Procyanidins: Structural Properties, Production Methods, and Modern Applications
Abstract
1. Introduction
2. Structural Properties
- Molecules of procyanidins have several chiral centers, which dictate stereospecific binding and enzymatic recognition, affecting bioavailability and stability;
- Heterocyclic ring C of flavanol subunits can adopt different conformations (armchair, semi-chair, boat), altering molecular flexibility and solubility in aqueous environments;
- Ring B can occupy either an axial or an equatorial position relative to ring C, impacting intermolecular hydrogen bonding and self-association tendencies;
- Procyanidin types B and C can have several rotamer forms around interflavan bonds, influencing aggregate formation and precipitation behavior (Figure 3).

2.1. A-Type Procyanidins
2.2. B-Type Procyanidins
2.3. C-Type Procyanidins
2.4. Conformations and Properties Relationships
3. Synthesis and Extraction of Procyanidins
3.1. Synthetic Methods
3.2. Isolation from Natural Sources
3.2.1. Ultrasonic-Assisted Extraction
3.2.2. Microwave-Assisted Extraction
3.2.3. Carbon Dioxide Supercritical Extraction
3.2.4. Pressurized Liquid Extraction
3.2.5. Extraction with Deep Eutectic Solvents
3.2.6. Non-Extractable Procyanidins
3.3. Purification of Extracts Containing Procyanidins
3.4. Patents
3.5. Clinical Studies of Procyanidins
3.6. Metabolism and Bioavailability of Proanthocyanidins
4. Challenges and Future Outlook
- Development of effective methods for deep purification of multicomponent extracts and for isolating individual procyanidins from natural raw materials.
- Development of synthetic regioselective methods for obtaining procyanidins B5, B7 and B8 and other analogs not yet synthesized.
- Development and construction of predictive models that could work both in vitro and in vivo.
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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| Procyanidin Type | Conformation (C-F Rings) | Eq-Eq, % | Eq-Ax, % | Ax-Eq, % | Sum, % |
|---|---|---|---|---|---|
| B1 | compact (exp.) | 83.7 | 5.7 | 2.6 | 92.0 |
| compact (theor.) | 96.7 | 0.2 | 1.9 | 98.8 | |
| extended (exp.) | 7.3 | 0.5 | 0.2 | 8.0 | |
| extended (theor.) | 0.4 | 0.0 | 0.8 | 1.2 | |
| B2 | compact (exp.) | 53.4 | 0.0 | 1.6 | 55.0 |
| compact (theor.) | 96.2 | 0.3 | 1.6 | 98.1 | |
| extended (exp.) | 43.7 | 0.0 | 1.3 | 45.0 | |
| extended (theor.) | 0.95 | 0.05 | 0.9 | 1.9 | |
| B3 | compact (exp.) | 75.0 | 14.3 | 4.7 | 95.0 |
| compact (theor.) | 98.2 | 0.2 | 0.9 | 99.3 | |
| extended (exp.) | 4.0 | 0.8 | 0.2 | 5.0 | |
| extended (theor.) | 0.7 | 0.0 | 0.0 | 0.7 | |
| B4 | compact (exp.) | 70.0 | 9.0 | 4.0 | 83.0 |
| compact (theor.) | 96.5 | 1.1 | 0.6 | 98.2 | |
| extended (exp.) | 14.0 | 1.0 | 2.0 | 17.0 | |
| extended (theor.) | 1.7 | 0.1 | 0.0 | 1.8 |
| Procyanidin Type and Conformation | Surface Area, Å2 | ΔEwater, kcal/mol |
|---|---|---|
| A1 | 710.0 | 0.8 |
| A2 | 725.0 | 0.0 |
| B1 extended | 725.0 | 4.86 |
| B1 compact | 709.0 | 0.0 |
| B2 extended | 726.0 | 0.8 |
| B2 compact | 699.0 | 0.0 |
| B3 extended | 745.9 | 6.49 |
| B3 compact | 678.5 | 3.49 |
| B4 extended | 744.4 | 0.23 |
| B4 compact | 677.3 | 0.0 |
| B5 | 748.3 | 5.05 |
| B6 | 751.4 | 3.12 |
| B7 | 745.3 | 4.63 |
| B8 | 749.8 | 4.55 |
| C1 compact-compact | 979.0 | 1.38 |
| C1 compact-extended | - | 1.89 |
| C1 extended-compact | 1038.0 | 0.0 |
| C1 extended-extended | - | 1.9.0 |
| Procyanidin Type | Synthesis Type | Ref |
|---|---|---|
| A1, A2 | Radical or fermentative oxidation of B1 or B2 procyanidins | [115,116,129,130,131] |
| Intermolecular condensation of catechin blocks | [115,116,132,133] | |
| Synthesis using non-catechin precursors (diphenyl-propene derivatives) | [116] | |
| B1-B4 | Intermolecular condensation of catechin blocks (nucleophilic and electrophilic) in the presence of Lewis acids | [120,122,134,135,136] |
| Intramolecular condensation of a molecule with a glutar or amber bridge | [137] | |
| Orthogonal synthesis | [122] | |
| B5-B8 | Intermolecular condensation of catechin blocks (nucleophilic and electrophilic) in the presence of Lewis acids | [120,138] |
| Intramolecular condensation of a molecule with an azelaine bridge | [123] | |
| Orthogonal synthesis | [122] | |
| C1, C2 | Intermolecular condensation of B-type procyanidins and catechin blocks in the presence of Lewis acids with an excess of a nucleophilic agent | [119,139,140] |
| Orthogonal synthesis | [122] |
| Plant | Waste Type | Procyanidin Type | Concentration | Ref |
|---|---|---|---|---|
| Lychee (Litchi chinensis) | Leaves | A2 | 44.8–69.6 mg/g | [6] |
| Common grape vine (Vitis vinifera L.) | Pomace | Dimeric procyanidins | 1.0–3.0 mg/g | [153] |
| Total polymeric procyanidins | 27.0–43.3 mg/g | |||
| Saskatoon berry (Amelanchier alnifolia) | Peel and seeds | A-type dimers | 0.2–0.46 mg/g | [154] |
| B-type dimers | 0.026–0.06 mg/g | |||
| Polymeric procyanidins | 14.5–26.6 mg/g | |||
| Cacao (Theobroma cacao L.) | Husk | B1 | 0.55–0.83 mg/g | [13] |
| B2 | 0.23–0.90 mg/g | |||
| Nepali hog plum (Choerospondias axillaris) | Peel | Total procyanidins | 42.8–120.0 mg/g | [155] |
| Monterey pine (Pinus radiata) | Bark | Total procyanidins | 404.0 mg/g | [156] |
| Pitch pine (Pinus rigida) | 489.0 mg/g |
| Part of a Plant | Raw Material | Preliminary Preparation | Extraction | Purification | Ref. |
|---|---|---|---|---|---|
| Bark | Young shoots of hawthorn (Crataegus monogyna Jacq.) | Washed with 80% acetone; stored for 24 h at 18 °C; sonicated for 30 min at −20 °C | Water and chloroform (ratio not established) | 1. NaCl solutions; 2. Acetate water 0.5:5 (v/v) 3. Chloroform and hexane | [174] |
| Maritime pine (Pinus pinaster Ait.) | Grinding, screening through 60 and 18 mesh | CO2-ethanol (90:10), 3 times, 323 and 303 °C, 20.3 and 25.1 MPa, 370 and 360 min; 7.6, 13.2, and 19.1 kg/s × 105, solvent-to-solid mass ratio 28:1, 2:1, 20:1 | Hydrodistillation in a Schilcher apparatus, following the AOAC 962.17 method | [186] | |
| Flowers | Small-leaved linden (Tilia cordata Mill.) | Dry in the dark; fine grind | Acetone methanol water (3:1:1, v/v/v); exhaustive ultrasonic-assisted extraction 5 times for 30 min | Column chromatography using Sephadex LH-20; Column chromatography using Toyopearl HW-40F; Column chromatography using Diaion HP-20 | [170] |
| Fruits | Lychee pericarp (Litchi chinensis Sonn.) | Mix with chilled aqueous ethanol for 3 min and then homogenize in ice bath at 10,000 rpm for 5 min | Ultra-high-pressure extraction pressure 295 MPa, holding time under pressure 13 min, liquid to solid ratio 16:1, 70% ethanol, 25 °C | Information is not presented | [180] |
| Apples (Malus domestica) | (Not described) | Supercritical fluid, sublimation | HPLC followed by polyamide MN column | [11] | |
| Grape pericarp (Vitis vinifera L.) | Freezed in liquid nitrogen; grinded with a pestle in a mortar | Acetone/water (70 30, v/v) containing 0.05% (v/v) trifluoroacetic acid Stir for 1 h at room temperature in the dark | Column chromatography using Toyopearl TSK-HW 50F | [143] | |
| Grape pomace (V. vinifera L. cv. ‘Tempranillo’) | Frozen at 80 °C, freeze-dried under vacuum and milled | Pressurized hot water extraction 2 cycles; 10 min; 1500 psi. Choline chloride/oxalic acid (1:1, v/v) 30% mixture in water | Extracts were filtered through 0.20 μm polyester filters, then separated on an Ascentis Express C18 (HPLC) | [188] | |
| Avocado (Persea americana Mill.) | Washed; sublimated; grinded | Ultrasonic-assisted extraction three times with a solution of acetone/water (70:30, v/v) at 25 °C; add 0.1% ascorbic acid | Column chromatography using Sephadex LH-20 (50% MeOH/H2O and 70% Acetone/H2O) | [7] | |
| Seeds | Peanut peel (Arachis hypogaea cv. Runner 886) | Lyophilization | Acetone water (60:40), pH 1.5; 70 °C; 30 min | Amberlite XAD-2; Sephadex LH-20; TCX | [166] |
| Cacao beans (Theobroma cacao L.) | Washed; frozen; (liquid nitrogen); ground | Extracted three times with n-hexane (solid/liquid 1:5, w/v), 80% aqueous methanol (v/v) and 75% aqueous acetone (v/v), evaporated at 30 °C, extraction with an equal volume of chloroform three times | High performance counter current chromatography (HPCCC) | [14] | |
| Blackberry (Rubus spp.) | Pressed to obtain pulp, the pulp was roughly homogenized | Extracted by distilled water, methanol and ethanol (conventional solvents) or Natural deep eutectic solvents in a sonication water bath. An amount of 0.5 g was mixed with 10 mL of conventional or Natural deep eutectic solvents. The mixture was ultrasonicated at 25 °C for 20 min. Filtered through Whatman filter paper No.1 three times. | HPLC using Inertsil ODS-4 | [187] | |
| Iris lactea (Iris lactea Pall. var. Chinensis (Fisch.)) | Air dry; grinded to powder | Supercritical extraction with carbon dioxide; residue 80% ethanol (3 × 25 L, every 3 h) at 60 °C | Column chromatography using silicagel; HPCCC | [183] | |
| Grape seeds (Vitis vinifera L.) | The samples were processed to granulometry of 2 mm | ultrasound bath (Water ethanol (3:7 v/v), 34 kHz), vacuum rotary evaporation (35 °C), and wash by n-hexane, vacuum rotary evaporation. | A Sephadex LH-20 column rinse sequentially by ethanol/water 80:20 (v/v) and ethanol/water 50:50 (v/v), | [190] | |
| Black soy husk (Glycine max) | Stored at 10 °C before use | 70% acetone/0.5% acetic acid solution for 3 h at room temperature | Column chromatography using Sepabeads SP700; reverse phase preparative HPLC | [169] |
| Extraction Technic | Advantages | Disadvantages |
|---|---|---|
| Classical extraction | Easy Very low costs | Long time of extraction (hours) Low efficiency |
| UAE | Medium time of extraction (dozens of minutes) Low costs | Medium efficiency |
| MAE | Short time of extraction (minutes) High efficiency Low solvent consumption | High costs The impossibility of extracting heat-sensitive components |
| Supercritical CO2 | Maximal efficiency | Very high costs |
| PLE | High efficiency Low solvent consumption | High costs |
| DES assisted extraction | Short time of extraction (minutes) Low solvent consumption Great potential of combination with other technics | Questionable results |
| Source | NEPs Release Method | Main Compounds | References |
|---|---|---|---|
| Apple pomace | Sequence extraction combining acid and alkaline hydrolysis | The highest total phenolic content, reaching 12.38–13.76 mg GAE/g dry weight, with quercetin-3-O-galactoside identified as the predominant compound (by MS). | [229] |
| Sequential extraction facilitated by microwave | Flavan-3-ols constitute the major polyphenolic class (2.88 g/kg dry weight) with an average degree of polymerization of 4.7. Alkaline hydrolysis of apple procyanidins generates 3,4-dihydroxybenzoic acid (0.67 M/kg) and catechol (0.15 M/kg) as the principal degradation products. | [178] | |
| Grape pomace | Enzyme hydrolysis | Under optimized conditions the total phenolic content reaches 0.81 g GAE/100 g dry weight, with gallic acid (0.16 g/100 g dry weight) emerging as the main hydrolysis product. | [230] |
| Roselle by-products | Acid hydrolysis | The contents of hydrolysable polyphenols and proanthocyanidins are 6.18 mg GAE/g and 6.67 mg proanthocyanidin eq/g, respectively. Notably, NEPs account for 71.2% of the total phenolic content. | [69] |
| Brown rice bran | Alkaline hydrolysis | The total phenolic content reaches 276 mg GAE/100 g dry weight. Ferulic acid (1617 μg/g dry weight) and p-coumaric acid (394 μg/g dry weight) are the main compounds after hydrolysis. | [235] |
| NEPs Release Methods | Advantages | Disadvantages | Improvements |
|---|---|---|---|
| Acid hydrolysis | Cleavage of glycosidic bonds in the cell wall | Waste generation. High temperatures and acid concentrations | Milder conditions |
| Alkaline hydrolysis | Break ester bonds in the cell walls, releasing phenolic polysaccharide compounds | Waste generation. Complex pre-treatment process Inert gas atmosphere to prevent NEPs oxidation | Milder conditions |
| Enzymatic hydrolysis | Fast Low temperature Green technology | High cost Low specificity | Further studies about the methodology and recovery of enzymes |
| Additional extraction technologies | Break bonds with mechanical actions, increasing the solubility Increasing the efficiency of the extraction Reducing time Green technology | High cost Specific equipment | Further studies about the methodology |
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Zakharov, A.Y.; Berillo, D.; Ng, A.; Aidarkhanov, D.S.; Tukesheva, A.V.; Temirkulova, K.M.; Tanybayeva, A.; Mansurov, Z.A.; Balanay, M.P.; Pavlenko, V.V. Procyanidins: Structural Properties, Production Methods, and Modern Applications. Molecules 2026, 31, 223. https://doi.org/10.3390/molecules31020223
Zakharov AY, Berillo D, Ng A, Aidarkhanov DS, Tukesheva AV, Temirkulova KM, Tanybayeva A, Mansurov ZA, Balanay MP, Pavlenko VV. Procyanidins: Structural Properties, Production Methods, and Modern Applications. Molecules. 2026; 31(2):223. https://doi.org/10.3390/molecules31020223
Chicago/Turabian StyleZakharov, Aleksandr Yu., Dmitriy Berillo, Annie Ng, Damir S. Aidarkhanov, Anna V. Tukesheva, Kamila M. Temirkulova, Ainur Tanybayeva, Zulkhair A. Mansurov, Mannix P. Balanay, and Vladimir V. Pavlenko. 2026. "Procyanidins: Structural Properties, Production Methods, and Modern Applications" Molecules 31, no. 2: 223. https://doi.org/10.3390/molecules31020223
APA StyleZakharov, A. Y., Berillo, D., Ng, A., Aidarkhanov, D. S., Tukesheva, A. V., Temirkulova, K. M., Tanybayeva, A., Mansurov, Z. A., Balanay, M. P., & Pavlenko, V. V. (2026). Procyanidins: Structural Properties, Production Methods, and Modern Applications. Molecules, 31(2), 223. https://doi.org/10.3390/molecules31020223

