A prototype of shipping container equipped with controlled atmosphere (CA) system (CA-prototype), was used for the simulation of the cold transport of table grapes (cv Italia). The CAprototype was realised by IFAC SPA, within the Research Project Continnova. It is equipped with a cooling system in order to work at a temperature between –20°C and +15°C. The CA management is realised through the control system and the connections with the remote application. The experimental simulation of the cold transport was realised putting 20 boxes of table grapes inside the CA-prototype (set at 20% O2 + 10% CO2 in nitrogen), other 20 in a refrigerated room using a SO2 pad inside each box, the remaining 20 in a cold room (Control) without SO2 pad for 12 days at 5°C. At the end of the simulated transport, for each postharvest solution, 10 table grapes boxes were analysed, while the remaining 10 were stored for 3 days at 20°C in air with the aim to simulate a shelf-life period. CA-prototype allows preserving table grapes visual quality, delaying browning and maintaining berry turgidity, extending the shelf-life until 12 days at 5°C. Finally, CA-prototype resulted a valid alternative to the commonly used SO2 pads, which are under constant revision because of its potential allergenic effects.
Fresh fruits and vegetables are perishable products and from the field to the table, during the postharvest supply chain, they might loss the organoleptic and nutritional characteristics that determine their quality to the consumer (Kader, 2002a). During the logistic chain, temperature management is the most effective tool for preserving the quality of fresh horticultural commodities (Kader, 2002a). Additional postharvest life may be achieved through modification of the atmosphere surrounding the product: modified (MA) and controlled atmospheres (CA) usually involve a reduction of O2 and/or an increase in CO2 levels and can result in many benefits. In fact, it has been reported that a proper modification of the atmosphere, in combination with the appropriate temperature, can reduce the commodity’s respiration rate, mass loss and the sensitivity to ethylene. Moreover, MA or CA can delay ripening and softening, and could minimise the incidence of some physiological disorders and decay, thereby maintaining product freshness and quality longer than might otherwise be possible (Zagory and Kader, 1989; Kader, 2002b; Yahia, 2009; Amodio et al., 2018). The main difference between CA and MA storage is in the degree of control of the gaseous composition of the storage atmosphere. The CA implies a higher degree of control than MA in maintaining specific levels of O2, CO2, and other gases (Kader, 2002b). Currently CA is used for the storage of apples, kiwifruit, and pears and remain at experimental level on other horticultural commodities. The effectiveness of CA depends on cultivar, climacteric nature, storage temperature, selected concentration of gases, stage of maturity, commodity quality at harvest and pre-storage treatments. If the conditions are optimal for the chosen crop, senescence will be delayed by reducing respiration rate and substrate oxidation, delaying ripening of climacteric fruit and reducing the rate of ethylene production (Thomson, 2010). The effects of CA conditions on the physiology and quality of many table grape varieties have been evaluated (Crisosto et al., 2002; Artes-Hernandez et al., 2004). These Authors have shown that, in table grapes, the application of CA of high CO2 could retard senescence, reduce stem and berry respiration, limit rachis browning and decay and preserve berry firmness. In agreement, Cefola and Pace (2016) found good results in terms of preservation of sensory as well as nutritional quality using an atmosphere concentration 20% O2 plus 10% CO2 on organically-grown table grapes (cv. Italia).
Nowadays, CA technology is applied mainly for storage and less for transportation. Factors that limit its wider use are mainly due to the high costs associated with the preparation and management of the system, but also the lack of know-how and efficient technologies. Currently for the transport of fresh fruits and vegetable are used shipping containers, which are mainly based on the management of low temperature. Recently Maersk Container Industry (https://www.mcicontainers.com/products/star-cool/starcool- ca-plus) has developed a shipping container (Star Cool CA and CA+) equipped with a membrane system constructed of multilayered, high-tech polymer film, that allows the controlled removal of carbon dioxide while the auto-fresh air intake regulates oxygen level for the optimum atmosphere. The active CA technology proposed by Daikin’s is based on a zeolite active atmosphere separation technology. It reduces the O2 concentration inside container using N2 from air.
Another available technology is Purfresh’ CA technology, which works increasing CO2, decreasing O2, and adding ozone inside the refrigerated container environment. Starting from these considerations, the aim of this paper is: i) to describe a prototype of container equipped with CA system (CA-prototype); ii) to evaluate the performance of the CA-prototype during the simulated transport of table grape respect to the storage in cold room with or without SO2 pads.
Materials and methods
Storage facilities and experiments
Table grapes (Vitis vinifera L., cv Italia), 70 boxes of about 7 kg each one, were provided by a farm (Ermes snc, Noicattaro, Italy) at the maturity stage (total soluble solid content of 16° Brix, according to OIV, 2008) (Figure 1). Ten boxes were used for analysis at harvest, while the remaining 60 boxes were divided in three lots, each one representative of one postharvest solution applicable during the transport. In detail, 20 boxes were put inside a CA-prototype (set at 20% O2 + 10% CO2 in nitrogen, without SO2 pad), other 20 in a refrigerated room (EVERmed mod. LCRR 625 S, forced-air refrigeration, 700 L., RH 90%) using a SO2 pad (IMAL Ltda Los Canteros Santiago Chile) inside each box, the remaining 20 in a refrigerated room (EVERmed mod. LCRR 625 S, forcedair refrigeration, 700 L., RH 90%) without SO2 pad. The storage in presence of SO2 pads represents a common storage solution applied for table grapes (Melgarejo-Flores et al., 2013). All storage facilities were used to simulate a transport of 12 days at 5°C. At the end of the simulated transport, for each postharvest solution, 10 table grapes boxes were analysed, while the remaining 10 were stored for 3 days at 20°C in air with the aim to simulate a period of shelf-life. Table grapes were analysed in 10 replicates, at harvest, after the transport and at the end of the shelf-life period for the main quality traits.
Description of the controlled atmospheres-prototype
The prototype was realised by IFAC spa, within the Regional Research Project Continnova (Figure 2A and B). It is composed by isothermal sandwich panels manufactured by a well-known wet on wet method. Each isothermal sandwich panel had a size of 2×2×2 m (Figure 2C). A deep description of the materials used to assemble the prototype are reported in Table 1.
|Materials||Thickness||Mechanical characteristics||Thermal characteristics|
|CORAFOAM-HPT 40||76 mm||Compressive strength 350 (±50) kPa||Thermal conductivity 20 mW mk–1|
|Low density and very low||(density 40 kg m–3)||Tensile strength 580 (±60) kPa|
|thermal conductivity||Perpendicular strength 260 (±40) kPa|
|Glass fibre fabrics|
|Complex ROV/R3D/WR/ROV||3 mm||High integrity- good processing -|
|Polyester resins based on||(mass 1.5 kg m–2 )||good mechanical properties -|
|dicyclopentadiene, having||Distitron 100 CS||Excellent impregnations|
|styrene content lower than||DCPD - 28% styrene||Tensile strength 75 MPa|
|conventional resins||Resistance to bending 130 MPa|
|Tensile modulus 3400 MPa|
|Door dimensions||920×1840 mm||Density 1.2 g cm–3||–35°C+125°C|
|Door rubber in EPDM|
The CA-prototype load is possible by two front doors assembled and equipped with triple level of rubber specific to limit the gas losses during the transport and to guarantee a hermetical closing. Moreover, it is equipped with a cooling system (Thermoking V300 20) in order to work at a temperature between –20°C and +15°C. As for the CA management, the block diagram of the CA prototype with the control system and connections with the software to remote application for data and settings exchange is reported in Figure 3. In detail, the CA-prototype is equipped with the following components: i) CO2 and N2 gas cylinders, located below the CA-prototype; ii) CO2 preheating device, electrically powered from electronic control unit (ECU); iii) CO2 and N2 diffusers that allow controlled gas injection into CA-prototype; iv) controlled system for air introduction or extraction into or out from CA-prototype, atmosphere recirculation system, for homogenous gas mixing in the atmosphere; v) sensors set, respectively to monitoring pressure (P) (Jumo Midas 40.1001, 0-100 bar }0.5%), temperature (T) and relative humidity (RH) (Aecl AHT303-Vax-A, RH 0-100% }2%; T –20°C-85°C }0.3°C) and concentrations of CO2 (NDIR sensor, 0-100% }0.002%) and O2 (Alfa sense, O2-A2, 0-20.9% }0.6%) into the CA-prototype. These sensors are connected to the ECU. The management of CA inside the CA-prototype is operated by hardware and software components below reported.
Hardware components: i) ECU; ii) signal sensors and transducers; iii) input/output modules (Shj Electronic S5140 - S5134) connected to ECU; iv) geo-localisation device connected to ECU; v) GPRS/UMTS/HSDPA device for data transfer to ECU.
Software components: i) embedded Linux operative system; ii) software module to acquire and record data from input/output modules; iii) software application to set process values in CA-prototype; iv) software module to record process values in CA-prototype; v) software module to transfer data recorded from CA-prototype to the digital platform. Moreover, with the aim to describe the prototype operation modes, in Figure 4 a detailed flow chart is reported. To keep desired O2 and CO2 concentration values during transportation, process control system performs the following tasks: i) process control system cyclically measures the CO2 and O2 concentrations; ii) process control system compares measured values with CO2 and O2 settings; iii) process control system calculates control actions.
Regarding, the last point, ECU software compute control actions. O2 increments are obtained with air injection (opening shutters), while O2 reduction are obtained adding N2. On the other hand, CO2 increments are obtained with CO2 injection, despite its reduction is realised by air injection. The controller checks the O2 and CO2 concentration each hour, for 7 min, and restores the setpoint values. This allows maintaining almost constant at the setpoint values the O2 and CO2 percentage.
Visual quality (VQ), was evaluated using a hedonic scale from 5 to 1 (5=excellent; 4=good; 3=fair, limit of sensory acceptability; 2=poor; 1=very poor). Rachis browning (rB), was scored on a rating scale from 1 to 5 (1=absence, 2=light; 3=moderate; 4=severe; 5=extreme). For rB evaluation, panellists used the scale reported by Lichter et al. (2011) as reference.
Berry firmness was measured using a firmness tester (ZwickLine Z0.5; Zwick/Roell, Ulm, Germany) as the relative deformation of the berry fruits up to a 10 N load (deformation method), by using a plate of 100 mm of diameter, and was expressed in percentage respect to berry diameter (Cefola et al., 2011). Samples were weighed individually and mass loss was expressed as g per 100 g of fresh mass .
Colour parameters (L*, a* and b*) were measured, for each replicate, on 3 random points on peel surface of 10 berries using a colorimeter (CR-400, Konica Minolta, Osaka, Japan) in the reflectance mode and in the CIE L* a* b* colour scale. The colorimeter was calibrated with a standard reference having values of L*, a* and b* corresponding to 97.55, 1.32 and 1.41, respectively. In order to measure colour variations respect to fresh berries, at each sampling day ΔE was calculated using the following formula: ΔE = [(L0* – L*)2 + (a0* – a*)2 + (b0* – b*)2]1/2 (Martinez-Sanchez et al., 2011). The relative water content (RWC) of rachis was measured initially and during storage on rachis pieces of about one centimetre each one for a total of 4 (}0.3) g of rachis for each replicate (Rosales et al., 2013). The pieces were obtained cutting the rachis with a knife cutter. They were weighed fresh (Fw), after 24 h rehydration (Rw) in distilled water at ambient temperature and after drying (Dw) at 65°C in oven until constant mass. The RWC was calculated as percentage, using the following formula (Sanchez-Ballesta et al., 2006): RWC (%) = (Fw – Dw) / (Rw – Dw) × 100.
Data related to table grape were subjected to one-way ANOVA to evaluate significant difference (P≤0.05) between the two-storage condition (12 days at 5°C or 3 days at 20°C) and among fresh samples and that one stored in each postharvest solution (CA-prototype or SO2 pad or cold room) after the simulated transport (12 days at 5°C) and shelf-life (3 days at 20°C). Mean were separated applying the least significant difference test.
Results and discussion
Changes in O2, CO2, and temperature inside CA-prototype during the experiment are reported in Figure 5. It is possible to note as the CA-prototype is able to correct the gas composition maintaining the atmosphere composition at the set-up level. The effectiveness of CA for reefer containers is dependent the maintenance of the temperature and on commodity respiration rate and maturity level (Bessemans et al., 2016). Potential air leakage in a reefer especially through the doors and fitting plastics curtains inside the doors, can reduce the degree of control over the gases in CA containers (Thompson, 2010).
Table grapes showed a good visual quality after the simulated transport in the CA-prototype and after the relative period of shelflife; similar results were obtained by table grapes stored in the presence of SO2 pads (Figure 6 and 7A). Considering the score 3 as the marketability limit, it is possible to transport table grapes in the CA-prototype for 12 days, with a consequent shelf-life of 3 days at 20°C. Despite, table grapes samples cold stored (control) were scored at the marketability limit just at the end of the period of transport. Whereas, by using the SO2 pads the marketability is lost at the end of the shelf-life period (Figure 7A). These results on visual quality are in agreement with that one related to browning. Rachis browning was delayed by transport with CA-prototype, with positive effect also during the shelf-life (Figure 7B). As for the berry deformation and colour variation respect to fresh sample (ΔE), table grapes transported in the CA-prototype showed performance similar to SO2 pads; whereas a loss of turgidity and a browning was measured in table grapes stored only with the use of low temperature (Figure 7C and D). No significant differences among samples transported with the different system were detected for RWC (data not shown) and mass loss. The CA-prototype allows to preserve table grapes quality and to extend the shelf-life for the effect of atmosphere composition set (20% O2 + 10% CO2 in nitrogen) on the respiration rate delay as previously reported (Cefola and Pace, 2016; Cefola et al., 2018). Moreover, it resulted a valid alternative to the common use of SO2 pads, which is under constant revision because of its potential allergenic effects (Balic et al., 2012; Cefola et al., 2015).
Results demonstrated that it is possible to transport table grapes in CA-prototype for 12 days (20% O2 + 10% CO2 in nitrogen), time enough to reach new market. Moreover, after the transport period, table grapes can be marketable for 3 days at 20°C, with a positive effect of CO2 residual on the overall quality. Moreover, the CA-prototype presents a high flexibility for the possibility to set all needed combination of atmosphere composition (O2, CO2, N2) and temperature (from –20 to 15°C). The proposed system might be used to transport also other commodities, by setting the suitable atmosphere composition. Finally, the flexibility of the CA-prototype regards the possibility to use it as ripening chamber during transport, by improving it with ethylene sensors and gas cylinders.
Future researches are aimed to apply this system to other perishable commodities.
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