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JPH0375560B2 - - Google Patents
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JPH0375560B2 - - Google Patents

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Publication number
JPH0375560B2
JPH0375560B2 JP4099983A JP4099983A JPH0375560B2 JP H0375560 B2 JPH0375560 B2 JP H0375560B2 JP 4099983 A JP4099983 A JP 4099983A JP 4099983 A JP4099983 A JP 4099983A JP H0375560 B2 JPH0375560 B2 JP H0375560B2
Authority
JP
Japan
Prior art keywords
guanosine
inosine
reaction
added
solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP4099983A
Other languages
Japanese (ja)
Other versions
JPS59167599A (en
Inventor
Masaaki Tsurushima
Koji Kokubu
Yoshitaka Uesugi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Takeda Pharmaceutical Co Ltd
Original Assignee
Takeda Chemical Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Takeda Chemical Industries Ltd filed Critical Takeda Chemical Industries Ltd
Priority to JP4099983A priority Critical patent/JPS59167599A/en
Publication of JPS59167599A publication Critical patent/JPS59167599A/en
Publication of JPH0375560B2 publication Critical patent/JPH0375560B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、ヌクレオシドを化学的にリン酸化し
て化学調味料として有用な5′−ヌクレオチドを工
業的に、かつ安価に製造する方法に関する。 さらに詳しくは、本発明は、イノシンおよびグ
アノシンを、その糖部分(リボース)の2′−およ
び3′−位の水酸基(2級水酸基)を保護すること
なく、5′−位の水酸基(1級水酸基)を直接リン
酸化するに際し、グアノシンとイノシンとの混晶
を用いるもので、その目的とするところは、グア
ノシン−5′−リン酸収率の向上と、グアノシン−
5′−ジリン酸、グアノシン−2′(3′),5′−二リン
酸等のグアノシン−ジホスフエート類の副生を抑
制することにある。 従来、5′−ヌクレオシドの製造法としては、リ
ボヌクレオシドを、そのリボフラノシル基の2′,
3′−位をアシル基あるいはアルキリデン基で保護
した後、各種の反応溶媒存在下で、種々のリン酸
化剤を用いて、諸種の条件でリン酸化し、次いで
保護基を加水分解して脱離し5′−リボヌクレオチ
ドとする方法が知られているが、このリン酸化方
法は、反応に多段階を要する、リン酸化剤の
使用量が多い、かならずしも収率が良好でない
などの欠点がある。 また、これらの欠点を解決するために、従来、
無保護のヌクレオシドを化学的にリン酸化する方
法として、特定の極性有機溶媒の存在下で、ヌク
レオシドとリン酸化剤を反応せしめる方法が知ら
れている。このようなリン酸化方法としては、(A)
ニトリル化合物を用いる方法(特公昭42−
20316)、(B)有機酸エステルを用いる方法(特公昭
42−21351)、(C)リン酸トリアルキルエステルを用
いる方法(Tetrahedron Letters No.50,
pp.5065,1967;Bulletin of the Chemical
Society of Japan Vol.42,3505(1969);特公昭
42−11071)、(D)リン酸トリ(アルコキシアルキ
ル)エステルを用いる方法(特開昭51−86482)、
(E)エチレングリコールジアルキルエーテルを用い
る方法(特公昭46−31865)、および(F)極性有機溶
媒と有機アミンまたは有機アミンの無機酸塩を用
いる方法(Bulletin of the Chemical Society
of Japan,Vol.48,2084(1975)などが知られて
いる。 しかし、これらの無保護リン酸化法をグアノシ
ンのリン酸化に適用した場合、目的とするグアノ
シン−5′−リン酸への転換率は、いずれの方法に
よつても高々約90%であり、イノシンの場合、そ
のイノシン−5′−リン酸への転換率が95%にも及
ぶことと対比するならば、工業的に満足すべきも
のではない。 また、グアノシン−5′−リン酸との分離が困難
なグアノシン−5′−二リン酸、グアノシン−
2′(3′),5′−二リン酸等のジホスフエート類が約
10%以上も副生するという欠点がある。 こうした状況のもとで、本発明者らは、従来の
無保護リン酸化法をグアノシンのリン酸化に適用
する場合に起こる上述の障害を克服して、工業的
に有利なグアノシン−5′−リン酸の製造法を確立
すべく広く検討した結果、グアノシンとイノシン
との混晶を原料として用いることにより、イノシ
ンだけでなくグアノシンもまた極めて高収率で
5′−モノホスフエートに導かれ、ジホスフエート
類の副生も著しく減少することを発見し、さらに
検討して本発明を完成したものである。 すなわち、本発明は、極性有機溶媒中、グアノ
シンとイノシンとの混晶にオキシハロゲン化リン
もしくはその水和物を作用させることを特徴とす
るグアノシン−5′−リン酸とイノシン−5′−リン
酸との混合物の製造法である。 本発明の製造法において、グアノシンとイノシ
ンとの混晶は、自体公知の方法で得られたものを
用いることができる。例えば、グアノシンおよび
イノシンを含む水溶液より通常溶質を析出させる
手段によつて晶出させて得た混晶が用いられる
(特公昭47−38199参照)。 この場合、晶出の方法としては、例えば冷却、
濃縮(水の除去)、種晶の添加、グアノシンおよ
びイノシンを溶解しない親水性溶媒(例えばアセ
トン)の添加、PH調整(グアノシンおよびイノシ
ンの溶解度が大きいPH3以下の酸性域あるいはPH
9以上のアルカリ性域からPH3〜9の範囲に調整
する)などおよびこれらの組合せの方法を適宜採
用できる。このような方法でグアノシンおよびイ
ノシンを含む溶液よりグアノシンとイノシンとの
混晶を析出させた後、吸引または加圧過、遠心
分離、遠心沈降等の通常用いられる方法で該混晶
を分離し、例えば減圧下に加熱乾燥する等により
水などの溶媒を除去し、次いでリン酸化反応に供
するのが望ましい。 この際、分離された湿結晶をアセトン、メチル
エチルケトンなどの親水性で、かつグアノシンお
よびイノシンを溶解しない溶媒で洗滌すると、低
温短時間で乾燥することができるので有利であ
る。 また乾燥された混晶を適宜粉砕してから篩過
し、例えば100メツシユ以下に整粒して反応に供
してもよい。 本発明の製造法を適用するにあたつてグアノシ
ンとイノシンとの混晶中のイノシン含量が低過ぎ
たり、また高過ぎる場合は、グアノシンの5′−モ
ノホスフエートへの転換率の向上とジホスフエー
ト類の副生抑制という本発明の効果を奏し難いこ
とがある。通常、イノシンのグアノシンに対する
割合が約0.1〜10(モル/モル)、好ましくは約0.2
〜4(モル/モル)の混晶を用いるのが有利であ
る。 混晶中のイノシンとグアノシンとの量比は、前
述の方法において晶出原液中のこれらの濃度比あ
るいは(および)晶出方法を適宜選ぶことによ
り、任意に調節することが可能である。 本発明の製造法で用いられる極性有機溶媒とし
ては、アセトニトリル、プロピオニトリル等のニ
トリル化合物、酢酸エチル、酢酸メチル、プロピ
オン酸メチル等の有機酸エステル類、リン酸トリ
メチル、リン酸トリエチル等のリン酸トリ低級ア
ルキルエステル類、リン酸トリ(メトキシエチ
ル)、リン酸トリ(エトキシエチル)等のリン酸
トリ(アルコキシアルキル)エステル類、エチレ
ングリコールジメチルエーテル、エチレングリコ
ールジエチルエーテル等のエチレングリコールジ
アルキルエーテル類、テトラヒドロフラン、1,
4−ジオキサン等の環状エーテル類、ジクロロメ
タン、クロロホルム、1,2−ジクロロエタン等
のハロゲン化炭化水素類、ニトロメタン、ニトロ
エタン、ニトロベンゼン等のニトロ化合物等が挙
げられる。 これらの極性有機溶媒は2種以上を混合して用
いてもよく、また、これら以外の有機溶媒でも例
えばベンゼン、トルエン等の芳香族炭化水素類、
エチルエーテル等のエーテル類のように反応に悪
影響を及ぼさないものであれば、これらの溶媒と
混合して用いることができる。 極性有機溶媒の使用量は、その種類により異な
るが、通常グアノシンおよびイノシンの量に対し
て約5〜約30倍量の範囲で適宜選択され、好まし
くは10〜20倍量程度である。 また、上記溶媒に、ピリジン、γ−ピコリン、
N,N−ジメチル−アニリン等の3級アミン類も
しくはその無機酸塩をグアノシンおよびイノシン
量に対し、約1〜5倍モル程度、適宜添加するこ
とにより、さらに反応促進、収率向上等の好まし
い効果をもたらすことが多い。 本発明の製造法で用いられるリン酸化剤は、オ
キシ塩化リン、オキシ臭化リン等のオキシハロゲ
ン化リンである。 オキシハロゲン化リンの使用量は通常、グアノ
シンおよびイノシンの約1〜5倍モル量、好まし
くは約1.5〜4倍モル量である。その使用量が少
な過ぎるとグアノシンおよびイノシンが未反応の
まま残り、また、過度の使用量ではジホスフエー
ト類の副生が増えると同時に目的とする5′−モノ
ホスフエートの収率が下がるので好ましくない。
通常、前記の使用範囲から、リン酸化剤あるいは
溶媒の種類等を考慮し適宜に選択される。 リン酸化に際し、オキシハロゲン化リンをその
まま反応に供するよりも、一旦、部分水和物とし
てから用いる方が、通常5′−モノホスフエート生
成への選択性が高く、2′または3′−モノホスフエ
ート、ジホスフエート類の副生量がすくなくなる
ので好ましい。 オキシハロゲン化リンの水和物を得る方法は、
オキシハロゲン化リンを上記反応溶媒に加えて溶
解してから、これに少量の水またはメタノール、
エタノール、三級ブタノール等のアルコール類、
もしくはギ酸、酢酸等の有機酸類を加えて反応さ
せればよく、生成した部分水和物は分離すること
なく、溶液として本発明のリン酸化反応に供され
る。この際の水またはアルコール類、もしくは有
機酸の添加量はオキシハロゲン化リンのグアノシ
ンとイノシンとの混晶に対する仕込割合によつて
異なるが、通常オキシハロゲン化リンに対して約
0.1〜0.7倍モル量であり、好ましくは0.3〜0.6倍
モル量である。 ただし、本発明の製造法で反応溶媒として用い
られる上記の極性有機溶媒類のうち、ニトリル
類、エチレングリコールジアルキルエーテル類、
環状エーテル類、ハロゲン化炭化水素類、もしく
はニトロ化合物を用い、これにピリジン、γ−ピ
コリン、N,N−ジメチルアニリン等の無機酸塩
を添加して反応に供するときは、オキシハロゲン
化リンは部分水和する必要はなく、そのまま反応
に使用しても、部分水和物を用いる場合と同様に
良好な効果が得られる。 本発明の製造法は、約10℃以下に冷却しなが
ら、前記反応溶媒にリン酸化剤を加え、これに所
定量の水(またはアルコール類もしくは有機酸)
を添加し、場合によつてはさらに、3級アミン
(またはその無機酸塩)を添加して溶解し、続い
てグアノシンとイノシンとの混晶を加え、撹拌、
冷却下に反応させることにより行われる。 反応温度は−30゜〜+50℃の範囲が実用的であ
り、中でも−10゜〜+30℃が特に好ましい。 この温度範囲において、反応時間は溶媒の種
類、促進剤添加の有無等によつて異なるが、一般
に30分〜10時間である。当反応方法においては、
グアノシンを単独にリン酸化する従来の方法に比
べ、反応は短時間で終了する。 このようにして得られた反応生成物を常法によ
り冷水と混合することによつて、未反応のリン酸
化剤および生成したヌクレオシドホスホハロゲネ
ートを加水分解し、グアノシン−5′−リン酸およ
びイノシン−5′−リン酸を含む溶液(加水分解
液)を得る。 このようにして得られたグアノシン−5′−ホス
フエートおよびイノシン−5′−ホスフエートを精
製する方法としては、例えば、 1 加水分解液のPHを水酸化ナトリウムで約1.5
に調整した後、活性炭で処理する方法、 2 反応溶媒を他の有機溶媒を用いて抽出分離し
た後、水酸化ナトリウムなどのアルカリで中和
してから、吸着樹脂処理あるいは晶析により精
製する方法、 3 反応溶媒を他の有機溶媒を用いて抽出分離し
た後、活性炭で処理する方法、 などが挙げられる。次いで、これらの精製方法の
いずれかを経た後、常法によりグアノシン−5′−
リン酸二ナトリウムとイノシン−5′−リン酸二ナ
トリウムとの混晶として取得することができる。
また必要ならば、例えば活性炭カラムを用いる分
別溶出法等により、グアノシン−5′−リン酸およ
びイノシン−5′−リン酸を分離した後、所望のア
ルカリ金属の塩としてそれぞれを純度の高い単一
物の結晶として取得することも可能である。これ
らの5′−ヌクレオチドまたはその混合物は呈味性
に富み、化学調味料として有用な物質である。 本発明の製造法を適用するこによりグアノシン
の5′−モノホスフエートへの転換率が向上し、ま
たジホスフエート類の副生量も大幅に下がるが、
この場合のイノシンの5′−モノホスフエートへの
転換率は、イノシンを単独に同条件でリン酸化し
た場合の転換率とほとんど変わらない。 以下、参考例および実施例を挙げて本発明をさ
らに具体的に説明する。 参考例 1 アセトニトリル100ml、ピリジン37.9gの溶液
に氷冷下オキシ塩化リン67.5gを滴下し、次に水
4.5gをゆつくり添加した。得られた混合液を0゜
〜2℃に保ち、撹拌しながらこれにグアノシン
28.3gを加えた。この温度で6時間連続撹拌し反
応した後、反応液を700gの氷水と混合した。こ
の水溶液を高速液体クロマトで分析し、第1表の
結果を得た。
The present invention relates to a method for industrially and inexpensively producing 5'-nucleotides useful as chemical seasonings by chemically phosphorylating nucleosides. More specifically, the present invention provides inosine and guanosine without protecting the 2'- and 3'-position hydroxyl groups (secondary hydroxyl groups) of the sugar moiety (ribose). A mixed crystal of guanosine and inosine is used for direct phosphorylation of guanosine-5'-phosphoric acid (hydroxyl group).
The objective is to suppress the by-product of guanosine diphosphates such as 5'-diphosphoric acid, guanosine-2'(3'), and 5'-diphosphoric acid. Conventionally, the method for producing 5'-nucleosides involves converting ribonucleosides into 2'-,
After protecting the 3'-position with an acyl group or alkylidene group, phosphorylation is performed using various phosphorylating agents in the presence of various reaction solvents under various conditions, and then the protecting group is hydrolyzed and removed. A method for producing 5'-ribonucleotides is known, but this phosphorylation method has drawbacks such as requiring multiple steps for the reaction, requiring a large amount of phosphorylating agent, and not necessarily providing a good yield. In addition, in order to solve these drawbacks, conventional
As a method for chemically phosphorylating unprotected nucleosides, a method is known in which a nucleoside is reacted with a phosphorylating agent in the presence of a specific polar organic solvent. Such phosphorylation methods include (A)
Method using nitrile compounds (Special Publication 1977-
20316), (B) method using organic acid ester (Tokukosho
42-21351), method using (C) phosphoric acid trialkyl ester (Tetrahedron Letters No. 50,
pp.5065, 1967; Bulletin of the Chemical
Society of Japan Vol.42, 3505 (1969); Tokko Akira
42-11071), (D) method using phosphoric acid tri(alkoxyalkyl) ester (Japanese Patent Application Laid-Open No. 51-86482),
(E) A method using ethylene glycol dialkyl ether (Japanese Patent Publication No. 46-31865), and (F) A method using a polar organic solvent and an organic amine or an inorganic acid salt of an organic amine (Bulletin of the Chemical Society
of Japan, Vol. 48, 2084 (1975). However, when these unprotected phosphorylation methods are applied to guanosine phosphorylation, the conversion rate to the desired guanosine-5'-phosphate is at most about 90%, and inosine In this case, the conversion rate to inosine-5'-phosphate is as high as 95%, which is not industrially satisfactory. In addition, guanosine-5'-diphosphate, which is difficult to separate from guanosine-5'-phosphate,
Diphosphates such as 2′(3′), 5′-diphosphoric acid
It has the disadvantage that more than 10% is produced as a by-product. Under these circumstances, the present inventors have overcome the above-mentioned obstacles that occur when applying the conventional unprotected phosphorylation method to guanosine phosphorylation, and have developed an industrially advantageous guanosine-5'-phosphorylation method. As a result of extensive research to establish a method for producing acid, we found that by using a mixed crystal of guanosine and inosine as a raw material, not only inosine but also guanosine could be produced at extremely high yields.
It was discovered that the by-product of diphosphates was also significantly reduced by 5'-monophosphate, and after further investigation, the present invention was completed. That is, the present invention provides guanosine-5'-phosphoric acid and inosine-5'-phosphoric acid, which is characterized in that phosphorus oxyhalide or its hydrate is reacted with a mixed crystal of guanosine and inosine in a polar organic solvent. This is a method for producing a mixture with an acid. In the production method of the present invention, a mixed crystal of guanosine and inosine obtained by a method known per se can be used. For example, a mixed crystal obtained by crystallizing an aqueous solution containing guanosine and inosine by a method of precipitating a solute is used (see Japanese Patent Publication No. 38199/1983). In this case, the crystallization method includes, for example, cooling,
Concentration (removal of water), addition of seed crystals, addition of hydrophilic solvents (e.g. acetone) that do not dissolve guanosine and inosine, pH adjustment (acidic range below PH3 where guanosine and inosine have high solubility, or pH
Adjustment to pH 3 to 9 from an alkaline range of 9 or more) and combinations thereof can be appropriately employed. After precipitating a mixed crystal of guanosine and inosine from a solution containing guanosine and inosine by such a method, the mixed crystal is separated by a commonly used method such as suction or pressurization, centrifugation, centrifugal sedimentation, etc. For example, it is desirable to remove the solvent such as water by heating and drying under reduced pressure, and then to subject it to the phosphorylation reaction. At this time, it is advantageous to wash the separated wet crystals with a hydrophilic solvent such as acetone or methyl ethyl ketone, which does not dissolve guanosine and inosine, since it can be dried at low temperatures and in a short time. Alternatively, the dried mixed crystal may be appropriately pulverized and then passed through a sieve, sized to, for example, 100 mesh or less, and subjected to the reaction. When applying the production method of the present invention, if the inosine content in the mixed crystal of guanosine and inosine is too low or too high, it is necessary to improve the conversion rate of guanosine to 5'-monophosphate and In some cases, it may be difficult to achieve the effect of the present invention of suppressing by-products such as. Usually, the ratio of inosine to guanosine is about 0.1 to 10 (mol/mol), preferably about 0.2
It is advantageous to use mixed crystals of ˜4 (mol/mol). The quantitative ratio of inosine and guanosine in the mixed crystal can be arbitrarily adjusted by appropriately selecting their concentration ratio in the crystallization stock solution and/or the crystallization method in the above-mentioned method. The polar organic solvents used in the production method of the present invention include nitrile compounds such as acetonitrile and propionitrile, organic acid esters such as ethyl acetate, methyl acetate, and methyl propionate, and phosphoric acid esters such as trimethyl phosphate and triethyl phosphate. Acid tri-lower alkyl esters, phosphoric acid tri(alkoxyalkyl) esters such as tri(methoxyethyl) phosphate and tri(ethoxyethyl) phosphate, ethylene glycol dialkyl ethers such as ethylene glycol dimethyl ether and ethylene glycol diethyl ether, Tetrahydrofuran, 1,
Examples include cyclic ethers such as 4-dioxane, halogenated hydrocarbons such as dichloromethane, chloroform, and 1,2-dichloroethane, and nitro compounds such as nitromethane, nitroethane, and nitrobenzene. These polar organic solvents may be used in combination of two or more, and organic solvents other than these may also be used, such as aromatic hydrocarbons such as benzene and toluene,
Any ether such as ethyl ether that does not adversely affect the reaction can be used in combination with these solvents. The amount of the polar organic solvent to be used varies depending on the type thereof, but is usually appropriately selected within the range of about 5 to about 30 times the amount of guanosine and inosine, preferably about 10 to 20 times. In addition, pyridine, γ-picoline,
By appropriately adding tertiary amines such as N,N-dimethyl-aniline or their inorganic acid salts in a molar amount of about 1 to 5 times the amount of guanosine and inosine, it is preferable to further accelerate the reaction and improve the yield. Often effective. The phosphorylating agent used in the production method of the present invention is a phosphorus oxyhalide such as phosphorus oxychloride and phosphorus oxybromide. The amount of phosphorus oxyhalide used is usually about 1 to 5 times the molar amount of guanosine and inosine, preferably about 1.5 to 4 times the molar amount. If the amount used is too small, guanosine and inosine will remain unreacted, and if it is used in an excessive amount, the by-product of diphosphates will increase and the yield of the desired 5'-monophosphate will decrease, which is undesirable. .
Usually, it is appropriately selected from the above-mentioned range of use, taking into consideration the type of phosphorylating agent or solvent. During phosphorylation, rather than subjecting phosphorus oxyhalide to the reaction as it is, it is usually better to use it as a partially hydrated product, which has higher selectivity for the formation of 5'-monophosphate, This is preferable because the amount of by-products of phosphates and diphosphates is reduced. The method for obtaining hydrated phosphorus oxyhalide is
After adding and dissolving the phosphorus oxyhalide in the above reaction solvent, add a small amount of water or methanol,
Alcohols such as ethanol and tertiary butanol,
Alternatively, an organic acid such as formic acid or acetic acid may be added to cause the reaction, and the resulting partial hydrate is subjected to the phosphorylation reaction of the present invention as a solution without being separated. The amount of water, alcohol, or organic acid added at this time varies depending on the ratio of phosphorus oxyhalide to the mixed crystal of guanosine and inosine, but usually approximately
It is 0.1 to 0.7 times the molar amount, preferably 0.3 to 0.6 times the molar amount. However, among the above polar organic solvents used as reaction solvents in the production method of the present invention, nitriles, ethylene glycol dialkyl ethers,
When using cyclic ethers, halogenated hydrocarbons, or nitro compounds and adding inorganic acid salts such as pyridine, γ-picoline, and N,N-dimethylaniline to the reaction, phosphorus oxyhalide is It is not necessary to partially hydrate it, and even if it is used as it is in the reaction, good effects can be obtained as in the case of using a partially hydrated product. In the production method of the present invention, a phosphorylating agent is added to the reaction solvent while cooling to about 10°C or less, and a predetermined amount of water (or alcohol or organic acid) is added to the reaction solvent.
and, if necessary, further add and dissolve a tertiary amine (or its inorganic acid salt), then add a mixed crystal of guanosine and inosine, stir,
The reaction is carried out under cooling. The reaction temperature is practically in the range of -30° to +50°C, with -10° to +30°C being particularly preferred. In this temperature range, the reaction time varies depending on the type of solvent, presence or absence of promoter addition, etc., but is generally 30 minutes to 10 hours. In this reaction method,
Compared to the conventional method of phosphorylating guanosine alone, the reaction completes in a shorter time. By mixing the reaction product thus obtained with cold water in a conventional manner, the unreacted phosphorylating agent and the generated nucleoside phosphohalogenate are hydrolyzed to produce guanosine-5'-phosphate and inosine. A solution (hydrolysis solution) containing -5'-phosphoric acid is obtained. As a method for purifying the guanosine-5'-phosphate and inosine-5'-phosphate obtained in this way, for example, 1. The pH of the hydrolyzed solution is adjusted to about 1.5 with sodium hydroxide.
2. A method in which the reaction solvent is extracted and separated using another organic solvent, neutralized with an alkali such as sodium hydroxide, and then purified by adsorption resin treatment or crystallization. 3. A method in which the reaction solvent is extracted and separated using another organic solvent and then treated with activated carbon. Next, after passing through any of these purification methods, guanosine-5′-
It can be obtained as a mixed crystal of disodium phosphate and inosine-5'-disodium phosphate.
If necessary, guanosine-5'-phosphate and inosine-5'-phosphate are separated by a fractional elution method using an activated carbon column, and then each is converted into a highly pure single salt of the desired alkali metal. It is also possible to obtain it as a crystal. These 5'-nucleotides or mixtures thereof have rich taste and are useful substances as chemical seasonings. By applying the production method of the present invention, the conversion rate of guanosine to 5'-monophosphate is improved, and the amount of diphosphate by-products is also significantly reduced.
The conversion rate of inosine to 5'-monophosphate in this case is almost the same as the conversion rate when inosine is phosphorylated alone under the same conditions. Hereinafter, the present invention will be explained in more detail with reference to Reference Examples and Examples. Reference example 1 67.5 g of phosphorus oxychloride was added dropwise to a solution of 100 ml of acetonitrile and 37.9 g of pyridine under ice cooling, and then water was added.
4.5g was added slowly. Keep the resulting mixture at 0° to 2°C and add guanosine to it while stirring.
Added 28.3g. After reacting with continuous stirring at this temperature for 6 hours, the reaction solution was mixed with 700 g of ice water. This aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 1 were obtained.

【表】 参考例 2 リン酸トリエチル300mlに氷冷下オキシ塩化リ
ン46.0gを加えて溶解し、続いて水1.8gをゆつ
くり添加した。得られた混合液を10℃に保ち、撹
拌しながらこれにグアノシン28.3gを加えた。こ
の温度で5時間連続して撹拌し反応した後、反応
液を500gの氷水と混合した。この水溶液を高速
液体クロマトで分析し、第2表の結果を得た。
[Table] Reference Example 2 46.0 g of phosphorus oxychloride was added and dissolved in 300 ml of triethyl phosphate under ice cooling, and then 1.8 g of water was slowly added. The resulting mixture was kept at 10° C. and 28.3 g of guanosine was added thereto while stirring. After reacting by stirring continuously at this temperature for 5 hours, the reaction solution was mixed with 500 g of ice water. This aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 2 were obtained.

【表】 参考例 3 アセトニトリル200ml、ピリジン75.1gの溶液
に氷冷下オキシ塩化リン67.5gを滴下し、次に水
8.9gをゆつくり添加した。得られた混合液を0゜
〜2℃に保ち、撹拌しながらこれにグアノシン
28.3g続いてイノシン26.3gを加えた。この温度
で6時間連続撹拌し反応した後、反応液を1.4Kg
の氷水と混合した。この水溶液を高速液体クロマ
トで分析し、第3表の結果を得た。
[Table] Reference Example 3 Add 67.5 g of phosphorus oxychloride dropwise to a solution of 200 ml of acetonitrile and 75.1 g of pyridine under ice cooling, then add water.
8.9g was slowly added. Keep the resulting mixture at 0° to 2°C and add guanosine to it while stirring.
28.3 g followed by 26.3 g of inosine were added. After continuously stirring and reacting at this temperature for 6 hours, 1.4Kg of the reaction solution was
of ice water. This aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 3 were obtained.

【表】 参考例 4 リン酸トリエチル700ml、オキシ塩化リン115.0
gの混液に氷冷下、水4.5gを滴下して加え、次
にこれにグアノシン28.3g、続いてイノシン40.2
gを加え5℃で6時間連続撹拌し反応させた。反
応液を1.2Kgの氷水と混合し、その水溶液を高速
液体クロマトで分析し、第4表の結果を得た。
[Table] Reference example 4 Triethyl phosphate 700ml, phosphorus oxychloride 115.0
4.5 g of water was added dropwise to the mixed solution of 1.5 g under ice cooling, then 28.3 g of guanosine was added, followed by 40.2 g of inosine.
g was added thereto, and the mixture was stirred continuously at 5° C. for 6 hours to react. The reaction solution was mixed with 1.2 kg of ice water, and the aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 4 were obtained.

【表】 実施例 1 アセトニトリル120ml、ピリジン46.7gの溶液
に氷冷下オキシ塩化リン83.0gを滴下し、次に水
5.5gをゆつくり添加した。得られた溶液を0〜
2℃に保ち、撹拌しながらこれにグアノシン28.3
gおよびイノシン6.2gを含む混晶を加えた。こ
の温度で5時間連続撹拌し反応させた後、反応液
を900mlの氷水と混合した。この水溶液を高速液
体クロマトで分析し、第5表の結果を得た。
[Table] Example 1 83.0 g of phosphorus oxychloride was added dropwise to a solution of 120 ml of acetonitrile and 46.7 g of pyridine under ice cooling, and then water was added.
5.5g was added slowly. The obtained solution is
Keep at 2℃ and add guanosine 28.3 to this while stirring.
g and a mixed crystal containing 6.2 g of inosine were added. After reacting with continuous stirring at this temperature for 5 hours, the reaction solution was mixed with 900 ml of ice water. This aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 5 were obtained.

【表】 実施例 2 ニトロメタン140mlにピリジン塩酸塩76.1gを
加え、これに氷冷下オキシ塩化リン52.5gを滴下
した。得られた溶液を2゜〜3℃に保ち、撹拌しな
がらこれにグアノシン28.3gおよびイノシン9.9
gを含む混晶を加えた。この温度で5時間連続し
て反応させた後、反応液を600gの氷水と混合し
た。この水溶液をエチルエーテルで抽出してニト
ロメタンを除き、抽残液を高速液体クロマトで分
析し、第6表の結果を得た。
[Table] Example 2 76.1 g of pyridine hydrochloride was added to 140 ml of nitromethane, and 52.5 g of phosphorus oxychloride was added dropwise thereto under ice cooling. The resulting solution was maintained at 2° to 3°C, and 28.3 g of guanosine and 9.9 g of inosine were added to it while stirring.
A mixed crystal containing g was added. After continuously reacting at this temperature for 5 hours, the reaction solution was mixed with 600 g of ice water. This aqueous solution was extracted with ethyl ether to remove nitromethane, and the raffinate was analyzed by high performance liquid chromatography to obtain the results shown in Table 6.

【表】 実施例 3 ジクロルメタン200ml、γ−ピコリン44.2gの
混液に氷冷下オキシ塩化リン133.6gを滴下し、
次にメタノール15.2gをゆつくり添加した。得ら
れた溶液を2゜〜3℃に保ち、撹拌しながらこれに
グアノシン28.3gおよびイノシン26.3gを含む混
晶を加えた。この温度で5時間連続撹拌し反応さ
せた後、反応液を1400gの氷水と混合した。得ら
れた液のジクロルメタン層と水層を分液し、水層
を高速液体クロマトで分析し、第7表の結果を得
た。
[Table] Example 3 133.6 g of phosphorus oxychloride was added dropwise to a mixture of 200 ml of dichloromethane and 44.2 g of γ-picoline under ice cooling.
Next, 15.2 g of methanol was slowly added. The resulting solution was maintained at 2 DEG to 3 DEG C., and a mixed crystal containing 28.3 g of guanosine and 26.3 g of inosine was added thereto while stirring. After reacting by continuously stirring at this temperature for 5 hours, the reaction solution was mixed with 1400 g of ice water. The obtained liquid was separated into a dichloromethane layer and an aqueous layer, and the aqueous layer was analyzed by high performance liquid chromatography, and the results shown in Table 7 were obtained.

【表】 実施例 4 アセトニトリル320ml、N,N−ジメチルアニ
リン91.8gの混液に氷冷下オキシ塩化リン213.2
gを滴下し、次にギ酸29.1gをゆつくり添加し
た。得られた溶液を2゜〜3℃に保ち、撹拌しなが
らこれにグアノシン28.3gおよびイノシン57.9g
を含む混晶を加えた。この温度で4時間連続撹拌
し反応させた後、反応液を2.2Kgの氷水と混合し
た。この水溶液を高速液体クロマトで分析し、第
8表の結果を得た。
[Table] Example 4 Add 213.2 g of phosphorus oxychloride to a mixture of 320 ml of acetonitrile and 91.8 g of N,N-dimethylaniline under ice cooling.
g was added dropwise, and then 29.1 g of formic acid was slowly added. The resulting solution was maintained at 2° to 3°C, and 28.3 g of guanosine and 57.9 g of inosine were added to it while stirring.
Added mixed crystals containing. After reacting by continuously stirring at this temperature for 4 hours, the reaction solution was mixed with 2.2 kg of ice water. This aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 8 were obtained.

【表】 実施例 5 リン酸トリエチル400ml、オキシ塩化リン59.7
gの混液に氷冷下、水2.3gを滴下して加え、次
にこれにグアノシン28.3gおよびイノシン8.0g
を含む混晶を加え10℃で4時間連続撹拌し反応さ
せた。反応液を600gの氷水と混合し、その水溶
液を高速液体クロマトで分析し、第9表の結果を
得た。
[Table] Example 5 Triethyl phosphate 400ml, phosphorus oxychloride 59.7
2.3g of water was added dropwise to the mixed solution of
A mixed crystal containing . The reaction solution was mixed with 600 g of ice water, and the aqueous solution was analyzed by high performance liquid chromatography to obtain the results shown in Table 9.

【表】 実施例 6 リン酸トリメチル500ml、オキシ塩化リン82.9
gの混液に氷冷下、水3.2gを滴下して加え、次
にこれにグアノシン28.3gおよびイノシン21.5g
を含む混晶を加え10℃で3時間連続撹拌し反応さ
せた。反応液を900gの氷水と混合し、その水溶
液を高速液体クロマトで分析し、第10表の結果を
得た。 この水溶液を1,2−ジクロルエタンで抽出し
てリン酸トリメチルを除き、抽残液を炭末塔に通
してグアノシン−5′−リン酸等のヌクレオチドを
吸着させ、よく水洗し、次に2%水酸化ナトリウ
ム水溶液で溶出した。溶出液を塩酸でPH8.5に調
整してから減圧下に水を留去し、濃縮液を熱時脱
色過した後メタノールを添加して晶析し、グア
ノシン−5′−リン酸二ナトリウムおよびイノシン
−5′−リン酸二ナトリウムの混晶(含水塩、純度
98%)を得た。
[Table] Example 6 Trimethyl phosphate 500ml, phosphorus oxychloride 82.9
3.2g of water was added dropwise to the mixed solution of
A mixed crystal containing . The reaction solution was mixed with 900 g of ice water, and the aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 10 were obtained. This aqueous solution was extracted with 1,2-dichloroethane to remove trimethyl phosphate, and the raffinate was passed through a charcoal tower to adsorb nucleotides such as guanosine-5'-phosphate, thoroughly washed with water, and then 2% It was eluted with an aqueous sodium hydroxide solution. The eluate was adjusted to pH 8.5 with hydrochloric acid, water was distilled off under reduced pressure, and the concentrated solution was decolorized and filtered under heat, and then methanol was added to crystallize it to obtain disodium guanosine-5'-phosphate and Mixed crystal of inosine-5'-disodium phosphate (hydrated salt, purity
98%).

【表】 実施例 7 リン酸トリエチル700ml、オキシ塩化リン115.0
gの混液に氷冷下、水4.5gを滴下して加え、次
にこれにグアノシン28.3gおよびイノシン40.2g
を含む混晶を加え5℃で6時間連続撹拌し反応さ
せた。反応液を1.2Kgの氷水と混合し、その水溶
液を高速液体クロマトで分析し、第11表の結果を
得た。 この水溶液をトルエンで抽出してリン酸トリエ
チルを除き、抽残液を炭末塔に通してグアノシン
−5′−二リン酸等のヌクレオチドを吸着させ、よ
く水洗し、次に1.5%塩化アンモニウム水溶液に
アンモニア水を加えてPH10.0にした液を通してイ
ノシン−5′−リン酸を溶出(第1溶出)させ、続
いて2%水酸化ナトリウム水溶液を通してグアノ
シン−5′−リン酸等を溶出(第2溶出)させた。
第1溶出液に水酸化ナトリウムを加えて濃縮し、
放冷晶析してイノシン−5′−リン酸二ナトリウム
の結晶(8水塩、純度99%)を得た。
[Table] Example 7 Triethyl phosphate 700ml, phosphorus oxychloride 115.0
4.5 g of water was added dropwise to the mixture of g under ice cooling, and then 28.3 g of guanosine and 40.2 g of inosine were added to the mixture.
A mixed crystal containing . The reaction solution was mixed with 1.2 kg of ice water, and the aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 11 were obtained. This aqueous solution is extracted with toluene to remove triethyl phosphate, and the raffinate is passed through a charcoal tower to adsorb nucleotides such as guanosine-5'-diphosphate, washed thoroughly with water, and then 1.5% ammonium chloride aqueous solution Inosine-5'-phosphoric acid is eluted through a solution adjusted to pH 10.0 by adding ammonia water (first elution), and then guanosine-5'-phosphoric acid etc. are eluted through a 2% aqueous sodium hydroxide solution (first elution). 2 elution).
Add sodium hydroxide to the first eluate and concentrate,
Crystallization was performed while cooling to obtain crystals of inosine-5'-disodium phosphate (octahydrate, purity 99%).

【表】 また、第2溶出液を塩酸でPH8.5に調整してか
ら濃縮し、放冷晶析して、グアノシン−5′−リン
酸二ナトリウムの結晶(7水塩、純度98%)を得
た。 実施例 8 リン酸トリメチル1.1、オキシ塩化リン184.9
gの混液に氷冷下、水7.2gを滴下して加え、次
にこれにグアノシン28.3gおよびイノシン81.0g
を含む混晶を加え5℃で4時間連続撹拌し反応さ
せた。反応液を2Kgの氷水と混合し、その水溶液
を高速液体クロマトで分析し、第12表の結果を得
た。
[Table] In addition, the second eluate was adjusted to pH 8.5 with hydrochloric acid, concentrated, and crystallized while standing to cool to give crystals of guanosine-5'-disodium phosphate (heptahydrate, purity 98%). I got it. Example 8 Trimethyl phosphate 1.1, phosphorus oxychloride 184.9
7.2 g of water was added dropwise to the mixed solution of g under ice cooling, and then 28.3 g of guanosine and 81.0 g of inosine were added to the mixture.
A mixed crystal containing . The reaction solution was mixed with 2 kg of ice water, and the aqueous solution was analyzed by high performance liquid chromatography, and the results shown in Table 12 were obtained.

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 極性有機溶媒中、グアノシンとイノシンとの
混晶にオキシハロゲン化リンもしくはその水和物
を作用させることを特徴とするグアノシン−5′−
リン酸とイノシン−5′−リン酸との混合物の製造
法。
1. Guanosine-5′-, which is characterized by reacting phosphorus oxyhalide or its hydrate with a mixed crystal of guanosine and inosine in a polar organic solvent.
A method for producing a mixture of phosphoric acid and inosine-5'-phosphoric acid.
JP4099983A 1983-03-11 1983-03-11 Chemical phosphatization of inosine and guanosine Granted JPS59167599A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4099983A JPS59167599A (en) 1983-03-11 1983-03-11 Chemical phosphatization of inosine and guanosine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4099983A JPS59167599A (en) 1983-03-11 1983-03-11 Chemical phosphatization of inosine and guanosine

Publications (2)

Publication Number Publication Date
JPS59167599A JPS59167599A (en) 1984-09-21
JPH0375560B2 true JPH0375560B2 (en) 1991-12-02

Family

ID=12596113

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4099983A Granted JPS59167599A (en) 1983-03-11 1983-03-11 Chemical phosphatization of inosine and guanosine

Country Status (1)

Country Link
JP (1) JPS59167599A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW279165B (en) * 1992-07-08 1996-06-21 Takeda Pharm Industry Co Ltd

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JPS59167599A (en) 1984-09-21

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