TW518331B - Process for the production of 2H-1-benzopyrans - Google Patents
Process for the production of 2H-1-benzopyrans Download PDFInfo
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經濟部中央標準局員工消費合作社印製 518331 A7 ____B7 五、發明説明(1 ) 本發明爲關於一種製備卜表並喃類之製程,係沪 由在第一階段中令脂族醛類與脂族醇類於脱水化合物及胃氧 化鋁/氧化矽觸媒存在下轉換成脂族縮醛類且其在第二階 段中 1賓爾類於蒼存在下T情娘貧機溶劑中反應。2h + 苯並αΑ喃類在藥劑之製造中爲重要的中間產物或終產物 (North等人,J.0.C·,60.3397,1995; Bell等人,Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 518331 A7 ____B7 V. Description of the Invention (1) The present invention relates to a process for preparing tables and naming, which is the first step in the process of ordering aliphatic aldehydes and aliphatics. Alcohols are converted into aliphatic acetals in the presence of dehydrated compounds and gastric alumina / silica catalysts and they react in the second stage with T-beautiful organic solvents in the presence of Cang. 2h + benzoαArans are important intermediate or end products in the manufacture of pharmaceuticals (North et al., J.0.C., 60.3397, 1995; Bell et al.,
Synthesis, 707,1995)例如在製造用於治療癲癇和偏頭 痛之oit喃基氰基胍類中爲重要的中間產物或終產物(EP-A 0 629 619)。 可依據本發明製造之2H~1-苯並mt喃類爲具有下列通式 痛 R2 :;r :?ll 1 :卞‘代丨 其中Ri爲氳、(Ci -C4 )烷基,R2爲氫、(c^g6 )燒基 且R 3爲氳、(C 1 -C 4 )垸基、(C 1 -C 4 )由烷基、(C 2 -C4 )烯基、(Cl -C4 )垸氧羰基、(C! -c4 )燒氧甲基、 (Cl -C4 )燒酿基、(Cl -C4 )坑氧基、(C! -C4 )燒續酿 基、卣素、胺基、垸胺基、二烷胺基、胩、硝基或羥基。 於文獻中已描述使用氧化鋁/氧化矽觸媒,以酮類爲基 礎(Thuy et Maite,Bui 1· Soc· Chim· Fr 11 2558; 1975)和以仲甲醛爲基礎(Deshmukh等人,Synth commun. 25, 3939; 1995)製造縮醛類。此些文獻已知之合成方法 的缺點在於合成中所使用之觸媒相對於起始產物的高比例 〇 -3 - 本紙張尺度適用中國國家標準(CNS ) Μ規格(210 X 297公釐) (請先閲讀背面之注意事項再填寫本頁) 訂 518331 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(3 ) 基或兩個R4共同爲環狀之(C2 -C4 )烷二基。 R 1意指氫或具有1-4個碳原子之直鏈或支鏈燒基。可爲 甲基、乙基、正丙基、異丙基、正-、異-、第三-丁基。 R 1特隹爲I和措量或类者卜❼餘碳|子之直 鍵或支鏈燒基。可爲甲基、乙基、正丙基、異丙基、正_ 、異-、第三-丁基、戊基和其異構物及己基和其異構物。 若R 2爲氫和甲基則爲特佳。R4意指具有1-4個碳原子之 直鏈或支鏈烷基◊可爲甲基、乙基、正丙基、異丙基、正_ 、異、第二-丁基。务R4爲甲基和己基則爲特佳。兩個 R4共同意指具有2-4個碳原子之環狀垸二基。可爲乙燒― 1,2_二基、丙烷-1,3-二基、丙烷-1,2-二基、丁烷-1,4-二基、丁垸-1,3-二基、丁烷-1,2-二基。若兩個R 4共同 爲乙燒-1,2 -—基和丙统-1,3~·二基則爲特佳。R5意指具 有1-4個碳原子之直鏈或支鏈烷基。可爲甲基、乙基、正 丙基、異丙基、正_、異-、第三-丁基。若R5爲甲基和乙 基則爲特佳。 脂族醛可簡單地如依US-A 3 994 936和ΕΡ-Α 0 240 431 所述之異構化作用,而由2-甲基-3-丁坱-2-醇製得。 轉換作用爲有利與脂族醇R4 ΟΗ或HOR4 ΟΗ進行,其中 R4具有所述之定義。較佳使用甲醇、乙醇、乙二醇或丙 二醇。 較佳使用原甲酸三甲酯或原甲酸三乙酯作爲脱水化合物 HC(0R5)3,其中R5具有所述之定義。 具有100至27〇m2/g (BET-測量)比表面積及大於〇 冬'為張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) 、一*5 τ 518331Synthesis, 707, 1995) is, for example, an important intermediate or end product in the manufacture of oitaminocyanoguanidines for the treatment of epilepsy and migraine (EP-A 0 629 619). The 2H ~ 1-benzopyrans which can be produced according to the present invention have the following general formula R2:; r:? Ll1: 卞 'generation 丨 where Ri is 氲, (Ci-C4) alkyl, and R2 is hydrogen , (C ^ g6) alkyl and R 3 is fluorene, (C 1 -C 4) fluorenyl, (C 1 -C 4) alkyl, (C 2 -C4) alkenyl, (Cl -C4) fluorene Oxycarbonyl group, (C! -C4) oxymethyl group, (Cl-C4) oxy group, (Cl-C4) oxy group, (C! -C4) oxy group, halogen, amine group, amidine Amine, dialkylamino, hydrazone, nitro or hydroxyl. The use of alumina / silica catalysts has been described in the literature based on ketones (Thuy et Maite, Bui 1. Soc. Chim. Fr 11 2558; 1975) and based on paraformaldehyde (Deshmukh et al., Synth commun 25, 3939; 1995) to make acetals. The disadvantages of the synthetic methods known in these documents are the high proportion of the catalyst used in the synthesis relative to the starting product. 0-3-This paper size is applicable to the Chinese National Standard (CNS) M specification (210 X 297 mm) (please Read the notes on the back before filling this page) Order 518331 Printed by the Consumer Standards Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Description of the invention (3) or two R4 are cyclic (C2-C4) alkanediyl . R 1 means hydrogen or a linear or branched alkyl group having 1 to 4 carbon atoms. It may be methyl, ethyl, n-propyl, isopropyl, n-, iso-, tert-butyl. R 1 is particularly a straight bond or branched chain radical of I and a measure or the like. It may be methyl, ethyl, n-propyl, isopropyl, n-, iso-, tert-butyl, pentyl and its isomers, and hexyl and its isomers. It is particularly preferred if R 2 is hydrogen and methyl. R4 means a straight or branched chain alkyl group having 1 to 4 carbon atoms, which may be methyl, ethyl, n-propyl, isopropyl, n-, iso, second-butyl. R4 is particularly preferably methyl and hexyl. The two R4s collectively refer to a cyclic fluorenediyl group having 2-4 carbon atoms. May be ethane-1,2-diyl, propane-1,3-diyl, propane-1,2-diyl, butane-1,4-diyl, butane-1,3-diyl, Butane-1,2-diyl. It is particularly preferred if the two R 4 are common to the ethane-1,2-, and the C-1,3 ~ · diyl groups. R5 means a straight or branched chain alkyl group having 1 to 4 carbon atoms. It may be methyl, ethyl, n-propyl, isopropyl, n-, iso-, tert-butyl. It is particularly preferred if R5 is methyl and ethyl. Aliphatic aldehydes can be prepared from 2-methyl-3-butydin-2-ol simply by isomerization as described in US-A 3 994 936 and EP-A 0 240 431. The conversion is carried out favorably with an aliphatic alcohol R4 0Η or HOR4 0Η, where R4 has the definition described. Preferably, methanol, ethanol, ethylene glycol or propylene glycol is used. It is preferred to use trimethyl orthoformate or triethyl orthoformate as the dehydrating compound HC (0R5) 3, wherein R5 has the above-mentioned definition. It has a specific surface area of 100 to 27〇m2 / g (BET-measurement) and a size greater than 0. The standard is China Standard (CNS) A4 (210X297 mm) (please read the precautions on the back before filling this page) , A * 5 τ 518331
OHOH
IV A7 五、發明説明(4 /g ( Hg孔度計測量)微孔體積(7 5_8〇nm)之蒙脱石爲有利 於選擇作爲氧化鋁/氧化矽觸媒。其爲以K-觸媒,如κριό 、Κ10、KOIKS (Sud-Chemie)之名稱市售。特佳爲具有15〇 ⑼· i8nrir/g微亦禮翁抒· 5 - gOirn)之蒙脱右 ’其爲以KP10 (Sud-Chemie)之名稱市售。有利加入之觸 媒量爲相對於所使用之脂族醛之〇 〇5至3〇%重量比,較佳 以相對於所使用之脂族醛之〇 ^至以重量比。 反應有利在-401〇至40eC,較佳爲51〇至201〇之反應溫度 下進行。於3至6小時之正常轉換時間後,式j|化合物爲 以粗產物型式取得c 可如下進行操作處理:以過濾分離觸媒,其在清洗及乾 燥後可再使用、加入碳酸鉀且最後令產物蒸餾。選擇性地 ’可在蒸餘前將碳酸鉀減除並以乙醇清洗。 於第二階段中,令脂族縮醛(式ΙΠ )與下式之酚 靡專 hr «:IV A7 V. Explanation of the invention (4 / g (measured by Hg porometer) microporous volume (75-80nm)) is a good choice for alumina / silica catalyst. It is K-catalyst , Such as κριό, Κ10, KIKKS (Sud-Chemie), are commercially available. Particularly good is a montmorillon right with 15〇⑼i8nrir / g 微 亦 礼 翁 · 5-gOirn), which is based on KP10 (Sud- Chemie) is commercially available. The amount of the catalyst to be advantageously added is from 0.05 to 30% by weight relative to the aliphatic aldehyde used, and preferably from ^ to the weight ratio relative to the aliphatic aldehyde used. The reaction is favorably carried out at a reaction temperature of -401 to 40 eC, preferably 51 to 201. After a normal conversion time of 3 to 6 hours, the compound of formula j | is obtained as a crude product. C can be processed as follows: the catalyst is separated by filtration, which can be reused after washing and drying, potassium carbonate is added and finally The product was distilled. Optionally, 'K2CO3 can be removed and washed with ethanol before distillation. In the second stage, the aliphatic acetal (formula IΠ) and the phenol of the following formula are used: hr «:
L 二 J ·***.; $553 ·$Τ八 其中R3具有前述定義,於鹼存在下,惰性有機溶劑中縮 合成式I之終產物。 R3意指氫或具有1-4個碳原子之直鏈或分支烷基、具有 1 一4個破原子之直鏈或分支烷基之由垸基、具有2至4個 碳原子之直鏈或分支烯基、具有1至4個碳原子之直鏈或 分支烷基之垸氧羰基、具有1至4個碳原子之直鏈或分支 本紙張尺度適用中國國Α4—ϋ I 訂 (讀先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 經濟、那中央標準局員工消費合作社印製 A7 五、發明説明(ς ) 境基之境氧甲基、具有1至4個竣原子之燒酿基、具有1 至4個碳原子之直鍵或分支燒基之燒氧基、具有1至4個 碳原子之直鏈或分支燒基之梡績酿基、南素、胺基、具有 1至^^原子垸基之燒霜基、具有兩甸具i至2値碳原 子垸基之二烷胺基、腌、硝基或鲽基。可爲甲基、乙基、 正丙基、異丙基、正_、異_、第三-丁基、鹵甲基、鹵乙 基、卜由丙基、2-由丙基、卣基-異丙基、卜由丁基、2-由丁基、3-由丁基、1-南基-2-甲基-丙基、2-南基_2-甲 基—丙基、卣基-第三丁基、乙烯基、埽丙基、丙烯基、異 _丙烯基、丁烯基、丁-2-烯基、丁-3-埽基、異-丁-p 埽基、異-丁-2-烯基、甲氧羰基、乙氧琰基、正-、異-丙 氧羰基、正-、異-、第三-丁氧羰基、甲氧甲基、乙氧甲 基、正〜、異-丙氧甲基、正-、異-、第三丁氧甲基、甲醯 、乙醯、正_、異-丙醯、正_、異_、第三-丁醯、甲氧基 乙氧基、正-、異-、第二-丙氧基、正-、異-、第三丁 氧基、甲垸磺醢、乙垸磺醯、丙烷-3-磺醯、丙烷-2-磺醯 、丁垸-4-磺醯、丁烷-3-續醯、丁烷-2-磺醯、甲胺基、 乙胺基、二乙胺基。氟、氣和溴可被解釋作爲卣素或鹵基 取代基。若R 3爲甲醯、乙醯、甲氧羰基和乙氧羰基則爲 特佳。 轉換作用有利於觸媒量之無機或有機鹼存在下進行。碳 酸鉀(較佳爲無水的)、或氫氧化鈉爲便於使用作爲無機 鹼,而眯啶或3-甲基mt啶作爲有機鹼。若使用無水碳酸钟 則爲特佳。有利加入之鹼量爲相對於所使用之4-羥基-乙 -7 - . 本紙張尺度適用中國國家檩準(CNS ) M規格(21〇χ297公釐) (請先閲讀背面之注意事項再填寫本頁) -訂 518331 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(6 ) 驢苯以0·001至5%重量比,較佳爲相對於所使用之41虽基一 乙醯苯以0.005至0.1%重量比。 非極性有機溶劑如二甲苯或甲苯爲利於選擇作爲惰性有 機溶劑1二甲苯爲特隹f 第二階段之反應利於在90°C至180eC,便利於130¾至 150¾之間之反應溫度下進行。於總計24小時之正常的轉 換時間之後,式I化合物爲以粗產物型式取得。 可如下簡單地進行操作處理,例如:令有機相冷卻後, 其可以5% NaOH清洗並將溶劑完全蒸發。終產物其後可經 由高眞空蒸餾作用予以分離。 選擇性地,亦可未分離出中間產物(式JU )而進行轉換成 終產物(式I )。 實施例1(本發明) 1 一卜二乙氧基-3 -甲基-2-丁埽之製備 於氮氛園氣中,將1.25克未乾燥之觸媒κρ-10 (sud-Chemie)和ι89·25克原甲酸三乙酯放入燒瓶之225毫升絶對 酒精中。於5¾冷卻下,令Π0.5克3-甲基-丁烯醛歷30分 鐘逐滴加入。其後停止冷卻,令反應混合液缓慢加熱至20 •C且在加入3-甲基-丁烯醛後總計攪拌3·5小時。反應過程 爲以氣相層析予以偵測。 其後經由吸濾器令觸媒濾除並以20毫升乙醇清洗,於過 濾液中加入2·6克碳酸鉀並於眞空下蒸除乙醇(23〇 mbar/ 501〇/〇·5小時和mbar/52ec/l小時)。濾除碳酸 钟並以20毫升乙醇清洗後,令產物於187 mbar/114eC下蒸 本火張尺度通州甲囤國家檩準(CNS ) a4規格(210X297公釐) (讀先閲讀背面之注意事項再填寫本頁)L 2 J · *** .; $ 553 · $ Τ 八 Wherein R3 has the aforementioned definition, in the presence of a base, the final product of Formula I is condensed in an inert organic solvent. R3 means hydrogen or a straight-chain or branched alkyl group having 1-4 carbon atoms, a straight-chain or branched alkyl group having 1 to 4 broken atoms, a straight-chain or branched group having 2 to 4 carbon atoms Branched alkenyl, linear or branched alkoxycarbonyl group with 1 to 4 carbon atoms, linear or branched alkoxy group with 1 to 4 carbon atoms This paper is applicable to China A4—ϋ I Order (read first read Note on the back, please fill in this page again) The economy is printed by the Consumers' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs, and printed by A7 by the Consumer ’s Cooperatives of the Central Standards Bureau. 5. Description of invention (ς) Environment-based environment oxymethyl, with 1 to 4 An atomic radical, a radical having 1 to 4 carbon atoms or a branched radical, an oxygen radical having 1 to 4 carbon atoms or a straight or branched radical, a southern element, An amine group, a frost group having a fluorene group with 1 to ^^ atoms, a dialkylamino group having two fluorene groups with i to 2 carbon atoms, a salted, nitro, or fluorenyl group. May be methyl, ethyl, n-propyl, isopropyl, n-, iso-, tert-butyl, halomethyl, haloethyl, propyl, 2-propyl, fluorenyl- Isopropyl, butyl, 2-butyl, 3-butyl, 1-syl-2-methyl-propyl, 2-syl-2-methyl-propyl, fluorenyl- Tertiary butyl, vinyl, fluorenyl, propenyl, iso-propenyl, butenyl, but-2-enyl, but-3-fluorenyl, iso-but-p-fluorenyl, iso-but- 2-alkenyl, methoxycarbonyl, ethoxyfluorenyl, n-, iso-propoxycarbonyl, n-, iso-, third-butoxycarbonyl, methoxymethyl, ethoxymethyl, n- ~, iso -Propoxymethyl, n-, iso-, tertiary butoxymethyl, formamidine, acetamidine, n-, iso-propylamidine, n-, iso-, third-butylammonium, methoxyethoxy Radical, n-, iso-, second-propoxy, n-, iso-, third-butoxy, formamidinesulfonium, acetamidinesulfonium, propane-3-sulfonium, propane-2-sulfonyl , Butane-4-sulfonium, butane-3-continium, butane-2-sulfonium, methylamino, ethylamino, diethylamino. Fluorine, gas and bromine can be interpreted as halogen or halo substituents. It is particularly preferred if R 3 is formamidine, acetamidine, methoxycarbonyl and ethoxycarbonyl. The conversion is facilitated by the presence of an inorganic or organic base in the amount of catalyst. Potassium carbonate (preferably anhydrous), or sodium hydroxide is convenient for use as an inorganic base, and pyridine or 3-methyl mtidine is used as an organic base. It is especially good if you use anhydrous carbonic acid clock. The amount of alkali to be added is relative to the 4-hydroxy-ethyl-7-used. This paper size is applicable to China National Standard (CNS) M specification (21〇 × 297 mm) (Please read the precautions on the back before filling (This page)-Order 518331 Printed by the Consumer Standards Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7 V. Description of the invention (6) Donkey benzene is in a weight ratio of 0.001 to 5%, preferably relative to 41, although it is based on 1-B Benzene is in a weight ratio of 0.005 to 0.1%. Non-polar organic solvents such as xylene or toluene are favorable for selection as inert organic solvents. 1 Xylene is special. The second-stage reaction is convenient at 90 ° C to 180eC, which is convenient for reaction temperatures between 130¾ to 150¾. After a normal conversion time of a total of 24 hours, the compound of formula I was obtained as a crude product. The operation can be simply carried out as follows, for example: after cooling the organic phase, it can be washed with 5% NaOH and the solvent is completely evaporated. The final product can then be separated by high-altitude air distillation. Alternatively, the intermediate product (formula JU) can be converted into the final product (formula I) without isolation. Example 1 (Invention) 1 Preparation of diethoxy-3-methyl-2-butane in a nitrogen atmosphere, 1.25 g of undried catalyst κρ-10 (sud-Chemie) and 89.25 grams of triethyl orthoformate was placed in 225 ml of absolute alcohol in a flask. With 5¾ cooling, 0.5 g of 3-methyl-butenal was added dropwise over 30 minutes. After that, the cooling was stopped, the reaction mixture was slowly heated to 20 ° C, and after adding 3-methyl-butenal, it was stirred for a total of 3.5 hours. The reaction process was detected by gas chromatography. After that, the catalyst was filtered off through a suction filter and washed with 20 ml of ethanol. 2.6 g of potassium carbonate was added to the filtration solution and the ethanol was distilled off under a vacuum (23 mbar / 501 / 0.5 hour and mbar / 52ec / l hour). After filtering off the carbonic acid bell and washing it with 20 ml of ethanol, the product was steamed at 187 mbar / 114eC. The standard of Tongzhou Jiahuo National Standard (CNS) a4 (210X297 mm) (read the precautions on the back before reading) (Fill in this page)
、1T 經濟部中央檩準局員工消費合作社印製 518331 A7 _— ______B7_ 五、發明説明(7 ) 餾。所得之1,卜二乙氧基-3-甲基-2-丁烯蒸餾物(143·4 克’ 86·4%產率)具有97.1%之含量(於187 mbar下之滞點 :114eC ) 〇 , &u 11. Soc. Ch im. Fr. 11,2558; 1975之比較):1. Printed by the Consumer Cooperatives of the Central Procurement Bureau of the Ministry of Economic Affairs of 1T 518331 A7 __ ______B7_ V. Description of the invention (7) Distillation. The obtained 1,2-diethoxy-3-methyl-2-butene distillate (143.4 g '86 .4% yield) had a content of 97.1% (dead point at 187 mbar: 114eC) 〇, & u 11. Soc. Ch im. Fr. 11, 2558; 1975):
1,卜二乙氧基-3 -甲基-2-丁歸之製備 依據實施例1所述之步驟,但使用4克未乾燥之觸媒KSF (Aldrich)代替 1.25克未乾燥之觸媒KP-10 (sud-Chemie) ,使用37·78克之[sic]原甲酸乙酯代替189 25克,使用90 耄升乙醇代替225毫升,使用21·9克3-甲基-丁烯搭代替 110.5克並使用4克碳酸鉀代替2·6克。其產物( 29.82克 ,70·3%產率〉具有94·1%之含量。 實施例 3 (依據Thuy和Maite, Bull. Soc· Chim. Fr. 11,2558; 1975之比較): 1,1_二乙氧基-3 -甲基-2-丁烯之製備1. Preparation of didiethoxy-3 -methyl-2-butyrate was performed according to the procedure described in Example 1, but 4 g of undried catalyst KSF (Aldrich) was used instead of 1.25 g of undried catalyst KP -10 (sud-Chemie), 37.78 g of [sic] ethyl orthoformate was used instead of 189 25 g, 90 liters of ethanol was used instead of 225 ml, and 21.9 g of 3-methyl-butene substituted 110.5 g And use 4 grams of potassium carbonate instead of 2.6 grams. The product (29.82 g, 70.3% yield) has a content of 94.1%. Example 3 (based on the comparison of Thuy and Maite, Bull. Soc. Chim. Fr. 11, 2558; 1975): 1, 1 _Preparation of diethoxy-3 -methyl-2-butene
依據實施例1所述之步驟,但使用4克未乾燥之觸媒KSF (Aldrich)代替ι·25克未乾燥之觸媒[P-ίο (Sud-Chemie) 二使用37.65克之[sic]原甲酸乙酯代替189 25克,使用9〇 毫升乙醇代替225毫升,使用22·25克3-甲基-丁烯醛代替 11〇.5克並使用4克碳酸鉀代替26克。其產物(29 65克 ,69.5%產率)具有95%之含量。 實施例4 (本發明) 3_甲基-2-丁基4,3_二谔茂烷之製備 於氮氛圏氣中,將〇·5克未乾燥之觸媒以_1() (Sud_ 9 ~ ---------! (請先閲讀背面之注意事項再填寫本頁)According to the procedure described in Example 1, but using 4 g of KSF (Aldrich) catalyst instead of 25 g of catalyst [P-ίο (Sud-Chemie)] 37.65 g of [sic] orthoformic acid Ethyl acetate was used instead of 25g, 90ml ethanol was used instead of 225ml, 22.25g 3-methyl-butenal was used instead of 10.5g and 4g potassium carbonate was used instead of 26g. The product (29 65 g, 69.5% yield) has a content of 95%. Example 4 (Invention) Preparation of 3-methyl-2-butyl 4,3_dioxane in a nitrogen atmosphere, 0.5 g of an un-dried catalyst was used as _1 () (Sud_ 9 ~ ---------! (Please read the notes on the back before filling this page)
、1T, 1T
518331 A7 ____B7 五、發明説明(8 )518331 A7 ____B7 V. Description of the invention (8)
Chemie)、79·6克原甲酸三乙酯和48·2克3-甲基-丁歸塔放 入燒瓶之34.3克乙二醇中並於4¾下攪拌15小時。其後經 由吸濾器令觸媒濾除並以20毫升乙醇清洗。產物爲經由分 餾爷及^夯雨(於20T mbar/TarC T之2餘 得之3-甲基-2-丁烯-1,3-二e?茂燒餘分具有(39 2克) 和86.9% (3克)之含量(47¾產率)。 實施例5 (本發明) 6 -乙酿-2,2-二甲基-2心1-苯並〇比喃之製備 於氬氛園氣中,將83.8克4-經基乙醢苯和〇 576克無水 碳酸鉀放於600毫升二甲苯中並加熱至140¾。將162·3克 1,1-二乙氧基甲基丁稀(於乙醇中,77⑽)歷5小 時逐滴加至此沸騰溶液並繼續蒸餾所形成之乙醇。此溶液 於140eC下挽拌18小時後,令其冷卻至2〇°c並以200毫升 NaOH(5%)清洗有機相且於眞空中濃縮。將粗產物(橘色油) 於高眞空下(2·8 nbar/1431〇)蒸餾。所得之6-乙醯-2,2-二甲基-2H-1-苯並mt喃蒸餾物(90.2克,71.3%產物)具 有94.9%之含量。 實施例6 (本發明) 6-乙酿-2,2-二甲基-211-1-苯並口比喃之製備 經濟部中央標準局員工消費合作社印製 於氬氛園氣中,將60毫克未乾燥之觸媒KP-10 (Sub-Chemie)和35· 8克原甲酸三乙酯放入燒瓶之45毫升絶對酒 精中。於5¾冷卻下,將19.56克3-甲基-丁烯醛歷30分鐘 逐滴加入。其後令反應混合液於51〇下再攪拌一小時。加 入195毫克碳酸鉀、1〇〇毫升二甲苯和2〇.95克4-難基-乙婊 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 518331 A7 B7 五、發明説明(9 ) 苯後,將反應混合液加熱至140eC —小時並連績蒸除所形 成之乙醇。令溶液於140¾下再攪拌4小時。冷卻後,有 機相以NaOH (5%)清洗並濃縮。粗產物於高眞空下(0.5 mbarYmj)蒸曹。所得之該化合物餾分具有76·4% (0·91 克)和94·3% (15·8克)之含量(51.8¾產率)。 (請先聞讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)Chemie), 79.6 grams of triethyl orthoformate, and 48.2 grams of 3-methyl-butyric acid tower were placed in 34.3 grams of ethylene glycol in the flask and stirred at 4¾ for 15 hours. The catalyst was then filtered off with a suction filter and washed with 20 ml of ethanol. The product is 3-methyl-2-butene-1,3-di-eocene with a residual fraction of (39 2 g) and 86.9 g. % (3 g) content (47¾ yield). Example 5 (Invention) Preparation of 6-Ethyl-2,2-dimethyl-2oxo-1-benzopyran in argon atmosphere 83.8 g of 4-Acetomethylbenzene and 0576 g of anhydrous potassium carbonate were placed in 600 ml of xylene and heated to 140 ¾. 162.3 g of 1,1-diethoxymethylbutane (in ethanol Medium, 77⑽) was added dropwise to this boiling solution over 5 hours and the ethanol formed was continuously distilled. After stirring the solution at 140eC for 18 hours, it was cooled to 20 ° C and washed with 200 ml of NaOH (5%) The organic phase was concentrated in the air. The crude product (orange oil) was distilled under high air (2 · 8 nbar / 1431〇). The resulting 6-acetamidine-2,2-dimethyl-2H-1- Benzo mt-distillate (90.2 g, 71.3% product) has a content of 94.9%. Example 6 (Invention) 6-Ethyl-2,2-dimethyl-211-1-benzopyran The Consumer Cooperative of the Central Standards Bureau of the Ministry of Preparation and Economics printed it in argon atmosphere, and 60 mg was not dried. The catalyst KP-10 (Sub-Chemie) and 35.8 g of triethyl orthoformate were placed in 45 ml of absolute alcohol in the flask. With 5¾ cooling, 19.56 g of 3-methyl-butenal was removed for 30 minutes. Add dropwise. After that, the reaction mixture was stirred for an additional hour at 51 ° C. 195 mg of potassium carbonate, 100 ml of xylene and 20.95 g of 4-anthyl-acetamidine were added. (CNS) A4 specification (210X297 mm) 518331 A7 B7 V. Description of the invention (9) After benzene, the reaction mixture is heated to 140eC for one hour and the ethanol formed is distilled off continuously. The solution is stirred at 140¾ and then stirred for 4 hours. Hours. After cooling, the organic phase was washed with NaOH (5%) and concentrated. The crude product was steamed under high vacuum (0.5 mbarYmj). The resulting fraction of the compound had 76.4% (0.91 g) and 94.3 % (15 · 8g) content (51.8¾ yield). (Please read the notes on the back before filling out this page.) Printed on the paper standard printed by the Employees' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs, the Chinese National Standard (CNS) A4 specifications (210X297 mm)
Claims (1)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH198496 | 1996-08-13 | ||
| GBGB9620141.3A GB9620141D0 (en) | 1996-09-27 | 1996-09-27 | Process |
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| Publication Number | Publication Date |
|---|---|
| TW518331B true TW518331B (en) | 2003-01-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW86112051A TW518331B (en) | 1996-08-13 | 1997-08-22 | Process for the production of 2H-1-benzopyrans |
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| Country | Link |
|---|---|
| ID (1) | ID18740A (en) |
| TW (1) | TW518331B (en) |
-
1997
- 1997-08-20 ID IDP972908A patent/ID18740A/en unknown
- 1997-08-22 TW TW86112051A patent/TW518331B/en not_active IP Right Cessation
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| Publication number | Publication date |
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| ID18740A (en) | 1998-05-07 |
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