This application claims priority to Japanese patent application serial number 2020-031330, filed Feb. 27, 2020, the contents of which is hereby incorporated herein by reference in its entirety for all purposes.
Embodiments in the present disclosure relate to a fuel vapor processing apparatus.
Some fuel vapor processing apparatuses may include a casing, a most upstream side adsorption chamber, and a most downstream side adsorption chamber. The casing forms a flow passage, through which an evaporated fuel flows from one end to the other end. The most upstream side adsorption chamber is disposed on one end of the flow passage and stores an adsorbent capable of adsorbing and desorbing evaporated fuel. The most downstream side adsorption chamber is disposed on the other end of the flow passage and stores an adsorbent capable of adsorbing and desorbing evaporated fuel. Further, the fuel vapor processing apparatus is provided with a heat exchanger (air flow channel) between the most upstream side adsorption chamber and the most downstream side adsorption chamber. The heat exchanger has a heat exchange function for exchanging heat between the inside and outside of the flow passage.
In accordance with an aspect of the present disclosure, a first embodiment includes a fuel vapor processing apparatus comprises a casing, a most upstream side adsorption chamber, a most downstream side adsorption chamber, and at least one intermediate adsorption chamber. The casing may form a flow passage through which an evaporated fuel flows from one end to the other end of the casing. The most upstream side adsorption chamber may be disposed on one end of the flow passage and may store an adsorbent configured to adsorb and desorb the evaporated fuel. The most downstream side adsorption chamber may be disposed on the other end of the flow passage and may store the adsorbent configured to adsorb and desorb the evaporated fuel. The intermediate adsorption chamber may be disposed in series between the most upstream side adsorption chamber and the most downstream side adsorption chamber. The intermediate adsorption chamber may store an adsorbent configured to adsorb and desorb the evaporated fuel. In the fuel vapor processing apparatus, the casing comprises a main-case including the most upstream side adsorption chamber and the intermediate adsorption chamber; and a sub-case formed separately from the main-case and including the most downstream adsorption chamber. The most downstream adsorption chamber of the sub-case and the most upstream side adsorption chamber are disposed adjacent to each other without a gap on a downstream side than a center of the most upstream side adsorption chamber in the flowing direction of evaporated fuel during adsorption. The most upstream side adsorption chamber and the most downstream side adsorption chamber are configured to exchange heat therebetween.
According to the first embodiment, at the time of adsorption, the most downstream side adsorption chamber may be heated by the transfer of adsorption heat generated by the adsorbent in the most upstream side adsorption chamber. Therefore, the adsorption capacity of the adsorbent in the most downstream adsorption chamber may be reduced, and the amount of adsorption may be reduced. Further, if residual heat remains in the most downstream side adsorption chamber at the time of desorption, the amount of desorption of the adsorbent in the most downstream side adsorption chamber may be larger than that at room temperature. Therefore, the residual amount of the adsorbent remaining in the most downstream adsorption chamber may be reduced, at least in part due to reducing the amount of adsorption by the adsorbent in the most downstream adsorption chamber during adsorption and increasing the amount of desorption during desorption. As a result, the blow-out performance in the soak time may be improved, thereby improving the Diurnal Breathing Loss (DBL) performance. Further, in the casing having the sub-case formed separately from the main-case, the adsorption heat generated by the adsorbent in the most upstream side adsorption chamber may be transferred to the most downstream side adsorption chamber via the contact portion between the main-case and the sub-case.
In accordance with another aspect of the present disclosure, a second embodiment may be the fuel vapor processing apparatus according to the first embodiment, wherein an adjacent portion between the most upstream side adsorption chamber and the most downstream side adsorption chamber are partitioned by a common wall shared by the main-case and the sub-case.
According to the second embodiment, the adsorption heat generated by the adsorbent in the most upstream side adsorption chamber may be transferred to the most downstream side adsorption chamber via the common wall.
In accordance with another aspect of the present disclosure, a third embodiment may be the fuel vapor processing apparatus according to the first or second embodiments, wherein a heat conductive member having a thermal conductivity higher than that of the main-case and the sub-case may be disposed on the wall portion interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber.
According to the third embodiment, the heat transfer efficiency from the most upstream side adsorption chamber to the most downstream side adsorption chamber may be improved by the heat conductive member disposed on the wall portion interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber.
In accordance with another aspect of the present disclosure, a fourth means may be the fuel vapor processing apparatus according to any one of the first to third embodiments, wherein a concave-convex portion that increases a heat transfer area may be formed as or on the surface of at least one adsorption chamber side of the wall portion interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber.
According to the fourth embodiment, the heat transfer efficiency from the most upstream side adsorption chamber to the most downstream side adsorption chamber may be improved by the concave-convex portion formed on the wall portion interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber.
In accordance with another aspect of the present disclosure, a fifth embodiment may be the fuel vapor processing apparatus according to any one of the first to fourth embodiments, wherein the most downstream adsorption chamber may be disposed adjacent to the intermediate adsorption chamber so as to be heat exchangeable. This allow the most downstream adsorption chamber to also transfer heat with the intermediate adsorption chamber. As a result, the adsorption capacity of the adsorbent in the most downstream adsorption chamber may be further reduced, which may also further reduce the amount of adsorption.
According to the fifth embodiment, at the time of adsorption, the most downstream side adsorption chamber may be heated due to the transfer of the adsorption heat generated by the adsorbent in the most upstream side adsorption chamber and the adsorption heat generated by the adsorbent in the intermediate adsorption chamber.
In accordance with another aspect of the present disclosure, a sixth embodiment may be the fuel vapor processing apparatus according to the fifth embodiments, wherein the casing may include a main-case and a sub-case. The main-case may comprise a first straight portion having the most upstream side adsorption chamber, a second straight portion having the intermediate adsorption chamber, and a connecting portion that connects the first straight portion and the second straight portion. Due to the arrangement of these portions, the main-case may be formed in a U-shape. The sub-case may be disposed in a recess formed between the first straight portion and the second straight portion of the main-case.
According to the sixth embodiment, in the casing having the sub-case formed separately from the main-case, the adsorption heat generated by both the adsorbent in the most upstream adsorption chamber and the adsorbent in the intermediate adsorption chamber may be transferred to the most downstream adsorption chamber, via the contact portion between the main-case and the sub-case.
In accordance with another aspect of the present disclosure, a seventh embodiment may be the fuel vapor processing apparatus according to the sixth embodiment, wherein adjacent portions between the most upstream side adsorption chamber and the most downstream side adsorption chamber, and between the intermediate adsorption chamber and the most downstream side adsorption chamber are partitioned by a common wall shared by the main-case and the sub-case.
According to the seventh embodiment, the adsorption heat generated by both the adsorbent in the most upstream adsorption chamber and the adsorbent in the intermediate adsorption chamber may be transferred to the most downstream adsorption chamber via the common wall.
In accordance with another aspect of the present disclosure, an eighth embodiment may be the fuel vapor processing apparatus according to any one of the sixth to seventh embodiments, wherein a heat conductive member, which may have a thermal conductivity higher than that of both the main-case and the sub-case, may be disposed on the wall portion interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber. The thermal conductive member may also be interposed between the intermediate adsorption chamber and the most downstream side adsorption chamber.
According to the eighth embodiment, the efficiency of the transfer of heat from the most upstream adsorption chamber to the most downstream chamber and from the intermediate adsorption chamber to the most downstream adsorption chamber may be improved. This is at least in part due to the heat conductive member disposed on the wall portion interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber and between the intermediate adsorption chamber and the most downstream side adsorption chamber.
In accordance with another aspect of the present disclosure, an ninth embodiment may be the fuel vapor processing apparatus according to any one of the sixth to eighth embodiments, wherein the concave-convex portion, which increases the heat transfer area, may be formed as or on at least one adsorption chamber side surface of the wall portion interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber, and between the intermediate adsorption chamber and the most downstream side adsorption chamber.
According to the ninth embodiment, the efficiency of the transfer of heat from the most upstream adsorption chamber to the most downstream adsorption chamber, and from the intermediate adsorption chamber to the most downstream adsorption chamber may be improved. This is at least in part due to the concave-convex portion formed on the wall interposed between the most upstream side adsorption chamber and the most downstream side adsorption chamber, and between the intermediate adsorption chamber and the most downstream side adsorption chamber.
In accordance with another aspect of the present disclosure, a tenth embodiment may be the fuel vapor processing apparatus according to the any one of the first to ninth embodiments, wherein the fuel vapor processing apparatus may be provided with a heat insulating member that covers the exposed portion(s), which are exposed to the outside of the sub-case. The heat insulating member has a heat retaining function.
According to the tenth embodiment, the heat retaining member, which covers the exposed portion(s) of the sub-case, may improve the heat retaining effect of the adsorption chamber on the most downstream side.
According to the present disclosure, the amount desorbed by the adsorbent in the most downstream adsorption chamber at the time of desorption may be increased. This may reduce the residual amount in the most downstream adsorption chamber.
As previously described, some fuel vapor processing apparatuses include a casing, a most upstream side adsorption chamber, and a most downstream side adsorption chamber. The casing forms a flow passage, through which an evaporated fuel flows from one end to the other end. A heat exchanger (air flow channel) extends between the most upstream side adsorption chamber and the most downstream side adsorption chamber. At the time of adsorption, the air, which has been heated due to the adsorption heat generated by the adsorbent in the most upstream side adsorption chamber, is cooled by the heat exchanger. Then, the most downstream adsorption chamber is cooled by the cooled air. Therefore, at the time of desorption, it becomes difficult for the evaporated fuel to be desorbed from the adsorbent in the most downstream adsorption chamber. Accordingly, an increased amount of residual adsorbed vapor (e.g., a residual amount of butane) may be maintained. This may reduce the blow-out performance during the soak time (in the inoperative state). In general, an adsorbent, such as activated carbon, has the characteristic that the higher the temperature, the smaller the amount of fuel that can be adsorbed. Additionally, the higher the temperature, the larger the amount of fuel that may be desorbed. On the other hand, the lower the temperature, the larger the amount of fuel that may be adsorbed and the smaller the amount of fuel that may be desorbed.
Therefore, there has conventionally been a need to reduce the residual amount of fuel vapor in the adsorbent in the most downstream adsorption chamber.
Embodiments in the present disclosure will now be described with reference to the figures.
In a first embodiment, a canister installed in a vehicle, such as an automobile, equipped with an engine, such as an internal combustion engine, will be exemplified.
As shown in
The main canister 11 includes a main-case 14 having an elongate, square, box-shape. The main-case 14 includes a main-case body 15 and a main-case lid 16. The main-case 14 may be made of, for example, resin. In this embodiment, the main-case body 15 has a square tubular shape, with an upper surface thereof closed. The main-case lid 16 closes a lower surface opening in the main-case body 15. In general, the main-case body 15 and the main-case lid 16 may be joined by any suitable joining means, such as heat welding or adhesion.
A division wall 19 is provided in the main-case 14, so as to form a U-shaped main passage 18. The main passage 18 has a first passage 18a, a second passage 18b, and a communication part 18c in fluid communication with the lower ends of both passages 18a, 18b. In this embodiment, the first passage 18a is a straight portion on one side of the main passage 18 (the right side in
A tank port 20 and a purge port 21, both of which are in fluid communication with the first passage 18a, are formed on the upper wall portion of the main-case body 15. A main side connection port 22 in fluid communication with the second passage 18b is also be formed on the upper wall portion of the main-case body 15. The tank port 20 is a port for introducing evaporated fuel from a fuel tank 23 into the main passage 18. The purge port 21 is a port for purging the evaporated fuel from the main passage 18 to an intake passage of an engine 24. The main side connection port 22 is a port to which one end of a connection pipe 25 is connected. The upper end of the first passage 18a is partitioned by a partition wall 26 into a portion in fluid communication with the tank port 20 and a portion in fluid communication with the purge port 21.
The first passage 18a is provided with a first adsorption chamber 28. The first adsorption chamber 28 occupies most of the first passage 18a. The first adsorption chamber 28 stores a first adsorbent 29, such as activated carbon, configured to adsorb and desorb evaporated fuel. The second passage 18b is provided with a second adsorption chamber 31 and a third adsorption chamber 34, positioned in series. The third adsorption chamber 34 is disposed above the second adsorption chamber 31. The second adsorption chamber 31 stores a second adsorbent 32, such as activated carbon, configured to adsorb and desorb evaporated fuel. The third adsorption chamber 34 stores a third adsorbent 35, such as activated carbon, configured to adsorb and desorb evaporated fuel. An air chamber 36 is provided between the second adsorption chamber 31 and the third adsorption chamber 34.
The sub canister 12 includes a sub-case 38 having an elongate, square, box-shape. A sub-case body 39 of the sub-case 38 may be formed separately from the main-case body 15. The sub-case 38 includes the sub-case body 39 and a sub-case lid 40. The sub-case 38 may be made of, for example, resin. The sub-case body 39 has a square, tubular shape, with an upper surface thereof closed. The sub-case lid 40 closes a lower surface opening of the sub-case body 39. The sub-case body 39 and the sub-case lid 40 may be joined by any suitable joining means, such as heat welding or adhesion.
A sub passage 42, having a straight shape, is formed in the sub-case 38. A sub side connection port 43 in fluid communication with the sub-passage 42 is formed on the sub-case lid 40. The other end of the connection pipe 25, the end opposite that connected to the main side connection port 22, is connected to the sub side connection port 43. An atmospheric port 44 is formed on the upper wall of the sub-case body 39. The atmospheric port 44 may open to the atmosphere.
The sub passage 42 is provided with a fourth adsorption chamber 46. The fourth adsorption chamber 46 may occupy most of the sub passage 42. A fourth adsorbent 47 configured to adsorb and desorb evaporated fuel, such as activated carbon, is stored in the fourth adsorption chamber 46.
A casing 50 is generally composed of the main-case 14, the connecting pipe 25, and the sub-case 38. A flow passage 51, in which evaporated fuel flows from the tank port 20 side (an upstream side) to the atmospheric port 44 side (a downstream side) at the time of adsorption, is formed by the main passage 18, the sub passage 42, and the connection pipe 25. The tank port 20 side of the flow passage 51 may also be referred to as “one end” in the present disclosure. The atmospheric port 44 side of the flow passage 51 may also be referred to as “the other end” in the present disclosure.
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The main-case body 15 may also be referred to as the “main-case body” in the present disclosure. The sub-case body 39 may correspond to the “sub-case body” in the present disclosure. The first adsorption chamber 28 may also be referred to as the “most upstream side adsorption chamber” in the present disclosure. The fourth adsorption chamber 46 may also be referred to as the “most downstream adsorption chamber” in the present disclosure. The second adsorption chamber 31 and the third adsorption chamber 34 may each be referred to as the “intermediate adsorption chamber” in the present disclosure. The contact portion between the front-side wall 15a of the main-case body 15 and the rear-side wall 39a of the sub-case body 39 may be referred to as a wall portion interposed between the first adsorption chamber 28 and the fourth adsorption chamber 46. The same adsorbent may be used for the first adsorbent 29, the second adsorbent 32, the third adsorbent 35, and the fourth adsorbent 47. Alternatively, different adsorbents may be used.
The effect of the canister 10 at the time of adsorption (mainly at the time of refueling) will be described. Evaporated fuel containing air in the fuel tank 23 is introduced from the tank port 20 into the flow passage 51 of the casing 50. The evaporated fuel flows through the first adsorption chamber 28, the second adsorption chamber 31, the third adsorption chamber 34, and the fourth adsorption chamber 46, in this order, to reach the atmospheric port 44. At that time, the evaporated fuel is sequentially adsorbed on the first adsorbent 29, the second adsorbent 32, the third adsorbent 35, and the fourth adsorbent 47. After the evaporated fuel has been adsorbed, air is then be discharged from the atmospheric port 44.
At the time of adsorption, each of the adsorbents 29, 32, 35, 47 generate adsorption heat in response to adsorbing the evaporated fuel. In particular, the adsorption heat generated by the first adsorbent 29 is relatively high. This adsorption heat tends to accumulate on the downstream side of the first adsorption chamber 28. The adsorption heat generated by the first adsorbent 29 is transferred to the fourth adsorption chamber 46, via the contact wall portion 15c of the front-side wall 15a of the main-case body 15 and the rear-side wall 39a of the sub-case body 39. As a result, the fourth adsorption chamber 46 is heated, which may cause the adsorption capacity of the fourth adsorbent 47 to be reduced and may cause the adsorption amount to be reduced.
Next, the effect of the canister 10 at the time of soaking (for instance, when parked) will be described. At the time of soaking (for instance, when parked), the fourth adsorption chamber 46 may be kept warm by receiving the adsorption heat and residual heat of the first adsorbent 29 of the first adsorption chamber 28.
Next, the effect of the canister 10 at the time of desorption (for instance, during a purging operation) will be described. At the time of desorption (for instance, during a purging operation), the intake negative pressure of the engine 24 acts on the purge port 21 to create flow within the flow passage 51 of the casing 50. Along with this, atmospheric air (fresh air) is introduced from the atmospheric port 44 into the flow passage 51 of the casing 50. The air flows in a path opposite to that at the time of adsorption. As a result, the evaporated fuel is sequentially desorbed from the fourth adsorbent 47, the third adsorbent 35, the second adsorbent 32, and the first adsorbent 29. The desorbed fuel vapor is purged from the purge port 21 to the engine 24.
According to the canister 10 described above, at the time of adsorption, the fourth adsorption chamber 46 is heated by the transfer of the adsorption heat generated by the first adsorbent 29. Therefore, the adsorption capacity of the fourth adsorbent 47 and the amount of adsorption may be reduced. Further, at the time of desorption, if residual heat remains in the fourth adsorption chamber 46, the amount of desorption by the fourth adsorbent 47 may be larger than that at ambient temperature. Therefore, the residual amount of fuel vapor on the fourth adsorbent 47 may be reduced, due to reducing the amount of adsorption of the fourth adsorbent 47 at the time of adsorption and increasing the amount of desorption at the time of desorption. As a result of the reduced residual amount of fuel vapor on the fourth adsorbent 47, the blow-by performance at the time of soaking may be improved and the Diurnal Breathing Loss (DBL) performance may be improved.
Further, the fourth adsorption chamber 46 is disposed adjacent to the downstream end of the first adsorption chamber 28, so as to allow heat to be exchanged therebetween. Accordingly, the heat exchange efficiency may be improved, as compared with the case where the fourth adsorption chamber 46 is disposed at a position other than the downstream end portion of the first adsorption chamber 28 (for example, at the upstream end portion). The fourth adsorption chamber 46 is disposed so it may exchange heat with a portion other than the downstream end portion of the first adsorption chamber 28.
Further, even though the casing 50 includes a sub-case body 39 formed separately from a main-case body 15, the adsorption heat generated by the first adsorbent 29 is transferred to the fourth adsorption chamber 46, via the contact wall portion 15c of the front-side wall 15a of the main-case body 15 and the rear-side wall 39a of the sub-case body 39.
A second embodiment is a modification of the positioning of the sub canister 12 of the first embodiment (see
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A third embodiment is a modification of the contact portion between the main-case body 15 and the sub-case body 39 of the first embodiment (see
As shown in
According to the third embodiment, in the casing 150 that includes the sub-case body 139 formed with the main-case body 115, the adsorption heat generated by the first adsorbent 29 is transferred to the fourth adsorption chamber 46 via the common wall 153. The modifications described with respect to the third embodiment may be applied to the casing 50 of the second embodiment (see
A fourth embodiment is a modification of the contact portion between the main-case body 15 and the sub-case body 39 of the first embodiment (see
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According to the fourth embodiment, the heat transfer efficiency from the first adsorption chamber 28 to the fourth adsorption chamber 46 may be improved at least in part due to the heat conductive member 53, which is disposed between the contact wall portion 15c of the front-side wall 15a of the main-case body 15 and the rear-side wall 39a of the sub-case body 39.
A fifth embodiment is a modification of the contact portion between the main-case body 15 and the sub-case body 39 of the first embodiment (see
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According to the fifth embodiment, the heat transfer efficiency from the first adsorption chamber 28 to the fourth adsorption chamber 46 may be improved at least in part due to the heat conductive member 54, which also serves as the rear-side wall 39a of the sub-case body 39 in this embodiment.
A sixth embodiment is a modification of the contact portion between the main-case body 15 and the sub-case body 39 of the first embodiment (see
As shown in
According to the sixth embodiment, the heat transfer efficiency from the first adsorption chamber 28 to the fourth adsorption chamber 46 may be improved at least in part due to the heat conductive member 55, which also serves as the contact wall portion 15c of the front-side wall 15a of the main-case body 15 in this embodiment.
A seventh embodiment is a modification of the common wall portion 153 of the casing 150 of the third embodiment (see
As shown in
According to the seventh embodiment, the heat transfer efficiency from the first adsorption chamber 28 to the fourth adsorption chamber 46 may be improved at least in part due to the heat conductive member 56, which also serves as the common wall 153 of the casing 150.
An eighth embodiment is a modification of the contact portion between the main-case body 15 and the sub-case body 39 of the first embodiment (see
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According to the eighth embodiment, the heat transfer efficiency from the first adsorption chamber 28 to the fourth adsorption chamber 46 may be improved at least in part due to the concave-convex portion 60 formed on the rear-side wall 39a of the sub-case body 39. In other embodiments, the concave-convex portion 60 is formed on the first adsorption chamber 28 side of the contact wall portion 15c of the front-side wall 15a of the main-case body 15. In yet other embodiments, the concave-convex portion 60 is formed as the common wall 153 of the third embodiment at the first adsorption chamber 28 side and/or at the fourth adsorption chamber 46 side (see
A ninth embodiment is a modification of the sub canister 12 of the first embodiment (see
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According to the ninth embodiment, the heat retaining effect of the fourth adsorption chamber 46 may be improved at least in part due to the insulating sheet 52 covering the exposed portion(s) of the sub-case 38. Further, the insulating sheet 52 is provided so as to completely cover the exposed portion(s) of the sub-case 38.
A tenth embodiment is a modification of the arrangement of the sub canister 12 of the first embodiment (see
As shown in
The sub-case body 239 is formed separately from the main-case body 215. The sub-case body 239 has a fourth adsorption chamber 46. The sub-case 239 is disposed horizontally on the bottom of the recess 261 of the main-case body 215 (see
The sub-case body 239 has a cylindrical shape that fits into the bottom of the recess 261 of the main-case body 215, with almost no gap. That is, a semi-cylindrical lower half peripheral wall 239a in the lower half of the sub-case body 239 is in contact with a semi-cylindrical bottom wall 215a of the recess 261 of the main-case body 215. As a result, the fourth adsorption chamber 46 is disposed adjacent to not only the first adsorption chamber 28 but also the second adsorption chamber 31. In particular, they are so positioned so as to allow heat to be exchangeable therebetween. The adsorption heat of the first adsorbent 29 and the adsorption heat of the second adsorbent 32 are transferred to the fourth adsorption chamber 46 via a total of three surfaces, that is, the right side surface, the lower surface, and the left side surface of the contact portion between the main-case body 215 and the sub-case body 239. Further, the contact portion between the bottom wall 215a of the recess 261 of the main-case body 215 and the lower half peripheral wall 239a of the sub-case body 239 correspond to a wall portion interposed between the first adsorption chamber 28 and the fourth adsorption chamber 46 and between the second adsorption chamber 31 and the fourth adsorption chamber 46.
Similar effects as those of the first embodiment may be realized by the tenth embodiment. Further, at the time of adsorption, the fourth adsorption chamber 46 may be heated due to the transfer of heat from both the adsorption heat generated by the first adsorbent 29 and the adsorption heat generated by the adsorbent of the second adsorption chamber 31. Therefore, at the time of adsorption, the adsorption capacity of the fourth adsorbent 47 and the amount of adsorption may be further reduced.
Further, the sub-case body 239 is disposed in the recess 261. The recess 261 has a substantially a U-shaped portion formed between the first straight portion 255 and the second straight portion 257 of the main-case body 215 of the casing 250. As a result, the fourth adsorption chamber 46 of the sub-case body 239 is disposed so as to be able to exchange heat with both the first adsorption chamber 28 and the second adsorption chamber 31 of the main-case body 215.
Further, even though the sub-case body 239 is formed separately from the main-case body 215, the adsorption heat generated by the first adsorbent 29 and the second adsorbent 32 is transferred to the fourth adsorption chamber 46, via the contact portion between the main-case body 215 and the sub-case body 239.
In the tenth embodiment, the following means may be taken in order to further improve the heat transfer efficiency from both the first adsorption chamber 28 and the second adsorption chamber 31 to the fourth adsorption chamber 46:
(1) Similar to the fourth embodiment (see
(2) Similar to the fifth embodiment (see
(3) Similar to the sixth embodiment (see
(4) Similar to the eighth embodiment (see
In the tenth embodiment, in order to improve the heat retaining effect of the fourth adsorption chamber 46, an insulating sheet is provided to cover the exposed portion(s) of the sub-case 38, similar to the ninth embodiment (see
An eleventh embodiment is a modification of the contact portion between the main-case body 215 and the sub-case body 239 of the tenth embodiment (see
As shown in
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According to the eleventh embodiment, even if the sub-case body 339 is formed with the main-case body 315, the adsorption heat generated by the first adsorbent 29 and the second adsorbent 32 is transferred to the fourth adsorption chamber 46 via the common wall 353.
In the eleventh embodiment, the following means may be taken in order to further improve the heat transfer efficiency from the first adsorption chamber 28 and the second adsorption chamber 31 to the fourth adsorption chamber 46:
(1) Similar to the seventh embodiment (see
(2) Similar to the eighth embodiment (see
In the eleventh embodiment, in order to improve the heat retaining effect of the fourth adsorption chamber 46, an insulating sheet is provided to cover the exposed portion(s) of the sub-case 338, as in the ninth embodiment (see
The arts disclosed in the present disclosure is not limited to the above-described embodiment, and may be implemented in various other embodiments. For example, the shapes of the casings 50, 150, 250 may be changed, as appropriate. Further, the number of intermediate adsorption chambers may be at least one. Further, as the adsorbent, a honeycomb-structured adsorbent may be used instead of activated carbon.
The various examples described above in detail with reference to the attached drawings are intended to be representative in the present disclosure and are thus non-limiting embodiments. The detailed description is intended to teach a person of skill in the art to make, use, and/or practice various aspects of the present teachings, and thus does not limit the scope of the disclosure in any manner. Furthermore, each of the additional features and teachings disclosed above may be applied and/or used separately or with other features and teachings in any combination thereof, to provide an improved fuel vapor processing apparatus, and/or methods of making and using the same.
Number | Date | Country | Kind |
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2020-031330 | Feb 2020 | JP | national |