WO2017086462A1

WO2017086462A1 - Ice making device, moving body, flake ice production device, and flake ice production method

Info

Publication number: WO2017086462A1
Application number: PCT/JP2016/084320
Authority: WO
Inventors: 美雄廣兼; 知昭秋山; 伊朗井筒
Original assignee: ブランテック株式会社
Priority date: 2015-11-19
Filing date: 2016-11-18
Publication date: 2017-05-26
Also published as: CA3004245A1; CA3004245C; MY187613A; TWI747517B; TW202110330A; WO2017086461A1; WO2017086463A1; WO2017086464A1

Abstract

Provided is a means for more efficiently generating ice which has a high cooling capacity. A flake ice production device 10 generates ice by cooling the wall surface of an inner cylinder 22 and freezing brine that has adhered to the wall surface of the cooled inner cylinder 22. A spraying unit 13 supplies brine to the wall surface of the inner cylinder 22 by causing the brine to adhere thereto. A stripping unit 14 collects the ice generated on the wall surface of the inner cylinder 22. In addition, the flake ice production device 10 is designed such that formula (1) is satisfied when Y represents an ice making speed indicating the amount of ice generated on the wall surface of the inner cylinder 22 per unit time, and x1 represents the thermal conductance rate of the wall surface of the inner cylinder 22. Formula (1): Y = f(x1) .

Description

Ice making device, moving body, flake ice production device, flake ice production method

The present invention relates to an ice making device, a moving body, a flake ice production device, and a flake ice production method.

Conventionally, as a technique for maintaining the freshness of animals and plants such as fresh seafood or parts thereof, a technique of cooling animals and plants such as fresh seafood or parts thereof with ice water has been used. However, in the case of ice made from fresh water, when the ice melts, the solute concentration of seawater used for maintaining freshness decreases. As a result, due to osmotic pressure, there is a problem that water enters the body of the animal or plant immersed in water ice or the portion thereof, and the freshness or the like falls.

Therefore, in Patent Document 1, in a salt-containing water ice making method in which salt-containing ice obtained by freezing salt-containing water having a solute concentration of approximately 0.5 to 2.5% is formed into a slurry, filtration is performed. Sterilized raw water, such as seawater, is adjusted to a salt content to obtain a salt-containing water having a solute concentration of about 1.0 to 1.5%, and the salt-containing water is rapidly cooled to cope with the solute concentration- A method is disclosed for producing slurry-like salt-containing ice having a freezing point temperature of 5 to -1 ° C.
However, in the conventional techniques including Patent Document 1, water in fresh seafood crystallizes when frozen, but since ice crystals in fresh seafood become large, the cellular structure of fresh seafood is destroyed, and freshness and taste are reduced. There is a problem that it cannot be maintained.
In addition, ice frozen in salt water begins to freeze from the fresh water portion with a high freezing point, and a portion where a small amount of salt water has frozen or salt deposited around the ice adheres to the portion that will eventually freeze. As a result, the solute concentration of ice becomes uneven. At the time of thawing, the part that was finally frozen thaws first, and high-concentration salt water comes out, so that the solute concentration in the melted water changes significantly during the melting process, or the temperature goes to 0 ° C. There was a technical problem of rising.
Therefore, the present applicant has already filed a patent application for an apparatus for producing flake ice that is excellent in cooling ability and can maintain a state in which it is not separated for a long time (Japanese Patent Application No. 2016-103637).

JP 2002-115945 A

However, in the ice making device including the flake ice manufacturing device for which a patent application has been filed by the present applicant, there has been a demand for realizing a technology that can generate ice with high cooling ability more efficiently.

The present invention has been made in view of such a situation, and an object of the present invention is to provide a technique for generating ice with higher efficiency and higher cooling ability.

In order to achieve the above object, an ice making device of one embodiment of the present invention includes:
An ice making surface, and a cooling unit that cools the ice making surface; and an ice making unit that generates ice by freezing brine attached to the cooled ice making surface;
A brine supply unit for supplying the brine by attaching the brine to the ice making surface;
A recovery unit for recovering the ice generated by the ice making unit;
With
In the ice making section, when the ice making speed indicating the amount of ice produced per unit time is Y and the thermal conductivity of the ice making surface is x1, the following equation (1) is established.
Y = f (x1) (1)

Also,
The thermal conductivity of the ice making surface at 20 ° C. can be 70 W / mK or more.

Further, when the ice making speed is Y and the area of the ice making surface where the brine may be attached is x2, the following equation (2) can be established.
Y = f (x2) (2)

The cooling unit further includes a refrigerant supply unit that supplies a predetermined refrigerant to cool the ice making surface.
When the ice making speed is Y and the temperature of the ice making surface is x3, the following equation (3) can be established.
Y = f (x3) (3)

The brine supply unit
The brine can be deposited by spraying onto the ice making surface.

The brine supply unit
The brine can be adhered to the ice making surface by naturally flowing down.

Also, the thermal conductivity at 20 ° C. of the ice making surface can be configured to be 70 W / mK or more.

Further, the refrigerant can be LNG.

In addition, the ice making part
Further comprising a liner covering the ice making surface,
The liner can be replaceable.

The flake ice manufacturing apparatus of one aspect of the present invention includes the ice making unit, the brine supply unit, and the recovery unit,
The ice making part is
A drum including an inner cylinder having the ice making surface, an outer cylinder surrounding the inner cylinder, a clearance formed between the inner cylinder and the outer cylinder, and a refrigerant that supplies refrigerant to the clearance And further comprising a supply unit,
The brine supply unit
A rotation unit that rotates around a central axis of the drum, and further includes an injection unit that injects the brine toward the ice making surface of the inner cylinder;
The collection unit
The brine jetted from the jetting unit is further attached to the inner surface of the inner cylinder cooled by the refrigerant supplied to the clearance, and further comprises a stripping unit for stripping off the ice generated as a result,
In the ice making section, when the production rate indicating the amount of ice produced per unit time is Y and the thermal conductivity of the ice making surface is x1, the above equation (1) is established. it can.

Further, the thermal conductivity of the ice making surface at 20 ° C. can be 70 W / mK or more.

Further, when the ice making speed is Y and the area of the ice making surface where the brine may be attached is x2, the above equation (2) can be established.

Further, when the ice making speed is Y and the temperature of the ice making surface is x3, it can be designed so that the above formula (3) is established.

Further, the refrigerant can be LNG.

Moreover, the flake ice manufacturing apparatus of one embodiment of the present invention can be mounted on a moving body.

According to the present invention, it is possible to provide a method of generating ice with higher efficiency and higher cooling ability.

It is an image figure containing the partial cross section perspective view which shows the outline | summary of the flake ice manufacturing apparatus which concerns on one Embodiment of the ice making apparatus of this invention. It is a figure which shows the heat conductivity for every member used for the ice making surface of the flake ice manufacturing apparatus of FIG. It is an image figure which shows the outline | summary of the whole flake ice manufacturing system containing the flake ice manufacturing apparatus of FIG.

<Ice>
The ice produced by the ice making device of the present invention is liquid ice containing an aqueous solution containing a solute that satisfies the following conditions (a) and (b). “Flake ice” refers to ice processed into flakes.
(A) The temperature at the completion of melting is less than 0 ° C. (b) The change rate of the solute concentration of the aqueous solution generated from the ice during the melting process is within 30%.

It is known that when a solute is melted in water, a freezing point depression occurs in which the freezing point of the aqueous solution is lowered. The freezing point of an aqueous solution in which a solute such as sodium chloride has been melted due to the action of lowering the freezing point is lowered. That is, ice made of such an aqueous solution is ice that has solidified at a lower temperature than ice made of fresh water.
Here, the heat required when ice changes to water is referred to as “latent heat”, but this latent heat is not accompanied by a temperature change. Due to the effect of such latent heat, the ice having a reduced freezing point as described above continues to be stable at a temperature below the freezing point of fresh water when melted, so that the state where cold energy is stored continues.
Therefore, the cooling ability of the object to be cooled should be higher than that of ice made of fresh water. However, the present inventors have found that the ice produced by the conventional technique does not have sufficient ability to cool the object to be cooled, such as the temperature of the ice rising rapidly with time. The present inventors examined the reason, and even if ice was produced from an aqueous solution containing a solute such as salt in the conventional technique, in practice, ice containing no solute was first produced before the aqueous solution was frozen. As a result, a mixture of ice and solute containing no solute is produced, or only a small amount of ice having a reduced freezing point is produced, so that ice with high cooling capacity is not produced. I found out.

However, the present inventors have succeeded in inventing an ice making device capable of producing liquid ice containing an aqueous solution having a reduced freezing point by a predetermined method (details will be described later). The ice produced by such an ice making device of the present invention satisfies the above conditions (a) and (b). Hereinafter, the above conditions (a) and (b) will be described.

(Temperature at the completion of melting)
Regarding the above (a), since the ice produced by the ice making device of the present invention is liquid ice containing an aqueous solution containing a solute, the temperature of the freezing point is lower than the freezing point of fresh water (water containing no solute). . Therefore, it has the characteristic that the temperature at the time of completion of melting is less than 0 ° C. “Temperature at the completion of melting” means that the ice produced by the ice making apparatus of the present invention is placed in an environment above the melting point (for example, room temperature and atmospheric pressure) to start melting of the ice. It refers to the temperature of water when it melts into water.

The temperature at the completion of melting is not particularly limited as long as it is less than 0 ° C., and can be appropriately changed by adjusting the kind and concentration of the solute. The temperature at the completion of melting is preferably lower in terms of higher cooling ability, and specifically, -1 ° C or lower (-2 ° C or lower, -3 ° C or lower, -4 ° C or lower, -5 ° C or lower, -6 ° C or lower, -7 ° C or lower, -8 ° C or lower, -9 ° C or lower, -10 ° C or lower, -11 ° C or lower, -12 ° C or lower, -13 ° C or lower, -14 ° C or lower, -15 Or less, −16 ° C. or less, −17 ° C. or less, −18 ° C. or less, −19 ° C. or less, −20 ° C. or less, and the like. On the other hand, it may be preferable to bring the freezing point closer to the freezing point of the object to be cooled (for example, to prevent damage to fresh animals and plants). In such a case, it is preferable that the temperature at the completion of thawing is not too high. Preferably, 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 ° C 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, etc.).

(Change rate of solute concentration)
Regarding the above (b), the ice produced by the ice making apparatus of the present invention is the rate of change in the solute concentration of the aqueous solution generated from the ice during the melting process (hereinafter referred to as the “rate of change in solute concentration” in this specification). Is) within 30%. Even with the conventional technique, ice having a slightly reduced freezing point may be generated, but most of them are a mixture of water-free ice and solute crystals, so that the cooling capacity is not sufficient. When there is a large mixture of ice and solute crystals of water that does not contain solute in this way, when the ice is placed under melting conditions, the elution rate of the solute accompanying melting is unstable, The more the solute is eluted, the more the solute is eluted, the less the amount of the solute is eluted. On the other hand, the ice produced by the ice making device of the present invention is composed of liquid ice containing 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 generated from ice during the melting process is 30%. The “rate of change in the solute concentration of an aqueous solution generated from ice 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 generated at an arbitrary point in the melting process. The “solute concentration” means the concentration of the mass of the solute in the aqueous solution.

The rate of change of the solute concentration in the ice produced by the ice making apparatus of the present invention is not particularly limited as long as it is within 30%, but the smaller the rate of change, the higher the purity of the ice of the aqueous solution with a reduced freezing point, that is, This means that the cooling capacity is high. From this viewpoint, the change rate of solute concentration is within 25% (within 24%, within 23%, within 22%, within 21%, within 20%, within 19%, within 18%, within 17%, within 16%. Within 15%, within 14%, within 13%, within 12%, within 11%, within 10%, within 9%, within 8%, within 7%, within 6%, within 5%, within 4%, 3 %, Within 2%, within 1%, within 0.5%, etc.). On the other hand, the change rate of the solute concentration is 0.1% or more (0.5% or more, 1% or more, 2% or more, 3% or more, 4% or more, 5% or more, 6% or more, 7% or more, 8 % Or more, 9% or more, 10% or more, 11% or more, 12% or more, 13% or more, 14% or more, 15% or more, 16% or more, 17% or more, 18% or more, 19% or more, 20% or more Etc.).

(Solute)
The type of solute contained in the ice produced by the ice making apparatus of the present invention is not particularly limited as long as it is a solute when water is used as a solvent, and is appropriately selected depending on the desired freezing point, the intended use of the ice to be used, etc. can do. Examples of the solute include solid solutes and liquid solutes, and typical solid solutes include salts (inorganic salts, organic salts, etc.). Particularly, among salts, sodium chloride (NaCl) is preferable because it does not excessively lower the temperature of the freezing point and is suitable for cooling fresh animals and plants or a part thereof. Moreover, since salt is contained in seawater, it is also preferable 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.

The concentration of the solute contained in the ice produced by the ice making apparatus of the present invention is not particularly limited, and can be appropriately selected according to the kind of solute, the desired freezing point, the use of the ice to be used, and the like. For example, when sodium chloride is used as the solute, the concentration of the sodium chloride is 0.5% (w / v) or more (1% (w / v) in that the freezing point of the aqueous solution can be further lowered to obtain a high cooling capacity. v) or more, 2% (w / v) or more, 3% (w / v) or more, 4% (w / v) or more, 5% (w / v) or more, 6% (w / v) or more, 7 % (W / v) or more, 8% (w / v) or more, 9% (w / v) or more, 10% (w / v) or more, 11% (w / v) or more, 12% (w / v) ), 13% (w / v) or more, 14% (w / v) or more, 15% (w / v) or more, 16% (w / v) or more, 17% (w / v) or more, 18% (W / v) or more, 19% (w / v) or more, 20% (w / v) or more, etc.). On the other hand, when the ice produced by the ice making apparatus of the present invention is used for cooling fresh animals or plants or a part thereof, it is preferable not to excessively reduce the temperature of the freezing point. From this viewpoint, 23% (w / v) or less (20% (w / v) or less, 19% (w / v) or less, 18% (w / v) or less, 17% (w / v) or less, 16% (w / v) or less, 15 % (W / v) or less, 14% (w / v) or less, 13% (w / v) or less, 12% (w / v) or less, 11% (w / v) or less, 10% (w / v ), 9% (w / v) or less, 8% (w / v) or less, 7% (w / v) or less, 6% (w / v) or less, 5% (w / v) or less, 4% (W / v) or less, 3% (w / v) or less, 2% (w / v) or less, 1% (w / v) or less, etc.).

Since the ice produced by the ice making apparatus of the present invention is excellent in cooling ability, it is suitable for use as a refrigerant for cooling an object to be cooled. Examples of the low-temperature refrigerant for cooling the object to be cooled include organic solvents used as an antifreeze liquid such as ethanol in addition to ice, but ice has higher thermal conductivity and higher specific heat than these antifreeze liquids. For this reason, ice having a low freezing point by dissolving a solute such as ice produced by the ice making apparatus of the present invention is superior in cooling ability to other refrigerants of less than 0 ° C. such as antifreeze. Useful.

The ice produced by the ice making apparatus of the present invention may or may not contain components other than the above solute.

In the present invention, “ice” refers to a frozen liquid containing an aqueous solution.

Also, since the ice produced by the ice making device of the present invention continues to be stable at a temperature below the freezing point of fresh water, that is, it can be kept in a state where it is not separated for a long time. Therefore, for example, as described later, when the liquid constituting the ice produced by the ice making device of the present invention is a liquid containing oil in addition to the aqueous solution containing the solute, the oil is uniform. The state lasts for a long time, that is, the state that does not separate can be maintained for a long time.

As described above, the liquid constituting the ice produced by the ice making device of the present invention may be a liquid containing oil in addition to the aqueous solution containing the solute. Examples of such liquids include raw milk and industrial waste (such as waste milk) containing water and oil. When the liquid is raw milk, it is preferable in terms of improving the functionality when eating the ice. Thus, it is estimated that the reason why the functionality is improved is that oil (fat) contained in raw milk is confined in ice. In addition, you may comprise the ice produced | generated by the ice making apparatus of this invention only from what frozen the aqueous solution containing said solute.

When the liquid constituting the ice produced by the ice making device of the present invention further contains oil, the ratio of water to oil in the liquid is not particularly limited, and is, for example, 1:99 to 99: 1 (10:90). To 90:10, 20:80 to 80:20, 30:80 to 80:30, 40 to 60:40 to 60, etc.).

Further, the ice produced by the ice making apparatus of the present invention may be an aqueous ice containing two or more solutes having different freezing point depression degrees. In this case, the ice produced by the ice making apparatus of the present invention may be a mixture of ice of an aqueous solution containing one solute and ice of an aqueous solution containing the other solute. In such a case, for example, by adding ice of an aqueous solution containing sodium chloride as a solute having a different freezing point depression degree from that of ethylene glycol to ice of an aqueous solution containing ethylene glycol as a solute, melting of the ice of the aqueous solution containing ethylene glycol can be delayed. it can. Or the ice produced | generated by the ice making apparatus of this invention may be the ice of the aqueous solution which melt | dissolved 2 or more types of solutes in the same aqueous solution. Further, when two or more kinds of solutes having different degrees of freezing point depression are used in combination, it is also useful for lowering the melting point of ice of an aqueous solution containing the target solute. For example, when salt is used as the solute, the melting point of the ice in the salt solution can be lowered by using a solute (ethylene glycol, calcium chloride, etc.) that can lower the melting point further than the salt. A temperature around -30 ° C that cannot be achieved with ice alone can be achieved. The ratio of two or more solutes having different freezing point depression degrees can be appropriately changed according to the purpose.

(Refrigerant that cools the object to be cooled)
The ice produced by the ice making device of the present invention can be used as a refrigerant for cooling the object to be cooled. As described above, the ice produced by the ice making device of the present invention is excellent in cooling ability, and thus is suitable as a refrigerant for cooling an object to be cooled.
In order to prevent confusion between the refrigerant for cooling the object to be cooled and the refrigerant for cooling the inner cylinder 22 (see FIG. 1), the refrigerant for cooling the object to be cooled is hereinafter referred to as “ice slurry”. Call it. The ice slurry is a mixture of ice produced by the ice making device of the present invention and a liquid containing an aqueous solution.

The ice slurry containing the ice produced by the ice making device of the present invention may contain other components of the above ice, for example, a mixture of ice and water by containing water in addition to the above ice. May be. For example, when it further contains water containing the same solute as that contained in ice, the solute concentration in ice and the solute concentration in water are preferably close. The reason is as follows.

When the solute concentration of ice is higher than the solute concentration of water, the temperature of the ice is lower than the saturation freezing point of water, so that water freezes immediately after mixing water with a low solute concentration. On the other hand, when the solute concentration of ice is lower than the solute concentration of water, the saturated freeze point of water is lower than the saturated freeze point of ice, so the ice melts and the temperature of the ice slurry consisting of a mixture of ice and water decreases. To do. That is, in order not to change the state of the mixture of ice and water (the state of the ice slurry), it is preferable that the solute concentrations of the ice and water to be mixed are approximately the same as described above. In the case of a mixture of ice and water, the water may be one obtained by melting the ice, or one prepared separately, but one obtained by melting the ice. It is preferable that

Specifically, when the ice slurry containing ice produced by the ice making apparatus of the present invention is composed of a mixture of ice and water, the ratio of the solute concentration in ice to the solute concentration in water is 75. : 25 to 20:80 is more preferable, 70:30 to 30:70 is further preferable, 60:40 to 40:60 is still more preferable, and 55:45 to 45:55 is used. Even more preferably, it is particularly preferably 52:48 to 48:52, and most preferably 50:50. In particular, when salt is used as the solute, the ratio of the solute concentration in ice to the solute concentration in water is preferably within the above range.

The water that is the raw material of ice produced by the ice making device of the present invention is not particularly limited, but when using salt as a solute, it is ice of seawater, water obtained by adding salt to seawater, or seawater dilution water. It is preferable. Seawater, water obtained by adding salt to seawater, or seawater-diluted water can be easily procured, thereby reducing costs.

The ice slurry containing ice produced by the ice making device of the present invention may further contain a solid having a higher thermal conductivity than the ice produced by the above ice making device of the present invention. However, it is preferable to contain. When trying to cool an object to be cooled in a short time, it can be achieved by using a solid with high thermal conductivity, but in this case, the solid itself also loses cold energy in a short time and the temperature tends to rise. Not suitable for long-time cooling. On the other hand, although not using a solid with high thermal conductivity is suitable for long-time cooling, it is not suitable for cooling an object to be cooled in a short time. However, since the ice produced by the ice making apparatus of the present invention has a high cooling capacity as described above, it is possible to cool for a long time while obtaining a cooling capacity for a short time by a solid having high thermal conductivity. Useful. Examples of solids having higher thermal conductivity than ice produced by the ice making apparatus of the present invention include metals (aluminum, silver, copper, gold, duralumin, antimony, cadmium, zinc, tin, bismuth, tungsten, titanium, iron , Lead, nickel, platinum, magnesium, molybdenum, zirconium, beryllium, indium, niobium, chromium, cobalt, iridium, palladium), alloy (steel (carbon steel, chromium steel, nickel steel, chromium nickel steel, silicon steel, tungsten steel) , Manganese steel, etc.), nickel-chromium alloy, aluminum bronze, gunmetal, brass, manganin, silver, constantan, solder, alumel, chromel, monel metal, platinum iridium, etc.), silicon, carbon, ceramics (alumina ceramics, forsterite ceramics, steer) tight La mix, etc.), marble, brick (magnesia bricks, a Col Hult bricks, etc.) and the like, can be mentioned those having a higher thermal conductivity than generated ice by the ice making apparatus of the present invention. In addition, the solid having higher thermal conductivity than ice produced by the ice making apparatus of the present invention has a thermal conductivity of 2.3 W / m K or more (3 W / m K or more, 5 W / m K or more, 8 W / m K. Etc.), preferably a solid having a thermal conductivity of 10 W / m K or more (20 W / m K or more, 30 W / m K or more, 40 W / m K or more, etc.) It is more preferable that it is a solid having a conductivity of 50 W / m K or more (60 W / m K or more, 75 W / m K or more, 90 W / m K or more, etc.), and a thermal conductivity of 100 W / m K or more (125 W / m K or more, 150 W / m K or more, 175 W / m K or more) is more preferable, and the thermal conductivity is 200 W / m K or more (250 W / m K or more, 300 W / m K or more, 350 W / m K And the like, more preferably a solid having a thermal conductivity of 200 W / m K or more, and a solid having a thermal conductivity of 400 W / m K or more (410 W / m K or more). It is particularly preferred.

When the ice slurry containing ice produced by the ice making apparatus of the present invention contains a solid having a higher thermal conductivity than the above-described ice of the present invention, as described above, even if it contains many solids, it is cooled for a long time. For example, the mass of ice produced by the ice making device of the present invention contained in the mass / ice slurry of solids having a higher thermal conductivity than the ice produced by the ice making device of the present invention (or The total mass of the ice of the present invention and the liquid containing the aqueous solution is 1 / 100,000 or more (1/50000 or more, 1/10000 or more, 1/5000 or more, 1/1000 or more, 1/500 or more, 1 / 100 or more, 1/50 or more, 1/10 or more, 1/5 or more, 1/4 or more, 1/3 or more, 1/2 or more, and the like.

The solid contained in the ice slurry containing ice produced by the ice making apparatus of the present invention may have any shape, but is preferably particulate. Further, the solid may be contained in a form contained in the ice produced by the ice making apparatus of the present invention, and may be contained in a form contained outside the ice. Since it is easier to directly contact the object to be cooled if it is included in the form of being included outside, the cooling ability is increased. For this reason, it is preferable to be included in a form included outside the ice. When the ice slurry containing ice produced by the ice making device of the present invention contains the solid, it may be mixed with the solid after producing ice by the ice making device of the present invention described later, You may produce | generate ice with the ice making apparatus of this invention in the state mixed with the water used as a raw material.

Hereinafter, a flake ice manufacturing apparatus 10 according to an embodiment of the ice making apparatus of the present invention and an ice making system 60 including the flake ice manufacturing apparatus 10 according to an embodiment of the ice making apparatus of the present invention will be described with reference to the drawings.

[Flake ice production equipment]

FIG. 1 is an image diagram including a partial cross-sectional perspective view showing an outline of a flake ice manufacturing apparatus 10 according to an embodiment of the ice making apparatus of the present invention.

Even if the liquid containing the aqueous solution stored in the container is cooled from the outside, ice similar to the ice generated by the flake ice manufacturing apparatus 10 cannot be generated. This is considered to be due to the insufficient cooling rate. However, according to the flake ice manufacturing apparatus 10, the aqueous solution that is atomized by spraying a liquid containing an aqueous solution containing a solute (hereinafter referred to as “brine”) is directly applied to the wall surface maintained at a temperature below the freezing point. By contacting, rapid cooling that has not been possible in the past is possible. Thereby, it is thought that the ice with high cooling ability which satisfy | fills the conditions of said (a) and (b) can be produced | generated.

The wall surface is, for example, the wall surface of the inner wall 22 of a cylindrical structure such as the drum 11 described later, but is not particularly limited as long as it can be maintained at a temperature below the freezing point of the aqueous solution. The temperature of the wall surface is not particularly limited as long as it is maintained at a temperature lower than or equal to the freezing point of the aqueous solution. However, the wall surface temperature is higher than the freezing point of the aqueous solution in that ice having high purity of ice satisfying the above conditions (a) and (b) can be produced. 1 ° C or more lower temperature (2 ° C or more lower temperature, 3 ° C or more lower temperature, 4 ° C or more lower temperature, 5 ° C or more lower temperature, 6 ° C or more lower temperature, 7 ° C or more lower temperature, 8 ° C or more lower temperature, 9 ° C Lower temperature, lower than 10 ° C, lower than 11 ° C, lower than 12 ° C, lower than 13 ° C, lower than 14 ° C, lower than 14 ° C, lower than 15 ° C, lower than 16 ° C, lower than 17 ° C Temperature, temperature lower than 18 ° C, temperature lower than 19 ° C, temperature lower than 20 ° C, temperature lower than 21 ° C, temperature lower than 22 ° C, temperature lower than 23 ° C, temperature lower than 24 ° C, temperature lower than 25 ° C, etc. Preferred to be retained) Arbitrariness.

Although the injection method is not particularly limited, for example, it is possible to inject by injecting from an injection means having an injection hole 13a like an injection unit 13 described later. In this case, the water pressure at the time of injection is, for example, 0.001 MPa or more (0.002 MPa or more, 0.005 MPa or more, 0.01 MPa or more, 0.05 MPa or more, 0.1 MPa or more, 0.2 MPa or more, etc.). 1 MPa or less (0.8 MPa or less, 0.7 MPa or less, 0.6 MPa or less, 0.5 MPa or less, 0.3 MPa or less, 0.1 MPa or less, 0.05 MPa or less, 0.01 MPa or less, etc.) There may be.

Alternatively, a rotating means such as a rotatable rotating shaft 12 may be provided on the center axis of the saddle drum 11 to be described later, and continuous injection such as injection while rotating may be performed.

(Recovery process)
The flake ice manufacturing apparatus 10 has a step of recovering the ice generated on the wall surface after the above-described ice generation step.

The method of collecting is not particularly limited, and for example, the ice on the wall surface may be scraped or peeled off by means such as a blade 15 described later, and the dropped ice may be collected.

Also, when ice is generated, ice making heat is generated, but this ice making heat may affect the actual melting completion temperature. Thus, it is considered that the melting completion temperature is affected not only by the type and concentration of the solute but also by the ice making heat. Therefore, the actual melting completion temperature can be adjusted by adjusting the amount of ice making heat remaining in the ice. The ice making heat can be adjusted by adjusting the holding time of the ice on the wall surface in the ice collecting step.

As shown in FIG. 1, the flake ice manufacturing apparatus 10 includes a drum 11, a rotary shaft 12, an injection unit 13, a stripping unit 14, a blade 15, a flake ice discharge port 16, and an upper bearing member 17. , A heat protection cover 19, a geared motor 20, a rotary joint 21, a refrigerant clearance 24, a bush 28, a refrigerant supply unit 29, and a rotation control unit 27.
The drum 11 includes an inner cylinder 22, an outer cylinder 23 surrounding the inner cylinder 22, and a refrigerant clearance 24 formed between the inner cylinder 22 and the outer cylinder 23. The outer peripheral surface of the drum 11 is covered with a cylindrical heat-resistant protective cover 19.

The inner cylinder 22 has a wall surface, and when the wall surface is cooled, the brine attached to the wall surface is frozen and ice is generated.
Here, the flake ice manufacturing apparatus 10 sets the ice making speed indicating the amount of ice generated per unit time generated on the wall surface of the inner cylinder 22 to Y, and sets the thermal conductivity of the members constituting the wall surface of the inner cylinder 22 to x1. , It is designed so that the following equation (1) is established (f means a function).
Y = f (x1) (1)

That is, the higher the thermal conductivity of the wall surface of the inner cylinder 22 to which the brine adheres, the faster the temperature of the refrigerant that cools the wall surface of the inner cylinder 22 is transmitted to the brine, so that more ice is generated in a short time.
For this reason, the ice making speed | rate can be raised by making the member which comprises the inner cylinder 22 into a member with high heat conductivity. On the other hand, the ice making speed can be reduced by making the member constituting the inner cylinder 22 a member having low thermal conductivity.
In the present embodiment, a member having a higher thermal conductivity than stainless steel or iron is employed as a member constituting the wall surface of the inner cylinder 22, and more specifically, the thermal conductivity at 20 ° C. is 70 W / mK or more. These members (for example, copper) are employed. For this reason, the flake ice manufacturing apparatus 10 can produce a lot of ice in a shorter time than when stainless steel or iron is adopted as a member constituting the wall surface of the inner cylinder 22. Generally, when producing a large amount of ice, in order to produce ice efficiently in a short time, it is necessary to increase the surface area of the wall surface of the inner cylinder 22, but the wall surface of the inner cylinder 22 has a high thermal conductivity. Since the production speed of ice is increased by using the members, it is not necessary to widen the wall surface of the inner cylinder 22, and as a result, it is possible to produce ice in a relatively narrow space. In this respect, the member constituting the wall surface of the inner cylinder 22 is preferably a member having a high thermal conductivity, more specifically, a member having a thermal conductivity at 20 ° C. of 100 W / mK or more is more preferable. A member having a thermal conductivity at 20 ° C. of 150 W / mK or more is still more preferable, a member having a thermal conductivity at 20 ° C. of 200 W / mK or more is more preferable, and a member having a thermal conductivity at 20 ° C. of 250 W / mK or more is further preferable. A member having a thermal conductivity of 300 W / mK or more at 20 ° C. is particularly preferable. The upper limit of the thermal conductivity is not particularly limited. For example, the thermal conductivity at 20 ° C. is 1000 W / mK or less (900 W / mK or less, 800 W / mK or less, 700 W / mK or less, 600 W / mK or less, 500 W / mK or less, 400 W / mK or less). Specific examples of the members constituting the wall surface of the inner cylinder 22 include zinc, aluminum, geralumin, gold, silver, tungsten, copper, aluminum bronze, seven-three brass, naval brass, nickel (99.9%), molybdenum, palladium. , Silicon and the like. Moreover, as described above, the flake ice production apparatus of the present invention is suitable for production in a relatively narrow space, for example, a limited space such as the inside of a transportation device (for example, a vehicle (such as a truck) or a ship) It is suitable for manufacturing in places where there is only one.
In addition, the relationship between the member which comprises the wall surface of the inner cylinder 22, and heat conductivity is later mentioned with reference to the specific example of the member shown in FIG.

Further, the flake ice manufacturing apparatus 10 is configured such that the following equation (2) is established when the ice making speed is Y and the area of the wall surface of the inner cylinder 22 where the brine may be attached is x2. Designed.
Y = f (x2) (2)
That is, if the area of the portion of the wall surface of the inner cylinder 22 where the brine can be attached is increased, the amount of brine that can be attached to the wall surface of the inner cylinder 22 increases accordingly. As a result, the amount of ice generated on the wall surface of the inner cylinder 22 also increases. On the contrary, if the area of the portion of the wall surface of the inner cylinder 22 where the brine can be attached is reduced, the amount of brine that can be attached to the wall surface of the inner cylinder 22 is reduced accordingly. As a result, the amount of ice produced on the wall surface of the inner cylinder 22 is also reduced.
In this way, the ice making speed is adjusted by adjusting the area of the portion of the wall surface of the inner cylinder 22 where the brine can be attached.

The material of the outer cylinder 23 is not particularly limited. In this embodiment, steel is employed.
Refrigerant is supplied to the refrigerant clearance 24 from the refrigerant supply unit 29 via the refrigerant pipe 35. Thereby, the wall surface of the inner cylinder 22 is cooled.

The rotary shaft 12 is arranged on the central axis of the drum 11 and rotates around the material axis with the central shaft as an axis, using a geared motor 20 installed above the upper bearing member 17 as a power source. The rotational speed of the geared motor 20 is controlled by a rotation control unit 27 described later.
A rotary joint 21 is attached to the top of the rotating shaft 12. Rotary joint 21 In addition, the upper part of the rotating shaft 12 is formed with a pothole 12a extending in the material axis direction and communicating with each pipe 13 (see FIG. 3).

The injection unit 13 is composed of a plurality of pipes having injection holes 13 a for injecting brine toward the wall surface of the inner cylinder 22 at the tip, and rotates together with the rotating shaft 12. The brine injected from the injection hole 13a adheres to the wall surface of the inner cylinder 22 cooled by the refrigerant, and freezes rapidly without giving a time for separation.
The plurality of pipes constituting the injection unit 13 extend radially from the rotary shaft 12 in the radial direction of the drum 11. The installation height of each pipe is not particularly limited, but in this embodiment, the installation height is set at an upper position of the inner cylinder 22 of the drum 11. Note that a spray nozzle or the like may be employed instead of the pipe.

Moreover, the flake ice manufacturing apparatus 10 can also be made to adhere by making a brine flow naturally on the wall surface of the inner cylinder 22, without employ | adopting the method by the above injection. In this case, the volume of the brine adhering to the wall surface of the inner cylinder 22 is larger than the case of adhering to the wall surface of the inner cylinder 22 by injecting brine. For this reason, the ice generated by the natural flow of the brine is not easily affected by the temperature in the air inside the drum 11 which is higher than the temperature of the wall surface of the inner cylinder 22, and therefore melts more than the ice generated by the injection of the brine. It has the advantageous property of being difficult.

The stripping unit 14 is composed of a plurality of arms on which the blade 15 that strips off the ice generated on the wall surface of the inner cylinder 22 is attached to the tip. The stripping part 14 extends in the radial direction of the drum 11 and rotates together with the rotating shaft 12.
The plurality of arms constituting the stripping portion 14 are mounted so as to be symmetric with respect to the rotation shaft 12. The number of arms is not particularly limited, but in the present embodiment, the number of arms is two. The size and material of the blade 15 attached to the tip of each arm are not particularly limited as long as the ice generated on the wall surface of the inner cylinder 22 can be peeled off. For example, the tip of the blade may scrape or scrape off the ice. The blade 15 in the present embodiment is made of a stainless steel plate having a length substantially equal to the entire length (total height) of the inner cylinder 22, and a plurality of saw teeth 15 a are formed on the end surface facing the inner cylinder 22. .
When the ice generated on the wall surface of the inner cylinder 22 is peeled off by the blade 15, it becomes flake ice. The flake ice falls from the flake ice discharge port 16. The flake ice that has fallen from the flake ice discharge port 16 is stored in a flake ice storage tank 34 (see FIG. 3) disposed immediately below the flake ice production apparatus 10.

The upper bearing member 17 has a shape in which the pan is inverted, and seals the upper surface of the drum 11. A bush 24 that supports the rotating shaft 12 is fitted in the center of the upper bearing member 17. The rotating shaft 12 is supported only by the upper bearing member 17, and the lower end portion of the rotating shaft 12 is not pivotally supported.
That is, since there is no obstacle below the drum 11 when the flake ice peeled off by the blade 15 falls, the lower surface of the drum 11 serves as a flake ice discharge port 16 for discharging the flake ice.

The refrigerant supply unit 29 supplies a refrigerant for cooling the wall surface of the inner cylinder 22 to the refrigerant clearance 24 via the refrigerant pipe 35. The refrigerant supplied by the refrigerant supply unit 29 is not particularly limited as long as it cools the wall surface of the inner cylinder 22. Specifically, for example, LNG (Liquid Natural Gas / liquefied natural gas) can be employed as the refrigerant.

Conventionally, imported LNG is stored in the LNG storage tank in a liquid state at -160 ° C. The LNG at -160 ° C is vaporized until it reaches room temperature, adjusted for calorific value, and given odor. And supplied for city gas or GT power generation. For example, as a method for effectively utilizing the exhaust heat of LNG, at the LNG terminal, the heat of exhaust cooling until LNG at −160 ° C. reaches room temperature, the production of liquid oxygen and liquid nitrogen, freezing warehouses, cold power generation, seawater as the heat source The technique used for the vaporization of LNG (ORV type) is used.

When the exhaust cooling heat of LNG is used for the above-described application, it has the following merits as compared with the conventional cooling method by electric power or engine drive. That is, (1) less power is required, (2) the cold energy of LNG that is not being used can be used effectively, (3) a large generator is not required, and (4) pollution factors are low. (5) It has the merit that cost is reduced.
On the other hand, when trying to use the exhaust cooling heat of LNG, there were the following disadvantages. In other words, the use of LNG exhaust heat is normally limited to continuous use at locations around the LNG base. This is because LNG has a risk of combustion during transportation. That is, when using the LNG exhaust cooling heat, the side that receives the LNG exhaust cooling heat needs to return the gas after receiving the LNG supply from the LNG base through the piping and using the LNG exhaust cooling heat. For this reason, it has been difficult to transport the LNG itself to a remote location, where the LNG exhaust heat can be used batchwise.
In addition, since a fixed facility is required to continuously use the exhaust heat of LNG at a location around the LNG base, there is a demerit that it can only be handled for a long-term stable project. Furthermore, there is a demerit that direct heat exchange between the LNG and the object to be cooled is dangerous.

However, when LNG is used as the refrigerant of the flake ice manufacturing apparatus 10 described above, the above-described disadvantages are eliminated. That is, by using LNG as a refrigerant in the flake ice production apparatus 10, ultra-low temperature flake ice can be produced. For this reason, if the manufactured flake ice is transported to a remote place, the waste heat of LNG can be used batchwise without transporting the LNG itself to the remote place.
In addition, the flake ice manufacturing apparatus 10 does not need to be fixed at a specific place, and can be mounted on a moving body such as a vehicle, a ship, an aircraft, etc., and thus has mobility. Furthermore, since there is an intermediate refrigerant called flake ice, there is no danger of direct heat exchange between the LNG and the object to be cooled.

Also, by using -160 degrees LNG as a refrigerant in the flake ice production apparatus 10, it is possible to produce ultra-low temperature flake ice in which brine having a freezing point of up to about -150 degrees is instantaneously frozen. That is, when brine is salt water (sodium chloride aqueous solution), flake ice can be produced at a saturated state of -21.2 ° C, and when magnesium chloride aqueous solution is saturated at -26.27 ° C, The freezing point is lower than that of glycol salt water and magnesium chloride aqueous solution, and substances that could not be used as brine in the past as “antifreeze liquid” can also be used as flake ice by instant freezing. Specifically, for example, flake ice using ethylene glycol as a brine can be produced.

That is, by using an ultra-low temperature refrigerant of -160 degrees LNG as the refrigerant of the flake ice manufacturing apparatus 10, it becomes possible to manufacture ultra-low temperature flake ice at about -150 ° C. In other words, the required cold-retention temperature varies depending on the type of the object to be cooled, and for example, -1 ° C is suitable, and -150 ° C is suitable. In other words, when the wall surface of the inner cylinder 22 is cooled, flake ice matched with a widely required cold insulation temperature can be easily manufactured by using an ultra-low temperature refrigerant of −160 degrees LNG.
Thus, the flake ice manufacturing apparatus 10 can not only supply cold heat as an alternative to a conventional refrigerator, but also can improve energy efficiency by utilizing the exhausted cold heat of LNG. That is, it is possible to construct a cogeneration system.

The flake ice manufacturing apparatus 10 is designed so that the following equation (3) is established when the ice making speed is Y and the temperature of the refrigerant supplied to the refrigerant clearance 24 is x3.
Y = f (x3) (3)
That is, the flake ice manufacturing apparatus 10 is designed such that the ice making speed changes according to the temperature of the refrigerant supplied to the refrigerant clearance 24 by the refrigerant supply unit 29.
That is, the flake ice manufacturing apparatus 10 can freeze the brine attached to the wall surface of the inner cylinder 22 faster as the temperature of the wall surface of the inner cylinder 22 is lower. That is, the flake ice production apparatus 10 can generate more ice in a shorter time as the temperature of the refrigerant supplied to the refrigerant clearance 24 is lower.
Specifically, for example, when LNG at −160 ° C. is supplied to the refrigerant clearance 24, the temperature of the wall surface of the inner cylinder 22 rapidly decreases. For this reason, the flake ice manufacturing apparatus 10 can generate a large amount of ice up to about −150 ° C. in a short time.

In the present embodiment, the refrigerant supplied to the refrigerant clearance 24 can be circulated between the refrigerant clearance 24 and the refrigerant supply unit 29 via the refrigerant pipe 35. Thereby, the refrigerant | coolant currently supplied to the refrigerant | coolant clearance 24 can be maintained in a state with a high cooling function.
The rotation control unit 27 adjusts the rotation speed of the ejection unit 13 and the stripping unit 14 that rotate together with the rotating shaft 12 by adjusting the rotation speed of the geared motor 20. Note that the method by which the rotation control unit 27 controls the rotation speed is not particularly limited. Specifically, for example, a control method using an inverter may be employed.

FIG. 2 is a diagram showing the thermal conductivity of each member used on the ice making surface (for example, the wall surface of the inner cylinder 22 in FIG. 1).

As shown in FIG. 2, the members constituting the ice making surface have different thermal conductivities. For this reason, the ice making speed varies depending on which member is used for the ice making surface. Specifically, for example, the thermal conductivity (W / m · K) of stainless steel is 16 when the temperature is 20 ° C. Moreover, the thermal conductivity (W / m · K) of pure iron is 67 when the temperature is 20 ° C., which is higher than that of stainless steel. Further, the thermal conductivity (W / m · K) of copper (ordinary product) is 372 when the temperature is 20 ° C., which is higher than that of pure iron. In addition, the thermal conductivity (W / m · K) of silver is 418 when the temperature is 20 ° C., and is higher than copper (ordinary product). That is, the thermal conductivity of the ice-making member illustrated in FIG. 2 increases in the order of silver> copper (ordinary product)> pure iron> stainless steel under the same temperature condition. For this reason, the ice making speed also increases in the order of silver> copper (ordinary product)> pure iron> stainless steel.

Specifically, for example, when the wall surface (ice making surface) of the inner cylinder 22 is made of copper, the ice making speed can be increased by changing the wall surface of the inner cylinder 22 from copper to silver. On the other hand, the ice making speed can be reduced by changing the wall surface of the inner cylinder 22 from copper to pure iron or stainless steel.
Thus, the flake ice manufacturing apparatus 10 can adjust the ice making speed by arbitrarily changing the members constituting the wall surface of the inner cylinder 22.

At this time, a member having a high thermal conductivity such as silver or copper is selected as a member constituting the wall surface of the inner cylinder 22, and an ultra-low temperature refrigerant such as LNG is selected as a refrigerant for cooling the wall surface of the inner cylinder 22. May be. In such a case, the enormous amount of cold energy supplied from the ultra-low temperature refrigerant is efficiently transmitted to the brine by the member having high thermal conductivity, so that more efficient generation of ice can be realized.

[Flake ice production system]
FIG. 3 is an image diagram showing an overview of the entire flake ice production system 60 including the flake ice production apparatus 10 of FIG.

The flake ice production system 60 includes a flake ice production apparatus 10, a brine storage tank 30, a pump 31, a brine pipe 32, a brine tank 33, a flake ice storage tank 34, a refrigerant pipe 35, and a freezing point adjustment unit. 36.
The brine storage tank 30 stores brine as a raw material for flake ice. The brine stored in the brine storage tank 30 is fed to the rotary joint 21 via the brine pipe 32 by operating the pump 31, and becomes flake ice by the flake ice manufacturing apparatus 10. That is, the brine fed to the rotary joint 21 is fed to the pit hole 12 a formed in the rotary joint 21 and the rotary shaft 12, and is fed from the pit hole 12 a to each pipe constituting the injection unit 13.

The brine tank 33 supplies brine to the brine storage tank 30 when the brine in the brine storage tank 30 is low.
Note that the brine that has flowed down without freezing on the wall surface of the inner cylinder 22 is stored in the brine storage tank 30 and is fed again to the rotary joint 21 via the brine pipe 32 by operating the pump 31.
The flake ice storage tank 34 is disposed immediately below the flake ice manufacturing apparatus 10 and stores the flake ice that has fallen from the flake ice discharge port 16 of the flake ice manufacturing apparatus 10.

The freezing point adjustment unit 36 adjusts the freezing point of the brine supplied to the brine storage tank 30 by the brine tank 33. For example, when the brine is salt water, the freezing point of the salt water varies depending on the concentration, so the freezing point adjustment unit 36 adjusts the concentration of the salt water stored in the brine storage tank 30.
The method for adjusting the freezing point of the brine is not particularly limited to this. For example, the following method can also be employed.
That is, a plurality of brine storage tanks 30 are provided, and a plurality of types of brines having different freezing points are stored in each of several brine storage tanks 30. The brine freezing point adjustment unit 37 selects a predetermined type of brine based on the required temperature of the flake ice (for example, the required cool temperature for the transported product transported by the flake ice), The flake ice production apparatus 10 is supplied.
Thus, the temperature of the flake ice produced can be adjusted by adjusting the freezing point of the brine.

Next, operation | movement of the flake ice manufacturing system 60 containing the flake ice manufacturing apparatus 10 which has the said structure is demonstrated on the assumption that a brine is salt water.
First, the refrigerant supply unit 29 supplies the refrigerant to the refrigerant clearance 24 and sets the temperature of the wall surface of the inner cylinder 22 to be about −10 ° C. lower than the freezing point of the salt water. Thereby, the salt water adhering to the wall surface of the inner cylinder 22 can be frozen.
At this time, the ice making speed in the flake ice manufacturing apparatus 10 is adjusted according to the thermal conductivity of the member employed as the wall surface of the inner cylinder 22.
In addition, the ice making speed in the flake ice manufacturing apparatus 10 is adjusted according to the area of the portion of the wall surface of the inner cylinder 22 where the brine may adhere.
Further, the ice making speed in the flake ice manufacturing apparatus 10 is adjusted according to the temperature of the refrigerant supplied by the refrigerant supply unit 29.

When the wall surface of the inner cylinder 22 is cooled, the rotation control unit 27 drives the geared motor 20 to rotate the rotating shaft 12 around the material axis.
When the rotary shaft 12 rotates, the pump 31 supplies brine that is brine into the rotary shaft 12 from the brine storage tank 30 via the rotary joint 21.
When salt water is supplied to the inside 12 of the rotating shaft, the injection unit 13 that rotates together with the rotating shaft 12 injects salt water toward the wall surface of the inner cylinder 22. When the salt water sprayed from the spray unit 13 comes into contact with the wall surface of the inner cylinder 22, it freezes instantly and ice is generated.
When the brine is attached to the wall surface of the inner cylinder 22 by naturally flowing down, it is generated because the volume of the brine attached to the wall surface of the inner cylinder 22 is larger than when the brine is attached by injection. The ice volume also increases. For this reason, it is possible to generate ice that hardly melts on the wall surface of the inner cylinder 22.
At this time, the rotation control unit 27 controls the rotation speed of the rotating shaft 12 to 2 to 4 rpm. When a spray nozzle is used instead of a pipe as a component of the injection unit 13, the rotation control unit 27 controls the rotation speed of the rotary shaft 12 to 10 to 15 rpm.
The ice generated on the wall surface of the inner cylinder 22 is peeled off by the peeling unit 14 that rotates together with the rotating shaft 12. The ice peeled off by the peeling unit 14 falls from the discharge port 16 as flake ice. The flake ice that has fallen from the discharge port 16 is stored in a flake ice storage tank 34 disposed immediately below the flake ice manufacturing apparatus 10.
As described above, the salt water that does not become ice but flows down the wall surface of the inner cylinder 22 is stored in the brine storage tank 30, and is fed again to the rotary joint 21 via the brine pipe 32 by operating the pump 31. . In addition, when the salt water in the brine storage tank 30 decreases, the brine tank 33 supplies the salt water stored in itself to the brine storage tank 30.

Here, the rotation control unit 27 can change the temperature of the flake ice manufactured by the flake ice manufacturing apparatus 10 by changing the rotation speed of the geared motor 20.
For example, it is assumed that salt water is adopted as the brain. In this case, it has been conventionally considered that the freezing point at which salt water freezes depends only on the solute concentration. For example, it has been conventionally considered that when the solute concentration is 0.8%, salt water freezes at −1.2 ° C. in any case.
However, when the applicant adopts salt water as a brain and changes the rotation speed of the rotary shaft 12 using the flake ice production apparatus 10 of the present embodiment, flake ice produced from the same concentration of salt water is obtained. It has been found that the temperature of the liquid crystal changes according to the rotational speed, and in particular, the temperature decreases as the rotational speed decreases.
The reason for this is that the flake ice is maintained until the ice-heated state is completely melted.
Thereby, the temperature of flake ice can be adjusted, fixing the density | concentration of a brine to the desired value according to refrigeration and freezing object.

[Ice slurry manufacturing method]
Next, an example of a method for producing an ice slurry using the above-described brine and flake ice as materials will be described. The ice slurry can be manufactured according to the required cold insulation temperature and cold preservation time by using a plurality of types of brine prepared in advance.
It is assumed that the brine is salt water, the to-be-cooled product is a fresh seafood, and that the frozen seafood is immediately frozen by placing the fresh to-be-cooled product directly in the ice slurry.

In order to instantly freeze fresh seafood, the solute concentration of salt water, which is the raw material of ice slurry, is set to be significantly higher than before. The theoretical saturation freezing point of salt water having a solute concentration of 13.6% is −9.8 ° C., and the theoretical saturation freezing point of salt water having a solute concentration of 23.1% is −21.2 ° C.
When the solute concentration of salt water is less than 13.6%, the freezing rate of fresh seafood by the produced ice slurry becomes slow. On the other hand, when the solute concentration of the salt water exceeds 23.1%, the salt content is precipitated as crystals, so that the saturation freezing point of the salt water increases.
When the fresh seafood is directly put into the ice slurry, even if the solute concentration of the ice slurry is high, the surface of the fresh seafood freezes and freezes, so that the salt does not enter the fresh seafood.

It is preferable that the solute concentrations of the flake ice and the salt water to be mixed for producing the ice slurry are approximately the same (concentration difference within several percent). When the solute concentration of the flake ice is higher than the solute concentration of the salt water, the temperature of the flake ice is lower than the saturation freezing point of the salt water, so that the water freezes immediately after mixing the salt water having a low solute concentration. On the other hand, when the solute concentration of the flake ice is lower than the solute concentration of the salt water, since the saturation freezing point of the salt water is lower than the saturation freezing point of the flake ice, the flake ice melts and the temperature of the ice slurry decreases.
Therefore, in order not to change the state of the ice slurry, it is desirable that the solute concentrations of the flake ice and the salt water to be mixed are approximately the same.

The mass ratio of flake ice and salt water to be mixed is flake ice: salt water = 75: 25 to 20:80, preferably flake ice: salt water = 60: 40 to 50:50. In addition, since the ratio of solid content will become high when the mass ratio of flake ice exceeds 75 mass%, a clearance gap will generate | occur | produce between fresh seafood and ice slurry, and ice slurry 3 will not adhere to fresh seafood. On the other hand, when the mass ratio of ice is less than 20% by mass, it is difficult to instantly freeze fresh seafood by the produced ice slurry.

That is, when the brine is salt water, the flake ice produced by the flake ice manufacturing apparatus 10 using the salt water having a solute concentration (brine concentration) of 13.6% to 23.1%, and the solute concentration is 13.6%. An ice slurry is prepared by mixing with ˜23.1% brine.
In this embodiment, the temperature of the produced ice slurry is −9.8 ° C. to −21.2 ° C. The temperature of the salt water mixed with the manufactured flake ice is set to room temperature or lower. In addition, ice-making efficiency becomes high, so that the temperature of salt water is low.

When the brine is other than salt water, the concentration of the brine and the mass ratio of the mixed flake ice and brine are adjusted so that the temperature of the produced ice slurry becomes the required temperature.
Thus, by adjusting the concentration of the brine and the mass ratio of the flake ice and the brine to be mixed, it is possible to produce an ice slurry having a plurality of types of temperatures.

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.

For example, the ice making device of the present invention does not need to be configured as the flake ice manufacturing device 10 shown in FIG. 1 as an embodiment, and may be an ice making device including the components of the present invention.
The ice produced by the ice making apparatus of the present invention is preferably liquid ice containing an aqueous solution containing a solute that satisfies the above conditions (a) and (b). Ice) that does not satisfy one or both of the conditions. That is, the object to be cooled may be kept cold using ice slurries having different solute concentrations of ice and water.

In addition, according to the flake ice manufacturing apparatus 10 according to an embodiment of the ice making apparatus of the present invention, flake ice at an arbitrary temperature can be efficiently manufactured, so the size of the flake ice manufacturing apparatus 10 itself is made more compact. Can be made. Thereby, for example, in a moving body such as a vehicle, a ship, or an aircraft for transporting the object to be cooled, the flake ice manufacturing apparatus 10 having a smaller volume than the entire volume of the cooled object to be loaded can be mounted.
That is, when transporting a cold object, an ice slurry for cooling the cold object is required in proportion to the amount of the cold object to be transported. Vehicles, ships, and aircraft have maximum loading capacity. In order to maximize the load amount of the object to be cooled within the range of the maximum load amount, it is necessary to minimize the amount of ice slurry within the range in which the cooling effect can be maintained. At this time, if the flake ice manufacturing apparatus 10 is made compact, the volume of the cold-reserved object can be maximized within the range of the maximum load capacity because the volume of the ice-cold object can be smaller than that of the entire cold-retained object to be loaded. It becomes possible to make it.

The saw teeth 15 a touch the wall surface of the inner cylinder 22 when the ice attached to the wall surface of the inner cylinder 22 is peeled off. For this reason, the wall surface of the inner cylinder 22 is easily worn and deteriorated. In particular, when the material is softer than the saw tooth 15a such as copper, the deterioration becomes remarkable. On the other hand, although not shown, a replaceable liner can be attached to the wall surface of the inner cylinder 22. Thereby, the quality of the wall surface of the inner cylinder 22 can be maintained by replacing only the liner without performing a large-scale repair work such as replacing the inner cylinder 22 or the entire drum 11. At this time, in consideration of the uniformity of the thermal conductivity, the liner is preferably made of the same material as the wall surface of the inner cylinder 22, but may not be the same material.
The method for attaching the liner to the wall surface of the inner cylinder 22 is not particularly limited. For example, a spiral groove is provided in each of the liner and the wall surface of the inner cylinder 22 in contact with the liner so that the liner is screwed into the drum 11 so that the liner is screwed into the drum 11. It may be attached to the wall. Alternatively, the liner may be once cooled to shrink the volume and then attached to the wall surface of the inner cylinder 22. In this case, since the volume of the liner expands when the temperature of the liner returns to room temperature, the liner can be adhered and fixed to the wall surface of the inner cylinder 22.
In addition, when it is set as the structure which attaches a liner to the wall surface of the inner cylinder 22, you may give fine unevenness | corrugation to the surface where the wall surface of the inner cylinder 22 and a liner contact | adhere using sandpaper etc. As a result, a constant frictional force can be generated between the wall surface of the inner cylinder 22 and the surface where the liner is in close contact, so that it is possible to prevent an accident in which the liner slips from the wall surface of the inner cylinder 22 and falls off. it can.

In addition, the brine is salt water (sodium chloride aqueous solution) in the above-described embodiment, but is not particularly limited. Specifically, for example, an aqueous calcium chloride solution, an aqueous magnesium chloride solution, ethylene glycol, or the like can be employed. Thereby, a plurality of types of brines having different freezing points according to differences in solute or concentration can be prepared.

In addition, when the ice slurry containing ice produced by the ice making device of the present invention contains a solid having a higher thermal conductivity than the ice produced by the ice making device of the present invention, in the step of cooling the object to be cooled, It is preferable to perform cooling so that solids having higher thermal conductivity than ice produced by the ice making device of the present invention are interposed between the ice contained in the ice slurry and the object to be cooled. Accordingly, it is possible to cool an object to be cooled for a long time while obtaining a cooling capacity for a short time by a solid having high thermal conductivity. In such a case, another object may be interposed between ice, a solid having a higher thermal conductivity than ice, and an object to be cooled, depending on the purpose. For example, it is not preferable to be in direct contact with the object to be cooled in the ice slurry (for example, it is not preferable to be in contact with the object to be cooled from the viewpoint of safety, a solid having a higher thermal conductivity than ice (metal such as copper) ) Etc.), either the ice slurry or the object to be cooled may be accommodated in the bag, and the ice slurry and the object to be cooled may be cooled so as not to be in direct contact with each other.

As described above, the ice generated by the flake ice manufacturing apparatus 10 can be used for the following applications in addition to cooling the object to be cooled. That is, it can also be used for freezing industrial waste liquid, freezing manure, liquefying gas, and the like.

In summary, the ice making apparatus to which the present invention is applied only needs to have the following configuration, and can take various embodiments.
That is, the ice making device to which the present invention is applied (for example, the flake ice making device 10 in FIG. 1)
It has an ice making surface (for example, the wall surface of the inner cylinder 22 in FIG. 1) and a cooling unit (for example, the inner cylinder 22 in FIG. 1) for cooling the ice making surface, and freezes the brine adhering to the cooled ice making surface. An ice making part (for example, the inner cylinder 22, the outer cylinder 23, and the refrigerant clearance 24 in FIG. 1) that generates ice by
A brine supply unit (for example, the injection unit 13 in FIG. 1) that supplies the brine by attaching the brine to the ice making surface;
A collecting unit (for example, the stripping unit 14 in FIG. 1) that collects the ice generated by the ice making unit;
With
In the ice making section, when the ice making speed indicating the amount of ice produced per unit time is Y and the thermal conductivity of the ice making surface is x1, the following equation (1) is established.
Y = f (x1) (1)
As a result, it is possible to realize a technique that makes it possible to more efficiently generate ice with high cooling ability.

The ice making surface can be made of copper.
Thereby, ice with high cooling ability can be generated more efficiently.

Further, when the ice making speed is Y and the area of the ice making surface where the brine may be attached is x2, the following equation (2) can be established.
Y = f (x2) (2)
Thus, the ice making speed can be adjusted by adjusting the area of the ice making surface where the brine may adhere.

The cooling unit further includes a refrigerant supply unit (for example, the refrigerant supply unit 29 in FIG. 1) for supplying a predetermined refrigerant to cool the ice making surface.
When the ice making speed is Y and the temperature of the ice making surface is x3, the following equation (3) can be established.
Y = f (x3) (3)
Thus, the ice making speed can be adjusted by selecting the refrigerant and adjusting the temperature of the ice making surface.

The brine supply unit
The brine can be deposited by spraying onto the ice making surface.
The brine supply unit
The brine can be adhered to the ice making surface by naturally flowing down.
Thereby, the ice making speed can be adjusted according to the method of attaching the brine to the ice making surface.

The ice making surface is made of copper,
The refrigerant can be LNG.
As a result, even the ultra-low temperature ice can be efficiently generated, and therefore flake ice matched with a wide range of required cold insulation temperatures can be easily produced.

In addition, the ice making part
Further comprising a liner covering the ice making surface,
The liner can be replaceable.
Thereby, the quality of the ice making surface can be maintained by replacing only the liner without performing a large repair work such as replacing the entire ice making unit.

The flake ice manufacturing apparatus to which the present invention is applied includes the ice making unit, the brine supply unit, and the recovery unit.
The ice making part is
A drum including an inner cylinder having the ice making surface, an outer cylinder surrounding the inner cylinder, a clearance formed between the inner cylinder and the outer cylinder, and a refrigerant that supplies refrigerant to the clearance And further comprising a supply unit,
The brine supply unit
A rotation unit that rotates around a central axis of the drum, and further includes an injection unit that injects the brine toward the ice making surface of the inner cylinder;
The collection unit
The brine jetted from the jetting unit is further attached to the inner surface of the inner cylinder cooled by the refrigerant supplied to the clearance, and further comprises a stripping unit for stripping off the ice generated as a result,
In the ice making section, when the production rate indicating the amount of ice produced per unit time is Y and the thermal conductivity of the ice making surface is x1, the design (1) is established. it can.
Thereby, ice with high cooling ability can be generated more efficiently.

Further, the thermal conductivity at 20 ° C. of the ice making surface can be 70 W / mK or more.
Further, when the ice making speed is Y and the area of the ice making surface where the brine is likely to be attached is x2, it can be designed so that the formula (2) is satisfied.
Moreover, when the said ice making speed is set to Y and the temperature of the said ice making surface is set to x3, it can design so that the said Formula (3) may be formed.

The brine supply unit
The brine can be adhered to the ice making surface by naturally flowing down.
The refrigerant may be LNG.
In addition, the ice making part
Further comprising a liner covering the ice making surface,
The liner can be replaceable.

Moreover, the flake ice manufacturing apparatus of 1 aspect of this invention can be mounted in a moving body.
Thereby, since flake ice of arbitrary temperature can be manufactured efficiently, the size of flake ice manufacturing apparatus itself can be made more compact. For this reason, for example, in a vehicle, a ship, and an aircraft for transporting the object to be cooled, a flake ice manufacturing apparatus having a smaller volume than the volume of the entire cold object to be loaded can be mounted.

DESCRIPTION OF SYMBOLS 10: Flakes ice production apparatus, 11: Drum, 12: Rotating shaft, 12a: Coffin hole, 13: Injection part, 13a: Injection hole, 14: Stripping part, 15: Blade, 15a: Saw tooth, 16: Flake ice discharge port 17: Upper bearing member, 19: Thermal protection cover, 20: Geared motor, 21: Rotary joint, 22: Inner cylinder, 23: Outer cylinder, 24: Refrigerant clearance, 27: Rotation controller, 28: Bush, 29: Refrigerant supply unit, 30: brine storage tank, 31: pump, 32: brine piping, 33: brine tank, 34: flake ice storage tank, 35: refrigerant piping, 36: freezing point adjustment unit, 60: flake ice production system

Claims

An ice making surface, and a cooling unit that cools the ice making surface; and an ice making unit that generates ice by freezing brine attached to the cooled ice making surface;
A brine supply unit for supplying the brine by attaching the brine to the ice making surface;
A recovery unit for recovering the ice generated by the ice making unit;
With
When the ice making speed indicating the amount of ice produced per unit time in the ice making unit is Y and the thermal conductivity of the ice making surface is x1, the following equation (1) is established.
Ice making equipment.
Y = f (x1) (1)
The thermal conductivity at 20 ° C. of the ice making surface is 70 W / mK or more.
The ice making device according to claim 1.
When the ice making speed is Y and the area of the ice making surface where the brine may be attached is x2, the following formula (2) is established.
The ice making device according to claim 1 or 2.
Y = f (x2) (2)
In order to cool the ice making surface to the cooling unit, further comprising a refrigerant supply unit for supplying a predetermined refrigerant,
When the ice making speed is Y and the temperature of the ice making surface is x3, the following equation (3) is established.
The ice making device according to any one of claims 1 to 3.
Y = f (x3) (3)
The brine supply unit
The brine is deposited by spraying on the ice making surface;
The ice making device according to any one of claims 1 to 4.
The brine supply unit
The brine is allowed to adhere to the ice making surface by allowing it to flow down naturally.
The ice making device according to any one of claims 1 to 4.
The refrigerant is LNG.
The ice making device according to claim 4.
The ice making part is
Further comprising a liner covering the ice making surface,
The liner is replaceable,
The ice making device according to any one of claims 1 to 7.
A flake ice production apparatus comprising: the ice making unit according to claim 1; the brine supply unit according to claim 1; and the recovery unit according to claim 1.
The ice making part is
A drum including an inner cylinder having the ice making surface, an outer cylinder surrounding the inner cylinder, a clearance formed between the inner cylinder and the outer cylinder, and a refrigerant that supplies refrigerant to the clearance A supply section,
The brine supply unit
An injection unit that rotates together with a rotation shaft that rotates about the central axis of the drum, and that injects the brine toward the ice making surface of the inner cylinder;
The collection unit
The brine jetted from the jetting unit is further attached to the inner surface of the inner cylinder cooled by the refrigerant supplied to the clearance, and further comprises a stripping unit for stripping off the ice generated as a result,
In the ice making part, when the production rate indicating the production amount of the ice per unit time is Y and the thermal conductivity of the ice making surface is x1, the above formula (1) is established.
Flakes ice making equipment.
The thermal conductivity at 20 ° C. of the ice making surface is 70 W / mK or more.
The flake ice manufacturing apparatus of Claim 9.
When the ice making speed is Y and the area of the ice making surface where the brine may be attached is x2, the above formula (2) is established.
The flake ice manufacturing apparatus of Claim 9 or 10.
In order to cool the ice making surface to the cooling unit, further comprising a refrigerant supply unit for supplying a predetermined refrigerant,
When the ice making speed is Y and the temperature of the ice making surface is x3, the above formula (3) is established.
The flake ice manufacturing apparatus of any one of Claims 9 thru | or 11.
The brine supply unit
The brine is deposited by spraying on the ice making surface;
The flake ice manufacturing apparatus of any one of Claims 9 thru | or 12.
The brine supply unit
The brine is allowed to adhere to the ice making surface by allowing it to flow down naturally.
The flake ice manufacturing apparatus of any one of Claims 9 thru | or 12.
The refrigerant is LNG.
The flake ice manufacturing apparatus of Claim 9.
The ice making part is
Further comprising a liner covering the ice making surface,
The liner is replaceable,
The flake ice manufacturing apparatus of any one of Claims 9 thru | or 15.
A flake ice production method using the flake ice production apparatus according to any one of claims 9 to 16.
A moving body on which the flake ice manufacturing apparatus according to any one of claims 9 to 17 is mounted.