Meena
Bisht
*a,
Margarida
Martins
a,
Ana C. R. V.
Dias
b,
Sónia P. M.
Ventura
*a and
João A. P.
Coutinho
a
aCICECO – Aveiro Institute of Materials, Department of Chemistry, University of Aveiro, 3810-193 Aveiro, Portugal. E-mail: meenabisht56@gmail.com; spventura@ua.pt
bCESAM – Centre for Environmental and Marine Studies, Department of Environment and Planning, University of Aveiro, 3810-193 Aveiro, Portugal
First published on 25th October 2021
Marine fish industries discard huge amounts of fish waste every year, which in turn impose problems of environmental pollution and loss of economic value. About 75% of the total weight of fish is discarded in the form of skins, bones, fins, heads, guts, and scales, which contain high levels of collagen type I. Generally, major sources for commercial collagens are the skin and bone of pigs and cows; however, these sources are chiefly associated with the risk of transference of zoonotic diseases or religious issues. Traditional protocols applied to the extraction of collagen are outdated, mainly with respect to present demands to develop more sustainable processes. This work explores the use of sustainable solvents, such as deep eutectic solvents (DES), to develop a more efficient, cost-effective and biocompatible process to extract collagen from waste from the fish industry waste. The extraction of collagen from the skin of Atlantic cod (Gadus morhua) using aqueous solutions of various eutectic solvents was studied, and after selection of the best solvent, an aqueous solution of urea (U) and lactic acid (LA) at a molar ratio of 1
:
2 (U
:
LA 1
:
2), the collagen extracted was properly characterized using SDS-PAGE, CD, FTIR, and XRD, and shown to be of type I. The results obtained here demonstrate an improvement in the yield and quality of the extracted collagen when eutectic mixtures were applied instead of acetic acid. After optimization of the process conditions, a maximum extraction yield of 6% was obtained for the aqueous solution of U
:
LA 1
:
2 at 0.75 M. The present work demonstrates the potential use of codfish skin waste and an aqueous solution of a DES to develop a more environmentally-friendly process to obtain high-quality collagen type I. It is an effort to convince industries to valorize their own residues under the guidelines of a circular economy.
6–8
Europe has dominated the collagen market with a share of 35.1% in 2019, which is attributed to multiple nutritional, skin, and health benefits of collagen and growing per capita healthcare spending in the region. In the specific case of collagen type I, the type most abundantly found in fish-derived materials, the principal applications are those related to the biomedical sector.5–7 Generally, major sources of commercial collagens are the skin and bone of pigs and cows (see Fig. S1†). However, these sources are chiefly associated with the risk of transference of zoonotic diseases or religious issues.8,9 Thus, there is a strong need to search for alternative sources of collagen, for which collagen from fish can be considered the best alternative.8,10 Codfish is thus a good example to consider. It is consumed daily in large quantities and in several countries, among which Portugal stands out. As a result, huge amounts of skin, scales, and bone residues are generated, in which the presence of collagen type I is significant. In recent years, collagen from Baltic cod (Gadus morhua), silvertip shark (Carcharhinus albimarginatus), deep-sea redfish (Sebastes mentella), striped catfish (Pangasianodon hypophthalmus), carp (Catla catla and Cirrhinus mrigala) and of Nile tilapia (Oreochromis niloticus) has been extracted and characterized.11–13 In the literature, the most common processes represent the use of acidic treatments or enzymatic hydrolysis. In spite of their capacity to recover collagen, there are some drawbacks, such as the complexity of some processes and the harsh operational conditions used13–16 that need further attention. As an example, the extraction of collagen performed by acids occurs traditionally at high temperatures, which does not help preserve its structural integrity, consequently inhibiting the capacity of the process to control the degradation rate.17 In recent years, deep eutectic solvents (DES) and eutectic mixtures have been reported for the dissolution and extraction of many bioactive compounds.18–25 DES are composed of at least a hydrogen bond acceptor (HBA) and a hydrogen bond donor (HBD) species, which upon mixing establish strong hydrogen bond interactions leading to the formation of eutectic mixtures, often becoming liquid at conditions close to room temperature.21 The use of eutectic mixtures, by the addition of water to DES for extraction purposes is a well-established procedure.22,23 It helps reduce the solvents’ viscosity, thus facilitating the mass transfer process. Moreover, the aqueous solutions exhibited higher dissolving rates and lower cost compared to neat DES.24 Indeed, after the work done by Triolo and co-workers26 and already adopted and accepted by other authors, water may be a component of the DES, being able to act as an HBD or an HBA. It is probably true that the hydrogen bonding network between the starting materials present in the neat DES is destroyed up to specific amounts of water, but a new hydrogen bonding network would be formed in which water participates with a positive impact on developing extraction processes. Therefore, the use of aqueous solutions of DES extracting collagen type I represents here a poorly explored but highly promising strategy25 to reduce the adverse environmental effects of the overall process, but mainly to improve the yield of extraction and purity level of the collagen. Nevertheless, and although the work of Bai et al.25 reports the use of DES to process a similar raw material – codfish skins – their objective is different, since they were focused on the extraction and purification of collagen peptides (a product of the thermal degradation of collagen). Furthermore, we also intend to use the DES as a way to have better control over the temperature of extraction (low temperatures will be preferred), to avoid the thermal degradation of collagen.17
Collagen type I was extracted from codfish skin waste using 0.5 M of acetic acid as the control solvent, with these results compared with those obtained with aqueous solutions of DES. DES containing betaine (Bet), urea (U), and cholinium chloride (CC) as hydrogen bond acceptors (HBA) and formic acid (FA), acetic acid (AA), propanoic acid (PA), and lactic acid (LA) as hydrogen bond donors (HBD) were applied (Fig. 1). The solid–liquid ratio, pH, and concentration of DES were the conditions investigated and further optimized. The molar ratio of DES used was 1
:
2, except for the cases of U
:
FA (1
:
4) and U
:
AA (1
:
5). The extracted collagen was characterized using Fourier Transform Infrared Spectroscopy (FTIR), Sodium Dodecyl Sulfate-Polyacrylamide Gel Electrophoresis (SDS-PAGE), X-Ray Diffraction (XRD), Circular Dichroism (CD), and Differential Scanning Calorimetric (DSC) studies and the process was developed by considering the best DES analysed regarding its life cycle assessment (LCA). The total impacts evaluated relating to the environmental categories of global warming, ozone formation, human health, terrestrial acidification, mineral and fossil resources scarcity were the issues determined.
:
10 (w/v) for 24 h, where the NaOH solution was changed after every 5–6 h. After that, the samples were washed with cold distilled water until a neutral pH was obtained. The deproteinized skins were defatted using a 10% (v/v) butyl alcohol solution with a solid to solvent ratio of 1
:
10 (w/v) for 48 h and the solvent was changed after every 6–7 h. Again, the samples were washed with cold distilled water. Then, the extractions were performed at 4 °C for 48 h using an optimized solid–liquid ratio of 1
:
10 (w/v) in 0.5 M of acetic acid or aqueous solutions of DES and using an orbital shaker. The resultant viscous solution was centrifuged to remove insoluble substances. The supernatants were salted-out by adding NaCl to a final concentration of 0.9 M, followed by precipitation of the collagen by the addition of NaCl (final concentration of 2.6 M) at neutral pH (0.05 M Tris-HCl, pH 7.5). The resultant precipitate was obtained by centrifugation at 15
000g for 1 h and dialyzed against deionized water at 4 °C for 72 h. Finally, the collagen was dried by lyophilization, and its yield was calculated using eqn (1):29![]() | (1) |
:
LA (1
:
2) and U
:
PA (1
:
2). The data on the inputs of each system are presented in Table S2† and the impacts of producing those inputs were taken from the ecoinvent database version 3.7.1.30 ReCiPe 2016 was the impact assessment method selected.31
:
U (1
:
2), which may be explained by the high pH value (pH 7) of this DES, which is far from the acidic media required for collagen extraction. Therefore, we have prepared DESs using three different types of HBA (CC, Bet, and U) and acid HBD (FA, AA, PA, and LA) at various molar ratios, whose pH values are given in Table S3 from ESI.† Among the studied DESs (Fig. 2), CC-based DESs were found to be the least effective at extracting collagen.
![]() | ||
| Fig. 2 Yield of extraction of collagen type I (%) and pH obtained by applying several aqueous solutions of DES in comparison with acetic acid (AA) at 0.5 M. All the extractions were done at 4 °C. | ||
Nevertheless, a remarkable improvement in the yield of extraction was recorded when collagen type I was recovered using U-based DES, particularly in the case of Bet
:
AA (1
:
2), Bet
:
PA (1
:
2), U
:
PA (1
:
2), and U
:
LA (1
:
2). The yields of extraction of collagen with Bet
:
AA (1
:
2), Bet
:
PA (1
:
2), U
:
PA (1
:
2), and U
:
LA (1
:
2) were, respectively, 4.3%, 4.4%, 5.0%, and 5.2% on the basis of lyophilized dry weight. Furthermore, the extraction efficiency of the individual starting materials was compared with the data obtained for the eutectic mixtures, U
:
LA (Fig. S3†). From the results, we conclude that the individual aqueous solutions, namely LA and U, are not that effective at extracting collagen type I compared to the eutectic mixtures selected as the best solvents.
O stretching, the amide II band is related to N–H bending vibrations, and the amide III band represents C–H stretching.31–36 The amide I band is associated with the secondary structure of the protein, and the amide III band confirmed the existence of a helical structure. The absorption ratio between the amide III and 1450 cm−1 bands was close to 1 for the control solvent, and for Bet
:
PA (1
:
2), U
:
LA (1
:
2) (Table S4 in ESI†), indicating the existence of a triple helix in the collagen extracted from codfish skin,28,29 since these findings are similar for codfish and other marine species.29,38–40 The similarities between commercial collagen and collagen extracted from codfish skin confirmed maintenance of the secondary and triple helical structures of collagen type I with aqueous solutions of DES.
In this analysis, two α-chains and one β-chain can be observed, which confirm the collagen extracted as being of type I. Some weak bands below 100 kDa were also observed when acetic acid was used as solvent, whereas no such bands were observed when the aqueous solutions of Bet
:
PA (1
:
2) and U
:
LA (1
:
2) were applied. These lower bands represent products of degradation of collagen type I promoted during the extraction process.43 These results show the advantages of using aqueous solutions of DES as solvents instead of the conventional aqueous solution of acetic acid given the high extraction yields and purity achieved while maintaining the structural stability of collagen type I. Taking into account the whole set of results (extraction yields, chemical stability, and purity), the aqueous solution of U
:
LA at 1
:
2 was selected as the best solvent to extract collagen type I from codfish skin waste.
:
LA (1
:
2)
:
LA (1
:
2) were further investigated by CD analysis. In the far UV region, the CD spectrum of collagen type I shows a positive maximum at 220–222 nm, representative of a triple helix, and a pronounced negative minimum at 196–200 nm defining the random coil structure.23,38 From Fig. 5, both the positive and negative bands appeared for commercial collagen type I. A similar result was found for collagen type I extracted by U
:
LA (1
:
2), where a positive band, characteristic of the triple helix, was observed at 222 nm. However, no positive band was found for collagen type I extracted by acetic acid, indicating that its triple helix was not preserved, due to the dissociation of intermolecular interactions29 occurring when the control solvent was applied. Contrary to what happened to collagen extracted by acetic acid, the CD results confirmed the maintenance of the triple helix of collagen type I extracted by U
:
LA (1
:
2), a result previously corroborated by FTIR. All the results allow us to conclude that the collagen type I extracted using U
:
LA (1
:
2) is not denatured.
![]() | ||
Fig. 5 Far-UV CD spectra of commercial collagen and collagen type I extracted from codfish skin using aqueous solutions of acetic acid and U : LA (1 : 2), obtained at 4 °C. | ||
:
LA (1
:
2)![]() | ||
Fig. 6 Thermal denaturation curve of collagen type I from codfish skins extracted using an aqueous solution of U : LA (1 : 2) at 222 nm; heating rate of 0.1 °C min−1. | ||
Moreover, the thermal stability of collagen type I extracted from codfish skin wastes using U
:
LA (1
:
2) was reconfirmed by differential scanning calorimetry (DSC) (Fig. S5 from ESI†), where the melting temperature was found to be 10.5 °C.
:
LA (1
:
2)
:
LA (1
:
2). Two diffraction peaks at diffraction angles (2θ) around 7.6° (representing the triple helix conformation) and 20° were identified, both characteristic of collagen.30,47 Moreover, the same conclusion is made considering the similarity between the XRD patterns obtained for the commercial collagen and collagen type I extracted using an aqueous solution of U
:
LA (1
:
2).
![]() | ||
Fig. 7 XRD spectra of commercial collagen type I, and collagen extracted from codfish skin using AA and U : LA (1 : 2) at room temperature. | ||
:
LA (1
:
2) on the extraction of collagen type I
:
LA (1
:
2) as the most efficient at extracting collagen type I from codfish skins without compromising its chemical structure and thermal properties, its concentration in water was optimized. An initial screening with U
:
LA (1
:
2) at different concentrations from 0.15 to 1 M was performed, with the results depicted in Fig. 8. An increase in the concentration of U
:
LA (1
:
2) leads to an increase in the collagen type I extraction yield from 3.4 to 6.0%.
![]() | ||
Fig. 8 pH and yield (%) of collagen type I obtained at various concentrations of U : LA (1 : 2) in water, for extractions done at 4 °C. | ||
However, a decrease in the yield of extraction above 0.75 M was observed, which may be a result of the more acidic pH created when the DES concentration is increased (pH values in Fig. 9 – blue line). The extracted collagen samples were again characterized by FTIR (Fig. 9A) and SDS-PAGE (Fig. 9B). For all concentrations, and at room temperature, the collagen samples exhibited amide A, amide B, amide I, amide II, and amide III, as expected.
![]() | ||
Fig. 9 Characterization of collagen extracted from the skin of codfish using U : LA (1 : 2) at different concentrations: (A) FTIR spectra; (B) SDS-PAGE. | ||
To confirm the purity of the extracted collagen, an SDS-PAGE was performed, where two clear bands attributed to α-chains and one β-chain were found (Fig. 9B), thus demonstrating the typical result obtained for collagen type I. All the results allow us to conclude that aqueous solutions of DES display much better performance in extracting pure collagen type I from codfish skins than the conventional approach using aqueous solutions of organic acids.
:
LA (1
:
2) and U
:
PA (1
:
2) reduces the environmental impacts by 13–16% in all categories other than mineral resource scarcity in which the impacts decrease by only 4 and 10%, respectively, compared with AA (conventional solvent). The higher impacts of the conventional system result mainly from the lower collagen yield obtained. The system based on U
:
LA (1
:
2) has a slightly higher collagen yield, which leads to lower impacts in the steps of codfish skin preparation and collagen extraction (Fig. S6†) compared with the system using U
:
PA (1
:
2). Consequently, the system based on U
:
LA (1
:
2) has impacts similar to those of the system based on U
:
PA (1
:
2), although about 7% higher in the mineral resource scarcity category. It is no surprise that the step of collagen extraction and purification has the largest share of impacts followed by codfish skin preparation and, finally, solubilisation of collagen, for all impact categories and systems (Fig. S6†). Most of the total impacts of the three systems derive from electricity consumption (51–77%) followed by butyl alcohol consumption (19–42%), with the exception being mineral resource scarcity. In this category, 32–37% of the impacts come from butyl alcohol consumption, 27–32% from electricity consumption, and 16–19% from deionized water consumption. The mix of electricity production technology in Portugal was considered in the calculations, which includes almost 55% of renewable sources. The impacts can be reduced by changing the electricity mix. For example, if 100% photovoltaic electricity was consumed, the carbon footprint would be reduced by 64–69%.
:
LA (1
:
2) was selected as the most efficient. The extraction yield, the purity, chemical structure, and thermal stability of collagen obtained with U
:
LA (1
:
2) from codfish skins were far superior to those obtained in the conventional process using an aqueous solution of AA. This work is expected to contribute to the development of sustainable downstream processes positioned at the interface between green technology and blue economy, following the guidelines of the sustainable utilization of the oceans under the scope of a circular economy approach.
Footnote |
| † Electronic supplementary information (ESI) available: Detailed data for the phase diagrams are presented. See DOI: 10.1039/d1gc01432c |
| This journal is © The Royal Society of Chemistry 2021 |