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Journal of Food Science and Technology logoLink to Journal of Food Science and Technology
. 2012 Jun 6;51(10):2560–2567. doi: 10.1007/s13197-012-0750-8

Heat penetration characteristics and physico-chemical properties of in-pouch processed dairy dessert (kheer)

Alok Jha 1,, A A Patel 2, T K Srinivasa Gopal 3, C N Ravishankar 3
PMCID: PMC4190199  PMID: 25328196

Abstract

Kheer, a traditional milk product of South East Asia, containing cooked rice grains in a creamy sweetened concentrated milk, has no large-scale production due to its poor shelf life. Shelf-life was improved by development of a process based on in-pouch thermal processing employing a rotary retort. Product development included optimization of rice-to-milk solids ratio (0.18–0.52) and total milk solids levels (16–26 %) to simulate the conventional product in taste, appearance and textural attributes. Various Fo values (12.4–14.8) were examined with regard to product quality. While the TBA value tended to increase (0.073–0.081) the reflectance value (35.3–43.4) declined with increasing Fo. The pH of the product (6.04–6.10) showed a slight tendency to increase with Fo. Sensorily, the product was found to be acceptable for a period of 150 days at 37 °C.

Keywords: In-pouch processed kheer, Rotary retort, TBA value, Fo value, Rice-to-milk solids ratio

Introduction

The manufacture of indigenous milk products is confined mainly to the non-industrial sector in India. It is reported that about 50 % of milk produced in the country is converted into numerous sweets and desserts, which are deep rooted in ancient traditions and have a strong cultural heritage. One such product is known as kheer. It is a semi-solid to fluid dairy product with partially disintegrated cooked rice grains dispersed in viscous liquid comprising of soluble starch from rice grains (Rangappa and Achaya 1974). Conventionally prepared kheer has a dark creamish colour as a result of prolonged cooking of rice grains in milk, which normally takes approximately one hour depending on the type of rice and the quantity of the product required to be made. Kheer is made by concentrating milk with simultaneous cooking of rice grains and addition of sugar during the process (De et al. 1976). Shelf life of kheer is very poor and even under refrigeration, it does not keep well for more than two days (Singh et al. 1987). In spite of its religious value, nutritional significance and commercial potential, manufacture of kheer remains confined to domestic kitchens. One of the reasons for the lack of its organized manufacture and marketing is poor shelf-life and lack of technology for large-scale manufacture. In the past, attempts have been made, though with only a limited success, to enhance the shelf-life of kheer by means of preservatives such as nisin and sodium metabisulphite (De et al. 1976; Singh et al. 1987; Eapen et al. 1988). Attempts have also been made to modify the conventional kheer making process in order to have a more uniform product (Srivatsa et al. 1993). Similar to kheer, a canned dairy dessert called ‘creamed rice’ with a shelf-life of 12 months has also been reported (Keogh 1970). A milk-wheat based dalia dessert processed in a rotary retort using tin-free steel cans with a shelf life of 72 days at 37 °C has also been reported by Jha et al. (2012). Among several methods of processing and preserving foods, thermal processing, especially use of retort pouches, has several advantages over tin cans. Consumption of canned foods is declining (Nair and Girija 1994; Dileep and Sudhakara 2007) due to high cost of tin for making cans acceptable to the market (Srivatsa et al. 1993). Retort pouch can be imprinted, its shape and size is flexible, and can be very well displayed on shelves. Food can be cooked faster in flexible pouches than in tin cans due to faster heat transfer rates. It also helps in reducing the cost of delivery and storage of food products (Dushyanthan 2002). Retortable pouches have been used in the past for several food products such as Kerala style fish curry (Gopal et al. 2001), seer fish curry (Shankar et al. 2002), tuna in oil (Ali et al. 2006), ready-to-eat pearlshot fish curry (Pandey et al. 2007) and prawn kurma (Mohan et al. 2008).

In view of the immense possibilities which the thermal processing using retortable pouches offers for newer food products with long-shelf life, present work was undertaken with the following objectives: to study the effect different Fo values on the shelf life of kheer as compared to just one to two days to promote its transportation and marketing and also to develop a proper package i.e. retort pouch for the product, which hitherto has been marketed without any packaging. This paper discusses the physico-chemical properties, heat penetration characteristics and sensory properties of in-pouch processed kheer as influenced by various formulation and processing parameters.

Materials and methods

Materials

Milk was obtained from the Ernakulam Co-operative Milk Producers’ Union Ltd., Kochi (India) and it contained 3.0 % fat and 8.5 % SNF. Rice used in the present investigation was obtained from Chaman Lal Rice Exporters Ltd., Karnal, India ensuring commercially pure variety of Basmati (3/4 brokens). Cane-sugar procured from the local market of Kochi (India) was used. BHA used as an anti-oxidant in long-life kheer was procured from the Sigma Chemical Co. (St-Louis, MO, USA).

Retort pouches

Retort pouches made of polyester/aluminium/polypropylene laminate for in-package processing of long-life kheer were obtained from M/s MH Packaging, Ahmedabad, India. These rectangular (12 cm × 15 cm) pouches had a thickness of 115.0 μ (15.0 μ polyester, 12.5 μ aluminium foil and 87.5 μ polypropylene).

Processing equipment

For experiments on process development for long-life kheer, the pilot-scale Millwall Model 24 Rotary Retorting System (John Fraser Co., UK) was used. The retort with a rotary square-cage was operated in the steam–air mixture mode for sterilization. It was set at 121.1 °C, with a steam pressure of 1.05 bar and an overpressure of 2.1 bar was maintained during each process cycle. The retort was used in rotary mode with cage rotation speed of 2 rpm.

Product formulation

Variables for product formulation included total milk solids (TMS) in pre-concentrated milk and rice-to-milk solids (RMS) ratio. Sugar was used at the rate of 12 % of milk. Three levels of TMS were used namely 16-17 % (low), 22–23 % (medium) and 25–26 % (high) for the rice-to-milk-solid ratio ranging from 0.18 to 0.52.

Production of long-life kheer

A detailed flow chart for the manufacture of in-pouch processed kheer is given in Fig. 1. As compared to this, conventional kheer was made in open steam kettles by slowly cooking rice grains in milk for around 1 h with the addition of sugar in the middle of the cooking process. In-pouch temperature and time profile was monitored during the complete sterilization cycle (Patashnik 1953). Fo values were provided by the computer using the Ellab software as discussed in detail separately.

Fig. 1.

Fig. 1

Schematic diagram for the manufacture of retort processed kheer

Chemical analysis of long-life kheer

Twelve lots of long-life kheer produced with process times corresponding to Fo values of 12.4, 13.2 and 14.6 (in quadruplicates) were stored at 37 °C and monitored for TBA value, reflectance and pH for a period of 5 months. The contents of a kheer pouch were subjected to vacuum filtration using plastic sieve (14 square holes per cm) held in a ceramic filtration funnel to separate the particulate rice mass or the solid fraction from the liquid phase. The rice (particulate) phase and the liquid phase were separately analyzed. Also kheer from another pouch was ground in a Sumeet mixer (SP-16 Electronic Model, India; wet grinding blade-speed code: Red) for 5 min. The colour of the liquid phase of stored kheer was measured in terms of reflectance value using a reflectometer with an exposure unit (search unit) (CL-28, Elico Pvt. Ltd., Hyderabad, India) fitted with a 450 nm filter. The instrument was standardized using a standard plate with a reflectance value of 50. The sample (tempered at 25 °C for 3 h) was transferred into a 200 ml dilution bottle leaving no headspace. It was placed under the search unit and reflectance value read out (in %) at 10 different places on the bottle and the average taken as reflectance value. The extent of oxidation of fat in the product was measured in terms of Thiobarbituric acid (TBA) value and using 90 g of ground kheer prepared as per the procedure given by Sidwell et al. (1955). TBA was expressed as optical density (OD) take at 530 nm. The pH was measured at 25 °C by a microprocessor controlled pH meter (Labindia Instruments Pvt. Ltd., Mumbai, India) fitted with an Orion gel-filled combined electrode.

Generation of heat penetration data

For every production trial, two of the pouches, transferred to the retort were fitted with thermocouples for measurement of the product temperature every 30 s during the process. A specially designed packing gland (Type GTK-21009-C000, ELLAB Co. Denmark) was used to enable the penetration of thermocouples into the retort pouch. Sets of thermocouple wires placed inside the pouch and the retort were linked to a precision data logging device (Model CTF 84, ELLAB Co., Denmark) which was capable of converting the temperature input data into corresponding process lethality values. These process lethality values were expressed as Fo values.

Construction of a heat penetration curve

Heat penetration data were plotted on a semi-logarithmic paper. While Fo value was obtained from the software used along with the data logger, the following formula was employed to calculate the sterilization time (U defined as the equivalent, in minutes at retort temperature, of all lethal heat received during the process) at 121.1 °C:

graphic file with name M1.gif 1

where

T

Set retort temperature (°C)

z

10 °C for Clostridium botulinum

The thermal process time (B) i.e. time in minutes, when no time is required to bring the retort to processing temperature, was calculated, as per the procedure suggested by Patashnik (1953):

graphic file with name M2.gif 2

where

B

process time to achieve final temperature deficit

g

final temperature deficit at the end of heating obtained from fh/U: g and Jc tables.

Total process time (B’) was calculated by adding to 58 % of the come-up time to B.

Sensory evaluation

Five lots of long-life kheer (TS: 32.5–34.0 % and RMS ratio: 0.36–0.40) stored at 37 °C were subjected to sensory evaluation for a period of 5 months. Sensory evaluation of long-life kheer was performed by a panel of 9 trained judges from the faculty of the Dairy Technology Division at National Dairy Research Institute, Karnal. A special laboratory with necessary facilities viz., separate booths, provisions for adequate diffused light and air-conditioned odour free environment was employed for product evaluation. Hedonic rating (9-point scale) was used for colour, texture, flavour and overall acceptability of the conventional as well as long-life kheer.

Statistical analysis

Data obtained from the various experiments during standardization process and storage studies of long-life kheer were subjected to analysis of variance (ANOVA) as described by Snedecor and Cochran (1994). All the experiments were conducted in triplicate.

Results and discussion

Physico-chemical properties of long-life kheer

Results of physico-chemical properties of long-life kheer and the influence of Fo values are presented in Table 1. pH of long-life kheer varied from 6.04 to 6.10. It appeared to increase with increasing Fo value (r = 0.90, P < 0.01). This lower than the normal pH (as compared to milk) may be attributed to the concentration of milk and the heat treatment given to the product in the retort. However, the increase in pH with the intensity of heat treatment was inexplicable. An interaction between the rice components and milk system could be one of the possible reasons. The TBA value of long-life kheer ranged from 0.073 to 0.081. It appeared to be directly related to the process lethality value (Fo). TBA value was higher in products that received a higher heat treatment. This could be because TBA is also a measure of the generation of TBA reactive products, which depends on extent of heat treatment. The reflectance value for the long-life kheer declined perceivably as the Fo value increased, the correlation (r = −0.97) being highly significant (P < 0.001). It ranged from 35.3 to 43.3 and was indicative of the fact that the degree of browning of the product increased as the retort process time increased. The colour of long-life kheer was considerably dark (‘definite browning’) in comparison to the colour of the conventional kheer (‘slight browning’). This difference could be attributed to the high process lethality values (Fo) for making long-life kheer.

Table 1.

Physico-chemical properties of long-life kheer made with different process lethality values

Fo pHa TBA valuea (OD at 530 nm) Reflectance valueb (at 450 nm)
12.4 6.05 0.073 43.3
12.5 6.04 0.075 43.2
12.6 6.06 0.075 43.2
12.8 6.04 0.075 42.5
12.9 6.05 0.076 42.3
13.0 6.07 0.074 41.3
13.2 6.07 0.075 40.8
13.4 6.08 0.078 40.9
13.5 6.08 0.079 40.7
13.7 6.08 0.079 39.4
14.5 6.09 0.080 36.4
14.6 6.09 0.076 38.0
14.8 6.10 0.081 35.3

a n = 3

bMeasured on the liquid phase of the products

Heat penetration characteristics of long-life kheer

Lag period for heating curve (jh)

Thermal process parameters of long-life kheer are presented in Table 2. The jh value given as pseudo-initial temperature deficit (PID) divided by the actual initial temperature deficit (ID) ranged from 0.44 to 1.17. The kheer mix comprising of rice and sugar, subjected to thermal processing could be considered as essentially a liquid product and the mode of heating could be said to be convective. For purely convective packs, there is little or no lag period (i.e. the come-up time is very short); hence, PID and ID coincide, so that jh is equal to 1.0 (Jones 1968). However, in actual practice, there is always some gap in time period before a product could reach the retort temperature, leading to differences in come up time depending on the composition, size etc. and hence, to variations in jh value. The variations observed in the present study, however, could not be related to the product’s composition in terms of TS or RMS ratio. Condensed cream of celery soup was reported to have a jh value of 1.3 (Berry and Bradshaw 1982). Products heated under agitation have large jh values, but it takes some for the viscous forces of the product to be overcome by the inertial forces induced by the rolling of the can (Berry and Bradshaw 1980). jh value for retort processed dalia dessert was reported to be in the range of 0.40 - 0.85 indicating a convective heating regime (Jha et al. 2012).

Table 2.

Thermal process parametersa of long-life kheer

Trial No. TS/RMS Parameters
jh fh jc B Fo Cg
1 41.8/0.21 1.17 2.82 2.31 15.66 12.4 76.2
2 36.2/0.28 0.45 5.65 1.40 20.05 13.2 84.1
3 33.8/0.32 0.90 6.40 1.06 21.52 14.6 90.5
4 29.2/0.18 0.47 3.55 1.31 16.19 13.0 78.3
5 30.6/0.30 0.81 4.40 1.18 18.29 13.7 83.2
6 30.6/0.40 0.57 4.10 1.51 15.77 12.9 76.4
7 37.9/0.18 0.52 4.30 1.10 14.89 13.4 87.1
8 39.0/0.24 0.51 6.30 1.16 19.65 14.8 96.5
9 39.3/0.29 0.44 4.10 1.50 15.53 12.6 80.4
10 32.8/0.31 0.88 5.50 1.09 21.08 14.5 93.0
11 33.4/0.43 0.79 5.44 1.40 19.13 13.5 84.1
12 34.4/0.52 0.69 5.72 1.37 18.71 13.4 87.7
13 34.0/0.36 0.98 5.40 1.09 18.59 12.5 79.7
14 33.1/0.39 0.73 6.40 1.29 19.87 13.0 85.9
15 32.9/0.39 0.79 8.70 1.92 18.32 12.8 87.0
16 32.5/0.40 0.47 6.50 1.51 18.75 13.7 86.9

a n = 3

TS Total solids in milk; RMS Rice to milk solids ratio

Heating rate index (fh)

The time taken for a heat penetration curve to traverse one log cycle is called the fh value. In the present study, fh values were in the range of 2.82 to 8.70 min. These values are in the range of the values reported for convection heating products, in contrast to conduction heating products whose fh values are reportedly 15 or more times than this viz. 30–40 min (Horner 1992). Heating rate index (fh) for convective heating products has been reported to be dependent upon temperature of heating medium and condensing surface, steam–air flow rate and direction, surface size and orientation, viscosity, film thickness and stagnant air layer thickness (Tung et al. 1990). Compared to conduction-heating products, convection heating products have a large heat capacity and thermal diffusivity, and reach retort temperature very quickly after which they remain essentially inert with respect to heat transfer (Weintraub et al. 1989). The fh value for mushrooms in brine was also found to be in the range of 4.7 to 5.8 min depending on the can size and weight of the product (Berry and Bradshaw 1982).

Lag factor for cooling curve (jc)

Lag factor in cooling curve occurs because the product temperature does not fall as rapidly as the retort temperature falls. jc values for convective heating products are reported to be close to 1 and for conducting heating packs jc values could be much higher as the cooling process is much slower for these products. jc values for the pre-mix of long-life kheer ranged from 1.06 to 2.31, which were in conformity with the values reported for convective heating liquid products (Horner 1992).

Process time (B)

The total process time (B) and operator’s process time (Pt) depend greatly on fh and jh values obtained for each process. B value for kheer ranged from 14.89 to 21.52 min depending on the Fo value (12.4–14.8) and related factors. Process time for products heated in conduction-heating regime are generally very long as compared to the ones observed in this study (Thijssen et al. 1978). The low process time coincided with the low values for fh and jh for the convection heated kheer as compared to conduction heated products. Process time for soybean paste and soybean in brine at 121.1 °C were 25 and 18 min, respectively (Guedez and Bath 1975). Pouch thickness affects the process times. Pflug et al. (1963) demonstrated a three-fold reduction in the process time necessary to achieve an Fo of 9 min simply by reducing the pouch thickness from 25.4 to 6.4 mm. Mango juice had a process time of 45 min corresponding to an Fo of 11.0 (Nanjundaswamy et al. 1973).

Cook value (Cg)

While process value (Fo) may be defined with respect to the effect of exposure time at a specific temperature on a specific organism, cook value (Cg) encompasses a multiplicity of physical and biochemical changes. Cook value (reference temperature, 100 °C and z value, 33 °C) for long-life kheer ranged from 78.3 to 96.5 min. It increased or decreased with an increase or decrease in Fo value (Table 2). Such a large cook value was expected to result in extensive softening of rice grains, but it did not so happen, and the grains were rather tough. It could be because the rice grains after gelatinization underwent retrogradation during cooling process resulting in softer grains. However, the product, as anticipated, underwent considerable browning.

Effect of process lethality (Fo value) on physico-chemical properties of stored long-life kheer

Data presented in Fig. 2a show that the TBA value increased during the storage at 37 °C, the increase being rapid after 90 days and was generally higher in formulations with higher process lethality values. For the formulations receiving heat treatment equivalent to Fo of 12.4, the TBA value increased from initial 0.073 to 0.123 at the end of storage, while for formulations with Fo of 13.7 and 14.6, the respective increases were from 0.075 to 0.129 and 0.076 to 0.138. However, statistical analysis of the data (Table 3) revealed that only the effect of storage period was significant (P < 0.01); the TBA value was significantly higher after 120 days of storage. It thus appeared that fat oxidation took place during storage of the product. Use of antioxidant (0.01 % BHA) did not make any perceivable difference in the TBA value (0.114 with the antioxidant and 0.124 without the antioxidant). TBA value of UHT soy beverage increased from 0.068 (OD) to 0.199 (OD) after 10 days of storage at 45 °C (Narayanan et al. 1993). Changes in the reflectance value of in-pouch processed kheer during storage at 37 °C are presented in Fig. 2b. It can be seen that formulations with a higher Fo had a lower reflectance value as compared to formulations with a lower Fo and the values declined in all the samples during storage. The reflectance value for the products with Fo of 12.4 decreased from the initial 43.30 % to 33.05 % after 150 days of storage. The corresponding values were 40.77 and 30.55 % for Fo of 13.7, and 38.01 and 27.02 % for Fo of 14.6. Statistical analysis (Table 3) showed that the effects of both the storage period and Fo value had a significant effect on the reflectance value (P < 0.01). Thus, browning of the product was significant after 75 days in products of Fo 12.4 and 13.2, and after 60 days in that of Fo 14.6. Product with higher Fo was accompanied by greater browning as observed during the entire storage period. Reflectance of UHT soy beverage dropped from 52.3 % to 49.5 % after 10 days of storage at 45 °C (Narayanan et al. 1993). Singh and Patil (1989) also reported a similar decrease in reflectance of UHT milk during storage and attributed it to the non-enzymatic browning reactions. The effect of storage on pH of long-life kheer made with different Fo values is shown in Fig. 2c. It is clear that the storage led to a significant decrease in pH of all the formulations. pH declined from the initial values in the range of 6.05–6.09 to 5.83–5.86 at the end of storage. The Fo value, however, had no significant effect on pH (Table 1). This decrease in pH, could be attributed to the Maillard reaction, taking place during storage leading to the production of organic acids. A similar drop in pH of sterilized soy beverage during storage has also been reported by Tomar and Chauhan (1988).

Fig. 2.

Fig. 2

a Thiobarbituric acid (TBA) value (OD value at 530 nm), b Reflectance value (450 nm) and c pH of long-life kheer as influenced by Fo value and period of storage at 37 °C (values are mean of triplicate experiments)

Table 3.

Analysis of variance: Changes in physico-chemical properties of long-life kheer during storage

Source of variation DF TBA Reflectance pH
F -ratio CD F -ratio CD F –ratio CD
Replicates 3 1.70NS 2.63 NS 1.51 NS
Storage period 8 2.01** 0.040 9.87 ** 2.97 27.75 ** 0.089
Treatment (Fo value) 2 0.52 NS 18.25 ** 1.71 0.82 NS
Interaction (treatment x period) 16 1.62 NS 0.57 NS 0.33 NS
Error 51

CD Critical Difference; NS Not significant

**P < 0.01

Sensory properties of long-life kheer

Sensory properties of long-life kheer both when it was fresh and after storage upto 150 days at 37 °C are presented in Table 4. It can be seen that colour score decreased from 6.92 to 4.72 after 150 days. Poor colour scores could be attributed to high Fo values. Texture score declined from 8.00 to 6.72 after storage till 150 days. Texture scores of in-pouch processed product were comparable to that of conventional kheer. There was a decline on flavour score from an initial value of 7.26 to 5.92 after 150 days of storage. This could be attributed to increase in oxidative rancidity during storage. In-pouch processed kheer was almost comparable to conventional product in terms of overall acceptability rating. However, its overall acceptability declined from 7.54 to 5.77 at the end of storage studies. This could be expected in a product which will undergo deterioration during storage in terms of colour and flavour.

Table 4.

Sensory properties of long-life kheer in comparison to conventional kheer and effect of storage

Properties (on 9-point hedonic scale) Conventional kheer Long-life kheer Long-life kheer CD (p < 0.05)
0 day 150 day
Colour score 8.5 ± 0.15 6.9 ± 0.17 4.7 ± 0.21 0.50
Texture score 9.0 ± 0.00 8.0 ± 0.11 6.7 ± 0.17 0.30
Flavor score 8.5 ± 0.15 7.3 ± 0.09 5.9 ± 0.15 0.39
Overall acceptability score 8.5 ± 0.15 7.5 ± 0.13 5.8 ± 0.16 0.21

a n = 7 panelists

CD Critical difference

Conclusion

Perceiving the potential of kheer as a value-added product in the International dairy market, ready-to-serve milk-rice kheer was developed employing a rotary retort system. The in-pouch processed product had a commercially useful shelf life of 5 months without refrigeration. Total process time (B value) for long-life kheer ranged from 14.89 to 21.52 min depending on the Fo value (12.4–14.8). Fo values employed in manufacturing had a profound effect on product properties such as pH, TBA value and colour. pH of long-life kheer varied from 6.04 to 6.10. TBA value of long-life kheer ranged from 0.073 to 0.081. As the product could be stored upto 5 months at ambient temperature without any appreciable loss in terms of chemical and sensory attributes, it could be used as a potential means of product diversification in the dairy industry.

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