首页> 外文期刊>Гальванотехникаи обработка поверхностей >The Use of Non-flowing Rinsing Tanks for the Restriction of Water Consumption
【24h】

The Use of Non-flowing Rinsing Tanks for the Restriction of Water Consumption

机译:使用不流动的冲洗水箱限制用水量

获取原文
获取原文并翻译 | 示例
           

摘要

Replacement of flowing rinses by non-flowing ones with periodic dumping of the latters is one of the ways for restricting water consumption. In such an ease every rinsing tunk once filled with fresh water is operating without water exchange over a certain period of time and is dumped only, when the concentration of contaminants reaches certain critical value. After dumping the tank is filled with fresh water and the whole cycle is repeated again. Considerable reduction effect in water consumption can be reached only, if the number of such tanks equals at least two. Single flowing rinses, multistage concurrent and countercurrent rinses and reclaim tanks have been considered. If a single rinsing tank is attached to a process tank, its conversion to non-flowing rinse is not suitable. Table 1 and 2 contain data for the calculation of the duration of a single cycle of a continuous operation of two- and three-tanks system between the dumpings. The volume of each tank was taken equal to 1000 l(V_(Пр)), the surface area of treated parts per hour was taken equal to F m~2/hr, the specific dray-out (q) was assumed to be 0,2 l/m~2. Concentration of a component in process solution is designated by C_o and its limiting admissible concentration - by C_П. Water consumption per hour for rinsing is found as a ratio of the total volume of all rinsing tanks and the duration of a single cycle. In particular cases, when the actual values of C_o, V_(Пр), F and q do not coincide with those given in the tables, the latters are corrected to fit the actual situation using eq. 1. An example of the operation of the rinsing tanks under non-flowing conditions is given for the cyanide zinc-plating process (C_o 50 g/l; C_(П)0,01 g/l; q 0,31/m~2; F 1,5m~2/hr). The duration of the dumping cycle in this example is equal to 31 hr for the two rinsing tanks with V_(П) 7001 each and 169 hr for 3 similar tanks. Thus, in case of 2 tanks this cycle corresponds to 4 days and for 3 tanks it corresponds to 1 month which is very convenient from the point of view of water consumption regulation. Such a method of the regulation does not depend neither on the availability of water-controlling equipment, nor on the pressure fluctuations in the water-supplying system. The above-described approach to water-consumption regulation leads, obviously, to the regulation of the amounts of disposed liquid wastes, and long periods of operation between dumping mean higher concentrations of dissolved compounds in the waste water. A combination of these two conditions (low volumes and high concentrations) allows to create a new form of operation of waste-treatment facilities and utilize or even recuperate and return to the plating process certain valuable and high-toxic components (precious metals, chromium (Vl)- and nickel-compounds, etc.). And finally, if only deionized water is used in the plating and rinsing processes, the installation of a cascade of more than 4 non-flowing rinses allow to create a completely closed-loor process cycle.
机译:用不流动的冲洗液代替流动的冲洗液并定期倾倒冲洗液是限制用水量的方法之一。这样一来,每个装满淡水的冲洗缸都可以在一定时间内无水交换地运行,并且仅在污染物的浓度达到一定临界值时才丢弃。倾倒后,水箱将充满淡水,并再次重复整个循环。仅当这种水箱的数量至少等于两个时,才能达到显着的节水效果。已经考虑过单流冲洗,多级同时和逆流冲洗以及回收罐。如果将单个冲洗池连接到处理池,则不适合将其转换为非流动冲洗。表1和表2包含了用于计算倾倒之间两槽和三槽系统连续运行的单个周期的持续时间的数据。每个罐的容积取为1000 l(V_(Пр)),每小时处理零件的表面积取为F m〜2 / hr,比色散量(q)假定为0 ,2 l / m〜2。过程溶液中组分的浓度由C_o表示,其极限容许浓度-由C_П表示。每小时冲洗用水量是所有冲洗槽总体积与单个循环持续时间的比值。在特定情况下,当C_o,V_(Пр),F和q的实际值与表中给出的值不一致时,可以使用eq校正后者以适合实际情况。 1.给出了氰化物镀锌过程中漂洗槽在不流动条件下的运行示例(C_o 50 g / l; C_(П)0.01 g / l; q 0.31 / m〜 2; F 1,5m〜2 / hr)。在此示例中,对于每个分别具有V_(П)7001的两个冲洗水箱,倾倒周期的持续时间等于31 hr,对于三个相似水槽,倾倒周期的持续时间等于169 hr。因此,对于2个水箱,此周期对应4天,对于3个水箱,则对应1个月,从水消耗调节的角度来看,这非常方便。这种调节方法既不取决于水控制设备的可用性,也不取决于供水系统中的压力波动。上述用于调节水消耗的方法显然导致对所处置的液体废物的量的调节,并且倾倒之间的长时间操作意味着废水中溶解的化合物的浓度较高。将这两种条件(低容量和高浓度)结合起来,可以创建一种新的废物处理设施操作方式,并利用甚至回收利用某些有价值和高毒性的成分(贵金属,铬( VII)和镍化合物等)。最后,如果在电镀和漂洗过程中仅使用去离子水,则安装多于4种不流动的漂洗液可以形成一个完全封闭的落地工艺流程。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

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