Patent Application
20240090535
The present invention relates to a method of producing a two-layered feed or food product having an outer layer and an inner layer. Specifically, the present invention relates to a method suitable for mass-producing a feed or food product in which an inner layer is encrusted with an outer layer, the method involving the use of an extruder provided with a double nozzle.
Encrusting machines are widely used to manufacture filled food products such as Japanese manju bean paste cakes. Encrusting machines are used to shape and fill outer layers of glutinous rice, wheat, or the like with fillings such as sweet bean paste. Various types of encrusting machines exist in order to allow for the production of breads, confections, and the like that have complicated shapes or require delicate handling; in particular, various modifications have been made to the function of encrusting bean paste with outer layers and to sealing-cutting machines (Patent Documents 1 to 4).
Patent Document 5 discloses a method of combining an extruder and a cutter in order to efficiently produce a multi-layered filled food product from a multi-layered cylindrically shaped food product composed of two or more types of food product material arrayed in concentric circular layers as seen in cross section.
Patent Document 6 discloses a two-layered feed in which an inner layer is entrusted with an outer layer, and teaches that an extruder with a double nozzle can be used to produce the feed.
Patent Document 1: Japanese Patent No. 3377964
Patent Document 2: Japanese Patent No. 3415072
Patent Document 3: Japanese Patent No. 3758901
Patent Document 4: Japanese Patent No. 2537751
Patent Document 5: Japanese Patent No. 2641033
Patent Document 6: WO/2010/011032
Problems that the Invention is to Solve
Various types of encrusting machines exist in order to produce food products having a two-layered structure comprising an outer layer and an inner layer; however, conventional methods involving using an encrusting machine to encrust a filling and performing heating are unrealistic for producing a two-layered fish feed such as that disclosed in Patent Document 5 due to the large production volume involved and the fact that, although the product, being a feed, does not need as delicate a finish as a food product, it must be produced cheaply and in mass quantities.
Methods involving shaping an outer layer and an inner layer using an encrusting machine, followed by heating the shaped products, are not suited to the mass production of filled feeds or food products due to involving a two-step process and requiring a laborious step of transporting the unheated shaped product to the heating step in a manner so as not to ruin the shape thereof. An object of the present invention is to provide a method suitable for the mass production of a filled feed or food product.
The inventors attempted to efficiently produce a two-layered feed using encrusting machines widely used in fields such as bread or confections, but none of these was suited for inexpensive, efficient mass production. One major problem was the need to separately heat the outer layer after being shaped by the encrusting machine, leading to inefficiencies in the transportation and storage of the shaped product. The inventors therefore investigated performing shaping and heating in a single step, rather than as two separate processes. The inventors discovered that a feed featuring an inner layer completely encrusted with an outer layer could be produced by shaping into a two-layered structure using an extruder provided with a double nozzle, followed by filling and cutting using a shutter mechanism while the temperature is still high, thereby arriving at the present invention.
The present invention is a method of producing a feed or food product according to the following (1) to (8).
(1) A method of producing a feed or food product in which an inner layer is encrusted with a gelled outer layer composition, the method comprising the steps of: preparing an outer layer composition feedstock by adding a secondary feedstock to a protein feedstock and/or a starch feedstock that forms a gel upon heating and then mixing by stirring, and preparing an inner layer composition that is encrusted with the outer layer composition; extrusion molding with an extruder provided with a double nozzle so as to cover a surface of the inner layer composition while simultaneously gelling the outer layer composition feedstock by heat treatment; and cutting a continuously extruded cylindrically shaped product to a fixed length with a shutter mechanism while simultaneously encrusting a cut surface with the gelled outer layer composition.
(2) The method of producing a feed or food product according to (1), wherein the shutter mechanism is a shutter device provided with a plurality of open-and-closable shutter pieces.
(3) The method of producing a feed or food product according to (3), wherein there is a combination of at least six shutter pieces.
(4) The method of producing a feed or food product according to any one of (1) to (3), wherein the shutter is manufactured from a heat-resistant material.
(5) The method of producing a feed or food product according to any one of (1) to (4), wherein the shutter mechanism is crankshaft-driven.
(6) The method of producing a feed or food product according to any one of (1) to (5), wherein the protein feedstock that forms a gel upon heating is one selected from among surimi, ground fish meat, krill, gelatin, collagen, gluten, egg albumen, and soy protein, or a combination of two or more thereof.
(7) The method of producing a feed or food product according to any one of (1) to (5), wherein the starch feedstock that forms a gel upon heating is one selected from among tapioca starch, wheat starch, potato starch, corn starch, bean starch, waxy corn starch, and processed starches thereof, or a combination of two or more thereof.
(8) The method of producing a feed or food product according to any one of (1) to (7), wherein the heating temperature of the extruder is from 60 to 110° C.
In accordance with the production method according to the present invention, it is possible to mass-produce, at high speed, a double-layered feed or food product in which an inner layer is encrusted with an outer layer.
The present invention is a method of producing a filled feed or food product in which an inner filling is covered with an outer skin. The method involves using an extruder provided with a double nozzle to simultaneously heat an outer layer via extrusion cooking and coat an inner layer with the outer layer, and cutting an extruded cylindrically shaped product to a fixed length using a rising and descending shutter mechanism in synch with the speed at which the shaped product is extruded while simultaneously encrusting the cut surface with the outer layer. There is no need for a separate process of heating the outer layer after shaping, as in the case of production using an encrusting machine, allowing a finished product to be produce from raw outer layer feedstock in a single step.
The extruder used in the present invention may be a single-screw or a twin-screw extruder as long as it possesses an extrusion function and a heating function. The outer layer composition feedstock is fed into the extruder and kneaded, and the outer layer composition feedstock is heated to gelling temperature and extruded. A nozzle for supplying the inner layer composition into the outer layer composition is disposed near an outlet of the extruder, and the inner layer composition is extruded into the center of the outer layer, which is extruded in a cylindrical shape, to create a two-layered structure.
The heating temperature of the extruder will vary according to the outer layer feedstock; the feedstock is gelled by being heated to from 60 to 110° C., preferably from 60 to 100° C., especially preferably from 70 to 90° C. If swelling is permissible, the product can also be produced at a temperature greater than or equal to 110° C. If it is not desirable for the extruded outer layer to swell, the outer layer composition feedstock is preferably degassed in advance.
The two-layered shaped product continuously extruded from the extruder is dispensed vertically downward into the shutter mechanism.
Various types of shutter mechanisms used in encrusting machines can be used for the shutter mechanism. In order to reliably encrust the cut surface with the outer layer, a sliding shutter having a structure in which a uniform opening shape is maintained by a plurality of shutter pieces while growing gradually smaller and closing in the middle is preferable. As the shutter draws in the heated gel of the outer layer of the shaped product that is being extruded from the extruder, the shutter begins to pinch shut, the opening narrows, and the outer layer of the shaped product is finally cut off in the center. Closing the shutter before the heated gel coming out of the extruder cools allows for reliable closing.
Regarding the specific shape of the shutter, examples of shutters include those disclosed in Japanese patents 3016246, 3377964, and 3415072 and Japanese Utility Model H05-025432 granted to Rheon Automatic Machinery Co., Ltd., and Japanese Patent 2641033 granted to Kobird Co., Ltd. In particular, a combination of at least six shutter pieces that maintain an opening shape in a regular polygonal shape when opening and closing is preferable, as this will allow the outer layer to be uniformly drawn together.
The cross-sectional thickness of the shutter pieces is preferably at least half the radius of the final product in order to reliably cover the cut surface with the outer layer. For example, if the final product has a diameter of 26 mm, a shutter piece cross-sectional thickness of about 15 mm is appropriate, or a thickness of about 10 mm is appropriate if the final product has a diameter of 18 mm.
However, shutters used in conventional encrusting machines cannot be applied to the extruder without modification. In order to match the speed of the extruder, the open/close speed and vertical motion speed of the shutter must be increased. In addition, because of the high speed of the operation and the fact that the heated gel being expelled from the extruder is at a temperature of 60 to 100° C., the shutter is exposed to heat, and expands. Moreover, if a hard material such as fish meal is included in the raw material for the feed, the surfaces of the shutter pieces will be abraded and exhibit severe wear. In order to solve this problem, the shutter must be made of a heat-resistant, slidable, strong material. Conventional Newlight resins have low heat resistance (60° C.) and are soft. In the present invention, it is preferable to use a PEEK resin or a material having comparable or better properties. The shutter may also be cooled as necessary. Specifically, a method such as blowing compressed air or cooled air can be used.
Cam-driven mechanisms exhibit durability problems at high-speed operation, preventing speed from being increased over a certain level. The present invention is crankshaft-driven rather than cam-driven. The rotational motion of the crankshaft drives the invention, allowing the cutting speed and vertical speed of the shutter device to be increased. Speed can also be adjusted by altering the vertical stroke speed. This drive format allows for a shutter sealing/cutting speed of 120 to 140 strokes/minute or faster.
The finished product, after being encrusted and cut by the shutter mechanism, is a cylindrically shaped product of a constant length in which the inner layer is completely covered by the outer layer, and can be used as a feed or food product without further modification.
In the present invention, it is vital that a feedstock containing a protein feedstock and/or a starch feedstock that forms a gel upon heating be used for the outer layer constituting the outer skin. Using a raw material that gels upon heating and has a certain level of resiliency, extensibility, and adhesiveness will allow for reliable encrusting of the inner layer.
In the present invention, a heat-induced gel means a gel able to be formed by heating a protein to 60° C. or higher or by heating a protein to 60° C. or higher and then cooling, or a gel able to be formed by adding water to a starch and then heating to 60° C. or higher so as to cause gelatinization.
The composition of the outer layer may be any which has the above-mentioned physical properties and which covers the inner layer composition, but it was found that the physical properties of a gel able to be formed by heating a protein or a gel able to be formed by heating a starch is suitable for use in the present invention from the perspectives of softness, extensibility, and the like. For example, a protein having gel-forming properties is preferred, such as fish meat, surimi, krill, gluten, collagen, soy bean protein, enzymatically degraded soy bean protein, gelatin, egg albumen, or a combination of two or more types thereof. Preferred starches include tapioca starch, wheat starch, potato starch, corn starch, bean starch, waxy corn starch, or a processed product of these starches. It is possible to use food ingredients that contain large quantities of these proteins and/or starches. By heating an outer layer composition that contains these proteins and/or starches, the gel is immobilized and the inner layer composition has softness, holding power, and a certain degree of strength.
For example, if surimi is used as the outer layer composition, this can be produced using a method for producing a fish paste product such as kamaboko (semi-cylindrical processed fish paste). Specifically, 2% or more of common salt is added to the surimi, which is left to stand for 10 minutes or longer at a temperature of 10° C. or higher, and preferably 30° C. to 40° C., and then heated for 10 minutes or longer at a temperature of 80° C. to 90° C. Alternatively, if egg albumen is used, egg albumen, starch, fish meal, and water are blended at a weight ratio of, for example, 1:1:2:6 and then heated, thereby producing a composition having the desired physical properties.
It is allowable to add a variety of secondary feedstock to the outer layer at levels that have no adverse effect on the gelling of the outer layer.
In case of feed, it is allowable to add fish meal and oil to the outer layer at levels that have no adverse effect on the gelling of the outer layer. Depending on the type of gel used, it is possible to add up to 60 wt. % of fish meal and up to 30 wt. % of oil to the outer layer. It is preferable to add approximately 20 to 30 wt. % of fish meal and 5 to 10 wt. % of fat.
In order to further improve the quality of the gel in the outer layer, it is possible to add additives that are used as improving agents in fish paste products and the like. It is possible to add a starch, a polysaccharide thickener, a soy protein isolate, baking soda, a polyphosphate, egg albumen, transglutaminase, a protease inhibitor, and the like. In particular, in order to enhance the strength of the gel, a thickening agent such as agar, gellan gum, pullulan, a starch, mannan, carrageenan, xanthan gum, locust bean gum, curdlan, pectin, alginic acid or a salt thereof, gum arabic, chitosan, dextrin, or an edible water-soluble cellulose can be blended in the gel as appropriate.
As another preferred aspect of the outer layer of the present invention, it was found that a heat-induced gel having a starch as a primary component has excellent resiliency and softness. A gel obtained by adding water to a starch, kneading, and then heating exhibits elasticity, softness, and extensibility. In particular, a variety of processed starches have individual characteristics, and by using two or more types thereof, it is possible to obtain an outer layer having properties such as resiliency, softness, and extensibility. For example, it is possible to combine different types of processed starches, such as a combination of an etherified starch and a phosphoric acid-crosslinked starch. It is possible to obtain an even stronger gel by adding a protein such as gluten or soy bean protein to a starch. It is also possible to use, for example, gluten-containing wheat flour instead of gluten. Other secondary raw materials able to be added include cereal flours such as wheat flour, proteins such as soy bean protein, gluten, or egg albumen, sugars and sugar alcohols such as table sugar or starch syrup, thickening agents such as carrageenan, agar, gellan gum, pullulan, mannan, xanthan gum, locust bean gum, curdlan, pectin, alginic acid or a salt thereof, gum arabic, chitosan, dextrin, or an edible water-soluble cellulose, and salts such as phosphates. For example, by adding wheat flour to a starch, it is possible to impart strength to the outer layer. In addition, by adding a certain quantity of a protein, it is possible to suppress surface stickiness following heating.
The starch used in the present invention is not particularly limited, but can be tapioca starch, wheat starch, potato starch, corn starch, bean starch, and the like, and processed starches obtained by subjecting these starches to etherification, acetylation, acetyl crosslinking, ether crosslinking, phosphoric acid-crosslinking or gelatinized hydroxypropylphosphoric acid-crosslinking are particularly preferred. The feed of the present invention is produced by adding other secondary raw materials such as proteins to these starches, adding water thereto and kneading, covering the inner layer by means of an encrusting machine and the like, and then heating. Alternatively, the feed of the present invention can be produced by feeding the outer layer raw materials and the inner layer raw materials into an extruder having a double nozzle, and blending and heat treating the outer layer raw materials while simultaneously extruding so as to cover the inner layer with the outer layer. The quantity of water added to the raw material such as a starch should be a quantity able to be handled by the encrusting machine or extruder, but approximately 30 to 50 wt. % is appropriate. The heating temperature should be not lower than the temperature at which the starch or added protein gels, and the product temperature should be 60 to 110° C., preferably 70 to 100° C., and more preferably approximately 80 to 90° C. Fish oils are easily oxidized, and high temperatures should therefore be avoided.
Moisture in the outer layer of the present invention, which covers an inner layer of a heat-induced gel of a starch, is approximately 25 to 50 wt. %. When storing for a long period of time in this state, it is possible to store the feed in a refrigerated or frozen state. In addition, by further drying this feed to reduce the moisture to 10 to 20 wt. %, it is possible to obtain a feed having good shelf life. By drying the outer layer and also adding additives thereto so as to reduce water activity, it is possible to produce a feed able to be stored for a long period of time at room temperature. The water content is preferably 10 to 20 wt. % and the water activity is preferably 0.8 or lower, and more preferably 0.6 or lower.
Various patterns have been considered for formulating the composition of a starch-containing outer layer. In case of feed, the nutrients and calories required in a feed differ according to the species and growth stage of fish. As the quantity of fish meal or fish oil increases, the outer layer needs to be precisely formulated, but in cases where the quantity of fish meal or fish oil is low, the outer layer can be formulated more freely. In terms of dry product, at least 20 to 80 wt. % of starch is incorporated. In the case of an outer layer in which 25 to 50 wt. % (in terms of dry product) of fish meal is added, it is preferable to add, in terms of dry product, 20 to 65 wt. % of starch, 5 to 20 wt. % of wheat flour, and a total of 5 to 15 wt. % of proteins, oils, thickening agents, salts, and the like. It is preferable to add approximately 1 to 5 wt. % of fish oil, 1 to 2 wt. % of phosphate salts, 1 to 5 wt. % of protein, and 1 to 5 wt. % of thickening agent.
When used as a secondary raw material, wheat flour is preferably strong flour having a high gluten content, but may also be weak flour.
In order to further improve the quality of the outer layer, it is possible to add additives that are used as improving agents in starch-based foods.
In case of feed, the composition of the inner layer contains mainly fish meal and oils, but it is also possible to add other nutrient ingredients known as nutrient ingredients for fish farming, such as vitamins and minerals. In addition, although the inner layer is covered by the outer layer, because it is not desirable for fish meal and liquid oils to leak from the inner layer, it is possible to stabilize the inner layer by blending a polysaccharide or hydrogenated oil or by emulsification. In particular, when producing in a machine, it is preferable for the physical properties of the inner composition to encompass fluidity and physical properties that are appropriate for the machining. Examples of polysaccharides (fat-absorbing agents) include Oil Q (produced by Nippon Starch Chemical Co., Ltd.), and examples of hydrogenated oils include Unishort K (produced by Fuji Oil Co., Ltd.) and New Fujipro SEH (produced by Fuji Oil Co., Ltd.).
Furthermore, raw materials for conventional artificial feeds for farmed fish can be added to the composition of the inner layer. For example, proteins such as live fish, squid meal, krill meal, soy bean lees, and corn gluten meal, oils and fats such as krill oil, whale oil, soy bean oil, corn oil, rape seed oil, and hydrogenated oils, starch-based materials such as starches, wheat flour, rice flour, tapioca powder, and corn powder, alginic acid and salts thereof, polysaccharides such as sodium carboxymethyl cellulose (CMC), guar gum, dextrins, chitosan, curdlan, pectin, carrageenan, mannan, gellan gum, gum arabic, and edible water-soluble celluloses, vitamins, minerals, and the like.
The composition of the inner layer contains 20 to 70 mass % of oils and, in cases where the feed is fed to large farmed fish, the oil content is preferably 30 mass % or higher, more preferably 35 mass % or higher, and most preferably 45 mass % or higher. A high fat content achieves excellent effects in terms of growth and growth efficiency of farmed fish, but if the oil content exceeds 70 mass %, the content of other blending components must fall, meaning that it is difficult to obtain balanced nutrition. Fish oils and other plant-based oils are highly fluid and may be used without further modification, but it is preferable to reduce the fluidity by using oil-absorbing polysaccharides such as Vitacel WF200, Vitacel WF600, or Vitacel WF600/30 (all produced by J. Rettenmaier & Söhne GmbH+Co. KG), Oil Q No. 50 or Oil Q-S (produced by Nippon Starch Chemical Co., Ltd.), or a dextrin such as Pine Flow (produced by Matsutani Chemical Industry Co., Ltd.), oil-absorbing proteins such as fermented soy beans and isoflavones, or hydrogenated oils obtained by hydrogenating oils and fats such as soy bean oil, rape seed oil, or palm oil. Alternatively, it is possible to reduce the fluidity by emulsifying fish oils. However, in view of the digestive properties of fish, the content of these components that reduce fluidity is preferably 10 mass % or lower, and more preferably 5 mass % or lower, of the composition of the inner layer. Fish oils are most preferred as the oil, but it is also possible to replace part of the fish oils with other plant-based oils.
The fish meal, which is an essential component of the inner layer, can be a variety of fish meals or a powder of crustaceans such as krill, which are commonly used as raw materials for feeds for fish farming. The fish meal content is 30 to 70 mass %, preferably 30 mass % or higher, more preferably 35 mass % or higher, and most preferably 45 mass % or higher. It is preferable to add an excipient having binding properties, such as a polysaccharide, a hydrogenated oil, or an emulsifier, to the inner layer composition in order to prevent the inner layer composition from disintegrating.
In view of the shelf life of the feed of the present invention, the water activity thereof may be adjusted. It is possible to adjust the water activity by adjusting the composition of the inner layer or outer layer. For example, it is possible to reduce the water activity of the composition of the inner layer by adjusting the quantity of water added thereto. In addition, it is possible to adjust the water activity of the composition by adding a water activity-adjusting agent, such as a salt (common salt, sodium malate, sodium lactate, and the like), a sugar (table sugar, lactose, maltose, sorbitol, and the like), a sugar alcohol, an amino acid, a nucleic acid related compound, an organic acid, an alcohol, propylene glycol, glycerin, a starch, or a protein.
The foregoing detailed description has focused primarily on feeds, but the components of the outer layer can be planned according to similar criteria in the case of a food product as well. As there is no need to consider nutritional efficiency in the case of a food product, as opposed to a feed, there is a high degree of freedom in designing the product according to taste or texture. An outer layer composition containing protein or starch can be used to encrust various food ingredients such as bean paste, chocolate, and cream, as well as vegetables, fruits, meat, fish, poultry, eggs, and cereals. Any material may be used for the composition of the inner layer as long as it has physical properties allowing it to be dispensed from the nozzle of the extruder. The inner layer may be processed or unprocessed, and may be a single ingredient or a prepared food product.
The present invention will now be described in greater detail through the use of working examples, but is in no way limited to these working examples.
A production apparatus configured as shown in
In order to allow for high-speed production, a completely intermeshing co-rotational twin-screw extruder (manufactured by Buhler) having an output capacity of 1 t/h was used.
A shutter mechanism having the configuration shown in
The shutter is a sliding shutter 13, and a motor 14 of a controlled rotational speed rotates a crankshaft 15, a coupling rod 16 converts the rotational movement of the crankshaft 15 to forward-and-backward movement, moving a drive lever 17 coupled to the coupling rod 16 forwards and backwards, and gears within a housing 18 convert the forward-and-backward movement of the drive lever 17 to rotational movement, opening/closing the shutter.
A shutter mechanism having a configuration similar to that of a sealing-cutting shutter from Rheon Automatic Machinery Co., Ltd. (Japanese Patent No. 3377964) was used. As shown in
Using the production apparatus from working example 1, a fish feed of units having a diameter of 3 cm and a length of 15 cm was produced.
An outer layer composition raw material was prepared by blending 18 wt % tapioca starch (etherified starch), 4 wt % waxy starch (pregelatinized hydroxypropylphosphoric acid-crosslinked starch), 1 wt % bean starch (acetylated starch), 3 wt % isolated soy bean protein powder (New Fujipro SEH, produced by Fuji Oil Co., Ltd.), 3 wt % krill meal, 3 wt % wheat flour, 1 wt % gluten, 0.5 wt % carrageenan, 0.5 wt % disodium hydrogen phosphate, 3 wt % egg albumen, 20 wt % fish meal, 3 wt % starch syrup, 2 wt % fish oil, and 40 wt % water in a silent cutter.
An inner layer composition was prepared by blending 60 wt % fish meal, 36 wt % fish oil, 1.2 wt % hydrogenated oil, 3 wt % krill meal, 2.5 wt % vitamins, 1 wt % minerals, 1.2 wt % calcium phosphate, and 0.1 wt % of an organic acid in a mixer.
These were dispensed from the outer layer composition feedstock feeder device 1 and the inner layer composition feeder device 2 of the production apparatus of working example 1, and mixed and heated by an extruder at a screw speed of 450 rpm, an output temperature of 90° C., and an outlet pressure of 45 bar. The apparatus of working example 1 is capable of production at a rate of 145 units/minute, with the cut surface being encrusted with the outer layer and there being no leakage of the inner layer contents.
The present invention can provide a method of mass-producing a feed, food product, or the like having a two-layered structure comprising an outer layer and an inner layer at high speed.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2011-235325 | Oct 2011 | JP | national |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 14354034 | Apr 2014 | US |
| Child | 18522613 | US |
