Edible refined salt and production method thereof
A production method and refined salt technology, applied in the direction of food science, etc., can solve the problems that the uniform mixing of anti-caking agent and sodium chloride crystal cannot be guaranteed, the anti-caking effect of edible salt cannot be improved, and the effect of anti-caking agent is limited, so as to avoid Poor anti-caking effect, less addition, good anti-caking effect
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2021-02-02
Abstract
Description
technical field
[0001] The invention belongs to the technical field of edible refined salt preparation, and in particular relates to edible refined salt and a production method thereof. Background technique
[0002] Refined edible salt is an indispensable edible product in people's daily life. In the process of using a large amount of edible salt, the agglomeration of salt is a difficult problem to solve; in the prior art, most of the agglomeration of edible salt is improved by adding anti-caking agents, but the existing methods of adding mostly:
[0003] 1. Spray the anti-caking agent on the surface of the sodium chloride crystal to form a hydrophobic protective film, so as to achieve the anti-caking effect;
[0004] Second, the anti-caking agent is directly blended with sodium chloride crystals to absorb water through the anti-caking agent, so as to achieve the anti-caking effect;
[0005] However, the above two methods cannot guarantee the uniform mixing of the anti-ca...
Examples
Embodiment 1
[0034] A method for producing refined edible salt, comprising the steps of:
[0035] S1. prepare 1000kg saturated edible brine with a pH value of 7, place it in a high-speed mixer, add 3g of potassium ferrocyanide to saturated edible brine, then mix at a high speed at a mixing speed of 10000 rpm to make ferrous Potassium cyanide is completely dissolved to obtain a uniformly mixed mixed aqueous solution;
[0036] S2. Put the mixed aqueous solution in the evaporation tank, and set the steam pressure in the evaporation tank to 0.2MPa to ensure that the evaporation rate of the evaporation tank is not higher than 0.4t / h m 3 After evaporation, concentration and crystallization, the salt is discharged to obtain a salt slurry with a solid-to-liquid ratio of 2:6;
[0037] S3. Use brine with divalent magnesium ion content less than 0.3g / kg to stir and wash the salt slurry. Specifically, during the washing process, the sodium sulfate in the salt slurry can be effectively dissolved, and ...
Embodiment 2
[0044] A method for producing refined edible salt, comprising the steps of:
[0045] S1. Prepare 1000kg of saturated edible brine with a pH value of 7.5, place it in a high-speed mixer, add 4g of potassium ferrocyanide to the saturated brine, and then mix at a high speed at a mixing speed of 15000 rpm to make ferrous Potassium cyanide is completely dissolved to obtain a uniformly mixed mixed aqueous solution;
[0046] S2. Put the mixed aqueous solution in the evaporation tank, and set the steam pressure in the evaporation tank to 0.25MPa to ensure that the evaporation rate of the evaporation tank is not higher than 0.4t / h m 3 After evaporation, concentration and crystallization, the salt is discharged to obtain a salt slurry with a solid-to-liquid ratio of 2:7;
[0047] S3. Use brine with divalent magnesium ion content less than 0.3g / kg to stir and wash the salt slurry. Specifically, during the washing process, the sodium sulfate in the salt slurry can be effectively dissolve...
Embodiment 3
[0054] A method for producing refined edible salt, comprising the steps of:
[0055] A method for producing refined edible salt, comprising the steps of:
[0056] S1. prepare 1000kg saturated edible brine with a pH value of 7.7, place it in a high-speed mixer, add the potassium ferrocyanide of 4.5g in the saturated edible brine, then mix at a high speed at a mixing speed of 20000 rpm to make sub Potassium ferricyanide is completely dissolved to obtain a uniformly mixed mixed aqueous solution;
[0057] S2. Put the mixed aqueous solution in the evaporation tank, and set the steam pressure in the evaporation tank to 0.3MPa to ensure that the evaporation rate of the evaporation tank is not higher than 0.4t / h m 3 After evaporation, concentration and crystallization, the salt is discharged to obtain a salt slurry with a solid-to-liquid ratio of 3:7;
[0058] S3. Use brine with a divalent magnesium ion content of less than 0.3g / kg to stir and wash the salt slurry. Specifically, dur...