METHOD FOR PRODUCING A DRY FILM, ROLLING DEVICE, DRY FILM, AND SUBSTRATE COATED WITH THE DRY FILM
20240274784 ยท 2024-08-15
Assignee
- Fraunhofer-Gesellschaft zur Foerderung der angewandten Forschung e.V. (Muenchen, DE)
- Technische Universitat Dresden (Dresden, DE)
Inventors
- Holger Althues (Dresden, DE)
- Sebastian TSCHOECKE (Dresden, DE)
- Benjamin Schumm (Dresden, DE)
- Stefan Kaskel (Dresden, DE)
- Christian Girsule (Dresden, DE)
- Daniel Jordan (Dresden, DE)
- Kay Schoenherr (Dresden, DE)
Cpc classification
Y02P70/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01G11/28
ELECTRICITY
H01M4/525
ELECTRICITY
H01G11/50
ELECTRICITY
H01M4/505
ELECTRICITY
B29C43/58
PERFORMING OPERATIONS; TRANSPORTING
Y02E60/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M4/1391
ELECTRICITY
B29C43/28
PERFORMING OPERATIONS; TRANSPORTING
H01M4/58
ELECTRICITY
B29K2705/00
PERFORMING OPERATIONS; TRANSPORTING
H01M4/485
ELECTRICITY
B29C2043/5833
PERFORMING OPERATIONS; TRANSPORTING
B29C43/32
PERFORMING OPERATIONS; TRANSPORTING
H01M4/663
ELECTRICITY
B29L2031/3468
PERFORMING OPERATIONS; TRANSPORTING
B29C43/006
PERFORMING OPERATIONS; TRANSPORTING
B29K2427/18
PERFORMING OPERATIONS; TRANSPORTING
H01M10/0525
ELECTRICITY
International classification
H01M4/485
ELECTRICITY
H01M4/505
ELECTRICITY
H01M4/525
ELECTRICITY
H01M4/58
ELECTRICITY
H01M4/62
ELECTRICITY
Abstract
The invention relates to a method for producing dry film (3), wherein a dry powder mixture is processed into the dry film (3) by a rolling device comprising a first roller (2a) and a second roller (2b). The first roller (2a) has a higher circumferential rotational peripheral speed than the second roller (2b), and the dry film (3) is placed on the first roller (2a) wherein the rotational peripheral speed of the first roll to the rotational peripheral speed of the second roll of 10:9 to 10:1 is maintained.
Claims
1-22. (canceled)
23. A method for producing a dry film, in which a dry powder mixture is processed into the dry film by a rolling device having a first roll and a second roll, wherein the first roll has a higher rotational peripheral speed than the second roll and the dry film is supported on the first roll, wherein a ratio of the rotational peripheral speed of the first roll to the rotational peripheral speed of the second roll of 10:9 to 10:1 is maintained.
24. The method as claimed in claim 23, wherein a ratio of the rotational peripheral speed of the first roll to the rotational peripheral speed of the second roll of 10:5 to 10:1 is maintained.
25. The method as claimed in claim 23, wherein the dry powder mixture contains a material suitable for forming fibrils upon shearing.
26. The method as claimed in claim 25, wherein by shearing in a nip, the dry film is formed having fibrils formed anisotropically in the running direction of the first roll and of the second roll.
27. The method as claimed in claim 23, wherein the dry powder mixture contains a transition-metal oxide and/or sulfur.
28. The method as claimed in claim 23, wherein the first roll is provided with an adhesion-enhancing modification, and/or the second roll is provided with an adhesion-reducing modification.
29. The method as claimed in claim 23, wherein the dry film is applied to a substrate, wherein prior to lamination of the dry film on the substrate, the substrate is provided with thermoplastic primer; and/or the substrate consisting of a metal wire mesh, a nonwoven fabric, or an aluminum foil with an applied carbon primer is used.
30. The method as claimed in claim 23, wherein the dry film is formed by the first roll and the second roll with a linear force, acting in a nip between the rolls, of 100 N/cm to 10 kN/cm; and/or with a thickness less than 500 ?m.
31. A dry film produced with the method of claim 25, wherein the fibrils have a length of 0.1 ?m to 1000 ?m.
32. The dry film as claimed in claim 31, wherein the dry film is applied to a substrate.
33. An electrochemical store element or electrochemical converter, which has a dry film as claimed in claim 31.
34. A rolling device, wherein the rolling device has a first calendar roll and a second calendar roll, wherein a dry powder mixture is introduced into a nip between the first calender roll and the second calender roll, wherein the first and the second calender rolls are configured or driven such that the first calender roll has a higher rotational peripheral speed than the second calender roll, and such that the first and the second calender rolls respectively have an opposite direction of rotation, wherein the rolling device is configured to maintain a ratio of the rotational peripheral speed of the first calendar roll to the rotational peripheral speed of the second calendar roll of 10:9 to 10:1.
35. The rolling device as claimed in claim 34, wherein the rolling device is configured to maintain a ratio of the rotational peripheral speed of the first calendar roll to the rotational peripheral speed of the second calendar roll of 10:5 to 10:1.
36. The rolling device as claimed in claim 34, wherein the dry powder mixture contains a material suitable for forming fibrils upon shearing.
37. The rolling device as claimed in claim 36, wherein, by shearing in the nip, the dry film is formed having fibrils formed anisotropically in the running direction of the first calendar roll and of the calendar second roll.
38. The rolling device as claimed in claim 34, wherein the dry powder mixture contains a transition-metal oxide and/or sulfur.
39. The rolling device as claimed in claim 34, wherein the first calendar roll is provided with an adhesion-enhancing modification, and/or the second calendar roll is provided with an adhesion-reducing modification.
40. The rolling device as claimed in claim 34, wherein the dry film is applied to a substrate, wherein prior to lamination of the dry film on the substrate, the substrate is provided with thermoplastic primer; and/or the substrate consisting of a metal wire mesh, a nonwoven fabric, or an aluminum foil with an applied carbon primer is used.
Description
DESCRIPTION OF THE DRAWINGS
[0033] Illustrative embodiments of the invention are represented in the drawings and are explained below with reference to
[0034]
[0035]
[0036]
DETAILED DESCRIPTION OF THE INVENTION
[0037] In
[0038] In the represented illustrative embodiment, the used dry powder exists in the premixed state and comprises 90 percent by weight Ketjenblack/sulfur (1:2 m/m), 3 percent by weight polytetrafluoroethylene (PTFE) and 7 percent by weight multi-walled carbon nanotubes (MWCNT). For a lithium ion electrode, 95 percent by weight lithium manganese oxide, 3 percent by weight a conductive additive (in this case multi-walled carbon nanotubes, MWCNT) and 2 percent by weight PTFE is typically used. In a calender nip located between the first roll 2a and the second roll 2b, a fibrillation of the dry powder mixture takes place, whereby the closed dry film 3 is produced.
[0039] The rotation speeds of the first roll 2a and of the second roll 2b lie within a range between 10:9 and 10:4, in the shown illustrative embodiment around 2:1, namely either 10 mm/s:5 mm/s or 20 mm/s:10 mm/s. In further Illustrative embodiments, depending on the parameter window and powder condition, 80 mm/s:40 mm/s can however also be used as the rotation speeds. Higher rotation speeds hereupon result in thinner dry films having a less pronounced corrugated structure or less pronounced fibrils 8, thus a lower surface roughness Ra. In the shown illustrative embodiment, the fibrils 8 have a length of, on average, 10 ?m, and are formed anisotropically in the running direction of the rolls 2a and 2b. As a result of the rotation speeds, to the powder in the nip 6, which latter, in the represented illustrative embodiment, has a width of 50 ?m but can also be between 10 ?m and 300 ?m in width, is applied a shearing force, which produces a fibrillation along the running direction. This results in a mechanical stabilization and film formation on the first roll 2a rotating at higher speed, and the formation of a free-standing film is avoided (where necessary, however, can be achieved by mechanical removal, for instance by means of a doctor blade, from the roll 2a). Instead, a dry film 3 supported on the faster roll 2a is obtained, which is of advantage, especially for dry films having a thickness less than 200 ?m, due to the limited mechanical stability.
[0040] In the represented illustrative embodiment, the first roll 2a and the second roll 2b can respectively be heated to a temperature of 100? C. Moreover, the first roll 2a can be provided with an adhesion-enhancing surface, to which the dry film 3 adheres, while the second roll 2b has a, for the dry film, adhesion-reducing surface. In the represented illustrative embodiment, an acting linear force between the first roll 2a and the second roll 2b amounts to 400 N.
[0041] By subsequent lamination to a current collector provided with thermoplastic primer or binder, the dry film 3 can be removed from the first roll 2a, and thus, for instance, an electrode produced in a solvent-free manner can be generated.
[0042] In
[0043] In the represented illustrative embodiment, the substrate 4 is fed through a further nip 7 between two first rolling devices 2a, which are arranged in mirror symmetry to one another. The two first rolls 2a, on which respectively one of the dry films 3 is run, are mutually facing, and have a further nip 7 between them so that the substrate 4 can on both sides be provided with the dry film 3, since both surfaces are respectively facing toward one of the rolls 2a. To this end, the substrate 4 is moved at a speed which precisely corresponds to the rotational peripheral speed of the two first rolls 2a. In the shown illustrative embodiment, the two rolling devices, apart from the mirror-symmetrical arrangement, are identically constructed, thus have, in particular, equal dimensions, and are operated at equal rotation speeds or rotational peripheral speeds. In further Illustrative embodiments, dry films 3 which differ from one another in terms of their composition can also be applied to the substrate 4, yet in the illustrative embodiment represented in
[0044] Moreover, the described method allows the production of an electrode with alternative current collectors as the substrate 4, for example perforated substrates with low basis weight, such as perforated metal foils or conductive fabrics. In the illustrative embodiment shown in
[0045] A continuous film production for battery electrodes for primary and secondary batteries, for example lithium ion batteries, lithium sulfur batteries, sodium sulfur batteries, solid-state batteries, supercap electrodes, electrodes for fuel cells, electrodes for electrolytic cells, electrodes for further electrochemical elements, but also filter membranes or adsorptive coatings through the use of porous particles, decorative layers, optical layers for absorption and/or layers of moisture-sensitive or solvent-sensitive materials is thus enabled.
[0046]
[0047] The described method therefore allows an electrode to be produced directly from a premixed dry film powder without additional steps for fibrillation purposes, so that also no free-standing film has to be formed. The method can be employed for a prefibrillation, in which an enhancement of the mechanical stability of the dry film is possible. Moreover, the free-standing film can be realized by detachment from the carrier roller. By the peripheral speed or the rotational peripheral speeds of the first roll 2a and the second roll 2b and of the pressing force acting in the direction of the calender nip 6 or a nip 6 between rolls, a load and density can be set. The dry film formation is realized in a self-dosing manner, the resulting layer thickness derives from the used pressing force of the two rolls 2a and 2b. Via a continuous input of a specific (process-parameter-adapted) powder quantity, for instance via the powder conveyor 1 or a feed substrate, a pre-dosing is realized. In this way, the layer thickness can likewise be influenced.
[0048] The mechanical stability of the dry film 3 is set by the pressing forces and rotation speeds (shearing rates) which are used. In comparison to free-standing films, which, given equal rotation speeds of the rolls 2a and 2b, have merely been pressed in the nip 6, the dry films 3 produced with the proposed method exhibit a considerably increased mechanical stability.
[0049] Only those features of the various embodiments which are disclosed in the Illustrative embodiments can be combined with one another and individually claimed.