JPS623839B2 - - Google Patents
Info
- Publication number
- JPS623839B2 JPS623839B2 JP3472480A JP3472480A JPS623839B2 JP S623839 B2 JPS623839 B2 JP S623839B2 JP 3472480 A JP3472480 A JP 3472480A JP 3472480 A JP3472480 A JP 3472480A JP S623839 B2 JPS623839 B2 JP S623839B2
- Authority
- JP
- Japan
- Prior art keywords
- adenine
- formic acid
- purifying
- arylazomalononitrile
- reacting
- 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
- GFFGJBXGBJISGV-UHFFFAOYSA-N Adenine Chemical compound NC1=NC=NC2=C1N=CN2 GFFGJBXGBJISGV-UHFFFAOYSA-N 0.000 claims description 58
- 229930024421 Adenine Natural products 0.000 claims description 57
- 229960000643 adenine Drugs 0.000 claims description 57
- 238000000034 method Methods 0.000 claims description 23
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 15
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 15
- 235000002639 sodium chloride Nutrition 0.000 claims description 13
- 239000012535 impurity Substances 0.000 claims description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 9
- 150000003839 salts Chemical class 0.000 claims description 9
- 238000010531 catalytic reduction reaction Methods 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 8
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 7
- 229910021529 ammonia Inorganic materials 0.000 claims description 7
- 239000006227 byproduct Substances 0.000 claims description 7
- 235000019253 formic acid Nutrition 0.000 claims description 7
- 239000010446 mirabilite Substances 0.000 claims description 7
- 239000003054 catalyst Substances 0.000 claims description 6
- 238000004042 decolorization Methods 0.000 claims description 6
- 150000004675 formic acid derivatives Chemical class 0.000 claims description 6
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical group [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 5
- 229910017053 inorganic salt Inorganic materials 0.000 claims description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 239000011780 sodium chloride Substances 0.000 claims description 4
- KLMBASWITNCMTF-UHFFFAOYSA-N 2-phenyldiazenylpropanedinitrile Chemical group N#CC(C#N)N=NC1=CC=CC=C1 KLMBASWITNCMTF-UHFFFAOYSA-N 0.000 claims description 3
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 2
- 229910019142 PO4 Inorganic materials 0.000 claims description 2
- 239000001099 ammonium carbonate Substances 0.000 claims description 2
- 235000012501 ammonium carbonate Nutrition 0.000 claims description 2
- 239000010452 phosphate Substances 0.000 claims description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims 2
- 238000000926 separation method Methods 0.000 claims 2
- XVFXUMLDSMFSPX-UHFFFAOYSA-N 5-phenyl-2-(pyrimidin-2-yldiazenyl)pyrimidine-4,6-diamine Chemical compound N=1C(N)=C(C=2C=CC=CC=2)C(N)=NC=1N=NC1=NC=CC=N1 XVFXUMLDSMFSPX-UHFFFAOYSA-N 0.000 claims 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims 1
- 235000019270 ammonium chloride Nutrition 0.000 claims 1
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 claims 1
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 claims 1
- 235000019837 monoammonium phosphate Nutrition 0.000 claims 1
- 239000006012 monoammonium phosphate Substances 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 36
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 21
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 10
- 239000013078 crystal Substances 0.000 description 9
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 239000008213 purified water Substances 0.000 description 7
- 235000011121 sodium hydroxide Nutrition 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 229910052500 inorganic mineral Inorganic materials 0.000 description 5
- 235000010755 mineral Nutrition 0.000 description 5
- 239000011707 mineral Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000007868 Raney catalyst Substances 0.000 description 3
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 3
- 229910000564 Raney nickel Inorganic materials 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000010979 pH adjustment Methods 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000007810 chemical reaction solvent Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 239000012286 potassium permanganate Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- RSIJVJUOQBWMIM-UHFFFAOYSA-L sodium sulfate decahydrate Chemical compound O.O.O.O.O.O.O.O.O.O.[Na+].[Na+].[O-]S([O-])(=O)=O RSIJVJUOQBWMIM-UHFFFAOYSA-L 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 238000004847 absorption spectroscopy Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 229920001429 chelating resin Polymers 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 239000002198 insoluble material Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 235000011181 potassium carbonates Nutrition 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- JVBXVOWTABLYPX-UHFFFAOYSA-L sodium dithionite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])=O JVBXVOWTABLYPX-UHFFFAOYSA-L 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- DJWUNCQRNNEAKC-UHFFFAOYSA-L zinc acetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O DJWUNCQRNNEAKC-UHFFFAOYSA-L 0.000 description 1
Description
本発明はアデニンの有利な精製法に関する。更
に詳しくはアリールアゾマロノニトリルの起源の
アデニン例えばアリールアゾマロノニトリルをア
ンモニアの共存下ギ酸あるいはギ酸誘導体と接触
還元条件下反応させて得られたアデニンあるいは
アリールアゾマロノニトリルをアンモニアの共存
下ギ酸あるいはギ酸誘導体と反応させて得られた
4・6−ジアミノ−5−アリールアゾピリミジン
を接触還元条件下ギ酸あるいはギ酸誘導体と反応
させて得られたアデニンあるいはこれらと類似の
方法で得られたアデニンを精製するに当り触媒お
よび反応副生物との分離を、系のPHを7.5〜9.0に
することおよび又は芒硝、食塩等の無機塩を添加
することによつて行い次いで脱色をアデニンの無
機塩の形で行うことを特徴とするアデニンの精製
法に関する。
アデニンの精製法として知られている方法は反
応物と水と共に煮沸して活性炭等の吸着剤で脱色
精製する方法が一般的である。また特殊な例とし
て、活性炭カラムに吸着させアンモニア水で溶離
させる方法、陽イオン交換樹脂(例えばアンバー
ライト120B)カラムを通す方法、酸性条件で過
マンガン酸カリで酸化分解することによつて不純
物を除去し、次いで活性炭を脱色することによつ
て精製する方法が知られている。また昇華による
精製例もある。
アリールアゾマロノニトリルを出発原料とする
アデニンの製造法は例えば特公昭51−23516(特
許第931627号)に記載のアリールアゾマロノニト
リルとホルムアミドを接触還元条件下アンモニア
の存在においてアデニンを製造する方法であり、
あるいは特開昭49−81394に開示のアリールアゾ
マロノニトリルをアンモニアの存在下でギ酸ある
いはその誘導体と反応させ4・6−ジアミノ−5
−アリールアゾピリミジンを得これとギ酸あるい
はギ酸の誘導体と接触還元条件下反応させること
によるアデニンの製造方法で代表されるが本発明
はこれらの出願の方法およびそれから類推できる
反応試薬を用いる反応、反応推進効果を有する試
薬等を適用する反応など類似の反応によるアデニ
ンの精製に適用できる。これらの方法で得られた
粗製アデニンの純度はおよそ80〜90%で残りは接
触還元触媒と無定形の副生物である。
接触還元触媒としてはラネーニツケルが一般的
であり無定形の副生物は緑灰色をした粘土状のも
のである。この粗製アデニンを精製するために、
アデニンの一般的な方法すなわち粗製アデニンを
その40〜50倍の水と共に加熱還流しアデニンを溶
解させ活性炭で脱色する方法を検討したが純度お
よび白色度において不都合であつた。更に既知の
方法についても検討してみたが、効果が不充分、
精製ロスが多い、コストアツプになる等いずれも
満足出来るものでなかつた。
発明者は工業的に採用可能な精製法を種々研究
し副生物がその液のPHを7.5〜9.0の弱アルカリ性
にすることおよびまたは芒硝、食塩等の塩類を添
加することによつて熱溶液から不溶物として析出
することを見出した。更に脱色は系に硫酸、塩
酸、リン酸等の鉱酸を加えPHをアデニンがそれら
の酸と塩を形成する点以下まで下げ活性炭と加熱
することによつて効果的に行うことができること
を見出した。この二つのプロセスをセツトするこ
とによつて非常に純度の高いかつ白色度も高いア
デニンを得ることが可能となつた。
精製のプロセスは反応物から反応溶媒を回収
し、得られた残渣にその35〜80倍好ましくは45〜
60倍の水を加えアルカリ(好ましくは水酸化ナト
リウム)でPHを7.5〜9.0好ましくは7.5〜8.5に調
節しそれに加えてあるいはPHの調整なしに無機塩
類を残渣に対して10〜100%好ましくは25〜50%
添加し、加熱してアデニンを溶解し熱時過して
不溶物を除き、次いで鉱酸を加えて塩類を形成す
るPHまで下げ活性炭を加え熱時脱色を行い廃活性
炭を過した後液を苛性ソーダの様なアルカリ
で中和後冷却し晶析させることから成る、この場
合勿論各工程毎に結晶を取り出しても良い。また
副生物の除去にPH調整と塩類添加を併用しても勿
論かまわない。
ここに用いるアルカリとは一般的に苛性ソーダ
が便利であるが、苛性カリ、炭酸ソーダ、炭酸カ
リ、水酸化カルシウム等でも何んら問題はない。
また無機塩類とは、芒硝、食塩、炭酸アンモン、
リン酸−アンモニウム等であるが、芒硝が最も便
利である。鉱酸は硫酸、リン酸、塩酸等が利用で
きる。
不定形の副生物の除去法として過酸化水素、次
亜塩素酸ソーダ、過マンガン酸カリによる酸化、
酢酸一亜鉛、亜二チオン酸ナトリウムによる還元
法についても検討したが、本発明の方法に比べる
とその効果は低位であつた。また、脱色時イオン
交換樹脂の効果も検討したが不充分の結果しか得
られなかつた。
各鉱酸の塩を形成するPHとは硫酸、塩酸、リン
酸共PH約3以下であり好適には2.5〜1.5が採用さ
れる。
次に実施例をあげて本発明の方法を具体的に説
明するが、本発明はこの実施例によつて何ら限定
されるものではない。
実施例 1
フエニルアゾマロノニトリル68.1gを6%アン
モニアを含むホルムアミド681gに溶解させオー
トクレープ中150〜155℃で2時間反応させた。熱
時揮発性ガスを放出し、冷後ラネーニツケル10g
を加え水素初圧80Kg/cm2下で150〜155℃で5時間
還元反応を行つた。冷後オートクレープから取り
出し、ホルムアミドを減圧蒸留し回収後析出物を
取り出しメタノールで洗浄した。粗製アデニン
44.2gを得た。
得られた粗製アデニン10gを精製水500mlに加
え加熱し、80〜90゜で48%苛性ソーダを少量づつ
加えてPHを8.5に調整した。1時間90〜95゜で加
熱してアデニンを溶解させ、熱時触媒および析出
した不溶物を別し、液を冷却し10℃で10時間
晶析した。析出したアデニンの結晶を吸引取し
少量の精製水で洗浄した。得られた結晶を精製水
100mlに加えその懸濁液に濃硫酸を徐々に加えPH
を2.0に調整した後加熱して結晶を溶解させ活性
炭を加え1時間加熱還流して脱色を行い、熱時活
性炭を別し冷却晶析後析出結晶を取した。こ
の硫酸塩を精製水500mlに溶解し苛性ソーダでPH
を6.5〜7に調整し、少量の活性炭を加え30分加
熱した後活性炭を去、液を冷却してアデニン
を白色の結晶として晶析させ、吸引取し精製水
で充分洗浄してから乾燥しアデニン7.5gを得
た。本品の純度は紫外部吸収スペクトル法
(UV)で99.8%であり、陽イオン交換カラムによ
る高速液体クロマトグラム(HPLC)による不純
物の定量では0.083%であつた。波長430nmでの
白色度の測定は95.2%であつた。
実施例 2
硫酸の代りに塩酸を用いた以外は実施例1と同
様に操作してアデニン6.9gを得た。
純 度 100.3%
不純物 0.096%
白色度 95.0%
実施例 3
硫酸の代りにリン酸(75%)を用い、リン酸塩
の溶解用の水として180mlを用いた以外は実施例
1と同様に操作してアデニン7.8gを得た。
純 度 99.5%
不純物 0.033%
白色度 96.1%
比較例 1
実施例1の粗製アデニン10gを水500mlに加え
加熱還流してアデニンを溶解させ、熱時不溶物を
別し液に活性炭を加え1時間加熱還流脱色し
活性炭を別した。液はまた薄褐色を呈してい
るので再度活性炭を加えて脱色を繰返した後晶析
した。アデニン6.5g
純 度 95.3%
不純物 4.2%
白色度 83.4%
実施例 4
実施例1の粗製アデニン10gを精製水500に
加えその混合物に芒硝3.0gを加え1時間加熱還
流した。熱時過して触媒および不溶物を分離
し、液を冷却し、10℃で10時間晶析した。得ら
れたアデニンの結晶を以下実施例2と同様に操作
してアデニン7.5gを得た。
純 度 99.4%
不純物 0.38%
白色度 93.7%
実施例 5〜14
実施例1の粗製アデニン10gを実施例1および
4に準じて、塩類の種類および量を変えた場合並
びにPH調整と塩類の添加を並用した場合について
操作した結果を第表に示す。
The present invention relates to an advantageous method for the purification of adenine. More specifically, adenine, which is the origin of arylazomalononitrile, is obtained by reacting arylazomalononitrile with formic acid or a formic acid derivative under catalytic reduction conditions in the presence of ammonia, or adenine or arylazomalononitrile, which is obtained by reacting arylazomalononitrile with formic acid or a formic acid derivative in the presence of ammonia. Purifying adenine obtained by reacting 4,6-diamino-5-arylazopyrimidine obtained by reacting with a derivative with formic acid or a formic acid derivative under catalytic reduction conditions, or adenine obtained by a similar method. The catalyst and reaction by-products are separated by adjusting the pH of the system to 7.5-9.0 and/or by adding an inorganic salt such as mirabilite or common salt, followed by decolorization in the form of an inorganic salt of adenine. The present invention relates to a method for purifying adenine characterized by the following. A common method known for purifying adenine is to boil the reactant with water and decolorize it using an adsorbent such as activated carbon. In addition, as special examples, impurities can be removed by adsorption on an activated carbon column and elution with aqueous ammonia, passing through a cation exchange resin (e.g. Amberlite 120B) column, or oxidative decomposition with potassium permanganate under acidic conditions. Methods of purification by removal and subsequent decolorization of activated carbon are known. There are also examples of purification by sublimation. A method for producing adenine using arylazomalononitrile as a starting material is, for example, a method for producing adenine in the presence of ammonia under catalytic reduction conditions of arylazomalononitrile and formamide described in Japanese Patent Publication No. 51-23516 (Patent No. 931627). can be,
Alternatively, 4,6-diamino-5
The present invention is typified by a method for producing adenine by obtaining an arylazopyrimidine and reacting it with formic acid or a derivative of formic acid under catalytic reduction conditions, and the present invention relates to the methods of these applications and reactions and reactions using reaction reagents that can be analogized thereto. It can be applied to the purification of adenine by a similar reaction such as a reaction using a reagent with a promoting effect. The purity of the crude adenine obtained by these methods is approximately 80-90%, with the remainder being the catalytic reduction catalyst and amorphous by-products. Raney nickel is commonly used as a catalytic reduction catalyst, and the amorphous by-product is a greenish-gray clay-like substance. In order to purify this crude adenine,
A general method for preparing adenine, namely, heating and refluxing crude adenine with 40 to 50 times as much water as it, dissolving the adenine, and decolorizing it with activated carbon, was investigated, but this method was inconvenient in terms of purity and whiteness. We also investigated known methods, but they were not sufficiently effective.
Both were unsatisfactory, such as a large amount of refining loss and increased costs. The inventor researched various industrially applicable purification methods, and found that by-products can be removed from hot solutions by making the pH of the solution slightly alkaline at 7.5 to 9.0, or by adding salts such as mirabilite and common salt. It was found that it precipitates as an insoluble substance. Furthermore, it was discovered that decolorization can be effectively carried out by adding mineral acids such as sulfuric acid, hydrochloric acid, and phosphoric acid to the system to lower the pH to below the point at which adenine forms salts with those acids, and then heating the system with activated carbon. Ta. By combining these two processes, it became possible to obtain adenine with extremely high purity and high whiteness. The process of purification involves recovering the reaction solvent from the reactants and adding 35 to 80 times the amount of the reaction solvent to the resulting residue, preferably 45 to 80 times as much.
Add 60 times as much water and adjust the pH to 7.5 to 9.0, preferably 7.5 to 8.5 with an alkali (preferably sodium hydroxide), and in addition or without adjusting the pH, add inorganic salts to the residue preferably 10 to 100%. 25-50%
Add mineral acid to dissolve the adenine, heat to remove insoluble matter, then add mineral acid to lower the pH to the point at which salts are formed. Add activated carbon to decolorize when heated, pass through the waste activated carbon, and pour the liquid into caustic soda. The process consists of neutralizing with an alkali such as, cooling and crystallizing. In this case, of course, crystals may be taken out after each step. Of course, PH adjustment and salt addition may be used in combination to remove by-products. The alkali used here is generally conveniently caustic soda, but there is no problem with caustic potash, soda carbonate, potassium carbonate, calcium hydroxide, etc.
Inorganic salts include mirabilite, common salt, ammonium carbonate,
Examples include ammonium phosphate, but mirabilite is the most convenient. Sulfuric acid, phosphoric acid, hydrochloric acid, etc. can be used as mineral acids. Oxidation with hydrogen peroxide, sodium hypochlorite, and potassium permanganate is a method for removing amorphous byproducts.
Reduction methods using monozinc acetate and sodium dithionite were also investigated, but their effectiveness was lower than that of the method of the present invention. In addition, the effect of ion exchange resin on decolorization was investigated, but only unsatisfactory results were obtained. The pH for forming each mineral acid salt is sulfuric acid, hydrochloric acid, and phosphoric acid, each having a pH of about 3 or less, preferably from 2.5 to 1.5. Next, the method of the present invention will be specifically explained with reference to Examples, but the present invention is not limited to these Examples in any way. Example 1 68.1 g of phenyl azomalononitrile was dissolved in 681 g of formamide containing 6% ammonia and reacted in an autoclave at 150 to 155°C for 2 hours. Releases volatile gas when hot, then cools down to 10g of Raney Nickel
was added and a reduction reaction was carried out at 150 to 155°C for 5 hours under an initial hydrogen pressure of 80 kg/cm 2 . After cooling, it was taken out from the autoclave, formamide was distilled under reduced pressure, and the precipitate was taken out and washed with methanol. crude adenine
44.2g was obtained. 10 g of the obtained crude adenine was added to 500 ml of purified water and heated, and the pH was adjusted to 8.5 by adding 48% caustic soda little by little at 80-90°. Adenine was dissolved by heating at 90-95° for 1 hour, the hot catalyst and precipitated insoluble matter were separated, and the liquid was cooled and crystallized at 10°C for 10 hours. The precipitated adenine crystals were collected by suction and washed with a small amount of purified water. The obtained crystals are purified with water.
100ml and gradually add concentrated sulfuric acid to the suspension to adjust the pH.
After adjusting the temperature to 2.0, the mixture was heated to dissolve the crystals, activated carbon was added, and heated under reflux for 1 hour to decolorize the mixture.The hot activated carbon was separated, and the precipitated crystals were collected after cooling and crystallization. Dissolve this sulfate in 500ml of purified water and pH it with caustic soda.
Adjust the temperature to 6.5 to 7, add a small amount of activated carbon, heat for 30 minutes, remove the activated carbon, cool the liquid, crystallize adenine as white crystals, suck it up, wash thoroughly with purified water, and dry. 7.5 g of adenine was obtained. The purity of this product was 99.8% as determined by ultraviolet absorption spectroscopy (UV), and 0.083% as determined by high performance liquid chromatography (HPLC) using a cation exchange column. The measured whiteness at a wavelength of 430 nm was 95.2%. Example 2 6.9 g of adenine was obtained in the same manner as in Example 1 except that hydrochloric acid was used instead of sulfuric acid. Purity 100.3% Impurities 0.096% Whiteness 95.0% Example 3 The procedure was the same as in Example 1 except that phosphoric acid (75%) was used instead of sulfuric acid and 180 ml of water was used to dissolve the phosphate. 7.8g of adenine was obtained. Purity: 99.5% Impurities: 0.033% Whiteness: 96.1% Comparative Example 1 10 g of the crude adenine from Example 1 was added to 500 ml of water and heated to reflux to dissolve the adenine, the insoluble matter was separated when heated, activated carbon was added to the liquid and heated for 1 hour. It was decolorized under reflux and the activated carbon was separated. Since the liquid had a light brown color, activated carbon was added again and decolorization was repeated, followed by crystallization. 6.5 g of adenine Purity: 95.3% Impurities: 4.2% Whiteness: 83.4% Example 4 10 g of the crude adenine from Example 1 was added to 500 g of purified water, and 3.0 g of Glauber's salt was added to the mixture and heated under reflux for 1 hour. The catalyst and insoluble matter were separated by heating, and the liquid was cooled and crystallized at 10° C. for 10 hours. The obtained adenine crystals were treated in the same manner as in Example 2 to obtain 7.5 g of adenine. Purity: 99.4% Impurities: 0.38% Whiteness: 93.7% Examples 5 to 14 10 g of crude adenine from Example 1 was prepared in the same manner as in Examples 1 and 4, with different types and amounts of salts, PH adjustment, and addition of salts. The results of the manipulations when used together are shown in Table 1.
【表】
比較例 2
PH調整の代りに過酸化水素(30%)5ml用いた
以外実施例1と同様に操作してアデニン7.1gを
得た。
純 度 98.0%
不純物 1.5%
白色度 92.5%
実施例 15
実施例1の粗製アデニン10.0gを精製水500ml
に加え加熱して80〜90゜で48%苛性ソーダを徐々
に加えてPHを8.0に調整した。90〜95゜に加熱し
てアデニンを溶解せしめ不溶物を別した。液
に30%の硫酸を徐々に加えてPH2.5に調整した。
活性炭を加えて1時間加熱脱色を行い活性炭を
別した。液に48%苛性ソーダを加えてPH7に中
和した。少量の活性炭を加えて脱色した後その活
性炭を去、液を冷却してアデニンの結晶を析
出させた。結晶を吸引取して精製水で充分洗滌
し乾燥した。アデニン8.2g
純 度 98.9%
不純物 0.26%
白色度 93.1%
実施例 16
芒硝4.5gを更に添加した以外は実施例15と同
様に操作して、アデニン8.5gを得た。
純 度 99.3%
不純物 0.12%
白色度 93.6%
実施例 17
フエニルアゾマロノニトリル68.1gを6%アン
モニアを含むホルムアミド681gに溶解させ、ラ
ネーニツケル10gを加え、オートクレープ中水素
初圧100Kg/cm2下で130〜135゜で1.5時間還元を行
い次いで温度を上げて150〜155゜で5時間反応さ
せた。冷後反応物をオートクレープから取り出し
減圧蒸留してホルムアミドを回収し残渣を取り出
し、メタノールで洗滌して粗製のアデニン35.1g
を得た。得られた粗製アデニン10.0gを実施例2
と同様に操作してアデニン6.8gを得た。
純 度 100.3%
不純物 0.13%
白色度 93.5%
実施例 18
実施例17の粗製アデニン10.0gを実施例15と同
様に操作してアデニン7.3gを得た。
純 度 98.8%
不純物 0.48%
白色度 92.8%[Table] Comparative Example 2 7.1 g of adenine was obtained in the same manner as in Example 1 except that 5 ml of hydrogen peroxide (30%) was used instead of pH adjustment. Purity 98.0% Impurities 1.5% Whiteness 92.5% Example 15 10.0 g of crude adenine from Example 1 was added to 500 ml of purified water.
The pH was adjusted to 8.0 by gradually adding 48% caustic soda at 80-90°. The adenine was dissolved by heating to 90-95° and the insoluble materials were separated. 30% sulfuric acid was gradually added to the solution to adjust the pH to 2.5.
Activated carbon was added and decolorized by heating for 1 hour, and the activated carbon was separated. 48% caustic soda was added to the solution to neutralize it to pH 7. After decolorizing the mixture by adding a small amount of activated carbon, the activated carbon was removed and the liquid was cooled to precipitate adenine crystals. The crystals were collected by suction, thoroughly washed with purified water, and dried. 8.2 g of adenine Purity: 98.9% Impurities: 0.26% Whiteness: 93.1% Example 16 8.5 g of adenine was obtained in the same manner as in Example 15, except that 4.5 g of Glauber's salt was further added. Purity 99.3% Impurities 0.12% Whiteness 93.6% Example 17 68.1 g of phenylazomalononitrile was dissolved in 681 g of formamide containing 6% ammonia, 10 g of Raney nickel was added, and the mixture was dissolved in an autoclave under an initial hydrogen pressure of 100 Kg/cm 2 Reduction was carried out at 130-135° for 1.5 hours, then the temperature was raised and the reaction was carried out at 150-155° for 5 hours. After cooling, the reaction product was taken out of the autoclave and distilled under reduced pressure to recover formamide, and the residue was washed with methanol to obtain 35.1 g of crude adenine.
I got it. Example 2 10.0g of the obtained crude adenine
6.8g of adenine was obtained in the same manner as above. Purity: 100.3% Impurities: 0.13% Whiteness: 93.5% Example 18 10.0 g of the crude adenine from Example 17 was treated in the same manner as in Example 15 to obtain 7.3 g of adenine. Purity 98.8% Impurities 0.48% Whiteness 92.8%
Claims (1)
アデニンを精製するに当り触媒を含む反応副生物
との分離を、系のPHを7.5〜9.0にすることおよび
または無機塩類の添加により行い、次いで脱色を
アデニンの無機塩の形において行うことを特徴と
するアデニンの精製法。 2 アデニンがアリールアゾマロノニトリルをア
ンモニアの共存下ギ酸あるいはギ酸誘導体と接触
還元条件下反応させて得られたアデニンである特
許請求の範囲1のアデニンの精製法。 3 アデニンがアリールアゾマロノニトリルをア
ンモニアの共存下ギ酸あるいはギ酸誘導体と反応
させ、得られた4・6−ジアミノ−5−フエニル
アゾピリミジンを接触還元条件下ギ酸あるいはギ
酸誘導体と反応させて得られたアデニンである特
許請求範囲1のアデニンの精製法。 4 アデニンの無機塩が硫酸塩、リン酸塩、塩酸
塩である特許請求範囲1のアデニンの精製法。 5 不純物の分離促進剤としての添加無機塩類が
芒硝、食塩、塩化アンモニウム、炭酸アンモニウ
ム、リン酸一アンモニウムからえらばれる特許請
求範囲1のアデニンの精製法。 6 アリールアゾマロノニトリルをフエニルアゾ
マロノニトリルである特許請求範囲1のアデニン
の精製法。[Claims] 1. In purifying adenine produced from arylazomalononitrile, separation from reaction by-products containing catalysts is carried out by adjusting the pH of the system to 7.5 to 9.0 and/or adding inorganic salts. , followed by decolorization in the form of an inorganic salt of adenine. 2. The method for purifying adenine according to claim 1, wherein the adenine is an adenine obtained by reacting arylazomalononitrile with formic acid or a formic acid derivative under catalytic reduction conditions in the presence of ammonia. 3 Adenine is obtained by reacting arylazomalononitrile with formic acid or a formic acid derivative in the presence of ammonia, and reacting the resulting 4,6-diamino-5-phenylazopyrimidine with formic acid or a formic acid derivative under catalytic reduction conditions. A method for purifying adenine according to claim 1, which is adenine. 4. The method for purifying adenine according to claim 1, wherein the inorganic salt of adenine is a sulfate, a phosphate, or a hydrochloride. 5. The method for purifying adenine according to claim 1, wherein the added inorganic salt as an impurity separation promoter is selected from mirabilite, common salt, ammonium chloride, ammonium carbonate, and monoammonium phosphate. 6. The method for purifying adenine according to claim 1, wherein the arylazomalononitrile is phenyl azomalononitrile.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3472480A JPS56131585A (en) | 1980-03-21 | 1980-03-21 | Purifying method of adenine |
| US07/323,709 US4997939A (en) | 1980-03-21 | 1989-03-15 | Process for preparing adenine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3472480A JPS56131585A (en) | 1980-03-21 | 1980-03-21 | Purifying method of adenine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56131585A JPS56131585A (en) | 1981-10-15 |
| JPS623839B2 true JPS623839B2 (en) | 1987-01-27 |
Family
ID=12422265
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3472480A Granted JPS56131585A (en) | 1980-03-21 | 1980-03-21 | Purifying method of adenine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56131585A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100341793C (en) * | 2003-12-24 | 2007-10-10 | 天津渤海化工有限责任公司天津碱厂 | Method for improving whiteness of heavy soda ash prepared by liquid phase hydration method |
| CN112679502A (en) * | 2020-12-31 | 2021-04-20 | 河南巨龙生物工程股份有限公司 | Method for green recovery of adenine from adenosine crude product mother liquor |
-
1980
- 1980-03-21 JP JP3472480A patent/JPS56131585A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56131585A (en) | 1981-10-15 |
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