Method and device for analyzing a coating on a coated material web with respect to moisture contained therein

Abstract

The invention relates to a method for analyzing a coating (1a) on a coated material web (1) with respect to moisture contained therein, wherein: a) a measuring chamber (3) is filled with measuring chamber air (AI), which has a predetermined relative humidity (HU) and a predetermined temperature (TP) at the start of a time interval (IN) which begins after the filling of the measuring chamber (3); b) the coated material web (1) is transported through the filled measuring chamber (3) and, during the transport of the material web (1), one or more parameters of the measuring chamber air (AI) comprising the relative humidity (HU') of the measuring chamber air (AI) are measured at least at the end of the time interval (IN); c) moisture information (HI) describing the water content in the coating (1a) of the coated material web (1) is determined from the change in the relative humidity of the measuring chamber air (AI) within the time interval (IN) with the aid of the predetermined temperature (TP) of the measuring chamber air (AI) and / or with the aid of a temperature (TP'), measured in step b), of the measuring chamber air (AI) at the end of the time interval (IN).

Description

[0001] P3777PC00

[0002] 1

[0003] Jagenberg Converting Solutions GmbH

[0004] Konrad-Zuse-Straße 16

[0005] 46397 Bocholt

[0006] Germany

[0007] Method and apparatus for analyzing a coating on a coated material web with regard to the moisture contained therein

[0008] The invention relates to a method and a device for analyzing a coating on a coated material web with regard to the moisture contained therein.

[0009] In numerous technical applications, material webs are coated during a manufacturing process. Often, it is necessary to keep the moisture content of the coating as low as possible. Here and in the following, moisture refers to the water content of the coating. The water content is preferably described as a relative proportion of water compared to the dry coating without water, e.g., expressed as ppm (parts per million).

[0010] To reduce residual moisture in the coating of a material web, drying systems are frequently used. The coated material web is transported through these systems and exposed to drying air. Such drying systems are used, for example, for coated material webs used in battery electrodes. P3777PC00

[0011] 2

[0012] To measure the water content of coated material webs, spectrometers are known from the prior art that determine the moisture content of the coating using light, for example in the near-infrared range. However, this spectroscopic moisture measurement is complex and expensive.

[0013] The object of the invention is to create a method and a device for analyzing a coating on a coated material web, with which the degree of moisture in the coating can be determined simply and cost-effectively.

[0014] This problem is solved by the method according to claim 1 or the device according to claim 14. Further developments of the invention are defined in the dependent claims.

[0015] In step a) of the method according to the invention, a measuring chamber is filled with chamber air, which has a predetermined relative humidity and a predetermined temperature at the beginning of a time interval that starts after the chamber is filled. The relative humidity and temperature of the chamber air at the beginning of the time interval are thus known. They can, for example, be determined or monitored by sensors in the measuring chamber. Depending on the embodiment, the beginning of the above time interval can be defined differently. For example, the time interval can begin immediately after the chamber is filled with chamber air. Furthermore, the time interval can also begin only when a temperature equilibrium has been established in the measuring chamber, i.e., from a point in time at which the temperature in the measuring chamber remains essentially constant.

[0016] In one variant, the air supplied to the measuring chamber is ambient air from the area surrounding the measuring chamber. However, it is also possible that the ambient air or air from another source is pre-conditioned to a specific relative P3777PC00.

[0017] 3

[0018] Humidity and temperature are set. The pre-conditioned air is then supplied to the measuring chamber as measuring chamber air.

[0019] In step b) of the method according to the invention, the coated material web is transported through the filled measuring chamber, and during the transport of the material web, one or more parameters of the measuring chamber air, including the relative humidity of the measuring chamber air, are measured at least at the end of the time interval. Optionally, the relative humidity of the measuring chamber air can also be measured several times during the time interval, i.e., the relative humidity of the measuring chamber air is measured not only at the end of the time interval but also before it.

[0020] In step c) of the method according to the invention, moisture information is determined from the change in the relative humidity of the measuring chamber air within the time interval, using the predetermined temperature of the measuring chamber air and / or using a temperature of the measuring chamber air at the end of the time interval measured in step b). This moisture information describes the water content in the coating of the coated material web. In one variant, the moisture information directly indicates the water content in the coating. However, the moisture information can also describe the water content in other ways, e.g., based on exceeding or falling below a threshold value, as explained below. The measured temperature of the measuring chamber air at the end of the time interval represents a corresponding (measured) parameter of the measuring chamber air.Preferably, this temperature is also measured whenever the relative humidity is measured in step b).

[0021] The method according to the invention is based on the finding that the change in the relative humidity of the measuring chamber air, which is caused by the exchange of water molecules between the measuring chamber air and the coating of the material web, allows conclusions to be drawn about the water content in the coating P3777PC00

[0022] 4. Allow to set and consequently moisture information regarding the water content in the coating can be determined.

[0023] The method according to the invention can optionally be repeated at predetermined time intervals, whereby the existing measuring chamber air is drained from the measuring chamber and the measuring chamber is refilled with measuring chamber air with a predetermined relative humidity and a predetermined temperature.

[0024] In a preferred embodiment of the method according to the invention, the temperature of the measuring chamber air remains essentially constant within the time interval. This can be achieved, for example, by a suitable selection of the beginning of the time interval or by a device for heating and / or cooling the measuring chamber air.

[0025] In a particularly preferred embodiment, the humidity information is derived from at least one sorption isotherm and / or at least one desorption isotherm. The at least one sorption isotherm or the at least one desorption isotherm represents an equilibrium state between the water content in the coating and the water content in the surrounding air at the predetermined temperature and / or the measured temperature at the end of the time interval. In this equilibrium state, no further water molecules are exchanged between the coating and the surrounding air. In the case of sorption (i.e., adsorption and possibly also absorption) of water into the coating from the surrounding air at the predetermined or measured temperature occurring before the equilibrium state is reached, the corresponding sorption isotherm describes...When the coating is re-moistened with water from the surrounding air, the dependence of the water content in the coating on the relative humidity of the surrounding air at the specified or measured temperature in equilibrium. Sorption isotherms are often also referred to as adsorption isotherms, even though absorption of water can occur alongside adsorption during sorption. The corresponding P3777PC00.

[0026] 5

[0027] The desorption isotherm describes, in the case of desorption of water from the coating into the surrounding air at the specified or measured temperature before reaching equilibrium, i.e., when water is released from the coating into the surrounding air, the dependence of the water content in the coating on the relative humidity of the surrounding air at the specified or measured temperature in the equilibrium state.

[0028] Sorption isotherms and desorption isotherms and their measurement are well known from the prior art (see, for example, publications [1] and [2]). In the embodiment of the invention described above, a sorption or desorption isotherm that has been measured or calculated in advance for the corresponding coating at the predetermined temperature of the surrounding air or at the temperature measured at the end of the time interval is used. For certain coatings, the sorption isotherm and the desorption isotherm may coincide.

[0029] In a further preferred embodiment of the method according to the invention, in step c) when the relative humidity of the measuring chamber air decreases from the predetermined relative humidity within the time interval, the water content in the coating is determined as at least part of the moisture information, which results from the sorption isotherm for the measured relative humidity of the measuring chamber air and the measured temperature of the measuring chamber air at the end of the time interval, wherein the length of the time interval is preferably chosen such that it can be assumed that the equilibrium state between the water content in the coating and the water content in the measuring chamber air has been established.This variant of the invention is used when re-moistening of the coating is observed due to a decrease in the relative humidity of the measuring chamber air, so that the dependence of the coating's water content on the relative humidity of the measuring chamber air at equilibrium is described via the sorption isotherm. P3777PC00.

[0030] 6

[0031] In a further embodiment of the method according to the invention, in step c) as the relative humidity of the measuring chamber air increases from the predetermined relative humidity within the time interval, the water content in the coating is determined as at least part of the moisture information, which results from the desorption isotherm for the measured relative humidity of the measuring chamber air and the measured temperature of the measuring chamber air (AI) at the end of the time interval, wherein the length of the time interval is preferably chosen such that it can be assumed that the equilibrium state between the water content in the coating and the water content in the measuring chamber air has been established.This variant of the invention is used when water is released from the coating into the measuring chamber air, so that the dependence of the relative humidity of the measuring chamber air on the water content in the coating is described via the desorption isotherm.

[0032] If the relative humidity of the measuring chamber air does not change from the predetermined relative humidity within the time interval, the water content can be determined according to the two methods described above, either using the sorption isotherm or the desorption isotherm. The deviations between the sorption isotherm and the desorption isotherm are generally small.

[0033] In another preferred embodiment, a threshold value for the water content in the coating is defined. This threshold value, which is, for example, between 100 ppm and 200 ppm, generally indicates the maximum permissible water content in the coating; that is, if this threshold is exceeded, the coating is not yet sufficiently dry. The specified humidity and temperature of the measuring chamber air are adjusted such that the sorption isotherm, which represents the equilibrium between the water content in the coating and the water content in the surrounding air, is determined by P3777PC00.

[0034] Section 7 describes the specified temperature for which the threshold value is determined for the specified relative humidity of the surrounding air. At least part of the moisture information is determined by stating that the water content in the coating is less than or equal to the threshold value if the relative humidity of the measuring chamber air decreases or remains constant within the specified time interval, starting from the specified relative humidity. Conversely, the water content in the coating is greater than the threshold value if the relative humidity of the measuring chamber air increases within the specified relative humidity, starting from the specified relative humidity. With this variant, the time interval can be set relatively short, as it is only necessary to detect an increase or decrease in the relative humidity of the measuring chamber air. Moisture information regarding the coating can thus be determined quickly.

[0035] Depending on the design, the time interval at the end of which the relative humidity of the measuring chamber air is measured can be defined differently. In one variant, the time interval is fixed and preferably lies between 10 seconds and 10 minutes, more preferably between 20 seconds and 1 minute.

[0036] In another embodiment, the time interval is determined variably depending on the changing relative humidity of the measuring chamber air. The time interval ends when the change in relative humidity of the measuring chamber air falls below a predefined threshold, indicating that equilibrium has been reached between the water content in the coating and the water content in the measuring chamber air. The change in relative humidity can be determined, for example, as the gradient of the humidity over time or as the difference between two humidity levels within a short period. P3777PC00

[0037] 8

[0038] In another preferred embodiment, the measuring chamber air circulates in the measuring chamber, thereby ensuring a good exchange of water molecules between the coating of the material web and the measuring chamber air.

[0039] In another preferred embodiment, the air in the measuring chamber is pressurized relative to the surrounding air. This allows for a rapid supply and removal of air from the measuring chamber to carry out the method according to the invention. Simultaneously, the overpressure within the measuring chamber ensures that no ambient air enters the chamber. Preferably, the overpressure is kept constant, which can be monitored by a suitable pressure measurement device. A constant overpressure within the measuring chamber ensures a constant air volume within the chamber.

[0040] To establish equilibrium between the water content in the coating and the water content in the measuring chamber air as quickly as possible, the dimensions of the measuring chamber should not be too large. In a preferred embodiment, the measuring chamber has a preferably constant length in the transport direction of the material web between 20 cm and 40 cm, preferably 30 cm, and / or a preferably constant height in the direction perpendicular to the plane of the material web between 3 cm and 5 cm, preferably 4 cm, and / or a preferably constant width perpendicular to the transport direction of the material web between 200 mm and 1600 mm. Preferably, the distance between the top of the measuring chamber and the material web is the same as the distance between the bottom of the measuring chamber and the material web. That is, the material web passes through the center of the measuring chamber.

[0041] A particularly preferred application of the method according to the invention is the analysis of the coating of a coated electrode material web for a battery. The electrode material can be the anode or the cathode of the battery, which is coated with a so-called slurry during the manufacturing process. P3777PC00

[0042] 9

[0043] In a further preferred embodiment, the inventive method is carried out after a drying process of the coated material web. If necessary, parameters of the drying process can be changed if the inventive method detects excessive moisture in the coating of the material web.

[0044] In addition to the method described above, the invention relates to a device for analyzing a coating on a coated material web with respect to its moisture content, wherein the device is configured to carry out the inventive method or one or more preferred variants thereof. In other words, the device includes a corresponding measuring chamber, means for filling and preferably also emptying the measuring chamber with measuring chamber air, a humidity sensor and optionally a temperature sensor for measuring the relative humidity and the temperature of the measuring chamber air, as well as an evaluation unit which determines the moisture information from the change in the relative humidity of the measuring chamber air using the predetermined temperature of the measuring chamber air and / or using the measured temperature of the measuring chamber air at the end of the time interval.

[0045] Exemplary embodiments of the invention are described in detail below with reference to the accompanying figures.

[0046] They show:

[0047] Fig. 1 shows a schematic sectional view of a measuring device for carrying out an embodiment of the method according to the invention; P3777PC00

[0048] 10

[0049] Fig. 2 shows a diagram depicting a calculated sorption isotherm and a calculated desorption isotherm for the coating of an electrode material web; and

[0050] Fig. 3 shows a diagram illustrating the change in relative humidity over time in a measuring chamber as a function of different water contents of the coating of the material web using the sorption isotherm of Fig. 2.

[0051] A variant of the inventive method is described below using a coated material web in the form of an electrode material web.

[0052] Nevertheless, the invention can also be used for any other material webs.

[0053] In Fig. 1, the material web is designated by reference numeral 1. This material web has a coating 1a on both its upper and lower surfaces, applied using a known manufacturing process for battery electrodes. Depending on the specific configuration, the material web 1 can be coated anode material or cathode material. The cathode is, for example, an aluminum foil with a coating containing lithium nickel manganese cobalt oxides as the active material. The anode is, for example, a copper foil with a coating containing graphite as the active material.

[0054] In the scenario shown in Fig. 1, the web of material 1 was calendered (i.e., compressed by rollers) and then dried in a dryer to remove unwanted water from the coating 1a of the web. Fig. 1 schematically shows the outlet 2 of the corresponding dryer. After drying, the web of material 1 is conveyed in the direction indicated by arrow T. P3777PC00

[0055] 11

[0056] To ensure that the coating la of the material web 1 is sufficiently dry and has only a low residual moisture content, the water content of the coating la is measured indirectly in a measuring chamber 3, which is largely sealed from the environment. The material web 1 is moved through this measuring chamber during transport, for which purpose rollers 6 are provided.

[0057] To measure the water content of the coating 1a, measuring chamber 3 is first purged or filled with measuring chamber air AI. At the beginning of a time interval IN, which starts after the filling process, the measuring chamber air AI has a predetermined (i.e., pre-known) relative humidity HU and a predetermined (i.e., pre-known) temperature TP. The humidity HU and the temperature TP can, for example, be measured by means of a sensor (not shown) in the supply air to measuring chamber 3. Likewise, the humidity sensor 4 or the temperature sensor 5 described below can be used to measure the predetermined relative humidity HU or the predetermined temperature TP, respectively.

[0058] The filling of measuring chamber 3 is indicated by the directional arrow PI in Fig. 1. The ambient air surrounding measuring chamber 3 can optionally be used as measuring chamber air AI, provided that the temperature and humidity of this ambient air remain constant. However, the air supplied to the measuring chamber can also be preconditioned to achieve the desired humidity and temperature. For example, the measuring chamber air AI can have a temperature of 20 °C and a relative humidity of 5%.

[0059] After filling measuring chamber 3, the measuring chamber air AI is held in the chamber for a specific period of time with a slight air circulation (approximately 5 m / s). Simultaneously, the material web 1 is transported through measuring chamber 3. Subsequently, the measuring chamber air AI is extracted from measuring chamber 3 one or more times at predetermined intervals, as by the P3777PC00.

[0060] 12

[0061] Directional arrow P2 indicates the direction of air extraction. With each extraction, the relative humidity HU' of the measuring chamber air AI is measured using a humidity sensor 4, and the temperature TP' of the measuring chamber air AI is measured using a temperature sensor 5. The time interval IN represents the period from the filling of the measuring chamber with measuring chamber air until the last measurement of the relative humidity HU' and the temperature TP'. Optionally, the temperature TP' can also be measured only during the last extraction of measuring chamber air AI at the end of the time interval IN. Preferably, the temperature of the measuring chamber air AI remains constant within the time interval IN, i.e., the predetermined temperature TP does not change and corresponds to the measured temperature TP' at the end of the time interval IN. This can be achieved, for example, by selecting the beginning of the time interval IN such that a temperature equilibrium has been established. Furthermore, if necessary,A heating and / or cooling device must be provided to keep the temperature in measuring chamber 3 constant.

[0062] The invention utilizes the fact that the measured relative humidity HU' provides information about the water content of the coating 1a. In the embodiment described here, the sorption isotherm and the desorption isotherm of the corresponding coating are used to determine this water content at the temperature TP' of the measuring chamber air AI present at the end of the time interval IN. Fig. 2 shows a diagram illustrating, by way of example, the course of a sorption isotherm ST and a desorption isotherm DT, which were calculated using a model based on equation (3.1.13) from publication [2]. The coating used is the substance with the parameters from Table 5.4 of publication [2]. This substance is used in coatings for anodes. The ambient air temperature TP' was assumed to be 22 °C.

[0063] The sorption isotherm ST of Fig. 2 represents the equilibrium state between the water content of the substance and the water content of the surrounding air in the case of prior sorption of water molecules into the substance from P3777PC00

[0064] 13 of the surrounding air (so-called sorption equilibrium). In this equilibrium state, a specific humidity level is established in the air, which, given a known air temperature, allows the calculation of the dew point temperature (TDP). This temperature is correlated with the water content (i.e., residual moisture) WC of the substance via the sorption isotherm ST. Since the temperature of the surrounding air is known, the dew point temperature corresponds to the relative humidity of the surrounding air, and vice versa. As an example, Fig. 2 shows the correlated water content of the substance of 157 ppm for a dew point temperature of 19.3 °C (corresponding to a relative humidity of 5%).

[0065] The desorption isotherm DT in Fig. 2 shows the same relationship as the sorption isotherm ST, but for the case where equilibrium is reached between the water content of the substance and the water content of the surrounding air following prior desorption of water molecules from the substance into the surrounding air. In the example of Fig. 2, the desorption isotherm DT of the substance under consideration essentially corresponds to its sorption isotherm ST.

[0066] In the embodiment shown in Fig. 1, the measured relative humidity(s) HU' is processed in an evaluation unit 7, which determines a humidity value HI from it. For this purpose, a sorption isotherm and a desorption isotherm for the temperature TP' at the end of the time interval IN and the corresponding coating 1a, such as the sorption isotherm ST and the desorption isotherm DT from Fig. 2, are stored in the evaluation unit 7. The time interval IN is selected such that the corresponding equilibrium state is reached by the end of the time interval at the latest. The evaluation unit then determines the water content of the coating as humidity value HI from the last measured relative humidity HU', which is linked to a dew point temperature. If this relative humidity is less than or equal to the predefined relative humidity HU, it uses the relationship from P3777PC00.

[0067] 14

[0068] Sorption isotherm. If this relative humidity is greater than the specified humidity HU, it uses the relationship from the desorption isotherm.

[0069] Figure 3 shows an example of the change in relative humidity RH in measuring chamber 3 over time t within the corresponding time interval IN, using the sorption isotherm ST from Figure 2. A scenario is considered in which the temperature of the measuring chamber air AI remains essentially constant during the time interval IN. An initial relative humidity HU of the measuring chamber air AI of 5% and a temperature TP of the measuring chamber air AI of 22°C were assumed. According to Figure 2, this corresponds to a sorption equilibrium for a coating water content of 157 ppm. The individual lines LH to LI4 in Figure 3 were determined based on a simulation and refer to the substance underlying the sorption isotherm ST of Figure 2, but with different water contents.Specifically, line LH corresponds to a water content of 157 ppm, line LI2 to a water content of 150 ppm, line LI3 to a water content of 100 ppm, and line LI4 to a water content of 50 ppm. As can be seen in Fig. 3, a sorption equilibrium is established for lines L2 to L4 after a certain time, because the relative humidity of the measuring chamber air AI no longer changes. For line LI, the sorption equilibrium was already present at time t = 0.

[0070] As mentioned above, the time interval IN, i.e., the time at which the relative humidity HU' is last measured according to Fig. 1, is set in the embodiment described here such that sorption equilibrium is reached. For example, the time interval IN for the scenario of Fig. 3 can be set to 50 seconds, since after this time the relative humidity RH is largely constant. The time interval IN need not be fixed, but can also be determined depending on the change over time of the measured relative humidity in measuring chamber 3. In this case, the relative humidity is measured several times within the time interval IN.

[0071] 15 measured. The end of the time interval, and thus the last measurement time, can be linked to the fact that the change in the measured relative humidity (e.g., represented by the slope of the corresponding lines from Fig. 3) is below a predetermined threshold.

[0072] In an alternative approach, the humidity information HI does not directly indicate the water content of the coating, but rather based on a threshold value. In this case, the corresponding sorption isotherm for the specified relative humidity HU and the specified temperature TP of the measuring chamber air AI provides the threshold value for the water content of the coating. If it is subsequently observed that the measured relative humidity HU' of the measuring chamber air AI decreases, it can be concluded that the water content of the coating is lower than the threshold value. Conversely, if the measured relative humidity increases, it can be concluded that the water content of the coating is higher than the threshold value. If the measured relative humidity does not change compared to the originally specified relative humidity, it can be ruled out that the water content of the coating corresponds to the threshold value.

[0073] The embodiments of the invention described above offer a number of advantages. In particular, the water content or residual moisture in the coating of a material web is determined indirectly and simply by measuring the relative humidity of the air in a measuring chamber, without requiring complex sensors for direct measurement of the water content. This method utilizes the fact that an equilibrium is established between the water content of a coating and the water content of the surrounding air after a certain period of time, whereby the water content or moisture of the coating can be inferred from the humidity of the surrounding air at equilibrium. P3777PC00

[0074] 16

[0075] Bibliography chni s

[0076] [1] M. Kosfeld et al., Journal of Energy Storage 57 (2023) 106174 [2] Jochen Eser, On the mass transport and sorption behavior in the post-drying process of electrodes for Li-ion batteries, Dissertation Karlsruhe Institute of Technology (2021)

[0077] P3777PC00

[0078] 17

[0079] Reference symbol list

[0080] 1 coated material web la coating

[0081] 2 dryer outlet

[0082] 3 measuring chambers

[0083] 4 humidity sensors

[0084] 5 Temperature sensor

[0085] 6 rolls

[0086] 7 Evaluation unit

[0087] AI measuring chamber air

[0088] HU specified relative humidity

[0089] HU' measured relative humidity

[0090] TP specified temperature

[0091] TP' measured temperature

[0092] IN time interval

[0093] T Transport direction of the material track

[0094] Pl, P2 Directional arrows

[0095] ST sorption isotherm

[0096] DT Desorption isotherm

[0097] WC water content

[0098] TDP dew point temperature

[0099] LH, LI2, LI13, LI4 lines of relative humidity

[0100] RH relative humidity t time

Claims

P3777PC00 18 Patent claims 1. Method for analyzing a coating (1a) on a coated material web (1) with respect to moisture contained therein, wherein: a) a measuring chamber (3) is filled with measuring chamber air (AI) having a predetermined relative humidity (HU) and a predetermined temperature (TP) at the beginning of a time interval (IN) starting after the measuring chamber (3) is filled; b) the coated material web (1) is transported through the filled measuring chamber (3) and, during the transport of the material web (1), one or more parameters of the measuring chamber air (AI) comprising the relative humidity (HU) are measured. 1) the measurement chamber air (AI) is measured at least at the end of the time interval (IN); c) from the change in the relative humidity of the measurement chamber air (AI) within the time interval (IN) using the predetermined temperature (TP) of the measurement chamber air (AI) and / or using a temperature (TP) measured in step b). 1 ) of the measuring chamber air (AI) at the end of the time interval (IN) a moisture information (HI) is determined which describes the water content in the coating (1a) of the coated material web (1).

2. Method according to claim 1, characterized in that the temperature of the measuring chamber air (AI) remains essentially constant within the time interval (IN).

3. Method according to claim 1 or 2, characterized in that the moisture information (HI) is derived from at least one sorption isotherm (ST) and / or at least one desorption isotherm (DT), each of which represents an equilibrium state between the water content in the coating (1a) and the water content in the surrounding air at the predetermined temperature (TP) and / or the measured temperature (TP0). 1 ) at the end of the P3777PC00 19 time interval (IN) represent, where at least one sorption isotherm (ST) in the case of sorption of water into the coating (1a) from the surrounding air at the specified temperature (TP) and / or the measured temperature (TP) has occurred before reaching equilibrium. 1) at the end of the time interval (IN) the dependence of the water content in the coating (1a) on the relative humidity of the surrounding air at the specified temperature (TP) and / or the measured temperature (TP 1 ) at the end of the time interval (IN) in equilibrium and represents at least one desorption isotherm in the case of desorption of water from the coating (1a) into the surrounding air at the specified temperature (TP) and / or the measured temperature (TP) before reaching equilibrium. 1 ) at least at the end of the time interval (IN) the dependence of the water content in the coating (1a) on the relative humidity of the surrounding air at the specified temperature (TP) and / or the measured temperature (TP 1 ) at the end of the time interval (IN) in equilibrium.

4. Method according to claim 3, characterized in that in step c) when the relative humidity of the measuring chamber air (AI) decreases from the predetermined relative humidity (HU) within the time interval (IN), the water content in the coating (Ia) is determined as at least a part of the humidity information (HI), which is derived from the sorption isotherm (ST) for the measured relative humidity (HU). 1 ) the measuring chamber air (AI) and the measured temperature (TP) 1 ) of the measuring chamber air (AI) at the end of the time interval (IN).

5. Method according to claim 3 or 4, characterized in that in step c) as the relative humidity of the measuring chamber air (AI) increases from the predetermined relative humidity (HU) within the time interval (IN), the water content in the coating (Ia) is determined as at least a part of the moisture information (HI), which is derived from the P3777PC00 20 Desorption isotherm (4) for the measured relative humidity (HU) 1 ) the measuring chamber air (AI) and the measured temperature (TP) 1 ) of the measuring chamber air (AI) at the end of the time interval (IN).

6. A method according to any one of claims 3 to 5, characterized in that a threshold value for the water content in the coating (1a) is defined and the predetermined relative humidity (HU) and the predetermined temperature (TP) of the measuring chamber air (AI) are set such that the threshold value is obtained from the sorption isotherm (ST) for the predetermined relative humidity (HU) and the predetermined temperature (TP) of the surrounding air, wherein at least part of the moisture information (HI) is determined to show that the water content in the coating (1a) is less than or equal to the threshold value when the relative humidity of the measuring chamber air (AI) decreases or remains constant from the predetermined relative humidity (HU) within the time interval (IN), and that the water content in the coating (1a) is greater than the threshold value.when the relative humidity of the measuring chamber air (AI) increases from the predetermined relative humidity (HU) within the time interval (IN).

7. Method according to one of the preceding claims, characterized in that the time interval (IN) is fixed and preferably lies between 10 seconds and 10 minutes, particularly preferably between 20 seconds and 1 minute.

8. Method according to one of claims 1 to 6, characterized in that the time interval (IN) is terminated when the change in the relative humidity of the measuring chamber air (AI) is below a predetermined threshold.

9. Method according to one of the preceding claims, characterized in that the measuring chamber air (AI) circulates in the measuring chamber (3). P3777PC00 21 10. Method according to one of the preceding claims, characterized in that the measuring chamber air (AI) is under overpressure relative to the air in the vicinity of the measuring chamber (3).

11. Method according to one of the preceding claims, characterized in that the measuring chamber (3) has a length in the transport direction (T) of the material web (1) between 20 cm and 40 cm and / or a height in the direction perpendicular to the plane of the material web (1) between 3 cm and 5 cm and / or a width perpendicular to the transport direction of the material web (1) between 200 mm and 1600 mm.

12. Method according to one of the preceding claims, characterized in that the coated material web (1) is an electrode material web for a battery.

13. Method according to one of the preceding claims, characterized in that the method is carried out after a drying process of the coated material web (1).

14. Device for analyzing a coating (1a) on a coated material web (1) with respect to moisture content therein, the device being configured to carry out a method in which: a) a measuring chamber (3) is filled with measuring chamber air (AI) having a predetermined relative humidity (HU) and a predetermined temperature (TP) at the beginning of a time interval (IN) starting after the measuring chamber (3) is filled; b) the coated material web (1) is transported through the filled measuring chamber (3) and, during the transport of the material web (1), one or more parameters of the measuring chamber air (AI) comprising the relative humidity (HU) and the temperature (TP) are measured. P3777PC00 22 Humidity (HU) 1) the measurement chamber air (AI) is measured at least at the end of the time interval (IN); c) from the change in the relative humidity of the measurement chamber air (AI) within the time interval (IN) using the predetermined temperature (TP) of the measurement chamber air (AI) and / or using a temperature (TP) measured in step b). 1 ) of the measuring chamber air (AI) at the end of the time interval (IN) a moisture information (HI) is determined which describes the water content in the coating (1a) of the coated material web (1).

15. Device according to claim 14, characterized in that the device is configured to carry out a method according to one of claims 2 to 13.

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