Abstract:
A method for producing bacteriorhodopsin-containing microcapsules is described, which can be optically activated, having a diameter of less than 50 μm, preferably less than 10 μm, comprising an enveloping layer, which protects the bacteriorhodopsin from harmful environmental factors, while at the same time preserving the functionality thereof. In doing so, bacteriorhodopsin is suspended in a first step, in the form of PM/BR patches in an aqueous medium having a pH value ranging from 6-9 in the presence of a water-retaining polymer, and said suspension is spray-dried to form a powder, or is dried in an aliphatic solvent using low steam pressure and subsequent dehydration to form a powder. In a second step, the powder obtained in this way is provided with an envelope, which is substantially completely translucent to light in the visible range and made of a polymer and/or a paraffin having a solidification point ranging between 45° C. and 65° C. and/or a carnauba wax having a melting range of 70-90° C. Furthermore, such microcapsules are described, and uses of such microcapsules.

Description:
TECHNICAL FIELD 
       [0001]    The present invention relates to the field of methods for producing bacteriorhodopsin pigments and to pigments based thereon and uses of such pigments. 
       PRIOR ART 
       [0002]    Bacteriorhodopsin, and especially bacteriorhodopsin in its customarily existing form as two-dimensional crystalline patches as purple membrane, is an intensively studied system. The system is of great interest, in particular, because it is able as an extremely resistant optical system to adopt different optical states which have half lives of interest. Thus, for example, in particular in the mutant D96N there is a transition from the light-adapted (mustard-yellow) state to the dark state (violet) with a half life of about 20 s. This half life is affected by various factors of the environment, in particular by the pH existing in the environment. 
         [0003]    It is a problem with this system, inter alia, that bacteriorhodopsin in purple membrane can be easily denatured by environmental influences, in particular when it comes into contact with certain organic solvents or surfactants. 
         [0004]    A recent publication (cf. Soft Matter, 2008, 4, 1249-1254) discloses a method in which bacteriorhodopsin in the purple membrane is coated on the charged surfaces with a thin layer of water glass in a biomimetic process. For this purpose, in a first step a polyelectrolyte (polyethyleneimine) is first adsorbed solely on the charged surface, that is to say not all-round, and then, in a second step, a water glass layer is built up on this polyelectrolyte with the aid of TEOS. The resultant systems correspondingly comprise a layer of water glass which is not completely enveloping but is substantially only on the charged surface. This layer protects the bacteriorhodopsin in the purple membrane from the harmful effect of organic solvents, but the water glass is not completely impermeable. It is permeable, in particular, to small ions, in particular protons and hydroxide ions. Larger ions and large particles are substantially excluded. The biomimetic nanoencapsulation therefore does not completely isolate the PM/BR from the environment. The bacteriorhodopsin therefore continues to react to changes in the pH of the environment. Correspondingly, such systems can only be used in situations where the pH of the environment can also be kept within a range where the desired optical properties of the bacteriorhodopsin are present. 
       DESCRIPTION OF THE INVENTION 
       [0005]    It is therefore one of the objects of the present invention to provide an improved method for producing bacteriorhodopsin/purple membrane fragments or bacteriorhodopsin/purple membrane patches, which method does not have the disadvantages of the abovementioned prior art. 
         [0006]    Accordingly, the present invention relates, inter alia, to a method for producing optically activatable bacteriorhodopsin-containing microcapsules having a diameter of less than 50 μm, preferably less than 20 μm, or further preferably less than 10 μm, having an enveloping layer which protects the bacteriorhodopsin from harmful environmental effects while simultaneously retaining functionality thereof. In this case the coating layer protects not only from organic solvents and surfactants, but also to a certain extent from the pH of the environment. In other words, in the microcapsule there is a defined pH which is not substantially affected by the pH of the environment of the microcapsule. Thus it can be ensured that, independently of the pH of the environment, the microcapsules or the bacteriorhodopsin/purple membrane system enclosed therein has the desired optical properties. The microcapsules can also be termed pigments. 
         [0007]    The method in this case is characterized in particular in that, in a first step, bacteriorhodopsin is suspended in the form of bacteriorhodopsin/purple membrane patches in an aqueous medium at a pH in the range of 6-9 in the presence of a water-retaining polymer and this suspension is spray dried to form a powder or is dried in an aliphatic solvent with low vapor pressure and subsequent water removal to form a powder. In this first step, a precursor capsule is effectively generated, in which precursor capsule the bacteriorhodopsin/purple membrane is fixed in a pH range suitable for the optical activity thereof. This precursor capsule, however, typically does not yet have a sufficiently stable outer skin, the outer skin can still be dissolved in water. The precursor capsule, also termed activatable powder, because this powder already has stabilized optical properties of bacteriorhodopsin, can, however, already be dried and be stored in a stable manner for a relatively long time. 
         [0008]    Accordingly, in a second step the resultant powder is preferably provided with a sheath that is substantially completely permeable to light in the visible range and is made of a polymer (or a precursor thereof, polymer or precursor preferably in dispersion in the process) and/or a long-chain saturated (preferably unbranched) hydrocarbon and/or a long-chain saturated (preferably unbranched) fatty acid (including fatty acid derivatives). In the context of long-chain saturated hydrocarbons or fatty acids, long-chain here means that (in the case of a mixture on average) at least 15, preferably at least 18, particularly preferably at least 25, carbon atoms are present. Also coming into consideration, for example, as long-chain saturated hydrocarbon, are mixtures such as, for example, paraffin, preferably having a solidification point in the range of 45° C.-65° C., and, as long-chain saturated fatty acid, for example, esters of aliphatic unbranched C20 to C30 acids with C30 to C34 alcohols (these likewise aliphatic and unbranched) such as, for example, a carnauba wax (myricyl cerotate, carnaubic acid, cerotic acid and hydrocarbons in a mixture), preferably having a melting range of 70-90° C. 
         [0009]    Accordingly, the following aims can be achieved individually and/or in combination:
       transparency of the wall material to visible light/very low inherent color   decoupling the compartment in the capsule from the environment around the capsule   control of the conditions in the capsule: content of bacteriorhodopsin (BR); pH; water content, salt content   particle fineness less than 50 μm, or less than 20 micrometers, preferably less than 10 μm   resistance of the capsules to 10% strength ethanolic solution over 24 h at 25° C.   retention of the color change functionality on storage in 10% strength ethanolic solution   the method can be employed both with natural bacteriorhodopsin and also with mutants, in particular with mutant D96N.       
 
         [0017]    The color change pigment bacteriorhodopsin can only fulfill its function when it is embedded in bacteriogenic purple membrane. This embedding is destroyed by harmful chemicals such as surfactants, polar solvents or other components, such as are typical of printing inks. 
         [0018]    In addition, the color change functionality is only ensured when the proton availability is known and constant. For this purpose both pH and the water content must be adjusted and kept constant. 
         [0019]    In order firstly to keep remote the harmful effects from the outside and secondly to retain the suitable composition in the interior, the proposed encapsulation is performed. 
         [0020]    Conventional microencapsulation methods, such as are prior art for flavors or pharmaceutically active ingredients, cannot be employed for the present problem. During the encapsulation of flavors, bathing additives or other similarly lipophilic substances, the encapsulation succeeds via utilization of the lipophilicity and an emulsion polymerization. An aqueous suspension as in the present case is not lipophilic, and a w/w emulsion thus will not succeed. 
         [0021]    Pharmaceutically active ingredients are sheathed with materials which either dissolve under predetermined physiological conditions (e.g. passage through the stomach, dissolution in the intestine) or else the materials are permeable in order to enable controlled release of active ingredient. Neither dissolution nor passage of substances can be accepted in the present case. 
         [0022]    Methods as are used for producing self-copying papers (e.g. U.S. Pat. No. 3,432,327 (1969)) are unsuitable, since they are directed towards hard spheres which must burst under mechanical stress in a targeted manner. Bursting of the capsules can also not be tolerated. 
         [0023]    Therefore, only methods for encapsulation are possible which effectively freeze or encapsulate exactly the environmental conditions necessary for the color-change functionality for the system bacteriorhodopsin/purple membrane. 
         [0024]    Color change protein encapsulated according to the invention is in a structure as follows: 
         [0025]    In a spherical shell (outer diameter less than 50 μm, preferably less than 20 or 10 μm) of suitable wall thickness, consisting of a preferably crosslinked polymer such as polyacrylate or a sufficiently long-chain polymer such as paraffin there is situated a core made of a water-retaining polymer such as gelatin, polyethylene glycol, acrylic acid-sodium acrylate copolymer, polyvinylpyrrolidone, polyvinyl alcohol or suitable polysaccharides such as gum arabic, derivatized cellulose, glycogen, starch or derivatized chitin, in addition xanthan, sugar alcohols, pectins, guar, carob bean meal or carrageenan, superabsorbers or other sufficiently water-retaining polymers. 
         [0026]    Into this (these) water-retaining polymer(s), the color change protein is embedded at a concentration typically not less than 20% by weight at a suitable pH (6-9). 
         [0027]    The embedding is achieved preferably by spray drying a solution which contains not only the color-change protein, and a suitable buffer system, but also the water-retaining polymer or polymers at a concentration of less than 3% by weight. 
         [0028]    Alternatively, the embedding can also proceed by suspending an aqueous solution of the color-change protein, buffer system and water-retaining polymer in an aliphatic solvent of low vapor pressure and subsequent water removal by suitable molecular sieves such as zeolites. 
         [0029]    A further alternative is embedding by means of coacervation by gelatin/gum arabic. 
         [0030]    Color-change protein encapsulated in such a manner is sealed from the outside by a preferably crosslinkable plastic or by a paraffin layer or another layer made of a material such as described above. An important criterion for selecting a suitable envelope material can be that the plastic, the fatty acid (or the fatty acid derivative) or the hydrocarbon, at the temperatures important for the desired pigment system, is sufficiently above its glass transition point Tg. Provided that, in addition, the Tg is not above the temperature at which the BR denatures, and provided that the merging of the polymer droplets is not inhibited by inherent properties of the system. 
         [0031]    The inclusion proceeds after formation of the core by
       suspension of the spray-dried core material in a suitable precursor of the crosslinkable plastics such as light-curable or thermally curable acrylates   suspension of the spray-dried core material in a melt of a paraffin having a melting point not above 75° C.   spraying the spray-dried core material into an atomized spray of the preferably crosslinkable precursor   spraying the spray-dried core material into an atomized spray of a paraffin having a melting point not above 75° C.   coacervation of the core material with gelatin/gum arabic       
 
         [0037]    Color-change protein included according to the invention exhibits unrestricted color change functionality even after storage over 14 days in 10% strength ethanolic solution at 25° C. 
         [0038]    A first preferred embodiment of the method is correspondingly characterized in that in the first step, the pH is set using a buffer system in the range 7.5-9, preferably in the range 8-8.5. 
         [0039]    Generally, preferably the buffer system used is a system selected from the following group: phosphate buffer, TRIS/HCl (TRIS stands for tris(hydroxymethyl)aminomethane), ammonia buffer, carbonic acid/hydrogencarbonate systems, diglycine (corresponds to glycylglycine or glycylglycine), bicine (corresponds to N,N-bis(2-hydroxyethyl)glycine), HEPPS (abbreviation of: 4-(2-hydroxyethyl)piperazine-1-propanesulfonic acid), HEPES (abbreviation of: 2-(4-(2-hydroxyethyl)-1-piperazinyl)ethanesulfonic acid), HEPBS (abbreviation of: N-(2-hydroxyethyl)piperazine-N′-(4-butanesulfonic acid)), TAPS (abbreviation of: N-[tris(hydroxymethyl)methyl]-3-aminopropanesulfonic acid or [(2-hydroxy-1,1-bis(hydroxymethyl)ethyl)amino]-1-propanesulfonic acid, AMPD (or ammediol; abbreviation of: 2-amino-2-methyl-1,3-propanediol)) or a combination thereof. 
         [0040]    With respect to the buffer, preferably care is taken that its total concentration is not too high, since otherwise the optical properties can be limited. Correspondingly, the buffer is preferably at a concentration of less than 0.03M, particularly preferably at a concentration of less than 0.02M. As already discussed, firstly the pH in the environment of the bacteriorhodopsin is important, but secondly also the water content. According to a further preferred embodiment, the water content in the environment of bacteriorhodopsin is controlled in a targeted manner. This can be achieved, preferably, by adding in the first step, in the suspension, at least one moisture-retention agent as auxiliary. 
         [0041]    This moisture-retention agent can be suitable potassium salts or a sugar-based moisture-retention agent or sugar-alcohol-based moisture-retention agent. Particularly preferably, it is a mixture of potassium salts such as, e.g., potash, with a sugar-alcohol-based moisture-retention agent, since such systems do not have a strong tendency to crystallization and do not impair the optical properties. Particularly preferably, it is a mixture of potash with xylitol and/or sorbitol, particularly preferably in the ratio 1:2-2:1 (for example approximately in the ratio 1:1). 
         [0042]    A further preferred embodiment is characterized in that, in the first step, the total fraction of bacteriorhodopsin/purple membrane, buffer and auxiliary in the suspension makes up less than  3  percent by weight. 
         [0043]    As already explained above, preferably, bacteriorhodopsin in the form of PM/BR patches in the water-retaining polymer is present in a fraction of at least 20 percent by weight. 
         [0044]    Generally, the water-retaining polymer is preferably a system selected from the following group: gelatin, polyethylene glycol, acrylic acid-sodium acrylate copolymer, polyvinylpyrrolidone, polyvinyl alcohol, polysaccharides, sugar alcohols, gum arabic, derivatized cellulose, glycogen, starch, derivatized chitin, xanthan, pectins, guar, carob bean meal, carrageenan, superabsorbers, zeolites and combinations or mixtures of such water-retaining polymers. Other water-retaining polymers are also possible, provided that they do not exhibit any adverse chemical and/or optical interaction with the bacteriorhodopsin/purple membrane system. 
         [0045]    A further preferred embodiment is characterized in that the polymer of the sheath is selected from the following group: polystyrene, polyacrylate, styrene-acrylate copolymer, polyurethane, polyvinyl alcohol, polyvinyl butyral, modified starch, modified cellulose, or copolymers, mixtures and/or crosslinked or crosslinkable forms thereof. The polymers can be, for example, polymers that are crosslinkable under the action of light and/or heat, or catalytically crosslinkable polymers. 
         [0046]    A further preferred embodiment is distinguished in that, in the second step, the sheath is generated with the aid of a spray encapsulation, preferably by means of a 3-component nozzle or by means of spray solidification, or with the aid of a suspension polymerization. 
         [0047]    In addition, the present invention relates to a microcapsule containing optically activatable bacteriorhodopsin, the microcapsule having a diameter of less than 10 μm, and having an envelope layer which protects the bacteriorhodopsin from harmful environmental effects while simultaneously retaining functionality thereof. In this case the bacteriorhodopsin is embedded in the form of PM/BR patches in an aqueous medium at a pH in the range of 6-9 in the presence of a water-retaining polymer, and this inner capsule is provided with a sheath that is substantially completely permeable to light in the visible range and is made of a polymer and/or a long-chain saturated hydrocarbon and/or a long-chain saturated fatty acid, preferably a paraffin having a solidification point in the range of 45° C.-65° C. and/or a carnauba wax having a melting range of 70-90° C. 
         [0048]    Such a microcapsule is preferably produced or producible by a method as has been described above. 
         [0049]    Preferably, such a method is characterized in that the bacteriorhodopsin in the capsule is present at a pH in the range of 8-8.5 and is substantially completely unaffected by the pH present outside the sheath. 
         [0050]    The bacteriorhodopsin is preferably present in the capsule in a buffer system preferably selected from the following group: phosphate buffer, TRIS/HCl, ammonia buffer, carbonic acid/hydrogencarbonate, HEPES, HEPES, AMPD, preferably at a concentration of less than 0.03M, particularly preferably at a concentration of less than 0.02M. 
         [0051]    The bacteriorhodopsin is situated in the capsule in the presence of a moisture-retention agent (optionally in combination with further auxiliaries such as, for example, biocides or the like), wherein it is preferably a mixture of a potassium salt such as, e.g., potash with a sugar-based (also sugar alcohol-based; see further above) moisture retention agent, in particular preferably a mixture of potash with xylitol and/or sorbitol, very particularly preferably in the ratio 1:2-2:1. 
         [0052]    A further preferred embodiment of the microcapsule is characterized in that the bacteriorhodopsin in the form of PM/BR patches in the water-retaining polymer is present in a fraction of at least 20 percent by weight, wherein the water-retaining polymer is preferably a system selected from the following group: gelatin, polyethylene glycol, acrylic acid-sodium acrylate copolymer, polyvinylpyrrolidone, polyvinyl alcohol, polysaccharides, gum arabic, derivatized cellulose, glycogen, starch, derivatized chitin, xanthan, sugar alcohols, pectins, guar, carob bean meal, carrageenan, superabsorbers, zeolites and combinations or mixtures of such water-retaining polymers. 
         [0053]    The polymer of the sheath can in turn be selected from the following group: polystyrene, polyacrylate, styrene-acrylate copolymer, polyurethane, polyvinyl alcohol, polyvinyl butyral, modified starch, modified cellulose, or copolymers, mixtures and/or crosslinked or crosslinkable forms thereof. 
         [0054]    In addition, the present invention relates to the use of such microcapsules as pigment for a paint, for a coating, for a coating formulation, for a filler, for an adhesive layer, for a hologram, for an inkjet ink, for an offset ink, for a gravure ink, for printed circuit boards, in particular preferably as pigment for a security ink. 
         [0055]    Possible applications are, correspondingly, multi-layer structures having such microcapsules, adhesives or sizes containing such microcapsules, hot-melt adhesives and also cold-cure adhesives, coatings for paper, plastic and other substrates, for example as coating formulations together with pigments and binders, lacquers, as fillers, as pouring agents, as component of a wet-strength agent, for capsules, pills, powders, tablets, suppositories, for biometric applications such as, for example, passes, identification documents and security documents, security films, labels, sealing films, transfer films, vouchers, cards, safety threads, overlays, safety fibers, holograms, bank note component, photographs, packages and packaging components, data storage applications. 
         [0056]    In addition, the present invention relates to a security ink having such microcapsules. Such a security ink can be used, for example, in screenprinting, in inkjet methods, in gravure printing methods, in lithographic printing methods (e.g. offset printing), in high pressure methods (e.g. flexography), in spraying methods, in dispensers or in the offset method. 
         [0057]    Such a safety ink can be cured in various drying methods: conventionally by solvent evaporation, by UV drying (free-radical or cationic), by chemical reaction, by heat-set, by IR drying or by combinations of these methods. 
         [0058]    Further exemplary embodiments are described in the dependent claims. 
     
    
     DESCRIPTION OF PREFERRED EMBODIMENTS 
       [0059]    With the aid of a detailed description of the exemplary embodiments, the invention, that is to say the microencapsulation of PM/BR with simultaneous retention of functionality, is explained hereinafter. The following explanations should not be used to restrict the subject matter of the invention as worded hereinabove in general form and also in the patent claims. 
         [0060]    Production of the activatable powder: 
         [0061]    The activatable powder is produced starting from a spray solution with the aid of a spray dryer: 
       Production of the Spray Solution: 
       [0062]    In a first step a buffer is produced by dissolving 60 g of KH 2 PO 4  (solid) in 500 g of deionized water with stirring. The pH is then adjusted to pH 8.3 with stirring at room temperature by adding KOH (10% by weight in deionized water) dropwise. 
         [0063]    The actual spray solution is made up as follows: 
         [0064]    Weigh out and dissolve with stirring in a water bath (approximately 60° C.): 60 g of gum arabic (FLUKA) [EG #2325 195]; 30 g of maltodextrin (VWR) [CAS #9050-36-6]; 25 g of phosphate buffer (produced as stated above); 0.2 g of Mergal D9N (Troy); 900 g of deionized water. Allow to cool to RT with stirring. Weigh out and dissolve with stirring at RT: 1000 g of aqueous suspension PM/BR (approximately 8% solids, ACTILOR); 2 g of potash (Roth) [CAS #584-08-7]; 2 g of xylitol (VWR) [CAS #87-99-0]. Readjust pH to pH=8.3 (±0.2) at room temperature. 
       Spraying the “Activatable Powder”: 
       [0065]    Spray conditions: B-290 laboratory spray dryer (BÜCHI), 2-component nozzle; inlet temperature of the intake air: 140° C.; outlet temperature (downstream of spray cylinder): 79° C. (±2° C.); aspirator power: 95%; 
         [0066]    transport power peristaltic pump: 25%-30% (ISMATEC peristaltic pump, twin-head pump, criterion: optimum spray pattern); spray air rotameter: 55 SKT. 
         [0067]    Under the above-described spray conditions, around 0.5 liter of PM/BR suspension was sprayed per hour. A violet powder is obtained which, on illumination with white light (sunlight, halogen lamp or white light LED), reversibly changes to beige. The color change is reversed back to violet after approximately 20 seconds without illumination. 
         [0068]    The product thus obtained is termed “activatable powder” hereinafter. It already consists of capsules, but the capsule walls are not yet completely inert. They can redissolve in pure water. 
         [0069]    The activatable powder can be stored for months at room temperature without exhibiting signs of degradation. 
         [0070]    The activatable powder can be processed to form encapsulated particles within the meaning of the invention with the aid of various methods. Three possible methods will be presented hereinafter, firstly spray encapsulation by means of a 3-component nozzle (A), spray encapsulation by means of spray solidification (B), and suspension polymerization (C). 
       A: Spray Encapsulation by Means of a 3-Component Nozzle 
       [0071]    Suspension: The starting material for the suspension is the activatable powder produced as described above. It is slurried to form a suspension in the following method: To 100 g of deionized water there are added 2.7 g of K 3 PO 4 .3H 2 O (solid, Roth) [CAS #7778-53-2]) and dissolved with stirring, then at room temperature the pH is adjusted to 8.3 using KOH(aq). Then, 4 g of maltodextrin 4.0 g (VWR, [CAS #9050-36-6]) are added and the mixture is stirred until a clear solution is obtained. Then, 4 g of activatable powder are added just shortly before the actual spraying of the solution and suspended. The solution is further stirred slowly during the spraying. 
         [0072]    Dispersion for sheath: starting material for the sheath is a styrene-acrylate copolymer as dispersion in water. Specifically in this case the Joncryl 77 system is used (Johnson polymer; solids content: 46.2%). In this case 4 g of Joncryl 77 are introduced into 80 g of deionized water and stirred. 
         [0073]    The acrylate dispersion Joncryl 77 can also be replaced by other adhesive dispersions (acrylate, polyurethane, polyvinyl alcohol, polyvinyl butyral, modified starch, modified cellulose, etc.). It is important in this case that the pH of the sheating dispersion is in the slightly alkaline range, in order to provide compatibility with the PM/BR system and the film that forms is sufficiently stable to denaturing molecules such as ethanol, isopropyl alcohol methanol, acetone or surfactants. 
         [0074]    Spray conditions for the spray encapsulation: In a B-290 laboratory spray dryer (BÜCHI) with inserted 3-component nozzle, the work is carried out at an inlet temperature of the intake of approximately 140° C. and at an outlet temperature (downstream of spray cylinder) of approximately 60° C. (±2° C.). The aspirator output is set to approximately 95%, the transport output of the ISMATEC peristaltic pump used is set to 8.0. Rotameter spray air: 50 SKT. 
         [0075]    A violet powder is obtained which, on illumination with white light (sunlight, halogen or LED) exhibits the BR-typical color change. 
         [0076]    This optical behavior of the powder obtained is retained in the long term, even if the powder is slurried in aqueous solution, stored at a pH in the acidic range (below pH 7) or in a strongly basic range (above pH=9). That is to say the local environment in the capsule at pH 8.3, in which the PM/BR system is stored, is not affected by the acidic or strongly basic environment outside the sheath. The optical system is therefore encapsulated from harmful environmental effects while simultaneously retaining functionality. In addition, it is also actually found that the addition of substances that per se denature the PM/BR system, such as, for example, ethanol, isopropyl alcohol, methanol, acetone or surfactants, cannot impair the thus encapsulated systems in their optical function. 
       B: Spray Encapsulation by Means of Spray Solidification: 
       [0077]    The B-290 laboratory spray dryer (BÜCHI) also permits spray solidification. For this purpose the apparatus is modified. During the spray solidification, only operation with a 2-component nozzle is possible. For the spray solidification, activatable powder as described above is used: 
         [0078]    Suspension: Starting material for the suspension is the activatable powder produced as described above. It is slurried to form a suspension in the following method: To 100 g of deionized water are added 2.7 g of K 3 PO 4 .3H 2 O (solid, K 3 PO 4 .3H 2 O (Roth) [CAS #7778-53-2]) and dissolved with stirring, then the pH is set to 8.3 at room temperature using KOH(aq). Then, 4 g of maltodextrin 4.0 g (VWR, [CAS #9050-36-6]) are added and the mixture is stirred until a clear solution is obtained. Then, 4 g of activatable powder are added just shortly before the actual spraying of the solution and suspended. The solution is slowly stirred further during the spraying. 
         [0079]    Double emulsion: The resultant suspension (approximately 50% strength of activatable powder) is suspended in molten paraffin (melting range 60° C. to 65° C.), or alternatively in molten carnauba wax (melting range 80° C. to 87° C.) with stirring. 
         [0080]    Spraying conditions for the spray solidification: In a B-290 laboratory spray dryer (BÜCHI), the work is carried out at an inlet temperature (intake air) of room temperature and an outlet temperature (downstream of spray cylinder) likewise of room temperature. The aspirator output is set to 95%. 
         [0081]    Here also a violet powder is obtained which, on illumination with white light (sunlight, halogen or LED) exhibits the BR-typical color change. 
         [0082]    This optical behavior of the resultant powder is again retained in the long term, even when the powder is slurried in aqueous solution, stored at a pH in the acidic range (below pH 7) or in a strongly basic range (above pH=9). That is to say the local environment, in the capsule at pH 8.3 in which the PM/BR system is stored, is not affected by the acidic or strongly basic environment outside the sheath. The addition of substances that inherently denature the unprotected PM/BR system such as, for example, ethanol, isopropyl alcohol, methanol, acetone or surfactants, also cannot impair the thus encapsulated systems in their optical function. The optical system is therefore, in this exemplary embodiment as well, encapsulated from harmful environmental effects while simultaneously retaining functionality. 
       C: Suspension Polymerization 
       [0083]    A suspension of activatable powder in aqueous solution is produced as follows: 
         [0084]    Starting material for the suspension is the activatable powder produced as described above. It is slurried to form a suspension in the following method: To 100 g of deionized water are added 2.7 g of K 3 PO 4 .3H 2 O (solid, K 3 PO 4 .3H 2 O (Roth) [CAS #7778-53-2]) and dissolved with stirring, then at room temperature, the pH is set to 8.3 using KOH(aq). Then, 4 g of maltodextrin 4.0 g (VWR, [CAS #9050-36-6]) are added and the mixture is stirred until a clear solution is obtained. Then, 4 g of activatable powder are added just shortly before the actual initiation of the polymerization and suspended. The suspension thus produced is suspended in a dry aliphatic solvent (cyclohexane or petroleum ether). If necessary, a surfactant is added for adaptation of the surface tension. The solvent is dried by pouring in molecular sieve beads or by forcing in sodium wire. The work should proceed under sharply dried air or under dry nitrogen. 
         [0085]    To this double emulsion, cyanomethacrylate or cyanoacrylate (obtainable, e.g., under the name Hernon Quantum from Ellsworth Adhesives, US) is added dropwise with stirring. The stirrer speed is selected in such a manner that the size of the suspended particles is less than 10 μm. Around the suspended particles of activatable powder with sheaths of polycyanomethacrylate or polycyanoacrylate form. 
         [0086]    Here also a violet powder is obtained which, on illumination with white light (sunlight, halogen or LED) exhibits the BR-typical color change. 
         [0087]    This optical behavior of the resultant powder is again retained in the long term, even when the powder is slurried in aqueous solution, stored at a pH in the acidic range (below pH 7) or in a strongly basic range (above pH=9). That is to say the local environment in the capsule at pH 8.3, in which the PM/BR system is stored, is not affected by the acidic or strongly basic environment outside the sheath. The addition of substances that inherently denature the unprotected PM/BR system such as, for example, ethanol, isopropyl alcohol, methanol, acetone or surfactants, also cannot impair the thus encapsulated systems in their optical function. The optical system is therefore, even in this exemplary embodiment, encapsulated from harmful environmental effects while simultaneously retaining functionality.