Method for removing nitrite from milk by utilizing membrane separation technology
A technology for nitrite and membrane separation, applied in applications, milk preparations, dairy products, etc., can solve the problem of inedible milk, and achieve the effect of reducing ash content and improving quality
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Embodiment 1
[0022] Firstly, the milk whose nitrite content exceeds the standard (1.0mg / kg) is subjected to ultrafiltration treatment. The molecular weight cut-off of the organic ultrafiltration membrane is 10,000MW, the pressure difference of each membrane module is 0.07MPa, the operating temperature is 10°C, and the diafiltration solvent is Purified water, continuously add water for diafiltration until the nitrite contained in the milk drops below 0.1mg / kg, and the volume of diafiltration water is 5 times the volume of the milk to be treated. Then the ultrafiltration permeate is subjected to nanofiltration treatment, the molecular weight cut-off of the organic nanofiltration membrane is 100-300MW, the pressure difference of each membrane module is 0.1MPa, and the operating temperature is 10°C. Finally, after mixing the qualified ultrafiltration retentate (nitrite content≤0.1mg / kg) with the nanofiltration retentate (nitrite content≤0.1mg / kg), homogenize and sterilize (treatment at 135°C) ...
Embodiment 2
[0024] Firstly, the milk whose nitrite content exceeds the standard (0.6mg / kg) is subjected to ultrafiltration treatment. The molecular weight cut-off of the organic ultrafiltration membrane is 10,000MW, the pressure difference of each membrane module is 0.1MPa, the operating temperature is 15°C, and the diafiltration solvent is Purified water, continuously add water for diafiltration until the nitrite contained in the milk drops below 0.1mg / kg, and the volume of diafiltration water is twice the volume of the milk to be treated. Then the ultrafiltration permeate is subjected to nanofiltration treatment, the molecular weight cut-off of the organic nanofiltration membrane is 100-300MW, the pressure difference of each membrane module is 0.15MPa, and the operating temperature is 20°C. Finally, after mixing the qualified ultrafiltration retentate (nitrite content≤0.1mg / kg) with the nanofiltration retentate (nitrite content≤0.1mg / kg), homogenize and sterilize (treatment at 135°C) 5s...
Embodiment 3
[0026] Firstly, the milk whose nitrite content exceeds the standard (0.4mg / kg) is subjected to ultrafiltration treatment, the inorganic ultrafiltration membrane has a molecular weight cut-off of 20,000MW, the pressure difference of each membrane module is 0.2MPa, the operating temperature is 20°C, and the diafiltration solvent is Purified water, continuously add water for diafiltration until the nitrite contained in the milk drops below 0.1mg / kg, and the volume of diafiltration water is 1 times the volume of the milk to be treated. Then the ultrafiltration permeate is subjected to nanofiltration treatment, the molecular weight cut-off of the organic nanofiltration membrane is 100-300MW, the pressure difference of each membrane module is 0.2MPa, and the operating temperature is 30°C. Finally, after mixing the qualified ultrafiltration retentate (nitrite content≤0.1mg / kg) with the nanofiltration retentate (nitrite content≤0.1mg / kg), homogenize and sterilize (treatment at 135°C) ...
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