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Supercritical CO2 Extraction Process for Plant Essential Oils And Bioactive Substances

Supercritical CO2 extraction of Essential Oils
Essential Oils

We have collected some supercritical carbon dioxide extraction methods of plant essential oils and bioactive substances on the Internet, and we hope to show them here to help you

In each article we try to give the source of the article, or the name of the author.

If there are any mistakes, please email us and we will correct them in time.

1: Supercritical CO2 extraction of orange olein from honey pomelo peel

2: Deacidification and Deodorization of Tea Oil with Countercurrent Supercritical CO2 Extraction

3: Supercritical CO2 extraction and concentration of natural carotene

4: Reduction of cholesterol in lard by supercritical CO2 distillation process

5: Supercritical fluid co2 extraction extracts naringenin from Dendrobium officinale Kimura et Migo

6: Supercritical CO2 extraction process of maggot oil

7: Supercritical CO2 extraction machine for separating garlic oil and nervonic acid

8: Extraction of 10-DAB from Taxus Leaves by Supercritical CO2 Extraction Process

9: Supercritical CO2 extraction of Lepidium meyenii Walp oil

10: SFE CO2 extraction process of Pandanus amaryllifolius Roxb. Leaves

11: Konjac seed oil supercritical co2 extraction process

12: Supercritical CO2 extraction of thyme essential oil

13: Supercritical CO2 extraction of rosemary antioxidants and essential oils

14: Supercritical CO2 extraction of chili oleoresin

15: Supercritical extraction method of tea extract

16: Removal of caffeine from green tea concentrate by supercritical CO2

17: Supercritical CO2 extraction of ginger oleoresin

18: Tea seed oil supercritical extraction process

19: Supercritical carbon dioxide fluid extraction of artepillin C from propolis

20: Supercritical co2 extraction of grape seed oil extraction pressure, temperature, time

21: The best process for extracting magnolol by supercritical co2 extraction equipment

22: Study on supercritical CO2 extraction of millet bran oil

23: Supercritical co2 extraction distillation of millet bran oil

24: Comparison of extraction technology of artemisinin by supercritical CO2 extraction equipment

25: Extraction of ergosterol from Ganoderma lucidum mycelium by supercritical CO2 extraction equipment

26: Extract essential oil of cuminum cyminum L by supercritical fluid extraction

27: High efficiency supercritical co2 extraction technology of cinnamon essential oil

28: Extraction of Camellia oleifera Polyphenols by supercritical CO2 extraction equipment

29: Composition Analysis of Black Pepper Oil Resin by Supercritical Fluid Extraction

30: Extraction of Celery Seed Oil by Supercritical CO2 extraction

31: Study on Supercritical CO2 Fluid Extraction of Sardine Oil

32: Research on supercritical CO2 extraction of propolis active ingredients

33: Super Critical CO2 Extraction Machine for Hemp Tea Leaf Herb Pea Protein

34: Supercritical co2 extraction machine for olive oil

35: Supercritical co2 extraction of jackfruit seeds

36: Supercritical Co2 Extraction Natural Astaxanthin,Astaxanthin Oil

37: Supercritical CO2 Extraction Equipment For Fish Oil

38: Supercritical co2 fluid extraction machine for flax seed peel

39: Supercritical Fluid Extraction For Hemp & Herbs

40: Supercritical co2 oil extraction plant for Ginger oil extraction

41: supercritical extraction of rosemary essential oil

42: Supercritical co2 extraction of lycopene

43: Supercritical Carbon Dioxide Extraction and Fatty Acid Composition Analysis of Blackberry Seed Oil

44: Herbal Hemp Supercritical CO2 CBD Oil Extraction Systems

45: Supercritical CO2 Fluid Extraction for Palm Seed Oil

46: Supercritical CO2 countercurrent extraction concentrated capsicum pigmen

47: Study on supercritical fluid extraction of amygdaloside

48: Supercritical fluid extraction technology and its application in food industry

Supercritical CO2 extraction of orange olein from honey pomelo peel

Abstract::

It is feasible to use supercritical CO2 extraction technology to extract orange olein from honey pomelo peel. The extraction pressure is 25MPa, extraction temperature is 328K, extraction time is 2h, and the use of entrainer is not used. The extraction rate can exceed 60%.

Supercritical co2 extraction process

Pulverization degree:80 mesh

Laboratory equipment:HA230-50-05

Extraction pressure: 25 MPa

Extraction temperature: 45°C

Separation kettle Ⅰ pressure: 0.5 MPa

Extraction time: 120 min

Deacidification and Deodorization of Tea Oil with Countercurrent Supercritical CO2 Extraction

The effects of extraction pressure on the effect of deacidification were investigated under the conditions that the temperature of the four stages of the extraction column were 35 ° C, 50 ° C, 65 ° C and 80 ° C, the separation kettle pressure was 5 MPa and the separation kettle temperature was 40 ° C. It can be seen from Table 5 that under various pressures, the odor of the extracted tea oil is less than 1/4 of the original odor. The odorous substances are concentrated in the extract and have a significant deodorizing effect.

Supercritical CO2 extraction and concentration of natural carotene

Abstract:

The composition of 10% carotene raw materials is complex, and it is difficult to increase the content of carotene by supercritical CO2 extraction at a fixed pressure; the use of supercritical CO2 gradient pressure extraction method can concentrate 10% of natural carotene samples to 20.14%, optimized Later, the concentration is expected to increase further.

Reduction of cholesterol in lard by supercritical CO2 distillation process

Supercritical co2 distilltionation process

Distilltionation column down temperature: 60°C

Distilltionation column upper temperature: 70°C

Mass ratio of supercritical co2 : 10: 1

Supercritical fluid co2 extraction extracts naringenin from Dendrobium officinale Kimura et Migo

Supercritical co2 extraction process

Pulverization degree:40 mesh

Laboratory equipment:HA231-50-06

Extraction pressure: 35 MPa

Extraction temperature: 50°C

Separation kettle Ⅰ pressure: 0.5 MPa

Cosolvent: Ethanol; Concentration :18 wt%

Extraction time: 9HR

Supercritical CO2 extraction process of maggot oil

Abstract::

Chinese medicine maggot oil was exacted with supercritical CO2. On the basis of single factor test, the effects of exaction temperature, CO2 flow rate, exaction time and exaction pressure on the yield of maggot oil were studied by the response surface methodology. The results showed that the optimal exaction conditions of maggot oil with supercritical CO2 were as follows: exaction temperature 45 ℃, CO2 flow rate 23 L•h-1, exaction time 100 min and exaction pressure 29 MPa. Under these conditions, the yield of maggot oil was 18.87%.

Supercritical co2 extraction process

Pulverization degree:40 mesh

Laboratory equipment:HA231-50-06

Extraction pressure: 29 MPa

Extraction temperature: 45°C

Separation kettle Ⅰ pressure: 0.5 MPa

Extraction time: 100 min

Supercritical CO2 extraction machine for separating garlic oil and nervonic acid

Abstract::

The single-factor test method was used to investigate the impact trends of the crushing particle size, extraction time, and extraction pressure of the raw materials in the supercritical CO2 extraction process. The optimal extraction process was screened by orthogonal experiments, and the best process garlic extract was GC-MS. The fatty acid composition of the oil was analyzed; the method of saponification and crystallization was used to separate the neural acids.

Supercritical co2 extraction process

Pulverization degree:8 mesh

Laboratory equipment:HA221-50-06

Extraction pressure: 35 MPa

Extraction temperature: 45°C

Separation kettle Ⅰ pressure: 6 MPa

Separation kettle Ⅰ temperature: 55°C

Extraction time: 120 min

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A more suitable extraction process was determined: the crushed particle size of the raw material was 8 meshes, the extraction pressure was 35 MPa, and the extraction temperature was 45 ° C; the pressure in the separation tank was 6 MPa, the analysis temperature was 55 ° C, and the extraction time was 2 hours; the yield of garlic oil was 32.3%, and the acid The content was 5.4%; the fatty acids in garlic oil were analyzed, and 12 kinds of fatty acid components were identified; the yield of neural acid isolated from the oil was 4.6%, and the purity of the neural acid was 96%. Conclusion: Supercritical CO2 extraction of garlic oil and neural acid separation process is stable and feasible, with good reproducibility, and can effectively enrich neural acid.

Extraction of 10-DAB from Taxus Leaves by Supercritical CO2 Extraction Process

Supercritical co2 extraction process

Laboratory equipment:HA231-50-06

Extraction pressure: 30 MPa

Extraction temperature: 50°C

Separation kettle Ⅰ pressure: 10 MPa

Separation kettle Ⅰ temperature: 60°C

Separation kettle Ⅱ pressure: 6 MPa

Separation kettle Ⅱ temperature: 45°C

Entrainer: 80% ethanol solution

80% ethanol entrainer volume (ml) : 1: 1.5

Extraction time: 90 min

Supercritical CO2 extraction of Lepidium meyenii Walp oil

Supercritical CO2 extraction of Lepidium meyenii Walp oil process

Maca granularity:: 40 mesh

Laboratory equipment:HA230-50-06

Extraction pressure: 32 MPa

Extraction temperature: 45°C

Separation kettle Ⅰ pressure: 8 MPa

Separation kettle Ⅰ temperature: 45°C

Separation kettle Ⅱ pressure: 6 MPa

Separation kettle Ⅱ temperature: 40°C

Separation kettle Ⅲ pressure: 6 MPa

Separation kettle Ⅲ temperature: 40°C

95% ethanol entrainer volume (ml) : 1: 2

Extraction time: 120 min

SFE CO2 extraction process of Pandanus amaryllifolius Roxb. Leaves

SFE CO2 extraction process of Pandanus amaryllifolius Roxb. Leaves

Laboratory equipment:HA231-50-06

Extraction pressure: 20 MPa

Extraction temperature: 45°C

Separation kettle Ⅰ pressure: 12 MPa

Separation kettle Ⅰ temperature: 45°C

Separation kettle Ⅱ pressure: 12 MPa

Separation kettle Ⅱ temperature: 40°C

Separation kettle Ⅲ pressure: 6 MPa

Separation kettle Ⅲ temperature: 40°C

Extraction time: 60 min

Konjac seed oil supercritical co2 extraction process

Supercritical co2 extraction process

Laboratory equipment:HA231-50-06

Extraction pressure: 20 MPa

Extraction temperature: 60°C

Separation kettle Ⅰ pressure: 15 MPa

Separation kettle Ⅰ temperature: 50°C

Separation kettle Ⅱ pressure: 6 MPa

Separation kettle Ⅱ temperature: 45°C

Extraction time: 90 min

Supercritical CO2 extraction of thyme essential oil

Process conditions for preparing thyme essential oil by supercritical carbon dioxide

Laboratory equipment: HA120-50-01

Extraction pressure: 25 MPa

Extraction temperature: 40°C

Extraction time: 240 min

Summary

The experimental results show that the process conditions for preparing thyme essential oil by supercritical carbon dioxide are: extraction pressure 25 MPa, extraction temperature 40 ℃, and extraction time 4 h. Under these conditions, the extraction yield was 4.2 2%.

Supercritical CO2 extraction of rosemary antioxidants and essential oils

Optimum experimental process parameters for supercritical extraction of chilli oleoresin

Laboratory equipment: HA120-50-02

Pulverization degree: 50 mesh

Extraction pressure: 20 MPa

Extraction temperature: 40°C

Extraction time: 240 min

Separate pressure I: 5 MPa

Separate I temperature: 70°C

Separate pressure II: 4 MPa

Separate II temperature: 40°C

Summary

Average yield of rosemary oiO was 1.80 % . Resultr of ccnstituent analysia of rosemary oit ohowed that the essentiat oit mainly ccntains 1,8-cineeIe, camphor, a-terpineoI, borneel, verbenone, terpinen-4-oI, bornyS acctate and linaloI. Average yield oS rosemary antioxidant was 11.93 % . Main active ccmponentr oS rosemary antioxidant were ccrnosic acid, ccrnosol, and rosmarinic acid, whose ccntentr were 23.61 % , 7.33% and 5. 13 % , respectively.

Supercritical CO2 extraction of chili oleoresin

Optimum experimental process parameters for supercritical extraction of chilli oleoresin

Laboratory equipment: HA120-50-01 Supercritical co2 extraction equipment

Pulverization degree: 50 mesh

Extraction pressure: 30 MPa

Extraction temperature: 315k

Extraction time: 36 min

Summary

In summary, the experimental extraction pressure is 30 MPa, temperature is 315 K, time is 3.0 h, and CO2 flow is 0.40 m3 / h.

Supercritical extraction method of tea extract

Supercritical CO2 extraction of ginger oleoresin extraction process data from ginger:

Pulverization degree: 40 mesh

Extraction pressure: 30 MPa

Extraction temperature: 45°C

Separation pressure : 20 MPa

Separation temperature:70°C

Extraction time: 10 min 5 times

Summary

Supercritical extraction method of tea extract
Supercritical extraction method of tea extract

Black tea is crushed, and the loading requires 20kg / 100L supercritical CO2; supercritical CO2 extraction technical requirements: pressure is 30MPa, extraction temperature is 45 ° C, separation temperature is 80 ° C, extraction method: static extraction 5 times, each static The extraction time was 10 min. 142 g of essence was obtained by extraction, and the extraction rate was 0.71%. Analysis by GC-MS: The product is rich in more than 60 aroma components such as alcohols, ketones, aldehydes, ethers and esters, among which dimethyl sulfide, 2-methyl-propane Aldehydes, 2-methylbutyraldehyde and dehydrolinalool have higher aroma components.

Removal of caffeine from green tea concentrate by supercritical CO2

Removal of caffeine from green tea concentrate by supercritical CO2:

Extraction pressure: 30 MPa

Extraction temperature: 56°C

Extraction time: 36 min

Summary

It can be envisaged that the continuous operation of decaffeinated tea concentrate or instant tea can be realized by connecting a production-type supercritical CO 2 extraction device on the instant tea production line.

Supercritical CO2 extraction of ginger oleoresin

Supercritical CO2 extraction of ginger oleoresin extraction process data from ginger:

Pulverization degree: 120 mesh

Extraction pressure: 35 MPa

Extraction temperature: 35°C

Extraction time: 90 min

Summary

The single-factor test and orthogonal test were used to discuss the process conditions that affect the supercritical CO2 extraction of ginger oleoresin, and the optimal extraction process parameters were determined: fresh ginger dried at 50 ° C in far-infrared, crushed through a 120 mesh screen, 35MPa Extracted at 35 ℃ for 2.5h, the mass extraction rate was 6.08%, and the curcumin extraction rate was 2.78%.

Antioxidant activity experiments show that the extract has a strong ability to scavenge DPPH free radicals, and the scavenging ability has a clear dose-effect relationship with concentration.

Tea seed oil supercritical extraction process

Supercritical CO2 extraction of tea seed oil extraction process data from tea seeds:

Pulverization degree: 40 mesh

Extraction pressure: 35 MPa

Extraction temperature: 45°C

Extraction time: 150 min

Summary

Tea seed oil supercritical extraction process includes washing, drying, pulverizing, CO2 supercritical extraction and freeze centrifugation steps.

The supercritical extraction process of tea seed oil keeps squalene in tea seed oil as much as possible.

Supercritical carbon dioxide extraction can be performed at a temperature close to room temperature, which can effectively prevent the oxidation and escape of heat-sensitive substances, and is a suitable method for extracting health tea seed oil.

Supercritical CO2 fluid extraction of tea seed oil has the advantages of simple operation, short extraction time, and low extraction temperature.

This technology has the advantages of non-toxicity, harmlessness, product oxidation avoidance, no chemical reagent residues and pollution, and no refining required. Therefore, it is a good method to extract health tea seed oil.

Supercritical carbon dioxide fluid extraction of artepillin C from propolis

Supercritical CO2 extraction of artepillin C extraction process data from  propolis:

Extraction pressure: 28 MPa

Extraction temperature: 60°C

Entrained solvent: Ethanol

Separation temperature : 60°C

Separation pressure : 20 MPa

Separation temperature Ⅱ :60°C

Separation pressure Ⅱ: 20 MPa

Extraction time: 120 min

Summary

Using supercritical carbon dioxide as a solvent, combined with chromatography and adsorption technology, a large number of active components of artepillin C in propolis can be separated and purified, and the biological activity of active components of artepillin C can be maintained. Eliminates the need for complicated solvent removal, concentration, and separation procedures, and no safety concerns such as solvent residues, low production costs, environmental protection, safety, and practical value;

Supercritical co2 extraction of grape seed oil extraction pressure, temperature, time

The best parameters for extracting grape seed oil using a supercritical co2 extraction machine:

Pulverization degree: 40 mesh

Extraction pressure:28Mpa

Extraction temperature:35 °C

Extraction time:80 minutes

The best process for extracting magnolol by supercritical co2 extraction equipment

The best parameters for extracting Magnolol using a supercritical co2 extraction machine:

Pulverization degree: 40 mesh

Extraction pressure:25-27Mpa

Extraction temperature:35-45 °C

Extraction time:120-240 minutes

Separation pressure:6Mpa

Separation soaking time:300 minutes

Flow rate of CO2:25Kg–35Kg/h

Study on supercritical CO2 extraction of millet bran oil

The best parameters for extracting millet bran oil using a supercritical co2 extraction machine:

Moisture content:8%

Extraction pressure:30Mpa

Extraction temperature:45 °C

Extraction time:240 minutes

Extraction efficiency19.69%

Summary

Under the condition of 50 kg/h CO2 flow rate, the orthogonal test of three factors and three levels was carried out for extraction pressure, extraction temperature and extraction time. Based on the results of single factor test and orthogonal test, when the pressure was 35 MPa, the oil quality was relatively turbid, and the equipment investment, power consumption and risk were large. The final conditions for supercritical CO2 extraction of millet bran oil are: extraction pressure 30 MPa, extraction temperature 45 ℃, extraction time 2 h, CO2 flow rate 50 kg/h. Under the optimum conditions, the yield of millet bran crude oil can reach 19.69%.

Supercritical co2 extraction distillation of millet bran oil

The millet bran oil extracted by supercritical extraction contains high unsaturated fatty acids, especially containing up to 67.8% of linoleic acid.

Extraction pressure: 30 MPa

Extraction temperature: 45°C

Extraction time: 2 h

Co2 flow: 50 kg/h

Rectification column pressure: 10 MPa

Rectification temperature rectification I: 40°C

Fine Distillation II: 45°C

Rectification III: 50°C

Rectification IV: 55°C

Comparison of extraction technology of artemisinin by supercritical CO2 extraction equipment

The optimal parameters for the extraction of artemisinin from supercritical CO2 extraction equipment can be more than 95% pure:

Extraction pressure: 20 MPa

Extraction temperature: 333K

Extraction time: 2h

Summary

Artemisinin was extracted from Artemisia annua by supercritical CO2 extraction. The effects of extraction pressure, temperature and time on the yield of artemisinin were investigated. The results showed that the best extraction conditions were extraction pressure 20MPa, temperature 333k and extraction time 2H. The purity of artemisinin product was more than 95% after simple separation. Supercritical CO2 extraction process has many advantages, such as high selectivity, especially suitable for extraction of heat sensitive substances, simple separation process, energy saving, non-toxic, tasteless, pollution-free and residue free solvent CO2, which is very safe. However, due to high pressure requirements on equipment and small polarity of CO2, its extraction rate of macromolecular substances is low, which leads to extensive application in industry. Use is limited.

Extraction of artemisinin by supercritical CO2 extraction equipment
Extraction of artemisinin by supercritical CO2 extraction equipment

Extraction of ergosterol from Ganoderma lucidum mycelium by supercritical CO2 extraction equipment

Supercritical CO2 extraction of ergosterol extraction process data from Ganoderma lucidum mycelium:

Extraction pressure: 20 MPa

Extraction temperature: 50°C

CO2 flow: 2.5 L / min

Extraction time: 120 min

Summary

In the process of extracting ergosterol from Ganoderma lucidum mycelium by supercritical CO2, single factor experiments show that the extraction pressure, extraction temperature and CO2 flow rate have different effects on the extraction amount of ergosterol. L934 orthogonal experiment optimizes the extraction conditions. The results show that the extraction pressure and extraction temperature have significant effects, while the CO2 flow rate has no significant effects.

The appropriate combination of the three factors A2b3c3, i.e. extraction pressure 20 MPa, extraction temperature 50 ℃, CO2 flow rate 2.5 L / min, the extraction amount of ergosterol in this combination is 1.1362 mg / g, which is higher than that in the orthogonal combination.

Extract essential oil of cuminum cyminum L by supercritical fluid extraction

Optimal Process Parameters for Extracting Fennel Essential Oil by Supercritical Fluid Extraction

Pulverization degree: 40 mesh

Extraction pressure: 35 MPa

Extraction temperature: 40°C

Extraction time: 150 min

Yield : 13.56%

Summary

The essential oil of cumin was extracted and purified by supercritical combined molecular distillation. The volatile components of cumin essential oil were qualitatively analyzed by GC-MS and double column retest. 44 components were identified on DB-5 column and 39 components were identified on inno-wax column, 20 of which existed on both columns. A method for the simultaneous determination of the main aromatic compounds (β - pinene, paracymene, γ - Terpinene, cumin aldehyde) in cumin oil by capillary gas chromatography with n-dodecane as internal standard was established.

The results showed that there was a good linear relationship between the peak area of four aromatic substances and their mass concentration under the selected chromatographic conditions, and R2 was greater than 0.9996. After molecular distillation and purification, the content of cumin aldehyde, the main component of cumin essential oil, increased from 11.48% to 30.30% before purification.

High efficiency supercritical co2 extraction technology of cinnamon essential oil

The optimum conditions for the extraction of cinnamon by supercritical co2 :

Extraction pressure: 35 MPa

Extraction temperature: 40°C

CO 2 flow rate: 30 kg / h

Bulk density: (0.44 ± 0.02) g / mL

Extract yield: 5.8% ~ 6.0%

Extraction of Camellia oleifera Polyphenols by supercritical CO2 extraction equipment

Experimental results of extracting tea seed oil from tea seeds by supercritical CO2 fluid extraction:

Extraction temperature: 35 °C

Extraction pressure: 30 MPa

Separation temperature: 55 °C

Separation pressure: 8 MPa

Extraction time: 2 h

Tea seed oil yield: 15.4%

Composition Analysis of Black Pepper Oil Resin by Supercritical Fluid Extraction

The optimum conditions for supercritical CO2 extraction of Black Pepper Oil were as follows:

Pulverization degree: 60 mesh

Extraction pressure: 30 Mpa

Extraction temperature: 50°C

Extraction time: 3h

Abstract

Under the static conditions of supercritical CO2 extraction pressure of 30 Mpa, extraction time of 3 h and extraction temperature of 50 °C, the black pepper raw materials without any treatment, absolute ethanol treatment and ethyl acetate treatment were extracted. The oleoresin was analyzed by gas chromatography-mass spectrometry coupled with GCMS for the component analysis of the extracted black pepper oleoresin, and the material was qualitatively analyzed by retention index and MS. The results showed that under supercritical extraction conditions, there were 22 aroma components of black pepper oleoresin without pretreatment, and 17 kinds of aroma components of black pepper oleoresin pretreated with absolute ethanol. There are 41 aroma components of the pre-treated black pepper oleoresin.

Extraction of Celery Seed Oil by Supercritical CO2 extraction

The best parameters for extracting celery seed oil using a supercritical co2 extraction machine:

Pulverization degree: 60 mesh

Extraction pressure:20Mpa

Extraction temperature:45 °C

Extraction time:120 minutes

Flow rate: 15 l/h

Study on Supercritical CO2 Fluid Extraction of Sardine Oil

The optimum conditions for supercritical CO2 extraction of sardine fish oil were as follows:

Extraction pressure: 2900 psi

Extraction temperature: 40°C

Extraction time: 3h

Fish oil yield: 0.3246%

Research on supercritical CO2 extraction of propolis active ingredients

The optimized conditions for the supercritical extraction of propolis are:

Extraction temperature:50 ° C,

Extraction pressure:25 MPa,

Entrainer:95% ethanol,

Solid-liquid ratio:6: 1.

Propolis was extracted under the optimal conditions, and the flavonoid content of the obtained extract was 14.8%.

Super Critical CO2 Extraction Machine for Hemp Tea Leaf Herb Pea Protein

Working principle of supercritical extraction equipment: The principle of the separation process is to use the relationship between the solubility of supercritical fluid and its density, that is, the influence of pressure and temperature on the solubility of supercritical fluid. In the supercritical state, the supercritical fluid is brought into contact with the substance to be separated, so that the components of the polarity, the boiling point, and the molecular weight are selectively extracted in order. Of course, the extract obtained for each pressure range may not be single, but it is possible to control the conditions to obtain the optimum proportion of the mixed components, and then to reduce the supercritical fluid into a normal gas by means of decompression and temperature rise, and the extracted material is Complete or basic precipitation to achieve the purpose of separation and purification, so the supercritical CO2 fluid extraction process is a combination of extraction and separation processes.

Supercritical co2 extraction machine for olive oil

Supercritical co2 extraction is anExtraction method of non-pollution,undamage.

It can reserve natural composition.it willnot intermix chemical composition.

The extracted components are relatively singleand high in purity.

Supercritical co2 extraction of jackfruit seeds

Supercritical co2 extraction technology is thelatest subject in modern chemical separation and it is an advanced separationtechnology rising in the world. The so-called supercritical fluid is thethermodynamic state liquid which is above the critical point and the criticalpoint is the point at which the gas-liquid interface just disappears. Thesupercritical fluid has a very unique physical and chemical properties, itsdensity close to the liquid, viscosity close to the gas. The big diffusioncoefficient, low viscosity, big dielectric constant and other characteristicsmake its separation effect better, so it is a good solvent.

Supercritical Co2 Extraction Natural Astaxanthin,Astaxanthin Oil

Supercritical Co2 Extraction technology is a newsubject of modern chemical & industry, and is an advanced separatingprocess arising in the international market at present. The so calledsupercritical fluid is the fluid when the thermodynamic state is over thecritical point (Pc, Tc), and the critical point is the state that the interfacebetween gas and liquid just disappears. There are special physical/ chemicalcharacteristics for the supercritical fluid, its density is near to liquid's,and its viscosity is near to gas', with the big diffusion coefficient, smallviscosity and big dielectric constant, etc, 

Supercritical CO2 Extraction Equipment For Fish Oil

Supercritical fluid extraction(supercritical fluid extraction) is an advanced separation process in the worldat present. Supercritical fluid extraction is more than 75, more than that inatmospheric pressure 31.2C temperature, the solvent extraction kettle, fullcontact with the extract was, because the infiltration fluid with gas andsolvent have easy diffusion characteristics, in accordance with the polardissolved in polar and non polar non soluble chemical principle of polarity.Will not matter in the level of solute solute directly to nonpolar substancesdissolved in the solvent, the solvent selection of carbon dioxide to the moststable, when carbon dioxide in the mixed solution of nonpolar substancesdissolved in the supercritical state, with strong pressure in the extractionkettle, kettle and separated into change the temperature conditions, thenon-polar material produce timely solute separation, in order to achieve non polarsubstance extraction of solute to nonpolar substances containing plantessential oil, wax, pigment and other non-polar substances, Some of the solutescan use ethanol as a entrainer, and some of the polar substances are also takenout together.

Supercritical co2 fluid extraction machine for flax seed peel

Supercritical Co2 fluid extraction machine for flax seed peel (the SFE) is an application of a strong green separation technology, adopts CO2 as the solvent.
Supercritical CO2 fluid under greater density and dielectric constant, the solubility of the material is large, and with the pressure and temperature changes rapidly changing, therefore, not only the solubility of certain substances selective, and easy separation of solvent and extract.

Supercritical Fluid Extraction For Hemp & Herbs

The best parameters for extracting CBD oil using a supercritical co2 extraction machine:

Pulverization degree:20-40 mesh

Moisture content:<8%

Extraction pressure:30Mpa

Extraction temperature:50-60 °C

Extraction time:90-120 minutes

CO2 flow:150~200kg/h

Summary

Supercritical extraction is the most common way of plant extraction. Supercritical materials use the movement of carbon dioxide gas to gradually dissolve liquid and other substances, and finally provide safe and pure CBD products.

When extracting industrial hemp oil rich in cannabidiol, the selected industrial hemp (including leaves, stems and seeds) is first placed in an oven and dried at 50 ° C for 12 hours; then pre-dried The industrial hemp is put into a pulverizer and pulverized into 20-mesh industrial hemp powder. The industrial hemp powder is placed in an oven and dried at 50 ° C for 12 hours; the dried industrial hemp powder remains in the drying oven. The inside is naturally cooled to normal temperature; 132.0 g of cooled industrial hemp powder is weighed into a material bucket of the extraction kettle, and C0 2 gas is injected into the extraction kettle for extraction, the extraction temperature is 60 ° C, the pressure is 30 MPa; the CO 2 gas is extracted by extraction. The flow rate of the kettle is 200kg/h, and the extraction time is 1.5h. The industrial hemp oil rich in cannabisdiol in industrial hemp powder is dissolved in the supercritical CO 2 fluid, and then the industrial hemp oil rich in cannabidiol is used. The C02 fluid was analyzed from the extractor by throttling expansion to the separation vessel to obtain 6.49 g of industrial hemp oil rich in cannabidiol, and the oil yield was 4.92%. Finally, the industrial hemp oil rich in cannabisdiol is dissolved in a homogenizer after heating at 80 °C, homogenized and filled, and stored in the dark.

Supercritical co2 oil extraction plant for Ginger oil extraction

Supercritical Co2 fluid extraction technology was mainly working for natural product extraction, separation and purification. The whole extracting process diversified and versatile, this device use Co2 as supercritical solvent, according to Co2 solvency ability, through operating and adjusting its parameter( mainly pressure and temperature), thus to change natural product density, Co2 reached into critical state, thereby acquired the inner active ingredient from natural product.

supercritical extraction of rosemary essential oil

The technology of Supercritical Fluid Extraction is a new subject from Modern Chemicals Industries, which is one of the advanced Separation Technology. As for SCF(Supercritical Fluid), it is was that fluid on Critical Point(Pc, Tc) under Thermodynamic State,&nbsp;&nbsp;the Critical Point is the state point when interface of Gas and Liquid disappear, which process very novel physical&amp; chemical characters. It density degree close to liquid, viscosity degree close to gas, but bigger diffusion coefficient &amp;dielectric constant, smaller viscosity etc. these characters have contributed to good separation effects. So the SFE is mainly about Separation,&nbsp;&nbsp;the solution will touch with extracted materials under High Pressure&amp; Suitable Temperature, the Solutes would be diffused into the solution, then change the operation Conditions, to make the Solutes separate out.

Supercritical co2 extraction of lycopene

Supercritical Co2 Fluid Extraction Machine for lycopene tomato (the SFE) is an application of a strong green separation technology, adopts CO2 as the solvent. Supercritical CO2 fluid under greater density and dielectric constant, the solubility of the material is large, and with the pressure and temperature changes rapidly changing, therefore, not only the solubility of certain substances selective, and easy separation of solvent and extract. Compared with conventional separation methods, has low extraction temperature strong selectivity, high efficiency, low energy consumption, no pollution and other characteristics, especially for fat-soluble, high boiling point, heat sensitive material extraction, but also for different components Fine separation. Widely used in pharmaceutical, food industry, health care products, cosmetics, perfume an other industries.

Supercritical Carbon Dioxide Extraction and Fatty Acid Composition Analysis of Blackberry Seed Oil

The best parameters for extracting blackberry seed oil using a supercritical co2 extraction machine:

Pulverization degree: 40 mesh

Extraction pressure:30Mpa

Extraction temperature:35 °C

Separation temperature: 55 °C

Separation pressure: 12 MPa

Extraction time:50 minutes

Extraction efficiency16.10%

Summary

Supercritical CO2 Blackberry Seed Oil Extraction Equipment
Supercritical CO2 Blackberry Seed Oil Extraction Equipment

Objective: To extract blackberry seed oil from blackberry seeds with supercritical carbon dioxide and determine its fatty acid composition. Methods: Operating parameters that influence the extraction of blackberry seed oil were optimized using an orthogonal array design. The fatty acid composition of blackberry seed oil was analyzed by gas chromatography-mass spectrometry (GC-MS). Results: The optimal extraction conditions were extraction temperature of 35 ℃, extraction pressure of 12 MPa, separation pressure of 12 MPa and separation temperature of 55 ℃. Under thess conditions, the yield of blackberry seed oil was up to 16.10%. The major fatty acids were palmic acid (5.38%), stearic acid (3.53%), oleic acid (13.70%), linoleic acid (60.48%), gamma-linolenic acid (11.16%) and total unsaturated fatty acid (85.34%).

Herbal Hemp Supercritical CO2 CBD Oil Extraction Systems

Summary

Cannabidiol is extracted from industrial cannabis and is the main active ingredient in cannabinoids. It has neuroprotective effects, is non-addictive, and has antispasmodic, rheumatoid arthritis and anxiolytic effects. It is used in medicine And other fields have attracted widespread attention and become a research focus in recent years. At present, most industrial hemp oils are extracted by solvent extraction. Existing extraction methods require a large amount of expensive organic solvents, high energy consumption, high extraction costs, and solvent residues and odors in the extracted cannabidiol. Low purity.

  Supercritical CO2 extraction of CBD Oil can improve the extraction purity and extraction rate of industrial cannabis oil rich in cannabidiol, and can also reduce environmental pollution and extraction costs.

Supercritical CO2 Fluid Extraction for Palm Seed Oil

The best parameters for Supercritical CO2 extraction combined with adsorption method for the treatment of high concentration organic wastewater:

Extraction pressure:30Mpa

Extraction temperature:45 °C

Extraction time:120 minutes

Test volume:15ml

Summary

The seed oil of palm (Trachycarpus fortunei) harvested from two sampling places of West Hunan province was extracted by supercritical CO2 fluid extraction technology, and its components was analyzed by GC-MS. The results showed that the optimal process conditions are as follows: extraction pressure 30 MPa, temperature 45 ℃, and time 2 h. The oil yield is 14.6% under the above conditions. According to GC-MS results, there are eight and seven kinds of fatty acid in Trachycarpus fortunei seed oil from the two sampling places, respectively. The common components of the two seed oils are 10,13-octadecadienoic acid (36.58%), (z)- 9-octadecenoic acid (29.93%), hexadecanoic acid (13.22%), dodecanoic acid (8.74%), methyl tetradecanoate (6.62%), octade- canoic acid (2.63%) and (z)-9-hexadecenoic acid (1.28%). Trachycarpus fortunei seed oil contains abundant unsaturated fatty acids, which can be used as edible oil and industrial oil after refinement.

Supercritical co2 palm seed oil extraction equipment
Supercritical co2 palm seed oil extraction equipment

Key words: Trachycarpus fortunei;seed oil;supercritical CO2 fluid extraction;gas chromatography-mass spectrometry

Supercritical CO2 countercurrent extraction concentrated capsicum pigmen

Supercritical CO2 countercurrent extraction concentrated capsicum pigmen

Chili Pigment Ingredients color:24000

Pressure:36Mpa

CO2 flow:30000M3 / h M2

Pepper color: 150000

Abstract:

As a green technology, supercritical CO2 extraction has widely applied in extraction of natural materials. The annual production capacity ranges from hundreds of tons to tens of thousands of. However, the separation efficiency of supercritical CO2 extraction is very low, especially for mixtures with small different properties of composition, because it is only one stage separation. Continuous countercurrent supercritical CO2 extraction (CC--SCE) is a multistage separation process, which enables isolation and purification of components with very similar properties. But, CC-SCE is far behind the development of supercritical CO2 extraction technology. This paper introduced CC-SCE’s process and its application in concentrating paprika pigment in terms of industrial scale. The prospect of CC-SCE was also made in other applications, like purification of ginger oil, tocopherol and citrus oil etc.Key words: supercritical CO2; countercurrent extraction; natural material.

Description

Continuous countercurrent supercritical CO2 extraction (CC-SCE) is an effective way to achieve continuous operation of liquid materials. The countercurrent extraction process in the tower equipment is a differential contact extraction process, and the CO2 phase fills the entire column. Continuous phase, the raw materials are distributed in the continuous phase in the form of droplets, which is a dispersed phase. The CO2 phase is added from the bottom of the tower and led out from the top of the tower; the raw materials enter from the top of the tower or the side of the tower, and the raffinate is collected from the bottom of the tower. At the same time, in the presence of a temperature gradient, the solute can form an internal reflux, like distillation. After multi-stage equilibrium of dissolution-precipitation-dissolution, the solute comes out of the column with CO2 into the separator and is collected separately. Feeding and discharging are realized by high-pressure pump and valve automatic control. Due to the continuous operation of the extraction process, the equipment processing capacity is greatly increased, the process energy and gas consumption are reduced, and the production cost is reduced. In addition, the materials and supercritical CO2 pass through the packing in the tower. Or the plate is used for mass transfer, and the number of theoretical plates is high, which can achieve effective separation and purification of the mixed solution with small separation factor and difficult to separate.

Shi Bingjie used methylated soybean oil deodorized distillate as raw material, studied the process route of CC-SCE concentration of natural vitamin E, and discussed the effects of temperature, pressure, filler height and other factors on the extraction process. When the raw material feed rate is 0.02 kg / h, the extraction pressure is 20 MPa, the extraction temperature gradient is 40-45-50-60-70 ℃, and the gas-liquid ratio is 80 kg / kg under the experimental conditions, the mass fraction of vitamin E And the yield reached 24.3% and 81.5%, respectively. When using double-column continuous countercurrent operation, the natural vitamin E mass fraction increased to about 54%, and the yield reached 95%.

  The color price of raw material for capsicum pigment is 24000. Under the CO2 flow rate of 30000M3 / h M2 and the pressure is 36MPa, the color value of capsicum pigment increases by more than 6 times, up to 150,000. Compared with the results of supercritical CO2 extraction, under the same volume of autoclave and processing capacity, the countercurrent treatment time is only half of the traditional processing time, and the color value concentration multiple of the countercurrent extraction product is much larger than that of the first-stage extraction. It can be seen that the countercurrent extraction process greatly improves the production efficiency of the equipment, reduces the production cost, and has high practical value.

Q uote

Tan Huijun, Liu Wenqi, Zhao Yaping

1School of Chemistry and Chemical Engineering, Shanghai Jiao Tong University, Shanghai 200240, P. R. China.

Study on supercritical fluid extraction of amygdaloside

Supercritical fluid technology has been widely used in food, medicine, spices and natural pigments. Supercritical CO2 fluid technology as a solvent has the advantages of no pollution, no solvent residue, no damage to the effective ingredients in bitter almond, targeted extraction, making the bitter almond saponins safer, more reliable and more valuable. Therefore, it can reduce costs, save time and bring greater economic benefits for enterprises.

Supercritical fluid extraction technology and its application in food industry

Summary:

Traditional extraction methods of natural products in the food industry generally have many shortcomings such as the heavy use of organic solvents in the production process, pollution of the environment, long processing time, complicated operating steps, low extraction rate, and low purity of the extract.Therefore, green and efficient supercritical Fluid extraction, especially supercritical CO2 extraction technology, has received widespread attention and application in the field of natural product extraction in recent years.

Supercritical co2 extraction Capsicum red pigment
Supercritical co2 extraction Capsicum red pigment

Supercritical fluid extraction technology has attracted extensive attention as a new and green extraction process. Compared with traditional extraction processes, it has better extraction and separation capabilities and does not cause pollution to the environment.

We will to mainly introduces the basic principle of supercritical fluid extraction, the important variables affecting the extraction process and how to optimize it. Focuses on the application of supercritical fluid extraction technology in the food industry, such as extracting active ingredients from plants, animals and agricultural by-products.

Solve the problems of organic solvent residues in the traditional extraction process, provide new methods for the preparation and extraction of samples in the test, provide new technical means for small and medium-sized industrial production, and provide theoretical basis and technical support for the development of new products.