CN1962647A - Preparation process of intermediate 2-cyanpyrazine of pyrazinamide drug - Google Patents
Preparation process of intermediate 2-cyanpyrazine of pyrazinamide drug Download PDFInfo
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- CN1962647A CN1962647A CN 200610154723 CN200610154723A CN1962647A CN 1962647 A CN1962647 A CN 1962647A CN 200610154723 CN200610154723 CN 200610154723 CN 200610154723 A CN200610154723 A CN 200610154723A CN 1962647 A CN1962647 A CN 1962647A
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- pyrazine
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- alkali metal
- bromopyrazine
- bromo
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- PMSVVUSIPKHUMT-UHFFFAOYSA-N cyanopyrazine Chemical compound N#CC1=CN=CC=N1 PMSVVUSIPKHUMT-UHFFFAOYSA-N 0.000 title claims abstract description 29
- IPEHBUMCGVEMRF-UHFFFAOYSA-N pyrazinecarboxamide Chemical compound NC(=O)C1=CN=CC=N1 IPEHBUMCGVEMRF-UHFFFAOYSA-N 0.000 title claims abstract description 11
- 229940079593 drug Drugs 0.000 title abstract description 6
- 239000003814 drug Substances 0.000 title abstract description 6
- 229960005206 pyrazinamide Drugs 0.000 title abstract description 6
- 238000002360 preparation method Methods 0.000 title description 4
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims abstract description 36
- WGFCNCNTGOFBBF-UHFFFAOYSA-N 2-bromopyrazine Chemical compound BrC1=CN=CC=N1 WGFCNCNTGOFBBF-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000003054 catalyst Substances 0.000 claims abstract description 27
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 18
- 229910052763 palladium Inorganic materials 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 239000000706 filtrate Substances 0.000 claims abstract description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 9
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000007810 chemical reaction solvent Substances 0.000 claims abstract description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 239000012450 pharmaceutical intermediate Substances 0.000 claims description 6
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 6
- XOGGUFAVLNCTRS-UHFFFAOYSA-N tetrapotassium;iron(2+);hexacyanide Chemical compound [K+].[K+].[K+].[K+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] XOGGUFAVLNCTRS-UHFFFAOYSA-N 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 4
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 4
- 235000017550 sodium carbonate Nutrition 0.000 claims description 4
- GTSHREYGKSITGK-UHFFFAOYSA-N sodium ferrocyanide Chemical group [Na+].[Na+].[Na+].[Na+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] GTSHREYGKSITGK-UHFFFAOYSA-N 0.000 claims description 4
- 235000012247 sodium ferrocyanide Nutrition 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 3
- 235000015320 potassium carbonate Nutrition 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims 4
- 239000002253 acid Substances 0.000 claims 1
- 239000003513 alkali Substances 0.000 claims 1
- 230000006837 decompression Effects 0.000 claims 1
- WMKGGPCROCCUDY-PHEQNACWSA-N dibenzylideneacetone Chemical compound C=1C=CC=CC=1\C=C\C(=O)\C=C\C1=CC=CC=C1 WMKGGPCROCCUDY-PHEQNACWSA-N 0.000 claims 1
- 238000005194 fractionation Methods 0.000 claims 1
- 229910052783 alkali metal Inorganic materials 0.000 abstract description 12
- 150000001340 alkali metals Chemical class 0.000 abstract description 12
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 abstract description 8
- 229910000288 alkali metal carbonate Inorganic materials 0.000 abstract description 8
- 150000008041 alkali metal carbonates Chemical class 0.000 abstract description 8
- 239000002585 base Substances 0.000 abstract description 3
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 2
- 150000001875 compounds Chemical class 0.000 abstract description 2
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 2
- 231100000252 nontoxic Toxicity 0.000 abstract description 2
- 230000003000 nontoxic effect Effects 0.000 abstract description 2
- 238000010189 synthetic method Methods 0.000 abstract description 2
- CAWHJQAVHZEVTJ-UHFFFAOYSA-N methylpyrazine Chemical compound CC1=CN=CC=N1 CAWHJQAVHZEVTJ-UHFFFAOYSA-N 0.000 description 8
- 239000007983 Tris buffer Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- YJVFFLUZDVXJQI-UHFFFAOYSA-L palladium(ii) acetate Chemical group [Pd+2].CC([O-])=O.CC([O-])=O YJVFFLUZDVXJQI-UHFFFAOYSA-L 0.000 description 4
- 239000000276 potassium ferrocyanide Substances 0.000 description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000000543 intermediate Substances 0.000 description 3
- 239000000264 sodium ferrocyanide Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- LCTONWCANYUPML-UHFFFAOYSA-M Pyruvate Chemical compound CC(=O)C([O-])=O LCTONWCANYUPML-UHFFFAOYSA-M 0.000 description 2
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 238000012805 post-processing Methods 0.000 description 2
- 229910000027 potassium carbonate Inorganic materials 0.000 description 2
- 235000011181 potassium carbonates Nutrition 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 1
- 239000011609 ammonium molybdate Substances 0.000 description 1
- 235000018660 ammonium molybdate Nutrition 0.000 description 1
- 229940010552 ammonium molybdate Drugs 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- UNTBPXHCXVWYOI-UHFFFAOYSA-O azanium;oxido(dioxo)vanadium Chemical compound [NH4+].[O-][V](=O)=O UNTBPXHCXVWYOI-UHFFFAOYSA-O 0.000 description 1
- 229910052797 bismuth Inorganic materials 0.000 description 1
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000003426 co-catalyst Substances 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 235000011182 sodium carbonates Nutrition 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 201000008827 tuberculosis Diseases 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
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- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
本发明公开了一种吡嗪酰胺类药物中间体2-氰基吡嗪的生产工艺。它是以N,N-二甲基乙酰胺为反应溶剂,以钯配合物为催化剂,以碱金属碳酸盐作碱,2-溴吡嗪和碱金属亚铁氰化物在氮气保护下在100~150℃反应1~6小时,随后过滤,滤液减压分馏得到2-氰基吡嗪,2-溴吡嗪和碱金属亚铁氰化物的摩尔当量比例为1∶0.15~0.3;催化剂钯配合物的用量为2-溴吡嗪的0.1~5%摩尔当量;碱金属碳酸盐用量为2-溴吡嗪的0.5~2摩尔当量。本发明与已有的合成方法相比,具有以下优点:1)反应条件安全温和,产率高;2)反应流程短;3)使用廉价的、无毒的碱金属亚铁氰化物作氰化试剂;4)投料和后处理都非常简单,污染小,易于实现工业化大生产。The invention discloses a production process of 2-cyanopyrazine, an intermediate of pyrazinamide drugs. It uses N,N-dimethylacetamide as reaction solvent, palladium complex as catalyst, alkali metal carbonate as base, 2-bromopyrazine and alkali metal ferrocyanide under nitrogen protection at 100 React at ~150°C for 1-6 hours, then filter, and fractionate the filtrate under reduced pressure to obtain 2-cyanopyrazine, the molar equivalent ratio of 2-bromopyrazine and alkali metal ferrocyanide is 1:0.15-0.3; catalyst palladium complex The dosage of the compound is 0.1-5% molar equivalent of 2-bromopyrazine; the dosage of alkali metal carbonate is 0.5-2 molar equivalent of 2-bromopyrazine. Compared with the existing synthetic method, the present invention has the following advantages: 1) the reaction conditions are safe and mild, and the yield is high; 2) the reaction process is short; 3) the cyanide is made of cheap and non-toxic alkali metal ferrocyanide Reagent; 4) Feeding and post-treatment are very simple, with little pollution, and easy to realize industrialized large-scale production.
Description
技术领域technical field
本发明涉及医药中间体制备方法,尤其涉及一种吡嗪酰胺类药物中间体2-氰基吡嗪的生产工艺。The invention relates to a preparation method of a pharmaceutical intermediate, in particular to a production process of a pyrazinamide drug intermediate 2-cyanopyrazine.
背景技术Background technique
2-氰基吡嗪生产治疗结核病药物吡嗪酰胺的重要原料。因此如何高效地合成2-氰基吡嗪受到人们的巨大关注。2-氰基吡嗪的合成已有一些文献报道,比如文献《精细化工》报道了特殊催化剂催化2-甲基吡嗪氨氧化制2-氰基吡嗪的研究。文献Applied Catalsis,1986,20:219-222报道先将乙二胺与丙二醇在催化剂作用下环合脱水脱氢为2-甲基吡嗪,再高温高压催化氨氧化为2一氰基吡嗪。文献CN1398855报道了通过采用以2-甲基吡嗪、氨和氧为原料,在反应温度为300~500℃,以表压计反应压力为-0.05~0.05MPa条件下,原料通过以钒、铬催化体系以及非强制性添加磷及选自碱金属或碱土金属组成的流化床催化剂床层的技术方案用于2-氰基吡嗪的工业生产中。文献CN1408711报道了一种2-甲基吡嗪合成2-氰基吡嗪使用的催化剂,该催化剂采用偏钒酸氨、五氧化二钒,钼酸铵、磷酸经浸渍制备体系的负载型催化剂。文献CN1429820报道了一种氨氧化法制备2-氰基吡嗪的方法及专用催化剂,它是以钒、钛为主催化剂,磷、铁、镍、钴、铋、锰、铬、钼、铜、锌、锡、硼、钾、锂、镁等为助催化剂的多组分催化剂。上述这些合成工艺催化剂制备复杂,反应流程周期时间长,条件苛刻,或有不少实验过程涉及高温高压条件、低产率、后处理复杂等种种问题。因而,在温和的条件下,高效的解决2-氰基吡嗪的合成工艺是非常重要和迫切的。2-cyanopyrazine is an important raw material for the production of pyrazinamide, a drug for treating tuberculosis. Therefore, how to efficiently synthesize 2-cyanopyrazines has attracted great attention. The synthesis of 2-cyanopyrazine has been reported in some literatures. For example, the literature "Fine Chemical Industry" reported the research on the preparation of 2-cyanopyrazine by ammoxidation of 2-methylpyrazine with a special catalyst. The literature Applied Catalsis, 1986, 20: 219-222 reported that ethylenediamine and propylene glycol were dehydrated and dehydrogenated into 2-methylpyrazine under the action of a catalyst, and then catalyzed by high temperature and high pressure for ammoxidation to 2-cyanopyrazine. The document CN1398855 reports that by using 2-methylpyrazine, ammonia and oxygen as raw materials, the reaction temperature is 300-500 ° C, and the reaction pressure is -0.05-0.05 MPa in terms of gauge pressure. The catalytic system and the technical scheme of optional addition of phosphorus and a fluidized bed catalyst bed composed of alkali metals or alkaline earth metals are used in the industrial production of 2-cyanopyrazine. Document CN1408711 reports a catalyst used for synthesizing 2-cyanopyrazine from 2-methylpyrazine. The catalyst uses ammonium metavanadate, vanadium pentoxide, ammonium molybdate, and phosphoric acid to prepare a supported catalyst for the system by impregnation. Document CN1429820 has reported a method for preparing 2-cyanopyrazine by ammoxidation and a special catalyst. It is based on vanadium and titanium as the main catalyst, phosphorus, iron, nickel, cobalt, bismuth, manganese, chromium, molybdenum, copper, Zinc, tin, boron, potassium, lithium, magnesium, etc. are multi-component catalysts as co-catalysts. The preparation of catalysts in the above-mentioned synthesis processes is complex, the reaction process cycle time is long, and the conditions are harsh, or many experimental processes involve high temperature and high pressure conditions, low yield, and complicated post-processing. Therefore, under mild conditions, it is very important and urgent to efficiently solve the synthesis process of 2-cyanopyrazine.
发明内容Contents of the invention
本发明的目的是提供一种吡嗪酰胺类药物中间体2-氰基吡嗪的生产工艺。The object of the present invention is to provide a kind of production technology of pyrazinamide drug intermediate 2-cyanopyrazine.
它是以N,N-二甲基乙酰胺为反应溶剂,以钯配合物为催化剂,以碱金属碳酸盐作碱,2-溴吡嗪和碱金属亚铁氰化物在氮气保护下在100~150℃反应1~6小时,随后过滤,滤液减压分馏得到2-氰基吡嗪,2-溴吡嗪和碱金属亚铁氰化物的摩尔当量比例为1∶0.15~0.3;催化剂钯配合物的用量为2-溴吡嗪的0.1~5%摩尔当量;碱金属碳酸盐用量为2-溴吡嗪的0.5~2摩尔当量,反应式为:It uses N,N-dimethylacetamide as reaction solvent, palladium complex as catalyst, alkali metal carbonate as base, 2-bromopyrazine and alkali metal ferrocyanide under nitrogen protection at 100 React at ~150°C for 1-6 hours, then filter, and fractionate the filtrate under reduced pressure to obtain 2-cyanopyrazine, the molar equivalent ratio of 2-bromopyrazine and alkali metal ferrocyanide is 1:0.15-0.3; catalyst palladium complex The consumption of compound is 0.1~5% molar equivalent of 2-bromopyrazine; The consumption of alkali metal carbonate is 0.5~2 molar equivalent of 2-bromopyrazine, and reaction formula is:
所述的催化剂钯配合物为醋酸钯或双(二亚苄基丙酮酸)钯;碱金属亚铁氰化物是亚铁氰化钠或亚铁氰化钾;碱金属碳酸盐是碳酸钠或碳酸钾。反应时间优选为1~5小时。反应温度优选为100~140℃。2-溴吡嗪和碱金属亚铁氰化物的摩尔当量比例优选为1∶0.15~0.25;催化剂钯配合物的用量为2-溴吡嗪的0.1~4%摩尔当量;碱金属碳酸盐的用量优选为2-溴吡嗪的1~2摩尔当量。Described catalyst palladium complex is palladium acetate or two (dibenzylidene aceruvate) palladium; Alkali metal ferrocyanide is sodium ferrocyanide or potassium ferrocyanide; Alkali metal carbonate is sodium carbonate or potassium carbonate. The reaction time is preferably 1 to 5 hours. The reaction temperature is preferably 100 to 140°C. The molar equivalent ratio of 2-bromopyrazine and alkali metal ferrocyanide is preferably 1: 0.15~0.25; The consumption of catalyst palladium complex is 0.1~4% molar equivalent of 2-bromopyrazine; The amount used is preferably 1 to 2 molar equivalents of 2-bromopyrazine.
本发明与已有的合成方法相比,具有以下优点:Compared with existing synthetic methods, the present invention has the following advantages:
1)反应条件安全温和,产率高;1) The reaction conditions are safe and mild, and the yield is high;
2)反应流程短;2) The reaction process is short;
3)使用廉价的、无毒的碱金属亚铁氰化物作氰化试剂;3) Use cheap, non-toxic alkali metal ferrocyanide as cyanide reagent;
4)投料和后处理都非常简单,污染小,易于实现工业化大生产。4) The feeding and post-processing are very simple, the pollution is small, and it is easy to realize industrialized large-scale production.
具体实施方式Detailed ways
2-氰基吡嗪的分子式为:The molecular formula of 2-cyanopyrazine is:
吡嗪酰胺类药物中间体2-氰基吡嗪的生产工艺的具体反应步骤如下:The concrete reaction steps of the production technology of pyrazinamide drug intermediate 2-cyanopyrazine are as follows:
以N,N-二甲基乙酰胺为反应溶剂,以钯配合物为催化剂,以碱金属碳酸盐作碱,2-溴吡嗪和碱金属亚铁氰化物在氮气保护下在100~150℃反应1~6小时,随后过滤,滤液减压分馏得到高产率、高纯度的2-氰基吡嗪。其中2-溴吡嗪和碱金属亚铁氰化物的摩尔当量比例为1∶0.15~0.3;催化剂钯配合物的用量为2-溴吡嗪的0.1~5%摩尔当量;碱金属碳酸盐用量为2-溴吡嗪的0.5~2摩尔当量。推荐反应时间为1~5小时;推荐反应温度为100~140℃; 推荐2-溴吡嗪和碱金属亚铁氰化物的摩尔当量比例为1∶0.15~0.3;推荐催化剂钯配合物的用量为2-溴吡嗪的0.1~5%摩尔当量;推荐碱金属碳酸盐的用量为2-溴吡嗪的1~2摩尔当量。With N,N-dimethylacetamide as the reaction solvent, palladium complex as the catalyst, alkali metal carbonate as the base, 2-bromopyrazine and alkali metal ferrocyanide under the protection of nitrogen at 100-150 ℃ for 1-6 hours, then filtered, and the filtrate was fractionated under reduced pressure to obtain 2-cyanopyrazine with high yield and high purity. Wherein the molar equivalent ratio of 2-bromopyrazine and alkali metal ferrocyanide is 1: 0.15~0.3; The consumption of catalyst palladium complex is 0.1~5% molar equivalent of 2-bromopyrazine; The consumption of alkali metal carbonate It is 0.5-2 molar equivalents of 2-bromopyrazine. The recommended reaction time is 1 to 5 hours; the recommended reaction temperature is 100 to 140°C; the molar equivalent ratio of 2-bromopyrazine and alkali metal ferrocyanide is recommended to be 1:0.15 to 0.3; the recommended amount of catalyst palladium complex is 0.1-5% molar equivalent of 2-bromopyrazine; the recommended dosage of alkali metal carbonate is 1-2 molar equivalent of 2-bromopyrazine.
以下实施例将有助于理解本发明,但不限于本发明的内容:The following examples will help to understand the present invention, but are not limited to the content of the present invention:
实施例1Example 1
在1000毫升三颈瓶中,氮气保护下依次加入500毫升N,N-二甲基乙酰胺溶剂,48克(300毫摩尔)2-溴吡嗪,25克(60毫摩尔,0.2当量)三水合亚铁氰化钾,680毫克(3毫摩尔,0.3mol%)醋酸钯催化剂,35克碳酸钠(330毫摩尔,1.1当量),在氮气保护下在120℃搅拌反应2小时,结束反应,随后过滤,滤液减压分馏得到透明液体2-氰基吡嗪,沸点:84-87℃(18-20mmHg),产率88%,纯度98%(GC)。In a 1000 ml three-necked flask, 500 ml of N,N-dimethylacetamide solvent, 48 g (300 mmol) of 2-bromopyrazine, 25 g (60 mmol, 0.2 equivalents) of tris Potassium ferrocyanide hydrate, 680 milligrams (3 millimoles, 0.3mol%) palladium acetate catalyst, 35 grams of sodium carbonate (330 millimoles, 1.1 equivalents), under nitrogen protection at 120 ℃ stirring reaction 2 hours, finish reaction, Then filtered, the filtrate was fractionated under reduced pressure to obtain transparent liquid 2-cyanopyrazine, boiling point: 84-87°C (18-20mmHg), yield 88%, purity 98% (GC).
实施例2Example 2
在1000毫升三颈瓶中,氮气保护下依次加入500毫升N,N-二甲基乙酰胺溶剂,48克(300毫摩尔)2-溴吡嗪,28克(66毫摩尔,0.22当量)三水合亚铁氰化钾,340毫克(15毫摩尔,5mol%)醋酸钯催化剂,31.8克碳酸钠(300毫摩尔,1.0当量),在氮气保护下在100℃搅拌反应13小时,结束反应,随后过滤,滤液减压分馏得到透明液体2-氰基吡嗪,产率90%,纯度99%。In a 1000 ml three-necked flask, 500 ml of N,N-dimethylacetamide solvent, 48 g (300 mmol) of 2-bromopyrazine, 28 g (66 mmol, 0.22 equivalent) of tris Potassium ferrocyanide hydrate, 340 milligrams (15 millimoles, 5mol%) palladium acetate catalyst, 31.8 gram sodium carbonates (300 millimoles, 1.0 equivalents), under nitrogen protection, stirred reaction at 100 ℃ for 13 hours, ended the reaction, then After filtration, the filtrate was fractionated under reduced pressure to obtain transparent liquid 2-cyanopyrazine with a yield of 90% and a purity of 99%.
实施例3Example 3
在1000毫升三颈瓶中,氮气保护下依次加入500毫升N,N-二甲基乙酰胺溶剂,48克(300毫摩尔)2-溴吡嗪,20克(45毫摩尔,0.15当量)三水合亚铁氰化钠,1.5毫摩尔(0.5mol%)双(二亚苄基丙酮酸)钯催化剂,31.8克碳酸钠(300毫摩尔,1.0当量),在氮气保护下在120℃搅拌反应4小时,结束反应,随后过滤,滤液减压分馏得到透明液体2-氰基吡嗪,产率80%,纯度99%。In a 1000 ml three-necked flask, 500 ml of N,N-dimethylacetamide solvent, 48 g (300 mmol) of 2-bromopyrazine, 20 g (45 mmol, 0.15 equivalent) of tris Sodium ferrocyanide hydrate, 1.5 millimoles (0.5mol%) two (dibenzylidene pyruvate) palladium catalysts, 31.8 grams of sodium carbonate (300 millimoles, 1.0 equivalent), under nitrogen protection, at 120 ℃ stirring reaction 4 Hours, the reaction was terminated, followed by filtration, and the filtrate was fractionated under reduced pressure to obtain a transparent liquid 2-cyanopyrazine with a yield of 80% and a purity of 99%.
实施例4Example 4
在1000毫升三颈瓶中,氮气保护下依次加入500毫升N,N-二甲基乙酰胺溶剂,48克(300毫摩尔)2-溴吡嗪,28克(66毫摩尔,0.25当量)三水合亚铁氰化钾,0.3毫摩尔(0.1mol%)双(二亚苄基丙酮酸)钯催化剂,66克碳酸钾(600毫摩尔,2.0当量),在氮气保护下在120℃搅拌反应6小时,结束反应,随后过滤,滤液减压分馏得到透明液体2-氰基吡嗪,产率86%,纯度97%。In a 1000 ml three-necked flask, 500 ml of N,N-dimethylacetamide solvent, 48 g (300 mmol) of 2-bromopyrazine, 28 g (66 mmol, 0.25 equivalent) of tris Potassium ferrocyanide hydrate, 0.3 millimoles (0.1mol%) bis(dibenzylidene pyruvate) palladium catalyst, 66 grams of potassium carbonate (600 millimoles, 2.0 equivalents), stirred reaction at 120 ℃ under nitrogen protection 6 Hours, the reaction was terminated, followed by filtration, and the filtrate was fractionated under reduced pressure to obtain a transparent liquid 2-cyanopyrazine with a yield of 86% and a purity of 97%.
实施例5Example 5
在1000毫升三颈瓶中,氮气保护下依次加入500毫升N,N-二甲基乙酰胺溶剂,48克(300毫摩尔)2-溴吡嗪,44克(90毫摩尔,0.3当量)三水合亚铁氰化钠,270毫克(1.2毫摩尔,0.4mol%)醋酸钯催化剂,33克碳酸钾(300毫摩尔,1.0当量),在氮气保护下在150℃搅拌反应3小时,结束反应,随后过滤,滤液减压分馏得到透明液体2-氰基吡嗪,产率90%,纯度99%。In a 1000 ml three-necked flask, 500 ml of N,N-dimethylacetamide solvent, 48 g (300 mmol) of 2-bromopyrazine, 44 g (90 mmol, 0.3 equivalents) of tris Sodium ferrocyanide hydrate, 270 milligrams (1.2 millimoles, 0.4mol%) palladium acetate catalyst, 33 grams of salt of wormwood (300 millimoles, 1.0 equivalent), under the protection of nitrogen at 150 ℃ stirring reaction 3 hours, finish reaction, Then it was filtered, and the filtrate was fractionated under reduced pressure to obtain transparent liquid 2-cyanopyrazine with a yield of 90% and a purity of 99%.
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