CN103137997A

CN103137997A - Manufacturing method and manufacturing apparatus for electrical device with film covering

Info

Publication number: CN103137997A
Application number: CN2012105183527A
Authority: CN
Inventors: 高田孝一; 本桥裕太
Original assignee: Nissan Motor Co Ltd
Current assignee: Vision Aesc Japan Co ltd
Priority date: 2011-12-05
Filing date: 2012-12-05
Publication date: 2013-06-05
Anticipated expiration: 2032-12-05
Also published as: KR20130062884A; KR101395497B1; CN103137997B

Abstract

The invention provides a manufacturing method and a manufacturing apparatus for an electrical device with film covering. The manufacturing method for the electrical device with film covering according to the invention can be employed to realize the effect that electrolyte is hard to be uneven in permeation in a battery set so that the electrolyte can be filled within a short time period. The manufacturing method for the electrical device with film covering comprises a pressure reducing procedure for reducing the pressure inside an electrolyte filling cavity equipped with a bag-shaped laminated film package body to lower than the atmospheric pressure, wherein the bag-shaped laminated film package body is provided with an opening part and accommodates the battery set, and the battery set is provided with an anode and a cathode which are laminated up and separated by an insulating film; an electrolyte filling procedure for filling the electrolyte of a specified amount from the opening part into the package body, after the pressuring reducing procedure; and a pressuring increasing and reducing procedure for increasing the pressure inside the electrolyte filling cavity to higher than the pressure in the electrolyte filling procedure and then reducing the pressure, after the electrolyte filling procedure and before sealing the opening part.

Description

The manufacture method of thin-film package electric device and manufacturing installation

Technical field

The present invention relates to take battery, capacitor as representative, manufacture method and manufacturing installation that the electric device element is housed in the thin-film package electric device in laminated film.

Background technology

Electric device take electrolytic capacitor, battery as representative is by injecting electrolytic solution being obtained the electric device element in the shell of being made by metal etc. that is incorporated with the electrode group, and subsequently shell seal being made.In addition, in the explanation of this specification, the assembly that will have the complete state (stage) before of a series of fluid injection operation that clips the stacked positive pole of barrier film and negative pole and be in electrolyte is called " electrode group ", the assembly that will be in a series of fluid injection operation of the electrolyte state (stage) after complete is called " electric device element ", to distinguish.

In the past, by in the shell that the injecting electrolytic solution of ormal weight is erect to vertical ground, and long-time standing making in the gap that electrolyte is penetrated into the electrode group gradually subsequently.Yet, usually, due to the electrode group by battery lead plate closely is laminated, so need the time that electrolyte is impregnated in the gap of electrode group.Naturally till being penetrated in gap between electrode to standing electrolyte, need to place for example diel, the production efficiency extreme difference.

In addition, because the wetting-out rate of electrolyte is extremely slow, so if supply in shell the electrolyte of needed amount is disposable, electrolyte can overflow from shell.Therefore, adopted in advance the peristome watertight ground mounting cup of shell and with the electrolyte fluid injection in advance of ormal weight in this cover etc. method.Yet, due to the method mounting cup and labor intensive and time singly on shell, therefore be difficult to improve and make efficient.

Method is soaked in the fluid injection that discloses a kind of electrolyte be used to solving such problem in patent documentation 1.That is, after being sealed airtightly, the peristome of shell reduces pressure, in the shell with injecting electrolytic solution after be depressurized and electrolyte is impregnated in the gap of electrode group.Be not to reduce pressure after fluid injection electrolyte, but fluid injection electrolyte after reducing pressure in shell form an end hydrops.In the shell after be depressurized with injecting electrolytic solution and make electrolyte permeability in the gap of electrode group after, then make the pressure rise in shell and the electrolyte permeability that makes hydrops in the gap of electrode group.

The method is temporarily to form decompression state and will be present in the air exhausting that soaks in the gap of electrode group, that hinder electrolyte and remove, form and make electrolyte be easy to be penetrated into after state in the gap fluid injection electrolyte again, afterwards, then pressurize and with the injecting electrolytic solution of hydrops.Utilize like this combination of decompression and pressurization, not only shortened and soaked into the needed time of electrolyte, but also prevented that electrolyte disperses in the time pressurizeing release.

On the other hand, except the electric device of the metal shell of use as described above, also developed the thin-film package electric device, it is superimposed and constitute the laminated film packaging body that film forms that the packaging body of this thin-film package electric device has used the resin bed with the metal levels such as aluminium and thermal welding to clip binding agent.Usually, the laminated film packaging body forms two structures that surface coverage forms of the thinner resin bed of the utilization metal level that aluminium etc. is thinner, its acidproof, alkaline-resisting and lightweight and have flexibility.

Patent documentation 1: No. 3467135 communique of Japan's special permission

Different from metal shell, the laminated film packaging body of thin-film package electric device has flexibility.That is to say, the laminated film packaging body easily is out of shape, the also unexistent problem of on-deformable metal shell in the time of therefore can being created in fluid injection electrolyte.

At first, the electrolyte that is injected in the peristome of bag-shaped laminated film packaging body can not form hydrops at peristome, and can flow between the interarea and laminated film of electrode group.Therefore, utilize hydrops temporarily with the electrode group with respect to outside sealing, make the electrolyte that between electrode group and outside, pressure differential is set and has formed hydrops be impregnated into the electrode group in so disclosed method of patent documentation 1 can not directly be adopted.Therefore, in the thin-film package electric device that consists of using the laminated film packaging body, as mentioned above, need the time that electrolyte is impregnated in the gap of electrode group.Naturally till being penetrated in gap between electrode to standing electrolyte, need to place for example diel, the production efficiency extreme difference.

In addition, have following problem: electrolyte is not to soak in the electrode group with same speed, at the position that electrolyte is soaked into, and particularly at the central portion of electrode group, the phenomenon (soaking into inequality) that the liquid that is easy to produce electrolysis can not fully soak into.Soaking into of this electrolyte uneven also may appear on the surface of laminated film with the form of fold because laminated film has flexibility.

In addition, the soak into inequality of this electrolyte in the electrode group makes the lower zone of ionic conduction characteristic that produces partly between both positive and negative polarity in face, its result, and the electrical characteristic that produces battery reduces such unfavorable condition.

Summary of the invention

Therefore, the object of the present invention is to provide a kind of manufacture method and device thereof of thin-film package electric device, the manufacture method of this thin-film package electric device and device thereof make electrolyte be difficult to produce in the electrode group to soak into inequality, and can promote electrolyte to permeate at short notice after fluid injection, soak into.

In order to reach above-mentioned purpose, the manufacture method of thin-film package electric device of the present invention has the feature of each operation that comprises following (1)～(3).

(1) has the decompression operation, this decompression operation is used for being provided with in the fluid injection chamber of bag-shaped laminated film packaging body and reduces pressure to the pressure that forces down than atmosphere, this bag-shaped laminated film packaging body has peristome, and taken in the electrode group, this electrode group has and clips positive pole and the negative pole that separating film layer gathers into folds.

(2) comprise the fluid injection operation, after above-mentioned decompression operation, with the regulation reservoir quantity electrolyte from above-mentioned peristome to packaging body in fluid injection.

(3) comprise and add the decompression operation, the pressure to than above-mentioned fluid injection operation the time is high with the exert pressure in the fluid injection chamber after above-mentioned fluid injection operation, before the above-mentioned peristome of sealing, then reduces pressure.

In addition, in order to reach above-mentioned purpose, the manufacturing installation of thin-film package electric device of the present invention has the feature of each parts that comprise following (1)～(3).

(1) has the pressure adjustment component, this pressure adjustment component is used for the pressure in the fluid injection chamber that is provided with bag-shaped laminated film packaging body is adjusted, this bag-shaped laminated film packaging body has peristome, and taken in the electrode group, this electrode group has and clips positive pole and the negative pole that separating film layer gathers into folds.

(2) have the fluid injection parts, these fluid injection parts are used for electrolyte is injected in packaging body from above-mentioned peristome.

(3) have control assembly, this control assembly carries out following control: utilize above-mentioned pressure adjustment component to make in the fluid injection chamber decompression to the pressure that forces down than atmosphere, after reducing pressure, utilize the fluid injection in the packaging body of electrolyte that above-mentioned fluid injection parts make the regulation reservoir quantity.Also have control assembly, this control assembly carries out following control: before the above-mentioned peristome of sealing, the pressure to than above-mentioned fluid injection the time is high with the exert pressure in the fluid injection chamber to utilize above-mentioned pressure adjustment component, then reduces pressure.

Adopt the present invention, owing to adding decompression after fluid injection, before sealing, so can promote electrolyte to soak into after fluid injection.Because being adds decompression after fluid injection, so being isolated film, electrolyte keeps, even add decompression, can not cause yet and disperse.Its result can provide and electrolyte be produced soak into inequality, and can make manufacture method and the device thereof of the thin-film package electric device that electrolyte permeates at short notice, soaks into after fluid injection.

Description of drawings

Fig. 1 is the cutaway view of formation that schematically shows the cell coated with film of the 1st execution mode.

Fig. 2 (a) be schematically show the 1st execution mode cell coated with film complete stereogram.

Fig. 2 (b) schematically shows the exploded perspective view that the cell coated with film of the 1st execution mode of Fig. 2 (a) is resolved into the state of each composed component.

Fig. 3 is the schematic stereogram of the generating element that describes for interarea and stacked side to the generating element in the cell coated with film of the 1st execution mode.

Fig. 4 means the schematic diagram as the formation of the fluid injection soakage device of a representational execution mode (the 1st execution mode) of thin-film package electric device manufacturing installation of the present invention, and this fluid injection soakage device is used for electrolyte is soaked into to taking in the interior fluid injection of bag-shaped laminated film packaging body (battery unit) the electrode group, that have peristome.

(j) of (a)～Fig. 5 of Fig. 5 means that the fluid injection of the electrolyte that the fluid injection soakage device by present embodiment carries out soaks into the resulting fluid injection curve of method and soak into the figure of state.

Fig. 6 means that the fluid injection of the electrolyte that the fluid injection soakage device by present embodiment carries out soaks into the reservoir quantity of each fluid injection step of method and the figure of vacuum pressure.

(a) of Fig. 7, (b) of Fig. 7 mean the figure that produces the situation of foam when fluid injection.

Embodiment

Below, illustrate referring to the drawings embodiments of the present invention.In addition, in the description of the drawings, to the identical Reference numeral of identity element mark, the repetitive description thereof will be omitted.In addition, for convenience of explanation, the dimension scale of accompanying drawing is exaggerated, sometimes different with the ratio of reality.

Fig. 1 is the cutaway view of formation that schematically shows the cell coated with film of the 1st execution mode.Fig. 2 is the stereogram that schematically shows the cell coated with film of the 1st execution mode, Fig. 2 (a) is the stereogram of completing of cell coated with film, and Fig. 2 (b) schematically shows the exploded perspective view that the cell coated with film of the 1st execution mode of Fig. 2 (a) is resolved into each composed component state.

Cell coated with film

Formation summary to the cell coated with film 10 of the 1st execution mode describes.

As shown in Figure 1, the cell coated with film 10 of present embodiment has such structure: the actual generating element 21 that discharges and recharges the essentially rectangular of reaction is enclosed in inside as the bag-shaped laminated film of packaging body 29.Specifically, the cell coated with film 10 of present embodiment has generating element 21 and packaging body 29, this packaging body 29 is made of bag-shaped laminated film, and this packaging body 29 is taken in generating element 21 together with the anodal curren-collecting part 12b that is located at generating element 21 and negative pole curren-collecting part 11b.Cell coated with film 10 also has the anodal corbel back slab 27 that is connected in anodal curren-collecting part 12b and the negative pole corbel back slab 25 that is connected in negative pole curren-collecting part 11b.

Here, in the present embodiment, the assembly that will have the complete state (stage) before of a series of fluid injection operation that clips the stacked positive plate of barrier film (positive pole) 16 and negative plate (negative pole) 14 and be in electrolyte 20 is called " electrode group ", to be in the assembly conduct " generating element " of the complete state (stage) afterwards of a series of fluid injection operation of electrolyte 20, distinguish with this.Electrolyte 20 is mainly used in dielectric substrate 17, and this dielectric substrate 17 is used for consisting of generating element 21.Specifically, can form dielectric substrate 17 in barrier film by electrolyte 20 is impregnated into.But, 20 of all electrolyte are impregnated in barrier film, making also to soak in electrode

active material layer

13,15 has electrolyte 20 comparatively desirable, and electrolyte can also be present in gap (space part) between generating element 21 and packaging body 29.

As shown in Fig. 2 (a), Fig. 2 (b), for from each layer electrode of generating element 21 (negative electrode collector 11, positive electrode collector 12) extracted current, be extended with the epitaxy part 12a that is consisted of by metallic plate (perhaps metal forming) of the epitaxy part 11a, the anodal curren-collecting part 12b that are consisted of by metallic plate (perhaps metal forming) of negative pole curren-collecting part 11b from each layer electrode of generating element 21 (negative electrode collector 11, positive electrode collector 12).Each layer electrode (negative electrode collector 11, positive electrode collector 12)

epitaxy part

11a, 12a separately is connected in negative pole corbel back slab 25, anodal corbel back slab 27 at negative pole curren-collecting part 11b, anodal curren-collecting part 12b place respectively.Specifically, be connected with respectively the end of

epitaxy part

11a, 12a on each negative electrode collector 11 and positive electrode collector 12, arrange or be connected with each curren-collecting

part

11b, 12b on the other end of each epitaxy part 11a, 12a.In addition, negative pole corbel back slab 25 and anodal corbel back slab 27 have following structure: the outside that is exported this packaging body 29 in the mode of the end (closure or mouth-sealed portion 29f) that is sandwiched in the packaging body 29 that is made of bag-shaped laminated film.It is comparatively desirable that the connection between separately of the epitaxy part 12a of negative pole corbel back slab 25, anodal corbel back slab 27, the epitaxy part 11a of negative pole curren-collecting part 11b, anodal curren-collecting part 12b, the negative electrode collector 11 of each electrode and positive electrode collector 12 utilizes ultrasonic bonding, resistance welded etc. to install.

In Fig. 2 (a), Fig. 2 (b), be formed with on the packaging body 29 that is consisted of by bag-shaped laminated film be used to the recess 29e that takes in generating element 21, in addition, show the type that makes two laminated films relatively and 4 bandings are closed about packaging body 29.But, present embodiment is not limited to this, also can be with the smooth laminated film that is not formed with recess as packaging body 29, and the type that also goes for 1 laminated film is turned back and 3 bandings are closed.Perhaps, also can be with two smooth laminated films not being formed with recess as packaging body, also go for making superimposed and type that 4 bandings are closed of two laminated films etc., there is no particular restriction.

As shown in Figure 1, generating element 21 with all in the form of a substantially rectangular a plurality of negative plates (negative pole) 14 and a plurality of positive plate (positive pole) 16 clip all in the form of a substantially rectangular dielectric substrate 17 alternately stacked multilayer consist of.Negative plate (negative pole) 14 is made of negative electrode collector 11 and the negative electrode active material layer 13 that is formed at the two sides of this negative electrode collector 11.Positive plate (positive pole) 16 is made of positive electrode collector 12 and the positive electrode active material layer 15 that is formed at the two sides of this positive electrode collector 12.In addition, dielectric substrate 17 is electrolyte 20 is impregnated in the barrier film (comprising the nonwoven fabrics barrier film) of Porous and consists of.Namely, with this sequential cascade multilayer, it is relative and consist of 1 monocell layer 19 that 1 positive electrode active material layer 15 of 1 negative electrode active material layer 13 that makes negative plate 14 and adjacent with it positive plate 16 clips dielectric substrate 17 with negative plate (negative pole) 14, dielectric substrate 17 and positive plate (positive pole) 16.Thereby, can say that the cell coated with film 10 of present embodiment has by the stacked multilayer of monocell layer 19 being made the structure of the monocell layer 19 electric parallel connection of multilayer.In addition, be all only to dispose negative electrode active material layer 13 at a face although be positioned at two outermost outermost layer negative electrode collectors of generating element 21, also negative electrode active material layer 13 can be set on the two sides.That is, also can not form the collector body that only is provided with the outermost layer special use of active material layer at a face, but there is the collector body of active material layer on the two sides directly as outermost collector body.In addition, also can be opposite with Fig. 1 by the configuration that makes anodal configuration and negative pole, make the outermost layer positive electrode collector be positioned at two outermost layers of generating element 21, positive electrode active material layer 15 is configured on face or two sides of this outermost layer positive electrode collector.Below, regulation in the present embodiment, as shown in Figure 3, the face of the generating element 21 that will see at stacked direction is called interarea 21a, and the face of the generating element 21 that will see from the direction vertical with stacked direction is called stacked side 21b.

As shown in Figure 1, each negative plate 14 is at negative electrode collector 11(Copper Foil for example) the two sides be formed with negative electrode active material layer (negative electrode) 13 by coating, each positive plate (positive pole) 16 is at positive electrode collector 12(aluminium foil for example) the two sides be formed with positive electrode active material layer (anode electrode) 15 by coating.Negative electrode collector 11 and positive electrode collector 12 extend out from lamination area.Specifically, as shown in Fig. 1, Fig. 2 (b), for the epitaxy part that there is no the coated electrode material of each negative electrode collector 11, positive electrode collector 12, with the epitaxy part 11a of negative plate side each other and the epitaxy part 12a of positive plate side ultrasonic bonding once separately from each other.Anodal curren-collecting part 12b and negative pole curren-collecting part 11b as relay have been formed thus.Meanwhile, also make negative pole corbel back slab 25 and negative pole curren-collecting part 11b be connected, make anodal corbel back slab 27 to be connected with anodal curren-collecting part 12b by ultrasonic bonding.

As 1 example, laminated film packaging body 29 is formed by the laminated film doubling of 1 rectangular shape as described above, is used for generating element 21 is clamped and it is surrounded from its thickness direction both sides.The laminated film that packaging body 29 uses is that the thermal welding resin bed that will have thermal welding, metal level (for example aluminium foil) and (insulating properties) protective layer are stacked and consist of.For 1 example, making the polypropylene by PP() the thermal welding resin bed that consists of becomes the layer of inboard of the cell coated with film 10 of present embodiment, thermal welding section thermal welding by with the peripheral part (outer edge) of laminated film packaging body 29 forms closure (mouth-sealed portion) 29f.Thus with generating element 21 sealings (sealing or insulation sealing) of taking in.But, about the laminated film packaging body 29 of present embodiment, be not subjected to any restriction of above-mentioned formation, can suitably use known various laminated film packaging body in the past.

As electrolyte 20, can use the LiPF that rises with 1mol/ ₆Be supporting electrolyte, electrolyte take the mixed solvent (mass ratio 50:50) of propene carbonate and ethylene carbonate as solvent.But, in the present embodiment, electrolyte 20 is not subjected to any restriction of above-mentioned electrolyte.That is, electrolyte 20 has the form that is dissolved with appropriate supporting electrolyte in solvent.As solvent, for example, except above-mentioned ethylene carbonate (EC) and propene carbonate (PC), can also use the carbonates equal solvents such as dimethyl carbonate (DMC), diethyl carbonate (DEC).Above-mentioned solvent can use separately a kind, also can two or morely use together.In addition, as supporting electrolyte, except above-mentioned LiPF ₆, can also use Li(CF ₃SO ₂) ₂N, Li(C ₂F ₅SO ₂) ₂N, LiBF ₄, LiAsF ₆, LiTaF ₆, LiClO ₄, LiCF ₃SO ₃Deng.Above-mentioned supporting electrolyte can use separately a kind, also can two or morely use together.In addition, the concentration of supporting electrolyte also can suitably determine in 0.5mol/ liter～2mol/ rises the scope of left and right, but is not subjected to any restriction of this scope.

The manufacturing installation of cell coated with film

Below, use accompanying drawing that the formation of the fluid injection soakage device in the present embodiment that is used for electrolyte is soaked into to cell coated with film unit fluid injection is described.

Fig. 4 means as a schematic diagram representational execution mode (the 1st execution mode) of thin-film package electric device manufacturing installation of the present invention, formation that be used for fluid injection soakage device that electrolyte is soaked into to cell coated with film unit fluid injection.

As shown in Figure 4, the fluid injection soakage device 1 of present embodiment has fluid injection chamber 2, has filling box 3, electrolyte supply pipeline 4, exhaust line 5, gas introduction tube line 6 and the control part 7 of pressing fixture 3a.

The container 4a that 7 pairs of control parts press fixture 3a, be connected in the vacuum pump 5b of exhaust line 5, be connected in the electrolyte of electrolyte supply pipeline 4 carries out action control.In addition, below, the action of the each several part controlled by control part 7 is elaborated.

Be provided with filling box 3 in fluid injection chamber 2, this filling box 3 has the fixture of pressing 3a, this presses battery unit 10a(Fig. 4 that fixture 3a is used for taking in the state of a plurality of not yet fluid injection electrolyte 20), be connected with respectively electrolyte supply pipeline 4, exhaust line 5 and gas introduction tube line 6 on the wall in fluid injection chamber 2.

Filling box 3 is equipped with, and to press fixture 3a be the tabular fixture (board member) that arranges in the mode that a plurality of battery unit 10a of the state of fluid injection electrolyte not yet stably keep.During to the interior fluid injection electrolyte 20 of this bag-shaped laminated film packaging body 29, can utilize this to press fixture 3a from thickness direction both sides (the two interarea 21a sides of electrode group 21 ' from the peristome 29a of the bag-shaped laminated film packaging body 29 of taking in electrode group 21 '; With reference to Fig. 3) clamping packaging body 29 and with its maintenance.

The laminated film packaging body 29 of taking in the electrode group 21 ' of the fixture 3a clamping that is pressed forms bag-shaped.That is, bag-shaped laminated film packaging body 29 except above peristome 29a limit place by thermal welding, only having peristome 29a is opening.This is the bag shape that can electrolyte 20 be injected into from peristome 29a in the bag-shaped laminated film packaging body 29 of taking in electrode group 21 ' in order to form.

An end that consists of the electrolyte supply pipeline 4 of fluid injection parts is connected in for the case 4a that stores electrolyte.The other end of electrolyte supply pipeline 4 is divided into many halfway, and each system is connected to electrolyte shifting pump (the electrolyte supply pump on the electrolyte supply pipeline) 4c.Electrolyte shifting pump 4c is connected in valve (switching valve or flow control valve on the electrolyte supply pipeline) 4d.Valve 4d carries out open and close controlling or regulation by control part 7, can be at every turn marginally fluid injection in each system several times.Above-mentioned pump 4c and valve 4d are arranged on the outside in fluid injection chamber 2, and are connected with each fluid injection nozzle 4b that is located in fluid injection chamber 2.The distolateral fluid injection nozzle 4b of another of electrolyte supply pipeline 4 with configure towards the corresponding mode of the peristome 29a of the laminated film packaging body 29 of top opening.This is in order to inject from peristome 29a from the electrolyte 20 that electrolyte supply pipeline 4 is supplied with.

In the present embodiment, a plurality of fluid injection nozzle 4b can move to the peristome 29a top of a plurality of battery unit 10a side by side successively.Thereby, can repeatedly supply with electrolyte 20 to a plurality of battery unit 10a successively by 1 nozzle 4b.As the structure that fluid injection nozzle 4b is moved, can consider for example to be located at the running rail (not shown) in fluid injection chamber 2.Can make fluid injection nozzle 4b along this rail moving.

The exhaust line 5 that consists of pressure adjustment component (being mainly the adjusting parts of depressurised side) mainly has valve 5a and vacuum pump 5b, and is connected in control part 7, makes fluid injection chamber 2 inner pressure relieves in order to 2 inside, fluid injection chamber can be vacuumized.

The gas introduction tube line 6 that consists of pressure adjustment component (being mainly the adjusting parts of pressure side) is used for making the interior pressure in fluid injection chamber 2 increase from vacuum state or decompression state by inner dry airs or the non-active gas of importing in the fluid injection chamber 2 after utilize exhaust line 5 to vacuumize.This gas introduction tube line 6 mainly has valve (switching valve or flow control valve on the gas introduction tube line) 6a and air receiver 6b, and valve 6a is connected in control part 7 etc., in order to can make 2 inside, fluid injection chamber from vacuum state or decompression state rising (pressurize, boost).

The manufacture method of cell coated with film

Next the included operation of manufacture method of the cell coated with film of present embodiment described.

Method is soaked in the fluid injection of electrolyte

Below, use accompanying drawing to soak into method to the fluid injection of the electrolyte 20 that utilizes the fluid injection soakage device 1 that is used for present embodiment that electrolyte is soaked into to cell coated with film unit fluid injection and carry out and describe.(a)～(j) of Fig. 5 means that the fluid injection of the electrolyte 20 that the fluid injection soakage device 1 by present embodiment carries out soaks into the resulting fluid injection curve of method and soak into the figure of state.Fig. 6 means that the fluid injection of the electrolyte 20 that the fluid injection soakage device 1 by present embodiment carries out soaks into the reservoir quantity of each fluid injection step of method and the figure of vacuum pressure.(a) of Fig. 7, (b) of Fig. 7 mean the figure that produces the situation of foam when fluid injection.

In addition, the electrolyte the pressure operation process after from (a) to (j) in Fig. 5 means from the fluid injection initial stage to fluid injection final stage, fluid injection is impregnated into the figure of situation of battery surface of the left end of filling box.In figure, the part that represents with white is to be located at the part of the not yet fluid injection of outermost layer barrier film before electrolyte soaks into of battery surface.On the other hand, the part that represents with black be located at battery surface the outermost layer barrier film soak into the part that electrolyte is arranged.This battery obtains as follows: as shown in Figure 1, electrode is positioned at the surface of common battery, but in this figure, the state that soaks in order to be easy to monitor that electrolyte soaks into to barrier film also is provided with barrier film on battery surface.Like this, in the cell coated with film of present embodiment, do not get rid of the mode that any outermost layer in the electrode group arranges barrier film.

In Fig. 5 (a)～(j), chart shown in Figure 6, expression is about by the fluid injection of fluid injection nozzle, reservoir quantity battery unit 10a of Fig. 4 and the relation between the time.

Decompression degree when (a) of Fig. 7 means fluid injection improves the figure that (as condition of high vacuum degree) produces foam to the pressure that causes the air that the soaks into expansion that hinders electrolyte and caused the existing fluid injection state that electrolyte disperses.Decompression degree when (b) of Fig. 7 means fluid injection is suppressed to and can not causes that pressure that the air that soaks into that hinders electrolyte expands suppresses that foam produces and the figure that suppressed the fluid injection state of the present embodiment that electrolyte disperses.

As shown in Fig. 5 (a)～(j), utilize the fluid injection of the electrolyte 20 that the fluid injection soakage device 1 of present embodiment carries out to soak into method and be maintained under the constant state of the pressure that forces down than atmosphere full dose with the electrolyte 20 of regulation reservoir quantity from above-mentioned peristome 29a to the interior fluid injection of packaging body 29 in fluid injection chamber 2.The time point of the A of the zone circle in Fig. 5 (a)～(j) with the time point of the full dose fluid injection of the electrolyte 20 of regulation reservoir quantity.The fluid injection of the electrolyte 20 of present embodiment is soaked under the state that method remains unchanged after with the decompression of the pressure (decompression) in fluid injection chamber 2 the peristome 29a fluid injection to the bag-shaped laminated film packaging body 29 of taking in electrode group 21 ' of the full dose of electrolyte 20, specifically, as Fig. 5 (a)～(j), shown in Figure 6, carry out in the following order the fluid injection of electrolyte 20 keeping under the constant state of pressure (decompression) during #1 fluid injection step～#7 fluid injection step.

The decompression operation

As shown in Figure 4, fitly be arranged with a plurality of battery unit 10a in fluid injection chamber 2.

Next, by control part 7, drive under the state that valve 5a is opened exhaust line 5 vacuum pump 5b and with fluid injection chamber 2 interior decompressions to the pressure that forces down than atmosphere.Having reached after the vacuum degree of regulation is valve-off 5a.Under this state, comprise that the pressure of regulation has been arrived in the inside in fluid injection chamber 2 of the inside of above-mentioned electrode group 21 ' by decompression equably.In addition, as shown in Fig. 5 (a)～(j), at fluid injection stage (for example, before the T1 of Fig. 5 (a)～(j)), carry out fluid injection with the high pressure of decompression degree of (for example, T5, T8, the T10 of Fig. 5 (a)～(j)) when carrying out pressure operation after fluid injection comparatively desirable.Carry out like this fluid injection following advantage is arranged: in the fluid injection stage, during soaking in the barrier film etc. at electrolyte 20, can effectively prevent because of foaming disperse etc. (contrast is with reference to (a) of Fig. 7 and (b) of Fig. 7).In addition, as Fig. 5 (a)～(j), shown in Figure 6, although the decompression degree in fluid injection chamber 2 preferably acutely reduce pressure in the scope of foamed state not causing electrolyte 20 boilings more near the pressure of vacuum so long as the pressure that forces down than atmosphere get final product.Thus, the unnecessary air (gas) in battery unit 10a can be extruded, can prevent pneumatosis, electrolyte can fully be soaked into.For example, be preferably the following pressure of 5kPa, the following pressure of 3kPa more preferably is in the scope of 1.5kPa～2kPa left and right.But, present embodiment is not subjected to any restriction of this scope.

As shown in Fig. 5 (a), the state that soaks in this operation is that whole face is all white to electrolyte less than soaking in barrier film.

The fluid injection operation

Next, be maintained in above-mentioned fluid injection chamber 2 under the constant state of the pressure (pressure that forces down than atmosphere) reached by above-mentioned decompression operation, will stipulate that the full dose of electrolyte of reservoir quantity (electrolyte content of regulation) is from above-mentioned peristome 29a to the interior fluid injection of described packaging body 29.

Specifically, via the peristome 29a of the upper section of packaging body 29 from electrolyte supply pipeline 4 by fluid injection nozzle 4b at every turn marginally several times (among Fig. 5 (a)～(j), Fig. 6 minute 7 times) full dose inject the electrolyte 20 of regulation reservoir quantity (electrolyte content of regulation).Because the be pressed whole interarea of board member of fixture 3a of the thickness direction of electrode group 21 ' is moderately pressed, so do not have electrolysis liquid 20 to flow into the gap of central portion of the interarea 21a side of electrode group 21 ' in electrode group 21 '.In addition, because the fixture 3a that is pressed presses, so the gap that consists of between a plurality of positive plates, barrier film, negative plate of electrode group 21 ' is less, electrolyte 20 can flow between a plurality of positive plates, barrier film, negative plate hardly.And, because comprise electrode group 21 '

Inside in interior fluid injection chamber 2 inside by decompression equably to the pressure of regulation, so electrolyte 20 can attracted to because of the effect of the negative pressure in electrode group 21 ' inside of electrode group 21 ' hardly.Therefore, in the fluid injection operation, the electrolyte 20 that to stipulate reservoir quantity (electrolyte content of regulation) marginally injects (with reference to Fig. 5 (a) → (b) → (d ')) at every turn several times, until from the peripheral part of electrode group 21 ' to all becoming the state that is soaked by electrolyte 20 near central portion.

Specifically, as shown in Fig. 5 (d '), as can be known: at the complete time point of this operation, electrolyte 20 is not impregnated into the central portion of the interarea 21a side of electrode group 21 ', the state that soaks into of barrier film is also that central portion still keeps white constant, and central portion not yet soaks into.

In addition, as Fig. 5 (a)～(j), shown in Figure 6, why in this operation with electrolyte 20 marginally fluid injection several times at every turn, be in order to prevent that electrolyte from overflowing and dispersing from packaging body 29.Need spended time that electrolyte is impregnated in electrode group 21 '.Even the electrolyte of the amount of finally soaking into, if carry out disposable fluid injection under the state that can not soak into fully, electrolyte also might overflow from packaging body 29.But, in this operation, even in the situation that each marginally separately fluid injection does not also supply the quick gap that flows into of electrolyte 20 of institute's fluid injection.Therefore as can be known: the electrolyte 20 of fluid injection in this operation produces some foams (with reference to (b) of Fig. 7) in the upper side of electrode group 21 ' on one side, on one side be easier to immersed (that is, have some gaps, be difficult to apply pressing force) peripheral part from the ratio of electrode group 21 ' at leisure and permeate (soaking into) enter (with reference to Fig. 5 (a) → (b) → (d ')).In addition, as Fig. 5 (a)～(j), shown in Figure 6, the vacuum pressure in this operation is maintained in front operation decompression to the state of the pressure that forces down than atmosphere and keeps constant.

In addition, in this operation, marginally injected several times the electrolyte 20 of regulation reservoir quantity (electrolyte content of regulation) in the battery unit 10a by fluid injection nozzle 4b at every turn.Particularly, as shown in the chart of Fig. 5 (a)～(j), fluid injection curve shown in Figure 6, from #1 fluid injection step to #7 fluid injection step divide 7 times with regulation reservoir quantity (electrolyte content of regulation) in setting time fluid injection at leisure.

As Fig. 5 (a)～(j), shown in Figure 6, from 1 battery unit 10a, it can be again by fluid injection after other battery unit 10a is by fluid injection after self is by fluid injection.Thereby as can be known: during other battery unit 10a was by fluid injection, this 1 battery unit 10a kept not by the state of fluid injection.By carrying out like this fluid injection, promote in the constant time after each fluid injection electrolyte to soak into this respect comparatively desirable.But, in the present embodiment, be not subjected to any restriction of foregoing, fluid injection number of times, reservoir quantity, fluid injection time, decompression degree etc. are suitably determined to get final product according to battery size, shape, concentration of electrolyte etc.For example, comparatively desirable fluid injection number of times is: reduce as far as possible the fluid injection number of times in the scope that can not spray, disperse because of a large amount of fluid injections with electrolyte, thereby with electrolyte content not lavishly, fluid injection effectively, shorten fluid injection time of electrolyte.In the situation that the way that increases the fluid injection number of times because of pressure condition can shorten the fluid injection time of electrolyte, can say that to increase the fluid injection number of times comparatively desirable.

As previously discussed, determine that in making the optimized process of various conditions optimal fluid injection number of times etc. gets final product.In addition, as shown in Figure 6, at this in-process, reservoir quantity has along with the fluid injection number of steps increases and the tendency of minimizing.This is because along with the fluid injection number of times increases, the central portion that electrolyte 2 becomes the interarea 21a side that is difficult to be impregnated into electrode group 21 ' is so by reservoir quantity is reduced along with the fluid injection number of steps increases, can effectively suppress to disperse.The fluid injection time can be according to vacuum degree, suitably determine to the wetting-out rate of electrode group 21 '.The decompression degree is made as higher vacuum degree within can suppressing as described above the scope that electrolyte 20 acutely foams, disperses because of boiling comparatively desirable.This be because: because air residual is inner at battery unit 10a, in the fluid injection stage, electrolyte can not be penetrated in this residual air part, might produce pneumatosis.

In addition, battery unit number, fluid injection nozzle number are also suitably determined to get final product.For example, also can make battery unit 10a and fluid injection nozzle 4b is identical quantity, uses fixed nozzle, the system that omit movable mechanism, this movable mechanism is controlled etc., thus reduce the system failure.In addition, also depend on the size in fluid injection chamber 2, both can be with a plurality of filling box settings planar, also a plurality of filling boxes can be carried out three-dimensional stacked mode and arrange to separate suitable interval, aforesaid way can also be made up.Filling box 3 can be both also the mode of as shown in Figure 4 a plurality of battery unit 10a being lined up 1 row, can be also the mode of multiple row that a plurality of battery unit 10a are lined up.In addition, filling box 3 can be both box-shaped as shown in Figure 4, can be also circular.In the situation that filling box 3 is circular, a plurality of battery unit 10a are arranged in order on radial direction and get final product.

From #1 fluid injection step to #7 fluid injection step, why the reservoir quantity of each step reduces gradually, this be because: need to further soak into into towards central portion from the periphery of electrode group 21 ' along with the fluid injection step goes on, the reservoir quantity that electrolyte 20 can soak into also tails off gradually.Therefore, in this operation, even after (electrolyte content of regulation) carry out fluid injection with the regulation reservoir quantity, sizable part of the central portion of the barrier film of electrode group 21 ' also still is in fluid injection state not yet (with reference to Fig. 5 (a) → (b) → (d ')).

The variation of fluid injection operation

Next, soak into the preferred variation of method as the fluid injection of the electrolyte 20 of present embodiment, as above-mentioned fluid injection operation, carry out the 1st following fluid injection operation: be maintained under the constant state of post-decompression pressure in the fluid injection chamber, with the part of the electrolyte of regulation reservoir quantity from above-mentioned peristome to packaging body in fluid injection.Afterwards, carry out the 2nd following fluid injection operation: after boosting to than the high pressure of above-mentioned pressure, the pressure after boosting is kept the constant time and with the remainder fluid injection of the regulation reservoir quantity of electrolyte in further making the fluid injection chamber.Below, describe the preference that carries out preferred the 1st fluid injection operation and the 2nd fluid injection operation as the above-mentioned fluid injection operation of present embodiment in detail.

the fluid injection of the electrolyte 20 of this variation is soaked into method and is characterised in that, with electrolyte 20 in the process of the peristome 29a fluid injection of the bag-shaped laminated film packaging body 29 of taking in electrode group 21 ', make pressure (decompression) go up and keep the constant time to atmospheric pressure side (less than atmospheric pressure), specifically, the fluid injection of the electrolyte 20 of this variation is soaked into method and is characterised in that, (a)～(j) as Fig. 5, shown in Figure 6, between #4 fluid injection step and #5 step, pressure (decompression) is gone up to atmospheric pressure side (less than atmospheric pressure), during #5 fluid injection step～#7 fluid injection step, this pressure is kept the constant time.So, carry out in the following order the fluid injection of electrolyte 20.

The 1st fluid injection operation

Next, in the preferred mode of present embodiment, be maintained in fluid injection chamber 2 under the constant state of the pressure (pressure that forces down than atmosphere) reached by above-mentioned decompression operation, will stipulate that the part of electrolyte of reservoir quantity (electrolyte content of regulation) is from above-mentioned peristome 29a to the interior fluid injection of above-mentioned packaging body 29.

Specifically, via the peristome 29a of the upper section of packaging body 29, from electrolyte supply pipeline 4 by fluid injection nozzle 4b at every turn marginally several times (among Fig. 5 (a)～(j), Fig. 6 minute 4 times) inject the part of the electrolyte 20 of regulation reservoir quantity (electrolyte content of regulation).For example, as shown in the fluid injection curve of Fig. 5 (a)～(j), Fig. 6, about 60% fluid injection that will stipulate the electrolyte 20 of reservoir quantity (electrolyte content of regulation).

Because the be pressed whole interarea appropriateness of board member of fixture 3a of the thickness direction of electrode group 21 ' is pressed, so do not have electrolysis liquid 20 to flow into the gap of central portion of the interarea 21a side of electrode group 21 ' in electrode group 21 '.In addition, because the fixture 3a that is pressed presses, so the gap that consists of between a plurality of positive plates, barrier film, negative plate of electrode group 21 ' is less, electrolyte 20 can flow between a plurality of positive plates, barrier film, negative plate hardly.And, due to the inside in the fluid injection chamber 2 of the inside that comprises electrode group 21 ' by decompression equably to the pressure of regulation, so electrolyte 20 can not attracted to because of the negative pressure in electrode group 21 ' inside of electrode group 21 ' yet.Therefore, in the 1st fluid injection operation, to stipulate a part (in Fig. 5 (a)～(j), Fig. 6 for whole about 6 one-tenths) the marginally injection (with reference to (b) of Fig. 5) several times at every turn of the electrolyte 20 of reservoir quantity (electrolyte content of regulation), until become the state that the peripheral part of electrode group 21 ' is soaked by electrolyte 20.

Specifically, as soaking into as shown in state, as can be known of Fig. 5 (b): at the complete time point of this operation, electrolyte 20 is not impregnated into the central portion of the interarea 21a side of electrode group 21 ', the state that soaks into of barrier film is also that central portion still keeps white constant, and central portion not yet soaks into.In addition, as Fig. 5 (a)～(j), shown in Figure 6, why in this operation with electrolyte marginally fluid injection several times at every turn, this is in order to prevent that electrolyte from overflowing and dispersing from packaging body 29.Need spended time that electrolyte is impregnated in electrode group 21 '.Even the electrolyte of the amount of finally soaking into, if carry out to property fluid injection at the state that can not soak into fully next time, electrolyte also might overflow from packaging body 29.But, in this operation, even in the situation that marginally separately carry out fluid injection at every turn, the gap that does not also flow into fast for the electrolyte 20 of institute's fluid injection.Therefore, as can be known: electrolyte 20 produces some foams (with reference to (a) of Fig. 7) in the upper side of electrode group 21 ' on one side, on one side be easier to immersed (that is, have some gaps, be difficult to apply pressing force) peripheral part from the ratio of electrode group 21 ' at leisure and permeate (soaking into) enter (with reference to (b) of Fig. 5).In addition, as Fig. 5 (a)～(j), shown in Figure 6, the vacuum pressure in this operation is maintained in front operation decompression to the state of the pressure that forces down than atmosphere and keeps constant.

In addition, in this operation, marginally injected several times the part of the electrolyte 20 of regulation reservoir quantity (electrolyte content of regulation) in the battery unit 10a by fluid injection nozzle 4b at every turn.Particularly, as shown in the chart of Fig. 5 (a)～(j), fluid injection curve shown in Figure 6, from #1 fluid injection step to #4 fluid injection step divide 4 times slowly fluid injection to 60% left and right of regulation reservoir quantity (electrolyte content of regulation).

As previously discussed, determine that in making the optimized process of various conditions optimal fluid injection number of times etc. gets final product.In addition, as shown in Figure 6, at this in-process, reservoir quantity has along with the fluid injection number of steps increases and the tendency of minimizing.Can say accordingly: for shortening the viewpoint of the fluid injection time of electrolyte when preventing the dispersing of electrolyte, will be under the state of keeping the pressure that forces down than atmosphere can fluid injection reservoir quantity be made as that roughly 50%～70% left and right is comparatively desirable.The wetting-out rate that the fluid injection time can soak into according to vacuum degree, to electrode group 21 ' is suitably determined.The decompression degree can be made as comparatively ideal of higher vacuum degree as described above in the scope that inhibition electrolyte 20 acutely foams, disperses because of boiling.This be because: because air residual is inner at battery unit 10a, in the fluid injection stage, electrolyte can not be penetrated in this residual air part, might produce pneumatosis.

In addition, battery unit number, fluid injection nozzle number are also suitably determined to get final product.For example, also can make battery unit 10a and fluid injection nozzle 4b is identical quantity, uses fixed nozzle, the system that omit movable mechanism, this movable mechanism is controlled etc., thus reduce the system failure.In addition, also depend on the size in fluid injection chamber, both can be with a plurality of filling box settings planar, also a plurality of filling boxes can be carried out three-dimensional stacked mode and arrange to separate suitable interval, aforesaid way can also be made up.Filling box 3 can be both also the mode of as shown in Figure 4 a plurality of battery unit 10a being lined up 1 row, can be also the mode of multiple row that a plurality of battery unit 10a are lined up.In addition, filling box 3 can be both box-shaped as shown in Figure 4, can be also circular.In the situation that filling box 3 is circular, a plurality of battery unit 10a are arranged in order on radial direction and get final product.

As mentioned above, from #1 fluid injection step to #4 fluid injection step, why the reservoir quantity of each step reduces gradually, and this is that the reservoir quantity that electrolyte 20 can soak into also tails off gradually because need to further soak into into towards central portion from the periphery of electrode group 21 ' along with the fluid injection step goes on.Therefore, in the fluid injection operation of above-mentioned present embodiment, after (electrolyte content of regulation) carried out fluid injection with the regulation reservoir quantity, sizable part of the central portion of the barrier film of electrode group 21 ' also still was in fluid injection state not yet (with reference to Fig. 5 (a) → (b) → (d ')).On the other hand, in the fluid injection operation of the preferred mode of present embodiment, by implement the 2nd fluid injection operation as next process after the 1st fluid injection operation of this operation, significantly shortened the time that regulation reservoir quantity (electrolyte content of regulation) has been soaked in fluid injection.And can also be till the central portion of the barrier film that forms electrode group 21 ' after fluid injection the fluid injection state of fluid injection fully basically.(contrast with reference to until the state that soaks into of (a) → (b) → (c) → (d) of Fig. 5 and until (a) → (b) of Fig. 5 → state that soaks into of (d ')).

The 2nd fluid injection operation

In the preferred mode of present embodiment, as the 2nd fluid injection operation, after boosting to than the high pressure of above-mentioned pressure (pressure that forces down than atmosphere), this pressure (pressure after boosting) is kept the constant time and with the remainder fluid injection (with reference to (a)～(j), Fig. 6 of Fig. 5) of the regulation reservoir quantity (electrolyte content of regulation) of above-mentioned electrolyte in making fluid injection chamber 2.

Particularly, the valve 6a with gas introduction tube line 6 opens by control part 7, to fluid injection chamber 2 interior importing gases, boosts to than the high pressure of the above-mentioned pressure in fluid injection chamber 2 (pressure that forces down than atmosphere).By carrying out this operation, the interarea 21a side of electrode group 21 ' becomes the state that soaks into of Fig. 5 (c) from the state that soaks into of Fig. 5 (b), can't see large variation.Can say that this is: owing to there is no during this period fluid injection electrolyte 20, so be not impregnated into the required electrolyte content of central portion, the state that soaks into of barrier film is also that central portion still keeps white constant, can not produce large variation.

After boosting to than the high pressure of above-mentioned pressure (pressure that forces down than atmosphere), close the valve 6a of gas introduction tube line 6 and this pressure (pressure after boosting) is kept the constant time.During this period, via the peristome 29a of the upper section of packaging body 29, from electrolyte supply pipeline 4 by fluid injection nozzle 4b with (among Fig. 5 (a)～(j), Fig. 6 minute 3 times) fluid injection at every turn marginally several times of the remainder of the regulation reservoir quantity (electrolyte content of regulation) of electrolyte 20.Particularly, as shown in the fluid injection curve of Fig. 5 (a)～(j), Fig. 6, as can be known: will stipulate reservoir quantity (electrolyte content of regulation) electrolyte 20 be about 40% remainder fluid injection.Through this operation, can make electrolyte 20 be impregnated into the central portion of the interarea 21a side of electrode group 21 '.In addition, by stipulating all fluid injections of reservoir quantity (electrolyte content of regulation), will be injected into the state that liquid level becomes more top than the upper surface of electrode group 21 '.In addition, even if will stipulate that all fluid injections of reservoir quantity (electrolyte content of regulation), liquid level are also than the upper surface state on the lower of electrode group 21 ', it is the state of fluid injection deficiency, in charge and discharge process, the part of electrode, the part of barrier film can become drying regime, might cause battery performance to reduce.Can think that its reason is: because the part of electrolyte is dispersed in the fluid injection process, can not be with desired electrolyte content fluid injection in the battery unit 10a etc.Therefore, in this case, being injected into liquid level by the fluid injection of further carrying out electrolyte 20 becomes comparatively more desirable than the top state in the upper surface of electrode group 21 '.

As shown in Fig. 5 (d), as can be known: at the complete time point of this operation, electrolyte 20 has been impregnated into the central portion of the interarea 21a side of electrode group 21 ', and it is still white that the state that soaks into of barrier film also only has the part of central portion, can fully soak into.Its reason is: although make owing to importing gas that pressure in fluid injection chamber 2 is instantaneous rises to the pressure higher than above-mentioned pressure, the inside of electrode group 21 ' is still to be evacuated and post-decompression state.Therefore, produce pressure differential between can be in the inside of the electrode group 21 ' of battery unit 10a and fluid injection chamber 2.Namely, because the inside of electrode group 21 ' is higher vacuum state (decompression state), so by with electrolyte 20 (in Fig. 5 (a)～(j), Fig. 6 minute 3 times) fluid injection at every turn marginally several times, electrolyte will be impregnated into rapidly the central portion (being inhaled into) of electrode group 21 ' under the effect of this negative pressure.Its result, the impregnability of electrolyte improves, and can shorten the fluid injection time.On the other hand, as can be known: the decompression state when keeping the 1st fluid injection operation constant and do not boost to than the high pressure of this pressure but with electrolyte 20 (in the situation that always being divided into 7 times in Fig. 5 (a)～(j)) fluid injection at every turn marginally several times until the A of the zone circle shown in (a)～(j) of Fig. 5 order, as the state that soaks into of Fig. 5 (d '), to the not progress of soaking into almost of central portion, result is in the residual larger part of not yet soaking into of central portion.

In addition, in the situation that the amount of electrolyte 20 not as the needed amount of cell coated with film 10, can further repeat this operation as the operation of marginally carrying out several times fluid injection at every turn.

In this operation, make half value low comparatively desirable (with reference to (a)～(j) and Fig. 6 of Fig. 5) of vacuum pressure when pressure ratio the 1st fluid injection operation of fluid injection 2 interior constant times of maintenance of chamber and atmospheric pressure sum.That is, the value of the vacuum pressure due to than the 1st fluid injection operation time the and half of atmospheric pressure sum is low, so the pressure differential of the pressure during with the 1st fluid injection operation (pressure that forces down than atmosphere) can be not excessive, can prevent electrolyte disperse (with reference to (a) of Fig. 7).But, in contrast, even too small with the pressure differential of before pressure (pressure that forces down than atmosphere), also might can not obtain sufficient impregnability as Fig. 5 (d ') and improve effect, therefore, particularly, can say to arrange to be at least comparatively ideal of the above pressure differential of 1kPa, the above pressure differential of 10kPa preferably is set, the pressure differential about 15kPa～20kPa further preferably is set.But, the preferred mode of present embodiment is not subjected to any restriction of this scope.

In addition, in this operation, on one side the pressure stage property ground in fluid injection chamber 2 is raise, Yi Bian pressure is kept the constant time in each stage and with electrolyte 20 fluid injections.In this case, also satisfy above-mentioned pressure condition more desirable.By carrying out this operation, have advantages of as follows: can promote to soak into (speed) interimly, can shorten the fluid injection time.Though not shown, this operational example is as also carrying out as follows: Yi Bian the pressure in fluid injection chamber 2 is for example raise in the mode that the pressure of the past operation plays (1) 15kPa → (2) 20kPa → (3) 25kPa interimly, Yi Bian pressure is kept the constant time in each stage and with electrolyte 20 fluid injections.At this, for example, in above-mentioned (1) stage, with the pressure hold time TA of 15kPa, during this period with electrolyte 20 marginally fluid injection at twice at every turn, boost to afterwards the pressure in above-mentioned (2) stage in the time T B shorter than time T A.Equally, in above-mentioned (2) stage, with the pressure hold time TA of 20kPa, during this period with electrolyte 20 marginally fluid injection at twice at every turn, boost to afterwards the pressure in above-mentioned (3) stage in time T B.At last, in above-mentioned (3) stage, also can be with the pressure hold time TA of 25kPa, during this period with electrolyte 20 marginally fluid injection at twice at every turn.But, the preferred mode of present embodiment is not subjected to any restriction of above-mentioned example.By making the ground rising of pressure stage property, can promote to soak into (speed) interimly, for this viewpoint, can say: if make above-mentioned (3) stage (=and front operation between stage of pressure differential maximum) in retention time and reservoir quantity (and fluid injection number of times) more than other stages, more effective.

In addition, as Fig. 5 (a)～(j), shown in Figure 6, in the 1st fluid injection operation and these two operations of Ben Di 2 fluid injection operations, electrolyte (each a small amount of) minute several is carried out fluid injection, and make the reservoir quantity of each time in this 2nd fluid injection operation how comparatively desirable than the last reservoir quantity of the 1st fluid injection operation.By carrying out this operation, pressure changes in last procedure and this operation, can increase reservoir quantity thereby become to be easy to soak into correspondingly with electrolyte in this operation, can shorten the fluid injection time.This effect is as follows: stop at last the fluid injection of the electrolyte 20 that undertaken by fluid injection nozzle 4b.Particularly, by control part 7, the drive motors of each pump 4c, valve 4d and fluid injection nozzle 4b is stopped.Can finish thus the 2nd fluid injection operation, can realize that the fluid injection of the electrolyte of present embodiment soaks into the preferred mode of method.

As described above, in the preferred mode of method is soaked in the fluid injection of the electrolyte of present embodiment, owing to keeping the constant time, so can utilize pressure differential to promote to soak into, can shorten the fluid injection time under higher pressure.In addition, lax even if the laminated film of use softness as the encapsulating material of cell coated with film, can not produce between lamination surface yet, in the time of can also suppressing injecting electrolytic solution, barrier film produces fold.

Operation after the fluid injection operation

Reprocessing (1)

Present embodiment is characterised in that, as Fig. 5 (a)～(j), shown in Figure 6, as reprocessing (1), after above-mentioned fluid injection operation, the sealing above-mentioned peristome before, add the decompression operation, that is, the pressure when becoming the exert pressure in the fluid injection chamber than above-mentioned fluid injection operation is high, then reduces pressure.Afterwards, go up to the atmospheric operation of boosting by make the pressure in fluid injection chamber 2 after the closing step of having carried out closed peristome 29a, with injecting electrolytic solution, can access the cell coated with film 10 that is further soaked into.Illustrate and add the decompression operation.

Add the decompression operation

In adding the decompression operation, after above-mentioned fluid injection operation, before closed peristome 29a, add the decompression operation, that is, the pressure when becoming the exert pressure in fluid injection chamber 2 than above-mentioned fluid injection operation is high, then reduces pressure.Thus, due to after fluid injection, the sealing before add decompression, so can promote to soak into.Because being adds decompression after fluid injection, so have advantages of as follows: electrolyte 20 is isolated film and keeps, and also can not cause and disperses even add decompression.

For example, as Fig. 5 (a)～(j), shown in Figure 6, after above-mentioned fluid injection operation before (with reference to Fig. 5 (d), (d ')), closed peristome 29a, the pressure when becoming the exert pressure in fluid injection chamber 2 than above-mentioned fluid injection operation (the 1st fluid injection operation and the 2nd fluid injection operation that comprise above-mentioned preferred mode) is high.This operation is carried out as follows: the valve 6a with gas introduction tube line 6 opens by control part 7, gas is imported in fluid injection chamber 2 pressure that the pressure when being pressurized to than above-mentioned fluid injection operation in fluid injection chamber 2 is high (with reference to the boost phase of T1～T2 of Fig. 5 (a)～(j), Fig. 6).

In this operation, when pressurizeing, as Fig. 5 (a)～(j), shown in Figure 6, be pressurized to atmospheric pressure comparatively desirable.This be because: by being pressurized to atmospheric pressure, can obtain and the pressure during fluid injection between larger pressure differential, can promote to soak into.In addition, owing to only need stopping vacuumizing getting final product in order to go back up to atmospheric pressure, also has advantages of simple structure.By carrying out this operation, the interarea 21a side of electrode group 21 ' becomes the state that soaks into of Fig. 5 (d ') → (e ') and even becomes the state that soaks into of Fig. 5 (d) → (e), thinks to have promoted to soak at central portion.In addition, in the situation that adopted the variation of above-mentioned fluid injection operation, as the state that soaks into of Fig. 5 (e), the electrolyte 20 of institute's fluid injection has been impregnated into electrode group 21 ' inside, as Fig. 5 (a)～(j), shown in Figure 6, even carry out sharply pressurization (boosting), the electrolyte 20 that soaks into can not disperse yet, can go up at short notice to atmospheric pressure, can help to shorten the fluid injection operation.

Until the A point of the zone circle shown in (a)～(j) of Fig. 5 be maintained under the constant state of the pressure that forces down than atmosphere, after with electrolyte 20 fluid injections, the atmospheric pressure that the B that makes pressure in fluid injection chamber 2 go back up to the zone circle shown in (a)～(j) of Fig. 5 is ordered, in this case, become the state that soaks into of Fig. 5 (e ').Namely, as can be known: large variation does not occur in the state that soaks into of the Fig. 5 of ordering from the A of the zone circle shown in Fig. 5 (a)～(j) (d '), fully do not promote that electrolyte 20 does not soak into to central portion, becoming has a larger result of not yet soaking into part central portion is residual.

And, as Fig. 5 (a)～(j), shown in Figure 6, when pressurizeing, pressure is kept the constant time comparatively desirable (with reference to the atmospheric stage of maintenance in during the TC of T2～T3 of Fig. 5 (a)～(j), Fig. 6).By when pressurizeing, pressure being kept the constant time, can promote to soak into.By carrying out this operation, the interarea 21a side of electrode group 21 ' becomes the state that soaks into of Fig. 5 (f) from the state that soaks into of Fig. 5 (e), (e '), think to have promoted significantly electrolyte soaking at central portion.This can be described as: due to pressurized in electrode group during this period 21 ', so can obtain and the pressure during fluid injection between larger pressure differential, promoted significantly the electrolyte 20 of institute's fluid injection to soak into to central portion.

In this operation, after carrying out above-mentioned pressurization, then the pressure in fluid injection chamber 2 are reduced pressure.When reducing pressure, the lower pressure of the pressure of decompression to than the fluid injection of above-mentioned fluid injection operation (the 1st fluid injection operation and the 2nd fluid injection operation that comprise above-mentioned preferred mode) time is ideal comparatively.This operation is carried out as follows: by control part 7, drive the vacuum pump 5b of exhaust line 5 under the state of having opened valve 5a, make fluid injection chamber 2 interior decompressions (the lower pressure of pressure when preferred decompression is arrived than the fluid injection of above-mentioned fluid injection operation).The vacuum degree that has reached regulation is valve-off 5a afterwards.In this operation, owing to reducing pressure again after pressurization, and the lower pressure of pressure owing to preferably reducing pressure into again than fluid injection after pressurization, so have advantages of as follows: further condensing and further infiltration in the time of can making electrolyte 20 than fluid injection.At this moment, as can be known: as the state that soaks into of Fig. 5 (g), make the condensing and further infiltration (soaking into) of electrolyte 20 to electrode group 21 ' inside, promote electrolyte 20 to be impregnated into the central portion of barrier film, the still unsoaked white portion of central portion is further reduced.In addition, as shown in Fig. 5 (a)～(j), the lower pressure of pressure when even sharply decompression is arrived than fluid injection, electrolyte 20 boilings that also can suppress to soak into, therefore, neither can cause electrolyte to disperse, can reduce pressure at short notice again, by adding the decompression operation and can help significantly to shorten and make electrolyte soak into the needed time after fluid injection electrolyte in present embodiment.

In addition, in this operation, comparatively it is desirable to: in pressurization and when decompression, respectively pressure is kept the constant time, and the retention time of the pressure of the retention time of the pressure when making pressurization during than decompression is long.Its reason is: because when pressurization makes and soak into progress, so the retention time of the pressure when making this pressurization is longer, can promote to soak into.Particularly, as Fig. 5 (a)～(j), shown in Figure 6, as can be known: when pressurization, keep atmospheric pressure in during the TC of T2～T3, when decompression, during this TD shorter than TC of T4～T5 in the pressure low pressure of maintenance during than fluid injection.Pressure hold time when the pressure hold time ratio during pressurization reduces pressure is long.

And, in this operation, the circulation of repeatedly pressurizeing and reducing pressure comparatively desirable (example that 3 circulations have been carried out in expression in Fig. 5 (a)～(j), Fig. 6).Owing to carrying out a plurality of circulations, so can further promote to soak into.Particularly, as can be known: carry out a plurality of circulations the state that respectively soaks into of the Fig. 5 when (h) of the Fig. 5 when (g) of the Fig. 5 the during decompression of (e) of the Fig. 5 by from the pressurization of the 1st circulation time the, (f) that keep the Fig. 5 after the constant time, the 1st circulation, the pressurization of the 2nd circulation, the pressurization of the 3rd circulation (i), can more promote soaking into of electrolyte.

In the process operations of above-mentioned reprocessing (1), by carry out successively following closing step, the operation of boosting after operation is reduced pressure in above-mentioned adding, can access the cell coated with film 10 that (production) fluid injection is soaked into electrolyte.In addition, in reprocessing (1), not under the state of the pressure after fluid injection, but under the state of the pressure after keeping adding the decompression operation, perhaps reduce pressure in the scope that electrolyte does not seethe with excitement and arrived under the state of lower pressure (high vacuum state), peristome 29a is sealed (sealing, sealing) by thermal welding.Afterwards, boost and just can obtain having become from the state that soaks into of Fig. 5 (i) battery unit of the state that soaks into of Fig. 5 (j).

Closing step

In closing step, above-mentioned add the decompression operation after, keeping under the constant state of this pressure (pressure of the time point of the C of the zone circle of Fig. 5 (a)～(j)), perhaps decompression (high vacuum state) under the state of lower pressure in the scope that electrolyte does not seethe with excitement, by thermal welding with peristome 29a sealing (sealing, sealing).In the latter case, by control part 7, drive under the state that valve 5a is opened exhaust line 5 vacuum pump 5b and in the scope that electrolyte does not seethe with excitement with fluid injection chamber 2 interior decompressions to lower pressure (high vacuum state).Having reached after the vacuum degree of regulation is valve-off 5a.Next, use thermo-compressed (welding) parts (not shown) be located in fluid injection chamber 2, by thermal welding, peristome 29a sealing (sealing, sealing) is got final product.

But, after first charge-discharge the time when initial charge (particularly), have in this distinctive phenomenon of the many gas of the interior generation of cell coated with film 10, just can find to produce hardly such gas when the 2nd later discharging and recharging.Therefore, in this closing step, mode with the part that keeps peristome is carried out thermal welding and seals, and use the suitable dismounting such as clip closure member freely with the peristome sealing (temporary enclosed) that keeps become to open and close place after freely state comparatively desirable.And, carried out pulling down after first charge-discharge the closure member such as this clip and made the peristome opening that keeps in rear operation, with many air scavenge of cell coated with film 10 interior generations after cell coated with film 10 outsides (for example, after decompression is removed), by thermal welding the most at last this peristome seal reliably (sealing, sealing) comparatively desirable.

The operation of boosting

After closing step, go up to the atmospheric operation of boosting by making the pressure in fluid injection chamber 2, can access the cell coated with film 10 that (production) fluid injection is soaked into electrolyte 20.Specifically, by control part 7, the valve 6a of gas introduction tube line 6 is opened, to fluid injection chamber 2 interior importing gases, the pressure in fluid injection chamber 2 are gone up to atmospheric pressure.Thus, method is soaked in the fluid injection that can complete the electrolyte 20 that the fluid injection soakage device 1 that utilizes present embodiment carries out.By carrying out this operation, the interarea 21a side of electrode group 21 ' becomes the state that soaks into of Fig. 5 (j) from the state that soaks into of Fig. 5 (i), but two kinds soak into state and have all promoted to soak into until central portion, so the state that soaks into of barrier film is also can find white portion hardly at central portion, the state that soaks into of barrier film is also that central portion still keeps white constant, can say large variation does not occur.

Reprocessing (3)

And, in the present embodiment, as Fig. 5 (a)～(j), shown in Figure 6, as reprocessing (3), the decompression operation after the fluid injection of the pressure that the pressure in the time of also can carrying out after above-mentioned fluid injection operation reducing pressure the pressure in fluid injection chamber 2 than above-mentioned fluid injection operation is low.Afterwards, carry out as required with reprocessing (1) same add the decompression operation, carry out closing step, the boost operation same with reprocessing (1), also can access thus the cell coated with film 10 that is further soaked into.

Decompression operation after fluid injection

In decompression operation after fluid injection, in above-mentioned fluid injection operation (comprising above-mentioned preferred mode) afterwards, the low pressure of pressure when reducing pressure the pressure in fluid injection chamber 2 than above-mentioned fluid injection operation.The low pressure of pressure owing to reducing pressure the pressure in fluid injection chamber 2 than fluid injection is so have advantages of in the time of can making electrolyte than fluid injection further condensing and further infiltration.Particularly, as representing with hollow thick arrow in Fig. 5 (a)～(j), it is comparatively desirable that the pressure in Fig. 5 (g) (peak suction after fluid injection) is depressurized to the pressure lower than the pressure in Fig. 5 (b) (peak suction during fluid injection).In (a)～(j) of Fig. 5, the pressure low pressure of (g) decompression that both can be from Fig. 5 (d ') to Fig. 5 to than the fluid injection operation time, the low pressure of pressure when also can (g) from Fig. 5 (d) to Fig. 5 reducing pressure than the fluid injection operation.The preferred low pressure of pressure to than the fluid injection operation time from (g) decompression of (f) → Fig. 5 of Fig. 5 (d) or (d ') → Fig. 5 (e) or (e ') → Fig. 5.The low pressure of pressure when particularly preferably utilizing (g) this solid line route through (f) → Fig. 5 of (e) → Fig. 5 of variation, (d) → Fig. 5 Fig. 5 of fluid injection operation to reduce pressure than the fluid injection operation.

In this operation, with the pressure in above-mentioned fluid injection operation (comprising above-mentioned preferred mode) be made as can not cause hinder pressure that air that electrolyte soaks into to above-mentioned electrode group expands and the pressure in the decompression operation after above-mentioned fluid injection be made as the pressure that electrolyte can not seethe with excitement comparatively desirable.Its reason is: before fluid injection is complete, air residual in electrode group 21 ' is more, so if excessively decompression will produce foam, do not soak into and can make progress (with reference to Fig. 7 (b)), therefore, be made as the pressure of having considered this point, after fluid injection is complete, be made as and considered to make the boiling point of electrolyte to become the pressure of processing temperature, rather than considered it is the pressure of residual air.In addition, as the pressure that can not cause the air expansion that obstruction electrolyte soaks into, as shown in Fig. 7 (a), produce, the pressure that can carry out that soaks into of electrolyte is got final product so long as suppress foam.In the situation that surpass this pressure, can regard producing tempestuously foam as shown in Fig. 7 (b), the situations such as electrolyte disperses occur and cause the pressure that hinders the air expansion that electrolyte soaks into as.In addition, the temperature in the fluid injection chamber after complete to fluid injection from the fluid injection process need not to manage especially, can implement under the room temperature scope of 0 ℃～40 ℃ (roughly) state.Therefore, what is called has considered that the processing temperature of fluid injection after complete is that the pressure of processing temperature that is no more than the boiling point of electrolyte can be also the pressure (high vacuum state) of C of zone circle of Fig. 5 (a)～(j).As can be known: under the state that soaks into of Fig. 5 of the time point of the C of the zone circle of Fig. 5 (a)～(j) (g), also do not find the boiling of electrolyte, satisfy above-mentioned necessary condition.That is, can say: so long as the pressure in Fig. 5 (a)～(j), the scope that is pressed onto peak suction (pressure during decompression after the fluid injections such as C of the zone circle of Fig. 5 (a)～(j)) from atmosphere shown in Figure 6 just satisfies above-mentioned necessary condition.

In addition, in this operation, as Fig. 5 (a)～(j), shown in Figure 6, after above-mentioned fluid injection operation, carry out this operation before, the pressure in fluid injection chamber 2 can be in advance pressurized.Be pressurized to atmospheric pressure comparatively desirable when pressurization.This be because: owing to being pressurized to atmospheric pressure, thus can obtain and the pressure during fluid injection between larger pressure differential, can promote to soak into.In addition, also because only need stop vacuumizing getting final product in order to go back up to atmospheric pressure, so simple in structure.By carrying out this operation, in the situation that pressurize after preferred fluid injection operation, the interarea 21a side of electrode group 21 ' becomes the state that soaks into of Fig. 5 (e) from the state that soaks into of Fig. 5 (d), think to have promoted to soak at central portion.This can be described as: due to pressurized in electrode group during this period 21 ', so can obtain and the pressure of fluid injection between larger pressure differential, promoted the electrolyte 20 of institute's fluid injection to soak into to central portion.In addition, as Fig. 5 (e), electrolyte 20 after fluid injection has been impregnated into electrode group 21 ' inside, as Fig. 5 (a)～(j), shown in Figure 6, even pressurization (boosting) sharp, the electrolyte 20 that soaks into can not disperse yet, and can go up at short notice to atmospheric pressure, can help to shorten the fluid injection operation.

And, as Fig. 5 (a)～(j), shown in Figure 6, after the fluid injection operation during pressurization (boosting) in advance, pressure is kept the constant time comparatively desirable (with reference to the atmospheric stage of maintenance during the TC of T2～T3 of Fig. 5 (a)～(j), Fig. 6).When pressurization, by pressure is kept the constant time, can promote to soak into.By carrying out this operation, the interarea 21a side of electrode group 21 ' becomes the state that soaks into of (f) of (e ') → Fig. 5 of Fig. 5 (e) or Fig. 5, thinks to have promoted to soak at central portion.This can be described as: due to pressurized in electrode group during this period 21 ', so can obtain and the pressure during fluid injection between larger pressure differential, promoted the electrolyte 20 of institute's fluid injection to soak into to central portion.

In decompression operation after fluid injection in the present embodiment, after pressurizeing as required as described above, the low pressure of pressure when reducing pressure the pressure in fluid injection chamber 2 than above-mentioned fluid injection operation.But, self-evident, after fluid injection, can not pressurize yet, but the low pressure of pressure when reducing pressure the pressure in the fluid injection chamber than above-mentioned fluid injection operation.

The improvement of the fluid injection of electrolyte

Next, method is soaked in the fluid injection of using Fig. 4 to describe the electrolyte 20 in present embodiment.Electrolyte 20 has been impregnated into cell device 21 from the stacked side 21b side of electrode group 21 '.The cell device 21 of rectangular shape has 4 stacked side 21b, considers from the aspect that shortens the fluid injection time and prevent from making laminated film packaging body 29 to produce fold, importantly: effectively utilize all above-mentioned 4 stacked side 21b and carry out the fluid injection of electrolyte 20.Therefore, also can make fluid injection nozzle 4b fluid injection as follows: often carry out 1 fluid injection, just on one side the end from peristome 29 marches to the other end, Yi Bian the electrolyte 20 that makes ormal weight distributes equably from the end to end of peristome 29.Can also carry out as follows fluid injection: use the top can under to the fluid injection nozzle 4b that tilts to the left and right 45 ° of left and right, top (movably), just can make the electrolyte 20 of ormal weight carry out fluid injection in the mode that the end to end from peristome 29 distributes equably often to carry out 1 fluid injection.But, present embodiment is not subjected to any restriction of above-mentioned example, can suitably select the existing fluid injection of fluid injection equably to soak into method.

As described above, adopt the cell coated with film of present embodiment manufacture method and device thereof, especially soak into method and the device thereof of electrolyte to cell coated with film unit fluid injection, can obtain following action effect.(1) due to after fluid injection, before sealing, the high pressure of pressure when being pressurized to than fluid injection, then reduce pressure is so can promote significantly electrolyte to soak into.In addition, because being adds and subtracts pressure after fluid injection, keep so electrolyte is isolated film, even add decompression, also can not cause and disperse.In addition, (2) when carrying out above-mentioned pressurization, by being pressurized to atmospheric pressure, can obtain and the pressure during fluid injection between larger pressure differential, can promote to soak into.Owing to only need stopping vacuumizing getting final product in order to go back up to atmospheric pressure, so simple in structure.(3) when reducing pressure, due to the pressure low pressure (inlet side) of decompression to than fluid injection the time, so further condensing and further infiltration in the time of can making electrolyte than fluid injection.(4) when above-mentioned pressurization and decompression, pressure is kept the constant time, and make the retention time of the pressure when pressurizeing longer than the retention time of decompression, because when pressurization soaks into and makes progress, thus longer by the retention time that makes the pressure when pressurizeing, can promote to soak into.(5) circulation by repeatedly pressurizeing and reducing pressure can further promote to soak into.

Description of reference numerals

1, the fluid injection soakage device of electrolyte; 2, fluid injection chamber; 3, filling box; 3a, press fixture; 4, electrolyte supply pipeline; The container of 4a, electrolyte; 4b, fluid injection nozzle; Electrolyte supply pump on 4c, electrolyte supply pipeline; Switching valve on 4d, electrolyte supply pipeline or fluid flow are adjusted valve; 5, exhaust line; 5a, exhaust are with opening and closing valve; The vacuum pump that 5b, exhaust are used; 6, gas introduction tube line; Switching valve on 6a, gas introduction tube line or gas flow are adjusted valve; The container of 6b, gas; 7, control part; 10, cell coated with film (thin-film package electric device); 10a, cell coated with film unit; 11, negative electrode collector; 11a, negative pole (coming from collector body) epitaxy part; 11b, negative pole curren-collecting part; 12, positive electrode collector; 12a, positive pole (coming from collector body) epitaxy part; 12b, anodal curren-collecting part; 13, negative electrode active material layer; 14, negative plate (=negative pole); 15, positive electrode active material layer; 16, positive plate (=positive pole); 17, dielectric substrate (soaking into the barrier film that electrolyte is arranged); 19, monocell layer; 20, electrolyte; 21, cell device; The interarea of 21a, cell device; The stacked side of 21b, cell device; 25, negative pole corbel back slab; 27, anodal corbel back slab; 29, laminated film packaging body; The peristome of 29a, laminated film packaging body; The bottom of 29b, laminated film packaging body; The recess of 29e, laminated film packaging body; The closure of 29f, laminated film packaging body or mouth-sealed portion.

Claims

1. the manufacture method of a thin-film package electric device, wherein,

The manufacture method of this thin-film package electric device comprises following operation:

The decompression operation, in the fluid injection chamber of bag-shaped laminated film packaging body, decompression is to the pressure that forces down than atmosphere with being provided with, and this bag-shaped laminated film packaging body has peristome, and has taken in the electrode group, and this electrode group has and clips positive pole and the negative pole that separating film layer gathers into folds;

The fluid injection operation, after above-mentioned decompression operation, with the regulation reservoir quantity electrolyte from above-mentioned peristome to packaging body in fluid injection;

Add the decompression operation, after above-mentioned fluid injection operation, before the above-mentioned peristome of sealing, the pressure with the exert pressure in the fluid injection chamber to than above-mentioned fluid injection operation the time is high, then reduces pressure.

2. the manufacture method of thin-film package electric device according to claim 1, is characterized in that,

Above-mentioned add the decompression operation in, when pressurizeing, be pressurized to atmospheric pressure.

3. the manufacture method of the thin-film package electric device of described year according to claim 1 and 2, is characterized in that,

Add the decompression operation above-mentioned, when reducing pressure, the pressure low pressure of decompression to than the fluid injection of fluid injection operation the time.

4. the manufacture method of wantonly 1 described thin-film package electric device according to claim 1～3, is characterized in that,

Add the decompression operation above-mentioned, when pressurizeing, pressure is kept the constant time, when reducing pressure, pressure is kept the constant time, the retention time of the pressure during than decompression retention time of the pressure during pressurization is long.

5. the manufacture method of wantonly 1 described thin-film package electric device according to claim 1～4, is characterized in that,

Above-mentioned add the decompression operation in, the circulation of repeatedly pressurizeing and reducing pressure.

6. the manufacture method of wantonly 1 described thin-film package electric device according to claim 1～5, is characterized in that,

In above-mentioned fluid injection operation, be maintained under the constant state of post-decompression pressure in the fluid injection chamber, with at least a portion of the electrolyte of regulation reservoir quantity from above-mentioned peristome to packaging body in fluid injection.

7. the manufacturing installation of a thin-film package electric device, is characterized in that,

The manufacturing installation of this thin-film package electric device has:

The pressure adjustment component, it is used for the pressure in the fluid injection chamber that is provided with bag-shaped laminated film packaging body is adjusted, this bag-shaped laminated film packaging body has peristome, and has taken in the electrode group, and this electrode group has and clips positive pole and the negative pole that separating film layer gathers into folds;

The fluid injection parts, it is used for electrolyte is injected in packaging body from above-mentioned peristome;

Control assembly, it carries out following control: utilize above-mentioned pressure adjustment component to make in the fluid injection chamber decompression to the pressure that forces down than atmosphere, after decompression, utilize the fluid injection in the packaging body of electrolyte that above-mentioned fluid injection parts make the regulation reservoir quantity, afterwards, before the above-mentioned peristome of sealing, the pressure to than above-mentioned fluid injection the time is high with the exert pressure in the fluid injection chamber to utilize above-mentioned pressure adjustment component, then reduces pressure.