[go: up one dir, main page]

JP2017029002A - Process for producing processed meat products - Google Patents

Process for producing processed meat products Download PDF

Info

Publication number
JP2017029002A
JP2017029002A JP2015148927A JP2015148927A JP2017029002A JP 2017029002 A JP2017029002 A JP 2017029002A JP 2015148927 A JP2015148927 A JP 2015148927A JP 2015148927 A JP2015148927 A JP 2015148927A JP 2017029002 A JP2017029002 A JP 2017029002A
Authority
JP
Japan
Prior art keywords
meat
salt
extruder
temperature
minced
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.)
Granted
Application number
JP2015148927A
Other languages
Japanese (ja)
Other versions
JP6584850B2 (en
Inventor
久志 佐々木
Hisashi Sasaki
久志 佐々木
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.)
Prima Meat Packers Ltd
Original Assignee
Prima Meat Packers 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 Prima Meat Packers Ltd filed Critical Prima Meat Packers Ltd
Priority to JP2015148927A priority Critical patent/JP6584850B2/en
Publication of JP2017029002A publication Critical patent/JP2017029002A/en
Application granted granted Critical
Publication of JP6584850B2 publication Critical patent/JP6584850B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Meat, Egg Or Seafood Products (AREA)

Abstract

【課題】食肉加工品の製造において、塩溶化を促進させて製造工程の短期間化を図る製造方法の提供。【解決手段】食肉10をミンチ状に挽くミンチ工程S2の後に、5℃〜10℃の温度下にて、塩漬剤13を含む挽肉14を、その移送方向の川上側よりも川下側の圧縮力を高くする加圧押出手段を直列に2以上接続したルートに通して、前記挽肉14中の筋原線維を構成する蛋白質の一部を塩溶化させることを含む塩溶化工程S4を行う食肉加工品の製造方法。前記加圧押出手段が、温度保持機能を有するエクストルーダ15である、食肉加工品の製造方法。【選択図】図1[Problem] To provide a production method for shortening the production process by promoting salt solubilization in the production of processed meat products. After mincing step S2 for mincing meat 10 in a minced state, the minced meat 14 containing the salting agent 13 is compressed downstream from the upstream side in the transport direction at a temperature of 5 ° C to 10 ° C. Meat processing which performs salt solubilization process S4 including passing through the route which connected the pressure extrusion means which raises force two or more in series, and salt-soluting a part of protein which comprises the myofibril in the said meat 14 Product manufacturing method. A method for producing a processed meat product, wherein the pressure extrusion means is an extruder 15 having a temperature maintaining function. [Selection] Figure 1

Description

本発明は、食肉加工品を製造する方法に関する。   The present invention relates to a method for producing a processed meat product.

ソーセージ、ハム、ハンバーグ、肉団子などの食肉加工品は、外食産業および家庭で欠くことのできない食肉の一つである。例えば、練肉あるいは挽肉を用いた加工食品の代表であるソーセージは、一般的に、畜肉から塊状の肉を切り離した後、チョッパーなどを用いて挽肉とし、塩漬、ケーシングへの充填、くん煙および加熱の工程(ただし、非加熱ソーセージの場合には加熱工程は無い)を順に経て製造される。また、プレスハムは、挽肉とつなぎとの練り合わせ、塩漬、ケーシングへの充填、加熱の工程を順に経て製造される。これらの各工程の内、塩漬工程は、挽肉の結着性、食肉加工品の弾力性、保水性および発色性を決める重要な工程であり、各食品加工メーカーにて様々な工夫がなされている。塩漬工程にて挽肉に添加される塩漬剤には、例えば、食塩; 蛋白素材から成る結着剤; 重合リン酸塩などの結着補強剤; 香辛料; 調味料; 亜硝酸塩などの発色剤; 保存料; 甘味料などを含むものが知られている(特許文献1を参照)。   Processed meat products such as sausages, hams, hamburgers and meat dumplings are one of the indispensable meats in the food service industry and at home. For example, sausages, which are representative of processed foods using kneaded meat or minced meat, generally cut off lump meat from livestock meat, then crush it into ground meat, salted, filled into casings, smoked And a heating process (however, there is no heating process in the case of non-heated sausage). Press ham is manufactured through the steps of kneading minced meat and tuna, salting, filling into a casing, and heating. Among these processes, the salting process is an important process that determines the binding properties of minced meat, the elasticity of processed meat products, water retention and color development, and various ingenuity has been made by each food processing manufacturer. Yes. Examples of salting agents added to minced meat in the salting process include salt; a binder made of a protein material; a binding reinforcing agent such as a polymerized phosphate; a spice; a seasoning; and a coloring agent such as nitrite. A preservative; one containing a sweetener or the like is known (see Patent Document 1).

挽肉の結着性は、筋原線維を構成する蛋白質の一種であるミオシンの他、アクチンとミオシンとが結合したアクトミオシンに起因することが知られている。挽肉を2〜5%程度の食塩水に漬けると、筋原線維からミオシンおよびアクトミオシンが溶解抽出され、挽肉が粘り気を帯びてくる。この粘り気の正体は、アクトミオシンゾルとも称し、挽肉の結着性を決める。また、その後の加熱工程にて、アクトミオシンゾルは分子間架橋を経て三次元網目構造を形成し、その網目の中に水を封じ込める。この結果、ソーセージ等の食肉加工品は、適度な弾力性と保水性を有するようになる(特許文献2を参照)。   The binding property of minced meat is known to be attributed to actomyosin in which actin and myosin are bound in addition to myosin, which is a kind of protein constituting myofibrils. When minced meat is soaked in about 2 to 5% saline, myosin and actomyosin are dissolved and extracted from myofibrils, and the minced meat becomes sticky. This sticky identity is also called actomyosin sol and determines the binding of minced meat. Further, in the subsequent heating step, actomyosin sol forms a three-dimensional network structure through intermolecular crosslinking, and encloses water in the network. As a result, processed meat products such as sausages have moderate elasticity and water retention (see Patent Document 2).

特開2012−147768号公報JP 2012-147768 A 特開2005−065550号公報Japanese Patent Laying-Open No. 2005-065550

しかし、上述の従来から公知の塩漬工程には、次のような問題がある。挽肉の筋原線維からミオシンやアクトミオシンを十分に抽出するには、塩漬剤を挽肉に添加後、通常、5℃〜10℃の温度で0.5〜7日間、冷蔵室にて塩漬し熟成させる必要がある。この塩溶化を進行させるための熟成期間がソーセージ等の食肉加工品の製造工程の全期間に占める比率は、比較的大きい。このため、ソーセージ等の食肉加工品の製造期間の短縮を図るうえで、塩溶化の短期間化が強く望まれていた。   However, the above-described conventionally known salting process has the following problems. To fully extract myosin and actomyosin from minced myofibrils, salting agent is usually added to minced meat and then salted in a refrigerated room at a temperature of 5-10 ° C for 0.5-7 days. Need to be matured. The ratio of the aging period for promoting the salt solubilization to the whole period of the manufacturing process of processed meat products such as sausages is relatively large. For this reason, in order to shorten the manufacturing period of processed meat products such as sausages, it has been strongly desired to shorten the salt solubilization period.

本発明は、かかる課題を解決するためになされたものであり、食肉加工品の製造において、塩溶化を促進させて製造工程の短期間化を図ることを目的とする。   This invention is made | formed in order to solve this subject, and aims at shortening of a manufacturing process by promoting salt solubilization in manufacture of processed meat products.

本発明者は、上記目的を達成するために鋭意、研究開発を重ねてきた結果、挽肉に塩漬剤を添加後、若しくは塩漬剤を添加したカット肉を挽肉にした後、塩漬剤を含む挽肉を加圧し、かつ冷却しながら充填工程へと移送することにより、長期間の冷蔵を行うことなく塩溶化を進めることができるとの知見を得て、本発明の完成に至った。課題解決の具体的な手段は、以下のとおりである。   As a result of intensive research and development to achieve the above object, the present inventor has added a salting agent to the minced meat, or after cutting the cut meat to which the salting agent has been added, and then adding the salting agent. Obtaining the knowledge that salt solubilization can be promoted without performing long-term refrigeration by pressurizing and transferring the ground meat containing it to the filling step while cooling, has led to the completion of the present invention. Specific means for solving the problem are as follows.

上記目的を達成するための本発明の一実施の形態に係る食肉加工品の製造方法は、食肉をミンチ状に挽くミンチ工程の後に、5℃〜10℃の温度下にて、塩漬剤を含む挽肉を、その移送方向の川上側よりも川下側の圧縮力を高くする加圧押出手段に通して、挽肉中の筋原線維を構成する蛋白質の一部を塩溶化させることを含む塩溶化工程を行う製造方法である。   In order to achieve the above object, a method for producing a processed meat product according to an embodiment of the present invention is characterized in that a salting agent is added at a temperature of 5 ° C. to 10 ° C. after the mincing step of mincing meat into minced form. The salt solubilization includes salt-solubilizing a part of the protein constituting the myofibrils in the minced meat by passing the minced meat containing it through a pressure extruding means that makes the compressive force on the downstream side higher than the upstream side in the transport direction. It is the manufacturing method which performs a process.

別の実施の形態に係る食肉加工品の製造方法は、さらに、塩溶化工程を、加圧押出手段を直列に2以上接続したルートに、塩漬剤を含む挽肉を通すことを含めて行っても良い。   The method for producing a processed meat product according to another embodiment further includes performing a salt solubilization step by passing ground meat containing a salting agent through a route in which two or more pressure extrusion means are connected in series. Also good.

別の実施の形態に係る食肉加工品の製造方法は、また、塩溶化工程を、塩漬剤を含む挽肉を、上述の温度下に保持しながら、1または2以上のエクストルーダに通過させることを含む工程としても良い。   The method for producing a processed meat product according to another embodiment also includes passing the salt solubilizing step through one or more extruders while maintaining the ground meat containing the salting agent at the above-described temperature. It is good also as a process including.

別の実施の形態に係る食肉加工品の製造方法は、さらに、エクストルーダとして、上述の温度下に保持する温度保持機能を有するエクストルーダを用いて行っても良い。   The method for manufacturing a processed meat product according to another embodiment may further be performed using an extruder having a temperature holding function of holding at the above-described temperature as an extruder.

本発明によれば、食肉加工品の製造において、塩溶化を促進させて製造工程の短期間化を図ることができる。   According to the present invention, in the manufacture of processed meat products, salt solubilization can be promoted to shorten the manufacturing process.

図1は、本発明の一実施の形態に係る食肉加工品の製造方法の例示的なフローを示す。FIG. 1 shows an exemplary flow of a method for manufacturing a processed meat product according to an embodiment of the present invention. 図2は、図1の加圧押出の工程で好適に用いられるエクストルーダの断面図(2A)および該エクストルーダ内に供された挽肉をその反対側に向かって押し出す状況の断面図(2B)をそれぞれ示す。FIG. 2 is a cross-sectional view (2A) of an extruder suitably used in the pressure extrusion process of FIG. 1 and a cross-sectional view (2B) of a situation in which ground meat provided in the extruder is pushed out to the opposite side. Show. 図3は、図2のエクストルーダの変形例の断面図およびその一部の拡大断面図をそれぞれ示す。FIG. 3 shows a sectional view of a modification of the extruder of FIG. 2 and an enlarged sectional view of a part thereof. 図4は、図2のエクストルーダを複数個直列に接続して、挽肉を複数のエクストルーダに通して塩溶化を促進する方法を説明する模式図を示す。FIG. 4 is a schematic diagram for explaining a method of connecting a plurality of extruders of FIG. 2 in series and passing ground meat through the plurality of extruders to promote salt solubilization. 図5は、図1のフローの変形例を示す。FIG. 5 shows a modification of the flow of FIG.

次に、本発明に係る食肉加工品の製造方法の実施の形態について、図面を参照しながら説明する。なお、以下に説明する実施の形態は、本発明を限定するものではなく、また、実施の形態の中で説明されている諸要素およびその組み合わせの全てが本発明の解決手段に必須であるとは限らない。   Next, an embodiment of a method for producing a processed meat product according to the present invention will be described with reference to the drawings. Note that the embodiments described below do not limit the present invention, and that all the elements and combinations thereof described in the embodiments are essential for the solution means of the present invention. Is not limited.

1.定義
本願における「食肉加工品」は、ソーセージ類; プレスハムなどの小肉塊と挽肉、練肉からなるつなぎにより結着加工されるハム類; ハンバーグ; 肉団子などを含むように広義に解釈される。「塩溶化工程」は、加圧押出のみで、あるいは加圧押出と冷蔵庫等の一定温度環境下での静置との組み合わせで塩溶化を行う工程である。「塩漬剤」は、少なくとも塩を含み、食肉中に存在する塩溶性の筋原線維蛋白質の一部を抽出させる作用を有する添加剤をいう。また、「塩」は、酸と塩基との中和反応によって生じるイオン化合物であり、その代表例として塩化ナトリウムを挙げることができる。ただし、「塩」は、塩化ナトリウム以外に、例えば、塩化カリウム若しくは塩化マグネシウムなどの他種アルカリ金属塩若しくはアルカリ土類金属塩も含む。
1. Definitions “Processed meat products” in this application are broadly interpreted to include sausages; hams that are processed by binding of small lumps such as press ham and ground meat and paste; hamburgs; meat dumplings, etc. The The “salt solubilization step” is a step of performing salt solubilization only by pressure extrusion or by a combination of pressure extrusion and standing in a constant temperature environment such as a refrigerator. “Saling agent” refers to an additive containing at least a salt and having an action of extracting a part of a salt-soluble myofibrillar protein present in meat. A “salt” is an ionic compound produced by a neutralization reaction between an acid and a base, and a typical example thereof is sodium chloride. However, the “salt” includes, in addition to sodium chloride, other alkali metal salts or alkaline earth metal salts such as potassium chloride or magnesium chloride.

2.食肉加工品の製造方法
図1は、本発明の一実施の形態に係る食肉加工品の製造方法の例示的なフローを示す。以下、ソーセージを例に説明する。
2. Method for Manufacturing Processed Meat FIG. 1 shows an exemplary flow of a method for manufacturing a processed meat product according to an embodiment of the present invention. Hereinafter, sausage will be described as an example.

この実施の形態に係るソーセージの製造方法は、例えば、図1に示すように、骨からの肉塊の分離(ステップS1)、肉挽(ステップS2)、塩漬剤との混合(ステップS3)、加圧押出を含む塩溶化(ステップS4)、充填(ステップS5)、くん煙処理(ステップS6)、加熱処理(ステップS7)および冷却処理(ステップS8)の各工程を含む。以下、各工程を説明する。   The sausage manufacturing method according to this embodiment includes, for example, as shown in FIG. 1, separation of meat chunks from bone (step S1), meat grinding (step S2), and mixing with a salting agent (step S3). Each process includes salt solubilization including pressure extrusion (step S4), filling (step S5), smoke treatment (step S6), heat treatment (step S7) and cooling treatment (step S8). Hereinafter, each process will be described.

(1)骨からの肉塊の分離(ステップS1)
この工程は、牛、豚、羊、山羊、鳥などの家畜あるいは鯨などの海獣(家畜等という)を解体して、家畜等の骨から、食肉に供する肉塊10を切り離す工程である。通常、この工程では、家畜等の部位ごとに肉塊10を切り離すが、部位ごとの切り離しを要しない場合もある。
(1) Separation of meat chunks from bone (step S1)
This process is a process of disassembling livestock such as cattle, pigs, sheep, goats and birds, or sea beasts such as whales (referred to as livestock), and separating the meat lump 10 for meat from bones of livestock and the like. Normally, in this step, the meat chunk 10 is cut for each part of the livestock or the like, but there is a case where it is not necessary to cut the part for each part.

(2)肉挽(ミンチ: ステップS2)
この工程は、ブロック状の肉塊10をミンチ状に細かく挽くミンチ工程である。肉挽の工程は、チョッパーと称する肉挽き機11を用いて、目開き2〜5mmのプレートから挽肉を練り出して行われる。なお、あら挽きの場合には、目開き5mmを超えるプレートを用いる。なお、この工程に先立ち、肉塊を細切りする工程を行っても良い。
(2) Meat grinding (mince: step S2)
This process is a mincing process in which the block-shaped meat lump 10 is finely ground into a minced shape. The meat grinding step is performed by kneading the ground meat from a plate having an opening of 2 to 5 mm using a meat grinder 11 called a chopper. In the case of rough grinding, a plate having an opening exceeding 5 mm is used. Prior to this step, a step of cutting the meat chunk may be performed.

(3)塩漬剤との混合(ステップS3)
この工程は、挽肉に、塩漬剤13と、好ましくは異種蛋白質とを混合する工程であり、塩漬工程ともいう。異種蛋白質としては、例えば、大豆蛋白質、卵白蛋白質を挙げることができる。異種蛋白質の添加方法は、特に限定されるものではないが、粉末状で添加、水などでゲル化してからの添加、細かく粉砕して添加等を例示できる。塩漬剤13(液状のものを、特に、ピックル液という)は、塩化ナトリウムに代表される塩を少なくとも含む。塩漬剤13は、塩以外に、例えば、発色剤、結着補強剤、香辛料、調味料、保存料および甘味料の少なくとも1以上を含むものでも良い。発色剤は、肉中のミオグロビンを変化させ、後の加熱によってソーセージの色が灰色にならずにサーモンピンクを保持するための添加物である。発色剤としては、硝酸カリウムあるいは硝酸ナトリウム等の硝酸塩の他、亜硝酸ナトリウムなどの亜硝酸塩を好適に例示できる。結着補強剤は、挽肉の結着性を高めるための添加物であり、リン酸一ナトリウム、リン酸二カリウムなどの正リン酸塩の他、ポリリン酸ナトリウム、メタリン酸ナトリウムなどの重合リン酸塩を好適に例示できる。香辛料および調味料は、主に味付けを行うための添加剤であり、唐辛子、バジリコ、ヒメウイキョウの他、グルタミン酸ナトリウム、イノシン酸ナトリウムなどを好適に例示できる。保存料は、ソーセージを長期に保存あらしめる添加剤であり、ソルビン酸カリウム、ソルビン酸カルシウムなどを好適に例示できる。甘味料は、甘み成分であり、スクラロース、ステビアなどを好適に例示できる。その他、アスコルビン酸、ビタミンCなどの酸化防止剤を加えても良い。塩漬剤13と挽肉との混合方法は、塩漬剤13と挽肉とを混合できる限り、如何なる方法でも良い。例えば、ミキサーを用いて、ミキサー内で塩漬剤13と挽肉とを混合することができる。
(3) Mixing with salting agent (step S3)
This step is a step of mixing the salting agent 13 and preferably a heterologous protein into the minced meat, and is also referred to as a salting step. Examples of the heterologous protein include soy protein and egg white protein. The method for adding the heterogeneous protein is not particularly limited, and examples thereof include addition in a powder form, addition after gelation with water, fine addition after pulverization, and the like. The salting agent 13 (a liquid thing, especially a pickle liquid) contains at least a salt typified by sodium chloride. In addition to salt, the salting agent 13 may contain, for example, at least one or more of a color former, a binder reinforcing agent, a spice, a seasoning, a preservative, and a sweetener. The color former is an additive for changing the myoglobin in the meat and maintaining salmon pink without causing the sausage color to become gray by subsequent heating. Preferred examples of the color former include nitrates such as potassium nitrate and sodium nitrate, and nitrites such as sodium nitrite. Binder reinforcement is an additive for enhancing the binding properties of minced meat. In addition to normal phosphates such as monosodium phosphate and dipotassium phosphate, polymerized phosphoric acid such as sodium polyphosphate and sodium metaphosphate. A salt can be illustrated suitably. Spices and seasonings are mainly additives for seasoning, and can be suitably exemplified by sodium glutamate, sodium inosinate, and the like in addition to chili, basil, and Japanese fennel. The preservative is an additive that preserves sausage for a long period of time, and examples thereof include potassium sorbate and calcium sorbate. The sweetener is a sweetening ingredient, and sucralose, stevia and the like can be suitably exemplified. In addition, antioxidants such as ascorbic acid and vitamin C may be added. The mixing method of the salting agent 13 and the minced meat may be any method as long as the salting agent 13 and the minced meat can be mixed. For example, the salting agent 13 and the minced meat can be mixed in the mixer using a mixer.

(4)加圧押出を含む塩溶化(ステップS4)
この工程は、塩漬剤を加えた挽肉14(単に、挽肉14ともいう)を、その移送方向の川上側よりも川下側の圧縮力を高くする加圧押出手段に通して、当該挽肉14中の筋原線維を構成する蛋白質の一部を塩溶化させる加圧押出の処理を含む塩溶化工程である。加圧押出手段としては、所定の方向に向かう挽肉14に対して、その移動を妨げる抵抗力を加えて押し出す手段であれば、その形態の如何を問わない。この実施の形態では、加圧押出手段として、エクストルーダ15を好適に例示できる。エクストルーダ15の一方側から挽肉14を入れて、加圧しながら、その反対側に向かって挽肉14を押し出していくと、挽肉14の外周に加えられる上記加圧作用によって、塩溶化を促進することができる。このため、0.5〜7日間冷蔵庫に挽肉14を静置させて塩溶化を行う従来の方法に比べて、極めて短時間にて塩溶化工程を行うことができる。具体的には、早ければ10〜60秒、少し時間を要するものでも1〜5時間にて塩溶化工程を完了することができる。具体的には、エクストルーダ15に挽肉14を入れて加圧押出を行うことにより塩溶化を完了できる場合には、10〜60秒の加圧押出の処理時間だけで済む。一方、エクストルーダ15に挽肉14を入れて加圧押出を行った後若しくは行う前に、冷蔵庫にて静置する必要がある場合には、10〜60秒の加圧押出時間と冷蔵庫内での静置時間とを加えて合計1〜5時間の塩溶化処理時間を要する。冷蔵庫内での静置を伴う場合でも、加圧押出を行うことにより静置時間を著しく低減できるというメリットがある。また、エクストルーダ15に挽肉14を通すだけで塩溶化を終了できる場合には、特に、挽肉14を移送する過程で塩溶化を行うことができるので、挽肉14を移送する工程から一旦、挽肉14を別の場所(冷蔵庫など)に移動することなく、スムーズに塩溶化工程を行うことができるというメリットもある。加圧押出によって行う塩溶化工程は、塩漬剤を含む挽肉14を、5℃〜10℃の温度に保持しながら、1または2以上のエクストルーダ15に通過させる工程とするのが好ましい。かかる温度保持の方法については後述する。
(4) Salt solubilization including pressure extrusion (step S4)
In this process, the minced meat 14 to which the salting agent is added (also simply referred to as the minced meat 14) is passed through a pressure extrusion means for increasing the compressive force on the downstream side relative to the upstream side in the transfer direction. This is a salt solubilization step including a pressure extrusion treatment in which a part of the protein constituting the myofibrils is salt-solubilized. The pressurizing and extruding means may be of any form as long as it is a means for extruding the ground meat 14 heading in a predetermined direction by applying a resistance force that prevents its movement. In this embodiment, the extruder 15 can be suitably exemplified as the pressure extrusion means. When the minced meat 14 is put from one side of the extruder 15 and pressed while pushing the minced meat 14 toward the opposite side, salt pressurization is promoted by the pressurizing action applied to the outer periphery of the minced meat 14. it can. For this reason, the salt solubilization process can be performed in an extremely short time as compared with the conventional method in which the ground meat 14 is allowed to stand in the refrigerator for 0.5 to 7 days for salt solubilization. Specifically, the salt solubilization step can be completed in 1 to 5 hours even if it takes 10 to 60 seconds at the earliest time. Specifically, if salt solubilization can be completed by putting the minced meat 14 into the extruder 15 and performing pressure extrusion, only the processing time of pressure extrusion of 10 to 60 seconds is required. On the other hand, if it is necessary to place the ground meat 14 in the extruder 15 and leave it in the refrigerator before or after performing the pressure extrusion, the pressure extrusion time of 10 to 60 seconds and the static A total of 1 to 5 hours of salt solution treatment time is required. Even when standing still in the refrigerator, there is a merit that the standing time can be remarkably reduced by performing pressure extrusion. Further, when salt soaking can be completed simply by passing the minced meat 14 through the extruder 15, salt solubilization can be performed in the process of transferring the minced meat 14, so that the minced meat 14 is temporarily removed from the process of transferring the minced meat 14. There is also an advantage that the salt solubilization process can be performed smoothly without moving to another place (such as a refrigerator). The salt solubilization step performed by pressure extrusion is preferably a step of passing the ground meat 14 containing the salting agent through one or more extruders 15 while maintaining the temperature at 5 ° C. to 10 ° C. A method for maintaining the temperature will be described later.

(5)充填(ステップS5)
この工程は、塩溶化工程後の挽肉14を、羊や豚等に由来する天然ケーシングあるいは人工的に製造されたケーシングに充填する工程である。この工程によって、複数個のソーセージがつながったリンク状ソーセージ16が出来上がる。
(5) Filling (step S5)
This step is a step in which the minced meat 14 after the salt solubilization step is filled into a natural casing derived from sheep, pigs or the like or an artificially manufactured casing. By this process, a linked sausage 16 in which a plurality of sausages are connected is completed.

(6)くん煙処理(ステップS6)
この工程は、例えば、サクラ、ブナ、カシなどのチップを用いて、50℃〜85℃の温度条件でリンク状ソーセージ16を燻す工程である。くん煙に含まれる特有の香味成分、表面光沢成分、フェノール物質がリンク状ソーセージ16に付着および浸透することにより、リンク状ソーセージ16内部の脂質成分に抗酸化力および高菌力を付与できる。なお、ノンスモーク製品の場合、この工程は省かれる。
(6) Smoke treatment (step S6)
This step is a step of pouring the linked sausage 16 under a temperature condition of 50 ° C. to 85 ° C., for example, using chips such as cherry, beech and oak. The specific flavor component, surface gloss component, and phenol substance contained in the smoke are attached to and penetrated into the linked sausage 16, so that the lipid component in the linked sausage 16 can be imparted with antioxidant power and high bacterial power. In the case of a non-smoked product, this process is omitted.

(7)加熱処理(ステップS7)
この工程は、くん煙処理後のソーセージ17(以後、単に、ソーセージ17ともいう)を湯釜18に投入してボイルする工程である。湯の好適な温度は、63℃〜90℃である。また、ボイルに代えて、ソーセージ17をスモークハウス内で蒸気加熱することもできる。この場合の蒸気の好適な温度は、ボイルと同様、63℃〜90℃である。
(7) Heat treatment (step S7)
This step is a step in which the sausage 17 after the smoke treatment (hereinafter simply referred to as sausage 17) is put into the kettle 18 and boiled. A suitable temperature of the hot water is 63 ° C to 90 ° C. Moreover, it can replace with a boil and the sausage 17 can also be steam-heated in a smoke house. The suitable temperature of the vapor | steam in this case is 63 to 90 degreeC like a boil.

(8)冷却処理(ステップS8)
この工程は、加熱処理後のソーセージ17を室温まで冷却する工程である。冷却の方法は、自然放冷の他、冷蔵室内で積極的に冷やす方法でも良い。
(8) Cooling process (step S8)
This step is a step of cooling the sausage 17 after the heat treatment to room temperature. As a cooling method, in addition to natural cooling, a method of actively cooling in a refrigerator compartment may be used.

上記工程の内、食肉加工品の種類によっては、くん煙処理(ステップS6)および/または加熱処理(ステップS7)を行わなくとも良い。例えば、サラミソーセージのような非加熱食肉加工品の場合には、充填(ステップS5)の後、乾燥工程を行い、法律で定める水分活性値となるまで乾燥して仕上げることができる。   Of the above processes, depending on the type of processed meat product, the smoke treatment (step S6) and / or the heat treatment (step S7) may not be performed. For example, in the case of a non-heated meat processed product such as salami sausage, after filling (step S5), a drying process is performed, and the product can be dried and finished until it reaches a water activity value stipulated by law.

3.加圧押出手段
図2は、図1の加圧押出の工程で好適に用いられるエクストルーダの断面図(2A)および該エクストルーダ内に供された挽肉をその反対側に向かって押し出す状況の断面図(2B)をそれぞれ示す。なお、(2B)では、(2A)に示す冷媒の循環ルートが省略されている。
3. FIG. 2 is a cross-sectional view (2A) of an extruder suitably used in the pressure-extrusion process of FIG. 1 and a cross-sectional view of a situation in which ground meat provided in the extruder is pushed out toward the opposite side ( 2B) respectively. In (2B), the refrigerant circulation route shown in (2A) is omitted.

図2(2A)に示すように、エクストルーダ15は、好適には金属から構成され、長さ方向両端を開口する筒体20である。筒体20の一方の開口部21は、挽肉14を供給可能な大きさである。筒体20の開口部21と反対側にある開口部22は、開口部21よりも小径に開口される。筒体20は、その内部にあって筒体20の長さ方向に延出する回転軸23を回転可能に固定する。回転軸23は、その周囲に、回転軸23の長さ方向に進行するスクリュー24を形成してなる。スクリュー24の外周と筒体20の内壁との隙間は、開口部21から開口部22に進むに従い狭くなっている。   As shown in FIG. 2 (2A), the extruder 15 is a cylindrical body 20 that is preferably made of metal and opens at both ends in the length direction. One opening 21 of the cylindrical body 20 has a size capable of supplying the ground meat 14. The opening 22 on the opposite side of the opening 21 of the cylindrical body 20 is opened with a smaller diameter than the opening 21. The cylindrical body 20 is rotatably fixed to a rotary shaft 23 that is inside and extends in the length direction of the cylindrical body 20. The rotary shaft 23 is formed with a screw 24 that travels in the length direction of the rotary shaft 23 around the rotary shaft 23. The gap between the outer periphery of the screw 24 and the inner wall of the cylindrical body 20 becomes narrower as it proceeds from the opening 21 to the opening 22.

エクストルーダ15は、5℃〜10℃の温度下に保持する温度保持機能を有するエクストルーダであるのが好ましく、筒体20の外周には、例えば、冷媒26を流すための中空状のチューブ25が巻回されている。冷媒26は、筒体20の内部に供された挽肉14から熱を奪って気化し、コンプレッサ27に送られて高圧ガスとなる。高圧ガスは、放熱器28にて放熱して液体に戻る。液体に戻った冷媒26は、エクスパンションバルブ29に送られて低圧ガスとなる。低圧ガスは、チューブ25を通過する際に再び挽肉14から熱を奪って気化し、コンプレッサ27に送られる。このように、筒体20、コンプレッサ27、放熱器28、エクスパンションバルブ29を順々に移動するサイクルによって、気化圧縮型の冷却システムを構築できる。これによって、エクストルーダ15内にて加圧押出しされる挽肉14の温度が上昇して蛋白質変性を生じないレベルに冷却できるようにしている。筒体20にチューブ25を巻回する方法以外に、スクリュー24内に冷媒26を流しても良い。エクストルーダ15で保持する温度範囲は、5℃〜10℃、好ましくは6℃〜9℃、さらに好ましくは7℃〜8℃の範囲である。5℃以上の温度とすることにより、挽肉14の塩溶化をスムーズに進行させることができる。また、10℃以下の温度とすることにより、挽肉14の蛋白質変性を防止できる。エクストルーダ15の特に内部の温度を上記温度範囲とすることにより、エクストルーダ15内で挽肉14を加圧した際に挽肉14の塩溶化を進め、かつ挽肉14が局部的に温度上昇するのを効果的に抑制することができる。かかる温度を維持するための冷媒26としては、例えば、二酸化炭素、空気、代替フロンなどを挙げることができる。また、気化圧縮型の冷却システム以外に、よりシンプルな冷水循環システムを採用しても良い。その場合の冷媒26は水である。冷水循環システムを採用する場合、エクストルーダ15の保持温度は、5℃〜10℃の範囲内において10℃に近い温度(例えば、8℃〜10℃)の場合に特に有効である。   The extruder 15 is preferably an extruder having a temperature holding function of holding at a temperature of 5 ° C. to 10 ° C. A hollow tube 25 for flowing the refrigerant 26 is wound around the outer periphery of the cylindrical body 20, for example. It has been turned. The refrigerant 26 takes heat from the minced meat 14 provided inside the cylindrical body 20 and vaporizes it, and is sent to the compressor 27 to become high-pressure gas. The high-pressure gas radiates heat at the radiator 28 and returns to the liquid. The refrigerant 26 returned to the liquid is sent to the expansion valve 29 and becomes low-pressure gas. When passing through the tube 25, the low-pressure gas again takes heat from the minced meat 14 and vaporizes, and is sent to the compressor 27. Thus, a vaporization compression type cooling system can be constructed by a cycle in which the cylindrical body 20, the compressor 27, the radiator 28, and the expansion valve 29 are moved in order. As a result, the temperature of the minced meat 14 that is pressure-extruded in the extruder 15 rises so that it can be cooled to a level that does not cause protein denaturation. In addition to the method of winding the tube 25 around the cylindrical body 20, the refrigerant 26 may flow through the screw 24. The temperature range held by the extruder 15 is 5 ° C to 10 ° C, preferably 6 ° C to 9 ° C, more preferably 7 ° C to 8 ° C. By setting the temperature to 5 ° C. or higher, salt solubilization of the minced meat 14 can proceed smoothly. Moreover, protein modification | denaturation of the minced meat 14 can be prevented by setting it as the temperature of 10 degrees C or less. By setting the temperature inside the extruder 15 in particular within the above-mentioned temperature range, it is effective that the ground meat 14 is salted when the ground meat 14 is pressurized in the extruder 15 and the temperature rises locally. Can be suppressed. Examples of the refrigerant 26 for maintaining the temperature include carbon dioxide, air, and alternative chlorofluorocarbon. In addition to a vaporization compression type cooling system, a simpler cold water circulation system may be adopted. In this case, the refrigerant 26 is water. When the cold water circulation system is employed, the holding temperature of the extruder 15 is particularly effective when the temperature is close to 10 ° C. (for example, 8 ° C. to 10 ° C.) within the range of 5 ° C. to 10 ° C.

上記気化圧縮型の冷却システム以外に、例えば、アブソーバー、ジェネレーター、セパレーター、コンデンサ、エバポレーター(筒体20側)を接続する循環システムによる気化吸収型の冷却システムを採用しても良い。この場合、冷媒26としてアンモニアを用い、吸収液として水を用いることができる。また、冷媒26として水を用い、吸収液として臭化リチウムを用いても良い。   In addition to the vaporization compression type cooling system, for example, a vaporization absorption type cooling system by a circulation system connecting an absorber, a generator, a separator, a condenser, and an evaporator (on the cylinder 20 side) may be adopted. In this case, ammonia can be used as the refrigerant 26 and water can be used as the absorbing liquid. Further, water may be used as the refrigerant 26 and lithium bromide may be used as the absorbing solution.

図2(2B)に示すように、回転軸23を矢印Bの方向に回転させ、挽肉14を矢印Aの方向から筒体20の内部に向けて供給すると、挽肉14は開口部22に向かって移動する。挽肉14は、筒体20の壁面などからの圧力を受けて圧縮されながら、矢印Cに示すように、開口部22から出てくる。開口部22から出てくる挽肉14は、開口部21から供給された状態と比べて圧縮された状態となる。スクリュー24で開口部22に向かって送られながら筒体20内にて加圧されることにより、挽肉14の塩溶化を促進することができる。この結果、挽肉14を、長時間、冷蔵庫にて静置する工程を行うことなく、エクストルーダ15を通すだけ、あるいはエクストルーダ15を通した後若しくは通す前に冷蔵庫内で従来よりも短い時間の静置を行うだけで塩溶化工程を完了することができる。   As shown in FIG. 2 (2 B), when the rotating shaft 23 is rotated in the direction of the arrow B and the ground meat 14 is supplied from the direction of the arrow A toward the inside of the cylindrical body 20, the ground meat 14 is directed toward the opening 22. Moving. The ground meat 14 emerges from the opening 22 as indicated by an arrow C while being compressed by receiving pressure from the wall surface of the cylindrical body 20 or the like. The minced meat 14 coming out of the opening 22 is in a compressed state compared to the state supplied from the opening 21. By being pressurized in the cylindrical body 20 while being sent toward the opening 22 by the screw 24, salt solubilization of the minced meat 14 can be promoted. As a result, the ground meat 14 is allowed to stand for a shorter time in the refrigerator than before without passing through the extruder 15 or after passing through the extruder 15 without performing the process of leaving the ground meat 14 in the refrigerator for a long time. The salt solubilization step can be completed simply by performing the step.

図3は、図2のエクストルーダの変形例の断面図およびその一部の拡大断面図をそれぞれ示す。   FIG. 3 shows a sectional view of a modification of the extruder of FIG. 2 and an enlarged sectional view of a part thereof.

図3に示すエクストルーダ15aは、図2のエクストルーダ15と異なり、気化に伴う除熱ではなく、ペルチェ方式によって筒体20を冷却する構成を有する。具体的には、エクストルーダ15aは、筒体20の外側に、ペルチェ素子30を備える温度保持機能(例えば、冷却機能)付きエクストルーダである。エクストルーダ15aの上記以外の構成は、図2のエクストルーダ15と共通する。   Unlike the extruder 15 of FIG. 2, the extruder 15a shown in FIG. 3 has the structure which cools the cylinder 20 not by the heat removal accompanying vaporization but by the Peltier method. Specifically, the extruder 15 a is an extruder with a temperature holding function (for example, a cooling function) that includes the Peltier element 30 on the outside of the cylindrical body 20. The other configuration of the extruder 15a is the same as that of the extruder 15 in FIG.

エクストルーダ15aの一部Dの拡大断面図に示すように、ペルチェ素子30は、金属板31と金属板32との間において、金属板31側に複数枚の導電板33を、所定間隔をあけて直列に配置し、金属板32側に複数枚の導電板34を、所定間隔をあけて、かつ対向する導電板33と一部重なるように配置する構成を備える。導電板33と導電板34との重複領域の隙間には、n型半導体35、p型半導体36を交互に配置する。この結果、金属板31から金属板32に向かって、導電板33、n型半導体35、導電板34の順に積層し、金属板32から金属板31に向かって、導電板34、p型半導体36、導電板33の順に積層したn字形状の基本ユニットが形成される。金属板31と金属板32との間には、かかる基本ユニットを直列に接続した構造が形成されている。金属板32は筒体20に接している。図3中の左端の導電板33から右端の導電板33に向かって電圧をかけると、金属板32側が吸熱、金属板31側が放熱となる熱サイクルを構成できる。これによって、エクストルーダ15aの筒体20を冷却することができる。冷媒を用いることなく、電力調整によって、金属板32の温度を調整できるので、筒体20のより正確な温度制御が可能となる。なお、外気が5℃以下であって、筒体20が5℃〜10℃よりも低温の場合には、電流の向きを変え、あるいは金属板31側を筒体20に接するようにペルチェ素子30を筒体20に固定して、5℃〜10℃の温度範囲内の所定温度に筒体20を維持できるようにしても良い。   As shown in the enlarged sectional view of a part D of the extruder 15a, the Peltier element 30 includes a plurality of conductive plates 33 on the metal plate 31 side with a predetermined interval between the metal plate 31 and the metal plate 32. It has a configuration in which a plurality of conductive plates 34 are arranged in series and arranged on the metal plate 32 side so as to partially overlap the conductive plate 33 facing each other with a predetermined interval. N-type semiconductors 35 and p-type semiconductors 36 are alternately arranged in the gaps between the overlapping regions of the conductive plates 33 and 34. As a result, the conductive plate 33, the n-type semiconductor 35, and the conductive plate 34 are sequentially stacked from the metal plate 31 toward the metal plate 32, and the conductive plate 34 and the p-type semiconductor 36 are directed from the metal plate 32 toward the metal plate 31. The n-shaped basic unit is formed by laminating the conductive plates 33 in this order. A structure in which such basic units are connected in series is formed between the metal plate 31 and the metal plate 32. The metal plate 32 is in contact with the cylindrical body 20. When a voltage is applied from the leftmost conductive plate 33 to the rightmost conductive plate 33 in FIG. 3, a heat cycle in which the metal plate 32 side absorbs heat and the metal plate 31 side dissipates heat can be configured. Thereby, the cylinder 20 of the extruder 15a can be cooled. Since the temperature of the metal plate 32 can be adjusted by adjusting the electric power without using a refrigerant, more accurate temperature control of the cylindrical body 20 is possible. When the outside air is 5 ° C. or lower and the cylinder 20 is lower than 5 ° C. to 10 ° C., the direction of the current is changed, or the Peltier element 30 is in contact with the cylinder 20 on the metal plate 31 side. May be fixed to the cylinder 20 so that the cylinder 20 can be maintained at a predetermined temperature within a temperature range of 5 ° C to 10 ° C.

4.食肉加工品の製造方法の変形例
図4は、図2のエクストルーダを複数個直列に接続して、挽肉を複数のエクストルーダに通して塩溶化を促進する方法を説明する模式図を示す。なお、図4では、冷媒26の循環システムは省略されている。
4). 4 shows a schematic diagram for explaining a method for promoting salt solubilization by connecting a plurality of the extruders of FIG. 2 in series and passing the ground meat through the plurality of extruders. In FIG. 4, the circulation system of the refrigerant 26 is omitted.

エクストルーダ15を直列に3つ接続し、矢印Eで示すように、挽肉14を最初のエクストルーダ15の開口部21から供給し、その反対側の開口部22から加圧押出し、押し出された挽肉14を、二番目のエクストルーダ15の開口部21に供給し、その反対側の開口部22から加圧押出する要領で最後のエクストルーダ15の開口部22から挽肉14を押し出すと、挽肉14の塩溶化を容易に促進できる。エクストルーダ15,15は、配管40を介在して容易に接続できる。なお、エクストルーダ15は、2個あるいは4個以上を接続しても良い。さらに、エクストルーダ15に代えてあるいはこれに加えて、エクストルーダ15aを接続しても良い。このように、塩溶化工程を、エクストルーダ15,15aなどの加圧押出手段を直列に2以上接続したルートに挽肉14を通すことにより行っても良い。   Three extruders 15 are connected in series, and as shown by an arrow E, the ground meat 14 is supplied from the opening 21 of the first extruder 15 and is extruded by pressing from the opening 22 on the opposite side. When the ground meat 14 is pushed out from the opening 22 of the last extruder 15 in the manner of being supplied to the opening 21 of the second extruder 15 and pressurized and extruded from the opening 22 on the opposite side, the salt solution of the ground meat 14 is easily salted. Can be promoted. The extruders 15 and 15 can be easily connected via a pipe 40. Note that two or four extruders 15 may be connected. Furthermore, instead of or in addition to the extruder 15, an extruder 15a may be connected. In this way, the salt solubilization step may be performed by passing the ground meat 14 through a route in which two or more pressure extrusion means such as the extruders 15 and 15a are connected in series.

図5は、図1のフローの変形例を示す。   FIG. 5 shows a modification of the flow of FIG.

図5に示すフローは、図1に示す塩漬剤との混合(ステップS3)を、肉挽(ステップS2)の前に行う製造方法を示す。図5では、充填(ステップS5)以降のステップは図1のフローと共通するため省略されている。この例の場合、塩漬剤13を混合する対象は、挽肉ではなくブロック状の塊肉である。このため、塩漬剤13は、塊肉中にシリンジなどを用いて注入されるのが好ましい。この製造方法は、塩漬剤13を塊肉中に注入後、肉挽(ステップS2)を経て、加圧押出を含む塩溶化(ステップS4)以降の工程に進む。   The flow shown in FIG. 5 shows a manufacturing method in which mixing with the salting agent shown in FIG. 1 (step S3) is performed before meat grinding (step S2). In FIG. 5, the steps after filling (step S5) are omitted because they are the same as the flow of FIG. In this example, the object to which the salting agent 13 is mixed is not a minced meat but a block-like chunk. For this reason, it is preferable to inject the salting agent 13 into the lump using a syringe or the like. In this manufacturing method, the salting agent 13 is injected into the lump meat, followed by meat grinding (step S2), and then proceeds to the steps after salt solubilization including pressure extrusion (step S4).

このように、加圧押出を含む塩溶化(ステップS4)の前に、塩漬剤13を添加した挽肉14が存在する限り、塩漬剤13の添加時期がいつであっても良い。   Thus, as long as the ground meat 14 which added the salting agent 13 exists before salt solubilization including pressure extrusion (step S4), the addition time of the salting agent 13 may be anytime.

5.その他の実施の形態
以上、本発明に係る食肉加工品の製造方法の好適な実施の形態について説明したが、本発明は、上記実施の形態に限定されず、種々変形を施した形態にて実施可能である。
5). Other Embodiments While the preferred embodiment of the method for manufacturing a processed meat product according to the present invention has been described above, the present invention is not limited to the above-described embodiment, and is implemented in various modified forms. Is possible.

上述のエクストルーダ15,15a以外の加圧押出手段を用いて塩溶化工程を行っても良い。例えば、入口から投入された挽肉14を複数に区分けされた出口から押し出して、挽肉14の進行に対して抵抗を生じるようにする1または2以上の加圧器具を用いても良い。複数に区分けされた出口を挽肉14が通過する際、挽肉の粒子に対して物理的にしごく効果が生じ、それにより加圧押出手段と同様の肉に対する加圧の効果が生じる。また、エクストルーダ15,15a自体が温度保持機能(例えば、冷却機能)を持っていなくとも良い。例えば、冷蔵室内に、エクストルーダに代表される加圧押出手段を設置して、加圧押出手段が外気によって冷却された条件下で、塩溶化工程を行っても良い。また、加圧押出手段の入口若しくはそれより川上側に、温度保持機器(例えば、冷却機器)を設置して、挽肉14をその冷却機器を通すことによって、若しくはその冷却機器からの冷気を挽肉14に接触させることによって、挽肉14を冷却してから加圧押出手段に入るようにしても良い。そのような場合、加圧押出手段の温度は、5℃〜10℃、好ましくは6℃〜9℃、さらに好ましくは7℃〜8℃の範囲である。   You may perform a salt solution process using pressure extrusion means other than the above-mentioned extruders 15 and 15a. For example, one or more pressurizing devices that push the ground meat 14 introduced from the inlet through a plurality of divided outlets so as to create resistance against the progress of the ground meat 14 may be used. When the minced meat 14 passes through a plurality of outlets, a physically squeezing effect is produced on the particles of the minced meat, thereby producing a pressurizing effect on the meat similar to the pressure extrusion means. Further, the extruders 15 and 15a themselves do not have to have a temperature holding function (for example, a cooling function). For example, a pressure extrusion means typified by an extruder may be installed in the refrigerator compartment, and the salt solubilization step may be performed under conditions where the pressure extrusion means is cooled by the outside air. Further, a temperature holding device (for example, a cooling device) is installed at the inlet of the pressure extruding means or upstream of the river, and the ground meat 14 is passed through the cooling device, or the cold air from the cooling device is ground into the ground meat 14. The ground meat 14 may be cooled before entering the pressure extrusion means. In such a case, the temperature of the pressure extrusion means is in the range of 5 ° C to 10 ° C, preferably 6 ° C to 9 ° C, more preferably 7 ° C to 8 ° C.

塩漬剤13は、塩を少なくとも含む限り、発色剤、結着補強剤、香辛料、調味料、保存料、甘味料あるいは酸化防止剤などの他の添加剤を含まなくとも良い。その場合、当該他の添加剤の少なくとも一種は、充填工程の前の工程において、塩漬剤13とは別に添加されるのが好ましい。   The salting agent 13 may not contain other additives such as a color former, a binder reinforcing agent, a spice, a seasoning, a preservative, a sweetener, or an antioxidant as long as it contains at least salt. In that case, it is preferable that at least one of the other additives is added separately from the salting agent 13 in the step before the filling step.

本発明は、食肉加工品の製造に利用できる。   The present invention can be used for manufacturing processed meat products.

13 塩漬剤
14 塩漬剤を含む挽肉
15,15a (温度保持機能付き)エクストルーダ(加圧押出手段の一例)
13 Salting agent 14 Minced meat 15,15a containing salting agent (with temperature maintaining function) Extruder (an example of pressure extrusion means)

Claims (4)

食肉をミンチ状に挽くミンチ工程の後に、
5℃〜10℃の温度下にて、塩漬剤を含む挽肉を、その移送方向の川上側よりも川下側の圧縮力を高くする加圧押出手段に通して、前記挽肉中の筋原線維を構成する蛋白質の一部を塩溶化させることを含む塩溶化工程を行う食肉加工品の製造方法。
After the minced process of grinding meat into minced shapes,
At a temperature of 5 ° C. to 10 ° C., the ground meat containing the salting agent is passed through a pressure extrusion means for increasing the compressive force on the downstream side of the upstream side in the transport direction, and the myofibrils in the ground meat A method for producing a processed meat product, which comprises performing a salt solubilization step comprising salt-solubilizing a part of the protein constituting the salt.
前記塩溶化工程は、前記加圧押出手段を直列に2以上接続したルートに前記塩漬剤を含む挽肉を通すことを含んで行われる請求項1に記載の食肉加工品の製造方法。   The method for producing a processed meat product according to claim 1, wherein the salt solubilization step is performed by passing ground meat containing the salting agent through a route in which two or more pressure extrusion means are connected in series. 前記塩溶化工程は、前記塩漬剤を含む挽肉を、前記温度下に保持しながら、1または2以上のエクストルーダを通過させる工程を含む請求項1または請求項2に記載の食肉加工品の製造方法。   The said salt solubilization process manufactures the processed meat product of Claim 1 or Claim 2 including the process which passes 1 or 2 or more extruders, hold | maintaining the ground meat containing the said salting agent under the said temperature. Method. 前記エクストルーダは、前記温度下に保持する温度保持機能を有するエクストルーダである請求項3に記載の食肉加工品の製造方法。   The method for producing a processed meat product according to claim 3, wherein the extruder is an extruder having a temperature holding function of holding at the temperature.
JP2015148927A 2015-07-28 2015-07-28 Process for producing processed meat products Active JP6584850B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2015148927A JP6584850B2 (en) 2015-07-28 2015-07-28 Process for producing processed meat products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2015148927A JP6584850B2 (en) 2015-07-28 2015-07-28 Process for producing processed meat products

Publications (2)

Publication Number Publication Date
JP2017029002A true JP2017029002A (en) 2017-02-09
JP6584850B2 JP6584850B2 (en) 2019-10-02

Family

ID=57985153

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2015148927A Active JP6584850B2 (en) 2015-07-28 2015-07-28 Process for producing processed meat products

Country Status (1)

Country Link
JP (1) JP6584850B2 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07107941A (en) * 1993-10-15 1995-04-25 Kanegafuchi Chem Ind Co Ltd Method of manufacturing meat products
JPH07194342A (en) * 1993-12-29 1995-08-01 Kureha Chem Ind Co Ltd Production of dry sausage
JP2002514050A (en) * 1996-07-18 2002-05-14 ウェンガー マニュファクチュアリング アイ エヌ シー. Short length tapered extrusion cooker
US20040170745A1 (en) * 2003-02-27 2004-09-02 Newkirk Kyle A. Extruded dry and semi-dry sausage product processing and to products thereform

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07107941A (en) * 1993-10-15 1995-04-25 Kanegafuchi Chem Ind Co Ltd Method of manufacturing meat products
JPH07194342A (en) * 1993-12-29 1995-08-01 Kureha Chem Ind Co Ltd Production of dry sausage
JP2002514050A (en) * 1996-07-18 2002-05-14 ウェンガー マニュファクチュアリング アイ エヌ シー. Short length tapered extrusion cooker
US20040170745A1 (en) * 2003-02-27 2004-09-02 Newkirk Kyle A. Extruded dry and semi-dry sausage product processing and to products thereform

Also Published As

Publication number Publication date
JP6584850B2 (en) 2019-10-02

Similar Documents

Publication Publication Date Title
JP6637973B2 (en) Non-meat food products having the appearance and texture of cooked meat
US8628815B2 (en) Low shear meat analog
AU2012201435B2 (en) Meat-based semi-moist animal food product and method for production thereof
Aykın Dinçer Dried meat products obtained by different methods from past to present
CN105792662B (en) Functional protein derived from animal muscle tissue or mechanically deboned meat and method for producing the same
CN105960172B (en) Pet meat food product without wheat gluten
US20080118607A1 (en) Use of Structured Plant Protein Products to Produce Emulsified Meat Products
Yasin et al. Optimization and rheological properties of chicken ball as affected by κ-carrageenan, fish gelatin and chicken meat
CN101489422A (en) A protein composition and its use in restructured meat and food products
AU2017203064B2 (en) Methods and devices for heating or cooling viscous materials
Gurikar et al. Effect of meat chunk size, massaging time and cooking time on quality of restructured pork blocks
JP2013509195A (en) Gluten-free structured protein products
KR20120105404A (en) Method for the preparation of oil-containing meat-based products comprising a reduced amount of additives
CN105517442A (en) Method and device for treating food by means of a heating process
Cortez-Vega et al. Optimization of parameters for obtaining surimi-like material from mechanically separated chicken meat using response surface methodology
JP6584850B2 (en) Process for producing processed meat products
CN104855526B (en) A kind of imitative beef product based on dregs of beans
Reddy et al. Quality characteristics of restructured mutton slices developed by cold-set binding system
JPH099921A (en) Antioxidative sausage and its production
KR20170007633A (en) Pork head sausage and method for preparing the same
Malav et al. Quality characteristics and storage stability of restructured chicken meat blocks extended with different combinations of vegetative extenders
JP2014023493A (en) Production method of pulverized raw meat-containing processed meat product
Elavarasan Fish sausage-a ready to eat product
KR20150098530A (en) Lamb sausages and threrof manufacturing method
CN102793200A (en) Meat product containing lycopene and production method thereof

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20180417

RD03 Notification of appointment of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7423

Effective date: 20180831

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20190227

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20190312

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20190412

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20190903

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20190904

R150 Certificate of patent or registration of utility model

Ref document number: 6584850

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250