Аннотация

Introduction. The fisheries industry generates large amounts of fish by-products. Their utilization is one of the relative tasks for fish manufacturers. Hydrolysate from fish by-products is regarded as a valuable bioactive protein source for feed production. In this study, we aimed to optimize hydrolysis conditions for the industrial by-products of catfish.
Study objects and methods. We studied the by-products of industrially processed Pangasius hypophthalmus fillet using biochemical methods to find the optimum hydrolysis conditions (enzyme type, enzyme/substrate ratio, temperature, water amount, and time). Then we built a regression model and verified it experimentally.
Results and discussion. According to the Box-Behnken design model, the optimum hydrolysis conditions were determined as 10% of water, 0.48% of SEB-Neutral PL enzyme, 57°C temperature, and 6 h duration. We found no significant differences between the modelled and the verified experimental values. The resulting hydrolysate was rich in nitrogen from amino acids, and its other parameters complied with the current national standards. The microbal and sensory attribites satisfied quality requirements as an animal feed supplement.
Conclusion. The study results are commercially applicable in feed production, providing a solution for the fisheries industry in byproduct treatment.

Ключевые слова

Fish, protein, hydrolysate, Pangasius hypophthalmus, catfish, by-products, enzyme

ВВЕДЕНИЕ

Tra catfish (Pangasius hypophthalmus L.) accounts for an essential part of Mekong Delta’s and Vietnamese fisheries’ yield. In 2019, their production area totaled 6600 ha yielding 1.42 million tons, of which 60–70% were by-products [1–3]. The production expansion in order to meet the domestic and export demand has caused a growing concern about the fisheries’ by-product treatment, especially from Pangasius processing. The Mekong Delta, where Pangasius production and processing are more developed, needs economical and environmentally friendly solutions for large amounts of by-products generated by the local manufacturing facilities [4]. Recent years have seen an interest in the utilization of Pangasius by-products to manufacture value-added products, such as fish powder, fish skin, and viscera.

Fish powder is the most popular by-product used as a primary protein supplement for animal feeds. Fish byproducts are a major source of lipids, native proteins, and hydrolysates, accounting for 10–20% of the total fish protein [5, 6]. Presently, most fish powder manufacturers use the traditional procedure with high pressure and temperature, resulting in products with a low digestive and absorptive index.

Enzymatic protein hydrolysis of fish by-products is currently a promising approach to making products with various applications and high nutritional values [5, 7–10]. Proteases are among common enzymes used in this process [6]. They hydrolyze protein in fish byproducts to smaller peptides that usually contain 2–20 amino acids. Fish hydrolysate is a liquid of amino acids – peptides produced by speeding up fish protein hydrolysis using proteases under controlled conditions. When applied in animal feed products, fish hydrolysate improves the digestion and absorption of proteins, as well as feed intake, efficiency, and protein utilization [11–14]. Furthermore, protein hydrolysate enhances the attractiveness and palatability of the feed, thus increasing its consumption [15].

There have been several studies in Vietnam on different aspects of enzymes for hydrolysis of catfish by-products. Nguyen Cong Ha et al. found that possible substrate concentrations for an optimal enzyme to substrate ratio were 108.4 g/L for neutrase, 36.2 g/L for papain, and 135.8 g/L for bromelain [16]. Nguyen Thi Thuy et al. investigated Pangasius by-product hydrolysis using commercialized papain as a protein source for animal feeds [17]. Dang Minh Hien et al. also studied papain for application in Bacillus subtilis cultivation with satisfactory results [18]. Phan Viet Nam et al. hydrolyzed catfish by-product using a combination of enzymatic hydrolysis and thermal treatment, having achieved over 30% hydrolysis, 80% nitrogen recovery, and a large amount of essential amino acids [3]. The researchers showed the potential of catfish by-product treatment with protease enzymes and possible application of hydrolysates in feed production. Therefore, an investigation of optimal hydrolysis conditions is essential for further commercial application.

This study assessed optimal conditions for Pangasius hydrolysis, such as the type of enzyme, enzyme/substrate ratio, temperature, time, and the amount of water added by analyzing total nitrogen and amino acids. As a result, we identified the initial conditions to produce hydrolysates from Pangasius by-products for the animal feed industry.

ОБЪЕКТЫ И МЕТОДЫ ИССЛЕДОВАНИЯ

Study objects. This study featured the by-products of industrially processed Pangasius catfish (Pangasius hypophthalmus) fillet.

Materials. Pangasius by-products, including heads, bones, and fins (Fig. 1), were collected from the processing factory of the Travel Investment and Seafood Development Corporation (Trisedco, Vietnam). They were minced into small pieces of 3–5 mm and stored at –20°C until use.

The enzymes were obtained from ICFood Vietnam, including bromelain (active pH 5.5–7.0, 55–60°C, 500 IU/g), papain (pH 4.5–8.5, 60–70°C, 500 IU/g), protease (pH 4.5–8.5, 50–60°C, 500 IU/g), and SEB-Neutral PL (pH 5.5–7.5, 35–60°C, 750 IU/g). They are commercial enzymes commonly used in animal feed production.

Optimal hydrolysis conditions. The materials were defrosted, mixed with 20% water, and heated to 55°C before adding enzymes. Hydrolysis was performed in a pilot-scale hydrolysis equipment with a capacity of 80 kg/batch. It was terminated by heating to 85–90°C in 10 min.

After hydrolysis reactions, the mixtures were filtered and analyzed for total nitrogen (N_aa). The optimal hydrolysis conditions were obtained by optimizing a single condition at a time in consecutive order. The resulting condition in the previous experiments was used as a constant condition in the later experiments. The protein recovery efficiency was evaluated using the ratio of nitrogen amino acid (N_aa) to total nitrogen (N_t) in the hydrolysates.

Evaluating the chemical composition of the materials. We analyzed such parameters as crude protein, moisture content, lipid, ash, TVB-N, and total aerobic microorganisms.

Choosing the enzyme. We assessed four enzymes, namely protease, bromelain, papain, and SEB-Neutral PL. Hydrolysis reactions were performed with the enzyme/substrate (E/S) ratio of 0.3%, temperature of 55°C, and 20% water added in 5 h. The hydrolyzed products were then analyzed for total protein and N_aa to choose the most effective enzyme. The chosen enzyme was used in the later experiments.

Choosing the optimal enzyme/substrate ratio. Seven enzyme/substrate ratios, namely 0.0, 0.1, 0.2, 0.3, 0.4, 0.5, and 0.6%, were analyzed during hydrolysis. The hydrolysis reactions were performed at a temperature of 55°C, with 20% of water added in 5 h. The chosen enzyme/substrate ratio was then used in the later experiments.

Choosing the optimal temperature. Five temperatures (45, 50, 55, 60, and 65°C) were assessed. The hydrolysis was performed with the optimal enzyme and enzyme/substrate ratio from the previous experiments and with 20% water added in 5 h.

Choosing the optimal amount of added water. Water in amounts of 0, 5, 10, 15, 20, 25, and 30% was used for hydrolysis under the optimal conditions chosen from the previous experiments in 5 h. The products were then analyzed to choose the optimal ratio of water required for hydrolysis.

Choosing the optimal hydrolysis time. Hydrolyses with the optimal conditions from the previous experiments were performed in five different periods, from 3 to 7 h. The products were then analyzed to choose the optimal reaction time.

Optimizing the hydrolysis procedure. A Box-Behnken design was used to investigate the effect of three factors: A – hydrolysis time, B – enzyme/substrate ratio, and C – temperature on the N_aa/N_t ratio [19]. An optimal scenario was obtained, and a verification experiment with the optimum conditions was performed in the lab.

Analysis methods. The following Vietnamese standards (abbreviated TCVN) were used to analyze the chemical quality parameters in this study: TCVN 3705:1990 for crude protein; TCVN 3708:1990 for amino acid nitrogen; TCVN 3700:1990 for water amount; TCVN 9215:2012 for vaporized acid-base; TCVN 3706:1990 for ammonia nitrogen; and TCVN 5165:1990/TCVN 4884:2005 for total aerobic microorganisms.

Data analysis. Each experiment was done in triplicate, each time with three samples, and the results were averaged. The data were processed and charted in MS Excel 2007 and model analysis was performed in Design Expert (version 10).

РЕЗУЛЬТАТЫ И ИХ ОБСУЖДЕНИЕ

Materials’ quality. The quality of the by-products used for hydrolysate production was evaluated through chemical and microbiological parameters, as shown in Table 1.

The materials’ crude protein and moisture contents were 12.76 and 59.27%, respectively, similar to other research in Vietnam [20]. TVB-N, a freshness quality indicator, was 13.45 mg/100 g, which was much better than the best quality limit of 25 mg/100 g. Although the total microorganism count was 1.13×10⁵, a large number relating to long storage before use, the TVB-N result indicated that the materials were still fresh and did not contain any spoilage compounds that could adversely affect the quality of hydrolysates [21].

Optimal hydrolysis conditions. Choosing the hydrolysis enzyme. The N_aa/N_t ratios obtained from the hydrolysis with four enzymes under study are shown in Fig. 2.

Under the same hydrolysis conditions, SEB-neutral PL resulted in the highest N_aa amount (36.12 ± 0.31%), equivalent to 1.4 times from bromelain hydrolysis and 1.3 times from protease or papain. The SEB-neutral PL enzyme was chosen to be used in the later experiments in this study.

Choosing the enzyme/substrate ratio. The effect of the enzyme/substrate ratios on the N_aa/N_t ratio is presented in Fig. 3.

The lowest N_aa/N_t ratio demonstrated the reaction without enzyme (14.96 ± 0.38%), and the highest was from 0.6% enzyme added (45.22 ± 0.32%), though the ratios of 0.4 and 0.5% were not much different from 0.6%. The enzyme/substrate range of 0.3–0.5% was chosen for further analysis, and the enzyme/substrate ratio of 0.4% was chosen for the later experiments.

Choosing the hydrolysis temperature. Figure 4 shows the effect of hydrolysis temperatures on N_aa/N_t ratios.

The results showed that the higher the temperature, the better the hydrolysis performance till it reached optimum at 55°C. The effective ratio went down as the temperature increased beyond that. Thus, 55°C was chosen for use in later experiments, and the range of 55–60°C was used in the optimal analysis.

Choosing the amount of added water. The amount of added water influences the enzyme’s dispersal and contact with substrates. As we can see in Fig. 5, hydrolysis performance increased steeply when the water amount went up from 0 to 10%. Then it slowed down considerably with water increasing from 10 onward to 30%, suggesting an equivalent efficiency. To economically use other substances in the hydrolysis reaction, we chose 10% added water to use in later experiments.

Choosing the hydrolysis time. The samples were hydrolyzed in 3, 4, 5, 6, and 7 h under the conditions from the previous experiments (0.4% SEB-neutral PL, 55°C, and 10% added water). The hydrolysis performance increased sharply from 34.44 ± 0.34% (3 h) to 43.90 ± 0.26% (5 h), then slowing down and reaching highest at 44.65 ± 0.30% (7 h). The difference between the samples hydrolyzed in 6 and 7 h was not statistically significant (P > 0.05). Although nitrogen solubility increases with time in enzyme hydrolysis, after a certain period, the formation of hydrolysis products and the reduction of peptide bonds during hydrolysis inhibit enzyme activities and decrease hydrolysis rate [22, 23]. Therefore, the effective range of duration was determined to be from 4 to 6 h.

Optimizing Pangasius by-product hydrolysis with Seb-Neutral PL enzyme. We studied the influence of different variables on the outcome of hydrolysis by performing Box-Behnken Designs in Design-Expert. In particular, we used the following factors: A – enzyme/substrate ratio (0.3–0.4–0.5%); B – temperature (50–55–60°C); and C – hydrolysis duration (4–5–6 h).

The ANOVA results are presented in Table 2.

The model was significant with the F-ratio of 155.85 (P < 0.0001) and the lack of fit of 3.72 (P = 0.2190). The variables AB, AC, BC, A², B², and C² all had P < 0.05 and therefore were significant and included in the regression formula. The model to determine the relationship between the dependent variable N_aa/N_t and enzyme/substrate ratio, temperature, and duration, as well as their interactions, was presented in the following formula:

y = a + b₁·A + b₂·B + b₃·C + b₁₂·AB + b₁₃·AC + b₂₃·BC + b₁²·A² + b₂²·B² + b₃²·C²

N_aa /N_ts ratio = 43.79 + 3.81·A + 1.74·B + 2.96·C + 1.10·AB + 1.17·AC – 1.08·BC – 4.00·A² – 5.52·B² – 1.85·C²    (1)

In formula (1), b₁, b₂, and b₃ were positive, showing that the hydrolysis performance (N_aa/N_t) was directly proportional to the analyzed factors: enzyme/substrate ratio, temperature, and duration. ǀb₁ǀ < ǀb₃ǀ < ǀb₂ǀ suggested that the enzyme/substrate ratio had a more substantial influence on the performance of the hydrolysis reaction than the other factors. The coefficients b₁², b₂², and b₃² were negative, suggesting that the graphs were parabolic faces with concave surfaces facing downwards and having extreme points. The coefficients b₁₂ and b₁₃ were positive, showing a positive interaction between temperature and time, with the enzyme/substrate ratio increasing hydrolysis performance. At the same time, b₂₃ was negative, indicating that the interaction between temperature and time was inversely proportional to the N_aa/N_t ratio. This could be explained by the nature of enzyme reactions, where high temperature and prolonged duration might cause unstable enzymes and reduce enzyme hydrolysis activities. The effects of these factors on the N_aa/N_t ratio were graphically presented in Fig. 7.

Based on the Box–Behnken design model, the optimum hydrolysis conditions (enzyme/substrate ratio = 0.48%, temperature = 56.52°C, and duration = 5.77 h) was chosen to conduct a laboratory experiment. The results of the laboratory experiment in comparison with the predicted values are shown in Table 3.

There were no significant differences between the predicted and experimental values. Therefore, we proposed the following optimum hydrolysis conditions for Pangasius by-products: 10% added water, 0.48% SEB-Neutral PL enzyme, 57°C, and 6 h.

Product quality. The results of the hydrolysate quality evaluation are presented in Table 4.

The resulting Pangasius hydrolysate was a highquality source of nutrition with 12.41 g/L nitrogen from amino acids, accounting for 46.08% of total nitrogen (26.94 g/L). Its other parameters fully complied with the current national standard QCVN 01-190:2020/BNNPTNT, making it suitable for use as a supplement to animal feed to improve its amino acid content and aroma.

ВЫВОДЫ

We investigated the initial hydrolysis conditions to produce hydrolysates from Pangasius hypophthalmus by-products. The regression model prediction and laboratory verification determined the following optimum hydrolysis conditions: 10% water amount, 0.48% SEB-Neutral PL enzyme, 57°C temperature, and 6 h hydrolysis time. The hydrolysates yielded from the proposed hydrolysis procedure satisfied the quality requirements for animal feed supplements and complied with the national standard QCVN 01-190: 2020/BNNPTNT. Thus, our study results were commercially applicable for feed production and provided a solution for by-product treatment in the fisheries.

Вклад авторов

B.T.T. Hien designed the study concept. P.T. Diem developed the methodology. L.A. Tung, T.T. Huong, and N.H. Hoang performed the validation experiment. N.H. Hoang and N.K. Bat conducted formal analysis. N.V. Nghia and B.T.T. Hien drafted, reviewed, and edited the manuscript. All the authors were involved in the investigation, as well as read and agreed to the final version of the manuscript.

КОНФЛИКТ ИНТЕРЕСОВ

The authors declare that there is no conflict of interest.

ФИНАНСИРОВАНИЕ

This research was funded by the Ministry of Science and Technology through the project “Improving technology and equipment for producing fishmeal and seasoning powder from Pangasius by-products” (Code DM.49.DN/20). The study was also part of the project “Improving the production technology of lysine-rich aquatic feed from Pangasius by-products” (Code SXTN. 05.19/CNSHCB) approved by the Ministry of Industry and Trade.

СПИСОК ЛИТЕРАТУРЫ

1. VASEP General information of Shark catfish aquaculture [Internet]. [cited 2021 Jun 10]. Accessed from: https://vasep.com.vn/san-pham-xuat-khau/ca-tra/tong-quan-nganh-ca-tra.
2. Nguyen TNH, Huynh TD. Research on increasing the extraction yield of gelatin from Pangasius hypophthalmus by ultrasonic. Journal of Science and Technology (JST-UD). 2019;17(7):15–18. (In Vietnamese).
3. Nam PV, Hoa NV, Anh TTL, Trung TS. Towards zero-waste recovery of bioactive compounds from catfish (Pangasius hypophthalmus) by-products using an enzymatic method. Waste and Biomass Valorization. 2019;11(8):4195–4206. https://doi.org/10.1007/s12649-019-00758-y.
4. Phan UN, Tran PN. Conditions for hydrolysing catfish by-product as food for tam hoang chicken by Bacillus subtilis. Dong Thap University Journal of Science. 2018;35(12–2018):99–105. (In Vietnamese).
5. Zamora-Sillero J, Gharsallaoui A, Prentice C. Peptides from fish by-product protein hydrolysates and its functional properties: an overview. Marine Biotechnology. 2018;20(2):118–130. https://doi.org/10.1007/s10126-018-9799-3.
6. Wang CH, Doan CT, Nguyen VB, Nguyen AD, Wang S-L. Reclamation of fishery processing waste: A mini-review. Molecules. 2019;24(12). https://doi.org/10.3390/molecules24122234.
7. Araujo J, Sica P, Costa C, Márquez MC. Enzymatic hydrolysis of fish waste as an alternative to produce high value-added products. Waste and Biomass Valorization. 2021;12(2):847–855. https://doi.org/10.1007/s12649-020-01029-x.
8. Gao R, Yu Q, Shen Y, Chu Q, Ghen C, Fen S, et al. Production, bioactive properties, and potential applications of fish protein hydrolysates: Developments and challenges. Trends in Food Science and Technology. 2021;110:687–699. https://doi.org/10.1016/j.tifs.2021.02.031.
9. Lapeña D, Vuoristo KS, Kosa G, Horn SJ, Eijsink VGH. Comparative assessment of enzymatic hydrolysis for valorization of different protein-rich industrial byproducts. Journal of Agricultural and Food Chemistry. 2018;66(37):9738–9749. https://doi.org/10.1021/acs.jafc.8b02444.
10. Wangkheirakpam MR, Mahanand SS, Majumdar RK, Sharma S, Hidangmayum DD, Netam S. Fish waste utilization with reference to fish protein hydrolysate – A review. Fishery Technology. 2019;56(3):169–178.
11. Khieokhajonkhet A, Surapon K. Effects of fish protein hydrolysate on the growth performance, feed and protein utilization of Nile tilapia (Oreochromis niloticus). International Journal of Agricultural Technology. 2020;16(3):641–654.
12. Olsen RL, Toppe J. Fish silage hydrolysates: Not only a feed nutrient, but also a useful feed additive. Trends in Food Science and Technology. 2017;66:93–97. https://doi.org/10.1016/j.tifs.2017.06.003.
13. Wei Y, Liang M, Xu H, Zheng K. Taurine alone or in combination with fish protein hydrolysate affects growth performance, taurine transport and metabolism in juvenile turbot (Scophthalmus maximus L.). Aquaculture Nutrition. 2018;25(2):396–405. https://doi.org/10.1111/anu.12865.
14. Wei Y, Liang M, Xu H. Fish protein hydrolysate affected amino acid absorption and related gene expressions of IGF-1/AKT pathways in turbot (Scophthalmus maximus). Aquaculture Nutrition. 2020;26(1):145–155. https://doi.org/10.1111/anu.12976.
15. Alves DRS, Oliveira SRD, Luczinski TG, Paulo IGP, Boscolo WR, Bittencourt F, et al. Palatability of protein hydrolysates from industrial byproducts for Nile tilapia juveniles. Animals. 2019;9(6). https://doi.org/10.3390/ani9060311.
16. Ha NC, Hien DM, Thuy NT, Nguyen LT, Devkota L. Enzymatic hydrolysis of catfish (Pangasius hypophthalmus) by-product: kinetic analysis of key process parameters and characteristics of the hydrolysates obtained. Journal of Aquatic Food Product Technology. 2017;26(9):1070–1082. https://doi.org/10.1080/10498850.2017.1376027.
17. Nguyen TT, Phan NT, Le NDD, Nguyen CH. Evaluating the performance of enzyme Papain in hydrolyzing protein from Catfish by-products (Pangasius hypophthalmus). Journal of Animal Science and Technology. 2015;53:77–87. (In Vietnamese).
18. Dang MH, Nguyen TD, Le NQ, Nguyen CH. Use of papain enzyme hydrolysis of Pangasius blood by-product using for Bacillus subtilis cultivation. Journal of Agricultural and Rural Development. 2020;9:49–56. (In Vietnamese).
19. Box GEP, Behnken DW. Some new three level designs for the study of quantitative variables. Technometrics. 1960;2(4):455–475. https://doi.org/10.2307/1266454.
20. Vo DLT, Nguyen THT, Phan VD, Nguyen DMH, Tran QH. Assessing the antioxidant properties of hydrolysates from catfish by-products using Alcalase® 2.4L FG and application as a natural antioxidant. Science and Technology Development Journal. 2016;K6:109–121. (In Vietnamese).
21. Hien BTT, Diem PT, Quyen VT, Nguyet BTM, Tung LA, Binh NT, et al. The variation of sensorial, physiochemical and microbiological quality index in Indian mackerel, Rastrelliger kanagurta in ice storage procedure. Bioscience Biotechnology Research Communications. 2020;13(2). https://doi.org/10.21786/bbrc/13.2/12.
22. Liaset B, Nortvedt R, Lied E, Espe, M. Studies on the nitrogen recovery in enzymic hydrolysis of Atlantic salmon (Salmo salar, L.) frames by ProtamexTM protease. Process Biochemistry. 2002;37(11):1263–1269. https://doi.org/10.1016/S0032-9592(02)00003-1.
23. Guerard F, Guimas L, Binet A. Production of tuna waste hydrolysates by a commercial neutral protease preparation. Journal of Molecular Catalysis B: Enzymatic. 2002;19(20):489–498. https://doi.org/10.1016/S1381-1177(02)00203-5.