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. 2015 Mar;53(1):48–56. doi: 10.17113/ftb.53.01.15.3663

Chemical, Physicochemical, Nutritional, Microbiological, Sensory and Rehydration Characteristics of Instant Whole Beans (Phaseolus vulgaris)

José Armando Ulloa 1,2,3,, Silvia Jazmin Ibarra-Zavala 2, Silvia Patricia Ramírez-Salas 2, Petra Rosas-Ulloa 1,2, José Carmen Ramírez-Ramírez 4, Blanca Estela Ulloa-Rangel 2
PMCID: PMC5068434  PMID: 27904331

Summary

Instant whole beans obtained by drying at 25 °C were evaluated for their chemical, physicochemical, nutritional, microbiological, sensory and rehydration characteristics. The proximal composition of instant whole beans was typical of this kind of food, whereas aw and L*, a* and b* values were 0.639, 98.55, –0.28 and –1.52, respectively. In instant whole beans, 75% of the essential amino acids had a value greater or equal to the reference standard for adult humans; the protein quality in terms of chemical score was 95%. Microbiological counts of aerobic mesophilic bacteria, moulds, yeasts and total coliforms of rehydrated instant whole beans were <10 CFU/g, whereas the scores for colour, flavour, texture and overall acceptability were 7.22, 7.68, 7.24 and 7.34, respectively, on a 1–9 hedonic scale. The logarithmic and Pilosof models showed close fits (R2>0.99) to the experimental data for drying of cooked beans and rehydration of instant whole beans, respectively. In the light of the chemical, physicochemical, nutritional, microbiological, sensory and rehydration characteristics of instant whole beans found in this study, drying at 25 °C is recommended for the production of such food.

Key words: instant whole beans, protein quality, sensory quality, rehydration

Introduction

Beans of Phaseolus vulgaris (common beans) are an important food crop both from the economic and nutritional points of view, and are cultivated and consumed worldwide (1). They are a rich source of proteins, complex carbohydrates, dietary fibres and minerals, but they also contain biologically active phytochemicals that are important for human health (2). Clinical studies have shown that regular consumption of beans helps to decrease colon cancer incidence and multiplicity, and it can prevent alterations in the gastrointestinal tract, cardiovascular disease and diabetes (3, 4).

The physiological effects of dry bean consumption may be due to the presence of abundant phytochemicals, including polyphenolics, which possess both anticarcinogenic and antioxidant properties (5). Compared to other carbohydrate sources, beans have a low glycemic index, so incorporation of this foodstuff into the diet may help control the blood glucose level in people with diabetes and other chronic degenerative diseases (6, 7).

Beans also contain several antinutritional factors such as inhibitors of trypsin, chymotrypsin, and amylase, as well as phytic acid, flatulence-producing oligosaccharides, saponins, and lectin, which interfere with the bioavailability of nutrients (8). However, the contents of all of these antinutritional factors can be reduced or eliminated by certain culinary practices such as discarding the soaking water before cooking or the use of a soaking solution of sodium bicarbonate or citric acid prior to cooking (8, 9).

The major obstacle in encouraging the use of dry beans is their tough seed coats and consequently the long cooking time needed to tenderize them. Thus, the development of value-added bean-based products as dehydrated precooked beans is now in high demand by the food industry, fast-food restaurants, and domestic consumers (10). Process conditions required for the production of dehydrated precooked beans of acceptable quality have been defined in previous studies. However, most methods are associated with problematic butterflying and splitting, which usually results in the loss of bean structure, flavour, texture and identity (11).

The high rate of drying of cooked beans causes seed coat splitting, which can be minimized by the use of low air velocity and low temperature during drying (11). Lowering the process temperature has great potential for improving the quality of dried products (12). Indeed, some studies have focused on the use of low drying air temperature and the impact it has on product quality (13).

Several changes of quality parameters occur during the drying process. The extent of changes depends both on the care taken in preparing the material before drying and on the process used. Major quality parameters associated with dried food products include sensory and rehydration properties, microbial load, retention of nutrients, and water activity amongst others (14). To our knowledge, there are no reports about the chemical, physicochemical, nutritional, microbiological, sensory and rehydration characteristics of instant whole beans produced by drying at room temperature. Therefore, the main aim of this research is to study the chemical, physicochemical, nutritional, microbiological, sensory and rehydration properties of instant whole beans (Phaseolus vulgaris) obtained by drying at room temperature.

Materials and Methods

Raw material

Bean (Phaseolus vulgaris L. var. Flor de Mayo) seeds harvested in November 2012 were purchased from the Mercado de Abastos, located at Tepic, Nayarit, Mexico. This bean variety is the second most commonly consumed in the West region of Mexico, and it is classified as medium size (between 25 and 40 g per 100 g of seeds). The chemicals were purchased from Sigma-Aldrich (Mexico, D.F., Mexico) and reagents and the amino acid standard from Waters (Mexico, D.F., Mexico). All chemicals used were of analytical grade and deionized water was used.

Cooking beans

Before cooking, the dry beans were sorted to remove broken, cracked, and damaged ones. Batches of 200 g were washed with tap water. Beans were blanched in tap water at bean per water ratio 1:4 and 95 °C for 3 min. After blanching, the beans were soaked in tap water at bean per water ratio 1:7 and 45 °C for 120 min, and then the hydrated beans were cooked in a pot at 97 °C for 120 min.

Drying method

The cooked beans were dried in a drying cabinet at room temperature (25 °C) under an air velocity of (180±1) m/min and relative humidity of (55±5) %. In this dryer, air was flowing horizontally through cooked beans. The velocity of the air passing through the system was measured using a CEM DT-618 thermo-anemometer (Shenzhen Everbest Machinery Industry, Co., Ltd, Nanshan, Shenzhen, PR China). For drying, 400 g of precooked beans were uniformly spread in a single layer on a rectangular tray formed by an aluminium frame (size: 40 cm ×30 cm) and a plastic mesh where the distance between wires was 1.3 mm. The samples of beans were removed from the dryer at 30-min intervals during the drying process, and their mass was recorded with a digital scale with 0.01 g accuracy (Ohaus Corporation, Parsippany, NJ, USA). Drying of the cooked beans continued until the decrease in mass was negligible, which was achieved at a final moisture content of (1.46±0.09) g of water per 100 g of dry matter. Three replicates of the drying experiment were carried out. The final moisture content was considered to be the value of equilibrium moisture content. Moisture ratio (MR) was calculated with the following equation:

graphic file with name FTB-53-048-e1.jpg

where X is the moisture content at any time (g of water per g of dry solid), Xe is the equilibrium moisture content (g of water per g of dry solid), and X0 is the initial moisture content (g of water per g of dry solid).

The experimental data obtained from drying study were fitted to the moisture ratio models detailed in Table 1 (15, 16), in order to determine the kinetic parameters of drying, and then define which one best describes drying behaviour.

Table 1. Mathematical models for fitting drying data (15, 16).

Model Model equation
Henderson and Pabis MR = a ·ek·t
Lewis MR = ek·t
Logarithmic MR = a ·ek·t+ c
Midelli et al. MR = a ·ek·t+ b ·t
Modified Henderson and Pabis MR = a ·ek·t+ b ·eg·t+ c ·eh·t
Modified Midelli et al. MR = ek·t+b ·t
Page MR = ek·tn
Two term MR = a ·ek1·t+ b ·ek2·t
Wang and Singh MR = 1+ a ·t + b ·t2

MR=moisture ratio; a, b, c, n=drying coefficients; k, k1, k2, g, h=drying constants, t=time

Chemical and physicochemical analyses

Moisture, fat, protein (N×6.25), ash, and total carbohydrate contents were determined in triplicate using standard methods reported by AOAC (17). Water activity (aw) was measured in triplicate at 25 °C by using a Decagon Aqualab meter CX-2 (Pullman, WA, USA), on coarse powder samples (3 g), which were obtained by grinding the precooked beans with a mortar and pestle. Prior to testing the samples, the water activity meter was turned on and allowed to warm up for 30 min and calibrated by filling half a plastic disposable cup with a saturated sodium chloride solution. The accuracy of water activity values was (±0.003). Colour was determined with a Minolta CR- -300 colour meter (Minolta, Tokyo, Japan). The measured values were expressed according to the CIELAB colour scale: L* (lightness), a* (redness–greenness), and b* (yellowness–blueness). The L*, a* and b* values of the white standard tile used as reference were 97.14, 0.19 and 1.84, respectively. The colour was measured directly on the surface of each bean in a sample of 10 precooked beans. Precooked whole beans were examined to establish if they had either a crack between the cotyledons or a transverse fissure in the seed coat >2 mm wide. The beans with split seed coats or cracked cotyledons in triplicate samples were counted. The results are reported as the percentage of split beans. Butterflied beans were defined as those with two cotyledons separated by more than half of the length of the bean (16).

Amino acid analyses and protein quality

The hydrolysis and quantification of amino acids were performed according to the methods reported by Erkan et al. (18), using a Waters high-performance liquid chromatographic system (Milford, MA, USA) consisting of a system controller, auto injector, liquid chromatographic pump, fluorescence detector, and degasser. The tryptophan content was determined according to AOAC method (17). The quality of protein was estimated by determination of total amino acids, as well as the fraction of the exogenous amino acids (EAA). Amino acids were expressed on a protein basis, equivalent to g per 16 g of protein. The chemical score (CS) was calculated as per the procedure described previously by Sujak et al. (19) based on the comparison of the mass fraction of the amino acid having the shortest supply, w(ai) (restrictive amino acid) with the mass fraction of this amino acid in the standard, w(as):

graphic file with name FTB-53-048-e2.jpg

We followed the recommendation of the FAO/WHO for choosing the amino acid standards (20). The recommended intake of exogenous amino acids for adult humans was as follows (in g per 16 g of N): lysine 5.5, methionine plus cysteine 3.5, threonine 4.0, isoleucine 4.0, tryptophan 1.0, valine 5.0, leucine 7.0, histidine 0, and phenylalanine plus tyrosine 6.0. The EAA were estimated according to Oser (21) in terms of geometric mean of mass fractions of participating exogenous amino acids, a1 to an, compared to a mass fraction of corresponding standard, a1s to ans (in g per 16 g of N):

graphic file with name FTB-53-048-e3.jpg

where n is the number of participating amino acids, and ns is the number of corresponding amino acids in the standard.

The essential amino acid index (EAAI) was calculated as follows:

graphic file with name FTB-53-048-e4.jpg

Protein efficiency ratio (PER) was estimated according to the Alsmeyer et al. (22) method using the following equation:

graphic file with name FTB-53-048-e5.jpg

where w(Leu) and w(Tyr) are mass fractions of leucine and tyrosine, respectively, expressed in g per 16 g of N.

Microbiological analysis

For microbiological analysis, 10 g of beans were homogenized with 90 mL of sterile buffered peptone water (0.1%) in a Stomacher® Lab Blender (model 400, Seward, Worthing, UK) for 2 min. Decimal dilutions were made in sterile peptone water (0.1%) and bacteria were plated in duplicate onto the specific media. Total aerobic bacterial counts were determined on plate count agar at 37 °C for 48 h, yeast and moulds on malt extract agar at 25 °C for 72 h, and total coliforms on violet red bile agar at 35 °C for 24 h (23). The counts were expressed as colony forming units (CFU) per gram. All the culture media used were from BD Difco (Becton, Dickinson and Co., Franklin Lakes, NJ, USA).

Sensory evaluation

Beans for the sensory analysis were prepared by adding 300 g of instant whole beans and 18 g of salt to 1.6 L of water at 95 °C, and maintaining this temperature for 15 min. A 50-member consumer panel, comprised mostly of students from the Autonomous University of Nayarit (Mexico) evaluated the reconstituted instant whole bean. A sample of 10 g of reconstituted instant whole beans was presented to each member of the consumer panel. The panellists were asked to evaluate the sensory quality in terms of colour, texture, flavour and overall acceptability on a 1–9 hedonic scale, where a score of 1 indicated dislike extremely, 2 dislike very much, 3 dislike moderately, 4 dislike slightly, 5 neither like nor dislike, 6 like slightly, 7 like moderately, 8 like very much, and 9 like extremely (24). All evaluations were conducted at room temperature (25 °C) on the same day. A score of 5 was considered the limit of acceptability for all sensory attributes tested.

Rehydration characteristics

Water absorption of dried precooked beans was determined according to a modification of the method described by Abu-Ghannam and McKenna (25). A sample of 30 beans (10 g, weighed exactly) was placed in a net basket and immersed into a 250-mL glass jar with lid containing 100 mL of distilled water, which was previously heated to the required soaking temperature (40, 60, or 80 °C) by placement in a water bath thermostatically controlled at the required temperature (±1 °C). Water absorption was recorded on a digital scale (Ohaus Corporation) by measuring the increase in bean mass every 3 min until the difference between consecutive mass measurements was insignificant ((0.05±0.01) g); this was considered to represent the saturation moisture content. There was no correction for lost solids. After the specified soaking time, the beans were removed from the soaking solution, drained on a kitchen strainer for 0.5 min, blotted with paper tissue, and weighed. The mass gain was measured, and the beans were returned to the soaking solution at the required temperature. All soaking tests were done in triplicate and a percentage of moisture in dry matter was recorded. The rehydration rate was calculated using the following equation:

graphic file with name FTB-53-048-e6.jpg

where ww is water gain (g of water per g of solid) at any time, mr is rehydrated sample mass (g) and md is initial mass of dry sample (g).

The experimental data were adjusted to the Pilosof’s model (16) which is calculated as follows:

graphic file with name FTB-53-048-e7.jpg

where ww is water gain (g of water per g of solid) at any time, wweq is water gain (g of water per g of solid) at equilibrium, t is time (min), and t1/2 is time needed to gain half of equilibrium value (wweq/2).

The rehydration rate was derived by differentiation equation with respect to time:

graphic file with name FTB-53-048-e8.jpg

to give a specific rate constant, kr:

graphic file with name FTB-53-048-e9.jpg

To illustrate the effects of soaking temperature on ww, the Arrhenius equation was applied. The Arrhenius law can be represented as follows:

graphic file with name FTB-53-048-e10.jpg

where kr is the constant of rehydration rate (min–1), k is pre-exponential factor having units equivalent to the rehydration constant, Ea is activation energy (kJ/mol), R is universal gas constant (0.8314 kJ/mol K), and T is temperature (°K).

Statistical analysis

Fitting procedure and the drying and rehydration constants were obtained using least squares analysis by Solver in Microsoft Excel 2010 (Microsoft Corporation Inc., New York, NY, USA) (26). The coefficient of determination (R2), reduced chi-square (χ2), and root mean square error (RMSE) were the three criteria of statistical analysis used to evaluate the adjustment of the experimental data from the drying and rehydration studies to the different models. Lower values of χ2 and RMSE, and higher value of R2 indicate better fitting (27). All experiments and analysis were conducted in triplicate, and data are expressed as the mean value±standard deviation (S.D.).

Results and Discussion

Drying of cooked beans

The initial moisture content of the cooked beans used in the dehydration experiment was (1.839±0.027) g of water per g of dry matter. Moisture ratio (MR) as a function of dehydration time is shown in Fig. 1. It decreased with time to an asymptotic value of 0 in 23 h. A drying study of cooked whole beans of the variety Canario at 25 °C under an air velocity of (180±1) m/min and relative humidity of (55±5) % showed a drying time of 25 h (28).

Fig. 1.

Fig. 1

Drying kinetics of cooked beans at room temperature (25 °C): circle=experimental data, line=logarithmic model; MR=moisture ratio

A close fit between the logarithmic semitheoretical model (Table 2) and the experimental data was obtained when the kd value of 1.84·10–3 min–1 (a=1.12960, c =–0.11122) was identified. This model showed the lowest values of χ2 and RMSE, as well as the highest value of R2 in comparison with the other tested models. The same model has been employed to describe the dehydration kinetic of apricots and sweet cherry (29), sweet pepper (30) and tomatoes (31). In recent years, microwave dehydration has gained popularity as an alternative dehydration method for a wide variety of food and agricultural products. Microwave treatment can greatly reduce the dehydration time of biological products without compromising their quality (32). Dehydration of cooked chickpeas and soya beans using a combination of microwave and air convection produced highly rehydratable products in short dehydration times (33). However, in the case of instant whole beans, a low dehydration rate is required to avoid or significantly reduce the incidence of splitting or butterflying, which was achieved with the dehydration conditions employed in this experiment.

Table 2. Curve fitting criteria for the mathematical models (15, 16) and parameters of cooked beans dried at room temperature.

Model name Model constant R2     χ2 RMSE
Henderson and Pabis a: 1.06141; k: 0.00241 0.99284 0.001095 0.032389
Lewis k: 0.00228 0.99053 0.001417 0.037242
Logarithmic a: 1.12960; k: 0.00184; c: –0.11122 0.99896 0.000161 0.012292
Midelli et al. a: 0.75583; k: –5.37·10–3; b: –0.00066 0.94655 0.008004 0.088513
Modified Henderson and Pabis a: 0.35380; k: 0.00241; b: 0.35380; g: 0.00241; c: 0.35380; h: 0.00241 0.99284 0.001202 0.032389
Modified Midelli et al. k: 0.00195; b=–6.98·10–5 0.99835 0.000251 0.015509
Page k: 0.00052; n: 1.23406 0.99828 0.000262 0.015860
Two term a: 0.53070; k1: 0.00241; b: 0.53070; k2: 0.00241 0.99284 0.001146 0.032389
Wang and Singh a: –0.00164; b: 6.81·10–7 0.99859 0.000215 0.014371

a, b, c, n=drying coefficients; k, k1, k2, g, h=drying constants

Chemical and physicochemical characteristics

Table 3 shows the proximal composition and some physicochemical characteristics of instant whole beans. Other studies have reported similar values for moisture, protein, and aw of ready-to-eat beans obtained by dehydration with air at 49–65 °C (11). The aw observed for instant whole beans is below limiting level of this parameter to ensure microbial stability, because it is generally accepted that no microbial growth will occur at aw<0.66 (34). With respect to colour, according to the L*, a* and b* values, the instant whole beans were coloured with slightly greenish and bluish hues, producing a light brown visual appearance, which is typical of cooked bean of light bean varieties. The most common factors that can affect the colour of foods during processing are pigment degradation, browning reactions, ascorbic acid oxidation, acidity, and the presence of copper and iron in the cooking medium (35). The decrease in redness and yellowness of legumes might be explained by the degradation of colour pigments during cooking, while the darkening process caused by the presence of metals during cooking might result in an increase in redness and yellowness (36). In this study, the decrease in yellowness of precooked bean could be due to the degradation of pigments during cooking.

Table 3. Proximal composition and physicochemical properties of instant whole beans.

Characteristics Value
w(moisture)/(g per 100 g) 12.8±0.4
w(ash)/(g per 100 g) 1.95±0.07
w(protein)/(g per100 g) 18.5±0.1
w(fat)/(g per 100 g) 3.2±0.1
w(total carbohydrates)/(g per 100 g) 63.6±0.2
aw 0.64±0.01
L* 98.6±0.3
a* –0.3±0.1
b* –1.5±0.3
Splitting/% 1.2±0.1

aw=water activity; values are means±standard deviation of triplicate analyses

Composition of amino acids and nutritive value

Table 4 shows the results of the amino acid profile and indicators of the nutritional value of instant whole beans. In the instant whole beans obtained in this study, 75% of the essential amino acids (lysine, threonine, isoleucine, valine, leucine, phenylalanine and tyrosine) had a value greater or equal to the reference standard for adults (20), while the tryptophan and sulphur-containing amino acids (methionine and cysteine) were the limiting amino acids, as it has been observed in other bean varieties and legume seed protein isolates (37, 38). In contrast, the protein quality of instant whole beans in terms of chemical score was 95%, in comparison with the values of 80–82% reported for other varieties of cooked beans (37, 39), while the essential amino acid index was 104.1%, indicating a high nutritive value of the protein but lower than the reported values of 112–115% for raw and processed French beans (40). The protein efficiency ratio of the instant whole beans calculated from the regression equation of Alsmeyer et al. (22) had a value of 2.3. According to AOAC (17), the protein efficiency ratio is the ratio of the mass gain and the protein consumed, where casein is the reference protein in the assay. Therefore, the protein efficiency ratio of casein from the Alsemeyer et al. (22) equation can be extrapolated to estimate the relative nutritive quality of another protein. According to Li et al. (41) the contents of leucine and tyrosine of casein were 8.82 and 5.06 g per 16 g of N, respectively. Therefore, the protein efficiency ratio of this protein extrapolated from the Alsmeyer et al. (22) equation is 3.0, and the relative protein efficiency ratio of instant whole beans to casein is 76.6%.

Table 4. Composition of amino acids and nutritive quality of instant whole beans.

Parameter Instant whole beans FAO/WHO reference for adults (20)
w(EAA)/(g per 16 g of N)
Lysine
Methionine+cystine
Cystine
Threonine
Isoleucine
Tryptophan
Valine
Leucine
Phenylalanine+tyrosine
Tyrosine
9.19
3.33
1.96
4.37
4.46
0.95
5.16
7.76
8.59
3.06
5.5
3.5
4.0
4.0
1.0
5.0
7.0
6.0
w(NEAA)/(g per 16 g of N)
Arginine
Aspartic acid
Serine
Glutamic acid
Proline
Glycine
Alanine
Histidine
7.66
11.10
5.26
13.16
3.64
3.72
3.74
3.48
Σ(EAA)/(g per 16 g of N) 43.81
Σ(EAA)/(g per 16 g of N) 51.76
CS
EAAI
PER
95.00
114.78
2.73

EAA=essential amino acids, NEAA=non-essential amino acids, CS=chemical score, EAAI=essential amino acid index, PER=protein efficiency ratio

Microbiological characteristics

Results of the microbiological counts of instant whole beans are shown in Table 5. Microbiological counts of moulds, yeasts and total coliforms of instant whole beans and the rehydrated product were undetectable under the conditions applied for sensory evaluation (95 °C for 15 min). In the case of aerobic mesophilic bacteria, the instant whole beans showed a count of 8.6·102 CFU/g, which was eliminated with the rehydration procedure. The acceptable microbiological quality of the dried food varies widely depending on the type of food and microbial group. In the case of dried food-grade gelatin, dehydrated space food, and processed spices, the limits of the aerobic mesophilic bacteria counts are 103, 104 and 106 CFU/g, respectively (42). In contrast, the safety limit for total coliforms in dehydrated egg products, dry milk powder, and dehydrated products (which require heating before consumption) are 103, 102 and 102 CFU/g, respectively (43). Therefore, instant whole beans from this study had better microbiological characteristics compared with the above-mentioned foods.

Table 5. Microbial counts (CFU/g) of instant whole beans and the rehydrated product.

Product Aerobic
mesophilic
bacteria
Moulds Yeast Total
coliforms
Instant whole beans 8.6·102±20 <10 <10 <10
Rehydrated instant
whole beans*
<10 <10 <10 <10

*at 95 °C in water for 15 min

Sensory quality

Considering ready-to-eat products that require rehydration, the importance of sensory quality comes into play (44). Characteristics such as seed size, colour, shape, textural properties and cooked-bean flavours greatly affect the consumers’ acceptance (45). The results of sensory evaluation of instant whole beans are presented in Fig. 2. The average scores for colour, flavour, texture, and overall acceptability were 7.22, 7.68, 7.24, and 7.34, respectively. None of the four evaluated attributes scored lower than 5, a score that is considered the limit of acceptability (46). Therefore, we conclude that instant whole beans are considered acceptable by consumers.

Fig. 2.

Fig. 2

Sensory scores of rehydrated instant whole beans

Rehydration of instant whole beans

A good fit was obtained when the experimental data were fitted to the Pilosof’s model (16, Eq. 7). As shown in Fig. 3, water absorption curves of instant whole beans exhibited an initial high rate of rehydration followed by progressively lower uptake rates at later stages. The rapid initial water uptake by legumes is attributed to the filling of capillaries on the surface of the seed coats and at the hilum (47). The decline in rehydration rates at later stages is related to the combined effects of increased extraction rates of soluble materials and lower water absorption, presumably because of the filling of free capillaries and intermicellar spaces with water (48). Subsequently, amounts of water absorbed with further soaking were minimal until equilibrium was attained, which signalled the maximum water capacity of instant whole beans, as has been observed for red kidney beans (25). Similar rehydration patterns for a variety of legumes had been reported previously (49, 50).

Fig. 3.

Fig. 3

Effect of temperature on rehydration of instant whole beans (circle, square, triangle=experimental data, line=Pilosof’s model (16)); dm= dry matter

The kr values of instant whole beans at different soaking temperatures obtained from Eq. 10, as well as the empirical rehydration equations related to the rate of moisture absorption are shown in Table 6. In general, increasing the soaking temperature resulted in an increase in both kr and in the equilibrium moisture content. Increasing the soaking temperature from 40 to 60 °C increased kr by 2.67-fold, but a further increase from 60 to 80 °C resulted only in 1.94-fold elevated kr.

Table 6. Rehydration characteristics of cooked beans dried at room temperature and then soaked at different temperatures.

t(soaking)
°C
kr
min
wweq
g per g of dm
Regression equation of
rehydration rate
χ2 RMSE R2
40 19.62·10–3±2.94·10–4 1.154±0.011 dwW/dt=50.96·w2–58.86·w+69.91 0.000876 0.028398 0.99309
60 5.24·10–2±6.80·10–4 1.300±0.013 dwW/dt=19.07·w2–51.30·w+32.23 0.000345 0.017730 0.99731
80 10.19·10–2±1.12·10–3 1.494±0.014 dwW/dt=9.80·w2–29.29·w+21.88 0.000173 0.012516 0.99877

kr=rehydration rate constant, wweq=equilibrium moisture content, χ2=reduced chi-square, RMSE=root mean square error, R2=coefficient of determination, dm=dry matter. Results for kr and wweq are expressed as mean values±standard deviations (N=3)

The rehydration characteristics of a dehydrated product can be used as a quality index. Such characteristics reflect the physical and chemical changes that occurred during dehydration, and these changes, in turn, are influenced by the composition of the samples, the conditions during drying, and by any pretreatment to which the products have been subjected (51). The amount and rate of absorbed water determine the sensorial properties and the preparation time required by the consumer. During rehydration, volume changes in biological materials are often proportional to the amount of absorbed water: the increase in volume because of water absorption equals the volume of imbibed water. Some research shows that the rehydration temperature markedly affects the increase in volume; moisture content (during processing time) increases with an increase in temperature, as was observed in the present study for instant whole bean. This trend has been observed for temperatures in the range of 40–80 °C for many fruits and vegetables (52).

The values of ln kr plotted vs. the reciprocal temperature values for instant whole beans are shown in Fig. 4. The high value of R2 confirmed that the water absorption rate of instant whole beans during soaking was temperature-dependent. The slope of the resulting straight line was used to calculate an Ea of 37.96 kJ/(mol·K), which is within the range of values reported for foods (27). According to the results of a study of hydration of red kidney beans, the Ea of blanched beans was 27.11 kJ/(mol·K) (25), which shows less sensitivity of the diffusivity against temperature than the instant whole beans in this study, because a greater value of Ea means higher sensibility of the diffusivity to temperature (27).

Fig. 4.

Fig. 4

Arrhenius plot of rehydration rate constant vs. reciprocal temperature (K) for instant whole beans

Conclusions

Drying at room temperature for obtaining instant whole beans generated a product of acceptable quality in the light of its chemical, physicochemical, nutritional, microbiological, sensory and rehydration characteristics. Because of the nutritional and health-promoting properties of dry beans, instant whole beans obtained by drying at room temperature could represent a good quality bean-based product for new market opportunities in the functional food and nutraceutical industry.

Acknowledgements

The authors wish to thank Promep-SEP-México for providing funds to support this research through grant 2649-UANCA-6.

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