JPS6250103B2 - - Google Patents

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Publication number
JPS6250103B2
JPS6250103B2 JP55082719A JP8271980A JPS6250103B2 JP S6250103 B2 JPS6250103 B2 JP S6250103B2 JP 55082719 A JP55082719 A JP 55082719A JP 8271980 A JP8271980 A JP 8271980A JP S6250103 B2 JPS6250103 B2 JP S6250103B2
Authority
JP
Japan
Prior art keywords
chili
powder
steam
sterilization
chili pepper
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP55082719A
Other languages
Japanese (ja)
Other versions
JPS578755A (en
Inventor
Daikichi Koshida
Akira Sugisawa
Fumio Matsui
Masanori Yamamoto
Masaru Shibuki
Yoshuki Ooshima
Noriaki Yamaguchi
Morio Taniguchi
Atsuro Takagaki
Masato Nakayama
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
House Foods Corp
Original Assignee
House Food Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by House Food Industrial Co Ltd filed Critical House Food Industrial Co Ltd
Priority to JP8271980A priority Critical patent/JPS578755A/en
Publication of JPS578755A publication Critical patent/JPS578755A/en
Publication of JPS6250103B2 publication Critical patent/JPS6250103B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は品質の改善されたトウガラシ粉末の製
造法に関する。従来一般的なトウガラシ粉末の製
造法は篩別、乾燥、製粉、殺菌の4工程からなつ
ている。 その殺菌にはエチレンオキサイドやプロピレン
オキサイドが適しているとされ、その殺菌効果は
多くの実験者によつて報告されている。しかしな
がら、上記殺菌剤は引火性、可燃性であり、使用
に当つては周囲の作業環境の整備が必要であり、
且つ密封状態で処理しなければならない等取り扱
い上種々の問題があるために、必ずしも工業的実
用面において適しているとはいえない。 それにもかかわらず多くの実験者が上記殺菌剤
等による殺菌効果について種々の実験結果を報告
しているのは、香辛料の主成分には揮発性のもの
が多いのでその殺菌に当つて加熱殺菌することは
香辛料にとつて致命的であり、従つて加熱殺菌は
避けねばならない(総合食料工業:恒星社厚生閣
版1130頁、特公昭39−11248号公報)という見解
が当業界の常識として定着しており、加熱殺菌と
は異なつた熱を加えない殺菌方法を開発すべくそ
の必要に迫られているからである。 換言するならば、従来技術はトウガラシの香辛
味を変質させないように加熱以外の殺菌方法によ
つてトウガラシ粉末を殺菌する技術の開発に集中
していたのである。またトウガラシ粉末の品質改
善殊に香り出し、色出し(鮮やかな赤色にする)
を加熱によつて積極的に改善する技術についての
研究は発表されていない。 本発明者等はこうした現状に鑑み、トウガラシ
粉末の品質殊に香り出し、色出しの向上という問
題に着目し、トウガラシ粉末の特有の香り、色を
単に保持させるだけでなく更に向上させるための
技術についてトウガラシ粉末の殺菌技術と共に研
究を行なつた。その結果トウガラシのホールを粉
砕した後、特定の条件下にて蒸気と接触させた後
特定条件下で焙煎処理することによつて殺菌、香
り出し、色出しに関して充分に満足できるトウガ
ラシ粉末を得ることができるという知見を得た。 上記知見を基に完成された本発明の要旨はトウ
ガラシを粉砕し、その後100〜145℃の温度で蒸気
と接触させて600〜1秒間保持して殺菌及び10重
量%以下の水分含量の増加をなした後、40〜80℃
の温度で30〜100分間焙煎、乾燥するか、又は上
記条件で焙煎した後乾燥して水分含量を5〜7重
量%にした後、常法により冷却することを特徴と
するトウガラシ粉末の製造法にある。 以下本発明のトウガラシ粉末の製造法を具体的
に述べる。まずトウガラシのホールを高速粉砕
機、スタンプ式粉砕機等によつて粉砕する。トウ
ガラシのホールを殺菌前に予め粉砕するのはトウ
ガラシを効果的に殺菌するためである。即ちトウ
ガラシホールの多くのものにはひび割れがあり、
そこから細菌がホールの内部に侵入しているの
で、単にトウガラシホールの殺菌処理を施しても
効果的な殺菌は望み難い。 以上の理由から本発明の場合殺菌に先立つてト
ウガラシのホールを粉砕するが、この場合トウガ
ラシの粉末粒度を10〜100メツシユのものが70%
以上になるように粉砕するのが好ましい。粉末の
粒径の大きいものが多くなつてくると、後の焙煎
処理による香り出し、色出し効果が低下しやすく
なり、反対に粉末の粒径の小さいものが多くなつ
てくると、殺菌処理時の熱による香りの揮散、変
質が顕著になる。 次に粉砕して得られたトウガラシ粉末を100〜
145℃の温度で蒸気と接触させて600〜1秒間保持
して殺菌及び10重量%以下の水分の含量を増加さ
せる。この場合ノズル等から噴出する蒸気を使用
することによつてトウガラシ粉末の温度を急速に
上昇させることができるので、短時間での殺菌が
可能となりトウガラシ粉末の香辛味の損失を抑制
することができる共に、殺菌条件の設定を簡便に
且つ正確に行なうことができる。 トウガラシ粉末を蒸気と接触させる方法として
は容器に水を入れ容器内の水と接触しない位置に
網状の棚を設け、そこにトウガラシ粉末を静置し
た後、容器を加熱して蒸気を発生せしめてトウガ
ラシ粉末と蒸気とを接触させる方法も考えられる
が、このような方法ではトウガラシ粉末の温度を
急速に上昇させることができず、従つて長時間ト
ウガラシ粉末が加熱雰囲気中にさらされることに
なつてトウガラシの有する香辛味を損う原因にな
るばかりでなく、殺菌条件を常時一定にすること
はほとんど不可能である。 本発明においてトウガラシ粉末と蒸気とを接触
させる第一の目的はトウガラシ粉末を殺菌するた
めである。この場合トウガラシ粉末と蒸気との接
触条件が上記した条件より緩やかであれば充分な
殺菌効果が望めず、反対に上記条件より厳しい場
合はトウガラシが本来有している香辛味を損う原
因になる。 トウガラシ粉末と蒸気との接触条件において、
殺菌効果及び香辛味保持効果の両面をより完全に
達成するためには常圧下で実施する方が好まし
く、この場合トウガラシ粉末を蒸気と接触させる
に当つては静止した蒸気雰囲気中で接触させるよ
りは、蒸気を積極的にトウガラシ粉末に吹き付け
る方がトウガラシ粉末の隅々にまで速やかに蒸気
を行き渡らせることができ、その結果トウガラシ
が元来有している香辛味の損失をできるだけ抑制
して極めて短時間で殺菌を完全に行うことができ
る。具体的には蒸気の吹込み流量を1m3当り7.0
Kg/分以上の条件で実施することが好ましい。 トウガラシ粉末と蒸気とを接触させる第二の目
的はトウガラシ粉末の水分含量を10重量%以下増
加させるためである。該増加水分含量の限定は後
の焙煎効果を高めるためである。水分含量の増加
が多すぎると焙煎による蒸れ臭が発生する原因と
なる。 以上の二つの目的を達成するために本発明にお
いては、トウガラシ粉末を蒸気と接触させる。こ
の場合上記した如く常圧下で実施するのが好まし
いが、レトルト釜の如き加圧釜で実施してもよ
く、更には過熱蒸気と接触させてもよい。 次に蒸気処理したトウガラシ粉末を40〜80℃の
温度で30〜100分間焙煎、乾燥するか、又は上記
条件で焙煎した後乾燥して水分含量を5〜7重量
%にする。 トウガラシ粉末は蒸気との接触によつてその香
りがある程度損われているので、上記焙煎処理に
よつて香り出しをし、それと同時に色出しを行な
つてトウガラシ粉末の香り、色を向上させる。 上記焙煎処理は開放状態で行なつてもよく、密
閉状態で行なつてもよい。開放状態で上記焙煎処
理を行なう場合は乾燥も同時に行なえるが、密閉
状態で上記焙煎処理を行なう場合は焙煎処理後に
乾燥を行なう必要がある。そして上記いずれの場
合も得られるトウガラシ粉末の水分含量を5〜7
重量%にする。その後常法によつて上記トウガラ
シ粉末を冷却する。 以上の方法によつて得られるトウガラシ粉末の
殺菌並びに香辛味保持の効果を確認するために以
下の比較実験例を示す。 比較実験例 水分含量10.5重量%のトウガラシを高速粉砕機
で粉砕し、その後篩で19〜80メツシユの粉末を選
別して第1表に示す条件で蒸気殺菌処理及び焙煎
処理を行なつた。
The present invention relates to a method for producing chili powder with improved quality. The conventional method for producing chili powder generally consists of four steps: sieving, drying, milling, and sterilization. Ethylene oxide and propylene oxide are said to be suitable for sterilization, and their sterilization effects have been reported by many experimenters. However, the above disinfectants are flammable and combustible, and it is necessary to prepare the surrounding work environment when using them.
In addition, there are various problems in handling such as the necessity of processing in a sealed state, so it cannot be said that it is necessarily suitable for industrial practical use. Despite this, many experimenters have reported various experimental results regarding the bactericidal effects of the above-mentioned bactericidal agents, etc. The reason is that many of the main components of spices are volatile, so heat sterilization is used to sterilize them. This is fatal to spices, and therefore, heat sterilization must be avoided (General Shokuhin Kogyo: Seiseisha Koikaku edition, p. 1130, Special Publication No. 11248, 1973), which has become common knowledge in the industry. This is because there is an urgent need to develop a sterilization method that does not apply heat, which is different from heat sterilization. In other words, the prior art has concentrated on developing techniques for sterilizing chili pepper powder using sterilization methods other than heating so as not to alter the spiciness of chili peppers. We also improved the quality of chili pepper powder, especially to bring out its aroma and color (make it bright red).
No research has been published on technology to actively improve this by heating. In view of the current situation, the present inventors focused on the problem of improving the quality of chili powder, especially its aroma and color, and developed a technology that not only preserves but also further improves the unique aroma and color of chili powder. We conducted research on this along with sterilization technology for chili pepper powder. As a result, after crushing the whole chili pepper, it is brought into contact with steam under specific conditions, and then roasted under specific conditions to obtain a chili powder that is fully satisfactory in terms of sterilization, aroma release, and color development. I learned that it is possible. The gist of the present invention, which was completed based on the above knowledge, is to crush chili peppers, then bring them into contact with steam at a temperature of 100 to 145 degrees Celsius and hold for 600 to 1 second to sterilize and increase the moisture content by 10% by weight or less. After heating, 40~80℃
or roasted under the above conditions and dried to a moisture content of 5 to 7% by weight, and then cooled by a conventional method. It's in the manufacturing method. The method for producing chili pepper powder of the present invention will be specifically described below. First, whole chili peppers are crushed using a high-speed crusher, stamp type crusher, or the like. The purpose of crushing whole chili peppers before sterilization is to effectively sterilize the chili peppers. In other words, many chili pepper holes have cracks,
Since bacteria invade the inside of the hole from there, it is difficult to expect effective sterilization even if the chili pepper hole is simply sterilized. For the above reasons, in the case of the present invention, the whole of the chili pepper is crushed before sterilization, but in this case, the powder particle size of the chili pepper is 70% of the powder size of 10 to 100 mesh.
It is preferable to grind the powder to the above-mentioned size. As the powder particles become larger in size, the aroma and coloring effects of the subsequent roasting process tend to decline.On the other hand, as the powder particles become more small in size, the sterilization process becomes more difficult. The aroma evaporates and changes in quality due to the heat of time. Next, add 100~
Contact with steam at a temperature of 145° C. and held for 600-1 seconds to sterilize and increase the moisture content up to 10% by weight. In this case, the temperature of the chili pepper powder can be rapidly raised by using steam emitted from a nozzle, etc., which enables sterilization in a short time and suppresses loss of the spiciness of the chili pepper powder. In both cases, sterilization conditions can be easily and accurately set. The method of bringing chili pepper powder into contact with steam is to fill a container with water, set up a net-like shelf in a position where it will not come into contact with the water in the container, leave the chili pepper powder there, and then heat the container to generate steam. A method of bringing the chili powder into contact with steam is also considered, but such a method does not allow the temperature of the chili powder to be raised rapidly, and therefore the chili powder is exposed to a heated atmosphere for a long period of time. Not only does this cause loss of the spiciness of chili peppers, but it is also almost impossible to keep the sterilization conditions constant at all times. In the present invention, the first purpose of bringing the chili powder into contact with steam is to sterilize the chili powder. In this case, if the contact conditions between the chili pepper powder and the steam are milder than the above conditions, a sufficient sterilizing effect cannot be expected; on the other hand, if the conditions are harsher than the above conditions, the inherent spiciness of the chili peppers may be lost. . Under the conditions of contact between chili powder and steam,
In order to more fully achieve both the sterilization effect and the flavor retention effect, it is preferable to carry out the process under normal pressure. By actively blowing steam onto the chili pepper powder, the steam can quickly spread to every corner of the chili powder, and as a result, the loss of the original spiciness of the chili pepper can be suppressed as much as possible and the process can be completed in an extremely short period of time. Sterilization can be completed in just a few hours. Specifically, the steam injection flow rate is 7.0 per 1m3 .
It is preferable to carry out the test under conditions of Kg/min or higher. The second purpose of contacting the chili powder with steam is to increase the water content of the chili powder by 10% by weight or less. The purpose of limiting the increased moisture content is to enhance the subsequent roasting effect. If the moisture content increases too much, it will cause a stuffy odor due to roasting. In order to achieve the above two objects, according to the present invention, chili pepper powder is brought into contact with steam. In this case, as mentioned above, it is preferable to carry out the process under normal pressure, but it may also be carried out in a pressure vessel such as a retort vessel, or it may be brought into contact with superheated steam. The steamed chili pepper powder is then roasted and dried at a temperature of 40 to 80°C for 30 to 100 minutes, or roasted under the above conditions and then dried to a moisture content of 5 to 7% by weight. Since the aroma of chili powder is lost to some extent by contact with steam, the aroma is brought out by the above-mentioned roasting process, and at the same time color is imparted to improve the aroma and color of the chili pepper powder. The above roasting process may be performed in an open state or in a closed state. When the above-mentioned roasting process is performed in an open state, drying can be performed at the same time, but when the above-mentioned roasting process is performed in a closed state, it is necessary to perform drying after the roasting process. In any of the above cases, the moisture content of the chili powder obtained is 5 to 7.
Convert to weight%. Thereafter, the chili pepper powder is cooled by a conventional method. In order to confirm the effectiveness of sterilizing and preserving the spiciness of chili pepper powder obtained by the above method, the following comparative experimental example is shown. Comparative Experimental Example Chili peppers with a moisture content of 10.5% by weight were ground using a high-speed grinder, and then 19 to 80 mesh powder was sorted using a sieve and steam sterilized and roasted under the conditions shown in Table 1.

【表】 第1表中増加水分量は蒸気殺菌前後のトウガラ
シ粉末の重量差を増加水分とした。 尚本発明A、B及び比較、、、は常圧
下で、本発明C、D及び比較、はレトルト釜
で実施し、本発明Eは過熱蒸気を使用した。実験
結果を第2表に示す。評価の対象は大腸菌群数、
10点採点法による香り、色の官能評価で、大腸菌
群数はB.G.L.B.法により測定し、官能評価は各々
のトウガラシ粉末を専門パネル10名により最良を
10点とし、最不良を1点とする10点採点法で行な
い、それぞれのトウガラシ粉末に対する評価点の
総和の平均値をもつて官能評価点とした。
[Table] The increased moisture content in Table 1 is defined as the difference in weight of chili pepper powder before and after steam sterilization. Inventions A, B, and Comparison were conducted under normal pressure, Inventions C, D, and Comparison were conducted in a retort pot, and Invention E used superheated steam. The experimental results are shown in Table 2. The targets of evaluation are the number of coliform bacteria,
The number of coliform bacteria was measured using the BGLB method, and the sensory evaluation was based on a 10-point scoring system for scent and color.
A 10-point scoring system was used, with the worst score being 1 point, and the average value of the sum of the evaluation scores for each chili pepper powder was taken as the sensory evaluation score.

【表】 第2表中水分含量の測定はカールフイツシヤー
法で行なつた。 上記第1表及び第2表から以下のことが明白と
なつた。本発明A〜Eと比較〜を対比するこ
とによつて本発明の焙煎条件がトウガラシ粉末の
香り出し、色出しに重要な影響を与えることがわ
かる。即ち比較〜は本発明の蒸気殺菌条件を
満足するが、本発明の焙煎条件から逸脱してお
り、その結果得られたトウガラシ粉末の香り、色
共に本発明A〜Dより劣つているばかりでなく無
処理粉末のそれよりも劣つている。 次に本発明A、Bと比較、を対比すること
によつて本発明の蒸気殺菌条件がトウガラシ粉末
の殺菌効果乃至香り出し、色出し効果に重要な影
響を与えることがわかる。即ち比較、は本発
明の焙煎条件を満足するが、本発明の蒸気殺菌条
件から逸脱している。その結果得られたトウガラ
シ粉末のうち比較の場合殺菌効果は認められる
が香り、色共に本発明Aより劣つており、比較
の場合、殺菌効果において生菌数が2.0×102とな
つており、明らかに本発明Bよりも劣つている。 上記した本発明A〜Eと比較〜とを対比す
ることによつて蒸気殺菌条件のうち温度と時間が
殺菌効果に大きく影響しており、該蒸気殺菌条件
のうち増加水分量が焙煎条件と相関してトウガラ
シ粉末の香り出し、色出しに影響を与えることが
わかる。 以上の如く本発明の目的を達成するためには、
本発明の蒸気殺菌条件及び焙煎条件の双方を満足
しなければならず、いずれか一方の条件を逸脱す
ると殺菌効果及び/又は香り出し、色出し効果を
満足し得なくなる。 このように本発明の方法によつて得られるトウ
ガラシ粉末は病原性菌が陰性であり、香り、色共
に従来のトウガラシホールを単に粉砕したものよ
りも優れており、明らかに品質の改善されたもの
である。更に、上記本発明方法は特殊な機械及び
装置を必ずしも必要とせず簡易な装置によつて実
施し得るので工業的実用面においても優れてい
る。 また、トウガラシ粉末の蒸気殺菌処理によつて
油の加水分解酵素であるリパーゼを失活すること
ができるので、本発明方法によつて得られるトウ
ガラシ粉末をラー油等に使用する場合、油の変
敗、変質等を防止することもできる。 実施例 1 水分含量10.5重量%のトウガラシのホール1.0
Kgを高速粉砕機で粉砕して10〜100メツシユのも
のが60%、100メツシユパスのものが30%10メツ
シユオンのものが10%、という粒度分布を有する
トウガラシ粉末を得た。 次にこのトウガラシ粉末0.5Kgを長方形の容器
に薄層状に0.1Kg宛入れそれをレトルト釜に装填
した後、110℃の蒸気で200秒間処理した。得られ
たトウガラシ粉末の増加水分量は9.0重量%であ
つた。次に上記トウガラシ粉末を油による間接加
熱機構を有する密閉式回転焙煎釜で70℃、35分間
焙煎処理した後、流動層乾燥に入れ120℃の熱風
で1分間乾燥して水分含量5.0重量%のトウガラ
シ粉末を得た。得られたトウガラシ粉末に殺菌効
果及び香り出し、色出し効果共に優れたものであ
つた。 実施例 2 実施例1と同様の方法で粉砕したトウガラシ粉
末を篩にかけて16〜80メツシユのトウガラシ粉末
1.0Kgを得た。次に該トウガラシ粉末0.5Kgをネツ
トコンベア上に薄層状に置き、約100℃の蒸気を
直接吹き付けて100秒間処理した。得られたトウ
ガラシ粉末の増加水分量は7重量%であつた。次
に該トウガラシ粉末を開放式焙煎釜で60℃、40分
間焙煎、乾燥処理して水分含量6.0重量%のトウ
ガラシ粉末を得た。得られたトウガラシ粉末は殺
菌効果及び香り出し、色出し効果共に優れたもの
であつた。
[Table] The moisture content in Table 2 was measured by the Karl Fischer method. From Tables 1 and 2 above, the following became clear. By comparing Inventions A to E with Comparison to Comparison, it can be seen that the roasting conditions of the invention have an important effect on the aroma and color development of chili pepper powder. That is, Comparison ~ satisfies the steam sterilization conditions of the present invention, but deviates from the roasting conditions of the present invention, and the resulting chili pepper powder is inferior to Inventions A to D in both aroma and color. However, it is inferior to that of untreated powder. Next, by comparing Inventions A and B, it can be seen that the steam sterilization conditions of the present invention have an important influence on the sterilization effect, aroma release, and color release effect of chili pepper powder. That is, the comparison satisfies the roasting conditions of the present invention, but deviates from the steam sterilization conditions of the present invention. Among the chili powder obtained as a result, in the case of comparison, the bactericidal effect was observed, but both the aroma and color were inferior to Invention A, and in the case of comparison, the number of viable bacteria was 2.0 × 10 2 in terms of the bactericidal effect. It is clearly inferior to Invention B. By comparing the present inventions A to E and the comparisons described above, it is found that among the steam sterilization conditions, temperature and time greatly influence the sterilization effect, and among the steam sterilization conditions, the increased moisture content is different from the roasting condition. It can be seen that there is a correlation between this and the effect on the aroma and color appearance of chili pepper powder. In order to achieve the purpose of the present invention as described above,
Both the steam sterilization conditions and the roasting conditions of the present invention must be satisfied, and if either one of the conditions is violated, the sterilization effect and/or aroma and color development effects will not be satisfied. As described above, the chili pepper powder obtained by the method of the present invention is negative for pathogenic bacteria, has a better aroma and color than conventional chili powder simply crushed, and is clearly of improved quality. It is. Furthermore, the method of the present invention does not necessarily require any special machinery or equipment and can be carried out using a simple device, and is therefore excellent in terms of industrial practicality. In addition, steam sterilization of chili pepper powder can deactivate lipase, which is an oil hydrolyzing enzyme. , deterioration, etc. can also be prevented. Example 1 Capsicum whole 1.0 with moisture content 10.5% by weight
Kg was ground using a high-speed grinder to obtain a chili pepper powder having a particle size distribution of 60% from 10 to 100 meshes, 30% from 100 meshes, and 10% from 10 meshes. Next, 0.5 kg of this chili powder was placed in a thin layer of 0.1 kg in a rectangular container, which was then loaded into a retort pot and treated with steam at 110° C. for 200 seconds. The increased moisture content of the obtained chili pepper powder was 9.0% by weight. Next, the above chili pepper powder was roasted at 70℃ for 35 minutes in a closed rotary roasting pot with an indirect heating mechanism using oil, and then placed in a fluidized bed dryer and dried with hot air at 120℃ for 1 minute to reduce the water content to 5.0 weight. % of chili powder was obtained. The obtained chili powder had excellent bactericidal effect, aroma and color effect. Example 2 Capsicum powder crushed in the same manner as in Example 1 was sieved to obtain 16 to 80 mesh capsicum powder.
Obtained 1.0Kg. Next, 0.5 kg of the chili pepper powder was placed in a thin layer on a net conveyor, and steam at about 100° C. was directly blown onto it for 100 seconds. The increased moisture content of the obtained chili pepper powder was 7% by weight. Next, the chili powder was roasted in an open roasting oven at 60°C for 40 minutes and dried to obtain a chili powder with a water content of 6.0% by weight. The obtained chili pepper powder was excellent in both sterilizing effect, aroma-releasing effect, and color-releasing effect.

Claims (1)

【特許請求の範囲】[Claims] 1 トウガラシを粉砕し、その後100〜145℃の温
度で蒸気と接触させて600〜1秒間保持して殺菌
及び10重量%以下の水分含量を増加させた後、40
〜80℃の温度で30〜100分間焙煎と同時に乾燥す
るか、又は上記条件で焙煎した後乾燥して水分含
量を5〜7重量%にし、更に常法により冷却する
ことを特徴とするトウガラシ粉末の製造法。
1. After grinding the chili pepper and then contacting it with steam at a temperature of 100-145 ° C and holding for 600-1 seconds to sterilize and increase the moisture content by 10% by weight or less, 40
It is characterized by drying at the same time as roasting at a temperature of ~80°C for 30 to 100 minutes, or by roasting under the above conditions and then drying to a moisture content of 5 to 7% by weight, and further cooling by a conventional method. Method for producing chili pepper powder.
JP8271980A 1980-06-20 1980-06-20 Preparation of guinea pepper flour Granted JPS578755A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8271980A JPS578755A (en) 1980-06-20 1980-06-20 Preparation of guinea pepper flour

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8271980A JPS578755A (en) 1980-06-20 1980-06-20 Preparation of guinea pepper flour

Publications (2)

Publication Number Publication Date
JPS578755A JPS578755A (en) 1982-01-18
JPS6250103B2 true JPS6250103B2 (en) 1987-10-22

Family

ID=13782212

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8271980A Granted JPS578755A (en) 1980-06-20 1980-06-20 Preparation of guinea pepper flour

Country Status (1)

Country Link
JP (1) JPS578755A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0731704U (en) * 1993-11-19 1995-06-16 正人 山口 Suppression plate of plastic trash container and plastic trash container integrally formed with the suppression plate

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Publication number Priority date Publication date Assignee Title
JPH0649518B2 (en) * 1986-06-30 1994-06-29 三菱重工業株式会社 Pressure difference relief type container
BRPI0512080A (en) * 2004-06-15 2008-02-06 Ajinomoto Kk methods for drying a material to be dried in the form of chilli peppers containing capsinoid by means of a box-type batch drier and by means of a continuous drier
KR101948866B1 (en) * 2017-03-30 2019-02-18 영월농업협동조합 A process for the preparation of red-pepper powder
JP7169101B2 (en) * 2018-06-26 2022-11-10 ハウス食品株式会社 Method for producing powdered red pepper
JP7250481B2 (en) * 2018-11-12 2023-04-03 ハウス食品株式会社 Hayashi sauce and base material for preparing it

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0731704U (en) * 1993-11-19 1995-06-16 正人 山口 Suppression plate of plastic trash container and plastic trash container integrally formed with the suppression plate

Also Published As

Publication number Publication date
JPS578755A (en) 1982-01-18

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