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In the study conventional refining, microfiltration and ultrafiltration processes have been used experimentally to pretreat crude palm oil (CPO) samples with the aim of moving from the usual huge refinery plant to a more process integrated membrane module at ultrascale size that will even perform better than the former. Reduction of phosphorus for the membrane‐permeate of 43.4% was higher than that of bleached oil of 34.4%. When ceramic membranes with pore diameters of 0.45 µm and 0.2 µm were used in microfiltration, it was found that membrane with pore size of 0.45 µm was able to reject 14% of phosphorus, while ceramic membrane with pore size of 0.2 µm showed better phosphorus rejection of 56.8%. Upon applying ceramic membrane with pore sizes of 20 nm and 50 nm, 78.1% and 60% of phosphorus were rejected, respectively. Attributed to the superior performance of the membrane with 20 nm pore size over other membranes and conventional refining method on phosphorus content, a simulation study thus made, showed that the average slurry volume after about 22‐min runs for membrane with pore sizes of 0.45 µm, 0.2 µm, 50 nm and 20 nm, and the average slurry volumes are 0.05, 0.09, 0.13 and 0.18 m 3 , respectively. The percentage decrease between membrane pore size of 0.45 µm and 0.2 µm; 0.45 µm and 50 nm; and 0.45 µm and 20 nm are 73, 49 and 24%, respectively. The ultrafiltration achieved order of process miniaturization of about 10 2 ?10 3 , which is in accordance with literature. This is a considerable size reduction in the process size, which reflects the magnitude of slurry volume that can be produced within a given time and meets every standard for process intensification through simulated process miniaturization.  相似文献   

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Crude palm oil and crude palm olein were hydrolyzed with lipase from Candida rugosa to produce a free fatty acid (FFA) rich oil. The percentages of FFA produced and carotene degradation after the hydrolysis process were determined. The palm oil and hydrolyzed palm oil were subsequently subjected to column chromatography. Diaion HP-20 adsorbent was used for reverse phase column chromatography at 50C. Isopropanol or ethanol, and n-hexane were used as the first and second eluting solvents, respectively. The objective of hydrolyzing the palm oil was to produce more polar FFA-rich oil in order to enhance the nonpolar carotene bind to the nonpolar HP-20 adsorbent in the column chromatography process. Hydrolyzing palm oil with lipase from Candida rugosa gave 30- and 60-fold, respectively, of FFA in the crude palm oil and crude palm olein in 24 h at 50C. Approximately, 15.56 and 17.48% of carotene degraded in crude palm oil and crude palm olein, respectively. For column chromatography, using isopropanol or ethanol as the first eluting solvent, unhydrolyzed oil and hydrolyzed oil showed the carotene recovery infraction two (carotene-rich fraction) of about 36–37 and 90–96%, respectively. Over 90% of carotene recovery was obtained from  相似文献   

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Membrane separation technology offers a potential application in the processing of crude palm oil. Ceramic membranes with different pore diameters (0.45 and 0.2 micron) were used to conduct the study on micromembrane process. Quality parameters of membrane-processed oils examined included free fatty acid (FFA), carotene, fatty acid composition (FAC), phosphorus and iron contents. The effect of operating parameters such as transmembrane pressure, feed flow and time on permeate flux were evaluated. It was found that 'Ceraflo'ceramic membrane with a pore size of 0.45 micron was only able to reject 14% of phosphorus from the crude oil. Ceramic membrane with pore size of 0.2 micron showed a better phosphorus rejection of 56.8%. The permeate was found to contain 7.13 ppm of phosphorus. The 0.2 micron membrane was also able to remove more than 80% of the iron from crude palm oil. Pore sizes for both membranes were not small enough to remove other components such as FFA, and carotene. Both membranes showed a similar trend in which the permeate flux increased with transmembrane pressure and feed flow until a certain limit where the flux declined with increasing pressure and feed flow. The limits in transmembrane pressures for membrane with pore sizes of 0.45 and 0.2 micron were 1.65 and 1.25 bar, respectively. Whereas the limits in feed flow for 0.45 micron and 0.2 micron membranes were 9.2 and 9.8 L/min  相似文献   

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蚕蛹油中多不饱和脂肪酸的分离研究   总被引:2,自引:0,他引:2  
蚕蛹油富含亚油酸、α-亚麻酸等多不饱和脂肪酸,这些多不饱和脂肪酸有多方面的生理功能.主要介绍蚕蛹油中多不饱和脂肪酸的尿素包合分离和硝酸银络合分离.结果表明,适宜的尿素包合条件为:尿素/脂肪酸的质量比15:1、包合温度5℃、包含时间2 h,在上述条件下多不饱和脂肪酸得率为70.0%,含量达到92.4%;适宜的硝酸银络合条件为:AgNO32mol/L、40%甲醇-水溶液、络合温度0 ℃,在上述条件下α-亚麻酸收率达50%,纯度达99%.  相似文献   

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澳大利亚菜籽浸出毛油,采用水化法、酸脱胶、吸附法等脱胶方法不能有效脱除磷酯。通过实践研究找出了脱除不同非水化磷脂组分的方法。  相似文献   

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Vitamin E from palm fatty acid distillate (PFAD) was concentrated in this study by removing the extraneous matters, especially free fatty acids (FFA) and acylglycerols. Original PFAD used in this study contained 85 and 13.7% of FFA and acylglycerols, respectively. Acylglycerols in PFAD were first hydrolyzed using commercially available immobilized Candida antarctica lipase at 60C for 6 h. The fatty acids liberated, together with the existing FFA were then removed by neutralization. Hydrolysis followed by neutralization step concentrated vitamin E from an initial amount of 0.37 to 4.32%. Hydrolysis was an important step as without hydrolysis, neutralization could only concentrate vitamin E to 1.80%. Oil extracted from hydrolyzed and neutralized PFAD was then subjected to a normal-phase silica adsorption chromatography. The column was first eluted with hexane followed by isopropanol. A large amount of acylglycerols was removed during the first elution, while vitamin E was desorbed by isopropanol, with a recovery of >90%. Vitamin E concentration after hydrolysis, neutralization and adsorption chromatography was 15.2%. The method described in this study offers an alternative for the existing separation methods. It could be applied as one of a series of steps in producing high-purity vitamin E concentrates.  相似文献   

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A two-stage optimization of ingredients in durian leather formulations was conducted using Response Surface Methodology (RSM). In stage 1, the independent variables were glucose syrup solids (GSS) and sucrose, and in stage 2, the variables were hydrogenated palm oil (HPO) and soy-lecithin (SL). Based on the responses to sensory acceptability attributes including taste, aroma, texture, appearance and overall acceptability, the most acceptable formulation was a combination of 10% GSS, 5% sucrose, 2.67% HPO and 0.452% SL. Chemical analysis also showed that during processing nutrient composition was relatively unchanged.  相似文献   

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对苎麻脱胶进行了小试,研究了其化学组成及脱胶对苎麻的影响,筛选出一种独特有效的煮炼助剂,并结合生产实际,证明其碱煮炼脱胶效果相当明显。  相似文献   

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