Fatty Acid Composition of Oil Obtained from Soybeans by
- Type: soybean oil extraction machine
- Usage/Application: soybean
- Main components: Motor
- Voltage: 380 V
- Dimension (L*W*H): Type
- Weight: 3000 kg
- Power: 2.2 KW
- Country: tanzania
(1984) found that the fractionation of soybean oil in supercritical carbon dioxide extraction at 550 bar and 50°C only occurred in the last 10–15% of the oil extracted in which the composition of fatty acid in triglycerides varied. In our earlier papers (Jokić et al. 2011a,b), we studied the solubility behaviour of soybean oil and
Original article: Supercritical CO2 extraction of soybean oil
- Type: soybean oil processing machine
- Customized: Customized
- Suit for: sunflower, soybean, peanut
- Mainly machine: combined with whole oil press line
- Size: 2700*1000 *2700 mm
- Large capacity: 1t-30t/D for oil press machine
Friedrich & List (1982) reported that the soybean oil obtained by supercritical CO 2 is essentially equivalent to hexane-extracted oil. The supercritical CO 2 extraction in the above mentioned study was conducted at 345 bar and 50 °C, flow rate of CO 2 was 2 kg per h. In comparison with this investigation, the significant difference in the
Soybean oil 57.05 28.77%. Rapeseed oil 27.83 14.08%. Sunflower oil 17.75 8.95%. Peanut oil 5.53 2.79%. TABLE 6 Supercritical Fluid extraction of oil from different oilseeds. Experimental
Effects of supercritical CO2 extraction parameters on soybean
- Usage: soybean oil
- Production capacity: 50 tons/day
- Dimension (length*width*height): 16*4.2*6.6 feet
- Warranty service: On-site repair and maintenance service field
- Oil Full warranty service: On-site video technical support
- Weight: 24500 KG
A series of operational parameters of supercritical fluid extraction of soybean oil (pressure: 300–500 bar, temperature: 40–60 °C, CO 2 mass flow rate: 0.194–0.436 kg/h and characteristic particle size: 0.238–1.059 mm) were investigated in a laboratory scale apparatus. The results show that the extraction yields were significantly
The model had a deviation of 7.4% from the experimental values for the sesame seed oil extraction. In another study by Carvalho et al. [23], a kinetic model for the sesame seed oil extraction was developed to compare the time required for extraction with and without a co-solvent. Palmitic, stearic, oleic, linoleic and others were the fatty
Fatty acid composition of the oil obtained from soybeans by
- Type: cooking oil extraction machine
- Structure: Fixed
- Performance: Efficient filtration
- Mechanical principle: Pressure filtration
- Color: Green/Blue/Silver
- Material: stainless steel or carbon steel
Fatty acid composition of soybean oil extracts/fractions obtained by supercritical CO 2 (SC-CO 2 ) at constant pressure and by soxhlet extraction *extraction conditions: P E = 400 bar, mass flow rate = 0.194 kg/h, d 0 = 0.383 mm; fractions were obtained at different extraction temperature conditions and were collected every two hours -F1 after
The aim of this study was to obtain the optimum condition of soybean oil extraction by modified supercritical carbon dioxide. The soybean oil was extracted by using modified supercritical carbon dioxide (SC-CO 2 ) under the temperatures of 40, 60, 80 °C, pressures of 150, 250, 350 Bar, and constant flow-rate of 10 g/min as the parameters of
Investigation of Process Variables in Supercritical CO2
- Raw Material: soybean
- Voltage: 220V/380V/440V
- Dimension (L* W*H): 1050*660*760mm
- Power (W): 15KW cooking oil solvent extraction equipment
- Weight: 1100kg
- Certification: ISO9001
supercritical CO2 through the soybean meal. The use of the higher temperature in this study, extraction effi-ciency was improved, requiring smaller residence times and solvent mass to meal ratios. This process has appli-cations in both the food and biofuel industries for generation of soybean oil. References 1. N. Wilkinson, R. Hilton, D
Different empirical models were used to describe the supercritical CO 2 extraction of soybean oil obtained at series of operational parameters namely pressure, temperature, solvent flow rate and characteristic particle size. Process yields obtained