Classifications

• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F3/00—Tea; Tea substitutes; Preparations thereof
  • A23F3/16—Tea extraction; Tea extracts; Treating tea extract; Making instant tea
  • A23F3/30—Further treatment of dried tea extract; Preparations produced thereby, e.g. instant tea
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F3/00—Tea; Tea substitutes; Preparations thereof
  • A23F3/16—Tea extraction; Tea extracts; Treating tea extract; Making instant tea
  • A23F3/22—Drying or concentrating tea extract
  • A23F3/26—Drying or concentrating tea extract by lyophilisation
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F5/00—Coffee; Coffee substitutes; Preparations thereof
  • A23F5/24—Extraction of coffee; Coffee extracts; Making instant coffee
  • A23F5/28—Drying or concentrating coffee extract
  • A23F5/32—Drying or concentrating coffee extract by lyophilisation
• • A—HUMAN NECESSITIES
  • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
  • A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
  • A23F5/00—Coffee; Coffee substitutes; Preparations thereof
  • A23F5/24—Extraction of coffee; Coffee extracts; Making instant coffee
  • A23F5/36—Further treatment of dried coffee extract; Preparations produced thereby, e.g. instant coffee

Definitions

• This invention relates to a low density but attrition- resistant hot soluble extractable food product, specifically freeze dried tea or coffee granules, and a process for preparing same.
• tea is the most widely consumed of all beverages. In fact, the worldwide per capita consumption has been estimated at 0.1 litre per day. Coffee is another beverage that is consumed in great volumes around the world. But while the invention is suitable for manufacturing low density and attrition- resistant coffee granules, the following description generally refers to tea.
• black tea which is obtained by harvesting new leaves of the plant Camellia sinensis and withering, rolling, enzymatically oxidizing, firing and sorting them.
• tea In Western countries consumers tea is generally sold in bags which are placed in hot water and allowed to stew but discarded prior to drinking the tea. However, more recently tea can also be prepared by dissolving a powdered or granulated tea product in hot water thus avoiding the need to handle and dispose of soggy bags.
• This powdered or granulated tea is known as instant tea and consists of the hot soluble product of black tea leaves that have been extracted, concentrated and dried.
• Flavours may be added or components such as caffeine may be removed during this process to meet the tastes and demands of consumers.
• the freeze dried tea granules typically prepared by known methods tend to be prepared from an extract of high solids concentration, for example 20-60%, which provides a density of about 90-100 g/1. This is equivalent to a weight per teaspoon of about 0.5 g of tea solids.
• Consumers in the United Kingdom typically enjoy their tea at a strength of about 0.5 grams of tea solids per cup and may add milk or cream so it is convenient to simply add one teaspoon of granules to a cup of hot water.
• consumers on the European continent generally prefer their tea to be weaker, typically about 0.35 grams of tea solids per cup, and tend not to add any milk. Consequently, continental tea drinkers would find one teaspoon of tea granules weighing 0.5 g provides an unacceptably strong cup of tea.
• USP 3,749,378 discloses an apparatus for foaming coffee or tea extracts and emulsions using carbon dioxide, nitrous oxide or more preferably nitrogen to a certain density which can then be freeze or spray dried.
• carbon dioxide does not give the same low bulk density products at the same initial foam density of nitrogen.
• the products that might be obtained by the apparatus are not characterised.
• spray dried coffee granules having a bulk density of 52 g/1 can be prepared when foaming with nitrogen but there is no indication as to their friability. Furthermore, freeze drying is discouraged on a cost basis.
• the present inventors have developed a novel process for preparing freeze dried extractable food granules from extracts having a low solids concentration, for example 10-25%, giving a product density of 50-80 g/1 and which are characterised by an attrition-resistant structure. Furthermore, insofar as tea is concerned the granules are darker in colour and look more tea-like than tea granules prepared by known methods. The inventors obtained similar results using coffee rather than tea.
• the invention may be said in broad terms to relate to a hot soluble extractable food product comprising granules characterised in that the granules are prepared from an extract containing less than about 25% soluble food solids, have a bulk density of no more than about 80 g/1 and a Friability Index (as herein described) of less than about 40%.
• Friability Index of a granule refers to the tendency of that granule to break down by attrition. This term is defined below along with a method of accurately and reproducibly quantifying same.
• the extractable food is tea or coffee and the granules are freeze dried.
• the liquor contains between about 10 to about 25% or especially about 16 to about 21% soluble food solids prior to freeze drying.
• the granules have a bulk density of about 50 to about 80 g/1 or especially about 60 to about 70 g/1 and a Friability Index less than about 30% or especially less than about 25%.
• the invention in broad terms may also be said to relate to a process for preparing a hot soluble extractable food product comprising:
• the extractable food is tea or coffee and is concentrated to between about 10 and about 25% or especially between about 16% to about 21% tea or coffee solids by weight and kept at a temperature of about 10°C prior to the cooling and aerating.
• the cooling and aerating is preferably carried out substantially simultaneously in one unit such as an ice cream freezer or other art-known apparatus.
• the cooling involves lowering the extract to a temperature of no less than about -5°C.
• the extract is preferably aerated with carbon dioxide, nitrous oxide, a mixture of those, or a mixture of nitrogen and either or both carbon dioxide and nitrous oxide. It is also preferred that the foam is cooled in liquid nitrogen and the frozen mass thus obtained shattered into granules smaller than about 5 mm in diameter by a hammer mill or the like.
• Figure 1 is a photographic representation of freeze dried low density tea granules that have been prepared by foaming a concentrated tea extract with nitrogen.
• Figure 2 is a photographic representation of freeze dried low density tea granules that have been prepared by foaming a concentrated tea extract with carbon dioxide.
• Figure 3 is a photographic representation of a scanning electron micrograph of a freeze dried low density tea granule that has been prepared by foaming a concentrated tea extract with nitrogen.
• Figure 4 is a photographic representation of a scanning electron micrograph of a freeze dried low density tea granule that has been prepared by foaming a concentrated tea extract with carbon dioxide.
• Tea liquor is extracted from tea leaves by art known means to give a tea solids concentration of typically 3 to 12%. This is concentrated by art known means to less than about 25% by weight tea solids, preferably between about 10 and about 25%, or more preferably between about 16% to 21% by weight tea solids.
• the concentrated tea extract is preferably brought to a temperature of about 10°C then cooled, for example to a temperature not less than about -5°C, and aerated, perhaps substantially simultaneously in one art-known apparatus such as an ice cream freezer, with a gas comprising: (i) a gas or mixture of gases substantially more soluble than nitrogen; or (ii) a mixture of nitrogen and a gas or mixture of gases substantially more soluble than nitrogen.
• Gases substantially more soluble than nitrogen (2.35 cm 3 in 100 cm 3 H 2 0 at 0°C) include carbon dioxide and nitrous oxide (179.7 cm 3 and 130.52 cm 3 in 100 cm 3 H 2 0 at 0°C respectively) . Foaming with carbon dioxide alone is especially preferred.
• the foamed concentrated extract is substantially frozen, preferably rapidly, by art known means such as by immersion into liquid nitrogen and the frozen mass thus produced is shattered in to granules smaller than about 5 mm in diameter on average using a hammer mill or the like. These granules are then freeze dried to yield a low density product, that is typically having a bulk density of about 50 to about 80 g/1 but preferably of about 60 to about 70 g/i.
• the granules are also characterised by being less friable or more ready to resist attrition than hot soluble extractable vegetable food granules manufactured by the methods described in the prior art .
• the friability of a granule depends on the nature of the applied forces as well as the intrinsic mechanical properties of the granule itself. That is why instant tea granules despite being less dense than similar granules such as those of coffee do not necessarily have a lower compressive strength.
• friability tests break down granules in different ways and therefore apply different types and degrees of force.
• the intrinsic mechanical properties of the material and the structure of the granule are also very important.
• Friability can be measured by testing a given mass or volume of granules. But it is often difficult to relate the results from such tests to single granule properties as packing and intergranule forces can greatly influence the measurements. It might therefore be desirable to perform mechanical tests on standard shaped blocks or bars so that friability measurements can be directly related to material and structural properties.
• the friability of granular material is based on the proportion of fines, that is granules having a diameter of less than 1 mm, that are generated when a known mass of freshly granulated material is subjected to the sort of abrasive forces they might experience during further processing, packing and transportation.
• This parameter is expressed as a percentage and termed the "Friability Index”.
• a low Friability Index indicates that a granulated product is attrition resistant and is desirable to consumers as they associate fragile granules and an abundance of dust with poor quality.
• Friability Index of a granulated material as defined above is determined as follows:
• the particle size range of a given granulated product is ascertained by vibrating a 50 g sample of same on a sieve stack at an amplitude of 0.58 mm for 2 minutes.
• the sieve stack comprises four sieves that comprise mesh sizes of 5 mm, 2.5 mm, 2.0 mm and 1.0 mm respectively;
• the Friability Index of granules according to the present invention is less than 40%, preferably less than 30% and more preferably less about 25%.
• the unique structural characteristics of the attrition- resistant granules of the present invention affects their appearance to the naked or partially aided eye. This is evident by comparing the freeze dried granules shown in Figure 1 with those shown in Figure 2.
• the freeze dried granules shown in Figure 1 were prepared by aerating a concentrated tea extract with nitrogen whereas the freeze dried granules shown in Figure 2 were prepared by aerating a similarly concentrated tea extract with carbon dioxide.
• the granules shown in Figure 2 have a "crisper", more glassy appearance than those shown in Figure 2.
• the pore sizes are greater.
• the granules are also slightly darker in colour (this is more noticeable when viewed by the naked eye) . This darker colour is considered desirable by consumers as it suggests a richer and higher quality product.
• the differences in the microscopic structures of granules prepared by aerating carbon dioxide rather than nitrogen are apparent when comparing the scanning electron micrographs of each shown in Figures 4 and 3 respectively.
• the microscopic structure of the granule prepared by nitrogen aeration shown in Figure 3 at a magnification of 200X resembles a brittle sponge-like structure wherein the solid portions are highly pitted. This explains why small parts of the granules readily break away to form dust .
• the microscopic structure of the granule prepared by carbon dioxide aeration shown in Figure 4 also at a magnification of 200X, also resembles a sponge-like structure, the solid portions much smoother and almost free of pitting. This granule structure is more resistant to attrition; less of the structure breaks off to form dust.
• a tea extract was obtained from black tea and concentrated to 16% tea solids by weight at a temperature of 10°C. This extract was divided into two substantially equal portions which were brought to 10°C then foamed with nitrogen gas and carbon dioxide gas respectively using a Crepaco type W- 104G ice cream freezer equipped with a type 30 dasher until a foam density of 0.45 g/cm 3 was obtained. The pressure within the freezing barrel of the freezer was maintained at 4 bar gauge throughout the freezing and the barrel walls were also kept refrigerated so that an extruded foamed product temperature of -2.5 to -3°C could be obtained.
• the extrudate was immersed in liquid nitrogen to stabilise the foam and the frozen mass obtained shattered using a hammer mill into granules of about 1 to 4 mm in diameter. These granules were then freeze dried and the resulting products subjected to a test of strength against attrition to determine their respective Friability Indices.
• the test involved vibrating 2.5-4 mm granules for 5 minutes with an amplitude of 1.58 mm vertically and the Friability Index was calculated as the percentage of fines (ie average diameter ⁇ 1 mm) generated from the original mass tested.
• the Friability Index of the nitrogen foamed product was found to be 45-49%. However, the Friability Index of the carbon dioxide foamed product was measured at 25-27% which represents a significant increase in strength against attrition. Furthermore, the carbon dioxide foamed product had an "agglomerated" appearance not usually associated with freeze dried beverage products and the colour was darker and more "tea-like". The bulk density of both products was 0.060 g/cm 3 .
• a coffee extract was prepared and concentrated to 16% coffee solids by weight.
• the concentrated extract was then cooled to 10°C, partially frozen and then aerated with carbon dioxide gas to a foam density of 0.6 g/cm 3 , frozen to stabilise the foam, shattered into granules and freeze dried in the same way as the described in Example 1 above.
• the final product was found to have a bulk density of 0.06 g/cm 3 and a friability index of 27%. Its appearance and structure also resembled the carbon dioxide foamed product obtained by the experiment described above as Example 1.

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• Life Sciences & Earth Sciences (AREA)
• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Food Science & Technology (AREA)
• Polymers & Plastics (AREA)
• Tea And Coffee (AREA)
• General Preparation And Processing Of Foods (AREA)

Priority Applications (3)

Applications Claiming Priority (2)

Publications (1)

Family

ID=10736629

Family Applications (1)

Country Status (8)

Cited By (7)

Citations (9)

• 1993
  • 1993-06-04 GB GB939311536A patent/GB9311536D0/en active Pending
• 1994
  • 1994-06-03 IN IN254BO1994 patent/IN178217B/en unknown
  • 1994-06-03 ZA ZA943908A patent/ZA943908B/xx unknown
  • 1994-06-04 AU AU71837/94A patent/AU7183794A/en not_active Abandoned
  • 1994-06-04 EP EP94920908A patent/EP0701404A1/en not_active Withdrawn
  • 1994-06-04 CA CA002164116A patent/CA2164116A1/en not_active Abandoned
  • 1994-06-04 JP JP7501313A patent/JPH08510917A/ja active Pending
  • 1994-06-04 WO PCT/EP1994/001848 patent/WO1994028736A1/en not_active Application Discontinuation

Patent Citations (9)

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