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    • 4. 发明授权
    • Process for the production of non-aqueous hydrogen peroxide solutions
and their use
    • 用于生产非水过氧化氢溶液及其用途的方法
    • US4686010A
    • 1987-08-11
    • US648137
    • 1984-09-07
    • Karlheinz DrauzAxel Kleemann
    • Karlheinz DrauzAxel Kleemann
    • C07C37/58B01J27/00C01B15/017C07C27/00C07C67/00B01D3/36
    • C01B15/017
    • The production of solutions of hydrogen peroxide in phenol or its derivatives, e.g. hydrocarbyl substituted phenols, halo substituted phenols or phenol ethers, is carried out in a single step. Practically no loss of hydrogen peroxide occurs since a total distillation of hydrogen peroxide together with phenol or phenol derivative is avoided. Simultaneously the solutions obtained are practically free from water. The mixture of phenol or phenol derivative and aqueous hydrogen peroxide is treated with a material that boils below the boiling point of hydrogen peroxide, phenol or phenol derivative or forms an azeotrope with water that boils below the boiling point of hydrogen peroxide, phenol or phenol derivative and the water removed as an azeotrope. The solution of hydrogen peroxide in phenol or phenol derivative which remains behind is suitable for carrying out oxidation reactions and above all, also for hydroxylation reactions.
    • 生产苯酚或其衍生物中过氧化氢的溶液,例如 烃基取代的酚,卤代酚或苯酚醚在一个步骤中进行。 实际上不会发生过氧化氢的损失,因为避免了与苯酚或苯酚衍生物一起完全蒸馏过氧化氢。 同时获得的溶液实际上不含水。 苯酚或苯酚衍生物与过氧化氢水溶液的混合物用沸点低于过氧化氢,苯酚或苯酚衍生物的沸点的物质处理,或与沸点低于过氧化氢,苯酚或苯酚衍生物沸点的水形成共沸物 并将水作为共沸物除去。 过氧化氢在苯酚或苯酚衍生物中残留的溶液适用于进行氧化反应,尤其是羟基化反应。
    • 5. 发明授权
    • Process for the production of water-free organic hydrogen peroxide
solution
    • 生产无水有机过氧化氢溶液的方法
    • US4564514A
    • 1986-01-14
    • US510162
    • 1983-07-01
    • Karlheinz DrauzAxel KleemannRolf Wirthwein
    • Karlheinz DrauzAxel KleemannRolf Wirthwein
    • C01B15/017C01B15/023
    • C01B15/017
    • The production of organic hydrogen peroxide solutions which are practically water-free until now has had the problem of either too high a water content of the solution or too great a loss of hydrogen peroxide through decomposition and passing over as distillate during the distillative drying. By selection of specific esters in combination with commensurately high pressures in the azeotropic removal of water, these disadvantages can be avoided. Extremely low water content solutions of hydrogen peroxide in high boiling solutions are produced by mixing hydrogen peroxide solutions in solvents whose azeotropic boiling point with water is below the boiling point of hydrogen peroxide with higher boiling solvents which form the highest azeotrope with water, whose boiling point is near or above the boiling point of hydrogen peroxide. Thereupon, the mixture is freed from both water and the lower boiling solvent. The mixture can be formed by an in situ method. Production of extremely low water containing solutions of hydrogen peroxide in high boiling solvents are produced by mixing hydrogen peroxide solutions in solvents whose azeotrope boiling point with water is below the boiling point of hydrogen peroxide with higher boiling solvents which form the highest azeotrope with water, whose boiling point is near or above the boiling point of hydrogen peroxide. Thereupon, the mixture is freed from both water and the lower boiling solvent. The above-mentioned mixture can also be produced by an in situ method.
    • 迄今为止几乎无水的有机过氧化氢溶液的生产具有溶液中水含量过高或分解过程中过氧化氢过多或蒸馏干燥过程中作为馏出物流失的问题。 通过选择特定的酯与共沸去除水中相当高的压力相结合,可以避免这些缺点。 过氧化氢在高沸点溶液中的极低含水量溶液是通过将过氧化氢溶液与共沸点与水低于过氧化氢沸点的溶剂混合,通过与沸水形成最高共沸物的较高沸点溶剂混合而制得的,其沸点 接近或高于过氧化氢的沸点。 因此,混合物从水和低沸点溶剂中释放出来。 混合物可以通过原位法形成。 在高沸点溶剂中生产极低含水量的过氧化氢的溶液是通过将过氧化氢溶液与沸点高于沸点溶剂的沸点高于沸点的溶剂在水中沸点高于沸点的溶剂混合, 沸点接近或高于过氧化氢的沸点。 因此,混合物从水和低沸点溶剂中释放出来。 上述混合物也可以通过原位法制备。
    • 6. 发明授权
    • Process for the production of non-aqueous hydrogen peroxide solutions
and their use
    • 用于生产非水过氧化氢溶液及其用途的方法
    • US4760199A
    • 1988-07-26
    • US81366
    • 1987-08-04
    • Karlheinz DrauzAxel Kleemann
    • Karlheinz DrauzAxel Kleemann
    • C07C37/58B01J27/00C01B15/017C07C27/00C07C67/00C07C37/60
    • C01B15/017
    • The production of solutions of hydrogen peroxide in phenol or its derivatives, e.g. hydrocarbyl substituted phenols, halo substituted phenols or phenol ethers, is carried out in a single step. Practically no loss of hydrogen peroxide occurs since a total distillation of hydrogen peroxide together with phenol or phenol derivative is avoided. Simultaneously the solutions obtained are practically free from water. The mixture of phenol or phenol derivative and aqueous hydrogen peroxide is treated with a material that boils below the boiling point of hydrogen peroxide, phenol or phenol derivative or forms an azeotrope with water that boils below the boiling point of hydrogen peroxide, phenol or phenol derivative and the water removed as an azeotrope. The solution of hydrogen peroxide in phenol or phenol derivative which remains behind is suitable for carrying out oxidation reactions and above all, also for hydroxylation reactions. The latter as especially advantageously carried out in the presence of sulfur-, selenium-, or tellurium oxide.
    • 生产苯酚或其衍生物中过氧化氢的溶液,例如。 烃基取代的酚,卤代酚或苯酚醚在一个步骤中进行。 实际上不会发生过氧化氢的损失,因为避免了与苯酚或苯酚衍生物一起完全蒸馏过氧化氢。 同时获得的溶液实际上不含水。 苯酚或苯酚衍生物与过氧化氢水溶液的混合物用沸点低于过氧化氢,苯酚或苯酚衍生物的沸点的物质处理,或与沸点低于过氧化氢,苯酚或苯酚衍生物沸点的水形成共沸物 并将水作为共沸物除去。 过氧化氢在苯酚或苯酚衍生物中残留的溶液适用于进行氧化反应,尤其是羟基化反应。 后者特别有利地在硫,硒或氧化碲的存在下进行。