Liquid state low calorie fat mixed triglyceride
A low-calorie oil and triglyceride technology, applied in the fields of edible oil/fat, food science, application, etc., can solve problems affecting food quality, rough taste, etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0021] Soybean oil 30kg, glycerol 2.9kg, consumption is 0.1% tetrabutylammonium chloride and K 2 SO 4 co-catalysis at 130 °C, N 2 Glycerol hydrolysis was carried out under protection for 40 min, and then the glycerol was removed by centrifugation. Esterification was carried out under reflux conditions. Firstly, acetic acid was used in an amount of 3.3 kg for 2.0 h, and then acetic anhydride was used for 1.0 h in an amount of 3.3 kg to obtain a crude product. Finally, refining processes such as alkali refining and dehydration are carried out to obtain finished products. The proportion of long and short chain acylglycerides in the mixture is 65% (percentage by weight), and the heat is 27% of the raw material oil.
Embodiment 2
[0023] Peanut oil 30kg, glycerin 3.5kg, consumption is the tetrabutyl ammonium bromide of 0.1% of raw material and K 2 SO 4 co-catalysis at 120 °C, N 2 Glycerolysis was carried out under protection for 100 min, and then the glycerol was removed by centrifugation. Esterification was carried out under reflux conditions. Firstly, acetic acid was used in an amount of 3.7 kg for 2.0 h, and then acetic anhydride was used for 1.3 h in an amount of 3.1 kg to obtain a crude product. Finally, refining processes such as alkali refining and dehydration are carried out to obtain finished products. The proportion of long and short chain acylglycerides in the mixture is 73% (percentage by weight), and the heat is 30% of the raw material oil.
Embodiment 3
[0025] Rapeseed oil 30kg, glycerin 2.9kg, consumption is 0.1% tetraethylammonium chloride and Na 2 SO 4 co-catalysis at 110 °C, N 2 Glycerolysis was carried out under protection for 150 min, and then the glycerol was removed by centrifugation. Esterification was carried out under reflux conditions. Firstly, propionic acid was used in an amount of 3.3 kg for 2.0 h, and then propionic anhydride was used for 1.0 h in an amount of 3.3 kg to obtain a crude product. Finally, refining processes such as alkali refining and dehydration are carried out to obtain finished products. The ratio of long and short chain acylglycerides in the mixture is 68% (percentage by weight), and the heat is 28% of the raw material oil.
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com