CN114181210B - Preparation method of tetrahydrofolic acid - Google Patents
Preparation method of tetrahydrofolic acid Download PDFInfo
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- CN114181210B CN114181210B CN202111457715.6A CN202111457715A CN114181210B CN 114181210 B CN114181210 B CN 114181210B CN 202111457715 A CN202111457715 A CN 202111457715A CN 114181210 B CN114181210 B CN 114181210B
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- MSTNYGQPCMXVAQ-KIYNQFGBSA-N 5,6,7,8-tetrahydrofolic acid Chemical compound N1C=2C(=O)NC(N)=NC=2NCC1CNC1=CC=C(C(=O)N[C@@H](CCC(O)=O)C(O)=O)C=C1 MSTNYGQPCMXVAQ-KIYNQFGBSA-N 0.000 title claims abstract description 58
- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- OVBPIULPVIDEAO-LBPRGKRZSA-N folic acid Chemical compound C=1N=C2NC(N)=NC(=O)C2=NC=1CNC1=CC=C(C(=O)N[C@@H](CCC(O)=O)C(O)=O)C=C1 OVBPIULPVIDEAO-LBPRGKRZSA-N 0.000 claims abstract description 118
- OVBPIULPVIDEAO-UHFFFAOYSA-N N-Pteroyl-L-glutaminsaeure Natural products C=1N=C2NC(N)=NC(=O)C2=NC=1CNC1=CC=C(C(=O)NC(CCC(O)=O)C(O)=O)C=C1 OVBPIULPVIDEAO-UHFFFAOYSA-N 0.000 claims abstract description 59
- 239000011724 folic acid Substances 0.000 claims abstract description 59
- 229960000304 folic acid Drugs 0.000 claims abstract description 59
- 235000019152 folic acid Nutrition 0.000 claims abstract description 59
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims abstract description 51
- 238000006243 chemical reaction Methods 0.000 claims abstract description 43
- 239000003054 catalyst Substances 0.000 claims abstract description 33
- 239000001257 hydrogen Substances 0.000 claims abstract description 27
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 27
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000006479 redox reaction Methods 0.000 claims abstract description 13
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 6
- 238000011049 filling Methods 0.000 claims abstract description 4
- 239000000243 solution Substances 0.000 claims description 71
- MSTNYGQPCMXVAQ-RYUDHWBXSA-N (6S)-5,6,7,8-tetrahydrofolic acid Chemical compound C([C@H]1CNC=2N=C(NC(=O)C=2N1)N)NC1=CC=C(C(=O)N[C@@H](CCC(O)=O)C(O)=O)C=C1 MSTNYGQPCMXVAQ-RYUDHWBXSA-N 0.000 claims description 44
- 239000005460 tetrahydrofolate Substances 0.000 claims description 44
- 239000007853 buffer solution Substances 0.000 claims description 35
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 24
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 13
- 239000011259 mixed solution Substances 0.000 claims description 12
- 229910052757 nitrogen Inorganic materials 0.000 claims description 11
- 230000035484 reaction time Effects 0.000 claims description 11
- 239000007787 solid Substances 0.000 claims description 10
- 239000012670 alkaline solution Substances 0.000 claims description 7
- 239000008055 phosphate buffer solution Substances 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 239000011261 inert gas Substances 0.000 claims description 5
- 239000006171 Britton–Robinson buffer Substances 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 3
- 229910021538 borax Inorganic materials 0.000 claims description 3
- HDFXRQJQZBPDLF-UHFFFAOYSA-L disodium hydrogen carbonate Chemical compound [Na+].[Na+].OC([O-])=O.OC([O-])=O HDFXRQJQZBPDLF-UHFFFAOYSA-L 0.000 claims description 3
- CBMPTFJVXNIWHP-UHFFFAOYSA-L disodium;hydrogen phosphate;2-hydroxypropane-1,2,3-tricarboxylic acid Chemical compound [Na+].[Na+].OP([O-])([O-])=O.OC(=O)CC(O)(C(O)=O)CC(O)=O CBMPTFJVXNIWHP-UHFFFAOYSA-L 0.000 claims description 3
- 239000004328 sodium tetraborate Substances 0.000 claims description 3
- CIJQGPVMMRXSQW-UHFFFAOYSA-M sodium;2-aminoacetic acid;hydroxide Chemical compound O.[Na+].NCC([O-])=O CIJQGPVMMRXSQW-UHFFFAOYSA-M 0.000 claims description 3
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 claims description 3
- 239000007983 Tris buffer Substances 0.000 claims description 2
- BUCIWTBCUUHRHZ-UHFFFAOYSA-K potassium;disodium;dihydrogen phosphate;hydrogen phosphate Chemical compound [Na+].[Na+].[K+].OP(O)([O-])=O.OP([O-])([O-])=O BUCIWTBCUUHRHZ-UHFFFAOYSA-K 0.000 claims description 2
- 239000013049 sediment Substances 0.000 claims 4
- FTOAOBMCPZCFFF-UHFFFAOYSA-N 5,5-diethylbarbituric acid Chemical compound CCC1(CC)C(=O)NC(=O)NC1=O FTOAOBMCPZCFFF-UHFFFAOYSA-N 0.000 claims 2
- 238000004519 manufacturing process Methods 0.000 claims 2
- 230000001105 regulatory effect Effects 0.000 claims 2
- 239000003513 alkali Substances 0.000 claims 1
- 229960002319 barbital Drugs 0.000 claims 1
- 239000012266 salt solution Substances 0.000 claims 1
- OTNVGWMVOULBFZ-UHFFFAOYSA-N sodium;hydrochloride Chemical compound [Na].Cl OTNVGWMVOULBFZ-UHFFFAOYSA-N 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- VWBIJLFTDUZNDF-UHFFFAOYSA-J tetrasodium hydrogen phosphate Chemical compound [Na+].[Na+].[Na+].[Na+].OP([O-])([O-])=O.OP([O-])([O-])=O VWBIJLFTDUZNDF-UHFFFAOYSA-J 0.000 claims 1
- 239000002244 precipitate Substances 0.000 description 13
- 230000000694 effects Effects 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N hydrochloric acid Substances Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 8
- 238000002474 experimental method Methods 0.000 description 6
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 6
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000011734 sodium Substances 0.000 description 5
- 238000001291 vacuum drying Methods 0.000 description 5
- 238000001035 drying Methods 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 3
- AUHZEENZYGFFBQ-UHFFFAOYSA-N mesitylene Substances CC1=CC(C)=CC(C)=C1 AUHZEENZYGFFBQ-UHFFFAOYSA-N 0.000 description 3
- -1 mesitylene glycol Chemical compound 0.000 description 3
- CRUILBNAQILVHZ-UHFFFAOYSA-N 1,2,3-trimethoxybenzene Chemical compound COC1=CC=CC(OC)=C1OC CRUILBNAQILVHZ-UHFFFAOYSA-N 0.000 description 2
- FTHCZYMFYCBWMW-UHFFFAOYSA-N Cl.CNCO.CNCO.CNCO Chemical compound Cl.CNCO.CNCO.CNCO FTHCZYMFYCBWMW-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-WFGJKAKNSA-N Dimethyl sulfoxide Chemical compound [2H]C([2H])([2H])S(=O)C([2H])([2H])[2H] IAZDPXIOMUYVGZ-WFGJKAKNSA-N 0.000 description 2
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 2
- 101000827703 Homo sapiens Polyphosphoinositide phosphatase Proteins 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 2
- 102100023591 Polyphosphoinositide phosphatase Human genes 0.000 description 2
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 2
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 2
- 238000004108 freeze drying Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- LEAHFJQFYSDGGP-UHFFFAOYSA-K trisodium;dihydrogen phosphate;hydrogen phosphate Chemical compound [Na+].[Na+].[Na+].OP(O)([O-])=O.OP([O-])([O-])=O LEAHFJQFYSDGGP-UHFFFAOYSA-K 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 102000057846 EC 2.1.-.- Human genes 0.000 description 1
- 108700033392 EC 2.1.-.- Proteins 0.000 description 1
- 102000004357 Transferases Human genes 0.000 description 1
- 108090000992 Transferases Proteins 0.000 description 1
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
- DSVGQVZAZSZEEX-UHFFFAOYSA-N [C].[Pt] Chemical compound [C].[Pt] DSVGQVZAZSZEEX-UHFFFAOYSA-N 0.000 description 1
- YVZLYNHKJASIHA-UHFFFAOYSA-L [Na+].[K+].OP(O)([O-])=O.OP(O)([O-])=O Chemical compound [Na+].[K+].OP(O)([O-])=O.OP(O)([O-])=O YVZLYNHKJASIHA-UHFFFAOYSA-L 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- YKIOKAURTKXMSB-UHFFFAOYSA-N adams's catalyst Chemical compound O=[Pt]=O YKIOKAURTKXMSB-UHFFFAOYSA-N 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000005515 coenzyme Substances 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- OZRNSSUDZOLUSN-LBPRGKRZSA-N dihydrofolic acid Chemical compound N=1C=2C(=O)NC(N)=NC=2NCC=1CNC1=CC=C(C(=O)N[C@@H](CCC(O)=O)C(O)=O)C=C1 OZRNSSUDZOLUSN-LBPRGKRZSA-N 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- UKVIEHSSVKSQBA-UHFFFAOYSA-N methane;palladium Chemical compound C.[Pd] UKVIEHSSVKSQBA-UHFFFAOYSA-N 0.000 description 1
- RPNNPZHFJPXFQS-UHFFFAOYSA-N methane;rhodium Chemical compound C.[Rh] RPNNPZHFJPXFQS-UHFFFAOYSA-N 0.000 description 1
- 239000013081 microcrystal Substances 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012113 quantitative test Methods 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 229940030010 trimethoxybenzene Drugs 0.000 description 1
- 239000003656 tris buffered saline Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D475/00—Heterocyclic compounds containing pteridine ring systems
- C07D475/02—Heterocyclic compounds containing pteridine ring systems with an oxygen atom directly attached in position 4
- C07D475/04—Heterocyclic compounds containing pteridine ring systems with an oxygen atom directly attached in position 4 with a nitrogen atom directly attached in position 2
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
技术领域Technical Field
本发明涉及药物合成技术领域,特别涉及一种四氢叶酸的制备方法。The invention relates to the technical field of drug synthesis, and in particular to a method for preparing tetrahydrofolic acid.
背景技术Background technique
四氢叶酸是一碳基团(包括CH3、CH2、CHO等)转移酶的辅酶,四氢叶酸具有传递一碳基团的作用,参与很多重要反应及核酸和氨基酸的合成。Tetrahydrofolate is a coenzyme of one-carbon group (including CH 3 , CH 2 , CHO, etc.) transferase. Tetrahydrofolate has the function of transferring one-carbon groups and participates in many important reactions and the synthesis of nucleic acids and amino acids.
目前,四氢叶酸一般是通过由叶酸通过催化加氢还原法制备而得。Currently, tetrahydrofolic acid is generally prepared by catalytic hydrogenation reduction of folic acid.
催化加氢还原法中通常所用的催化剂为Pt/C(铂碳催化剂)、Rh/C(铑碳催化剂)和PtO2(二氧化铂催化剂)等,催化剂用的量大,且催化效果不理想,导致四氢叶酸的制备产率低。The catalysts commonly used in the catalytic hydrogenation reduction method are Pt/C (platinum-carbon catalyst), Rh/C (rhodium-carbon catalyst) and PtO 2 (platinum dioxide catalyst). The amount of catalyst used is large and the catalytic effect is not ideal, resulting in a low yield of tetrahydrofolate preparation.
发明内容Summary of the invention
基于此,本发明提供一种四氢叶酸的制备方法,在满足减少催化剂用量的要求下,解决四氢叶酸制备产率低的问题。Based on this, the present invention provides a method for preparing tetrahydrofolate, which solves the problem of low yield of tetrahydrofolate preparation while meeting the requirement of reducing the amount of catalyst used.
本发明提供一种四氢叶酸的制备方法,包括步骤:The present invention provides a method for preparing tetrahydrofolate, comprising the steps of:
将Pd/C催化剂和pH叶酸溶液加入反应釜中,向所述反应釜中充入氢气,将所述反应釜置于40-90℃的环境下,所述叶酸与所述氢气发生氧化还原反应,反应结束后,即得四氢叶酸;Adding a Pd/C catalyst and a pH folic acid solution into a reactor, filling the reactor with hydrogen, placing the reactor in an environment of 40-90° C., allowing the folic acid to undergo an oxidation-reduction reaction with the hydrogen, and obtaining tetrahydrofolic acid after the reaction is completed;
制备四氢叶酸的反应方程式如下:The reaction equation for preparing tetrahydrofolic acid is as follows:
其中,叶酸的化学式为: The chemical formula of folic acid is:
四氢叶酸的化学式为: The chemical formula of tetrahydrofolate is:
优选地,所述催化剂Pd/C包括10%Pd/C,所述叶酸与所述催化剂10%Pd/C的质量比为100:(0.1-20)。Preferably, the catalyst Pd/C comprises 10% Pd/C, and the mass ratio of the folic acid to the catalyst 10% Pd/C is 100:(0.1-20).
优选地,在所述叶酸与所述氢气发生氧化还原反应的步骤中,所述反应釜的压力范围为20-65bar。Preferably, in the step of the folic acid and the hydrogen undergoing redox reaction, the pressure range of the reactor is 20-65 bar.
优选地,所述叶酸与所述氢气发生氧化还原反应的反应时间为6-24h。Preferably, the reaction time of the redox reaction between the folic acid and the hydrogen is 6-24 hours.
优选地,在反应结束后,即得四氢叶酸的步骤中,包括:Preferably, after the reaction is completed, the step of obtaining tetrahydrofolic acid comprises:
在反应结束后,得到含有四氢叶酸的溶液,用酸溶液调节所述含有四氢叶酸的溶液的pH至3~3.5,得到含有四氢叶酸沉淀的溶液,将所述含有四氢叶酸沉淀的溶液过滤,收集所述四氢叶酸沉淀,干燥所述沉淀,即得四氢叶酸。After the reaction is completed, a solution containing tetrahydrofolic acid is obtained, and the pH of the solution containing tetrahydrofolic acid is adjusted to 3-3.5 with an acid solution to obtain a solution containing tetrahydrofolic acid precipitate, and the solution containing tetrahydrofolic acid precipitate is filtered to collect the tetrahydrofolic acid precipitate, and the precipitate is dried to obtain tetrahydrofolic acid.
优选地,所述叶酸溶液的pH为6~7,所述叶酸溶液的制备包括步骤:Preferably, the pH of the folic acid solution is 6-7, and the preparation of the folic acid solution comprises the steps of:
将固体叶酸加入烧瓶中,向所述烧瓶中充入氮气或惰性气体至烧瓶内形成无氧环境,向所述烧瓶中加入缓冲溶液,搅拌至均匀,得到混合溶液,用碱溶液调节所述混合溶液的pH至6~7,得到叶酸溶液。Solid folic acid is added into a flask, nitrogen or an inert gas is filled into the flask to form an oxygen-free environment, a buffer solution is added into the flask, and the mixture is stirred until uniform to obtain a mixed solution, and the pH of the mixed solution is adjusted to 6-7 with an alkaline solution to obtain a folic acid solution.
优选地,所述缓冲溶液pH为4~10。Preferably, the pH of the buffer solution is 4-10.
优选地,所述缓冲溶液包括磷酸氢二钠-柠檬酸缓冲溶液、磷酸二氢钠-磷酸氢二钠缓冲溶液、磷酸氢二钠-磷酸二氢钾缓冲溶液、巴比妥钠-盐酸缓冲溶液、三羟甲基氨基甲烷-盐酸缓冲溶液、硼酸-硼砂缓冲溶液、甘氨酸-氢氧化钠缓冲溶液、硼砂-氢氧化钠缓冲溶液、碳酸钠-碳酸氢钠缓冲溶液、Britton-Robinson缓冲溶液和Tris缓冲盐溶液中的任意一种。Preferably, the buffer solution includes any one of disodium hydrogen phosphate-citric acid buffer solution, sodium dihydrogen phosphate-disodium hydrogen phosphate buffer solution, disodium hydrogen phosphate-potassium dihydrogen phosphate buffer solution, sodium barbital-hydrochloric acid buffer solution, tris(hydroxymethylaminomethane)-hydrochloric acid buffer solution, boric acid-borax buffer solution, glycine-sodium hydroxide buffer solution, borax-sodium hydroxide buffer solution, sodium carbonate-sodium bicarbonate buffer solution, Britton-Robinson buffer solution and Tris buffer saline solution.
优选地,所述碱溶液包括NaOH溶液和KOH溶液中的任意一种。Preferably, the alkaline solution includes any one of a NaOH solution and a KOH solution.
优选地,所述缓冲溶液的用量为10-15ml/1g固体叶酸。Preferably, the amount of the buffer solution is 10-15 ml/1 g of solid folic acid.
与现有方案相比,本发明具有以下有益效果:Compared with the existing solutions, the present invention has the following beneficial effects:
本发明通过将叶酸在催化剂Pd/C的催化下还原制备得到四氢叶酸,催化剂Pd/C的催化效率高且可以循环使用,克服了现有技术中催化剂用量大和产量低的问题。The invention prepares tetrahydrofolic acid by reducing folic acid under the catalysis of a catalyst Pd/C. The catalyst Pd/C has high catalytic efficiency and can be recycled, thus overcoming the problems of large catalyst dosage and low yield in the prior art.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为叶酸溶液的pH对四氢叶酸产率的影响的实验结果图;FIG1 is a graph showing the experimental results of the effect of pH of a folic acid solution on tetrahydrofolate yield;
图2为反应时间对四氢叶酸产率的影响的实验结果图;FIG2 is a graph showing the experimental results of the effect of reaction time on tetrahydrofolate yield;
图3为反应温度对四氢叶酸产率的影响的实验结果图;FIG3 is a graph showing the experimental results of the effect of reaction temperature on tetrahydrofolate yield;
图4为催化剂Pd/C的用量对四氢叶酸产率的影响的实验结果图;FIG4 is an experimental result diagram showing the effect of the amount of catalyst Pd/C on the yield of tetrahydrofolate;
图5为产物四氢叶酸的核磁图。FIG5 is the NMR image of the product tetrahydrofolate.
具体实施方式Detailed ways
下面将结合本发明实施例,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的一部分实施例,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作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 following will be combined with the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.
下述实施例中的实验方法,如无特殊说明,均为常规方法。下述实施例中所用的试验材料和试剂等,如无特殊说明,均可从商业途径获得。以下实施例中的定量试验,均设置三次重复实验,数据为三次重复实验的平均值或平均值±标准差。The experimental methods in the following examples are conventional methods unless otherwise specified. The experimental materials and reagents used in the following examples are all commercially available unless otherwise specified. The quantitative tests in the following examples were performed in triplicate, and the data are the average or average ± standard deviation of the triplicate experiments.
另外,全文中的“和/或”包括三个方案,以A和/或B为例,包括A技术方案、B技术方案,以及A和B同时满足的技术方案;另外,各个实施例之间的技术方案可以相互结合,但是必须是以本领域普通技术人员能够实现为基础,当技术方案的结合出现相互矛盾或无法实现时应当认为这种技术方案的结合不存在,也不在本发明要求的保护范围之内。In addition, the "and/or" in the full text includes three solutions. Taking A and/or B as an example, it includes technical solution A, technical solution B, and a technical solution that satisfies both A and B. In addition, the technical solutions between the various embodiments can be combined with each other, but it must be based on the ability of ordinary technicians in the field to implement. When the combination of technical solutions is contradictory or cannot be implemented, it should be deemed that such a combination of technical solutions does not exist and is not within the scope of protection required by the present invention.
本发明提供了一种四氢叶酸的制备方法,包括步骤:The present invention provides a method for preparing tetrahydrofolic acid, comprising the steps of:
将Pd/C催化剂和叶酸溶液加入反应釜中,向反应釜中充入氢气,将反应釜置于40-90℃的环境下,叶酸与氢气发生氧化还原反应,反应结束后,即得四氢叶酸;Pd/C catalyst and folic acid solution are added into a reactor, hydrogen is introduced into the reactor, and the reactor is placed in an environment of 40-90° C., folic acid and hydrogen undergo redox reaction, and tetrahydrofolic acid is obtained after the reaction is completed;
制备四氢叶酸的反应方程式如下:The reaction equation for preparing tetrahydrofolic acid is as follows:
其中,固体叶酸的化学式为: Among them, the chemical formula of solid folic acid is:
四氢叶酸的化学式为: The chemical formula of tetrahydrofolate is:
本发明通过将叶酸在催化剂Pd/C的催化下还原制备得到四氢叶酸,催化剂Pd/C的催化效率高且可以循环使用,克服了现有技术中催化剂用量大和产量低的问题。The invention prepares tetrahydrofolic acid by reducing folic acid under the catalysis of a catalyst Pd/C. The catalyst Pd/C has high catalytic efficiency and can be recycled, thus overcoming the problems of large catalyst dosage and low yield in the prior art.
氢气还原叶酸中的碳氮双键,具体是氢气吸附在催化剂Pd/C表面上,叶酸与催化剂配位,氢气的氢分子在催化剂Pd/C催化下发生键的断裂,形成活泼的氢原子,氢气的氢原子与叶酸的碳氮双键结合,还原形成碳氮单键,生成四氢叶酸。Hydrogen reduces the carbon-nitrogen double bond in folic acid. Specifically, hydrogen is adsorbed on the surface of the catalyst Pd/C, folic acid coordinates with the catalyst, and the hydrogen molecules of hydrogen break their bonds under the catalysis of the catalyst Pd/C to form active hydrogen atoms. The hydrogen atoms of hydrogen combine with the carbon-nitrogen double bond of folic acid to reduce to form a carbon-nitrogen single bond, thereby generating tetrahydrofolic acid.
Pd/C是指钯碳,钯微晶均匀浸布在特制的多孔碳载体上。Pd/C refers to palladium carbon, in which palladium microcrystals are evenly impregnated on a special porous carbon carrier.
具体地,向反应釜中充入氢气至反应釜中至反应釜中不含除氢气之外的气体;Specifically, hydrogen is charged into the reactor until the reactor contains no gas other than hydrogen;
在将催化剂Pd/C加入反应釜中,将叶酸溶液加入反应釜中的步骤中,向反应釜内充入氮气或惰性气体以使所述反应釜内形成无氧环境。In the steps of adding the catalyst Pd/C into the reactor and adding the folic acid solution into the reactor, nitrogen or an inert gas is charged into the reactor to form an oxygen-free environment in the reactor.
在一些实施例中,催化剂Pd/C包括10%Pd/C,叶酸与催化剂10%Pd/C的质量比为100:(0.1-20)。In some embodiments, the catalyst Pd/C includes 10% Pd/C, and the mass ratio of folic acid to the catalyst 10% Pd/C is 100:(0.1-20).
在一些实施例中,在叶酸与氢气发生氧化还原反应的步骤中,反应釜的压力范围为30-65bar。In some embodiments, in the step of redox reaction of folic acid and hydrogen, the pressure of the reactor is in the range of 30-65 bar.
在一些实施例中,叶酸与氢气发生氧化还原反应的反应时间为6-24h。In some embodiments, the reaction time of the redox reaction of folic acid and hydrogen is 6-24 hours.
在一些实施例中,在反应结束后,即得四氢叶酸的步骤中,包括:In some embodiments, after the reaction is completed, the step of obtaining tetrahydrofolic acid includes:
在反应结束后,得到含有四氢叶酸的溶液,用酸溶液调节含有四氢叶酸沉淀的pH至3~3.5,得到含有四氢叶酸沉淀的溶液,将含有四氢叶酸沉淀的溶液过滤,收集四氢叶酸沉淀,干燥沉淀,即得四氢叶酸。After the reaction is completed, a solution containing tetrahydrofolic acid is obtained, and the pH of the solution containing tetrahydrofolic acid precipitate is adjusted to 3-3.5 with an acid solution to obtain a solution containing tetrahydrofolic acid precipitate, and the solution containing tetrahydrofolic acid precipitate is filtered to collect the tetrahydrofolic acid precipitate, and the precipitate is dried to obtain tetrahydrofolic acid.
具体地,反应结束后,整个体系是均相的,四氢叶酸在酸性条件下会析出,pH为3-3.5是四氢叶酸析出产率最高的时候;Specifically, after the reaction is completed, the entire system is homogeneous, and tetrahydrofolate will precipitate under acidic conditions, with pH 3-3.5 being the time when the precipitation yield of tetrahydrofolate is the highest;
四氢叶酸对氧敏感,易被氧化为二氢叶酸,因此整个反应过程需要无氧环境;Tetrahydrofolate is sensitive to oxygen and can be easily oxidized to dihydrofolate, so the entire reaction process requires an anaerobic environment;
具体地,干燥方式包括冷冻干燥、真空干燥等,在无氧的条件下干燥,防止四氢叶酸被氧化;Specifically, the drying method includes freeze drying, vacuum drying, etc., and drying under anaerobic conditions to prevent tetrahydrofolate from being oxidized;
在氮气或惰性气体的条件下进行过滤过滤,避免四氢叶酸被氧化。Filtration should be performed under nitrogen or inert gas to avoid oxidation of tetrahydrofolate.
在一些实施例中,叶酸溶液的pH为6~7,叶酸溶液的制备包括步骤:In some embodiments, the pH of the folic acid solution is 6-7, and the preparation of the folic acid solution comprises the steps of:
将固体叶酸加入烧瓶中,向烧瓶中充入氮气或惰性气体至烧瓶内形成无氧环境,向烧瓶中加入pH为4~7缓冲溶液,搅拌至均匀,得到混合溶液,用碱溶液调节混合溶液的pH至6~7,得到叶酸溶液。Solid folic acid is added to a flask, nitrogen or an inert gas is filled into the flask to form an oxygen-free environment, a buffer solution with a pH value of 4 to 7 is added to the flask, and the mixture is stirred until uniform to obtain a mixed solution, and the pH value of the mixed solution is adjusted to 6 to 7 with an alkaline solution to obtain a folic acid solution.
具体地,叶酸溶液于室温环境下制而得,即25-35℃。Specifically, the folic acid solution is prepared at room temperature, i.e., 25-35°C.
具体地,添加缓冲溶液是为了控制溶液的pH,避免出现滴定突跃;Specifically, the buffer solution is added to control the pH of the solution and avoid titration jumps;
具体地,叶酸会溶解在碱溶液中,利用碱溶液将叶酸溶液调至pH=7时,叶酸反应生成四氢叶酸的产率达到最高。Specifically, folic acid will dissolve in an alkaline solution. When the pH of the folic acid solution is adjusted to 7 using an alkaline solution, the yield of tetrahydrofolic acid generated by the reaction of folic acid reaches the highest.
在一些实施例中,缓冲溶液包括磷酸氢二钠-柠檬酸缓冲溶液、磷酸二氢钠-磷酸氢二钠缓冲溶液、磷酸氢二钠-磷酸二氢钾缓冲溶液、巴比妥钠-盐酸缓冲溶液、三羟甲基氨基甲烷-盐酸缓冲溶液、硼酸-硼砂缓冲溶液、甘氨酸-氢氧化钠缓冲溶液、硼砂-氢氧化钠缓冲溶液、碳酸钠-碳酸氢钠缓冲溶液、Britton-Robinson缓冲溶液和Tris缓冲盐溶液中的任意一种。In some embodiments, the buffer solution includes any one of disodium hydrogen phosphate-citric acid buffer solution, sodium dihydrogen phosphate-disodium hydrogen phosphate buffer solution, sodium dihydrogen phosphate-potassium dihydrogen phosphate buffer solution, sodium barbital-hydrochloric acid buffer solution, tris(hydroxymethylaminomethane)-hydrochloric acid buffer solution, boric acid-borax buffer solution, glycine-sodium hydroxide buffer solution, borax-sodium hydroxide buffer solution, sodium carbonate-sodium bicarbonate buffer solution, Britton-Robinson buffer solution and Tris buffered saline solution.
在一些实施例中,碱溶液包括NaOH溶液和KOH溶液中的任意一种。In some embodiments, the alkaline solution includes any one of a NaOH solution and a KOH solution.
在一些实施例中,缓冲溶液的用量为10-15ml/1g固体叶酸。In some embodiments, the amount of buffer solution used is 10-15 ml/1 g solid folic acid.
具体地,干燥方式包括冷冻干燥、真空干燥等,在无氧的条件下干燥,防止四氢叶酸被氧化。Specifically, the drying method includes freeze drying, vacuum drying, etc., and drying is performed under anaerobic conditions to prevent tetrahydrofolate from being oxidized.
在一些实施例中,还包括:In some embodiments, it also includes:
用均三甲氧基苯作为内标,对四氢叶酸进行核磁检测。Tetrahydrofolate was detected by NMR using trimethoxybenzene as an internal standard.
实施例1Example 1
于25℃环境下,向100mL的三口烧瓶中加入1g固体叶酸,将烧瓶用氮气置换3次后,向烧瓶中加入10mL 0.2mol/L pH为7的NaH2PO4-Na2HPO4缓冲溶液,搅拌至均匀,得到混合溶液,用20%的NaOH溶液调节混合溶液的pH至7,得到叶酸溶液;Under 25°C, 1 g of solid folic acid was added to a 100 mL three-necked flask, the flask was replaced with nitrogen three times, 10 mL of 0.2 mol/L NaH 2 PO 4 -Na 2 HPO 4 buffer solution with a pH of 7 was added to the flask, and the mixture was stirred until uniform to obtain a mixed solution, and the pH of the mixed solution was adjusted to 7 with a 20% NaOH solution to obtain a folic acid solution;
向50mL的反应釜中加入0.1g10%Pd/C,将反应釜用氮气置换3次后,向反应釜中加入pH为7的叶酸溶液,将反应釜用氢气置换5次后,向反应釜中充入氢气,调反应釜压力至50bar,将反应釜置于60℃的环境下,发生氧化还原反应,反应15h,反应结束后,得到含有四氢叶酸的溶液,用1mol/L盐酸溶液调节含有四氢叶酸的溶液的pH至3,析出四氢叶酸沉淀,将沉淀过滤后,利用真空干燥箱干燥8h,即得四氢叶酸。0.1 g of 10% Pd/C was added to a 50 mL reactor. After the reactor was replaced with nitrogen for 3 times, a folic acid solution with a pH of 7 was added to the reactor. After the reactor was replaced with hydrogen for 5 times, hydrogen was filled into the reactor. The pressure of the reactor was adjusted to 50 bar. The reactor was placed in an environment of 60° C. for redox reaction. The reaction was performed for 15 hours. After the reaction was completed, a solution containing tetrahydrofolic acid was obtained. The pH of the solution containing tetrahydrofolic acid was adjusted to 3 with a 1 mol/L hydrochloric acid solution to precipitate tetrahydrofolic acid. The precipitate was filtered and dried in a vacuum drying oven for 8 hours to obtain tetrahydrofolic acid.
用均三甲氧基苯作为内标,对四氢叶酸进行检测,测得四氢叶酸的产率为93%。Tetrahydrofolate was detected using mesitylene glycol as an internal standard, and the yield of tetrahydrofolate was found to be 93%.
实施例2Example 2
于28℃环境下,向100mL的三口烧瓶中加入1g固体叶酸,将烧瓶用氮气置换3次后,向烧瓶中加入10mL 0.2mol/L pH为7的NaH2PO4-Na2HPO4缓冲溶液,搅拌至均匀,得到混合溶液,用20%的NaOH溶液调节混合溶液的pH至7,得到叶酸溶液;At 28°C, 1 g of solid folic acid was added to a 100 mL three-necked flask, the flask was replaced with nitrogen three times, 10 mL of 0.2 mol/L NaH 2 PO 4 -Na 2 HPO 4 buffer solution with a pH of 7 was added to the flask, and the mixture was stirred until uniform to obtain a mixed solution, and the pH of the mixed solution was adjusted to 7 with a 20% NaOH solution to obtain a folic acid solution;
向50mL的反应釜中加入0.2g10%Pd/C,将反应釜用氮气置换3次后,向反应釜中加入pH为7的叶酸溶液,将反应釜用氢气置换5次后,向反应釜中充入氢气,调反应釜压力至30bar,将反应釜置于70℃的环境下,发生氧化还原反应,反应15h,反应结束后,得到含有四氢叶酸的溶液,用1mol/L盐酸溶液调节含有四氢叶酸的溶液的pH至3,析出四氢叶酸沉淀,将沉淀过滤后,利用真空干燥箱干燥8h,即得四氢叶酸。0.2 g of 10% Pd/C was added to a 50 mL reactor. After the reactor was replaced with nitrogen for 3 times, a folic acid solution with a pH of 7 was added to the reactor. After the reactor was replaced with hydrogen for 5 times, hydrogen was filled into the reactor. The pressure of the reactor was adjusted to 30 bar. The reactor was placed in an environment of 70° C. for oxidation-reduction reaction. The reaction was performed for 15 hours. After the reaction was completed, a solution containing tetrahydrofolic acid was obtained. The pH of the solution containing tetrahydrofolic acid was adjusted to 3 with a 1 mol/L hydrochloric acid solution to precipitate tetrahydrofolic acid. The precipitate was filtered and dried in a vacuum drying oven for 8 hours to obtain tetrahydrofolic acid.
用均三甲氧基苯作为内标,对四氢叶酸进行检测,测得四氢叶酸的产率为91%。Tetrahydrofolate was detected using mesitylene glycol as an internal standard, and the yield of tetrahydrofolate was found to be 91%.
实施例3Example 3
于30℃环境下,向100mL的三口烧瓶中加入1g固体叶酸,将烧瓶用氮气置换3次后,向烧瓶中加入10mL 0.2mol/LpH为7的NaH2PO4-Na2HPO4缓冲溶液,搅拌至均匀,得到混合溶液,用20%的NaOH溶液调节混合溶液的pH至7,得到叶酸溶液;At 30°C, 1 g of solid folic acid was added to a 100 mL three-necked flask. After the flask was replaced with nitrogen three times, 10 mL of a 0.2 mol/L NaH 2 PO 4 -Na 2 HPO 4 buffer solution with a pH of 7 was added to the flask, and the mixture was stirred until uniform to obtain a mixed solution. The pH of the mixed solution was adjusted to 7 with a 20% NaOH solution to obtain a folic acid solution.
向50mL的反应釜中加入0.1g10%Pd/C,将反应釜用氮气置换3次后,向反应釜中加入pH为7的叶酸溶液,将反应釜用氢气置换5次后,向反应釜中充入氢气,调反应釜压力至50bar,将反应釜置于80℃的环境下,发生氧化还原反应,反应15h,反应结束后,得到含有四氢叶酸的溶液,用1mol/L盐酸溶液调节含有四氢叶酸的溶液的pH至3.5,析出四氢叶酸沉淀,将沉淀过滤后,利用真空干燥箱干燥8h,即得四氢叶酸。0.1 g of 10% Pd/C was added to a 50 mL reactor. After the reactor was replaced with nitrogen for 3 times, a folic acid solution with a pH of 7 was added to the reactor. After the reactor was replaced with hydrogen for 5 times, hydrogen was filled into the reactor. The pressure of the reactor was adjusted to 50 bar. The reactor was placed in an environment of 80° C. for a redox reaction to occur for 15 hours. After the reaction was completed, a solution containing tetrahydrofolic acid was obtained. The pH of the solution containing tetrahydrofolic acid was adjusted to 3.5 with a 1 mol/L hydrochloric acid solution to precipitate tetrahydrofolic acid. The precipitate was filtered and dried in a vacuum drying oven for 8 hours to obtain tetrahydrofolic acid.
用均三甲氧基苯作为内标,对四氢叶酸进行检测,测得四氢叶酸的产率为91%。Tetrahydrofolate was detected using mesitylene glycol as an internal standard, and the yield of tetrahydrofolate was found to be 91%.
实施例4Example 4
其他步骤如实施例1,反应时间为24h,反应温度为80℃,改变叶酸溶液的pH进行实验,以验证反应pH对四氢叶酸产率的影响,其实验结果如图1所示。The other steps were the same as in Example 1, with a reaction time of 24 h and a reaction temperature of 80° C. The pH of the folic acid solution was changed to conduct experiments to verify the effect of the reaction pH on the yield of tetrahydrofolate. The experimental results are shown in FIG1 .
由图1可知,当pH选定为10时,四氢叶酸的产率只有23%,当pH选定为6时,四氢叶酸的产率为79%,而当pH选定为7时,四氢叶酸的产率达到了81%并达到了峰值,说明pH为7时,反应的产率最高。As shown in Figure 1, when the pH is selected as 10, the yield of tetrahydrofolate is only 23%, when the pH is selected as 6, the yield of tetrahydrofolate is 79%, and when the pH is selected as 7, the yield of tetrahydrofolate reaches 81% and reaches a peak value, indicating that the yield of the reaction is highest when the pH is 7.
实施例5Example 5
其他步骤如实施例1,改变反应的反应时间进行实验,以验证反应时间对四氢叶酸产率的影响,其实验结果如图2所示。The other steps were the same as in Example 1, and the reaction time was changed to conduct experiments to verify the effect of reaction time on the yield of tetrahydrofolate. The experimental results are shown in FIG2 .
由图2可知,当反应时间为6h时,四氢叶酸的产率只有79%,当反应时间为12h时,四氢叶酸的产率为85%,当反应时间为15h,四氢叶酸的产率达到90%并达到峰值,说明反应时间为15h,反应的产率最高。As shown in Figure 2, when the reaction time is 6 hours, the yield of tetrahydrofolate is only 79%, when the reaction time is 12 hours, the yield of tetrahydrofolate is 85%, and when the reaction time is 15 hours, the yield of tetrahydrofolate reaches 90% and reaches a peak value, indicating that the reaction yield is highest when the reaction time is 15 hours.
实施例6Example 6
其他步骤如实施例1,改变反应的反应温度进行实验,以验证反应温度对四氢叶酸产率的影响,其实验结果如图3所示。The other steps were the same as in Example 1, and the reaction temperature was changed to conduct experiments to verify the effect of reaction temperature on the yield of tetrahydrofolate. The experimental results are shown in FIG3 .
由图3可知,当反应温度为30℃时,四氢叶酸的产率只有10%,当反应温度为50时,四氢叶酸的产率只有79%,当反应温度为60℃,四氢叶酸的产率达到90%,当反应温度为70℃时,四氢叶酸的产率为92%并达到峰值,说明反应温度为70℃,反应的产率最高。As shown in Figure 3, when the reaction temperature is 30°C, the yield of tetrahydrofolic acid is only 10%, when the reaction temperature is 50, the yield of tetrahydrofolic acid is only 79%, when the reaction temperature is 60°C, the yield of tetrahydrofolic acid reaches 90%, and when the reaction temperature is 70°C, the yield of tetrahydrofolic acid is 92% and reaches a peak value, indicating that the reaction yield is highest when the reaction temperature is 70°C.
实施例4Example 4
其他步骤如实施例1,改变反应的催化剂Pd/C的用量进行实验,以验证反应催化剂Pd/C的用量对四氢叶酸产率的影响,其实验结果如图4所示。The other steps were the same as in Example 1, and the amount of the catalyst Pd/C was changed to conduct experiments to verify the effect of the amount of the catalyst Pd/C on the yield of tetrahydrofolate. The experimental results are shown in FIG4 .
由图4可知,当催化剂Pd/C的质量为叶酸质量的0.5%时,四氢叶酸的产率只有13%,提高催化剂的量,当催化剂Pd/C的质量大于叶酸质量的5%时,产率趋于稳定,反应产率>90%As shown in Figure 4, when the mass of catalyst Pd/C is 0.5% of the mass of folic acid, the yield of tetrahydrofolate is only 13%. When the amount of catalyst is increased, when the mass of catalyst Pd/C is greater than 5% of the mass of folic acid, the yield tends to be stable, and the reaction yield is >90%.
图5为产物四氢叶酸的核磁图,其结果如下:FIG5 is an NMR image of the product tetrahydrofolate, and the results are as follows:
1H NMR(400MHz,DMSO-d6)δ8.10(d,J=7.7Hz,1H),7.66(d,J=8.5Hz,2H),6.63(d,J=8.5Hz,2H),6.42(s,1H),6.18(s,1H),5.74(s,2H),4.35(ddd,J=9.7,7.6,4.9Hz,1H),3.36(d,J=11.3Hz,1H),3.13(s,3H),3.06–2.91(m,1H),2.33(t,J=7.5Hz,2H),2.05(ddd,J=12.9,9.4,5.3Hz,1H),1.93(ddd,J=13.8,9.6,6.9Hz,1H).. 1 H NMR (400 MHz, DMSO-d6) δ8.10 (d, J = 7.7 Hz, 1H), 7.66 (d, J = 8.5 Hz, 2H), 6.63 (d, J = 8.5 Hz, 2H), 6.42 (s, 1H), 6.18 (s, 1H), 5.74 (s, 2H), 4.35 (ddd, J = 9.7, 7.6, 4.9 Hz, 1H), 3.36 (d, J = 11.3 Hz, 1H), 3.13 (s, 3H), 3.06–2.91 (m, 1H), 2.33 (t, J = 7.5 Hz, 2H), 2.05 (ddd, J = 12.9, 9.4, 5.3 Hz, 1H), 1.93 (ddd, J = 13.8, 9.6, 6.9 Hz, 1H).
以上所述实施例仅表达了本发明的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对发明专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围。因此,本发明专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only express several implementation methods of the present invention, and the descriptions thereof are relatively specific and detailed, but they cannot be understood as limiting the scope of the invention patent. It should be pointed out that, for ordinary technicians in this field, several variations and improvements can be made without departing from the concept of the present invention, and these all belong to the protection scope of the present invention. Therefore, the protection scope of the patent of the present invention shall be subject to the attached claims.
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