Patent Application
20180207344
The present invention relates to an artificial lung.
In the related art, in cardiotomy for heart disease performed through an extracorporeal circulation method, an artificial lung has been used for replacing the function of a lung of a living body. In this case, blood of a patient is introduced into an artificial lung outside the body. In order to reduce the blood transfusion amount of a patient and to reduce adverse reaction caused due to blood transfusion, the filling amount of blood in an artificial lung is required to be reduced.
Various attempts have been made in this regard. For example, according to the artificial lung disclosed in JP-A-2010-200884, the filling amount of blood is reduced by reducing a storage space for blood.
In the related art, a heat exchange portion which controls the temperature of blood and a gas exchange portion which performs gas exchange are separately provided inside a housing to be filled with blood, and a gap therebetween becomes a dead space.
In some artificial lungs in the related art, a partition wall is provided in a gap between the heat exchange portion and the gas exchange portion. Although a dead space is slightly reduced due to the partition wall, since blood moves between the heat exchange portion and the gas exchange portion, a large window-shaped opening portion is formed in the partition wall. Therefore, a large dead space still remains.
Moreover, in some artificial lungs in the related art, a header having a partition wall with a thickness greater than a gap between a heat exchange layer and a gas exchange layer constituted of hollow fibers is forcibly inserted and is disposed therebetween. In this case, the hollow fibers of the heat exchange layer and the gas exchange layer are squashed by the partition wall of the header. Asa result, there is a possibility that heat exchange performance and gas exchange performance will deteriorate.
The present invention has been made in consideration of the foregoing problems, and an object thereof is to provide an artificial lung in which a filling amount of blood is more effectively reduced and a function of the artificial lung can be favorably exhibited.
In order to achieve the object, according to the present invention, there is provided an artificial lung including a filling portion that communicates with an inlet port and an outlet port for blood and is filled with blood, a heat exchange portion that includes a bundle of a plurality of hollow fibers for heat exchange and is provided inside the filling portion, a gas exchange portion that includes a bundle of a plurality of hollow fibers for gas exchange and is provided inside the filling portion to be adjacent to the heat exchange portion, and a porous member that is disposed in a gap between the heat exchange portion and the gas exchange portion and blocks the gap.
According to the artificial lung having the configuration described above, the gap between the heat exchange portion and the gas exchange portion is blocked by the porous member, and a useless space inside the filling portion to be filled with blood is reduced. Therefore, the filling amount of blood can be effectively reduced. In addition, blood moves between the heat exchange portion and the gas exchange portion through holes of the porous member, and a heat exchange and a gas exchange are smoothly performed. Therefore, the function of the artificial lung can be favorably exhibited.
Hereinafter, with reference to the accompanying drawings, an embodiment of the present invention will be described. Note that, for the convenience of description, the dimensional ratios of the drawings are exaggerated and are different from the actual ratios.
As illustrated in
In addition, as illustrated in
A flow path 151 communicating with the inlet port 101 for blood is formed in the inner cylindrical member 150, and the outlet port 102 for blood is formed in the outer cylindrical member 120. The header 130 is attached to one end portion of the outer cylindrical member 120 and the inner cylindrical member 150, and the header 140 is attached to the other end portion of the outer cylindrical member 120 and the inner cylindrical member 150.
The inlet port 103 for a heat transfer medium and an inlet path 131 for a heat transfer medium are formed in the header 130. The inlet port 103 for a heat transfer medium and the inlet path 131 for a heat transfer medium communicate with each other.
In addition, the inlet port 105 for gas and an inlet path 132 for gas are formed in the header 130. The inlet port 105 for gas and the inlet path 132 for gas communicate with each other. The inlet path 131 for a heat transfer medium and the inlet path 132 for gas are isolated so as not to communicate with each other.
The outlet port 104 for a heat transfer medium and an outlet path 141 for a heat transfer medium are formed in the header 140. The outlet port 104 for a heat transfer medium and the outlet path 141 for a heat transfer medium communicate with each other.
In addition, the outlet port 106 for gas and an outlet path 142 for gas are formed in the header 140. The outlet port 106 for gas and the outlet path 142 for gas communicate with each other. The outlet path 141 for a heat transfer medium and the outlet path 142 for gas are isolated so as not to communicate with each other.
The housing 110 internally includes a heat exchange portion 160, a gas exchange portion 170, and a porous member 180.
The heat exchange portion 160 cylindrically extends around the inner cylindrical member 150. One end portion 161 of the heat exchange portion 160 is fixed to the inlet path 131 for a heat transfer medium using an adhesive, for example. The other end portion 162 of the heat exchange portion 160 is fixed to the outlet path 141 for a heat transfer medium using an adhesive, for example.
The gas exchange portion 170 is provided to be adjacent to the heat exchange portion 160 and cylindrically extends around the heat exchange portion 160. One end portion 171 of the gas exchange portion 170 is fixed to the inlet path 132 for gas using an adhesive, for example. The other end port ion 172 of the gas exchange portion 170 is fixed to the outlet path 142 for gas using an adhesive, for example.
The porous member 180 is disposed between the heat exchange portion 160 and the gas exchange portion 170 and blocks a gap therebetween. The porous member 180 blocks the entire gap between the heat exchange portion 160 and the gas exchange portion 170. A material forming the porous member 180 is not particularly limited. For example, a resin having biocompatibility is used.
Blood introduced through the inlet port 101 for blood fills the inside of the housing 110. The heat exchange portion 160 performs temperature control, and the gas exchange portion 170 performs gas exchange.
Blood which has been introduced from the inlet port 101 for blood passes through the flow path 151 and is guided to the heat exchange portion 160. Blood moves radially outward through the heat exchange portion 160, the porous member 180, and the gas exchange portion 170.
The heat exchange portion 160 is constituted of a bundle of a plurality of hollow fibers 163 (hollow fibers for heat exchange), and blood passes through the heat exchange portion 160 through gaps among the hollow fibers 163.
Each of the hollow fibers 163 extends from a side of the inlet path 131 for a heat transfer medium to a side of the outlet path 141 for a heat transfer medium in a substantially straight manner. Each of the hollow fibers 163 communicates with the inlet path 131 for a heat transfer medium at one end portion and communicates with the outlet path 141 for a heat transfer medium at the other end portion.
A heat transfer medium is introduced from the inlet port 103 for a heat transfer medium and enters the inside of the hollow fibers 163 through the inlet path 131 for a heat transfer medium. The heat transfer medium which has flowed inside the hollow fibers 163 goes out to the outlet path 141 for a heat transfer medium and flows out from the outlet port 104 for a heat transfer medium.
Blood comes into contact with the hollow fibers 163 while moving through the gaps among the hollow fibers 163 and is subjected to heat exchange with the heat transfer medium flowing inside the hollow fibers 163. For example, the heat transfer medium is warm water or cold water controlled to have a predetermined temperature. However, the heat transfer medium is not limited thereto.
In the end portions 161 and 162 of the heat exchange portion 160, for example, the gaps among the hollow fibers 163 are in a liquid-tight state blocked by an adhesive. Therefore, blood does not flow out to the inlet path 131 and the outlet path 141 for a heat transfer medium. In addition, the heat transfer medium does not enter the gaps among the hollow fibers 163 and is not mixed with blood.
The gas exchange portion 170 is constituted of a bundle of a plurality of hollow fibers 173 (hollow fibers for gas exchange), and blood passes through the gas exchange portion 170 through gaps among the hollow fibers 173. The diameter of a hollow fiber 173 is smaller than the diameter of a hollow fiber 163.
Each of the hollow fibers 173 extends from a side of the inlet path 132 for gas to a side of the outlet path 142 for gas in a substantially straight manner. Each of the hollow fibers 173 communicates with the inlet path 132 for gas at one end portion and communicates with the outlet path 142 for gas at the other end portion.
Gas is introduced from the inlet port 105 for gas and enters the inside of the hollow fibers 173 through the inlet path 132 for gas. The gas which has flowed inside the hollow fibers 173 goes out to the outlet path 142 for gas and flows out from the outlet port 106 for gas.
Blood comes into contact with the hollow fibers 173 while moving through the gaps among the hollow fibers 173. Micro-holes for internal communication are formed in a surrounding wall of the hollow fibers 173. When blood comes into contact with the hollow fibers 173, oxygen, that is, gas flowing inside the hollow fibers 173 is taken into blood through the holes. In addition, at this time, carbon dioxide in blood is taken into the hollow fibers 173.
In the end portions 171 and 172 of the gas exchange portion 170, for example, the gaps among the hollow fibers 173 are in a liquid-tight state blocked by an adhesive. Therefore, blood does not flow out to the inlet path 132 and the outlet path 142 for gas. In addition, gas does not enter the gaps among the hollow fibers 173 and is not mixed with blood.
Blood is suitably subjected to temperature control and gas exchange through the heat exchange portion 160 and the gas exchange portion 170. Thereafter, the blood flows out through the outlet port 102 for blood.
As illustrated in
The porous member 180 reduces the extent of an otherwise useless space, suppresses the blood filling amount, and enables blood to move by blocking a portion of a gap 190 between the heat exchange portion 160 and the gas exchange portion 170.
A mesh opening dimension A of the hole 181 is not particularly limited. The mesh opening dimension A preferably ranges from 200 μm to 4,000 μm, and the opening ratio of the holes 181 preferably ranges from 15% to 50%. The opening ratio of the holes 181 indicates a ratio of the surface area of a mesh opening part per unit area of the cylindrical wall of the porous member 180.
If the mesh opening dimension A is reduced, the bulk volume of the porous member 180 disposed in the gap 190 increases and an effect of reducing the blood filling amount becomes significant. However, resistance when blood passes through the holes 181 increases. As a factor increasing resistance at this time, air in blood is clogged in the holes 181 of which the mesh opening dimension A is reduced, and blood is inhibited from passing through. In addition, when resistance in the holes 181 increases and blood is hindered from smoothly flowing, blood becomes stagnant in the heat exchange portion 160 and the gas exchange portion 170, so that there is a possibility that heat exchange and gas exchange will not be favorably performed, and heat exchange performance and gas exchange performance will deteriorate.
Meanwhile, although resistance in the holes 181 is reduced by increasing the mesh opening dimension A, the bulk volume occupied by the porous member 180 for partially filling the gap 190 is reduced. Therefore, an effect of reducing the blood filling amount deteriorates.
In this manner, the mesh opening dimension A and reduction of the blood filling amount are in a trade-off relationship, and the inventors calculated and verified the relationship. The calculation result is indicated in Table 1 below.
The reduction amounts of filling blood indicated in Table 1 were obtained from the volume of the porous member 180, and it was considered that the amount of filling blood was reduced as much as the solid volume of the porous member 180. The volume of the porous member 180 was obtained by multiplying the superficial surface area of the porous member 180 including the mesh opening part of the holes 181 by the thickness of the porous member 180, and subtracting the total volume of the holes 181 therefrom. Here, a preferred thickness of the porous member 180 of 1 mm was used. In addition, the total volume of the holes 181 was obtained by multiplying the volume of each of the holes 181 by the total number of the holes 181.
The heat exchange performance in Table 1 was evaluated based on a temperature change of blood at the inlet port 101 and the outlet port 102 for blood and a temperature change of a heat transfer medium at the inlet port 103 and the outlet port 104 for a heat transfer medium in the artificial lung 100.
The heat exchange performance of Calculation Examples 1 and 2 was within a permissible range but was inferior to those of Calculation Examples 3 to 5. Meanwhile, the heat exchange performance of Calculation Examples 3 to 5 was favorable.
When the mesh opening dimension A was significant such as 200 μm or greater as in Calculation Example 3 to 5, flow resistance in the holes 181 was reduced, blood flowed smoothly, and heat exchange was favorably performed in the heat exchange portion 160.
Actually, as illustrated in the graph of
From the result of the calculation and the experiment, it is determined that performance becomes preferable when the mesh opening dimension A ranges from 200 μm to 1,800 μm and the opening ratio ranges from 40% to 60%.
In addition, in regard to reduction of the blood filling amount as well, the filling amount of blood to fill the gas exchange portion 170 was approximately 60 mL. On the other hand, 4.3 mL was reduced in Calculation Example 5 having the least reduction amount of blood. Accordingly, it was found that at least 7% or higher reduction rate of the blood filling amount could be obtained.
The reduction rate of the blood filling amount is obtained based on the ratio of the filling amount of blood to fill the gas exchange portion 170 and the volume of a substrate part of the porous member 180 excluding the holes 181. The reduction rate of the blood filling amount is preferably 10% or higher. However, the reduction rate is not limited thereto. In addition, the upper limit for the reduction rate of the blood filling amount is not particularly limited. For example, the upper limit is 20% or lower.
Next, an operational effect of the present embodiment will be described.
According to the artificial lung 100 of the present embodiment, the gap 190 between the heat exchange portion 160 and the gas exchange portion 170 is partially occupied by the porous member 180, and a useless space inside the housing 110 to be filled with blood is reduced. Therefore, the filling amount of blood can be effectively reduced. In addition, blood moves between the heat exchange portion 160 and the gas exchange portion 170 through the holes 181 of the porous member 180, and a heat exchange and a gas exchange are smoothly performed. Therefore, the function of the artificial lung 100 can be favorably exhibited.
When the mesh opening dimension A of the holes 181 ranges from 200 μm to 1,800 μm and the opening ratio ranges from 40% to 60%, resistance in the holes 181 is particularly and effectively suppressed, and a flow of blood is unlikely to be hindered. Therefore, it is possible to more reliably exhibit favorable heat exchange performance and gas exchange performance.
In addition, when the reduction rate of the blood filling amount due to the porous member 180 is 10% or higher, blood to fill the artificial lung 100 can be particularly and effectively reduced. Therefore, the blood transfusion amount with respect to a patient can be suppressed and a low-invasive technique can be performed.
The present invention is not limited to the embodiment described above and can be variously changed within the scope of Claims.
For example, in the embodiment, the housing 110, the heat exchange portion 160, the gas exchange portion 170, and the porous member 180 have a cylindrical shape. However, the shape thereof is not particularly limited. For example, the present invention includes a form in which a housing has a hollow rectangular parallelepiped shape, and a heat exchange portion having a flat rectangular shape, a porous member, and a gas exchange portion are stacked in this order inside thereof.
In addition, the porous member is not limited to a punching mesh obtained by forming a plurality of holes in a thin material. For example, the porous member may be a woven net formed with warp and weft. In addition, the porous member may be a porous body such as a sponge.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015-188693 | Sep 2015 | JP | national |
This application is a continuation of PCT Application No. PCT/JP2016/071323, filed Jul. 20, 2016, based on and claiming priority to Japanese Application No. 2015-188693, filed Sep. 25, 2015, both of which are incorporated herein by reference in their entirety.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/JP2016/071323 | Jul 2016 | US |
| Child | 15919511 | US |
