Patent Publication Number: US-2023160139-A1

Title: Electroless plated fiber material, manufacturing method, and manufacturing system therefor

Description:
TECHNICAL FIELD 
     The present invention relates to a manufacturing method for an electroless plated fiber material including a step of applying electroless plating processing to a fiber material with the use of a solution containing metal ions and a solution containing a reducing agent. The present invention relates to an electroless plated fiber material manufactured by such manufacturing method. The present invention also relates to a manufacturing system for an electroless plated fiber material, the manufacturing system including an electroless plating apparatus configured to apply electroless plating processing to a fiber material with the use of a solution containing metal ions and a solution containing a reducing agent. 
     BACKGROUND ART 
     Electroless plating processing may be applied to a fiber material in order to produce a fiber material having conductivity, for example. In the electroless plating processing, a plated film obtained by depositing metal by reducing metal ions with use of a reducing agent is formed on a fiber material. One example in a technology of manufacturing the electroless plated fiber material includes an electroless plating processing step of immersing a fiber material in a plating solution. (For example, see Patent Documents 1 to 3.) 
     Another example in the technology of manufacturing the electroless plated fiber material includes an electroless plating processing step of spraying a solution containing metal ions onto a fiber material containing a reducing agent by electrospraying, to thereby generate metal particles in the fiber material by a reaction between the metal ions and the reducing agent. (For example, see Patent Document 4.) 
     Yet another example in the technology of manufacturing the electroless plated fiber material includes an electroless plating processing step of spraying a solution containing metal ions in a state of being electrically charged to either a positive potential or a negative potential by electrospraying and spraying a solution containing a reducing agent in a state of being electrically charged to the other of the positive potential and the negative potential by electrospraying onto a fiber material, to thereby generate metal particles in the fiber material by a reaction between the metal ions and the reducing agent. (For example, see Patent Document 5.) 
     In one example, another example, and yet another example in the technology of manufacturing the electroless plated fiber material, preparation steps such as a cleaning processing step of immersing the fiber material in a cleaning fluid, a tannic acid processing step of immersing the fiber material in a tannic acid solution in order to increase the adhesion between the fiber material and the plated film, and a catalyzing processing step of immersing the fiber material in a catalyzing processing fluid in order to adhere a catalyst to the fiber material, are performed before the electroless plating processing step. (For example, see Patent Documents 1 to 5.) 
     CITATION LIST 
     Patent Literature 
     
         
         Patent Document 1: 
         Patent Document 2: 
         Patent Document 3: 
         Patent Document 4: 
         Patent Document 5: 
         U.S. Pat. No. 3,877,965 
         Japanese Patent Laid-Open No. 7-173636 
         Japanese Patent Laid-Open No. 2003-105552 
         International Publication No. WO 2015/060341 
         International Publication No. WO 2015/060342 
       
    
     SUMMARY OF INVENTION 
     Problem to be Solved by the Invention 
     In the electroless plating processing step of one example in the technology of manufacturing the electroless plated fiber material and the preparation steps in one example and another example in the technology of manufacturing the electroless plated fiber material, the fiber material needs to be immersed in various processing solutions collected in a tank and the like. However, the processing solution may contain precious metal, and using a large amount of such processing solution increases the manufacturing cost. The solution after usage contains environmentally hazardous substances, and it incurs high costs to perform waste disposal processing of such solutions in a manner complying with environmental regulations. When the fiber material is immersed in the processing solution, batch processing needs to be performed in the tank in which the solution is collected and the like. The usage of an apparatus for performing the batch processing also causes the manufacturing cost to increase. The above also causes a decrease in the manufacturing efficiency of the electroless plated fiber material. 
     There is room for improvement for the electroless plated fiber material regarding increasing the quality thereof. For example, it has been desired that the conductivity of the electroless plated fiber material be increased and that the thickness of the plated film of the electroless plated fiber material be reduced. 
     In view of such actual circumstances, in the manufacturing method for the electroless plated fiber material, it is desired that the amount of the processing solution used be reduced, and the quality of the electroless plated fiber material manufactured be increased. In the manufacturing method for the electroless plated fiber material, it is desired that the conductivity of the electroless plated fiber material manufactured be increased, the thickness of the plated film of the electroless plated fiber material manufactured be reduced, the manufacturing cost of the electroless plated fiber material be reduced, the environmental load be reduced, and the manufacturing efficiency of the electroless plated fiber material be improved. 
     In the electroless plated fiber material, it is desired that the amount of the processing solution to be used at the time of manufacturing be reduced and the quality be increased. In the electroless plated fiber material, it is desired that the conductivity be increased, the thickness of the plated film be reduced, the manufacturing cost be reduced, the environmental load that may occur at the time of manufacturing be reduced, and the manufacturing efficiency be improved. 
     In a manufacturing system of the electroless plated fiber material, it is desired that the amount of the processing solution used be reduced and the quality of the electroless plated fiber material manufactured be increased. In the manufacturing system of the electroless plated fiber material, it is desired that the conductivity of the electroless plated fiber material manufactured be increased, the thickness of the plated film of the electroless plated fiber material manufactured be reduced, the manufacturing cost be reduced, the environmental load be reduced, and the manufacturing efficiency of the electroless plated fiber material be improved. 
     Means for Solving the Problems 
     A manufacturing method for an electroless plated fiber material according to one aspect includes: a catalyzing step of electrostatically spraying a catalyst solution containing a catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto a fiber material which is grounded or electrically charged to a potential opposite from the potential of the catalyst solution and which is moistened, and electrostatically spraying a first reducing agent solution containing a reducing agent of the catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material which is grounded or electrically charged to a potential opposite from the potential of the first reducing agent solution and which is moistened, to thereby obtain a catalyst-applied fiber material in which a catalyst is given to the fiber material; and an electroless plating step of electrostatically spraying each of a metal ion solution containing metal ions and a second reducing agent solution containing a reducing agent of the metal ions, each in a state of being electrically charged to a positive potential or a negative potential in a similar manner, onto the catalyst-applied fiber material which is grounded or electrically charged to a potential opposite from the potential of the metal ion solution and the second reducing agent solution and which is moistened, such that the metal ion solution and the second reducing agent solution react with each other in the same electric field on the catalyst-applied fiber material, to thereby obtain an electroless plated fiber material in which a plated film is formed on the catalyst-applied fiber material. 
     An electroless plated fiber material according to one aspect is manufactured by a manufacturing method including: a catalyzing step of electrostatically spraying a catalyst solution containing a catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto a fiber material which is grounded or electrically charged to a potential opposite from the potential of the catalyst solution and which is moistened, and electrostatically spraying a first reducing agent solution containing a reducing agent of the catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material which is grounded or electrically charged to a potential opposite from the potential of the first reducing agent solution and which is moistened, to thereby obtain a catalyst-applied fiber material in which a catalyst is applied to the fiber material; and an electroless plating step of electrostatically spraying each of a metal ion solution containing metal ions and a second reducing agent solution containing a reducing agent of the metal ions, each in a state of being electrically charged to a positive potential or a negative potential in a similar manner, onto the catalyst-applied fiber material which is grounded or electrically charged to a potential opposite from the potential of the metal ion solution and the second reducing agent solution and which is moistened, such that the metal ion solution and the second reducing agent solution react with each other in the same electric field on the catalyst-applied fiber material, to thereby obtain an electroless plated fiber material in which a plated film is formed on the catalyst-applied fiber material. 
     A manufacturing system of an electroless plated fiber material according to one aspect includes: a catalyzing apparatus configured to obtain a catalyst-applied fiber material in which a catalyst is applied to a fiber material; an electroless plating apparatus configured to obtain an electroless plated fiber material in which a plated film is formed on the catalyst-applied fiber material; and a fiber material sent to the catalyzing apparatus. In the manufacturing system, the catalyzing apparatus has: a nozzle for a catalyst configured to electrostatically spray a catalyst solution containing a catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material which is grounded or electrically charged to a potential opposite from the potential of the catalyst solution and which is moistened; and a nozzle for a first reducing agent configured to electrostatically spray a first reducing agent solution containing a reducing agent of the catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material which is grounded or electrically charged to a potential opposite from the potential of the first reducing agent solution and which is moistened, the electroless plating apparatus has: a nozzle for metal ions configured to electrostatically spray a metal ion solution containing metal ions in a state of being electrically charged to a positive potential or a negative potential onto the catalyst-applied fiber material; and a nozzle for second reducing agent configured to electrostatically spray a second reducing agent solution containing a reducing agent of the metal ions in a state of being electrically charged to the same potential as the potential of the metal ion solution onto the catalyst-applied fiber material, and the electroless plating apparatus is configured to cause the metal ion solution electrostatically sprayed from the nozzle for metal ions and the second reducing agent solution electrostatically sprayed from the nozzle for second reducing agent to react with each other in the same electric field on the catalyst-applied fiber material which is grounded or electrically charged to a potential opposite from the potential of the metal ion solution and the second reducing agent solution and which is moistened. 
     Advantageous Effects of Invention 
     In the manufacturing method for the electroless plated fiber material according to one aspect, the amount of the processing solution to be used can be reduced, and the quality of the electroless plated fiber material to be manufactured can be increased. In the manufacturing method for the electroless plated fiber material according to one aspect, the conductivity of the electroless plated fiber material to be manufactured can be increased, the thickness of the plated film of the electroless plated fiber material to be manufactured can be reduced, the manufacturing cost of the electroless plated fiber material can be reduced, the environmental load can be reduced, and the manufacturing efficiency of the electroless plated fiber material can be improved. 
     In the electroless plated fiber material according to one aspect, the amount of the processing solution to be used at the time of manufacturing can be reduced, and the quality can be increased. In the electroless plated fiber material according to one aspect, the conductivity can be increased, the thickness of the plated film can be reduced, the manufacturing cost can be reduced, the environmental load that may occur at the time of manufacturing can be reduced, and the manufacturing efficiency can be improved. 
     In the manufacturing system of the electroless plated fiber material according to one aspect, the amount of the processing solution to be used can be reduced, and the quality of the electroless plated fiber material to be manufactured can be increased. In the manufacturing system of the electroless plated fiber material according to one aspect, the conductivity of the electroless plated fiber material to be manufactured can be increased, the thickness of the plated film of the electroless plated fiber material to be manufactured can be reduced, the manufacturing cost can be reduced, the environmental load can be reduced, and the manufacturing efficiency of the electroless plated fiber material can be improved. 
    
    
     
       BRIEF DESCRIPTION OF DRAWINGS 
         FIG.  1    is a flowchart for describing a manufacturing method for an electroless plated fiber material according to a first embodiment. 
         FIG.  2    is a front view schematically illustrating a catalyzing apparatus used in a catalyzing step of the manufacturing method for the electroless plated fiber material according to the first embodiment with a supporting apparatus that supports the fiber material. 
         FIG.  3    is a front view schematically illustrating an electroless plating apparatus used in an electroless plating step of the manufacturing method for the electroless plated fiber material according to the first embodiment with the supporting apparatus. 
         FIG.  4    is a cross-sectional view schematically illustrating a degreasing apparatus used in a degreasing step of the manufacturing method for the electroless plated fiber material according to the first embodiment. 
         FIG.  5    is a cross-sectional view schematically illustrating a preprocessing apparatus used in a preprocessing step of the manufacturing method for the electroless plated fiber material according to the first embodiment. 
         FIG.  6    is a front view schematically illustrating a cleaning apparatus used in each of a precleaning step, an intermediate cleaning step, and a post-cleaning step of the manufacturing method for the electroless plated fiber material according to the first embodiment with the supporting apparatus. 
         FIG.  7    is a schematic view of a manufacturing system of an electroless plated fiber material according to a second embodiment. 
     
    
    
     MODE FOR CARRYING OUT THE INVENTION 
     Electroless plated fiber materials and manufacturing methods and manufacturing systems thereof according to a first embodiment and a second embodiment are described below. In each of the manufacturing methods and the manufacturing systems according to the first and second embodiments, a fiber material having a plated film obtained by depositing metal by electroless plating processing, in other words, an electroless plated fiber material, is produced. 
     First Embodiment 
     The electroless plated fiber material and the manufacturing method and the manufacturing system thereof according to the first embodiment are described. 
     Overview of Electroless Plated Fiber Material and Manufacturing Method Therefor 
     An outline of an electroless plated fiber material A 4  and a manufacturing method therefor according to the present embodiment is described with reference to  FIG.  1    to  FIG.  3   . As illustrated in  FIG.  1   , the manufacturing method for the electroless plated fiber material A 4  roughly includes a catalyzing step S 5  (details shown in  FIG.  2   ) and an electroless plating step S 7  (details shown in  FIG.  3   ). 
     In such a manufacturing method, as illustrated in  FIG.  2   , the following is performed in the catalyzing step S 5 . While a fiber material A 2  described below is being grounded and the fiber material A 2  is being moistened, a catalyst solution B that is a solution containing a catalyst precursor in a state of being electrically charged to a positive potential (indicated by character+) is electrostatically sprayed onto the fiber material A 2 . However, in the catalyzing step, instead of grounding the fiber material, the fiber material can be electrically charged to a potential opposite from the potential of the catalyst solution. The catalyst solution can also be electrostatically sprayed onto the fiber material in a state of being electrically charged to a negative potential. 
     In the catalyzing step S 5 , while the fiber material A 2  is being grounded and the fiber material A 2  is being moistened, a first reducing agent solution C that is a solution containing a reducing agent of the catalyst precursor in a state of being electrically charged to a positive potential (indicated by character+) is electrostatically sprayed onto the fiber material A 2 . The potential of the catalyst solution B and the potential of the first reducing agent solution C are the same. 
     However, in the catalyzing step, instead of grounding the fiber material, the fiber material can be electrically charged to a potential opposite of the potential of the first reducing agent solution. The first reducing agent solution can also be electrostatically sprayed onto the fiber material in a state of being electrically charged to a negative potential. The potential of the first reducing agent solution can also be different from the potential of the catalyst solution. 
     In the catalyzing step S 5  as above, a catalyst-applied fiber material A 3  in which a catalyst is applied to the fiber material A 2  is obtained. The catalyst-applied fiber material A 3  is simply referred to as a fiber material A 3  as needed below. 
     As illustrated in  FIG.  3   , in the electroless plating step S 7 , while the catalyst-applied fiber material A 3  is being grounded and the fiber material A 3  is being moistened, each of a metal ion solution D that is a solution containing metal ions and a second reducing agent solution E that is a solution containing a reducing agent of the metal ions each in a state of being electrically charged to a positive potential (indicated by a “+”) is electrostatically sprayed onto the fiber material A 3  such that the metal ion solution D and the second reducing agent solution E react with each other in the same electric field on the fiber material A 3 . The potential of the metal ion solution D and the potential of the second reducing agent solution E are the same. The potentials of the metal ion solution D and the second reducing agent solution E are the same as the potentials of the catalyst solution B and the first reducing agent solution C. 
     However, in the electroless plating step, instead of grounding the fiber material, the fiber material can be electrically charged to a potential opposite of the potentials of the metal ion solution and the second reducing agent solution. The metal ion solution and the second reducing agent solution can also be electrostatically sprayed onto the fiber material in a state of being electrically charged to a negative potential. The potentials of the metal ion solution and the second reducing agent solution can also be different from one or both of the potentials of the catalyst solution and the first reducing agent solution. 
     In the electroless plating step S 7  as above, an electroless plated fiber material A 4 , in which a plated film is formed on the fiber material A 3 , is obtained. The electroless plated fiber material A 4  is simply referred to as a fiber material A 4  as needed below. The electroless plated fiber material A 4  according to the present embodiment can be generally manufactured by such manufacturing method. 
     Details of Electroless Plated Fiber Material and Manufacturing Method Therefor 
     Details of the electroless plated fiber material A 4  and the manufacturing method therefor according to the present embodiment are described with reference to  FIG.  1    to  FIG.  6   . As illustrated in  FIG.  1   , in detail, the manufacturing method for the electroless plated fiber material A 4  can include a degreasing step S 1  (details shown in  FIG.  4   ), a pre-drying step S 2 , a pre-processing step S 3  (details shown in  FIG.  5   ), a pre-cleaning step S 4  (details shown in  FIG.  6   ), a catalyzing step S 5  (details shown in  FIG.  2   ), an intermediate cleaning step S 6  (details shown in  FIG.  6   ), an electroless plating step S 7  (details shown in  FIG.  3   ), a post-cleaning step S 8  (details shown in  FIG.  6   ), and a post-drying step S 9 . 
     In such manufacturing method, as illustrated in  FIG.  4   , a fiber material A 1  is degreased in the degreasing step S 1 . Although not particularly clearly illustrated, the fiber material A 1  is dried in the pre-drying step S 2  after the degreasing step S 1 . It is also possible to omit the pre-drying step S 2  when the degreasing fluid F is volatile. 
     As illustrated in  FIG.  5   , in the pre-processing step S 3 , pre-processing is applied so as to electrically charge the fiber material A 1  dried in the pre-drying step S 2  to a negative charge in order to increase the adhesion between the pre-processed fiber material A 2  described below and the plated film. In the pre-processing step S 3 , the pre-processed fiber material A 2  in which pre-processing is applied to the fiber material A 1  is obtained. The pre-processed fiber material A 2  is simply referred to as a fiber material A 2  as needed below. However, it is also possible to omit the pre-processing step when one or both of the catalyzing step and the electroless plating processing step includes or include an operation of electrostatically spraying a solution electrically charged to a negative potential onto the fiber material as described above. 
     As illustrated in  FIG.  6   , after the pre-processing step S 3 , the pre-processed fiber material A 2  is cleaned in the pre-cleaning step S 4 . As illustrated in  FIG.  2   , in the catalyzing step S 5 , while the fiber material A 2  cleaned in the pre-cleaning step S 4  is being grounded and the fiber material A 2  is being moistened, the catalyst solution B in a state of being electrically charged to a positive potential is electrostatically sprayed onto the fiber material A 2 . In the catalyzing step S 5 , while the fiber material A 2  is being grounded and the fiber material A 2  is being moistened, the first reducing agent solution C in a state of being electrically charged to a positive potential is electrostatically sprayed onto the fiber material A 2 . In the catalyzing step S 5 , the catalyst-applied fiber material A 3  is obtained. 
     As illustrated in  FIG.  6   , after the catalyzing step S 5 , the catalyst-applied fiber material A 3  is cleaned in the intermediate cleaning step S 6 . As illustrated in  FIG.  3   , in the electroless plating step S 7 , while the fiber material A 3  cleaned in the intermediate cleaning step S 6  is being grounded and the fiber material A 3  is being moistened, each of the metal ion solution D and the second reducing agent solution E each in a state of being electrically charged to a positive potential is electrostatically sprayed onto the fiber material A 3  such that the metal ion solution D and the second reducing agent solution E react with each other in the same electric field on the fiber material A 3 . In the electroless plating step S 7 , the electroless plated fiber material A 4  is obtained. 
     As illustrated in  FIG.  6   , after the electroless plating step S 7 , the electroless plated fiber material A 4  is cleaned in the post-cleaning step S 8 . Although not particularly clearly illustrated, the fiber material A 4  cleaned in the post-cleaning step S 8  is dried in the post-drying step S 9 . The manufacturing method for the electroless plated fiber material can also include an annealing processing step of applying annealing processing to the electroless plated fiber material after the post-drying step. The electroless plated fiber material A 4  according to the present embodiment can be manufactured by such manufacturing method in detail. 
     Details of Fiber Material 
     In detail, the fiber material A 1  may be as follows. The specific material quality, the difference between natural fiber and synthetic fiber, the form of the material, and the like of the fiber material A 1  are not particularly limited as long as the fiber material A 1  is a filiform material containing a high polymer compound as a component or is a material (cotton, woven fabric, non-woven fabric, paper, and the like) obtained by bundling the filiform material. Examples of the type of the fiber material include plant fiber such as hemp and cotton, animal fiber such as wool and silk, regenerated fiber such as rayon, polyamide synthetic fiber such as nylon (nylon 6,6 and the like), polyester synthetic fiber, acrylic synthetic fiber, polyvinylalcohol synthetic fiber, polyolefin synthetic fiber, polyurethane synthetic fiber, cellulose semi-synthetic fiber, and protein-based semi-synthetic fiber. The fiber material is more preferably thread, woven fabric, non-woven fabric, knit fabric, paper, or film. 
     When the fiber material is thread, the thickness of the thread can be from about 30 denier to about 1200 denier, for example. The thickness of the thread is preferably from about 30 denier to about 300 denier. 
     The fiber material A 1  is preferably hydrophilic considering the fact that the fiber materials A 2 , A 3  are moistened in the catalyzing step S 5  and the electroless plating step S 7 . However, the fiber material may be hydrophobic. In this case, processing for providing a hydrophilic property to the fiber material such as surface modification processing is preferably applied to the fiber material. 
     Details of Degreasing Step 
     In detail, the degreasing step S 1  can be as follows, as illustrated in  FIG.  4   . In the degreasing step S 1 , the fiber material A 1  is immersed in the degreasing fluid F. As a result, the fiber material A 1  is degreased. In the degreasing step S 1 , raw thread oil, woven fabric oil, knit fabric oil, dirt, and the like can be removed from the fiber material A 1 . 
     In the degreasing step S 1 , a degreasing apparatus  10  configured to be able to degrease the fiber material A 1  is used. The degreasing apparatus  10  has a tank  11  configured to be able to collect the degreasing fluid F. In the degreasing step S 1 , the entirety of the fiber material A 1  is immersed in the degreasing fluid F in the tank  11 . 
     As the degreasing fluid F, a degreasing fluid normally used in the degreasing of fiber can be used depending on the type of the fiber. For example, the degreasing fluid F can be an organic solvent containing acetone, isopropyl alcohol, ethanol, chloroform, methanol, xylene, and the like. The degreasing fluid F can be an alkaline cleaning agent containing caustic soda, sodium carbonate, sodium tertiary phosphate, sodium tripolyphosphate, sodium orthosilicate, sodium metasilicate, non-ionic surfactant, and the like. 
     The atmospheric temperature of the environment in which the degreasing step S 1  is performed, in other words, the ambient temperature of the degreasing apparatus  10  can be room temperature. The processing temperature of the degreasing fluid F can be from normal temperature (about 20° C.) to about 80° C. The amount of immersing time by which the fiber material A 1  is immersed in the degreasing fluid F can be from about one minute to about 10 minutes. However, the atmospheric temperature, the processing temperature, and the amount of immersing time are not limited to the above. The atmospheric temperature, the processing temperature, and the amount of immersing time can be adjusted, as appropriate, such that raw thread oil, woven fabric oil, knit fabric oil, dirt, and the like can be efficiency removed from the fiber material. 
     Details of Pre-Drying Step and Post-Drying Step 
     Although not particularly illustrated in a clear manner, the pre-drying step and post-drying step S 2 , S 9  can be as follows. In the pre-drying step S 2 , warm air or hot air is applied to the fiber material A 1  degreased in the degreasing step S 1  so as to dry the fiber material A 1 . In the post-drying step S 9 , warm air or hot air is applied to the electroless plated fiber material A 4  cleaned in the post-cleaning step S 8  so as to dry the fiber material A 4 . 
     In each of the pre-drying step and post-drying step S 2 , S 9 , a drying apparatus (not shown) configured to be able to apply warm air or hot air to the fiber materials A 1 , A 4  is used. However, the fiber material can also be naturally dried in either the pre-drying step or the post-drying step. 
     Details of Preprocessing Step 
     In detail, the preprocessing step S 3  can be as follows as illustrated in  FIG.  5   . In the preprocessing step S 3 , the fiber material A 1  is immersed in a processing fluid G containing a processing agent. As a result, the fiber material A 1  is electrically charged to a negative charge. The adhesion between the preprocessing fiber material A 2  and the plated film can be increased by the preprocessing step S 3 . 
     In the preprocessing step S 3 , a preprocessing apparatus  20  configured to be able to perform preprocessing that enables the adhesion between the fiber material A 2  and the plated film to be increased is used. The preprocessing apparatus  20  has a tank  21  configured to be able to collect the processing fluid G. In the preprocessing step S 3 , the entirety of the fiber material A 2  is immersed in the processing fluid Gin the tank  21 . 
     The processing agent contained in the processing fluid G can be a solution containing a substance capable of providing a negative charge to the fiber material A 1  such as a polyphenol compound such as tannic acid, gallic acid, pyrogallol, and catechol. By providing a negative charge to the fiber material A 1  and electrically charging the fiber material A 1  to be negative, the adhesiveness of the metal ions that serve as the catalyst precursor to the preprocessing fiber material A 2  can be increased in the subsequent catalyzing step S 5 . The adhesion between the plated film formed thereafter and the catalyst-applied fiber material A 3  can be increased. When the processing agent is tannic acid, the processing fluid G can also be referred to as a tannic acid solution G and the preprocessing step S 3  can also be referred to as a tannic acid processing step S 3 . The concentration of the processing agent in the processing fluid G can be from about 0.1 mass % to about 5.0 mass %. 
     The atmospheric temperature of the environment in which the preprocessing step S 3  is performed, in other words, the ambient temperature of the preprocessing apparatus  20 , can be room temperature. The processing temperature of the processing fluid G can be from normal temperature (about 20° C.) to about 100° C. The amount of immersing time by which the fiber material A 1  is immersed in the processing fluid G can be from about one minute to about 10 minutes. However, the atmospheric temperature, the processing temperature, and the amount of immersing time are not limited to the above. The atmospheric temperature, the processing temperature, and the amount of immersing time can be regulated, as appropriate, such that the adhesion between the fiber material and the plated film can be increased. The preprocessing step may be other processing normally performed as the preprocessing of the electroless plating of the fiber depending on the type of the fiber material and is not limited to the preprocessing using fluid. 
     Details of Pre-cleaning Step, Intermediate Cleaning Step, and Post-cleaning Step 
     In detail, each of the pre-cleaning step, the intermediate step, and the post-cleaning step S 4 , S 6 , S 8  can be as follows as illustrated in  FIG.  6   . In the pre-cleaning step S 4 , the cleaning fluid H is discharged to the preprocessing fiber material A 2 . As a result, the fiber material A 2  is cleaned. In the intermediate cleaning step S 6 , the cleaning fluid H is discharged to the catalyst-applied fiber material A 3 . As a result, the fiber material A 3  is cleaned. In the post-cleaning step S 8 , the cleaning fluid H is discharged to the electroless plated fiber material A 4 . As a result, the fiber material A 4  is cleaned. In each of the pre-cleaning step, the intermediate step, and the post-cleaning step S 4 , S 6 , S 8 , a cleaning apparatus  30  that enables the cleaning fluid H to be discharged to the fiber materials A 2 , A 3 , A 4  is used. The cleaning apparatus  30  includes a cleaning nozzle  30   a  having a discharge port  30   b  configured to discharge the cleaning fluid H. 
     However, the fiber material can also be cleaned by being immersed in the cleaning fluid in at least one of the pre-cleaning step, the intermediate cleaning step, and the post-cleaning step. In this case, a cleaning apparatus having a tank that can collect the cleaning fluid can be used in at least one of the pre-cleaning step, the intermediate cleaning step, and the post-cleaning step. 
     The cleaning fluid H can be water. The water can be purified water such as distilled water, ion exchanged water, reverse osmosis (RO) water, pure water, and ultrapure water, tap water, natural water, and the like. The cleaning fluids H of the pre-cleaning step, the intermediate cleaning step, and the post-cleaning step can be the same. However, the cleaning fluid is not limited to water. The cleaning fluids of the pre-cleaning step, the intermediate step, and the post-cleaning step S 4 , S 6 , S 8  can be different from each other. One of the cleaning fluids of the pre-cleaning step, the intermediate cleaning step, and the post-cleaning step can also be different from the remaining two. 
     As illustrated in  FIG.  6   , the supporting apparatus  40  that supports the fiber materials A 2 , A 3 , A 4  in the pre-cleaning step, the intermediate step, and the post-cleaning step S 4 , S 6 , S 8  is described. The supporting apparatus  40  has two supporting portions  41 ,  42  disposed to be spaced apart from each other such that the fiber materials A 2  to A 4  are bridged thereover. One supporting portion  41  out of those two supporting portions  41 ,  42  is referred to as the first supporting portion  41 , and the other supporting portion  42  out of the two supporting portions  41 ,  42  is referred to as the second supporting portion  42  as needed. 
     The supporting apparatus  40  has a coupling portion  43  that couples the first and second supporting portions  41 ,  42  to each other. The fiber materials A 2  to A 4  are bridged over the first and second supporting portions  41 ,  42  in a state of being applied with a predetermined tension. At this time, a tension with which slacks that cause the positions of the fiber materials A 2  to A 4  to vary in the radial direction are not generated, is preferably applied to the fiber materials A 2  to A 4 . The supporting apparatus  40  is configured to fix the fiber materials A 2  to A 4  to the first and second supporting portions  41 ,  42 . However, the supporting apparatus can be configured to move the fiber materials along the longitudinal direction thereof while supporting the fiber materials by the first and second supporting portions. 
     In  FIG.  6   , the first supporting portion  41  is disposed to be spaced apart from the second supporting portion  42  to the upper side. The fiber materials A 2  to A 4  are bridged over the first and second supporting portions  41 ,  42  so as to be substantially along the vertical direction. However, the disposal relationship between the first and second supporting portions is not limited to the above. For example, the first and second supporting portions can be disposed to be spaced apart from each other in the horizontal direction. In this case, the fiber materials can be bridged over the first and second supporting portions so as to be substantially along the horizontal direction. 
     One or both of the two supporting portions  41 ,  42  is or are configured to have conductivity and be electrically grounded. The fiber materials A 2  to A 4  are grounded via one or both of the two supporting portions  41 ,  42  as above. In  FIG.  6   , the second supporting portion  42  has conductivity and is electrically grounded. In this case, it is possible to cause the first supporting portion  41  to have conductivity or not have conductivity. However, it is also possible to cause the first supporting portion to have conductivity and be electrically grounded instead of the second supporting portion. Both of the first and second supporting portions can also be grounded. 
     As described above, when the first supporting portion  41  is disposed to be spaced apart from the second supporting portion  42  to the upper side and the fiber materials A 2  to A 4  are disposed to be substantially along the vertical direction, the discharge port  30   b  of the cleaning nozzle  30   a  of the cleaning apparatus  30  is disposed above the first supporting portion  41 . The cleaning fluid H discharged from the discharge port  30   b  flows to the second supporting portion  42  from the first supporting portion  41  along the fiber materials A 2  to A 4  in accordance with gravity. The fiber materials A 2  to A 4  can be cleaned by the cleaning fluid H as above. 
     Although details are described below, the supporting apparatus  40  further supports the fiber materials A 2 , A 3  in the catalyzing step S 5  and the electroless plating step S 7 . The supporting apparatus  40  can also support the fiber material A 4  in the post-drying step S 9 . 
     Details of Catalyzing Step 
     In detail, the catalyzing step S 5  can be as follows as illustrated in  FIG.  2   . In the catalyzing step S 5 , the catalyst solution B is electrostatically sprayed onto the preprocessing fiber material A 2  in advance, and the first reducing agent solution C is electrostatically sprayed onto the fiber material A 2  following the catalyst solution B. However, in the catalyzing step, the catalyst solution and the first reducing agent solution can also be electrostatically sprayed onto the fiber material in a simultaneous manner. In the catalyzing step, it is also possible to electrostatically spray the first reducing agent solution onto the fiber material in advance and electrostatically spray the catalyst solution onto the fiber material following the first reducing agent solution. 
     In the catalyzing step S 5 , the fiber material A 2  is supported by the supporting apparatus  40 . In the catalyzing step S 5 , a catalyzing apparatus  50  configured to cause a reaction of applying a catalyst for an electroless plating reaction on the surface of the fiber material A 2  is used. 
     The catalyzing apparatus  50  has a catalytic nozzle mechanism  51  for catalyst configured to be able to electrostatically spray the catalyst solution B. The nozzle mechanism  51  for catalyst has a nozzle  51   a  for a catalyst having a spraying port  51   b  that electrostatically sprays the catalyst solution B. As indicated by double-headed arrow P 1 , the nozzle  51   a  for catalyst is configured to be able to move along the longitudinal direction of the fiber material A 2 . The nozzle  51   a  for catalyst can repeatedly move back and forth along the longitudinal direction of the fiber material A 2 . The nozzle mechanism  51  for catalyst has a supply pipe  51   c  for a catalyst configured to enable the catalyst solution B to be supplied to the nozzle  51   a  for the catalyst to pass therethrough. A power source (not shown) can be used to electrically charge the catalyst solution B to a positive potential (or a negative potential). 
     In the nozzle mechanism  51  for a catalyst as above, the catalyst solution B is sprayed from the spraying port  51   b  of the nozzle  51   a  for catalyst through the supply pipe  51   c  for catalyst in a droplet state. At this time, an electric field can be generated between the nozzle  51   a  for a catalyst and the fiber material A 2  by an electrospray phenomenon. When the fiber material is electrically charged to a potential opposite from the potential of the catalyst solution, the fiber material can be electrically charged to the opposite potential by use of the power source. 
     The electrospray phenomenon is described. For example, in the electric field between the nozzle  51   a  for catalyst of the nozzle mechanism  51  for catalyst and the fiber material A 2 , the side of the nozzle  51   a  for the catalyst is set to a positive potential, and the side of the grounded fiber material A 2  is set to about 0 kV or a negative potential by using the power source and the like. The electrospray phenomenon can be caused to occur by providing a potential gradient between the nozzle  51   a  for catalyst and the fiber material A 2  as above. 
     In a configuration in which the fiber material A 2  is fixed to the first and second supporting portions  41 ,  42  of the supporting apparatus  40 , the catalyst solution B can be sprayed onto the entirety of the fiber material A 2  when the catalyst solution B is sprayed from the nozzle  51   a  for the catalyst while the nozzle  51   a  for catalyst is moved along the longitudinal direction of the fiber material A 2 . However, in a configuration in which the supporting apparatus moves the fiber material along the longitudinal direction thereof while supporting the fiber material by the first and second supporting portions as above, the catalyst solution can be sprayed onto the entirety of the fiber material even when the nozzle for catalyst is fixed to a certain position. 
     The catalyzing apparatus  50  has a nozzle mechanism  52  for first reducing agent configured to be able to electrostatically spray the first reducing agent solution C. The nozzle mechanism  52  for first reducing agent includes a nozzle  52   a  for first reducing agent having a spraying port  52   b  that electrostatically sprays the first reducing agent solution C. As indicated by double-headed arrow P 2 , the nozzle  52   a  for first reducing agent is configured to be able to move along the longitudinal direction of the fiber material A 2 . The nozzle  52   a  for first reducing agent can repeatedly move back and forth along the longitudinal direction of the fiber material A 2 . The nozzle mechanism  52  for a first reducing agent has a supply pipe  52   c  for a first reducing agent configured to enable the first reducing agent solution C to be supplied to the nozzle  52   a  for first reducing agent to pass therethrough. A power source (not shown) can be used to electrically charge the first reducing agent solution C to a positive potential (or a negative potential). 
     In the nozzle mechanism  52  for the first reducing agent as above, the first reducing agent solution C is sprayed from the spraying port  52   b  of the nozzle  52   a  for the first reducing agent through the supply pipe  52   c  for the first reducing agent in a droplet state. By the electrospray phenomenon similar to that of the nozzle mechanism  51  for catalyst, an electric field can be generated between the nozzle  52   a  for first reducing agent and the fiber material A 2 . When the fiber material is electrically charged to a potential opposite from the potential of the first reducing agent solution, the fiber material can be electrically charged to be the opposite potential by use of the power source. 
     In a configuration in which the fiber material A 2  is fixed to the first and second supporting portions  41 ,  42  of the supporting apparatus  40 , the first reducing agent solution C can be sprayed onto the entirety of the fiber material A 2  when the first reducing agent solution C is sprayed from the nozzle  52   a  for first reducing agent while the nozzle  52   a  for first reducing agent is moved along the longitudinal direction of the fiber material A 2 . However, in a configuration in which the supporting apparatus moves the fiber material along the longitudinal direction thereof while supporting the fiber material by the first and second supporting portions as above, the first reducing agent solution can be sprayed onto the entirety of the fiber material even when the nozzle for the first reducing agent is fixed to a certain position. 
     Regarding the relationship between the nozzle mechanism  51  for a catalyst and the nozzle mechanism  52  for the first reducing agent, the nozzle  51   a  for the catalyst and the nozzle  52   a  for the first reducing agent are configured to be able to move so as not to hinder the movement of each other along the fiber material A 2 . In  FIG.  2   , the nozzle  51   a  for the catalyst and the nozzle  52   a  for first reducing agent are disposed to be shifted from each other in the circumferential direction of the fiber material A 2 . The nozzle  51   a  for the catalyst and the nozzle  52   a  for the first reducing agent can be disposed so as to face directions opposite from each other while the discharge ports  51   b ,  52   b  thereof face the fiber material A 2 . In this case, the distance between the discharge ports  51   b ,  52   b  in the longitudinal direction of the fiber material A 2  can also be changed in accordance with the separate movements of the nozzle  51   a  for the catalyst and the nozzle  52   a  for the first reducing agent in the longitudinal direction of the fiber material A 2 . 
     However, the nozzle for the catalyst and the nozzle for the first reducing agent can also be disposed to be spaced apart from each other in the longitudinal direction of the fiber material. When one of the nozzle for the catalyst and the nozzle for the first reducing agent is disposed in an electrostatically spraying position at which the nozzle approaches the fiber material in order to perform electrostatically spraying onto the fiber material, the nozzle for the catalyst and the nozzle for the first reducing agent can also be switched with each other so as to cause the other nozzle to retreat from the electrostatically spraying position. 
     As one example, the catalyst solution B can be a solution in which a salt of one or a composite of platinum, gold, silver, palladium, and the like, a complex compound thereof, and the like, or a mixture of two or more of the above are dissolved. The salt can be nitrate, sulfate, chloride, acetate, and the like. Therefore, metal ions of platinum, gold, silver, palladium, and the like serving as the catalyst precursor are contained in the catalyst solution B. 
     In particular, in order to reduce the surface tension of droplets sprayed from the nozzle  51   a  for catalyst, the catalyst solution B can contain C 1 -C 3  lower alcohols such as methanol, ethanol, and isopropyl alcohol; ketones such as acetone and methyl ethyl ketone; or a mixture of two or more of the above. The concentration of the catalyst precursor in the catalyst solution B can be adjusted, as appropriate. For example, the concentration of the catalyst precursor can be in a range of from about 0.01 mol/L or more and about 5 mol/L or less. 
     As the reducing agent contained in the first reducing agent solution C, an optimal reducing agent can be selected so as to be appropriate for the catalyst precursor species to be reduced. As one example, the reducing agent can be hydroxymethanesulfinic acid, thioglycolic acid, or sulfurous acid, salts thereof such as sodium salt, potassium salt, and ammonium salt, ascorbic acid, citric acid, sodium hydrosulfite, thiourea, dithiothreitol, hydrazines, formaldehydes, or boron hydrides, or a mixture of two or more thereof. 
     As one example, the hydrazines can be hydrazine, hydrazine hydrate, hydrazine salt, a substituent derivative of hydrazine or salt thereof, and the like. Specifically, examples include hydrazine hydrate, hydrazine monohydrochloride, hydrazine dihydrochloride, hydrazine sulfate, hydrazine bromate, hydrazine carbonate, methylhydrazine, phenylhydrazine, tert-butylhydrazine hydrochloride, and carbohydrazide. 
     One example of formaldehydes can be formaldehyde, paraformaldehyde, or the like, or a mixture of two or more thereof. Boron hydrides refers to a reducing compound having a boron-hydrogen bond. Specifically, examples include sodium borohydride, potassium borohydride, lithium borohydride, sodium cyanotrihydroborate, lithium triethylborohydride, a tetrahydrofuran-borane complex, a dimethylamine-borane complex, a diphenylamine-borane complex, and a pyridine-borane complex. In particular, the reducing agent is preferably ascorbic acid or a hydrazine. 
     The amount of the reducing agent added into the first reducing agent solution C can be adjusted, as appropriate, in correspondence with the type of the reducing agent, the concentration of the catalyst precursor in the catalyst solution B, and the like. For example, the amount of the reducing agent added is preferably in a range of from one time to two times as much as the chemical equivalent of the catalyst precursor. The reaction of reduction by the catalyst may not sufficiently progress when the amount of the reducing agent added is less than the chemical equivalent. In addition, the amount of the reducing agent added can exceed an amount that is two times as much as the chemical equivalent, but the cost increases. 
     The catalyst solution B and the first reducing agent solution C are preferably water-soluble or aqueous solution systems that are compatible with each other. As one example, the solvent used in each of the catalyst solution B and the first reducing agent solution C can be water, ethanol, DMF (N,N-dimethylformamide), acetone, or a mixture of two or more of the above. In particular, the solvent used in each of the catalyst solution B and the first reducing agent solution C is preferably water, or an aqueous solution of water and a water-soluble solvent such as ethanol, DMF, and acetone. The solvents used in the catalyst solution B and the first reducing agent solution C are preferably the same type. 
     In the nozzle  51   a  for catalyst and the nozzle  52   a  for first reducing agent, the diameter of each of the spraying ports  51   b ,  52   b  can be about 0.03 mm or more, preferably about 0.05 mm or more, and more preferably about 0.1 mm or more, and can be about 1.0 mm or less, preferably about 0.5 mm or less, and more preferably about 0.3 mm or less. The atmospheric temperature of the environment in which the catalyzing step S 5  is performed, in other words, the ambient temperature of the catalyzing apparatus  50  can be room temperature. 
     In the catalyzing step S 5 , each of the distance between the spraying port  51   b  of the nozzle  51   a  for catalyst and the fiber material A 2  and the distance between the spraying port  52   b  of the nozzle  52   a  for first reducing agent and the fiber material A 2  can be about 5 mm or more, preferably about 7 mm or more, and more preferably about 10 mm or more, and can be about 40 mm or less, preferably about 30 mm or less, and more preferably about 20 mm or less. 
     In the catalyzing step S 5 , each of the spraying amount of the catalyst solution B from the nozzle  51   a  for catalyst per unit time and the spraying amount of the first reducing agent solution C from the nozzle  52   a  for first reducing agent per unit time can be about 3 μL/min or more, preferably about 5 μL/min or more, and more preferably about 7 μL/min or more, and can be about 50 μL/min or less, preferably about 30 μL/min or less, and more preferably about 20 μL/min or less. In the catalyzing step S 5 , each of the positive potential on the side of the nozzle  51   a  for catalyst and the positive potential on the side of the nozzle  52   a  for first reducing agent can be about +2.0 kV or more, preferably about +3.0 kV or more, and more preferably about +4.5 kV or more, and can be about +10.0 kV or less, preferably about +8 kV or less, and more preferably about +7 kV or less. 
     In the catalyzing step S 5 , water I is discharged to the fiber material A 2 . As a result, the fiber material A 2  is moistened. The fiber material A 2  can be reliably grounded by moistening the fiber material A 2 . The catalyzing apparatus  50  has a first moisture supplying mechanism  53  configured to supply the water I to the fiber material A 2 . The first moisture supplying mechanism  53  has a first moisture supplying nozzle  53   a  having a discharge port  53   b  configured to discharge the water I. The supplying of the water I to the fiber material A 2  may be continuously performed or be intermittently performed while the catalyzing step S 5  is performed. 
     In the catalyzing step S 5 , the water I for moistening the fiber material A 2  can be purified water such as distilled water, ion exchanged water, reverse osmosis (RO) water, pure water, and ultrapure water. However, the water is not limited to the above. 
     As described above, when the first supporting portion  41  is disposed to be spaced apart from the second supporting portion  42  to the upper side and the fiber material A 2  is disposed to be substantially along the vertical direction, the discharge port  53   b  of the first moisture supplying nozzle  53   a  is disposed above the first supporting portion  41 . The water I discharged from the discharge port  53   b  flows to the second supporting portion  42  from the first supporting portion  41  along the fiber material A 2  in accordance with gravity. By the water I as above, the fiber material A 2  can be moistened. 
     However, the first moisture supplying mechanism can be configured to have a tank configured to be able to collect water when the supporting apparatus is configured to move the fiber material along the longitudinal direction thereof while supporting the fiber material by the first and second supporting portions as described above. In this case, the fiber material can pass through the water in the tank of the first moisture supplying mechanism in one or both of the time immediately before the catalyst solution is sprayed or the time immediately before the first reducing agent solution is sprayed. 
     By the catalyzing step S 5 , a catalyst metal film, for example, a film of metal palladium or platinum, can be formed on the fiber material A 2 . The amount of the catalyst given to the fiber material A 2  can be adjusted, as appropriate, in the electroless plating step S 7  thereafter such that the electroless plated fiber material A 4  having a desired electric resistance value, a desired film thickness of the plated metal film, and the like can be obtained. 
     Details of Electroless Plating Step 
     In detail, the electroless plating step S 7  can be as follows as illustrated in  FIG.  3   . In the electroless plating step S 7 , each of the metal ion solution D and the second reducing agent solution E, each in a state of being electrically charged to a positive potential, is electrostatically sprayed onto the fiber material A 3  in a simultaneous manner such that the metal ion solution D and the second reducing agent solution E react with each other in the same electric field on the catalyst-applied fiber material A 3 . 
     In the electroless plating step S 7 , the fiber material A 3  is supported by the supporting apparatus  40 . In the electroless plating step S 7 , an electroless plating apparatus  60  configured to perform the electroless plating processing on the fiber material A 3  is used. 
     The electroless plating apparatus  60  has a nozzle mechanism  61  for metal ions configured to be able to electrostatically spray the metal ion solution D. The nozzle mechanism  61  for metal ions has a nozzle  61   a  for metal ions having a spraying port  61   b  that electrostatically sprays the metal ion solution D. As indicated by double-headed arrow Q 1 , the nozzle  61   a  for metal ions is configured to be able to move along the longitudinal direction of the fiber material A 3 . The nozzle mechanism  61  for metal ions has a supply pipe  61   c  for metal ions configured to enable the metal ion solution D to be supplied to the nozzle  61   a  for metal ions to pass therethrough. A power source (not shown) can be used to electrically charge the metal ion solution D to a positive potential (or a negative potential). 
     In the nozzle mechanism  61  for metal ions as above, the metal ion solution D is sprayed from the spraying port  61   b  of the nozzle  61   a  for metal ions through the supply pipe  61   c  for metal ions in a droplet state. At this time, by the electrospray phenomenon similar to that of the nozzle mechanism  51  for catalyst described above, an electric field can be generated between the nozzle  61   a  for metal ions and the fiber material A 3 . When the fiber material is electrically charged to a potential opposite from the potential of the metal ion solution, the fiber material can be electrically charged to the opposite potential with use of the power source. 
     In a configuration in which the fiber material A 3  is fixed to the first and second supporting portions  41 ,  42  of the supporting apparatus  40 , the metal ion solution D can be sprayed onto the entirety of the fiber material A 3  when the metal ion solution D is sprayed from the nozzle  61   a  for metal ions while the nozzle  61   a  for metal ions is moved along the longitudinal direction of the fiber material A 3 . However, in a configuration in which the supporting apparatus moves the fiber material along the longitudinal direction thereof while supporting the fiber material by the first and second supporting portions as above, the metal ion solution can be sprayed onto the entirety of the fiber material even when the nozzle for metal ions is fixed at a certain position. 
     The electroless plating apparatus  60  has a nozzle mechanism  62  for a second reducing agent configured to be able to electrostatically spray the second reducing agent solution E. The nozzle mechanism  62  for the second reducing agent is configured in a similar manner as the nozzle mechanism  52  for the first reducing agent besides the feature in which the second reducing agent solution E is electrostatically sprayed instead of the first reducing agent solution C. A nozzle  62   a  for the second reducing agent, a spraying port  62   b , and a supply pipe  62   c  for the second reducing agent of the nozzle mechanism  62  for the second reducing agent are equivalent to the nozzle  52   a  for the first reducing agent, the spraying port  52   b , and the supply pipe  52   c  for the first reducing agent of the nozzle mechanism  52  for the first reducing agent, respectively. 
     As indicated by double-headed arrow Q 2 , the nozzle  62   a  for the second reducing agent can move along the longitudinal direction of the fiber material A 3 . A power source (not shown) can be used to electrically charge the second reducing agent solution E to a positive potential (or a negative potential). When the fiber material is electrically charged to a potential opposite from the potential of the second reducing agent solution, the fiber material can be electrically charged to the opposite potential by use of the power source. 
     In the electroless plating apparatus, it is also possible to use the nozzle mechanism for the first reducing agent instead of the nozzle mechanism for the second reducing agent. In this case, the nozzle mechanism for the first reducing agent is used in common in the catalyzing apparatus and the electroless plating apparatus. 
     Regarding the relationship between the nozzle mechanism  61  for metal ions and the nozzle mechanism  62  for the second reducing agent, the nozzle  61   a  for metal ions and the nozzle  62   a  for the second reducing agent are configured to be able to move so as not to hinder the movement of each other along the fiber material A 3 . In  FIG.  3   , the nozzle  61   a  for metal ions and the nozzle  62   a  for the second reducing agent are disposed to be shifted from each other in the circumferential direction of the fiber material A 3 . The nozzle  61   a  for metal ions and the nozzle  62   a  for the second reducing agent can be disposed to be maintained in a state of facing each other while the discharge ports  61   b ,  62   b  face the fiber material A 3 . 
     The metal ions contained in the metal ion solution D may be ions of desired metal to be plated on the fiber material A 3 . Therefore, as one example, the metal ion solution D can be a solution obtained by dissolving salt of one or a composite of platinum, gold, silver, copper, tin, nickel, iron, palladium, zinc, iron, cobalt, tungsten, ruthenium, indium, molybdenum, and the like, a complex compound thereof, and the like, or a mixture of two or more of the above in an appropriate solvent. The salt can be nitrate, sulfate, chloride, acetate, and the like. 
     In particular, in order to reduce the surface tension of the droplets sprayed from the nozzle  61   a  for metal ions, the metal ion solution D can contain C 1 -C 3  lower alcohols such as methanol, ethanol, and isopropyl alcohol; ketones such as acetone and methyl ethyl ketone; or a mixture of two or more of the above. The concentration of the metal ions in the metal ion solution D can be adjusted, as appropriate. For example, the concentration of the metal ions can be in a range of from 0.01 mol/L or more and about 5 mol/L or less. 
     As the reducing agent contained in the second reducing agent solution E, an optimal reducing agent can be selected so as to comply with the metal ion species to be reduced. Examples of the reducing agent contained in the second reducing agent solution E can include reducing agents similar to the reducing agents contained in the first reducing agent solution C. 
     The amount of the reducing agent added into the second reducing agent solution E can be adjusted, as appropriate, in correspondence with the type of the reducing agent, the concentration of the metal ions in the metal ion solution D, and the like. For example, the amount of the reducing agent added is preferably in a range of from one time to two times as much as the chemical equivalent of the metal ions. The reaction of reduction to the metal ions may not sufficiently progress when the amount of the reducing agent added is less than the chemical equivalent. In addition, the amount of the reducing agent added can exceed an amount that is two times as much as the chemical equivalent, but the cost increases. 
     The metal ion solution D and the second reducing agent solution E are preferably water-soluble or aqueous solution systems that are compatible with each other. As one example, the solvent used in each of the metal ion solution D and the second reducing agent solution E can be water, ethanol, DMF, acetone, or a mixture of two or more of the above. In particular, the solvent used in each of the metal ion solution D and the second reducing agent solution E is preferably water, or an aqueous solution of water and a water-soluble solvent such as ethanol, DMF, and acetone. The solvents used in the metal ion solution D and the second reducing agent solution E are preferably of the same type. 
     In the electroless plating step S 7 , water J is discharged to the fiber material A 3 . As a result, the fiber material A 3  is moistened. The electroless plating apparatus  60  has a second moisture supplying mechanism  63  configured to supply the water J to the fiber material A 3 . The second moisture supplying mechanism  63  has a second moisture supplying nozzle  63   a  having a discharge port  63   b  configured to discharge the water J. The supplying of the water J to the fiber material A 3  may be continuously performed or be intermittently performed while the electroless plating step S 7  is performed. 
     In the nozzle  61   a  for metal ions and the nozzle  62   a  for second reducing agent, the diameter of each of the spraying ports  61   b ,  62   b  can be about 0.03 mm or more, preferably about 0.05 mm or more, and more preferably about 0.1 mm or more, and can be about 1.0 mm or less, preferably about 0.5 mm or less, and more preferably about 0.3 mm or less. The atmospheric temperature of the environment in which the electroless plating step S 7  is performed, in other words, the ambient temperature of the electroless plating apparatus  60 , can be room temperature. 
     In the electroless plating step S 7 , each of the distance between the spraying port  61   b  of the nozzle  61   a  for metal ions and the fiber material A 3  and the distance between the spraying port  62   b  of the nozzle  62   a  for second reducing agent and the fiber material A 3  can be about 5 mm or more, preferably about 7 mm or more, and more preferably about 10 mm or more, and can be about 40 mm or less, preferably about 30 mm or less, and more preferably about 20 mm or less. 
     In the electroless plating step S 7 , each of the spraying amount of the metal ion solution D from the nozzle  61   a  for metal ions per unit time and the spraying amount of the second reducing agent solution E from the nozzle  62   a  for second reducing agent per unit time can be about 3 μL/min or more, preferably about 5 μL/min or more, and more preferably about 7 μL/min or more, and can be about 50 μL/min or less, preferably about 30 μL/min or less, and more preferably about 20 μL/min or less. In the electroless plating step S 7 , each of the positive potential on the side of the nozzle  61   a  for metal ions and the positive potential on the side of the nozzle  62   a  for the second reducing agent can be about +2.0 kV or more, preferably about +3.0 kV or more, and more preferably about +4.5 kV or more, and can be about +10.0 kV or less, preferably about +8 kV or less, and more preferably about +7 kV or less. 
     In the electroless plating step S 7 , the water J for moistening the fiber material A 3  can be purified water such as distilled water, ion exchanged water, RO water, pure water, and ultrapure water. The water J used in the electroless plating step S 7  can be the same type as the water I used in the catalyzing step S 5 . The water J used in the electroless plating step S 7  can also be a type different from that of the water I used in the catalyzing step S 5 . However, the water is not limited to the above. 
     In the electroless plating apparatus, it is also possible to use the first moisture supplying mechanism instead of the second moisture supplying mechanism. In this case, the first moisture supplying mechanism is used in common in the catalyzing apparatus and the electroless plating apparatus. 
     As described above, when the first supporting portion  41  is disposed to be spaced apart from the second supporting portion  42  to the upper side and the fiber material A 3  is disposed to be substantially along the vertical direction, the discharge port  63   b  of the second moisture supplying nozzle  63   a  is disposed above the first supporting portion  41 . The water J discharged from the discharge port  63   b  flows to the second supporting portion  42  from the first supporting portion  41  along the fiber material A 3  in accordance with gravity. By the water J as above, the fiber material A 3  can be moistened. 
     However, the second moisture supplying mechanism can be configured to have a tank configured to be able to collect water when the supporting apparatus is configured to move the fiber material along the longitudinal direction thereof while supporting the fiber material by the first and second supporting portions as described above. In this case, the fiber material can pass through the water in the tank of the second moisture supplying mechanism immediately before the metal ion solution and the second reducing agent solution are sprayed. 
     By the electroless plating step S 7 , a desired plated metal film can be formed on the catalyst metal film given to the fiber material A 3 . In the electroless plated fiber material A 4  on which the plated metal film is formed by the electroless plating step S 7 , the film thickness of the plated metal film can be reduced while the electric resistance value thereof is reduced as compared to the related art. Examples of the related art include a commercially available silver-plated conductive thread in which the electric resistance value is about 2.0 Ω/cm and the film thickness of the plated metal film is about 2.1 μm. For example, in the plated metal film of the electroless plated fiber material A 4 , the electric resistance value can be set to about 2.0 Ω/cm or less, and the film thickness of the plated metal film can be set in a range equal to or less than about 0.4 μm. 
     Manufacturing System for Electroless Plated Fiber Material 
     With reference to  FIG.  2    to  FIG.  6   , the manufacturing system of the electroless plated fiber material A 4  capable of performing the manufacturing method for the electroless plated fiber material A 4  according to the present embodiment is configured as follows. In other words, the manufacturing system roughly has the catalyzing apparatus  50  and the electroless plating apparatus  60 . The catalyzing apparatus  50  is configured to be able to perform the catalyzing step S 5 . The electroless plating apparatus  60  is configured to be able to perform the electroless plating step S 7 . 
     In detail, the manufacturing system can have the degreasing apparatus  10 , the preprocessing apparatus  20 , the cleaning apparatus  30 , the supporting apparatus  40 , the catalyzing apparatus  50 , the electroless plating apparatus  60 , and the drying apparatus (not shown). The degreasing apparatus  10  is configured to be able to perform the degreasing step S 1 . The preprocessing apparatus  20  is configured to be able to perform the preprocessing step S 3 . The cleaning apparatus  30  is configured to be able to perform the pre-cleaning step, the intermediate cleaning step, and the post-cleaning step S 4 , S 6 , S 8 . The supporting apparatus  40  is configured to be able to support the fiber materials A 2  to A 4 . The drying apparatus is configured to be able to perform the pre-drying step and post-drying step S 2 , S 9 . 
     When the manufacturing method for the electroless plated fiber material includes the annealing processing step, the manufacturing system of the electroless plated fiber material can include the annealing processing apparatus configured to be able to perform the annealing processing step. For example, the annealing processing apparatus can have a heating mechanism configured to be able to heat the fiber material. The heating mechanism can be a hot-air circulation oven. In this case, the annealing processing apparatus can also serve as the drying apparatus. The apparatus can also be referred to as a drying/annealing processing apparatus. 
     As above, the manufacturing method for the electroless plated fiber material A 4  according to the present embodiment includes the electroless plating step S 7  of electrostatically spraying the catalyst solution B containing a catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material A 2  which is grounded or electrically charged to a potential opposite from the potential of the catalyst solution B and which is moistened, and electrostatically spraying the first reducing agent solution C containing a reducing agent of the catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material A 2  which is grounded or electrically charged to a potential opposite from the potential of the first reducing agent solution C and which is moistened, to thereby electrostatically spray each of the metal ion solution D containing metal ions and the second reducing agent solution E containing a reducing agent of the metal ions each in a state of being electrically charged to a positive potential or a negative potential in a similar manner onto the catalyst-applied fiber material A 3  which is grounded or electrically charged to a potential opposite from the potential of the metal ion solution D and the second reducing agent solution E and which is moistened, such that the metal ion solution D and the second reducing agent solution E react with each other in a same electric field on the catalyst-applied fiber material A 3 , to thereby obtain the electroless plated fiber material A 4  in which a plated film is formed on the catalyst-applied fiber material A 3 . 
     An electroless plated fiber material A 4  according to the present embodiment is manufactured by a manufacturing method including the electroless plating step S 7  of electrostatically spraying the catalyst solution B containing a catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material A 2  which is grounded or electrically charged to a potential opposite from the potential of the catalyst solution B and which is moistened, and electrostatically spraying the first reducing agent solution C containing a reducing agent of the catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material A 2  which is grounded or electrically charged to a potential opposite from the potential of the first reducing agent solution C and which is moistened, to thereby electrostatically spray each of the metal ion solution D containing metal ions and the second reducing agent solution E containing a reducing agent of the metal ions each in a state of being electrically charged to a positive potential or a negative potential in a similar manner onto the catalyst-applied fiber material A 3  which is grounded or electrically charged to a potential opposite from the potential of the metal ion solution D and the second reducing agent solution E and which is moistened, such that the metal ion solution D and the second reducing agent solution E react with each other in a same electric field on the catalyst-applied fiber material A 3 , to thereby obtain the electroless plated fiber material A 4  in which a plated film is formed on the catalyst-applied fiber material A 3 . 
     A manufacturing system of an electroless plated fiber material A 4  according to the present embodiment includes: a catalyzing apparatus  50  configured to obtain the catalyst-applied fiber material A 3  in which a catalyst is given to the fiber material A 2 ; and the electroless plating apparatus  60  configured to obtain an electroless plated fiber material A 4  in which a plated film is formed on the catalyst-applied fiber material A 3 . In the manufacturing system, the catalyzing apparatus  50  has: the nozzle  51   a  for a catalyst configured to electrostatically spray the catalyst solution B containing a catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material A 2  which is grounded or electrically charged to a potential opposite from the potential of the catalyst solution B and which is moistened; and the nozzle  52   a  for first reducing agent configured to electrostatically spray the first reducing agent solution C containing a reducing agent of the catalyst precursor in a state of being electrically charged to a positive potential or a negative potential onto the fiber material A 2  which is grounded or electrically charged to a potential opposite from the potential of the first reducing agent solution C and which is moistened, the electroless plating apparatus  60  has: the nozzle  61   a  for metal ions configured to electrostatically spray the metal ion solution D containing metal ions in a state of being electrically charged to a positive potential or a negative potential onto the catalyst-applied fiber material A 3 ; and the nozzle  62   a  for second reducing agent configured to electrostatically spray the second reducing agent solution E containing a reducing agent of the metal ions in a state of being electrically charged to a same potential as the potential of the metal ion solution D onto the catalyst-applied fiber material A 3 , and the electroless plating apparatus  60  is configured to cause the metal ion solution D electrostatically sprayed from the nozzle  61   a  for metal ions and the second reducing agent solution E electrostatically sprayed from the nozzle  62   a  for second reducing agent to react with each other in a same electric field on the catalyst-applied fiber material A 3  which is grounded or electrically charged to a potential opposite from the potential of the metal ion solution D and the second reducing agent solution E and which is moistened. 
     In each of the electroless plating step S 7  and the electroless plating apparatus  60 , the metal ion solution D and the second reducing agent solution E are electrically charged to the same potential when the metal ion solution D and the second reducing agent solution E are electrostatically sprayed. Therefore, the metal ion solution D and the second reducing agent solution E do not collide with each other before reaching the fiber material A 3 . Then, the metal ion solution D and the second reducing agent solution E lose charges thereof when the metal ion solution D and the second reducing agent solution E reach the grounded fiber material A 3 . At this time, the metal ion solution D and the second reducing agent solution E come into contact, are mixed, and react with each other for the first time. Therefore, the metal ions of the metal ion solution D are efficiently reduced by the reducing agent of the second reducing agent solution E on the fiber material A 3 . As a result, a plated film obtained by depositing metal can be efficiently formed on the fiber material A 3 . In particular, the electroless plated fiber material A 4  having such plated film can increase the conductivity thereof and reduce the thickness of the plated film. Therefore, the quality of the electroless plated fiber material A 4  can be increased. 
     In the electroless plated fiber material A 4  and the manufacturing method and the manufacturing system thereof as above, in each of the catalyzing step S 5  and the catalyzing apparatus  50 , the usage amount of the processing solution to be electrostatically sprayed can be reduced as compared to the usage amount of the processing solution used in immersing as in the related art. In each of the electroless plating step S 7  and the electroless plating apparatus  60 , the usage amount of the processing solution to be electrostatically sprayed can be reduced as compared to the usage amount of the processing solution used in immersing as in the related art. By the reduction of the usage amount of the processing solution as above, the manufacturing cost can be reduced, the environmental load can be reduced, and the manufacturing efficiency of the electroless plated fiber material A 4  can be improved. In plating processing using a plating bath of the related art, the substance concentration in the plating bath changes over time. Therefore, the concentration management of the plating bath has been difficult. In the present invention, the processing solution is electrostatically sprayed, and hence problems relating to the concentration management of the plating bath can also be solved. 
     Second Embodiment 
     The electroless plated fiber material and the manufacturing method and the manufacturing system thereof according to the second embodiment are described. The fiber material A 1  used in the present embodiment is similar to the fiber material A 1  used in the first embodiment. 
     Overview of Electroless Plated Fiber Material and Manufacturing Method Therefor 
     An outline of the electroless plated fiber material A 4  and the manufacturing method thereof according to the present embodiment is described with reference to  FIG.  1    and  FIG.  7   . The manufacturing method for the electroless plated fiber material A 4  according to the present embodiment generally includes the catalyzing step S 5  and the electroless plating processing step S 7  similar to those in the first embodiment. 
     In the manufacturing method for the electroless plated fiber material A 4  according to the present embodiment, the fiber material A 2 , the catalyst-applied fiber material A 3 , and the electroless plated fiber material A 4  are integrated with each other so as to extend from the position in which the catalyzing step S 5  is performed toward the position in which the electroless plating processing step S 7  is performed. The fiber materials A 2  to A 4  integrated with each other as above are carried from the position in which the catalyzing step S 5  is performed toward the position in which the electroless plating processing step S 7  is performed. The electroless plated fiber material A 4  according to the present embodiment can be generally manufactured by such manufacturing method. 
     Details of Electroless Plated Fiber Material and Manufacturing Method Therefor 
     Details of the electroless plated fiber material A 4  and the manufacturing method therefor according to the present embodiment are described with reference to  FIG.  1    and  FIG.  7   . In detail, the manufacturing method for the electroless plated fiber material A 4  according to the present embodiment includes the degreasing step S 1 , the pre-drying step S 2 , the pre processing step S 3 , the pre-cleaning step S 4 , the catalyzing step S 5 , the intermediate cleaning step S 6 , the electroless plating step S 7 , the post-cleaning step S 8 , and the post-drying step S 9  similar to those in the first embodiment. It is also possible to omit the pre-drying step S 2  when the degreasing fluid F is volatile. 
     In the manufacturing method for the electroless plated fiber material A 4  according to the present embodiment, the fiber material A 1 , the preprocessing fiber material A 2 , the catalyst-applied fiber material A 3 , and the electroless plated fiber material A 4  are integrated with each other so as to extend from the position in which the degreasing step S 1  is performed toward the position in which the post-drying step S 9  is performed. The fiber materials A 1  to A 4  integrated with each other as above are carried from the position in which the degreasing step S 1  is performed toward the position in which the post-drying step S 9  is performed. The electroless plated fiber material A 4  according to the present embodiment can be manufactured by such manufacturing method in detail. 
     Manufacturing System for Electroless Plated Fiber Material 
     The manufacturing system of the electroless plated fiber material A 4  according to the present embodiment is described with reference to  FIG.  7   . Such manufacturing system generally includes a catalyzing apparatus  150 , an electroless plating apparatus  170 , and a carrying apparatus  200 . The catalyzing apparatus  150  is configured to be able to perform the catalyzing step S 5 . The electroless plating apparatus  170  is configured to be able to perform the electroless plating step S 7 . The carrying apparatus  200  is configured to be able to carry the fiber materials A 1  to A 4 . 
     In detail, the manufacturing system can have a degreasing apparatus  110 , a pre-drying apparatus  120 , a pre-processing apparatus  130 , a pre-cleaning apparatus  140 , the catalyzing apparatus  150 , an intermediate cleaning apparatus  160 , the electroless plating apparatus  170 , a post-cleaning apparatus  180 , a post-drying apparatus  190 , and the carrying apparatus  200 . The degreasing apparatus  110  is configured to be able to perform the degreasing step S 1 . The pre-drying apparatus  120  is configured to be able to perform the pre-drying step S 2 . The pre-processing apparatus  130  is configured to be able to perform the pre-processing step S 3 . The pre-cleaning apparatus  140  is configured to be able to perform the pre-cleaning step S 4 . The intermediate cleaning apparatus  160  is configured to be able to perform the intermediate cleaning step S 6 . The post-cleaning apparatus  180  is configured to be able to perform the post-cleaning step S 8 . The post-drying apparatus  190  is configured to be able to perform the post-drying step S 9 . The carrying apparatus  200  carries the fiber materials A 1  to A 4  such that the fiber materials A 1  to A 4  pass through the degreasing apparatus  110 , the pre-drying apparatus  120 , the preprocessing apparatus  130 , the pre-cleaning apparatus  140 , the catalyzing apparatus  150 , the intermediate cleaning apparatus  160 , the electroless plating apparatus  170 , the post-cleaning apparatus  180 , and the post-drying apparatus  190 , in the stated order. 
     Details of Degreasing Apparatus 
     The degreasing apparatus  110  can be configured as follows with reference to  FIG.  7   . In the manufacturing system, the degreasing apparatus  110  has a tank  111  configured to be able to collect the degreasing fluid F. The degreasing apparatus  110  has a roller  112  for degreasing disposed in the degreasing fluid F collected in the tank  111 . The fiber material A 1  passes through the inside of the tank  111  while being guided by the roller  112  for degreasing so as to be immersed in the degreasing fluid F. 
     Details of Pre-drying Apparatus 
     The pre-drying apparatus  120  can be configured as follows with reference to  FIG.  7   . The pre-drying apparatus  120  is configured to be able to apply warm air or hot air to the fiber material A 1  that has passed through the degreasing apparatus  110 . The fiber material A 1  is dried when the fiber material A 1  passes through the pre-drying apparatus  120 . It is also possible to omit the pre-drying apparatus  120  when the degreasing fluid F is volatile. 
     Details of Preprocessing Apparatus 
     The pre-processing apparatus  130  can be configured as follows with reference to  FIG.  7   . The pre-processing apparatus  130  has a tank  131  configured to be able to collect the processing fluid G. The pre-processing apparatus  130  has a plurality of rollers  132  for preprocessing disposed in the processing fluid G collected in the tank  131 . The fiber material A 1  that has passed through the pre-drying apparatus  120  passes through the inside of the tank  131  while being guided by the plurality of rollers  132  for preprocessing so as to make a round trip in the processing fluid G in order to be immersed in the processing fluid G. In the preprocessing apparatus  130 , the preprocessing fiber material A 2  in a state obtained by applying pre-processing to the fiber material A 1  is obtained. 
     Details of Pre-Cleaning Apparatus 
     The pre-cleaning apparatus  140  can be configured as follows with reference to  FIG.  7   . The pre-cleaning apparatus  140  has a tank  141  configured to be able to collect cleaning fluid H. The pre-cleaning apparatus  140  has a roller  142  for precleaning disposed in the cleaning fluid H collected in the tank  141 . The preprocessing fiber material A 2  that has passed through the pre-processing apparatus  130  passes through the inside of the tank  141  while being guided by the roller  142  for pre-cleaning so as to be cleaned by the cleaning fluid H. In the pre-cleaning apparatus  140 , the fiber material A 2  is grounded by the cleaning fluid H in the tank  141 . As a result, the fiber material A 2  positioned in the subsequent catalyzing apparatus  150  is also placed in the grounded state. 
     In the pre-cleaning apparatus  140 , the fiber material A 2  is moistened by the cleaning fluid H in the tank  141 . As a result, the fiber material A 2  positioned in the subsequent catalyzing apparatus  150  is also placed in a state in which it can be moistened. The cleaning fluid H as above can be the same as the water I used in the subsequent catalyzing apparatus  150 . 
     Details of Catalyzing Apparatus 
     The catalyzing apparatus  150  can be configured as follows, with reference to  FIG.  7   . The catalyzing apparatus  150  has nozzles  151   a  for a catalyst each configured as with the nozzle  51   a  for the catalyst of the first embodiment. Each of the nozzles  151   a  for the catalyst has a spraying port  151   b  similar to the spraying port  51   b  of the nozzle  51   a  for catalyst of the first embodiment. 
     The catalyzing apparatus  150  has a nozzle mechanism  151  for the catalyst having the plurality of nozzles  151   a  for the catalyst. The nozzle mechanism  151  for the catalyst has a plurality of supply pipes  151   c  for the catalyst configured to feed the catalyst solution B to the plurality of nozzles  151   a  for the catalyst, respectively. However, the nozzle mechanism for the catalyst can also be configured to have one nozzle for the catalyst, and one supply pipe for the catalyst that feeds the catalyst solution to the nozzle for the catalyst. 
     The catalyzing apparatus  150  has nozzles  152   a  for first reducing agent configured as with the nozzle  52   a  for first reducing agent of the first embodiment. Each of the nozzles  152   a  for the first reducing agent has a spraying port  152   b  similar to the spraying port  52   b  of the nozzle  52   a  for the first reducing agent of the first embodiment. 
     The catalyzing apparatus  150  includes a nozzle mechanism  152  for the first reducing agent having the plurality of nozzles  152   a  for the first reducing agent. The nozzle mechanism  152  for the first reducing agent has a plurality of supply pipes  152   c  for the first reducing agent configured to feed the first reducing agent solution C to the plurality of nozzles  152   a  for the first reducing agent, respectively. However, the nozzle mechanism for the first reducing agent can also be configured to have one nozzle for the first reducing agent, and one supply pipe for the first reducing agent that feeds the first reducing agent solution to the nozzle for the first reducing agent. 
     The plurality of nozzles  151   a  for catalyst and the plurality of nozzles  152   a  for the first reducing agent are arranged side by side in the direction in which the fiber material A 2  that passes through the catalyzing apparatus  150  is carried. The nozzle mechanism  151  for catalyst and the nozzle mechanism  152  for the first reducing agent are arranged side by side in the direction in which the fiber material A 2  that passes through the catalyzing apparatus  150  is carried. The nozzle mechanism  151  for the catalyst is preferably positioned upstream of the nozzle mechanism  152  for the first reducing agent in the direction in which the fiber material A 1  is carried. The nozzle mechanism  151  for the catalyst and the nozzle mechanism  152  for the first reducing agent can also be fixed. 
     However, the positions of the nozzle mechanism for the catalyst and the nozzle mechanism for the first reducing agent are not limited to the above. The nozzle mechanism for the catalyst can also be positioned downstream of the nozzle mechanism for the first reducing agent in the direction in which the fiber material is carried. One or both of the nozzle mechanism for the catalyst and the nozzle mechanism for the first reducing agent can also be movable. 
     Regarding the preprocessing fiber material A 2  that has passed through the pre-cleaning apparatus  140 , the catalyst solution B is electrostatically sprayed thereto by the nozzle mechanism  151  for the catalyst, and the first reducing agent solution C is electrostatically sprayed thereto by the nozzle mechanism  152  for the first reducing agent. At this time, the fiber material A 2  that passes through the catalyzing apparatus  150  is grounded by the pre-cleaning apparatus  140  described above and the intermediate cleaning apparatus  160  described below. The fiber material A 2  is moistened by the pre-cleaning apparatus  140  described above. In the catalyzing apparatus  150 , the catalyst-applied fiber material A 3  in a state obtained by giving the catalyst to the fiber material A 2  is obtained. 
     Details of Intermediate Cleaning Apparatus 
     The intermediate cleaning apparatus  160  can be configured as follows with reference to  FIG.  7   . The intermediate cleaning apparatus  160  has a tank  161  configured to be able to collect the cleaning fluid H. The intermediate cleaning apparatus  160  has a roller  162  for intermediate cleaning disposed in the cleaning fluid H collected in the tank  161 . The catalyst-applied fiber material A 3  that has passed through the catalyzing apparatus  150  passes through the inside of the tank  161  while being guided by the roller  162  for intermediate cleaning so as to be cleaned by the cleaning fluid H. In the intermediate cleaning apparatus  160 , the fiber material A 3  is grounded by the cleaning fluid H in the tank  161 . As a result, the fiber material A 2  positioned in the preceding catalyzing apparatus  150  and the fiber material A 3  positioned in the subsequent electroless plating apparatus  170  are also placed in the grounded state. 
     In the intermediate cleaning apparatus  160 , the fiber material A 3  is moistened by the cleaning fluid H in the tank  161 . As a result, the fiber material A 3  positioned in the subsequent electroless plating apparatus  170  is also placed in a state in which it is moistened. The cleaning fluid H as above can be the same as the water J used in the subsequent electroless plating apparatus  170 . 
     Details of Electroless Plating Apparatus 
     The electroless plating apparatus  170  can be configured as follows, with reference to  FIG.  7   . The electroless plating apparatus  170  has nozzles  171   a  for metal ions configured as with the nozzle  61   a  for metal ions of the first embodiment. Each of the nozzles  171   a  for metal ions has a spraying port  171   b  similar to the spraying port  61   b  of the nozzle  61   a  for metal ions of the first embodiment. 
     The electroless plating apparatus  170  includes a nozzle mechanism  171  for metal ions having the plurality of nozzles  171   a  for metal ions. The nozzle mechanism  171  for metal ions has a plurality of supply pipes  171   c  for metal ions configured to feed the metal ion solution D to the plurality of nozzles  171   a  for metal ions, respectively. However, the nozzle mechanism for metal ions can also be configured to have one nozzle for metal ions, and one supply pipe for metal ions that feeds the metal ion solution to the nozzle for metal ions. 
     The electroless plating apparatus  170  has nozzles  172   a  for second reducing agent configured as with the nozzle  62   a  for second reducing agent of the first embodiment. Each of the nozzles  172   a  for second reducing agent has a spraying port  172   b  similar to the spraying port  62   b  of the nozzle  62   a  for the second reducing agent of the first embodiment. 
     The electroless plating apparatus  170  has a nozzle mechanism  172  for the second reducing agent having the plurality of nozzles  172   a  for the second reducing agent. The nozzle mechanism  172  for the second reducing agent has a plurality of supply pipes  172   c  for the second reducing agent configured to feed the second reducing agent solution E to the plurality of nozzles  172   a  for the second reducing agent, respectively. However, the nozzle mechanism for the second reducing agent can also be configured to have one nozzle for the second reducing agent, and one supply pipe for the second reducing agent that feeds the second reducing agent solution to the nozzle for the second reducing agent. 
     Regarding the relationship between the nozzle mechanism  171  for metal ions and the nozzle mechanism  172  for the second reducing agent, the nozzles  171   a  for metal ions and the nozzles  172   a  for the second reducing agent are fixed. In  FIG.  7   , the nozzles  171   a  for metal ions and the nozzles  172   a  for the second reducing agent are disposed to be shifted from each other in the circumferential direction of the fiber material A 3 . The nozzles  171   a  for metal ions and the nozzles  172   a  for the second reducing agent can be disposed to be maintained in a state of facing each other while the discharge ports  171   b ,  172   b  face the fiber material A 3 . 
     Regarding the catalyst-applied fiber material A 3  that has passed through the intermediate cleaning apparatus  160 , the metal ion solution C is electrostatically sprayed thereto by the nozzle mechanism  171  for metal ions, and the second reducing agent solution E is electrostatically sprayed thereto by the nozzle mechanism  172  for the second reducing agent. At this time, the fiber material A 3  that passes through the electroless plating apparatus  170  is grounded by the intermediate cleaning apparatus  160  described above and the post-cleaning apparatus  180  described below. The fiber material A 2  is moistened by the intermediate cleaning apparatus  160  described above. In the electroless plating apparatus  170 , the electroless plated fiber material A 4  in a state in which a plated film is formed on the fiber material A 3  is obtained. 
     Details of Post-Cleaning Apparatus 
     The post-cleaning apparatus  180  can be configured as follows, with reference to  FIG.  7   . The post-cleaning apparatus  180  has a tank  181  configured to be able to collect the cleaning fluid H. The post-cleaning apparatus  180  has a roller  182  for post-cleaning disposed in the cleaning fluid H collected in the tank  181 . The electroless plated fiber material A 4  that has passed through the electroless plating apparatus  170  passes through the inside of the tank  181  while being guided by the roller  182  for post-cleaning so as to be cleaned by the cleaning fluid H. In the post-cleaning apparatus  180 , the fiber material A 4  is grounded by the cleaning fluid H in the tank  181 . As a result, the fiber material A 3  positioned in the preceding electroless plating apparatus  170  is placed in a grounded state. 
     Details of Post-Drying Apparatus 
     The post-drying apparatus  190  can be configured as follows, with reference to  FIG.  7   . The post-drying apparatus  190  is configured to be able to apply warm air or hot air to the fiber material A 4  that has passed through the post-cleaning apparatus  180 . The fiber material A 4  is dried when the fiber material A 1  passes through the post-drying apparatus  190 . 
     The post-drying apparatus  190  can be configured to be able to also perform an annealing processing step. For example, the post-drying apparatus  190  can have a heating mechanism configured to be able to heat the fiber material A 4 . The heating mechanism can be a hot-air circulation oven. In this case, the apparatus can also be referred to as a drying and annealing processing apparatus. However, an annealing processing apparatus can also be provided separately from the post-drying apparatus. 
     Details of Carrying Apparatus 
     The carrying apparatus  200  can be configured as follows, with reference to  FIG.  7   . The carrying apparatus  200  has an unwinding roller  201  configured to unwind the fiber material A 1 . The carrying apparatus  200  has a winding roller  202  configured to wind the electroless plated fiber material A 4 . The fiber material A 1 , the preprocessing fiber material A 2 , the catalyst-applied fiber material A 3 , and the electroless plated fiber material A 4  extend between the unwinding roller  201  and the winding roller  202  in an integrated manner. 
     The fiber material A 1  unwound from the unwinding roller  201  passes through the place from the degreasing apparatus  110  to the preprocessing apparatus  130  and then changes into the preprocessing fiber material A 2 . The preprocessing fiber material A 2  that has passed through the preprocessing apparatus  130  passes through the place from the pre-cleaning apparatus  140  to the catalyzing apparatus  150 , and then changes to the catalyst-applied fiber material A 3 . The catalyst-applied fiber material A 3  that has passed through the catalyzing apparatus  150  passes through the place from the intermediate cleaning apparatus  160  to the electroless plating apparatus  170  and then changes to the electroless plated fiber material A 4 . The electroless plated fiber material A 4  that has passed through the electroless plating apparatus  170  passes through the place from the post-cleaning apparatus  180  to the post-drying apparatus  190  and is then wound by the winding roller  202 . 
     As above, the manufacturing method and the manufacturing system of the electroless plated fiber material A 4  according to the present embodiment can yield effects similar to those of the manufacturing method and the manufacturing system of the electroless plated fiber material A 4  according to the first embodiment. In the manufacturing method and the manufacturing system according to the present embodiment, effects as follows can be obtained, in addition to the effects as above. 
     In the manufacturing method for the electroless plated fiber material A 4  according to the present embodiment, the fiber material A 2 , the catalyst-applied fiber material A 3 , and the electroless plated fiber material A 4  are carried from a position in which the catalyzing step S 5  is performed toward a position in which the electroless plating step S 7  is performed in a state of being integrated with each other so as to extend from the position in which the catalyzing step S 5  is performed toward the position in which the electroless plating step S 7  is performed. 
     The manufacturing system of the electroless plated fiber material A 4  according to the present embodiment further includes the carrying apparatus  200  configured to be able to carry the fiber material A 2 , the catalyst-applied fiber material A 3 , and the electroless plated fiber material A 4  from the catalyzing apparatus  150  toward the electroless plating apparatus  170  in a state of being integrated with each other so as to extend from the catalyzing apparatus  150  toward the electroless plating apparatus  170 . 
     In such a manufacturing method and manufacturing system, the fiber materials A 2  to A 4  can be efficiently carried. Therefore, the manufacturing efficiency can be improved. 
     The fiber material A 1 , the preprocessing fiber material A 2 , the catalyst-applied fiber material A 3 , and the electroless plated fiber material A 4  are integrated with each other so as to extend from the position in which the degreasing step S 1  is performed toward the position in which the post-drying step S 9  is performed. When the fiber materials A 1  to A 4  integrated with each other as above are carried from the position in which the degreasing step S 1  is performed toward the position in which the post-drying step S 9  is performed, the fiber materials A 1  to A 4  can be efficiently carried. Therefore, the manufacturing efficiency can be improved. 
     The embodiments of the present invention have been described above, but the present invention is not limited to the abovementioned embodiments, and the present invention can be modified and changed on the basis of the technical idea thereof. 
     EXAMPLE 
     An example and a comparative example are described. In the example, as illustrated in  FIG.  2    to  FIG.  6   , the electroless plated fiber material A 4  was produced from the fiber material A 1  configured by nylon 6,6. An electroless plated fiber material was also produced from a fiber material configured by nylon 6,6 in the comparative example. Each of the thickness of the fiber material A 1  of Example 1 and the thickness of the fiber material of the comparative example was 70 denier. 
     Example 
     First, the Example is described. In Example 1, the electroless plated fiber material A 4  was manufactured with use of the manufacturing method according to the first embodiment. Specifically, in the degreasing step S 1 , the fiber material A 1  was immersed in the degreasing fluid F. As a result, the fiber material A 1  was degreased. An acetone solution F was used as the degreasing fluid F. The atmospheric temperature of the degreasing step S 1  was room temperature. The amount of immersing time by which the fiber material A 1  was immersed in the acetone solution F was one minute. In the pre-drying step S 2 , hot air was applied to the fiber material A 1  degreased in the degreasing step S 1 . As a result, the fiber material A 1  was dried. 
     As illustrated in  FIG.  5   , in the preprocessing step S 3 , the fiber material A 1  dried in the pre-drying step S 2  was immersed in the processing fluid G, to thereby perform the pre processing so as to provide a negative charge to the fiber material A 1  in order to increase the adhesion between the fiber material A 2  after the processing and the plated film. The tannic acid solution G containing the tannic acid was used as the processing fluid G, and the tannic acid processing step S 3  was performed as the preprocessing step S 3 . The concentration of the tannic acid in the tannic acid solution G was 5 mass %. The temperature of the tannic acid solution G was 50° C. The amount of immersing time by which the fiber material A 1  was immersed in the tannic acid solution G was five minutes. 
     As illustrated in  FIG.  6   , after the pre-processing step S 3 , the pre-processed fiber material A 2  was cleaned with the cleaning fluid H in the pre-cleaning step S 4 . Purified water was used as the cleaning fluid H. 
     As illustrated in  FIG.  2   , in the catalyzing step S 5 , while the fiber material A 2  cleaned in the pre-cleaning step S 4  was being grounded and the fiber material A 2  is moistened, the catalyst solution B in a state of being electrically charged to a positive potential was electrostatically sprayed onto the fiber material A 2 . Regarding the electrostatically spraying of the catalyst solution B, the catalyst solution B was prepared by dissolving palladium acetate in a solvent of acetonitrile. The concentration of the palladium acetate in the catalyst solution B was 0.1 mol/L. 
     The spraying amount of the catalyst solution B from the nozzle  51   a  for catalyst per unit time was 0.03 mL/min, and the catalyst solution B was sprayed onto the fiber material A 2  of 30 cm for 5 minutes at that spraying amount. The potential on the side of the nozzle  51   a  for catalyst was +5 kV. The distance between the spraying port  51   b  of the nozzle  51   a  for catalyst and the fiber material A 2  was 1 cm. Purified water was supplied to the fiber material A 2  in order to moisten the fiber material A 2 . 
     After the catalyst solution B was electrostatically sprayed, the first reducing agent solution C in a state of being electrically charged to a positive potential was electrostatically sprayed onto the fiber material A 2  while the fiber material A 2  was being grounded and the fiber material A 2  is moistened. Regarding the electrostatically spraying of the first reducing agent solution C, hydrazine was used as the catalyst contained in the first reducing agent solution C. The concentration of hydrazine in the first reducing agent solution C was 1.0 mol/L. As the solvent of the first reducing agent solution C, a solution of 50% ethanol and 50% water was used. 
     The spraying amount of the first reducing agent solution C from the nozzle  52   a  for first reducing agent per unit time was 0.03 mL/min, and the first reducing agent solution C was sprayed onto the fiber material A 2  of 30 cm for 5 minutes at that spraying amount. The potential on the side of the nozzle  52   a  for the first reducing agent was +5 kV. The distance between the spraying port  52   b  of the nozzle  52   a  for the first reducing agent and the fiber material A 2  was 1 cm. Purified water was supplied to the fiber material A 2  in order to moisten the fiber material A 2 . 
     As illustrated in  FIG.  6   , after the catalyzing step S 5 , the catalyst-applied fiber material A 3  was cleaned with the cleaning fluid H in the intermediate cleaning step S 6 . Purified water was used as the cleaning fluid H. 
     As illustrated in  FIG.  3   , in the electroless plating step S 7 , while the catalyst-applied fiber material A 3  cleaned in the intermediate cleaning step S 6  was being grounded and the fiber material A 3  is moistened, each of the metal ion solution D and the second reducing agent solution E, each in a state of being electrically charged to a positive potential, was electrostatically sprayed onto the fiber material A 3  such that the metal ion solution D and the second reducing agent solution E reacted with each other in the same electric field on the fiber material A 3 . The metal ion solution D was prepared by dissolving silver nitrate in a mixed solvent formed by ethanol and water. The concentration of the silver nitrate in the metal ion solution D was 0.3 mol/L. 
     The spraying amount of the metal ion solution D from the nozzle  61   a  for metal ions per unit time was 0.03 mL/min, and the metal ion solution D was sprayed onto the fiber material A 3  of 30 cm for 15 minutes at that spraying amount. The potential on the side of the nozzle  61   a  for metal ions was +5 kV. The distance between the spraying port  61   b  of the nozzle  61   a  for metal ions and the fiber material A 3  was 1 cm. 
     Hydrazine was used as the reducing agent contained in the second reducing agent solution E. The concentration of hydrazine in the second reducing agent solution E was 0.5 mol/L. As the solvent of the second reducing agent solution E, a mixed solution formed by ethanol and water was used. 
     The spraying amount of the second reducing agent solution E from the nozzle  62   a  for second reducing agent per unit time was 0.03 mL/min, and the second reducing agent solution E was sprayed onto the fiber material A 3  of 30 cm for 15 minutes at that spraying amount. The potential on the side of the nozzle  62   a  for the second reducing agent was +5 kV. The distance between the spraying port  62   b  of the nozzle  62   a  for the second reducing agent and the fiber material A 3  was 1 cm. 
     As illustrated in  FIG.  6   , after the electroless plating step S 7 , the electroless plated fiber material A 4  was cleaned with the cleaning fluid H in the post-cleaning step S 8 . Purified water was used as the cleaning fluid H. 
     In the post-drying step S 9 , hot air was applied to the fiber material A 4  cleaned in the post-cleaning step S 8 . As a result, the fiber material A 4  was dried. Then, the electrical resistances of the plurality of electroless plated fiber materials A 4  were measured. 
     Comparative Example 
     Next, the comparative example is described. In the comparative example, first, the degreasing step, the pre-drying step, the pre-processing step, the pre-cleaning step, the catalyzing step, and the intermediate cleaning step similar to those in the example were performed. Then, the catalyst-applied fiber material cleaned in the intermediate cleaning step was immersed in the second reducing agent solution. The metal ion solution in a state of being electrically charged to a positive potential was electrostatically sprayed onto the catalyst-applied fiber material immersed in the second reducing agent solution by use of electrospraying. As a result, the electroless plated fiber material was obtained. The post-cleaning step and the post-drying step, similar to those in the example, were performed on the electroless plated fiber material. Then, the electrical resistances of the plurality of electroless plated fiber materials were measured. 
     Comparison of Example and Comparative Example 
     The electrical conductivities of the plurality of electroless plated fiber materials obtained in the comparative example were remarkably inferior to the electrical conductivities of the plurality of electroless plated fiber materials A 4  obtained in the example. In other words, the plurality of electroless plated fiber materials A 4  obtained in the example showed sufficient conductivity. In addition, even when the amount of time by which the metal ion solution in a state of being electrically charged to a positive potential was electrostatically sprayed with use of electrospraying was increased in the comparative example, the plurality of electroless plated fiber materials obtained in the comparative example hardly exhibited any conductivity. Therefore, in particular, it was confirmed that the electroless plated fiber material A 4  having sufficient conductivity was obtained by the electroless plating step S 7  in the example in contrast to the comparative example. 
     The electrical resistances of the plurality of electroless plated fiber materials A 4  obtained in the example were from 1.0 Ω/cm to 1.5 Ω/cm. In addition, the electrical resistance of the electroless plated fiber material of a commercial item is about 2.0 Ω/cm. Therefore, it was confirmed that the electroless plated fiber material A 4  obtained in the example had conductivity equal to or greater than that of the electroless plated fiber material of a commercial item. 
     REFERENCE SIGNS LIST 
     
         
         A 2  Pre-processed fiber material (fiber material) 
         A 3  Catalyst-applied fiber material (fiber material) 
         A 4  Electroless plated fiber material (fiber material) 
         B Catalyst solution 
         C First reducing agent solution 
         D Metal ion solution 
         E Second reducing agent solution 
         S 5  Catalyzing step 
         S 7  Electroless plating step 
           50 ,  150  Catalyzing apparatus 
           51   a ,  151   a  Nozzle for catalyst 
           52   a ,  152   a  Nozzle for first reducing agent 
           60 ,  170  Electroless plating apparatus 
           61   a ,  171   a  Nozzle for metal ions 
           62   a ,  172   a  Nozzle for second reducing agent 
           200  Carrying apparatus