A kind of method of from the tealeaves tree seeds, extracting tea seed oil
Technical field
The present invention relates to a kind of method of from the tealeaves tree seeds, extracting tea seed oil, especially relate to a kind of employing supercritical CO
2Abstraction technique extracts the method for tea seed oil from the tealeaves tree seeds.
Background technology
Tea tree (Camellia sinensis) belongs to the Theaceae Camellia, is the perennial evergreen xylophyta.The leaf ovalize of tea tree, there is sawtooth at the edge, opens five lobes between leaf and spends in vain, and fruit is oblate, and is triangular in shape, exposes seed after fruit is drawn up.The tender leaf tea making that can pick tea-leaves when spring, autumn and set, seed can extract oil, and the utility value of tea tree is mainly at tealeaves at present, and the utility value of seed does not obtain exploitation.
At present, from the tealeaves tree seeds, extract the method for tea seed oil, study lessly, and traditional oils process for extracting is generally milling process and organic solvent extraction; These methods are not only extracted long flow path, and energy consumption is high, and yield is low; Serious environment pollution, and the quality product of extracting is relatively poor, at the bottom of the purity; The product that organic solvent extraction obtains also has peculiar smell and harmful dissolvent residual.
Summary of the invention
The object of the present invention is to provide a kind of efficient high, energy consumption is low, good product quality, no solvent residue, the method for from the tealeaves tree seeds, extracting tea seed oil of environmentally safe.
The objective of the invention is to realize through following technical scheme.
It comprises the steps: (1) pulverizing: clean tealeaves tree seeds is dried or dried, be crushed to 16 ~ 40 orders (preferred 20 ~ 30 orders), place the extraction cylinder, install sealing-ring, the plug of screwing; (2) extraction: the ice chest temperature is set to-3 ℃ ~ 3 ℃ (preferred-2 ℃ ~ 2 ℃, more preferably 0 ℃), opens CO
2Steel cylinder, CO
2Come out from steel cylinder, get in the ice chest through the gas purifier I and liquefy, squeeze into the extraction cylinder by HPP through cleaner II, preheater I then, boost to 20MPa ~ 40MPa (preferred 25MPa ~ 35MPa), make CO
2Become supercutical fluid, control extraction cylinder temperature is 35 ℃ ~ 60 ℃, extraction time 2h ~ 4h, and the tea seed oil in the tealeaves tree seeds is extracted into CO
2In the fluid; (3) separate: the CO that contains tea seed oil
2Fluid after decompression gets into separation system, separates in separating still from the extraction cylinder, and the pressure of separating still I is 6MPa ~ 12MPa (preferred 8-10MPa; More preferably 9MPa); Temperature is 35 ℃ ~ 60 ℃, and the pressure of separating still II and way of escape balance, temperature are 35 ℃ ~ 55 ℃; With this understanding, grease and CO
2Realize effectively separating, and emit CO from the separating still bottom
2Draw from the separating still top, get in the ice chest through the cleaner I and liquefy, recycle.
Advantage of the present invention is: technical process is simple, and extraction efficiency is high, can contained grease in the tea-seed fully be extracted, and environmentally safe, and protected the natural nutrient component in the grease effectively.Gained tea seed oil quality product is pure; Free from extraneous odour, no solvent residue, many beneficiating ingredients such as rich in vitamin E, tea-polyphenol and unsaturated fatty acids; To reduce human blood viscosity, to reduce cardiovascula arteriosclerosis all helpful, has very high nutritive value and pharmaceutical use.
The present invention is to the economic worth of exploitation tealeaves tree seeds, and it is significant to make full use of tealeaves tree seeds resource.
Description of drawings
Fig. 1 is the present invention's technological process apparatus synoptic diagram.
Embodiment
Below in conjunction with accompanying drawing and preferred embodiment the present invention is further described, but and do not mean that the restriction scope of the present invention.
Embodiment 1
With reference to Fig. 1: (1) with the oven dry of 2Kg tealeaves tree seeds, is crushed to the barrel of putting into 5L extraction cylinder 8 behind 20 orders; (2) temperature of ice chest 5 is set to 0 ℃, and the temperature of extraction cylinder 8 is set to 35 ℃, and the temperature of separating still I 10 is set to 55 ℃, and the temperature of separating still II 12 is set to 55 ℃, opens CO
2Steel cylinder 2, CO
2Come out from steel cylinder 2, get into liquefaction in the ice chest 5, start HPP 6 then, CO through gas purifier I 3
2Through cleaner II 4, preheater I 7 is squeezed into extraction cylinder 8, boosts to 30MPa; Make it to become supercutical fluid and extract, get into separation system again after getting into 9 preheatings of preheater II, in order to realize separating fully of unsaturated fatty acids and non-lipid material; Reduce subsequent disposal work, adopt secondary to separate, the pressure of regulating separating still I 10 is 10MPa; The pressure of separating still II 12 keeps and way of escape balance, unsaturated fatty acids and CO
2Separate in separating still I 10, and emit from separating still I 10 bottoms, non-lipid material gets into separating still II 12 after 11 preheatings of preheater III, with CO
2In separating still II 12, separate CO
2Draw from separating still II 12 tops,, get into ice chest 5 liquefaction, recycle through cleaner I 3 through under meter 1.Extracted 2 hours, and collected grease 248g, percentage extraction is 12.4%.
Warp is 84.2% according to unsaturated fatty acid content in the GC-MS method working sample; According to containing tea-polyphenol 9.4% in the tartrate iron determination of color sample; According to containing vitamin E 1.47mg/g in the determined by ultraviolet spectrophotometry sample.
Embodiment 2
With the oven dry of 2Kg tealeaves tree seeds, be crushed to 30 orders, the pressure of control extraction cylinder is 35MPa; Temperature is set to 40 ℃, and the pressure of separating still I is adjusted to 9MPa, and temperature is set to 55 ℃; The temperature of separating still II is set to 55 ℃, and other extracted 3 hours with embodiment 1; Collect grease 308g, percentage extraction is 15.4%.
Warp is 82.7% according to unsaturated fatty acid content in the GC-MS method working sample; According to containing tea-polyphenol 8.3% in the tartrate iron determination of color sample; According to containing vitamin E 1.34mg/g in the determined by ultraviolet spectrophotometry sample.
Embodiment 3
With the oven dry of 2Kg tealeaves tree seeds, be crushed to 40 orders, the pressure of control extraction cylinder is 25MPa; Temperature is set to 55 ℃, and the pressure of separating still I is adjusted to 8MPa, and temperature is set to 60 ℃; The temperature of separating still II is set to 60 ℃, and other extracted 2.5 hours with embodiment 1; Collect grease 254g, percentage extraction is 12.7%.Warp is 83.4% according to unsaturated fatty acid content in the GC-MS method working sample; According to containing tea-polyphenol 7.9% in the tartrate iron determination of color sample; According to containing vitamin E 1.49mg/g in the determined by ultraviolet spectrophotometry sample.