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Production of high-purity hydrogen peroxide solution for use in electronics industry

机译:生产用于电子行业的高纯度过氧化氢溶液

摘要

Process for producing a high-purity aqueous hydrogen peroxide (H2O2) solution comprises passing a distilled and purified aqueous H2O2 solution through an ion-exchange column packed with cation and anion exchangers at a liquid hourly space velocity (LHSV) of 15-60 and a temperature of -5 to 15 deg C. The cation exchanger is a strongly acidic cation-exchange resin with a degree of crosslinking of at least 10%. The anion exchanger is a strongly basic anion-exchange resin in carbonate or bicarbonate form. The column has internal walls and fractionation elements made of a fluorinated resin. Preferably the solution is contacted with the cation exchanger before the anion exchanger or before and after the anion exchanger. The starting solution is produced by distilling a crude H2O2 solution, containing organic and inorganic impurities, in a bottom-fed distillation column whose internal walls and fractionation elements are made of a fluorinated resin, in which the overhead stream (OHS) is withdrawn without reflux and replaced by ultrapure water (UPW) in a UPW/(OHS-UPW) ratio of 0.1-20 and the purified H2O2 solution is withdrawn from the middle of the column. The crude solution contains 20-60% H2O2, 10-300 ppm total organic carbon and 5-500 ppm inorganic impurities. The distillation column is equipped with a downflow reboiler. The cation exchanger is a macroporous resin, preferably a divinylbenzene-crosslinked polystyrene resin with sulphonic acid groups. The anion exchanger is a macroporous resin, preferably a polystyrene resin with quaternary ammonium groups.
机译:生产高纯度过氧化氢(H2O2)水溶液的方法包括:将蒸馏和纯化的H2O2水溶液以15-60的液时空速(LHSV)通过装有阳离子和阴离子交换剂的离子交换柱。温度为-5至15摄氏度。阳离子交换剂是一种强酸性阳离子交换树脂,其交联度至少为10%。阴离子交换剂是呈碳酸盐或碳酸氢盐形式的强碱性阴离子交换树脂。该塔具有内壁和由氟化树脂制成的分馏元件。优选地,溶液在阴离子交换剂之前或在阴离子交换剂之前和之后与阳离子交换剂接触。通过在底部进料的蒸馏塔中蒸馏含有有机和无机杂质的粗制H2O2溶液来生产起始溶液,该蒸馏塔的内壁和分馏元件由氟化树脂制成,其中塔顶物流(OHS)无需回流即可取出并以UPW /(OHS-UPW)之比为0.1-20的超纯水(UPW)代替,然后从塔中取出纯化的H2O2溶液。粗溶液包含20-60%的H2O2、10-300 ppm的总有机碳和5-500 ppm的无机杂质。蒸馏塔配备有下流再沸器。阳离子交换剂是大孔树脂,优选具有磺酸基的二乙烯基苯交联的聚苯乙烯树脂。阴离子交换剂是大孔树脂,优选具有季铵基团的聚苯乙烯树脂。

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