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METHOD FOR PRODUCING ANTIBACTERIAL and antioxidant fraction from the buckthorn seed (HIPPOPHAE RHAMNOIDES L.)

机译:从沙棘种子(Hippophae Rhamnoides L.)生产抗菌和抗氧化剂成分的方法

摘要

1. method u043fu043eu043bu0443u0447u0435u043du0438u00a0 u0430u043du0442u0438u0431u0430u043au0442u0435u0440u0438u0430u043bu044cu043du043eu0439 factions of the innovative parts u043eu0431u043bu0435u043fu0438u0445u0438 (latvian private company rhamnoides l.) for the stage;(i) which u0441u0435u043cu00a0u043d u043eu0431u043bu0435u043fu0438u0445u0438 (latvian private company rhamnoides l.) water u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 any u0437u0435u043cu043bu00a0u043du043eu0433u043e and outside material, followed by drying.;(ii) the use u0441u0435u043cu00a0u043d dried in powder and particle size of 60 to 80 u043cu0435u0448.,;(iii) extractions of dried u0441u0435u043cu00a0u043d u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0u043cu0438 u043bu0435u043eu0442u0440u043eu043fu043du043eu0439 series in u043fu043eu0440u00a0u0434u043au0435 u0443u0432u0435u043bu0438u0447u0435u043du0438u00a0 effect u044du043bu044eu0438u0440u043eu0432u0430u043du0438u00a0 with subsequent least read several others methanol. the teachings of;(iv) filtering the extract obtained u0434u043bu00a0 u0443u0434u0430u043bu0435u043du0438u00a0 any particles and u043fu043eu043bu0443u0447u0435u043du0438u00a0 extract not containing particles;(v) u0434u0438u0441u0442u0438u043bu043bu00a0u0446u0438u044e extract not containing particles u0434u043bu00a0 regeneration of solvent;(vi) the concentration of u0434u0438u0441u0442u0438u043bu043bu0438u0440u043eu0432u0430u043du043du043eu0433u043e extract not containing particles in a vacuum to obtain crude u043cu0435u0442u0430u043du043eu043bu044cu043du043eu0433u043e extract.;(vii) drying a concentrated crude extract with an extract from u0430u043du0442u0438u0431u0430u043au0442u0435u0440u0438u0430u043bu044cu043du043eu0439 and / or u0430u043du0442u0438u043eu043au0438u0441u043bu0438u0442u0435u043bu044cu043du043eu0439 activity.;2. method for 1, in which the seeds u043eu0431u043bu0435u043fu0438u0445u0438 washed running water and then dried at 40 - between for 3 to 4 hours.;3. method for 1, in which the extractions of u0441u0435u043cu00a0u043d u043fu0440u043eu0432u043eu0434u00a0u0442 in the extractor u0441u043eu043au0441u043bu0435u0442u0430 at a temperature of 55 60u0441 for 8 to 9 hours.;4. method for 1, in which the filtrate extract u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 using filter paper Whatman no. 41.;5. method for 1, in which u043fu0435u0440u0435u0433u043eu043du043au0443 u043fu0440u043eu0432u043eu0434u00a0u0442 in u0434u0438u0441u0442u0438u043bu043bu00a0u0446u0438u043eu043du043du043eu0439 installation with 60 - ranging on the temperature u043au0438u043fu0435u043du0438u00a0 u0434u043bu00a0 regeneration of 80 - 90% of u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0.;6. method for u0440u0435u0446u0438u0440u043au0443u043bu0438u0440u0443u044eu0442 p.5, which u0440u0435u0433u0435u043du0435u0440u0438u0440u043eu0432u0430u043du043du044bu0439 solvent in extractor u0441u043eu043au0441u043bu0435u0442u0430 u0434u043bu00a0 u043fu0440u043eu0432u0435u0434u0435u043du0438u00a0 further extraction.;7. method for 1, in which the extract, containing particles, are concentrating in a vacuum at a pressure of 200 - 250 mbar and evaporator temperature 45 between receipt of raw u043cu0435u0442u0430u043du043eu043bu044cu043d wow extract.;8. method for 1, in which a drying concentrated crude extract u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 u0432u044bu043cu043eu0440u0430u0436u0438u0432u0430u043du0438u0435u043c gaining faction with the u0430u043du0442u0438u043eu043au0438u0441u043bu0438u0442u0435u043bu044cu043du043eu0439 activity.;9. method for 1, in which a drying concentrated crude extract u043fu0440u043eu0432u043eu0434u00a0u0442 vacuum furnace at a pressure of 175 - 200 mbar and 40 between during 8 - 9 hours to obtain the faction has the next u0430u043du0442u0438u0431u0430u043au0442u0435u0440u0438u0430u043bu044cu043du043eu0439 activity.
机译:1.方法 u043f u043e u043b u0443 u0447 u0435 u043d u0438 u00a0 u0430 u043d u0442 u0438 u0431 u0430 u043a u0442 u0435 u0435 u0440 u0438 u0430 u043b u044c u043d u043e u0439创新零件的派系 u043e u0431 u043b u0435 u043f u0438 u0445 u0438(拉脱维亚私人公司rhamnoides l。)为舞台;(i)其中 u0441 u0435 u043c u00a0 u043d u043e u0431 u043b u0435 u043f u0438 u0445 u0438(拉脱维亚私人公司rhamnoides l。)水 u0434 u043b u00a0 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0任何 u0437 u0435 u043c u043b u00a0 u043d u043e u0433 u043e和外部材料,然后干燥。(ii)使用 u0441 u0435 u043c u00a0 u043d以粉末形式干燥,粒径为60至80 u043c u0435 u0448。;;(iii)提取干的 u0441 u0435 u043c u00a0 u043d u0440 u0430 u0441 u0442 u0432 u0432 u043e u0440 u0438 u0442 u0435 u043b u043b u00a0 u043c u0438 u043b u0435 u043e u0442 u0440 u043e u043f u043d u043d u043e u0439系列 u043f u043e u0440 u00a0 u0434 u043a u0435 u0443 u0432 u0435 b u0438 u0447 u0435 u043d u0438 u00a0效果 u044d u043b u044e u0438 u0440 u043e u0432 u0430 u043d u0438 u00a0,随后至少要阅读其他几种甲醇。 (iv)过滤得到的提取物 u0434 u043b u00a0 u0443 u0434 u0430 u043b u0435 u043d u0438 u00a0任何粒子和 u043f u043e u043b u043b u0443 u0447 u0435 u043d u0438 u00a0提取物不含颗粒;(v) u0434 u0438 u0441 u0442 u0438 u043b u043b u00a0 u0446 u0438 u044e提取物不含颗粒 u0434 u043b u00a0溶剂再生;(vi )真空中不含颗粒的 u0434 u0438 u0441 u0442 u0438 u043b u043b u043b u0430 u04d u043d u043e u0432 u0432 u043e u0433 u043e的浓度以获得粗制的 u043c u0435 u0442 u0430 u043d u043e u043b u043c u043d u043e u0433 u043e提取物。(vii)用来自 u0430 u043d u0442 u0438 u0431 u0430 的提取物干燥浓缩的粗提取物u043a u0442 u0435 u0440 u0438 u0430 u043b u044c u043d u043e u0439和 /或 u0430 u043d u0442 u0438 u043e u043a u0438 u0441 u043b u0438 u0442 u043d u043b u044c u043d u043e u0439活动; 2。 1的方​​法,其中种子 u043e u0431 u043b u0435 u043f u0438 u0445 u0438洗净流水,然后在40-之间干燥3至4小时。3。 1的方​​法,其中提取器中的 u0441 u0435 u043c u00a0 u043d u043f u0440 u043e u0432 u043e u0434 u00a0 u0442的提取物 u0441 u043e u043e u043a u0441 u043b u0435在55 60 60 8 4小时; 4。 1的方​​法,其中滤液使用滤纸Whatman No.提取 u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u00a0 u044e u0442。 41.; 5。 1的方​​法,其中 u0434 u0438 u0441 u0442中的 u043f u0435 u0440 u0435 u0433 u043e u043d u043a u043a u0443 u043f u0440 u043e u043e u0432 u043e u0434 u00a0 u0442 u0438 u043b u043b u00a0 u0446 u0438 u043e u043d u043d u043e u0439安装温度为60-范围为温度 u043a u0438 u043f u0435 u043d u0438 u00a0 u0434 u043b u00a0 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0438 u0442 u0435 u043b u00a0的80-90%; 6。 u0440 u0435 u0446 u0438 u0440 u043a u0443 u043b u0438 u0440 u0443 u044e u0442第5页的方法,其中 u0440 u0435 u0433 u0435 u0435 u043d u043d u0435 u0440 u0438 u0440 u043e u0432 u0430 u043d u043d u044b u0439萃取器中的溶剂 u0441 u043e u043a u0441 u043b u0435 u0442 u0430 u0434 u043b u00a0 u043f u0440 u043e u0432 u0434 u0435 u043d u0438 u00a0进一步提取; 7。 1的方​​法,其中包含颗粒的提取物在200-250 mbar的压力下于真空中浓缩,蒸发器温度为45,在接收到原始的 u043c u0435 u0442 u0430 u04d u043d u043e u043b u044c 提取物; 8。 1的方​​法,其中干燥浓缩的粗提物 u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u00a0 u044e u0442 u0432 u044b u043c u043c u043e u0440 u0430 u0436 u0438 u0432 u0430 u043d u0438 u0435 u043c与 u0430 u043d u0442 u0438 u043e u043a u0438 u0441 u043b u0438 u0442 u0435 u043b u043c u043d u043c u0439活动;; 9。 1的方​​法,其中在175-200 mbar和40之间的压力下,在8-9个小时内干燥浓缩的粗提取物 u043f u0440 u043e u0432 u043e u0434 u00a0 u0442下一个 u0430 u043d u0442 u0438 u0431 u0430 u043a u0442 u0435 u0440 u0438 u0430 u043b u043c u043c u043d u043e u0439活动。

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