首页> 外国专利> STEIN HALL ADHESIVES With high dry matter content and methods of making STEIN HALL ADHESIVES With high solids

STEIN HALL ADHESIVES With high dry matter content and methods of making STEIN HALL ADHESIVES With high solids

机译:高干物质含量的斯坦霍尔胶粘剂及高固体含量的斯坦霍尔胶粘剂的制备方法

摘要

1.method u043fu043eu043bu0443u0447u0435u043du0438u00a0 u043au043bu0435u00a0 stein hall, including the stages of: obtaining portions u043du043eu0441u0438u0442u0435u043bu00a0 by u043au043bu0435u0439u0441u0442u0435u0440u0438u0437u0430u0446u0438u0438 in an alkaline medium, at least a part of the total amounts and starch in the glue; dilution of u043du043eu0441u0438u0442u0435u043bu00a0 certain amount of water; and adding u043eu0441u0442u0430u0432u0448u0435u0433u043eu0441u00a0 secondary starch, where in the first stage u0443u043fu043eu043cu00a0u043du0443u0442u0443u044e portion but u0441u0438u0442u0435u043bu00a0 receive in the use of lye.and in the second stage of u043du043eu0441u0438u0442u0435u043bu00a0 u0440u0430u0437u0431u0430u0432u043bu00a0u044eu0442 certain amount of water with the addition of at least portions of secondary starch, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 order what glue stein hall with a high content of dry matter produced using a mixing tank, where in the first stage of u043du043eu0441u0438u0442u0435u043bu00a0 u0443u043fu043eu043cu00a0u043du0443u0442u0443u044e floor hope in a mixing tank.and in the third stage u043eu0441u0442u0430u0432u0448u0443u044eu0441u00a0 alkaline u0434u043eu0431u0430u0432u043bu00a0u044eu0442 diluted with secondary starch.;2. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the addition of u043eu0441u0442u0430u0432u0448u0438u0445u0441u00a0 secondary starch and alkali u043fu0440u043eu0432u043eu0434u00a0u0442 u043fu043eu0441u0442u0430u0434u0438u0439u043du043e.;3. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 2, so that the addition of alkali, and starch u043fu0440u043eu0432u043eu0434u00a0u0442 at least in two stages.;4. way on any of the u043fu043f.1 - 3, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 so that, during the first stage receives a u043du043eu0441u0438u0442u0435u043bu00a0 containing from 2 to 9% of the total u0441u043eu0434u0435u0440u0436u0430u043du0438u00a0 starch by u043fu0435u0440u0435u043cu0435u0448u0438u0432u0430u043d u0438u00a0 starch with water and alkali until the starch will be u043au043bu0435u0439u0441u0442u0435u0440u0438u0437u043eu0432u0430u043d.;5. way on any of the u043fu043f.1 - 3, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 so that at the first stage of the content of alkali in the portions u043du043eu0441u0438u0442u0435u043bu00a0 usually less than 2 / 3 of the total number of required u0434u043bu00a0 received u043du0438u00a0 compositions u043au043bu0435u00a0.;6. way on any of the u043fu043f.1 - 3, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, however, that in the second stage of u043du043eu0441u0438u0442u0435u043bu00a0 u0440u0430u0437u0431u0430u0432u043bu00a0u044eu0442 volume of water corresponding to 60 to 85 per cent of the u043du043eu0441u0438u0442u0435u043bu00a0.;7. way on any of the u043fu043f.1 - 3, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, at the second stage u0434u043eu0431u0430u0432u043bu00a0u044eu0442 from 50 to 75% of secondary starch.;8. way on any of the u043fu043f.1 - 3, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 so that, after the third stage of u0434u043eu0431u0430u0432u043bu00a0u044eu0442 drill.;9. glue stein hall with high dry matter content, obtained by means of any of the preceding paragraph., u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 in that it contains from 32 to 45% u043du0430u0442u0438u0432u043du043eu0433u043e or stabilized starch; ratio of starch - u043du043eu0441u0438u0442u0435u043bu00a0 and secondary starch u0441u043eu0441u0442u0430u0432u043bu00a0u0435u0442 from 1: 50 to 1 : 11; has u0432u00a0u0437u043au043eu0441u0442u044cu044e on bauer from 21 to 60; and u043au043eu043du0446u0435u043du0442u0440u0430u0446u0438u00a0 lye in the glue is u0434u043bu00a0 u043eu0431u0435u0441u043fu0435u0447u0435u043du0438u00a0 sgp in the range from 45 to 53u0441.;10. glue stein hall with high dry matter content in u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 p.9, so that u043du0430u0442u0438u0432u043du044bu0439 or stabilized starch obtained from the u043au0440u0430u0445u043cu0430u043bu043eu0432 grains, clu bnei or roots.
机译:1.方法 u043f u043e u043b u0443 u0447 u0435 u043d u0438 u00a0 u043a u043b u0435 u00a0 stein大厅,包括以下步骤:获取部分 u043d u043d u043e u0441 u0438 u0442 在碱性介质中,至少要占总量和淀粉中的至少一部分,并且其中至少一部分是淀粉中的一部分胶水; u043d u043e u0441 u0438 u0442 u0435 u043b u00a0稀释一定量的水;并添加 u043e u0441 u0442 u0430 u0432 u0448 u0435 u0433 u043e u0441 u00a0辅助淀粉,其中在第一阶段 u0443 u043f u043e u043c u00a0 u043d u0443 u0442 u0443 u044e部分,但 u0441 u0438 u0442 u0435 u043b u00a0接收使用碱液,并且在第二阶段的 u043d u043e u0431 u0441 u0438 u0442 u0435 u043b u043b u00a0 u0440 u0430 u0437 u0431 u0430 u0432 u043b u00a0 u044e u0442一定量的水,并至少添加一部分二次淀粉, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0订购使用混合罐生产的具有高干物质含量的胶水施胶大厅,其中在第一阶段中, u043d u043e u0441 u0438 u0442 u0435 u043b u00a0 u0443 u043f u043e u043c u00a0 u043d u0443 u0442 u0443 u044e底部希望放在混合槽中,并在第三阶段 u043e u0441 u0442 u0430 u0432 u0448 u0443 u044e u0441 u0441 u00a0碱性 u0434 用二次淀粉稀释的u043e u0431 u0430 u0432 u043b u00a0 u044e u0442; 2。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,以便添加 u043e u0441 u0442 u0430 u0432 u0448 u0438 u0445 u0441 u00a0次级淀粉和碱 u043f u0440 u043e u0432 u043e u0434 u0431 u0441 u0442 u0430 u0434 u0438 u0439 u0439 u043d u043e。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 2的方法,以便添加碱和淀粉 u043f u0440 u043e u043e u0432 u043e u0434 至少分两个阶段; 4。 u043f u043f.1-3中的任何一个的方式, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0,以便在第一阶段接收到 u043d u043e u0441 u0438 u0442 u0435 u043b u00a0包含 u0441 u043e u0434 u0435 u0440 u0436 u0430 u043d u0438 u00a0淀粉总量中2%至9%的 u043f u0435 u0440 u0435 u043c u0435 u0448 u0438 u0432 u0430 u043d u0438 u00a0用水和碱将淀粉煮成 u043a u043b u0435 u0439 u0441 u0442 u0432 u0435 u0440 u0438 u0437 u043e u0432 u0430 u043d。; 5。 u043f u043f.1-3上的任何方式, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0,以便在第一阶段中 u043d u043e u0441 u0438 u0442 u0435 u043b u00a0的部分通常少于所接收的 u0434 u043b u00a0总数的2 / 3 u043d u0438 u00a0成分 u043a u043b u0435 u00a0。; 6。 u043f u043f.1-3中的任何一个, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0上的路径,但是,在 u043d 第二阶段u043e u0441 u0438 u0442 u0435 u043b u00a0 u0440 u0430 u0437 u0431 u0430 u0432 u043b u00a0 u044e u0442的水量相当于 u043d u043e 的60%至85% u0441 u0438 u0442 u0435 u043b u00a0。; 7。 u043f u043f.1-3, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0中的任何一个,在第二阶段 u0434 u043e u0431 从50%到75%的二次淀粉中; 8。 u043f u043f.1-3中的任何一个的方式, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0,这样,在 u0434 u043e的第三阶段之后 u0431 u0430 u0432 u043b u00a0 u044e u0442钻头;; 9。通过上一段落中的任何一个获得的具有高干物质含量的胶水斯坦斯坦大厅。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0其中包含32至45% u043d u0430 u0442 u0438 u0432 u043d u043e u0433 u043e或稳定的淀粉;淀粉- u043d u043e u0441 u0438 u0442 u0435 u043b u00a0与次生淀粉 u0441 u043e u0441 u0442 u0430 u0432 u043b u00a0 u0435 u0442的比例为1:50至1: 11;鲍尔(bauer)的 u0432 u00a0 u0437 u043a u043e u0441 u0442 u044c u044e从21到60;和 u043a u043e u043d u0446 u0435 u043d u0442 u0440 u0430 u0446 u0438 u00a0胶水中的碱液是 u0434 u043b u00a0 u043e u0431 u0435 u0441 u043f u0435 0 u0435 u043d u0438 u00a0 sgp的范围是45到53 u0441。; 10。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 p.9中具有高干物质含量的胶斯坦霍尔,因此 u043d u0430 u04430 u044a u0438 u0432 u043d u044b u0439或从 u043a u0440 u0430 u0445 u043c u0430 u043b u043e u043e谷物,根茎或根获得的稳定淀粉。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号