TW200305554A - Method for preparing p-aminobenzoic acid - Google Patents

Method for preparing p-aminobenzoic acid Download PDF

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TW200305554A
TW200305554A TW092104107A TW92104107A TW200305554A TW 200305554 A TW200305554 A TW 200305554A TW 092104107 A TW092104107 A TW 092104107A TW 92104107 A TW92104107 A TW 92104107A TW 200305554 A TW200305554 A TW 200305554A
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methyl
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reaction
benzoate
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TW092104107A
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TWI250971B (en
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Sung-Sam Park
Jung-Ho Park
Seung-Hwan Kim
Sung-Su Hwang
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Sk Chemicals Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/14Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof
    • C07C227/18Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton from compounds containing already amino and carboxyl groups or derivatives thereof by reactions involving amino or carboxyl groups, e.g. hydrolysis of esters or amides, by formation of halides, salts or esters
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/04Formation of amino groups in compounds containing carboxyl groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C229/00Compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C229/52Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to carbon atoms of six-membered aromatic rings of the same carbon skeleton
    • C07C229/54Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to carbon atoms of six-membered aromatic rings of the same carbon skeleton with amino and carboxyl groups bound to carbon atoms of the same non-condensed six-membered aromatic ring
    • C07C229/60Compounds containing amino and carboxyl groups bound to the same carbon skeleton having amino and carboxyl groups bound to carbon atoms of six-membered aromatic rings of the same carbon skeleton with amino and carboxyl groups bound to carbon atoms of the same non-condensed six-membered aromatic ring with amino and carboxyl groups bound in meta- or para- positions
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C231/00Preparation of carboxylic acid amides
    • C07C231/02Preparation of carboxylic acid amides from carboxylic acids or from esters, anhydrides, or halides thereof by reaction with ammonia or amines
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C235/00Carboxylic acid amides, the carbon skeleton of the acid part being further substituted by oxygen atoms
    • C07C235/70Carboxylic acid amides, the carbon skeleton of the acid part being further substituted by oxygen atoms having carbon atoms of carboxamide groups and doubly-bound oxygen atoms bound to the same carbon skeleton
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/30Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • C07C67/307Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by introduction of halogen; by substitution of halogen atoms by other halogen atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/76Esters of carboxylic acids having a carboxyl group bound to a carbon atom of a six-membered aromatic ring

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  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The method for preparing p-aminobenzoic acid using methyl-4-formylbenzoate as a starting material, which is a major by-product produced while synthesizing dimethylterphthalate is disclosed. The method comprises the steps of: chlorinating methyl-4-formylbenzoate to produce methyl-4-fchloromylbenzoate; amidating the methyl-4-chloroformylbenzoate to produce methyl-4-carbamoylbenzoate; and carrying out Hofmann reaction with the produced methyl-4-carbamoylbenzoate in aqueous solution. During the steps for preparing p-aminobenzoic acid, impurities in the methyl-4-formylbenzoate are removed.

Description

200305554 玖、發明說明 【發明所屬之技術領域】 本發明係關於一種製備對-胺基苯甲酸(以下簡稱 「PAB A」)的方法,詳言之,係關於一種以4-甲醯苯甲 酸甲酯為起始物來製備對-胺基苯甲酸的方法,其中該 4-甲醯苯甲酸甲酯為合成苯二甲酸二甲酯(以下稱 「DMT」)時所產生的主要副產物。200305554 发明 Description of the invention [Technical field to which the invention belongs] The present invention relates to a method for preparing p-aminobenzoic acid (hereinafter referred to as "PAB A"). In particular, it relates to a method for preparing 4-formamylbenzoic acid methyl ester A method for preparing p-aminobenzoic acid with an ester as a starting material, wherein the 4-formamidinebenzoic acid methyl ester is a main by-product generated during the synthesis of dimethyl phthalate (hereinafter referred to as "DMT").

【先前技術】[Prior art]

對-胺基苯甲酸(PABA)為一種可溶於水、乙醇及乙 醚的黃色結晶化合物。PABA被廣泛用於各種化學產業 中,其應用範圍包括當作防曬乳液中用來吸收UV的物 質,芳香性聚合物成分的起始物,製造直接染料(direct dye)或媒染染料(vat dye)時的中間產物,藥學中間物, 及可作為動物飼料之維生素B的辅助因子、維生素B 群、及一諸如苯佐卡因(即,對胺基苯曱酸乙酯)、普卡 因(procaine)等局部麻醉劑的起始物。習知用來製備 PABA的方法如下示: [反應式1] 4 200305554Para-aminobenzoic acid (PABA) is a yellow crystalline compound that is soluble in water, ethanol, and ether. PABA is widely used in various chemical industries, and its application scope includes being used as a substance for absorbing UV in sunscreen emulsions, the starting material of aromatic polymer components, and manufacturing direct dyes or vat dyes. Intermediates, pharmaceutical intermediates, and vitamin B cofactors, vitamin B groups, and a benzocaine (ie, p-aminophenylacetate), procaine ) And other starting materials for local anesthetics. The conventional method for preparing PABA is shown below: [Reaction 1] 4 200305554

如反應式1所示,甲苯係被硝化以產生鄰-硝基甲 苯及對-硝基甲苯,且所生成之鄰-硝基甲苯及對-硝基 甲苯彼此係被加以分開。之後,將對-硝基甲苯氧化生 成對-硝基苯曱酸。在最後一個步驟,對-硝基苯甲酸中 的硝基團係以諸如氮氯酸-锡混合物、白金、及雷尼錄 (Raney Nickel)等氫化催化劑還原成標的化合物,即 PABA。但是,反應式1的方法有一項缺點,亦即在將 曱苯硝化的時後,會同時生成鄰位-及對位-異構物,且 該異構物需以一諸如分餾結‘的方法加以分開。特別 是,該鄰位-異構物並不具任何用途,一般係直接將其 丟棄,因此會造成PABA的製造成本上升。此外,諸如 過氧化氫及氧化鎂之類用來氧化對-硝基曱苯的氧化 劑,及諸如白金-催化劑及鐵-催化劑之類用來還原對-硝基苯甲酸的還原劑均為非常昂貴的化合物,也會增加 製造成本。 200305554 另一種製備方法,揭示於美國專利第3,931,210號, 其係使用苯二甲酸之單甲酯化合物作為起始物來製造 PABA。該苯二甲酸之單甲酯化合物係為合成苯二甲酸 二甲酯(DM T)時的主要副產物,而該苯二甲酸二甲酯又 是合成聚酯樹脂時的主要原料。在此方法中,苯二甲酸 之單甲酯化合物係與按反應生成單醯胺化合物,並以霍 夫曼反應(Hofmann reaction)將該單酿胺化合物轉變成 PABA。可使用該苯二曱酸之單甲酯化合物或其之鋰鹽、 鈣鹽或鎂鹽。但是,該苯二甲酸之單曱酯化合物可大量 取自苯二甲酸二甲酯之工業或商業製程。因此,以製造 成本的角度而言,苯二曱酸之單曱酯化合物為製造 PABA較佳的起始化合物《但是,此方法亦有缺點,即 以合成苯二甲酸二甲酯時所產生的苯二甲酸之單甲醋化 合物為起始物,並無法充分降低PABA的製造成本,且 的苯二甲酸之單甲酯化合物的醯胺反應需要在高溫高壓 下進行。 【内容】As shown in Reaction Formula 1, the toluene system is nitrated to produce o-nitrotoluene and p-nitrotoluene, and the resulting o-nitrotoluene and p-nitrotoluene are separated from each other. Thereafter, p-nitrotoluene is oxidized to form p-nitrophenylarsinic acid. In the last step, the nitro group in p-nitrobenzoic acid is reduced to the target compound, PABA, with a hydrogenation catalyst such as a mixture of chlorin-tin, platinum, and Raney Nickel. However, the method of reaction formula 1 has a disadvantage, that is, after the toluene is nitrated, ortho- and para-isomers are simultaneously formed, and the isomers need to be processed by a method such as fractionation. Separate them. In particular, the ortho-isomer is not used for any purpose, and it is generally directly discarded, which will increase the manufacturing cost of PABA. In addition, oxidants such as hydrogen peroxide and magnesium oxide used to oxidize p-nitrobenzone, and reducing agents such as platinum-catalyst and iron-catalyst to reduce p-nitrobenzoic acid are very expensive. Compounds will also increase manufacturing costs. 200305554 Another preparation method is disclosed in U.S. Patent No. 3,931,210, which uses a monomethyl compound of phthalic acid as a starting material to produce PABA. The monomethyl compound of the phthalic acid is the main by-product in the synthesis of dimethyl phthalate (DM T), and the dimethyl phthalate is the main raw material in the synthesis of the polyester resin. In this method, a monomethyl compound of phthalic acid is reacted with a monomethylamine compound, and the monomethylamine compound is converted into PABA by a Hofmann reaction. The monomethyl compound of phthalic acid or a lithium salt, calcium salt or magnesium salt thereof can be used. However, the monomethyl ester compound of phthalic acid can be obtained in large quantities from industrial or commercial processes of dimethyl phthalate. Therefore, from the perspective of manufacturing cost, the monomethyl ester compound of phthalic acid is the preferred starting compound for the production of PABA. However, this method also has disadvantages, that is, the The monomethyl vinegar compound of phthalic acid is a starting material, which cannot sufficiently reduce the production cost of PABA, and the ammonium reaction of the monomethyl phthalate compound of phthalic acid needs to be performed at high temperature and pressure. 【content】

對-胺 因此,本發明曰的夕一及此,·· 益的方法,以由 基苯曱酸。P-Amine Therefore, the present invention is described as follows, and the method is beneficial to phenylbenzoic acid.

本發明之另一目 成製程中的副產物的 200305554 本發明之另一目的係提供一種無須使用保護基且無 需使用一單獨製程的情況下,來製備對-胺基苯甲酸的 方法。Another object of the present invention 200305554 Another object of the present invention is to provide a method for preparing p-aminobenzoic acid without using a protective group and without using a separate process.

為達成這些目的,本發明提供一製備對-胺基苯甲 酸的方法,其係包含下列步驟:將 4-甲醯苯曱酸甲酯 氯化生成4-氣甲醯苯甲酸曱酯;將4-氯甲醯苯甲酸甲 酯醯胺化以生成4-胺曱醢苯甲酸甲酯;並以所生成的4-胺曱醯苯甲酸曱酯於溶液中執行霍夫曼反應。在此方法 中,該氣化步驟較佳係藉由將 4-甲醯苯甲酸甲酯熔解 成液態相,並添加 1至3莫耳當量的氯氣(Cl2)方式來 執行。該醯胺化步驟較佳係藉由添加溶解於有機溶劑之 4-氯甲醯苯甲酸甲酯至氨水中來執行,或是藉由供應氨 氣至溶解於有機溶劑中的 4-氯甲醯苯曱酸曱酯中來執 行。該霍夫曼反應較佳係藉由添加i化鹼至溶於鹼性溶 液之4-胺曱醯苯曱酸曱酯中來執行。In order to achieve these objectives, the present invention provides a method for preparing p-aminobenzoic acid, which comprises the following steps: chlorinating methyl 4-formamylbenzoate to form 4-methylformylbenzoate; -Amine methyl chloroformate benzoate is aminated to form methyl 4-amine benzoate; and a Huffman reaction is performed with the resulting 4-amine benzoate benzoate in solution. In this method, the gasification step is preferably performed by melting methyl 4-formamidinebenzoate into a liquid phase and adding 1 to 3 mole equivalents of chlorine gas (Cl2). The amidation step is preferably performed by adding methyl 4-chloroformamidinebenzoate dissolved in an organic solvent to ammonia water, or by supplying ammonia gas to 4-chloroformamidine dissolved in an organic solvent. Acetyl phenylacetate was performed. The Huffman reaction is preferably performed by adding an alkali compound to 4-aminophosphonium benzoate dissolved in an alkaline solution.

【實施方式】 參照下列說明,將更能了解本發明的各項優點及其 應用。 依據本發明,用以製備對-胺基苯曱酸的起始物,4-曱醢苯曱酸甲酯(MFB),乃是合成 DMT製程中的一項 主要副產物。DMT是用來製備聚酯樹脂的原料,習知 係以下列反應式2進行製備,其中Me代表甲基基團。 [反應式2] 7 200305554[Embodiment] With reference to the following description, the advantages and applications of the present invention will be better understood. According to the present invention, the starting material for the preparation of p-aminophenylarsine, methyl 4-arsylbenzoate (MFB), is a major by-product in the process of synthesizing DMT. DMT is a raw material for preparing polyester resin, and it is conventionally prepared according to the following reaction formula 2, where Me represents a methyl group. [Reaction formula 2] 7 200305554

COOHCOOH

COOH COOMeCOOH COOMe

由上述DMT合成製程中所生成副產物之組成,會 隨著合成製程條件的改變而改變。當合成速率增加時, 所產生的副產物包括 80%(wt%)的 4-曱醯苯曱酸甲酯 (MFB)、9%(wt%)的 DMT、4%(wt%)的對-甲苯甲酯 (MPT),因此4-甲醯苯曱酸甲酯係為主要的副產物。已 知全球採用 DMT合成製程的伊士曼科達公司、杜邦公 司、及SK化學公司,一般都將其製程中的副產物加以 丟棄或焚毁。 本發明即係使用 4-甲醯苯曱酸甲酯作為起始物, 依下列反應式3來製備對-胺基苯甲酸。 [反應式3]The composition of the by-products generated in the DMT synthesis process described above will change as the conditions of the synthesis process change. When the synthesis rate is increased, the by-products produced include 80% (wt%) of methyl 4-benzophenylate (MFB), 9% (wt%) of DMT, and 4% (wt%) of p- Toluyl methyl ester (MPT), so methyl 4-formamylbenzoate is the main by-product. Eastman Kodak, DuPont, and SK Chemicals, which are known to use DMT synthesis processes worldwide, generally discard or incinerate by-products from their processes. In the present invention, p-aminobenzoic acid is prepared according to the following reaction formula 3 using methyl 4-formamylbenzoate as a starting material. [Reaction formula 3]

COOCH3 COOCH3 COOCH3 COOH 200305554COOCH3 COOCH3 COOCH3 COOH 200305554

如反應式3所示,在第一步驟中,4-甲醯苯甲酸甲 酿係被氣化以產生4_氣曱醯苯甲酸曱酯。此氯化步驟 較佳係藉由將4-曱醯苯甲酸甲酯於大氣壓下熔解成液 態相’並添加1至3莫耳當量的氣氣(C12)方式來執行。 反應物4-甲酿笨甲酸曱酯的熔化溫度較佳係介於4〇cc 至200 C間’更佳係介於40°C至100°C間,最佳係介於 50 C至70 C間。當熔解溫度低於40°C時,反應物4-甲 醯苯甲酸曱8旨無法被充分熔解,且反應速率將變慢,將 使反應無法有效地進行。當熔解溫度高於2 〇 〇它時,將 增加能量消耗’並產生副反應,且產率將明顯下降。如 果所用氣氣量低於1莫耳當量時,反應將不完全;但如 果所用氣氣量高於3莫耳當量時,也無法使產率再往上 增加。氯化製程的產物在反應溫度下係停留於液相,且 反應時間一般為1 〇小時,且反應產率約為90〇/〇。As shown in Reaction Formula 3, in the first step, the 4-formamylbenzoate methyl alcohol system is gasified to produce 4-methylammonium benzoate. This chlorination step is preferably performed by dissolving methyl 4-fluorenebenzoate into a liquid phase 'at atmospheric pressure and adding 1 to 3 molar equivalents of gas (C12). The melting temperature of the reactant 4-methylbenzyl benzate is preferably between 40 cc and 200 C, more preferably between 40 ° C and 100 ° C, and most preferably between 50 C and 70 C. between. When the melting temperature is lower than 40 ° C, the reactant 4-formamidinebenzoate 曱 8 cannot be fully melted, and the reaction rate will be slowed down, which will prevent the reaction from proceeding effectively. When the melting temperature is higher than 2000, it will increase energy consumption ' and cause side reactions, and the yield will decrease significantly. If the amount of gas used is less than 1 mole equivalent, the reaction will not be complete; but if the amount of gas used is greater than 3 mole equivalents, the yield cannot be increased further. The product of the chlorination process stays in the liquid phase at the reaction temperature, and the reaction time is generally 10 hours, and the reaction yield is about 90/0.

在第二步驟中,將氣化製程所生成的4_氯甲醯苯 甲酸甲酯醯胺化以生成4 -胺甲醯苯甲酸甲酯。此醯胺 化步驟較佳係藉由讓4-氣甲醯苯甲酸甲酯與氨水 (NHWH)或溶於水之氨氣(NH3)和/或有機溶劑反應的方 式來執行。詳言之,此醯胺化反應較佳係藉由將熔融態 的4-氣甲醯苯曱酸曱酯逐滴加入氨水中的方式來執 行,或藉由將溶於有機溶劑中的 4-氣曱醯苯甲酸甲醋 逐滴加入氨水中的方式來執行,或將氨氣供至已溶於有 機溶劑中的4-氣甲醯苯曱酸甲酯中的方式來執行。 可供此醢胺化製程使用的有機溶劑包括各類可溶解 9 200305554 4-氯甲酿苯甲酸甲醋之有機溶劑,且此類有機溶劑的較 佳範例包括例如曱苯、乙酸乙酯、及其之混合物之類的 疏水性有機溶劑。有機溶劑的用量較佳係為4_氣甲醢 苯甲酸甲醋重量的0倍到10倍間,更佳係為4_氯甲醯 苯曱酸甲酯重量的0.5倍到8倍間。在此醯胺化步驟中, 該4-氣曱醯苯甲酸甲酯係於固相中生成,因此可輕易 地將其自各種副產物溶液中分離出來。反應容器中諸如 對-曱本曱酯及本二甲酸二曱酯之類的副產物係溶於有 機溶劑中,因此可和4-氣曱醯苯甲酸甲酯分開。此醯 胺化步驟可於大氣壓下執行,且反應溫度較佳係介於i °C至5 0°C間,更佳係介於3°C至30°C間。如果氮的來 源為氨氣,此醯胺化步驟較佳係在相當高的溫度下進 行’例如在2 5 0 C下進行以提高氣體活性。如果反應溫 度低於1 C ’則反應速率將變慢;如果反應溫度低於5 〇 °C,將會產生產生副反應。有機溶劑的用量視雜質量而 定。如果有機溶劑的用量為4 -氣甲醯苯曱酸曱g旨重量 的1 0倍以上,則反應速率將下降,並增加製造成本。 在此醯胺化步驟中,當氮的來源為氨水(NH4〇jj) 時,氨水的量係介於5至20莫耳當量間,較佳係介於 7至15莫耳當量間。當氮的來源為氨氣(nh3)時,象氣 量係介於1.5至5莫耳當量間,較佳係介於2至3莫耳 當量間。如果氨水(nioh)及氨氣(NH3)的量係分別低 於5至1·5莫耳當量以下,則反應速率將變慢。如果氨 水(NK^OH)及氨氣(ΝΗ3)的量係分別高於20至5莫耳當 10 200305554 里以上’則不會出現其他額外的欲求效果。此醯胺化步 驟的產物是白色結晶化合物,反應時間約1小時,且反 應產率約98%。 在最後一步驟,以所生成的4-胺甲酿苯甲酸曱酯 來進行霍夫曼反應,藉以生成對-胺基苯甲酸。舉例來 說’霍夫曼反應係藉由讓4 -胺甲醢苯甲酸甲酯與1至1.5 宜 JB1 田 、备置的鹵化驗(例如,NaOCl及NaOBr)及3至15In the second step, methyl 4-chloroformamidinebenzoate produced by the gasification process is amidated to form methyl 4-amineformamate benzoate. This ammonium amination step is preferably performed by reacting methyl 4-gasformamidinebenzoate with ammonia (NHWH) or ammonia (NH3) dissolved in water and / or an organic solvent. In detail, the amidation reaction is preferably performed by adding the 4-gas mesylate sulfonate to ammonia water dropwise, or by adding 4- It is performed by adding trimethylammonium benzoate to ammonia water dropwise, or by supplying ammonia gas to 4-methylformamidine benzoate methyl ester which has been dissolved in an organic solvent. Organic solvents that can be used in this amidation process include various types of organic solvents that can dissolve 4-chloromethyl benzoate methyl vinegar, and preferred examples of such organic solvents include, for example, toluene, ethyl acetate, and A hydrophobic organic solvent such as a mixture thereof. The amount of the organic solvent used is preferably between 0 and 10 times the weight of 4-chloroformamidine benzoate, and more preferably between 0.5 and 8 times the weight of 4-chloroformamidine benzoate. In this ammonium amination step, the 4-gasobenzoic acid methyl ester is formed in the solid phase, so it can be easily separated from various by-product solutions. By-products such as p-galacene and diacetic acid in the reaction vessel are dissolved in an organic solvent, and thus can be separated from 4-pyridenebenzoate. This ammonium amination step can be performed under atmospheric pressure, and the reaction temperature is preferably between i ° C and 50 ° C, and more preferably between 3 ° C and 30 ° C. If the source of nitrogen is ammonia, this amination step is preferably performed at a relatively high temperature ', e.g., at 250 ° C to increase gas activity. If the reaction temperature is lower than 1 C ', the reaction rate will be slower; if the reaction temperature is lower than 50 ° C, side reactions will occur. The amount of organic solvent depends on the amount of impurities. If the amount of the organic solvent used is more than 10 times the weight of 4-g-methanetoluenebenzoate g, the reaction rate will decrease and the manufacturing cost will increase. In this ammonium amination step, when the source of nitrogen is ammonia water (NH4jj), the amount of ammonia water is between 5 and 20 mole equivalents, and preferably between 7 and 15 mole equivalents. When the source of nitrogen is ammonia (nh3), the amount of elephant gas is between 1.5 and 5 mole equivalents, preferably between 2 and 3 mole equivalents. If the amount of ammonia (nioh) and ammonia (NH3) is less than 5 to 1.5 mole equivalents, respectively, the reaction rate will be slowed down. If the amount of ammonia water (NK ^ OH) and ammonia gas (Ν) 3) is higher than 20 to 5 moles 10 200305554 miles or more ’, then there will be no additional desire effect. The product of this amidation step is a white crystalline compound with a reaction time of about 1 hour and a reaction yield of about 98%. In the final step, Huffman reaction is performed with the 4-aminomethyl acetobenzoate produced to form p-aminobenzoic acid. For example, the ‘Huffman reaction’ is based on the combination of methyl 4-aminoformamidine benzoate with 1 to 1.5 JB1 fields, prepared halogenation tests (eg, NaOCl and NaOBr), and 3 to 15

莫耳备量的NaOH溶液反應的方式來進行,或是該霍夫 又反應係藉由將鹵化鹼加入至4 _胺曱醯苯甲酸甲酯之 驗f生4液中的方式來進行。霍夫曼反應的反應溫度介於 〇 C至80 C間’較佳係介於3°C至6(TC間,反應壓力為 大氣壓’且反應時間為約2小時。如果反應物的量低於 斤述fe圍’產率將丁降,且即使反應物的量超出於上述 ^ 也無法提兩產率。如果霍夫曼反應的反應溫度低 於 〇 〇C , ’反應速率將下降,且如果霍夫曼反應的反應溫 度超2 80°c以上,則會產生副反應。A molar amount of NaOH solution was used to perform the reaction, or the Huff reaction was performed by adding a halogenated base to the 4-aminobenzoic acid methyl ester test solution. The reaction temperature of the Huffman reaction is between 0 ° C and 80 ° C, preferably between 3 ° C and 6 ° C, and the reaction pressure is atmospheric pressure, and the reaction time is about 2 hours. If the amount of reactants is lower than The yield rate will be reduced, and even if the amount of reactants exceeds the above, the two yields cannot be improved. If the reaction temperature of the Huffman reaction is lower than 0 ° C, the reaction rate will decrease, and if When the reaction temperature of Huffman reaction exceeds 2 80 ° c, side reactions will occur.

田霍夫曼反應完成後,可以酸性溶液來萃取對-胺 ^ ’較佳係以5 %至丨〇 %的氣化氫溶液·,之後以 一驗將口After the Huffman reaction is completed, the p-amine can be extracted with an acidic solution. It is preferably a 5% to 0% hydrogenated hydrogen solution.

應物的酸驗值中和至4.0左右,較佳係以NaOH 57L /1¾ Γχι 得純、〜的對-胺基笨甲酸。之後,將反應物過濾可 對-胺基苯甲酸。該霍夫曼反應之產率約為90%。 w. 提仏本發明較佳的實施例,但是本發明之範疇 並不偈限於下附實施例。 11 200305554 實施例1The acid value of the reaction product is neutralized to about 4.0, and it is preferable to use NaOH 57L / 1¾ Γχι to obtain pure, ~ p-amino stearic acid. After that, the reaction was filtered to make p-aminobenzoic acid. The Huffman reaction yields about 90%. w. The preferred embodiments of the present invention are mentioned, but the scope of the present invention is not limited to the following embodiments. 11 200305554 Example 1

將75%之4-曱醯苯曱酸曱酯(16.4克)於6〇。(:下熔 融,並加入1.5莫耳當量的氣氣並通氣1〇小時,以獲 得4-氯甲醯苯甲酸曱酯,產率為90%。將19.8克的4-氯甲醯苯甲酸甲酯於60°C下溶於80克的甲苯中,並於 2小時内將所得溶液逐滴加至1 〇〇/〇的氨水中,該氨水中 所含I的重量為4-氣甲醯苯甲酸曱酯重的1〇倍。在此 反應中,反應溫度係維持在5。(:至2(TC間。之後,停止 冷卻反應物溫度,並將溫度提高至室溫。過濾反應物可 得4-胺甲醯苯甲酸甲酯結晶,產率為98%,純度為95%。75% of ethyl 4-benzylbenzoate (16.4 g) was added to 60%. (: Melt down, and add 1.5 molar equivalents of gas and aeration for 10 hours to obtain ethyl 4-chloroformamidine benzoate, the yield is 90%. 19.8 g of 4-chloroformamidine benzoate The ester was dissolved in 80 g of toluene at 60 ° C, and the resulting solution was added dropwise to 100/0 ammonia water within 2 hours. The weight of I contained in the ammonia water was 4-gastoluene Ten times the weight of ethyl formate. In this reaction, the reaction temperature was maintained at 5. (: to 2 (TC). After that, the temperature of the reactant was stopped to cool and the temperature was raised to room temperature. The reaction was filtered to obtain Crystallization of methyl 4-aminoformamylbenzoate with a yield of 98% and a purity of 95%.

1N的氫氧化鈉溶液中包含相對於4-胺曱醯苯甲酸 曱酯重量而言為5莫耳當量之氫氧化鈉,將其冷卻至〇 °C並加入1 7 · 9克之-胺曱醯苯曱酸曱酯。將反應物溫度 維持在(TC至10°C間,並加入10%之NaOCl溶液(其中 包含1·05莫耳當量之NaOCl)30分鐘,使反應持續進行 2小時。之後,將反應物溫度提高至5 0 °C,並維持1小 時。藉著加入NaOH,可將反應物酸鹼值調整至4.0, 同時可使標的化合物沉澱出來。過濾反應物,可得標的 化合物,對-胺基苯曱酸,產率為9 5 %。 2 在此實施例中,係以溶於乙酸乙酯之4 -氯甲醯苯 甲酸曱酯來代替60°C之4-氣甲醯苯甲酸甲酯。所使用 乙酸乙酯的體積為4-氣曱醯苯曱酸曱酯體積之4倍。 12 200305554 除此外,均依據上述實施例 1的方法來製備對-胺基苯 甲酸。醯胺化步驟的產率為9 5 %,且所得醯胺化合物之 純度為9 6 %。 實施例3The 1N sodium hydroxide solution contained 5 mol equivalents of sodium hydroxide relative to the weight of the 4-amine benzoate benzoate, cooled to 0 ° C and added 17.9 grams of amine amine Benzyl benzoate. The temperature of the reactant was maintained at (TC to 10 ° C), and a 10% NaOCl solution (containing 1.05 Molar equivalent of NaOCl) was added for 30 minutes to allow the reaction to continue for 2 hours. After that, the temperature of the reactant was increased To 50 ° C, and maintained for 1 hour. By adding NaOH, the pH value of the reactant can be adjusted to 4.0, while the target compound can be precipitated out. The reactant can be filtered to obtain the target compound, p-aminophenylhydrazone Acid with a yield of 95%. 2 In this example, 4-chloroformamidine benzoate methyl ester dissolved in ethyl acetate was used in place of 60 ° C methyl 4-methaneformylbenzoate. The volume of ethyl acetate used is 4 times the volume of 4-gasoylbenzoic acid ethyl ester. 12 200305554 In addition, the p-aminobenzoic acid was prepared according to the method of Example 1 above. The rate was 95%, and the purity of the obtained amidine compound was 96%. Example 3

將2莫耳當量之無水氨氣加到4-氯曱醢苯甲酸甲 酯之甲苯溶液中約 2小時。曱苯的體積為 4-氣甲醯苯 曱酸甲酯體積之4倍。之後,將曱苯蒸餾掉,並以純水 清洗反應物,過濾後可得 4-胺甲醯苯甲酸甲酯的白色 結晶,產率為96%。除此外,均依據上述實施例1的方 法來製備對-胺基苯曱酸。2 molar equivalents of anhydrous ammonia were added to a toluene solution of methyl 4-chloroacetobenzoate for about 2 hours. The volume of toluene is four times the volume of 4-gastoluene methyl methyl acetate. After that, the toluene was distilled off, and the reaction product was washed with pure water. After filtration, white crystals of methyl 4-aminoformamidinebenzoate were obtained with a yield of 96%. Except this, p-aminophenylarsinic acid was prepared according to the method of Example 1 above.

如上述,本發明提供一新穎之製備對-胺基苯曱酸 之方法。在此方法中所用的 4-甲醯苯甲酸曱酯係為合 成DMT時的主要副產物,其不需經過純化,即可作為 合成對-胺基苯甲酸之原料。4-甲醯苯甲酸曱酯中的雜 質可於製備對-胺基苯甲酸的過程中被移除。本發明新 穎的製備方法係利用4-曱醯苯曱酸曱酯的不對稱性, 且無須使用保護基基團。因此,本發明製備對-胺基苯 甲酸之方法的步驟非常簡單,並可降低製造成本。在本 發明中,也可於步驟間使用其他的純化方法,或是在獲 得標地化合物後再以其他的純化方法加以純化。 本發明已藉由實施例詳述如上,習知技藝者將能了 解本發明方法的其他改良或替換,在不悖離本發明精神 13 200305554 下,仍屬後附申請專利範圍之範_。As described above, the present invention provides a novel method for preparing p-aminophenylarsine. The 4-methylammonium benzoate ethyl ester used in this method is the main by-product when synthesizing DMT, and it can be used as a raw material for the synthesis of p-aminobenzoic acid without purification. The impurities in ethyl 4-formamylbenzoate can be removed during the preparation of p-aminobenzoic acid. The novel preparation method of the present invention utilizes the asymmetry of acenaphthyl 4-phenylbenzoate and does not require the use of a protecting group. Therefore, the method of the present invention for preparing p-aminobenzoic acid is very simple and can reduce the manufacturing cost. In the present invention, other purification methods can also be used between the steps, or the target compound can be purified by other purification methods after obtaining the target compound. The present invention has been described in detail through the examples above. The skilled artisan will be able to understand other improvements or replacements of the method of the present invention, and without departing from the spirit of the present invention 13 200305554, it still belongs to the scope of the appended patent application.

1414

Claims (1)

200305554 拾、申請專利範圍 1. 一種製備對-胺基苯曱酸的方法,其係包含如下之步 驟: 將 4-曱醢苯甲酸曱酯氯化以生成 4-氯曱醯苯甲酸甲 酯; 將 4-氯甲醯苯甲酸甲酯醯胺化以生成 4-胺甲醯苯甲 酸甲酯;200305554 Scope of application and patent application 1. A method for preparing p-aminophenylbenzoic acid, comprising the steps of: chlorinating ethyl 4-benzoate benzoate to form methyl 4-chloroacetobenzoate; Amidation of methyl 4-chloroformamidinebenzoate to form methyl 4-amineformamidinebenzoate; 並以所生成的 4-胺甲醯苯曱酸甲酯於溶液中執行霍 夫曼反應。 2 ·如申請專利範圍第1項所述之方法,其中該氯化步驟 係藉由將 4-甲醯苯曱酸曱酯熔解成液態相,並添加 1 至3莫耳當量之氣氣(Cl2)的方式來進行。 3 ·如申請專利範圍第1項所述之方法,其中該醯胺化步 驟係藉由添加溶解於有機溶劑中之4-氣甲醯苯曱酸甲 酯至氨水中的方式來進行。 · 4·如申請專利範圍第1項所述之方法,其中該醯胺化步 驟係藉由供應氨氣至溶解於有機溶劑中的 4-氣曱醯苯 曱酸曱酯中的方式來進行。 5·如申請專利範圍第1項所述之方法,其中該霍夫曼反 應係藉由添加鹵化鹼至溶於鹼性溶液之4-胺曱醯苯曱 15 200305554 酸曱酯中的方式來進行。 6·如申請專利範圍第3項所述之方法,其中之有機溶劑 係選自由甲苯、乙酸乙酯、及其之混合物所組成之群 組中。Huffman reaction was performed with the generated 4-aminoformamidine benzoate methyl ester in solution. 2. The method as described in item 1 of the scope of the patent application, wherein the chlorination step is performed by melting 4-methylpyrenebenzoate into a liquid phase, and adding 1 to 3 molar equivalents of gas (Cl2 ). 3. The method according to item 1 of the scope of patent application, wherein the amidation step is carried out by adding 4-methylformamidine benzoate methyl ester dissolved in an organic solvent to ammonia water. 4. The method as described in item 1 of the scope of the patent application, wherein the ammonium amination step is performed by supplying ammonia gas into 4-gas ammonium phenylacetate dissolved in an organic solvent. 5. The method as described in item 1 of the scope of patent application, wherein the Huffman reaction is performed by adding a halogenated base to 4-amine benzophenone 15 200305554 acid ester dissolved in an alkaline solution. . 6. The method according to item 3 of the scope of patent application, wherein the organic solvent is selected from the group consisting of toluene, ethyl acetate, and mixtures thereof. 7.如申請專利範圍第4項所述之方法,其中之有機溶劑 係選自由甲苯、乙酸乙酯、及其之混合物所組成之群 組中。7. The method according to item 4 of the scope of patent application, wherein the organic solvent is selected from the group consisting of toluene, ethyl acetate, and mixtures thereof. 16 200305554 陸、(一)、本案指定代表圖為:第_圖 (二)、本代表圖之元件代表符號簡單說明: 柒、本案若有化學式時,請揭示最能顯示發明 特徵的化學式·16 200305554 Lu, (1), the designated representative of the case is: Figure _ (2), the representative symbols of the representative diagram are briefly explained: 柒, if there is a chemical formula in this case, please reveal the chemical formula that best shows the characteristics of the invention ·
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CN100427457C (en) 2008-10-22
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CN1625545A (en) 2005-06-08

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