Juicing device and working method for fruit and vegetable processing
A fruit and vegetable, juicing technology, applied in application, juice extraction, food science and other directions, can solve the problems of difficult juice separation, low efficiency, poor juicing effect, etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0070] According to the following steps to prepare the present invention Juicing turntable 4-3 , and in parts by weight:
[0071] Step 1: In the high-pressure stirred reactor, add 321.6 parts of ultrasonically atomized gas-phase pure water and 113.6 parts of methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 114rpm, Start the heating oil heater in the high-pressure stirring reactor, raise the temperature to 129.6°C, add 116.0 parts of 4-methoxy-α-methylphenylacetic acid methyl ester and stir evenly, carry out the reaction for 106.6 minutes, add methyl n-hexane 112.2 parts, the flow rate is 105.8 m 3 The hydrogen gas per min was 106.6 minutes; after that, 115.8 parts of zymosan were added to the high-pressure stirred reactor, and the heating oil temperature device in the high-pressure stirred reactor was started again, and the temperature was raised to 146.0°C, kept for 106.2 minutes, and 4 , 118.2 parts of polymers of 4'-(1-methy...
Embodiment 2
[0078] According to the following steps to prepare the present invention Juicing turntable 4-3 , and in parts by weight:
[0079] Step 1: In the high-pressure stirred reactor, add 546.2 parts of ultrasonically atomized gas-phase pure water and 155.9 parts of methyl dodecyl siloxane, start the mixer in the high-pressure stirred reactor, set the speed at 160rpm, Start the heating oil heater in the high-pressure stirring reactor, raise the temperature to 130.2°C, add 225.9 parts of 4-methoxy-α-methylphenylacetic acid methyl ester and stir evenly, carry out the reaction for 117.9 minutes, add methyl n-hexane 129.1 parts, the flow rate is 146.1 m 3 The hydrogen gas per min was 117.9 minutes; after that, 172.9 parts of zymosan were added to the high-pressure stirred reactor, and the heating oil temperature device in the high-pressure stirred reactor was started again to raise the temperature to 179.9°C, and the temperature was kept for 117.1 minutes, and 4 , 179.8 parts of polyme...
Embodiment 3
[0086] According to the following steps to prepare the present invention Juicing turntable 4-3 , and in parts by weight:
[0087] Step 1: In the high-pressure stirred reactor, add 321.9 parts of ultrasonically atomized gas-phase pure water and 113.9 parts of methyl dodecyl siloxane, start the stirrer in the high-pressure stirred reactor, and set the speed at 114rpm, start the heating oil heater in the high-pressure stirring reactor, raise the temperature to 129.9°C, add 116.9 parts of 4-methoxy-α-methylphenylacetic acid methyl ester and stir evenly, carry out the reaction for 106.9 minutes, add methyl 112.9 parts of n-hexane, the flow rate is 105.9 m 3 The hydrogen gas of / min is 106.9 minutes; Add 115.9 parts of zymosan in the high-pressure stirred reactor afterwards, start the heating oil temperature device in the high-pressure stirred reactor again, make the temperature rise to 146.9 ℃, keep warm for 106.9 minutes, add 4 , 118.9 parts of polymers of 4'-(1-methylethylene)...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


