首页> 外国专利> VERFAHREN UND VORRICHTUNG ZUR AUFBEREITUNG UND DESINFEKTION VON SCHWIMM- UND BADEBECKENWASSER UNTER VERWENDUNG VON CHLOR UND OZON

VERFAHREN UND VORRICHTUNG ZUR AUFBEREITUNG UND DESINFEKTION VON SCHWIMM- UND BADEBECKENWASSER UNTER VERWENDUNG VON CHLOR UND OZON

机译:用氯和臭氧处理和消毒游泳池水和废水的方法和装置

摘要

Ozone treatment of the bathing water removed from the pool (1) is conventionally effected with the very high ozone quantities of 0.5 - 1.5 g/h of ozone in 45 - 50 l/h of (pre-treated) air per 1 m3/h of raw water, and requires a specific and aerated ozonization reactor for contact times of up to 1.5 minute and a downstream ozone eliminator for reducing the ozone content of the water to below 0.02 g ozone/m3 of raw water before the latter is chlorinated and returned to the pool. This conventional ozone treatment necessitates huge investment and expenditure energy. In contrast, it is sufficient to use a proposed ozone quantity of 1% by using 1 - 1.2 g/h of ozone in 700 l/h of (untreated) air from a handy ozoniser (7) having this capacity per 100 m3 of raw water. Ozone treatment is effected without an ozone reactor and eliminator directly and under pressure in the pipe (2) of the raw water flow (Q). For this, the ozone-containing air is swirled together with a partial flow (q) of the raw water in a flow spiral (9) into an aerosol-like blended state and injected into the main flow of the raw water. The high interphases thus obtaind provide rapid ozone treatment with a quantitative ozone consumption. The uncomplicated conversion of baths having an originally purely chlorination-type operation to the ozone/chlorine treatment method of the invention enables the expenditure on chemicals to be reduced by up to 70%, while offering at the same time a significant improvement in the quality of the water.
机译:从池(1)中取出的沐浴水的臭氧处理通常采用每1 m3 / h的45-50 l / h(预处理)空气中0.5-1.5 g / h的非常高的臭氧量进行原水,并且需要一个专用的充气臭氧化反应器来进行长达1.5分钟的接触时间,以及一个下游的臭氧消除器,用于将水的臭氧含量降低至0.02 g臭氧/ m3以下,然后再对其进行氯化和回流到游泳池。这种常规的臭氧处理需要大量的投资和支出能量。相比之下,在每100立方米的原始臭氧发生器中,在700 l / h的(未经处理的)空气中使用1-1.2 g / h的臭氧(建议使用的臭氧量)就足够了,建议的臭氧量为100立方米水。在没有臭氧反应器和消除器的情况下,直接在原水流(Q)的管道(2)中加压进行臭氧处理。为此,含臭氧的空气与原水的部分流(q)一起以螺旋流(9)的形式涡旋成气溶胶状的混合状态,并注入原水的主流中。由此获得的高相间提供了具有定量臭氧消耗的快速臭氧处理。将本来具有纯粹纯氯化类型的操作的浴简单地转换为本发明的臭氧/氯处理方法,可以使化学品支出减少多达70%,同时显着提高了水的质量。水。

著录项

  • 公开/公告号DE3790094D2

    专利类型

  • 公开/公告日1990-07-19

    原文格式PDF

  • 申请/专利权人 TAMIR SHLOMO 6000 FRANKFURT DE;

    申请/专利号DE19873790094T

  • 发明设计人 TAMIR SHLOMO 6000 FRANKFURT DE;

    申请日1987-02-13

  • 分类号C02F1/78;C02F1/76;

  • 国家 DE

  • 入库时间 2022-08-22 06:10:39

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