CN108178731A - Green synthesis method for preparing AMP-95 by one-pot method - Google Patents

Green synthesis method for preparing AMP-95 by one-pot method Download PDF

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CN108178731A
CN108178731A CN201810052336.0A CN201810052336A CN108178731A CN 108178731 A CN108178731 A CN 108178731A CN 201810052336 A CN201810052336 A CN 201810052336A CN 108178731 A CN108178731 A CN 108178731A
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propanol
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杨海玉
黄春龙
朱红军
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Guangzhou Yintian New Material Co ltd
Nanjing Tech University
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Guangzhou Yintian New Material Co ltd
Nanjing Tech University
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/02Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reactions involving the formation of amino groups from compounds containing hydroxy groups or etherified or esterified hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C201/00Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
    • C07C201/06Preparation of nitro compounds
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C201/00Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
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Abstract

本发明公开了一种一锅法制备AMP‑95的绿色合成方法,包括以下步骤:S1、在醇溶液中,丙酮、双氧水和氨在催化剂的催化作用下生成2‑硝基丙烷;S2、所述S1步骤中反应液不经提纯在碱性条件下直接和甲醛或多聚甲醛反应生成2‑硝基‑2‑甲基‑1‑丙醇;S3、所述S2步骤中反应产物不经提纯直接加氢得到产物2‑氨基‑2‑甲基‑1‑丙醇(AMP‑95),经精馏纯度达到99.5%以上。本发明原料廉价易得,反应步骤简单,对环境污染小,成本低,产率高,产品易提纯,适合工业化生产。The invention discloses a green synthesis method for preparing AMP-95 by a one-pot method, comprising the following steps: S1, in an alcohol solution, acetone, hydrogen peroxide and ammonia are catalyzed by a catalyst to generate 2-nitropropane; S2, the In the S1 step, the reaction solution directly reacts with formaldehyde or paraformaldehyde under alkaline conditions without purification to generate 2-nitro-2-methyl-1-propanol; in S3, the reaction product in the S2 step is not purified The product 2-amino-2-methyl-1-propanol (AMP-95) is obtained by direct hydrogenation, and the purity reaches more than 99.5% through rectification. The invention has cheap and easy-to-obtain raw materials, simple reaction steps, little environmental pollution, low cost, high yield, easy purification of products, and is suitable for industrialized production.

Description

一锅法制备AMP-95的绿色合成方法A Green Synthetic Method for One-Pot Preparation of AMP-95

技术领域technical field

本发明涉及精细化工产品的合成制备技术领域,具体为一种一锅法制备AMP-95的绿色合成方法。The invention relates to the technical field of synthesis and preparation of fine chemical products, in particular to a green synthesis method for preparing AMP-95 by a one-pot method.

背景技术Background technique

2-氨基-2-甲基-1-丙醇简称为AMP-95,为白色结晶或无色粘稠液体,能与水混溶,可溶于乙醇。AMP-95是一种广为人知的多功能添加剂,广泛运用于涂料油墨、金属加工液、个人护理和医药中间体等行业中。AMP-95作为一种伯胺,其高pKa值使得其有着较高的pH值,同时,由于其为有机碱,相对较柔和,与多种乳液均有较好的配伍性,对产品的其它性能影响较小。与其它有机碱例如氨水、三甲胺和三乙胺等相比,AMP-95的稳定性好,不易黄变,同时毒性小,且不易挥发,可减少系统的气味,降低腐蚀和闪锈,属于环保型的调节剂。目前全球前十大涂料企业都在使用AMP-95TM作为pH调节剂和配方优化助剂,AMP-95TM帮助他们提高了产品的性能,同时降低了成本。在中国的涂料市场中,AMP-95TM也是涂料生产厂家的首选,AMP-95TM的市场覆盖率大于80%。国内知名的涂料生产厂家从上个世纪90年代开始使用该产品沿用至今,AMP-95TM的稳定性和优越性赢来客户的一致好评。2-Amino-2-methyl-1-propanol is called AMP-95 for short. It is white crystal or colorless viscous liquid, miscible with water and soluble in ethanol. AMP-95 is a well-known multifunctional additive widely used in industries such as coating ink, metalworking fluid, personal care and pharmaceutical intermediates. As a primary amine, AMP-95 has a higher pH value due to its high pKa value. At the same time, because it is an organic base, it is relatively soft and has good compatibility with various emulsions. The performance impact is minor. Compared with other organic bases such as ammonia, trimethylamine, and triethylamine, AMP-95 has good stability, is not easy to yellow, and has low toxicity and is not volatile. It can reduce the odor of the system, reduce corrosion and flash rust, and belongs to Environmentally friendly conditioner. At present, the top ten coating companies in the world are using AMP-95TM as a pH regulator and formulation optimization aid. AMP-95TM has helped them improve the performance of their products while reducing costs. In China's paint market, AMP-95TM is also the first choice of paint manufacturers, and the market coverage of AMP-95TM is greater than 80%. Well-known domestic paint manufacturers have been using this product since the 1990s, and the stability and superiority of AMP-95TM have won unanimous praise from customers.

现有的2-氨基-2-甲基-1-丙醇的合成方法有很多,美国专利US20110224460以2-硝基丙烷与甲醛溶液发生反应生成2-硝基-2-甲基-1-丙醇,再在金属镍催化剂下进行加氢反应,分离得到2-氨基-2-甲基-1-丙醇。该方法原料成本高,危险性大,不易储存运输,生产设备投资大,产品纯度低等缺点。中国专利CN1810767采用异丙醇与亚硝酸钠、多聚甲醛在0-25℃下发生反应,再经过萃取、洗涤和蒸馏得到2-硝基-2-甲基-1-丙醇,再催化加氢得到产品。该方法合成条件复杂,反应时间长,后处理难度大。中国专利CN1911899公开了一条通过异丁烯的Ritter过程制备2-氨基-2-甲基-1-丙醇的制备方法。该方法反应原料种类多,制备步骤复杂,且收率较低,收率为50-70%。中国专利CN201310152527介绍了以α-氨基异丁酸烷基酯的醇溶液在金属催化剂存在下与氢气发生氢解还原反应,一步得到2-氨基-2-甲基-1-丙醇的方法,该方法原料成本较高,步骤繁琐,对环境污染大,产率低,且产品不易提纯,不适合工业化生产。There are many existing synthesis methods of 2-amino-2-methyl-1-propanol. In US20110224460, 2-nitropropane reacts with formaldehyde solution to generate 2-nitro-2-methyl-1-propanol. Alcohol, and then carry out hydrogenation reaction under the metal nickel catalyst, and separate to obtain 2-amino-2-methyl-1-propanol. The method has the disadvantages of high raw material cost, high risk, difficult storage and transportation, large investment in production equipment, and low product purity. Chinese patent CN1810767 uses isopropanol to react with sodium nitrite and paraformaldehyde at 0-25°C, then extracts, washes and distills to obtain 2-nitro-2-methyl-1-propanol, and then catalyzes Hydrogen gives the product. The synthesis conditions of this method are complex, the reaction time is long, and the post-processing is difficult. Chinese patent CN1911899 discloses a method for preparing 2-amino-2-methyl-1-propanol through the Ritter process of isobutylene. The method has many kinds of reaction raw materials, complicated preparation steps, and low yield, which is 50-70%. Chinese patent CN201310152527 introduces a method for obtaining 2-amino-2-methyl-1-propanol in one step by hydrogenolysis and reduction reaction of an alcohol solution of alkyl α-aminoisobutyrate with hydrogen in the presence of a metal catalyst. The raw material cost of the method is high, the steps are cumbersome, the environmental pollution is large, the yield is low, and the product is difficult to purify, so it is not suitable for industrial production.

发明内容Contents of the invention

(一)解决的技术问题(1) Solved technical problems

针对现有技术的不足,本发明提供了一种一锅法制备AMP-95的绿色合成方法,解决了传统的方法原料成本较高,步骤繁琐,对环境污染大,产率低,且产品不易提纯,不适合工业化生产的问题。Aiming at the deficiencies of the prior art, the present invention provides a green synthesis method for preparing AMP-95 by a one-pot method, which solves the problem that the traditional method has high cost of raw materials, cumbersome steps, great environmental pollution, low yield, and the product is not easy Purification is not suitable for industrial production.

(二)技术方案(2) Technical solution

为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:

一种一锅法制备AMP-95的绿色合成方法,包括以下步骤:A green synthetic method for preparing AMP-95 by a one-pot method, comprising the following steps:

S1、在醇溶液中,丙酮、双氧水和氨在催化剂的催化作用下生成2-硝基丙烷;S1, in the alcohol solution, acetone, hydrogen peroxide and ammonia generate 2-nitropropane under the catalysis of the catalyst;

其中,所述S1步骤中制备2-硝基丙烷所需要的条件为:在一定的温度范围和时间范围下,所述催化剂为多孔骨架金属杂化催化剂,多孔骨架金属杂化催化剂其骨架主要为硅、氧和杂化金属,其中杂化金属为钛、锆、钒和钼的一种或两两组合,硅和杂化金属原子的比为20~100:1,且杂化双金属摩尔比为1:20~1:100;该催化剂的构型为ZSM-5、MCM-41、SBA-15、及其微孔-介孔复合结构和介孔-大孔复合结构之一,其中催化剂的用量为物料总量的0.001~10%;Wherein, the conditions required for preparing 2-nitropropane in the S1 step are: under a certain temperature range and time range, the catalyst is a porous skeleton metal hybrid catalyst, and the skeleton of the porous skeleton metal hybrid catalyst is mainly Silicon, oxygen and hybrid metals, wherein the hybrid metals are one or two combinations of titanium, zirconium, vanadium and molybdenum, the ratio of silicon to hybrid metal atoms is 20-100:1, and the molar ratio of hybrid double metals 1:20~1:100; the configuration of the catalyst is one of ZSM-5, MCM-41, SBA-15, and its micropore-mesoporous composite structure and mesoporous-macropore composite structure. The dosage is 0.001-10% of the total amount of materials;

S2、所述S1步骤中反应液不经提纯在碱性条件下直接和甲醛或多聚甲醛反应生成2-硝基-2-甲基-1-丙醇;S2, the reaction solution in the S1 step is directly reacted with formaldehyde or paraformaldehyde under alkaline conditions without purification to generate 2-nitro-2-methyl-1-propanol;

其中,所述S2步骤中制备2-硝基-2-甲基-1-丙醇所需要的条件为:在一定的温度范围和时间范围下,碱为氢氧化钠、氢氧化钾、氢氧化钙、氢氧化镁、碳酸钠、碳酸钾、碳酸氢钠、碳酸氢钾、二甲胺、三乙胺、二乙胺、吡啶和氨水中的一种或几种,碱的用量为2-硝基丙烷质量的0.001-2;Wherein, the conditions required for the preparation of 2-nitro-2-methyl-1-propanol in the S2 step are: under a certain temperature range and time range, the alkali is sodium hydroxide, potassium hydroxide, hydroxide One or more of calcium, magnesium hydroxide, sodium carbonate, potassium carbonate, sodium bicarbonate, potassium bicarbonate, dimethylamine, triethylamine, diethylamine, pyridine and ammonia water, the amount of alkali is 2-nitrate 0.001-2 of the mass of propane;

S3、所述S2步骤中反应产物不经提纯直接加氢得到产物2-氨基-2-甲基-1-丙醇(AMP-95),经精馏纯度达到99.5%以上;S3, the reaction product in the step S2 is directly hydrogenated without purification to obtain the product 2-amino-2-methyl-1-propanol (AMP-95), and the purity reaches more than 99.5% through rectification;

其中,所述S3步骤中2-硝基-2-甲基-1-丙醇加氢制备AMP-95所需要的条件为:在一定的温度范围、时间范围下和加氢压力范围下,加氢催化剂为钯碳或雷尼镍,加氢催化剂用量为2-硝基-2-甲基-1-丙醇的0.001-30%。Wherein, the conditions required for preparing AMP-95 by hydrogenation of 2-nitro-2-methyl-1-propanol in the S3 step are: under a certain temperature range, time range and hydrogenation pressure range, hydrogenation The hydrogenation catalyst is palladium carbon or Raney nickel, and the amount of hydrogenation catalyst is 0.001-30% of 2-nitro-2-methyl-1-propanol.

优选的,所述S1步骤中,双氧水和丙酮摩尔比为0.1:1~5:1,丙酮和氨摩尔比为1:0.01~1:3,且反应温度范围为20-120℃,且反应时间范围为0.5-5h。Preferably, in the S1 step, the molar ratio of hydrogen peroxide to acetone is 0.1:1 to 5:1, the molar ratio of acetone to ammonia is 1:0.01 to 1:3, and the reaction temperature range is 20-120°C, and the reaction time is The range is 0.5-5h.

优选的,所述S1步骤中,醇溶液为水或甲醇、乙醇、正丁醇、异丁醇、丙醇、异丙醇、叔丁醇、乙二醇和丙二醇之中的一种或几种。Preferably, in the S1 step, the alcohol solution is water or one or more of methanol, ethanol, n-butanol, isobutanol, propanol, isopropanol, tert-butanol, ethylene glycol and propylene glycol.

优选的,所述S2步骤中反应所需要的温度范围为10-120℃,且反应所需要的时间范围为0.5-12h,且甲醛或多聚甲醛与2-硝基丙烷的摩尔比为1:1-5:1。Preferably, the temperature range required for the reaction in the S2 step is 10-120°C, and the time range required for the reaction is 0.5-12h, and the molar ratio of formaldehyde or paraformaldehyde to 2-nitropropane is 1: 1-5:1.

优选的,所述S3步骤中加氢压力范围为0.1-10MPa,反应温度范围为10-120℃,且反应时间范围为0.5-10h。Preferably, in the step S3, the hydrogenation pressure ranges from 0.1-10 MPa, the reaction temperature ranges from 10-120° C., and the reaction time ranges from 0.5-10 h.

(三)有益效果(3) Beneficial effects

本发明提供了一种一锅法制备AMP-95的绿色合成方法,具备以下有益效果:The invention provides a green synthesis method for preparing AMP-95 by a one-pot method, which has the following beneficial effects:

(1)、本发明原料廉价易得,反应步骤简单,对环境污染小,成本低,产率高,产品易提纯,适合工业化生产。(1) The raw materials of the present invention are cheap and easy to obtain, the reaction steps are simple, the environmental pollution is small, the cost is low, the yield is high, the product is easy to purify, and is suitable for industrial production.

具体实施方式Detailed ways

下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are only some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

本发明提供一种技术方案:The invention provides a technical solution:

一种一锅法制备AMP-95的绿色合成方法,包括以下步骤:A green synthetic method for preparing AMP-95 by a one-pot method, comprising the following steps:

S1、在醇溶液中,丙酮、双氧水和氨在催化剂的催化作用下生成2-硝基丙烷;S1, in the alcohol solution, acetone, hydrogen peroxide and ammonia generate 2-nitropropane under the catalysis of the catalyst;

其中,S1步骤中制备2-硝基丙烷所需要的条件为:反应温度范围为20-120℃,且反应时间范围为0.5-5h,催化剂为多孔骨架金属杂化催化剂,多孔骨架金属杂化催化剂其骨架主要为硅、氧和杂化金属,其中杂化金属为钛、锆、钒和钼的一种或两两组合,硅和杂化金属原子的比为20~100:1,且杂化双金属摩尔比为1:20~1:100;该催化剂的构型为ZSM-5、MCM-41、SBA-15、及其微孔-介孔复合结构和介孔-大孔复合结构之一,其中催化剂的用量为物料总量的0.001~10%,双氧水和丙酮摩尔比为0.1:1~5:1,丙酮和氨摩尔比为1:0.01~1:3,醇溶液为水或甲醇、乙醇、正丁醇、异丁醇、丙醇、异丙醇、叔丁醇、乙二醇和丙二醇之中的一种或几种;Among them, the conditions required for the preparation of 2-nitropropane in step S1 are: the reaction temperature range is 20-120°C, and the reaction time range is 0.5-5h, the catalyst is a porous framework metal hybrid catalyst, a porous framework metal hybrid catalyst Its skeleton is mainly silicon, oxygen and hybrid metal, wherein the hybrid metal is one or two combinations of titanium, zirconium, vanadium and molybdenum, the ratio of silicon to hybrid metal atoms is 20-100:1, and the hybrid The bimetallic molar ratio is 1:20~1:100; the configuration of the catalyst is one of ZSM-5, MCM-41, SBA-15, and its microporous-mesoporous composite structure and mesopore-macroporous composite structure , wherein the amount of catalyst used is 0.001-10% of the total amount of materials, the molar ratio of hydrogen peroxide to acetone is 0.1:1-5:1, the molar ratio of acetone to ammonia is 1:0.01-1:3, and the alcohol solution is water or methanol, One or more of ethanol, n-butanol, isobutanol, propanol, isopropanol, tert-butanol, ethylene glycol and propylene glycol;

S2、S1步骤中反应液不经提纯在碱性条件下直接和甲醛或多聚甲醛反应生成2-硝基-2-甲基-1-丙醇;In the steps S2 and S1, the reaction solution directly reacts with formaldehyde or paraformaldehyde under alkaline conditions without purification to generate 2-nitro-2-methyl-1-propanol;

其中,S2步骤中制备2-硝基-2-甲基-1-丙醇所需要的条件为:反应所需要的温度范围为10-120℃,且反应所需要的时间范围为0.5-12h,碱为氢氧化钠、氢氧化钾、氢氧化钙、氢氧化镁、碳酸钠、碳酸钾、碳酸氢钠、碳酸氢钾、二甲胺、三乙胺、二乙胺、吡啶和氨水中的一种或几种,碱的用量为2-硝基丙烷质量的0.001-2,且甲醛或多聚甲醛与2-硝基丙烷的摩尔比为1:1-5:1;Wherein, the conditions required for the preparation of 2-nitro-2-methyl-1-propanol in step S2 are: the temperature range required for the reaction is 10-120°C, and the time range required for the reaction is 0.5-12h, The alkali is one of sodium hydroxide, potassium hydroxide, calcium hydroxide, magnesium hydroxide, sodium carbonate, potassium carbonate, sodium bicarbonate, potassium bicarbonate, dimethylamine, triethylamine, diethylamine, pyridine and ammonia One or several kinds, the amount of alkali is 0.001-2 of the mass of 2-nitropropane, and the molar ratio of formaldehyde or paraformaldehyde to 2-nitropropane is 1:1-5:1;

S3、S2步骤中反应产物不经提纯直接加氢得到产物2-氨基-2-甲基-1-丙醇(AMP-95),经精馏纯度达到99.5%以上;In steps S3 and S2, the reaction product is directly hydrogenated without purification to obtain the product 2-amino-2-methyl-1-propanol (AMP-95), and the purity reaches more than 99.5% through rectification;

其中,S3步骤中2-硝基-2-甲基-1-丙醇加氢制备AMP-95所需要的条件为:加氢压力范围为0.1-10MPa,反应温度范围为10-120℃,且反应时间范围为0.5-10h,加氢催化剂为钯碳或雷尼镍,加氢催化剂用量为2-硝基-2-甲基-1-丙醇的0.001-30%。Wherein, the conditions required for the preparation of AMP-95 by hydrogenation of 2-nitro-2-methyl-1-propanol in step S3 are: the range of hydrogenation pressure is 0.1-10MPa, the range of reaction temperature is 10-120°C, and The reaction time range is 0.5-10h, the hydrogenation catalyst is palladium carbon or Raney nickel, and the hydrogenation catalyst consumption is 0.001-30% of 2-nitro-2-methyl-1-propanol.

且本发明所用的催化剂为专利号为ZL201510866441.4中提及的多孔骨架金属杂化催化剂。And the catalyst used in the present invention is the porous framework metal hybrid catalyst mentioned in the patent No. ZL201510866441.4.

实施例一Embodiment one

将催化剂10g(Ti-V-ZSM-5),丙酮58.08g,氨水20g加入到400ml甲醇中,升温至70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,滴加甲醛(40%水溶液),滴加完以后继续反应3h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)44.6g。Add 10g of catalyst (Ti-V-ZSM-5), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, raise the temperature to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and maintain the temperature at 65- React at 75°C for 1 hour to obtain 2-nitropropane reaction solution; filter, add 5g of sodium hydroxide to the reaction solution, heat up to 35°C, add formaldehyde (40% aqueous solution) dropwise, and continue to react for 3 hours after the dropwise addition to obtain 2-nitropropane -Methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, the reaction temperature is 75°C, the reaction pressure is 3MPa, and the reaction is 4h to obtain 2-methyl-2-amino- The crude product of 1-propanol was rectified to obtain 44.6g of product (AMP-95).

实施例二Embodiment two

将催化剂10g(Zr-V-SBA-15),丙酮58.08g,氨水20g加入到400ml甲醇中,升温至70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应2h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,滴加甲醛(40%水溶液),滴加完以后继续反应3h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)53.4g。Add 10g of catalyst (Zr-V-SBA-15), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, raise the temperature to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and maintain the temperature at 65- React at 75°C for 2 hours to obtain a 2-nitropropane reaction solution; filter, add 5g of sodium hydroxide to the reaction solution, heat up to 35°C, add formaldehyde (40% aqueous solution) dropwise, and continue the reaction for 3 hours after the dropwise addition to obtain 2-nitropropane -Methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, the reaction temperature is 75°C, the reaction pressure is 3MPa, and the reaction is 4h to obtain 2-methyl-2-amino- The crude product of 1-propanol was rectified to obtain 53.4g of product (AMP-95).

实施例三Embodiment three

将催化剂10g(Zr-Mo-MCM-41),丙酮58.08g,氨水20g加入到400ml甲醇中,升温至70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,滴加甲醛(40%水溶液),滴加完以后继续反应3h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)50.9g。Add 10g of catalyst (Zr-Mo-MCM-41), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, raise the temperature to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and maintain the temperature at 65- React at 75°C for 1 hour to obtain 2-nitropropane reaction solution; filter, add 5g of sodium hydroxide to the reaction solution, heat up to 35°C, add formaldehyde (40% aqueous solution) dropwise, and continue to react for 3 hours after the dropwise addition to obtain 2-nitropropane -Methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, the reaction temperature is 75°C, the reaction pressure is 3MPa, and the reaction is 4h to obtain 2-methyl-2-amino- The crude product of 1-propanol was rectified to obtain 50.9 g of the product (AMP-95).

实施例四Embodiment four

将催化剂10g(钛锆掺杂介孔-大孔复合催化剂),丙酮58.08g,氨水20g加入到400ml甲醇中,升温至70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,滴加甲醛(40%水溶液),滴加完以后继续反应3h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)57.5g。Add 10g of catalyst (titanium-zirconium-doped mesoporous-macroporous composite catalyst), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, heat up to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and keep The temperature is 65-75°C, react for 1h to obtain 2-nitropropane reaction liquid; filter, add 5g sodium hydroxide to the reaction liquid, raise the temperature to 35°C, add formaldehyde (40% aqueous solution) dropwise, and continue the reaction after the dropwise addition 3h, to obtain 2-methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, reaction temperature 75 ° C, reaction pressure 3MPa, reaction 4h, 2-methyl- The crude product of 2-amino-1-propanol was rectified to obtain 57.5 g of the product (AMP-95).

实施例五Embodiment five

将催化剂10g(钛锆掺杂介孔-大孔复合催化剂),丙酮58.08g,氨水20g加入到400ml甲醇中,升温至70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,分批加入多聚甲醛20g,继续反应3h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)55.9g。Add 10g of catalyst (titanium-zirconium-doped mesoporous-macroporous composite catalyst), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, heat up to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and keep The temperature was 65-75°C, reacted for 1h, and obtained 2-nitropropane reaction liquid; filtered, added 5g of sodium hydroxide to the reaction liquid, raised the temperature to 35°C, added 20g of paraformaldehyde in batches, continued the reaction for 3h, and obtained 2- Methyl-2-nitro-propanol reaction solution; put the reaction solution into an autoclave, add 14g of Raney nickel, reaction temperature 75°C, reaction pressure 3MPa, reaction for 4h to obtain 2-methyl-2-amino-1 - propanol crude product, rectification obtains product (AMP-95) 55.9g.

实施例六Embodiment six

将催化剂10g(钛锆掺杂介孔-大孔复合催化剂),丙酮58.08g,氨水10g加入到400ml甲醇中,升温至70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,分批加入多聚甲醛20g,继续反应3h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)40.6g。Add 10g of catalyst (titanium-zirconium-doped mesoporous-macroporous composite catalyst), 58.08g of acetone, and 10g of ammonia water into 400ml of methanol, heat up to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and keep The temperature was 65-75°C, reacted for 1h, and obtained 2-nitropropane reaction liquid; filtered, added 5g of sodium hydroxide to the reaction liquid, raised the temperature to 35°C, added 20g of paraformaldehyde in batches, continued the reaction for 3h, and obtained 2- Methyl-2-nitro-propanol reaction solution; put the reaction solution into an autoclave, add 14g of Raney nickel, reaction temperature 75°C, reaction pressure 3MPa, reaction for 4h to obtain 2-methyl-2-amino-1 - propanol crude product, rectification obtains product (AMP-95) 40.6g.

实施例七Embodiment seven

将催化剂10g(钛锆掺杂介孔-大孔复合催化剂),丙酮58.08g,氨水20g加入到400ml甲醇中,升温50℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在50-60℃,反应2h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,分批加入多聚甲醛20g,滴加完以后继续反应4h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)50.1g。Add 10g of catalyst (titanium-zirconium-doped mesoporous-macroporous composite catalyst), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, raise the temperature to 50°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and maintain the temperature after the dropwise addition React at 50-60°C for 2 hours to obtain 2-nitropropane reaction solution; filter, add 5g of sodium hydroxide to the reaction solution, raise the temperature to 35°C, add 20g of paraformaldehyde in batches, continue the reaction for 4h after the dropwise addition, Obtain 2-methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, the reaction temperature is 75°C, the reaction pressure is 3MPa, and the reaction is 4h to obtain 2-methyl-2- The crude product of amino-1-propanol was rectified to obtain 50.1 g of the product (AMP-95).

实施例八Embodiment Eight

将催化剂20g(钛锆掺杂介孔-大孔复合催化剂),丙酮58.08g,氨水20g加入到400ml甲醇中,升温70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入5g氢氧化钠,升温至35℃,分批加入多聚甲醛20g,滴加完以后继续反应4h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)59.1g。Add 20g of catalyst (titanium-zirconium-doped mesoporous-macroporous composite catalyst), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, raise the temperature to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and maintain the temperature after the dropwise addition React at 65-75°C for 1 hour to obtain 2-nitropropane reaction solution; filter, add 5g of sodium hydroxide to the reaction solution, raise the temperature to 35°C, add 20g of paraformaldehyde in batches, continue the reaction for 4 hours after the dropwise addition, Obtain 2-methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, the reaction temperature is 75°C, the reaction pressure is 3MPa, and the reaction is 4h to obtain 2-methyl-2- The crude product of amino-1-propanol was rectified to obtain 59.1 g of the product (AMP-95).

实施例九Embodiment nine

将催化剂20g(钛锆掺杂介孔-大孔复合催化剂),丙酮58.08g,氨20g加入到400ml甲醇中,升温70℃,缓慢滴加双氧水(35%)226.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入10g氢氧化钠,升温至55℃,分批加入多聚甲醛20g,滴加完以后继续反应2h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)53.6g。Add 20g of catalyst (titanium-zirconium-doped mesoporous-macroporous composite catalyst), 58.08g of acetone, and 20g of ammonia into 400ml of methanol, raise the temperature to 70°C, slowly add 226.7g of hydrogen peroxide (35%) dropwise, and maintain the temperature after the dropwise addition is completed React at 65-75°C for 1 hour to obtain 2-nitropropane reaction solution; filter, add 10g of sodium hydroxide to the reaction solution, raise the temperature to 55°C, add 20g of paraformaldehyde in batches, continue the reaction for 2 hours after the dropwise addition, Obtain 2-methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, the reaction temperature is 75°C, the reaction pressure is 3MPa, and the reaction is 4h to obtain 2-methyl-2- The crude product of amino-1-propanol was rectified to obtain 53.6g of product (AMP-95).

实施例十Embodiment ten

将催化剂20g(钛锆掺杂介孔-大孔复合催化剂),丙酮58.08g,氨水20g加入到400ml甲醇中,升温70℃,缓慢滴加双氧水(35%)326.7g,滴加完毕后维持温度在65-75℃,反应1h,得到2-硝基丙烷反应液;过滤,向反应液加入10g氢氧化钠,升温至55℃,分批加入多聚甲醛20g,滴加完以后继续反应2h,得到2-甲基-2-硝基-丙醇反应液;将反应液加入高压釜中,加入雷尼镍14g,反应温度75℃,反应压力3MPa,反应4h,得到2-甲基-2-氨基-1-丙醇粗品,精馏得到产品(AMP-95)54.9g。Add 20g of catalyst (titanium-zirconium-doped mesoporous-macroporous composite catalyst), 58.08g of acetone, and 20g of ammonia water into 400ml of methanol, raise the temperature to 70°C, slowly add 326.7g of hydrogen peroxide (35%) dropwise, and maintain the temperature after the dropwise addition React at 65-75°C for 1 hour to obtain 2-nitropropane reaction solution; filter, add 10g of sodium hydroxide to the reaction solution, raise the temperature to 55°C, add 20g of paraformaldehyde in batches, continue the reaction for 2 hours after the dropwise addition, Obtain 2-methyl-2-nitro-propanol reaction solution; put the reaction solution into the autoclave, add 14g of Raney nickel, the reaction temperature is 75°C, the reaction pressure is 3MPa, and the reaction is 4h to obtain 2-methyl-2- The crude product of amino-1-propanol was rectified to obtain 54.9 g of the product (AMP-95).

综上可得,本发明原料廉价易得,反应步骤简单,对环境污染小,成本低,产率高,产品易提纯,适合工业化生产。In summary, the present invention has cheap and easy-to-obtain raw materials, simple reaction steps, less environmental pollution, low cost, high yield, easy purification of the product, and is suitable for industrial production.

尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although the embodiments of the present invention have been shown and described, those skilled in the art can understand that various changes, modifications and substitutions can be made to these embodiments without departing from the principle and spirit of the present invention. and modifications, the scope of the invention is defined by the appended claims and their equivalents.

Claims (5)

1. a kind of one kettle way prepares the green synthesis method of AMP-95, which is characterized in that includes the following steps:
S1, in alcoholic solution, acetone, hydrogen peroxide and ammonia generate 2- nitropropanes under the catalytic action of catalyst;
Wherein, the required condition of 2- nitropropanes is prepared in the S1 steps is:In certain temperature range and time range Under, the catalyst is stephanoporate framework metal hybrid catalyst, its skeleton of stephanoporate framework metal hybrid catalyst is mainly silicon, oxygen And hybridized metal, wherein hybridized metal be titanium, zirconium, vanadium and molybdenum one kind or combination of two, the ratio of silicon and hybridized metal atom is 20~100:1, and hydridization bimetallic molar ratio is 1:20~1:100;The catalyst is configured as ZSM-5, MCM-41, SBA- 15 and its one of micropore-mesopore composite construction and mesopore-macropore composite construction, the wherein dosage of catalyst is material total amount 0.001~10%;
The not purified direct and formaldehyde under alkaline condition of reaction solution or polyformaldehyde reaction generation 2- nitre in S2, the S1 steps Base -2- methyl-1s-propyl alcohol;
Wherein, 2- nitros -2- methyl-1s-required condition of propyl alcohol is prepared in the S2 steps is:In certain temperature range Under time range, alkali for sodium hydroxide, potassium hydroxide, calcium hydroxide, magnesium hydroxide, sodium carbonate, potassium carbonate, sodium bicarbonate, One or more of saleratus, dimethylamine, triethylamine, diethylamine, pyridine and ammonium hydroxide, the dosage of alkali is 2- nitropropane matter The 0.001-2 of amount;
The not purified direct hydrogenation of reaction product obtains product 2-amino-2-methyl-1-propanol (AMP- in S3, the S2 steps 95), reach more than 99.5% through rectifying purity;
Wherein, 2- nitros -2- methyl-1s-propyl alcohol Hydrogenation is for the required conditions of AMP-95 in the S3 steps:Certain Temperature range, under time range and under hydrogenation pressure range, hydrogenation catalyst is palladium carbon or Raney's nickel, hydrogenation catalyst dosage 0.001-30% for 2- nitros -2- methyl-1s-propyl alcohol.
2. one kettle way according to claim 1 prepares the green synthesis method of AMP-95, it is characterised in that:The S1 steps In, hydrogen peroxide and acetone molar ratio are 0.1:1~5:1, acetone and ammonia molar ratio are 1:0.01~1:3, and range of reaction temperature It it is 20-120 DEG C, and reaction time range is 0.5-5h.
3. a kind of one kettle way according to claim 1 prepares the green synthesis method of AMP-95, it is characterised in that:The S1 In step, alcoholic solution is water or methanol, ethyl alcohol, n-butanol, isobutanol, propyl alcohol, isopropanol, the tert-butyl alcohol, ethylene glycol and propylene glycol One or more of.
4. one kettle way according to claim 1 prepares the green synthesis method of AMP-95, it is characterised in that:The S2 steps The middle required temperature range of reaction is 10-120 DEG C, and reacts required time range for 0.5-12h, and formaldehyde or poly The molar ratio of formaldehyde and 2- nitropropanes is 1:1-5:1.
5. one kettle way according to claim 1 prepares the green synthesis method of AMP-95, it is characterised in that:The S3 steps Middle hydrogenation pressure ranging from 0.1-10MPa, range of reaction temperature are 10-120 DEG C, and reaction time range is 0.5-10h.
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Application publication date: 20180619