Method and apparatus for producing oxygen-containing reducing aqueous beverage
A technology for beverages and manufacturing methods, applied in the field of production of oxygen-reducing water beverages and production equipment, capable of solving problems such as functions and dangers that hinder neutral environments
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Embodiment 1- Embodiment 3
[0095] As Examples 1-3, tap water (oxidation-reduction potential +420 mV, pH=7.2) in Chuo-ku, Tokyo was used as raw material water. Using the manufacturing apparatus 10 of the oxygen-containing reducing water drink shown in FIG. 1, oxygen-containing reducing water is manufactured as follows. First, the device using only injectors 50A and 50B without using a static mixer is referred to as Example 1, and the device using an 8-element type static mixer in combination with the device of Example 1 is referred to as Example 2, and also in Example 1 A device using a 32-element static mixer in conjunction with the device is used as Example 3.
[0096] Therefore, in Example 1-Example 3, the same raw material water flow rate, raw material water pressure, oxygen-containing water flow rate, oxygen pressure, oxygen-containing water pressure, and hydrogen pressure were used to produce oxygen-containing reduced water. The individual manufacturing conditions and measurement results are colle...
Embodiment 4
[0103] As Embodiment 4, the production apparatus 10 of an oxygen-containing reducing water beverage that only has the same first injector 50A and second injector 50B as in Embodiment 1 without using a static mixer is used, and a commercially available tea beverage is used as water beverage to make oxygen-reducing tea beverage. First, the oxidation-reduction potential, dissolved oxygen content, and pH of the tea beverage were measured. The oxidation-reduction potential was +60mV, the dissolved oxygen content was 1.55 mg / L, and the pH was 6.1. The tea beverage was pressurized at a rate of 500 ml / min at 8 atmospheres, and oxygen was supplied to the first injector 50A while being pressurized at a rate of 150 ml / min at 8 atmospheres. After the oxygen was dissolved, the pressure was returned to normal pressure, and the oxygen dissolved amount of the oxygen-containing tea beverage obtained in the receiver 21 was measured to be 31.00 mg / L.
[0104] This oxygen-containing tea beverage...
Embodiment 5
[0106] As Example 4, an oxygen-reducing coffee drink was produced in the same manner as in Example 3 using a commercially available coffee drink. The redox potential of this coffee drink was +85mV, the dissolved oxygen content was 1.22 mg / L, and the pH was 5.0. The coffee drink was pressurized at a rate of 500 ml / min at 8 atmospheres, and oxygen was pressurized at a rate of 150 ml / min at 8 atmospheres and simultaneously supplied to the first injector 50A. After the oxygen was dissolved, return to normal pressure, measure the oxygen dissolved amount of the oxygen-containing coffee beverage obtained in the receiver 21, and obtain an oxygen-containing coffee beverage with an oxygen dissolved amount of 32.70 mg / L.
[0107] The oxygen-containing coffee drink was pressurized at a rate of 500 ml / min at 8 atmospheres, and hydrogen gas was pressurized at a rate of 150 ml / min at 8 atmospheres, and simultaneously supplied to the second injector 50B. After the hydrogen is dissolved, retu...
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