A BLACK LEAF TEA PRODUCT

Abstract

The present invention relates to a black leaf tea product. More particularly a black leaf tea product with altered aroma characteristics. The present invention provides a black leaf tea product comprising methylbutanal compounds in the range of 4.5 to 10 mg/kg of tea leaf.

Claims

1. A black leaf tea product comprising methylbutanal compounds in an amount of 4.5 to 10 mg/kg of tea leaf.

2. The tea product as claimed in claim 1, wherein the methylbutanal compounds comprise 2-methylbutanal and 3-methylbutanal.

3. The tea product as claimed in claim 2, wherein the methylbutanal compounds are 2-methylbutanal and 3-methylbutanal.

4. The tea product as claimed in claim 1, further comprising 2 methylpropanal.

5. The tea product as claimed in claim 4, wherein the 2-methylpropanal is in an amount of 2 to 7 mg/kg of tea leaf.

6. The tea product as claimed in claim 1, wherein the tea product comprises 2-methylbutanal, 3-methylbutanal and 2-methylpropanal, and wherein the combined amount of 2-methylbutanal, 3-methylbutanal and 2-methylpropanal is of 6.5 to 17 mg/kg of tea leaf.

7. The tea product as claimed in claim 1, further comprising phenylacetaldehyde.

8. The tea product as claimed in claim 1, wherein the black leaf tea product is obtained from the plant Camelia sinensis.

9. A tea blend comprising 5 to 99% of the tea product as claimed in claim 1.

10. The tea blend as claimed in claim 9 comprising 5 to 50% of the tea product.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0013] “Tea” for the purposes of the present invention preferably means material from Camellia sinensis var. sinensis and/or Camellia sinensis var. assamica. Especially preferred is material from var. assamica as this has a higher level of tea actives than var. sinensis.

[0014] “Leaf tea” for the purposes of this invention preferably means a tea product that contains tea leaves and/or stem in an uninfused form, and that has been dried to a moisture content of less than 30% by weight, and usually has a water content in the range 1 to 10% by weight (i.e. “made tea”).

[0015] “Fresh tea leaf” refers to tea leaf, buds and/or stem that have never been dried to a water content of less than 30% by weight, and usually have moisture content in the range 60 to 90%.

[0016] “Fermentation” refers to the oxidative and hydrolytic process that tea undergoes when certain endogenous enzymes and substrates are brought together, e.g. by mechanical disruption of the cells by maceration of the leaves. During this process, colourless catechins in the leaves are converted to a complex mixture of yellow and orange to dark-brown polyphenolic substances.

[0017] “Black tea” refers to substantially fermented tea. Black tea has different characteristics to green tea. Black tea is more astringent in taste and less bitter than green tea. The redness of black tea liquor is also significantly higher than that of green tea. Black tea also contains higher level of theaflavins.

[0018] The present invention provides a black leaf tea product comprising methylbutanal compounds is in the range of 4.5 to 10 mg/kg of tea leaf. Preferably the amount of methylbutanal compounds is in the range of 4.75 to 10 mg/kg of tea leaf, more preferably in the range of 5.0 to 8 mg/kg of tea leaf and most preferably in the range of 5 to 7 mg/kg of tea leaf.

[0019] The preferred methylbutanal compounds comprise 2-methylbutanal and 3-methylbutanal. In the most preferred aspect of the present invention the methylbutanal compounds are 2-methylbutanal and 3-methylbutanal. The structures of 2-methylbutanal and 3-methylbutanal are represented below:

##STR00001##

[0020] The tea product of the present invention preferably further comprises 2-methylpropanal. 2-methylpropanal has the following structure:

##STR00002##

[0021] The 2-methylpropanal is preferably present in the range of 2 to 7 mg/kg of tea leaf, more preferably in the range of 2 to 6 mg/kg of tea leaf and most preferably in the range of 2 to 5 mg/kg of tea leaf.

[0022] The tea product of the present invention also preferably comprises phenylacetaldehyde, which is having the following structure:

##STR00003##

[0023] The combined amount of 2-methylbutanal, 3-methylbutanal and 2-methylpropanal is preferably in the range of 6.5 to 17 mg/kg of tea leaf, more preferably in the range of 6.5 to 12 and most preferably in the range of 7 to 12 mg/kg of tea leaf.

[0024] The tea product of the present invention is preferably a black tea product. The tea product is preferably obtained from the plant Camelia sinensis.

[0025] The tea product of the present invention may preferably be prepared by adding methyl butanal compounds in the final leaf tea product at a desired ratio as disclosed above. The most preferred leaf tea product is a black leaf tea product.

[0026] Alternatively, the tea product of the present invention may be obtained by producing a black tea product with tea leaves that preferably have a conductivity greater than 100 μS wherein the conductivity is measured by placing the leaf in water for about 10 minutes to 2 hours and measuring the conductivity of the resulting water. More preferably the conductivity is greater than 150 μS and most preferably greater than 200 μS. The tea leaves are preferably placed in water for about 15 minutes to 1 hours and most preferably for 30 minutes to 45 minutes.

[0027] The tea leaves that provides conductivity greater than 100 μS as disclosed above are preferably obtained by keeping the fresh tea leaves in a carbon dioxide enriched environment with humidity greater than 90%, preferably greater than 95% and most preferably greater than 98%.

[0028] The above-mentioned tea leaves are then preferably subjected to a step of maceration to produce dhool. This step of size reduction is preferably carried out by crushing, tearing and curling (known in the art of tea processing as CTC). One or more CTC steps may be carried out. In this step the incubated leaf breaks up and releases enzymes that exist in the leaf.

[0029] Alternatively, the maceration step can be carried out by rolling the tea leaves in an orthodox roller or comminuted in a rotorvane, or a combination thereof. During these steps, precursors present in the tea leaf become amenable to the enzymes.

[0030] The macerated leaves then preferably undergo fermentation. It is a process in which the macerated tea leaves undergo biochemical changes in presence of endogenous enzymes present in the tea leaves. This process leads to the formation of the typical organoleptic properties of black leaf tea products. Fermentation is preferably carried out by keeping the leaf at a temperature of from 10° C. to 60° C. for 15 minutes to 5 hours. Preferably, the temperature of the fermentation is from 25 to 45° C. and more preferably from 25 to 40° C. The time for fermentation is preferably 30 minutes to 4 hours, more preferably 1 to 4 hours and most preferably 1 to 3 hours.

[0031] After fermentation, the fermented dhool may preferably be dried. During the drying step, the dhool is dried to a moisture content preferably less than 10% by weight of the tea leaf, more preferably less than 5% by weight of the tea leaf, to obtain the black leaf tea product.

[0032] The drying step is preferably carried out by thermal drying, freeze drying or vacuum drying.

[0033] Thermal drying is preferably carried out by contacting the leaf with air; with the temperature of air being preferably 80 to 160° C., more preferably 90 to 150° C., most preferably 100 to 130° C. Thermal drying may be carried out in any conventional dryer. However, a fluidized bed dryer or a tray dryer is particularly preferred for thermal drying. The leaf can also be dried by vacuum drying. During vacuum drying the tea leaf is subjected to an absolute pressure of preferably from 66.7 to 6.67×10.sup.4 Pa, more preferably from 6.67×10.sup.3 to 3.9×10.sup.4 Pa and most preferably from 1.3×10.sup.4 to 2.67×10.sup.4 Pa. Vacuum drying is carried out at a temperature in the range of preferably 20 to 70° C., more preferably 25 to 60° C. and most preferably 30 to 55° C. Vacuum drying may be carried out in any suitable vacuum drier, preferably in a rotary vacuum drier.

[0034] The present invention also provides a tea blend comprising 5 to 99%, preferably 5 to 50% by weight of the tea product of the present invention.

[0035] The invention will now be demonstrated in terms of examples. The following examples are for illustration alone and in no way limit the scope of the present invention.

EXAMPLES

[0036] Preparation of Different Tea Products:

[0037] All the experiments were carried out in Kenya using fresh tea leaf obtained from a Kenyan tea garden.

Example a

[0038] Fresh tea leaves were harvested from a Kenyan tea garden. The moisture content of the tea product was around 78%. The tea leaves were withered for 72 hours at a temperature of 25° C. The tea leaves were then subjected to CTC (cut tear curl) for 4 times to obtain macerated dhool. The macerated dhool was then fermented (exposed to air at 25° C.) for 90 minutes and then dried to a moisture content of less than 5% by weight (at 140° C.) to obtain a black leaf tea product.

Example 1

[0039] Fresh tea leaves were harvested from a Kenyan tea garden. The moisture content of the tea product was around 78%. The tea leaves were placed in an environment enriched (about 20% by volume) with carbon di-oxide with a humidity of 98% for 24 hours at a temperature of 25° C. until the conductivity reached 250 μS. The tea leaves were then subjected to CTC for 4 times to obtain macerated dhool. The macerated dhool was then fermented (exposed to air at 25° C.) for 90 minutes and then dried to a moisture content of less than 5% by weight (at 140° C.) to obtain a black leaf tea product.

Example 2

[0040] Fresh tea leaves were harvested from a Kenyan tea garden. The moisture content of the tea product was around 78%. The tea leaves were placed in an environment enriched (about 20% by volume) with carbon di-oxide with a humidity of 98% for 72 hours at a temperature of 25° C. until the conductivity reached 250 μS. The tea leaves were then subjected to CTC (cut tear curl) for 4 times to obtain macerated dhool. The macerated dhool was then fermented (exposed to air at 25° C.) for 90 minutes and then dried to a moisture content of less than 5% by weight (at 140° C.) to obtain a black leaf tea product.

[0041] The above tea products were analyzed for 2-methylbutanal (2 MB), 3-methylbutanal (3 MB) and 2-methylpropanal (2 MP) using the following protocol:

[0042] First, 2 g of the tea was brewed with 200 mL of hot water for 2 min and strained to generate black tea infusions.

[0043] Gas chromatography (GC) was used to characterize the aroma profiles of the tea infusions as follows. 4 mL of infusion was placed in a capped GC vial. Aroma was measured in the headspace using a SPME (solid phase micro extraction) fibre after the samples were pre-incubated (10 min) and then kept at 70° C. for 20 min. The conditions for gas chromatography and aroma extraction by SPME are given below.

[0044] Gc-Ms Conditions:

[0045] Volatile compounds from tea samples were analysed using a gas chromatograph with a MS detector (Agilent 7890B). A CP-wax 52 CB (30 m×0.25 mm, film thickness 0.15 μm) column was used for analysis. The injector was operated in a split less configuration with helium as the carrier gas at a constant flow rate of 1.0 mL/min. The injector was maintained at 230° C. The oven ramp was given as follows: initial temperature of 45° C. held for 3 min, followed by 5° C. /min to 180° C. hold for Om in and finally 10° C. /min to 230° C. for 10 min.

[0046] Spme Conditions:

[0047] Analysis of volatile compounds released from the tea samples was carried out using SPME. More particularly, a 2 cm stable flex fiber, coated with 50/30 μm poly(divinylbenzene) (DVB)/carboxen (CAR)/poly(dimethylsiloxane) (PDMS) (Supelco, Bellefonte, Pa.) was used with automated SPME system (Combi PAL system).

[0048] Equipment Specifications and Experimental Conditions:

[0049] SPME Fiber: Grey fiber (PDMS/DVB/CAR)

[0050] Pre-Incubation time: 10:00 min

[0051] Incubation temp: 70° C.

[0052] Needle Penetration: 12 mm

[0053] Fiber Penetration: 20 mm

[0054] Extraction Time: 20:00 min

[0055] Desorb to: GC Injector port 1

[0056] Injection Time: 5:00 min

[0057] Post fiber Condition time: 15 min

[0058] GC Run time: 40 min

[0059] Cooling time: 10 min

[0060] Fiber conditioning temp: 230° C.

[0061] MS conditions:

[0062] Tune type: El

[0063] Tune EMV: 1073

[0064] MS Source: 230° C.

[0065] Scan Range: 50-500 (mass)

[0066] Gain factor: 1

[0067] The peak area was calculated for the individual volatile compounds from the GC chromatograms. Standard concentration curves are generated for each volatile. These standard curves are used to convert the peak area to a concentration for the respective volatiles,

[0068] The results are summarized below:

TABLE-US-00001 TABLE 1 (2MB + 3MB + Example No. 2MB + 3MB (mg/kg) 2MP (mg/kg) 2MP) (mg/kg) A 2.95 1.7 4.65 1 4.75 2.55 7.3 2 5.15 2.05 7.2

[0069] Tasting the Tea Products of the Present Invention

[0070] The above tea products were also tasted by a panel of trained tea tasters. First, a difference test was carried out separately between example A and example 1 and then between example A and example 2 to test whether the panelists were able to pick any difference in the sample set. In both cases, the panelists were able to pick up products of example 1 and 2 as different from example A.

[0071] In the next study, a descriptive analysis to get product descriptions in terms of sensory attributes was carried out. [0072] For sample A, the main descriptors were that of woody, fresh green and black tea aroma. [0073] For both samples 1 and 2, the main descriptors were that of caramellic and malty with quite low intensity of fresh green and black tea aroma.

[0074] From the above examples it is evident that the tea products within the scope of the present invention (Example 1 and 2) have enhanced malty aroma notes compared to a control tea product (Example A).