GB2085274A - A method for the production of decaffeinated tea - Google Patents
A method for the production of decaffeinated tea Download PDFInfo
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- GB2085274A GB2085274A GB8131172A GB8131172A GB2085274A GB 2085274 A GB2085274 A GB 2085274A GB 8131172 A GB8131172 A GB 8131172A GB 8131172 A GB8131172 A GB 8131172A GB 2085274 A GB2085274 A GB 2085274A
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- GB
- United Kingdom
- Prior art keywords
- tea
- caffeine
- solvent
- saturated
- extraction
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- 238000000034 method Methods 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 6
- 235000015092 herbal tea Nutrition 0.000 title description 7
- RYYVLZVUVIJVGH-UHFFFAOYSA-N caffeine Chemical compound CN1C(=O)N(C)C(=O)C2=C1N=CN2C RYYVLZVUVIJVGH-UHFFFAOYSA-N 0.000 claims abstract description 139
- 244000269722 Thea sinensis Species 0.000 claims abstract description 103
- 235000013616 tea Nutrition 0.000 claims abstract description 79
- LPHGQDQBBGAPDZ-UHFFFAOYSA-N Isocaffeine Natural products CN1C(=O)N(C)C(=O)C2=C1N(C)C=N2 LPHGQDQBBGAPDZ-UHFFFAOYSA-N 0.000 claims abstract description 68
- 229960001948 caffeine Drugs 0.000 claims abstract description 68
- VJEONQKOZGKCAK-UHFFFAOYSA-N caffeine Natural products CN1C(=O)N(C)C(=O)C2=C1C=CN2C VJEONQKOZGKCAK-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000002904 solvent Substances 0.000 claims abstract description 47
- 238000000605 extraction Methods 0.000 claims abstract description 37
- 239000000796 flavoring agent Substances 0.000 claims abstract description 34
- 235000019634 flavors Nutrition 0.000 claims abstract description 34
- 235000006468 Thea sinensis Nutrition 0.000 claims abstract description 27
- 235000020279 black tea Nutrition 0.000 claims abstract description 27
- 229920006395 saturated elastomer Polymers 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000009835 boiling Methods 0.000 claims abstract description 9
- 150000008282 halocarbons Chemical class 0.000 claims abstract description 8
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical group ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 33
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 239000003729 cation exchange resin Substances 0.000 claims description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 2
- 240000007154 Coffea arabica Species 0.000 description 13
- 235000016213 coffee Nutrition 0.000 description 13
- 235000013353 coffee beverage Nutrition 0.000 description 13
- 239000002609 medium Substances 0.000 description 11
- 239000000284 extract Substances 0.000 description 9
- 241000533293 Sesbania emerus Species 0.000 description 5
- 239000003463 adsorbent Substances 0.000 description 5
- YZUPZGFPHUVJKC-UHFFFAOYSA-N 1-bromo-2-methoxyethane Chemical compound COCCBr YZUPZGFPHUVJKC-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000012736 aqueous medium Substances 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000004151 fermentation Effects 0.000 description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000006286 aqueous extract Substances 0.000 description 2
- 229940023913 cation exchange resins Drugs 0.000 description 2
- -1 chloroform or Chemical class 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 244000013123 dwarf bean Species 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 235000021331 green beans Nutrition 0.000 description 2
- 238000001802 infusion Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000005418 vegetable material Substances 0.000 description 2
- 235000019737 Animal fat Nutrition 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical group C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- IPMYMEWFZKHGAX-UHFFFAOYSA-N Isotheaflavin Natural products OC1CC2=C(O)C=C(O)C=C2OC1C(C1=C2)=CC(O)=C(O)C1=C(O)C(=O)C=C2C1C(O)CC2=C(O)C=C(O)C=C2O1 IPMYMEWFZKHGAX-UHFFFAOYSA-N 0.000 description 1
- 206010062519 Poor quality sleep Diseases 0.000 description 1
- UXRMWRBWCAGDQB-UHFFFAOYSA-N Theaflavin Natural products C1=CC(C2C(CC3=C(O)C=C(O)C=C3O2)O)=C(O)C(=O)C2=C1C(C1OC3=CC(O)=CC(O)=C3CC1O)=CC(O)=C2O UXRMWRBWCAGDQB-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229930013930 alkaloid Natural products 0.000 description 1
- 150000003797 alkaloid derivatives Chemical class 0.000 description 1
- 235000019606 astringent taste Nutrition 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 235000019658 bitter taste Nutrition 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000002027 dichloromethane extract Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000019225 fermented tea Nutrition 0.000 description 1
- 229910000286 fullers earth Inorganic materials 0.000 description 1
- 235000009569 green tea Nutrition 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 150000008442 polyphenolic compounds Chemical class 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000013557 residual solvent Substances 0.000 description 1
- 230000000638 stimulation Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- IPMYMEWFZKHGAX-ZKSIBHASSA-N theaflavin Chemical compound C1=C2C([C@H]3OC4=CC(O)=CC(O)=C4C[C@H]3O)=CC(O)=C(O)C2=C(O)C(=O)C=C1[C@@H]1[C@H](O)CC2=C(O)C=C(O)C=C2O1 IPMYMEWFZKHGAX-ZKSIBHASSA-N 0.000 description 1
- 229940026509 theaflavin Drugs 0.000 description 1
- 235000014620 theaflavin Nutrition 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
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
- A23F3/40—Tea flavour; Tea oil; Flavouring of tea or tea extract
- A23F3/42—Isolation or recuperation of tea flavour or tea oil
- A23F3/423—Isolation or recuperation of tea flavour or tea oil by solvent extraction; Tea flavour from tea oil
-
- 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
- A23F3/36—Reducing or removing alkaloid content; Preparations produced thereby; Extracts or infusions thereof
- A23F3/366—Reducing or removing alkaloid content; Preparations produced thereby; Extracts or infusions thereof by extraction of the leaves with selective solvents
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Tea And Coffee (AREA)
Abstract
A method for the production of black tea having a reduced caffeine content comprises:- a) treating black tea with water to increase its moisture content and thereby break down caffeine complexes; b) extracting the treated tea with a low boiling halogenated hydrocarbon solvent for caffeine which is substantially saturated with flavour components of tea but which is not saturated with respect to caffeine; and c) separating the extracted tea from the solvent. The extraction medium used in step b) may be prepared by previously extracting tea with a halogenated hydrocarbon solvent to extract flavour components and caffeine and optionally removing at least part of the caffeine from the solvent.
Description
SPECIFICATION
A method for the production of decaffeinated tea
The present invention relates to decaffeinated tea
and a process for its production.
Both tea and coffee contain relatively large quantisties of the alkaloid caffeine, which is responsible for
their stimulant properties. On a weight basis, dry tea
contains more caffeine than dry ground coffee, but, -conversely, a conventional cup of tea only contains
about 75 mg caffeine, whereas an average cup of
coffee contains about 150 mg, due to the larger
amount of ground coffee needed to give the required
flavour level. Nevertheless, it will be seen that the
amount of caffeine in tea is substantial.
While it has long been recognised that the caffeine
in coffee could lead to over stimulation and, when
drunk late in the evening, to unwanted wakefulness,
this is not popularly recognised in the case of tea.
There are many brands of decaffeinated coffee on
the market, but only one or two brands of decaffein
ated tea. More recently, doubts have been expressed
as to the general physiological effects of caffeine,
when taken habitually in relatively large quantities in
drink such as coffee.
One reason why comparatively little decaffeinated
tea has been marketed is the difficulty of achieving
acceptable flavour in decaffeinated tea. The problem
is quite different in the case of coffee, in that it has
been found possible to extract caffeine from coffee
beans at the green stage, the characteristic flavours
of coffee being developed only in the subsequent
roasting. Tea, however, is prepared by a fermenta
tion process, the tea leaves being left to ferment for a
period before being dried to give the traditional
"black tea". In the case of tea, extraction at the green
stage has been found to inactivate certain of the
enzymes necessary for fermentation. In fact, the
flavour profile of tea is very unstable, particularly in
the presence of water, so that it is also found that
extraction of the green tea after fermentation but
before drying is also unsatisfactory.We have found,
therefore, that it is necessary in the case of tea for
decaffeination to be carried out on the dried fer
mented tea, that is using "black tea". At this stage,
however, all the desired flavours have already been
developed, so that the extraction procedure can very
readily affect seriously the final flavour of the tea.
It has been proposed to extract caffeine from tea ' or coffee by contacting with an organic solvent such
as dichloromethane. However, when such a solvent
is used for decaffeinating black tea, a substantial
proportion of the flavour components are also
removed resulting in a product which is very inferior
compared to the starting tea. Decaffeinated tea
prepared in this way has never been commercially
popular due to poor flavour characteristics.British
Patent Specification No. 1 516 208 describes a
process for the decaffeination of vegetable materials
such as coffee or tea as well as aqueous extracts
thereof, by extraction with a fatty material, the fatty
material being an animal or vegetable fat or oil or
admixture or fraction thereof which is liquid and
capable of removing caffeine from a caffeine containing composition. This is alleged to be superior to the use of solvents such as dichloromethane.
In a preferred embodiment, the flavour components of the vegetable material are removed priorto extraction of caffeine and then reintroduced at a later stage. In one embodiment, this specification describes a process in which green coffee beans are first extracted with water to remove caffeine therefrom, and the caffeine in the aqueous extract is removed by further extraction with the fatty material.In orderto avoid substantial loss of flavour components from the green coffee beans when extracting with water, a closed cyclic circulation of the aqueous extraction medium may be employed whereby the green beans are contacted with the aqueous medium, the aqueous medium has caffeine selectively removed therefrom by extraction with the fatty material, and the aqueous medium is recycled for further selective caffeine removal from the green beans without removing other water-soluble components such as flavour components. It should be noted that this embodiment is particularly described in relation to the treatment of green coffee beans, where the flavour profile has not been developed in contrast to black tea where the final flavour characteristics are unstable.The flavours of coffee are not developed until the roasting stage, whereas the flavours of black tea are already developed and may be very easily adversely affected. Thus, techniques which may be used for treating green coffee beans cannot readily be used for treating black tea, where it is essential that the delicate flavours are not harmed.
To our knowledge, the above process has never been applied commercially to the direct extraction of black tea musing fatty or oily solvents.
We have now found a method which allows the removal of caffeine from black tea without substantially affecting the flavour of the tea.
We have found that it is possible to extract caffeine from black tea without substantial deterioration of flavour, or even with some improvement of flavour, if the tea is extracted with a low boiling halogenated hydrocarbon solvent for caffeine which is substantially saturated with the flavour components of tea but which is not saturated with respect to caffeine.
By using a low boiling solvent, such as dichloromethane the extracted tea may readily be freed from traces of solvent, in contrast to the use of oily or fatty solvents.
Thus, the invention provides a method for the production of black tea having a reduced caffeine content which comprises the steps of a) treating black tea with water to increase its moisture content and thereby break down at least part of any caffeine complexes present therein; b) extracting the treated tea with a low boiling halogenated hydrocarbon solvent for caffeine which is substantially saturated with flavour components of tea but which is not saturated with respect to caffeine; and c) separating the extracted tea from said solvent.
The extraction medium used according to the invention may be prepared by previously extracting a batch of tea with the solvent for caffeine in such a way that any flavour components of the tea which are extractable by that solvent reach saturation or near-saturation concentrations in the solvent and optionally then removing at least part of any caffeine present in the solvent, for example by adsorption. In order to avoid wastage, the tea used for the preparation of the extraction medium, which will lack some flavour components, may be mixed in minor amounts with tea treated by the method of the invention. For example, up to about 5% by weight of tea used for preparing the extraction medium may be mixed in without substantially affecting the flavour of the tea.
The flavour saturated solvent will possess useful solvent power for caffeine even when significant quantities of caffeine are present as long as the caffeine concentration is well below the saturation level. It is naturally preferable to remove substantially all of the caffeine from the initial flavour saturated solvent prior to using this to extract tea, but this can then be used to extract several successive batches of further black tea until the caffeine in the extract has built up to a level just below that which is detrimental to the solvent power of the medium for caffeine in the tea, whereupon the medium can be subjected to further caffeine removal, most simply by adsorption as previously. However, for maximum caffeine extraction efficiency we have found it preferable to subject the extraction medium to caffeine removal prior to extraction of each successive batch of tea.
Once caffeine has been removed, the solvent can be used to extract further tea, followed by further caffeine removal and this procedure can be repeated many times. Evenutally, however, it may be necessary to re-start the procedure either with fresh solvent, or, more economically, with solvent distilled from the previously described extraction medium.
The solvent for caffeine used in the method of the invention is a low boiling halogenated hydrocarbon such as chloroform or, more preferably, dichloromethane. Byte term "low boiling" we mean that the solvent is readily volatilised, having a boiling point, for example, in the range 35"C to 65"C.
The ratio of the solvent such as dichloromethane to the tea, on a weight basis, varies somewhat with the nature and moisture content of the black tea to be extracted, but is generally in the range 10:1 to 60:1, and preferably about 15:1 to 40:1, e.g. about 20:1. The time and temperature of extraction are related, in that longer extraction times are required at lower temperature and vice versa, but extraction times are generally in the range 30 minutes to 3 hours, while extraction temperatures are generally in the range 20-44"C.
We have found that the caffeine in black tea tends to be complexed, for example with polyphenols such as theaflavin, and in that form is resistant to extraction with solvents such as methylene chloride.
However, such complexes are readily cleaved at room temperature by increasing the moisture content of the black tea to above its usual level (generally about 7.5%) prior to extraction. In the preliminary treatment the moisture content ofthe tea is conveniently increased to 10 to 31i36, and preferably about 25%, by weight of water. This treatment step may conveniently be effected by agitating the tea at ambient temperature (e.g. in the range 10-30"C) with the required amount of additional water for a suitable time, for example 15 to 45 minutes, e.g. 30 minutes, immediately prior to extraction.
The removal of the caffeine from the extraction solvent is preferably effected by adsorption, either batchwise or continuously. A number ofsuitable adsorbents are known from the literature. In that caffeine is a base, cation-exchange resins can be used, as well as minerals such as Fullers earth having ion-exchange properties of a similar type.
Preferred adsorbents are cation-exchange resins of the macro-reticular type, especially Amberlyst 15.
The ratio of adsorbent to extract necessary to remove the caffeine can readily be determined by experiment but when Amberlyst 15 is used, the ratio of adsorbent to extract, on a weight basis, is generally in the range 1:30 to 1:60.
In general, the most suitable time and temperature for the adsorption step may be determined by experiment, but 30-60 minutes at room temperature are suitable when Amberlyst 15 is used.
The removal of caffeine from the extraction medium may be carried out after each extraction of fresh black tea or, as indicated above, it may be possible to extract a succession of batches of tea and to permit the caffeine concentration to build up over a number of extraction stages before removal. In general, the caffeine concentration in the extraction medium may be permitted to reach about 20% of saturation before such removal.
After separation of the extracted tea from the extraction medium, for example by simple filtration, the extracted tea may be subsequently treated to remove residual solvent and moisture. As the solvent is low boiling, it may be adequate simply to subject the tea to tumble-drying in a stream of air, preferably hot air, or it may, in some cases, be preferable to remove the solvent under vacuum, for example by flash evaporation.
Where it is desired to recover the caffeine removed from the tea, the adsorbent may be treated to liberate the caffeine, normally by displacement by alkali. Such techniques are well described in the literature.
We have found that the method according to the invention allows the caffeine content of black tea to be substantially reduced without adversely affecting the flavour. For example, we have been able to reduce the caffeine content of black tea by more than 75%, e.g. to less than 0.7% by weight of caffeine. Tea having such a low caffeine content would, on infusion, give typical levels of caffeine in a standard cup of less than 14 mg, and this compares very favourably with commercial decaffeinated coffees which give typical caffeine levels of 20 mg per cup.
The tea produced by the extraction procedure according to the invention has markediy superior flavour properties as compared with tea which has been extracted with pure solvent. Indeed, in tastings which have been carried out, the tea prepared according to the invention has been judged to be marginally superior to the tea from which it was prepared.
The following examples are given by way of
illustration only; all temperatures are in degrees C:
Example 1
20 g Tea with an integral moisture content of 7.5% were placed in a flask and 500ml of dichloromethane were added. A reflux condenser was connected to the flask and the contents stirred for 1 hour at 25 .
The contents of the flask were then filtered. The
extracted tea was tumble dried and set aside.
The dichloromethane tea extract was used for a
subsequent extraction as follows:
A further 1 0g of tea were placed in a flask, the
moisture content of the tea was adjusted to 25% by the addition of 2.58ml distilled water, and the flask
connected to a reflux condenser. The contents of the
flask were agitated for 30 minutes at 25 in this
conditioning stage. 400ml Of the extract from the
first extraction were added to the flask and agitation was continued for 1 hour. At the end of the
extraction the contents of the flask were filtered and
the recovered tea was tumble dried in a stream of air
at 45 until a moisture content of 7.5% was reached.
The dichloromethane extract was decaffeinated by
stirring at room temperature with 10g Amberlyst 15
macro-recticular ion exchange resin in the sodium
form for 30 minutes, followed by filtration. The
decaffeinated extract was subsequently used to
extract 25 further batches of tea with its volume
being adjusted as necessary to 400 ml with fresh
dichloromethane. It was necessary to decaffeinate
the extract after extraction of every 8th batch of tea.
It was possible by this method to reduce the
caffeine content of the black tea from 3.9% to 0.38%.
Organoleptic assessment of infusions prepared from
this decaffeinated product indicated a loss of bitter
ness and astringency in comparison to those pre
pared from the untreated tea.
It was possible to re-cycle the tea set aside at the
end of the first extraction into subsequent batches of
tea prior to the decaffeination step without signifi
cantly affecting the quality of the end product.
Example 2
The procedure was similar to that in Example 1
except that the tea was extracted for 30 minutes with
2 x 200 ml of the first extract.
The caffeine content of black tea was reduced from 4.0% to 0.38%.
Example 3
500 g Tea are placed in a rotatable container of 26
litres capacity and 11 litres of dichloromethane are
added. The container is rotated at 26 r.p.m. for 1
hour, whereupon the solvent extract is discharged to
a storage vessel and the tea put on one side. A
further 500 g of tea are placed in the container and
sufficient water added to increase the moisture
content of the tea to 25%. The container is closed
and allowed to stand for 30 minutes. 10 Litres of
solvent extract are then introduced into the contain
er, and this is then rotated at 26 r.p.m. for 3 hours.
The tea and extract are then removed and the tea
dried at 60 to 65"C for 2 hours. If necessary the
moisture content of the tea may be adjusted to 7%.
The caffeine content of the tea is typically 0.69% by weight. The solvent, after separation from the tea, is decaffeinated as described in Example 1 and used to extract a further batch of black tea. The overall procedure is repeated with successive batches of tea.
Claims (10)
1. A method for the production of black tea having a reduced caffeine content which comprises the steps of a) treating black tea with water to increase its moisture content and thereby break down at least part of any caffeine complexes present therein; b) extracting the treated tea with a low boiling halogenated hydrocarbon solvent for caffeine which is substantially saturated with flavour components of tea but which is not saturated with respect to caffeine; and c) separating the extracted tea from said solvent.
2. A method according to claim 1 wherein the solvent is dichloromethane.
3. A method according to either of claims 1 and 2 wherein the weight ratio of tea to solvent is from 1:10to1:60.
4. A method according to claim 3 wherein the weight ratio is about 1:20.
5. A method according to any one of the preceding claims wherein the halogenated hydrocarbon solvent which is substantially saturated with flavour components of tea but which is not saturated with respect to caffeine is first prepared by extracting a batch of black tea with the solvent in such a way that any flavour components of the tea which are extractable by the solvent reach substantially saturation concentrations in the solvent and, if necessary or desired, at least a part of any caffeine then present in the solvent is subsequently removed therefrom.
6. A method according to any one of the preceding claims wherein the halogenated hydrocarbon solvent saturated with flavour components is used to extract successive batches of treated tea, optionally after removal of at least a part of any caffeine present in the solvent.
7. A method according to claim 6 wherein caffeine is removed from the solvent prior to extraction of each successive batch of treated tea.
8. A method according to any one of claims 5 to 7 wherein caffeine removal is effected by adsorption onto a cation-exchange resin.
9. A method according to any one of the preceding claims wherein in step a) the moisture content of the tea is increased to 10 to 35% by weight.
10. Blacktea having a reduced caffeine content produced by a method according to any one of the preceding claims.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB8131172A GB2085274A (en) | 1980-10-16 | 1981-10-15 | A method for the production of decaffeinated tea |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB8033356 | 1980-10-16 | ||
| DE19803039348 DE3039348A1 (en) | 1980-10-17 | 1980-10-17 | PROTEIN-BASED SNACK PRODUCT AND METHOD FOR THE PRODUCTION THEREOF |
| GB8131172A GB2085274A (en) | 1980-10-16 | 1981-10-15 | A method for the production of decaffeinated tea |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB2085274A true GB2085274A (en) | 1982-04-28 |
Family
ID=27188916
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB8131172A Withdrawn GB2085274A (en) | 1980-10-16 | 1981-10-15 | A method for the production of decaffeinated tea |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB2085274A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4839187A (en) * | 1984-06-14 | 1989-06-13 | Nestec Sa | Antioxidant compositions |
| US4844925A (en) * | 1984-07-25 | 1989-07-04 | Nestec S.A. | Process for inhibiting formation of N-nitrosamines in a nitrite-cured food product |
| US4891231A (en) * | 1983-12-15 | 1990-01-02 | Nestec S.A. | Process for inhibiting liquid oxidation in food |
| CN110129169A (en) * | 2019-05-22 | 2019-08-16 | 遵义医科大学 | Method for reducing caffeine content in distilled tea wine |
-
1981
- 1981-10-15 GB GB8131172A patent/GB2085274A/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4891231A (en) * | 1983-12-15 | 1990-01-02 | Nestec S.A. | Process for inhibiting liquid oxidation in food |
| US4839187A (en) * | 1984-06-14 | 1989-06-13 | Nestec Sa | Antioxidant compositions |
| US4844925A (en) * | 1984-07-25 | 1989-07-04 | Nestec S.A. | Process for inhibiting formation of N-nitrosamines in a nitrite-cured food product |
| CN110129169A (en) * | 2019-05-22 | 2019-08-16 | 遵义医科大学 | Method for reducing caffeine content in distilled tea wine |
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