[0007] However,
sea salt (including lake salt) has the following serious disadvantages: (1) its
salt content (
sodium chloride) is 92%, which is lower than 97.5% of mineral salt. For a long time, its price is higher than that of mineral salt, while chlor-alkali The average daily consumption of raw salt in enterprises is tens or even hundreds of tons, and its high price leads to high costs; (2) For the majority of inland chlor-alkali enterprises, sea salt still has the problems of difficult transportation and easy stock out of stock, which will give enterprises Production and operation have serious consequences
Usually, in order to stabilize the supply and production, the majority of inland chlor-alkali enterprises purchase raw salt for about 2-3 months each time, and the quantity reaches thousands or even tens of thousands of tons.
(3) Because the
salt content of sea salt (92%) is lower than that of mineral salt (97.5%), and its
impurity content is higher, the amount of salt mud formed during the purification process accounts for about 7% of the
raw material, and more salt mud is needed Expenses are used for
environmental protection treatment, which also affects the operation and development of enterprises
[0009] The problem of
ion adsorption method: because the brine is alkaline, various metals basically exist in the form of
hydroxide, it is difficult to remove them by adsorption resin, and the special adsorption equipment is expensive and costly, which is not conducive to
market competition. , the
ion adsorption method has no practical production value
[0010]
Flocculation problems: commonly used flocculants are FeCl 3 , aluminum
chloride,
iron sulfate,
sodium polyacrylate, etc., but because the
electrolysis process has strict requirements on the content of organic impurities, it is required that no organic impurities harmful to electrolysis be introduced during
flocculation. Therefore,
sodium polyacrylate cannot be used, and it is currently preferred. FeCl 3 as flocculant
However, increasing FeCl for mineral salt 3 As a result of the dosage, although most of the
metal ions can be separated from the
solid and liquid, the stubborn problem of iron and aluminum exceeding the standard in the primary brine is difficult to solve; and this will lead to an increase in the electrolysis
voltage of the ion membrane in subsequent electrolysis, reducing the ion membrane The efficiency of electrolysis will increase the
energy consumption, even damage the ion membrane, shorten the service life of the ion membrane, which is very unfavorable to the production of chlor-alkali
[0011] In order to solve the problems caused by the different advantages and disadvantages of sea salt and mineral salt in the above-mentioned production process, some domestic enterprises have adopted the method of mixing part of sea salt with mineral salt, which has achieved certain results in improving the quality of primary brine, but this method needs to be adjusted according to the quality of mineral salt. The proportion of sea salt, firstly, the production of sea salt is greatly affected by the climate, the transportation is inconvenient, the supply is unstable, and the problem of out-of-stock cannot be solved fundamentally; secondly, this method greatly increases the links and costs of the production and operation management of the enterprise, making it difficult to continue to implement
Third, after mixing part of sea salt, the amount of salt mud will increase, which will increase the cost of
environmental protection treatment at the same time
[0012] At the same time, some domestic enterprises adopt the method of recycling part of the salt mud produced by a brine
filtration in the pre-
filtration system to increase the adsorption capacity of impurities during the
filtration of the brine system. Practice has proved that the salt mud circulation technology has a certain effect on the above-mentioned raw salt problem. Relief, you can reduce the amount of sea salt, but when it is reduced to about 15%, the impurity content is abnormal, and the
treatment effect is not ideal
[0013] It can be seen from the above that in the traditional process, mineral salt alone cannot meet the quality requirements of ion membrane electrolysis production, and cannot be used as raw salt for ion membrane electrolysis