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A kind of method for preparing 4n level calcium nitrate solution

A technology of calcium nitrate and solution, applied in the direction of calcium/strontium/barium nitrate, etc.

Active Publication Date: 2022-04-12
NANCHANG HANGKONG UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] It can be seen that there is no method for directly preparing 4N grade calcium nitrate with no calcium nitrate enrichment solution as feed solution at present.

Method used

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  • A kind of method for preparing 4n level calcium nitrate solution

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] The P507 organic phase is a kerosene solution of P507 and TBP, wherein the concentration of P507 is 1.0 mol / L, and the concentration of TBP is 0.05 mol / L. When in use, the P507 organic phase is saponified with sodium hydroxide to obtain the sodium saponified P507 organic phase.

[0022] The element concentrations in the calcium nitrate enrichment solution are: Cl 0.30 g / L, Si 0.010 g / L, P 0.010 g / L, Na 0.10 g / L, Mg 1.0 g / L, Ca 100.0 g / L, Ba 1.0 g / L, Pb 0.010 g / L, Al 0.010 g / L, Fe 0.010 g / L.

[0023] Step 1: Separation of NaMgCa / CaBaPbAlFe by fractional distillation with full load

[0024] The balanced load P507 organic phase obtained at the 18th stage of the NaMg / Ca full-load fractionation extraction system in step 2 is the extraction organic phase, the calcium nitrate enrichment solution is the feed liquid, and the Ca / BaPbAlFe fractionation extraction system of step 3 is obtained at the 20th stage The equilibrium aqueous phase is the detergent. The balanced load P50...

Embodiment 2

[0031] The P507 organic phase is a kerosene solution of P507 and TBP, wherein the concentration of P507 is 1.0 mol / L, and the concentration of TBP is 0.05 mol / L. When in use, the P507 organic phase is saponified with sodium hydroxide to obtain the sodium saponified P507 organic phase.

[0032] The element concentrations in the calcium nitrate enrichment solution are: Cl 0.60 g / L, Si 0.020 g / L, P 0.020 g / L, Na 0.30 g / L, Mg 3.0 g / L, Ca 110.0 g / L, Ba 2.0 g / L, Pb 0.020 g / L, Al 0.030 g / L, Fe 0.020 g / L.

[0033] Step 1: Separation of NaMgCa / CaBaPbAlFe by fractional distillation with full load

[0034] The balanced load P507 organic phase obtained at the 16th stage of the NaMg / Ca full-load fractionation extraction system in step 2 is the extraction organic phase, the calcium nitrate enrichment solution is the feed liquid, and the Ca / BaPbAlFe fractionation extraction system of step 3 is obtained at the 22nd stage The equilibrium aqueous phase is the detergent. The balanced load P50...

Embodiment 3

[0041] The P507 organic phase is a kerosene solution of P507 and TBP, wherein the concentration of P507 is 1.0 mol / L, and the concentration of TBP is 0.05 mol / L. When in use, the P507 organic phase is saponified with sodium hydroxide to obtain the sodium saponified P507 organic phase.

[0042] The element concentrations in the calcium nitrate enrichment solution are: Cl 0.90 g / L, Si 0.030 g / L, P 0.030 g / L, Na 0.50 g / L, Mg 5.0 g / L, Ca 120.0 g / L, Ba 3.0 g / L, Pb 0.030 g / L, Al 0.050 g / L, Fe 0.030 g / L.

[0043] Step 1: Separation of NaMgCa / CaBaPbAlFe by fractional distillation with full load

[0044] The balanced load P507 organic phase obtained at the 14th stage of the NaMg / Ca full-load fractionation extraction system in step 2 is the extraction organic phase, the calcium nitrate enrichment solution is the feed liquid, and the Ca / BaPbAlFe fractionation extraction system of step 3 is obtained at the 22nd stage The equilibrium aqueous phase is the detergent. The balanced load P50...

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Abstract

A method for preparing 4N grade calcium nitrate solution of the present invention uses calcium nitrate enrichment solution as feed liquid, P507 as extractant, and TBP as modifier, extracts and separates NaMgCa / CaBaPbAlFe by full-load fractional distillation, extracts and separates NaMg / Ca by full-load fractional distillation It consists of three steps of fractional distillation, extraction and separation of Ca / BaPbAlFe, and directly prepares 4N grade calcium nitrate solution. The purity of 4N grade calcium nitrate solution is 99.992% to 99.997%, and the yield of calcium is 97% to 99%. The invention has the advantages of high product purity, high calcium yield, less reagent consumption, high separation efficiency, short process flow, low production cost and the like.

Description

technical field [0001] The invention relates to a method for preparing 4N grade calcium nitrate solution, which specifically relates to the separation and removal of sodium, magnesium, barium and lead in the feed liquid by using the calcium nitrate enrichment solution as the feed liquid, P507 as the extraction agent, and TBP as the modifier , aluminum, iron and other metal elements, as well as the separation and removal of chlorine, silicon, phosphorus and other non-metallic elements, directly prepare 4N grade calcium nitrate solution. The specific technical field of the present invention is the preparation of 4N grade calcium nitrate. Background technique [0002] The raw materials for preparing calcium nitrate are mostly limestone and quicklime, and the calcium-containing raw materials are dissolved in nitric acid to obtain a calcium nitrate enrichment solution. The calcium nitrate enrichment solution usually contains a certain amount of metal element impurities such as s...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01F11/36
CPCC01F11/36C01P2006/80
Inventor 严文思钟学明姚玉芳
Owner NANCHANG HANGKONG UNIVERSITY