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ARTICLE ORIGINAL ORIGINAL PAPER

Drying performance of five Italian apricot cultivars

A. Piga1*, M. Poiana2, I. Pinna1, M. Agabbio1, A. Mincione2

RÉSUMÉ

Performance de séchage de cinq variétés d’abricots italiens

Le séchage d’abricots est réalisé presque exclusivement par énergie solaire.

Cette technologie peut entraîner différents problèmes au point de vue de la qualité et aussi en ce qui concerne l’aspect sanitaire du produit soumis à séchage. Pourtant, la plupart de ces problèmes peut être résolu par le biais d’un séchage contrôlé. Dans ce projet, cinq variétés d’abricots italiens ont été séchés en utilisant un four à air chaud et flux tangentiel.

Avant le séchage, les fruits ont été soumis à un prétraitement au SO2 pour prévenir le brunissement. Au début du procédé, les fruits ont été échan- tillonnés pour vérifier la perte de qualité du produit et pour mesurer la courbe de séchage. Les résultats montrent que l’utilisation des basses tem- pératures du procédé porte à des cinétiques de séchage plus lente même si les prétraitements réduisent le temps de dessiccation. En outre, les pré- traitements permettent de conserver la couleur des fruits pendant le pro- cédé, sans dépasser, dans la pulpe, les niveaux de SO2 légaux ; qu’ils permettent d’obtenir une excellente stabilité microbienne. L’analyse senso- rielle a donné de bons résultats même si une des variétés avait un goût légèrement acidulé.

Mots clés

abricot, activité d’eau, cinétique de séchage, qualité de fruit, sulfitation.

SUMMARY

Apricot drying is almost entirely carried out using solar energy. This technol- ogy poses concern about the quality and safety of the end product. Control- led drying may solve most of the problems encountered in sun drying.

Apricot fruits of five Italian cultivars underwent hot air drying in a tangential

1. Dipartimento di Scienze Ambientali Agrarie e Biotecnologie Agro-Alimentari, Università degli Studi, Viale Italia 39, 07100 Sassari, Italy.

2. Dipartimento di Biotecnologie per il Monitoraggio Agroalimentare ed Ambientale, Università degli Studi Mediterranea, Piazza San Francesco di Sales 4, 89061 Gallina, Reggio Calabria, Italy.

* Correspondence: [email protected]

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air-flow cabinet dryer. Sampling was done at the beginning and end of the process and at regular intervals throughout, to calculate drying curves and quality loss.

Results showed that mild drying temperatures led to slow drying kinetics, although pre-treatments reduced drying time to a certain extent. Pre-treat- ments resulted in good colour maintenance during the process, without tres- passing legal limits of SO2 in the pulp, and microbial stability was excellent.

Sensorial assessment was good, although one of the cultivars resulted in a slightly high acidic taste.

Key words

apricot, drying kinetic, fruit quality, sulfiting, water activity.

1 – INTRODUCTION

Air dehydration is one of the oldest methods by which foods have been pre- served, along with meat and fish salting. Canning, freezing and chilling are the main food stabilisation techniques used nowadays for fruits and vegetables, as dried items no longer satisfied changing consumer demands for convenience and functional foods. However, the increasing need for processing plants to have standardised raw materials and the traditional use of dried fruits has led to a renewed interest in dried products (BARBANTI et al., 1994). Among fruits, apri- cots are processed in some form on a basis of 40-45% of total world produc- tion (CRIVELLI, 1997). Drying is one of the technologies commonly used (BOLIN et al., 1981). Sun drying is the conventional method, requiring low capital, simple equipment and low energy input. In particular, this method is able to produce apricots of a rich orange colour, translucent appearance and very good gummi- ness (EL HALOUAT and LABUZA, 1987). Nonetheless, mechanical air dehydration has gained importance because it has many advantages over sun drying, such as the following (BARBOSA-CÁNOVAS and VEGA-MERCADO, 1996): a) the process is carried out under better sanitary conditions as a result of reduced contamina- tion by dust and other foreign matter; b) drying parameters can be accurately set, controlled and changed throughout the process, thus a more uniform prod- uct can be achieved with less quality degradation; c) dehydration is not condi- tioned by rain or weather changes; d) when the dehydration rate becomes constant, increasing the air flow results in shorter drying times; e) labour costs are lower. We also have to remember that Aspergillus spp. fungi contamination is dramatically increased by the contact of apricots with the soil, resulting in higher aflatoxin development. A number of research papers on air dehydration of the main apricot cultivars grown in the world have been published over the last thirty years (BOLIN and STAFFORD, 1974; SANSAVINI et al., 1976; EL HALOUAT

and LABUZA, 1987; SENHAJI et al., 1991; SHARMA et al., 1993), thus data are available on drying kinetics, quality loss and storage potential. On the other hand, few data can be found for the local fruit germplasm, almost completely under-utilised and under risk of extinction in several countries. The south of Italy, in this regard, has a certain number of local apricot cultivars (apart from

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traditional well known varieties such as “Cafona”), and up to now all those stud- ied have proved to be not well suited to drying.

In this paper, the air-drying performance of five local apricot cultivars (three from Apulia and two from Sardinia) is considered, as well as quality changes after processing.

2 – MATERIALS AND METHODS

2.1 Plant material

The Sardinian “Pibirinada bianca” and “Bisucciu” and the Apulian “Crisom- mola piccola”, “Crisommola rossa” and “Crisommola tardiva” were used for the experiment. Fruits were harvested between the end of June and the first decade of July at the proper stage of maturity and immediately transported to the labo- ratory, where only fruits with no or minimal peel defects were selected. Calibra- tion by weight was performed to have uniform fruit size, so that size would not affect dehydration times within a given cultivar. The cultivars were divided by size. According to the IBPGR-FAO (1984) descriptor list for apricot we have:

Very small fruits: 20g<weight<30 g: Crisommola piccola.

Small fruits: 30g <weight<40 g: Bisucciu, Pibirinada bianca and Crisommola tardiva.

Big fruits: 60g <weight<70 g: Crisommola Rossa.

Before drying, fruits had been pre-treated, in order to reduce enzymatic and non-enzymatic browning and speed up the drying process. Before pre-treating, fruits were cut in half along the suture line with a knife and the stone carefully removed by hand. Pre-treatments were:

1) Blanching in boiling water for 2 minutes, cooling to ambient temperature with tap water and dipping for 3 minutes in a 3% K2S2O5 solution (solu- tion to fruit rate was 7/1 by weight);

2) Dipping for 15 minutes in a 3% K2S2O5 solution (solution to fruit rate was 7/1 by weight);

3) Untreated control.

It was not possible to carry out treatment n.2 on “Crisommola piccola” and

“Crisommola rossa” as we did not have enough fruit material.

The apricots were then dried with paper and air-dried, after damaged fruits had been discarded.

2.2 Drying equipment and process parameters

Fruits were dried in a laboratory pilot dryer. The air drier was a tangential air- flow cabinet (a modified model of “Scirocco”, Società Italiana Essiccatoi, Milan, Italy), equipped with automatic temperature and air moisture control devices.

Air flows tangentially to the shelves carrying the fruits, while a particular air

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recycling system allows mixing exhaust air with fresh air and then reheating and redirecting to the product, in order to achieve the desired air moisture. The par- ticular construction of the drier allows a continuous airflow on the fruits, avoid- ing turbulence, and consequently it is particularly suited to calculate drying kinetics. Fruits were placed on steel shelves (product load from 7.5 to 10 kg/m2) using three shelves per treatment (the drier holds ten shelves). Fruits were removed when an estimated 15% water content (based on weight loss calcula- tions) was attained. Processing parameters were as follows:

– Air temperature at ambient conditions = 25˚C – Drying air temperature = 55˚C

– Relative humidity of air at entrance <40%

– Volumetric flow rate = 1840 m3/h

– Air recycling to keep relative humidity below 40%.

Dried fruits were packaged inside water barrier plastic bags (coextruded pol- yethylene/polypropylene, 95 µm of thickness) and stored at –18˚C until analysis.

2.3 Assessments and determinations

A sample of 50 fresh fruits of each cultivar was used to determine mean weight, pulp and stone mean weight, relative percentages, pulp to stone ratio and percentage yield of dried product. Fresh and dried fruits were inspected for water and dry matter content (%), water activity, pH value, total acidity, ascorbic acid and carotenoid content, residual SO2 and peel colour. Drying kinetics was calculated by plotting the water content revealed at regular intervals during processing versus process times, while drying rates were computed from water loss and process times. In particular, water content was determined in a vacuum oven for 12 h at 70˚C (AOAC, 1990). Water activity of fruit puree was assessed by an electronic hygrometer (model Aw-Win, Rotronic, equipped with a Karl-Fast probe), calibrated in the range 0.1-0.95 with solutions of LiCl of known activity.

The pH was determined after homogenisation of the flesh by a digital pH meter.

The acidity was determined (expressed as mg of malic acid per g of fresh or dried matter) by titration with 0.1N NaOH of homogenised fruit flesh to end point (pH 8.3). Ascorbic acid was determined by HPLC as follows: 10 g of pulp were mixed with 40 mL of 0.05N H3PO4 (pH 2.3) and centrifuged at 4000 rpm for 15 minutes. The supernatant was collected and made up to 50 mL with 0.05N H3PO4, then 3 mL were passed through a C18 Sep-Pak cartridge previously conditioned with 2 mL of acetonitrile and 5 mL of deionised water. The eluate was filtered through a disposable 0.45 µm filter and then subjected to HPLC analysis with an HP 1050 chromatograph (Palo Alto, California); chromato- graphic conditions were: RP-C18 column at ambient temperature, mobile phase 2% KH2PO4 at 0.4 mL/min, sample 20 µL. Detection was carried out at 260 nm and calibration was performed against an external standard. Results are expressed as mg/g of dry matter. Carotenoids were assessed with a spectro- photometer at 450 nm after extraction from fruit puree with a mixture of petrol ether and methanol (90/10 V/V) and subsequent drying with sodium sulphate.

Results are expressed as mg of β-carotene per kg of dry matter. Residual SO2 was also determined on dried fruits according to AOAC (1990). The peel colour was assessed with a tristimulus colorimeter (Chromameter-2 Reflectance, Minolta, Osaka, Japan), fitted with a CR-300 measuring head. Colour was

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expressed as L, a, b* Hunter scale parameters, and “a” and “b” were used to compute hue angle (tan-1 b*/a*) (LITTLE, 1975). To minimise fruit to fruit variabil- ity, during the process inspection of the colour was always recorded on the same ten fruits chosen at the start of the experiment. A informal panel of six untrained assessors evaluated rehydrated samples on a scale of 1 to 10, on the basis of degree of acceptability. Chemicophysical parameters and colour were subjected to one way analysis of variance (ANOVA) using the MSTAT-C soft- ware, considering as the group variable the processing time (fresh and dried), while means were separated, when required, by Multiple Duncan’s range test at P<0,01 level of significance.

3 – RESULTS AND DISCUSSION

Data regarding marketing quality and chemicophysical parameters are shown in tables 1 and 2, respectively. The cultivar “Crisommola piccola”

showed two unfavourable values, the mean weight and the pulp to stone ratio.

We took this cultivar into consideration because of its very low acidity, very similar to that of Turkish cultivars, like Hacihaliloglu (CRIVELLI, 1997). An acid content of more than 0.5% may lead to acid crystallisation and produce senso- rial problems in the final product, due to a too acidic taste. This cultivar showed a significantly higher yield of dried material and ascorbic acid content than the others. It must be pointed out that this cultivar had a very good resistance to handling even at full maturity, thus we were able to harvest and process the fruits when they had reached a lower and higher content of acids and dry mat- ter, respectively, compared with the other cultivars (table 2).

Table 1

Main properties of fruits of five Italian apricot cultivars.

Tableau 1

Principales propriétés des fruits de cinq cultivars italiens d’abricot.

Cultivar Property

Mean weight (g)

Pulp mean weight (g)

Stone mean weight (g)

Pulp (%)

Stone (%)

Ratio Pulp/stone

Yield of dried fruits

(%)

Bisucciu 30.15 27.96 2.25 92.5 67.5 12.33 16.3

Pibirinada bianca

38.86 35.34 3.52 90.9 69.1 69.99 18.5

Crisommola rossa

65.16 62.36 3.36 95.7 64.3 22.26 18.9

Crisommola tardiva

31.36 28.56 2.86 91.9 68.1 11.35 18.0

Crisommola piccola

21.36 18.86 2.56 88.3 11.7 67.54 24.2

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Table 2 Chemical-physical characteristics of fresh and dried fruits of five Italian apricot cultivars (fw = fresh weight, dm = dry matter). Tableau 2 Caractéristiques chimiques et physiques de fruits frais et séchés de cinq cultivars italiens d’abricot (fw = poids frais, dm = matière séchée). CultivarSampleDry matter (%)AwpHAcidity (mg malic ac. g fw-1 ) Acidity (mg malic ac. g dm-1 ) Ascorbic acid (mg g dm-1 )

Residual SO2 (mg kg dm-1) Bisucciufresh 14.67c*0.997a3.84a11.9c81.1a19.95a control, dried 75.15b0.699b4.04a45.1b60.0b43.92b sulfited92.24a0.571c3.88a58.7a63.6b42.84c261.85a blanched and sulfited91.51a0.595c3.86a59.6a65.1b43.01c210.25b Pibirinada biancafresh19.29c0.990a4.01b11.0d57.0a26.24a control, dried 77.71b0.725b4.48a19.5c25.1c43.79b sulfited89.80a0.596c4.47a28.0b31.2c43.05c309.95a blanched and sulfited93.25a0.582c3.92b47.7a51.1b43.03c213.10b Crisommola rossafresh17.31b0.990a3.91a45.6c32.3b21.12a control, dried 79.37a0.612b3.96a27.1b34.1b43.42b blanched and sulfited84.13a0.502c4.02a48.9a58.1a42.94c286.14 Crisommola tardivafresh16.49c0.985a3.51a49.1d55.1c25.24a control, dried 76.31b0.662b3.55a52.3b68.5b43.51b sulfited82.36a0.527c3.63a67.2a81.5a42.86c272.16a blanched and sulfited85.64a0.461d3.56a46.3c54.1c42.91c254.14a Crisommola piccolafresh22.17c0.982a4.46a42.9c13.1b28.12a control, dried 72.83b0.751b4.44a15.1b20.7a44.24b blanched and sulfited86.62a0.452c4.40a441.91a42.2043.52c194.65 * Data followed by different letters within each column and cultivar differ significantly at P<0.01 according to Duncan’s Multiple Range Test. * Les données marquées avec des lettres différentes dans la colonne et dans le cultivar diffèrent de façon significative pour P<0.01, en accord avec le Test Multiple Range de Duncan.

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3.1 Drying kinetics

Figures 1-5 show dehydration kinetics of the five cultivars, Crisommola pic- cola, Crisommola rossa, Pibirinada bianca, Bisucciu and Crisommola tardiva, respectively. In our experimental conditions, which we can define as mild, as the temperature was quite low compared to the normal processing conditions of other species (BARBANTI et al., 1995; MASTROCOLA et al., 1989), the time to reach the estimated water content ranged from 18 h for the “Crisommola pic- cola” fruits (Figure 5) to 32 h for the “Crisommola Rossa” cultivar (Figure 3), in accordance with fruit size. “Pibirinada bianca” was the exception (Figure 2). The

“Bisucciu” fruits (Figure 1) showed the highest drying rate (expressed as water loss per unit of time) (data not shown). The pre-treatments were beneficial in lowering drying times (figures 1-5). In fact, both sulfiting alone and blanching plus sulfiting, but mainly the latter, drastically reduced drying times.

Figure 1

Drying kinetics of “Bisucciu” apricot fruits as M (g H2O/g dry matter) versus drying time (hours). Data are the mean of three determinations

± standard deviation.

Cinétique de déshydratation de « Bisucciu » fruit d’abricot à M (gH2O/g matière séchée) contre le temps de déshydratation (heures).

Les données représentent la moyenne de trois déterminations

± la déviation standard.

0 1 2 3 4 5 6 7

0 5 10 15 20

Drying time (hours)

Control Sulfited Blanched and sulfited

M(gH2O/g dry matter)

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Figure 2

Drying kinetics of “Pibirinada bianca” apricot fruits as M (g H2O/g dry matter) versus drying time (hours). Data are the mean of three determinations ± standard deviation.

Cinétique de déshydratation de « Pibirinada bianca » fruit d’abricot à M (gH2O/g matière séchée) contre le temps de déshydratation (heures). Les données

représentent la moyenne de trois déterminations ± la déviation standard.

Figure 3

Drying kinetics of “Crisommola rossa” apricot fruits as M (g H2O/g dry matter) versus drying time (hours). Data are the mean of three determinations ± standard deviation.

Cinétique de déshydratation de « Crisommola rossa » fruit d’abricot à M (gH2O/g matière séchée) contre le temps de déshydratation (heures).

Les données représentent la moyenne de trois déterminations ± la déviation standard.

0 0,5 1 1,5 2 2,5 3 3,5 4 4,5 5

0 5 10 15 20

Drying time (hours)

Control Sulfited Blanched and sulfited

M (g H2O/g dry matter)

0 1 2 3 4 5 6

0 5 10 15 20 25 30 35

Drying time (hours)

Control Blanched and sulfited

M (g H2O/g dry matter)

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Figure 4

Drying kinetics of “Crisommola tardiva” apricot fruits as M (g H2O/g dry matter) versus drying time (hours). Data are the mean

of three determinations ± standard deviation.

Cinétique de déshydratation de « Crisommola tardiva » fruit d’abricot à M (gH2O/g matière séchée) contre le temps de déshydratation (heures).

Les données représentent la moyenne de trois déterminations ± la déviation standard.

Figure 5

Drying kinetics of “Crisommola piccola” apricot fruits as M (g H2O/g dry matter) versus drying time (hours). Data are the mean

of three determinations ± standard deviation.

Cinétique de déshydratation de « Crisommola piccola » fruit d’abricot à M (gH2O/g matière séchée) contre le temps de déshydratation (heures).

Les données représentent la moyenne de trois déterminations ± la déviation standard.

0 1 2 3 4 5

0 5 10 15 20

Drying time (hours)

Control Sulfited Blanched and sulfited

M (g H2O/g dry matter)

0 0,5 1 1,5 2 2,5 3 3,5 4

0 5 10 15

Drying time (hours)

Control Blanched and sulfited

M (g H2O/g dry matter)

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3.2 Chemicophysical and colorimetric changes

Tables 2 and 3 report changes in chemicophysical and colorimetric parame- ters of fruits after processing. Ascorbic acid and carotenoids underwent a signifi- cant decrease following drying. Loss of the two vitamins due to air-drying has been widely documented (DELLAMONICA and MCDOWELL, 1965; LUND, 1988; RYLEY

and KAJDA, 1993). The main degrading effect can be ascribed to oxidation (we used air to dry) and thermolability of the vitamins (mainly for ascorbic acid), but we cannot exclude the possibility that some ascorbic acid may act as a carbon- ylic substrate in the Maillard reaction (GREGORY, 1993). Ascorbic acid and β-caro- tene loss ranged from 51 to 89% and from 18 to 48%, respectively. Pre- treatments significantly increased ascorbic acid loss, compared with the untreated assays, in contrast to results indicating otherwise (BOLINAND STAFFORD, 1974), while no effect was observed on β-carotene. Regarding the other chemical parameters, a rise in pH and a decrease in dry matter acidity can be observed in fruits of Sardinian cultivars, with the exception of pH for “Bisucciu”. “Crisommola piccola” fruits showed a final acidity value comparable to that of Turkish dried apricots (MAHMUTOGLU et al., 1996). Aw values were always under the threshold of microbial growth in the pre-treated thesis, therefore we did not assess micro- bial load. As regards SO2 residues, all fruits treated with SO2 showed a residual content below Italian legal limits (600 mg/kg) after processing.

Colorimetric data of fresh and processed fruits are reported in table 3. Col- our was strongly influenced by drying. In particular, sulfiting and blanching plus sulfiting resulted in a significantly lower reduction in tonality, expressed as hue angle, with the exception of “Crisommola piccola”. If we look at the single “a”

and “b” factors, a more pronounced shift to a redder and deeper zone in the Hunter solid is evident in the control fruits, a clear sign of non-enzymatic browning (LITTLE, 1975; MASTROCOLAAND LERICI, 1991). Blanched and sulphited

“Crisommola rossa” fruits did not experience any change in the hue angle after processing. Both pre-treatments helped in reducing loss of lightness “L”, with the exception of “Crisommola piccola” cultivar. Our results appear better than those obtained by exposing fruits to SO2 gas (which had very high amounts of residual SO2) and then drying them with a solar dryer (MAHMUTOGLU et al., 1996).

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Table 3

Colour parameters of the peel of fresh and dried fruits of five Italian apricot cultivars.

Tableau 3

Paramètres des couleurs de la peau des fruits séchés et frais de cinq cultivars italiens d’abricot.

3.3 Sensorial analysis

Rehydration was needed to make the fruit edible. It was achieved by dipping fruits in boiling water for 3 to 5 minutes, which resulted in fruits having a 30 to 35% water content and a water activity value of 0.75-0.78. The panellists gave very high scores of acceptability at the end of the drying periods (data not shown), as they judged fruits to be excellent for flavour, consistency and chewi- ness. They did not perceive any taste resulting from the Maillard reaction (cook- ing flavour) and gumminess was at acceptable levels. Only “Bisucciu” fruits were judged slightly acid.

Cultivar Colour

Sample L a b Hue angle

(tan-1 b/a)

Bisucciu fresh 72.92a* – 2.36d 42.27a 93.20a

control, dried 34.34c 10.94a 21.54b 63.08d

sulfited 53.11b 47.69b 45.31a 80.36c

blanched and sulfited 52.92b 44.14c 44.67a 84.70b

Pibirinada bianca fresh 74.43a 4– 0.06d 56.84a 90.06a

control, dried 34.19d 414.28b 23.51c 58.73d

sulfited 41.67c 415.63a 30.94b 63.20c

blanched and sulfited 60.11b 445.02c 58.48a 85.10b

Crisommola rossa fresh 56.78a 425.08a 38.30a 56.78a

control, dried 28.57c 415.76c 12.52c 38.46b

blanched and sulfited 41.64b 419.87b 27.58b 56.62a

Crisommola tardiva fresh 61.82a 44.64c 49.72a 84.66a

control, dried 35.87c 415.27b 21.14c 54.17c

sulfited 40.37b 415.43b 25.76b 59.07b

blanched and sulfited 40.17b 416.31a 27.08b 58.93b

* Data followed by different letters within each column and cultivar differ significantly at P<0.01 according to Duncan’s Multiple Range Test.

* Les données marquées avec des lettres différentes dans la colonne et dans le cultivar diffèrent de façon significative pour P<0.01, en accord avec le Test Multiple Range de Duncan.

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4 – CONCLUSION

Use of mild drying conditions resulted in slow drying kinetics for the five apricot cultivars. Pre-treatments gave faster drying kinetics and better col- our preservation, but with greater loss of ascorbic acid compared to the control fruits. Very good microbial stability was achieved only in pre-treated apricots. Very good dehydrated fruits from the sensorial point of view were obtained, especially with the low acid “Crisommola piccola”. Hot air dehy- dration allows complete control of process parameters and sanitary condi- tions. However, further studies should be carried out in order to ensure that the quality of the product, especially with regard to colour changes, is main- tained when drying times are reduced.

5 – ACKNOWLEDGEMENTS

Research supported by EE.CC. (FEOGA), Multi Regional Operative Program (POM) “Attività di sostegno ai servizi di sviluppo per l'agricoltura” finanziato dalla Comunita’ Europea and by Italian Government Reg. (C.E.) 2052/88 modified by Reg. C.E. 2081/93 – Quadro Comunitario di Sostegno per le regioni italiane Obiettivo 1, 1994/99. [Dec. C/(95) 2040 -19.10.95], Misura 2

“Innovazioni tecnologiche e trasferimento dei risultati della ricerca”, title of project “Valorizzazione delle risorse frutticole locali mediante tecniche di essiccazione delicate”.

A special thanks to Mrs. Alessandra Nieddu and Mr. Paolo Fenu and Mr. Luigi Conti for helpful technical collaboration.

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(eds.), Nutritional evaluation of Food Pro- cessing, 3rd ed., 319-354, Van Nostrand Reinhold, New York.

MAHMUTOGLU T., SAYGI Y.B., BORCAKLI M., ÖZAY G., 1996. Effects of pretreat- ment-drying method combinations on the drying rates, quality and storage

stability of apricots. Leb. Wiss. Techn., 29, 418-424.

MASTROCOLA D., SEVERINI C., BARBANTI D., PINNAVAIA G., 1989. Essiccamento in corrente d’aria della frutta: effetti di alcuni pretrattamenti. Ind. Alim., 28,1175-1179.

MASTROCOLA D., LERICI C.R., 1991. Colori- metric measurement of enzymatic and non-enzymatic browning in apple purees.

Ital. J. Food Sci., 2, 97-108.

RYLEY J., KAYDA P., 1993. Vitamins in ther- mal processing. Food Chem., 49,119-129.

SANSAVINI S., CRISTOFERI G., FILITI N., GALLIS A., GRANDI M., SARTI D., 1976.

Ricerche sull'attitudine alla trasformazione industriale delle albicocche (sciroppatura, essiccazione, surgelazione). In: Atti Incontro Frutticolo su Problemi e Prospet- tive della Coltura dell'Albicocco, Società Orticola Italiana, July 1975, 101-122, Imola.

SENHAJI F.A., BIMBENET J.J., HAKAM B., 1991. Data on apricot drying: kinetics and product quality. Sci. Alim., 11, 499-512.

SHARMA T.R., SEKHON K.S., SAINI S.P.S, 1993. Colour changes during drying of apricot. J. Food Sci. Techn. Mys., 30, 306-308.

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© Lavoisier – La photocopie non autorisée est un délit La revue SCIENCESDESALIMENTSpublie des arti-

cles originaux, des notes de recherche et des revues bibliographiques, en français et en anglais, dans les différents secteurs de la science et de la technologie des aliments.

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Les photos de dessins ou tracés ont un fond blanc.

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— article standard dans un périodique TAUREILLES C., ROBIN J.P., FLANZY C., 1992.

Grape (Vitis vinifera L.) malate dehydrogenase.

Partial purification and isoelectric heterogeneity.

Sci. Aliments,12, 649-663.

— ouvrage cité dans son ensemble

BENDER A.E., 1978. Food processing and nutri- tion. Academic Press, London.

— citation d'une partie d'ouvrage

GASTINEAU I., De MATHAN I., 1981. La prépa- ration industrielle de la protéine verte de luzerne.

In: COSTES C. (ed.), Protéines foliaires et ali- mentation, 159-182, Gauthier-Villars, Paris.

— thèse

CUQ J.L., 1981. Modifications chimiques d'acides aminés indispensables sous l'influence de traitements technologiques alimentaires. Thèse de Doctorat d'Etat, Université des Sciences et Techniques du Languedoc, Montpellier.

— Communication (publiée) d'un colloque ou d'un congrès

AUBERT S., 1990. Intérêt des mesures de couleur dans l'amélioration de la qualité des fruits. In: DUPONT J. (ed.), 9eColloque sur les recherches fruitières, Avignon, 4-6 décembre 1990, 239-246, CTIFL-INRA, Montfavet.

La mention de « communication personnelle » ou

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— Brevet

CARON J.P., ROUSSEL H., CUQ J.L., ALLIOTTE T., 1989. Procédés d'inactivation des enzymes de détérioration des aliments. Brevet français n° 8911010 du 19 août 1989.

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© Lavoisier – La photocopie non autorisée est un délit SCIENCESDESALIMENTSpublishes original papers,

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References

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"g/100 g" is incorrect. Mixtures are expressed in proportions (eg. 2:3:3) followed by the cor- responding indications of weight or volume (eg. w:w:v).

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A N INTERNATIONAL JOURNAL OF FOOD SCIENCE AND TECHNOLOGY

INSTRUCTIONS FOR AUTHORS

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References should be cited in the text as follows (DUPONT and DUVAL, 1954). When there are more than two authors, only the first author should be cited, followed by et al.At the end of the article, references should be listed by authors in alphabetical order and in date order for the same authors in the following form :

— Standard journal article

TAUREILLES C., ROBIN J.P., FLANZY C., 1992.

Grape (Vitis viniferaL.) malate dehydrogenase.

Partial purification and isoelectric heterogeneity.

Sci. Aliments,12, 649-663.

— Book

BENDER A.E., 1978.Food processing and nutri- tion.Academic Press, London.

— Chapter in a book

GASTINEAU I., De MATHAN I., 1981. La prépa- ration industrielle de la protéine verte de luzerne.

In: COSTE C. (ed.), Protéines foliaires et alimen- tation,159-182, Gauthier-Villars, Paris.

— Thesis

CUQ J.L., 1981. Modifications chimiques d'acides aminés indispensables sous l'influence de traitements technologiques alimentaires. Thèse de Doctorat d'Etat, Université des Sciences et Techniques du Languedoc, Montpellier.

— Paper published in conference procee- dings

AUBERT S., 1990. Intérêt des mesures de couleur dans l'amélioration de la qualité des fruits. In: DUPONT J. (ed.), 9eColloque sur les recherches fruitières,Avignon, 4-6 décembre 1989, 239-246, CTIFL-INRA, Montfavet.

Where necessary, indicate a source by (personal communication) or (unpublished date). When a refe- rence is taken from Abstracts, it should be indicated in parentheses after the title of the article (abstr.).

— Patent

CARON J.P., ROUSSEL H., CUQ J.L., ALLIOTTE T., 1989. Procédés d'inactivation des enzymes de détérioration des aliments. French patent n°

8911010 of 19 August 1989.

All listed references must correspond to references cited in the text and vice versa.

Manuscripts reviewed by the referees and the Editorial Board are returned to the authors. After correction in response to the referees' comments, papers (2 copies) should be returned to the Secretariat. For the parts of the article written in a language different from that of the author's, the journal reserves the right to make the finalcorrections that it deems necessary.

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