Preparation and application of a refined decolorizer for edible oil and cleaning
A decolorizing agent and edible oil technology, applied in the fields of fat oil/fat refining, chemical instruments and methods, inorganic chemistry, etc.
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Embodiment 1
[0053] 1. Add sodium chloride and sodium chlorate to the batching tank (1) according to the mass ratio of 0.3:1, add water to dissolve into a mixed aqueous solution A, adjust the concentration to 300-600g / L, and heat to 50°C to dissolve it; Then add ventilated airtight reaction tank (2) for subsequent use.
[0054] The 2nd, by the quality of 1.2:1 molar ratio of hydrochloric acid and sodium chlorate, hydrochloric acid is injected the first step reaction tank (2) of ventilating with metering pump and does redox reaction; Redox reaction process material is in reaction tank (2) ) in the reaction formula is as follows:
[0055] NaCl+6NaCl+HCl+3H 2 o 2 +H 2 O=3O 2 +6Cl 2 +SO 2 +H 2 O.
[0056] 3. Regulate the flow rate of the high-pressure fan, cooperate with the air flow rate of the monitoring instrument, the data of the online available chlorine concentration display instrument, and adjust the amount of hydrochloric acid added, so that the ratio of the air volume to the g...
Embodiment 2
[0071] Embodiment 2, application of reaction waste recovery
[0072] During the production process of the refined decolorizer, about 2.7 cubic meters of reaction waste liquid is produced per ton of finished product (dry product). According to laboratory analysis, the content of hydrochloric acid in the waste liquid is 23% to 27%, and the content of Glauber's salt mixture is 30% to 50%. The technical scheme adopted for waste liquid purification and reuse of the present invention comprises the following steps:
[0073] 1) Pour the waste liquid into a vacuum concentration tank that can be practiced by professionals in the industry, and then add concentrated sulfuric acid. The concentrated sulfuric acid and waste liquid are added at a volume ratio of 0.005:1. Carry out vacuum evaporation and concentration at 50°C to 200°C, preferably 80°C to 120°C, and stop the concentration when the evaporation reaches 40% of the total waste liquid;
[0074] 2) Pour the concentrated solution of ...
Embodiment 3
[0080] Take sodium chlorate with a content of 99% and sodium chloride with a content of 98% and mix it at a mass ratio of 1:0.06, mix it with water at a concentration of 350g / L, add it to the batching tank, and dissolve it under the conditions of 40r / min and 50°C. Add the reaction tank; start the high-pressure fan, and temporarily adjust the initial air volume to 908m 3 / h. Then 10mol / L hydrochloric acid solution is slowly added to the reaction tank with a metering pump, and at this time, sodium chloride is converted into Cl under the redox of hydrochloric acid. 2 , sodium chlorate releases ClO 2 Gas, at this time there is ClO in the reaction tank 2 , Cl 2 、H 2 , O 2 , a variety of mixed gases, the present invention is collectively referred to as compound available chlorine. Composite available chlorine and air flow are discharged from the reaction tank in time according to the volume ratio of 0.1-50:100. At the same time, the effective chlorine content in the reaction ...
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