JPS6241520B2 - - Google Patents
Info
- Publication number
- JPS6241520B2 JPS6241520B2 JP6582579A JP6582579A JPS6241520B2 JP S6241520 B2 JPS6241520 B2 JP S6241520B2 JP 6582579 A JP6582579 A JP 6582579A JP 6582579 A JP6582579 A JP 6582579A JP S6241520 B2 JPS6241520 B2 JP S6241520B2
- Authority
- JP
- Japan
- Prior art keywords
- estrone
- tetrahydrofuran
- water
- crude
- present
- 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
Links
- DNXHEGUUPJUMQT-UHFFFAOYSA-N (+)-estrone Natural products OC1=CC=C2C3CCC(C)(C(CC4)=O)C4C3CCC2=C1 DNXHEGUUPJUMQT-UHFFFAOYSA-N 0.000 claims description 50
- DNXHEGUUPJUMQT-CBZIJGRNSA-N Estrone Chemical compound OC1=CC=C2[C@H]3CC[C@](C)(C(CC4)=O)[C@@H]4[C@@H]3CCC2=C1 DNXHEGUUPJUMQT-CBZIJGRNSA-N 0.000 claims description 50
- 229960003399 estrone Drugs 0.000 claims description 50
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 46
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 15
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 4
- 239000012141 concentrate Substances 0.000 claims 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 12
- 239000002904 solvent Substances 0.000 description 8
- 239000013078 crystal Substances 0.000 description 7
- 239000000243 solution Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- QPUYECUOLPXSFR-UHFFFAOYSA-N 1-methylnaphthalene Chemical compound C1=CC=C2C(C)=CC=CC2=C1 QPUYECUOLPXSFR-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 229930195733 hydrocarbon Natural products 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 3
- 150000001340 alkali metals Chemical class 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 238000004817 gas chromatography Methods 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N tetralin Chemical compound C1=CC=C2CCCCC2=C1 CXWXQJXEFPUFDZ-UHFFFAOYSA-N 0.000 description 3
- 239000008096 xylene Substances 0.000 description 3
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- 235000002597 Solanum melongena Nutrition 0.000 description 2
- DHKHKXVYLBGOIT-UHFFFAOYSA-N acetaldehyde Diethyl Acetal Natural products CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 description 2
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- -1 methyl alkali metal Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- ZYURHZPYMFLWSH-UHFFFAOYSA-N octacosane Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCCCCC ZYURHZPYMFLWSH-UHFFFAOYSA-N 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- FWRJQALYSMXXLH-MVWRLGRASA-N (8r,9s,13s,14s)-3-hydroxy-2,13-dimethyl-7,8,9,11,12,14,15,16-octahydro-6h-cyclopenta[a]phenanthren-17-one Chemical compound C([C@@H]12)C[C@]3(C)C(=O)CC[C@H]3[C@@H]1CCC1=C2C=C(C)C(O)=C1 FWRJQALYSMXXLH-MVWRLGRASA-N 0.000 description 1
- VOXZDWNPVJITMN-ZBRFXRBCSA-N 17β-estradiol Chemical compound OC1=CC=C2[C@H]3CC[C@](C)([C@H](CC4)O)[C@@H]4[C@@H]3CCC2=C1 VOXZDWNPVJITMN-ZBRFXRBCSA-N 0.000 description 1
- AIBFRTWVQFOKIS-DRMAHVMPSA-N 3-Hydroxy-1-methylestra-1,3,5(10)-trien-17-one Chemical compound C([C@]1(C)C(=O)CC[C@H]1[C@@H]1CC2)C[C@@H]1C1=C2C=C(O)C=C1C AIBFRTWVQFOKIS-DRMAHVMPSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 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 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 238000011276 addition treatment Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- CZZYITDELCSZES-UHFFFAOYSA-N diphenylmethane Chemical compound C=1C=CC=CC=1CC1=CC=CC=C1 CZZYITDELCSZES-UHFFFAOYSA-N 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229960005309 estradiol Drugs 0.000 description 1
- 229930182833 estradiol Natural products 0.000 description 1
- 229940011871 estrogen Drugs 0.000 description 1
- 239000000262 estrogen Substances 0.000 description 1
- OSVMTWJCGUFAOD-KZQROQTASA-N formestane Chemical compound O=C1CC[C@]2(C)[C@H]3CC[C@](C)(C(CC4)=O)[C@@H]4[C@@H]3CCC2=C1O OSVMTWJCGUFAOD-KZQROQTASA-N 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000003054 hormonal effect Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- VIKNJXKGJWUCNN-XGXHKTLJSA-N norethisterone Chemical compound O=C1CC[C@@H]2[C@H]3CC[C@](C)([C@](CC4)(O)C#C)[C@@H]4[C@@H]3CCC2=C1 VIKNJXKGJWUCNN-XGXHKTLJSA-N 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
Landscapes
- Steroid Compounds (AREA)
Description
【発明の詳細な説明】
本発明は、エストロンの精製法に関する。さら
に詳しくは、本発明は、粗エストロンに含まれる
不純物、例えば、1−メチルエストロン、2−メ
チルエストロン、4−メチルエストロン、seco−
エストロン等を除去してエストロンを精製する方
法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying estrone. More specifically, the present invention deals with impurities contained in crude estrone, such as 1-methylestrone, 2-methylestrone, 4-methylestrone, seco-
The present invention relates to a method for purifying estrone by removing estrone and the like.
エストロンは、それ自体エストロゲンとして使
用される他、エストラジオール及びその誘導体、
19−ノルエチステロン等のホルモン活性を有する
医薬品の製造原料として重要であり、高品質のも
のが要求される。例えば、米国の国民医薬品集
(The National Formulary)(通称NF)第14巻の
記載によれば、エストロンについては、純度は
97.0〜103.0%、色は、白ないし乳白色、不純物
は、3%以下であることが要求される。 Estrone is used as an estrogen itself, as well as estradiol and its derivatives,
It is important as a raw material for manufacturing pharmaceuticals with hormonal activity such as 19-norethisterone, and high quality is required. For example, according to Volume 14 of the US National Formulary (commonly known as NF), the purity of estrone is
It is required that the content is 97.0 to 103.0%, the color is white to milky white, and the content of impurities is 3% or less.
従来、粗エストロンは、テトラヒドロフラン、
アルコール等のエストロンを比較的よく溶解する
溶剤に溶解して、不溶物を除去した後、再結晶等
により精製されているが、現在工業的に用いられ
ている比較的安価な溶剤の中で、エストロンを最
もよく溶解するテトラヒドロフランでさえも、30
℃に於て100gのテトラヒドロフランに5.1gのエ
ストロンが溶けるだけである。従つて、エストロ
ンの工業的精製に於て、加熱装置を装備していな
い過装置により粗エストロンを過して不溶物
を除く場合には、上記のエストロンの溶解度によ
り用いるテトラヒドロフランの必要最少量が定ま
り、一バツチの仕込量に上限が生じる。 Conventionally, crude estrone is obtained from tetrahydrofuran,
Estrone is dissolved in a solvent such as alcohol that dissolves it relatively well, and after removing insoluble matter, it is purified by recrystallization, etc. Among the relatively inexpensive solvents currently used industrially, Even tetrahydrofuran, which dissolves estrone best, has 30
Only 5.1 g of estrone dissolves in 100 g of tetrahydrofuran at ℃. Therefore, in industrial purification of estrone, when crude estrone is passed through a filtration device not equipped with a heating device to remove insoluble matter, the minimum amount of tetrahydrofuran required is determined by the solubility of estrone mentioned above. , there is an upper limit to the amount of preparation per batch.
本発明者らは、以上のような事情に鑑み、通常
の装置を用いてエストロン精製の仕込量を増加で
きるような方法を鋭意検討した結果、従来の約2
倍の仕込量が得られる本発明に到達した。 In view of the above circumstances, the inventors of the present invention have conducted intensive studies on a method that can increase the amount of estrone refining using ordinary equipment, and have found that the amount of estrone refining can be increased by approximately 2
We have arrived at the present invention, which allows twice the amount of preparation.
本発明の要旨は、粗エストロンを2〜14重量%
の水を含むテトラヒドロフランに溶解し、不溶物
が残存する場合にはこれを過後、得られた溶液
を芳香族炭化水素の存在下又は非存在下濃縮する
か、或いは、該溶液を濃縮後芳香族炭化水素で処
理して、エストロンを晶析させ、固体のエストロ
ンを分離する方法に存する。 The gist of the present invention is to contain 2 to 14% by weight of crude estrone.
If insoluble matter remains, it is dissolved in tetrahydrofuran containing water, and after filtration, the resulting solution is concentrated in the presence or absence of aromatic hydrocarbons, or after concentrating the solution, aromatic hydrocarbons are dissolved. The present invention consists in a method of crystallizing estrone by treatment with a hydrocarbon and separating solid estrone.
次に、本発明を更に詳細に説明する。 Next, the present invention will be explained in more detail.
本発明方法で精製の対象となるエストロンの製
造方法は、特に制限されないが、例えば、アンド
ロスタ−1・4・6−ジエン−3・17−ジオン
(以下ADDと略称する)を熱分解する方法(特開
昭51−26865号公報及び特開昭52−48655号公報参
照)、アルカリ金属を用いてADDから製造する方
法(特公昭42−1226号公報参照)等で得られた粗
エストロンを使用することができる。 The method for producing estrone, which is the target of purification in the method of the present invention, is not particularly limited, but for example, a method of thermally decomposing androsta-1,4,6-diene-3,17-dione (hereinafter abbreviated as ADD) (Refer to JP-A-51-26865 and JP-A-52-48655), using crude estrone obtained by the method of producing from ADD using an alkali metal (Refer to JP-A-42-1226), etc. can do.
熱分解法によれば、ADDの炭化水素(トルエ
ン、キシレン等)溶液または懸濁液を、予め加熱
された炭化水素(燈油、軽油等)と混合した後、
ADDを450〜700℃で熱分解すると、エストロン
が得られる。 According to the pyrolysis method, after mixing a hydrocarbon (toluene, xylene, etc.) solution or suspension of ADD with a preheated hydrocarbon (kerosene, diesel oil, etc.),
Pyrolysis of ADD at 450-700°C yields estrone.
なお、本方法で得られたエストロンは、過時
洗浄が不十分な時には反応に使用した灯油等の炭
化水素を含むことがあるが、本発明方法の適用の
障害となるものではない。 Note that the estrone obtained by this method may contain hydrocarbons such as kerosene used in the reaction when the temporary washing is insufficient, but this does not impede the application of the method of the present invention.
アルカリ金属を使用する方法によれば、ADD
の17−エチレンアセタールを、テトラヒドロフラ
ン等のエーテル性溶媒中で、ジフエニルメタン、
メチルナフタレン等をメチルアルカリ金属のスカ
ベンジヤーとして共存させ、1−メチルナフタレ
ン、ビフエニルのような多環状芳香族化合物及び
リチウム、ナトリウムのようなアルカリ金属と処
理して得られるエストロンの17−エチレンアセタ
ールを加水分解するとエストロンが得られる。 According to the method of using alkali metals, ADD
17-ethylene acetal was dissolved in diphenylmethane,
The 17-ethylene acetal of estrone obtained by coexisting methylnaphthalene etc. as a methyl alkali metal scavenger and treating it with polycyclic aromatic compounds such as 1-methylnaphthalene and biphenyl and alkali metals such as lithium and sodium is Hydrolysis yields estrone.
本発明方法によれば、粗エストロンを2〜14重
量%の水を含むテトラヒドロフラン中に溶かし、
不溶物が存在する場合には、これを過して除い
た後、芳香族炭化水素の存在下又は非存在下で濃
縮によりテトラヒドロフランと水を留去してエス
トロンを晶析させるか、あるいは、濃縮後芳香族
炭化水素を添加処理して晶析するエストロンを含
む固体エストロンを過する。 According to the method of the present invention, crude estrone is dissolved in tetrahydrofuran containing 2 to 14% by weight of water;
If insoluble matter is present, after removing it by filtration, tetrahydrofuran and water are distilled off by concentration in the presence or absence of aromatic hydrocarbons to crystallize estrone, or estrone is crystallized by concentration. After the addition treatment of aromatic hydrocarbons, the solid estrone containing estrone to be crystallized is filtered.
粗エストロンを溶解するのに使用される溶媒と
しては、2〜14重量%の水を含むテトラヒドロフ
ランが選ばれるが、好ましくは、5〜11重量%の
含水テトラヒドロフラン、更に好ましくは、8〜
9重量%の含水テトラヒドロフランが選ばれる。
これらの溶媒の使用量は温度にもよるが、粗エス
トロン1gに対して5〜15ml程度が扱いやすい。 As the solvent used to dissolve the crude estrone, tetrahydrofuran containing 2-14% by weight of water is chosen, preferably tetrahydrofuran containing 5-11% by weight of water, more preferably 8-14% by weight of water.
Tetrahydrofuran containing 9% by weight of water is chosen.
The amount of these solvents to be used depends on the temperature, but it is easy to use about 5 to 15 ml per gram of crude estrone.
上記した溶媒にエストロンを溶解又は懸濁して
得られる溶液又は懸濁液に添加する芳香族炭化水
素としては、ベンゼン、トルエン、エチルベンゼ
ン、キシレン、テトラリン等の通常炭素数6〜20
の芳香族炭化水素及び灯油の如く芳香族炭化水素
の混合物が挙げられる。沸点の関係から、好まし
い芳香族炭化水素としては、トルエン及びキシレ
ンである。これらの芳香族炭化水素の使用量は特
に制限されないが、粗エストロン1gに対して5
〜30ml程度が扱いやすい。 The aromatic hydrocarbon to be added to the solution or suspension obtained by dissolving or suspending estrone in the above-mentioned solvent usually has 6 to 20 carbon atoms, such as benzene, toluene, ethylbenzene, xylene, and tetralin.
aromatic hydrocarbons and mixtures of aromatic hydrocarbons such as kerosene. In terms of boiling point, preferred aromatic hydrocarbons are toluene and xylene. The amount of these aromatic hydrocarbons used is not particularly limited, but 5 to 1 g of crude estrone
~30ml is easy to handle.
本発明の要点は、エストロンの含水テトラヒド
ロフラン中への溶解度が含水率8〜9重量%のテ
トラヒドロフランに於て最も大きいことにある。
図に30℃に於ける含水テトラヒドロフランに対す
るエストロンの溶解度曲線を示した。例えば、
100gのテトラヒドロフランには約5.1gのエスト
ロンが溶解するが、水が加わるにつれて溶解度が
増加し、約8.5重量%の含水テトラヒドロフラン
中には最高約9.3gのエストロンが溶解する。更
に水を加えていくと、溶解度は低下する。 The gist of the present invention is that the solubility of estrone in aqueous tetrahydrofuran is greatest in tetrahydrofuran with a water content of 8 to 9% by weight.
The figure shows the solubility curve of estrone in hydrous tetrahydrofuran at 30°C. for example,
Approximately 5.1 g of estrone is dissolved in 100 g of tetrahydrofuran, but the solubility increases as water is added, and up to about 9.3 g of estrone is dissolved in approximately 8.5 wt.% water-containing tetrahydrofuran. As more water is added, the solubility decreases.
以上、詳述したように、本発明によれば、特定
の溶媒を組み合わせて使用する晶析、洗浄操作か
らなる、工業的実施に適した簡便な方法によつて
粗エストロンを溶解し、さらに、不溶物を過す
るに際し、加熱配管、過装置等の特殊な装置を
用いることなしに、従来の約半分の溶媒量を用い
るだけで、高収率かつ高純度のエストロンを得る
ことができる。 As detailed above, according to the present invention, crude estrone is dissolved by a simple method suitable for industrial implementation, consisting of crystallization and washing operations using a combination of specific solvents, and further, When filtering insoluble matter, estrone can be obtained in high yield and purity by using only about half the amount of solvent used in the past, without using any special equipment such as heating piping or filtering equipment.
以下、本発明を実施例により具体的に説明する
が、本発明は、その要旨を超えない限り以下の実
施例に限定されない。 EXAMPLES Hereinafter, the present invention will be explained in detail with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof.
以下に述べる実施例に於て、粗エストロン及び
精製エストロンの純度は、誌料をシリル化後n−
オクタコサンをガスクロマトグラフイで定量した
値であり、±1%の誤差の可能性がある。 In the examples described below, the purity of crude estrone and purified estrone was determined by n-
This is a value determined by gas chromatography for octacosane, and there is a possibility of an error of ±1%.
実施例 1
撹拌装置及び窒素導入管を備えた100ml容のナ
スフラスコに、ADDの熱分解(特開昭51−26865
号公報の実施例1に記載の方法)で得られた純度
75.5%の粗エストロン2.00gを仕込み、17gの8
重量%含水テトラヒドロフランを加え30℃の水溶
上にて1時間撹拌する。この間に結晶は溶解す
る。この溶液をガラスフイルターを通して過
し、不溶物(エストロン以外の固形物)を除き、
撹拌装置留去管、温度計及び窒素導入管を備え
た。100ml容の四ツ口フラスコに仕込む。これに
トルエン60mlを加え油浴に浸し、油浴の温度を
120℃まで上げて、テトラヒドロフラン及び水を
留去する。留去の途中で結晶が析出するが、更に
留出温度が111℃になるまで留去を続けた後、油
浴中にて撹拌下室温まで放冷し、20℃の恒温槽中
に2時間放置する。析出した結晶を採取し、100
℃にて3時間減圧乾燥後ガスクロマトグラフイー
により結晶の純度を測定すると93.9%であり晶析
率は96.5%であつた。Example 1 In a 100 ml eggplant flask equipped with a stirring device and a nitrogen inlet tube, ADD thermal decomposition (Japanese Patent Application Laid-open No. 51-26865
Purity obtained by the method described in Example 1 of the publication
Prepare 2.00g of 75.5% crude estrone, 17g of 8
Add wt % water-containing tetrahydrofuran and stir for 1 hour over the aqueous solution at 30°C. During this time the crystals dissolve. Pass this solution through a glass filter to remove insoluble matter (solid matter other than estrone),
A stirring device was equipped with a distillation tube, a thermometer, and a nitrogen introduction tube. Pour into a 100ml four-necked flask. Add 60ml of toluene to this, immerse it in an oil bath, and adjust the temperature of the oil bath.
Raise the temperature to 120°C and distill off tetrahydrofuran and water. Crystals precipitate during distillation, but distillation is continued until the distillation temperature reaches 111°C, then cooled to room temperature with stirring in an oil bath, and then placed in a constant temperature bath at 20°C for 2 hours. put. Collect the precipitated crystals and
After drying under reduced pressure at ℃ for 3 hours, the purity of the crystals was measured by gas chromatography to be 93.9%, and the crystallization rate was 96.5%.
実施例 2
実施例1と同一のナスフラスコに、同じく同一
の粗エストロン2.00gを仕込み、18gの5重量%
含水テトラヒドロフランを加え30℃の水浴上にて
1時間撹拌する。この間に結晶は溶解する。この
溶液を実施例1と同一の四ツ口フラスコに仕込
み、80℃の水浴に浸し、テトラヒドロフラン及び
水を留去する。12.5gの溶媒が留去された時点で
留去を止め撹拌下放令し、20℃の恒温槽中に2時
間放置する。析出した結晶を採取し、100℃にて
3時間減圧乾燥後ガスクロマトグラフイーにより
結晶の純度を測定すると92.1%であり、晶析率は
87.1%であつた。Example 2 Into the same eggplant flask as in Example 1, 2.00 g of the same crude estrone was charged, and 5% by weight of 18 g was added.
Add aqueous tetrahydrofuran and stir on a 30°C water bath for 1 hour. During this time the crystals dissolve. This solution is placed in the same four-necked flask as in Example 1, immersed in a water bath at 80°C, and tetrahydrofuran and water are distilled off. When 12.5 g of solvent has been distilled off, the distillation is stopped, the mixture is allowed to stand under stirring, and the mixture is left in a constant temperature bath at 20°C for 2 hours. The precipitated crystals were collected and dried under reduced pressure at 100°C for 3 hours, and the purity of the crystals was measured by gas chromatography, and it was 92.1%, and the crystallization rate was
It was 87.1%.
図は、30℃での含水テトラヒドロフランに対す
るエストロンの溶解度を示す図である。縦軸は、
含水テトラヒドロフラン100gに溶解するエスト
ロンのg数を示し、横軸は、テトラヒドロフラン
に含まれる水の重量%を示す。
The figure shows the solubility of estrone in hydrous tetrahydrofuran at 30°C. The vertical axis is
The number of grams of estrone dissolved in 100 g of hydrous tetrahydrofuran is shown, and the horizontal axis shows the weight percent of water contained in tetrahydrofuran.
Claims (1)
ラヒドロフランに溶解し、不溶物が残存する場合
にはこれを過後、得られた溶液を芳香族炭化水
素の存在下又は非存在下濃縮するか、或いは、該
溶液を濃縮後芳香族炭化水素で処理して、エスト
ロンを晶析させ、固体エストロンを分離すること
を特徴とするエストロンの精製法。1. Dissolve crude estrone in tetrahydrofuran containing 2 to 14% by weight of water, and if any insoluble matter remains, after filtration, concentrate the resulting solution in the presence or absence of aromatic hydrocarbons, or Alternatively, a method for purifying estrone, which comprises concentrating the solution and then treating it with an aromatic hydrocarbon to crystallize estrone and separate solid estrone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6582579A JPS55157600A (en) | 1979-05-28 | 1979-05-28 | Purification of estrone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6582579A JPS55157600A (en) | 1979-05-28 | 1979-05-28 | Purification of estrone |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS55157600A JPS55157600A (en) | 1980-12-08 |
JPS6241520B2 true JPS6241520B2 (en) | 1987-09-03 |
Family
ID=13298183
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6582579A Granted JPS55157600A (en) | 1979-05-28 | 1979-05-28 | Purification of estrone |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS55157600A (en) |
-
1979
- 1979-05-28 JP JP6582579A patent/JPS55157600A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS55157600A (en) | 1980-12-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1395546B1 (en) | Process for the production of high purity iohexol | |
JPH06287161A (en) | Preparation of oxyphthalic dianhydride and purified oxyphthalic dianhydride from crude oxyphthalic dianhydride | |
US9518030B2 (en) | Purification of aryltriazoles | |
US3794647A (en) | Process for purifying lactams | |
JPS6241520B2 (en) | ||
EP1270548B1 (en) | Purification method of cyclohexanone-oxime | |
PL88936B1 (en) | ||
JP4219643B2 (en) | Method for recovering bisphenolfluorenes | |
RU2224749C2 (en) | Method for treatment of isoquinoline | |
EA002285B1 (en) | Process for the removal of heavy metals from organic compounds | |
US3037042A (en) | Method of purifying monoaminoalkyl sulfuric acid esters | |
JP2001226323A (en) | Method for recovering benzyl benzoate | |
JPS6241238B2 (en) | ||
JPS587618B2 (en) | How to remove boric acid from lactam | |
US4269987A (en) | Purification of triazoles | |
JP3157724B2 (en) | Indole purification method | |
JPH0469357A (en) | Method for purifying benzoic acid | |
JP3907449B2 (en) | Method for purifying fluorine-containing benzoic acid | |
JPH02172940A (en) | Production of p-hydroxybenzaldehyde | |
SU1084248A1 (en) | Method for purifying aluminium chloride | |
JPH03190847A (en) | Purification of 3,4-dichloronitrobenzene | |
WO2021078698A1 (en) | Processes for making tetrazolinone compounds | |
CN115850305A (en) | Refining method of high-purity Kribolol | |
JPS6157837B2 (en) | ||
PL125053B1 (en) | Method of purification of anthracene |