WO2017131222A1 - High-pressure treatment method for coffee berries, method for producing product of high-pressure treatment of coffee berries, and treated product obtained therefrom - Google Patents

High-pressure treatment method for coffee berries, method for producing product of high-pressure treatment of coffee berries, and treated product obtained therefrom Download PDF

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Publication number
WO2017131222A1
WO2017131222A1 PCT/JP2017/003099 JP2017003099W WO2017131222A1 WO 2017131222 A1 WO2017131222 A1 WO 2017131222A1 JP 2017003099 W JP2017003099 W JP 2017003099W WO 2017131222 A1 WO2017131222 A1 WO 2017131222A1
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pressure
coffee fruit
coffee
pressure treatment
enzyme
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PCT/JP2017/003099
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French (fr)
Japanese (ja)
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賢 渡邉
猪股 宏
リチャード リー ジュニア スミス
保正 佐々木
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国立大学法人東北大学
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Priority to JP2017563886A priority Critical patent/JP6746169B2/en
Publication of WO2017131222A1 publication Critical patent/WO2017131222A1/en

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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23FCOFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
    • A23F5/00Coffee; Coffee substitutes; Preparations thereof
    • A23F5/02Treating green coffee; Preparations produced thereby

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  • the present invention relates to a high-pressure treatment method for coffee fruit, a method for producing a high-pressure treatment product of coffee fruit, and a treatment product obtained from the method.
  • Coffee fruit has a structure of outer skin, pulp, slimy inner skin (parchment), silver skin (silver skin), and seed (FIG. 1).
  • Raw beans from which the outer part of the seeds has been removed are roasted and ground and used as a coffee beverage.
  • the pulp and pulp such as pulp are peeled off with a remover (pulper), and after a fermentation process, the seeds are removed by washing and drying. It is known to go through a process. This is (1) a purification method called a washing method (washed method).
  • threshing without slimming without going through the fermentation process (2) Sumatra type (wet hull method) or drying and threshing with slimming without going through the fermentation process (3) Brazilian style (pulp Natural method), and simple (4) natural drying method (natural method) in which the harvested coffee berries are sufficiently dried and then threshed, and these methods have been developed for a long time in coffee fruit production areas. Also, coffees with different flavors are favored due to differences in purification methods and roasting methods.
  • Patent Document 1 discloses a method for treating coffee fruit with hot water before the refining step as a method for treating coffee fruit for improving the shelf life of the harvested coffee fruit.
  • Patent Document 2 discloses that the entire coffee fruit (including the seed part) is rapidly dried and ground to extract the active ingredient with water.
  • a method for separating high-molecular to low-molecular polysaccharides, polyphenol-based caffeic acid, caffeine, and the like by the SEC method (size exclusion chromatography method) is disclosed.
  • Patent Document 3 also discloses an edible composition containing an extract of edible substances, wherein the extract contains water at an extraction temperature of about 0 ° C. to about 80 ° C. and an extraction pressure of at least about 2000 bar. Said composition is disclosed which is obtained from the extraction of edible substances in a medium.
  • Patent Document 4 discloses a method for producing an edible extract product, which comprises pulverizing an edible raw material into particles, and extracting the edible raw material particles in water to produce an extract of the edible raw material. Filtering the edible raw material extract using at least one filter so that the concentration of chlorogenic acid in the edible raw material extract is increased and at the same time the concentration of fat in the edible raw material extract is decreased And producing the edible extract product by separating the resulting filter retentate from the filtered extract of the edible raw material, wherein the method of filtration of the edible raw material extract is disclosed.
  • the use of enzymes that aggregate carbohydrates by adding enzymes to the edible raw material extract has been disclosed.
  • the present invention is not only used as a quick coffee bean while suppressing spoilage after harvesting coffee fruits, but also obtains effective ingredients in foods and the like from the skin and pulp parts of pulp and the like. It is an object.
  • the present inventors have found a high-pressure treatment method for coffee fruit and a method for producing a high-pressure treated product that can suppress the decay and oxidative degradation of the components contained in the pulp part and the seed part by performing high-pressure treatment on the coffee fruit.
  • the present invention provides the following means.
  • a method for producing a high-pressure processed product of coffee fruit comprising a step of separating at least one processed product of a seed part and a part other than the seed part after the step of subjecting the coffee fruit to a high-pressure treatment of 10 to 1000 MPa.
  • a method for producing a high-pressure processed product of coffee fruit comprising: [2] The method includes a step of adding enzyme-added water containing 0.001 to 10% by mass of enzyme in a range of 100 mass times or less with respect to the mass of coffee fruit before the step of applying the high-pressure treatment.
  • the step of subjecting the coffee fruit to a high pressure treatment of 10 to 1000 MPa comprises a first step of charging the coffee fruit into a high pressure device and a second step of carrying out the pressure in the high pressure device in the range of 10 to 1000 MPa. 5.
  • a method for high-pressure treatment of coffee fruit comprising subjecting coffee fruit to a high-pressure treatment of 10 to 1000 MPa.
  • the item 10 above wherein the enzyme-added water containing 0.001 to 10% by mass is added in a range of 100 mass times or less with respect to the mass of the coffee fruit before the high-pressure treatment.
  • High pressure processing method for coffee berries [12] The method for high-pressure treatment of coffee fruit according to item 10 or 11, wherein the temperature is in the range of 30 to 120 ° C.
  • coffee fruit pulper pulverization treatment and fermentation treatment (usually 1 to 2 days) for removing slime (smilage), parchment (endocarp) ) Is not required as a separate process, and the coffee fruit refining process can be greatly shortened and the production cost can be reduced.
  • the cross-sectional schematic of a coffee fruit is shown.
  • the schematic process (an example) of the high pressure process of the coffee fruit based on embodiment of this invention is shown.
  • Prior art (1) The outline process of the processing method of the coffee bean by a washing type is shown.
  • schematic process of the processing method of the coffee bean by a prior art (3) Brazilian type (pulp-to-natural method) is shown.
  • the outline process of the processing method of the coffee bean by the prior art (4) natural drying type (natural method) is shown.
  • the typical chemical structure of chlorogenic acid is shown. It is an example of the external appearance photograph of the coffee fruit (raw material) used in the Example.
  • FIG. 1 shows a cross-sectional view of coffee fruit.
  • Coffee fruits are generally picked from red ripe fruits (cherries).
  • the fruit component comprises an outer skin 1, a lower pulp 2, a mule 3 made of mucous pectin, an inner pericarp parchment 4, and two seeds 5.
  • FIG. 2 shows the outline (an example) of the manufacturing method of the high pressure processed material of the coffee fruit which concerns on embodiment of this invention.
  • the collected coffee berries are placed in an apparatus capable of high-pressure treatment, and after high-pressure treatment, the seeds and jelly-like materials are separated from the treated product that has been liquefied (the jelly-like materials are entangled around the seeds). To do.
  • the seed is dried after washing and recovered as green beans, and the jelly-like product represents a process of separating a liquid (aqueous solution) derived from pulp, mulege, and fermented parchment.
  • the liquid substance contains a substance that is an effective component for plant fiber decomposition products, foods, and the like.
  • Separation of the beneficial component substance can be achieved by removing the fibrous decomposition product by employing a filtration method, a compression dehydration method, a centrifugal separation method, or the like, thereby obtaining an aqueous solution portion in which the active ingredient is dissolved. Furthermore, this aqueous solution part can be isolated and collected as an active ingredient substance using size exclusion chromatography (SEC method, gel filtration chromatography, etc.).
  • SEC method size exclusion chromatography
  • the invention according to an embodiment of the present invention is a method for producing a high-pressure treated product of coffee fruit, wherein after the step of subjecting the coffee fruit to a high-pressure treatment of 10 to 1000 MPa, at least one kind of part other than the seed part and the seed part is provided.
  • a method for producing a high-pressure processed product of coffee fruit comprising a step of separating the processed product.
  • the pressure for performing the high-pressure treatment may be a pressure exceeding normal temperature, and in order to exert a remarkable effect, the pressure is preferably in the range of 10 to 1000 MPa, more preferably in the range of 30 to 800 MPa, and more preferably in the range of 50 to 600 MPa. A range of is desirable.
  • the present invention by applying a high pressure treatment to coffee fruit, it is possible to suppress the decay of coffee fruit and fungi, and to activate the action of the coffee fruit enzyme having an autolytic enzyme, Compared to the techniques (1) to (4), it is possible to remove the outer skin, pulp, mules, parchment, etc. in a short time that is not comparable and with simple work processes. Moreover, the effect of the present invention is accelerated by positively supplementing the enzyme from the outside.
  • the enzyme-added water containing 0.001 to 10% by mass of enzyme is added in a range of 100 mass times or less with respect to the mass of coffee fruit before the high-pressure treatment step. A process may be included.
  • the coffee fruit brought from the normal production area is also put into tank water or the like also for sorting, and after sorting the garbage and washing the coffee fruit, it is transferred into a high-pressure treatment apparatus, and no water is used.
  • the high-pressure treatment is performed under addition or by adding a predetermined amount of water.
  • the amount of water added is preferably less than 10 times, more preferably less than 5 times, and preferably less than 3 times the mass of coffee fruit to be processed. If the amount of water exceeds 10 times the amount, the amount of liquid obtained after high-pressure treatment increases, resulting in the subsequent concentration of the aqueous solution containing the active ingredient requires a lot of energy and time. Isolation may be difficult.
  • the enzyme is preferably added before the high-pressure treatment step.
  • the enzyme is used in the range of 0.01 to 5% by mass relative to the dry solid mass of the coffee fruit. The range of 0.1 to 2% by mass is more desirable. If the amount of enzyme added is less than 0.01, the liquefaction action of pulp or the like may not be exhibited to the maximum, and if it exceeds 5 mass%, the production cost will be significantly increased.
  • the enzyme has a function of fermenting in a water tank to remove part of the pulp remaining in the parchment, and further, the fermentation reaction is promoted in a high-pressure environment. As a result, many useful fermentation components can be produced.
  • the treatment temperature during the high-pressure treatment is usually preferably in the range of 30 to 120 ° C, more preferably in the range of 30 to 100 ° C, and preferably in the range of 30 to 80 ° C. If the processing temperature is lower than 30 ° C., the effect of the present invention may be significantly reduced. Further, when the processing temperature exceeds 120 ° C., the time required for heating to cooling becomes longer, which may result in greatly affecting the production cost. However, in the treatment in the high temperature range above room temperature, the effect of “boiled” can be imparted to the coffee beans (seed part), and as a result, the high pressure treatment at the high temperature of the present invention is applied. As the components of raw beans are decomposed, sugars and amino acids increase, and as a beverage after roasting coffee beans, the richness and umami components are expected to increase.
  • a pH adjusting agent may be added when the high pressure treatment is performed.
  • the pH adjuster any pH adjuster used for food pH adjustment can be widely used. Examples include citric acid, trisodium citrate, sodium carbonate, phosphoric acid and phosphoric acid.
  • the pH adjuster is preferably one that can be adjusted in the range of pH 4-9.
  • the step of subjecting the coffee fruit to a high-pressure treatment of 10 to 1000 MPa includes a first step of charging the coffee fruit into the high-pressure device and a pressure in the high-pressure device of 10 to It consists of the 2nd process implemented in the range of 1000 MPa.
  • a method for producing a high-pressure processed product of coffee fruit is provided, in which new coffee fruits are added to the first step and the first step to the third step are sequentially repeated.
  • the processed material obtained from the manufacturing method of the high pressure processed material of the coffee fruit of this invention is provided. Furthermore, the present invention provides a method for high-pressure treatment of coffee fruit, characterized by subjecting coffee fruit to a high-pressure treatment of 10 to 1000 MPa.
  • a flexible resin bag for example, a laminated bag
  • High pressure treatment can prevent coffee fruit oxidation.
  • a high-pressure processing apparatus that can be used for high-pressure processing
  • an apparatus that uses hydrostatic pressure in a sealed container can be generally employed.
  • high hydrostatic pressure devices such as known devices for food processing, CIP devices, pulse combined high pressure processing devices, medium and low hydrostatic pressure processing devices, direct pressurization method (400 MPa or more) and indirect pressure A pressure method (400 MPa or less) is suitable.
  • Kobe Steel's CIP equipment model CP900
  • Kobe Steel's pulse combined high-pressure treatment equipment Kobe Steel's WIP equipment
  • Kobe Steel's ultra-high pressure treatment equipment Dr. CHEF SUGINO Co., Ltd.
  • Machine servo pressure 500 HPV-50C20-S type
  • Food processing equipment manufactured by Ishikawajima-Harima Heavy Industries Co., Ltd.
  • HYPREX TEST 1TA-90 manufactured by Yamamoto Water Pressure Industrial Co., Ltd.
  • Examples include batch type devices such as BP800, Toyo Koatsu Co., Ltd. Whole Extract Device.
  • a horizontal HPP ultra-high pressure treatment device (trade name “FOOD FRESHER”) manufactured by Kobe Steel, a Hiperbaric (120 type, etc.) device, etc. are also applied.
  • the enzyme used in the present invention can be selected from at least one of oxidoreductase, transferase, hydrolase, eliminase, isomerase, and synthase. Of these, hydrolase is preferably used.
  • hydrolases examples include phosphatase (ALPAcP), amylase (starch degrading enzyme), leucine aminopeptidase (LAP), lipase, trypsin, chymotrypsin, protease (protein hydrolase), urokinase, urease, ⁇ -galactosidase, Glucosidase, lysozyme, ⁇ -lactamase, adenosine triphosphate hydrolase (ATPase), arginase, cellulase, hemicellulase, pectinase, xylanase, invertase, phospholipase, tanase, dextranase, etc. You can choose. Furthermore, cysteine enzyme, pineapple enzyme, papain enzyme (purified papain) and the like can be mentioned as well.
  • an enzyme agent using an enzyme as a main ingredient can also be used.
  • the enzyme agent include coculase P, ⁇ -amylase, glucoamylase, rotease “trade name coclase”, amylase “trade name coclase G2”, cellulase “trade name sucrase C”, and xylanase (hemicellulase) from Mitsubishi Foods Corporation.
  • At least one enzyme selected from the group consisting of proteolytic enzymes and plant fiber degrading enzymes (cellulase, pectinase, etc.). It is also effective to use a proteolytic enzyme alone or in combination with other enzymes.
  • Patent Document 4 discloses a method for producing an edible extract product from an edible raw material of coffee, before the edible raw material is pulverized into particles, the particles are extracted in water to produce an extract, and filtered using a filter.
  • a method of adding an enzyme for agglutinating carbohydrates in an extract is disclosed, but the present invention relates to a method for producing a high-pressure processed product of coffee fruit before the step of applying high-pressure treatment.
  • High-pressure treatment of coffee fruit that promotes liquefaction from coffee fruit by adding added water and performs predetermined high-pressure treatment to separate at least one processed product from the seed part and the part other than the seed part
  • the present invention relates to a method for manufacturing a product.
  • the step of subjecting the coffee fruit to a high pressure treatment of 10 to 1000 MPa includes the first step of charging the coffee fruit into the high pressure device and the pressure in the high pressure device in the range of 10 to 1000 MPa. It may comprise a second step to be performed, and may include a third step after the second step for removing the processed material from the high-pressure apparatus.
  • FIG. 3 shows a schematic process of a coffee bean processing method called a prior art (1) water-washing method (washed method).
  • the harvested coffee berries are removed with a pulper (pulp remover), then the outer skin and pulp are removed, and then transferred to a fermenter to decompose mucilage (pectin) that is slimy by the power of enzymes for 1-2 days.
  • pectin decompose mucilage
  • the slime may be forcibly removed by a machine called a musi-jim bar without using a fermenter.
  • the green coffee beans with parchment endum
  • the parchment is removed.
  • the parchment is removed with a threshing machine, and the green beans are taken out.
  • FIG. 4 shows a schematic process of the coffee beans processing method by the prior art (2) Sumatra method (wet hull method).
  • the harvested coffee berries are removed with a pulper, and the skin and flesh are removed and dried to a moisture content of 40 to 50% by mass with mucilage and parchment (endocarps) attached. Then, remove the parchment with a threshing machine and take out the green beans. The threshed raw beans are dried until the water content becomes about 11 to 12% by mass.
  • FIG. 5 shows a schematic process of a coffee bean processing method according to the prior art (3) Brazilian method (pulp to natural method).
  • the harvested coffee berries are crushed with pulper and the flesh is removed and dried to a crunchy state with mucilage and parchment. Then remove musilage and parchment with a threshing machine and take out the green beans.
  • FIG. 6 shows a schematic process of a coffee bean processing method according to the prior art (4) natural drying method (natural method).
  • This method is a simple method in which the harvested coffee fruit is spread on a rug and dried for a long period of time, and then threshed to take out raw beans. Adopted according to the natural environment of the production area.
  • the processing process includes a pulper (pulp removal machine) process, a fermentation process (about 1 to 2 days), a drying process (long-term air drying), a water washing process, and a threshing process. It is a process that takes advantage of the natural environment of the production area.
  • Typical compound derivatives include chlorogenic acid (also known as caffeoylquinic acid), polyphenolic compounds such as caffeoylquinic acid, high to low molecular weight polysaccharides, caffeine, and flavonols. Recently, it has been known that polyphenolic compounds have the effect of reducing active oxygen which causes illness and aging, etc.
  • Figure 7 shows the chemical structure of typical components of chlorogenic acid derivatives. Show.
  • the concentration of the aqueous solution containing the active ingredient after the high-pressure treatment does not require much energy and time, and the single active ingredient can be used. There is an advantage that separation is easy.
  • Example 1 (Sample 1) About 20 g of coffee fruit is weighed and placed in a transparent laminating bag (R type) manufactured by Fukusuke Kogyo Co., Ltd. (referred to as a laminating bag in this specification), and sucked and deaerated by a predetermined method with a sealer This was sealed and placed in a high-pressure treatment apparatus at a temperature of 75 ° C. and 100 MPa, and a high-pressure treatment for 24 hours was performed. When the laminating bag containing the coffee fruit was taken out of the high pressure processing apparatus, the liquid was oozing out although the shape of the coffee fruit was maintained .
  • FIG. 8 is an external appearance photograph of the coffee fruit (raw material) used in the example.
  • FIG. 8 is an external appearance photograph of the coffee fruit (raw material) used in the example.
  • Example 9 is an appearance photograph of coffee fruit (raw material) stored in a laminated bag before high pressure treatment.
  • the sample 1 figure of FIG. 10 is an external appearance photograph after performing the high-pressure process of Example 1 (refer Table 1).
  • Table 1 “ ⁇ ” indicates that the liquid leaching can be observed from the appearance of the laminated bag, “ ⁇ ” indicates that many liquids can be observed, and oozes the liquid in its original form. It was judged as “x” that no was observed.
  • Example 2 When carried out in the same manner as in Example 1 except that the same amount of water as that of the coffee fruit was sealed, the shape of the coffee fruit was maintained, but a liquid was leached (see Table 1).
  • Sample 2 in FIG. 10 is an appearance photograph after the high-pressure treatment of Example 2 is performed.
  • Example 3 (Sample 3) Except for adding 0.01 g of "Enzyme D” (cellulase + pectinase, plant fiber degrading enzyme) manufactured by Supercritical Technology Laboratory, the shape of the coffee fruit was greatly collapsed. Many liquids oozed from the coffee fruit (see Table 1). Sample 3 in FIG. 10 is an appearance photograph after the high-pressure treatment in Example 3 is performed.
  • Enzyme D cellulase + pectinase, plant fiber degrading enzyme
  • Example 4 (Sample 4) Except for adding 0.01 g of “Enzyme E” (protease, proteolytic enzyme) manufactured by Supercritical Technology Laboratory Co., Ltd., it was carried out in the same manner as in Example 2; Many liquids were leached (see Table 1). Sample 4 in FIG. 10 is an appearance photograph after the high-pressure treatment of Example 4 is performed.
  • Enzyme E proteolytic enzyme
  • Example 5 (Sample 5) Except for adding 0.01 g of “Enzyme P” (papain enzyme) manufactured by Mitsubishi Chemical Food Co., Ltd., it was carried out in the same manner as in Example 2; It oozed out (see Table 1). Sample 5 in FIG. 10 is an appearance photograph after the high-pressure treatment of Example 5 is performed.
  • the yields of these active ingredients are based on the theoretical values of the data values published by VDF FutureCeuticals (http://www.coffeeberry.com/chemistry-comparison-whole-coffee-green-coffee-bean). The yield was estimated to be about 20% to 50%.
  • Example 6 Except that the amount of “enzyme P” (papain enzyme) was changed from 0.01 g to 0.2 g, the same procedure as in Example 5 was carried out, and the components of the liquid material exuded from the coffee fruit were analyzed by HPLC (high performance liquid chromatography). ), Chlorogenic acid, caffeic acid and caffeine were detected as shown in FIG. In addition, the liquid which exuded from the coffee fruit was separated by filtering the liquid and coffee beans using a filter or the like by a predetermined method.
  • HPLC high performance liquid chromatography
  • HPLC measurement is a method commonly used by those skilled in the art, for example, ODS column, column oven 30 ° C., eluent; acetonitrile eluent of 1% by weight aqueous formic acid (1 part acetonitrile; 9 parts aqueous solution), flow rate 1 mL / min, detector An ultraviolet-visible spectroscopic detector UV-vis (325 nm).
  • Example 7 The same procedure as in Example 5 was carried out except that the high-pressure treatment time was changed to 17 hours and “enzyme P” (papain enzyme) was changed from 0.01 g to 0.2 g.
  • the pressure dependence with respect to extraction was investigated, the result shown in FIG. 12 was obtained.
  • FIG. 12 it compared with the component recovery amount when a pressure is not applied as a comparison.
  • the recovered amounts of the components were analyzed by a predetermined method after separating the liquid after high pressure treatment and adjusting the pH to 4 to 5 by a predetermined method. As is clear from FIG. 12, it was found that more chlorogenic acid (Chloro_A.) And caffeic acid (Caffe_A.) Can be extracted under a high pressure of 100 MPa.
  • Example 8 In order to investigate the dependence of the treatment temperature, the treatment temperature is set to 75 ° C. and 65 ° C., the enzyme “enzyme P” (papain enzyme) alone, and the enzyme P and “enzyme D” (cellulase system: cellulase + pectinase) The same procedure as in Example 5 was conducted except that the equivalent amount of enzyme P and “enzyme E” (protease) were used in equivalent amounts, and the total amount of enzyme used was changed from 0.01 g to 0.2 g. When the treatment temperature dependency on the extraction (recovered amount) of inacid was examined, the results shown in FIG. 13 were obtained. The amount of components recovered was the same as in Example 7. As is clear from FIG. 13, it was found that high-pressure treatment at 75 ° C. can extract more chlorogenic acid (Chloro_A.) And caffeic acid (Caffe_A.) Than 65 ° C.
  • Comparative Example 1 Weigh about 20 g of coffee fruit and 20 g of water (equal portion), put in a transparent laminated bag, suck and deaerate with a prescribed method, seal with a sealer, and let stand at room temperature and atmospheric pressure for 24 hours Observed. There was no change in the appearance of the coffee fruit in the laminated bag (see Table 2). The appearance determination in Table 2 was the same as that in Table 1.
  • Comparative Example 2 When carried out in the same manner as Comparative Example 1 except that 0.01 g of enzyme D was added, no change was observed in the appearance of the coffee fruit in the laminated bag (see Table 2).
  • an active ingredient of a plant fiber degradation product derived from coffee beans (seed), pulp, etc. which has not been conventionally available, can be produced.
  • Substances serving as active ingredients for foods and the like are further widely used for feed addition to cattle, pigs, birds, fish, etc., health maintenance supplements, and health drinks.

Abstract

[Problem] To provide a method for quickly removing, fermenting, and separating the pericarp, the sarcocarp, and the like of coffee berries. [Solution] A method for producing a product of high-pressure treatment of coffee berries characterized by including a step in which, after a step in which coffee berries are subjected to high-pressure treatment at 10-1,000 MPa, the result is separated into a bean part and at least one other treated product of a part other than the bean part.

Description

コーヒー果実の高圧処理方法、コーヒー果実の高圧処理物の製造方法及びその方法から得られた処理物Method for high-pressure treatment of coffee fruit, method for producing high-pressure processed product of coffee fruit, and processed product obtained from the method
 本発明は、コーヒー果実の高圧処理方法、コーヒー果実の高圧処理物の製造方法及びその方法から得られた処理物に関する。 The present invention relates to a high-pressure treatment method for coffee fruit, a method for producing a high-pressure treatment product of coffee fruit, and a treatment product obtained from the method.
 コーヒー果実は、外皮、果肉、ぬめりの有る内果皮(パーチメント)、銀皮(シルバースキン)、種子の構造になっている(図1)。種子の外側の部分を取り除いたものが生豆、さらに生豆を焙煎挽きしてコーヒー飲料として利用される。
 コーヒー果実からコーヒー豆に精製するためには、コーヒー果実を収穫した後に速やかにパルプ等の果皮や果肉を除去機(パルパー)で剥離し、発酵工程を経て、水洗・乾燥して種子が取り出される工程を経ることが知られている。これが、(1)水洗式(ウォッシュト法)と呼ばれる精製方法である。
Coffee fruit has a structure of outer skin, pulp, slimy inner skin (parchment), silver skin (silver skin), and seed (FIG. 1). Raw beans from which the outer part of the seeds has been removed are roasted and ground and used as a coffee beverage.
In order to refine coffee beans from coffee berries, after harvesting the coffee berries, the pulp and pulp such as pulp are peeled off with a remover (pulper), and after a fermentation process, the seeds are removed by washing and drying. It is known to go through a process. This is (1) a purification method called a washing method (washed method).
 一方、前記発酵工程を経ないでぬめりの付いたまま脱穀する(2)スマトラ式(ウエットハル法)や前記発酵工程を経ないでぬめりの付いたまま乾燥し脱穀する(3)ブラジル式(パルプトナチュラル法)、そして収穫したコーヒー果実をそのまま十分乾燥した後で脱穀するシンプルな(4)自然乾燥式(ナチュラル法)もあり、これら方法はコーヒー果実の生産地で古くから発展してきた。また精製方法や焙煎方法等の違いによって、風味の異なるコーヒーが愛用されている。 On the other hand, threshing without slimming without going through the fermentation process (2) Sumatra type (wet hull method) or drying and threshing with slimming without going through the fermentation process (3) Brazilian style (pulp Natural method), and simple (4) natural drying method (natural method) in which the harvested coffee berries are sufficiently dried and then threshed, and these methods have been developed for a long time in coffee fruit production areas. Also, coffees with different flavors are favored due to differences in purification methods and roasting methods.
 しかしながら、いずれの精製方式でも大きな問題点を有している。例えば(1)水洗式や(2)スマトラ式、(3)ブラジル式は、パルパー処理の際に大量の水を使用する為に果肉部から多くの水溶性成分が流出し、当該成分を回収する場合には濃縮工程が必要となり、またその為には多くのエネルギーと時間を要する問題がある。(4)自然乾燥式は、長時間の天日乾燥により抗酸化成分の多くが酸化反応により消失することや一部腐敗の危険性をはらむ等の問題を有する。また、(2)スマトラ式や(3)ブラジル式は、ぬめりの付いたまま乾燥する為に、(4)自然乾燥式と同様な問題を有している。 However, both purification methods have major problems. For example, (1) water-washing type, (2) Sumatra type, and (3) Brazilian type use a large amount of water during the pulper treatment, so that many water-soluble components flow out from the pulp and recover the components. In some cases, a concentration step is required, and for that purpose, there is a problem of requiring a lot of energy and time. (4) The natural drying method has problems such that many of the antioxidant components disappear due to oxidation reaction due to long-term sun drying, and there is a risk of partial corruption. In addition, (2) Sumatra type and (3) Brazilian type have the same problems as (4) natural drying type because they dry with sliminess.
 このように、世界で広く採用されている上記(1)~(4)のコーヒー豆の精製は、生産地の熱帯地域において行われることが多く、雑菌による種子の腐敗の進行も心配され、収穫後は速やかに精製工程を実施する必要がある。
 特許文献1には、収穫後のコーヒー果実の日持ちを良くする為のコーヒー果実の処理方法として、精製工程の前に、コーヒー果実を熱水で処理する方法が開示されている。
As described above, the refining of the coffee beans (1) to (4), which is widely adopted in the world, is often carried out in the tropical region of the production area, and there is concern about the progress of seed rot due to various germs. After that, it is necessary to carry out the purification process promptly.
Patent Document 1 discloses a method for treating coffee fruit with hot water before the refining step as a method for treating coffee fruit for improving the shelf life of the harvested coffee fruit.
 一方、コーヒー果実には多くの有益な食品有効成分が含まれていることから、特許文献2には、コーヒー果実全体(種子部を含む)を急速乾燥して粉砕して水で有効成分を抽出、そしてSEC法(サイズ排除クロマトグラフィー法)で高分子~低分子の多糖類、ポリフェノール系のコーヒー酸、カフェイン等を分離する方法が開示されている。 On the other hand, since coffee fruit contains many useful food active ingredients, Patent Document 2 discloses that the entire coffee fruit (including the seed part) is rapidly dried and ground to extract the active ingredient with water. In addition, a method for separating high-molecular to low-molecular polysaccharides, polyphenol-based caffeic acid, caffeine, and the like by the SEC method (size exclusion chromatography method) is disclosed.
 また、特許文献3には、食用物質の抽出物を含む食用組成物であって、前記抽出物が、約0℃~約80℃の抽出温度及び少なくとも約2000バールの抽出圧力で水を含む抽出媒体中での食用物質の抽出から得られるものである前記組成物が開示されている。 Patent Document 3 also discloses an edible composition containing an extract of edible substances, wherein the extract contains water at an extraction temperature of about 0 ° C. to about 80 ° C. and an extraction pressure of at least about 2000 bar. Said composition is disclosed which is obtained from the extraction of edible substances in a medium.
 さらに、特許文献4には、食用抽出生成物の製造方法であって、食用原材料を粒子へと粉砕すること、該食用原材料の粒子を水中で抽出して該食用原材料の抽出物を生成すること、該食用原材料の抽出物を少なくとも1つのフィルタを用いて、該食用原材料の抽出物中のクロロゲン酸の濃度が高まると同時に、該食用原材料の抽出物中の脂肪の濃度が低下するように濾過すること、そして得られた濾過保持液を該食用原材料の濾過された抽出物から分離して、食用抽出生成物を形成することを含む前記製造方法が開示され、食用原材料の抽出物の濾過の前に、該食用原材料の抽出物に酵素を添加することで、炭水化物を凝集する酵素の使用が開示されている。 Furthermore, Patent Document 4 discloses a method for producing an edible extract product, which comprises pulverizing an edible raw material into particles, and extracting the edible raw material particles in water to produce an extract of the edible raw material. Filtering the edible raw material extract using at least one filter so that the concentration of chlorogenic acid in the edible raw material extract is increased and at the same time the concentration of fat in the edible raw material extract is decreased And producing the edible extract product by separating the resulting filter retentate from the filtered extract of the edible raw material, wherein the method of filtration of the edible raw material extract is disclosed. Previously, the use of enzymes that aggregate carbohydrates by adding enzymes to the edible raw material extract has been disclosed.
:国際公開WO2006/126588号: International Publication WO2006 / 126588 :米国特許出願公開第2010/0080885号明細書: US Patent Application Publication No. 2010/0080885 :国際公開WO2013/103465号: International publication WO2013 / 103465 :国際公開WO2014/149512号: International Publication WO2014 / 149512
 しかしながら、コーヒー果実を収穫した後に腐敗を抑制しながら速やかにコーヒー生豆とするためには、パルプなどの果皮や果肉を速やかに剥離し発酵し又は乾燥させる必要があり、従来の上記(1)~(4)のコーヒー豆の精製では、パルプ部等に含まれている有効成分は利用されることなくパルパー除去され、またパルパー処理水内で腐敗(酸化分解)してしまい、利用できない課題があった。
 本発明は、上記課題に鑑み、コーヒー果実を収穫した後に腐敗を抑制しながら速やかにコーヒー生豆とする利用だけでなく、パルプなどの果皮や果肉部から食品等に有効な成分を収得することを目的としている。
However, in order to quickly produce green coffee beans while suppressing spoilage after harvesting coffee fruits, it is necessary to quickly peel, ferment or dry pulp and other pulps, and the conventional (1) In the refining of coffee beans in (4), the active ingredient contained in the pulp part is removed without using the pulper, and it is rotted (oxidative decomposition) in the pulper-treated water. there were.
In view of the above-mentioned problems, the present invention is not only used as a quick coffee bean while suppressing spoilage after harvesting coffee fruits, but also obtains effective ingredients in foods and the like from the skin and pulp parts of pulp and the like. It is an object.
 本発明者等は、コーヒー果実に高圧処理を施すことで、パルプ部に含有する成分や種子部の腐敗・酸化分解を抑制できるコーヒー果実の高圧処理方法及び高圧処理物の製造方法を見出し、本発明に想到した。即ち、本発明は以下の手段を提供する。
[1] コーヒー果実の高圧処理物の製造方法であって、コーヒー果実に10~1000MPaの高圧処理を施す工程後、種子部と種子部以外の部の少なくとも1種の処理物を分離する工程を含むことを特徴とする、コーヒー果実の高圧処理物の製造方法。
[2] 前記高圧処理を施す工程前に、コーヒー果実の質量に対して100質量倍以下の範囲で、0.001~10質量%の酵素を含む酵素添加水を投入する工程を含むことを特徴とする前項1に記載のコーヒー果実の高圧処理物の製造方法。
[3] 高圧処理の温度が30~120℃の範囲であることを特徴とする前項1又は2に記載のコーヒー果実の高圧処理物の製造方法。
The present inventors have found a high-pressure treatment method for coffee fruit and a method for producing a high-pressure treated product that can suppress the decay and oxidative degradation of the components contained in the pulp part and the seed part by performing high-pressure treatment on the coffee fruit. I came up with the invention. That is, the present invention provides the following means.
[1] A method for producing a high-pressure processed product of coffee fruit, comprising a step of separating at least one processed product of a seed part and a part other than the seed part after the step of subjecting the coffee fruit to a high-pressure treatment of 10 to 1000 MPa. A method for producing a high-pressure processed product of coffee fruit, comprising:
[2] The method includes a step of adding enzyme-added water containing 0.001 to 10% by mass of enzyme in a range of 100 mass times or less with respect to the mass of coffee fruit before the step of applying the high-pressure treatment. The method for producing a high-pressure processed product of coffee fruit according to item 1 above.
[3] The method for producing a high-pressure treated product of coffee fruit according to item 1 or 2, wherein the temperature of the high-pressure treatment is in the range of 30 to 120 ° C.
[4] pH調整可能な化合物を添加することを特徴とする前項1乃至3の何れか1項に記載のコーヒー果実の高圧処理物の製造方法。
[5] 前記コーヒー果実に10~1000MPaの高圧処理を施す工程が、コーヒー果実を高圧装置に投入する第1工程と前記高圧装置内の圧力を10~1000MPaの範囲で実施する第2工程からなることを特徴とする前項1乃至4の何れか1項に記載のコーヒー果実の高圧処理物の製造方法。
[6] 前記第2工程の後で、処理物を前記高圧装置から取り出す第3工程を含む、前項5に記載のコーヒー果実の高圧処理物の製造方法。
[4] The method for producing a high-pressure processed product of coffee fruit according to any one of items 1 to 3, wherein a compound capable of adjusting pH is added.
[5] The step of subjecting the coffee fruit to a high pressure treatment of 10 to 1000 MPa comprises a first step of charging the coffee fruit into a high pressure device and a second step of carrying out the pressure in the high pressure device in the range of 10 to 1000 MPa. 5. The method for producing a high-pressure processed product of coffee fruit according to any one of items 1 to 4 above.
[6] The method for producing a high-pressure processed coffee fruit product according to item 5, further including a third step of removing the processed product from the high-pressure apparatus after the second step.
[7] 前記第1工程~前記第3工程を行った後、新たなコーヒー果実を第1工程に投入して第1工程~第3工程を順次繰り返す前項6に記載のコーヒー果実の高圧処理物の製造方法。
[8] さらに、前記種子部を乾燥する工程又は前記種子部以外の部からコーヒー果実に含まれる成分を分離する工程を含むことを特徴とする、前項1乃至7の何れか1項に記載のコーヒー果実の高圧処理物の製造方法。
[9] 前項1乃至8の何れか1項に記載のコーヒー果実の高圧処理物の製造方法から得られた処理物。
[7] The high-pressure processed product of coffee fruit according to item 6 above, wherein after performing the first step to the third step, fresh coffee fruit is added to the first step and the first step to the third step are sequentially repeated. Manufacturing method.
[8] The method according to any one of items 1 to 7, further comprising a step of drying the seed part or a step of separating components contained in the coffee fruit from parts other than the seed part. A method for producing a high-pressure processed product of coffee fruit.
[9] A processed product obtained from the method for producing a high-pressure processed product of coffee fruit according to any one of 1 to 8 above.
[10] コーヒー果実に10~1000MPaの高圧処理を施すことを特徴とするコーヒー果実の高圧処理方法。
[11] 前記高圧処理を施す前に、0.001~10質量%を含む酵素添加水を、コーヒー果実の質量に対して100質量倍以下の範囲で投入することを特徴とする前項10に記載のコーヒー果実の高圧処理方法。
[12] 温度が30~120℃の範囲であることを特徴とする前項10又は11に記載のコーヒー果実の高圧処理方法。
[13] pH調整可能な化合物を添加することを特徴とする前項10乃至12の何れか1項に記載のコーヒー果実の高圧処理方法。
[10] A method for high-pressure treatment of coffee fruit, comprising subjecting coffee fruit to a high-pressure treatment of 10 to 1000 MPa.
[11] The item 10 above, wherein the enzyme-added water containing 0.001 to 10% by mass is added in a range of 100 mass times or less with respect to the mass of the coffee fruit before the high-pressure treatment. High pressure processing method for coffee berries.
[12] The method for high-pressure treatment of coffee fruit according to item 10 or 11, wherein the temperature is in the range of 30 to 120 ° C.
[13] The high pressure treatment method for coffee fruit according to any one of items 10 to 12, wherein a compound capable of adjusting pH is added.
 本発明のコーヒー果実の高圧処理方法及び高圧処理物の製造方法によれば、コーヒー果実のパルパー粉砕処理やぬめり(シュミレージ)除去の為の発酵処理(通常1日~2日間)、パーチメント(内果皮)の剥離処理を個別の工程として必要とせず、コーヒー果実の精製工程の大幅な時間短縮、生産コストの低減を図ることできる。 According to the coffee fruit high pressure treatment method and the high pressure treated product production method of the present invention, coffee fruit pulper pulverization treatment and fermentation treatment (usually 1 to 2 days) for removing slime (smilage), parchment (endocarp) ) Is not required as a separate process, and the coffee fruit refining process can be greatly shortened and the production cost can be reduced.
コーヒー果実の断面概略図を示す。The cross-sectional schematic of a coffee fruit is shown. 本発明の実施形態に係る、コーヒー果実の高圧処理の概略工程(一例)を示す。The schematic process (an example) of the high pressure process of the coffee fruit based on embodiment of this invention is shown. 従来技術(1)水洗式によるコーヒー豆の加工方式の概略工程を示す。Prior art (1) The outline process of the processing method of the coffee bean by a washing type is shown. 従来技術(2)スマトラ式(ウエットハル法)によるコーヒー豆の加工方式の概略工程を示す。The general | schematic process of the processing method of the coffee bean by a prior art (2) Sumatra type (wet hull method) is shown. 従来技術(3)ブラジル式(パルプトナチュラル法)によるコーヒー豆の加工方式の概略工程を示す。The general | schematic process of the processing method of the coffee bean by a prior art (3) Brazilian type (pulp-to-natural method) is shown. 従来技術(4)自然乾燥式(ナチュラル法)によるコーヒー豆の加工方式の概略工程を示す。The outline process of the processing method of the coffee bean by the prior art (4) natural drying type (natural method) is shown. クロロゲン酸の代表的な化学構造を示す。The typical chemical structure of chlorogenic acid is shown. 実施例で用いられたコーヒー果実(原料)の外観写真の一例である。It is an example of the external appearance photograph of the coffee fruit (raw material) used in the Example. 実施例で用いられたコーヒー果実(原料)のレトルト袋内に収納された状態の外観写真の一例である。It is an example of the external appearance photograph of the state accommodated in the retort bag of the coffee fruit (raw material) used in the Example. 各実施例において、高圧処理後の液状化状況を見た外観写真である。In each Example, it is the external appearance photograph which looked at the liquefaction state after a high pressure process. 液状物のHPLC成分分析結果の一例である。It is an example of the HPLC component analysis result of a liquid substance. クロロゲン酸及びカフェイン酸の抽出量(回収)に対する圧力依存性を示す図の一例である。It is an example of the figure which shows the pressure dependence with respect to the extraction amount (recovery) of chlorogenic acid and caffeic acid. クロロゲン酸及びカフェイン酸の抽出量(回収)に対する温度依存性を示す図の一例である。It is an example of the figure which shows the temperature dependence with respect to the extraction amount (recovery) of chlorogenic acid and caffeic acid.
 本発明は、前述の手段を提供するものであって、好ましくは、コーヒー果実の質量に対し100質量倍以下の範囲で、0.001~10質量%の酵素を含む水溶液をコーヒー果実に添加し10~1000MPaの高圧処理を施す工程と、その後、種子部と種子部以外の部の少なくとも1種の処理物を分離する工程とを有することを特徴とするコーヒー果実の高圧処理物の製造方法及び関連の従属発明を提供する。
 以下、本発明の実施形態を詳細に説明する。
 図1はコーヒー果実の断面図を示す。コーヒー果実は一般に赤く熟した果実(チェリー)を摘み取る。その果実の構成部は、外側から外皮1、その下部の果肉2、粘液質のペクチン質からなるミューレージ3、内果皮のパーチメント4、及び2つの種子5からなる。
The present invention provides the above-mentioned means. Preferably, an aqueous solution containing 0.001 to 10% by mass of an enzyme is added to the coffee fruit within a range of 100 mass times or less with respect to the mass of the coffee fruit. A method for producing a high-pressure processed product of coffee fruit, comprising a step of performing a high-pressure treatment of 10 to 1000 MPa, and then a step of separating at least one kind of processed product of a seed part and a part other than the seed part; Provide related dependent inventions.
Hereinafter, embodiments of the present invention will be described in detail.
FIG. 1 shows a cross-sectional view of coffee fruit. Coffee fruits are generally picked from red ripe fruits (cherries). The fruit component comprises an outer skin 1, a lower pulp 2, a mule 3 made of mucous pectin, an inner pericarp parchment 4, and two seeds 5.
 図2は、本発明の実施形態に係るコーヒー果実の高圧処理物の製造方法の概略(一例)を示す。図2では、集荷したコーヒー果実を高圧処理可能な装置内に入れ、高圧処理を施した後、液状物化(種子の周辺にゼリー状物が絡む)された処理物から種子とゼリー状物を分離する。
 種子は水洗後に乾燥して生豆として回収、またゼリー状物にはパルプやミューレージ、パーチメント発酵物由来の液状物(水溶液)を分離する工程を表している。
 ここで、液状物には、植物繊維質分解物や食品等に有効な成分の物質が含まれている。有益成分の物質の分離には、濾過法や圧縮脱水法、遠心分離法等の採用により、繊維質分解物を除去して、有効成分が溶解した水溶液部を収得することができる。さらにこの水溶液部は、サイズ排除クロマトグラフィー(SEC法、ゲルろ過クロマトグラフィー等)を用いて、有効成分の物質に単離収得することができる。
FIG. 2: shows the outline (an example) of the manufacturing method of the high pressure processed material of the coffee fruit which concerns on embodiment of this invention. In Fig. 2, the collected coffee berries are placed in an apparatus capable of high-pressure treatment, and after high-pressure treatment, the seeds and jelly-like materials are separated from the treated product that has been liquefied (the jelly-like materials are entangled around the seeds). To do.
The seed is dried after washing and recovered as green beans, and the jelly-like product represents a process of separating a liquid (aqueous solution) derived from pulp, mulege, and fermented parchment.
Here, the liquid substance contains a substance that is an effective component for plant fiber decomposition products, foods, and the like. Separation of the beneficial component substance can be achieved by removing the fibrous decomposition product by employing a filtration method, a compression dehydration method, a centrifugal separation method, or the like, thereby obtaining an aqueous solution portion in which the active ingredient is dissolved. Furthermore, this aqueous solution part can be isolated and collected as an active ingredient substance using size exclusion chromatography (SEC method, gel filtration chromatography, etc.).
 本発明の実施形態に係る発明は、コーヒー果実の高圧処理物の製造方法であって、コーヒー果実に10~1000MPaの高圧処理を施す工程後、種子部と種子部以外の部の少なくとも1種の処理物を分離する工程を含む、コーヒー果実の高圧処理物の製造方法を提供する。
 ここで、高圧処理を施す圧力は、常温を超える圧力下であれば良く、著しい効果を発揮する為には圧力10~1000MPaの範囲が好ましく、さらに30~800MPaの範囲がより好ましく、50~600MPaの範囲が望ましい。高圧処理を施す圧力が10MPa未満の場合、本発明の効果を著しく低減してしまう恐れがある。また、処理圧力が1000MPaを超える場合は、高圧処理を施す容器や動力設備等の耐圧性に信頼性を損なう恐れが生じ、安全性の低下や運転時間が長くなる結果、生産コストに大きく影響する結果を招いてしまう恐れがある。また、酵素活性を低減してしまう恐れがある。
The invention according to an embodiment of the present invention is a method for producing a high-pressure treated product of coffee fruit, wherein after the step of subjecting the coffee fruit to a high-pressure treatment of 10 to 1000 MPa, at least one kind of part other than the seed part and the seed part is provided. Provided is a method for producing a high-pressure processed product of coffee fruit, comprising a step of separating the processed product.
Here, the pressure for performing the high-pressure treatment may be a pressure exceeding normal temperature, and in order to exert a remarkable effect, the pressure is preferably in the range of 10 to 1000 MPa, more preferably in the range of 30 to 800 MPa, and more preferably in the range of 50 to 600 MPa. A range of is desirable. When the pressure which performs a high pressure process is less than 10 MPa, there exists a possibility that the effect of this invention may be reduced remarkably. In addition, when the processing pressure exceeds 1000 MPa, there is a risk of impairing the reliability of the pressure resistance of a container or power equipment that performs high-pressure processing, resulting in a decrease in safety and a longer operating time, which greatly affects production costs. There is a risk of incurring results. Moreover, there exists a possibility of reducing an enzyme activity.
 このように本発明において、コーヒー果実に高圧処理を施すことにより、コーヒー果実の腐敗や菌の働きを抑え、自己分解酵素を持っているコーヒー果実の酵素の作用を活性化させることができ、従来技術(1)~(4)に比べて、比べものにならない短時間で、かつ簡易な作業工程により、外皮や果肉、ミューレージ、パーチメント等を取り除くことが可能である。また、外部から積極的に酵素を補填することにより、前記の本発明の効果は加速される。
 また、本発明の製造方法では、前記高圧処理を施す工程前に、コーヒー果実の質量に対して100質量倍以下の範囲で、0.001~10質量%の酵素を含む酵素添加水を投入する工程を含んでも良い。
Thus, in the present invention, by applying a high pressure treatment to coffee fruit, it is possible to suppress the decay of coffee fruit and fungi, and to activate the action of the coffee fruit enzyme having an autolytic enzyme, Compared to the techniques (1) to (4), it is possible to remove the outer skin, pulp, mules, parchment, etc. in a short time that is not comparable and with simple work processes. Moreover, the effect of the present invention is accelerated by positively supplementing the enzyme from the outside.
In the production method of the present invention, the enzyme-added water containing 0.001 to 10% by mass of enzyme is added in a range of 100 mass times or less with respect to the mass of coffee fruit before the high-pressure treatment step. A process may be included.
 本発明の製造方法においては、通常生産地から運び込まれたコーヒー果実は選別も兼ねてタンク水等に投入され、ゴミ選別とコーヒー果実の洗浄の後に、高圧処理装置内に移され、水の無添加下又は所定量の水を投入して高圧処理が行われる。ここで、加水量は、好ましくは被処理物のコーヒー果実の質量に対して、10倍量未満が良く、さらに5倍量未満がより好ましく、3倍量未満が望ましい。加水量が10倍量を超えると、高圧処理後に収得する液状物の溶液量が増えてしまう結果、その後の有効成分を含む水溶液の濃縮に多くのエネルギーと時間を要してしまい、有効成分の単離を困難にする恐れがある。 In the production method of the present invention, the coffee fruit brought from the normal production area is also put into tank water or the like also for sorting, and after sorting the garbage and washing the coffee fruit, it is transferred into a high-pressure treatment apparatus, and no water is used. The high-pressure treatment is performed under addition or by adding a predetermined amount of water. Here, the amount of water added is preferably less than 10 times, more preferably less than 5 times, and preferably less than 3 times the mass of coffee fruit to be processed. If the amount of water exceeds 10 times the amount, the amount of liquid obtained after high-pressure treatment increases, resulting in the subsequent concentration of the aqueous solution containing the active ingredient requires a lot of energy and time. Isolation may be difficult.
 また、本発明では、好ましくは高圧処理を施す工程前に、酵素添加を行うのが良く、例えばコーヒー果実の乾燥固形質量に対して、酵素を0.01~5質量%の範囲で用いるのが良く、0.1~2質量%の範囲がさらに望ましい。酵素添加量が0.01未満であるとパルプ等の液状化の働きを最大限に発揮できない恐れがあり、また5質量%を超えて用いる場合には生産コストの大幅なアップになってしまう。酵素は、パーチメントに残った果肉の一部を除去するため水槽で発酵させる働きがあり、さらに高圧環境では発酵の反応が促進される。その結果、有益な発酵成分を多く産生することができる。 In the present invention, the enzyme is preferably added before the high-pressure treatment step. For example, the enzyme is used in the range of 0.01 to 5% by mass relative to the dry solid mass of the coffee fruit. The range of 0.1 to 2% by mass is more desirable. If the amount of enzyme added is less than 0.01, the liquefaction action of pulp or the like may not be exhibited to the maximum, and if it exceeds 5 mass%, the production cost will be significantly increased. The enzyme has a function of fermenting in a water tank to remove part of the pulp remaining in the parchment, and further, the fermentation reaction is promoted in a high-pressure environment. As a result, many useful fermentation components can be produced.
 高圧処理を施す際の処理温度は、通常30~120℃の範囲が好ましく、さらに30~100℃の範囲がより好ましく、30~80℃の範囲が望ましい。処理温度が30℃未満の低温では本発明の効果を著しく低減してしまう恐れがある。また処理温度が、120℃を超える場合は加熱~冷却等に係る時間が長くなる結果、生産コストに大きく影響する結果を招いてしまう恐れがある。
 しかしながら、室温以上の高い温度域の処理では、コーヒー豆(種子部)に「煮詰め」の効果を付与することができ、その結果、本発明の高い温度での高圧処理を施す結果、場合によっては生豆の成分分解も併発し、糖質、アミノ酸類が増えるので、コーヒー豆の焙煎後の飲料としてコクや旨味成分の増大が期待される。
The treatment temperature during the high-pressure treatment is usually preferably in the range of 30 to 120 ° C, more preferably in the range of 30 to 100 ° C, and preferably in the range of 30 to 80 ° C. If the processing temperature is lower than 30 ° C., the effect of the present invention may be significantly reduced. Further, when the processing temperature exceeds 120 ° C., the time required for heating to cooling becomes longer, which may result in greatly affecting the production cost.
However, in the treatment in the high temperature range above room temperature, the effect of “boiled” can be imparted to the coffee beans (seed part), and as a result, the high pressure treatment at the high temperature of the present invention is applied. As the components of raw beans are decomposed, sugars and amino acids increase, and as a beverage after roasting coffee beans, the richness and umami components are expected to increase.
 本発明では、また好ましくは高圧処理を施す際に、pH調整剤を添加しても良い。pH調整剤としては、食品のpH調整に用いられているpH調整剤ならば広く用いることができる。例えばクエン酸、クエン酸三ナトリウム、炭酸ナトリウム、リン酸及びリン酸等を挙げることができる。
 pH調整剤は、pH4~9の範囲で調整できるものが好ましい。
In the present invention, preferably, a pH adjusting agent may be added when the high pressure treatment is performed. As the pH adjuster, any pH adjuster used for food pH adjustment can be widely used. Examples include citric acid, trisodium citrate, sodium carbonate, phosphoric acid and phosphoric acid.
The pH adjuster is preferably one that can be adjusted in the range of pH 4-9.
 さらに、本発明のコーヒー果実の高圧処理物の製造方法では、コーヒー果実に10~1000MPaの高圧処理を施す工程が、コーヒー果実を高圧装置に投入する第1工程と高圧装置内の圧力を10~1000MPaの範囲で実施する第2工程からなる。また、第2工程の後で、処理物を高圧装置から取り出す第3工程を含むでも良い。そして、第1工程~前記第3工程を行った後、新たなコーヒー果実を第1工程に投入して第1工程~第3工程を順次繰り返す、コーヒー果実の高圧処理物の製造方法を提供する。
 さらに、本発明では、種子部を乾燥する工程又は種子部以外の部からコーヒー果実に含まれる成分を分離する工程を含んでも良い。
Furthermore, in the method for producing a coffee fruit high-pressure processed product of the present invention, the step of subjecting the coffee fruit to a high-pressure treatment of 10 to 1000 MPa includes a first step of charging the coffee fruit into the high-pressure device and a pressure in the high-pressure device of 10 to It consists of the 2nd process implemented in the range of 1000 MPa. Moreover, you may include the 3rd process which takes out a processed material from a high voltage | pressure apparatus after a 2nd process. Then, after performing the first step to the third step, a method for producing a high-pressure processed product of coffee fruit is provided, in which new coffee fruits are added to the first step and the first step to the third step are sequentially repeated. .
Furthermore, in this invention, you may include the process of isolate | separating the component contained in a coffee fruit from the process of drying a seed part, or parts other than a seed part.
 また、本発明のコーヒー果実の高圧処理物の製造方法から得られた処理物を提供する。
 さらに、本発明では、コーヒー果実に10~1000MPaの高圧処理を施すことを特徴とするコーヒー果実の高圧処理方法を提供する。
Moreover, the processed material obtained from the manufacturing method of the high pressure processed material of the coffee fruit of this invention is provided.
Furthermore, the present invention provides a method for high-pressure treatment of coffee fruit, characterized by subjecting coffee fruit to a high-pressure treatment of 10 to 1000 MPa.
 本発明では、コーヒー果実を高圧装置内に投入する際は、可撓性のある樹脂袋(例えばラミネート加工袋等)を使用して、所定の方法で脱気して密封、外気と遮断して高圧処理し、コーヒー果実の酸化を阻止することができる。ここで、高圧処理に利用できる高圧処理装置は、一般に密閉容器中で静水圧を利用する装置を採用することができる。例えば、公知な食品加工用で使用されている装置、CIP装置、パルス併用高圧処理装置、中低静水圧処理装置等の高静水圧装置が挙げられ、直接加圧方式(400MPa以上)や間接加圧方式(400MPa以下)が適する。 In the present invention, when the coffee fruit is put into the high-pressure apparatus, a flexible resin bag (for example, a laminated bag) is used to deaerate and seal with a predetermined method to shut off the outside air. High pressure treatment can prevent coffee fruit oxidation. Here, as a high-pressure processing apparatus that can be used for high-pressure processing, an apparatus that uses hydrostatic pressure in a sealed container can be generally employed. For example, high hydrostatic pressure devices such as known devices for food processing, CIP devices, pulse combined high pressure processing devices, medium and low hydrostatic pressure processing devices, direct pressurization method (400 MPa or more) and indirect pressure A pressure method (400 MPa or less) is suitable.
 より具体的には、神戸製鋼所製CIP装置(型式CP900)、神戸製鋼所製パルス併用高圧処理装置、神戸製鋼所製WIP装置、神戸製鋼所製 超高圧処理装置 Dr. CHEF、(株)スギノマシン製サーボプレッシャ500(HPV-50C20-S型)石川島播磨重工業(株)製の食品加工用装置、(株)山本水圧工業所製HYPREX TEST 1TA-90、NPSマシナリー(株)製高圧処理試験装置BP800、(株)東洋高圧製まるごとエキス装置等のバッチ式装置が挙げられる。 More specifically, Kobe Steel's CIP equipment (model CP900), Kobe Steel's pulse combined high-pressure treatment equipment, Kobe Steel's WIP equipment, Kobe Steel's ultra-high pressure treatment equipment Dr. CHEF, SUGINO Co., Ltd. Machine servo pressure 500 (HPV-50C20-S type) Food processing equipment manufactured by Ishikawajima-Harima Heavy Industries Co., Ltd., HYPREX TEST 1TA-90 manufactured by Yamamoto Water Pressure Industrial Co., Ltd., high-pressure processing test equipment manufactured by NPS Machinery Co., Ltd. Examples include batch type devices such as BP800, Toyo Koatsu Co., Ltd. Whole Extract Device.
 また、連続的な高圧処理ができる装置としては、神戸製鋼所製の横型HPP超高圧処理装置(商品名“FOOD FRESHER”)やHiperbaric社製(120型等)装置なども適用される。
 本発明で用いられる酵素には、酸化還元酵素、転移酵素、加水分解酵素、脱離酵素、異性化酵素、合成酵素から少なくとも1種を選択することができる。中でも加水分解酵素が好ましく使用される。加水分解酵素には、例えば、ホスファターゼ(ALPAcP)、アミラーゼ(でんぷん分解酵素)、ロイシンアミノペプチターゼ(LAP)、リパーゼ、トリプシン、キモトリプシン、プロテアーゼ(たんぱく質加水分解酵素)、ウロキナーゼ、ウレアーゼ、β-ガラクトシダーゼ、グルコシダーゼ、リゾチーム、β-ラクタマーゼ、アデノシン三リン酸加水分解酵素(ATPase)、アルギナーゼ、セルラーゼ、ヘミセルラーゼ、ペクチナーゼ、キシラナーゼ、インベルターゼ、ホスホリパーゼ、タンアーゼ、デキストラナーゼ等を挙げることができ、少なくとも1種を選択することができる。
 さらには、システイン酵素、パイナップル酵素、パパイン酵素(精製パパイン)なども同様に挙げることができる。
In addition, as a device capable of continuous high-pressure treatment, a horizontal HPP ultra-high pressure treatment device (trade name “FOOD FRESHER”) manufactured by Kobe Steel, a Hiperbaric (120 type, etc.) device, etc. are also applied.
The enzyme used in the present invention can be selected from at least one of oxidoreductase, transferase, hydrolase, eliminase, isomerase, and synthase. Of these, hydrolase is preferably used. Examples of hydrolases include phosphatase (ALPAcP), amylase (starch degrading enzyme), leucine aminopeptidase (LAP), lipase, trypsin, chymotrypsin, protease (protein hydrolase), urokinase, urease, β-galactosidase, Glucosidase, lysozyme, β-lactamase, adenosine triphosphate hydrolase (ATPase), arginase, cellulase, hemicellulase, pectinase, xylanase, invertase, phospholipase, tanase, dextranase, etc. You can choose.
Furthermore, cysteine enzyme, pineapple enzyme, papain enzyme (purified papain) and the like can be mentioned as well.
 本発明では、さらに酵素を主剤に用いた酵素剤も用いることができる。この酵素剤として、例えば三菱フード(株)のコクラーゼP、α-アミラーゼ、グルコアミラーゼ、ロテアーゼ「商品名コクラーゼ」、アミラーゼ「商品名コクラーゼG2」、セルラーゼ「商品名スクラーゼC」、キシラナーゼ(ヘミセルラーゼ)、「商品名スクラーゼX」、ペクチナーゼ「商品名スクラーゼN」、ペクチナーゼ「商品名スクラーゼS」、ペクチナーゼ、キシラナーゼ「商品名スクラーゼA」、インベルターゼ、パパイン「精製パパイン」、ホスホリパーゼ「ホスホリパーゼA1」、タンナーゼ、デキストラナーゼ「デキストラナーゼ2F」等を挙げることができ、少なくとも1種を選択することができる。さらにシステイン酵素やパイナップル酵素なども使用される。 In the present invention, an enzyme agent using an enzyme as a main ingredient can also be used. Examples of the enzyme agent include coculase P, α-amylase, glucoamylase, rotease “trade name coclase”, amylase “trade name coclase G2”, cellulase “trade name sucrase C”, and xylanase (hemicellulase) from Mitsubishi Foods Corporation. , "Trade name sucrase X", pectinase "trade name sucrase N", pectinase "trade name sucrase S", pectinase, xylanase "trade name sucrase A", invertase, papain "purified papain", phospholipase "phospholipase A1", tannase, Dextranase “dextranase 2F” and the like can be mentioned, and at least one can be selected. In addition, cysteine enzymes and pineapple enzymes are also used.
 本発明では、好ましくはタンパク質分解酵素や植物繊維分解酵素(セルラーゼ、ペクチナーゼ等)からなる群から選ばれた少なくとも1種の酵素を用いることが効果的である。さらにタンパク質分解酵素を単独又は他の酵素と共用して用いることも効果的である。 In the present invention, it is preferable to use at least one enzyme selected from the group consisting of proteolytic enzymes and plant fiber degrading enzymes (cellulase, pectinase, etc.). It is also effective to use a proteolytic enzyme alone or in combination with other enzymes.
 特許文献4には、コーヒーの食用原材料から食用抽出生成物を製造する方法について、食用原材料を粒子に粉砕し、粒子を水中で抽出して抽出物を生成させ、フィルタを用いて濾過する前に、抽出物中の炭水化物を凝集させる為に酵素を添加する方法が開示されているが、本発明は、コーヒー果実の高圧処理物の製造方法において、高圧処理を施す工程前に、所定濃度の酵素添加水を投入して所定の高圧処理を施すことにより、コーヒー果実からの液状化を促進して、種子部と種子部以外の部の少なくとも1種の処理物を分離する、コーヒー果実の高圧処理物の製造方法に関する。 Patent Document 4 discloses a method for producing an edible extract product from an edible raw material of coffee, before the edible raw material is pulverized into particles, the particles are extracted in water to produce an extract, and filtered using a filter. A method of adding an enzyme for agglutinating carbohydrates in an extract is disclosed, but the present invention relates to a method for producing a high-pressure processed product of coffee fruit before the step of applying high-pressure treatment. High-pressure treatment of coffee fruit that promotes liquefaction from coffee fruit by adding added water and performs predetermined high-pressure treatment to separate at least one processed product from the seed part and the part other than the seed part The present invention relates to a method for manufacturing a product.
 また、本発明の実施形態に係る発明では、コーヒー果実に10~1000MPaの高圧処理を施す工程が、コーヒー果実を高圧装置に投入する第1工程と高圧装置内の圧力を10~1000MPaの範囲で実施する第2工程からなり、第2工程の後で、処理物を高圧装置から取り出す第3工程を含んでも良い。 Further, in the invention according to the embodiment of the present invention, the step of subjecting the coffee fruit to a high pressure treatment of 10 to 1000 MPa includes the first step of charging the coffee fruit into the high pressure device and the pressure in the high pressure device in the range of 10 to 1000 MPa. It may comprise a second step to be performed, and may include a third step after the second step for removing the processed material from the high-pressure apparatus.
 その為、大量のコーヒー果実の高圧処理を行う際には、第1工程~第3工程を行った後、新たなコーヒー果実原料を第1工程に投入して第1工程~第3工程を流れ作業的に順次繰返して行うことができる高圧装置を用いることができる。このような高圧装置には、前記第1工程~前記第3工程を行った後、新たなコーヒー果実原料を第1工程に投入して第1工程~第3工程を順次流れ作業として行うことができる。 For this reason, when high-pressure processing of a large amount of coffee fruit is performed, after the first to third steps, a new coffee fruit raw material is added to the first step and the first to third steps flow. It is possible to use a high-pressure apparatus that can be sequentially and repeatedly performed in terms of work. In such a high-pressure apparatus, after performing the first step to the third step, a new coffee fruit raw material is introduced into the first step, and the first step to the third step are sequentially performed as a flow operation. it can.
 図3は、従来技術(1)水洗式(ウォッシュト法)と呼ばれるコーヒー豆の加工方式の概略工程を示す。この方式では、収穫したコーヒー果実はパルパー(果肉除去機)でその外皮と果肉を除去し、次いで発酵槽に移して1日~2日間、酵素の力でぬめりのあるミューシレージ(ペクチン質)を分解除去する。産地によっては、発酵槽を用いないで、ミューシレージムーバーと呼ばれる機械でぬめりを強制的に除去することもある。発酵槽処理後は、ぬめりの取れたパーチメント(内果皮)付きコーヒー生豆を水洗する。水洗後、含水率が11~12質量%程度になるまで乾燥し、脱穀機でパーチメントを取り除き、生豆を取り出す。 FIG. 3 shows a schematic process of a coffee bean processing method called a prior art (1) water-washing method (washed method). In this method, the harvested coffee berries are removed with a pulper (pulp remover), then the outer skin and pulp are removed, and then transferred to a fermenter to decompose mucilage (pectin) that is slimy by the power of enzymes for 1-2 days. Remove. Depending on the production area, the slime may be forcibly removed by a machine called a musi-jim bar without using a fermenter. After the fermenter treatment, the green coffee beans with parchment (endum) are removed. After washing with water, it is dried until the water content becomes about 11 to 12% by mass, the parchment is removed with a threshing machine, and the green beans are taken out.
 図4は、従来技術(2)スマトラ式(ウエットハル法)によるコーヒー豆の加工方式の概略工程を示す。この方式では、収穫したコーヒー果実はパルパーでその外皮と果肉を除去し、ぬめり(ミューシレージ)とパーチメント(内果皮)の付いたまま、水分40~50質量%程度まで乾燥する。その後、脱穀機でパーチメントを取り除き、生豆を取り出す。脱穀された生豆は、含水率が11~12質量%程度になるまで乾燥する。 FIG. 4 shows a schematic process of the coffee beans processing method by the prior art (2) Sumatra method (wet hull method). In this method, the harvested coffee berries are removed with a pulper, and the skin and flesh are removed and dried to a moisture content of 40 to 50% by mass with mucilage and parchment (endocarps) attached. Then, remove the parchment with a threshing machine and take out the green beans. The threshed raw beans are dried until the water content becomes about 11 to 12% by mass.
 図5は、従来技術(3)ブラジル式(パルプトナチュラル法)によるコーヒー豆の加工方式の概略工程を示す。この方式では、収穫したコーヒー果実はパルパーでその外皮と果肉を除去し、ぬめり(ミューシレージ)とパーチメント(内果皮)の付いたままで、カリカリの状態まで乾燥する。その後、脱穀機でミューシレージとパーチメントを取り除き、生豆を取り出す。 FIG. 5 shows a schematic process of a coffee bean processing method according to the prior art (3) Brazilian method (pulp to natural method). In this method, the harvested coffee berries are crushed with pulper and the flesh is removed and dried to a crunchy state with mucilage and parchment. Then remove musilage and parchment with a threshing machine and take out the green beans.
 図6は、従来技術(4)自然乾燥式(ナチュラル法)によるコーヒー豆の加工方式の概略工程を示す。この方式は、収穫したコーヒー果実を敷物の上に拡げて長期間乾燥してカリカリの状態になったところで脱穀し生豆を取り出すシンプルな方法である。産地の自然環境等に対応して採用される。 FIG. 6 shows a schematic process of a coffee bean processing method according to the prior art (4) natural drying method (natural method). This method is a simple method in which the harvested coffee fruit is spread on a rug and dried for a long period of time, and then threshed to take out raw beans. Adopted according to the natural environment of the production area.
 このように、従来技術(1)~(4)は、加工プロセスに、パルパー(果肉除去機)工程、発酵工程(1日~2日程度)、乾燥工程(長期風乾)、水洗工程、脱穀工程等の多くの工程を必要とするが、産地の自然環境を活かしたプロセスと言える。 As described above, in the prior arts (1) to (4), the processing process includes a pulper (pulp removal machine) process, a fermentation process (about 1 to 2 days), a drying process (long-term air drying), a water washing process, and a threshing process. It is a process that takes advantage of the natural environment of the production area.
(有益成分の物質の単離)
 前述のように、本発明のコーヒー果実の高圧処理物の製造方法によって得られるゼリー状物(液状物)から、食品等に有効な成分を単離することができる。その代表的な成分の化合物誘導体としては、クロロゲン酸誘導体(chlorogenic acid、別名;カフェオイルキナ酸 (caffeoylquinic acid) 等のポリフェノール系化合物、高分子~低分子の多糖類、カフェイン、フラボノール等が挙げられる。特に最近では、ポリフェノール系化合物は、病気や老化の原因となる活性酸素を減らす作用があることが知られている。図7は、このうちクロロゲン酸誘導体の代表的な成分の化学構造を示す。
(Isolation of beneficial ingredients)
As described above, components effective for foods and the like can be isolated from the jelly-like product (liquid product) obtained by the method for producing a high-pressure processed product of coffee fruits of the present invention. Typical compound derivatives include chlorogenic acid (also known as caffeoylquinic acid), polyphenolic compounds such as caffeoylquinic acid, high to low molecular weight polysaccharides, caffeine, and flavonols. Recently, it has been known that polyphenolic compounds have the effect of reducing active oxygen which causes illness and aging, etc. Figure 7 shows the chemical structure of typical components of chlorogenic acid derivatives. Show.
 本発明では従来技術(1)~(4)に比べて、用いる水量を限定できるために、高圧処理後の有効成分を含む水溶液の濃縮に多くのエネルギーと時間を要することなく、有効成分の単離を容易にできる利点がある。 In the present invention, since the amount of water used can be limited as compared with the prior arts (1) to (4), the concentration of the aqueous solution containing the active ingredient after the high-pressure treatment does not require much energy and time, and the single active ingredient can be used. There is an advantage that separation is easy.
 また、本発明のコーヒー果実の高圧処理を行った後、種子部と種子部以外の部の処理物に対して、CO2超臨界処理をさらに加えることにより、当該種子部と種子部以外の部の処理物からCO2流体に可溶な分解成分を取り除くことができ、前記有効成分の単離を容易にするだけでなく、コーヒー生豆(種子部)の焙煎後の飲料としてコクや旨味のバランスを改良することができる。 In addition, after performing the high pressure treatment of the coffee fruit of the present invention, by further adding a CO2 supercritical treatment to the treated product of the seed part and the part other than the seed part, Decomposed components soluble in CO2 fluid can be removed from the processed product, not only facilitating the isolation of the active ingredients, but also the balance of richness and taste as a beverage after roasting coffee beans (seed part) Can be improved.
 以下、本発明を実施例によってさらに詳細に説明するが、本発明は実施例に限定されない。 Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to the examples.
実施例1(サンプル1)
 コーヒー果実約20gを計量して、透明なラミネート加工袋(福助工業(株)製、Rタイプ)(本明細書ではラミネート加工袋と記載する)に入れ、所定の方法で吸引脱気しシーラーで密封、これを温度75℃、100MPa下の高圧処理装置内に設置して、24時間の高圧処理を実施した。コーヒー果実の入ったラミネート加工袋を高圧処理装置から取り出したところ、コーヒー果実の形状は保たれているものの液状物が浸み出していたなお、図8は、実施例で用いたコーヒー果実(原料)の外観写真である。図9は、高圧処理を施す前のラミネート加工袋内に収納されたコーヒー果実(原料)の外観写真である。図10のサンプル1図は、実施例1の高圧処理を施した後の外観写真である(表1参照)。表1中、液状物の浸み出しをラミネート加工袋の外観から観測できたものを「○」、多くの液状物の観測できたものを「◎」、原形のままで液状物の浸み出しが見られないのを「×」と判定して記載した。
Example 1 (Sample 1)
About 20 g of coffee fruit is weighed and placed in a transparent laminating bag (R type) manufactured by Fukusuke Kogyo Co., Ltd. (referred to as a laminating bag in this specification), and sucked and deaerated by a predetermined method with a sealer This was sealed and placed in a high-pressure treatment apparatus at a temperature of 75 ° C. and 100 MPa, and a high-pressure treatment for 24 hours was performed. When the laminating bag containing the coffee fruit was taken out of the high pressure processing apparatus, the liquid was oozing out although the shape of the coffee fruit was maintained . In addition, FIG. 8 is an external appearance photograph of the coffee fruit (raw material) used in the example. FIG. 9 is an appearance photograph of coffee fruit (raw material) stored in a laminated bag before high pressure treatment. The sample 1 figure of FIG. 10 is an external appearance photograph after performing the high-pressure process of Example 1 (refer Table 1). In Table 1, “○” indicates that the liquid leaching can be observed from the appearance of the laminated bag, “◎” indicates that many liquids can be observed, and oozes the liquid in its original form. It was judged as “x” that no was observed.
実施例2(サンプル2)
 コーヒー果実と等量の水を密封した以外は、実施例1と同様に実施したところ、コーヒー果実の形状は保たれているものの液状物が浸み出していた(表1参照)。図10のサンプル2図は、実施例2の高圧処理を施した後の外観写真である。
Example 2 (Sample 2)
When carried out in the same manner as in Example 1 except that the same amount of water as that of the coffee fruit was sealed, the shape of the coffee fruit was maintained, but a liquid was leached (see Table 1). Sample 2 in FIG. 10 is an appearance photograph after the high-pressure treatment of Example 2 is performed.
実施例3(サンプル3)
 (株)超臨界技術研究所製「酵素D」(セルラーゼ+ペクチナーゼ、植物繊維分解酵素)を0.01g添加した以外は、実施例2と同様に実施したところ、コーヒー果実の形状は大きく崩れ、コーヒー果実から多くの液状物が浸み出ていた(表1参照)。図10のサンプル3図は、実施例3の高圧処理を施した後の外観写真である。
Example 3 (Sample 3)
Except for adding 0.01 g of "Enzyme D" (cellulase + pectinase, plant fiber degrading enzyme) manufactured by Supercritical Technology Laboratory, the shape of the coffee fruit was greatly collapsed. Many liquids oozed from the coffee fruit (see Table 1). Sample 3 in FIG. 10 is an appearance photograph after the high-pressure treatment in Example 3 is performed.
実施例4(サンプル4)
 (株)超臨界技術研究所製「酵素E」(プロテアーゼ、タンパク質分解酵素)を0.01g添加した以外は、実施例2と同様に実施したところ、コーヒー果実の形状は大きく崩れ、コーヒー果実から多くの液状物が浸み出ていた(表1参照)。図10のサンプル4図は、実施例4の高圧処理を施した後の外観写真である。
Example 4 (Sample 4)
Except for adding 0.01 g of “Enzyme E” (protease, proteolytic enzyme) manufactured by Supercritical Technology Laboratory Co., Ltd., it was carried out in the same manner as in Example 2; Many liquids were leached (see Table 1). Sample 4 in FIG. 10 is an appearance photograph after the high-pressure treatment of Example 4 is performed.
実施例5(サンプル5)
 三菱化学フード(株)製「酵素P」(パパイン酵素)を0.01g添加した以外は、実施例2と同様に実施したところ、コーヒー果実の形状は大きく崩れ、コーヒー果実から多くの液状物が浸み出ていた(表1参照)。図10のサンプル5図は、実施例5の高圧処理を施した後の外観写真である。
Example 5 (Sample 5)
Except for adding 0.01 g of “Enzyme P” (papain enzyme) manufactured by Mitsubishi Chemical Food Co., Ltd., it was carried out in the same manner as in Example 2; It oozed out (see Table 1). Sample 5 in FIG. 10 is an appearance photograph after the high-pressure treatment of Example 5 is performed.
 なお、酵素D(実施例3)と酵素E(実施例4)を比べると、酵素Dを加えた場合の方がコーヒー果実の形状の崩れが大きく、より多くの液状物が生成していた。一方、酵素P(実施例5)を用いた場合は、多くの液状物の中に多くの生豆が抜け出ていた。このように、複数の酵素を用いた場合には、酵素添加効果が顕現に現れた。
 実施例5で高圧処理して得られたサンプル5から液状物とコーヒー豆を分離し、液状物を特許文献2の記述等を参照してその有効成分を分析したところ、カフェイン、クロロゲン酸、カテキン、エピカテキンを検出した。これらの有効成分の収得率は、VDF FutureCeuticals社の公開情報(http://www.coffeeberry.com/chemistry-comparison-whole-coffee-green-coffee-bean)のデータ値の理論値を参考にすると収率20%~50%程度と推定された。
In addition, when the enzyme D (Example 3) and the enzyme E (Example 4) were compared, when the enzyme D was added, the shape of the coffee fruit was greatly deformed, and more liquid product was produced. On the other hand, when the enzyme P (Example 5) was used, many green beans slipped out in many liquids. As described above, when a plurality of enzymes are used, the effect of enzyme addition appears clearly.
The liquid and coffee beans were separated from the sample 5 obtained by high-pressure treatment in Example 5, and the liquid was analyzed for its active ingredients with reference to the description of Patent Document 2, etc. As a result, caffeine, chlorogenic acid, Catechin and epicatechin were detected. The yields of these active ingredients are based on the theoretical values of the data values published by VDF FutureCeuticals (http://www.coffeeberry.com/chemistry-comparison-whole-coffee-green-coffee-bean). The yield was estimated to be about 20% to 50%.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
実施例6
 「酵素P」(パパイン酵素)を0.01gから0.2gに変更にした以外は、実施例5と同様に実施して、コーヒー果実から染み出た液状物の成分をHPLC(高速液体クロマトグラフィー)で分析したところ、図11に示すように、クロロゲン酸、カフェイン酸及びカフェインが検出された。なお、コーヒー果実から染み出た液状物は、所定の方法で液状物とコーヒー豆をフィルタ等を用いてろ過分離した。HPLC測定は、当業者が通常用いる方法、例えばODSカラム、カラムオーブン30℃、溶離液;1質量%ギ酸水溶液のアセトニトリル溶離液(アセトニトリル1部;当該水溶液9部)、流量1mL/分、検出器;紫外可視分光検出器UV-vis (325nm)で実施した。
Example 6
Except that the amount of “enzyme P” (papain enzyme) was changed from 0.01 g to 0.2 g, the same procedure as in Example 5 was carried out, and the components of the liquid material exuded from the coffee fruit were analyzed by HPLC (high performance liquid chromatography). ), Chlorogenic acid, caffeic acid and caffeine were detected as shown in FIG. In addition, the liquid which exuded from the coffee fruit was separated by filtering the liquid and coffee beans using a filter or the like by a predetermined method. HPLC measurement is a method commonly used by those skilled in the art, for example, ODS column, column oven 30 ° C., eluent; acetonitrile eluent of 1% by weight aqueous formic acid (1 part acetonitrile; 9 parts aqueous solution), flow rate 1 mL / min, detector An ultraviolet-visible spectroscopic detector UV-vis (325 nm).
実施例7
 高圧処理の時間を17時間に変更し、「酵素P」(パパイン酵素)を0.01gから0.2gに変更した以外は、実施例5と同様に実施して、クロロゲン酸及びカフェイン酸の抽出(回収量)に対する圧力依存性を調べたところ、図12に示す結果を得た。なお、図12では比較として圧力をかけない時の成分回収量と対比した。成分の回収量は、高圧処理後の液状物を分離し所定の方法でpHを4~5に調整して、所定の方法で分析した。図12で明らかなように、100MPaの高圧下の方がクロロゲン酸(Chloro_A.)及びカフェイン酸(Caffe_A.)を多く抽出できることがわかった。
Example 7
The same procedure as in Example 5 was carried out except that the high-pressure treatment time was changed to 17 hours and “enzyme P” (papain enzyme) was changed from 0.01 g to 0.2 g. When the pressure dependence with respect to extraction (recovery amount) was investigated, the result shown in FIG. 12 was obtained. In addition, in FIG. 12, it compared with the component recovery amount when a pressure is not applied as a comparison. The recovered amounts of the components were analyzed by a predetermined method after separating the liquid after high pressure treatment and adjusting the pH to 4 to 5 by a predetermined method. As is clear from FIG. 12, it was found that more chlorogenic acid (Chloro_A.) And caffeic acid (Caffe_A.) Can be extracted under a high pressure of 100 MPa.
実施例8
 処理温度の依存性を調べる為に、処理温度を75℃と65℃にし、酵素を「酵素P」(パパイン酵素)単独で、また酵素Pと「酵素D」(セルラーゼ系:セルラーゼ+ペクチナーゼ)を当量、及び酵素Pと「酵素E」(プロテアーゼ)を当量で用い、用いた酵素全量を0.01gから0.2gに変更した以外は、実施例5と同様に実施して、クロロゲン酸及びカフェイン酸の抽出(回収量)に対する処理温度依存性を調べたところ、図13に示す結果を得た。成分の回収量は、実施例7に準じて実施した。図13で明らかなように、75℃下での高圧処理の方が65℃よりもクロロゲン酸(Chloro_A.)及びカフェイン酸(Caffe_A.)を多く抽出できることがわかった。
Example 8
In order to investigate the dependence of the treatment temperature, the treatment temperature is set to 75 ° C. and 65 ° C., the enzyme “enzyme P” (papain enzyme) alone, and the enzyme P and “enzyme D” (cellulase system: cellulase + pectinase) The same procedure as in Example 5 was conducted except that the equivalent amount of enzyme P and “enzyme E” (protease) were used in equivalent amounts, and the total amount of enzyme used was changed from 0.01 g to 0.2 g. When the treatment temperature dependency on the extraction (recovered amount) of inacid was examined, the results shown in FIG. 13 were obtained. The amount of components recovered was the same as in Example 7. As is clear from FIG. 13, it was found that high-pressure treatment at 75 ° C. can extract more chlorogenic acid (Chloro_A.) And caffeic acid (Caffe_A.) Than 65 ° C.
比較例1
 コーヒー果実約20gと水20g(等量分)を計量して、透明なラミネート加工袋に入れ、所定の方法で吸引脱気しシーラーで密封、これを室温、大気圧下で24時間静して観察した。ラミネート加工袋中のコーヒー果実の外観には全く変化は見られなかった(表2参照)。なお、表2における外観判定は、表1と同じ判定とした。
Comparative Example 1
Weigh about 20 g of coffee fruit and 20 g of water (equal portion), put in a transparent laminated bag, suck and deaerate with a prescribed method, seal with a sealer, and let stand at room temperature and atmospheric pressure for 24 hours Observed. There was no change in the appearance of the coffee fruit in the laminated bag (see Table 2). The appearance determination in Table 2 was the same as that in Table 1.
比較例2
 酵素Dを0.01g添加した以外は、比較例1と同様に実施したところ、ラミネート加工袋中のコーヒー果実の外観には全く変化は見られなかった(表2参照)
Comparative Example 2
When carried out in the same manner as Comparative Example 1 except that 0.01 g of enzyme D was added, no change was observed in the appearance of the coffee fruit in the laminated bag (see Table 2).
Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002
 このように、本発明のコーヒー果実の高圧処理方法から、従来にはないコーヒー豆(種子)やパルプ等由来からくる植物繊維分解物の有効成分が製造できる。食品等用の有効成分となる物質は、さらに牛、豚、鳥、魚等への飼料添加用途や健康維持用サプリメント、健康飲料用途に幅広く利用される。 Thus, from the high-pressure treatment method for coffee fruit according to the present invention, an active ingredient of a plant fiber degradation product derived from coffee beans (seed), pulp, etc., which has not been conventionally available, can be produced. Substances serving as active ingredients for foods and the like are further widely used for feed addition to cattle, pigs, birds, fish, etc., health maintenance supplements, and health drinks.
1:外皮
2:果肉
3: ミューレージ(粘液質:ペクチン質)
4:パーチメント(内果皮)
5:種子
 
1: Hull 2: Flesh 3: Mureage (Mucous: Pectin)
4: Parchment (endocarp)
5: Seeds

Claims (11)

  1.  前記コーヒー果実の質量に対し100質量倍以下の範囲で、0.001~10質量%の酵素を含む水溶液を前記コーヒー果実に添加し10~1000MPaの高圧処理を施す工程と、
     その後、種子部と種子部以外の部の少なくとも1種の処理物を分離する工程とを
     有することを特徴とするコーヒー果実の高圧処理物の製造方法。
    A step of adding an aqueous solution containing 0.001 to 10% by mass of an enzyme to the coffee fruit within a range of 100 mass times or less with respect to the mass of the coffee fruit and subjecting the coffee fruit to a high pressure treatment of 10 to 1000 MPa;
    And a step of separating at least one processed product from the seed part and a part other than the seed part. A method for producing a high-pressure processed coffee fruit product.
  2.  前記高圧処理の温度が30~120℃の範囲であることを特徴とする請求項1に記載のコーヒー果実の高圧処理物の製造方法。 2. The method for producing a high-pressure processed coffee fruit product according to claim 1, wherein the temperature of the high-pressure treatment is in the range of 30 to 120 ° C.
  3.  前記高圧処理を施す際に、pH調整可能な化合物を添加することを特徴とする請求項1又は2に記載のコーヒー果実の高圧処理物の製造方法。 The method for producing a high-pressure treated product of coffee fruit according to claim 1 or 2, wherein a compound capable of adjusting pH is added when the high-pressure treatment is performed.
  4.  前記高圧処理を施す工程が、前記コーヒー果実と前記水溶液とを高圧装置に投入する第1工程と、前記高圧装置内の圧力を10~1000MPaの範囲にして前記高圧処理を実施する第2工程とを有することを特徴とする請求項1乃至3の何れか1項に記載のコーヒー果実の高圧処理物の製造方法。 The step of performing the high pressure treatment includes a first step of charging the coffee fruit and the aqueous solution into a high pressure device, and a second step of performing the high pressure treatment with the pressure in the high pressure device in the range of 10 to 1000 MPa. The method for producing a high-pressure processed product of coffee fruit according to any one of claims 1 to 3, wherein:
  5.  前記第2工程の後で、処理物を前記高圧装置から取り出す第3工程を含むことを特徴とする請求項4に記載のコーヒー果実の高圧処理物の製造方法。 The method for producing a high-pressure processed coffee fruit product according to claim 4, further comprising a third step of removing the processed product from the high-pressure apparatus after the second step.
  6.  前記第1工程から前記第3工程を行った後、新たなコーヒー果実を前記高圧装置に投入して第1工程から第3工程を順次繰り返すことを特徴とする請求項5に記載のコーヒー果実の高圧処理物の製造方法。 The coffee fruit according to claim 5, wherein after performing the third process from the first process, a new coffee fruit is put into the high-pressure apparatus and the first process to the third process are sequentially repeated. Manufacturing method of high-pressure processed product.
  7.  分離された前記種子部を乾燥する工程、又は、分離された前記種子部以外の部からコーヒー果実に含まれる成分を分離する工程を含むことを特徴とする請求項1乃至6の何れか1項に記載のコーヒー果実の高圧処理物の製造方法。 7. The method according to claim 1, further comprising a step of drying the separated seed part or a step of separating components contained in the coffee fruit from parts other than the separated seed part. The manufacturing method of the high pressure processed material of the coffee fruit of description.
  8.  請求項1乃至7の何れか1項に記載のコーヒー果実の高圧処理物の製造方法から得られることを特徴とする処理物。 A processed product obtained from the method for producing a high-pressure processed product of coffee fruit according to any one of claims 1 to 7.
  9.  コーヒー果実の質量に対し100質量倍以下の範囲で、0.001~10質量%の酵素を含む水溶液を前記コーヒー果実に添加し10~1000MPaの高圧処理を施すことを特徴とするコーヒー果実の高圧処理方法。 A high pressure of coffee fruit characterized by adding an aqueous solution containing 0.001 to 10% by mass of an enzyme to the coffee fruit within a range of 100 mass times or less with respect to the mass of the coffee fruit, and subjecting the coffee fruit to a high pressure treatment of 10 to 1000 MPa. Processing method.
  10.  前記高圧処理時の温度が30~120℃の範囲であることを特徴とする請求項9に記載のコーヒー果実の高圧処理方法。 The method for high-pressure treatment of coffee fruit according to claim 9, wherein the temperature during the high-pressure treatment is in the range of 30 to 120 ° C.
  11.  前記高圧処理を施す際に、pH調整可能な化合物を添加することを特徴とする請求項9又は10に記載のコーヒー果実の高圧処理方法。
     
    The method for high-pressure treatment of coffee fruit according to claim 9 or 10, wherein a compound capable of adjusting pH is added when the high-pressure treatment is performed.
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