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阳离子交换树脂的使用方法
1离子反应的效率是按极数增加的.举例:在标准流量下,假若1公升离子可以处理50升水的话,5公升离子就可以处理500升水,10公升能处理5吨水,15公升离子就可能处理15吨水.(以上数据举例说明,不准确.)
The efficiency of 1 ion reaction is increased according to very few. For example: in the standard flow, if 1 liter ion can handle 50 litres of water then, 5 liters of ion can handle 500 litres and 10 litres to handle 5 tons of water, 15 liters of ion can handle 15 tons of water. The above data (for example, not accurate.)
2阳离子商品状态都是钠型的.交换后的水呈碱性(详见本人的另一个帖子:给米老三的实验)因为钠型在每交换一个钙镁离子时相应的释放一个钠在水中,所以在碳酸盐硬度下降的同时PH要上升.
2, the state of cationic products is all sodium type. The water after exchange is alkaline. (see another thread in my post: give the experiment to MI Lao 3), because sodium type releases a sodium in water in every exchange of a calcium and magnesium ion, so when the hardness of carbonate decreases, PH will go up.
3使用阳离子得到软水时必须转型. 将钠型阳离子转为氢型,转型过程相对难度较大.简单介绍一下, 一酸\一碱\一酸\转为氢型. 一碱\一酸\一碱\又换原成钠型. 反应液配比为盐酸浓度:原液39%浓度稀释到8%浓度酸液. 反应液配比碱液浓度:97%含量干燥片碱兑制成7%浓度碱液. 酸液按每小时1.5-2.0吨量通过离子,然后纯水清洗到PH值为3.5左右. 同流量碱液通过离子,PH洗至14左右. 同流量再经过酸液,最后纯水洗至PH4.5以上即可. 转型的反应时间为每次25分钟.
3 the use of soft water must get cationic transition. The sodium cation into hydrogen, the transformation process relatively difficult. A brief introduction, a \ \ a acid alkali acid into a hydrogen type. \ \ \ alkali acid alkali and put into a \ sodium ratio of reaction solution of hydrochloric acid concentration. 39%: the solution concentration diluted to 8% concentration of acid solution. The reaction ratio of liquid alkali concentration: 97% content of dry protopine against made acid. 7% concentration of alkali by 1.5-2.0 tons per hour by ion, and then water washing to pH value is about 3.5. The same flow through the alkali ion, PH wash to about 14. After the same flow acid, water washing to last for more than PH4.5. The reaction time of transition for every 25 minutes.
4离子再生 氢型离子在中毒后(饱和)需要再生使用,8%浓度酸液加温到45度按每小时1.5-2.0吨量通过离子,最后纯水洗至PH4.5以上即可.(5倍离子量的再生液循环经过离子,此办法为动态再生)
4, ion regeneration hydrogen ions need to be regenerated after poisoning (saturation). The 8% concentration of acid is heated to 45 degrees, then it is washed to PH4.5 or more by ion and pure water at the rate of 45 1.5-2.0 per hour.
The efficiency of 1 ion reaction is increased according to very few. For example: in the standard flow, if 1 liter ion can handle 50 litres of water then, 5 liters of ion can handle 500 litres and 10 litres to handle 5 tons of water, 15 liters of ion can handle 15 tons of water. The above data (for example, not accurate.)
2阳离子商品状态都是钠型的.交换后的水呈碱性(详见本人的另一个帖子:给米老三的实验)因为钠型在每交换一个钙镁离子时相应的释放一个钠在水中,所以在碳酸盐硬度下降的同时PH要上升.
2, the state of cationic products is all sodium type. The water after exchange is alkaline. (see another thread in my post: give the experiment to MI Lao 3), because sodium type releases a sodium in water in every exchange of a calcium and magnesium ion, so when the hardness of carbonate decreases, PH will go up.
3使用阳离子得到软水时必须转型. 将钠型阳离子转为氢型,转型过程相对难度较大.简单介绍一下, 一酸\一碱\一酸\转为氢型. 一碱\一酸\一碱\又换原成钠型. 反应液配比为盐酸浓度:原液39%浓度稀释到8%浓度酸液. 反应液配比碱液浓度:97%含量干燥片碱兑制成7%浓度碱液. 酸液按每小时1.5-2.0吨量通过离子,然后纯水清洗到PH值为3.5左右. 同流量碱液通过离子,PH洗至14左右. 同流量再经过酸液,最后纯水洗至PH4.5以上即可. 转型的反应时间为每次25分钟.
3 the use of soft water must get cationic transition. The sodium cation into hydrogen, the transformation process relatively difficult. A brief introduction, a \ \ a acid alkali acid into a hydrogen type. \ \ \ alkali acid alkali and put into a \ sodium ratio of reaction solution of hydrochloric acid concentration. 39%: the solution concentration diluted to 8% concentration of acid solution. The reaction ratio of liquid alkali concentration: 97% content of dry protopine against made acid. 7% concentration of alkali by 1.5-2.0 tons per hour by ion, and then water washing to pH value is about 3.5. The same flow through the alkali ion, PH wash to about 14. After the same flow acid, water washing to last for more than PH4.5. The reaction time of transition for every 25 minutes.
4离子再生 氢型离子在中毒后(饱和)需要再生使用,8%浓度酸液加温到45度按每小时1.5-2.0吨量通过离子,最后纯水洗至PH4.5以上即可.(5倍离子量的再生液循环经过离子,此办法为动态再生)
4, ion regeneration hydrogen ions need to be regenerated after poisoning (saturation). The 8% concentration of acid is heated to 45 degrees, then it is washed to PH4.5 or more by ion and pure water at the rate of 45 1.5-2.0 per hour.
