Method for preparing rod-like magnesium hydroxide from salt lake brine

A salt lake brine and magnesium hydroxide technology, applied in the field of comprehensive utilization of salt lake resources, can solve the problems of polluting products and difficult cleaning of surfactants, and achieve the effects of separation and removal, easy washing, and wide source of raw materials

Inactive Publication Date: 2012-09-19
CENT SOUTH UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This new type of material called talc can be found naturally occurring or artificially produced on various types of rock surfaces such as limestone rocks during chemical processes like manufacturing ceramic products. It helps filter out unwanted substances while also acting as an effective agent for other purposes that may benefit the surrounding area's healthy flora.

Problems solved by technology

Technological Problem: Current technologies for producing magnetic iron sulfite (iron sesquioy) from salmonic acid include pyrochlore smellless crystal powder, sintered dolomites, and expensive chemicals like zinc hydride. Additionally, current techniques involve complex operations involving heat treatment at very specific temperatures and pressures, leading to increased costs associated with these treatments.

Method used

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  • Method for preparing rod-like magnesium hydroxide from salt lake brine
  • Method for preparing rod-like magnesium hydroxide from salt lake brine
  • Method for preparing rod-like magnesium hydroxide from salt lake brine

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Embodiment Construction

[0030] The salt lake brine is evaporated in the salt field, concentrated and crystallized to produce potassium sulfate, sodium chloride, and potassium chloride. After absorbing and extracting lithium, the old brine containing magnesium and boron is obtained. The composition is shown in Table 1.

[0031] 1) Concentrated crystalline bischofite

[0032] Add 10L of brine in the reaction tank, heat and concentrate at 118°C, when the volume of the brine is reduced to 6.5L, stop heating, seal and keep warm for 2-3 hours, then filter while it is hot, cool the filtrate to room temperature, and crystallize bischofite (composition See Table 2), the weight is 2.6kg.

[0033] 2) Preparation of basic magnesium chloride by ammonia precipitation

[0034] The bischofite obtained is dissolved in water, and the concentration of magnesium ions is made into a solution of 3.5mol / L, and the volume is 3.5L. In the ammonia distillation tank with a volume of 30L, 15L of ammonium chloride mother liquor...

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Abstract

The invention discloses a method for preparing rod-like magnesium hydroxide from salt lake brine. The method comprises the following steps of: concentrating and crystallizing salt lake brine, from which elements such as potassium and lithium are extracted, serving as a raw material to obtain bischofite; dissolving the bischofite separated by crystallization into water to prepare magnesium chloride solution; introducing ammonia gas to perform magnesium precipitation reaction; when the pH value reaches 7-8, stopping introducing the ammonia gas, reacting at the temperature of 30-50 DEG C for 0.5-2 hours, aging and filtering to obtain alkaline magnesium chloride and magnesium precipitation mother liquor; dispersing the alkaline magnesium chloride in mixed solution of ethanol and water to obtain alkaline magnesium chloride suspension; adding sodium hydroxide to further precipitate to obtain rod-like magnesium hydroxide; filtering and separating to obtain magnesium precipitation mother liquor; replenishing the bischofite and circulating for precipitating the alkaline magnesium chloride; feeding to an ammonia still process along with concentration enrichment of magnesium precipitation mother liquor in ammonia chloride; performing ammonia still with lime; and circulating the produced ammonia gas to precipitate the alkaline magnesium chloride of a next batch and producing byproduct calcium chloride, wherein the magnesium content in the brine is not less than 93.4 g/L. The method has the advantages of high product purity, good economic benefit, no environmental pollution, high operability and easiness for industrial production.

Description

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Claims

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Application Information

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Owner CENT SOUTH UNIV
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