JP2016183964A - Inspection sheet - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide an inspection sheet that can easily perform chemical analysis of a liquid and separation and purification of a component and is lower in cost and more excellent in handleability.SOLUTION: An inspection sheet 1A according to the present application includes: a base sheet 2 made of a mixture of a fibrous material and a thermo-fusible resin; and a flow channel 3 formed in the base sheet 2 for carrying an injected inspection target liquid to a surface direction of the base sheet 2. The thermo-fusible resin is melted around the flow channel 3 in the base sheet 2 and is not melted in the flow channel 3. A compaction pressure is applied to around the flow channel 3 in the base sheet 2 and is not applied to the flow channel 3.SELECTED DRAWING: Figure 1

Description

  The present invention relates to a test sheet that is useful as a liquid chemical analysis means and can be used for medical diagnosis, water quality analysis, protein analysis, and the like.

  In recent years, the need for medical care has expanded due to changes in social structure, and so on, so-called in-situ diagnosis (point-of-care) in which a patient himself diagnoses his / her physical condition using a diagnostic device. POC) is drawing attention. One of the devices attracting attention as a diagnostic apparatus useful for POC is a device called a biochip. A typical example of a biochip is a square chip made of resin or glass with a side of several centimeters to several tens of centimeters, and a groove having a width of about 100 microns to several millimeters called a flow path is formed on the surface. The groove is formed by laser irradiation, etching, or the like. Biochips are used for separation / analysis of test liquids, synthesis with test drugs, etc., and the method of use is simple: injecting a test liquid into a flow path with a micropipette or the like. The liquid to be inspected injected into the flow path is transferred through the flow path due to the surface tension of the biochip, and the components separated by the transfer distance, chemical synthesis with the reactants and test drugs connected to the flow path are performed. Is called. The separated components and synthesized substances are analyzed by a spectrophotometer or the like and taken out from the biochip as necessary. In addition to POC, biochips are also used for new drug development and protein analysis.

  In Non-Patent Document 1, as important elements for realizing POC, 1) a diagnostic device can be stored and used at home, 2) no complicated maintenance is required, 3) a diagnostic operation that anyone can understand, and 4) low Costs, 5) easy distribution / acquisition, 6) safety, and 7) easy disposal are listed, and a biochip based on paper is described as a diagnostic device that satisfies these factors. Non-Patent Document 1 includes, as a specific example of a paper-based biochip, one obtained by attaching toluene to a filter paper dip-coated with polyester using an inkjet printer. In the portion, polyester is dissolved and functions as a flow path for the liquid to be inspected.

  Patent Document 1 describes a sheet made of a composite sheet of paper and a resin film as an inspection sheet useful for POC. The inspection sheet described in Patent Document 1 is obtained by hot-pressing a composite sheet comprising a sheet-like paper base material and a liquid-resistant film covering the surface of the paper base material from the liquid-resistant film side, The liquid-resistant film and the paper base are integrally formed to form a concave flow path, and the upper opening of the flow path is sealed with another liquid-resistant film. In the inspection sheet described in Patent Document 1, a hot-pressed portion of the composite sheet, that is, a portion that is consolidated as compared with the peripheral portion is a flow path of the liquid to be inspected.

Kento Maejima, 4 others, “Printed Paper Electronics: Microfluidic Healthcare Chips Made with Paper and Inkjet Printer”, Journal of Functional Paper, October 2012, No. 51, p.35-44

JP 2012-47604 A

  An object of the present invention is to provide a test sheet that can easily perform chemical analysis of liquid, separation / purification of components, and the like, and is excellent in handling property at low cost.

  The present invention provides a base sheet in which a fibrous material and a heat-meltable resin are mixed, and a liquid to be inspected formed on the base sheet is transferred in the surface direction of the base sheet by capillary action. The inspection sheet has a flow path to be formed, and a peripheral portion of the flow path in the base material sheet is a test sheet that prevents capillary action due to melting of the hot-melt resin.

  ADVANTAGE OF THE INVENTION According to this invention, the chemical | medical analysis of a liquid, the isolation | separation and refinement | purification of a component, etc. can be performed simply, the test sheet which is excellent in the handleability at low cost is provided. The test sheet of the present invention can be used for various purposes such as medical diagnosis, water quality analysis, and protein analysis by utilizing its function, and can also be applied to paper chromatography. The liquid to be inspected is usually an aqueous liquid, and specific examples include blood, saliva, urine, seawater, river water, well water, soil suspension, and crushed extracts of plants and foods.

FIG. 1A is a schematic perspective view of an embodiment of an inspection sheet of the present invention, and FIG. 1B is a cross-sectional view schematically showing a cross section taken along line II of FIG. is there. 2A is a schematic perspective view of another embodiment of the inspection sheet of the present invention, and FIG. 2B is a cross-sectional view schematically showing a cross section taken along line II-II in FIG. FIG. FIG. 3 is a schematic exploded perspective view of still another embodiment of the inspection sheet of the present invention. FIG. 4A is a schematic perspective view of still another embodiment of the inspection sheet of the present invention, and FIG. 4B schematically shows a cross-section taken along line III-III in FIG. It is sectional drawing. FIG. 5 is a schematic perspective view of still another embodiment of the inspection sheet of the present invention. 6A is a schematic top view of still another embodiment of the inspection sheet of the present invention, FIG. 6B is a bottom view of the embodiment, and FIG. 6C is FIG. It is sectional drawing which shows typically the IV-IV line | wire cross section of (a) and FIG.6 (b). FIG. 7A is a schematic top view of still another embodiment of the inspection sheet of the present invention, FIG. 7B is a bottom view of the embodiment, and FIG. 7C is FIG. It is sectional drawing which shows typically the VV line | wire cross section of (a) and FIG.7 (b).

  Hereinafter, the inspection sheet of the present invention will be described based on its preferred embodiments with reference to the drawings. FIG. 1 shows an embodiment of the inspection sheet of the present invention. An inspection sheet 1A shown in FIG. 1 includes a base sheet 2 and a surface direction of the base sheet formed in the base sheet 2 by a capillary phenomenon (direction perpendicular to the thickness direction). And a flow path 3 to be transferred to the main body. The base sheet 2 has a rectangular plate shape in plan view, and a Y-shaped flow path 3 in plan view is formed in the center of one side of the base sheet 2. The Y-shaped flow path 3 in plan view includes three ends of a lower end portion 30, a left upper end portion 31, and an upper right end portion 32, and a linear portion 33 that connects the plurality of end portions. Each of the end portions 30, 31, and 32 has a circular shape in a plan view, and the linear portion 33 has a continuous linear shape in a Y shape in a plan view.

  The base material sheet 2 is a mixture of a fibrous material and a heat-meltable resin. That is, the base material sheet 2 is configured to include a fibrous material and a heat-meltable resin, and the fibrous material and the heat-meltable resin constituting the base material sheet 2 are each uniform in the base material sheet 2. Is distributed unevenly.

  And in the peripheral part of the flow path 3 in the base material sheet 2, the heat-meltable resin existing in the peripheral part is melted, whereas in the flow path 3, the heat-meltable resin existing in the flow path 3 is melted. It has not been. That is, in the peripheral part of the flow path 3, since the meltable resin is melted, the inter-fiber gap of the fibrous material is closed. That is, the peripheral part of the flow path 3 is melted by the melting of the hot melt resin. In contrast to the capillary phenomenon which does not appear, in the flow path 3, since the heat-meltable resin is not melted, the inter-fiber voids of the fibrous material are not blocked, and the capillary phenomenon appears. Therefore, in the base material sheet 2, only the flow path 3 can express high water diffusibility due to capillary action. When a liquid is injected into the flow path 3, the injected liquid is It is transferred along the flow path 3 by the capillary force and is not transferred to the periphery of the flow path 3. The degree of blockage of the interfiber gap in the periphery of the flow path 3 is influenced by the melting degree of the heat-meltable resin, and is not usually completely blocked, but at least to the extent that capillary action does not occur. Is blocked.

  In the inspection sheet 1A of the present embodiment, the flow path 3 has a Y-shape in plan view (having three or more end portions), so that the flow path 3 has two or more transfer patterns. Therefore, a plurality of inspection items can be performed simultaneously at the same time. For example, of the three ends of the Y-shaped flow path 3 in plan view, the lower end 30 is used as an injecting portion for the liquid to be inspected, and the remaining two upper end portions (reaching portions for the inspecting liquid) 31 and 32. When a reagent that reacts with a component in the liquid to be inspected to cause a color reaction is applied in advance, the liquid to be inspected injected into the lower end portion 30 is converted into the linear portion 33 by the capillary force of the flow path 3. And then, it is transferred to the upper end portions 31 and 32, and is split into two at the branch point at the intermediate position of the linear portion 33. Finally, the upper end portions 31 and 32 are reached almost simultaneously, and different color reactions occur in each. Since this occurs, two inspection items corresponding to the two color development reactions can be performed simultaneously. By appropriately setting the shape of the flow path 3 in plan view, it is possible to perform three or more inspection items simultaneously.

  In the inspection sheet 1A of the present embodiment, the peripheral portion of the flow path 3 in the base sheet 2 and more specifically the portions other than the flow path 3 are all consolidated, whereas the flow path 3 is consolidated. It has not been converted. Therefore, in the inspection sheet 1A, as shown in FIG. 1, the flow path 3 protrudes to the one surface side of the base sheet 2 from the peripheral portion. That is, the flow path 3 is relatively low density and bulky, while the portions other than the flow path 3 are relatively high density and less bulky. In this way, by selectively consolidating the part other than the flow path 3 in the base sheet 2, the non-consolidated flow path 3 is visually recognized by comparison with the periphery of the consolidated flow path 3. In addition, the inter-fiber gap in the periphery of the flow path 3 is closed by consolidation, so that the fibers in the periphery of the flow path 3 are coupled with the blockage of the inter-fiber gap due to melting of the hot-melt resin. The interstitial space is further blocked, and as a result, the functionality of the flow path 3 as the liquid transfer path can be further improved. In addition, the mode of the flow path 3 in FIG. 1 is schematically described mainly for the purpose of easy understanding, and the actual flow path in the inspection sheet does not necessarily protrude as shown in FIG. Not exclusively. Further, the protruding direction of the flow path 3 varies depending on the consolidation method or the like, and may protrude on both sides of the base sheet 2.

The density of the flow path 3 (the non-consolidated portion in the base material sheet 2) is preferably 0.3 to 1.0 g / cm ³ , more preferably 0.4 to 0.7 g / cm ³ .
On the other hand, the density of the consolidated portion in the base material sheet 2 such as the peripheral part of the flow path 3 is preferably 100 to 150%, more preferably 110 to 130% with respect to the density of the flow path 3. is there.

  In order to form the flow path in the base sheet, it is necessary to melt at least the heat-melting resin in the peripheral portion of the flow path in the base sheet. A method of heating at a temperature equal to or higher than the melting point of the hot-melt resin present in the part is effective. The heating method is not particularly limited, for example, a method in which a heating tool heated to a melting point or higher of the heat-meltable resin is brought into contact with the planned heating part of the base sheet, ultrasonic waves, lasers, etc. are applied to the planned heating part of the base sheet The method of irradiating is mentioned. In addition, when the width | variety of a flow path formation plan part is small etc., the flow path formation plan part which should not be heated by the surrounding heat when the peripheral part is heated may be heated, and the resin of this part may melt. Although there is a concern, such a concern can be wiped off by appropriately adjusting the heating method and heating time, and it is possible to selectively heat and melt portions other than the flow path formation scheduled portion in the base material sheet with high accuracy. .

  As in this embodiment, in the case where the peripheral portion of the flow path in the base sheet (the portion other than the flow path) is subjected not only to the melting process of the heat-meltable resin but also to the consolidation process, both processes are performed at once. Hot embossing that can be performed is effective. The hot embossing can be performed using a known embossing device, for example, using an embossing roll having a concave portion having a shape corresponding to the shape of the flow path on the outer peripheral surface and an anvil roll receiving the embossing roll. The nip portion between the two rolls in a state where the outer peripheral surface of the anvil roll and the outer peripheral surface of the embossing roll are heated to a temperature equal to or higher than the melting point of the hot-melt resin in the base sheet. By compressing the base sheet, a flow path corresponding to the recess is formed on the surface of the base sheet facing the embossing roll.

  The base material sheet according to the present invention will be described. The fibrous material constituting the base material sheet may be a natural fiber or a synthetic fiber. For example, softwood bleached kraft pulp (NBKP), hardwood bleached kraft pulp (LBKP), softwood bleached Wood pulp such as sulfite pulp (NBSP), thermomechanical pulp (TMP), etc .; other non-wood pulp such as hemp, bamboo, straw, kenaf, three bases, straw, cotton; modified pulp such as cationized pulp, mercerized pulp, etc. Regenerated cellulose fibers such as rayon and cupra; hydrophilic synthetic fibers such as polyvinyl alcohol fibers and polyacrylonitrile fibers; and synthetic fibers made of resins such as polyethylene, polypropylene and polyethylene terephthalate. Two or more kinds can be used in combination.

  As the fibrous material constituting the base sheet, a hydrophilic fiber is preferable considering that most of the liquids to be inspected are aqueous liquids (polar solvents). The hydrophilic fibers used in the present invention are not limited to those inherently hydrophilic fibers such as natural fibers typified by wood pulp, and weakly hydrophilic or hydrophobic fibers such as synthetic fibers are hydrophilized. Things can be used. The hydrophilization treatment can be performed, for example, by applying a hydrophilic agent such as a surfactant to the fiber surface or kneading into the fiber.

  Although the magnitude | size of the fibrous material which comprises a base material sheet is not specifically limited, From a viewpoint of performing the capillary transport of the to-be-tested liquid in a flow path more reliably, the fiber length of a fibrous material becomes like this. Preferably it is 0.1-15. 0.0 mm, more preferably 0.7 to 4.5 mm.

  The freeness (CSF) of the fibrous material constituting the base sheet is preferably 100 to 700 cc, more preferably 400 to 600 cc. Freeness is a value indicated by Canadian Standard Freeness (CSF) stipulated in JIS P8121, and beating of the fibrous material (mechanical beating of the fibrous material in the presence of water and grinding. It is a value indicating the degree of processing. Usually, the smaller the freeness value, the stronger the degree of beating, the greater the damage of the fibers due to beating, and the more fibrillation proceeds. If the freeness of the fibrous material is too low, the speed of the liquid flowing through the flow path formed on the base sheet may be remarkably reduced, and if the freeness is too high, the bonding between the constituent fibers of the base sheet will be reduced. There is little possibility that the base sheet itself becomes fragile.

  The heat-meltable resin constituting the base sheet is not particularly limited. For example, in addition to polyolefin resins such as polyethylene and polypropylene, polyester resins, polyethylene vinyl acetate resins, chloroprene rubber resins, polyester resins , Polyamide resins, polyvinyl chloride resins, and the like, and these can be used alone or in combination of two or more. Among these heat-meltable resins, polyolefin resins are preferably used in the present invention because of their high chemical resistance and low environmental load during incineration. Examples of the fibrous heat-meltable resin preferably used in the present invention include SWP (registered trademark) manufactured by Mitsui Chemicals. SWP is a fibrillated olefin synthetic pulp.

  The shape of the heat-meltable resin constituting the base sheet is not particularly limited. For example, in addition to the fiber shape, a particle shape such as a spherical shape or a lump shape can be used, and a plurality of types of heat-meltable resins having different shapes are used in combination. You may do it. The fiber length of the fibrous hot-melt resin is preferably 0.1 to 5.0 mm, more preferably 0.5 to 1.5 mm. The average particle diameter of the particulate heat-meltable resin is preferably 0.1 to 100 μm, more preferably 1 to 30 μm. Here, the average particle diameter of the heat-meltable resin is a value measured by a laser diffraction particle size meter (SALD-3100, manufactured by Shimadzu Corporation).

The content of the fibrous material in the substrate sheet is preferably 20 to 95% by mass, more preferably 60 to 90% by mass, based on the total mass of the substrate sheet.
The content of the heat-meltable resin in the substrate sheet is preferably 5 to 80% by mass, more preferably 10 to 40% by mass, based on the total mass of the substrate sheet.

  The content mass ratio between the fibrous material and the heat-meltable resin in the base sheet is not particularly limited as long as it is appropriately adjusted according to the use of the inspection sheet, the types of both components, and the like. When the hydrophilic fiber and the heat-melting resin are heat-melting synthetic fibers, the content ratio of these is preferably 95: 5 to 20:80, more preferably 90, as the hydrophilic fiber: heat-melting synthetic fiber. : 10-60: 40. If the content of the heat-meltable resin is too small, the gap between the fibers in the peripheral part of the flow path is not sufficiently blocked, and the function of the flow path as a liquid transfer path may be deteriorated. If the content of the heat-meltable resin is too large, the capillary force of the flow path may be reduced.

  The flow rate of the liquid in the flow path of the base sheet is such that the mass ratio of the fibrous material and the heat-meltable resin in the base sheet, the type of fibrous material (for example, wood pulp), the beating degree of the fibrous material, etc. Since it is affected, it can be adjusted by appropriately adjusting these. For example, immunochromatography and ELISA methods are analytical methods that require a relatively long time for reaction. Therefore, the inspection sheet used for these analyzes has a relatively slow flow rate of the liquid to be inspected in the flow path, and is on the inspection sheet. Where the reaction time of the liquid to be inspected can be obtained is preferable, in order to intentionally reduce the flow rate, for example, the content of the hot-melt resin in the base sheet is greater than the content of the fibrous material, It is possible to take measures such as reducing the freeness value of the fibrous material to increase the degree of beating.

  The base sheet may contain components other than the fibrous material and the heat-meltable resin. Examples of components other than fibers that can be contained in the base sheet include, for example, a paper strength enhancer or fixing agent such as starch, polyacrylamide, and polyamine polyamide epichlorohydrin, a sizing agent, a filler, a filtrate retention improver, and a water resistance agent. , Fixing agents, antifoaming agents, slime control agents, and the like. These can be used alone or in combination of two or more.

  As the base sheet, paper, cloth, or a composite thereof can be used. The fabric base sheet may be a woven fabric or a non-woven fabric by a dry method, a wet method, a spunbond method, or the like. The paper base sheet can be produced by a known wet papermaking method. In the wet papermaking method, a stock preparation step for preparing a stock (slurry) composed of an aqueous dispersion of a fibrous material and a heat-meltable resin is usually performed, and a fibrous material and a heat-meltable resin are made from the stock. And a paper making process for drying while conveying the fiber web. Particularly preferred as the base sheet is paper.

The basis weight of the base sheet is not particularly limited, and may be appropriately adjusted according to the use of the inspection sheet, but is usually preferably 30 to 500 g / m ² , more preferably 50 to 200 g / m ² . is there. In addition, the basic weight of a base material sheet here means the basic weight of each base material sheet in the case of the laminated structure of several base material sheets like the sheet | seat 1C for an inspection mentioned later.

  The shape of the inspection sheet of the present invention and the dimensions of each part are not particularly limited as long as it is appropriately adjusted according to the application. For example, in the case of a portable inspection sheet having a rectangular shape in plan view, the longitudinal direction is 2 to 20 cm, The short direction may be 1 to 10 cm, and the maximum thickness may be 0.04 to 2.00 mm. Moreover, the width of the flow path in the inspection sheet (the length in the direction orthogonal to the length direction of the flow path) is usually about 1 to 10 mm.

  2 to 7 show other embodiments of the inspection sheet of the present invention. In other embodiments to be described later, constituent parts different from the inspection sheet 1A of the above-described embodiment will be mainly described, and the same constituent parts will be denoted by the same reference numerals and description thereof will be omitted. The description of the inspection sheet 1 </ b> A is appropriately applied to components that are not particularly described.

  In the inspection sheet 1 </ b> B shown in FIG. 2, the portion other than the flow path 3 in the base material sheet 2 is not consolidated although the hot-melt resin is melted. Therefore, in the inspection sheet 1B, although there is a possibility that minute shrinkage due to melting of the heat-meltable resin occurs in the peripheral part of the flow path 3, the flow path 3 and its peripheral part (in the base sheet 2) The density and thickness are substantially the same in the portion other than the flow path 3). Formation of the flow path 3 in the inspection sheet 1B can be performed by a heat treatment that does not involve consolidation. Similarly to the inspection sheet 1A, the inspection sheet 1B can easily perform chemical analysis of liquid, separation / purification of components, and the like, and is excellent in handleability at low cost.

  Each of the inspection sheets 1A and 1B has a single layer structure composed of one base sheet 2, but the inspection sheet 1C shown in FIG. 3 is formed by laminating a plurality of base sheets in the thickness direction. It has the laminated structure formed. More specifically, as shown in FIG. 3, the inspection sheet 1 </ b> C has a two-layer structure in which one upper base sheet 20 and one lower base sheet 21 are stacked in the thickness direction. It has a structure 22. Each of the two base sheets 20 and 21 is formed with a non-melting portion 34 in which the hot-melt resin is not melted. The portions other than the non-melting portion 34 in each of the base material sheets 20 and 21 are subjected to a consolidation treatment in addition to the fusion treatment of the heat-meltable resin, and the heat-meltable resin is melted and consolidated. Therefore, the density is higher than that of the non-melting portion 34. The two base sheets 20 and 21 are joined to each other at a portion other than the non-melting portion 34 by a known joining means such as an adhesive or heat fusion. Each of the non-melting portions 34 formed across the plurality of base material sheets is a part of the Y-shaped flow path 3 in plan view, and the non-melting portion 34 of the upper base material sheet 20 is a flow path. 3 corresponds to the three end portions (circular portions) 30, 31, and 32, and the non-melting portion 34 of the lower base sheet 21 corresponds to the linear portion 33 that is a portion other than the end portions in the flow path 3. doing. And although not shown in figure, when the laminated structure 22 is planarly viewed, the non-melting part 34 formed in each of the two base material sheets 20 and 21 is connected to the surface direction to form the flow path 3. The flow path 3 of the inspection sheet 1 </ b> C formed in this way is continuous in plan view, but the position in the thickness direction is partially different.

Similarly to the inspection sheet 1A, the inspection sheet 1C can easily perform chemical analysis of liquid, separation / purification of components, and the like, and is excellent in handleability at low cost. Particularly in the inspection sheet 1C, for example, a chemical that causes a color reaction with the liquid to be inspected is applied only to the end portions 30, 31, and 32 of the flow path 3, and the chemical is applied to the linear portion 33 of the flow path 3. If not, in the manufacturing process of the inspection sheet 1C, before joining the two base sheets 20, 21, only the end portions 30, 31, 32 of the flow path 3 in one base sheet 20 It is possible to apply the chemical in advance and not to apply the chemical to the other base sheet 21 at all, and there is a disadvantage that the chemical is erroneously applied to the linear portion 33 by such a manufacturing process. Effectively prevented.
Although not shown, for example, if the linear parts 33 are provided in each of the base material sheets 20 and 21, and the respective flow paths are combined by joining them, the branch points of the flow paths and It is possible to earn a flow path length.

  In the inspection sheet 1D shown in FIG. 4, for the purpose of controlling the flow rate of the liquid in the flow path 3, the heat-meltable resin has been softened or melted in a part of the flow path 3 to such an extent that a capillary phenomenon can occur. A liquid low diffusion portion 35 is formed. The liquid low diffusion portion 35 is a portion where the degree of melting of the heat-meltable resin is lower than the peripheral portion of the flow path 3 (in this embodiment, the portion other than the flow path 3 in the base sheet 2). As a form, there can be a form in which the hot-melt resin is softened without melting, a form in which it is melted, and a form in which both are mixed. In the peripheral part of the flow path 3 where the melting degree of the heat-melting resin is relatively high, the interfiber spaces of the fibrous material are almost completely blocked by the melting resin, and the capillary phenomenon does not occur. The liquid low diffusion part 35 of the flow path 3 having a relatively low degree of melting is softer or the interfiber gap is closed by the molten resin as compared with the part other than the liquid low diffusion part 35 in the flow path 3. Capillary phenomenon may occur without being blocked. Accordingly, the liquid is not blocked by the liquid low diffusion portion 35, but the liquid low diffusion portion 35 has a reduced liquid diffusibility due to the inter-fiber gap being closed as compared with other portions in the flow path 3. Therefore, the liquid flow velocity is reduced in the liquid low diffusion portion 35.

  As shown in FIG. 4, the flow path 3 in the inspection sheet 1 </ b> D has one end portion serving as an injecting portion 30 for the liquid to be inspected and the other end serving as a reaching portion 31 for the liquid to be inspected. In between, three linear portions 33 extending from the injection portion 30 toward the reaching portion 31 are arranged in parallel at a predetermined interval in a direction orthogonal to the extending direction (width direction of the inspection sheet 1D), Both end portions 30 and 31 are connected to each other through the three linear portions 33. The inspection sheet 1D has three transfer paths that include any one of the three linear portions 33 arranged in parallel, and among the three transfer paths, The transfer path including the linear portion 33 disposed at the center has a straight line shape in plan view connecting both end portions 30 and 31, and has the shortest length. In the middle position of the three linear portions 33, there are provided reagent applying portions 36, 37, and 38 having a circular shape in plan view to which a reagent that reacts with the liquid to be inspected is provided. 36, 37, and 38 are in the same position in the extending direction of the linear portion 33, that is, in the longitudinal direction of the inspection sheet 1D. One liquid low diffusion portion 35 described above is formed on each of two of the three linear portions 33 arranged in parallel, and one liquid low diffusion portion 35 of the liquid low diffusion portions 35 is the injection portion 30. The one liquid low diffusing unit 35 is positioned between the reagent applying unit 38 and the reaching unit 31. In the inspection sheet 1D, the liquid low diffusion portion 35 of the flow path 3 and the peripheral portion of the flow path 3 are softened or melted, but are not consolidated. The density and thickness are substantially uniform throughout the sheet 1D.

  In this way, in the inspection sheet 1D having three transfer paths, the liquid to be inspected that is dropped or injected into the injection part 30 reaches the linear part 33 by the capillary force of the flow path 3. When transferred toward the unit 31, the reagent is distributed to three transfer paths through a branch point on the way, and the reagent previously applied to each of the transfer paths when passing through the reagent applying units 36, 37, and 38. After the contact, the flow merges again before the reaching portion 31 and then flows into the reaching portion 31. However, as described above, the flow rate of the liquid is reduced in the liquid low diffusion portion 35, so that the arrival portion after the liquid to be inspected is injected into the injection portion 30 depending on the presence or absence of the liquid low diffusion portion 35 in the three transfer paths. A difference occurs in the time (liquid transfer time) required to flow into 31. In the case of FIG. 4, the liquid transfer time is the shortest when it passes through the transfer path where the low liquid diffusion part 35 is not formed (the transfer path provided with the reagent applying part 36). The transfer time is short when the liquid has a low diffusion part 35 but the liquid transfer distance passes through a short transfer path (transfer path provided with the reagent applying unit 37), and the liquid transfer time is the longest. In this case, the liquid passing through the transfer path having the low liquid diffusion portion 35 and the liquid transfer distance is long (the transfer path provided with the reagent applying unit 38).

  As in the inspection sheet 1D, when there are a plurality of liquid transfer paths to be inspected and the liquid transfer time is different between the plurality of transfer paths, the liquid to be inspected can be injected only once. In addition, the reagent addition in the inspection sheet can be advanced step by step, and the analysis can be performed efficiently. For example, in detection using an antigen-antibody reaction such as an ELISA method or detection using other chemical reactions, it is necessary to add several kinds of chemicals step by step. It is possible to automatically perform a multi-stage reaction, which can be expected to improve work efficiency.

  The liquid low diffusion part 35 of the flow path 3 can be formed by heating the base material sheet 2 under milder conditions than the peripheral part of the flow path 3. That is, in order to form the liquid low diffusion portion 35, the base sheet 2 is heated at a lower heating temperature and / or shorter heating time than when the peripheral portion of the flow path 3 is formed, and the heated portion is melted. The soft resin may be softened or melted.

  In this way, forming a plurality of portions (the liquid low diffusion portion 35 of the flow channel 3 and the peripheral portion of the flow channel 3 in the inspection sheet 1D) having different melting degrees of the heat-meltable resin on the base sheet Although it can be carried out by appropriately changing the heating conditions depending on the degree of melting required for the part, from the viewpoint of more surely carrying out this, the base sheet has two or more types of hot melts having different melting temperatures. It is preferable that a functional resin is contained. Such a base sheet containing two or more kinds of heat-meltable resins has a plurality of melting temperatures due to the plurality of heat-meltable resins contained therein, and therefore the heating temperature for each part of the base sheet is set. By appropriately adjusting the relative relationship with the plurality of melting temperatures, the degree of melting of the heat-meltable resin in the portion can be controlled within a desired range. For example, in the case of the inspection sheet 1 </ b> D, in order to form the peripheral portion of the flow path 3, a temperature higher than the highest one among the plurality of melting temperatures caused by the plurality of heat-melting resins contained in the base sheet 2 is used. What is necessary is just to heat the formation scheduled site | part of the peripheral part of the flow path 3 in the base material sheet 2 with the heating temperature (maximum heating temperature) of this. Moreover, in order to form the liquid low diffusion part 35 of the flow path 3, since the liquid low diffusion part 35 is a part where the melting degree of the hot-melt resin is lower than the peripheral part of the flow path 3, it is less than the maximum heating temperature. In addition, the liquid low diffusion portion 35 is scheduled to be formed in the base sheet 2 at a heating temperature that is equal to or higher than the lowest one of the plurality of melting temperatures caused by the plurality of heat-meltable resins contained in the base sheet 2. What is necessary is just to heat a site | part. The “two or more heat-meltable resins having different melting temperatures” contained in the base sheet may be separate from each other or may be integrated like a core-sheath type composite fiber.

  The inspection sheet 1E shown in FIG. 5 is consolidated in addition to the melting process of the hot-melt resin for the liquid low diffusion portion 35 of the flow channel 3 and the peripheral portion of the flow channel 3 (the portion other than the flow channel 3). It differs from the inspection sheet 1D in which the consolidation process is not performed on these parts in that the process is performed. For this reason, although the thickness of the inspection sheet 1D is substantially uniform, in the inspection sheet 1E, the flow path 3 that has not been subjected to the consolidation treatment protrudes to the one surface side of the base sheet 2 from its peripheral portion. The flow path 3 is relatively low density and bulky, while the portions other than the flow path 3 are relatively high density and small in volume. Further, when the degree of consolidation (pressure during pressurization) is lower than the peripheral part of the flow path 3, the liquid low diffusion part 35 has a protruding height of the liquid low diffusion part 35 as shown in FIG. If the degree of consolidation (pressure at the time of pressurization) is the same as that of the peripheral part of the flow path 3, it is not shown in the figure, although it can be lower than the part other than the liquid low diffusion part 35 in the path 3. The protruding height of the liquid low diffusion portion 35 can be equivalent to the portion other than the liquid low diffusion portion 35 in the flow path 3. The inspection sheet 1E has the same effect as the inspection sheet 1D, and the flow path 3 selectively protrudes, so that the same effect as the inspection sheet 1A, that is, the visibility of the flow path 3 is obtained. The improvement effect and the improvement effect of the functionality of the flow path 3 as the transfer path of the liquid to be inspected are also exhibited.

  The inspection sheet 1F shown in FIG. 6 and the inspection sheet 1G shown in FIG. 7 each have a laminated structure 25 formed by laminating a plurality (two) of base sheets 23 and 24 in the thickness direction. When the material sheet 23 is on the upper surface side and the base material sheet 24 is on the lower surface side, the base material sheets 23 and 24 that are two layers adjacent in the thickness direction in the laminated structure 25 are contained in the base material sheets 23 and 24. The melting temperatures of the hot-melt resins are different from each other.

  In the inspection sheet 1F shown in FIG. 6, the base sheet 23 on the upper surface side contains a heat-meltable resin having a relatively high melting temperature, and the base sheet 24 on the lower surface side has a heat having a relatively low melting temperature. Contains a meltable resin. In the base material sheet 23, a flow path 3 having a linear shape in plan view extending in the longitudinal direction of the base material sheet 23 is formed at the center thereof, but no flow path is formed in the base material sheet 24. The portions other than the flow path 3 in the base sheet 23, 24 are subjected to the melting process of the heat-meltable resin, and the melting process applied to the base sheet 23 is applied to the base sheet 24. The temperature is higher than the melting process. For this reason, portions other than the flow path 3 in the base material sheet 23 have a higher degree of melting of the heat-meltable resin than the base material sheet 24, and the capillary phenomenon is difficult to occur. Since the flow path 3 is not formed in the lowermost base sheet 24 and the entire base sheet 24 is melted and the liquid diffusibility is reduced, the inspection sheet 1F has a flow path 3 is advantageous in that it is difficult for the liquid transferred through 3 to permeate the base sheet 24 in the thickness direction and ooze from the lower surface side.

  In the manufacturing method of the inspection sheet 1 </ b> F, the base material sheets 23 and 24 are laminated and integrated to obtain a laminated structure 25, and the laminated structure 25 is subjected to a melting process of a hot-melt resin to form the flow path 3. In this process, the melting treatment is first performed on the base sheet 24 containing the heat-melting resin having a relatively low melting temperature, and then the heat-melting resin having a relatively high melting temperature. It is preferable to implement with respect to the base material sheet 23 to contain. The reason is that, conversely, when the base material sheet 23 having a relatively high melting temperature is performed first, the influence of the melt processing on the base material sheet 23 may reach the base material sheet 24. This is to avoid such inconvenience.

  In the inspection sheet 1G shown in FIG. 7, the base sheet 23 on the upper surface side contains a heat-meltable resin having a relatively low melting temperature, and the base sheet 24 on the lower surface side has a heat having a relatively high melting temperature. Contains a meltable resin. In the base sheet 23, two end portions 39, 39 of the circular flow path 3 having a circular shape in plan view, which is the injection portion or the arrival portion of the liquid to be inspected, are provided at predetermined intervals in the longitudinal direction at the central portion in the width direction. The base material sheet 24 is formed with a linear portion 33 that is another part of the flow path 3 that is linear in plan view extending in the longitudinal direction of the base material sheet 24 at the center portion thereof, Both end portions 39, 39 are connected via a single linear portion 33. The portions other than the flow path 3 in the base sheet 23, 24 are subjected to a melting process of the heat-meltable resin, and the melting process applied to the base sheet 24 is applied to the base sheet 23. The temperature is higher than the melting process. For this reason, parts other than the flow path 3 (end part 39) in the base material sheet 24 are compared with parts other than the flow path 3 (linear part 33) in the base material sheet 23, and the melting degree of the heat-meltable resin. The capillarity is difficult to develop. In the inspection sheet 1G, a linear portion 33 (portion that functions as a flow path for the liquid to be inspected) and both end portions 39 and 39 (portions that function as dripping or detection spots of the liquid to be inspected) constituting the flow path 3; However, they are not formed in the same layer (the same substrate sheet), and the positions in the thickness direction are different from each other. The present invention includes a sheet having a complicated flow path such that the flow path is formed across a plurality of layers, such as the inspection sheet 1G.

The present invention is not limited to the above-described embodiment, and can be appropriately changed without departing from the gist of the present invention. For example, the shape of the flow channel according to the present invention in plan view, the dimensions of each part, use of the inspection sheet, etc. It can be set appropriately according to
Further, the laminated structure 22 of the inspection sheet 1C shown in FIG. 3 may be three or more layers, and other than the non-melting portion 34 (channel 3) in each of the base material sheets 20 and 21 constituting the laminated structure 22. This part may not be consolidated.

1A, 1B, 1C, 1D, 1E, 1F, 1G Inspection sheets 2, 20, 21, 23, 24 Base sheet 22, 25 Laminate structure 3 Channel 30 End of channel (injection part of liquid to be inspected)
31, 32 Ends of flow path (arrival part of liquid to be inspected)
33 Linear portion of flow path 34 Non-melting portion 35 Low liquid diffusion portion 36, 37, 38 Reagent application portion 39 End portion of flow channel (injection portion or arrival portion of liquid to be inspected)

Claims (6)

A base sheet in which a fibrous material and a heat-meltable resin are mixed, and a flow path formed on the base sheet and transporting the injected inspection liquid in the surface direction of the base sheet by a capillary phenomenon An inspection sheet having
An inspection sheet in which a peripheral portion of the flow path in the base material sheet does not cause capillary action due to melting of the heat-meltable resin.   The inspection sheet according to claim 1, wherein a peripheral portion of the flow path in the base material sheet has a relatively high density, and the flow path has a relatively low density.   The fibrous material is a hydrophilic fiber, the heat-meltable resin is a heat-meltable synthetic fiber, and the content ratio thereof is 95: 5 to 20:80 as a hydrophilic fiber: heat-meltable synthetic fiber. The inspection sheet according to claim 1 or 2. A non-melting part in which the heat-meltable resin is not melted is formed in each of the plurality of base material sheets, having a laminated structure in which a plurality of base material sheets are laminated in the thickness direction,
The planar view of the laminated structure, the non-melting part formed in each of the plurality of base material sheets is connected to the surface direction to form the flow path. Inspection sheet.   The inspection according to any one of claims 1 to 4, wherein a low-diffusion part in which the hot-melt resin is softened or melted to such an extent that a capillary phenomenon can occur is formed in a part of the flow path. Sheet.   The inspection sheet according to any one of claims 1 to 5, wherein the base sheet contains two or more kinds of the hot-melt resins having different melting temperatures.

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