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JP4453829B2 - Method for producing powder soluble coffee - Google Patents
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JP4453829B2 - Method for producing powder soluble coffee - Google Patents

Method for producing powder soluble coffee Download PDF

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JP4453829B2
JP4453829B2 JP2005067378A JP2005067378A JP4453829B2 JP 4453829 B2 JP4453829 B2 JP 4453829B2 JP 2005067378 A JP2005067378 A JP 2005067378A JP 2005067378 A JP2005067378 A JP 2005067378A JP 4453829 B2 JP4453829 B2 JP 4453829B2
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JP2006246784A (en
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昌志 神田
剛 前田
治 柏井
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ユーシーシー上島珈琲株式会社
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Description

本発明は粉末可溶性コーヒーの製造方法に関し、詳しくは、粉末コーヒーをそのままお湯などに溶解して飲むことができる粉末可溶性コーヒーの製造方法に関する。   The present invention relates to a method for producing powder-soluble coffee, and more particularly, to a method for producing powder-soluble coffee in which powdered coffee can be directly dissolved in hot water or the like.

レギュラーコーヒーは、生豆コーヒーを焙煎機で焙煎し、焙煎したコーヒー豆をロール状の粉砕機などを用いて粉砕し粉末コーヒーとなる。この粉末コーヒーに熱水を注いで抽出することにより、飲用する。抽出器具としては、ペーパーフィルターやサイフォン、パーコレーターなどが用いられるが、どの器具もろ過した抽出液を飲むためのものである。   Regular coffee is roasted using a roasting machine, and the roasted coffee beans are pulverized using a roll-type pulverizer to form powdered coffee. It is drunk by pouring hot water into this powdered coffee and extracting it. Paper filters, siphons, percolators, etc. are used as the extraction device, but all devices are for drinking filtered extracts.

このようなレギュラーコーヒーの一般的な飲用に対して、粉末コーヒーをそのままお湯に溶解して飲むことのできるレギュラーコーヒーも開発されている。例えば、焙煎コーヒー豆を微粉砕し、この微粉末コーヒーを抽出ろ過することなく溶解して飲用に供するようにした発明が、特許文献1に開示されている。   In contrast to the regular drinking of regular coffee, regular coffee that can be taken by dissolving powdered coffee directly in hot water has been developed. For example, Patent Document 1 discloses an invention in which roasted coffee beans are finely pulverized, and the fine powdered coffee is dissolved and extracted without being filtered.

特許文献1に記載されている発明は、焙煎したコーヒー豆を湿式粉砕し、これを噴霧乾燥して微粉末可溶性のレギュラーコーヒーを得るものである。
特開2003−9768号公報
In the invention described in Patent Document 1, roasted coffee beans are wet-ground and spray-dried to obtain fine powder-soluble regular coffee.
JP 2003-9768 A

コーヒーは、一般に、ろ過して飲用されるため、抽出液中には不溶性固形分はほとんど存在しておらず、従って、コーヒー飲用時に、容器の底部に沈殿物が残存することは品質上劣るとされるところ、上記従来技術の方法は、容器の底部に少なくない不溶性沈固形物が残存し、必ずしも品質上好ましいものではなく、改善が要請されていた。   Since coffee is generally drunk after filtration, there is almost no insoluble solid content in the extract. Therefore, when coffee is drunk, the presence of a precipitate at the bottom of the container is inferior in quality. However, the above-mentioned conventional method has a large amount of insoluble precipitated solids remaining at the bottom of the container, which is not necessarily preferable in terms of quality, and has been requested to be improved.

また、焙煎コーヒー豆をディスク式、衝撃式、ボールミル式、ジェット気流粉砕式などの方式を用いて、より一層微粉砕することも考えられるが、これらの方式を用いたとしても、コーヒー豆に含まれる油分が分離して、微粉砕したコーヒー粉体を凝集させ、結局、容器底部に固形分が残存することになる。   In addition, it is conceivable to further pulverize roasted coffee beans using a disc type, impact type, ball mill type, jet stream type, etc., but even if these methods are used, The contained oil component is separated and the finely ground coffee powder is agglomerated, so that the solid content remains at the bottom of the container.

本発明者らは、コーヒーの微粉末化について鋭意研究した結果、微細化した焙煎コーヒー豆を湿式粉砕し、得られた懸濁液中に含まれる50μm以上の粒子を湿式状態にてろ過分級し、後乾燥することにより容器底部に固形分が残存し難くなり、飲用時にざらつき感を消失させることを見出し、本発明を完成した。   As a result of diligent research on the pulverization of coffee, the present inventors conducted wet pulverization of the refined roasted coffee beans, and filtered and classified particles of 50 μm or more contained in the obtained suspension in a wet state. And after drying, it became difficult for solid content to remain in a container bottom part, and it discovered that a feeling of roughness was lost at the time of drinking, and completed the present invention.

そこで、本発明の目的は、上記従来技術の有する問題点に鑑みて、粉末コーヒーをそのままお湯などに溶解して飲むことができ、しかも容器底部に不溶性固形物が残存せず、飲用時にざらつき感のない粉末可溶性コーヒーの製造方法を提供することにある。   Therefore, in view of the above-described problems of the prior art, the object of the present invention is to allow powdered coffee to be directly dissolved in hot water and to drink it, and insoluble solids do not remain at the bottom of the container, making it feel rough when drinking. It is an object of the present invention to provide a method for producing a powder-soluble coffee having no powder.

上記課題は、各請求項記載の発明により達成される。すなわち、本発明に係る粉末可溶性コーヒーの製造方法の特徴構成は、焙煎コーヒー豆と水とを混合し、この焙煎コーヒー豆をメジアン径30μm以下に湿式粉砕し、得られたコーヒー懸濁液を55μm以下に分級し、その後乾燥することにある。   The above-mentioned subject is achieved by the invention described in each claim. That is, the characteristic constitution of the method for producing powder soluble coffee according to the present invention is that the roasted coffee beans and water are mixed, the roasted coffee beans are wet-ground to a median diameter of 30 μm or less, and the resulting coffee suspension Is classified to 55 μm or less and then dried.

この構成によれば、複雑で面倒な工程を経ることなく、溶解させた際に沈殿が残り難く、飲用した場合にはザラツキ感の感じられないコーヒー飲料が得られる。特に、湿式粉砕を採用しているので、他の粉砕方法、例えばディスク式粉砕法、衝撃式粉砕法、ボールミル法、ジェット気流法などで行う場合、コーヒー豆に含まれる油分の存在のため、微細に粉砕された粒子間に凝集が容易に生じて、メジアン径の小さい微細粉末が得られないのに対して、本発明によれば確実に微細粉末を得ることができる。また、凍結粉砕法によっても、メジアン径50μ以下にすることは一般に困難であり、しかも湿式粉砕に比べて、粉砕処理コストが高くなる。このように、本発明の場合、湿式粉砕した後、分級するようにしているので、粉体が凝集することなく、微細なコーヒー粒子として確実に分級ができ、設備コストおよび粉砕処理コストが安価に済み、メジアン径の小さい微細な粉体が比較的短時間で確実に得られるため、実生産に適する。   According to this configuration, a coffee beverage that does not have a precipitate when it is dissolved and does not feel rough when drunk can be obtained without going through complicated and troublesome processes. In particular, since wet pulverization is adopted, when using other pulverization methods such as disk pulverization method, impact pulverization method, ball mill method, jet stream method, etc. Aggregation easily occurs between the pulverized particles, and a fine powder having a small median diameter cannot be obtained. On the other hand, according to the present invention, a fine powder can be reliably obtained. Further, even by freeze pulverization, it is generally difficult to make the median diameter 50 μm or less, and the pulverization cost becomes higher than wet pulverization. Thus, in the case of the present invention, since it is classified after wet pulverization, the powder can be reliably classified as fine coffee particles without agglomeration, and the equipment cost and pulverization cost can be reduced. It is suitable for actual production because fine powder with a small median diameter can be obtained reliably in a relatively short time.

その結果、粉末コーヒーをそのままお湯などに溶解して飲むことができ、しかも容器底部に不溶性固形物が残存せず、飲用時にざらつき感のない粉末可溶性コーヒーの製造方法を提供することができた。   As a result, it was possible to provide a method for producing powdered soluble coffee that can be used by dissolving powdered coffee in hot water or the like as it is, and insoluble solids do not remain at the bottom of the container, and that does not feel rough during drinking.

前記湿式粉砕を行う前に、前記焙煎コーヒー豆を予め乾式粉砕または凍結粉砕を行い、メジアン径を100μm以下にすることが好ましい。   Before the wet pulverization, the roasted coffee beans are preferably dry pulverized or freeze pulverized in advance so that the median diameter is 100 μm or less.

この構成によれば、湿式粉砕を一層効率的に短時間に、メジアン径の小さい粒径のコーヒー粒子を得ることができる。   According to this configuration, it is possible to obtain coffee particles having a small median diameter in a shorter time by wet pulverization more efficiently.

前記湿式粉砕を、径0.5mm以下の球形ビーズを混在させて粉砕すると共に、前記分級を、篩を用いて行うことが好ましい。   It is preferable that the wet pulverization is performed by mixing spherical beads having a diameter of 0.5 mm or less and the classification is performed using a sieve.

この構成によれば、上記したように、湿式粉砕された微細なコーヒー粉末を篩により分級するので、乾式の状態で分級する場合(粉砕時に溶出した油分によって粒子が互いに凝集する)に比べて、粒子間の凝集を生じることがなく、メジアン径の小さい粒径のコーヒー粒子を得るのに一層短時間に行うことができる。   According to this configuration, as described above, the finely ground coffee powder that has been wet-ground is classified by the sieve, so compared to the case of classification in a dry state (particles agglomerate with each other by the oil eluted during the grinding), Aggregation between particles does not occur, and coffee particles having a small median diameter can be obtained in a shorter time.

本発明に係る粉末可溶性コーヒーの製造方法の実施形態を、図面を参照して詳細に説明する。本実施形態に係る粉末可溶性コーヒーの製造方法は、図1に示すように、コーヒー豆を常法により焙煎して焙煎コーヒー豆を製造する(♯1)。焙煎条件については、特に限定されるものではなく、各種焙煎度合いに応じた焙煎がなされればよい。   An embodiment of a method for producing a powder soluble coffee according to the present invention will be described in detail with reference to the drawings. As shown in FIG. 1, the method for producing powder-soluble coffee according to the present embodiment roasts coffee beans by a conventional method to produce roasted coffee beans (# 1). The roasting conditions are not particularly limited as long as roasting is performed according to various roasting degrees.

焙煎されたコーヒー豆は、湿式粉砕する前に、予備処理としてメジアン径約100μm以下程度にまで一次粉砕する(♯2)。この場合の粉砕方法は、特に限定されるものではなく、乾式、湿式、凍結粉砕など各種の粉砕方法を採用できる。この予備処理は、必ずしも必要ではないが、次工程で行う湿式粉砕を、短時間で所定の粒径に効率よく行うために実施することが望ましい。   The roasted coffee beans are first ground to a median diameter of about 100 μm or less as a pretreatment before being wet ground (# 2). The pulverization method in this case is not particularly limited, and various pulverization methods such as dry, wet, and freeze pulverization can be employed. Although this preliminary treatment is not always necessary, it is desirable to carry out wet grinding performed in the next step in order to efficiently perform a predetermined particle size in a short time.

一次粉砕した焙煎コーヒー豆と水とを混合し、メジアン径30μm以下に湿式による二次粉砕を行う(♯3)。焙煎コーヒー豆をメジアン径30μm以下に粉砕するには、乾式あるいは凍結粉砕では実生産レベルでの処理は難しく、湿式粉砕することにより初めて実生産レベルでの処理時間に達成できる。湿式粉砕は、粉体状の焙煎コーヒー豆と水との比率を、1:5〜1:20の範囲となるようにして行うことが好ましい。焙煎コーヒー粉と水の比率を1:5からコーヒー粉を多くすると、湿式粉砕時に懸濁液の流動性が低くなり、装置内でつまりが生じるなど、操業上の支障をきたすおそれがある。逆に、焙煎コーヒー粉と水の比率を1:20から水を多くすると、粉砕処理効率が低くなって好ましくない。   The primary pulverized roasted coffee beans and water are mixed, and wet secondary pulverization is performed to a median diameter of 30 μm or less (# 3). In order to pulverize roasted coffee beans to a median diameter of 30 μm or less, processing at the actual production level is difficult with dry or freeze pulverization, and the processing time at the actual production level can be achieved only by wet pulverization. The wet pulverization is preferably performed so that the ratio of the powdered roasted coffee beans to water is in the range of 1: 5 to 1:20. When the ratio of roasted coffee powder to water is increased from 1: 5, the fluidity of the suspension is lowered during wet pulverization, and there is a risk of causing operational problems such as clogging in the apparatus. Conversely, if the ratio of roasted coffee powder to water is increased from 1:20, the pulverization efficiency is lowered, which is not preferable.

この湿式粉砕は、粒径0.3〜0.5mm程度のジルコニア製ビーズを用いてビーズ式粉砕を採用することが好ましい。粒径0.3mm未満のジルコニア製ビーズを用いた場合には、所定粒度にまで粉砕するのに時間がかかり、粉砕効率が低くなり、粒径0.5mmを越えるジルコニア製ビーズを用いた場合には、均質な粒度に粉砕するまでの処理時間が長くかかる。   This wet pulverization preferably employs bead-type pulverization using zirconia beads having a particle size of about 0.3 to 0.5 mm. When zirconia beads having a particle size of less than 0.3 mm are used, it takes time to pulverize to a predetermined particle size, resulting in low pulverization efficiency and when using zirconia beads having a particle size of more than 0.5 mm. Takes a long processing time until it is pulverized to a uniform particle size.

次いで、得られたコーヒー懸濁液を目開き55μm以下のステンレス製あるいいは樹脂製篩を用いて分級し(♯4)、50μm以上のコーヒー粉を除去する。これにより、飲用時に不溶性の固形分を取り除き、ザラツキ感を確実に無くすことができる。   Next, the obtained coffee suspension is classified using a stainless steel or resin sieve having an opening of 55 μm or less (# 4) to remove coffee powder of 50 μm or more. Thereby, insoluble solid content can be removed at the time of drinking, and a rough feeling can be eliminated reliably.

その後、分級処理されたコーヒー液を乾燥する(♯5)。乾燥処理は、圧力ノズルあるいは高速アトマイザを備えた噴霧乾燥機で行うと、微細なコーヒー粉末粒子が得られるので都合がよく、また凍結乾燥法などにより行う場合に比べて乾燥コストが低く済む。   Thereafter, the classified coffee liquid is dried (# 5). When the drying process is performed with a spray dryer equipped with a pressure nozzle or a high-speed atomizer, fine coffee powder particles can be obtained, and the drying cost is lower than when the drying process is performed by a freeze-drying method or the like.

このようにして得られたコーヒー粉末は、温水または冷水に溶解・分散させて、沈殿がほとんどなく、ザラツキ感のないコーヒー飲料として供される。   The coffee powder thus obtained is dissolved and dispersed in hot water or cold water, and is provided as a coffee beverage with almost no precipitation and no feeling of roughness.

以下、より具体的に実施例を説明する。
(実施例1)
定法にて焙煎(約200℃、約10分)したコーヒー豆を乾式粉砕機にてメジアン径30μm程度にまで粉砕した。得られたコーヒー粉体をイオン交換水にて粉体:水=1:10の比率でディスパーサー(OMNI社製)にて約15分間混合し、この混合物を径約0.5mmの球形ジルコニア・ビーズをアイメックス社製粉砕機(ビーズミル)に投入し、回転数2000rpm、周速10m/秒、流量200mL/分にて4回湿式粉砕し、メジアン径約20μm以下程度にした。粉砕されたコーヒー粉を含む懸濁液に適宜加水しながら、目開き53μmのステンレス製篩を用いてろ過し、50μm以上のコーヒー粉を分級除去した。その後、分級処理した懸濁液を高速アトマイザーを有する噴霧乾燥機(MOBILE MINOR 2000NIRO A/S社製)を用いて、懸濁液スラリー濃度:6.5wt%、導入温度:280±5℃、排出温度:110±5℃、アトマイザー供給圧:400kPaの条件で噴霧乾燥し、コーヒー粉末を得た。
Hereinafter, examples will be described more specifically.
Example 1
Coffee beans roasted by a conventional method (about 200 ° C., about 10 minutes) were pulverized to a median diameter of about 30 μm by a dry pulverizer. The obtained coffee powder was mixed with ion-exchanged water at a ratio of powder: water = 1: 10 for about 15 minutes with a disperser (manufactured by OMNI), and this mixture was mixed with spherical zirconia, having a diameter of about 0.5 mm. The beads were put into an imex pulverizer (bead mill), and wet pulverized four times at a rotational speed of 2000 rpm, a peripheral speed of 10 m / sec, and a flow rate of 200 mL / min to a median diameter of about 20 μm or less. While appropriately adding water to the suspension containing the ground coffee powder, the mixture was filtered using a stainless steel sieve having a mesh size of 53 μm to classify and remove coffee powder of 50 μm or more. Thereafter, the suspension subjected to the classification treatment was sprayed using a spray dryer (manufactured by MOBILE MINOR 2000 NIRO A / S) having a high-speed atomizer, suspension slurry concentration: 6.5 wt%, introduction temperature: 280 ± 5 ° C., discharge Spray drying was performed under conditions of a temperature of 110 ± 5 ° C. and an atomizer supply pressure of 400 kPa to obtain coffee powder.

得られたコーヒー粉末については、コーヒー粉末2gを140g溶解して沈殿状態を目視で観察すると共に、粒度をレーザー回折・散乱粒子径測定装置(機種:LA920湿式。堀場製作所製)を用いて測定した。
(比較例1)
実施例1と同様のコーヒー豆を用いて同様の条件で焙煎し、予め予備粉砕することなく、イオン交換水にてコーヒー粉体:水=1:10の比率で混合し、この混合物をディスクミル(機種名:セレンディピターミニ。増幸産業社製)にて、クリアランス40μm、ディスク回転数2000rpm、焙煎コーヒー供給速度:0.2(kg/分)、水の供給速度:24L/分の条件で粉砕し、コーヒー粉を含む懸濁液を得た。得られた懸濁液は実施例1と同様の条件にて噴霧乾燥して粉末化し、実施例1と同様に熱水に溶解して沈殿状態を観察すると共に、粒度分布を測定した。
(比較例2)
実施例1と同様のコーヒー豆を用いて同様の条件で焙煎し、予備粉砕として、実施例1と同様に乾式粉砕機にてメジアン径30μm程度にまで粉砕した。得られたコーヒー粉体を、実施例1と同様の条件でディスパーサーにて混合し、この混合物をビーズミルに投入して4回湿式粉砕し、コーヒー粉末溶液を得た。ただし、実施例1とは異なり、分級処理をしなかった。得られた懸濁液を、実施例1と同様の条件にて噴霧乾燥して、コーヒー粉末を得た。得られた粉末は、実施例1と同様に熱水に溶解して沈殿状態を観察すると共に、粒度分布を測定した。
(比較例3)
実施例1と同様のコーヒー豆を用いて同様の条件で焙煎し、予備粉砕として焙煎したコーヒー豆を凍結粉砕機(リキッドガス社製)により、−130℃にて凍結粉砕し、コーヒー粉末を得た。得られた粉末は、実施例1と同様に熱水に溶解して沈殿状態を観察すると共に、粒度分布を測定した。
Regarding the obtained coffee powder, 140 g of 2 g of coffee powder was dissolved and the precipitation state was visually observed, and the particle size was measured using a laser diffraction / scattering particle size measuring device (model: LA920 wet, manufactured by Horiba Seisakusho). .
(Comparative Example 1)
Using the same coffee beans as in Example 1, roasting under the same conditions, mixing in a ratio of coffee powder: water = 1: 10 with ion-exchanged water without pre-grinding in advance, and this mixture is a disc. Mill (model name: Serendipita Mini, manufactured by Masuko Sangyo Co., Ltd.), clearance 40 μm, disc rotation speed 2000 rpm, roasted coffee supply rate: 0.2 (kg / min), water supply rate: 24 L / min By pulverizing under conditions, a suspension containing coffee powder was obtained. The obtained suspension was spray-dried under the same conditions as in Example 1 to be powdered, dissolved in hot water as in Example 1, and observed for precipitation, and the particle size distribution was measured.
(Comparative Example 2)
Using the same coffee beans as in Example 1, roasting was performed under the same conditions, and as a preliminary pulverization, the median diameter was pulverized to about 30 μm with a dry pulverizer as in Example 1. The obtained coffee powder was mixed with a disperser under the same conditions as in Example 1, and the mixture was put into a bead mill and wet-pulverized four times to obtain a coffee powder solution. However, unlike Example 1, no classification treatment was performed. The obtained suspension was spray-dried under the same conditions as in Example 1 to obtain coffee powder. The obtained powder was dissolved in hot water in the same manner as in Example 1 to observe the precipitation state, and the particle size distribution was measured.
(Comparative Example 3)
The coffee beans were roasted under the same conditions as in Example 1 and the coffee beans roasted as pre-ground were freeze-ground at −130 ° C. with a freeze pulverizer (manufactured by Liquid Gas Co.) to obtain coffee powder. Got. The obtained powder was dissolved in hot water in the same manner as in Example 1 to observe the precipitation state, and the particle size distribution was measured.

なお、以下の比較例6までは、得られた懸濁液を実施例1と同様の条件にて噴霧乾燥してコーヒーを粉末化し、実施例1と同様に熱水に溶解して沈殿状態を観察すると共に、レーザー回折・散乱粒子径測定装置(機種:LA920湿式。堀場製作所製)を用いて粒度分布を測定した。
(比較例4)
実施例1と同様のコーヒー豆を用いて同様の条件で焙煎し、焙煎したコーヒー豆を凍結粉砕機(リキッドガス社製)により、−130℃にて凍結し粉砕した。得られたコーヒー粉体を、イオン交換水にてコーヒー粉体:水=1:10の比率で混合し懸濁液を得た。この懸濁液をディスパーサーにて約15分間混合し、均一化した懸濁液に適宜水を加えながら、目開き53μmのステンレス製篩を用いてろ過し、コーヒー懸濁液を得た。
(比較例5)
実施例1と同様のコーヒー豆を用いて同様の条件で焙煎し、比較例4と同様に、焙煎したコーヒー豆を凍結粉砕機(リキッドガス社製)により、−130℃にて凍結し粉砕した。得られたコーヒー粉体を、イオン交換水にてコーヒー粉体:水=1:10の比率で混合し懸濁液を得た。この懸濁液をディスパーサーにて約15分間混合し、均一化した懸濁液に適宜水を加えながら、目開き75μmのステンレス製篩を用いてろ過し、コーヒー懸濁液を得た。
(比較例6)
実施例1と同様のコーヒー豆を用いて同様の条件で焙煎し、比較例4と同様に、焙煎したコーヒー豆を凍結粉砕機(リキッドガス社製)により、−130℃にて凍結し粉砕した。得られたコーヒー粉体を、イオン交換水にてコーヒー粉体:水=1:10の比率で混合し懸濁液を得た。この懸濁液をディスパーサーにて約15分間混合し、均一化した懸濁液に適宜水を加えながら、目開き106μmのステンレス製篩を用いてろ過し、コーヒー懸濁液を得た。
Until the following Comparative Example 6, the obtained suspension was spray-dried under the same conditions as in Example 1 to pulverize the coffee, and dissolved in hot water as in Example 1 to give a precipitated state. While observing, the particle size distribution was measured using a laser diffraction / scattering particle size measuring device (model: LA920 wet, manufactured by Horiba Seisakusho).
(Comparative Example 4)
The same coffee beans as in Example 1 were roasted under the same conditions, and the roasted coffee beans were frozen and pulverized at −130 ° C. with a freeze pulverizer (manufactured by Liquid Gas). The obtained coffee powder was mixed with ion exchange water at a ratio of coffee powder: water = 1: 10 to obtain a suspension. This suspension was mixed with a disperser for about 15 minutes, and filtered using a stainless steel sieve having a mesh size of 53 μm while adding water to the homogenized suspension appropriately to obtain a coffee suspension.
(Comparative Example 5)
The same coffee beans as in Example 1 were roasted under the same conditions, and the roasted coffee beans were frozen at −130 ° C. using a freeze pulverizer (manufactured by Liquid Gas) in the same manner as in Comparative Example 4. Crushed. The obtained coffee powder was mixed with ion exchange water at a ratio of coffee powder: water = 1: 10 to obtain a suspension. This suspension was mixed with a disperser for about 15 minutes, and filtered with a stainless steel sieve having an opening of 75 μm while adding water to the homogenized suspension as appropriate to obtain a coffee suspension.
(Comparative Example 6)
The same coffee beans as in Example 1 were roasted under the same conditions, and the roasted coffee beans were frozen at −130 ° C. using a freeze pulverizer (manufactured by Liquid Gas) in the same manner as in Comparative Example 4. Crushed. The obtained coffee powder was mixed with ion exchange water at a ratio of coffee powder: water = 1: 10 to obtain a suspension. This suspension was mixed with a disperser for about 15 minutes, and filtered with a stainless steel sieve having an opening of 106 μm while adding water to the homogenized suspension as appropriate, to obtain a coffee suspension.

上記実施例1および比較例1〜6の工程の内、主たる工程を表1に纏めると共に、得られたコーヒー粉末の粒径分布およびを飲用に供した評価結果を、それぞれ表2、3に示す。   Among the steps of Example 1 and Comparative Examples 1 to 6, the main steps are summarized in Table 1, and the particle size distribution of the obtained coffee powder and the evaluation results for drinking are shown in Tables 2 and 3, respectively. .

Figure 0004453829
Figure 0004453829

Figure 0004453829
Figure 0004453829

Figure 0004453829
表2、3に結果から、実施例1の場合、比較例1〜6に比べて、溶解時の沈殿は極めて少なく、飲用時のザラツキ感もみられず、コーヒー飲料として優れていることがわかる。その場合、湿式粉砕によりメジアン径を20μm以下程度にまですること(実施例1と比較例4の対比)と、55μm以下にまでろ過・分級処理する(実施例1と比較例2,4〜6の対比)ことを共に行うことが効果的である。
Figure 0004453829
From the results in Tables 2 and 3, it can be seen that in Example 1, compared with Comparative Examples 1 to 6, precipitation at the time of dissolution is extremely small, and no rough feeling at the time of drinking is observed, which is excellent as a coffee beverage. In that case, the median diameter is reduced to about 20 μm or less by wet pulverization (contrast between Example 1 and Comparative Example 4), and the filtration and classification are performed to 55 μm or less (Example 1 and Comparative Examples 2, 4 to 6). It is effective to do this together.

本発明の一実施形態に係る粉末可溶性コーヒーの製造方法を示すフローチャートThe flowchart which shows the manufacturing method of the powder soluble coffee which concerns on one Embodiment of this invention.

Claims (3)

焙煎コーヒー豆と水とを混合し、この焙煎コーヒー豆をメジアン径30μm以下に湿式粉砕し、得られたコーヒー懸濁液を55μm以下に分級し、その後乾燥する粉末可溶性コーヒーの製造方法。 A method for producing powder-soluble coffee, comprising mixing roasted coffee beans and water, wet-grinding the roasted coffee beans to a median diameter of 30 μm or less, classifying the resulting coffee suspension to 55 μm or less, and then drying. 前記湿式粉砕を行う前に、前記焙煎コーヒー豆を予め乾式粉砕または凍結粉砕を行い、メジアン径を100μm以下にする請求項1の粉末可溶性コーヒーの製造方法。 The method for producing powder-soluble coffee according to claim 1, wherein the roasted coffee beans are dry-grinded or freeze-milled in advance before the wet pulverization to reduce the median diameter to 100 µm or less. 前記湿式粉砕を、径0.5mm以下の球形ビーズを混在させて粉砕すると共に、前記分級を、篩を用いて行う請求項1又は2の粉末可溶性コーヒーの製造方法。
The method for producing powder-soluble coffee according to claim 1 or 2, wherein the wet pulverization is performed by mixing spherical beads having a diameter of 0.5 mm or less, and the classification is performed using a sieve.
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