JPH02253860A - Freeze crushing, mixing, pulverizing and continuously processing device - Google Patents

Abstract

PURPOSE:To effectively reveal the functionality of protein in the upper limit by utilizing a crushing cylinder in which a crushing rotary drum fitted with a quantitatively crushing blade, a feed blade and a delivery blade is incorporated. CONSTITUTION:A crushing cylinder 5 is provided with both one set or plural sets of feeders 2 for a frozen raw material block and a delivery port 3 of pulverized material. Further a crushing rotary drum 16 is incorporated which is fitted with a plurality of quantitatively crushing blades 13 described hereunder, a spiral feed blades 14 and a delivery blade 15. The crushing blades 13 have a feed structure of crushed material having a cutting-off and left/right lateral cutting knife-edge and furthermore have two kinds of right and left mirror-image pairs formed of this feed structure as a fundamental constitution. As a result, temp. rise is inhibited and the raw material is uniformly pulverized about to micron and simultaneously an additive is uniformly dispersed and mixed. The functionality of protein is effectively revealed at the upper limit.

Description

[Detailed Description of the Invention] [Industrial Application Field] The present invention is primarily concerned with continuous processing methods for livestock meat, fish meat, and soybeans, and aims to effectively and maximally express the functionality of proteins, which are the main components. The present invention relates to a mechanical device that can perform freeze-fracture, mixing, pulverization, and continuous processing.

[Summary of the invention]

Many foods that utilize the functionality of proteins, such as protein foods, are solid products with high moisture content.

The main functionality used in this protein food is to polymerize the protein in order to contain more water. but,
These raw materials, like other food products, are multi-component heterogeneous mixtures, so proteins cannot be handled independently, and the expression of protein functionality is a difficult problem for each raw material. There is.

In order to enhance the functionality of protein, it is possible to increase the protein concentration and eliminate other components, but this reduces the important overall nutritional value of food.

The present invention is an apparatus that efficiently establishes, by physical means, the direct action of substances that contribute to the reaction while suppressing the factors that inhibit the polymerization of proteins.

The technical point of this device is that by crushing frozen raw material blocks under conditions that do not thaw, the ice dispersed inside acts as a large number of blades during crushing. The second point is the blade system that cuts by applying motion, which is to continuously merge the crushed material and coagulant at a constant ratio, and to pass the merged material through a mechanism in which multiple stages of the blade systems are arranged at regular intervals. is the third point.

[Conventional technology]

In protein foods, raw materials are crushed to form a jelly to incorporate moisture, and heat-gelled products with a fixed protein network structure are common. Specific examples of foods that take advantage of the functionality of this protein include sausages for livestock meat, fish paste products for fish, and tofu for soybeans. In any case, the content is to destroy the cells of the raw material to expose the side chains of the protein, and to express the functionality of the protein by adding a small amount of common salt or calcium sulfate, which is commonly used as a coagulant. It increases water retention.

Expression of protein functionality is a type of chemical reaction.

When a small amount of additive is dissolved in the free water contained in the raw materials, it becomes an alkaline metal ion, which simultaneously acts on the side chains of proteins, resulting in a polymerization reaction in which the proteins become polymerized.

Generally, the value of food is evaluated based on nutritional value, palatability, and economic factors, but consumers are interested in whether or not the food is delicious. Taste, or palatability, can be obtained by understanding taste, aroma, texture, appearance, temperature, etc., and by comprehensively adjusting the cooking to suit the consumer's preferences.

For foods where protein is one of the main ingredients, it is important to adjust the texture in terms of hardness, stickiness, smoothness, brittleness, etc. In addition to retaining water, the form of the network structure produced by heating and gelation must also have the function of obtaining a texture that corresponds to the characteristics of each food. Cooking in response is what makes delicious food.

Foods that are sold in large quantities to general consumers must be commercialized with emphasis on product safety, using the company's technology for producing food that sells, and with economic efficiency in mind. At the same time, processing methods will be realized and production equipment will be converted into equipment. Processed meat and fish foods are difficult to handle due to the complicated shapes of the raw materials, so it is a combination of machines that perform relatively simple unit operations such as cutting and mixing, and requires manual labor. There are many manufacturing steps that require intervention. This has led to concerns about product safety and quality.
(The labor burden for manufacturing is heavy, and there are still many factors to reduce costs, such as improving the yield of raw materials and making energy use less efficient.)

In order to effectively express the functionality of proteins, it is necessary to uniformly destroy the cells that serve as the substrate to form fine particles, and to uniformly mix the additives that serve as catalysts. It is important to hold back 1]. This is because the degree of thermal denaturation in jelly formation is affected by the formation of a protein network structure during heat gelation, and directly affects the texture, which leads to the quality of taste.

A machine with functions such as a silent cutter is used for the finishing process and crushing before heating and gelling. This machine is assembled with a fixed dose container cutter,
The cutter function cuts and mixes raw materials. but,
In cutting, all the raw materials in the container are circulated, so the cutter does not contribute to the originally required cutting function.The cutter uses only the cutting edge to cut, The other functions are to support the cutting edge and to circulate the raw material. However, the burden of this raw material circulation is heavy, and in order to support the thrust, a thick plate-like and durable mechanism is used. This prevents contact with the raw material. The area is large and causes frictional heat to be generated.

In addition, since the mixing of additives begins after they have adhered to a portion of the raw materials, uniform dispersion is determined by the number of circulations5.
Its extent is limited by fever.

Expressing protein functionality with a silent cutter has significant mechanical limitations, such as the cutter's heat generation which limits the degree of micronization and the difficulty of uniformly dispersing additives that act as catalysts. . In other words, increasing the surface area of raw materials and uniformly dispersing additives, which are requirements for reaction promotion, cannot be achieved effectively, and the functionality of the proteins in the raw materials themselves is affected.
Not expressed in sufficient condition.

In livestock and fish meat, the salt concentration required for the reaction of myosin, a protein that becomes polymerized, is at least about 0.6.
%. However, the salt concentration in the production of sausages is about 5% based on meat standards, and about 3% based on final product standards, and the starch and gelatin used as sizing agents are about 18% in total. It is being said. In this way, mechanical devices such as the silent cutter can process low-salt products that meet the demands of health-conscious consumers.
This grinding method itself has functional limits.

[Problem to be solved by the invention]

When grinding protein foods using conventional technology, the cutting size of the raw materials can only be on the order of about 1 mm.
Moreover, the variation is large. In livestock meat, fish meat, and soybeans, which are protein foods, protein is contained in the cells of the raw materials, and the size thereof is on the order of micrometers. It is after the raw material is cleaved and the reactive groups that serve as its substrate are exposed that it becomes jelly-formed, emulsified, and heat-gelled by the action of the additive.

In other words, in order to effectively and maximally express the functionality of proteins, it is necessary to control the temperature rise of the raw materials to prevent protein denaturation and to uniformly atomize them into particles on the order of micrometers. , and additives are simultaneously uniformly dispersed and mixed.

The problems of each raw material that could not be solved by conventional techniques are as follows. Regarding livestock meat, reduce salt content;
The goal is to fix the color of meat without using nitrites, which have harmful effects, and to soften meat, which contains a lot of hard proteins such as collagen and elastin. Regarding fish meat, reducing the salt content, making fish meat into sushi meat by making all the bones into fine particles, and using all the components of red meat such as sardines to obtain a kamaboko-like texture and not discoloring the meat. It is to fix it like this. For soybeans, it is necessary to turn the undenatured protein into fine particles.

It is an object of the present invention to provide a continuous processing device for freezing, crushing, mixing and pulverizing, which solves the problems of each raw material that have not been achieved with the conventional techniques.

[Means to solve the problem]

In order to achieve the above object, the present invention comprises a frame cylinder (5) having an input port (21 (2+') for the frozen raw material block (1) and a crushed material delivery port (3), and 21 (21') is tilted outward, and the hopper (8
), a movable guide plate (9) and a holding plate α for the frozen raw material block (1) are provided on the inner periphery in a mutually interlocking manner, and a holding plate is provided outside the feeding tube (7) (7)'. It is equipped with a reciprocating device αυ that gives reciprocating motion to the plate OQ, and the crushing cylinder (5) is equipped with a left and right crushing material feeding structure having a parting shaft and a left or right cross-cutting cutting edge (12). A plurality of quantitative crushing blades (13 and a spiral feeding blade Q4) basically consisting of a pair of two types with opposite hands, and a feeding blade α9 provided in an arrangement corresponding to the crushed material sending port (3). It has a built-in crushing rotating drum (6) with An auxiliary part (17) for preventing the balls from coming out is provided, and a pulverizing cylinder round is provided which has a pulverized material inlet port αυ on the lower side and a pulverized material outlet port a on the upper side separately from the pulverizing cylinder (5). , and a plurality of mixed fine-pulverizing blades (1) having a large number of blade portions 02 arranged in opposite directions, each of which has a height that increases as it goes in the direction opposite to the fine-grinding cylinder (2), and which is slightly inclined with respect to the direction of rotation. A built-in pulverizing rotary drum Q4 is provided with a blade part arranged in a wavy manner, and a scraping blade (c) and Inclined feeding surface Ce
A large number of scraping feed blades with
A) is arranged to form a spiral body for upward feeding, and a finely pulverized material sending blade (c) is also provided around the location corresponding to the finely pulverized material delivery port Ql, and furthermore, these crushing cylinders (5
), an emulsifying cylinder 0 which has a finely pulverized material inlet on the upper side and an emulsion outlet (to) on the lower side, separately from the finely pulverized cylinder holder.
η, and in this emulsifying cylinder Gυ, an emulsifying rotary drum (to) having a mixing finely pulverizing emulsifying knife C33t having almost the same configuration as the above mixing finely pulverizing knife (c) is placed above and below the finely pulverizing rotary drum Q4. It is built in in the opposite direction, and in this emulsification rotary drum (to), a finely pulverized material inlet vane (b) is placed at a location corresponding to the finely pulverized material inlet (c), and also corresponds to the emulsion outlet (to). Emulsion delivery blades (to) are provided around the points, and the above-mentioned crushed material delivery port [3] and the crushed material inlet port α are connected to the initial crushing feed pipe 0η, which is made as straight as possible. The diameter of the base end of this crushed material outlet 0'rI is made slightly smaller to provide a shaped sealed tube (to), and the crushed material O9 sent from the shaped sealed tube to the crushed initial feed pipe Gη. A space (40) formed between the outer circumferential surface and the inner circumferential surface of the initial crushing cylinder (37) and a connection port 0υ for connecting a vacuum pump that evacuates the inside of the fine crushing cylinder (c). A first auxiliary raw material input port (429) is provided for connecting the first auxiliary raw material supply port, and the finely pulverized material delivery port α9 and the pulverized material inlet port (c) are made as straight as possible. The fine grinding initial feed pipe (4) is connected to the fine grinding initial feed pipe 03.
3 is provided with a second auxiliary raw material inlet (44J) for connecting the second auxiliary raw material supply device.

[For production]

When continuously processing livestock meat using the apparatus of the present invention, two raw materials are continuously crushed at the same time at a constant ratio, and the crushed material is sent out from the crushing cylinder using a spiral delivery blade and degassed. The porous crushed material solidified into a rod shape is degassed under vacuum through the shaped sealed tube at the equipment inlet, and the pH value of the raw material is adjusted to a range of 6 to 8 to dissolve sodium carbonate or sodium bicarbonate from 0 to 8.
05 parts and 0 to 2.5 parts of salt or 0 sodium caseinate
~10 parts of each are injected into an auxiliary raw material supply device at a ratio corresponding to the viscoelastic target value for heating gel formation, and the crushed material on which this auxiliary raw material is added is sent out by a mixing blade, and multiple pairs are added to the raw material. 2 to 6 parts of liquid B additive is injected at a constant ratio from the auxiliary raw material supply port after the mixing and pulverizing blade, which has the same function as the mixing and pulverizing blade. Mixing and emulsification is carried out using a mixing and finely pulverizing emulsifying knife.Furthermore, when continuously processing fish meat, frozen fish meat blocks at a temperature of 15°C to 30°C and frozen B additives are placed in two sets of frozen raw material block supply devices. 2 to 6 parts of additive B based on 100 parts of fish and meat are input into each block, and the number of reciprocating movements per unit time of the holding plate corresponding to the flow rate setting is set for multiple quantitative crushing. The two raw materials are continuously crushed simultaneously at a fixed ratio using a cutter, and the crushed materials are sent out from the crushing cylinder using a spiral delivery blade, and the porous material is solidified into a rod shape by a shaped sealed tube at the inlet of the deaerator. The crushed material is degassed under vacuum and carbonated with adjustment of the pH value of the raw material to the range 6-8) IJum or sodium bicarbonate 0-0.
5 parts and 0-2.5 parts of salt or 0-2.5 parts of sodium caseinate
10 parts of each are injected into an auxiliary raw material supply device at a ratio corresponding to the viscoelastic target value for heating gel formation, and the crushed material on which this auxiliary raw material is added is sent out by a feeding mixing blade, and the raw material is mixed with a plurality of pairs of The liquid A is mixed and pulverized using a multi-stage mixing and pulverizing knife.
3 to 9 parts of additives are injected at a fixed ratio from the auxiliary raw material supply port after the mixing and finely pulverizing cutter, and mixed and emulsified by the mixing and finely pulverizing and emulsifying cutter, which has the same function as the mixing and finely pulverizing cutter, and then continuous processing of soybeans. When doing so, the raw material is soybeans soaked in water, roughly crushed, molded and preserved, and this frozen soybean block is fed into a frozen raw material block supply device at a temperature of -5℃ to -30℃. , the number of reciprocating movements of the holding plate per unit time corresponding to the processing flow rate is set, and the crushed material is continuously crushed by a plurality of quantitative crushing blades, and the crushed material is sent out from the crushing cylinder by a spiral delivery blade, The porous crushed material solidified into a rod is degassed under vacuum through the shaped sealed tube of the deaerator inlet, and this crushed material is sent out using a mixing blade.
It is used for methods such as mixing and pulverizing raw materials with multiple pairs of multi-stage mixing and pulverizing blades.

Since the present invention is based on the above-mentioned system, the frozen raw material blocks (1) having the same rectangular cross-sectional area orthogonal to the moving direction are fed one after another into the frozen raw material block supply device, and the A constant cutting height is determined by the parting sheet, and then the other parts that are not parted off maintain the full cutting width, and by performing cross cutting with the holding movement, a constant amount of crushed material is ensured, and the parting sheet is In cross-cutting, the thickness of one cut is on the order of 1 millimeter due to the blade structure that ensures the biting width of the cutting edge at regular intervals. As the ice breaking becomes the function of the knife, the initial atomization is performed and a crushed product is obtained.

The crushed material that is recombined during cutting in this frozen state is processed by the ib-containing function of the quantitative crushing blade and the spiral feeding blade α of the crushing rotary drum.
The raw material is solidified into a porous rod shape by the feed blade α9 and the shaped sealed tube, and is flowed into the tube under vacuum, thereby blocking the outside air and removing the air inherent in the raw material. oxidation is suppressed.

A coagulant is injected in a fixed amount by an auxiliary raw material supply device onto the rod-shaped solidified material to be moved, and the coagulant is added onto the material to prepare for continuous mixing at a constant ratio.

Next, when the crushed material transfer port (1 second) is reached, it is divided into pieces by the scraping blade (c) and transferred upward to the inclined feeding surface (c) in a dispersed state, and this transferred material is While the dispersed material is being treated in a vacuum pulverizing cylinder, it is cut by the inclined cutting edge C!υ of the blade part 4 of the mixing and pulverizing cutter 03, and at the same time, the coagulant is dispersed and mixed. Due to the wavy arrangement of the blades of the mixing and pulverizing blades (c), the upward feeding function is impaired.

During mixing and feeding, a blade mechanism with a small contact area at the blade edge is arranged in multiple stages, and the structure has a retention amount equal to the width of the blade, which shortens the passing time to prevent heat generation and improve blade operation. By using the heat of fusion of the frozen and crushed material, we can suppress the temperature increase due to the movement of mechanical action, and we can achieve uniform particle size on the micrometer order, which suppresses protein denaturation, and the formation of reactive groups. By simultaneously uniformly dispersing and mixing the additives that act directly, the functionality of jelly-forming and emulsifying can be effectively expressed to the maximum extent.

The main problems that are aimed at in livestock meat, fish meat, and soybeans are: fixing the meat color by using the protein conalbumin of additive A, which is a metal complex, on myoglobin, and emulsifying fat with the action of additive B. For fish meat, additive B acts on water-soluble protein and fat to emulsify substances that inhibit gelation, and the color of the flesh is fixed by the action of additive KA.
The common problem with livestock meat and fish meat is that sodium carbonate or sodium bicarbonate is used to express the gelling function of myosin and actin, and the pH is adjusted to a range where bitterness is not felt. This is the effect of gelation due to reduction. A common problem throughout is the miniaturization of proteins by suppressing their denaturation (1).As well as the exposure of reactive groups, the hard proteins of livestock meat, the bones of fish, and the fibers of soybeans are each micronized. The continuous processing equipment for freeze-fracture mixing and pulverization, which is a means of these methods, is characterized by its characteristic quantitative freeze-fracture delivery, uniform atomization under 1f of temperature-elevated confinement, and uniform dispersion and mixing at the same time. By using these functions alone or in combination, processing methods using physical means can be applied to other fields besides livestock meat, fish meat, and soybeans, which has been difficult until now. It is predicted that this will lead to solutions to various problems that have been faced.

〔Effect of the invention〕

Since the present invention has the above configuration, it produces the effects described below.

The temperature of the frozen raw material block in the crushing cylinder is -5℃
Since it is a solid at a low temperature as shown below, there is no difference in the type of raw material, and the same cutting effect was obtained with either material. By applying a cutting speed that does not melt the ice, which causes a temperature rise of several degrees Celsius, the material becomes atomized to less than 100 micrometers, and at this stage the degree of atomization exceeds that of conventional methods. In the process of crushing seafood shreds, the temperature rise is limited to 10°C or less by using the raw material in a semi-frozen state or by adding ice. It is as follows. In addition, the crushing and delivery functions continuously process fixed ratio cutting, mixing, and delivery using multiple frozen raw material blocks, and the accuracy is linked to the variation in the cutting cross-sectional area of each solid.

Next, since this crushed material remains frozen, it is broken up at one end and then recombined, and the solidified porous rod is continuously passed through the deaerator and auxiliary raw material supply device. However, the air contained in the material was completely removed, and the additives were continuously added to the material, and a fixed proportion of the mixture was continuously fed to the pulverizing cylinder.

In the pulverizing cylinder, this mixture is supplied at an unfrozen temperature, and when the mixing pulverizing blade is given a cutting speed of energy equivalent to the temperature just before complete thawing at the exit side, the raw material is pulverized. It reached the order of several micrometers.

When a coagulating agent such as common salt is added, the polymerization reaction occurs instantaneously, turning into jelly, and the viscosity increases rapidly, immediately after the water content of the raw materials is completely melted. This instantaneous jellification indicates uniform micronization and uniform dispersion and mixing of the additives. In addition, although it is necessary to increase the degree of micronization to achieve low salinity, the water content of the raw materials that will be turned into jelly is completely dissolved during the pulverization process.
Ending the process immediately before is an important point in suppressing heat generation due to increased viscosity.

Next, regarding finely pulverized emulsification and cutlery after finely pulverized cutlery,
Further, auxiliary raw materials are additionally supplied and blended at a fixed ratio continuously, and jelly formation and emulsification are finally completed using a blade mechanism similar to that of a pulverizing blade. As a condition for heat gelation, in order to suppress protein denaturation, the treatment temperature is approximately 10
The final finish was achieved by giving the cutting speed within this temperature range to the mixing, finely pulverizing and emulsifying knife.

For livestock meat, the pH was adjusted to a level that did not cause bitterness at all pH values of 6 or higher, so Additive A worked effectively and the color of the meat was fixed at red (fixed).The addition of Additive B was added to strengthen and strengthen the pH. , it emulsifies fat and gives it a mellow taste.This pH-adjusting neutralizer is a food additive, sodium carbonate used in the production of Chinese soba, or sodium bicarbonate used in cakes, etc. Next, this neutralizing agent contributes in the same way as table salt, and jelly formation can be achieved with a total amount of addition of about 1 ton including table salt, and a texture similar to that of sausage can be obtained in the heating gelation process. This is about 75 on a sodium ion basis when compared with the conventional method.

In addition, when treating muscle containing a large amount of hard protein, it was made into fine particles and the texture was similar.

The processing and results for fish meat are similar to those for livestock meat, but the difference is that additive B leaves additive A first. This is because there is a difference in the amount of the substance to act; in livestock meat, the target is myoglobin, which is the cause of discoloration, and in fish meat, the target is aqueous protein, which has many substances that inhibit heat gelling.

For sardines, which had been considered the most difficult process to date, by using this continuous processing equipment, a kamaboko-like texture was obtained after heating and gelling the raw ingredients. This raw material, sardines, is said to be relatively fresh.
, I) H value is approximately 6. Pretreatment of raw materials involves removing the head, innards, tail, and skin. After heating and gelling, the back bones and small bones of the food became fine particles, and instead of the gray color typical of sardines, the food had a brown flesh color, and the fat was also emulsified, giving it a mellow taste.

In soybeans, the protein is undenatured and has a high concentration, and the fiber has been reduced to microparticles with the same size as the protein. When using this method to produce tofu from soy milk diluted with water, the amount of okara was about V2 in the conventional method.

In this way, the processing method using freeze-fractured mixed fine powder continuous processing equipment contributes to solving various problems that were considered difficult until now.
It is useful for new product development, leads to improved productivity, and has excellent effects that allow the intended purpose to be fully achieved.

〔Example〕

The embodiment shown in the figure constitutes a crushing cylinder (5) with legs (4) having input ports +21 (2)' on both left and right sides of the frozen raw material block (1) and a crushed material outlet (3). Opening (21F21')
) (7) ', a hopper (8) is attached to the outer end of each input cylinder (71 (7) ', and a movable guide plate (9) and a plate for holding the frozen raw material block (1) are attached to the inner circumference ( 11
are provided in a mutually interlocking manner, and each input cylinder (7)
(7) Equipped with a reciprocating device αυ that provides reciprocating motion against the holding plate OC outside the cylinder, and a cutting edge αυ for parting and left or right cross cutting inside the breaking cylinder (5). A plurality of fixed quantity crushing blades basically composed of a pair of two types with left and right hand, each having a crushed material feeding structure with a spiral shape, corresponds to a spiral feeding blade I, and a crushed material sending port (3). A crushing rotary drum (lI19
A comb tooth is provided on the inner peripheral wall of the crushing cylinder (5) to prevent crushed materials from crossing between the outer peripheral edge of the spiral feeding blade (14) and the inner peripheral surface of the crushing cylinder (5). In addition, separate from the crushing cylinder (5), there is a crushed material inlet α barrel on the lower side, four pulverized material delivery ports α9 on the upper side, and a finely pulverized material delivery port αl. This pulverizing cylinder diagram shows a large number of blade parts (shape) whose cutting edge shank becomes higher as it goes in the opposite direction of rotation and is slightly inclined with respect to the direction of rotation. ) with a plurality of mixing and finely pulverizing teeth (c) arranged in opposite directions so that the blade part (sha) is arranged in an undulating manner. A scraping blade (C) and an inclined feed surface 2 are installed at a location corresponding to the crushed material delivery port.
A large number of scraping blades with E9 are arranged so that the oblique feeding surface (1) forms a spiral body for upward feeding, and a finely pulverized material delivery port (corresponding to L) is installed. A finely pulverized material delivery blade (c) is installed around the place where the pulverized material is transported, and a pulverized material transfer inlet device is installed on the upper side and an emulsion inlet device is installed on the lower side separately from the crushing cylinder (5) and the pulverized material cylinder (■). An emulsifying cylinder (311) having an outlet (to) is constructed, and in this emulsifying cylinder Gυ, an emulsifying rotary drum (to) having a mixing finely pulverizing emulsifying cutter G3 having almost the same configuration as the above mixing finely pulverizing cutter is installed. The pulverizing rotary drum Q4J is built in an upside-down orientation, and in this emulsifying rotary drum, there is a pulverized material feeding blade (b) at a location corresponding to the pulverized material inlet device, and an emulsion outlet (7). Emulsion delivery blade (G) is placed in the corresponding location.
In addition, the above-mentioned crushed material outlet (3) and crushed material inlet (181
are connected by an initial crushing feed pipe 0η which is made as straight as possible, and this crushed material feed pipe C3? A shaped sealed tube (to) is provided with the base end portion of l having a slightly narrower diameter, and the crushed material C delivered from the shaped sealed tube (to) is placed in the initial crushing feed tube 07).
3), a space formed between the outer peripheral surface of the crushed material feed pipe 6η, and the inner peripheral surface of the crushed material feed pipe Gη (40 and a vacuum pump that evacuates the inside of the pulverizing cylinder canister). (not shown) and a first auxiliary raw material input port (43) for connecting the first auxiliary raw material supply device (not shown); The outlet a!J and the finely pulverized material delivery blade are connected to the initial fine pulverization feed pipe (43), which is made as straight as possible, and the second auxiliary raw material supply device (not shown) is connected to the first fine pulverization feed pipe (43). A second auxiliary raw material inlet (4) for connecting the
4).

In addition, in the figure (4f9 hakai)" plate (91O support shaft, (47
) G181 (49c Crushing rotating drum αG, pulverizing rotating drum (goods) and emulsifying rotating drum (to) drive shaft,
60 indicates an escape notch of the quantitative crushing blade 0.

The present invention uses egg whites, egg yolks, salt, sugar, starch, gelatin, vegetable oil, spices, fragrances, neutralizers, seasonings, etc. as auxiliary raw materials (additives), and is also practiced. At this time, the surface in contact with the workpiece from the input part of the freezing block (1) to the part past the feed mixing blade (5) (
(excluding cutlery) should be coated with tetrafluoroethylene. Furthermore,
The present invention may also be implemented with only one side of the input section for the frozen raw material block.

[Brief explanation of drawings]

FIG. 1 is a schematic front view showing the entire freeze-fracture-mixing-fine-pulverization continuous processing apparatus of the present invention, FIG. 2 is a schematic cross-sectional view from the front side showing the input part and the crushing cylinder part of the frozen raw material block,
Figure 3 is a schematic cross-sectional view of the same as seen from the side, and Figure 4 is a cross-sectional diagram of the 3rd section.
5 is a developed front view of the pulverizing rotary drum, FIG. 6 is a developed top view, FIG. 7 is a developed bottom view, and FIG. 8 is a developed side view. FIG. 9 is a developed front view of the emulsifying rotary drum, FIG. 10 is a sectional view showing the relationship between the pulverizing cylinder and the mixing and pulverizing cutter, and FIG. 11 is a sectional view showing the relationship between the emulsifying cylinder and the mixing pulverizing and emulsifying cutter. Figure 12 is a sectional view showing the relationship between the crushed material inlet and the scraping blade, Figure 13 is a front view showing the crushing blade, Figure 14 is a left side view, Figure 15 is a right side view, and Figure 16 is a left side view. 17 is a front view showing one of the oyster defeating blades, FIG. 18 is a left side view, FIG. 19 is a right side view, and FIG. 20 is a plan view. (1)...Frozen raw material block, +21 (21'...
・Input port, (3)...Crushed material delivery port, (4)...Bridge, (5)...Cylinder, (7)(7)'...Input cylinder, (8)...・Hopper, (9)...Guide plate, G
1... Holding plate, αυ... Reciprocating device, G2...
Blade tip, G3...quantitative crushing blade, I...feeding blade, α
Death... Delivery blade, (16)... Crushing rotating drum, αη
...Auxiliary part, Cod...Crushed material inlet, αl...Finely pulverized material delivery port, Han...Fine grinding cylinder, Ql)...Blade tip, (Sha)...Blade part, ( c)...Mixed fine grinding knife,
64... Fine grinding rotating drum, (c)... Scraping blade, (c)... Inclined feeding surface, (Foundation)... scraping feeding blade, (c)... Fine grinding Material delivery blade, (To)... Finely ground material inlet, (To)... Emulsion outlet, 0υ...
Emulsifying cylinder, G32...Mixing and finely pulverizing emulsifying blade, (to)...Emulsifying rotary drum, (2)...Finely ground product feeding blade, (G)...Emulsion sending blade, C3? )...Crushed material delivery pipe, (to)...Orthopedic sealed tube, OL...Crushed material, (41...Space, (4υ...Connection port, (42)...Input port , (43)... Finely ground material feed pipe, (44... Inlet, (4υ... Support shaft, (4η(4ε(41... Drive shaft, (501... Notch. Patent application) Hirozun Iwai Machine Industry Co., Ltd. 1 To the hill

Claims (1)

[Claims] 1, one or more sets of frozen raw material block supply devices and a crushed material delivery port (3), and a crushed material feed having cutting edges for parting and left or right cross cutting. Built-in is a plurality of quantitative crushing blades (13) basically consisting of a pair of left and right opposite-hand type crushing blades (13), and a crushing rotary drum (16) with spiral feeding blades (14) and delivery blades (15). A continuous processing device for freezing, crushing, mixing and pulverizing, characterized by having a crushing cylinder (5). 2. An auxiliary part (17) is provided on the inner circumferential surface of the crushing cylinder (5) to prevent crushed materials from overflowing between the outer circumferential edge of the spiral feeding blade (14) and the inner circumferential surface of the crushing cylinder (5). The freeze-fracture-mixing-fine-pulverization continuous processing apparatus according to claim 1. 3. An inlet (2) for the frozen raw material block (1) provided on the outer peripheral wall of the crushing cylinder (5), an inlet cylinder (7) fixed in an inclined manner on the outside of the inlet (2), and an inlet a hopper (8) attached to the outer end of the cylinder (7); a reciprocating device (11) that provides reciprocating motion to the holding plate (10) and the holding plate (10) of the frozen raw material block (1); Holding plate (10
3. The continuous freezing, crushing, mixing and pulverizing apparatus according to claim 1 or 2, further comprising a frozen raw material block feeding device comprising a movable guide plate (9) mounted on the upper end of the block. 4. Crushed material inlet (18) and finely pulverized material outlet (19)
), and also has a plurality of blade parts (22) arranged in opposite directions, each of which has a plurality of blade parts (22) whose blade edges (21) become higher as they go in the direction opposite to the direction of rotation and are slightly inclined with respect to the direction of rotation. It has a built-in pulverizing rotary drum (24) having a mixing and pulverizing cutter (23) arranged so that the blade part (22) has a wavy shape, and a crushed material inlet port (18) on the outer peripheral surface of the pulverizing rotary drum (24). Scrape blade (25
) and a plurality of scraping feed vanes (27) having an inclined feed surface (26) are provided in such a manner that the inclined feed surface (26) forms an upward feeding spiral, and also a finely ground material delivery port ( A continuous processing device for freezing, crushing, mixing and finely pulverizing, characterized by having a pulverizing cylinder (20) surrounded by a finely pulverized material delivery blade (28) at a location corresponding to 19). 5. Finely ground material inlet (29) and emulsion outlet (30)
), and a plurality of mixed pulverizers having multiple blade portions (22) in opposite directions, the blade edges becoming higher as they go in the direction opposite to the rotation direction and slightly inclined with respect to the rotation direction. It has a built-in emulsifying rotary drum (33) with cutters (23) arranged so that the blade portion (22) has a wavy shape, and further includes a finely pulverized material inlet (29) in the emulsifying rotary drum (33).
), and an emulsifying cylinder (31) having a finely ground material feeding blade (34) at a location corresponding to the emulsion outlet (30) and an emulsion sending vane (35) at a location corresponding to the emulsion outlet (30). Features: Continuous processing equipment for freezing, crushing, mixing and pulverizing. 6. The finely pulverized material delivery port (19) and the finely pulverized material inlet port (29) are connected by a pulverized material feed pipe (43) which is made as straight as possible, and the auxiliary material is supplied to this pulverized material feed pipe (43). A continuous processing device for freezing, crushing, mixing and pulverizing, characterized in that it is provided with an auxiliary raw material inlet (44) for connecting the device. 7. Claim characterized in that it has a crushing cylinder (5) and a pulverizing cylinder (20), and the crushed material delivery port (3) and the crushed material inlet port (18) of the crushing cylinder are connected by piping. 1, 2, 4 or 6. The continuous processing device for freezing, crushing, mixing and pulverizing. 8. The continuous freezing, crushing, mixing, and pulverizing apparatus according to claim 1, 2, 4, or 7, wherein a deaerator for degassing the crushed material is connected in the middle of the piping. 9. The crushed material delivery port (3) and the crushed material inlet (18) are connected by a crushed material feeding pipe (37) that is made as straight as possible, and the base end of this crushed material feeding pipe (37) is slightly A shaped sealed tube (38) with a small diameter is provided, and a vacuum pump is installed at an appropriate location in the crushed material feed pipe (37) and the pulverization cylinder (20) to evacuate the inside of the crushed material feed pipe (37) and the pulverization cylinder (20). 9. The continuous freezing, crushing, mixing and pulverizing apparatus according to claim 1, further comprising a connecting port (41) for connection.