JP2021173508A - Fluid treatment device, fluid treatment method, skin lotion water, skin lotion, and cosmetic - Google Patents

Abstract

To provide a fluid treatment device and a fluid treatment method capable of continuously carrying out heating treatment and cooling treatment, and skin lotion water, skin lotion, and cosmetics produced by the same device and the method.SOLUTION: A fluid treatment device includes a first heat exchange part 10 for heating fluid introduced into a first flow passage P1 to a prescribed temperature, and a second heat exchange part 20 being directly connected to a downstream side of the first heat exchange part and cooling the fluid introduced into a second flow passage P2 from the prescribed temperature. The first heat exchange part includes a plurality of first auxiliary flow passages SP1 extending in a first direction and a plurality of second auxiliary flow passages SP2 extending in a second direction perpendicular to the first direction and communicating the first auxiliary flow passages adjacent with each other. The fluid introduced into the first auxiliary flow passage on one end flows to the first auxiliary flow passage on the other end through the first auxiliary flow passages and the second auxiliary flow passages, and vertically collides against a wall of the first auxiliary flow passage to carry out heat exchange. The second heat exchange part has a similar configuration.SELECTED DRAWING: Figure 1

Description

The present invention relates to a fluid treatment apparatus for heat-treating and cooling a fluid, a fluid treatment method, and a lotion water, a lotion, and a cosmetic product produced thereby.

As a heat exchange device, there is a device that heats a fluid, and for example, a heat exchange device having a structure in which a gas is passed through a heated pipe is known. Further, for example, a heat exchange device having a structure in which a heating fluid is passed through a pipe with fins and the gas is heated through a gas to be heated between the fins is known.

The above heat exchange device is used not only for heating gas, but also for heating liquid, vaporization by heating liquid (for example, preparation of steam from water), and the like.

Patent Document 1 describes a heat exchanger having a plurality of stages of a first flow path formed on a substrate and a plurality of second flow paths communicating with the first flow path.

Patent Document 2 describes a fluid heating device in which a plurality of peripheral grooves are provided on the side surface of a pillar, and a plurality of connecting grooves for connecting the peripheral grooves to each of the adjacent peripheral grooves are provided.

Patent Document 3 is a fluid heat exchange device in which a plurality of tabs are provided on both the front and back surfaces of a plate, one tab on one side overlaps with a tab on the opposite side, and a hole for connecting the tabs on both sides is provided at the overlapping portion. Is described.

Japanese Patent No. 5923757 Japanese Patent No. 5955089 Japanese Patent No. 6115959

In a fluid treatment apparatus and a fluid treatment method using the above heat exchange apparatus, it is desired to continuously perform heat treatment and cooling treatment.

An object of the present invention is to provide a fluid treatment apparatus and a fluid treatment method capable of continuously performing heat treatment and cooling treatment, and a lotion water, a lotion water and a cosmetic product produced by the fluid treatment apparatus.

The fluid treatment apparatus of the present invention has a first substrate provided with a recess of the first substrate on the surface and a first airtight plate laminated on the first substrate, and the recess of the first substrate of the first substrate. Between the surface and the surface of the first sealing plate on the first substrate side, a plurality of first sub-fluids extending in the first direction and extending in a second direction perpendicular to the first direction. The fluid introduced into the first sub-channel at one end includes the first sub-channel and the second sub-channel, which includes a plurality of second sub-channels communicating with the first sub-channel adjacent to the first sub-channel. The fluid that flows through the flow path to the first sub-flow path at the other end, exchanges heat by colliding perpendicularly with the wall of the first sub-flow path, and flows through the second sub-flow path. A first flow path is provided so that the flow velocity of the fluid is higher than the flow velocity of the fluid flowing through the first sub-channel, and the fluid introduced into the first flow path is heated to a predetermined temperature. It has a first heat exchange portion, a second substrate provided with a second substrate recess on the surface, and a second airtight plate laminated on the second substrate, and the second substrate recess of the second substrate. Between the surface of the second sealing plate and the surface of the second sealing plate on the second substrate side, a plurality of third sub-fluids extending in a third direction and a fourth direction perpendicular to the third direction. The fluid introduced into the third sub-channel at one end includes the plurality of fourth sub-channels that extend and communicate with the adjacent third sub-channel, and the third sub-channel and the fourth sub-channel. The fluid flows to the third sub-fluid at the other end via the sub-fluid, exchanges heat by colliding perpendicularly with the wall of the third sub-fluid, and flows through the fourth sub-fluid. A second flow path is provided so that the flow velocity of the fluid is faster than the flow velocity of the fluid flowing through the third sub-channel, and the fluid introduced into the second flow path is heated to the predetermined temperature. It is provided with a second heat exchange unit directly connected to the downstream side of the first heat exchange unit, which is cooled from the water.

The fluid treatment method of the present invention has a first substrate provided with a recess of the first substrate on the surface and a first airtight plate laminated on the first substrate, and the recess of the first substrate of the first substrate. Between the surface and the surface of the first sealing plate on the first substrate side, a plurality of first sub-fluids extending in the first direction and extending in a second direction perpendicular to the first direction. The fluid introduced into the first sub-channel at one end includes the first sub-channel and the second sub-channel, which includes a plurality of second sub-channels communicating with the first sub-channel adjacent to the first sub-channel. The flow velocity of the fluid flowing through the second sub-flow path is the first in the first heat exchange portion provided with the first flow path that flows to the first sub-flow path at the other end via the flow path. The fluid is flowed so as to be faster than the flow velocity of the fluid flowing through the subchannel, and the fluid is collided perpendicularly with the wall of the first subchannel to exchange heat and is introduced into the first channel. It has a first heat exchange step of heating the fluid to a predetermined temperature, a second substrate provided with a second substrate recess on the surface, and a second airtight plate laminated on the second substrate. With respect to a plurality of third sub-fluids extending in a third direction and the third direction between the surface of the second base recess of the two bases and the surface of the second sealing plate on the second base side. A third sub-channel in which the fluid heated to a predetermined temperature is at one end, including a plurality of fourth sub-channels extending in a vertical fourth direction and communicating with adjacent third sub-channels. In the second heat exchange section provided with a second flow path that is introduced into the flow path and flows through the third sub-flow path and the fourth sub-flow path to the third sub-flow path at the other end. The fluid is flowed so that the flow velocity of the fluid flowing through the fourth sub-channel is faster than the flow velocity of the fluid flowing through the third sub-channel, and the fluid is perpendicular to the wall of the third sub-channel. It includes a second heat exchange step performed after the first heat exchange step, which exchanges heat by colliding and cools the fluid introduced into the second flow path from the predetermined temperature.

The water for lotion of the present invention has a first substrate provided with a recess of the first substrate on the surface and a first airtight plate laminated on the first substrate, and the recess of the first substrate of the first substrate. Between the surface and the surface of the first sealing plate on the first substrate side, a plurality of first sub-fluids extending in the first direction and extending in a second direction perpendicular to the first direction. The raw material fluid containing water or water vapor introduced into the first sub-flow path at one end of the first sub-flow path includes a plurality of second sub-flow paths communicating with the first sub-flow path adjacent to the first sub-flow path. The second sub-flow path of the raw material fluid is provided in a first heat exchange portion provided with a first flow path that flows to the first sub-flow path at the other end via the path and the second sub-flow path. The raw material fluid is flowed so that the flow velocity flowing through the first sub-channel is faster than the flow velocity flowing through the first sub-channel, and the raw material fluid is made to collide perpendicularly with the wall of the first sub-channel to exchange heat. After heating the raw material fluid introduced into one flow path to a predetermined temperature, it has a second substrate provided with a second substrate recess on the surface and a second airtight plate laminated on the second substrate. A plurality of third sub-fluids extending in a third direction and the third direction between the surface of the second base recess of the second base and the surface of the second sealing plate on the second base side. The raw material fluid is at one end, including a plurality of fourth subchannels extending in a fourth direction perpendicular to and communicating with adjacent third subchannels, and heated to a predetermined temperature. A second heat provided with a second flow path introduced into the third sub-flow path and flowing through the third sub-flow path and the fourth sub-flow path to the third sub-flow path at the other end. The raw material fluid is flowed through the exchange portion so that the flow velocity of the raw material fluid flowing through the fourth sub-channel is faster than the flow velocity flowing through the third sub-channel, and the raw material fluid is passed through the wall of the third sub-channel. The raw material fluid introduced into the second flow path is cooled from the predetermined temperature by performing heat exchange by colliding with the fluid vertically.

The lotion of the present invention contains the above-mentioned lotion water and an antibacterial substance.

The cosmetic product of the present invention contains the above-mentioned water for lotion or the above-mentioned lotion and vitamin C, and is in the form of a gel.

According to the present invention, a first heat exchange unit that heats the fluid introduced into the first flow path to a predetermined temperature and a first heat exchange unit that cools the fluid introduced into the second flow path from a predetermined temperature. It is possible to continuously perform the heat treatment and the cooling treatment of the fluid by the fluid treatment apparatus having the structure including the second heat exchange part directly connected to the downstream side of the part.

According to the present invention, there is a first heat exchange step of heating the fluid introduced into the first flow path to a predetermined temperature, and a first heat of cooling the fluid introduced into the second flow path from the predetermined temperature. By a fluid treatment method including a second heat exchange step performed after the exchange step, it is possible to continuously perform the heat treatment and the cooling treatment of the fluid.

According to the present invention, the raw material fluid containing water or water vapor introduced into the first flow path of the first heat exchange section is heated to a predetermined temperature and then introduced into the second flow path of the second heat exchange section. It is possible to provide water for lotion produced by cooling the raw material fluid from a predetermined temperature. It is possible to provide a fluid treatment apparatus capable of continuously performing heat treatment and cooling treatment and water for lotion produced by a fluid treatment method. This water for lotion can be used to provide lotion and cosmetics.

FIG. 1 is a schematic view showing a configuration of a fluid processing apparatus according to an embodiment of the present invention. FIG. 2 is a schematic view showing a first flow path of the first heat exchange section of the fluid processing apparatus of FIG. FIG. 3 is a schematic view showing a first subchannel of the first heat exchange section of the fluid processing apparatus of FIG. FIG. 4 is a schematic view showing a second subchannel of the first heat exchange section of the fluid processing apparatus of FIG. FIG. 5 is a schematic view showing a second flow path of the second heat exchange section of the fluid processing apparatus of FIG. FIG. 6 is a schematic view showing a third subchannel of the second heat exchange section of the fluid processing apparatus of FIG. FIG. 7 is a schematic view showing a fourth sub-channel of the second heat exchange section of the fluid processing apparatus of FIG. 8A and 8B are schematic views showing the configuration of the fluid treatment apparatus according to the first embodiment, FIG. 8A shows a plan view of a ZZ cross section of the first heat exchange section, and FIG. 8B shows a first heat. The YY cross-sectional view of the exchange part is shown, and FIG. 8C shows the XX cross-sectional view of the first heat exchange part. FIG. 9 is a schematic view showing the configuration of the fluid processing apparatus according to the second embodiment. FIG. 10 is a schematic cross-sectional view showing the configuration of the fluid treatment apparatus according to the third embodiment. FIG. 11 is a schematic view showing the configuration of the fluid processing apparatus according to the fourth embodiment.

Hereinafter, embodiments of the present invention will be described. The forms described below are merely examples, and can be appropriately modified to the extent obvious to those skilled in the art.

<First Embodiment>
(Configuration of fluid processing equipment)
FIG. 1 is a schematic view showing a configuration of a fluid processing apparatus according to the present embodiment. As shown in FIG. 1, the fluid processing apparatus 1 determines the first heat exchange unit 10 that heats the fluid introduced into the first flow path P1 to a predetermined temperature, and the fluid introduced into the second flow path P2. It has a second heat exchange unit 20 directly connected to the downstream side of the first heat exchange unit 10 for cooling from the temperature of.

The first heat exchange unit 10 has a first substrate provided with a recess of the first substrate on the surface, and a first airtight plate laminated on the first substrate. A first flow path P1 is provided between the surface of the recess of the first base of the first base and the surface of the first sealing plate on the side of the first base. The first flow path P1 communicates with a plurality of first sub-flow paths SP1 extending in the first direction and a first sub-flow path SP1 extending in a second direction perpendicular to the first direction and adjacent to each other. Includes a plurality of second subchannels SP2. When the fluid F1 is introduced from the introduction path 30 into the first sub-channel SP1 at one end, it passes through the first sub-channel SP1 and the second sub-channel SP2 and is the first sub at the other end. It flows to the flow path SP1. The first substrate is held at a predetermined temperature, and when the fluid F1 flows through the first flow path P1, it collides perpendicularly with the wall of the first sub-flow path SP1 so that the fluid F1 and the first sub-flow path SP1 Heat exchange takes place with the wall. When colliding vertically, a stagnation layer that resists heat transfer is formed or thinned. Heat exchange between the fluid F1 and the wall of the first subchannel SP1 is performed a plurality of times, and the fluid F2 that has been heat-exchanged by the first heat exchange unit 10 and heated to a predetermined temperature is led out from the lead-out path 31A. NS. The flow velocity of the fluid flowing through the second subchannel SP2 is configured to be faster than the flow velocity of the fluid flowing through the first subchannel SP1.

The second heat exchange unit 20 has the same configuration as the first heat exchange unit 10 described above, and cools the fluid from a predetermined temperature. The second heat exchange unit 20 has a second substrate provided with a recessed portion of the second substrate on its surface, and a second sealing plate laminated on the second substrate. A second flow path P2 is provided between the surface of the recess of the second base of the second base and the surface of the second sealing plate on the side of the second base. The second flow path P2 communicates with a plurality of third sub-flow paths SP3 extending in the third direction and a third sub-flow path SP3 extending in the fourth direction perpendicular to the third direction and adjacent to each other. Includes a plurality of fourth subchannels SP4. The lead-out path 31A of the first heat exchange section 10 is connected to the introduction path 31B of the second heat exchange section 20. When the fluid F2 is introduced from the introduction path 31B into the third sub-flow path SP3 at one end, the third sub-channel at the other end passes through the third sub-flow path SP3 and the fourth sub-flow path SP4. It flows to the flow path SP3. The second substrate is held at a temperature lower than the temperature at which the fluid is heated by the first heat exchange unit 10, and when the fluid F2 flows through the second flow path P2, it is perpendicular to the wall of the third sub-flow path SP3. Due to the collision, heat exchange is performed between the fluid F2 and the wall of the third auxiliary flow path SP3. When colliding vertically, a stagnation layer that resists heat transfer is formed or thinned. Heat exchange between the fluid F2 and the wall of the third subchannel SP3 is performed a plurality of times, and the fluid F3 that has been heat-exchanged by the second heat exchange unit 20 and cooled from a predetermined temperature is led out from the lead-out path 32. NS. The cooled fluid F3 is, for example, condensed from a gas and recovered as a liquid 40. The flow velocity of the fluid flowing through the fourth subchannel SP4 is configured to be faster than the flow velocity of the fluid flowing through the third subchannel SP3.

A first temperature control (not shown) such as a heater is provided on at least one of the first substrate and the first airtight plate so that the wall of the first sub-flow path SP1 that exchanges heat with a fluid has a predetermined temperature. A part is provided. The first temperature control unit allows the first heat exchange unit 10 including the wall of the first subchannel SP1 to be set to a predetermined temperature appropriately selected from, for example, 100 ° C. to 1000 ° C. Similarly, on at least one of the second substrate and the second sealing plate, the temperature of the wall of the third sub-channel SP3 that exchanges heat with the fluid is lower than the temperature of the wall of the first sub-channel SP1. As described above, a second temperature control unit (not shown) such as a cooler or a heater is provided. By the second temperature control unit, the second heat exchange unit 20 including the wall of the third subchannel SP3 is set to, for example, 0 in the range where the temperature of the second heat exchange unit 20 is lower than the temperature of the first heat exchange unit 10. It is possible to set a predetermined temperature selected from ° C. to 100 ° C.

FIG. 2 is a schematic view showing a first flow path P1 of the first heat exchange unit 10 of the fluid processing apparatus 1 of FIG. The first flow path P1 includes a plurality of first sub-flow paths SP1 and a plurality of second sub-flow paths SP2 communicating with adjacent first sub-flow paths SP1. When the fluid F1 flows through the first sub-flow path P1, it flows through the first sub-flow path SP1, flows from the first sub-flow path SP1 into the second sub-flow path SP2, and flows from the second sub-flow path SP2 to the first side flow. It flows out to the road SP1. At this time, the fluid F1 collides perpendicularly with the wall of the first subchannel SP1, and heat exchange is performed between the fluid F1 and the wall of the first subchannel SP1. The first sub-flow path SP1 is formed with a width W1 and the length from the second sub-flow path SP2 on the upstream side to the second sub-flow path SP2 on the downstream side is the length L1 of the first sub-flow path SP1. There is. Further, the second sub-flow path SP2 is formed with a width W2, where the length from the first sub-flow path SP1 on the upstream side to the first sub-flow path SP1 on the downstream side is the length L2 of the second sub-flow path SP2. Has been done. The distance between adjacent first sub-channels SP1 corresponds to the length L2 of the second sub-channel SP2. The pitch of the second subchannel SP2 corresponds to twice that of (L1 + W2).

FIG. 3 is a schematic view showing a first subchannel SP1 of the first heat exchange unit 10 of the fluid processing apparatus 1 of FIG. The first sub-channel SP1 has, for example, a rectangular shape having a cross-sectional area of S1.

FIG. 4 is a schematic view showing a second subchannel SP2 of the first heat exchange unit 10 of the fluid processing apparatus 1 of FIG. The second subchannel SP2 has, for example, a rectangular shape having a cross-sectional area of S2.

In the fluid processing apparatus 1 of the present embodiment, the cross-sectional area S1 of the first sub-flow path SP1 is larger than twice the cross-sectional area S2 of the second sub-flow path SP2, and the length L2 of the second sub-flow path SP2 is large. It is satisfied at the same time that it is longer than the SP1 width W1 of the first sub-flow path and that the arrangement pitch PT2 of the second sub-flow path SP2 is larger than twice the width W2 of the second sub-flow path SP2. It is preferable that the combination is satisfied.

FIG. 5 is a schematic view showing a second flow path P2 of the second heat exchange unit 20 of the fluid processing apparatus 1 of FIG. The second flow path P2 includes a plurality of third sub-flow paths SP3 and a plurality of fourth sub-flow paths SP4 communicating with adjacent third sub-flow paths SP3. When the fluid F2 flowing from the first heat exchange unit 10 flows through the second flow path P2, it flows through the third sub-flow path SP3 and flows from the third sub-flow path SP3 into the fourth sub-flow path SP4. It flows out from the fourth sub-flow path SP4 to the third sub-flow path SP3. At this time, the fluid F2 collides perpendicularly with the wall of the third subchannel SP3, and heat exchange is performed between the fluid F2 and the wall of the third subchannel SP3. The third sub-flow path SP3 is formed with a width W3, where the length from the fourth sub-flow path SP4 on the upstream side to the fourth sub-flow path SP4 on the downstream side is the length L3 of the third sub-flow path SP3. There is. Further, the fourth sub-flow path SP4 is formed with a width W4, where the length from the third sub-flow path SP3 on the upstream side to the third sub-flow path SP3 on the downstream side is the length L4 of the fourth sub-flow path SP4. Has been done. The distance between adjacent third sub-channels SP3 corresponds to the length L4 of the fourth sub-channel SP4. The pitch of the fourth subchannel SP4 corresponds to twice that of (L3 + W4).

FIG. 6 is a schematic view showing a third subchannel SP3 of the second heat exchange unit 20 of the fluid processing apparatus 1 of FIG. The third sub-channel SP3 has a rectangular cross-sectional shape with a cross-sectional area of S3.

FIG. 7 is a schematic view showing a fourth subchannel SP4 of the second heat exchange unit 20 of the fluid processing apparatus 1 of FIG. The fourth subchannel SP4 has a rectangular cross-sectional shape with a cross-sectional area of S4.

In the fluid processing apparatus 1 of the present embodiment, the cross-sectional area S3 of the third sub-channel SP3 is larger than twice the cross-sectional area S4 of the fourth sub-channel SP4, and the length L4 of the fourth sub-channel SP4 is large. It is satisfied at the same time that the width W3 of the third sub-flow path SP3 and the arrangement pitch PT4 of the fourth sub-flow path SP4 are larger than twice the width W4 of the fourth sub-flow path SP4 are satisfied at the same time. It is preferable that the combination is satisfied.

The fluid processed by the fluid processing apparatus 1 may change the state of matter from liquid to gas or from gas to liquid during processing. For example, the fluid is water or water vapor. For example, in the first heat exchange unit 10, water is vaporized into water vapor by heat exchange treatment and heated to a predetermined temperature, and then in the second heat exchange unit 20, the water vapor is condensed into water by heat exchange treatment to a predetermined temperature. It may be configured to be cooled from. When the fluid is water or steam, the first heat exchange unit 10 is heated to a temperature of, for example, 100 ° C. or higher, preferably 150 ° C. or higher, more preferably 200 ° C. or higher, and typically 500 ° C. or higher. The time required for heating (the time required for the fluid to pass through the first heat exchange section) is, for example, 1000 ms or less, typically 200 ms. Further, the second heat exchange unit 20 cools the temperature to, for example, room temperature or lower, typically 20 ° C. The time required for cooling (the time required for the fluid to pass through the second heat exchange section) is, for example, 1000 ms or less, typically 200 ms or less. Water vapor condenses into water as the temperature drops. When the fluid is used in a water vapor state, it may be cooled to a temperature at which the water vapor state can be maintained.

The fluid processed by the fluid processing apparatus 1 may be a fluid that does not change the state of matter during the processing. For example, as water vapor, heat exchange treatment may be performed by the first heat exchange unit 10 and the second heat exchange unit 20.

In addition to the above, the fluid processed by the fluid processing apparatus 1 may be a gas containing air or a liquid containing water. It is applicable to gases containing oxygen and gases containing hydrogen and formic acid.

In the fluid processing apparatus 1 of the present embodiment, the first substrate and the second substrate have, for example, any shape of a plate, a cylinder, a cylinder, and a prism, respectively. The shapes of the first substrate and the second substrate are not particularly limited, and can be applied to various shapes.

In the fluid treatment apparatus 1 of the present embodiment, the first substrate, the first sealing plate, the second substrate and the second sealing plate are each composed of, for example, metal, graphite, ceramics, plastic, composite material, or a combination thereof. Has been done. The composite material is, for example, a material in which at least one selected from metals, carbon nanotubes, graphene and carbon fibers is composited with plastic. The above metal is, for example, a fibrous metal. The fluid processing apparatus 1 can be realized by the first heat exchange unit 10 and the second heat exchange unit 20 formed of such a material.

The first base, the first sealing plate, the second base, and the second sealing plate may be made of a plate-like material. For example, a plate-shaped material may be processed with a mold or the like to form channels and tabs, and a plurality of sheets may be bonded and joined. If a deformable material is selected as the material, it is possible to form a flow path by die pressing. If a metal plate is selected, it can be joined by welding or electric welder. If it is plastic, it can be joined with an adhesive.

When the surrounding material or fluid in contact with the fluid treatment apparatus 1 of the present embodiment is corrosive, the material surface of the fluid treatment apparatus 1 can be lined with resin, painted, or plated. .. It is also possible to oxidize the material surface of the fluid treatment apparatus 1 and protect it with an oxide film. From these materials, it is possible to select a material that prevents corrosion and wear due to contact with a fluid or heat medium, and it is possible to exchange heat with a fluid such as a corrosive chemical or a permeable toxic gas.

When joining plate-shaped materials, screwing is possible. Rubber packing, carbon packing, and other seal packing can be used to join the plate-shaped materials. It is also possible to use an adhesive for joining the plate-shaped materials.

The first heat exchange unit 10 and the second heat exchange unit 20 are, for example, simple substances shown in the form of a plane. Alternatively, it may be bent into the shape of a triangle, a quadrangle, or another polygonal cylinder. It may be formed into a cylindrical shape by making it from a plate in the shape of a round cylinder instead of a flat surface. The first heat exchange unit 10 and the second heat exchange unit 20 can be attached to the surface of another cylinder or plate.

The number, shape, and mounting position of the introduction path 30 of the first heat exchange section 10 and the lead path 32 of the second heat exchange section 20 can be freely designed. The lead-out path 31A of the first heat exchange section 10 and the introduction path 31B of the second heat exchange section 20 are formed in a number, shape, and mounting position that can be connected to each other.

It is also possible to attach a heater to the first heat exchange section 10 to heat the fluid, or to place it in a heated medium to heat it. For example, it has been found that it is effective to introduce high-temperature heated air in order to increase the combustion efficiency of the boiler. For this purpose, for example, the first heat exchange unit 10 may be brought into contact with or placed in the combustion chamber or exhaust pipe of the boiler for heating, and heated air may be introduced through the first heat exchange unit 10.

Further, in order to cool the fluid to a temperature lower than the temperature heated by the first heat exchange unit, a cooling unit or a heater is attached to the second heat exchange unit 20, or the fluid is placed in a cooled or heated medium. It is also possible to cool or heat. In order to cool the fluid, for example, the cooling medium can be brought into contact with the second heat exchange unit 20, or the fluid can be cooled by placing it in a low temperature medium. For example, if the high temperature gas from the first heat exchange unit 10 is passed through the first heat exchange unit 10 as a fluid and immersed in seawater for cooling, the high temperature gas can be efficiently cooled.

In the fluid processing apparatus 1 of the present embodiment, the design guideline of the structure in which the fluid collides perpendicularly with the wall of the flow path can be applied regardless of whether the apparatus is large or small, or regardless of the shape.

In addition, it can be designed so that high-velocity collision occurs within the range allowed by the processing cost. If the flow rate is designed to be large, it is advisable to increase the flow path cross-sectional area within a range commensurate with the processing cost while maintaining the relationship.

In the fluid processing apparatus 1 of the present embodiment, the material can be selected according to the temperature to be used, the heat medium environment, and the cutting cost of the substrate.

(Fluid processing method)
Next, a fluid processing method using the above fluid processing apparatus 1 will be described. First, the fluid introduced into the first flow path P1 by the first heat exchange unit 10 is heated to a predetermined temperature (first heat exchange step).

The first heat exchange unit 10 has a first substrate provided with a concave portion of the first substrate on the surface and a first airtight plate laminated on the first substrate, and the surface of the concave portion of the first substrate of the first substrate. Between the surface of the first sealing plate and the surface of the first sealing plate on the side of the first substrate, a plurality of first sub-flow passages SP1 extending in the first direction extend in a second direction perpendicular to the first direction and are adjacent to each other. It includes a plurality of second sub-channels SP2 that communicate with the first sub-channel SP1.

The first that the fluid introduced into the first sub-flow path SP1 at one end flows to the first sub-flow path SP1 at the other end via the first sub-flow path SP1 and the second sub-flow path SP2. A fluid is flowed through the first heat exchange section 10 provided with the flow path P1 so that the flow velocity of the fluid flowing through the second sub-flow path SP2 is faster than the flow velocity of the fluid flowing through the first sub-flow path SP1. As a result, heat exchange is performed by causing the fluid to collide perpendicularly with the wall of the first secondary flow path SP1, and the fluid introduced into the first flow path P1 is heated to a predetermined temperature.

Next, after the first heat exchange step, the fluid introduced into the second flow path P2 by the second heat exchange unit 20 is cooled from a predetermined temperature (second heat exchange step).

The second heat exchange unit 20 has a second base having a second base recess provided on its surface and a second sealing plate laminated on the second base, and has a surface of the second base recess of the second base. And the surface of the second sealing plate on the second substrate side, a plurality of third auxiliary flow paths SP3 extending in the third direction and extending in the fourth direction perpendicular to the third direction and adjacent to each other. It includes a plurality of fourth sub-channels SP4 that communicate with the third sub-channel SP3.

A fluid heated to a predetermined temperature is introduced into the third sub-flow path SP3 at one end, passes through the third sub-flow path SP3 and the fourth sub-flow path SP4, and is the third sub at the other end. A fluid so that the flow velocity of the fluid flowing through the fourth subchannel SP4 is faster than the flow velocity of the fluid flowing through the third subchannel SP3 in the second heat exchange portion provided with the second flow path P2 flowing to the flow path SP3. Flow. As a result, heat exchange is performed by causing the fluid to collide perpendicularly with the wall of the third secondary flow path SP3, and the fluid introduced into the second flow path P2 is cooled from a predetermined temperature.

(Action / effect of fluid treatment equipment and fluid treatment method)
According to the fluid treatment apparatus and the fluid treatment method of the present embodiment, the heat treatment and the cooling treatment can be continuously performed. For example, when the fluid is water, by instantly heating and cooling it, it is possible to obtain a small-sized water molecule population that was difficult to obtain with ordinary distilled water or the like.

Here, one water molecule _{is referred to as [H 2} O], and one water molecule group is referred to as “[H ₂ O] _n ”. n is an index of the size of one water molecule population, and the n value and its distribution change at a certain moment. There are various opinions about the n value of the molecular population of water under equilibrium. It is considered that components having different n values are mixed in actual water. It is considered that the probability distribution of the n value of the stable water molecular population existing in a certain equilibrium state is constant. However, the probability distributions when heated or cooled rapidly are different, and it is considered that the distribution becomes stable and stable with the passage of time.

In the first heat exchange section of the present embodiment, a group of water molecules having a large n value collides with the wall of the first subchannel and exchanges heat with the wall of the first subchannel. In normal saturated steam heating, it is necessary to apply pressure to heat to a temperature higher than 100 ° C, but in the heat exchange in the first heat exchange section described above, the temperature can be freely set without depending on the pressure. be. In such a first heat exchange unit, for example, by rapidly heating to 500 ° C., the n value of the water molecule population can be reduced, and for example, steam having n of 1 or close to 1 can be obtained.

In the second heat exchange section of the present embodiment, water vapor collides with the wall of the third subchannel and exchanges heat with the wall of the third subchannel. When water vapor collides with a cold wall, it is deprived of heat energy and becomes water. In such a second heat exchange section, for example, by rapidly cooling from a temperature of 500 ° C. or higher to about room temperature, the liquid in the non-equilibrium state before the water molecules return to the normal stable state of water. Can be water. The distribution of n-values of water thus obtained is different from that of normal stable water. If the water having a different probability distribution of n values in the above water molecule population is left unattended, the distribution of n values changes with time and becomes normal water.

Rapidly cooled water, which is presumed to contain a population of water molecules with a small n-value, easily penetrates into cells, epidermis, dermis, and subcutaneous tissue on the surface of human skin. Toners and cosmetics using water containing a group of water molecules having a small n value have high penetrating power into the skin and can be expected to have an effect of improving skin quality.

<First Example>
(Structure example of the first heat exchange section and the second heat exchange section)
8A and 8B are schematic views showing the configuration of the fluid treatment apparatus according to the first embodiment, FIG. 8A shows a plan view of a ZZ cross section of the first heat exchange section, and FIG. 8B shows a first heat. The YY cross-sectional view of the exchange part is shown, and FIG. 8C shows the XX cross-sectional view of the first heat exchange part.

The first heat exchange unit 300 has a substrate 301 on which a groove serving as a first flow path is formed, and a sealing plate 302 that seals the groove to form a flow path. At least one of the substrate 301 and the sealing plate 302 is heated, and the fluid flows through the flow path to exchange heat with the wall of the substrate 301. Buffer tabs 305 and 306 as lateral groove flow paths for collecting fluids are provided at both ends of the flow path of FIG. 8 (A), and a fluid introduction path 303 and a fluid lead-out path 304 are provided connected to them. be.

Tabs T1, T2, T3, T4, and T5 are formed as the first sub-flow path constituting the first flow path. The tabs T1 to T5 have a width W1 and a depth DD. Tabs T1 to T5 are represented by tab T.

A channel flow path is formed as a second sub-flow path constituting the first flow path. Channel channels connected to the same tab channel are referred to as channel sequences, and the channel sequences are numbered in order and are referred to as channel sequences CH1, CH2, CH3, CH4, CH5, and CH6. Channels in the same channel sequence are numbered and the channels in channel sequence CH2 are designated as channels CH21, CH22, CH23, CH24, CH25, CH26 (see FIG. 8B). The channels of the channel sequence CH1 are referred to as channels CH11, CH12, CH13, CH14, CH15, CH16, and CH17 (see FIG. 8C). Channel CH on behalf of channel sequences CH1, CH2, CH3, CH4, CH5, CH6 (channels CH21, CH22, CH23, CH24, CH25, CH26, CH11, CH12, CH13, CH14, CH15, CH16, CH17 ...) Notated as.

The arrangement pitch PT2 of the second subchannel is the pitch of the channel arrangement of the same channel row. The channel CH has a width W2, a depth D, and a length L2.

The fluid passes through the tab T, which is the first subchannel, and the channel CH, which is the second subchannel.

The relationship between the cross-sectional area of the tab T (hereinafter referred to as St) and the cross-sectional area of the channel CH (hereinafter referred to as Sc) will be described. Since the structure is such that the fluid discharged from the channel CH flows separately in two directions, there is no change in the velocity of the fluid when 2Sc = St, and the fluid cannot be accumulated. That is, it is considered to be a dimension in which a flow having the same velocity without turbulence is formed.

When 2Sc> St, that is, when the fluid velocity of the channel CH is slower than the fluid velocity of the tab T, the fluid does not collide with the wall of the tab T, or the fluid becomes laminar. Forming a laminar flow along the wall of the tab T without turbulence of the fluid significantly reduces the efficiency of heat exchange with the wall. The fluid collides with the wall except for the condition where laminar flow is possible, and 2Sc <St.

The length L2 of the channel CH and the width W1 of the tab T are determined as follows. In order for the flow obtained with the high flow velocity in the channel CH to reach the wall of the tab T and collide with the wall, it is desirable that at least the width W1 of the tab T is shorter than the length L2 of the channel CH. Assuming that the distance at which the high flow velocity of the flow leaving the channel CH is transmitted to the wall corresponds to the length L2 of the channel CH, the fluid will collide with the wall when L2> W1.

The relationship between the arrangement of the channel CHs in the channel rows adjacent to each other with the tab T in between is determined as follows. When the central axes of the channel CHs of the adjacent channel rows are aligned, the fluid passing through the channel CH crosses the sandwiched tab T as a uniaxial laminar flow. That is, it does not collide with the wall of the tab T. Even if they do not exactly match, when the channel CHs of adjacent rows are overlapped, if there is an overlapping part, the fluid will flow preferentially to the flow path that is easy to flow, so a flow that does not collide with the wall of the tab T is formed. .. Therefore, it is essential that the channel CHs of adjacent channel rows do not overlap.

Expressed using the arrangement pitch PT2 of the channel CH and the width W2 of the channel CH, when PT2 ≦ 2W2, a portion overlapping the channel CH of the adjacent row is generated. Therefore, PT2> 2W2 is set so that the channels in the adjacent rows do not overlap each other.

In this embodiment, the first heat exchange unit 300 is configured as described above. The second heat exchange unit is realized by the same configuration as the first heat exchange unit 300, and illustration and description thereof will be omitted. However, the second heat exchange unit is provided so that the fluid can be cooled to a temperature lower than that of the first heat exchange unit 300. A fluid heat treatment apparatus is configured by having a first heat exchange unit and a second heat exchange unit as described above.

<Second Example>
(Structure example of the first heat exchange section and the second heat exchange section)
FIG. 9 is a schematic view showing the configuration of the fluid processing apparatus according to the second embodiment.

The first heat exchange unit 300 incorporates a cylindrical substrate 301 and a cylinder-shaped sealing plate 302 for accommodating the cylindrical substrate 301. The surface of the substrate 301 is in close contact with the inner wall of the sealing plate 302. The connections are welded to prevent fluid leakage to the outside.

The fluid introduced by pressurizing from the introduction path 303 passes through the circumferential grooves G1 to G6 which are the first auxiliary flow paths, and passes through the connecting grooves C1A, C2B, C3A, C4B, C5A, and C6B which are the second auxiliary flow paths. It becomes a high-speed fluid as it passes. The high-speed fluid collides vertically with the walls of the circumferential grooves G1 to G6 at high speed. When colliding vertically, a stagnation layer that resists heat transfer is formed or thinned.

The substrate 301 is heated by the heater 400 fed from the heater feeder line 401. The heater 400 is made of silicon carbide and can be heated up to 1000 ° C.

The sealing plate 302 and the base 301 are made of SUS310S and are resistant to heating up to 1000 ° C.

In this embodiment, the first heat exchange unit 300 is configured as described above. The second heat exchange unit is realized by the same configuration as the first heat exchange unit 300, and illustration and description thereof will be omitted. However, the second heat exchange unit is provided so that the fluid can be cooled to a temperature lower than that of the first heat exchange unit 300. A fluid heat treatment apparatus is configured by having a first heat exchange unit and a second heat exchange unit as described above.

<Third Example>
(Structure example of the first heat exchange section and the second heat exchange section)
FIG. 10 is a schematic cross-sectional view showing the configuration of the fluid treatment apparatus according to the third embodiment. The first heat exchange unit 300 has a base 301 and sealing plates 302A and 302B. Tabs G11 and G21 are formed on the upper surface of the substrate 301, and tabs G12 and G22 are formed on the lower surface. The tabs G11, G21, G12, and G22 are also referred to as tabs G on behalf of the tabs G11, G21, G12, and G22. Sealing plates 302A and 302B are provided on the upper surface and the lower surface of the substrate 301, and a part of the flow path is formed by the tab G and the sealing plates 302A and 302B.

The tab G12 is arranged in a plane straddling the tabs G11 and G21, and is connected to the tabs G11 and G21 by the connecting holes H12 and H21. The tab G21 is arranged in a plane straddling the tabs G12 and G22, and is connected to the tabs G12 and G22 by the connecting holes H21 and H22. The connecting holes H12, H21, and H22 are also referred to as the connecting holes H on behalf of the connecting holes H12, H21, and H22.

A fluid introduction path 303 is connected to the tab G11 at the upstream end of the tab arrangement. A fluid lead-out path 304 is connected to the tab G22 at the downstream end of the tab arrangement. The fluid F1 introduced from the introduction path 303 is discharged as the fluid F2 from the lead-out path 304 via the closed tabs G11, G12, G21, G22 and the connecting holes H12, H21, H22.

The sealing plates 302A and 302B are provided with heaters 400A and 400B so that they can be heated. The number of heaters can be freely adjusted according to the desired temperature and available power.

The fluid that has passed through the narrow connecting hole H12 increases in speed and collides vertically with the sealing plate 302B at high speed. In order to cause this vertical high-speed collision, the distance between the sealing plate 302B surrounding the tab G12 and the outlet of the connecting hole H12 is shorter than the length of the connecting hole H12. With such a structure, a stagnation layer between the vertical high-speed fluid and the wall of the sealing plate 302B cannot be formed or becomes thin. Heat exchange is instantaneously performed between the fluid and the sealing plate 302B, and the fluid is heated.

The same thing happens in the connecting holes H21, H22. When the vertical high-speed collision is repeated in this way, the heat of the sealing plates 302A and 302B heated by the heaters 400A and 400B is transferred to the fluid with high efficiency. As a result, the temperature of the fluid F2 becomes close to the temperature of the sealing plates 302A and 302B. The verticality of the high-speed collision does not have to be strict, as it is only necessary that the stagnation layer is not formed or thinned. In this way, heat exchange is instantaneously performed in the first heat exchange unit 300 shown in FIG. 10, and a heated fluid can be obtained.

In this embodiment, the first heat exchange unit 300 is configured as described above. The second heat exchange unit is realized by the same configuration as the first heat exchange unit 300, and illustration and description thereof will be omitted. However, the second heat exchange unit is provided so that the fluid can be cooled to a temperature lower than that of the first heat exchange unit 300. A fluid heat treatment apparatus is configured by having a first heat exchange unit and a second heat exchange unit as described above.

<Fourth Example>
(Structure example of the first heat exchange section and the second heat exchange section)
FIG. 11 is a schematic view showing the configuration of the fluid processing apparatus according to the fourth embodiment. In the first heat exchange section 300, a flow path is formed by sandwiching the substrate 301 between the sealing plates 302A and 302B. The sealing plates 302A and 302B are provided with heaters 401A and 401B.

The base 301 and the sealing plates 302A and 302B were made of stainless steel, and the standard SUS316L was used. Both sides of the substrate 301 were processed to provide tabs G11, G12, G21, G22, G31, G32, G41, G42, G51, G52, and G61 in a space of 2 mm. The tab depth is 1 mm and the area is 4 mm × 30 mm. Five connecting holes H12, H21, H22, H31, H32, H41, H42, H51, H52, and H61 for connecting the tabs were drilled per tab. The connecting hole has a diameter of 2 mm and a length of 3 mm.

The distance of the wall colliding from the outlet is shorter than the length of the connecting hole so that the fluid exits the connecting hole at high speed and collides with the wall surrounding the tab at high speed. This relationship between the distance and the length of the connecting hole is an effective relationship for efficiently causing heat exchange.

The connecting holes H11 and H62 connecting the fluid introduction path 303 and the fluid lead-out path 304 and the tab were drilled. The introduction path 303 was welded and then washed, and the sealing plates 302A and 302B and the base 301 were welded in the periphery. This formed a fluid flow path.

Heaters 401A and 401B are inserted into the sealing plates 302A and 302B. It is drawn so that the heater can be seen by protruding from the sealing plate. The heater may actually be inside.

The heater may be in the center of the sealed plate. Although four examples are shown, the number of heaters may be one and the design is free.

In this embodiment, the first heat exchange unit 300 is configured as described above. The second heat exchange unit is realized by the same configuration as the first heat exchange unit 300, and illustration and description thereof will be omitted. However, the second heat exchange unit is provided so that the fluid can be cooled to a temperature lower than that of the first heat exchange unit 300. A fluid heat treatment apparatus is configured by having a first heat exchange unit and a second heat exchange unit as described above.

<Application example>
(Application to lotion water)
Water for lotion can be produced by the above-mentioned fluid treatment apparatus and fluid treatment method. The lotion water is produced by heating the raw material fluid to a predetermined temperature by the first heat exchange section provided with the first flow path, and then cooling the raw material fluid from the above predetermined temperature by the second heat exchange section. Water is used as the raw material fluid.

The first heat exchange unit has a first substrate provided with a recess of the first substrate on the surface and a first airtight plate laminated on the first substrate. A first flow path is provided between the surface of the recess of the first substrate of the first substrate and the surface of the first sealing plate on the side of the first substrate. The first flow path is a plurality of first sub-channels extending in the first direction and a plurality of second channels extending in a second direction perpendicular to the first direction and communicating with adjacent first sub-channels. Includes a secondary flow path. The raw material fluid containing water or water vapor introduced into the first sub-channel at one end flows through the first sub-channel and the second sub-channel to the first sub-channel at the other end. .. Here, the raw material fluid is flowed so that the flow velocity flowing through the second subchannel of the raw material fluid is faster than the flow velocity flowing through the first subchannel. As a result, heat exchange is performed by causing the raw material fluid to collide perpendicularly with the wall of the first secondary flow path, and the raw material fluid introduced into the first flow path is heated to a predetermined temperature.

The second heat exchange unit has a second base having a recess on the surface of the second base and a second sealing plate laminated on the second base. A second flow path is provided between the surface of the recess of the second base of the second base and the surface of the second sealing plate on the side of the second base. The second flow path is a plurality of third sub-channels extending in the third direction and a plurality of fourth channels extending in a fourth direction perpendicular to the third direction and communicating with adjacent third sub-channels. Includes a secondary flow path. The raw material fluid heated to a predetermined temperature is introduced into the third sub-channel at one end, passes through the third sub-channel and the fourth sub-channel, and is the third sub-channel at the other end. Flow up to. Here, the raw material fluid is flowed so that the flow velocity flowing through the fourth subchannel of the raw material fluid is faster than the flow velocity flowing through the third subchannel. As a result, heat exchange is performed by causing the raw material fluid to collide perpendicularly with the wall of the third secondary flow path, and the raw material fluid introduced into the second flow path is cooled from a predetermined temperature.

The lotion water of this application example is produced by the above-mentioned fluid treatment apparatus and fluid treatment method. In the first heat exchange unit, water or steam is made to collide with the wall of the first subchannel to exchange heat with the wall of the first subchannel. In the first heat exchange unit, the gas phase can be independently heated in a state where the liquid phase and the gas phase are not in contact with each other, that is, in a state where the liquid phase and the gas phase do not maintain an equilibrium state. Further, in normal water heating, it is necessary to apply pressure to heat to a temperature higher than 100 ° C., but in the heat exchange in the first heat exchange section described above, the temperature can be freely set without depending on the pressure. Is. In such a first heat exchange unit, for example, by rapidly heating to 500 ° C. or higher, steam having an n value of 1 or close to 1 can be obtained.

In the second heat exchange section, water vapor is converted into water. In such a second heat exchange section where water vapor molecules collide with the wall of the third subchannel to exchange heat between the water molecules and the wall of the third subchannel and rapidly cool, for example, 500 ° C. or higher. Cool from the temperature of 1 to about room temperature within 1 second. As a result, water can be converted into water in a non-equilibrium state before the water molecules return to the normal stable state of water. The water thus obtained is considered to contain a large amount of components of a water molecule group having an n value smaller than that of ordinary stable water, and is a water for lotion preferably used for a lotion. This water is referred to as SA (Single Active) water here. SA water is not stable because it is produced in a non-equilibrium manner. It is considered that the probability distribution of the n value of the water molecule population changes with the passage of time to normal water in a stable equilibrium state.

Water containing a population of water molecules having a small n value easily permeates cells, for example, cells on the surface of human skin, epidermis, dermis, subcutaneous tissue, and the like. Toners and cosmetics using water (SA water) containing a group of water molecules having a small n have a high penetrating power to the skin and can be expected to have an effect of improving skin quality.

(Application to cosmetics)
Since the above SA water itself has the property of easily penetrating into the skin and plants, it can be used as cosmetics (toner), but the degree of antibacterial ability is unknown. SA water to which an antibacterial substance having an antibacterial ability such as an antibacterial agent (benzyl glycol) is added can be used as a cosmetic (toner) having an antibacterial ability.

Further, the gel-like cosmetics obtained by adding vitamin C to SA water or the above-mentioned cosmetics having antibacterial ability (cosmetic water) are cosmetics having a whitening effect by vitamin C. The above-mentioned water for lotion can realize a gel-like cosmetic product containing no emulsifier.

(Application of steam gas)
When water is steamed above 100 ° C. (called superheated steam), it can be heated or dried in an oxygen-free state. For example, when high-temperature steam of about 300 ° C. is brought into contact with the meat, the muscles of the meat are changed to have the effect of changing to a soft meat that is easy to chew. This can be applied to safe barbecues that do not use flames.

The gas having a high chemical potential taken out by contacting the high temperature steam with a gas containing waste or organic matter can be reused as an energy resource. Therefore, a fluid processing apparatus that does this can be applied to an organic matter processing apparatus.

<Fifth Example>
(Toner sensory test 1)
A test was conducted in which SA water was impregnated into human skin. SA water was produced by a fluid treatment device in which a fluid heat exchange device "heat beam cylinder (manufactured by Filtech)" was applied to each of the first heat exchange section and the second heat exchange section. The subject was a 66-year-old man with an amyloid plaque on his face. Every day around 6 am and 23:00 pm, SA water was sprayed 5 to 10 times on the entire face and rubbed against the skin of the face with the palm of the hand for massage. SA water used within one month after each production. When the test started in November 2016, in November 2019, some of the former amyloid plaques had disappeared, became smaller, and became lighter in color. It is considered that SA water easily permeates cells, for example, cells on the surface of human skin, epidermis, dermis, subcutaneous tissue, etc., and has high penetrating power to the skin, leading to improvement of skin quality.

(Toner sensory test 2)
The effects of the above-mentioned lotion sensory test 1 when a plurality of subjects continued for one year or more are summarized as follows. The period was from December 2017 to March 2019, and the subjects were 20 to 76 years old and consisted of 100 subjects including men and women.

The following results were obtained when the effects were aggregated assuming that multiple answers were possible.
(1) The skin is refreshing, moist, glossy, soft, and moisturized (55 cases).
(2) Spots, amyloid plaques, dullness, sunburn become lighter, wrinkles become lighter (21 cases)
(3) Repair of rough skin, improvement of atopic skin, elimination of troubles, elimination of itch (16 cases)
(4) Accelerate penetration of lotion and improve make-up glue (11 cases)
(5) The skin becomes bright and transparent (10 cases)
As described above, by applying SA water, the effect as a lotion was obtained as a sensory evaluation by the subject. SA water is water containing a large number of water molecules having a small n value, and easily penetrates into cells, for example, cells on the surface of human skin, epidermis, dermis, subcutaneous tissue, etc., and has high penetrating power to the skin. It is thought that this led to the improvement of skin quality.

1 Fluid processing device 10 1st heat exchange unit 20 2nd heat exchange unit 30 Introduction path 31A Outlet path 31B Introduction path 32 Outlet path 40 Liquid P1 1st flow path P2 2nd flow path SP1 1st sub flow path SP2 2nd sub Flow path SP3 3rd sub-flow path SP4 4th sub-flow path

Claims (10)

It has a first substrate provided with a first substrate recess on the surface and a first sealing plate laminated on the first substrate, and the surface of the first substrate recess of the first substrate and the first sealing plate A plurality of first sub-fluids extending in the first direction and the first side flow extending in a second direction perpendicular to the first direction and adjacent to the surface on the first substrate side. A fluid introduced into the first sub-channel at one end includes a plurality of second sub-channels communicating with the path, and the fluid introduced into the first sub-channel passes through the first sub-channel and the second sub-channel to the other. Heat exchange is performed by flowing to the first sub-flow path at the end of the first sub-flow path and colliding perpendicularly with the wall of the first sub-flow path, and the flow velocity of the fluid flowing through the second sub-flow path is the first side flow. A first heat exchange unit is provided with a first flow path configured to be faster than the flow velocity of the fluid flowing through the path, and heats the fluid introduced into the first flow path to a predetermined temperature. ,
It has a second substrate provided with a second substrate recess on its surface and a second sealing plate laminated on the second substrate, and the surface of the second substrate recess of the second substrate and the second sealing plate A plurality of third sub-fluids extending in the third direction and the third side flow extending in the fourth direction perpendicular to the third direction and adjacent to the surface on the second substrate side. A fluid introduced into a third sub-channel at one end, including a plurality of fourth sub-channels communicating with the path, passes through the third sub-channel and the fourth sub-channel to the other. The fluid flows to the third sub-flow path at the end of the water and collides perpendicularly with the wall of the third sub-flow path to exchange heat, and the flow velocity of the fluid flowing through the fourth sub-flow path is the third side flow. The first heat exchange is provided with a second flow path configured to be faster than the flow velocity of the fluid flowing through the path, and cools the fluid introduced into the second flow path from the predetermined temperature. A fluid processing apparatus including a second heat exchange unit directly connected to the downstream side of the unit. The cross-sectional area S1 of the first sub-channel is larger than twice the cross-sectional area S2 of the second sub-channel, and the length L2 of the second sub-channel is larger than the width W1 of the first sub-channel. It is satisfied at the same time that it is long and the arrangement pitch of the second sub-channel is larger than twice the width thereof, or a combination of either of them is satisfied.
The cross-sectional area S3 of the third sub-flow path is larger than twice the cross-sectional area S4 of the fourth sub-flow path, and the length L4 of the fourth sub-flow path is larger than the width W3 of the third sub-flow path. The fluid processing apparatus according to claim 1, wherein it is satisfied at the same time that the length and the arrangement pitch of the fourth subchannel are larger than twice the width thereof, or a combination of either of them is satisfied. The fluid treatment apparatus according to claim 1 or 2, wherein the first substrate and the second substrate have any shape of a plate, a cylinder, a cylinder, and a prism, respectively. Claims 1 to 3 wherein the first substrate, the first sealing plate, the second substrate, and the second sealing plate are each composed of metal, graphite, ceramics, plastic, a composite material, or a combination thereof. The fluid processing apparatus according to any one of the above items. The fluid treatment apparatus according to claim 4, wherein the composite material is a material in which at least one selected from metal, carbon nanotubes, graphene and carbon fiber is composited with plastic. The fluid treatment apparatus according to claim 5, wherein the metal is a fibrous metal. It has a first substrate provided with a first substrate recess on the surface and a first sealing plate laminated on the first substrate, and the surface of the first substrate recess of the first substrate and the first sealing plate A plurality of first sub-fluids extending in the first direction and the first side flow extending in a second direction perpendicular to the first direction and adjacent to the surface on the first substrate side. A fluid introduced into the first sub-channel at one end includes a plurality of second sub-channels communicating with the path, and the fluid introduced into the first sub-channel passes through the first sub-channel and the second sub-channel to the other. In the first heat exchange section provided with the first flow path that flows to the first sub-flow path at the end of the The fluid is flowed so as to be faster than the flow velocity, and heat exchange is performed by causing the fluid to collide perpendicularly with the wall of the first secondary flow path, and the fluid introduced into the first flow path is brought to a predetermined temperature. The first heat exchange process to heat and
It has a second substrate provided with a second substrate recess on its surface and a second sealing plate laminated on the second substrate, and the surface of the second substrate recess of the second substrate and the second sealing plate A plurality of third sub-fluids extending in the third direction and the third side flow extending in the fourth direction perpendicular to the third direction and adjacent to the surface on the second substrate side. A plurality of fourth sub-channels communicating with the path are included, and the fluid heated to a predetermined temperature is introduced into a third sub-channel at one end, and the third sub-channel and the fourth sub-channel are introduced. In the second heat exchange section provided with the second flow path that flows to the third sub-flow path at the other end via the flow path, the flow velocity of the fluid flowing through the fourth sub-flow path is the third. The fluid is flowed so as to be faster than the flow velocity of the fluid flowing through the subchannel, and the fluid is collided perpendicularly with the wall of the third subchannel to exchange heat and is introduced into the second channel. A fluid treatment method comprising a second heat exchange step performed after the first heat exchange step, which cools the fluid from the predetermined temperature. It has a first substrate provided with a first substrate recess on the surface and a first sealing plate laminated on the first substrate, and the surface of the first substrate recess of the first substrate and the first sealing plate A plurality of first sub-fluids extending in the first direction and the first side flow extending in a second direction perpendicular to the first direction and adjacent to the surface on the first substrate side. The raw material fluid containing water or water vapor introduced into the first sub-channel at one end, including a plurality of second sub-channels communicating with the path, is the first sub-channel and the second sub-channel. The flow velocity of the raw material fluid flowing through the second sub-channel is the first sub-passage in the first heat exchange section provided with the first sub-channel that flows to the first sub-channel at the other end via The raw material fluid was flowed so as to be faster than the flow velocity flowing through the flow path, and heat exchange was performed by causing the raw material fluid to collide perpendicularly with the wall of the first sub-flow path, and the raw material fluid was introduced into the first flow path. After heating the raw material fluid to a predetermined temperature,
It has a second substrate provided with a second substrate recess on its surface and a second sealing plate laminated on the second substrate, and the surface of the second substrate recess of the second substrate and the second sealing plate A plurality of third sub-fluids extending in the third direction and the third side flow extending in the fourth direction perpendicular to the third direction and adjacent to the surface on the second substrate side. The raw material fluid, which includes a plurality of fourth sub-channels communicating with the path and is heated to a predetermined temperature, is introduced into the third sub-channel at one end, and the third sub-channel and the fourth sub-channel are introduced. The flow velocity of the raw material fluid flowing through the fourth sub-channel is the flow velocity of the raw material fluid in the second heat exchange portion provided with the second flow path that flows to the third sub-channel at the other end via the sub-channel. The raw material fluid is flowed so as to be faster than the flow velocity flowing through the third secondary flow path, and heat exchange is performed by causing the raw material fluid to collide perpendicularly with the wall of the third secondary flow path and introduced into the second flow path. Manufactured by cooling the raw material fluid produced from the predetermined temperature.
Water for lotion. The lotion water according to claim 8 and
Toner containing antibacterial substances. The lotion water according to claim 8 or the lotion according to claim 9 and
Contains Vitamin C
Cosmetics that are gel-like.

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