EP2305839A2 - Process for retanning leather with hollow microspheres - Google Patents

Abstract

Retanning leather comprises: (a) treating a tanned leather in aqueous liquor in the presence of hollow micro spheres filled with blowing agent, (b) drying the leather obtained in step (a) after further optional retanning steps and (c1) treating with hot water steam at 80-120[deg] C, preferably at 80-100[deg] C, or (c2) treating with infrared radiation having a wavelength of 0.7-100 mu m, where a finishing step (b1) and/or a milling step (b2) can be carried out, after the drying step (b). Independent claims are included for: (1) the leather obtained by the process; and (2) a mixture containing micro hollow balls filled with blowing agent, preferably a liquid having boiling point of less than 60[deg] C in normal pressure and chrome tanning agent and/or synthetic retanning agent.

Description

The invention relates to a process for retanning leather, then produced leather, and mixtures of hollow microspheres and chrome tanning or synthetic tanning agents and their use.

State of the art

Hollow microspheres are also described in connection with leather meanwhile in a variety of ways. Thus, for example, they come into question superficially in the dressing of the grain side or meat-side coating or as retanning agent, incorporated in the aqueous post-treatment step.

In DE 202006005330 U1 For example, leather is coated with a hollow microsphere dispersion on the grain side and, after solidification of the dispersion, the hollow spheres are expanded with pressureless superheated steam (ie at most 100 ° C.). Thus produced leather has a nubuck-like surface, which has advantages in terms of shrinkage behavior and hardening of the leather in the formation of the foam structure. The disadvantage, however, is that the foam structure is formed only on the surface and the leather retains its original thickness and the method is only suitable for filling depressions in the grain layer. The water absorption of the leather is not changed per se and the water vapor permeability is essentially influenced by the thickness of the dressing layer.

In DE 10218076 B4 Foaming takes place with hollow microspheres on the meat side with subsequent treatment with hot air above 280 ° C for expansion of the hollow spheres. By inflating individual located on the surface of the meat side leather tufts a cushioning effect should be achieved. The disadvantage, however, is that the hollow microspheres are only on the surface at which a foam structure is formed during the expansion of the hollow microspheres. Inside the leather there are no hollow microspheres. The high temperatures used to expand the hollow microspheres can destroy the foam structure and lead to shrinkage of the leather.

In US-A-5,368,609 Micro hollow balls are introduced into the leather in an aqueous Nachgerbschritt in the barrel. The expansion of the hollow spheres takes place with hot water at 70 to 90 ° C in the barrel or during air drying. Other types of drying such as hot air, on the embossing rollers (hot plate) or superheated steam are given here, the hot air has the disadvantages described above, the embossing roller causes the hollow balls due to the high back pressure only partially for expansion and superheated steam itself as harmful to the Foam structure and the leather has proven. However, the expansion methods which are preferably used also lead to leathers which, with regard to the desired properties such as softness of the leather, greater thickness increase with reduced water absorption, very good water vapor permeability and tear resistance. can still be improved.

In EP-A 1 279 746 the basic use of hollow microspheres for incorporation into leather in the aqueous Nachgerbschritt is described. The expansion can then take place in various ways, for example by microwave, oven treatment, ironing (embossing roll), IR heat or steam treatment, wherein preferably a temperature of 100 to 130 ° C is used and only the furnace treatment and ironing (embossing roll) are described by way of example. The steam treatment in this temperature range would correspond to the use of superheated steam whose disadvantages are already described above. Disadvantages of the oven treatment and the embossing rollers are also described above.

However, the leather obtained in this way still have technical disadvantages. For example, the cavities are not completely filled. The expansion of introduced into the fiber braid hollow microspheres by means of embossing, as in EP-A 1279746 proposed, leads to a compression of the leather, with the result that the softness suffers. Furthermore, the expansion of the capsules over the entire cross section is very different. The tensile strength of leather generally decreases with decreasing density. According to the prior art, the retanning agents used to improve the durability of leathers lead to heavy leathers. A weight saving is for example in car upholstery leather or leather for aircraft seats, but also in shoe leather of interest.

It is an object of the present invention to provide leathers which do not have the disadvantages mentioned and in particular have a fiber structure completely filled with hollow microspheres which leads to a high volume increase of the leather, in particular more than 50% by weight, based on the starting thickness of the substrate (Reference point is in leather production, the folding thickness of the used wet blue) leads and gives the leather despite the reduced density by the incorporation of the hollow microspheres increased tensile strength and a high softness and low burring. To improve the assortment and improve the yield in the production of leather (cutting yield), it is furthermore desirable to use even very thin gaps, for example having a thickness of less than 1 mm, and to produce leathers which are also suitable for high-quality automotive leather.

• a) ein gegerbtes Leder in wässriger Flotte in Gegenwart von mit Treibmittel gefüllten Mikrohohlkugeln behandelt,
• b) das nach a) erhaltene Leder nach ggf. weiteren Nachgerbschritten trocknet und
• c1) mit 80 bis 120 °C heißem Wasserdampf oder
• c2) mit einer Infrarotstrahlung mit einer Wellenlänge von 0,7 bis 100 µm behandelt,

wobei sich zu einem Zeitpunkt nach dem Trockenschritt b) noch ein Zurichtschritt b1)
und/oder ein Millschritt b2) anschließen kann.We have now found a process for retanning leather, which is characterized in that

• a) treating a tanned leather in an aqueous liquor in the presence of propellant-filled hollow microspheres,
• b) the leather obtained according to a) dries after any further Nachgerbschritten and
• c1) with 80 to 120 ° C hot steam or
• c2) treated with an infrared radiation having a wavelength of 0.7 to 100 microns,

wherein at a time after the drying step b) is still a trimming b1)
and / or a mill step b2) can connect.

The time of the optional steps b1) and b2) is after the drying step b). This means that this can also be after the expansion step c). Under dressing step b1) is understood in this context, the application of a trimming layer (primer) and the subsequent application of a topcoat. However, this need not necessarily be immediately consecutive steps. Between the application of the primer and the topcoat, a milling step b2) and / or an expansion step c) may also be present.

The tanned leather used in the retanning in step a) comprises both a fully tanned leather (ie a leather whose shrinkage temperature can not be further increased) and a pretanned leather (ie a leather whose shrinkage temperature can be further increased by further tanning). As such, for example, chromium-tanned (wet blue), chromium-free pre-tanned and retanned as well as vegetable pre-tanned leather can be used. Preference is Mineralgerbstoffhaltiges or mineral tanner-free leather

In doing so, for tanning, the skin of animals, e.g. Beef, pork, goat, sheep, horse, kangaroo, yak, water buffalo, zebu and allied species are used. Cowhide is preferred. The method is also suitable for improving assortments that have a histologically loosely fibrous structure.

The tanned leather used preferably has a shrinkage temperature of 65 to 105 ° C, preferably 90 to 102 ° C. Low shrink temperature leathers are preferably then used when a portion of the tanning agent such as the chrome tanning agent is used to further increase the shrinkage temperature in Nachgerbschritt.

The tanned (and also the pretanned) leather is preferably folded to a desired thickness and placed in a conventional apparatus in a tannery, as usual aggregates in the tannery the barrel (about an axis rotating closed drum, such as wood or stainless steel manufactured), mixer (looks similar to a concrete mixer on a truck) or Y-barrel (keg with a barrel Y subdivision) are used.

The folding thickness of the tanned leather used is preferably greater than 0.5 mm, in particular from 0.8 to 5.0 mm.

The hollow microspheres preferably contain as the propellant a liquid which has a boiling point which does not exceed the softening temperature of the shell of the hollow microspheres. Particularly suitable are hydrocarbons such as n-butane, isobutane, n-pentane, neopentane, isopentane, hexane, isohexane, heptane, octane, cyclopentane, cyclopentene, pentene-1, hexene-1, etc. Very particularly preferred are hydrocarbons having a boiling point of less than 60 ° C at atmospheric pressure. Particularly preferred propellant liquid in the interior of the hollow microspheres is isobutane. Chlorine or fluorine containing compounds are also possible, but not preferred. It is also possible to use propellants which are generated in situ when the temperature is raised, for example by chemical reactions, in particular by the formation of gases. Such propellants are, for example, azo initiators known as polymerization initiators (such as 2,2'-azobisisobutyronitrile, AIBN). , Hydrogen peroxide, persulfates, percarbonates, or CO ₂ releasing compounds such as carbonates or bicarbonates. The blowing agent is usually 1 to 40 wt .-% of the total weight of the hollow microspheres.

As hollow microspheres, especially those having a diameter of 1 to 200 .mu.m, preferably from 1 to 80 .mu.m in question, particularly preferably 5 to 40 microns.

The hollow microspheres have a shell and an interior. The sheath is preferably constructed of an organic polymer or copolymer. Suitable monomers for setting up the shell of the hollow microspheres are, in particular, nitrile-containing monomers such as acrylonitrile, methacrylonitrile, fumaronitrile, crotononitrile, acrylates or methacrylic esters such as ethyl acrylate, methyl acrylate, methyl methacrylate, isobornyl methacrylate, hydroxyethyl methacrylate, vinyl halides such as vinyl chloride, vinylidene chloride, vinyl esters such as vinyl acetate, vinyl formate, Styrene and substituted styrene compounds. It is also advantageous to use in the construction of the shell polyunsaturated compounds that serve as crosslinkers. The amount of such crosslinkers is usually 0.1 to 2 wt .-% based on the sum of all comonomers. suitable Polyunsaturated compounds are, for example, allyl methacrylate, ethylene glycol dimethacrylate, diethylene glycol dimethacrylate, triethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, trimethylolpropane trimethacrylate, pentaerythritol tetramethacrylate, bis (methacryloyloxymethyl) tricyclodecane and the corresponding diacrylates, divinylbenzene, etc.

Particularly preferred are polymers and copolymers which are composed of vinylidene chloride, acrylonitrile and (meth) acrylic monomers and mixtures thereof. Polyurethanes and polyurethane ureas are also suitable as wall material.

More preferably, the thin shell of a co-polymer consists of more than 75% polyvinylidene chloride and less than 25% polyacrylonitrile. In the interior is preferably a liquid which has a boiling point of less than 60 ° C. Isobutane is used as the preferred blowing agent.

Hollow microspheres are commercially available. As exemplary hollow microspheres are the Expancel® hollow microspheres Akzo called.

A distinction is made between unexpanded and expanded hollow microspheres.

The expanded capsules are preferably those obtained from the unexpanded capsules after a heat treatment and can not be significantly further expanded by further heat treatment without being destroyed. The preferred diameter of the unexpanded hollow microspheres is 1 to 80 μm, preferably 5 to 40 μm. The preferred diameter for the expanded capsules is 10 to 160 μm, in particular 15 to 80 μm.

Preferably, hollow microspheres are used which can be expanded, wherein the starting point of the expansion in the temperature range of 30 to 130 ° C, in particular at 65 to 100 ° C.

The hollow microspheres are preferably used in an amount of 0.5 to 30 wt .-%, preferably 1 to 15 wt .-%, in particular 2 to 8 wt .-%, based on shaved weight.

Step a) of the process according to the invention is carried out in an aqueous liquor, the liquor ratio (leather to water) preferably being from 0 to 1000% by weight (based on shaved weight).

Step a) is preferably carried out at a temperature of 20 to 70 ° C, in particular at 30 to 60 ° C. Preference is given to working at a pH of 2.0 to 10.0. Very particularly preferred for the post-treatment step a) is the pH range from 3 to 8.

In addition to the hollow microspheres, other additives customary for the retanning can also be used in step a). As such, e.g. Dyes, synthetic tanning agents, resin tanning agents, vegetable tanning agents, polymer tanning agents based on acrylate copolymers, softening tanning agents based on polyamidecarboxylic acids (such as LEVOTAN® L) or based on esters of polycarboxylic acids and linear or branched polyetherpolyols, fatliquoring agents, and chromium To name aluminum or zirconium compounds. Binders, ie film-forming polymers, can likewise be used, but are not preferred. Suitable binders are, for example, natural caseins, butadiene copolymers, (meth) acrylate polymers (so-called polyacrylates) or polyurethanes. The content of binders is preferably less than 5% by weight, preferably less than 2% by weight, based on the shaved weight.

1. A) 1,0 bis 20 Gew.-% Mikrohohlkugeln, die ein Treibmittel, insbesondere eine Flüssigkeit mit einem Siedepunkt bei Normaldruck von kleiner 60 °C enthalten, und
2. B) 1,0 bis 20,0 Gew.-% Chromgerbstoff, und /oder
3. C) 1,0 bis 20,0 Gew.-% synthetische Gerbstoffe.

The hollow microspheres are preferably added as a solid or in the form of an aqueous suspension (slurry) in the post-treatment step a). Particularly preferred is a mixture containing microbeads and a chrome tanning agent and / or a synthetic retanning agent. Such a mixture preferably contains

1. A) 1.0 to 20 wt .-% hollow microspheres containing a propellant, in particular a liquid having a boiling point at normal pressure of less than 60 ° C, and
2. B) 1.0 to 20.0 wt .-% chrome tanning agent, and / or
3. C) 1.0 to 20.0% by weight of synthetic tanning agents.

Suitable chrome tanning agents are, for example, chromium sulfate tanning agents and complex chrome tanning agents with masking / buffering additives.

Further constituents which may be present are the abovementioned additives and water specified for the post-tanning step.

Suitable synthetic tanning agents are, for example, the condensation products based on aromatic compounds, such as phenol, naphthalene, ditolyl ether, phenolsulfonic acid, naphthalenesulfonic acid, ditolyl ether sulfonic acid, dihydroxydiphenyl sulfone and formaldehyde, which are known per se to the skilled worker. Other formaldehyde-reactive compounds, such as urea or substituted urea, can be used as raw materials ,

It is particularly preferred to use the hollow microspheres in an aqueous formulation as a slurry, which also contain the above-mentioned adjuvants, in particular chromium sulfate and / or synthetic tanning agent and optionally further auxiliaries.

Auxiliaries are, for example, customary products for retanning, such as bases and acids, dyes, fatliquors, water repellents. Such products are commercially available and known to those skilled in the art.

The maturity in the barrel for the application of the hollow microspheres is preferably 10 to 200 minutes, wherein the hollow microspheres penetrate into the leather cross section and fill the pores in the fiber braid to more than 90%. In particular, the hollow microspheres penetrate until just below the grain layer in the leather.

Subsequent to the post-treatment step a), in which the hollow microspheres are applied, it is possible for further retanning to include subsequent steps such as neutralization, optionally retanning with synthetic, vegetable retanning agents or the abovementioned polymer tanning agents, if appropriate followed by a Staining, fatliquoring and a final fixation preferably with formic acid. Furthermore, a surface dyeing with renewed fixation, preferably with formic acid is possible.

After completion of these retanning operations in the drum, the leathers are usually dried by a mechanical dewatering process to the various drying methods such as e.g. Stapling, vacuum and hanging drying prepared and carried out the drying.

The drying in the sense of step b) of the process according to the invention is generally carried out at a temperature of 30 to 70 ° C. The leather is preferably dried to a relative moisture content of 8 to 50 wt .-%, in particular from 8 to 25 wt .-%, preferably from 10 to 20 wt .-% dried. The dried leathers are preferably air conditioned and staked. Before the expansion of the microcapsules, the leather should each have a relative leather moisture of 8 to 25 wt .-%, preferably 10 to 20 wt .-% relative leather moisture or possibly adjusted by moistening or air conditioning in a corresponding air conditioning chamber to the corresponding water content. In the case of a subsequent infrared treatment, the leather moisture is preferably 20 to 50 wt .-%.

In the event that the dried leather obtained after step a) is additionally to be applied in a separate step b1), a priming formulation customary in dressing technology can now be applied to the usual application techniques by conventional application techniques, preferably by spraying Crust leather applied, then dried and embossed. Subsequently, a topcoat formulation customary in the dressing technique is applied to the primed and embossed leather and then dried.

The products customary for producing the primer and topcoat formulations, such as binders, crosslinkers, pigments, leveling agents, additives, etc., are known per se to the person skilled in the art and are commercially available products.

In the case where the leathers are milled in an additional step b2), the leathers are preferably transferred to a millimeter under standard conditions which are generally known to the person skilled in the art and milled until the desired optical and haptic properties are achieved. The mill process is usually carried out with the crust leather, with the primed leather or the primed and embossed / ironed leather or with the topcoat already provided finished finished leather.

The expansion of the hollow microspheres embedded in the leather is preferably carried out in the process according to the invention at the stage of the crust leather (after step b), after application of the primer (according to b1) or after application of the topcoate (according to b1). Also, a stepwise expansion in several places is possible.

If no dressing is applied, the expansion is preferably performed after step b) at the crust leather stage.

If the leather is to be milled (step b2), the expansion takes place before or after the mill process, but more preferably after the millen.

When a dressing is applied to the leather (step b1) and the leather is additionally subjected to a mill process (step b2), the mill process is preferably carried out after retanning at the crust leather or at the level of the primed, optionally embossed / ironed leather. In these cases, the expansion of the hollow microspheres is particularly preferably carried out either directly after the millenium of the crust leather or after completion of the trimming steps (b1) as the last step.

For the subsequent expansion of the hollow microspheres in step c), the leather is treated in the case c1) with steam at a temperature of 80 to 120 ° C, preferably from 80 to 100 ° C. Optimum values are achieved when the steam reacts on the retanned leather for a period of less than 7 seconds, preferably less than 3 seconds. It has been found that such a water vapor, if it impinges without pressure or almost without pressure - ie relaxed, preferably under an overpressure of less than 0.1 bar, briefly on the nachgegerbte with hollow microsphere leather, spontaneously causes the expansion of the hollow microspheres without As a result, the properties of the leather are adversely affected. The leather is preferably penetrated by the hot water vapor. The leather is used in this procedure no moisture removed, but rather supplied, whereby a hardening and shrinkage of the leather is prevented. The expanded hollow microspheres are also better than those formed by the application of pressure and heat or by hot air treatment in the known methods, and are not destroyed in particular in an application of relaxed water vapor in the manner indicated. In the application of water vapor, which contains no water but is 100% in the form of steam, the risk of destruction of the hollow microspheres by overheating is very high and the leather can shrink. In these cases, the increase in leather volume would be significantly lower and the leather would not be optimal in terms of grip and water absorption.

Expediently, the steam device for generating the hot steam (superheated steam) has at least one hot steam tank which communicates with hot steam outlet openings directed against the leather surface, in particular with outlet nozzles or slots, via whose openings the superheated steam separates the leather from the grain and / or grain the meat side is fed. In an expedient embodiment, the hot steam tank consists of at least one pipe with a round or rectangular cross-section, which is provided with the hot steam outlet openings. It has proven to be advantageous if this tube is meander-shaped, wherein preferably the individual sections transverse to the transport direction of the leather (ie the direction of the conveyor belt, with the help of the leather is moved past the hot steam outlet openings in the manufacturing process) run, and with Its two ends are connected to a hot steam source, so that the steam in the tube circulates in the circulation and thus cooling is prevented. It suffices here in the tube, a low vapor pressure of less than 5 bar, preferably less than 2 bar.

It is also possible to keep the superheated steam device movable and corresponding to the leather surface, wherein the direction of movement can be rectilinear, circular, elliptical or in a swinging motion, with the proviso that the outlet openings do not come into direct contact with the leather surface. There are also combinations of movements advantageous.

It is advantageous if a heat source is provided in the hot steam tank, preferably in a wall thereof, in particular in the wall surrounding the hot steam outlet openings. This heat source, when the temperature in the vicinity of the hot steam outlet openings through it is lower than the hot steam temperature, a condensed water formation.

However, this heat source can also be used to form the superheated steam only in the superheated steam container, namely, when this superheated steam container initially only water is supplied and the superheated steam is formed from this water in situ by supplying heat.

The heat source may consist of electric heating wires, which are embedded for example in the wall of the hot steam tank, or pipes formed by heated oil, which may be provided in the form of heating coils in the hot steam tank inside the same when forming the hot steam.

But it can also be provided an arrangement in which the hot steam device is designed as a transport device enclosing hot steam tank, the hot steam is supplied via a superheated steam source, or in which the superheated steam is formed in situ, so that the leather located on the conveyor during the Further movement is applied in this hot steam tank with the superheated steam in it. Appropriately, in this case, the superheated steam device is arranged adjacent to the leather supporting, circulating transport device, so that the passing of the hot steam device passing leather is continuously supplied with the superheated steam.

However, it is also possible according to the invention to form the superheated steam only directly on the surface of the leather. In this case, the superheated steam device has at least one hot water or wet steam tank, which is connected to outlet openings directed towards the leather, and a heat supply device arranged downstream of the hot water or wet steam tank, as seen in the transport direction. The warm water or the wet steam initially wets the surface of the leather and is subsequently converted by the heat supply device into superheated steam, which results in substantially the same effect as in the case of an immediate supply of superheated steam. The energy expenditure in this case, however, is greater than with a direct supply of superheated steam. As a heat supply device, for example, is an infrared radiator, preferably an infrared dimmer.

Preferably, the superheated steam device is made DE 20 2006 005 330 U1 , In particular, from FIG. 3 and their installation in one of the system described therein, the disclosure of which should also be the subject of this application. Of course, the application units for the plastic dispersions for the purpose of the method according to the invention are not required.

In the subsequent expansion of the hollow microspheres in step c), the leather for the case c2) is treated with an infrared radiation having a wavelength of 0.7 to 100 μm, in particular with an infrared dark radiation having a wavelength of 2 to 10 μm. Preference is given to a Distance between the leather surface (scars or meat side) and the beam surface of the IR emitter from 45 to 220 mm complied.

Preferably, the treatment is carried out for a period of less than 30 seconds, preferably less than 20 seconds. The leather is preferably heated to a temperature of 90 to 115 ° C.

The use of such an IR emitter causes uniform heat supply in all areas of the leather, even in the deeper areas, the expansion of the hollow microspheres takes place and also in these areas a foam structure is formed which is not subject to shrinking. Preferably, the IR radiator is designed as a surface radiator. It has proven to be expedient if the infrared radiator, seen in the transport direction of the leather, is provided after a running through the leather drying tunnel, so that filled with hollow microspheres leather is already dried and already has a temperature of 65 to 80 ° C. In this case, heating by means of infrared radiation to a temperature of 105 ° C. can take place in less than 12 seconds.

• Die so erhaltenen Leder besitzen eine uniforme Dicke, eine verbesserte Zugfestigkeit, gleichmäßigere Dichte durch selektive, besonders ausgeprägte Füllung der losen Bereiche im gesamten Lederquerschnitt. Gleichzeitig ist die Weichheit der Leder verbessert gegenüber einer Expansion unter Druck und die Losnarbigkeit deutlich geringer. Es ist weiterhin möglich, Narbenfehler sowie die Hohlräume der Haarwurzelscheide soweit mittels dieses Verfahrens und unter Verwendung der entsprechenden Mikrohohlkugeldurchmesser erreichbar, fast völlig zu füllen. Es ist daher möglich, auch minderwertige Rohware, insbesondere solche mit vielen Fehlern in der Narbenschicht, zu einem hochwertigen Leder zu verarbeiten, ohne dass separate Prozessschritte in der Lederherstellung erforderlich sind. Besonderes Merkmal der Leder ist, dass die großen Hohlräume die mittels dieses Verfahrens und unter Verwendung der entsprechenden Mikrohohlkugeldurchmesser erreichbar sind, zu mehr als 90 % mit Mikrohohlkugeln gefüllt sind und diese durch die Expansion dauerhaft im Substrat verankert sind.

Advantages:

• The leathers thus obtained have a uniform thickness, improved tensile strength, more uniform density through selective, particularly pronounced filling of the loose areas in the entire leather cross section. At the same time, the softness of the leather is improved over expansion under pressure and the loosening significantly lower. It is also possible to almost completely fill scar defects as well as the cavities of the hair root sheath as far as possible by means of this method and using the corresponding hollow microsphere diameter. It is therefore possible to process inferior raw materials, in particular those with many defects in the scar layer, to a high-quality leather, without separate process steps in leather production are required. A special feature of the leather is that the large cavities that can be reached by means of this method and using the corresponding hollow microsphere diameter are filled to more than 90% with hollow microspheres and they are permanently anchored by the expansion in the substrate.

Water vapor permeability and water absorption of the leather produced according to the invention are significantly improved. In particular, the density of the leather is drastically reduced due to the high volume increase. The leathers produced according to the invention have an improved tensile strength in comparison to the control without hollow microspheres or leathers in which the hollow microspheres do not penetrate to below the grain layer and are only partially covered by others.

The invention further relates to leather obtainable by the process according to the invention.

The leather contains expanded hollow microspheres embedded in the fiber braid and, despite the lower density, has an improved tensile strength compared to an untreated leather. Static water uptake (determined by the Kubelka method: by introducing a leather sample into a water bath for a defined period of time, for example 2, 8 and / or 24 hours and determining the weight increase in%) is significantly reduced, which is a considerable advantage ,

The invention further relates to the use of the leather according to the invention in particular as ground or full-grain leather or as split leather, for car, furniture, glove, bag and upper leather articles.

The use for leather fiber material comprising a mixture of chromium-containing or chromium-containing leather fibers, dyes, synthetic or vegetable tanning agents and binders such as e.g. Butadiene and acrylates is also possible.

1. A) 1 bis 20 Gew.-% Mikrohohlkugeln, die ein Treibmittel, insbesondere eine Flüssigkeit mit einem Siedepunkt bei Normaldruck von kleiner 60 °C enthalten, und
2. B) 1 bis 20 Gew.-% eines Chromgerbstoffs, vorzugsweise eines basischen Chromsulfats.

The invention further relates to a mixture containing

1. A) 1 to 20 wt .-% hollow microspheres containing a propellant, in particular a liquid having a boiling point at normal pressure of less than 60 ° C, and
2. B) 1 to 20 wt .-% of a chrome tanning agent, preferably a basic chromium sulfate.

The preferred embodiments for the hollow microspheres, blowing agents and chrome tanning agents are those mentioned above.

1. A) Mikrohohlkugeln, die ein Treibmittel, insbesondere eine Flüssigkeit mit einem Siedepunkt bei Normaldruck von kleiner 60 °C enthalten und
2. B) einen Neutralisationsgerbstoff.

The invention further relates to a mixture containing

1. A) hollow microspheres containing a blowing agent, in particular a liquid having a boiling point at atmospheric pressure of less than 60 ° C and
2. B) a neutralization tanning agent.

Both inventive mixtures preferably contain less than 5 wt .-%, in particular less than 2 wt .-% of a binder.

Chromium tanning agents which can be used as powder or in liquid form are particularly preferred, in particular basic chromium sulphates having a basicity between 20 and 70% and one

Chromium content, determined as Cr ₂ O ₃ , between 10 and 40%. Examples include tanning agents such as CHROMOSAL® B, CHROMOSAL®B liquid (Lanxess Deutschland GmbH).

Neutralization tanning agents are preferably aromatic compounds such as phenolic sulfonic acids or naphthalenesulfonic acid or their condensation products with formaldehyde, and mixtures thereof with carboxylic acids, dicarboxylic acids and polycarboxylic acids, these products have buffering properties and are used in the retanning and wherein by their neutralizing effect on the entire leather cross section, for example especially level dyeings are possible. It is also possible proportionally to use polymer tanners based on modified polyamide carboxylic acids having softening and filling properties or polyacrylate-based plasticizing and / or filling polymer tanning agents. Such products are commercially available and known in the art. Examples which may be mentioned as suitable retanning agents are TANIGAN® PAK-N, TANIGAN® PR, TANIGAN® SR, TANIGAN® PAK, LEVOTAN® L, LEVOTAN® C, LUBRITAN® GX, LUBRITAN® AS, LUBRITAN® TG etc. (Lanxess Deutschland GmbH) ,

The invention further relates to the use of the inventive mixture for retanning leather.

A possible dressing can be done before, during or after the expansion.

A possible mill process can already occur before, during or after the expansion. It is particularly preferable to carry out the mill process before the expansion.

Surprisingly, it has been shown that the leathers have a uniform aspect even without further process steps, such as, for example, grinding off the surface in the case of grain defects, and that they also meet the highest demands on the fastness properties. Furthermore, it is surprising that an almost complete filling of all achievable cavities, in particular of more than 90%, takes place. The proportion of voids filled with microballoons can be controlled by the amount used in combination with the conditions for expansion. In this case, the method according to the invention is suitable for converting even inferior raw materials into elegant, uniform leather surfaces, since the loose parts of the skin material are particularly strongly filled or undergo a greater expansion of the hollow microspheres than the parts with fibers lying closer together. The inventive method is simple and comes with a minimum of chemicals. This makes available stable, but nevertheless soft leather with a higher volume, which surprisingly exhibits improved tensile strength at lower density. The water absorption of the leather is reduced, which brings a significant advantage and also hydrophobized leather, for example, shoe upper leather, made of raw material, otherwise for this purpose completely unsuitable, accessible. The increase in volume can be controlled by the amount of use and the type of hollow microspheres, the auxiliary agents B) and C) and the expansion conditions of the hollow microspheres.

In the event that a dressing takes place as operation b1), the subsequent expansion of the hollow microspheres can be carried out before, during or after the trimming. It is preferred to carry out the trimming process before or after the expansion of the hollow microspheres. The optical properties of the surface can be influenced by the type of expansion.

In the event that a Mill process takes place as operation b2), the subsequent expansion of the hollow microspheres can be carried out before, during or after the millennium. It is preferred to carry out the mill process before the expansion of the hollow microspheres. The optical properties of the surface can be influenced by the type of expansion. In particular, depending on whether the energy supply for expansion from the grain side or the meat side takes place, different results can be achieved. In particular, the visual impression, for example, whether a rough or a smooth surface is formed, can be influenced in the inventive method by the type of expansion. In the expansion according to Schriott c1) from the meat side, for example, a rough, microstructured surface is achieved. In the expansion according to step c1) from the grain side, a very smooth surface is obtained as a rule.

Surprisingly, it has been found that it is particularly advantageous to combine the optional steps b1) and b2) with one another. It has further been found that, in particular in this embodiment, the operation for the expansion of the hollow microspheres has an influence on the properties of the obtained leather. In particular, in a leather exposed to the meat side of the expansion device (i.e., the steam device described above or the IR emitter), a rough surface may be created. If, on the other hand, expansion takes place from the side of the scars, in that, for expansion, the leather faces the grain side of said steam device, a smooth surface is generally produced.

In a particularly preferred embodiment, it is also possible to carry out the expansion after embossing and Millen of primed leather and to provide the resulting leather with a final finish as a topcoat, the optical effect achieved is permanently fixed.

Particular preference is furthermore given to an embodiment in which, after retanning and drying (step b), a mill process b 2) is followed and the leather is then expanded according to step c1) or c2). If necessary, a small amount of a topcoat can be injected as a final finish to improve the fastness properties.

With the method according to the invention it is also possible to control the surface structure and roughness by using amounts of hollow microspheres in the wet area. However, it is particularly advantageous for the effect "to fill the cavities in the fiber structure in the aftertreatment step a) as evenly as possible and as completely as possible with hollow microspheres.

Example 1 (according to the invention):

Half a wet skin was folded to a thickness of 1.2 mm (measured with a leather thickness gauge). Weighing was used to determine the shaved weight used for the additions of the chemicals as a reference, as was customary in leather production.

The retanning process was carried out as follows:

I. Preparation of a tanned leather First process step (preparation):

A wet blue half is placed in a V2A steel Nachgerbfass, which is provided with a double-wall drum casing with trapped water, which is electrically heated; then 300% water with a temperature of 40 ° C (all percentages also in the process steps described below are based on the shaved weight) and 0.3% formic acid 85% (this was 1 part of formic acid with 10 parts of water at 20 ° C prediluted). The running time in the rotating drum (rotational speed 15-18 revolutions per minute) with set at a temperature of 40 ° C heating was 20 minutes. The pH was 3.0. The liquor was drained through the perforated drum lid, which is located in the drum casing with rotating drum. The wet blue half remained in the barrel for the next step.

Second process step:

There was an addition of water of 150 wt .-% at a temperature of 40 ° C. Then, the first part of the neutralization is carried out by 4% of a neutralization tanning agent with strong neutralization and buffering (TANIGAN ^R PAH-N fl. Fa. Lanxess Germany GmbH) are added to the barrel. The running time in the rotating drum was 30 minutes with a heating setting of 40 ° C. This was followed by the addition of 1.5 wt .-% sodium bicarbonate (techn). The running time in the rotating drum was 30 minutes.

Third process step:

4.0% by weight of a commercially available fatliquoring agent (such as Lipodermlicker A1 (BASF AG, Ludwigshafen)) was added to the pre-lubrication. The running time in the rotating drum was 15 minutes.

Fourth process step:

Then, 4.5% by weight of a polymer retanning agent based on a modified polyamide carboxylic acid having a softening and filling action (such as LEVOTAN L, Lanxess Deutschland GmbH, Leverkusen) was added. The subsequent running time in the rotating drum was 30 minutes.

II. Inventive process step Step a)

To the described in 1. tanned leather is in the barrel 8% of a product mixture, which consists of 50 parts by weight of a self-dulling chromium sulfate tanning agent with about 17% chromium oxide content and 50 parts by weight unexpanded hollow microspheres based on a polyvinylidene chloride copolymer (such as Expancel 820 SL 40) is added. The hollow microspheres in the unexpanded state have a diameter of 2-30 microns and have a starting temperature for the expansion of 75-90 ° C. The running time in the rotating drum was: 90 minutes (heating setting 40 ° C / pH at the end about 4.8).

Thereafter, the barrel rotated at a rotational speed of 15 revolutions per minute, 10 minutes rotation and 20 minutes life in continuous change for 16 hours.

Thereafter, the second part of the neutralization with the use of 1% TANIGAN PAH-N fl. Runs for 10 minutes and an addition of 0.4 to 0.7 wt .-% sodium bicarbonate technically for 30 minutes (heating setting 40 ° C. / pH at the end about 5.9 to 6.4), followed by the steps of washing, retanning, dyeing, acidification, washing, overdyeing, acidification and washing.

The leather was deposited on a box.

Step b)

The next day, the leather was stretched out, wet tensioned and dried in the tenter frame drier for 2 to 8 hours while introducing low pressure steam at 40-70 ° C. This was followed by hanging drying and air conditioning overnight, a tunnel on the Stollmaschine and a subsequent millen in the Millfaß. The leather had a leather moisture content of 18%.

By treatment with relaxed water vapor at a temperature of 95 ° C by means of the superheated steam device, as in DE 20 2006 005 330 U1 described, the expansion took place the hollow microspheres and obtained a soft leather with excellent durability, low density and reduced water absorption.

Leather thickness: 1.7 mm; Density: 0.59 g / cm ³ , tensile strength: 16 daN. Static water absorption (Kubelka) after 2 hours: 59%, after 24 hours: 68%.

Example 2 (comparative experiment)

As a comparison, the process step II) a) described in Example 1 was modified as follows:

Step a)

To the described in Example 1 under point 1, tanned leather (which is used here as a reference material) is added to the barrel 30% water of 40 ° C and 4% of a self-rubbing chrome tanning agent with about 17% chromium oxide content. The running time in the rotating barrel was 60 minutes (heating setting 40 ° C / pH at the end about 4.8).

Thereafter, the barrel rotated at a rotational speed of 15 revolutions per minute, 10 minutes rotation and 20 minutes life in continuous change for 16 hours.

Thereafter, the second part of the neutralization with the use of 1% TANIGAN PAH-N fl. Runs for 10 minutes and an addition of 0.4 to 0.7 wt .-% sodium bicarbonate technically for 30 minutes (heating setting 40 ° C. / pH at the end about 5.9 to 6.4), followed by the steps of washing, retanning, dyeing, acidification, washing, overdyeing, acidification and washing.

The leather was deposited on a box.

Step b)

The next day, the leather was stretched out, wet tensioned and dried in the tenter frame drier for 2 to 8 hours while introducing low pressure steam at 40-70 ° C. Then the hanging drying and air conditioning took place overnight, a tunnel on the Stollmaschine and possibly a subsequent Millen in the Millfaß.

The leather did not change after steaming as in Example 1, but remained thin. In addition, it becomes partially hard due to the steaming and has a rough surface.

Leather thickness: 1.0 mm, tensile strength: 11 daN. Static water absorption (Kubelka) after 2 hours: 140%, after 24 hours: 180%.

Example 3 ( according to the invention) Step a)

4% of unexpanded hollow microspheres based on a polyvinylidene chloride copolymer such as Expancel® 820 SL 40 are added to the tanned leather described in Example 1 under point 1. The hollow microspheres in the unexpanded state have a diameter of 2-30 microns and have a starting temperature for the expansion of 75-90 ° C. The running time in the rotating drum was: 90 minutes (heating setting 40 ° C / pH at the end about 4.8).

Thereafter, the barrel rotated at a rotational speed of 15 revolutions per minute, 10 minutes rotation and 20 minutes life in continuous change for 16 hours.

The second part of the neutralization then takes place: 1% TANIGAN® PAK-N fl, was added and a running time of 10 minutes was set; then added 0.4-0.7 wt .-% sodium bicarbonate (techn.) And it was run time of 30 minutes (heating setting 40 ° C / pH at the end of about 5.9 to 6.4) set. This was followed by the steps of washing, retanning, dyeing, acidification, washing, overdyeing, acidification and washing.

The leather was deposited on a box.

Step b)

The next day, the leather was stretched out, wet tensioned and dried in the tenter frame for 2-8 hours while introducing low pressure steam at 40-70 ° C. This was followed by hanging drying and air conditioning overnight, a tunnel on the Stollmaschine and a subsequent millen in the Millfaß.

By treatment with relaxed superheated steam as in Example 1, the expansion of the hollow microspheres was carried out to give a soft leather with low density (0.39 g / cm ³ ) and compared to a leather without embedded microballoons significantly reduced static water absorption (Kubelka: after 2 hours: 54%, after 24 hours: 67%).

The volume increase of the leather is even more pronounced compared to the leather of Example 1. The leather differs from Example 1 in terms of the handle.

Example 4 ( according to the invention) The procedure was as in Example 3, but with the following change: in step b) Step b)

The next day, the leather was stretched out, wet tensioned and dried in the tenter frame for 2-8 hours while introducing low pressure steam at 40-70 ° C. This was followed by hanging drying and air conditioning overnight, a tunnel on the Stollmaschine and without a subsequent Millen.

By treatment with relaxed superheated steam as in Example 1, the expansion of the hollow microspheres was carried out to give a soft leather with low density (0.39 g / cm ³ ) and compared to a leather without embedded microballoons significantly reduced static water absorption (Kubelka: after 2 hours: 54%, after 24 hours: 67%).

The volume increase of the leather is unchanged from the leather of Example 3. The leather differs from Example 3 by a slightly less pronounced scar grain with almost the same pleasant grip.

Claims (2)

Mixture containing c) hollow microspheres containing a liquid having a boiling point at normal pressure of less than 60 ° C, and d) a softening retanning agent based on polyamide carboxylic acids or based on esters of polycarboxylic acids and linear or branched polyether polyols. Use of the mixture according to claim 1 for retanning leathers.