CN111995512B - Full racemization plant alcohol composition and preparation method and application thereof - Google Patents

Full racemization plant alcohol composition and preparation method and application thereof Download PDF

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CN111995512B
CN111995512B CN202010386025.5A CN202010386025A CN111995512B CN 111995512 B CN111995512 B CN 111995512B CN 202010386025 A CN202010386025 A CN 202010386025A CN 111995512 B CN111995512 B CN 111995512B
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CN111995512A (en
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易仕旭
何永耀
江伟
叶观浩
李彦霖
唐佳宾
高炳坤
罗杰
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Sichuan Haisco Pharmaceutical Co Ltd
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    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C50/00Quinones
    • C07C50/10Quinones the quinoid structure being part of a condensed ring system containing two rings
    • C07C50/14Quinones the quinoid structure being part of a condensed ring system containing two rings with unsaturation outside the ring system, e.g. vitamin K1
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    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
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    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/09Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis
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    • C07C33/02Acyclic alcohols with carbon-to-carbon double bonds
    • C07C33/025Acyclic alcohols with carbon-to-carbon double bonds with only one double bond
    • C07C33/03Acyclic alcohols with carbon-to-carbon double bonds with only one double bond in beta-position, e.g. allyl alcohol, methallyl alcohol
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    • C07C50/00Quinones
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    • C07C50/20Quinones the quinoid structure being part of a condensed ring system containing three rings with unsaturation outside the ring system
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    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/10Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with ester groups or with a carbon-halogen bond
    • C07C67/11Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with ester groups or with a carbon-halogen bond being mineral ester groups
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    • C07C2602/04One of the condensed rings being a six-membered aromatic ring
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Abstract

The invention provides a full racemization plant alcohol composition with high E type configuration content, a preparation method thereof and application thereof in preparing vitamin K 1 The composition comprises all-racemized plant alcohol with Z-type and E-type configurations, wherein Z/(Z+E) is less than or equal to 15%; the preparation method takes isophytol as a raw material, and the whole racemization phytol composition with high E-type configuration content is obtained through the steps of halogenation, esterification, de-esterification and the like.

Description

Full racemization plant alcohol composition and preparation method and application thereof
Technical Field
The invention provides a composition, a preparation method and application thereof, and in particular relates to a full racemization plant alcohol composition, a preparation method thereof and application thereof in preparing vitamin K 1 Belongs to the fields of organic chemistry and pharmacy.
Background
Vitamin K 1 Naturally occurring in a variety of plants, its naturally occurring form has the chemical name 2-methyl-3- [ (2E, 7R, 11R) -3,7,11, 15-tetramethylhexadec-2-en-1-yl]-1, 4-naphthoquinone with chemical structural formula as shown in formula I-1.
Vitamin K 1 Is a fat-soluble vitamin medicine, and has important functions in blood coagulation, energy metabolism and body tissue movement of human body. Vitamin K 1 Can be used for treating vitamin K 1 Bleeding caused by deficiency, such as bleeding caused by obstructive jaundice, biliary fistula, chronic diarrhea, etc., hypoproteinemia caused by coumarin, sodium salicylate, etc., neonatal hemorrhage, and vitamin K in vivo caused by long-term application of broad-spectrum antibiotics 1 Lack of. Vitamin K 1 It also has analgesic and bronchospasm relieving effects, and can be used for treating visceral smooth muscle angina, biliary tract spasm, and colic caused by intestinal spasm. Thus, vitamin K 1 The importance in the medical and health care fields is increasingly highlighted.
Vitamin K 1 The side chain structure has a double bond at the 2 position and two chiral centers at the 7 and 11 positions. Studies have shown that cis-trans (Z/E) isomerism of the side chain 2-position double bond affects vitamin K 1 Is of the E-type structureA shape; chiral configuration of side chain 7 and 11 positions for vitamin K 1 Has no influence on the activity of (2E, 7R, 11R), (2E, 7S, 11S), (2E, 7R, 11S) and (2E, 7S, 11R) of vitamin K 1 Is equivalent in activity. Thus, in the multinational formulary, only vitamin K is treated 1 The content of Z-type isomer in the preparation is controlled, such as vitamin K only in Chinese pharmacopoeia (2015 edition), united states pharmacopoeia (USP 41 edition), european pharmacopoeia (EP 9.0 edition), etc 1 The Z-type isomer content in the extract is not more than 21.0%, namely the vitamin K which accords with the medicinal standard in the early stage 1 May be present in the form of a composition as shown in formula I:
vitamin K 1 The 7 and 11 positions of the side chain contain two chiral centers, and are brought in by the side chain raw material. Early preparation of vitamin K 1 The side chain raw material of (2) is natural plant alcohol extracted from plants, and the 7 position and the 11 position of the side chain raw material are both R configuration. With the development of organic synthesis chemistry and the enhancement of environmental awareness, the side chain raw materials synthesized artificially replace the side chain raw materials extracted naturally. For example, in the latest United states pharmacopoeia of 2019 (USP 42) and European pharmacopoeia (EP 9.6), in which vitamin K is published 1 The structure of (C) is changed into vitamin K with side chain of formula II' being racemized 1 Namely, the full racemization vitamin K shown in the formula II 1 Comprising 4 forms with side chains in the (2E, 7R, 11R), (2E, 7S, 11S), (2E, 7R, 11S) and (2E, 7S, 11R) configurations.
In addition, to further promote the full racemization of vitamin K 1 In EP9.6, the Z isomer content is also reduced from the original "no more than 21.0%" to "no more than 15.0%"; and the specific rotation is controlled to be-0.05 degrees to minus 0.05 degrees. I.e. the upgraded version of the pharmaceutical vitamin K1 may be present in the form of a composition as shown in formula II:
thus, the side chain of industrialized development is artificially synthesized, full racemization and contains vitamin K with high E configuration content 1 (i.e., vitamin K represented by formula II) 1 Composition) will be a necessary trend.
Development of all-racemic vitamin K 1 The key to (a) is the choice of side chain starting materials. At present, the full racemization vitamin K is prepared 1 The side chain raw material of (a) is generally selected from artificially synthesized isophytol (CAS number: 505-32-8, chemical structural formula is shown as formula III), and the total racemization vitamin K is prepared by rearrangement of isophytol double bond and condensation with main ring 1 . For example, the following synthetic routes are disclosed in the literature, "organic communications.2003,33 (5): 763-772," et al:
however, according to the prior art, Z-isomer content is difficult to control when the isophytol double bond is rearranged to be lower than 15.0%, and the prior art does not provide further reduction of subsequent intermediates or products of vitamin K 1 A method for preparing the Z-type isomer content. Therefore, developing an artificially synthesized side chain raw material meeting specific requirements can effectively promote the full racemization of vitamin K 1 Is an industrial development of (a).
In order to overcome the defects in the prior art, the invention aims at the full racemization vitamin K 1 The side bond raw material and the preparation method thereof are researched, and on the basis of a large number of experimental researches, a novel full-racemization plant alcohol composition with high E-type configuration content is surprisingly developed, and the full-racemization plant alcohol composition not only can be directly used for preparing full-racemization vitamin K with high E-type configuration content 1 In addition, the preparation method of the full racemization plant alcohol composition is simple and convenient, the operation is easy to realize, the raw materials are easy to obtain, and the full racemization plant alcohol composition is suitable for industrial application.
Disclosure of Invention
One of the objects of the present invention is to provide a high E configurationThe full racemization plant alcohol composition with the content can be directly used for preparing full racemization vitamin K with high E configuration content 1 In addition, the preparation method of the full racemization plant alcohol is simple and convenient, the operation is easy to realize, the raw materials are easy to obtain, and the full racemization plant alcohol is suitable for industrial application.
The invention also aims to provide a preparation method of the full racemization plant alcohol with high E-type configuration content.
It is still another object of the present invention to provide a process for preparing full racemic vitamin K with high E-type configuration content using the full racemic plant alcohol with high E-type configuration content as described above 1 Is a method of (2).
In order to achieve the above purpose, the present invention adopts the following technical scheme:
in one aspect, the present invention provides a full racemic plant alcohol composition of formula VII having a high E-configuration content, the composition comprising a full racemic plant alcohol of formula VII-1 and a full racemic plant alcohol of formula VII-2, wherein the content of the full racemic plant alcohol of formula Z is not more than 15% relative to the total content of the full racemic plant alcohols of formula Z and E.
In the structural formula VII, a wave bond connected with a double bond represents that the bond can form an E-type configuration of the double bond or a Z-type configuration of the double bond; the expression "Z/(Z+E). Ltoreq.15%" means that the content of Z-type full racemic plant alcohol (represented by formula VII-2) in the composition is not more than 15% relative to the total content of Z-type (represented by formula VII-2) and E-type full racemic plant alcohol (represented by formula VII-1).
In one embodiment, the present invention provides a full racemic phytol composition with high E-configuration content selected from the group consisting of:
a full racemic plant alcohol composition comprising an E full racemic plant alcohol represented by formula VII-1 and a Z full racemic plant alcohol represented by formula VII-2, wherein the content of Z full racemic plant alcohol is not more than 12% relative to the total content of Z and E full racemic plant alcohols; or alternatively, the first and second heat exchangers may be,
a full racemic plant alcohol composition comprising an E full racemic plant alcohol represented by formula VII-1 and a Z full racemic plant alcohol represented by formula VII-2, wherein the content of Z full racemic plant alcohol is not more than 10% relative to the total content of Z full racemic plant alcohol and E full racemic plant alcohol; or alternatively, the first and second heat exchangers may be,
a full racemic plant alcohol composition comprising an E full racemic plant alcohol represented by formula VII-1 and a Z full racemic plant alcohol represented by formula VII-2, wherein the content of Z full racemic plant alcohol is not more than 8% relative to the total content of Z full racemic plant alcohol and E full racemic plant alcohol; or alternatively, the first and second heat exchangers may be,
a full racemic plant alcohol composition comprising an E full racemic plant alcohol represented by formula VII-1 and a Z full racemic plant alcohol represented by formula VII-2, wherein the content of Z full racemic plant alcohol is not more than 5% relative to the total content of Z full racemic plant alcohol and E full racemic plant alcohol.
The term "all-racemic plant alcohol" refers to an equal mixture of plant alcohols having R-type or S-type configuration in which the configurations of the two chiral centers at positions 7 and 11 are independent, respectively, that is, equal mixtures of four plant alcohols of (7R, 11R), (7S, 11S), (7R, 11S) and (7S, 11R). The three-dimensional configuration can be judged according to the synthetic raw materials and the synthetic method of the full racemization plant alcohol; one of the characteristics is that the specific rotation is-0.1 degree to-0.1 degree, preferably-0.05 degree to-0.05 degree, more preferably 0 degree, and the specific rotation test conditions and methods can be carried out according to the conventional methods in the art.
The 'E-type full racemization plant alcohol' refers to full racemization plant alcohol with 2-position double bond as E-type, and is shown as a formula VII-1.
The Z-type full racemization plant alcohol refers to full racemization plant alcohol with a Z-type double bond at a 2-position, and is shown as a formula VII-2.
The "all-racemic plant alcohol composition" may contain other impurities in addition to the E-type all-racemic plant alcohol and the Z-type all-racemic plant alcohol. The "impurities" refer to organic impurities, inorganic impurities, residual solvents, etc. associated with the full racemic plant alcohol composition or the preparation process thereof.
The expression "the content of Z-type full-racemized plant alcohol relative to the total content of Z-type and E-type full-racemized plant alcohols" means that Z-type full-racemized plants are contained in the compositionThe percentage of alcohol in total of Z-type and E-type full racemization plant alcohol can be rounded, and the obtained calculation result can be processed by rounding, and the characterization can be carried out in a conventional manner in the field. In one embodiment, the relative content is calculated by dividing the area of the Z-type full racemic plant alcohol peak by the sum of the areas of the Z-type and E-type full racemic plant alcohol peaks as measured by Gas Chromatography (GC) or Liquid Chromatography (LC), and then performing percent conversion and rounding; the selection of GC or LC chromatographic conditions can be made according to conventional techniques in the art. In another embodiment, nuclear magnetic resonance hydrogen spectrum is used 1 H NMR) dividing the characteristic hydrogen peak area of the Z-type full racemic plant alcohol by the sum of the characteristic hydrogen peak areas of the Z-type full racemic plant alcohol and the E-type full racemic plant alcohol, and performing percentage conversion and rounding treatment to calculate the relative content.
The characterization methods of the wave bond, Z/(Z+E) and the relative content in the structural formula can be correspondingly understood by referring to the above description unless otherwise specified.
In another aspect, according to the object of the present invention, there is provided a process for preparing the above all-racemic phytol composition, comprising: the isophytol is subjected to halogenation, esterification and de-esterification. The method specifically comprises the following steps:
(1) Carrying out halogenation reaction on isophytol shown in a formula III and a halogenating reagent to convert the isophytol into a composition shown in a formula V,
(2) Esterifying the composition shown in formula V with an esterifying reagent to obtain a composition shown in formula VIII,
(3) The composition shown in the formula VIII is subjected to hydrolysis or alcoholysis de-esterification reaction in the presence of alkali, and is separated to obtain the full racemization plant alcohol composition shown in the formula VII,
in the composition represented by the formula V, X is a halogen atom selected from fluorine, chlorine, bromine and iodine.
In the composition shown in the formula VIII, R is hydrogen, alkyl or substituted alkyl. The alkyl is selected from alkyl, alkenyl, alkyne, aryl and the like; the substituent of the substituted hydrocarbon group is selected from halogen, cyano, nitro, aryl, alkoxy, acyloxy, alkylthio, alkylamino, acyl and the like. Wherein R is preferably hydrogen or an alkanyl radical such as methyl, ethyl, propyl, phenyl, etc.
In the above process step (1), the isophytol is commercially available or prepared according to the prior art.
In the above method step (1), the halogenating reagent comprises phosphorus trichloride, phosphorus tribromide, hydrochloric acid, hydrobromic acid, hydroiodic acid, thionyl chloride, thionyl bromide, phosphorus oxychloride, phosphorus tribromide and the like, wherein phosphorus tribromide and phosphorus trichloride are preferred.
In the above method step (1), the solvent may be omitted or a suitable solvent may be added. Suitable solvents may be selected from ethers (such as diethyl ether, propyl ether, diisopropyl ether, methyl tert-butyl ether, methyl tetrahydrofuran, etc.), halogenated hydrocarbons (such as methylene chloride, chloroform, 1, 2-dichloroethane, etc.), alkanes (such as n-hexane, n-heptane, isooctane, etc.), aromatic hydrocarbons (such as toluene, benzene, xylene, etc.), etc. Among them, ethers such as diisopropyl ether, methyl tert-butyl ether, methyl tetrahydrofuran are preferable.
In the above method step (1), a phase transfer catalyst selected from tetrabutylammonium bromide (chloride, iodide), tetramethylammonium bromide (chloride, iodide), tetrapropylammonium bromide (chloride, iodide), tetraethylammonium bromide (chloride, iodide), dodecyltrimethylammonium bromide (chloride, iodide) and the like may be added.
In the above method step (1), the reaction monitoring and the post-treatment may be carried out in a manner conventional in the art.
In the above method step (2), the esterifying reagent is selected from the group consisting of salts of alkali metals or alkaline earth metals corresponding to formic acid, hydrocarbyl or substituted hydrocarbyl carboxylic acids, such as sodium formate, potassium formate, sodium acetate, potassium acetate, magnesium acetate, sodium benzoate, potassium benzoate, sodium trifluoroacetate, potassium trifluoroacetate, and the like.
In the above method step (2), the reaction solvent is preferably an aprotic polar solvent such as N, N-dimethylformamide, N-dimethylacetamide, dimethylsulfoxide, acetonitrile or the like.
In the above method step (2), a phase transfer catalyst selected from tetrabutylammonium bromide (chloride, iodide), tetramethylammonium bromide (chloride, iodide), tetrapropylammonium bromide (chloride, iodide), tetraethylammonium bromide (chloride, iodide), dodecyltrimethylammonium bromide (chloride, iodide) and the like may be added.
In the above method step (2), the reaction monitoring and post-treatment may be performed in a conventional manner in the art, or may be directly used for the next reaction after the reaction is completed.
In the above method step (3), the base comprises an organic base or an inorganic base, and may be selected from triethylamine, sodium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate, potassium carbonate, and the like.
In the above method step (3), the alcohol used for the alcoholysis may be selected from methanol, ethanol, n-propanol, isopropanol, etc.
In the above method step (3), the reaction monitoring and the post-treatment may be performed in a conventional manner in the art.
In the above method step (3), the separation may include further purification, and the purification method includes column chromatography, distillation, and the like. In one embodiment, further purification is performed by column chromatography, the packing is silica gel, and the eluent is n-hexane or a mixed solvent of n-heptane and ethyl acetate or methyl tert-butyl ether.
In still another aspect, the present invention provides a method for preparing a full racemic vitamin K with high E-type configuration content shown in formula II from the full racemic plant alcohol composition with high E-type configuration content shown in formula VII 1 The method comprises the following steps:
(i) Converting the full racemic phytol composition of formula VII into a composition of formula IX in the presence of a chlorinating or brominating agent,
(ii) Reacting the composition of formula IX with a compound of formula IV in the presence of a base to produce a composition of formula VI,
(iii) Decyclopentadiene of the composition of formula VI is removed to obtain the composition of formula II.
In the above method step (i), the chlorinating agent is selected from phosphorus trichloride, hydrochloric acid, thionyl chloride, phosphorus oxychloride and the like, wherein phosphorus trichloride and hydrochloric acid are preferable; the brominating reagent is selected from phosphorus tribromide, hydrobromic acid, dibromosulfoxide, phosphorus tribromide and the like, wherein phosphorus tribromide and hydrobromic acid are preferred.
In the above method step (i), the reaction solvent may be selected from ethers (such as diethyl ether, propyl ether, diisopropyl ether, methyl tert-butyl ether, methyl tetrahydrofuran, etc.), halogenated hydrocarbons (such as methylene chloride, chloroform, 1, 2-dichloroethane, etc.), alkanes (such as n-hexane, n-heptane, isooctane, etc.), aromatic hydrocarbons (such as toluene, benzene, xylene, etc.), etc.
In the above process step (i), the reaction monitoring and the post-treatment may be carried out in a manner conventional in the art.
In the above method step (ii), the compound of formula IV is commercially available or prepared as described in literature, "organic.communications.2003,33 (5): 763-772 et al.
In the above method step (ii), the base is selected from the group consisting of potassium tert-butoxide, sodium tert-butoxide, potassium isopropoxide, sodium amide and the like.
In the above method step (ii), the reaction solvent may be selected from ethers (e.g., tetrahydrofuran, methyltetrahydrofuran, diethyl ether, propyl ether, diisopropyl ether, methyl tert-butyl ether, etc.), alkanes (e.g., n-hexane, n-heptane, isooctane, etc.), aromatics (e.g., toluene, benzene, xylene, etc.), alcohols (e.g., methanol, ethanol, propanol, isopropanol, tert-butanol, etc.), etc.
In the above process step (ii), the reaction monitoring and the working-up can be carried out in a manner customary in the art.
In the above method step (iii), the said dicyclopentadiene removal is a retro Diels-Alder reaction, and the method is generally heating, the heating temperature is generally higher than 50 ℃, preferably higher than 70 ℃.
In the above process step (iii), the dicyclopentadiene may be removed in the absence of solvent, in the composition shown in directly heated VI; or in a solvent selected from n-heptane, isooctane, acetic acid, acetonitrile, chloroform, tetrachloromethane, toluene, benzene, xylene, ethanol, etc.
In the above process step (iii), the reaction monitoring and the post-treatment may be carried out in a manner conventional in the art.
In the above method step (iii), the resulting composition of formula II may be further purified by methods conventional in the art, such as column chromatography, distillation, and the like.
In one embodiment, the present invention provides a process for preparing full racemic vitamin K with high E-type configurational content 1 (composition of formula II) the following intermediate composition:
compared with the prior art, the full racemization plant alcohol composition with high E type configuration content prepared by the specific synthesis method has the following advantages:
(1) Provides a full racemization plant alcohol composition which is not provided by the prior art, and can efficiently prepare vitamin K with higher quality 1
(2) The preparation method of the full racemization plant alcohol composition is simple and convenient, the operation is easy to realize, the raw materials are easy to obtain, and the full racemization plant alcohol composition is suitable for industrial application.
Drawings
FIG. 1 is a hydrogen spectrum of a full racemic phytol composition of formula VII according to example 1 of the present invention;
FIG. 2 shows the preparation of example 5 of the invention of full-racemic vitamin K of formula II with a high E-type conformational content 1 Hydrogen profile of the composition;
FIG. 3 is a gas chromatogram of the full racemic phytol composition of formula VII of example 4 of the present invention.
Detailed Description
The invention will be further described in connection with test examples and examples which will enable those skilled in the art to more fully understand the invention, but without limiting the invention in any way.
EXAMPLE 1 preparation of full racemic phytol composition with high E-type configuration content (formula VII)
(1) Preparation of the composition of formula V-a
Dissolving isophytol (formula III) 5kg in methyl tertiary butyl ether 18kg, stirring and cooling to below-10deg.C, and dropwise adding solution prepared from phosphorus tribromide 2.28kg and methyl tertiary butyl ether 2kg at below 0deg.C; after the dripping is finished, continuously controlling the temperature to be below 0 ℃ for reaction; after TLC monitoring reaction is finished, dropwise adding 1kg of water at the temperature below 0 ℃; after the dripping, standing and separating, washing the obtained organic phase with water until the pH value is=5-6, drying with anhydrous sodium sulfate, filtering, concentrating to obtain a composition shown as a formula V-a, and directly using the composition for the next reaction.
(2) Preparation of the composition of formula VIII-a
Adding the composition shown in the formula V-a obtained above, 268g of tetrabutylammonium bromide and 1.80kg of potassium acetate into 6kg of N, N-dimethylformamide, and stirring and reacting at 50-60 ℃; TLC monitors the end of the reaction to obtain a mixed solution of the composition shown in VIII-a, which is directly used for the next reaction.
(3) Preparation of full racemic plant alcohol composition represented by formula VII
Adding 14kg of methanol and 5kg of anhydrous potassium carbonate into the mixed solution of the composition shown in the formula VIII-a, heating, refluxing and stirring for reaction; after TLC monitoring reaction is finished, filtering a reaction solution, and concentrating filtrate under reduced pressure to obtain a concentrate; adding methyl tertiary butyl ether and water into the concentrate for extraction, and collecting an organic phase; washing the organic phase with saturated sodium chloride aqueous solution, and concentrating under reduced pressure; subjecting the concentrate to silica gel column chromatography, eluting with n-heptane/ethyl acetate (10/1, v/v); collecting target fraction, and concentrating under reduced pressure to obtain full racemization plant alcohol composition shown in formula VII.
1 H NMR(400MHz,CDCl 3 ) δ:5.410 (t, 1H), 4.160-4.142 (d, 2H), 1.990 (t, 2H), 1.736-1.734 (s, 0.4H) and 1.669 (s, 2.6H), 1.541-1.508 (m, 1H), 1.410-1.352 (m, 4H), 1.297-1.251 (m, 8H), 1.232-1.049 (m, 6H), 0.875-0.836 (m, 12H). The method comprises 1 In the H NMR results, the signal peaks at chemical shifts 1.736-1.734 (s, 0.40H) and 1.669 (s, 2.68H) were assigned to 3H's on the double bond-linked methyl groups (labeled "position" in the above structure) in the Z-and E-type full racemic plant alcohols, respectively, and from the integrated areas of the two signal peaks, Z/(z+e) was calculated to be 13% in the sample.
Specific rotation: 0 deg..
EXAMPLE 2 preparation of full racemic phytol composition with high E-type configuration content (formula VII)
(1) Preparation of the composition of formula V-b
Mixing 0.5kg of isophytol (formula III), 3.5kg of concentrated hydrochloric acid and 20g of tetramethyl ammonium chloride, and stirring at a temperature of between 10 and 20 ℃ for reaction; after TLC monitoring reaction is finished, n-heptane is added for extraction; the organic phase was washed with water to ph=5-6, dried over anhydrous sodium sulfate, filtered, and concentrated to give a composition of formula V-b, which was directly used in the next reaction.
(2) Preparation of the composition of formula VIII-b
Adding the composition shown in the formula V-b, 30g of tetramethyl ammonium chloride and 344g of sodium formate into 5kg of acetonitrile, and stirring and reacting at 50-60 ℃; TLC monitoring reaction is finished, and filtering is carried out; the obtained filtrate is concentrated under reduced pressure to obtain the composition shown in VIII-b, which is directly used for the next reaction.
(3) Preparation of full racemic plant alcohol composition represented by formula VII
Mixing the composition shown in the formula VIII-b with 4kg of water and 135g of sodium hydroxide, and stirring and reacting at the temperature of 40-50 ℃; after TLC monitoring reaction is finished, filtering a reaction solution, and concentrating filtrate under reduced pressure; subjecting the concentrate to silica gel column chromatography, eluting with n-hexane/methyl tert-butyl ether (15/1, v/v); collecting target fraction, and concentrating under reduced pressure to obtain full racemization plant alcohol composition shown in formula VII.
GC:Z/(Z+E)=15%;
Specific rotation: 0 deg..
EXAMPLE 3 preparation of full racemic phytol composition with high E-type configuration content (formula VII)
(1) Preparation of the composition of formula V-a
Dissolving isophytol (formula III) 5kg in methyl tertiary butyl ether 18kg, stirring and cooling to below-10deg.C, and dropwise adding solution prepared from phosphorus tribromide 2.28kg and methyl tertiary butyl ether 2kg at below 0deg.C; after the dripping is finished, continuously controlling the temperature to be below 0 ℃ for reaction; after TLC monitoring reaction is finished, dropwise adding 1kg of water at the temperature below 0 ℃; after the dripping, standing and separating, washing the obtained organic phase by saturated sodium bicarbonate aqueous solution until the pH of the obtained aqueous phase is=5-6, drying the obtained organic phase by anhydrous sodium sulfate, filtering and concentrating to obtain the composition shown in the formula V-a, and directly using the composition in the next reaction.
(2) Preparation of the composition of formula VIII-a
Adding the composition shown in the formula V-a obtained above, 268g of tetrabutylammonium bromide and 1.80kg of potassium acetate into 6kg of N, N-dimethylformamide, and stirring and reacting at 20-30 ℃; TLC monitors the end of the reaction to obtain a mixed solution of the composition shown in VIII-a, which is directly used for the next reaction.
(3) Preparation of full racemic plant alcohol composition represented by formula VII
Adding 14kg of methanol and 5kg of anhydrous potassium carbonate into the mixed solution of the composition shown in the formula VIII-a, heating, refluxing and stirring for reaction; after TLC monitoring reaction is finished, filtering a reaction solution, and concentrating filtrate under reduced pressure to obtain a concentrate; adding methyl tertiary butyl ether and water into the concentrate for extraction, and collecting an organic phase; washing the organic phase with saturated sodium chloride aqueous solution, and concentrating under reduced pressure; the resulting concentrate was split in two parts:
subjecting the first concentrate to silica gel column chromatography, eluting with n-heptane/ethyl acetate (20/1, v/v); collecting target fraction, and concentrating under reduced pressure to obtain full racemization plant alcohol composition shown in formula VII. GC: z/(z+e) =8.7%, specific rotation: 0 deg..
Subjecting the second concentrate to silica gel column chromatography, eluting with n-heptane/ethyl acetate (20/1, 10:1, v/v); collecting target fraction, and concentrating under reduced pressure to obtain full racemization plant alcohol composition shown in formula VII.
GC:Z/(Z+E)=6.9%;
Specific rotation: 0 deg..
EXAMPLE 4 preparation of full racemic phytol composition with high E-type configuration content (formula VII)
(1) Preparation of the composition of formula V-a
2.5kg of isophytol (formula III) is dissolved in 9kg of methyl tertiary butyl ether, stirred and cooled to below-10 ℃, and solution prepared from 1.14kg of phosphorus tribromide and 1kg of methyl tertiary butyl ether is dropwise added at the temperature below 0 ℃; after the dripping is finished, continuously controlling the temperature to be below 0 ℃ for reaction; after TLC monitoring reaction, dropwise adding 0.5kg of water at the temperature below 0 ℃; after the dropping, standing and separating, washing the obtained organic phase with water until the pH of the water phase is=6-7, drying the obtained organic phase with anhydrous sodium sulfate, filtering and concentrating to obtain the composition shown in the formula V-a, and directly using the composition for the next reaction.
(2) Preparation of the composition of formula VIII-a
Adding the composition shown in the formula V-a obtained above, 134g of tetrabutylammonium bromide and 0.90kg of potassium acetate into 3kg of N, N-dimethylformamide, and stirring and reacting at 30-40 ℃; TLC monitors the end of the reaction to obtain a mixed solution of the composition shown in VIII-a, which is directly used for the next reaction.
(3) Preparation of full racemic plant alcohol composition represented by formula VII
Adding 7kg of methanol and 2.5kg of anhydrous potassium carbonate into the mixed solution of the composition shown in the formula VIII-a, heating, refluxing and stirring for reaction; after TLC monitoring reaction is finished, filtering a reaction solution, and concentrating filtrate under reduced pressure to obtain a concentrate; adding methyl tertiary butyl ether and water into the concentrate for extraction, and collecting an organic phase; washing the organic phase with saturated sodium chloride aqueous solution, and concentrating under reduced pressure; subjecting the concentrate to silica gel column chromatography, eluting with n-heptane/ethyl acetate (20/1, 10:1,5:1, v/v); collecting target fraction, and concentrating under reduced pressure to obtain full racemization plant alcohol composition shown in formula VII.
GC: z/(z+e) =1.1%, and the GC detection pattern is shown in fig. 3.
The results of the GC test are shown in the following table:
peak number Retention time (min) Peak width (min) Peak area Peak height Percent peak area (%)
1 18.852 0.0779 39.99957 7.00097 1.05757
2 19.460 0.1070 3721.21802 579.52155 98.38721
3 21.244 0.0589 20.99978 5.31842 0.55522
In the table, peak 1 is Z-configuration full-racemized plant alcohol, peak 2 is E-configuration full-racemized plant alcohol, and Z/(Z+E) =1.1% can be calculated from the peak area percentages of the two.
EXAMPLE 5 high E-configuration content full racemic vitamin K 1 (composition of formula II)
(1) Preparation of the composition of formula IX-a
1.24kg of the full racemic plant alcohol composition (formula VII, prepared according to example 1) was dissolved in 8.0kg of methyl tert-butyl ether, and the mixture was stirred and cooled to below-10℃and a solution of 0.57kg of phosphorus tribromide and 0.4kg of methyl tert-butyl ether was added dropwise at a temperature below 0 ℃. After the dripping is finished, continuously controlling the temperature to be below 0 ℃ for reaction; after TLC monitoring reaction, dropwise adding 0.4kg of water at the temperature below 0 ℃; after the dripping, standing and separating, washing the obtained organic phase with water until the pH value is=5-6, drying with anhydrous sodium sulfate, filtering and concentrating to obtain the composition shown in the formula IX-a, and directly using the composition in the next reaction.
(2) Preparation of the composition of formula VI
Under the protection of nitrogen, 8.0kg of tetrahydrofuran and 0.47kg of potassium tert-butoxide are mixed, stirred and cooled to below-3 ℃, and 1.0kg of a compound of formula IV dissolved in 3.0kg of tetrahydrofuran is added dropwise; after the dripping, stirring continuously for about 0.5 hour, and then dripping the composition shown in the formula IX-a obtained in the last step below the temperature of minus 3 ℃ into 2.0kg of solution of tetrahydrofuran; after the dripping, the temperature is controlled to be between 5 ℃ below zero and 5 ℃ for continuous reaction. After TLC monitoring reaction, controlling the temperature below 10 ℃ and adjusting the pH value to be between 5 and 6 by using 2mol/L hydrochloric acid; concentrating under reduced pressure, extracting the concentrated solution with methyl tert-butyl ether 15.0kg, and separating; the obtained organic phase is washed by saturated sodium chloride aqueous solution, dried by anhydrous sodium sulfate, filtered and concentrated under reduced pressure to obtain the composition shown in the formula VI, and the composition is directly used for the next reaction.
(3) Full racemization vitamin K shown in formula II 1 Is prepared from
Under the protection of nitrogen, the composition shown in the formula VI obtained in the previous step is dissolved in 5.0kg of acetic acid, stirred and heated to 90-100 ℃ for reaction in the absence of light; after TLC monitoring reaction, concentrating under reduced pressure to obtain full racemization vitamin K shown in formula II 1
HPLC:Z/(Z+E)=12%;
1 H NMR(400MHz,CDCl 3 ) δ:8.084-8.055 (m, 2H), 7.684-7.662 (m, 2H), 5.011-5.008 (t, 1H), 3.377-3.359 (d, 2H), 2.188 (s, 3H), 1.945-1.926 (t, 2H), 1.778-1.679 (s, 3H), 1.515-1.498 (m, 1H), 1.375-1.285 (m, 5H), 1.264-1.183 (m, 7H), 1.151-1.111 (m, 2H), 1.065-1.009 (m, 4H), 0.887-0.806 (m, 12H). Specific rotation: 0 deg..

Claims (2)

1. A process for preparing a full racemic phytol composition of formula VII comprising:
(1) Carrying out halogenation reaction on isophytol shown in a formula III and a halogenating reagent to convert the isophytol into a composition shown in a formula V,
(2) The composition shown in the formula V is subjected to esterification reaction with an esterification reagent to be converted into a composition shown in the formula VIII,
(3) The composition shown in the formula VIII is subjected to hydrolysis or alcoholysis de-esterification reaction in the presence of alkali, and is separated to obtain the full racemization plant alcohol composition shown in the formula VII,
the formula VII comprises a Z-type configuration and an E-type configuration, wherein Z/(Z+E) is less than or equal to 15%; the E-type and Z-type configurations are respectively shown as formulas VII-1 and VII-2:
x in the composition shown in the formula V is selected from fluorine, chlorine, bromine and iodine; r in the composition shown in the formula VIII is selected from methyl, ethyl, propyl or phenyl; in the step (1), the halogenating reagent is selected from phosphorus trichloride, phosphorus tribromide, hydrochloric acid, hydrobromic acid, hydroiodic acid, thionyl chloride, dibromosulfoxide, phosphorus oxychloride or phosphorus oxybromide; in step (2), the esterifying reagent is selected from sodium formate, potassium formate, sodium acetate, potassium acetate, magnesium acetate, sodium benzoate, or potassium benzoate; in step (3), the base is selected from triethylamine, sodium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate or potassium carbonate, the alcohol used for the alcoholysis is selected from methanol, ethanol, n-propanol or isopropanol, and the separation comprises further purification, and the purification method comprises column chromatography and distillation.
2. Preparation of all-racemic vitamin represented by formula II from all-racemic phytol composition prepared by the preparation method of claim 1K 1 Comprising:
(i) Converting the full racemic phytol composition of formula VII into a composition of formula IX in the presence of a chlorinating or brominating agent,
(ii) Reacting the composition of formula IX with a compound of formula IV in the presence of a base to produce a composition of formula VI,
(iii) Removing cyclopentadiene from the composition shown in the formula VI to obtain a composition shown in the formula II,
wherein in step (i), the chlorinating agent is selected from phosphorus trichloride, hydrochloric acid, thionyl chloride or phosphorus oxychloride; the brominating reagent is selected from phosphorus tribromide, hydrobromic acid, dibromosulfoxide or phosphorus tribromide; in step (ii), the base is selected from potassium tert-butoxide, sodium tert-butoxide, potassium isopropoxide, sodium isopropoxide or sodium amide;
the full racemization plant alcohol composition shown in the formula VII is prepared by the following steps:
(1) Carrying out halogenation reaction on isophytol shown in a formula III and a halogenating reagent to convert the isophytol into a composition shown in a formula V,
(2) The composition shown in the formula V is subjected to esterification reaction with an esterification reagent to be converted into a composition shown in the formula VIII,
(3) The composition shown in the formula VIII is subjected to hydrolysis or alcoholysis de-esterification reaction in the presence of alkali, and is separated to obtain the full racemization plant alcohol composition shown in the formula VII,
the formula VII comprises a Z-type configuration and an E-type configuration, wherein Z/(Z+E) is less than or equal to 15%; the E-type and Z-type configurations are respectively shown as formulas VII-1 and VII-2:
x in the composition shown in the formula V is selected from fluorine, chlorine, bromine and iodine; r in the composition shown in the formula VIII is selected from methyl, ethyl, propyl or phenyl; in the step (1), the halogenating reagent is selected from phosphorus trichloride, phosphorus tribromide, hydrochloric acid, hydrobromic acid, hydroiodic acid, thionyl chloride, dibromosulfoxide, phosphorus oxychloride or phosphorus oxybromide; in step (2), the esterifying reagent is selected from sodium formate, potassium formate, sodium acetate, potassium acetate, magnesium acetate, sodium benzoate, or potassium benzoate; in step (3), the base is selected from triethylamine, sodium hydroxide, potassium hydroxide, lithium hydroxide, sodium carbonate or potassium carbonate, the alcohol used for the alcoholysis is selected from methanol, ethanol, n-propanol or isopropanol, and the separation comprises further purification, and the purification method comprises column chromatography and distillation.
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