International Journal of Food Science and Technology 1999, 34, 365–370 The quality assessment of gari produced by using microwave energy Ibok Oduro1 & Brian Clarke2* 1 Present address: Department of Biochemistry (Food Science Section), University of Science and Technology, Kumasi, Ghana 2 School of Agriculture, Food and Environment, Silsoe College, Cranfield University, Bedfordshire, England, MK45 4DT, UK (Received 22 October 1996; Accepted in revised form 26 March 1999) Summary A novel technique using microwave energy for roasting and drying or garification of fermented cassava mash is investigated. The quality of gari produced using this method compared favourably with the standards quoted in the literature and with those of commercial gari purchased from a London market, in terms of colour, swelling capacity, moisture, pH and total acidity. Keywords Cassava, cooking, drying, gelatinization. Introduction Gari is the term used in West Africa for the partially gelatinized, fermented form of cassava (Manihot esculenta Crantz) (Ajibola et al., 1987a; Asiedu, 1989). It is also known as farinha de mandioca in South America, although variations exist in the length of time of fermentation. Cassava is a highly perishable, starchy root crop which starts to deteriorate within two or three days after harvest if not processed. Up to 300 kg/person/year of cassava is consumed, with an estimate of 30M tonnes/year consumed in Nigeria alone. Gari is a preservable, popular form of processed cassava which accounts for about 70% of the cassava eaten in Nigeria for example. In 1996 it was estimated by FAO that 70M tonnes were grown in Africa, (FAO, 1996) and it continues to be a major source of energy for millions of people. One of the drawbacks however, is that it consumes large amounts of fuel in its preparation, especially in the traditional technique where it is roasted and dried in a flat pan over an open *Correspondent: Fax: +44 1525 863277; e-mail: [email protected] © 1999 Blackwell Science Ltd wood fire. Population drift from rural to urban areas has increased the demand for ready packaged gari and there is a great need for better ways of preparing this food at both domestic and factory scale. The normal production stages (Lancaster et al., 1982; Bruinsma et al., 1985) consist of washing, peeling and grating the roots, and then fermenting the mash anaerobically for two to five days, pressing to remove the water which exudes during the fermentation stage, to give a moisture content of about 50%. The mash is then usually sieved before it is finally roasted and dried. Domestically, small open pans are used for frying, but in an attempt to increase production, larger rectangular pans of up to 2.5 3 1.5m are being introduced. For example, these are promoted by the Rural Agro-Industrial Development Scheme (RAIDS) of Nigeria and manufactured by several small companies in Ibadan. Similarly they are made by Agrico (Accra North, Ghana). In the automated factory systems, gently sloping, semi-circular troughs up to one metre diameter are often used, with rotating angled scrapers to move the gari along the trough (Fabrico Eng. & Production Co. Ltd., Issele-Uku, Nigeria). Flat 365 366 Quality of gari produced by microwave cooking I. Oduro & B. Clarke circular plate roasters are available up to 3m in diameter from Maquinas D’Andrea (Sao Paulo, Brazil), which also use mechanical scrapers to move the gari in a spiral fashion. Rotary drum roasters with internal baffle lifters have also been used in the past, which slope gently in the same way as the semi-circular trough. The important features are that a minimum temperature of about 80 °C is reached for the onset of gelatinization of starch, and then maintained over a residence time which permits a high percentage of the starch to be converted. The only other requirement is that some mixing or movement is carried out to prevent re-agglomeration of the granules or sticking of the gari to the base. Energy sources for gari production are quite varied and although wood is the principal fuel in rural districts, factories are increasingly using gas, oil and coal in West Africa. Wood may, of course, be considered as free, but it is a much depleted resource, and although it may be renewable in some areas, there is generally a large shortfall in timber availability in Africa and people are having to travel further and further in order to find sufficient wood for domestic or commercial usage. Electrical energy is fairly reliable in many urban townships in Africa, and oil is produced in Nigeria making the use of oilpowered electricity an attractive option for that country. Microwave energy was considered as a possible means of treatment due to its efficiency in heat transfer, (Oduro 1995) and the first stage was to see if the product could be prepared satisfactorily. The use of microwave ovens in food processing has been used in both domestic batch systems and continuous flow commercial systems for many years. Decareau (1985) reviewed many of these applications and the expanded use of microwave ovens since 1965 and listed the many advantages of these systems such as energy saving, rapid heating potential, shorter processing times and waste elimination. Cook-in-container (including plastic containers), defrosting and drying are other advantages of the system. The assessment of product quality, for either export or local use, is usually based on certain physical and chemical features. The quality standard for gari varies between countries as individual markets differ in their preferences. Variations in flavour depend mainly on the length of fermentation time, but variety of cassava and method of preparation are also important. It is necessary therefore to make sure that any new techniques of preparation are acceptable as well as being technically possible. Gari quality parameters have been reported by Sanni (1991); Chuzel et al. (1988); Codex Alimentarius Commission 1986 and Ingram (1975), but because most of the gari is processed by small scale producers, the application of these standards is not systematic. On the other hand because microwave techniques remove many of the risks associated with open frying pans, the chance of both small or large factories meeting the gari standard specification using microwave techniques could be much higher. Furthermore, microwave technology lends itself to better control over processing conditions such as time and temperature, so that a higher quality may be guaranteed. The authors further observed that microwave techniques require little handling and provide a high degree of protection to the product during processing, thus resulting in a higher standard of hygiene compared to that of other techniques. Domestic scale microwave ovens are available in West Africa and commercial scale microwave equipment could be imported if it were found to satisfy all the processing requirements. Other problems at commercial scale such as maintenance, reliability of electrical supply, training of manpower etc., would have to be addressed at some stage. For the present, however, a study was deemed necessary to see if gari could be produced satisfactorily by microwave technology, and to determine any technical limitations or advantages of this approach. Furthermore, the objective was to assess the quality of gari so produced in terms of swelling capacity, colour, moisture content, pH and total titratable acidity. Materials and methods Equipment A domestic microwave oven with a turntable (Toshiba model ER-7825 E/EW) was used. The input power was 1250W and the typical output power for water based products was 650W. The oven was operated from the ordinary International Journal of Food Science and Technology 1999, 34, 365–370 © 1999 Blackwell Science Ltd Quality of gari produced by microwave cooking I. Oduro & B. Clarke single phase mains supply and operated at a frequency of 2450MHz. Procedures Cassava mash (500g) with a wet particle size of between 3 and 5 mm was prepared by hand peeling and grating in a food processor. It was then allowed to ferment spontaneously in an incubator at 30 °C for four days. A cotton bag of the wet mash was then subjected to a heavy weight (10 kg) for several hours to expel the excess water down to a water content of about 50% (wet basis). The mash had a pH value of 4 when it was placed in the microwave oven. At 45 s intervals, the oven was switched off and the mash removed and stirred briskly by hand for one minute in order to prevent the formation of lumps. The mash was then returned to the oven for the next phase of the cooking cycle. After the predetermined cooking time intervals: 9, 12, 15, 18 and 21 minutes, the sample was removed from the oven and the moisture content was determined by the oven method. The gari samples were then dried down to about 10% moisture (wet basis) in an ordinary electrical laboratory oven at 60 °C in readiness for testing for swelling capacity, colour, pH and total acidity. room temperature, sealed with a rubber bung and then mixed by inverting. After two minutes the inversion was repeated and the sample left for a further three minutes, making a total of five minutes. Swelling capacity was calculated as the volume of gari in water after five minutes, divided by the initial volume of gari. Each measurement was replicated three times. Moisture content Triplicate samples of the microwaved product, weighing 10 g, were desiccated in a drying oven at 130 °C for three hours, then cooled, weighed, and the moisture content calculated on a wet basis percent. pH and total titratable acidity Samples weighing 10g were homogenized in 50 ml of distilled water for eight minutes using a magnetic stirrer. The pH was measured using a Jenway pH meter (Jenway Ltd, Dunmow, Essex, UK). The homogenized samples were filtered, 25 ml of the filtrate was titrated with 0.1M NaOH using phenolphthalein as an indicator and the percentage total acidity expressed as lactic acid equivalent. The measurements were replicated three times. Analyses of the gari produced by microwave Colour Swelling capacity was determined by the method devised by Bainbridge et al. (1996), similar to that used by Ajibola et al. (1987b). A 10 ml volume of gari was placed into a 50 ml measuring cylinder and topped up to 50 ml with distilled water at Colour was measured using a Minolta Chromameter (CR-200) colour difference meter (Minolta Co. Ltd, Osaka, Japan). The values read were L* and b* to indicate lightness and intensity of the yellowness of gari respectively, but a* val- Table 1 Physico-chemical characteristics (colour, pH, total titratable acidity and moisture content) of micro-waved gari samples. The standard deviations of triplicate measurements are given in parenthesis Time [min] L* 0 9 12 15 18 21 Commercial 92.3 82.5 84.4 85.1 87.2 86.4 81.6 b* (0.01) (0.98) (0.35) (1.09) (0.32) (0.60) (0.46) © 1999 Blackwell Science Ltd 10.0 19.1 18.3 17.6 21.6 23.7 22.7 pH (0.02) (0.28) (0.30) (0.96) (0.49) (0.73) (0.86) 3.98 3.99 4.00 4.01 4.01 4.05 (0.11) (0.10) (0.11) (0.00) (0.00) (0.60) Total titratable acidity [g of lactic acid/100g of gari] Moisture content (%wb) Swelling capacity 1.1 1.2 1.1 1.1 1.1 0.6 35.8 (2.7) 30.7 (2.1) 24.4 (2.0) 16.5 (1.7) 9.0 (1.6) 2.7 3.1 3.1 3.3 3.3 (0.01) (0.03) (0.05) (0.03) (0.11) (0.00 International Journal of Food Science and Technology 1999, 34, 365–370 367 368 Quality of gari produced by microwave cooking I. Oduro & B. Clarke ues were not recorded as they measure levels of green or redness which is not relevant in this case. High L* values indicate lighter colour and higher b* values indicate a more yellow colour. The measurements were replicated three times. Results and discussion Quality analysis Table 1 gives details of all the quality parameters measured. Swelling capacity The rehydration characteristic is very important, and the swelling power of gari was used to compare the rehydration properties of samples cooked for different times. Results in Table 1 show that swelling capacity increased with cooking time up to 18 minutes, and then remained constant up to 21 minutes. Statistical analysis gave a high correlation (r 5 0.95) between cooking time and swelling capacity. Samples cooked for 12–21 minutes gave a swelling capacity of between 2.7 and 3.3, which compares favourably with the Codex Alimentarius recommendation of a value of 3, while a range of 2.98 1 0.86 was found by Blanshard et al. (1994) in Sierra Leone and 2.84 1 0.26 by Ajibola et al. (1987b) in the Nigerian market. The cassava mash cooked for nine minutes was within the recommended values of 2.7–2.9 of Chuzel et al. (1988) in the Togo market, although a residence time of 12 minutes seems to satisfy all the various recommendations. This can however only be regarded as a guideline as preferences vary from one country to another. Furthermore, the required residence time will depend on the oven and the weight of cassava. Colour Variation in microwave treatment times produced slight differences in the colour of gari (Table 1). A greater intensity of yellow colour, indicated by higher b*, and a darker colour indicated by lower L* was obtained when compared with uncooked mash. Those samples micro-waved for a longer time of 18–21 minutes had higher b* values than those for 9–15 minutes. The L* values increased slightly with time, producing paler colours, and b* also increased with time producing more yellowness. These phenomena are no doubt associated with the greater percentage of gelatinization which occurs at longer cooking times. The acceptable range of colour values quoted by Codex Alimentarius (1986), Chuzel et al. (1988) and Sanni (1989), are: L* 80–85, b* 17–21. Cooking times greater than 15 minutes gave colour properties which fell beyond the accepted range. Samples cooked for 12–15 minutes would be regarded as high quality gari in Nigeria, Ghana and most other West African countries, where both yellow and creamy/white types are found. In certain markets in West Africa palm oil and other additives are added to the roasting pan in order to manipulate colour and flavour to suit some preferences. The results show that microwave energy produced gari with low colour variation compared to that of commercial gari. The L* and b* values of gari purchased from the London Market ranged from 77.5 to 85.8 and 18–27.5 respectively. These cannot be regarded as representative samples but they do represent typical quality that is available commercially and their properties do fall outside the recommended range. Blanshard et al. (1994) reported observing a wide range of colours in the gari samples purchased in Sierra Leone and no correlation between colour and sensory data from the consumers. It is not unknown however for commercial suppliers to incorporate additives such as palm oil in order to enhance both the colour and flavour substantially. pH and total titratable acidity The pH and total titratable acidity varied only slightly from 3.98 to 4.01 and 1.1–1.2% , respectively, over the cooking time periods 9–21 minutes. This was well within the range recommended by Codex Alimentarius Commission (1986), Chuzel et al. (1988) and Sanni (1991), of 3.5–4.5 for pH and 0.6–1.2% for total acidity. This, and earlier studies, found that pH and total titratable acidity could however vary quite widely because they depend on the duration of the fermentation stage, which also varies widely to suit different tastes, and also depends on the nature of mycofloras which occur. A previous study by Sanni (1989) showed that the pH of market sam- International Journal of Food Science and Technology 1999, 34, 365–370 © 1999 Blackwell Science Ltd Quality of gari produced by microwave cooking I. Oduro & B. Clarke ples varied from 3.9 to 7.3, with the peak between 3.5 and 4.5. Moisture content The results presented in Table 1 show that the moisture content decreased from 36% to 9% as microwave cooking time increased from nine to 21 minutes. Samples micro-waved for 9–18 minutes needed further drying to the required moisture of about 10%, while samples micro-waved for 21 minutes were dried sufficiently. The rate of drying may be expected to depend on temperature level, which did not vary much after reaching 100 °C, the residence time and the degree of stirring. Statistical analysis showed a very high correlation (r 5 20.99) between micro-waving time and the moisture content. Longer residence time enhances gelatinization of the starch component of the cassava mash. Ease of treatment The fermented cassava initially behaved in a manner which was difficult to handle, in that the whole mass became very hard when irradiated with microwaves. This was not impossible to overcome by grinding as there was also nonuniformity in the treatment, with hard and soft spots. The focal point of the microwaves appeared to be about 3 cm from the outer surface of the mash, which led initially to hardness in that region with a softer outside and a softer core. The effect of intermittent mixing was investigated, which lead to the establishment of the 45 s mixing cycle. This is, of course, a distinct drawback for batch ovens, but discussions with a microwave oven manufacturer have revealed the possibility of a continuous system in the form of a microwave tunnel with a mixer incorporated. The effect of the intermittent cooking resulted in some minor heat losses, but this was thought to be of negligible importance compared to the advantage of producing a uniform sample of gari. The formation of lumps is of course a problem in most garifying systems and some form of stirrer or separation is always required. In every other respect the gari produced was of acceptable quality according to the recommended standards, and it surpassed the standard of much © 1999 Blackwell Science Ltd commercial quality gari. With the exception of moisture content, all the quality standards were achieved after 12 minutes in the microwave oven. In a commercial production system a feasibility analysis would be needed to assess the best way to dry the gari. It would however be quite reasonable to expect that microwave energy would be the best way to achieve this. In the situation tested, 20 minutes approximately would be required to achieve both gelatinization and drying. The amount of energy consumed in microwave systems is only about half that of other cooking systems, which is one reason for making the system so popular. Furthermore the control of temperature and residence time can easily be automated in these ovens. The level of hygiene in such a fully enclosed system is another attractive feature which would be important in Africa, as elsewhere. There appears, from this study, to be very little reason why microwave ovens should not be used to make gari in the future. Conclusions The values obtained for the quality in terms of swelling capacity, colour, pH and total titratable acidity of samples prepared using microwave energy compare favourably with published recommended values for gari produced by conventional processing methods. A minimum of 12 minutes cooking time is recommended to achieve these quality standards, but additional drying would still be required and 20 minutes, approximately, would be required, to achieve both gelatinization and drying. The main drawback is that in a batch oven, the product has to be stirred because otherwise it would cake harden. The development of a continuous stirring mechanism which would prevent caking requires further investigation but, nevertheless, this technique could provide a useful alternative technology for cassava processing. References Ajibola, O.O., Ige, M.T. & Makanjuola, G.A. (1987a). Preliminary studies of a new technique of cassava mash gelatinization. Journal of Agricultural Engineering Research, 36, 97–100. Ajibola, O.O., Makanjuola, G.A. & Almazan, A.M. International Journal of Food Science and Technology 1999, 34, 365–370 369 370 Quality of gari produced by microwave cooking I. Oduro & B. Clarke (1987b). 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In: Proceedings of a Regional Workshop on Traditional African Foods Quality and Nutrition. 25–29 November (edited by A. Westby & P.T.A. Reilly). Pp. 133-137. Stockholm: International Foundation of Science. International Journal of Food Science and Technology 1999, 34, 365–370 © 1999 Blackwell Science Ltd
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