CN1100765C - Process for preparing tetramethyl pyrazine - Google Patents
Process for preparing tetramethyl pyrazine Download PDFInfo
- Publication number
- CN1100765C CN1100765C CN98124478A CN98124478A CN1100765C CN 1100765 C CN1100765 C CN 1100765C CN 98124478 A CN98124478 A CN 98124478A CN 98124478 A CN98124478 A CN 98124478A CN 1100765 C CN1100765 C CN 1100765C
- Authority
- CN
- China
- Prior art keywords
- tetramethylpyrazine
- preparation
- metal compound
- viii metal
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
本发明提供一种四甲基吡嗪的制备方法,在VIII族金属化合物与有机配体形成的配位催化剂存在下,通过氢气与2,3-丁二酮一肟反应而获得四甲基吡嗪。本发明所涉及催化剂制备简便,反应所需的氢气压力较低,四甲基吡嗪的产率较高。The invention provides a method for preparing tetramethylpyrazine. In the presence of a coordination catalyst formed by a VIII metal compound and an organic ligand, tetramethylpyrazine is obtained by reacting hydrogen with 2,3-butanedione monoxime. Zinc. The catalyst involved in the invention is easy to prepare, the hydrogen pressure required for the reaction is low, and the yield of tetramethylpyrazine is high.
Description
本发明是用2,3-丁二酮一肟为反应物,通过催化加氢制备四甲基吡嗪的方法。The invention uses 2,3-butanedione monoxime as a reactant to prepare tetramethylpyrazine through catalytic hydrogenation.
四甲基吡嗪(英文名称为:tetramethylpryazine,简写为TMP)可以用作香料、食品香味剂、光敏剂、医药和农药的中间体。近年来人们又发现,四甲基吡嗪是中药川芎(ligusticum wallichii franch)的有效成分之一,在临床上用于治疗脑血管供血不足、脑血栓及其它缺血性血管疾病(如冠心病、脉管炎等)已取得了明显的疗效,且几乎无毒副作用。Tetramethylpyrazine (English name: tetramethylpryazine, abbreviated as TMP) can be used as an intermediate for spices, food fragrances, photosensitizers, medicines and pesticides. In recent years, it has been found that tetramethylpyrazine is one of the active ingredients of the traditional Chinese medicine Ligusticum wallichii franch, which is clinically used to treat cerebrovascular insufficiency, cerebral thrombosis and other ischemic vascular diseases (such as coronary heart disease, Vasculitis, etc.) have achieved significant curative effect, and almost no toxic side effects.
已知的通过2,3-丁二酮一肟(英文名称2,3-Butanedione monoxime或Diacetyl monoxime,简写为:DAM)制备四甲基吡嗪的方法主要有两类。一类是用化学试剂还原2,3-丁二酮一肟;另一类是用氢气还原的方法。化学还原的例子之一是赵建华等报道的用Zn粉为还原剂,在NH4Cl、H2O和乙酸溶液中制备TMP的方法(《中草药》,1980,11(3):198)。另外一例是Ciurdaru G.等公开的专利方法(Rom.RO 67,281,1980年),在SnCl2和盐酸存在下,使2,3-丁二酮一肟环化生成二氢四甲基吡嗪,而后再于乙酸溶液中用过氧化氢氧化脱氢制得四甲基吡嗪。这两种方法都需要消耗大量化学试剂(如锌粉、过氧化氢、氢氧化钠等),还涉及到有较强腐蚀性的乙酸介质,所以不能令人满意。第二类例子是较早期的Winans C.F.等报道的在Raney镍催化剂存在下,用10.0-20.0MPa的氢气压力,使丁二酮肟还原制备四甲基吡嗪的方法(J.Am.Chem.Soc.55,4167(1933)),由于合成压力过高,难以在工业上推广应用。There are mainly two known methods for preparing tetramethylpyrazine from 2,3-butanedione monoxime (English name 2,3-Butanedione monoxime or Diacetyl monoxime, abbreviated as: DAM). One is the reduction of 2,3-butanedione-oxime with chemical reagents; the other is the method of reduction with hydrogen. One of the examples of chemical reduction is the method of preparing TMP in NH 4 Cl, H 2 O and acetic acid solution reported by Zhao Jianhua et al. using Zn powder as a reducing agent ("Chinese Herbal Medicine", 1980, 11(3): 198). Another example is the patent method disclosed by Ciurdaru G. et al. (Rom.RO 67,281, 1980), in the presence of SnCl 2 and hydrochloric acid, 2,3-butanedione monoxime is cyclized to generate dihydrotetramethylpyridine oxazine, and then oxidative dehydrogenation with hydrogen peroxide in acetic acid solution to obtain tetramethylpyrazine. These two methods all need to consume a large amount of chemical reagents (as zinc powder, hydrogen peroxide, sodium hydroxide etc.), also relate to the acetic acid medium that has stronger corrosiveness, so can not be satisfactory. The second type of example is the method of preparing tetramethylpyrazine by reduction of dimethylglyoxime under the presence of Raney nickel catalyst reported by earlier Winans CF etc. with a hydrogen pressure of 10.0-20.0MPa (J.Am.Chem. Soc.55, 4167 (1933)), because the synthesis pressure is too high, it is difficult to apply in industry.
本发明的目的是研制出一种能够在较低压力下,直接用氢气与2,3-丁二酮一肟反应,不涉及腐蚀性的反应介质,同时又能够获得较高产率的四甲基吡嗪的催化合成方法。The purpose of the present invention is to develop a kind of can under lower pressure, directly use hydrogen to react with 2,3-butanedione monoxime, do not involve the corrosive reaction medium, can obtain the tetramethylmethanol of higher yield simultaneously again Catalytic synthesis of pyrazines.
经过实验研究,我们发现在某些VIII族金属的配位催化剂存在下,可以使2,3-丁二酮一肟在很低的氢气压力下还原环化,得到较高产率的四甲基吡嗪。After experimental research, we found that in the presence of some coordination catalysts of Group VIII metals, 2,3-butanedione monoxime can be reductively cyclized under very low hydrogen pressure to obtain tetramethylpyridine in higher yields. Zinc.
本发明涉及的主要化学反应为: The main chemical reactions involved in the present invention are:
本发明的方法包括催化剂的组成与制备方法、在适当的温度和氢气压力下,2,3-丁二酮一肟在有机溶剂中与氢气反应。The method of the invention comprises the composition and preparation method of the catalyst, and reacts 2,3-butanedione monoxime with hydrogen in an organic solvent under proper temperature and hydrogen pressure.
催化剂体系包括VIII族金属化合物M和有机配体L两部分。The catalyst system includes two parts of Group VIII metal compound M and organic ligand L.
适合的VIII族金属化合物选自Pd,Co,Fe,Ni,Pt和Ru等的卤化物及其羧酸盐中的一种或两种,优选的金属组分是Pd,Co,Ni和Pt的卤化物。Pd是最优先选择的金属组分。Suitable Group VIII metal compounds are selected from one or both of halides and carboxylates of Pd, Co, Fe, Ni, Pt and Ru, etc., and the preferred metal components are those of Pd, Co, Ni and Pt halide. Pd is the most preferred metal component.
适合的有机配体是含有N,P原子的电子给予基团的有机化合物,通常为三烷基或三芳基胺NR1R2R3,三烷基或三芳基膦PR1R2R3,R1、R2和R3可以相同或不同,表示具有1~12碳原子的烷基或芳基,和式为 的含氮双齿配体。(CH)n和(CH)m表示相同或不相同的碳链,n和m代表碳链中的碳及氢原子个数。最优先选择的配体为三苯基膦和2,2’-联吡啶。Suitable organic ligands are organic compounds containing electron-donating groups of N, P atoms, typically trialkyl or triarylamine NR 1 R 2 R 3 , trialkyl or triaryl phosphine PR 1 R 2 R 3 , R 1 , R 2 and R 3 may be the same or different, and represent an alkyl or aryl group with 1 to 12 carbon atoms, and the formula is nitrogen-containing bidentate ligands. (CH)n and (CH)m represent the same or different carbon chains, and n and m represent the number of carbon and hydrogen atoms in the carbon chain. The most preferred ligands are triphenylphosphine and 2,2'-bipyridine.
反应物2,3-丁二酮一肟(英文名称为:2,3-Butanedione monoxime,又称二乙酰一肟),其分子结构式为: The reactant 2,3-butanedione monoxime (English name is: 2,3-Butanedione monoxime, also known as diacetyl monoxime), its molecular structural formula is:
由2,3-丁二酮一肟与氢气反应制备的四甲基吡嗪(又称为:2,3,5,6-四甲基吡嗪,或川芎嗪),其分子结构式为: Tetramethylpyrazine (also known as: 2,3,5,6-tetramethylpyrazine, or ligustrazine) prepared by the reaction of 2,3-butanedione-oxime and hydrogen, its molecular structural formula is:
本发明中涉及的VIII族金属化合物M与有机配体L的比例M/L=1∶0.5--1∶5(摩尔比)。反应物2,3-丁二酮一肟DAM与VIII族金属化合物M的比例通常为100--1000(摩尔比)。The ratio M/L of the Group VIII metal compound M to the organic ligand L involved in the present invention is 1:0.5--1:5 (molar ratio). The ratio of reactant 2,3-butanedione monooxime DAM to Group VIII metal compound M is usually 100--1000 (molar ratio).
本发明的方法需在适当的液体介质中进行反应。适当的液体介质最好是能够溶解催化剂组分和反应物的有机溶剂。通常可以是脂肪烃、芳香烃、醚、醇、酯类等的其中之一或它们的混合物。优选的液体介质为醇类、环烷烃和芳香烃中的一种或它们的混合物。The method of the present invention needs to carry out the reaction in a suitable liquid medium. A suitable liquid medium is preferably an organic solvent capable of dissolving the catalyst components and reactants. Usually it can be one of aliphatic hydrocarbons, aromatic hydrocarbons, ethers, alcohols, esters, etc. or a mixture of them. The preferred liquid medium is one or a mixture of alcohols, naphthenes and aromatic hydrocarbons.
本发明所涉及的反应温度在30-160℃,氢气压力通常在0.6-5.0MPa。The reaction temperature involved in the present invention is 30-160° C., and the hydrogen pressure is usually 0.6-5.0 MPa.
本发明的具体制备方法是:将VIII族金属化合物、有机配体溶解于有机溶剂中预先配制成催化剂,再与DAM分别加入反应器;或者将VIII族金属化合物、有机配体和反应物DAM一起加入反应器原位生成催化剂;然后充入氢气达到适当的压力,加热到一定温度下进行反应,直到观察氢气压力不再降低为止。一般反应时间在1--30小时。反应结束后,冷却至室温,取出液体进行分析。同时可以用蒸馏分离或通常的提纯方法分离出The specific preparation method of the present invention is: dissolving the Group VIII metal compound and the organic ligand in an organic solvent to prepare a catalyst in advance, and then adding DAM to the reactor separately; or mixing the Group VIII metal compound, the organic ligand and the reactant DAM together The catalyst is added into the reactor to generate the catalyst in situ; then filled with hydrogen to reach an appropriate pressure, and heated to a certain temperature for reaction until it is observed that the hydrogen pressure no longer decreases. The general reaction time is 1--30 hours. After the reaction, it was cooled to room temperature, and the liquid was taken out for analysis. At the same time, it can be separated by distillation or common purification methods
本发明提供的TMP制备方法具有所需氢气压力较低、介质腐蚀性小、催化剂制备方便和四甲基吡嗪的产率高等优点。The TMP preparation method provided by the invention has the advantages of low required hydrogen pressure, low medium corrosion, convenient catalyst preparation, high tetramethylpyrazine yield and the like.
实施例Example
下面通过一些实施例详细说明本发明的具体实施步骤,不应将这些实施例当作本发明范围的限制。The specific implementation steps of the present invention will be described in detail below through some examples, and these examples should not be regarded as limiting the scope of the present invention.
实施例1Example 1
将2.91mg的二氯化钯(PdCl2),6.30mg的三苯基膦(PPh3)分别溶解在1ml乙醇中,然后在室温下搅拌0.5小时制成催化剂溶液。2.91 mg of palladium dichloride (PdCl 2 ) and 6.30 mg of triphenylphosphine (PPh 3 ) were dissolved in 1 ml of ethanol, respectively, and stirred at room temperature for 0.5 hours to prepare catalyst solutions.
将上述催化剂溶液、0.5g的2,3-丁二酮一肟(以下均简写为DAM)加入盛有4ml乙醇的容积为20ml的不锈钢高压釜中,搅拌至混合均匀;充入氢气使压力达到2.4MPa,升温至150℃,开始反应,至5--6小时后,反应体系的压力不再下降,冷却至室温,取出反应液体进行分析,结果表明:DAM的转化率为94.61%,TMP的产率为85.53%。Add the above catalyst solution and 0.5 g of 2,3-butanedione monoxime (hereinafter abbreviated as DAM) into a stainless steel autoclave with a volume of 20 ml filled with 4 ml of ethanol, stir until evenly mixed; fill with hydrogen to make the pressure reach 2.4MPa, heat up to 150°C, start the reaction, after 5--6 hours, the pressure of the reaction system no longer drops, cool to room temperature, take out the reaction liquid for analysis, the results show: the conversion rate of DAM is 94.61%, the conversion rate of TMP is 94.61%. The yield was 85.53%.
实施例2--7Example 2--7
重复实施例1的操作步骤,只改变金属化合物的种类及用量,分别用氯化钴(CoCl2)、氯铂酸H2PtCl4、溴化镍NiBr2、三氯化钌RuCl3、乙酸钴CoOAc、三氯化铁FeCl3代替PdCl2;三苯基膦用量均12.6mg。有关用量及反应结果列入表1。Repeat the operation steps of Example 1, only changing the type and amount of the metal compound, using cobalt chloride (CoCl 2 ), chloroplatinic acid H 2 PtCl 4 , nickel bromide NiBr 2 , ruthenium trichloride RuCl 3 , cobalt acetate CoOAc and iron trichloride FeCl 3 replaced PdCl 2 ; the dosage of triphenylphosphine was 12.6 mg. The relevant dosage and reaction results are listed in Table 1.
实施例8Example 8
将2.12mg的氯化钴(CoCl2),2.91mg的二氯化钯和三苯基膦(PPh3)12.6mg分别溶解于少量乙醇后,混合起来加入盛有4ml乙醇的容积为20ml的不锈钢高压釜中,搅拌至混合均匀;充入氢气使压力达到0.5MPa,升温至100℃,搅拌1小时制成催化剂溶液,然后冷却至室温。Dissolve 2.12 mg of cobalt chloride (CoCl 2 ), 2.91 mg of palladium dichloride and 12.6 mg of triphenylphosphine (PPh 3 ) in a small amount of ethanol, mix them and add 4 ml of ethanol to a 20 ml stainless steel In an autoclave, stir until the mixture is uniform; fill with hydrogen to make the pressure reach 0.5 MPa, heat up to 100°C, stir for 1 hour to prepare a catalyst solution, and then cool to room temperature.
将0.5gDAM和4ml乙醇加入到盛有上述催化剂溶液的不锈钢高压釜中,充氢气至压力达到4.0MPa,升温至120℃,反应约6小时至反应体系的压力不再下降,冷却至室温,取出反应液体进行分析,结果表明:DAM的转化率为96.52%,TMP的产率为94.44%。Add 0.5g DAM and 4ml ethanol into the stainless steel autoclave containing the above catalyst solution, fill it with hydrogen until the pressure reaches 4.0MPa, raise the temperature to 120°C, and react for about 6 hours until the pressure of the reaction system no longer drops, cool to room temperature, and take out The reaction liquid was analyzed, and the results showed that the conversion rate of DAM was 96.52%, and the yield rate of TMP was 94.44%.
实施例9--11Example 9--11
重复实施例8的操作步骤,只是改变三苯基膦的用量,反应结果及三苯基膦的用量列入表2。Repeat the operation step of embodiment 8, just change the consumption of triphenylphosphine, reaction result and the consumption of triphenylphosphine are listed in table 2.
实施例12--16Example 12--16
重复实施例1的操作步骤,只是改变钯化合物组分及其与有机配体的比例,反应结果列入表2。Repeat the operation steps of Example 1, just change the palladium compound component and its ratio with the organic ligand, and the reaction results are listed in Table 2.
实施例19Example 19
将2.12mg的二氯化钴(CoCl2),12.6mg的三苯基膦(PPh3)加入2ml乙醇中,在室温下搅拌0.5小时,制成催化剂溶液。2.12 mg of cobalt dichloride (CoCl 2 ) and 12.6 mg of triphenylphosphine (PPh 3 ) were added to 2 ml of ethanol, and stirred at room temperature for 0.5 hour to prepare a catalyst solution.
将上述催化剂溶液、0.5gDAM和4ml乙醇加入到不锈钢高压釜中,充氢气至压力达到4.0MPa,升温至100℃,反应至反应体系的压力不再下降,冷却至室温,取出反应液体进行分析,结果表明:DAM的转化率为67.06%,TMP的产率为56.65%。Add the above catalyst solution, 0.5g DAM and 4ml ethanol into a stainless steel autoclave, fill with hydrogen until the pressure reaches 4.0MPa, raise the temperature to 100°C, and react until the pressure of the reaction system no longer drops, cool to room temperature, take out the reaction liquid for analysis, The results showed that the conversion rate of DAM was 67.06%, and the yield of TMP was 56.65%.
实施例17,18,20Examples 17, 18, 20
重复实施例19的操作步骤,只是改变反应体系中三苯基膦的用量,反应结果列入表2。Repeat the operation steps of Example 19, just change the amount of triphenylphosphine in the reaction system, and the reaction results are listed in Table 2.
实施例21Example 21
将2.13mg的二氯化镍(NiCl2),12.6mg的三苯基膦(PPh3)分别到加入1ml乙醇中溶解,在室温下搅拌混合0.5小时,制成催化剂溶液。2.13 mg of nickel dichloride (NiCl 2 ) and 12.6 mg of triphenylphosphine (PPh 3 ) were dissolved in 1 ml of ethanol respectively, and stirred and mixed at room temperature for 0.5 hour to prepare a catalyst solution.
将上述催化剂溶液、0.5gDAM和加入到盛有4ml乙醇容积为20ml的不锈钢高压釜中,搅拌混合均匀,充氢气至压力达到4.0MPa,然后在150℃下,反应至反应体系的压力不再下降,冷却至室温,取出反应液体进行分析,结果列入表2。Add the above catalyst solution, 0.5g DAM and 4ml ethanol into a stainless steel autoclave with a volume of 20ml, stir and mix evenly, fill with hydrogen until the pressure reaches 4.0MPa, and then react at 150°C until the pressure of the reaction system no longer drops , cooled to room temperature, and the reaction liquid was taken out for analysis, and the results are listed in Table 2.
实施例22--24Example 22--24
重复实施例21的操作过程,只是改变反应体系中三苯基膦的用量,反应结果列入表2。The operation process of Example 21 was repeated except that the amount of triphenylphosphine in the reaction system was changed, and the reaction results were listed in Table 2.
实施例25--27Example 25--27
按照实施例1的步骤制备PdCl2--PPh3催化剂,合成四甲基吡嗪的方法基本上与实施例1相同,只是改变反应的温度,结果列入表3。The PdCl 2 --PPh 3 catalyst was prepared according to the steps of Example 1. The method for synthesizing tetramethylpyrazine was basically the same as that of Example 1, except that the reaction temperature was changed. The results are listed in Table 3.
实施例28Example 28
将0.58mg的二氯化钯(PdCl2),0.5mg的2,2’-联吡啶(DPY)分别加入1ml乙醇中溶解,在室温下搅拌混合0.5小时,制成催化剂溶液。0.58 mg of palladium dichloride (PdCl 2 ) and 0.5 mg of 2,2'-bipyridine (DPY) were dissolved in 1 ml of ethanol respectively, and stirred and mixed at room temperature for 0.5 hour to prepare a catalyst solution.
将上述催化剂溶液、0.1gDAM和加入到盛有4ml乙醇容积为20ml的不锈钢高压釜中,搅拌混合均匀,充氢气至压力达到0.6MPa,然后在150℃下,反应6小时后,冷却至室温,取出反应液体进行分析,结果列入表4。Add the above catalyst solution, 0.1g DAM and 4ml ethanol into a stainless steel autoclave with a volume of 20ml, stir and mix evenly, fill with hydrogen until the pressure reaches 0.6MPa, then react at 150°C for 6 hours, then cool to room temperature, The reaction liquid was taken out for analysis, and the results are listed in Table 4.
实施例29-34Examples 29-34
重复实施例28的操作过程,只是改变氢气的压力,反应结果列入表4。Repeat the operation process of embodiment 28, just change the pressure of hydrogen, and reaction result is listed in table 4.
表1、不同金属组分的催化剂的反应结果实施例号 金属 金属化合物用量 DAM转化率 TMP产率Table 1, the reaction results of catalysts with different metal components Example number Metal Metal Compound Consumption DAM Conversion Rate TMP Productive Rate
(mg) (%) (%)(mg) (%) (%)
1 PdCl2 2.91 94.61 85.531 PdCl 2 2.91 94.61 85.53
2 CoCl2 2.13 76.47 72.102 CoCl 2 2.13 76.47 72.10
3 H2PtCl4 5.56 76.64 49.203 H 2 PtCl 4 5.56 76.64 49.20
4 NiBr2 3.58 96.25 56.184 NiBr 2 3.58 96.25 56.18
5 RuCl3 3.40 43.69 41.665 RuCl3 3.40 43.69 41.66
6 CoOAc 2.90 31.04 31.046 CoOAc 2.90 31.04 31.04
7 FeCl3 2.31 25.04 13.24比较例 空白 0.00 <1 <17 FeCl 3 2.31 25.04 13.24 Comparative Example Blank 0.00 <1 <1
表2、三苯基膦PPh3/金属M比例对反应结果的影响实施例 金属组分 PPh3/M 反应温度 氢气压力 DAM转化率 TMP产率Table 2, Example of Effect of Triphenylphosphine PPh3/Metal M Ratio on Reaction Results Metal Component PPh 3 /M Reaction Temperature Hydrogen Pressure DAM Conversion Rate TMP Productive Rate
号 (℃) (MPa) (%) (%)No. (℃) (MPa) (%) (%)
8 CoCl2,PdCl2 1.5 120 4.0 96.52 94.448 CoCl 2 , PdCl 2 1.5 120 4.0 96.52 94.44
9 CoCl2,PdCl2 2.0 120 4.0 90.29 73.549 CoCl 2 , PdCl 2 2.0 120 4.0 90.29 73.54
10 CoCl2,PdCl2 3.0 120 4.0 100.0 79.2910 CoCl 2 , PdCl 2 3.0 120 4.0 100.0 79.29
11 CoCl2,PdCl2 5.0 120 4.0 100.0 88.0比较例 PdCl2 0 150 2.4 1.93 0.0811 CoCl 2 , PdCl 2 5.0 120 4.0 100.0 88.0 Comparative example PdCl 2 0 150 2.4 1.93 0.08
12 PdCl2 0.5 150 2.4 78.65 43.6312 PdCl 2 0.5 150 2.4 78.65 43.63
13 PdCl2 1.5 150 2.4 94.61 85.5313 PdCl 2 1.5 150 2.4 94.61 85.53
14 PdOAc 2.0 150 2.4 75.94 52.9814 PdOAc 2.0 150 2.4 75.94 52.98
15 PdOAc 3.0 150 2.4 79.08 73.9815 PdOAc 3.0 150 2.4 79.08 73.98
16 PdCl2 5.0 150 2.4 69.03 59.6116 PdCl 2 5.0 150 2.4 69.03 59.61
17 CoCl2 1.5 100 4.0 14.42 10.5617 CoCl 2 1.5 100 4.0 14.42 10.56
18 CoCl2 2.0 100 4.0 49.83 40.1618 CoCl 2 2.0 100 4.0 49.83 40.16
19 CoCl2 3.0 100 4.0 67.06 56.6519 CoCl 2 3.0 100 4.0 67.06 56.65
20 CoCl2 5.0 100 4.0 44.09 35.1620 CoCl2 5.0 100 4.0 44.09 35.16
21 NiCl2 1.5 150 4.0 38.21 16.2521 NiCl2 1.5 150 4.0 38.21 16.25
22 NiCl2 2.0 150 4.0 26.23 12.7422 NiCl2 2.0 150 4.0 26.23 12.74
23 NiCl2 3.0 150 4.0 96.25 56.1823 NiCl2 3.0 150 4.0 96.25 56.18
24 NiCl2 5.0 150 4.0 73.98 25.5724 NiCl2 5.0 150 4.0 73.98 25.57
表3、温度对PdCl2-PPh3催化剂反应结果的影响实施例号 反应温度(℃) DAM转化率(%) TMP产率(%)25 30 5.96 3.2426 60 14.17 14.1727 120 80.14 51.421 150 94.61 85.53(其他反应条件为:氢气压力:2.4MPa,PdCl2/PPh3=1∶1.5,DAM=0.5g)Table 3, the influence of temperature on the PdCl2-PPh3 catalyst reaction results Example number Reaction temperature (℃) DAM conversion (%) TMP yield (%) 25 30 5.96 3.2426 60 14.17 14.1727 120 80.14 51.421 150 94.61 85.53 (other reaction conditions For: hydrogen pressure: 2.4MPa, PdCl 2 /PPh 3 =1:1.5, DAM=0.5g)
表4、氢气压力对PdCl2-联吡啶(DPY)催化剂体系的反应结果的影响实施例号 氢气压力(MPa) DAM转化率(%) TMP产率(%)比较例 0 <1.0 <1.028 0.6 40.78 39.4729 1.1 97.46 76.9830 1.3 97.22 89.9031 2.0 58.21 54.7432 3.0 100.0 63.8933 4.0 87.28 52.6934 4.6 95.64 49.28Table 4. Effect of hydrogen pressure on the reaction results of PdCl 2 -bipyridine (DPY) catalyst system Example number Hydrogen pressure (MPa) DAM conversion rate (%) TMP yield (%) Comparative example 0 <1.0 <1.028 0.6 40.78 39.4729 1.1 97.46 76.9830 1.3 97.22 89.9031 2.0 58.21 54.7432 3.0 100.0 63.8933 4.0 87.28 52.6934 4.6 95.64 49.28
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98124478A CN1100765C (en) | 1998-11-11 | 1998-11-11 | Process for preparing tetramethyl pyrazine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98124478A CN1100765C (en) | 1998-11-11 | 1998-11-11 | Process for preparing tetramethyl pyrazine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1253134A CN1253134A (en) | 2000-05-17 |
| CN1100765C true CN1100765C (en) | 2003-02-05 |
Family
ID=5228665
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98124478A Expired - Fee Related CN1100765C (en) | 1998-11-11 | 1998-11-11 | Process for preparing tetramethyl pyrazine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1100765C (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296409C (en) * | 2003-10-15 | 2007-01-24 | 北京理工大学 | Ligustrazine polyethleneglycol ester and preparation method thereof |
| CN100556895C (en) * | 2006-10-18 | 2009-11-04 | 张锋 | The preparation method of Ligustrazine |
| CN103664803A (en) * | 2012-09-17 | 2014-03-26 | 王天桃 | Novel synthesis method of 2, 3, 5, 6-tetramethylpyrazine |
| CN104341359B (en) * | 2014-11-11 | 2017-01-11 | 武汉武药制药有限公司 | Preparation method of tetramethyl-pyrazine |
| CN110156701B (en) * | 2019-06-25 | 2020-10-16 | 吴赣药业(苏州)有限公司 | Synthesis method of 2,3,5, 6-tetramethylpyrazine |
-
1998
- 1998-11-11 CN CN98124478A patent/CN1100765C/en not_active Expired - Fee Related
Non-Patent Citations (1)
| Title |
|---|
| 同位素,第5卷第4期 1992-11-01 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1253134A (en) | 2000-05-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Yuwen et al. | Additive-free cobalt-catalyzed hydrogenation of esters to alcohols | |
| JP5507525B2 (en) | Method for producing hydrogenation accelerator, hydrogenation catalyst and alkene compound | |
| CN101045213A (en) | Solid carried ion liquid-nanometer metal particle catalyst, and its preparing method, and application in synthesis of arylamine | |
| CN102177170A (en) | Novel ruthenium carbonyl complex having a tridentate ligand and manufacturing method and usage therefor | |
| JPH11189600A (en) | Ruthenium complex and method for producing alcohol compound using the same as catalyst | |
| CN109174088B (en) | A heterogeneous catalyst for selective hydrogenation of alkynes and its application | |
| Six et al. | Inter-and intramolecular thermal activation of sp3 C− H bonds with ruthenium bisallyl complexes | |
| CN107602357B (en) | A kind of method for preparing menthone | |
| CN105392563A (en) | Water-insoluble ruthenium catalyst composition for use in aqueous hydrogenation reactions | |
| CN1100765C (en) | Process for preparing tetramethyl pyrazine | |
| JP5177339B2 (en) | Metal nanoparticles, catalyst containing the same, and method for hydrogenating alkyne compounds | |
| CN105764611A (en) | Catalyst systems for use in continuous flow reactors and methods of manufacture and use thereof | |
| CN109704944B (en) | Method for preparing menthone from citronellal and catalyst system used in method | |
| CN103145545B (en) | A kind of method preparing hydroxymalonic acid for glycerol catalysis oxidation | |
| CN1926083A (en) | Manufacturing method of optical activity alcohol | |
| CN104492444A (en) | High-dispersion nanometer copper-based catalyst, and preparation method and application thereof | |
| CN110963902A (en) | A kind of method for synthesizing R-citronellal by water-oil two-phase asymmetric hydrogenation and catalyst for the method | |
| CN103764603A (en) | Method of producing olefins via metathesis | |
| EP2482978B1 (en) | Heterogeneous rhodium metal catalysts | |
| CN1226256C (en) | Method for producing adamantol and adamantone | |
| CN109126871A (en) | A kind of formate dehydrogenase catalyst and its application | |
| CN1944395A (en) | Process for preparing P-nitro benzoic acid by bionically catalystically oxidizing P-nitro toluene with oxygen | |
| Scalambra et al. | Photo-generation of H 2 by heterometallic complexes | |
| CN1239451C (en) | Process for preparing chiral desubstituted carbinol with high selectivity | |
| CN116574043A (en) | Preparation method of 2, 5-dimethyl-N-aryl pyrrole |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHEJIANG UNIVERSITY Free format text: FORMER OWNER: ROOM #, YINGYONGHUAXUEZHONGDIANYANJIUSHIYAN, ZHEJIANG PROVINCE Effective date: 20020920 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20020920 Address after: Hangzhou City, Zhejiang province 310027 Ancient Jade Road 20 Applicant after: Zhejiang University Address before: 310028, 34, Tianmu Road, Zhejiang, Hangzhou Applicant before: Key Laboratory of Applied Chemistry, Zhejiang Prov. |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |