JP2019207046A - Ice slurry manufacturing device and refrigeration system - Google Patents

Abstract

To provide an ice slurry manufacturing device which can manufacture ice slurry efficiently, and to provide a refrigeration system.SOLUTION: An ice slurry manufacturing device 1 of the invention includes: an ice slurry material manufacturing part (an ice slurry material manufacturing device) 200; an ice storage tank 500; and a return pipe 44. The ice slurry material manufacturing device 200 generates flake ice from a part of supplied brine and cools the other part of the supplied brine. The ice storage tank 500 is supplied with the flake ice generated by the ice slurry material manufacturing device 200 and the cooled brine and stores ice slurry S formed by mixing the flake ice with the cooled brine. The return pipe 44 returns the brine in the ice slurry S in the ice storage tank 500 to the ice slurry material manufacturing device 200 as raw water.SELECTED DRAWING: Figure 1

Description

  The present invention relates to an ice slurry production apparatus for producing an ice slurry for freezing frozen products such as fish and shellfish such as fresh seafood, various kinds of meat and other foods, foods to be stored and transported frozen, etc. And a refrigeration system.

  Various methods and apparatuses for cooling food are provided in the process of processing food. For example, in Patent Document 1, a chain conveyor that continuously suspends carcasses, a chiller tank that is disposed below the chain conveyor and stores ice slurry, and an inside of a poultry carcass upstream of the chiller tank. An apparatus for cooling poultry carcasses comprising a nozzle for filling ice slurry is described.

  The ice slurry stored in the chiller tank is manufactured in an ice heat storage tank and supplied through piping. The ice slurry in the chiller tank flows out as overflow water from the chiller tank and can be circulated. The inside of the carcass that has been conveyed to the upstream end of the chiller tank by the chain conveyor is filled with ice slurry from the nozzle. As a result, the carcass is cooled from the inside.

  The carcass is suspended by a chain conveyor, immersed in the ice slurry stored in the chiller tank on the upstream side, floated from the ice slurry on the downstream side, and transferred to the next cutting step. This cooling system for poultry carcasses cools the carcass from the inside and outside, eliminates the temperature difference between each part, shortens the cooling time, suppresses the moisture content of the carcass, and deteriorates the meat quality. Can be prevented.

JP 2009-034023 A

  The cooling device for a poultry carcass disclosed in Patent Document 1 includes an ice heat storage tank for producing ice slurry supplied to a chiller tank. Two pipe lines are connected to the ice heat storage tank. A three-way valve is connected to the two pipe lines so that the ice filling rate of the ice slurry can be adjusted. However, it is not efficient to adjust the ice filling rate of the ice slurry by a three-way valve.

  An object of the present invention is to provide an ice slurry manufacturing apparatus and a refrigeration system which can efficiently manufacture an ice slurry.

The ice slurry production apparatus according to the present invention is:
An ice slurry raw material production unit that generates flake ice from a part of the supplied brine and cools the remainder of the supplied brine;
An ice storage tank for storing an ice slurry in which the flake ice generated by the ice slurry raw material production unit and the cooled brine are supplied and the flake ice and the cooled brine are mixed;
Is provided.

In the ice slurry production apparatus according to the present invention,
A return pipe that returns the brine in the ice slurry in the ice storage tank to the ice slurry raw material production unit as raw water,
Is provided.

In the ice slurry production apparatus according to the present invention,
A stirring unit for stirring the ice slurry in the ice storage tank;
Is provided.

In the ice slurry production apparatus according to the present invention,
The ice slurry raw material production unit includes a drum having a refrigerant clearance, a refrigerant supply unit that supplies an inner cylinder refrigeration refrigerant to the refrigerant clearance,
Is provided.

The refrigeration system according to the present invention includes:
An ice slurry production apparatus according to the present invention;
A refrigeration apparatus for freezing the article to be frozen with the ice slurry;
Comprising
A refrigeration system,
The refrigeration apparatus is
An annular flow path through which the ice slurry circulates, the flow path having two parallel straight lines and two curved lines connecting adjacent ends of the two straight lines; ,
A propulsion unit that provides propulsion to the ice slurry;
A guide vane that divides at least one of the curved lines into a plurality of lanes;
Is provided.

  ADVANTAGE OF THE INVENTION According to this invention, the ice slurry manufacturing apparatus and refrigeration system which enabled it to manufacture an ice slurry efficiently can be provided.

1 is a schematic front view showing an embodiment of a refrigeration system according to the present invention. It is a cross-sectional perspective view which shows the outline of the ice slurry raw material manufacturing part contained in the ice slurry manufacturing apparatus which concerns on this invention. It is a schematic perspective view which shows one Embodiment of the freezing apparatus contained in the freezing system which concerns on this invention. 1 shows an embodiment of a refrigeration apparatus included in a refrigeration system according to the present invention, where (a) is a schematic plan view and (b) is a schematic front view.

  The refrigeration apparatus and refrigeration system of the present embodiment are an apparatus and a system for freezing (including cooling) frozen products such as seafood such as fresh seafood, various meats, and other foods with ice slurry.

  The ice slurry is a sherbet-like mixture in which flake ice (solid) obtained by processing hybrid ice (described later) into flakes (strips) and an aqueous solution (brine) containing a solute are mixed at a predetermined ratio. It has sex. By adding flake ice to the ice slurry, the constituent ratio of flake ice and brine contained in the ice slurry can be easily adjusted.

  Hybrid ice is ice obtained by coagulating an aqueous solution (brine) containing a solute so that the concentration of the solute is substantially uniform. Hybrid ice has at least (a) the temperature at the time of melting is less than 0 ° C., and (b) the change rate of the solute concentration of the aqueous solution (brine) in which the ice melted in the melting process (hereinafter referred to as “change rate of the solute concentration”). However, the product to be frozen can be efficiently frozen.

  The kind of solute contained in the hybrid ice is not particularly limited as long as it is a solute when water is used as a solvent, and can be appropriately selected according to a desired freezing point, use of ice to be used, and the like. Examples of the solute include a solid solute, a liquid solute, and the like. Typical examples of the solid solute include salts (inorganic salts, organic salts, and the like).

  In particular, sodium chloride (NaCl) among salts does not excessively lower the temperature of the freezing point and is suitable for freezing fresh animals and plants or a part thereof. Moreover, since salt is contained in seawater, it is also suitable in terms of easy procurement. Moreover, ethylene glycol etc. are mentioned as a liquid solute. In addition, a solute may be contained individually by 1 type and may be contained 2 or more types.

  Brine is an aqueous solution containing a solute and having a low freezing point, such as a sodium chloride aqueous solution (brine), a calcium chloride aqueous solution, a magnesium chloride aqueous solution, an ethylene glycol aqueous solution, and the like. Although the brine used as the raw material for the flake ice is not particularly limited, when salt is used as the solute, it is preferably seawater, water obtained by adding salt to seawater, or diluted water of seawater. This is because seawater, water obtained by adding salt to seawater, or seawater-diluted water is easy to procure, and thus the procurement cost can be reduced.

  The thermal conductivity of brine (brine) containing salt as a solute is about 0.58 W / m K, but the thermal conductivity of flake ice frozen from brine containing salt as a solute is about 2.2 W / m. K. That is, since the thermal conductivity of flake ice (solid) is higher than that of brine (liquid), flake ice (solid) can freeze the item to be frozen earlier.

  However, if the flake ice (solid) remains as it is, the area in contact with the article to be frozen will be small. Therefore, fluidity is imparted by mixing flake ice and brine into an ice slurry. Thereby, flake ice (solid) can be uniformly contacted with the product to be frozen, and the product to be frozen can be quickly frozen.

  The flake ice and the brine contained in the ice slurry both contain the same solute. At this time, it is preferable that the solute concentration of the flake ice and the solute concentration of the brine are close to each other. The reason is as follows.

  That is, when the solute concentration of the flake ice is higher than the solute concentration of the brine, the temperature of the flake ice becomes lower than the saturation freezing point of the brine, so that the brine freezes immediately after mixing the brine having a low solute concentration.

  On the other hand, when the solute concentration of flake ice is lower than the solute concentration of brine, the saturation freezing point of brine is lower than the saturation freezing point of flake ice. For this reason, the temperature of the ice slurry in which flake ice and brine are mixed decreases.

  Therefore, in order not to fluctuate the state of the mixture of flake ice and brine (the state of the ice slurry), it is preferable that the solute concentrations of the flake ice and the brine to be mixed are the same as described above.

  In the case of an ice slurry, the brine may be one obtained by melting flake ice or may be prepared separately, but it is preferably one obtained by melting flake ice.

  Here, an embodiment of a refrigeration apparatus and a refrigeration system for freezing a product to be frozen with ice slurry will be described with reference to FIGS. FIG. 1 is a partial sectional schematic front view showing an embodiment of a refrigeration system according to the present invention. FIG. 2 is a cross-sectional perspective view showing an outline of an ice slurry raw material manufacturing apparatus included in the refrigeration system according to the present invention. FIG. 3 is a schematic perspective view showing an embodiment of the refrigeration apparatus according to the present invention. FIG. 4 shows one embodiment of the refrigeration apparatus according to the present invention, where (a) is a schematic plan view and (b) is a schematic front view.

  As shown in FIG. 1, the refrigeration system includes an ice slurry manufacturing apparatus 1 and a refrigeration apparatus 6. The ice slurry manufacturing apparatus 1 includes an ice slurry raw material manufacturing unit (hereinafter referred to as “ice slurry raw material manufacturing apparatus”) 200 and an ice storage tank 500.

  As shown in FIG. 2, the ice slurry raw material manufacturing apparatus 200 includes a drum 21, a rotating shaft 22, an injection unit 23, a stripping unit 24, a blade 25, a flake ice discharge port 26, and an upper bearing member 27. An injection control unit 28, a heat protection cover 29, a geared motor 30, a rotary joint 31, a refrigerant clearance 34, a rotation control unit 37, a bush 38, a refrigerant supply unit 39, and a brine storage tank 40 ( 1).

  The drum 21 includes an inner cylinder 32, an outer cylinder 33 that surrounds the inner cylinder 32, and a refrigerant clearance 34 that is formed between the inner cylinder 32 and the outer cylinder 33. Further, the outer peripheral surface of the drum 21 is covered with a cylindrical heat-resistant protective cover 29. The inner cylinder refrigeration refrigerant is supplied to the refrigerant clearance 34 from the refrigerant supply unit 39 via the refrigerant pipe 42. Thereby, the inner peripheral surface of the inner cylinder 32 is cooled.

  The rotary shaft 22 is disposed on the central axis of the drum 21 and rotates around the material axis with the central shaft as an axis, using a geared motor 30 installed above the upper bearing member 27 as a power source. The rotational speed of the geared motor 30 is controlled by a rotation control unit 37 described later.

  The injection unit 23 is composed of a plurality of pipes having injection holes 23 a for injecting brine or ice slurry S (described later) toward the wall surface of the inner cylinder 32, and rotates together with the rotating shaft 22. The brine injected from the injection hole 23a adheres to the wall surface of the inner cylinder 32 cooled by the refrigerant, and quickly freezes to become hybrid ice without giving time for separation into the solute and the solvent. . The plurality of pipes constituting the injection unit 23 extend radially from the rotary shaft 22 in the radial direction of the drum 21.

  Virgin brine sprayed from the spray section 23 is stored in the brine storage tank 40. The brine storage tank 40 and the injection unit 23 are connected by a brine pipe 41.

  The stripping unit 24 includes a plurality of arms each having a blade 25 that strips hybrid ice generated on the inner peripheral surface of the inner cylinder 32 at the tip. The stripping part 24 extends in the radial direction of the drum 21 and rotates together with the rotating shaft 22. The plurality of arms constituting the stripping portion 24 are mounted so as to be symmetric with respect to the rotation shaft 22. In addition, although the peeling part 24 of the ice slurry raw material manufacturing apparatus 200 shown in FIG. 2 is comprised by two arms, the number of arms is not specifically limited.

  The blade 25 attached to the tip of the arm is made of a member having a length substantially equal to the entire length (total height) of the inner cylinder 32, and a plurality of saw teeth are provided at the end facing the inner peripheral surface of the inner cylinder 32. 25a is formed.

  The hybrid ice generated on the inner peripheral surface of the inner cylinder 32 becomes flake ice by being peeled off by the blade 25. The flake ice falls from the flake ice outlet 26. The flake ice that has fallen from the flake ice discharge port 26 is stored in an ice storage tank 500 (see FIG. 1) disposed immediately below the ice slurry raw material manufacturing apparatus 200.

  Moreover, the ice slurry raw material manufacturing apparatus 200 adjusts the quantity of the flake ice produced | generated by adjusting the quantity of the brine injected from the injection part 23. FIG. That is, the amount of flake ice produced can be increased by increasing the amount of brine ejected from the ejection unit 23. Conversely, the amount of flake ice produced can be reduced by reducing the amount of brine ejected from the ejection unit 23.

  The upper bearing member 27 has a shape in which the pan is inverted, and seals the upper surface of the drum 21. A bush 38 that supports the rotating shaft 22 is fitted in the central portion of the upper bearing member 27. The rotary shaft 22 is supported only by the upper bearing member 27, and the lower end portion of the rotary shaft 22 is not pivotally supported.

  The ejection control unit 28 adjusts the amount of brine ejected from the ejection unit 23 when the ejection unit 23 ejects brine. A specific method for adjusting the amount of brine to be ejected from the ejection unit 23 is not particularly limited. For example, for each of the plurality of pipes constituting the injection unit 23, the amount of brine to be injected may be adjusted by adjusting the number of pipes that inject brine and the number of pipes that do not inject brine. Further, for example, the amount of brine to be injected may be adjusted by increasing or decreasing the amount of brine sent to the plurality of pipes for injecting brine.

  From the injection unit 23, not only the brine is injected, but also the ice slurry S or a mixture of the brine and the ice slurry S may be injected. Therefore, the injection unit 23 is configured to be able to inject any of brine, ice slurry S, or a mixture thereof. Furthermore, the injection unit 23 is not limited to one that jets the brine, the ice slurry S, or a mixture thereof vigorously, but includes one that discharges along the inner peripheral surface of the inner cylinder 32.

  The ice slurry raw material manufacturing apparatus 200 generates flake ice by freezing a part of the brine, ice slurry S, or a mixture thereof injected from the injection unit 23 on the inner peripheral surface of the inner cylinder 32, and the remaining part Although it cools, it is set not to freeze. That is, the cold heat of the inner cylinder refrigeration refrigerant supplied from the refrigerant supply unit 39 to the ice slurry raw material manufacturing apparatus 200 is necessary for freezing all of the brine, ice slurry S, or a mixture thereof injected from the injection unit 23. It is set smaller than cold.

The thermal protection cover 29 has a cylindrical shape and seals the side surface of the drum 21.
The refrigerant supply unit 39 supplies the inner cylinder refrigeration refrigerant that freezes the inner peripheral surface of the inner cylinder 32 to the refrigerant clearance 34 via the refrigerant pipe 42. As shown in FIG. 1, the refrigerant supply unit 39 is installed adjacent to the ice storage tank 500.

  The inner cylinder refrigeration refrigerant supplied to the refrigerant clearance 34 circulates between the refrigerant clearance 34 and the refrigerant supply unit 39 via the refrigerant pipe 42. Thereby, the inner cylinder frozen refrigerant | coolant supplied to the refrigerant | coolant clearance 34 can be maintained in a state with high refrigerating capacity.

  As shown in FIG. 1, the ice slurry raw material manufacturing apparatus 200 is installed on an ice storage tank 500. The ice storage tank 500 includes a disk-shaped bottom surface portion 51, a cylindrical wall surface portion 52, and a top surface portion 53 that covers the upper surface of the wall surface portion 52, and stores the ice slurry S. An opening 53 a is provided at an eccentric position of the top surface portion 53. The drum 21 of the ice slurry raw material manufacturing apparatus 200 is installed so that the opening 53a and the flake ice discharge port 26 communicate with each other.

  In the ice storage tank 500, an agitation unit (hereinafter referred to as “agitation means”) 54 for agitating the stored ice slurry S is attached. The stirring means 54 includes a main body blade 54a, a rotating shaft 54b, and a drive unit 54c. The main body blade 54a is not limited to a propeller blade as illustrated, but may be various types such as a paddle blade, an anchor blade, a turbine blade, and a ribbon blade (not illustrated).

  The rotating shaft 54 b is arranged in a vertical posture on the central axis of the ice storage tank 500. The main wing 54a is fixed to the lower end of the rotating shaft 54b. The upper end portion of the rotation shaft 54 b protrudes upward from the top surface portion 53. The drive part 54c is attached to the upper end part of the rotating shaft 54b. The drive part 54c is installed on the top | upper surface part 53, and is provided with a motor. The drive unit 54c may rotate the stirring unit 54 at a constant speed, or may rotate it so as to repeat acceleration and deceleration.

  The ice storage tank 500 is connected to a return pipe 44 that supplies the ice slurry S in the ice storage tank 500 as raw water to the injection unit 23 of the ice slurry raw material manufacturing apparatus 200. A pump 57 is connected in the middle of the return pipe 44.

  The return pipe 44 has a concentration measuring unit (hereinafter referred to as “first measurement”) that measures the concentration of flake ice (IPF) in the ice slurry S stored in the ice storage tank 500 on the upstream side of the pump 57. Means ”) 55 is provided. The concentration IPF of the flake ice is calculated by “IPF = (mass of flake ice) / (mass of flake ice + mass of brine)”.

  The concentration of the flake ice in the ice slurry S is preferably 10% or more and 60% or less. The ice slurry manufacturing apparatus 1 can maintain the concentration of flake ice at a predetermined value (target) by controlling the amount of flake ice manufactured by the ice slurry raw material manufacturing apparatus 200. The target of the flake ice concentration may be appropriately selected depending on the type of the object to be frozen. The temperature of the ice slurry S can be adjusted by adding flake ice (adding cold heat to the ice slurry S) or conversely freezing the object to be frozen (even if the cold heat is removed from the ice slurry S). The concentration of the flake ice in the ice slurry S is changed by the heat transfer to the ice slurry S. Therefore, by controlling the concentration of the flake ice in the ice slurry S, the amount of heat transferred between the ice slurry S can be controlled.

  Although not shown, the first concentration measuring means 55 includes a heater and a thermometer in a substantial bypass pipe having an inlet and an outlet in the return pipe 44. The first concentration measuring means 55 closes the inlet and the outlet at the time of measurement, and collects a sample of the ice slurry S to be measured between the inlet and the outlet. The first concentration measuring means 55 may measure a temperature change of the sample by adding a predetermined amount of heat to the sample with a heater.

  That is, since the sample of ice slurry S maintains the freezing point temperature while the flake ice remains in the sample, the temperature rising timing from the freezing point temperature is related to the concentration of the flake ice (the amount of heat applied is constant). In this case, the higher the flake ice concentration, the later the temperature rise timing), and the concentration of the ice slurry S can be specified from the temperature change of the sample of the ice slurry S.

  When the measurement of the flake ice concentration is completed, the inlet and outlet of the bypass pipe provided in the first concentration measuring means 55 are opened, and the sampled ice slurry S flows out to the return pipe 44. After a predetermined time, the first concentration measuring means 55 again measures the concentration of flake ice in a similar manner with the inlet and outlet closed again. This sampling and measurement are continuously performed.

  The downstream end of the return pipe 44 is connected to the brine pipe 41 via the switching valve 43. Therefore, it is switched by the switching valve 43, and the virgin brine stored in the brine storage tank 40 and the recycled ice slurry S returned from the ice storage tank 500 are switched and supplied to the injection unit 23, or Virgin brine and recycled ice slurry S are mixed and supplied.

  The ice storage tank 500 and the refrigeration apparatus 6 are connected by an ice slurry supply pipe 45 and an ice slurry return pipe 46. The ice slurry supply pipe 45 and the ice slurry return pipe 46 are provided with on-off valves 45a and 46a. The ice slurry supply pipe 45 sends the ice slurry S in the ice storage tank 500 to the refrigeration apparatus 6. The ice slurry return pipe 46 returns the ice slurry S in the refrigeration apparatus 6 to the ice storage tank 500. Each of the ice slurry supply pipe 45 and the ice slurry return pipe 46 is provided with a pump (not shown), and each pump is driven in synchronization with opening and closing of the on-off valves 45a and 46a.

  The on-off valve 45a of the ice slurry supply pipe 45 and the on-off valve 46a of the ice slurry return pipe 46 are respectively “feed amount of ice slurry S to the refrigerating apparatus 6> return amount of ice slurry S from the refrigerating apparatus 6”. To be controlled. The water surface of the ice slurry S in the refrigeration apparatus 6 may be kept constant by an overflow not shown.

  Further, the amount of ice slurry S that can be stored in the ice storage tank 500 is sufficiently larger than the amount of ice slurry S necessary to fill the refrigeration apparatus 6, and even if the concentration of flake ice in the ice slurry S of the refrigeration apparatus 6 changes. The concentration of the flake ice in the ice slurry S stored in the ice storage tank 500 hardly changes.

  As described above, the ice storage tank 500 and the refrigeration apparatus 6 are connected by the ice slurry supply pipe 45 and the ice slurry return pipe 46, and the amount of ice slurry S that can be stored in the ice storage tank 500 is necessary to fill the refrigeration apparatus 6. Since the concentration of the ice slurry S is sufficiently larger than the amount of the ice slurry S, even if the concentration of the flake ice in the ice slurry S of the refrigeration apparatus 6 changes, the concentration of the flake ice in the ice slurry S stored in the ice storage tank 500 is Almost no change.

  Further, between the ice storage tank 500 and the refrigeration apparatus 6, the ice slurry S is controlled so that “the amount of ice slurry S fed to the refrigeration apparatus 6> the amount of ice slurry S returned from the refrigeration apparatus 6”. As a result, a part of the ice slurry S of the refrigeration apparatus 6 is discarded by an overflow not shown or the like, so that the change in the concentration of the flake ice in the ice slurry S stored in the ice storage tank 500 is even smaller.

  The concentration of the flake ice in the ice slurry S of the ice storage tank 500 is measured by the first concentration measuring means 55 and is fed back to the operation of the ice slurry raw material manufacturing apparatus 200 to be controlled to a predetermined concentration. ing.

  As shown in FIGS. 3 and 4, the refrigeration apparatus 6 is frozen by wrapping the article to be frozen A (see FIG. 4) with the ice slurry S, and therefore, the flow path 60, the guide vane 70, , “Promotion means”) 80 and second concentration measurement means 90. For example, the article A to be frozen is placed on a tray (not shown). The tray is held, for example, in a rack (not shown) that is stacked in a plurality of stages at intervals. For example, the rack has a frame shape having four columns and a beam on which the tray is placed. The article to be frozen A in the tray is wrapped in the ice slurry S.

  The channel 60 is annular and filled with the ice slurry S supplied from the ice slurry supply pipe 45, and the ice slurry S can be circulated. The flow path 60 includes a supply port 61 for the ice slurry S, and a first discharge port 62 and a second discharge port 63 for the ice slurry S. An ice slurry supply pipe 45 connected to the ice storage tank 500 is connected to the ice slurry S supply port 61. An ice slurry return pipe 46 connected to the ice storage tank 500 is connected to the first discharge port 62 of the ice slurry S. A nozzle 48 is connected to the second outlet 63 of the ice slurry S. The nozzle 48 is provided with an on-off valve 48a.

  As shown in FIG. 3, the flow path 60 is a race having two parallel straight lines 64 and two curved lines 65 connecting the adjacent ends of the two straight lines 64. It has a track shape. The channel 60 includes an oval outer wall portion 66, a partition portion 67 provided on the center line of the outer wall portion 66, and a bottom surface portion 68.

  The straight line 64 is a freezing area 69 where the article A to be frozen is placed and frozen. Between each end of the partition part 67 and the semicircular part of the outer wall part 66, a space is provided, and a curved line 65 in which the ice slurry S turns is formed. A line connecting each end edge of the partition portion 67 and the outer wall portion 66, that is, a perpendicular line virtually drawn at each end of the partition portion 67 becomes a boundary line between the straight line 64 and the curved line 65.

  As shown in FIG. 4 (b), at least one curved line 65 of the flow path 60 may be provided with a pit (deep part) at the bottom thereof. When the solute separates from the ice slurry S and precipitates during the freezing operation, the solute is collected in the pits. The solute collected in the pits does not affect the freezing operation.

  The curved line 65 is provided with a substantially semicircular (J-shaped) guide vane 70 that divides the curved line 65 into a plurality of (two in the drawing) lanes. Guide vanes 70 are installed on the bottom surface 68 so that the widths of the lanes are equal. When the guide vane 70 is not provided, the ice slurry S may stagnate in a region along the outer wall 66 on the upstream side of the straight line 64 that is continuous with the curved line 65. Note that the guide vane 70 may be installed on the bottom surface portion 68 so that the widths of the lanes are not uniform.

  The upstream end 71 of the guide vane 70 is located at the boundary line between the straight line 64 and the curved line 65 of the flow path 60. The downstream end portion 72 of the guide vane 70 extends beyond the downstream end of the curved line 65 to the upstream region of the straight line 64. Both ends of the guide vane 70 are not arranged side by side, but are formed in a J shape as a whole.

  Although not shown, the downstream end 72 of the guide vane 70 may be located downstream of the boundary line between the curved line 65 and the straight line 64, that is, upstream of the curved line 65. Although not shown, the end 71 on the upstream side of the guide vane 70 may be located on the boundary line between the straight line 64 and the curved line 65 or may be located on the downstream side of the curved line 65. Therefore, the guide vane 70 may be formed in a U shape.

  By providing the guide vane 70 on the curved line 65, the ice slurry S can flow in this region without stagnation. When the downstream end 72 of the guide vane 70 extends into the upstream side of the straight line 64, the downstream end 72 of the guide vane 70 extends into the curved line 65. The ice slurry S can flow more smoothly and smoothly without stagnation.

  The flow path 60 includes a propulsion unit 80 that imparts a propulsive force to the ice slurry S in the freezing region 69. The number of propulsion means 80 is not limited to two as shown, and it is sufficient that at least one propulsion means 80 is provided. Needless to say, three or more propulsion means 80 may be provided. The propulsion means 80 includes, for example, a screw 81 installed upstream of the straight line 64 in the flow path 60, a drive shaft 82 that connects the screw 81 at the tip and penetrates the semicircular portion of the outer wall portion 66, and a drive And a drive source 83 connected to the base end of the shaft 82 and installed outside the flow path 60.

  The second concentration measuring unit 90 is configured in the same manner as the first concentration measuring unit 55, and measures the concentration of the flake ice in the ice slurry S in the flow path 60. The second concentration measuring means 90 is not limited to one place as shown in FIG. 1, and may be placed at a plurality of places.

  Here, a method for producing the ice slurry S by the refrigeration system and freezing the article A to be frozen by the ice slurry S will be described. The ice slurry S is manufactured by the ice slurry raw material manufacturing apparatus 200 provided in the ice slurry manufacturing apparatus 1.

  The ice slurry raw material manufacturing apparatus 200 manufactures flake ice in a state where the inner cylinder 32 is cooled by the inner cylinder refrigeration refrigerant. Therefore, the inner cylinder refrigeration refrigerant is supplied from the refrigerant supply unit 39 to the refrigerant clearance 34 and is cooled so that the temperature of the inner peripheral surface of the inner cylinder 32 is lower by about −10 ° C. than the freezing point of the brine to be frozen.

  Under such a condition, the virgin brine stored in the brine storage tank 40, the ice slurry S supplied through the return pipe 44, or a mixture thereof is injected from the injection unit 23 toward the inner cylinder 32. Is done. A portion of the injected brine, ice slurry S, or a mixture thereof adheres to the inner cylinder 32, rapidly freezes without being given time to separate into solute and solvent, and becomes hybrid ice.

  The hybrid ice generated on the inner peripheral surface of the inner cylinder 32 is peeled off by the peeling unit 24 that rotates in the inner cylinder 32. The hybrid ice peeled off by the peeling unit 24 falls into the ice storage tank 500 from the flake ice discharge port 26 and is stored as flake ice. The portion of the sprayed brine, ice slurry S, or mixture thereof that has not been frozen falls from the flake ice discharge port 26 into the ice storage tank 500 and is stored.

  The ice slurry raw material manufacturing apparatus 200 freezes a portion of the brine, ice slurry S, or a mixture thereof injected from the injection unit 23 on the inner peripheral surface of the inner cylinder 32 to form flake ice. The concentration of the flake ice in the ice slurry S falling from the ice 26 into the ice storage tank 500 is the concentration of the flake ice in the ice slurry S before injection (that is, the concentration of the flake ice in the ice slurry S stored in the ice storage tank 500). ) Will be higher.

  The ice slurry S discharged from the ice slurry raw material manufacturing apparatus 200 and the ice slurry S stored in the ice storage tank 500 are mixed by the stirring means 54 and the flakes of the mixed ice slurry S in the ice storage tank 500 are mixed. The ice concentration is kept uniform.

  Therefore, the ice slurry raw material manufacturing apparatus 200 can increase the flake ice concentration of the ice slurry S in the ice storage tank 500 by operating it. The flake ice concentration of the ice slurry S is measured by the first concentration measuring means 55 provided in the return pipe 44 that is a passage for supplying the ice slurry S in the ice storage tank 500 to the injection unit 23 of the ice slurry raw material manufacturing apparatus 200. Is done.

  Moreover, the ice slurry raw material manufacturing apparatus 200 can increase the amount of the ice slurry S in the ice storage tank 500 by operating it. The amount of ice slurry S in the ice storage tank 500 can be increased by supplying virgin brine stored in the brine storage tank 40. The amount of ice slurry S in the ice storage tank 500 is measured by a storage amount sensor 56 provided in the ice storage tank 500.

  The ice slurry raw material manufacturing apparatus 200 is controlled to operate and stop depending on the concentration of the flake ice in the ice slurry S in the ice storage tank 500 and the amount of the ice slurry S. That is, the ice slurry raw material manufacturing apparatus 200 operates when the concentration of the flake ice in the ice slurry S in the ice storage tank 500 is lower than the target concentration, and the concentration of the flake ice in the ice slurry S in the ice storage tank 500 is lower than the target concentration. If it is high, stop temporarily. The ice slurry raw material manufacturing apparatus 200 operates when the amount of the ice slurry S in the ice storage tank 500 is lower than the target value, and temporarily when the amount of the ice slurry S in the ice storage tank 500 is higher than the target value. Stop.

  Further, the ice slurry raw material manufacturing apparatus 200 increases the supply amount of the inner cylinder refrigeration refrigerant from the refrigerant supply unit 39 to the refrigerant clearance 34 as well as the operation or temporary control, and the temperature of the inner peripheral surface of the inner cylinder 32. The amount of hybrid ice generated on the inner peripheral surface of the inner cylinder 32 is increased by lowering or the supply amount of the inner cylinder refrigeration refrigerant from the refrigerant supply unit 39 to the refrigerant clearance 34 is decreased. Control such as decreasing the amount of hybrid ice generated on the inner peripheral surface of the inner cylinder 32 by raising the temperature of the inner peripheral surface of the inner cylinder 32 may be performed.

  The ice slurry S stored in the ice storage tank 500 has (a) a temperature when melting is less than 0 ° C., and (b) a rate of change in the solute concentration of brine in which the ice has melted during the melting process is within 30%. This condition is met. The ice slurry S can take a large amount of latent heat from the surroundings when melting, but the temperature does not rise while the melting ice is not completely completed and the hybrid ice remains.

  The concentration of the flake ice in the ice slurry S in the ice storage tank 500 was measured by the first concentration measuring means 55, and the concentration of the flake ice was adjusted to a predetermined concentration (a predetermined concentration of 10% or more and 60% or less). The ice slurry S is sent from the ice slurry supply pipe 45 into the flow path 60 of the refrigeration apparatus 6. The refrigeration apparatus 6 performs the freezing operation of the article to be frozen A with the ice slurry S sent. The ice slurry S in the ice storage tank 500 is supplied to the refrigeration apparatus 6 through the ice slurry supply pipe 45 and the ice slurry return pipe 46 so as to ensure the cold heat required for the freezing operation of the article A to be frozen.

  The amount of ice slurry S stored in the ice storage tank 500 is measured by the storage amount sensor 56. When it is measured by the storage amount sensor 56 that the amount of ice slurry S in the ice storage tank 500 has decreased, virgin brine is supplied from the brine storage tank 40 to the ice slurry raw material manufacturing apparatus 200, and the ice slurry S is manufactured. Is done.

  When the refrigeration apparatus 6 does not perform a refrigeration operation, for example, when the refrigeration apparatus 6 is at rest, such as at night, if the flake ice concentration of the ice slurry S in the ice storage tank 500 is lower than the target concentration, the ice slurry raw material The manufacturing apparatus 200 manufactures the ice slurry raw material, and the flake ice concentration of the ice slurry S in the ice storage tank 500 is increased. At this time, the on / off valve 45a of the ice slurry supply rod 45 and the on / off valve 46a of the ice slurry return rod 46 may be closed, but the flakes of the ice slurry S of the entire system including the ice storage tank 500 and the refrigeration apparatus 6 are combined. In order to adjust the ice concentration to the target concentration region, it is preferably in an open state.

  Further, as described above, the amount of the ice slurry S stored in the ice storage tank 500 is measured by the storage amount sensor 56, and the ice slurry S until the amount of the ice slurry S in the ice storage tank 500 reaches a predetermined amount. S is manufactured.

  In the refrigerating operation of the product A to be frozen in the refrigeration apparatus 6, the product A to be frozen is arranged in a freezing region 69 provided in a straight line 64 of the flow path 60 through which the ice slurry S circulates. The article A to be frozen is placed on a tray (not shown), and the tray is held in a rack (not shown) with an interval. The plurality of racks are collectively arranged so as to be in series in the straight line 64 of the flow path 60. The product A to be frozen in the rack is immersed in the circulating ice slurry S and is quickly frozen.

  The ice slurry S filled in the flow path 60 is circulated in the flow path 60 with a propulsive force applied by the propulsion means 80. The ice slurry S flows smoothly in the region along the outer wall 66 on the upstream side of the straight line 64 continuous to the curved line 65 by providing the guide vane 70 in the curved line 65 of the water channel, The inside of the annular flow path 60 can be circulated with little resistance.

  When the solute is separated from the ice slurry S flowing through the flow path 60, the solute is collected in a pit provided at the bottom of at least one curved line 65. Therefore, the solute separated from the ice slurry S does not affect the freezing operation.

  Since the ice slurry S has fluidity, it can come into contact with the article to be frozen A more uniformly than the state of hard flake ice. Since the temperature of the ice slurry S is maintained at the melting point while the hybrid ice remains (for example, in the case of the ice slurry S of saturated saline, it is maintained at −21.3 ° C.) Thus, the article A to be frozen can be kept frozen. Moreover, even if the to-be-frozen goods A are foodstuffs, such as a fish, since the ice slurry S is harmless, there is no food safety problem.

  Here, a method for adjusting the concentration of the flake ice in the ice slurry S in the flow path 60 will be described. The ice slurry S circulating in the flow path 60 freezes the product to be frozen A placed in the freezing area 69 (that is, gives cold heat), so that the concentration of the flake ice in the ice slurry S becomes the ice storage tank 500. The concentration may decrease from within.

  Further, in order to quickly grasp the change in the concentration of the flake ice in the ice slurry S in the flow channel 60, a second concentration measuring unit 90 may be provided in the flow channel 60.

  The concentration of the flake ice in the ice slurry S in the flow path 60 measured by the second concentration measuring means 90 is based on the concentration of the flake ice in the ice slurry S in the ice storage tank 500 measured by the first concentration measuring means 55. If it is lower than the predetermined value, it is fed back to the operation of the ice slurry raw material manufacturing apparatus 200, whereby the concentration of the flake ice in the ice slurry S in the flow path 60 can be controlled more precisely.

  Since the ice slurry S thus adjusted in the concentration of flake ice contains a lot of fine voids (ie, air portions) in the state of being produced as flake ice, the voids are exhausted in the hybrid ice. And can be prepared in the form of snow or in the form of a sherbet. Since the hybrid ice prepared in the shape of snow or sherbet has flexibility as a whole, it does not damage the frozen product A, but rather functions as a sponge as a cushioning material to protect the frozen product A Fulfill.

  Moreover, even if the ice slurry S is in a state having many voids (air portions), or even if the voids are filled with brine by melting the ice slurry S, the ice slurry S as a whole As a result, sufficient fluidity (flexibility) can be maintained. For this reason, the ice slurry S can freeze the to-be-frozen goods A more efficiently.

  Here, when the ratio of the volume of the void portion (air portion) to the total volume of the ice slurry S is defined as “void ratio”, the lower the void ratio (that is, the higher the bulk density) is, the cold storage effect. Becomes higher. Therefore, when the ice slurry S is used for the purpose of refrigeration or freezing of fresh food products, the ice slurry S having a high porosity (that is, a low bulk density) is generated. In addition, when using the ice slurry S for the purpose of conveying cold energy, the ice slurry S having a low porosity (ie, a high bulk density) is generated.

  The thermal conductivity of brine (brine) containing salt as a solute is about 0.58 W / m K, but the thermal conductivity of flake ice frozen from brine containing salt as a solute is about 2.2 W / m K. It is. That is, since the thermal conductivity of flake ice (solid) is higher than that of brine (liquid), flake ice (solid) can freeze the item A to be frozen earlier.

  However, if the flake ice (solid) remains, the area in contact with the article A to be frozen will be small. Therefore, the flake ice and brine are mixed to form an ice slurry S, thereby providing fluidity. As a result, flake ice (solid) can be uniformly contacted with the item A to be frozen, and the item A to be frozen can be quickly frozen.

Here, specific numerical values for the bulk density of the ice slurry S are shown. The bulk density that can be defined as the ice slurry S is 0.48 g / cm ^{3 to} 0.78 g / cm ³ . When using ice slurry S for the purpose of freezing of fresh food ^is suitably a bulk density of ^{0.69g / cm 3 ~0.78g / cm 3} .

When using the ice slurry S for the purpose of fresh or chilled ^foodstuffs, it is preferable that a bulk density of ^{0.48g / cm 3 ~0.54g / cm 3} . Also, when using the ice slurry S for the purpose of delivery of cooling energy is the bulk density of ice with saturated brine was further mechanically compressed 0.75g ^/ cm ³ ~0.95g ^/ cm 3 It is good.

  Conventionally, it is known that when a solute is dissolved in a solvent, the freezing point of the aqueous solution becomes lower than the freezing point of the solvent before the solute is dissolved (freezing point depression phenomenon). In other words, ice frozen in an aqueous solution in which a solute such as salt is frozen is frozen at a lower temperature (ie, less than 0 ° C.) than ice in which fresh water (that is, water in which no solute such as salt is dissolved) is frozen. Ice.

  Here, the heat required when ice as a solid changes (melts) into water as a liquid is referred to as “latent heat”. Since this latent heat is not accompanied by a temperature change, the hybrid ice can continue to maintain a stable state at a temperature below the freezing point (0 ° C.) of fresh water at the time of melting. For this reason, the state which stored the cold energy can be maintained.

  In other words, the freezing ability of ice obtained by freezing an aqueous solution in which a solute such as salt is dissolved should be higher than that of ice obtained by freezing fresh water. However, even if an attempt is made to produce ice that is obtained by freezing an aqueous solution in which a solute such as salt is dissolved, the aqueous solution (for example, salt water) is hardly frozen as it is, and fresh water that does not contain a solute (salt etc.). The part of will freeze first.

  For this reason, as a result of freezing an aqueous solution in which a solute such as salt is dissolved, the substance produced is a mixture of ice frozen in fresh water not containing a solute (salt etc.) and a solute (for example, crystals such as salt). End up. Moreover, even if ice with a reduced freezing point (ice frozen with salt water or the like) is produced, the amount is very small and not practical. Thus, although the ice slurry S is [ice] having a freezing point lower than the freezing point (0 ° C.) of fresh water, it can be manufactured by a flake ice manufacturing system.

  The ice slurry S satisfies the condition (a) that the temperature at the completion of melting is less than 0 ° C. as described above. Since the ice slurry S is an aqueous solution (salt water or the like) containing a solute (salt etc.), the freezing point of the ice slurry S is lower than the freezing point of fresh water in which the solute is not dissolved. For this reason, the ice slurry S satisfies the condition that the temperature at the completion of melting is less than 0 ° C.

  The “temperature at the time of completion of melting” means that the ice slurry S is melted by placing the ice slurry S in an environment higher than the melting point (for example, room temperature and atmospheric pressure), and all the ice slurries S are melted. The temperature of the aqueous solution at the time when the aqueous solution (brine) is reached.

  On the other hand, it may be preferable to bring the freezing point of the ice slurry S closer to the freezing point of the article A to be frozen. For example, when there is a reason for preventing damage to fresh animals and plants, it is preferable that the temperature at the completion of melting is not too high, for example, −21 ° C. or higher (−20 ° C. or higher, −19 ° C. or higher, −18 ° C or higher, -17 ° C or higher, -16 ° C or higher, -15 ° C or higher, -14 ° C or higher, -13 ° C or higher, -12 ° C or higher, -11 ° C or higher, -10 ° C or higher, -9 ° C or higher, -8 Or higher, −7 ° C. or higher, −6 ° C. or higher, −5 ° C. or higher, −4 ° C. or higher, −3 ° C. or higher, −2 ° C. or higher, −1 ° C. or higher, −0.5 ° C. or higher. preferable.

  The ice slurry S satisfies the condition (b) that the rate of change in the solute concentration of the aqueous solution in which the ice has melted during the melting process is within 30%. The ice slurry S has a feature that the rate of change in the solute concentration of the aqueous solution in which the ice has melted in the melting process (hereinafter, sometimes referred to as “rate of change in solute concentration” in this specification) is within 30%. . Even when using a conventional technique, ice with a slightly reduced freezing point may be produced, but most of it is only a mixture of water-free ice and solute crystals. Therefore, the refrigerating capacity is not sufficient.

  Thus, in the case of a mixture of ice freezing solute-free water and solute crystals, the rate at which the solute elutes with melting becomes unstable when the ice is placed under melting conditions. . Specifically, the closer to the start of melting, the more solute elutes. As the melting progresses, the amount of solute eluting decreases. That is, the closer to the completion of melting, the smaller the amount of solute elution.

  On the other hand, hybrid ice is ice obtained by freezing an aqueous solution containing a solute, and therefore has a feature that there is little change in the elution rate of the solute during the melting process. Specifically, the change rate of the solute concentration of the aqueous solution in which the hybrid ice is melted in the process of melting the hybrid ice is 30%. Here, “the rate of change in the solute concentration of the aqueous solution in which the hybrid ice melted during the melting process” means the ratio of the concentration of the aqueous solution at the completion of melting to the solute concentration in the aqueous solution melted at an arbitrary timing in the melting process. . The “solute concentration” means the ratio of the mass of the solute dissolved in the aqueous solution.

  The change rate of the solute concentration in the hybrid ice is not particularly limited as long as it is within 30%. However, the smaller the change rate, the higher the purity of the hybrid ice, that is, the higher the freezing ability.

  Since the hybrid ice is excellent in refrigerating capacity, it is suitable for use as a refrigerant for freezing and freezing the article A to be frozen. As a low-temperature refrigerant | coolant which freezes the to-be-frozen goods A, the organic solvent used as antifreeze liquids, such as ethanol, is mentioned besides hybrid ice. However, hybrid ice has higher thermal conductivity and higher specific heat than these antifreezes. For this reason, hybrid ice is useful in that it has a higher refrigerating capacity than other refrigerants of less than 0 ° C. such as antifreeze.

  Although the embodiments of the present invention have been described above, the present invention is not limited to the configurations described in the above-described embodiments, and is considered within the scope of the matters described in the claims. Other embodiments and modifications are also included. Further, various modifications and combinations of the above embodiments may be made within the scope not departing from the gist of the present invention.

  As indicated by the phantom line in FIG. 1, the refrigeration system may connect the second ice slurry return pipe 47 that discharges the ice slurry S in the flow path 60 to the ice slurry raw material manufacturing apparatus 200. The downstream end of the second ice slurry return pipe 47 may be connected to a switching valve 43 between the brine pipe 41 and the return pipe 44. However, the switching valve 43 in this case includes three input ports and one output port.

  The refrigeration system in the embodiment described above includes the first concentration measuring unit 55 in the ice storage tank 500 and the second concentration measuring unit 90 in the flow path 60. However, the density measuring means 55 and 90 may be provided with only one or may not be provided.

  The ice slurry raw material manufacturing apparatus 200 in the embodiment described above includes the drum 21 having the inner cylinder 32. However, the ice slurry raw material manufacturing apparatus 200 may be configured by a plate having a flat surface on which the ice slurry S returned from the brine or the return pipe 44 is jetted. A refrigerant clearance is provided on the inner surface of the plate.

  As indicated by the phantom line in FIG. 1, the refrigeration system may connect the second ice slurry return pipe 47 that discharges the ice slurry S in the flow path 60 to the ice slurry raw material manufacturing apparatus 200. The downstream end of the second ice slurry return pipe 47 may be connected to a switching valve 43 between the brine pipe 41 and the return pipe 44. However, the switching valve 43 in this case includes three input ports and one output port. The upstream ends of the return pipe 44, the ice slurry return pipe 46, and the second ice slurry return pipe 47 may be provided with a filter (not shown).

  The refrigeration system in the embodiment described above includes the first concentration measuring means 55 in the bypass pipe provided in the return pipe 44 and the second concentration measuring means 90 in the flow path 60. However, the density measuring means 55 and 90 may be provided with only one or may not be provided.

  Further, the first concentration measuring means 55 may be provided in the ice storage tank 500. The concentration measuring means 55 in this case includes a thermometer, a densitometer, and a density meter, and calculates the concentration of the flake ice from electrical signals of temperature, concentration, and density measured from these meters. The first concentration measuring means 55 may be fixed to the inner surfaces of the two wall surface portions 52 on the bottom surface portion 51 side and the top surface portion 53 side. Even if the concentration of the flake ice is uneven in the ice storage tank 500, the average concentration of the flake ice can be detected by the respective first concentration measuring means 55.

  In the embodiment described above, the ice slurry raw material manufacturing apparatus 200 is activated or stopped depending on the concentration of the flake ice in the ice slurry S in the ice storage tank 500 and the amount of the ice slurry S. However, the concentration of flake ice may be adjusted by changing the temperature of the inner peripheral surface of the inner cylinder of the ice slurry raw material manufacturing apparatus 200.

  For example, when the concentration of flake ice is high, the supply amount of the inner cylinder refrigeration refrigerant from the refrigerant supply unit 39 to the refrigerant clearance 34 is decreased, and the temperature of the inner peripheral surface of the inner cylinder 32 is increased. Alternatively, the virgin brine supplied from the brine storage tank 40 to the injection unit 23 is reduced or heated. As a result, the amount of brine attached to the inner peripheral surface of the inner cylinder 32 decreases, and the brine falling into the ice storage tank 500 increases. When the hybrid ice adhering to the inner peripheral surface of the inner cylinder 32 decreases, the flake ice generated by peeling off the hybrid ice decreases. Due to the reduced flake ice and increased brine, the ice slurry S has a reduced flake ice concentration.

  Conversely, when the concentration of flake ice is low, the supply amount of the inner cylinder refrigeration refrigerant from the refrigerant supply unit 39 to the refrigerant clearance 34 is increased, and the temperature of the inner peripheral surface of the inner cylinder 32 is lowered. Alternatively, the amount of virgin brine supplied from the brine storage tank 40 to the injection unit 23 is increased or lowered. Then, the amount of brine attached to the inner peripheral surface of the inner cylinder 32 increases, and the brine falling into the ice storage tank 500 decreases. When the hybrid ice adhering to the inner peripheral surface of the inner cylinder 32 increases, flake ice generated by peeling off the hybrid ice increases. Due to the increased flake ice and the decreased brine, the ice slurry S has an increased flake ice concentration.

  The ice storage tank 500 in the above-described embodiment includes the stirring means 54. However, the ice storage tank 500 may include the flake ice and the cooled brine by rotating or vibrating the ice storage tank 500 itself without providing the stirring means 54.

  Although the to-be-frozen product A in the above-described embodiment is a food or the like, it may be a medicine or the like.

In summary, the ice slurry manufacturing apparatus 1 to which the present invention is applied only needs to have the following configuration, and can take various embodiments.
That is, the ice slurry manufacturing apparatus 1 to which the present invention is applied is
An ice slurry raw material production unit (ice slurry raw material production apparatus) 200 that generates flake ice from a part of the supplied brine and cools the remainder of the supplied brine;
The flake ice generated by the ice slurry raw material manufacturing unit (ice slurry raw material manufacturing apparatus) 200 and the cooled brine are supplied, and the ice slurry obtained by mixing the flake ice and the cooled brine is stored. An ice storage tank 500,
Is provided.

  As a result, the ice slurry production apparatus 1 produces flake ice from a part of the brine in the ice slurry raw material production unit (ice slurry raw material production apparatus) 200, the remaining part of the brine is cooled, and the flake ice and brine are stored in ice. By storing in the tank 500, the ice slurry S can be manufactured.

One aspect of the ice slurry manufacturing apparatus 1 to which the present invention is applied is as follows.
A return pipe 400 that returns the brine in the ice slurry S in the ice storage tank 500 as raw water to the ice slurry raw material manufacturing unit (ice slurry raw material manufacturing apparatus) 200;
Is provided.
Thereby, the brine in the ice slurry S stored in the ice storage tank 500 is returned to the ice slurry raw material manufacturing unit (ice slurry raw material manufacturing apparatus) 200 as a recycled brine and can be reused.

One aspect of the ice slurry manufacturing apparatus 1 to which the present invention is applied is as follows.
A stirring portion (stirring means) 54 for stirring the ice slurry S in the ice storage tank 500;
Is provided.
The ice slurry manufacturing apparatus 1 is provided with a stirring unit (stirring means) 54, so that the flake ice stored in the ice storage tank 500 and the brine are mixed to manufacture the ice slurry S in which the flake ice and the brine are made uniform. can do.

One aspect of the ice slurry manufacturing apparatus 1 to which the present invention is applied is as follows.
The ice slurry raw material production unit (ice slurry raw material production apparatus) 200 includes a drum 21 having a refrigerant clearance 34, a refrigerant supply unit 39 that supplies an inner cylinder refrigeration refrigerant to the refrigerant clearance 34,
Is provided.
As a result, the ice slurry raw material production unit (ice slurry raw material production device) 200 easily controls the temperature of the drum 21 by supplying the inner cylinder refrigeration refrigerant from the refrigerant supply unit 39 to the refrigerant clearance 34 of the drum 21. The ratio of the flake ice to be produced and the brine to be cooled can be easily adjusted.

The refrigeration system to which the present invention is applied,
An ice slurry manufacturing apparatus 1 to which the present invention is applied;
A refrigeration apparatus 6 for freezing the article to be frozen with the ice slurry S;
Comprising
A refrigeration system,
The refrigeration apparatus 6 includes:
An annular flow path 60 through which the ice slurry circulates, and includes two parallel straight lines 64 and two curved lines 65 that connect adjacent ends of the two straight lines 64. A flow path 60 having
A propulsion unit 80 for imparting propulsive force to the ice slurry;
A guide vane 70 that divides at least one of the curved lines 65 into a plurality of lanes;
Is provided.

  As a result, the refrigeration system is good in that the ice slurry S produced by the ice slurry production means 1 flows in the flow path 60 and the article A to be frozen placed in the flow path 60 is wrapped by the ice slurry S. Can be frozen.

1: Ice slurry manufacturing apparatus, 200: Ice slurry raw material manufacturing apparatus (ice slurry raw material manufacturing section), 21: Drum, 22: Rotating shaft, 23: Injection section, 23a: Injection hole, 24: Stripping section, 25: Blade , 26: flake ice discharge port, 27: upper bearing member, 28: injection control section, 29: heat protection cover, 30: geared motor, 31: rotary joint, 32: inner cylinder, 33: outer cylinder, 34: refrigerant clearance , 38: bush, 39: refrigerant supply section, 40: brine storage tank, 41: brine pipe, 42: refrigerant pipe, 44: return pipe, 45: ice slurry supply pipe, 46: ice slurry return pipe, 47: second Ice slurry return pipe, 48: nozzle, 500: ice storage tank, 54: stirring means (stirring section), 55: concentration measuring section (first concentration measuring means), 6: refrigeration apparatus, 60: 61, supply port, 62: discharge port (first discharge port), 63: second discharge port, 64: straight line, 65: curved line, 67: partition part, 68: bottom surface part, 69: freezing Area: 70: Guide vane, 80: Propulsion means (propulsion unit), 90: Second concentration measurement means, A: Product to be frozen, S: Ice slurry

Claims (5)

An ice slurry raw material production unit that generates flake ice from a part of the supplied brine and cools the remainder of the supplied brine;
An ice storage tank for storing an ice slurry in which the flake ice generated by the ice slurry raw material production unit and the cooled brine are supplied and the flake ice and the cooled brine are mixed;
Comprising
Ice slurry production equipment. A return pipe that returns the brine in the ice slurry in the ice storage tank to the ice slurry raw material production unit as raw water,
Comprising
The ice slurry manufacturing apparatus according to claim 1. A stirring unit for stirring the ice slurry in the ice storage tank;
Comprising
The ice slurry manufacturing apparatus according to claim 1 or 2. The ice slurry raw material production unit includes a drum having a refrigerant clearance, a refrigerant supply unit that supplies an inner cylinder refrigeration refrigerant to the refrigerant clearance,
Comprising
The ice slurry manufacturing apparatus according to any one of claims 1 to 3. The ice slurry manufacturing apparatus according to any one of claims 1 to 4,
A refrigeration apparatus for freezing the article to be frozen with the ice slurry;
Comprising
A refrigeration system,
The refrigeration apparatus is
An annular flow path through which the ice slurry circulates, the flow path having two parallel straight lines and two curved lines connecting adjacent ends of the two straight lines; ,
A propulsion unit that provides propulsion to the ice slurry;
A guide vane that divides at least one of the curved lines into a plurality of lanes;
Comprising
Refrigeration system.

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