JP2016006373A - Heat exchange body and process of manufacture of heat exchange body - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a heat exchange body showing a higher heat exchanging efficiency and a higher mechanical strength than that of the prior art.SOLUTION: A heat exchange body 1 includes a segment 10 of a ceramic sintered body formed into a honeycomb structure that comprises: a plurality of first slits 21 in which several partition walls 17 defining cells belonging to the same row every other row of cells 15 are excluded by the same length at a first end surface 11 side, passing in a direction crossing at a right angle with an axial direction thereof and keeping the axial length constant; a plurality of second slits 22 in which several partition walls defining cells belonging to a row different from the cells with the first slits formed are excluded by the same length at a second end surface 12 side, passing in a direction crossing at a right angle with an axial direction thereof and keeping the axial length constant; a first seal part 31 for sealing an opening at the first end surface of each of the first slits and an opening at the second side surface 14; and a second seal part 32 for sealing an opening at the second end surface side of each of the second slits and an opening at the first side surface 13.

Description

  The present invention relates to a heat exchange body using a ceramic honeycomb structure and a method for producing the heat exchange body.

  As a heat exchanger that recovers heat from high-temperature exhaust gas and wastewater, a honeycomb structure having a plurality of cells that are made of ceramics and partitioned by partition walls extending in a single axial direction has been used. Some have been proposed (see, for example, Patent Documents 1 and 2). Here, the heat exchanging body of Patent Document 1 exchanges heat between a fluid that flows through a plurality of cells penetrating in one direction in the honeycomb structure and a fluid that flows along the outer peripheral surface of the honeycomb structure. It is. In this case, although the fluid flowing through the outer cells close to the outer peripheral surface of the honeycomb structure can efficiently exchange heat with the fluid flowing along the outer peripheral surface, the fluid flowing through the inner cells of the honeycomb structure However, there is a problem that the efficiency of heat exchange with the fluid flowing along the outer peripheral surface is poor.

  On the other hand, in the heat exchange element of Patent Document 2, every other row of cells penetrating the honeycomb structure is sealed with the same row at both end faces to form a sealed portion, and the cells of the sealed row A slit formed by perforating a partition wall from a right angle direction is formed to be elongated so as to extend from the vicinity of the sealing portion on one end side to the vicinity of the sealing portion on the other end side. With such a configuration, heat exchange is performed between the fluid flowing through the cell that is not sealed at both end faces and the fluid flowing through the slit penetrating in the orthogonal direction via the partition wall. In this case, since heat exchange is performed between the fluids flowing in the orthogonal directions, there is a problem that the contact time through the partition walls of the two fluids is short, and the heat exchange efficiency is poor. Further, in the heat exchange element of Patent Document 2, the row in which the slit is formed is joined to the partition in the adjacent row only by the sealing portion or only by the partition that remains slightly between the sealing portion and the slit. Therefore, the mechanical strength may be insufficient.

  Accordingly, one of the present applicants uses a ceramic honeycomb structure as an air preheating device that preheats air by exchanging heat between exhaust and air, and distributes exhaust and air through adjacent cell rows. In addition, a heat exchanger having a structure in which the flow directions are opposed to each other has been proposed (see Patent Document 3). As illustrated in FIGS. 8 and 9, this is because, in a prismatic honeycomb structure, the partition wall 105 is obliquely cut off at the axial end portion 101 side of a certain cell row, and then the axial end portion thereof. By sealing 101 and forming the sealing portion 110, a joint flow path 120 that opens to only one of the pair of side surfaces 102 and expands toward the opening end 121 is formed.

  Here, in FIGS. 8 and 9, (a) and (b) respectively represent adjacent cell rows, and FIG. 8 shows that adjacent cell rows each have a merge channel 120 on a different end 101 side. FIG. 9 is an example in which the cell rows having the joint channel 120 on both end portions 101 side and the cell rows having no joint channel are alternately arranged in parallel. In addition, the reason why the partition wall 105 is obliquely cut is intended to suppress the pressure loss. In order to make the opening area of the combined flow path 120 and the sum of the cross-sectional areas of the cells in the cell row substantially equal, The cutting angle θ is set to 20 ° to 45 °.

Further, Patent Document 4 discloses a heat exchanger using a honeycomb structure in which slits obtained by cutting partition walls that divide cells in a direction of 90 ° with respect to the cell extending direction are provided at both ends of the same cell row. Is described.
With the configuration as described above, the exhaust gas and the air circulate in the opposite direction along the axial direction of the cell in the adjacent cell, so that the contact time through the partition wall is long and heat exchange can be performed with high efficiency. . In addition, there is an advantage that the mechanical strength is high because there is a partition wall between adjacent cells except for an end portion to be excised.

JP 2012-189229 A JP 61-24997 A JP 2012-193946 A Japanese Patent No. 5514190

  The present invention is an extension of the above-described circumstances, and its object is a heat exchange body using a ceramic honeycomb structure, which has higher heat exchange efficiency and higher mechanical strength than before. It is providing the manufacturing method of a heat exchanger and a heat exchanger.

  In order to solve the above-described problems, a heat exchanger according to an aspect of the present invention is a ceramic sintered body formed in a honeycomb structure having a plurality of cells partitioned by partition walls extending in a single axial direction. A plurality of partitions partitioning the cells belonging to the same row in every other row of the cells on one first end face side of the pair of end faces where the cells are opened are the segments of the united body. A plurality of first slits that are formed by removing the same length from each other and that penetrate in a direction orthogonal to the axial direction and have a constant axial length, and the other of the pair of end faces The shaft, wherein a plurality of the partition walls defining the cells belonging to a column different from the cell in which the first slit is formed on the second end surface side are formed by removing the same length from the second end surface. Penetrates in a direction perpendicular to the direction Both the plurality of second slits having a constant axial length and the opening on the first end face side of each of the first slits are sealed, and one of the pair of openings on the side face side is sealed. The first sealing portion that seals only the opening and the opening on the second end face side of each of the second slits are sealed, and only one of the pair of openings on the side face side is sealed. And a second sealing portion that is sealed.

The ceramic material constituting the “ceramic sintered body” is not particularly limited, and silicon carbide, alumina, cordierite, mullite, or the like can be used.
The “first sealing portion” and the “second sealing portion” are formed of a dense material. The material is not particularly limited, but a material having the same or similar composition as that of the ceramic material constituting the ceramic sintered body is desirable because it has a close thermal expansion coefficient and is unlikely to generate thermal stress or a crack caused by this.

  Since the “first slit” and the “second slit” penetrate in the direction orthogonal to the axial direction of the cell, both are opened on the side surface of the segment of the honeycomb structure. One of the pair of openings on the side surface side is sealed with the first sealing portion, and one of the pair of openings on the side surface side is the second sealing portion. It may be different or the same as the side surface where the second slit is opened by being sealed. When the side surface where the first slit opens and the side surface where the second slit opens are different, the discharge direction of the fluid with a temperature difference discharged from each of the first slit and the second slit after heat exchange is different. There is an advantage that it is easy to maintain the temperature difference. On the other hand, when the side surface where the first slit opens and the side surface where the second slit opens are the same, the entire heat exchanger provided with pipes communicating with the openings of the first slit and the second slit is compact. There are advantages that can be made.

  In the heat exchanger of this configuration, the first fluid that flows in from the cell that opens at the first end surface, flows out from the opening of the second slit that is not sealed, and flows from the cell that opens at the second end surface, and seals. Heat can be exchanged with the second fluid flowing out from the opening of the first slit which is not stopped through the partition wall. Or, it flows in from the opening of the first slit that is not sealed, flows out from the cell that opens at the second end surface, and flows from the opening of the second slit that is not sealed, Heat can be exchanged with the second fluid flowing out from the open cell via the partition wall. Therefore, since the first fluid and the second fluid flow in the opposite directions along the axial direction of the cells in the adjacent cells, the contact time through the partition wall between the first fluid and the second fluid Is long and can exchange heat with high efficiency.

  In addition, in this configuration, a plurality of partition walls that partition cells belonging to the same column are removed from the first end surface by the same length to form the first slit, and the adjacent column is the same in the same column. A plurality of partition walls partitioning cells belonging to the column are removed from the second end surface by the same length to form a second slit. In other words, the lengths of the flow paths in which the first fluid flows in the cell and exchanges heat with the second fluid flowing in the adjacent cells are all equal in the same cell row, and the second fluid is The lengths of the flow paths that circulate in the cells and exchange heat with the first fluid that circulates in the adjacent cells are all equal in the same cell row. As a result, as will be described in detail later, the thermal efficiency is higher compared to the prior art (Patent Document 3) in which the lengths of the partition walls partitioning the cells in the same cell row are different by obliquely cutting the partition walls. It has become a thing.

  Further, in the heat exchange body using the honeycomb structure, the mechanical strength is mainly secured by the partition walls. However, in the heat exchange body of this configuration, the cells from which the partition walls are removed in order to form the first slit, The cells from which the partition walls are removed to form the two slits are cells in different rows. Therefore, in any row, except for one end face where the slit is formed, the partition between adjacent cells can be left with a considerable length. Thereby, even if it has a slit in the both end surface sides of a segment, the fall of the mechanical strength of the whole segment is suppressed, and it is a heat exchanger with high mechanical strength. In addition, since the first slit and the second slit are provided in the cells in different rows adjacent to each other, the heat exchange area between the first fluid and the second fluid is increased, and compared with the conventional technique (Patent Document 4). The thermal efficiency is higher.

  In addition, in this configuration, the lengths of the partition walls defining the cells communicating with the first slit are all equal in the same cell row, and the lengths of the partition walls defining the cells communicating with the second slit are Are all equal in the same cell column. Thereby, compared with the case where the length of a partition differs in the same cell row | line | column, it becomes the structure by which mechanical strength is not biased (a part with high mechanical strength and a low part are not unevenly distributed). .

In this heat exchanger, in addition to the above configuration, the ceramic sintered body may be a silicon carbide ceramic sintered body, and may further include an antioxidant layer of silicate glass formed on the surface of the partition wall.
Silicon carbide is a material having high thermal conductivity among ceramics. Specifically, the thermal conductivity of alumina, cordierite, and mullite is 9-30 W / m · K, 0.6 W / m · K, and 1.5 W / m · K, respectively. The thermal conductivity of silicon carbide is as high as 75 to 130 W / m · K. Therefore, the partition wall interposed between two fluids having different temperatures is excellent in thermal conductivity and can exchange heat with high efficiency.

In addition, the thermal expansion coefficient of silicon carbide is as small as about 4 × 10 ⁻⁶ / ° C. This is about 1/2 of the thermal expansion coefficient of alumina. That is, since silicon carbide has a high thermal conductivity and a low coefficient of thermal expansion, it has excellent thermal shock resistance. Therefore, the heat exchanger formed of the silicon carbide based ceramic sintered body is suitable as a heat exchanger that becomes high temperature by circulating a high-temperature fluid.
However, there is a problem that silicon carbide is oxidized when heated to a high temperature in an atmosphere in which oxygen is present. On the other hand, in the heat exchange element of this structure, the oxidation prevention layer of the silicate type glass is formed on the surface of the partition which is a silicon carbide ceramic sintered body. Since the silicic glass layer prevents the silicon carbide ceramic partition from contacting the oxygen, oxidation of the silicon carbide ceramic is effectively suppressed. The antioxidant layer can be formed on the side surface of the segment in addition to the surface of the partition wall.

In addition, since the antioxidant layer of silicate glass is formed on the surface of the partition wall, even if the partition wall is porous, the open pores are covered and filled with the antioxidant layer. Thereby, it can prevent that a fluid distribute | circulates through a partition and two fluids which should be heat-exchanged mix.
In addition, silicate glass softens and stretches at high temperatures and plastically deforms. Therefore, even if a crack occurs in the silicon carbide ceramic sintered body, which is a brittle material, the softened silicate glass fills it, so that the crack is prevented from extending and breaking. . Therefore, the heat exchanger of the present invention is more excellent in thermal shock resistance by being composed of a silicon carbide ceramic with high thermal shock resistance, and further comprising a layer of silicate glass, High mechanical strength at high temperatures.

  Next, a manufacturing method of a heat exchange body according to another aspect of the present invention is a ceramic structure formed body having a plurality of cells partitioned by partition walls extending in a single axial direction and made of a ceramic raw material. A molding step of molding the molded body, a firing step of firing the molded body to obtain a segment of a ceramic sintered body, and a first end face side of one of the pair of end faces where the cell opens in the segment. Every other row, the plurality of partition walls defining the cells belonging to the same row are excised from the first end surface by the same length, penetrated in a direction orthogonal to the axial direction, and the axial length is constant. A plurality of the partition walls that form a plurality of first slits and partition the cells belonging to a column different from the cells in which the first slits are formed on the other second end face side of the pair of end faces The second end A slit forming step of forming a plurality of second slits having the same length in the axial direction and penetrating in a direction orthogonal to the axial direction, and the first of the first slits Only one of the opening on the one end surface side and the pair of openings on the side surface side is sealed, and the opening on the second end surface side of each of the second slits and the pair of openings on the side surface side A sealing step of sealing only one of the openings.

  According to the manufacturing method of the present configuration, the above-described segment of the ceramic sintered body formed in the honeycomb structure including the plurality of cells partitioned by the partition walls extending in a single axial direction is opened. A plurality of partition walls defining the cells belonging to the same row are formed by removing the same length from the first end surface at every other row of the cells on one first end surface side of the pair of end surfaces. A plurality of first slits penetrating in a direction perpendicular to the axial direction and having a constant length in the axial direction, and the first slit on the other second end face side of the pair of end faces. A plurality of the partition walls partitioning the cells belonging to a column different from the cell in which the is formed are formed by removing the same length from the second end surface, and penetrate in a direction perpendicular to the axial direction. And the axial length is one A plurality of second slits, and an opening on the first end surface side of each of the first slits, and only one of the pair of side surface openings is sealed. A second sealing that seals the opening on the second end face side of each of the second slits and seals only one of the pair of openings on the side face side. A heat exchange element having a configuration of “comparing with a part” can be manufactured.

  Further, in this method for producing a heat exchange element, the ceramic raw material becomes a silicon carbide based ceramic sintered body by firing, and the firing step is performed in a non-oxidizing atmosphere, Before or after, the surface of the partition wall is coated with an antioxidant containing silicon dioxide, the segment coated with the antioxidant on the surface of the partition wall is heated, and the antioxidant is made of silicate glass An antioxidant layer forming step for fixing to the surface of the partition as an antioxidant layer may be further provided.

As the “ceramic raw material that becomes a silicon carbide ceramic sintered body by firing”, a raw material containing silicon carbide powder can be used. Further, a raw material containing a silicon source and a carbon source that generate silicon carbide by heating can be used, and silicon carbide can be sintered while reacting (reaction sintering).
The “non-oxidizing atmosphere” in the “baking step” can be an inert gas atmosphere such as argon or helium, a nitrogen gas atmosphere, a mixed gas atmosphere thereof, or a vacuum atmosphere.

  "Antioxidant" becomes silicate glass by heating. In addition to silicon dioxide, alkali metal components such as sodium oxide, potassium oxide and potassium carbonate, alkaline earth metal components such as calcium oxide and calcium carbonate, silicon (Simple silicon), boron oxide, aluminum oxide, aluminum hydroxide and the like can be contained. Here, since the alkali metal component and the alkaline earth metal component melt or soften silicon dioxide under heating, the adhesiveness and permeability to the partition wall can be adjusted by the content thereof. Further, the thermal expansion coefficient of the silicate glass can be adjusted by the content of boron oxide. In addition, the strength of the silicate glass can be adjusted by the content of aluminum oxide or aluminum hydroxide (which becomes aluminum oxide under heating).

The “antioxidant coating step” can be a step of applying and spraying an antioxidant, a step of immersing the segment in the antioxidant, or a step of impregnating the segment with the antioxidant. In addition to the surface of the partition wall, the side surface of the segment can be coated with an antioxidant.
According to the manufacturing method of this configuration, in addition to the above-described configuration, “the ceramic sintered body is a silicon carbide ceramic sintered body, and further includes an antioxidant layer of silicate glass formed on the surface of the partition wall” A heat exchanger having a configuration can be manufactured.

  As described above, according to the heat exchanging body and the method for manufacturing the heat exchanging body according to the present invention, the heat exchanging body using the honeycomb structure of ceramics has a higher heat exchanging efficiency than before, and the machine Heat exchanger with high mechanical strength and a method for producing the heat exchanger can be provided.

It is the perspective view seen from the (a) front side of the heat exchanger of a first embodiment of the present invention, and (b) the perspective view seen from the back side. It is (a) top view and (b) bottom view of the heat exchange body of FIG. It is the (a) XX line end view of the heat exchange body of FIG. 1, and (b) YY line end view. It is the perspective view seen from the (a) front side of the heat exchange element of the second embodiment of the present invention, and (b) the perspective view seen from the back side. It is the (a) XX line end view of the heat exchange body of FIG. 2, and (b) YY line end view. It is the graph which compared the heat recovery ratio about an Example and Comparative Examples 1 and 2. FIG. It is the graph which plotted the flow rate ratio of the 1st fluid and the 2nd fluid with respect to the cell row about the example and comparative example 1. (A) About the heat exchange body of patent document 3, (a) Schematic of the cross section of a certain cell row | line | column, (b) Schematic of the cross section of an adjacent cell row | line | column. It is (a) schematic of the cross section in a certain cell row | line about the other example of the heat exchange body of patent document 3, and (b) the schematic diagram of the cross section in an adjacent cell row | line | column. It is the schematic of the cross section in a certain cell row | line | column about the heat exchange body which concerns on a comparative example, and (b) The schematic drawing of the cross section in an adjacent cell row | line | column.

  Hereinafter, the heat exchanger 1 which is 1st embodiment of this invention is demonstrated using FIG. 1 thru | or FIG. The heat exchange element 1 of the first embodiment includes a ceramic sintered body segment 10 formed in a honeycomb structure including a plurality of cells 15 that are partitioned by partition walls 17 extending in a single axial direction. On the first end surface 11 side of the pair of first end surface 11 and second end surface 12 in which the cells 15 open, a plurality of partition walls 17 that partition the cells 15 belonging to the same row are arranged in every other row of the cells 15. A plurality of first slits 21 that are formed by removing the same length from one end surface 11 and that penetrate in a direction orthogonal to the axial direction and have a constant axial length, and a pair of first end surfaces 11 The plurality of partition walls 17 partitioning the cells 15 belonging to a different column from the cells 15 in which the first slits 21 are formed on the other second end surface 12 side of the second end surface 12 have the same length from the second end surface 12. Directly formed in the axial direction A plurality of second slits 22 that are penetrated in the direction to be fixed and have a constant axial length, and the openings on the first end surface 11 side of the respective first slits 21 are sealed, The first sealing portion 31 that seals only one of the pair of openings and the opening on the second end face 12 side of each second slit 22 are sealed, and the pair of side faces And a second sealing portion 32 that seals only one of the openings.

  Here, in the present embodiment, when the first slit 21 is formed, all the partition walls 17 that partition the cells 15 belonging to different columns are also removed from the first end surface 11 by the same length, and the second slit 22 is formed. , The partition walls 17 that partition the cells 15 belonging to different columns are all removed from the second end face 12 by the same length. In addition, the length from which the partition wall 17 is removed to form the first slit 21 is the same as the length from which the partition wall 17 is removed to form the second slit 22. That is, in the heat exchanger element 1 of the present embodiment, the lengths of the partition walls 17 that partition the cell 15 through which the first fluid flows and the cell 15 through which the second fluid flows are all the same.

Further, in the above configuration, the segment 10 of the heat exchange element 1 has a quadrangular prism shape, the first slit 21 is opened at the first side surface 13, and the second slit 22 is the second surface facing the first side surface 13. Opened on the side surface 14.
Further, in the heat exchange body 1, the ceramic sintered body is a silicon carbide based ceramic sintered body, and the heat exchange body 1 further includes an antioxidant layer (not shown) of silicate glass formed on the surface of the partition wall 17. It has.

  Such a heat exchanger 1 can be manufactured by the following manufacturing method. That is, the manufacturing method of the heat exchange element 1 according to the first embodiment (the manufacturing method according to the first embodiment) is a ceramic raw material, and is a plurality of cells partitioned by partition walls 17 extending in a single axial direction. 15, a forming step of forming a formed body having a honeycomb structure, a firing step of firing the formed body to obtain a segment 10 of a ceramic sintered body, a pair of first end surfaces 11 and first openings 11 in which the cells 15 are opened in the segment 10. A plurality of partition walls 17 partitioning cells 15 belonging to the same row are cut out from the first end surface 11 to the same length on every other row of cells 15 on the first end surface 11 side of the two end surfaces 12, and axial direction A plurality of first slits 21 penetrating in a direction perpendicular to the first axis 21 and having a constant axial length, and the second end face 12 side of the pair of first end faces 11 and second end faces 12 One slit 21 is in shape The plurality of partition walls 17 partitioning the cells 15 belonging to a different column from the formed cell 15 are excised from the second end face 12 by the same length, penetrated in a direction orthogonal to the axial direction, and the axial length is constant. A slit forming step for forming a plurality of second slits 22, an opening on the first end face 11 side of each first slit 21, and an opening on the first side face 13 side and the second side face 14 side of the first slit 21. Among the openings, only the opening on the second side face 14 side is sealed, the opening on the second end face 12 side of each second slit 22, the opening on the first side face 13 side of the second slit 22 and the second side. A sealing step of sealing only the opening on the first side surface 13 side out of the side surface 14 side opening.

  Further, in the manufacturing method of the present embodiment, in the above, the ceramic raw material becomes a silicon carbide ceramic sintered body by firing, and the firing step is performed in a non-oxidizing atmosphere and before the sealing step. Alternatively, the surface of the partition wall 17 is coated with an antioxidant containing silicon dioxide, the segment 10 whose surface is coated with the antioxidant is heated, and the antioxidant is used to prevent oxidation of the silicate glass. The method further includes a step of forming an antioxidant layer that adheres to the surface of the partition wall 17 as a layer.

  More specifically, in the forming step, the raw material that becomes a silicon carbide ceramic sintered body by firing is mixed with water together with additives such as a binder and a surfactant to form a kneaded product, and this is extruded. Thus, a formed article having a honeycomb structure is obtained. Here, as a raw material, the mixed raw material of the silicon carbide powder used as an aggregate, the silicon source which produces | generates silicon carbide, and a carbon source can be used. The silicon carbide powder as the aggregate can be 65% by mass to 95% by mass with respect to the mixed raw material. When the ratio of the silicon carbide powder as the aggregate is smaller than 65% by mass, the strength of the obtained sintered body tends to be low. On the other hand, when it is more than 95% by mass, it tends to be a molded body that is difficult to sinter. In addition, if the ratio with respect to the mixed raw material of the silicon carbide powder as an aggregate is 75 mass%-85 mass%, the said conflicting effect | action can be taken and it is more desirable.

  With respect to the silicon source and carbon source that generate silicon carbide, when the molar ratio of silicon to carbon (Si / C) is 1, silicon carbide is generated in a stoichiometric amount, but Si / C is reduced to 0. .5 to 1.5 is desirable. When Si / C is less than 0.5, the remaining carbon content is excessive, which may cause rough atmospheric pores and inhibit the growth of the generated silicon carbide particles. On the other hand, when Si / C is larger than 1.5, the amount of silicon carbide produced is small, and reactive sintering tends to be insufficient. In addition, if Si / C is 0.8-1.2, there is little excess or deficiency of silicon and carbon, and it is more desirable. Note that silicon nitride and silicon (single silicon) can be used as the silicon source, and examples of the carbon source include graphite, coal, coke, and charcoal.

You may perform the drying process which dries the obtained molded object after a formation process and before a baking process. Such a drying process can be performed by air drying in a temperature-controlled humidity control tank, external heating drying, internal heating drying by microwave irradiation, or the like.
In the firing step, the heating furnace is maintained in a non-oxidizing atmosphere at a predetermined temperature of 1800 ° C. to 2300 ° C. for a predetermined time. If the firing temperature is lower than 1800 ° C, reactive sintering may be insufficient, and if it exceeds 2350 ° C, silicon carbide may sublime. A firing temperature of 2000 ° C. to 2200 ° C. is more desirable because a sintered body with sufficient strength can be obtained in a relatively short time. The sintering time depends on the size of the molded body, but can be, for example, 30 minutes to 3 hours.

  In addition, after the firing step, before the sealing step and the antioxidant layer forming step, it is removed for the purpose of burning and removing carbon sources that may remain in the firing step without being used in the silicon carbide formation reaction. A charcoal process can be provided. This decarburization step can be performed by holding at a temperature of 600 ° C. to 1200 ° C. for 1 hour to 15 hours in an oxidizing atmosphere (in an air atmosphere). With such a heating temperature and holding time, silicon carbide is hardly oxidized in the decarburization step.

  Through the above steps, a segment 10 of a silicon carbide based ceramic sintered body having a honeycomb structure is obtained. The length of the segment 10 (the length of the cell 15 in the axial direction) can be set to 100 mm to 500 mm. When the length is shorter than 100 mm, the axial length of the cell 15 through which the fluid flows is shortened, and the heat exchange efficiency may be reduced. On the other hand, when the length is longer than 500 mm, a temperature gradient is likely to occur in the segment 10 of the honeycomb structure, and there is a possibility that cracks and cracks are likely to occur due to thermal stress.

The cell density of the honeycomb structure is not particularly limited, but is desirably 50 cpsi to 500 cpsi (cell / square inch). By setting it as this range, the mechanical strength of the segment 10 can be ensured while suppressing an increase in pressure loss.
In the “slit forming step”, the partition walls 17 are cut every other row of the cells 15 so as to cut from the first end surface 11 to the second end surface 12 side of the segment 10, and penetrate from the first side surface 13 to the second side surface 14. The first slit 21 is formed. Moreover, the partition 17 is excised every other row of the cells 15 so as to cut from the second end surface 12 of the segment 10 toward the first end surface 11, and the second slit 22 penetrates from the first side surface 13 to the second side surface 14. Form. At this time, the column of cells 15 in which the first slits 21 are formed and the column of cells 15 in which the second slits 22 are formed are different columns, that is, adjacent columns.

  The cutting depth of the first slit 21, that is, the length by which the partition wall 17 is cut in the axial direction is the same between the cells 15 belonging to the same column, and in the present embodiment, also between the cells 15 belonging to different columns. Identical. In addition, the cutting depth of the second slit 22 is the same between the cells 15 belonging to the same column, and in the present embodiment, it is the same between the cells 15 belonging to different columns. In addition, in this embodiment, the cutting depth of the first slit 21 and the cutting depth of the second slit 22 are the same. In addition, if the cutting depth of the 1st slit 21 and the 2nd slit 22 shall be 1/3-1/10 of the full length of the segment 10, the fall of mechanical strength will be suppressed and the 1st slit 21 and the 2nd slit 22 can be formed and is desirable.

  In the “sealing step”, the opening on the first end surface 11 side and the opening on the second side surface 14 side of the first slit 21 are sealed with a sealing agent, and the second slit 22 on the second end surface 12 side is sealed. The opening and the opening on the first side surface 13 side are sealed with a sealant. Here, as the sealing agent, for example, a paste obtained by mixing silicon carbide powder with alumina powder, silica powder, or the like can be used. After sealing, the segment 10 is heat-treated or fired, so that the sealing agent is solidified and densified, and the first sealing portion 31 and the second sealing portion 32 are formed. Here, the heat treatment for solidifying and densifying the sealant can be performed by holding at a temperature of 1000 ° C. to 1200 ° C. for 1 hour to 5 hours in an air atmosphere.

The “antioxidation layer forming step” can be performed before or after the sealing step. This antioxidant layer forming step includes a coating step of coating the surface of the partition wall 17 with an antioxidant, and heating the segment 10 after coating of the antioxidant, and using the antioxidant as an antioxidant layer of silicate glass, A vitrification step for fixing to the surface.
The covering step can be a step of impregnating the segment 10 with the antioxidant. In this case, first, the segment 10 is accommodated in a container that can be sealed, and the air in the container is sucked with a vacuum pump or the like. Next, an antioxidant is introduced into the sealed container through a pipe or hose with an on-off valve. As the antioxidant, a suspension in which the above-mentioned subcomponents are added to silicon dioxide powder and water is added to obtain an appropriate viscosity is used. Thereby, the outer surface of the segment 10 and the surface of the partition wall 17 are covered with the antioxidant. Even if the partition wall 17 is porous, the antioxidant penetrates into the open pores.

  As the antioxidant, in addition to the subcomponents described above, an antioxidant mixed with silicon carbide powder can be used. Silicon carbide contained in the antioxidant is more easily oxidized than silicon carbide constituting the sintered body, and is easily oxidized to silicon dioxide by heating. And the silicon dioxide just produced | generated has the higher reactivity than the silicon dioxide contained from the beginning in antioxidant, and is easy to vitrify. Therefore, by containing silicon carbide in the antioxidant, it is possible to efficiently form the antioxidant layer of the silicate glass in the vitrification step.

  In the vitrification step, after performing a drying treatment to remove moisture in the impregnated antioxidant, heating is performed using the antioxidant as an antioxidant layer of silicate glass. This heating can be performed, for example, by heating the segment 10 impregnated with the antioxidant at a temperature of 800 ° C. to 1200 ° C. for 1 hour to 30 hours in an air atmosphere. By this heating, the antioxidant becomes silicate glass, softens and adheres to the surface of the segment 10 (the partition wall 17 and the side surface), and then solidifies by cooling to form a dense antioxidant layer.

  In the heat exchanger 1 manufactured through the above steps, as shown in FIG. 3A, an end view of the XX line, the first slit 21 opened to the first side surface 13 on the first end surface 11 side. Is in communication with the cell 15 opening in the second end face 12. 3B, the second slit 22 opened to the second side face 14 on the second end face 12 side is a cell 15 opened to the first end face 11. As shown in FIG. Communicated with. Accordingly, the first fluid that flows in from the cell 15 that opens to the first end surface 11 and flows out from the second slit 22 and the cell 15 that flows from the cell 15 that opens to the second end surface 12, Heat can be exchanged with the second fluid flowing out through the partition wall 17. And since the 1st fluid and the 2nd fluid distribute | circulate in the opposite direction in the cell 15 extended in the single axial direction, the time which has contacted via the partition 17 is long, and heat exchange is carried out with high efficiency. can do.

Actually, the heat exchange rate of the example of the heat exchange element 1 of the first embodiment and the comparative example created in the same manner as the above-described Patent Document 3 and Patent Document 4 are compared and measured as described below. As described above, it was confirmed that the heat exchange element of the present embodiment has a higher heat exchange rate.
And the cell 15 in which the 1st slit 21 was formed, and the cell 15 in which the 2nd slit 22 was formed are the cells 15 of a different row | line | column. For this reason, in each row, the partition wall 17 is cut out only for one of the first end surface 11 side and the second end surface 12 side to form a slit, and on the other side, the partition wall 17 extends to the end surface. Exists. Thereby, the possibility that the mechanical strength of the segment 10 is reduced by forming the first slit 21 and the second slit 22 is reduced, and the heat exchanger 1 having high mechanical strength can be obtained.

  In particular, in the present embodiment, the lengths of the partition walls 17 cut out to form the first slit 21 and the second slit 22 are equal, and the lengths of the partition walls 17 after the cutting are all in the heat exchanger 1. equal. The first slits 21 and the second slits 22 are formed every other row of the cells 15, and the direction in which the first slits 21 are opened is opposite to the direction in which the second slits 22 are opened. The heat exchanger 1 has a symmetrical configuration. Thereby, it is the structure with uniform mechanical strength in which the part with high mechanical strength and the low part do not unevenly distribute.

  Moreover, in this embodiment, since the segment 10 is a silicon carbide ceramic sintered body, the thermal conductivity is high. Therefore, heat can be exchanged between the first fluid and the second fluid through the partition wall 17 with higher efficiency. In addition, since silicon carbide has a high thermal conductivity and a low coefficient of thermal expansion, it has excellent thermal shock resistance. Therefore, the heat exchange element 1 of the present embodiment is suitable as the heat exchange element 1 that becomes high temperature by circulating a high-temperature fluid. On the other hand, when silicon carbide is oxidized by being heated to a high temperature in the presence of oxygen, an antioxidation layer of silicate glass is formed on the surface of the heat exchange element 1 of the present embodiment. The reaction is effectively prevented.

  In the above manufacturing method, a sintered body of a segment having a cell number of 224 × 224 and a length of 15 cm was obtained, and a heat exchanger having a first slit and a second slit each having a length of 5 cm was prepared. It was. A segment sintered body having a cell number of 224 × 224 and a length of 15 cm was obtained from the same raw material as in the example through the same manufacturing process as in the example except for the slit forming step. As described above with reference to FIGS. 8 (a) and 8 (b), after every other row of cells, the partition wall is obliquely cut off at one end side in the axial direction, and the end in the axial direction is then removed. By sealing, an opening is formed on only one of the pair of side surfaces, and a confluence channel that expands toward the opening end is formed, and a partition is obliquely formed on the other end side in the axial direction in a row adjacent thereto. After excision, the end in the axial direction was sealed to form a joint channel that opened only on the other side surface and expanded toward the opening end. In Comparative Example 1, the length of the opening end of the combined flow path, that is, the length at which the partition wall was cut longest was 5 cm. Further, as Comparative Example 2, a sintered body of a segment having a cell number of 224 × 224 and a length of 15 cm was obtained from the same raw material as in the Example through the same manufacturing process as in the Example except for the slit forming process. . In Comparative Example 2, in the slit forming step, as shown in FIG. 10, the partition walls 105 are cut at right angles to the cell extending direction at every other row of cells 101 and 101 at every other end 101, 101 in the axial direction. To form a slit, and this is formed as a combined flow path 120. One of the pairs of openings of the combined flow path 120 at both ends of the segment, and two pairs of openings that open to the side surface 102 of the segment at both ends of the segment. Only the opening was sealed to form a sealing portion 110. That is, in Comparative Example 2, the slits are formed at both ends 101 and 101 for the same row of cells, respectively, and two opening ends 121 and 121 are also provided for the cells of the same row.

  About Example and Comparative Examples 1 and 2, the heat exchange rate was measured according to JISB8628. As a result. The graph of the comparison of the heat exchange rate of each example is shown in FIG. Here, as a ratio to the heat exchange rate of Comparative Example 1, the value of (heat exchange rate) / (heat exchange rate of Comparative Example 1) of each example is shown as the heat recovery ratio on the vertical axis of the graph of FIG. . The heat recovery ratio of the example was 1.95, and the heat exchange rate was significantly increased. Although the heat exchange rate of Comparative Example 2 was higher than that of Comparative Example 1, it did not reach that of Example.

  As shown in FIG. 7, the significant increase in the heat exchange rate of Comparative Example 1 in this example is that the flow rates of the first fluid and the second fluid are almost equal in the heat exchange body of the example. The ratio was considered to be uniform throughout the heat exchanger. Here, FIG. 7 is a diagram illustrating a virtual divided body (112 cell rows) in which the heat exchange body is halved along the axial direction. For each of the 56 cell rows that circulate, the flow rate of the fluid was measured, and the ratio was determined between the Nth cell rows (N = 1 to 56).

  As apparent from FIG. 7, in the embodiment, the ratio of the flow rates of the first fluid and the second fluid is substantially 1 throughout the heat exchanger, and the first fluid and the second fluid are independent of the position of the cell row. It can be seen that the flow rates of the two fluids are approximately equal. This is because, in the embodiment, the length of the partition remaining after being cut to form the first slit and the second slit is equal in all the heat exchangers, and the first fluid flows for heat exchange. This is considered to be because the length of the flow path to be used and the length of the flow path through which the second fluid flows are equal in all the heat exchangers. On the other hand, in the comparative example, the flow of the fluid is biased, and the first fluid flows easily but the second fluid does not flow easily. Conversely, the second fluid easily flows but the first fluid flows. It was thought that heat exchange was not performed smoothly in the difficult part. This was thought to be due to the fact that the partition walls were cut obliquely for the formation of the combined flow path.

Further, the reason why the heat exchange rate of the example is larger than that of the comparative example 2 is considered to be that the example has a larger sectional area of the partition wall where heat exchange is performed than the comparative example 2.
Next, the heat exchange body 2 of 2nd embodiment of this invention is demonstrated using FIG.4 and FIG.5. The difference from the heat exchanger 1 of the first embodiment is that in the first embodiment, the first slit 21 and the second slit 22 are opened on different side surfaces (the first slit 21 is opened on the first side surface 13. The second slit 22 is opened on the second side surface 14). In the second embodiment, the first slit 21 and the second slit 22 are opened on the first side surface 13, which is the same side surface.

The manufacturing method of the heat exchange element 2 having such a configuration is the same as the manufacturing method of the first embodiment except for the sealing step. In the sealing step of the second embodiment, the opening on the first end surface 11 side of the first slit 21 and the opening on the second side surface 14 side are sealed with a sealant, and the second end surface of the second slit 22 is sealed. The opening on the 12 side and the opening on the second side surface 14 side are sealed with a sealant.
The plan view and the bottom view of the heat exchange element 2 are the same as the plan view and the bottom view of the heat exchange element 1 shown in FIGS. 2 (a) and 2 (b), respectively. A line end view is shown in FIG. 5 (a), and a YY line end view is shown in FIG. 5 (b). As can be seen from these drawings, in the heat exchange element 2 of the second embodiment, as in the heat exchange element 1 of the first embodiment, the air flows from the cell 15 opened in the first end surface 11 and the second slit. Heat exchange is performed between the first fluid flowing out from 22 and the second fluid flowing in from the cell 15 opened in the second end face 12 and flowing out from the first slit 21 via the partition wall 17. Can do. And since the 1st fluid and the 2nd fluid distribute | circulate in the reverse direction in the cell 15 extended in the single axial direction, the time which has contacted via the partition 17 is long, and heat exchange is carried out with high efficiency. can do.

  In the heat exchange element 1 of the first embodiment in which the side surface on which the first slit 21 opens and the side surface on which the second slit 22 opens are different, the heat is exchanged from each of the first slit 21 and the second slit 22 after heat exchange. Since the discharge directions of fluids having a temperature difference are different, there is an advantage that the temperature difference can be easily maintained. On the other hand, in the case of the heat exchange element 2 of the second embodiment in which the side surface where the first slit 21 opens and the side surface where the second slit 22 opens are the same, the opening of the first slit 21 and the opening of the second slit 22 respectively. There is an advantage that the entirety of the heat exchanger including the pipe that communicates with can be made compact.

The present invention has been described with reference to the preferred embodiments. However, the present invention is not limited to the above-described embodiments, and various improvements can be made without departing from the scope of the present invention as described below. And design changes are possible.
For example, in the above-described embodiment, the case where the shape of the segment is a quadrangular prism is illustrated, but the present invention is not limited to this, and the segment may be a columnar shape or an elliptical columnar shape. In the case of a columnar or elliptical column-shaped segment, the side surface is a continuous surface. Only one of the pair of openings of the slits that respectively open on the side surfaces of the slits may be sealed. The virtual divided body in which the opening of the first slit is sealed on the side surface side and the virtual divided body in which the opening of the second slit is sealed on the side surface side are different even if they are the same. Also good.

DESCRIPTION OF SYMBOLS 1, 2 Heat exchanger 10 Segment 11 1st end surface 12 2nd end surface 15 Cell 17 Partition 21 First slit 22 Second slit 31 First sealing part 32 Second sealing part

Claims (4)

A segment of a ceramic sintered body formed in a honeycomb structure having a plurality of cells partitioned by partition walls extending in a single axial direction,
A plurality of partition walls defining the cells belonging to the same row are separated from the first end surface by the same length on every other row of the cells on one first end surface side of the pair of end surfaces where the cells open. A plurality of first slits formed in a direction perpendicular to the axial direction and having a constant length in the axial direction;
Among the pair of end surfaces, on the other second end surface side, a plurality of the partition walls defining the cells belonging to a column different from the cell in which the first slit is formed are removed from the second end surface by the same length. A plurality of second slits formed in a direction perpendicular to the axial direction and having a constant length in the axial direction;
A first sealing portion that seals the opening on the first end surface side of each of the first slits and seals only one of the pair of side surface openings;
A second sealing portion that seals the opening on the second end face side of each of the second slits and seals only one of the pair of openings on the side face side. A heat exchanger characterized by. The ceramic sintered body is a silicon carbide ceramic sintered body,
The heat exchanger according to claim 1, further comprising an anti-oxidation layer of silicate glass formed on a surface of the partition wall. A forming step of forming a honeycomb structure formed body comprising a plurality of cells partitioned by partition walls extending in a single axial direction and made of ceramic raw materials;
A firing step of firing the molded body to obtain a segment of a ceramic sintered body,
In the segment, on one first end surface side of the pair of end surfaces where the cells open, the plurality of partition walls that partition the cells belonging to the same row are arranged from the first end surface in the same row. A plurality of first slits having a length cut, penetrating in a direction perpendicular to the axial direction and having a constant length in the axial direction, and on the other second end face side of the pair of end faces, A plurality of the partition walls defining the cells belonging to a column different from the cell in which the first slit is formed are excised from the second end surface by the same length, and penetrated in a direction orthogonal to the axial direction to pass through the axial direction. Slit forming step of forming a plurality of second slits having a constant length,
Sealing only one of the pair of openings on the first end surface side of the first slit and the side surface side, and opening on the second end surface side of the second slit, And the sealing process which seals only one opening among a pair of opening by the side is comprised, The manufacturing method of the heat exchanger characterized by the above-mentioned. The ceramic raw material becomes a silicon carbide ceramic sintered body by firing, and the firing step is performed in a non-oxidizing atmosphere,
Before or after the sealing step, the surface of the partition wall is coated with an antioxidant containing silicon dioxide, and the segment having the surface of the partition wall coated with the antioxidant is heated to prevent the oxidation The manufacturing method according to claim 3, further comprising an antioxidant layer forming step of fixing an agent as an antioxidant layer of silicate glass on the surface of the partition wall.

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