CA1043251A - Process for protecting organic materials - Google Patents
Process for protecting organic materialsInfo
- Publication number
- CA1043251A CA1043251A CA221,892A CA221892A CA1043251A CA 1043251 A CA1043251 A CA 1043251A CA 221892 A CA221892 A CA 221892A CA 1043251 A CA1043251 A CA 1043251A
- Authority
- CA
- Canada
- Prior art keywords
- bacteriostatic agent
- agent
- added
- acid
- bacteriostatic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000000034 method Methods 0.000 title claims abstract description 20
- 230000008569 process Effects 0.000 title claims abstract description 16
- 239000011368 organic material Substances 0.000 title claims abstract description 8
- 239000000022 bacteriostatic agent Substances 0.000 claims abstract description 37
- 239000000463 material Substances 0.000 claims abstract description 18
- 239000000284 extract Substances 0.000 claims abstract description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical group CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 17
- 239000012071 phase Substances 0.000 claims description 17
- 238000000605 extraction Methods 0.000 claims description 15
- 239000002904 solvent Substances 0.000 claims description 11
- 239000008346 aqueous phase Substances 0.000 claims description 9
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 claims description 5
- 239000011260 aqueous acid Substances 0.000 claims description 2
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 27
- RYYVLZVUVIJVGH-UHFFFAOYSA-N caffeine Chemical compound CN1C(=O)N(C)C(=O)C2=C1N=CN2C RYYVLZVUVIJVGH-UHFFFAOYSA-N 0.000 description 24
- 239000003795 chemical substances by application Substances 0.000 description 17
- 239000000243 solution Substances 0.000 description 13
- LPHGQDQBBGAPDZ-UHFFFAOYSA-N Isocaffeine Natural products CN1C(=O)N(C)C(=O)C2=C1N(C)C=N2 LPHGQDQBBGAPDZ-UHFFFAOYSA-N 0.000 description 12
- 229960001948 caffeine Drugs 0.000 description 12
- VJEONQKOZGKCAK-UHFFFAOYSA-N caffeine Natural products CN1C(=O)N(C)C(=O)C2=C1C=CN2C VJEONQKOZGKCAK-UHFFFAOYSA-N 0.000 description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 8
- 230000003385 bacteriostatic effect Effects 0.000 description 8
- 239000001993 wax Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 5
- 239000000796 flavoring agent Substances 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 4
- 235000019634 flavors Nutrition 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 241000533293 Sesbania emerus Species 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- 230000001476 alcoholic effect Effects 0.000 description 3
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 230000005764 inhibitory process Effects 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 235000020183 skimmed milk Nutrition 0.000 description 3
- 235000011149 sulphuric acid Nutrition 0.000 description 3
- 239000001117 sulphuric acid Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 241001660259 Cereus <cactus> Species 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000011534 incubation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000523 sample Substances 0.000 description 2
- 235000013599 spices Nutrition 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- CWVRJTMFETXNAD-FWCWNIRPSA-N 3-O-Caffeoylquinic acid Natural products O[C@H]1[C@@H](O)C[C@@](O)(C(O)=O)C[C@H]1OC(=O)\C=C\C1=CC=C(O)C(O)=C1 CWVRJTMFETXNAD-FWCWNIRPSA-N 0.000 description 1
- 240000007087 Apium graveolens Species 0.000 description 1
- 235000015849 Apium graveolens Dulce Group Nutrition 0.000 description 1
- 235000010591 Appio Nutrition 0.000 description 1
- 241000301512 Bacillus cereus ATCC 14579 Species 0.000 description 1
- PZIRUHCJZBGLDY-UHFFFAOYSA-N Caffeoylquinic acid Natural products CC(CCC(=O)C(C)C1C(=O)CC2C3CC(O)C4CC(O)CCC4(C)C3CCC12C)C(=O)O PZIRUHCJZBGLDY-UHFFFAOYSA-N 0.000 description 1
- 240000000467 Carum carvi Species 0.000 description 1
- 235000005747 Carum carvi Nutrition 0.000 description 1
- 241000235646 Cyberlindnera jadinii Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000191070 Escherichia coli ATCC 8739 Species 0.000 description 1
- 241001522878 Escherichia coli B Species 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- CWVRJTMFETXNAD-KLZCAUPSSA-N Neochlorogenin-saeure Natural products O[C@H]1C[C@@](O)(C[C@@H](OC(=O)C=Cc2ccc(O)c(O)c2)[C@@H]1O)C(=O)O CWVRJTMFETXNAD-KLZCAUPSSA-N 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 150000001558 benzoic acid derivatives Chemical class 0.000 description 1
- WHGYBXFWUBPSRW-FOUAGVGXSA-N beta-cyclodextrin Chemical compound OC[C@H]([C@H]([C@@H]([C@H]1O)O)O[C@H]2O[C@@H]([C@@H](O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O[C@H]3O[C@H](CO)[C@H]([C@@H]([C@H]3O)O)O3)[C@H](O)[C@H]2O)CO)O[C@@H]1O[C@H]1[C@H](O)[C@@H](O)[C@@H]3O[C@@H]1CO WHGYBXFWUBPSRW-FOUAGVGXSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- CWVRJTMFETXNAD-JUHZACGLSA-N chlorogenic acid Chemical compound O[C@@H]1[C@H](O)C[C@@](O)(C(O)=O)C[C@H]1OC(=O)\C=C\C1=CC=C(O)C(O)=C1 CWVRJTMFETXNAD-JUHZACGLSA-N 0.000 description 1
- 229940074393 chlorogenic acid Drugs 0.000 description 1
- FFQSDFBBSXGVKF-KHSQJDLVSA-N chlorogenic acid Natural products O[C@@H]1C[C@](O)(C[C@@H](CC(=O)C=Cc2ccc(O)c(O)c2)[C@@H]1O)C(=O)O FFQSDFBBSXGVKF-KHSQJDLVSA-N 0.000 description 1
- 235000001368 chlorogenic acid Nutrition 0.000 description 1
- BMRSEYFENKXDIS-KLZCAUPSSA-N cis-3-O-p-coumaroylquinic acid Natural products O[C@H]1C[C@@](O)(C[C@@H](OC(=O)C=Cc2ccc(O)cc2)[C@@H]1O)C(=O)O BMRSEYFENKXDIS-KLZCAUPSSA-N 0.000 description 1
- 239000010634 clove oil Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 125000004177 diethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000012470 diluted sample Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- XEKOWRVHYACXOJ-UHFFFAOYSA-N ethyl acetate Substances CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- ACGUYXCXAPNIKK-UHFFFAOYSA-N hexachlorophene Chemical compound OC1=C(Cl)C=C(Cl)C(Cl)=C1CC1=C(O)C(Cl)=CC(Cl)=C1Cl ACGUYXCXAPNIKK-UHFFFAOYSA-N 0.000 description 1
- 229960004068 hexachlorophene Drugs 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- -1 methylene - Chemical class 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000005445 natural material Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- VUXSPDNLYQTOSY-UHFFFAOYSA-N phenylmercuric borate Chemical compound OB(O)O[Hg]C1=CC=CC=C1 VUXSPDNLYQTOSY-UHFFFAOYSA-N 0.000 description 1
- 229960000247 phenylmercuric borate Drugs 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000004291 sulphur dioxide Substances 0.000 description 1
- 235000010269 sulphur dioxide Nutrition 0.000 description 1
- 235000018553 tannin Nutrition 0.000 description 1
- 229920001864 tannin Polymers 0.000 description 1
- 239000001648 tannin Substances 0.000 description 1
- 231100000027 toxicology Toxicity 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N65/00—Biocides, pest repellants or attractants, or plant growth regulators containing material from algae, lichens, bryophyta, multi-cellular fungi or plants, or extracts thereof
- A01N65/08—Magnoliopsida [dicotyledons]
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B2/00—Preservation of foods or foodstuffs, in general
- A23B2/70—Preservation of foods or foodstuffs, in general by treatment with chemicals
- A23B2/725—Preservation of foods or foodstuffs, in general by treatment with chemicals in the form of liquids or solids
- A23B2/729—Organic compounds; Microorganisms; Enzymes
- A23B2/733—Compounds of undetermined constitution obtained from animals or plants
-
- 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
- A23F5/20—Reducing or removing alkaloid content; Preparations produced thereby; Extracts or infusions thereof
- A23F5/206—Reducing or removing alkaloid content; Preparations produced thereby; Extracts or infusions thereof by extraction of the beans with selective solvents other than water or aqueous bean extracts, including supercritical gases
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- General Health & Medical Sciences (AREA)
- Biotechnology (AREA)
- Agronomy & Crop Science (AREA)
- Natural Medicines & Medicinal Plants (AREA)
- Microbiology (AREA)
- Mycology (AREA)
- Plant Pathology (AREA)
- Dentistry (AREA)
- Environmental Sciences (AREA)
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Dairy Products (AREA)
- Tea And Coffee (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
A process for protecting organic materials such as food-grade materials with a bacteriostatic agent, wherein an extract obtained from unroasted coffee is used as the bacteriostatic agent.
A process for protecting organic materials such as food-grade materials with a bacteriostatic agent, wherein an extract obtained from unroasted coffee is used as the bacteriostatic agent.
Description
~043Z5~ :
This invention relates to a process for protecting organic materials, more especially food-grade materials, by means of a bacteriostatic agent extracted from unroasted coffee.
It is known that the growth of bacteria on or in organic materials can be ret~rded and even completely I inhibited by the addition of a bacteriostatic agent. There I are a large number of active substances which are suitable ! f4r this purpose, including for example phenyl mercuricborate, hexachlorophene, sulphur dioxide, benzoates. --Unfortunately, problems are involved in the use of substances of this kind in the food industry (toxicology, laws, etc.).
It is for this reason that the food industry has turned towards natural substances or extracts. Various bacteriostatic agents hav~ been prepared from plants, above all from spices, for example from celery oil~ caraway oll, clove oil, etc.
Unfortunately, spices being by de~hition materials with distinctive flavours and odours, it is almost impossible ~;
to prepare by extraction bacteriostatic agents completely free of any organoleptic component. In addition~ these l agents are not very artive or, more preclsely, if they are very active, their activity is highly specific and they have ~,~ to be used in considerable quantities. As a result, they impart their flavour and odour to the food-grade products to which they are added.
The present invention relates to a process for protecting organic materials, especially food-grade materi~ls, by means of a bacteriostatic agent of remarkable activity which, ; .',` . . ' . .' ~` . }
l ~ - 2 -'1 .:
~C)43;~Sl ~:
organoleptically, does not betray its origins. The process according to the invention is distinguished by the fact that an extract obtained from unroasted ~ffee is used as the bacteriostatic agent.
This bacteriostatic agent is obtained by treating coffee waxes, that is to say the film of fat surrounding -the grain of unroasted coffee. The waxes themselves do not -have any significant bacteriostatic effect because the bacteriostatic agent present in them is too diluted. It is for this reason that the bacteriostatic agent is isolated by the treatment referred to above which comprises at least one so-called acid-base extraction of the type normally applied in the field of chemistry, for example a distribution , between a solvent phase and a basic aqueous phase, followed after decantation and separation by acidification of the basic aqueous phase and then by distribution between a ;
solvent phase and the aqueous phase thus acidlfied, separation of the solvent phase and evaporation of the solvent in cases where it is desired to recover the bacteriostatic agent in dry form. In one advantageous ;
method of extraction, the caffeine present in the unroasted ;
coffee is simultaneously extracted by any known decaffeination process using a solvent, after which the caffeine extraction residue is treated by a process ~5 comprising various purifications to eliminate the caffeine, ~;
and an acid-base extraction such as, for example, the acid-;;;
base extraction defined above.
The residue obtained in this way represents the bacteriostatic agent. It has an oily consistency, is yellowish to brownish in colour, has a moderate inherent .; . : ~.
~.~43Z~
taste and odour and is perfectly edible. It shows remarkable bacteriostatic activity which is governed to some extent by the method ~ extraction used and~ in particular, ~y the type of solvent(s) used. It is possible to use a wide variety of soIvents, such as methylene chloride, hexane, -ethyl acetate, although the best effects are achieved with `~
agents obtained by extraction with diethyl and diisopropyl ethers.
The results of preliminary chromatographic tests show that this bacteriostatic agent is in the form of a complex mixture of several substances of unknown type. In addition, it would seem that most of the bacteriostatic power derives `
from one or two substances and not from all the constituent substances of this mixture. Owing to its method of preparation, the whole has an acld character, but is non-phenolic in ~ I
nature, as shown by the negative results of ferric chloride tests, so that the substance!s in question are not tannins.
Providing it is not stored in dry form, the agent is stable at temperatures of up to approximately 60C and keeps well in air.
The bacteriostatic agent may be added to finished organic ! materials, more especially to food-grade materials ready for consumption, in quantitles by weight of at least 0.15 7O~
i i.e. 1.5 mg of dry agent per g of dry materials. In the case ~;
I ~ 25 of-a processed material, addition of the agent may thus form ¦ the last stage in the manufacturing process or may be made at any stage during manufacture, so that the agent is unable ¦~ to undergo any changes as a result. It may be added for example in solution or emulsion in a suitable carrier or ~,~ 30 solvent. The quantities normally used are sllghtly greater ~ ;
1: . . . .
~ -:
~432~
than the minimum dose by which bacterial growth is inhibited, for example 2 times greater, and have to be adapted according to the particular type of material to be protected and to the environmental conditions, especially the climatic conditions. -~
In addition, the bacteriostatic agent may be used as a bactericide, the doses required in that case being approximately 3 times greater. When used in doses of this order,the bacteriostatic agent, which has only a slight odour and .. . .
flavour, is too dilute to impart its odour and flavour to ;~
the food-grade material.
This agent may of course be added in admixture with other substances, such as antioxidants, flavourings, colorants, etc. Finally, where practical requirements dict~e, it is possible to treat only part of the organic material with the bacteriostatic agent in one form or another and then to mix the material thus treated with the ;~
rest of the u~treated material. It is then advisable to sub~ect the mixture to careful homogenisation.
In one preferred embodiment of the process according to ;~
the invention, the bacteriostatic agent is added in such a way that its concentration in the end food product is in the range from 0.15 to 0.6 %, i.e. in the range rom1.5 to 6 mg of dry agent per g of dry materials.
In a first modification of this embodiment, the bacteriostatic agent is prepared by directly treating unroasted caffee with methylene chloride in a quantity of ;~ approximately 10p~rts by weight of methylene chloride to 1 part by weight of unroasted coffee. Evaporation of the methylene chloride leaves a greasy residue which is taken ;
up in an aqueous alkaline soda solution with a pH-value of . :
";';
~L04;3Z~
from 10 to 12. After vigorous stirring at a temperature in ;
the range from 20 to 30C, the product is decanted and the supernatant fat phase is separated off. The aqueous phase -is then æ~ified with a 1 N to 5 N sulphuric acid solution until a pH-value in the range from 1 to 2 is obtained.
This acidified aqueous phase is then extracted with diethyl ether or diisopropyl ether, for example with 3 times the same volume of diisopropyl ether, after which the bacteriostatlic ~
agent is recovered by evaporating the ether, optionally :
after drying with an anhydrous salt. It is preferred to keep the agent in solution, even in concentrated solution, rather than in dry form. In this case, the ether does not have to be evaporated to dryness, or the bacteriostatic agent ls redissolved, for example in alcohol. It is also possible before evaporation to change the solvent, for example by adding alcohol to the ethereal phase, removing the ether and optionally concentrating the alcoholic phase containing the bacteriostatic agent.
In a second modification of this embodiment, the decaffeination residues obtained for example by treating previously moistened unroasted coffee with methylene -~
chloride are used as starti~g material. It is known that the water thus applied to the coffee beans makes them swell and, at the same time, causes the caffeine~chlorogenic acid complex to dissociate. Accordingly, the caffeine accompanies the waxes into the methylene chloride, so that evaporation of the methylene chloride leaves a fatty residue rich both in crystallised caffeine and in water. It is then possible as required either to filter the undissolved caffeine, to separate the waxes from the aqueous phase and then to treat ~
'" ':
., ~ - .
'' '' ' ' '~ ' ", .
J, ~ 4 3 ZS ~
, the waxes thus separated with an alkaline solution, or to take up the residue in an acid solution of pH 1 - 2, to separate ~1 the waxes from the aqueous acid phase, in which the caffeine ¦ is dissolved, and then to treat the waxes with an alkaline solution, or even to combine the purification processes described above. In both cases, the treatment by which the ~` bacteriostatic agent is isolated is with advantage continued in the same way as described earlier on in reference to the first embodiment. These operations involving crystallisation or dissolution in acid medium m~y of course be repeated as many times as necessary in order suitably to remove the ~ caffeine before the alkaline treatment of the waxes.
;j The process according to the invention is illustrated by the following Examples. Examples 1 and 2 relate to the extraction of the bacteriostatic agent, Example 3 describes the tests demonstrating the bacteriostatic power of the agent, ~ while Example 4 demonstrate~:J the efectiveness of the ! bacteriostatic ~gent in prolecting food-grade materials i against microbial growth.
j 20 EXAMPLE 1 240 kg of unroasted coffee beans are treated with vigorous stirring at 20C with 3 separate 800 litre batches of methylene chloride. These 3 volumes of liquid phase are combined and the methylene chloride removed in vacuo, leaving ; 25 2.5 kg of a greasy resîdue greenish in colour with an odour -j;~ of unroasted coffee which is immediately treated with 10 litres, and then 8 litres and then another 8 litres of a 0.05 N aqueous soda solution at a temperature of 25C.
After each operation, the mixture is left to settle, after which the supernatant fatty phase is separated from the .i ,. .
1~)4L3ZSl aqueous phase. These 3 volumes of aqueous alkaline phase are then com~ined and then acidified to pH 1 with 0.3 litre of a 5 N sulphuric acid solution. This aqueous acidified phase is then extracted with 3 volumes of diethyl ether measuring ~5 litres, 20 litres and 20 litres, respectively, after which the 3 volumes of ethereal phase are combined. 10 litres of ethanol are then added to the ethereal phase, after which the ether is removed in vacuo at a temperature kept below 30C. Finally, most of the ethanol is evaporated in vacuo at a temperature of approximately 35C, leaving approximately -~
1 litre of an alcoholic solution containing 18 g of bacterio- ~;
static agent which is maintained in this form. -. . .
60 kg of water are added to 240 kg of unroasted coffee beans at a temperature of 60C and under a pressure of 1.5 ~
atms. After a contact time of 1 hour, the pressure is ~ ;
reduced to 1 atm and the swollen beans are treated with 6 times320 litres of methylerle chloride. These 6 volumes of liquid phase are combined, after which the methylene chloride is removed in vacuo, leaving 10~2 kg of a non-homogeneous brown-green mixture, with the odour of unroasted coffee, consisting af a fatty phaseand an aqueous phase containing crystals of caffeine. The caffeine is removed by filtration :
(2.5 kg). The two liquid phases are then separated, followed by the successive addition to the fattyFhase of 3 separate -~
12.5 litre batches of a 0.05 N sulphuric acid solution.
After each operation, the mixture is left to seffle~ the two phases are separated and the fatty phase recovered.
On completion of these purify:ing operations, the fatty phase no longer contains caffeine. It is then treated with 10 litres , ,.......
"~;'': ' .
:: .
ZS~L
of a 0.05 N aqueous soda solution, and separation of the bacteriostatic agent is continued in the same way as described in Example 1, except that diisopropyl ether is used as the extraction solvent. The proportions of solvent used are the same or equivalent. 1 litre of an alcoholic solution containing 20 g of bacteriostatic agent is thus obtained, the bacteriostatic agent being maintained in that form.
j The bacteriostatic activity of the agent was assessed by the minimum inhibition concentration method ~ the - -Public Health Laboratory Service Committee described in British Med. J. 408 (1965).
Five cultures of the following microorganisms are prepared:
bacteria Escherichia coli ATCC 8739 Staphylt~lcoccus aureus ATCC 155 ~ ynas aeru~osa ATCC 10145 Bacillus cereus ATCC 14579 yeast Candida utilis CBS 567 containing approximately 2.108 cells/ml of nutrient medium (culture time approximately 24 hours).
At the same time, samples of the bacteriostatic agent to be tested are prepared by dilution from a mother suspension (2 g/100 ml, i.e. 2/100) in ethanol. 1 ml of water is added to a first 1 ml sample of this mother suspension, 2 ml of wate~ are added to a second sample ~; and so on, so as to obtain a series ranging in dilution from 1/100 to 1/300, after which this intermediate series and the initial mother suspension are diluted 10 times with the nutrient medium of m~roorganisms. A series of test :
- 9 ~ ~
'.
1 ~ ~ 3 Z 5 samples ranging in dilution from 1/500 to 1/3000 is prepared in this way.
0.2 ml of each of the aforementioned microorganism cultures are then added to 10 ml of each of the diluted samples thus prepared. This is followed by incubation for 24 hours at 30C for the bacteria and at 35C for the yeast, after which the optical density of the mixture is measured -~
at 600 nm and compared with the optical density of reference I -samples. ~; -Here now are the minimum inhibition concentrations found for the "diisopropylic" agent prepared in Example 2:
1/2500 against Ps. aeru~inosa .
1/1000 against E coli, Staph. aureus, B cereus no bacteriostatic activity against C utilis 1 15 The minimum inhibition concentrations for the "diethylic" agent prepared in Example 1 are approximately
This invention relates to a process for protecting organic materials, more especially food-grade materials, by means of a bacteriostatic agent extracted from unroasted coffee.
It is known that the growth of bacteria on or in organic materials can be ret~rded and even completely I inhibited by the addition of a bacteriostatic agent. There I are a large number of active substances which are suitable ! f4r this purpose, including for example phenyl mercuricborate, hexachlorophene, sulphur dioxide, benzoates. --Unfortunately, problems are involved in the use of substances of this kind in the food industry (toxicology, laws, etc.).
It is for this reason that the food industry has turned towards natural substances or extracts. Various bacteriostatic agents hav~ been prepared from plants, above all from spices, for example from celery oil~ caraway oll, clove oil, etc.
Unfortunately, spices being by de~hition materials with distinctive flavours and odours, it is almost impossible ~;
to prepare by extraction bacteriostatic agents completely free of any organoleptic component. In addition~ these l agents are not very artive or, more preclsely, if they are very active, their activity is highly specific and they have ~,~ to be used in considerable quantities. As a result, they impart their flavour and odour to the food-grade products to which they are added.
The present invention relates to a process for protecting organic materials, especially food-grade materi~ls, by means of a bacteriostatic agent of remarkable activity which, ; .',` . . ' . .' ~` . }
l ~ - 2 -'1 .:
~C)43;~Sl ~:
organoleptically, does not betray its origins. The process according to the invention is distinguished by the fact that an extract obtained from unroasted ~ffee is used as the bacteriostatic agent.
This bacteriostatic agent is obtained by treating coffee waxes, that is to say the film of fat surrounding -the grain of unroasted coffee. The waxes themselves do not -have any significant bacteriostatic effect because the bacteriostatic agent present in them is too diluted. It is for this reason that the bacteriostatic agent is isolated by the treatment referred to above which comprises at least one so-called acid-base extraction of the type normally applied in the field of chemistry, for example a distribution , between a solvent phase and a basic aqueous phase, followed after decantation and separation by acidification of the basic aqueous phase and then by distribution between a ;
solvent phase and the aqueous phase thus acidlfied, separation of the solvent phase and evaporation of the solvent in cases where it is desired to recover the bacteriostatic agent in dry form. In one advantageous ;
method of extraction, the caffeine present in the unroasted ;
coffee is simultaneously extracted by any known decaffeination process using a solvent, after which the caffeine extraction residue is treated by a process ~5 comprising various purifications to eliminate the caffeine, ~;
and an acid-base extraction such as, for example, the acid-;;;
base extraction defined above.
The residue obtained in this way represents the bacteriostatic agent. It has an oily consistency, is yellowish to brownish in colour, has a moderate inherent .; . : ~.
~.~43Z~
taste and odour and is perfectly edible. It shows remarkable bacteriostatic activity which is governed to some extent by the method ~ extraction used and~ in particular, ~y the type of solvent(s) used. It is possible to use a wide variety of soIvents, such as methylene chloride, hexane, -ethyl acetate, although the best effects are achieved with `~
agents obtained by extraction with diethyl and diisopropyl ethers.
The results of preliminary chromatographic tests show that this bacteriostatic agent is in the form of a complex mixture of several substances of unknown type. In addition, it would seem that most of the bacteriostatic power derives `
from one or two substances and not from all the constituent substances of this mixture. Owing to its method of preparation, the whole has an acld character, but is non-phenolic in ~ I
nature, as shown by the negative results of ferric chloride tests, so that the substance!s in question are not tannins.
Providing it is not stored in dry form, the agent is stable at temperatures of up to approximately 60C and keeps well in air.
The bacteriostatic agent may be added to finished organic ! materials, more especially to food-grade materials ready for consumption, in quantitles by weight of at least 0.15 7O~
i i.e. 1.5 mg of dry agent per g of dry materials. In the case ~;
I ~ 25 of-a processed material, addition of the agent may thus form ¦ the last stage in the manufacturing process or may be made at any stage during manufacture, so that the agent is unable ¦~ to undergo any changes as a result. It may be added for example in solution or emulsion in a suitable carrier or ~,~ 30 solvent. The quantities normally used are sllghtly greater ~ ;
1: . . . .
~ -:
~432~
than the minimum dose by which bacterial growth is inhibited, for example 2 times greater, and have to be adapted according to the particular type of material to be protected and to the environmental conditions, especially the climatic conditions. -~
In addition, the bacteriostatic agent may be used as a bactericide, the doses required in that case being approximately 3 times greater. When used in doses of this order,the bacteriostatic agent, which has only a slight odour and .. . .
flavour, is too dilute to impart its odour and flavour to ;~
the food-grade material.
This agent may of course be added in admixture with other substances, such as antioxidants, flavourings, colorants, etc. Finally, where practical requirements dict~e, it is possible to treat only part of the organic material with the bacteriostatic agent in one form or another and then to mix the material thus treated with the ;~
rest of the u~treated material. It is then advisable to sub~ect the mixture to careful homogenisation.
In one preferred embodiment of the process according to ;~
the invention, the bacteriostatic agent is added in such a way that its concentration in the end food product is in the range from 0.15 to 0.6 %, i.e. in the range rom1.5 to 6 mg of dry agent per g of dry materials.
In a first modification of this embodiment, the bacteriostatic agent is prepared by directly treating unroasted caffee with methylene chloride in a quantity of ;~ approximately 10p~rts by weight of methylene chloride to 1 part by weight of unroasted coffee. Evaporation of the methylene chloride leaves a greasy residue which is taken ;
up in an aqueous alkaline soda solution with a pH-value of . :
";';
~L04;3Z~
from 10 to 12. After vigorous stirring at a temperature in ;
the range from 20 to 30C, the product is decanted and the supernatant fat phase is separated off. The aqueous phase -is then æ~ified with a 1 N to 5 N sulphuric acid solution until a pH-value in the range from 1 to 2 is obtained.
This acidified aqueous phase is then extracted with diethyl ether or diisopropyl ether, for example with 3 times the same volume of diisopropyl ether, after which the bacteriostatlic ~
agent is recovered by evaporating the ether, optionally :
after drying with an anhydrous salt. It is preferred to keep the agent in solution, even in concentrated solution, rather than in dry form. In this case, the ether does not have to be evaporated to dryness, or the bacteriostatic agent ls redissolved, for example in alcohol. It is also possible before evaporation to change the solvent, for example by adding alcohol to the ethereal phase, removing the ether and optionally concentrating the alcoholic phase containing the bacteriostatic agent.
In a second modification of this embodiment, the decaffeination residues obtained for example by treating previously moistened unroasted coffee with methylene -~
chloride are used as starti~g material. It is known that the water thus applied to the coffee beans makes them swell and, at the same time, causes the caffeine~chlorogenic acid complex to dissociate. Accordingly, the caffeine accompanies the waxes into the methylene chloride, so that evaporation of the methylene chloride leaves a fatty residue rich both in crystallised caffeine and in water. It is then possible as required either to filter the undissolved caffeine, to separate the waxes from the aqueous phase and then to treat ~
'" ':
., ~ - .
'' '' ' ' '~ ' ", .
J, ~ 4 3 ZS ~
, the waxes thus separated with an alkaline solution, or to take up the residue in an acid solution of pH 1 - 2, to separate ~1 the waxes from the aqueous acid phase, in which the caffeine ¦ is dissolved, and then to treat the waxes with an alkaline solution, or even to combine the purification processes described above. In both cases, the treatment by which the ~` bacteriostatic agent is isolated is with advantage continued in the same way as described earlier on in reference to the first embodiment. These operations involving crystallisation or dissolution in acid medium m~y of course be repeated as many times as necessary in order suitably to remove the ~ caffeine before the alkaline treatment of the waxes.
;j The process according to the invention is illustrated by the following Examples. Examples 1 and 2 relate to the extraction of the bacteriostatic agent, Example 3 describes the tests demonstrating the bacteriostatic power of the agent, ~ while Example 4 demonstrate~:J the efectiveness of the ! bacteriostatic ~gent in prolecting food-grade materials i against microbial growth.
j 20 EXAMPLE 1 240 kg of unroasted coffee beans are treated with vigorous stirring at 20C with 3 separate 800 litre batches of methylene chloride. These 3 volumes of liquid phase are combined and the methylene chloride removed in vacuo, leaving ; 25 2.5 kg of a greasy resîdue greenish in colour with an odour -j;~ of unroasted coffee which is immediately treated with 10 litres, and then 8 litres and then another 8 litres of a 0.05 N aqueous soda solution at a temperature of 25C.
After each operation, the mixture is left to settle, after which the supernatant fatty phase is separated from the .i ,. .
1~)4L3ZSl aqueous phase. These 3 volumes of aqueous alkaline phase are then com~ined and then acidified to pH 1 with 0.3 litre of a 5 N sulphuric acid solution. This aqueous acidified phase is then extracted with 3 volumes of diethyl ether measuring ~5 litres, 20 litres and 20 litres, respectively, after which the 3 volumes of ethereal phase are combined. 10 litres of ethanol are then added to the ethereal phase, after which the ether is removed in vacuo at a temperature kept below 30C. Finally, most of the ethanol is evaporated in vacuo at a temperature of approximately 35C, leaving approximately -~
1 litre of an alcoholic solution containing 18 g of bacterio- ~;
static agent which is maintained in this form. -. . .
60 kg of water are added to 240 kg of unroasted coffee beans at a temperature of 60C and under a pressure of 1.5 ~
atms. After a contact time of 1 hour, the pressure is ~ ;
reduced to 1 atm and the swollen beans are treated with 6 times320 litres of methylerle chloride. These 6 volumes of liquid phase are combined, after which the methylene chloride is removed in vacuo, leaving 10~2 kg of a non-homogeneous brown-green mixture, with the odour of unroasted coffee, consisting af a fatty phaseand an aqueous phase containing crystals of caffeine. The caffeine is removed by filtration :
(2.5 kg). The two liquid phases are then separated, followed by the successive addition to the fattyFhase of 3 separate -~
12.5 litre batches of a 0.05 N sulphuric acid solution.
After each operation, the mixture is left to seffle~ the two phases are separated and the fatty phase recovered.
On completion of these purify:ing operations, the fatty phase no longer contains caffeine. It is then treated with 10 litres , ,.......
"~;'': ' .
:: .
ZS~L
of a 0.05 N aqueous soda solution, and separation of the bacteriostatic agent is continued in the same way as described in Example 1, except that diisopropyl ether is used as the extraction solvent. The proportions of solvent used are the same or equivalent. 1 litre of an alcoholic solution containing 20 g of bacteriostatic agent is thus obtained, the bacteriostatic agent being maintained in that form.
j The bacteriostatic activity of the agent was assessed by the minimum inhibition concentration method ~ the - -Public Health Laboratory Service Committee described in British Med. J. 408 (1965).
Five cultures of the following microorganisms are prepared:
bacteria Escherichia coli ATCC 8739 Staphylt~lcoccus aureus ATCC 155 ~ ynas aeru~osa ATCC 10145 Bacillus cereus ATCC 14579 yeast Candida utilis CBS 567 containing approximately 2.108 cells/ml of nutrient medium (culture time approximately 24 hours).
At the same time, samples of the bacteriostatic agent to be tested are prepared by dilution from a mother suspension (2 g/100 ml, i.e. 2/100) in ethanol. 1 ml of water is added to a first 1 ml sample of this mother suspension, 2 ml of wate~ are added to a second sample ~; and so on, so as to obtain a series ranging in dilution from 1/100 to 1/300, after which this intermediate series and the initial mother suspension are diluted 10 times with the nutrient medium of m~roorganisms. A series of test :
- 9 ~ ~
'.
1 ~ ~ 3 Z 5 samples ranging in dilution from 1/500 to 1/3000 is prepared in this way.
0.2 ml of each of the aforementioned microorganism cultures are then added to 10 ml of each of the diluted samples thus prepared. This is followed by incubation for 24 hours at 30C for the bacteria and at 35C for the yeast, after which the optical density of the mixture is measured -~
at 600 nm and compared with the optical density of reference I -samples. ~; -Here now are the minimum inhibition concentrations found for the "diisopropylic" agent prepared in Example 2:
1/2500 against Ps. aeru~inosa .
1/1000 against E coli, Staph. aureus, B cereus no bacteriostatic activity against C utilis 1 15 The minimum inhibition concentrations for the "diethylic" agent prepared in Example 1 are approximately
2 times higher. ;
4 groups of 4 sterile samples af reconstituted skimmed 1 20 milk, i.e. a total of 16 samples, are prepared and then inoculated with the bacteria mentioned in Example 3 and ~:
protected against them by variable doses of the bacteriostatic agent prepared in Example 2. Evolution of the colonies of bacteria in the samples incubated at 30C is then measured ~; 25 as a function of time by a conventional counting method.
¦ The results are set out in the following Table:
~ ~ . ,,. '.. ..
1 ;`~
~; .'' '.'.
- 1 0 !~ , 'I : . . .
.1 , ', .
~C~43Z~L
. ~ .
number of bacteria present per ml of skimmed milk :
~ of _ incubation ba~rio- Staph. E. coli B. cereus Ps. ~
time in h static aureus aeru~inosa .
addned ... _ ... _ .. . ........................... .. __ (control) :
inocula- . .
tion) 0~5 160 740 60 170 2 170 850 40 230 ~.
. _. . :.0 3800 3000 3000 9200 :
(control) . .
4 0.5 1600 18000 2300 1600 . .. _ , -: ,, 06500 0000870000000 12000000 290000000 .' (control)¦
. 0.5g20000 300000 300000 340000 2200 10 20 1500 :
. . _ * ' _ _ ., ', (control)¦ :
0.5140000000460000000 5800000 300000000 24 11 oooboooo300000000 6500000 140000000 , ~_ . 2¦ 150 10 10 120000000 :` :
. . .
* coagulated samples . .~
,.
..
In the above Table, the percentages of bacteriostatic ~.
agent added are percent of a 3 % ethanolic solution of that agent in skimmed milk which itself has a solids content :. :
of approximately 10 %. Accordingly, these percentages express the following quantities by weight:
0.5 % = O.S ml/100 ml = 1.5 mg/g of solids 1 % = 1 ml/100 ml = 3 mg/g of solids 2 % = 2 ml/100 ml = 6 mg/g of solids Naturally the figures quoted in the above Table are -by no means precise and are to be considered above all as orders of magnitude. Nevertheless it can be seen that :
the bacteriostatic agent is extremely effective in inhibiting ;:
¦ bacterial growth, except perhaps in the long term with ¦ respect ~ Ps. aeruginosa, for this particular substrate of ¦ 15 skimmed milk.
. ,'' ~ ''' -..........
~ ~.
`...~
. , ,~
"."' ";
.' '.
,~ - 12 -~ ,:
'`~ ' ' ~; .' . . .
4 groups of 4 sterile samples af reconstituted skimmed 1 20 milk, i.e. a total of 16 samples, are prepared and then inoculated with the bacteria mentioned in Example 3 and ~:
protected against them by variable doses of the bacteriostatic agent prepared in Example 2. Evolution of the colonies of bacteria in the samples incubated at 30C is then measured ~; 25 as a function of time by a conventional counting method.
¦ The results are set out in the following Table:
~ ~ . ,,. '.. ..
1 ;`~
~; .'' '.'.
- 1 0 !~ , 'I : . . .
.1 , ', .
~C~43Z~L
. ~ .
number of bacteria present per ml of skimmed milk :
~ of _ incubation ba~rio- Staph. E. coli B. cereus Ps. ~
time in h static aureus aeru~inosa .
addned ... _ ... _ .. . ........................... .. __ (control) :
inocula- . .
tion) 0~5 160 740 60 170 2 170 850 40 230 ~.
. _. . :.0 3800 3000 3000 9200 :
(control) . .
4 0.5 1600 18000 2300 1600 . .. _ , -: ,, 06500 0000870000000 12000000 290000000 .' (control)¦
. 0.5g20000 300000 300000 340000 2200 10 20 1500 :
. . _ * ' _ _ ., ', (control)¦ :
0.5140000000460000000 5800000 300000000 24 11 oooboooo300000000 6500000 140000000 , ~_ . 2¦ 150 10 10 120000000 :` :
. . .
* coagulated samples . .~
,.
..
In the above Table, the percentages of bacteriostatic ~.
agent added are percent of a 3 % ethanolic solution of that agent in skimmed milk which itself has a solids content :. :
of approximately 10 %. Accordingly, these percentages express the following quantities by weight:
0.5 % = O.S ml/100 ml = 1.5 mg/g of solids 1 % = 1 ml/100 ml = 3 mg/g of solids 2 % = 2 ml/100 ml = 6 mg/g of solids Naturally the figures quoted in the above Table are -by no means precise and are to be considered above all as orders of magnitude. Nevertheless it can be seen that :
the bacteriostatic agent is extremely effective in inhibiting ;:
¦ bacterial growth, except perhaps in the long term with ¦ respect ~ Ps. aeruginosa, for this particular substrate of ¦ 15 skimmed milk.
. ,'' ~ ''' -..........
~ ~.
`...~
. , ,~
"."' ";
.' '.
,~ - 12 -~ ,:
'`~ ' ' ~; .' . . .
Claims (7)
EXCLUSIVE PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for protecting organic materials with a bacteriostatic agent, which comprises adding to said materials an extract obtained from unroasted coffee by acid-base extraction as the bacteriostatic agent in a quantity of at least 1.5 mg/g of dry materials.
2. A process as claimed in claim 1, wherein the organic materials are food-grade materials.
3. A process as claimed in claim 11 wherein the bacteriostatic agent is added in a quantity of from 1.5 to 6 mg/g of dry materials.
4. A process as claimed in claim 1, wherein an extract obtained from decaffeination residues of unroasted coffee by acid-base extraction is added as the bacteriostatic agent.
5. A process as claimed in claim 1, wherein an extract obtained by acid-base extraction, in which the basic aqueous phase has a pH-value in the range from 10 to 12, is added as the bacteriostatic agent.
6. A process as claimed in claim 1, wherein an extract obtained by acid-base extraction, in which the aqueous acid phase has a pH-value in the range from 1 to 2, is added as the bacteriostatic agent.
7. A process as claimed in claim 1, wherein an extract obtained by acid-base extraction, in which the solvent phase is diethyl ether or diisopropyl ether, is added as the bacteriostatic agent.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH490774A CH586023A5 (en) | 1974-04-08 | 1974-04-08 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1043251A true CA1043251A (en) | 1978-11-28 |
Family
ID=4284609
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA221,892A Expired CA1043251A (en) | 1974-04-08 | 1975-03-12 | Process for protecting organic materials |
Country Status (11)
| Country | Link |
|---|---|
| JP (1) | JPS5411372B2 (en) |
| AR (1) | AR206813A1 (en) |
| CA (1) | CA1043251A (en) |
| CH (1) | CH586023A5 (en) |
| DE (1) | DE2425215C3 (en) |
| ES (1) | ES436347A1 (en) |
| FR (1) | FR2266465B1 (en) |
| GB (1) | GB1458795A (en) |
| NL (1) | NL7502482A (en) |
| OA (1) | OA04863A (en) |
| ZA (1) | ZA751106B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2705510A1 (en) * | 1977-02-10 | 1978-08-17 | Heinz Hoelter | Odoriferous garden pest repellent - contains coffee wax, pref. in soln. e.g. in xylene |
| JPS63230060A (en) * | 1987-03-18 | 1988-09-26 | Yamamoto Shokuhin Kenkyusho:Kk | Preservative and deodorant for food |
| JP3514636B2 (en) * | 1998-08-21 | 2004-03-31 | 株式会社大貴 | Sanitary sheets and manufacturing method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1668236C3 (en) * | 1968-01-11 | 1979-10-18 | Hag Ag, 2800 Bremen | Process for the extraction of antioxidants from green coffee beans and their use to protect autoxidizable foods |
-
1974
- 1974-04-08 CH CH490774A patent/CH586023A5/xx not_active IP Right Cessation
- 1974-05-24 DE DE2425215A patent/DE2425215C3/en not_active Expired
-
1975
- 1975-01-01 AR AR258191A patent/AR206813A1/en active
- 1975-02-21 ZA ZA00751106A patent/ZA751106B/en unknown
- 1975-02-24 GB GB760275A patent/GB1458795A/en not_active Expired
- 1975-02-28 FR FR7506380A patent/FR2266465B1/fr not_active Expired
- 1975-03-03 NL NL7502482A patent/NL7502482A/en unknown
- 1975-03-12 CA CA221,892A patent/CA1043251A/en not_active Expired
- 1975-03-20 OA OA55443A patent/OA04863A/en unknown
- 1975-04-07 JP JP4214475A patent/JPS5411372B2/ja not_active Expired
- 1975-04-07 ES ES436347A patent/ES436347A1/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE2425215B2 (en) | 1981-07-23 |
| ZA751106B (en) | 1976-01-28 |
| DE2425215C3 (en) | 1987-06-19 |
| AU7974575A (en) | 1976-10-07 |
| DE2425215A1 (en) | 1975-10-09 |
| AR206813A1 (en) | 1976-08-23 |
| FR2266465B1 (en) | 1980-09-05 |
| JPS5411372B2 (en) | 1979-05-15 |
| ES436347A1 (en) | 1977-01-01 |
| OA04863A (en) | 1980-10-31 |
| GB1458795A (en) | 1976-12-15 |
| CH586023A5 (en) | 1977-03-31 |
| FR2266465A1 (en) | 1975-10-31 |
| NL7502482A (en) | 1975-10-10 |
| JPS50140626A (en) | 1975-11-11 |
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