The main component is made of turpentine massoniana α- pinene, wherein的简体中文翻译

The main component is made of turpe

The main component is made of turpentine massoniana α- pinene, wherein L-α- pinene ee values ​​between 40 and 36% to 50%, optical purity is not high, the conventional method has poor resolution, back to purified difficult. It has been reported by catalytic hydrogenation of 36, 100% conversion, 38-cis-pinane selectivity of 98.3%. in 37 L-β- pinene turpentine Pinus elliottii higher levels can reach 20% to 35%, and after distillation of commercially ee of 37 may be up to 92.1% have been reported in diethylene glycol dimethyl ether with sodium borohydride, boron trifluoride reduction of L-β- pinene, 98 can % obtained in a yield of cis-pinane 38. the pyrolysis step 38, has been reported at a cracking temperature of 580 ℃, dihydromyrcenyl 39 content in the product can reach 71.2%. step preparation of dextrose citronella alcohol 40, has been reported with malonic acid and sodium borohydride malonyloxyborohydride generated by the reaction of sodium borohydride, reaction at 60 deg.] C in THF with 39 in 6 h, the reaction occurs in 100% of the terminal double bond, oxidation 40 mass fraction of 90%, and did not find one generation. the fourth step selectively oxidized with oxygen to give dextrorotatory hydroxy at catalytic tetrapropylammonium perruthenate 4 Mao aldehyde, yield 91% following step process consistent with Takasago (Scheme 10). This route convenient source of starting material, the yield of each step are high, industrial prospects clear [4].
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结果 (简体中文) 1: [复制]
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的主要成分是由松节油马尾松α-蒎烯,其中40和36之间%至50%L-α-蒎烯EE值,光学纯度不高,常规方法具有分辨率差,回纯化困难。已经报道由36催化氢化,转化率为100%,98.3%38顺式 - 蒎烷的选择性。在37 L-β-蒎烯松节油湿地松更高水平可达到20%至35%,和37市售EE的蒸馏后可达到92.1%的二甘醇二甲醚与硼氢化钠,三氟化硼的减少已经报道L-β-蒎烯,顺式蒎烷38.热解步骤38的收率得到98%罐,已报道在580的裂化温度℃,在产品二氢月桂39含量可达到71.2%。右旋糖醇香茅40的步骤制备,已经报道与丙二酸和硼氢化钠丙二酰氧基硼氢化钠的反应,反应在60℃下生成的。下在THF中用39在6小时,发生在末端双键的100%时,氧化的40质量分数的反应90%,并没有找到一个世代。与氧选择性氧化的第四步骤,得到右旋的羟基在催化四丙基过钌酸铵4茅醛,收率91%以下步骤的过程与高砂(方案10)是一致的。这条路线的原料的方便来源,每一步的产率是明确的。[4]高,工业前景。90%的氧化40质量分数,并没有找到一个世代。与氧选择性氧化的第四步骤,得到右旋的羟基在催化四丙基过钌酸铵4茅醛,收率91%以下步骤的过程与高砂(方案10)是一致的。这条路线的原料的方便来源,每一步的产率是明确的。[4]高,工业前景。90%的氧化40质量分数,并没有找到一个世代。与氧选择性氧化的第四步骤,得到右旋的羟基在催化四丙基过钌酸铵4茅醛,收率91%以下步骤的过程与高砂(方案10)是一致的。这条路线的原料的方便来源,每一步的产率是明确的。[4]高,工业前景。
正在翻译中..
结果 (简体中文) 2:[复制]
复制成功!
The main component is made of turpentine massoniana α- pinene, wherein L-α- pinene ee values ​​between 40 and 36% to 50%, optical purity is not high, the conventional method has poor resolution, back to purified difficult. It has been reported by catalytic hydrogenation of 36, 100% conversion, 38-cis-pinane selectivity of 98.3%. in 37 L-β- pinene turpentine Pinus elliottii higher levels can reach 20% to 35%, and after distillation of commercially ee of 37 may be up to 92.1% have been reported in diethylene glycol dimethyl ether with sodium borohydride, boron trifluoride reduction of L-β- pinene, 98 can % obtained in a yield of cis-pinane 38. the pyrolysis step 38, has been reported at a cracking temperature of 580 ℃, dihydromyrcenyl 39 content in the product can reach 71.2%. step preparation of dextrose citronella alcohol 40, has been reported with malonic acid and sodium borohydride malonyloxyborohydride generated by the reaction of sodium borohydride, reaction at 60 deg.] C in THF with 39 in 6 h, the reaction occurs in 100% of the terminal double bond, oxidation 40 mass fraction of 90%, and did not find one generation. the fourth step selectively oxidized with oxygen to give dextrorotatory hydroxy at catalytic tetrapropylammonium perruthenate 4 Mao aldehyde, yield 91% following step process consistent with Takasago (Scheme 10). This route convenient source of starting material, the yield of each step are high, industrial prospects clear [4].
正在翻译中..
结果 (简体中文) 3:[复制]
复制成功!
主要成分为松节油马尾松α-蒎烯,其中L-α-蒎烯ee值在40%-36%-50%之间,光学纯度不高,常规方法分辨率差,回纯化困难。报道了催化加氢36,100%转化率,38顺式蒎烷选择性为98.3%。在37种L-β-松节油中,松节油的含量可高达20%~35%,经工业蒸馏后37种ee可高达92.1%,在二甘醇二甲醚中用硼氢化钠、三氟化硼还原L-β-松节油,可得到98%的顺式蒎烷38。报道了裂解步骤38,在580℃的裂解温度下,产物中二氢月桂烯39的含量可达71.2%。报道了葡萄糖香茅醇40的分步制备,用丙二酸和硼氢化钠反应生成硼氢化钠丙二氧基硼氢化钠,在60℃下与39反应6h,反应发生在100%的末端双键上,氧化40质量分数为90%,却找不到一代人。第四步用氧气选择性氧化,在催化四丙基氨perruthenate 4 Mao醛上生成右旋羟基,步骤工艺符合Takasago(方案10)。该路线原料来源方便,各步骤收率高,产业前景明显[4]。<br>
正在翻译中..
 
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