Process water for producing salt by means of strong brine concentration after sea water desalination by using a two-way circulation method and bromine extraction
AssigneeWeifang Northsea Oasis Solar Powered Technology Co., Ltd.
InventorPanmin Cai
Life of this patent
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Abstract
A process produces salt by way of strong brine concentration after sea water desalination by using a two-way circulation method and bromine extraction. The process includes the following steps: A, preparing fresh water and strong brine from sea water in a high-pressure reverse osmosis unit by using a reverse osmosis method, wherein the concentration of the prepared strong brine is 70000 to 80000 PPM; and B, performing fresh and concentrated separation on the strong brine with the concentration of 70000 to 80000 PPM in a two-way circulation manner by using a concentration difference method till the strong brine is crystallized.
Claims6
A process for producing salt from strong brine produced from sea water desalination, comprising the following steps:
- A. preparing strong brine from sea water by a reverse osmosis method, wherein the concentration of the prepared strong brine is 7000˜80000 PPM;
- B. separating the strong brine in a two-way circulation manner by using a concentration difference method till the strong brine is crystallized, wherein the two-way circulation manner by the concentration difference method includes the following steps:
- a. setting several 12 m deep brine tanks and numbering them:
- I-XVII, in which:
- every brine tank is divided into three areas, among which an upper 4 m is a low salinity area, a middle 4 m is a medium salinity area and a lower 4 m is a high salinity area;
- each area of the brine tanks are separated by a concentration difference of 0.2˜1.5°, and a concentration difference of the same area of neighboring brine tanks is 1˜3°;
- the brine tanks I-XVII are divided into salt areas with brine concentrations ranging from 4˜29°;
- and the brine tanks I-XVII generally decrease in brine concentration;
- b. injecting the strong brine with the concentration of 7000˜80000 PPM 6 m deep into brine tank XV having a concentration of 7° in the medium salinity area;
- c. pumping the brine at a bottom of every brine tank into the medium salinity area of an adjacent brine tank having higher salt content, and the brine of low concentration at a top of a brine tank having higher salt content will overflow to an adjacent brine tank having lower salt content, forming a two-way circulation;
- d. extracting sodium chloride crystals in a strong brine area at 27˜29° after a crystallization of sodium chloride at around 29°.
Dependencies are inferred from the claim text.