Production process and system of propylene glycol type solar low-temperature heat utilization working medium
A production system, propylene glycol technology, applied in the direction of heat exchange materials, mixers, mixer accessories, etc., can solve the problems of unfavorable large-scale batch production, unfavorable product popularization and promotion, increase of production costs, etc., to avoid mechanical damage Risk, production process safety, and low investment costs
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0049] According to the order requirements, 50 tons of propylene glycol-type solar low-temperature heat utilization working fluid with a freezing point not higher than -20°C and an apparent color of yellow will be produced. First, determine the mass ratio of each component in the working fluid: propylene glycol 43%, deionized water 54%; the mass ratio of additives is: sebacic acid 0.5%, disodium hydrogen phosphate 0.8%, sodium nitrate 0.2%, benzene Sodium formate 0.4%, benzotriazole 0.4%, potassium hydroxide 0.6%; pigment (lemon yellow) 0.1%. Second, propylene glycol and deionized water are fed in the same proportion, and when the propylene glycol feed rate is 35% of the calculated value, add sebacic acid, disodium hydrogen phosphate, potassium hydroxide, then add sodium nitrate, sodium benzoate, benzotri Azole, and finally the coloring tartrazine. Third, when the addition of propylene glycol and deionized water reaches 90% of the calculated value, the control system will aut...
Embodiment 2
[0052] For a propylene glycol-type solar energy low-temperature heat utilization working medium production process and system involved in the present invention, the operation process of embodiment 2 is the same as that of embodiment 1. The difference between embodiment 2 and embodiment 1 is:
[0053] Producing 80 tons of propylene glycol-based solar low-temperature heat utilization working fluid with a freezing point not higher than -25°C and an apparent color of green according to the order requirements. First, determine the mass ratio of each component in the working fluid: propylene glycol 44.8%, deionized water 52.2%; the mass ratio of additives is: sebacic acid 0.7%, disodium hydrogen phosphate 0.7%, sodium nitrate 0.4%, benzene Sodium formate 0.3%, benzotriazole 0.2%, potassium hydroxide 0.6%; pigment (weak acid green) 0.1%. The second, propylene glycol and deionized water are fed in the same proportion first, and when the propylene glycol feed rate is 38% of the calcul...
Embodiment 3
[0056] For a propylene glycol-type solar energy low-temperature heat utilization working medium production process and system involved in the present invention, the operation process of embodiment 3 is the same as that of embodiment 1. The difference between embodiment 3 and embodiment 1 is:
[0057] Producing 100 tons of propylene glycol-based solar low-temperature heat utilization working fluid with a freezing point not higher than -30°C and an apparent color of blue according to the order requirements. First, determine the mass ratio of each component in the working fluid: propylene glycol 46.3%, deionized water 50.7%; the mass ratio of additives is: sebacic acid 0.7%, disodium hydrogen phosphate 0.7%, sodium nitrate 0.4%, benzene Sodium formate 0.3%, benzotriazole 0.2%, potassium hydroxide 0.6%; pigment (weak acid blue) 0.1%. The second, propylene glycol and deionized water are fed in the same proportion first, and when the propylene glycol feed rate is 40% of the calcula...
PUM
| Property | Measurement | Unit |
|---|---|---|
| freezing point | aaaaa | aaaaa |
| boiling point | aaaaa | aaaaa |
| freezing point | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 


