of Flavonoids and Carotenoids from Hypericum maculatum L. Olha - - PowerPoint PPT Presentation

of flavonoids and carotenoids from hypericum
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of Flavonoids and Carotenoids from Hypericum maculatum L. Olha - - PowerPoint PPT Presentation

Factors Affecting the Efficiency of Two-Phase Extraction of Flavonoids and Carotenoids from Hypericum maculatum L. Olha Protunkevych * , Kostiantyn Prysiazhniuk Odessa National Polytechnic University , 1 Shevchenko avenue, 65044, Odessa,


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Factors Affecting the Efficiency of Two-Phase Extraction

  • f Flavonoids and Carotenoids from Hypericum

maculatum L.

Olha Protunkevych*, Kostiantyn Prysiazhniuk Odessa National Polytechnic University , 1 Shevchenko avenue, 65044, Odessa, Ukraine *Correspondence

  • .o.protunkevych@opu.ua

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Factors Affecting the Efficiency of Two-Phase Extraction of Flavonoids and Carotenoids from Hypericum maculatum L.

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Abstract: Current problem in pharmacy is the creation of complex drugs based on Hypericum maculatum L., which have anti-inflammatory, astringent, antispasmodic and tonic

  • effects. Hypericum herb contains a complex of biologically active substances of

different polarity: flavonoids, hypericin, tannins, vitamins, carotenoids. Biphasic extraction solvents system allows, by one cycle, to simultaneously obtain two extracts, alcohol and oil, containing a complex of hydrophilic and lipophilic

  • compounds. The dependence of the ratio of the polar and non-polar phases on the

biologically active substances extraction from the Hypericum herb was studied. The effectiveness of two-phase extraction was determined by the content of flavonoids in the water-alcohol phases and carotenoids in oil phases. It was determined that a two-phase solvent system extracts a complex of biologically active substances of Hypericum maculatum L. more effectively than a sequential extraction with separate solvents of different polarities. The polar phase enhances the processes of desorption, diffusion and phase transfer of not only hydrophilic, but also lipophilic Hypericum herb substances. The optimal ratio of raw materials: 70% ethanol: oil, which provided the maximum yield of flavonoids and carotenoids from raw materials, was 1:10:10. Keywords: two-phase extraction; Hypericum; flavonoids; carotenoids.

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One of the actual problems of modern pharmacy is the creation of complex drugs and dietary supplements based on Hypericum maculatum L., which have anti-inflammatory, astringent, antispasmodic, and tonic effects. A rational plant materials use requires the development of modern technologies of the extraction process, ensuring maximum yield of biologically active substances. The dependence of the ratio of the polar and non-polar phases on the biologically active substances extraction from the Hypericum herb was studied.

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Inroduction

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SLIDE 5

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Hypericum herb contains a complex of biologically active substances of different polarity: flavonoids: hyperoside, rutin, quercetin up to 7%; hypericin (up to 0.4%), pigments (anthocyanins), tannins (8-10%), water-soluble vitamins, choline, saponins, carotenoids (about 50 mg %), essential oil (up to 3%)

The chemical composition

  • f the herb Hypericum maculatum L.
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rutin quercetin β-carotin

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  • Biphasic extraction solvents

system

  • f

different polarities, such as a water- alcohol solution and vegetable oil.

  • This method allows, by one

cycle, to simultaneously

  • btain two extracts, alcohol

and

  • il,

containing a complex

  • f

various lipophilic hydrophilic and compounds.

vegetable oil

water-alcohol solution Hypericum herb

The principle of two-phase extraction from plant raw materials

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The dependence of the ratio of the polar and non-polar phases on the biologically active substances extraction from the Hypericum herb was studied

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Resuts and discussion

1 1 1 5 10 15 10 10 10 10 10

Raw material 70% ethanol

1 1

Oleum Helianthi

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SLIDE 9

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Single phase extraction

Single phase flavonoid extraction The ratio of raw materials: extract 1:10 (extractant - 70% ethanol). Raw materials were soaked in the extractant for 60 minutes, extracted for 30 minutes (t =100ºС). Extract was cooled and filtered under vacuum. Single phase oil extraction The ratio of raw materials: extract 1:10 extractant - Oleum Helianthi Extracted for 120 min (t = 100ºС). Еxtract was cooled and filtered under vacuum.

Resuts and discussion

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Raw material preparation Hypericum herb was crushed to particles 2-4 mm in size, then was soaked in 70% ethanol in accordance with specified ratios (1:10; 1:20, 1:30) for 60 minutes (t = 20ºС). Extraction An oil phase was added to the plant raw material. Then a two-phase extraction was performed for 120 minutes in the heating mode (t = 100 ° C) and stirring. The extract was cooled and the phases were separated and filtered under vacuum. Quantitative analysis of extracts The content of flavonoids (X,%, in terms of rutin) was determined in a water-alcohol extract, and the content of carotenoids (mg %) was determined in the oil extract.

Resuts and discussion

Stages of DF extraction from Hypericum

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Сontent of flavonoids in the water-alcohol phases (X%, in terms of rutin)

11 0,2 0,18 0,16 0,14 0,12 0,1 0,08 0,06 0,04 0,02 water-alcohol extract 1:05:10 1:10:10 1:10:15

ratio of raw materials: 70% ethanol: oil flavonoids (X%, in terms of rutin)

Resuts and discussion

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Сontent of carotenoids in oil phases (mg%)

12 0,6 0,5 0,4 0,3 0,2 0,1

  • il extract

1:05:10 1:10:10 1:10:15

ratio of raw materials: 70% ethanol: oil carotenoids in oil phases (mg%)

Resuts and discussion

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Conclusions

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  • Two-phase solvent system extracts a complex of biologically active substances
  • f Hypericum maculatum L. more effectively than a sequential extraction with

separate solvents of different polarities.

  • The polar phase enhances the processes of desorption, diffusion and phase

transfer of not only hydrophilic, but also lipophilic Hypericum herb substances.

  • The optimal ratio of raw materials: 70% ethanol: oil, which provided the

maximum yield of flavonoids and carotenoids from raw materials, was 1:10:10.

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SLIDE 14

Acknowledgments

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The authors are grateful to the staff

  • f the Organic and Pharmaceutical T

echnologies Department

  • f the Chemical T

echnology Faculty

  • f Odessa National Polytechnic University

.