JP2006262706A - Apparatus and method for drying fish meat or meat - Google Patents
Apparatus and method for drying fish meat or meat Download PDFInfo
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本発明は、蒸気加熱装置により昇温した過熱水蒸気を熱媒体として乾燥室内で魚肉や食肉を短時間で均質乾燥させる魚肉や食肉の乾燥装置および乾燥方法に関するものである。 The present invention relates to a fish meat and meat drying apparatus and a drying method for uniformly drying fish meat and meat in a drying chamber in a drying chamber using superheated steam heated by a steam heating device as a heat medium.
従来の魚肉や食肉の生産は、自然乾燥または人工乾燥が主流であり、後者の人工乾燥では含水率12〜15%程度を乾燥食品として出荷されている。人工乾燥機は魚肉や食肉を昇温し、水分の蒸発、除去をはかるものであるが、その加熱方法は水蒸気、空気、高周波加熱等、多岐に渡るものが開発されている。魚肉や食肉は、細胞膜を形成する蛋白質や脂肪等からなり、魚肉や食肉の水分は魚肉や食肉の細胞内の結合水と魚肉や食肉の細胞間の自由水に大別され、概ね含水率20%程度以上は自由水、以下では結合水が主となる。自由水の除去は比較的容易とされているが、結合水の除去は魚肉や食肉の細胞の影響等などから一般に困難とされ、さまざまな試み、開発の対象となっている。 In the conventional production of fish meat and meat, natural drying or artificial drying is the mainstream, and in the latter artificial drying, a moisture content of about 12 to 15% is shipped as dried food. Artificial dryers heat fish and meat to evaporate and remove moisture, but various heating methods such as steam, air, and high-frequency heating have been developed. Fish meat and meat are composed of proteins, fats, and the like that form cell membranes, and the water content of fish meat and meat is broadly divided into free water between fish and meat cells and free water between fish and meat cells. More than about% is free water, and below is combined water. Removal of free water is considered to be relatively easy, but removal of bound water is generally considered difficult due to the influence of fish and meat cells, and has been the subject of various attempts and development.
魚肉や食肉の細胞組織と水分の関係から、乾燥プロセスは3段階に分けられる。第1段階は、昇温プロセスである。魚肉や食肉は熱伝導度が低いため、表面から熱が伝わり、表面温度と中心部温度がほぼ等しくなるまで相当の時間を要する段階である。この表面部と中心部で大きな温度勾配がある状態では、熱膨張率の差から内部応力が発生し、熱流入が一定限度を超えると、「身割れや欠損が発生し」内部応力は開放される。この段階では、内部応力の発生を抑えつつ、温度分布の均一化をはかることが重要である。第2段階は、恒常乾燥プロセスである。自由水の蒸発段階であり、入熱量にほぼ比例して蒸発が進む。第3段階は減率乾燥プロセスである。自由水の蒸発がほぼ終わり、魚肉や食肉の細胞内の結合水の移動、拡散、蒸発の段階である。魚肉や食肉の細胞膜を水分が通過するプロセスであるので、温度設定等の乾燥手法によっては魚肉や食肉の細胞膜を傷める恐れがある。 The drying process is divided into three stages based on the relationship between the cellular structure of fish and meat and moisture. The first stage is a temperature raising process. Since fish and meat have low thermal conductivity, heat is transferred from the surface, and it takes a considerable time until the surface temperature and the center temperature are substantially equal. In the state where there is a large temperature gradient between the surface and the center, internal stress is generated due to the difference in the coefficient of thermal expansion, and if the heat inflow exceeds a certain limit, `` cracking or chipping occurs '' and the internal stress is released. The At this stage, it is important to make the temperature distribution uniform while suppressing the generation of internal stress. The second stage is a constant drying process. This is the free water evaporation stage, and evaporation proceeds almost in proportion to the amount of heat input. The third stage is a reduced rate drying process. The evaporation of free water is almost over, and it is the stage of movement, diffusion, and evaporation of bound water in fish and meat cells. Since the moisture passes through the cell membrane of fish or meat, the cell membrane of fish or meat may be damaged depending on the drying method such as temperature setting.
従来の方法は、魚肉や食肉の熱伝導度が低いことから、熱伝達におけるエネルギー損失が大きく、運転コストが高くなる、あるいは魚肉や食肉の細胞膜を破壊せず、結合水を除去するには、比較的低レベルの熱量を長時間にわたって与える手法が採られ、従って乾燥に長時間を要するなどの欠点があった。 The conventional method has low heat conductivity of fish and meat, so energy loss in heat transfer is large, operation cost is high, or to remove bound water without destroying cell membrane of fish and meat, There has been a drawback that a relatively low level of heat is applied over a long period of time, thus requiring a long time for drying.
この改善策として、遠赤外線照射による乾燥での熱効率が低いので、熱風の直接噴射による手法等が考案されているが、昇温プロセスでは有効でも、恒常乾燥、減率乾燥プロセスでは露点を下回ると水分の供給となり、水蒸気温度を上げる工夫があるが、圧力もそれに伴って上昇し、魚肉や食肉に対しては外圧となって、水分の蒸発を妨げることになり乾燥時間の延長と品質が安定しない。過熱蒸気存在下でマイクロ波加熱の手法で、魚肉や食肉の熱的均質化が図れる利点はあるが、昇温プロセスでは蒸気等による加湿設備を併設せざるを得ず、設備コストが高い上、連続制御が難しいため短時間の処理が難しい。
これら従来の魚肉や食肉の乾燥機は、乾燥室内制御を熱風や遠赤外線で乾燥する方式やマイクロ波乾燥する方法であり、魚肉や食肉を短時間に安定して、均質に乾燥できない諸問題点をかかえているものである。 These conventional fish and meat dryers have a drying chamber control method that uses hot air or far-infrared drying, or microwave drying, and various problems that prevent stable drying of fish and meat in a short time. It is something that has
本発明は、魚肉や食肉の固有の乾燥プロセスに応じて過熱水蒸気を蒸気加熱装置(3)に通して熱媒体として、ほぼ大気圧下の乾燥室に供給した魚肉や食肉の乾燥機(4)および最適な魚肉や食肉の乾燥方法を最も主要な特徴とする。
上述した問題点を解決する請求項1の発明は、水蒸気ボイラー(1)によって供給される過熱水蒸気で魚肉や食肉の昇温段階、恒常乾燥段階の熱供給、並びに恒常乾燥段階、減率乾燥段階に応じた温度状態に蒸気加熱装置(3)によって昇温し、これらを熱媒体として乾燥室内(4)で魚肉や食肉を短時間で高付加乾燥させる魚肉や食肉の乾燥装置である。請求項2の発明は、温度制御と流量制御は乾燥室内温度検出器(9)、魚肉や食肉の温度検出器(10)からの信号によって制御、すなわち、乾燥室内温度検出器(9)の温度上昇割合に比べ魚肉や食肉の温度検出器(10)の温度上昇割合が高い時は蒸気加熱装置(3)の設定温度を下げ、逆の場合は温度を上げて、処理プロセスによって設定した温度範囲に乾燥室(4)内を制御しする水蒸気流量調整弁(7)によって、流量を調整することで、魚肉や食肉の昇温段階、恒常乾燥段階、減率乾燥段階のそれぞれの魚肉や食肉の最適乾燥条件とするために乾燥室(4)内の過熱水蒸気量を水蒸気流量調整弁(7)で自動又は半自動で調整乾燥させる魚肉や食肉の乾燥装置である。請求項1は、ドレン分離器(5)でドレンを排出するための装置を配置した魚肉や食肉の乾燥装置である。
The present invention relates to a fish or meat dryer (4) which supplies superheated steam as a heat medium through a steam heating device (3) according to a specific drying process of fish or meat to a drying chamber under almost atmospheric pressure. And the most important feature is the optimal method of drying fish and meat.
Invention of
請求項1の発明によると、水蒸気ボイラー(1)によって供給される水蒸気を蒸気加熱装置(3)によって昇温された熱媒体を乾燥室内(4)に投入できるので、魚肉や食肉の乾燥プロセスに応じた熱供給が可能となり魚肉や食肉を短時間で処理が可能となり、熱供給量を自由に調整できるため魚肉や食肉に適した高付加乾燥が可能となる。請求項2の発明によると、魚肉や食肉の昇温段階、減率乾燥段階、恒常乾燥段階のそれぞれの魚肉や食肉の最適乾燥条件とするために乾燥室(4)内の過熱水蒸気及を水蒸気流量調整弁および制御装置(11)で自動又は半自動で制御が可能であり高付加乾燥(品質の均質及び殺菌を同時に行う短時間乾燥)させることができる。また、本乾燥方法は、ほぼ大気圧下で露点以上の高温常圧過熱水蒸気を発生させることができ、昇温プロセスでの加湿、恒常乾燥プロセスでの乾燥した過熱水蒸気の供給、減率乾燥プロセスでの高温過熱水蒸気の供給という、それぞれのプロセスに最適な熱媒体温度が1台の加熱装置で実現可能である蒸気加熱装置によって運転できるという利点がある。
According to the first aspect of the present invention, the steam supplied from the steam boiler (1) can be fed into the drying chamber (4) with the heat medium heated by the steam heating device (3). The heat supply according to this becomes possible, fish and meat can be processed in a short time, and the amount of heat supply can be adjusted freely, so that high addition drying suitable for fish and meat is possible. According to the invention of
蒸気加熱装置(3)の入口側に水蒸気ボイラー(1)を魚肉や食肉の各プロセスに必要な熱媒量をバルブで調整できるように接続し効率的な熱伝達法で、魚肉や食肉を短時間に安定して、高付加乾燥できる魚肉や食肉の乾燥装置が実現した。 A steam boiler (1) is connected to the inlet side of the steam heating device (3) so that the amount of heat medium required for each process of fish and meat can be adjusted with a valve. A fish and meat drying device that can perform high-addition drying stably over time has been realized.
図1は、本発明装置の1実施例であって、(1)は水蒸気ボイラー、(2)は空気送風機、(3)は蒸気加熱装置、(4)は乾燥室、(5)はドレン分離器、(6)は水蒸気減圧弁、(7)は水蒸気流量調整弁、(8)は空気流量調整弁、(9)は乾燥室内温度検出器、(10)は魚肉や食肉の温度検出器、(11)は制御装置、(12)は魚肉や食肉の原料(生魚や生肉)である。 FIG. 1 shows an embodiment of the apparatus of the present invention, where (1) is a steam boiler, (2) is an air blower, (3) is a steam heating device, (4) is a drying chamber, and (5) is drain separation. (6) is a steam pressure reducing valve, (7) is a steam flow rate regulating valve, (8) is an air flow rate regulating valve, (9) is a drying chamber temperature detector, (10) is a fish or meat temperature detector, (11) is a control device, and (12) is a raw material for fish or meat (raw fish or raw meat).
水蒸気ボイラー(1)からの水蒸気は水蒸気減圧弁(6)による圧力調整、水蒸気流量調整弁(7)による流量制御を経て、蒸気加熱装置(3)に入り、過熱水蒸気に加熱したのち乾燥室(4)に供給される。その温度制御と流量制御は乾燥室内温度検出器(9)、魚肉や食肉の温度検出器(10)からの信号によって制御される。すなわち、乾燥室内温度検出器(9)の温度上昇割合に比べ魚肉や食肉の温度検出器(10)の温度上昇割合が高い時は蒸気加熱装置(3)の設定温度を下げ、逆の場合は温度を上げて、処理プロセスによって設定した温度範囲に乾燥室(4)を制御する。 The steam from the steam boiler (1) is subjected to pressure regulation by the steam pressure reducing valve (6) and flow control by the steam flow rate regulating valve (7), enters the steam heating device (3), is heated to superheated steam, and then dried to the drying chamber ( 4). The temperature control and flow rate control are controlled by signals from a drying chamber temperature detector (9) and a fish or meat temperature detector (10). That is, when the temperature rise rate of the fish or meat temperature detector (10) is higher than the temperature rise rate of the drying room temperature detector (9), the set temperature of the steam heating device (3) is lowered, and vice versa. The temperature is raised and the drying chamber (4) is controlled within the temperature range set by the treatment process.
乾燥室内(4)の温度を急速冷却させる場合は、空気送風機(2)により空気流量調整弁(8)を経て冷却空気を供給できる。 When the temperature in the drying chamber (4) is rapidly cooled, cooling air can be supplied by the air blower (2) through the air flow rate adjustment valve (8).
乾燥室(4)内に発生する液体水分はドレン分離器(5)によって、乾燥室(4)外に排出される。 Liquid moisture generated in the drying chamber (4) is discharged out of the drying chamber (4) by the drain separator (5).
プロセスごとの熱媒体の使用方法は、昇温プロセス、恒常乾燥プロセス、減率乾燥プロセス、減率乾燥において過熱水蒸気の流量を自動又は半自動で調節する。 The method of using the heat medium for each process adjusts the flow rate of superheated steam automatically or semi-automatically in a temperature raising process, a constant drying process, a reduced rate drying process, and a reduced rate drying.
水蒸気は、大気圧下でも容易に結露に至らない温度まで、蒸気加熱装置(3)で加熱し、乾燥室(4)内に充満させるために水蒸気流量調整弁(7)を調整して、乾燥室(4)内を、ほぼ大気圧に制御する。 The steam is heated by the steam heating device (3) to a temperature at which dew condensation does not easily occur even under atmospheric pressure, and the steam flow rate adjusting valve (7) is adjusted to fill the drying chamber (4), followed by drying. The inside of the chamber (4) is controlled to almost atmospheric pressure.
乾燥室(4)内における温度分布を均一化するため、過熱水蒸気の噴出しノズルを乾燥室の各部に配列する。 In order to make the temperature distribution in the drying chamber (4) uniform, a superheated steam jet nozzle is arranged in each part of the drying chamber.
魚肉や食肉の温度検出器(10)は、魚肉や食肉の原料(生魚や生肉)の中央部に差し込む検出器(10)を利用して魚肉や食肉の乾燥の自動制御を制御装置(11)によっておこなう。 The fish and meat temperature detector (10) is a control device (11) that automatically controls the drying of fish and meat using the detector (10) inserted into the center of the fish and meat raw materials (raw fish and raw meat). To do.
図2は、本発明の応用事例であり、(12)は魚肉や食肉の原料(生魚や生肉)、(13)は乾燥食品、(14)は味液、(15)は味漬け込み容器である。 FIG. 2 is an application example of the present invention, where (12) is a raw material of fish meat or meat (raw fish or raw meat), (13) is a dried food, (14) is a taste liquid, and (15) is a container for pickling. .
本発明の応用事例は高付加価値味付け乾燥製品の製造プロセスであり、生魚や生肉(12)を梅酢、醤油、みりん等の味液(14)にあらかじめ肉の中身まで味漬け込み容器(15)内で浸透させておいて、従来技術では長時間処理のため味が抜けるが、短時間で乾燥処理することが可能な本蒸気加熱装置(3)により、味は魚肉や食肉の乾燥食品に残せることができ、従来にない味付き乾燥食品の製造ができる。短時間処理とは例えば、従来技術が生鰹を乾燥食品の鰹節に2日〜7日必要としていたが、本発明装置では、7〜8時間処理を可能とした。このような方法で、梅酢に漬けて乾燥させた乾燥食品は「梅鰹節」、醤油に漬けて乾燥させた乾燥食品は「醤油鰹節」等として二つの機能を備えた調味液不要の食材ともなる。 An application example of the present invention is a manufacturing process of a high-value-added seasoned dry product, in which raw fish and raw meat (12) are pre-seasoned in a taste solution (14) such as plum vinegar, soy sauce, mirin, etc. in a container (15) In the conventional technology, the taste is lost due to the long-term treatment in the prior art, but the steam heating device (3) that can be dried in a short time allows the taste to remain in the fish or meat dried food. It is possible to produce a seasoned and dry food. With short-time treatment, for example, the prior art required ginger for dried food bonito for 2-7 days, but the apparatus of the present invention enabled 7-8 hours of treatment. In this way, dried foods soaked in plum vinegar and dried are `` meat bonito '', dried foods soaked in soy sauce and `` soy sauce bonito '' are two ingredients that do not require seasoning liquid .
従来の魚肉や食肉の乾燥機では、実現できなかった短い処理時間と高付加乾燥の高品質な魚肉や食肉の乾燥を実行できるので、使用価値は高いと考える。また、図2のように、予め味液(梅酢や醤油など)に漬けた生魚や生肉を本乾燥装置で処理することで味付き乾燥食品の製造もできる。 The conventional fish meat and meat dryers can be used to dry high-quality fish and meat with a short processing time and high addition drying that could not be realized. Moreover, as shown in FIG. 2, a seasoned dry food can also be manufactured by processing raw fish and raw meat previously soaked in a taste liquid (plum vinegar, soy sauce, etc.) with this drying apparatus.
1 水蒸気ボイラー
2 空気送風機
3 蒸気加熱装置
4 乾燥室
5 ドレン分離器
6 水蒸気減圧弁
7 水蒸気流量調整弁
8 空気流量調整弁
9 乾燥室内温度検出器
10 魚肉や食肉の温度検出器
11 制御装置
12 魚肉や食肉の原料(生魚や生肉)
13 乾燥食品
14 味液
15 味漬け込み容器
DESCRIPTION OF
11 Control device
12 Raw materials for fish and meat (raw fish and raw meat)
13 Dried food 14 Taste liquid 15 Taste pickle container
Claims (5)
In Claim 4, it is processed with the automatic or semi-automatic drying apparatus of Claim 1 after immersing in seasoning liquids, such as a plum flavor liquid and soy sauce, in the pre-processing process for manufacturing the dried food of fish meat and meat with various tastes. how to.
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US10006714B2 (en) | 2007-08-07 | 2018-06-26 | Mars, Incorporated | Apparatus for drying a material |
US10113794B2 (en) | 2007-08-07 | 2018-10-30 | Mars, Incorporated | Method for drying a material |
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