基苯酚苯环上羟基氢的特征峰;将甲基氢的积分定义为3,得到苯环上氢、羟基氢和甲基氢的积分比为0.98:0.99:0.98:0.97:3.00,接近理论值1:1:1:1:3,所以从核磁分析可知制备得到了目标产物聚异丁烯基邻甲基苯酚。It can be seen from Figures 2 and 3 that at the chemical shift of 2.261, there is a characteristic peak of methyl hydrogen on the benzene ring of polyisobutenyl o-methylphenol; at the chemical shift of 4.561, there is a characteristic peak of hydroxyl hydrogen on the benzene ring of polyisobutenyl o-methylphenol; the integral of methyl hydrogen is defined as 3, and the integral ratio of hydrogen, hydroxyl hydrogen and methyl hydrogen on the benzene ring is 0.98:0.99:0.98:0.97:3.00, which is close to the theoretical value of 1:1:1:1:3. Therefore, it can be seen from the nuclear magnetic resonance analysis that the target product polyisobutenyl o-methylphenol has been prepared.

实施例1的示例反应方程式如下。An exemplary reaction equation for Example 1 is as follows.

实施例2合成曼尼希碱Example 2 Synthesis of Mannich Base

在装有N2通入管、热电偶温度计、球形冷凝管和进料泵的四口烧瓶中,加入实施例1中的聚异丁烯基邻甲基苯酚55.11g、二甲苯56.03g、N,N-二甲基-1,4-苯二胺6.14g,滴加质量浓度为37%的甲醛水溶液4.89g,升温至150℃反应3h,反应结束后,减压蒸馏得到本发明的曼尼希碱。In a four-necked flask equipped with a N2 inlet tube, a thermocouple thermometer, a spherical condenser and a feed pump, 55.11 g of the polyisobutylene-o-methylphenol in Example 1, 56.03 g of xylene and 6.14 g of N,N-dimethyl-1,4-phenylenediamine were added, 4.89 g of a 37% formaldehyde aqueous solution was added dropwise, the temperature was raised to 150°C and the reaction was carried out for 3 hours. After the reaction was completed, the Mannich base of the present invention was obtained by distillation under reduced pressure.

图4为实施例2产物的红外谱图。由图4可知,合成曼尼希碱后产生的特征峰有:3500-3300cm-1(N-H伸缩振动,和O-H伸缩振动重叠,峰形进一步变宽),1749.35cm-1(发生1,2,4,6取代时苯环的C-H面外弯曲振动的泛频带),1162.11cm-1和1056.47cm-1(脂肪胺C-N伸缩振动),871.49cm-1(发生1,2,4,6取代时苯环的C-H面外弯曲振动)。Fig. 4 is an infrared spectrum of the product of Example 2. As shown in Fig. 4, the characteristic peaks generated after the synthesis of the Mannich base are: 3500-3300 cm -1 (NH stretching vibration, overlapping with OH stretching vibration, the peak shape is further broadened), 1749.35 cm -1 (overtone band of CH out-of-plane bending vibration of benzene ring when 1, 2, 4, 6 substitution occurs), 1162.11 cm -1 and 1056.47 cm -1 (aliphatic amine CN stretching vibration), 871.49 cm -1 (CH out-of-plane bending vibration of benzene ring when 1, 2, 4, 6 substitution occurs).

图5是实施例2产物的核磁共振氢谱。FIG5 is a hydrogen nuclear magnetic resonance spectrum of the product of Example 2.

由图5可知,曼尼希产物核磁谱图中化学位移5.23处为N,N-二甲基-1,4苯二胺发生曼尼希反应的仲胺基上的质子氢,4.47处为由甲醛羰基转化生成的亚甲基上氢质子的位移峰,化学位移2.84处为N,N-二甲基-1,4苯二胺的甲基质子峰,三者面积比为1:1.99:6.03,符合理论面积比。另外,低场处的较杂乱,是因为两个苯环的峰互相重叠,但仍然可以看出偏高场的苯环峰为N,N-二甲基-1,4苯二胺上的苯环,且面积符合比例。苯环上的羟基的化学位移峰消失,这是因为羟基在整个化学分子中的含量很低,且部分羟基参与了反应,使得羟基的含量进一步降低,故导致羟基质子化学位移峰的消失,可知副产物较少。As shown in Figure 5, the chemical shift of 5.23 in the NMR spectrum of the Mannich product is the proton hydrogen on the secondary amine group of N,N-dimethyl-1,4-phenylenediamine that undergoes the Mannich reaction, the chemical shift of 4.47 is the displacement peak of the hydrogen proton on the methylene group generated by the conversion of the formaldehyde carbonyl group, and the chemical shift of 2.84 is the methyl proton peak of N,N-dimethyl-1,4-phenylenediamine. The area ratio of the three is 1:1.99:6.03, which is consistent with the theoretical area ratio. In addition, the low field is more chaotic because the peaks of the two benzene rings overlap each other, but it can still be seen that the high-field benzene ring peak is the benzene ring on N,N-dimethyl-1,4-phenylenediamine, and the area is consistent with the ratio. The chemical shift peak of the hydroxyl group on the benzene ring disappears because the content of the hydroxyl group in the entire chemical molecule is very low, and some of the hydroxyl groups participate in the reaction, which further reduces the content of the hydroxyl group, resulting in the disappearance of the chemical shift peak of the hydroxyl proton, which shows that there are fewer by-products.

氧含量分析可得收率为84%。Oxygen content analysis gave a yield of 84%.

实施例2的示例反应方程式如下。An exemplary reaction equation for Example 2 is as follows.

实施例3Example 3

在装有N2通入管、热电偶温度计、球形冷凝管和进料泵的四口烧瓶中,加入实施例1中的聚异丁烯基邻甲基苯酚33.14g、甲苯溶剂34.91g、对苯二胺3.34g,以0.06ml/min的流速滴加质量浓度为37%的甲醛水溶液2.92g,升温至90℃反应3h,反应结束后,减压蒸馏得本发明的曼尼希碱。In a four-necked flask equipped with a N2 inlet tube, a thermocouple thermometer, a spherical condenser and a feed pump, 33.14 g of the polyisobutylene-o-methylphenol in Example 1, 34.91 g of toluene solvent and 3.34 g of p-phenylenediamine were added, and 2.92 g of a 37% formaldehyde aqueous solution was added dropwise at a flow rate of 0.06 ml/min. The temperature was raised to 90°C and the reaction was carried out for 3 hours. After the reaction was completed, the Mannich base of the present invention was obtained by distillation under reduced pressure.

实施例3的示例反应方程式如下。An exemplary reaction equation for Example 3 is as follows.

对比例1Comparative Example 1

在装有N2通入管、热电偶温度计、球形冷凝管和进料泵的四口烧瓶中,加入实施例1中的聚异丁烯基邻甲基苯酚55.11g、二甲苯56.03g,升温至45℃,加入1,3,5-三(二甲基胺丙基)-1,3,5-六氢化三嗪5.17g,升温至140℃反应4h,减压蒸馏得到对比清净剂产物。In a four-necked flask equipped with a N2 inlet tube, a thermocouple thermometer, a spherical condenser and a feed pump, 55.11 g of polyisobutylene o-methylphenol and 56.03 g of xylene in Example 1 were added, the temperature was raised to 45°C, 5.17 g of 1,3,5-tris(dimethylaminopropyl)-1,3,5-hexahydrotriazine was added, the temperature was raised to 140°C, the reaction was carried out for 4 hours, and a comparative detergent product was obtained by distillation under reduced pressure.

图6为对比例1产物的红外谱图。FIG6 is an infrared spectrum of the product of Comparative Example 1.

由图6可知,合成曼尼希碱后产生的特征峰有:3500-3300cm-1(N-H伸缩振动,和O-H伸缩振动重叠,峰形进一步变宽),1748.64cm-1(仲胺的N-H弯曲振动峰),1015.76cm-1(C-N伸缩振动峰)。As shown in Figure 6, the characteristic peaks produced after the synthesis of the Mannich base are: 3500-3300 cm -1 (NH stretching vibration, overlapping with OH stretching vibration, the peak shape is further broadened), 1748.64 cm -1 (NH bending vibration peak of secondary amine), 1015.76 cm -1 (CN stretching vibration peak).

图7是对比例1产物的核磁共振氢谱。FIG. 7 is a hydrogen nuclear magnetic resonance spectrum of the product of Comparative Example 1.

由图7可知,苯环部分化学位移复杂,存在多种结构,化学位移4.82和3.92为不同结构中的仲胺基-NH-的氢质子位移峰,化学位移3.61为由甲醛羰基转化生成的亚甲基上氢质子的位移峰,化学位移2.71为与发生曼尼希反应的胺基相连的亚甲基的位移峰。As shown in Figure 7, the chemical shifts of the benzene ring are complex and there are multiple structures. The chemical shifts 4.82 and 3.92 are the hydrogen proton shift peaks of the secondary amine group -NH- in different structures, the chemical shift 3.61 is the shift peak of the hydrogen proton on the methylene generated by the conversion of the formaldehyde carbonyl group, and the chemical shift 2.71 is the shift peak of the methylene connected to the amine group that undergoes the Mannich reaction.

由对比例1的红外谱图和核磁共振氢谱可以看出该对比例中存在双曼尼希和环曼尼希副产物,符合US7384434B2中的报道。From the infrared spectrum and hydrogen nuclear magnetic resonance spectrum of comparative example 1, it can be seen that there are bis-Mannich and cyclo-Mannich by-products in the comparative example, which is consistent with the report in US7384434B2.

对比例1的示例反应方程式如下。An exemplary reaction equation for Comparative Example 1 is as follows.

对比例2Comparative Example 2

在装有N2通入管、热电偶温度计、球形冷凝管和进料泵的四口烧瓶中,加入实施例1中的聚异丁烯邻甲酚38.14g、二甲苯38.13g、N,N-二甲基-1,3-丙二胺3.29g,滴加质量浓度为37%的甲醛水溶液3.44g,升温至150℃反应3h,反应结束后,减压蒸馏得到对比清净剂产物。In a four-necked flask equipped with a N2 inlet tube, a thermocouple thermometer, a spherical condenser and a feed pump, 38.14 g of polyisobutylene o-cresol, 38.13 g of xylene and 3.29 g of N,N-dimethyl-1,3-propylenediamine in Example 1 were added, 3.44 g of a 37% formaldehyde aqueous solution was added dropwise, the temperature was raised to 150°C and the reaction was carried out for 3 hours. After the reaction was completed, the comparative detergent product was obtained by distillation under reduced pressure.

对比例2的示例反应方程式如下。An exemplary reaction equation for Comparative Example 2 is as follows.

对比例3Comparative Example 3

在装有N2通入管、热电偶温度计、球形冷凝管和进料泵的四口烧瓶中,加入实施例1中的聚异丁烯基邻甲基苯酚33.12g、甲苯溶剂35.7g、乙二胺1.64g,以0.06ml/min的流速滴加质量浓度为37%的甲醛水溶液2.89g,升温至110℃反应3h,反应结束后,减压蒸馏得本发明的曼尼希碱。In a four-necked flask equipped with a N2 inlet tube, a thermocouple thermometer, a spherical condenser and a feed pump, 33.12 g of the polyisobutylene-o-methylphenol in Example 1, 35.7 g of toluene solvent and 1.64 g of ethylenediamine were added, and 2.89 g of a 37% formaldehyde aqueous solution was added dropwise at a flow rate of 0.06 ml/min. The temperature was raised to 110°C and the reaction was carried out for 3 hours. After the reaction was completed, the Mannich base of the present invention was obtained by distillation under reduced pressure.

对比例3的示例反应方程式如下。An exemplary reaction equation for Comparative Example 3 is as follows.

实施例4Example 4

在300ml符合国Ⅵ标准的95#汽油中加入300ppm(约0.0673g)实施例的曼尼希碱或对比清净剂(包括对比例1~3的对比曼尼希碱和6416商用对比剂)和300ppm聚醚基础油,分别混合调制为包含曼尼希碱清净剂的汽油组合物。300 ppm (about 0.0673 g) of the Mannich base or comparative detergent (including the comparative Mannich base of comparative examples 1 to 3 and 6416 commercial comparative agent) and 300 ppm of polyether base oil were added to 300 ml of 95 # gasoline meeting the National VI standard, and the mixture was mixed to prepare a gasoline composition containing the Mannich base detergent.

实施例5清净性能评价Example 5 Cleaning Performance Evaluation

分别向实施例4的汽油组合物及空白汽油中加入740μl双环戊二烯生焦剂,根据GB/T 37322-2019《汽油清净性评价汽油机进气阀沉积物模拟试验法》,采用兰州维科石化仪器公司生产的L-2型进气阀沉积物模拟试验机评定本发明曼尼希碱与对比清净剂的清净性能。740 μl of dicyclopentadiene coking agent was added to the gasoline composition of Example 4 and blank gasoline respectively, and the cleaning performance of the Mannich base of the present invention and the comparative detergent was evaluated using an L-2 intake valve deposit simulation tester produced by Lanzhou Weike Petrochemical Instrument Co., Ltd. according to GB/T 37322-2019 “Test method for simulation of gasoline engine intake valve deposits for evaluation of gasoline detergency”.

具体操作方法如下:The specific operation method is as follows:

称量并记录干燥沉积物收集器和参比板各两次取平均值后,将沉积物收集器装入试验设备并夹紧,进行清净性能评定试验,试验时间为85min,喷油时间为75min,试验温度为175℃,温控精度±1℃。接通气源后空气压力为80kPa±1kPa,空气流量为700L/h±20L/h。试验结束后用镊子取出沉积物收集器,冷却至室温,将其置于盛有正庚烷的容器中静置浸泡6min后取出,置于盛有石油醚(60℃~90℃)的容器中,静置浸泡1min后取出,用纸棒塞入收集器的测温孔中,吸去孔内的试剂,称量收集器的重量,计算沉积物质量。沉积物清净效果见表1。After weighing and recording the dry sediment collector and the reference plate twice and taking the average value, the sediment collector is loaded into the test equipment and clamped to conduct a cleaning performance evaluation test. The test time is 85 minutes, the oil injection time is 75 minutes, the test temperature is 175°C, and the temperature control accuracy is ±1°C. After connecting the air source, the air pressure is 80kPa±1kPa, and the air flow rate is 700L/h±20L/h. After the test, the sediment collector is taken out with tweezers, cooled to room temperature, placed in a container filled with n-heptane and soaked for 6 minutes, then taken out, placed in a container filled with petroleum ether (60℃~90℃), soaked for 1 minute, then taken out, and a paper stick is inserted into the temperature measuring hole of the collector to absorb the reagent in the hole, weigh the weight of the collector, and calculate the mass of the sediment. The sediment cleaning effect is shown in Table 1.

表1Table 1

清净剂Detergent 沉积物量Sediment volume 沉积物下降率Sediment decline rate 空白blank 9.0mg9.0mg -- 实施例2Example 2 1.10mg1.10mg 87.78%87.78% 实施例3Example 3 1.27mg1.27mg 85.88%85.88% 对比例1Comparative Example 1 2.02mg2.02mg 77.56%77.56% 对比例2Comparative Example 2 1.56mg1.56mg 82.67%82.67% 对比例3Comparative Example 3 1.78mg1.78mg 80.22%80.22% 6416商用对比剂6416 Commercial contrast agent 1.43mg1.43mg 84.11%84.11%

实施例6防锈性能评定Example 6 Evaluation of rust prevention performance

采用GB/T19230.1-2003汽油清净剂防锈性能试验方法评价防锈性能。该方法是在(38±1)℃温度条件下,将圆柱型的试棒完全浸入搅拌条件下的30ml试验汽油与30ml蒸馏水的混合物,进行4h锈蚀试验,观察试棒的锈蚀程度。The anti-rust performance of gasoline detergents was evaluated using the GB/T19230.1-2003 gasoline detergent anti-rust performance test method. This method involves completely immersing a cylindrical test rod in a mixture of 30 ml of test gasoline and 30 ml of distilled water under stirring conditions at a temperature of (38±1)°C for 4 hours to observe the degree of corrosion of the test rod.

评价腐蚀程度的分类如下:The classification for evaluating the degree of corrosion is as follows:

轻度锈蚀:限于锈点不超过6个,每个锈点的直径小于等于1mm。Mild rust: limited to no more than 6 rust spots, and the diameter of each rust spot is less than or equal to 1mm.

中度锈蚀:锈点超过6个,但少于试棒的表面积的5%。Moderate rust: There are more than 6 rust spots, but less than 5% of the surface area of the test bar.

严重锈蚀:锈点超过试棒表面积的5%。Severe rust: Rust spots exceed 5% of the test bar surface area.

对实施例的曼尼希碱或对比清净剂以及空白样进行了防锈性能评定,测定结果见表2。The anti-rust performance of the Mannich base or comparative detergent of the examples and the blank samples was evaluated. The test results are shown in Table 2.

表2Table 2

清净剂Detergent 加剂量/mg/kgAdded dose/mg/kg 锈蚀程度Degree of rust 空白blank -- 严重serious 实施例2Example 2 100100 轻度Mild 实施例3Example 3 100100 轻度Mild 对比例1Comparative Example 1 100100 中度Moderate 对比例2Comparative Example 2 100100 中度Moderate 对比例3Comparative Example 3 100100 中度Moderate 6416商用对比剂6416 Commercial contrast agent 100100 中度Moderate

Claims (10)

1.曼尼希碱,其结构如式(I)所示:1. Mannich base, the structure of which is shown in formula (I): 在式(I)中,R0选自C1~8的直链或支链亚烷基;各个R1彼此相同或不同,各自独立地选自H、C1~4的直链或支链烷基;各个R1’各自独立地选自H、C1~4的直链或支链烷基和苯基;R2选自数均分子量Mn为300~3000的烃基;R3选自C1~6的直链或支链烷基。In formula (I), R 0 is selected from a C 1-8 straight chain or branched alkylene group; each R 1 is the same as or different from each other and is independently selected from H, a C 1-4 straight chain or branched alkyl group; each R 1 ' is independently selected from H, a C 1-4 straight chain or branched alkyl group and a phenyl group; R 2 is selected from a hydrocarbon group with a number average molecular weight Mn of 300 to 3000; R 3 is selected from a C 1-6 straight chain or branched alkyl group. 2.按照权利要求1所述的曼尼希碱,其特征在于,R0选自C1~4的直链或支链亚烷基,各个R1各自独立地选自H或甲基,各个R1’各自独立地选自H、甲基,R2选自数均分子量Mn为500~2500的聚异丁烯基;R3选自C1~4的直链或支链烷基。2. The Mannich base according to claim 1, characterized in that R 0 is selected from a C 1-4 straight chain or branched alkylene group, each R 1 is independently selected from H or methyl, each R 1 ' is independently selected from H, methyl, R 2 is selected from a polyisobutylene group with a number average molecular weight Mn of 500 to 2500; and R 3 is selected from a C 1-4 straight chain or branched alkyl group. 3.曼尼希碱的制备方法,包括使式(X)所示化合物、脂肪醛、式(Y)所示化合物发生反应,收集产物;3. A method for preparing a Mannich base, comprising reacting a compound represented by formula (X), a fatty aldehyde, and a compound represented by formula (Y), and collecting the product; 在式(X)中,R2选自数均分子量Mn为300~3000的烃基;R3选自C1~6的直链或支链烷基;In formula (X), R 2 is selected from a hydrocarbon group having a number average molecular weight Mn of 300 to 3000; R 3 is selected from a C 1 to 6 straight chain or branched alkyl group; 所述脂肪醛的碳数为1~8;The carbon number of the fatty aldehyde is 1 to 8; 在式(Y)中,各个R1彼此相同或不同,各自独立地选自H、C1~4的直链或支链烷基;各个R1’各自独立地选自H、C1~4的直链或支链烷基和苯基。In formula (Y), each R 1 is the same as or different from each other and is independently selected from H, C 1-4 linear or branched alkyl; each R 1 ′ is independently selected from H, C 1-4 linear or branched alkyl and phenyl. 4.按照权利要求3所述的方法,其特征在于,在式(X)中,R2选自数均分子量Mn为500~2500的聚异丁烯基,R3选自C1~4的直链或支链烷基;所述脂肪醛的碳数为1~4;在式(Y)中,各个R1各自独立地选自H或甲基,各个R1’各自独立地选自H、甲基。4. The method according to claim 3, characterized in that, in formula (X), R2 is selected from polyisobutylene with a number average molecular weight Mn of 500 to 2500, R3 is selected from a C1 to 4 straight chain or branched alkyl group; the carbon number of the fatty aldehyde is 1 to 4; in formula (Y), each R1 is independently selected from H or methyl, and each R1 ' is independently selected from H or methyl. 5.按照权利要求3所述的方法,其特征在于,所述脂肪醛为甲醛或乙醛;式(Y)所示化合物选自对苯二胺、2-甲基对苯二胺、四甲基对苯二胺、N,N-二甲基-1,4-苯二胺、N-乙基对苯二胺、N,N-二乙基对苯二胺和N,N-二乙基-3-甲基对苯二胺中的一种或多种。5. The method according to claim 3, characterized in that the fatty aldehyde is formaldehyde or acetaldehyde; and the compound represented by formula (Y) is selected from one or more of p-phenylenediamine, 2-methyl-p-phenylenediamine, tetramethyl-p-phenylenediamine, N,N-dimethyl-1,4-phenylenediamine, N-ethyl-p-phenylenediamine, N,N-diethyl-p-phenylenediamine and N,N-diethyl-3-methyl-p-phenylenediamine. 6.按照权利要求3所述的方法,其特征在于,所述式(X)所示化合物、脂肪醛、式(Y)所示化合物之间的摩尔比为1:0.1~3.5:0.3~3。6. The method according to claim 3, characterized in that the molar ratio between the compound represented by formula (X), the fatty aldehyde and the compound represented by formula (Y) is 1:0.1-3.5:0.3-3. 7.按照权利要求3所述的方法,其特征在于,所述式(X)所示化合物、脂肪醛、式(Y)所示化合物之间发生反应的温度为50℃~200℃。7. The method according to claim 3, characterized in that the temperature at which the compound represented by formula (X), the fatty aldehyde and the compound represented by formula (Y) react is 50°C to 200°C. 8.按照权利要求3所述的方法,其特征在于,在所述式(X)所示化合物、脂肪醛、式(Y)所示化合物的反应中加入溶剂,所述溶剂选自沸点在100℃~160℃之间的烃类。8. The method according to claim 3, characterized in that a solvent is added during the reaction of the compound represented by formula (X), the fatty aldehyde and the compound represented by formula (Y), and the solvent is selected from hydrocarbons with a boiling point between 100°C and 160°C. 9.按照权利要求3所述的方法,其特征在于,在所述式(X)所示化合物、脂肪醛、式(Y)所示化合物的反应中加入稀释剂,所述稀释剂为矿物润滑油、聚烯烃和聚醚中的一种或多种。9. The method according to claim 3, characterized in that a diluent is added during the reaction of the compound represented by formula (X), the fatty aldehyde and the compound represented by formula (Y), and the diluent is one or more of mineral lubricating oil, polyolefin and polyether. 10.权利要求1或2的曼尼希碱或者按照权利要求3~9之一方法所制得的曼尼希碱用作汽油清净剂的用途。10. Use of the Mannich base according to claim 1 or 2 or the Mannich base prepared by the method according to any one of claims 3 to 9 as a gasoline detergent.
CN202310066511.2A 2023-01-13 2023-01-13 Mannich base and preparation method and application thereof Pending CN118344511A (en)

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