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    • 专利摘要:
    The present invention relates to a three-dimensional cellulosis molded body having an optically detectable core-shell structure, wherein the shell has a higher density and a lower crystallinity than the core and the core has a sponge-like structure. Furthermore, the invention relates to a method for producing this shaped body and its use, in particular in cosmetics and pharmacy.
    公开号:AT515180A1
    申请号:T794/2013
    申请日:2013-10-15
    公开日:2015-06-15
    发明作者:
    申请人:Chemiefaser Lenzing Ag；
    IPC主号:
    专利说明:

    Lenzing $ Mi P18546 endMlsrnVen ^ hdugg
    Pouring broadcast describes iw neui ^^ 'type of Cipiiiose * H # sspeifts as well as suitable processing methods. The properties of dimer particles make them especially suitable for use in Köcmetife and pharmaceuticals. The particles are formed by a black-horned fine structure in the interior, which is surrounded by a fabulous feishhila.
    Stsndiarteehhik;
    Geiluteseguivaf and other systems, up to parfeläm Celteiosenenihalien, have been known for a long time, and it is also on this Gebsei speÄ in the last «
    Years has increasingly given new intwisktengen. The most widely dried fibrous powders which are formed by the pulping of pulp by means of suitable aggregates, produce a variety of qualities after the use of shredding methods, and a variant may also be considered here, that not pulpis should be crushed directly. The particles obtained contain, in addition to non-eponymous, "other substances, such as llgnini or Hsmiceiiuiosae in higher proportions," and exhibit greater variations in homogeneity., Due to the macromolecular structure of cellulose, all previously described powders are fibrous, d, h, the particle species pronounced UP ratio on
    Another widespread gravel from Ceiluic seepuivores are the so-called microcrystalline solutes (MCC). In addition to mechanical decomposition, the treatment of Shore with MCC is carried out in addition to the mechanical decomposition, which degrades the: amorphous "parts of cellulose" and a matenai crystalline portion is formed. "Depending on the method used, the individual crystals may be brought into later-shifting forms - so here" fibrous particles "are the aggregates / agglomerates of approximately spherical Perm.
    In. MCC or konvendoneliem fibrous geiioiosepuiver are the possibilities to incorporate or apply additional Msteriaiten in the Pa dike] limited an application of additives is only as coating or ice storage in the aggregates or agglomerates «possible. A frequently used
    Procedure Is dabate oils; Granuleikm, wherein the desired final particles of smaller particles are built up, partly these Aysganpparflksl had been self-made again by grinding, which makes the whole process consuming.
    All the materials described hitherto have the same microstructure, that is to say an arrangement of the ceycinnase molecules which is referred to in the specialist literature as a structure type - in this case, the cellulose "! Structure. This type is that which is formed by plants and is also changed by the methods used in the production of the already described particles.
    In addition to cellulose »! There is another common type of struc- ture known as cellulose, which is the thermodynamically more stable form. The two types of fructies can be easily distinguished by X-ray analysis or NMR, and supernatants can be allowed to dissolve in suitable solvents followed by regeneration in cellulose. This process is also used in industrially used processes for the production of fibers, such as in viscose * and in LyooelF. There are also a number of publications on the subject of ionic liquids as solvents for cellulose ", which is still outstanding in this case The method is that by dissolving and subsequently regenerating the cellulose a much more variable shaping of the particles is possible. Indeed, natively spherical particles are actually possible here, without having to be built up from subunits in MCC. Another advantage is that as the process progresses, additional substances may also be incorporated directly into the particles and, of course, superficially applied as well.
    Hubs of these dry powders of fibrous or spherical particles are also suspensions of cailulosischeo particles, often referred to as cellulose gel. The simplest method of preparing them is to disperse suitable water in water, but the trend is clearly more sophisticated. Ancestors and materials. In the last tent, especially micro- and nano-cellulosic cellulosic suspensions are in the center of interest. They come under a variety of names such as
    Lending A Approx. PLD546 MäCroTipfsiiierce weiSM ^ o & e rii.) Oasr Napöeiiuiuwsr "ot," kitulw m "fe; sasieivkwho ©" again be based either on Ceüulosa'i or cellulose. The processes here are usually very elaborate and energy intensive and only conditionally transferable to larger scales.
    As this grebe review already shows, the skilled artisan is well aware of a variety of analgesic paftic systems to which he may depend. Thus, the fields of application for fulgurous particles are now diverse and range from the perspective of nuclear fusion to mPharmacy end cosmetics. With the known particles, many applications can be covered. but this is in addition to additional expenditure, since the requirements of the existing defects are not completely fulfilled, and in addition © Verarbeilungesohride {modifications) are necessary,
    In addition to pure caty ose, fjords are also used in cosmetics) © flieheCeJIulosadsnVaie (such as methyl pills or CadsSkymethyfeelfolös ©) «omisins, some of which are soluble in water In addition: © s a V! Eizsh !: of particles on mineral © of synthetic Aysgeopdäsis Especially the more modifi ed possibilities of modification have much more complex properties. Especially elaborate cosmetic products contain a large number of fertilizers to achieve the desired effects, which of course makes the formulation a complex process The spheres were then dried by a thermal exchange, but the structure of these spheres is not revealed, nor is the appearance of the Kupin nac shaping, such as washing or removing pesticidal agents, is not specified
    Df ©; WD20SM / Ö | B4SÖÄ1 ofehbart dl © Annunciation of spherical Geilufosepardkel from as amorphous as possible Cellülossiieung, with several Zerkleinarungsachdttesiatttnnden. This document reveals that in the first deconvolution stage, other aggregates can become a subprpiggiator © ingpbtxt. What structure has this done © Intermediate product is not revealed
    Subsequently, the m intermediate intermediate is further reduced in the never-fused state.
    In WO 2009/037146 Caflüloseperleri are also disclosed. These are stork-like growths cjueiv © met2t (to increase the firmness, cross-linking also causes an almost complete loss of the beneficial properties of the celluiose beads,
    WO 02/57319 discloses monodisperse celulogenesis, but does not make any quantitative statements beyond their internal structure. However, in the examples, a maximum of 4% by weight of cellulose is used, which suggests that the use of high concentrated cellulosic adhesions was not possible with the invention of WO 02/57319, US 2004/011090 teaches the preparation of celMoseperiän for use in cosmetics, Rharmazie or similar areas, Oie Cefluioeeperäen are formed by agglomeration of microcrystalline cellulose with additional additives, The cellulose beads are therefore rather a »rogranuiab or, Agglomerai and no compact cellulose panikei. The structure of cellulite beads is not mistaken
    A review on Calluloae beads can be found in ,, M, Gericke et. A .. · Functional Cellulose Beads: Preparations, Characterization and Applications, Chemical Reviews113, 21, p. 45 " 2 * 4836 ", however, the manufacturing methods described are ascribed to taboos, patterns and the like, but are not described in detail, and the relationships between manufacture and structure are only suggested. Most of the article deals with the further functionalization of cellulosic beads,
    A more detailed description of the relationships between the production of celluiose beads and their structure can be found in "J, Trygg et. ai "Bhyaicochemiea) design of the morphology and ultrastructure of pellet beads. Carbohydrate Polymers 93, 2013, p. 291-290,1: Described is the solvent system HaOH * urea with Celluloeekonzentratlonen to 6%. Under certain conditions, according to this document, Kem-Holio structures can be created using the bedsing A & PJS4§ shell, however, usually only a few pm thick. Only under the conditions of the uterus (1ö-motam-nitric acid) can the thickness of the skin be increased to SO pm: otherwise it can hardly influence standing. Itesganauar® CCsrakteHsferüng of hell (for example: In Versieh sum Kam) stands stad.
    So summary must be fesigesteüt that in the state of the art for applications in cosmetics and pharmacy only such ceitelostecba Partlk® It is important to note how slow, controlled fifties of pharmaceutic or cosmetic substances change the effects of overexposure, such as on prick ("stimulant keappdse") and |, sanserte "| göstaf ^ properties in kwasss ^ Among other things, you are very energy-intensive in the artifacts, but on the other hand, in the prior art, oesculosis particles are already known which have been known for their use Applications © rferdsiiCHi f ärtikelgrää © herekshave, rather, these particles do not have the above-mentioned functional properties.
    Problematung exists especially in the härsrrtigsnAufungsbereichen cosmetics and pharmacy still a need for CeilUlosepartikain with correspondingly improved properties. 0 < e particle söllfand these properties already by itself mitbhngert and these not only by t'teädausätzilchan step in the preparation or by the addition of other aids, such as cis | atat cum part necessary. The following characteristics are of particular interest: slow, coniroiliary release - "sloviccicase" - by tphamtsseufisph or cosmetically), change in the rate of ulceration; | fnwfri "un§ ~" stimulationPasponsW * (about on pressure), improved quality, defined internal structure (For example, one clearly defined, reproducible and reliable, and defined, oversight) .This, and possibly other functionalities, are to be incorporated into the manufacturing process during manufacture.Additionally, the manufacturing processes may be feasible, so that they can be easily implemented It is also intended to simplify the formulation and preparation of the final product in the case of a daily drop, since then fewer inhalants are needed, and another advantage may be obtained by using new synthetic cellulose particles can be. This could address the increased demand for renewable raw materials,
    The solution according to the invention for the above-described task consisted of not constructing the cube tubes from subparticles, but rather in a stepping stone. More importantly, the Wehl of the corresponding behavioral parameters applies, as they already define the properties of the particles.
    Saechreltag the invention
    This object has now been achieved by a three-dimensional cellulosic foam body having an optically fixable Kem * M "fitef" structure, wherein the sheath has a higher density and a lower crystallinity than the core and the core has a spongy structure "optically detectable" means in Eusemmenhsng with In this case, the microscopy is suitable for both dry and swollen samples, while X-ray is for dry, especially dry, samples and NMR spectroscopy on shaped bodies In the swollen state, Pies responds to the need for the preparation of frog preparations. Since the effi cence of the shaped bodies is prepared from a ceiuiosel solution, they always have the structure type of Cellulosedl.
    The shell of the inventive permeable body preferably has a relative density of 66% to 8% and the core has a relative density of 20% to 60%. Oierelative density is related to compact cellulose, in a preferred Ausföhrungstorm the manteidicke between §Ö pm and 206 pm. tensing AG, FLO 54b
    Since the ratio of the thickness of the membrane to the total diameter of the shaped body is preferably between 1; S and 1-SO.
    The preferred preparation bodies are preferably substantially hypersensitive, but may also be cylindrical: ellipsoidal or ovoidal. However, the ratio of the half-axes (length: diameter) of the shaped body should not increase 3: 1,
    The shaped bodies according to the invention can be further dried depending on the application, either dried or never dried, the non-dried variant of the gellulose preferably having a firing rate of 25% by weight. based on the amount of cefiùsuf.
    Depending on the purpose of use, the disinfectant may contain additives which have been incorporated during their preparation,
    Dips® Substance Substances are preferably selected from the group comprising ZnO, TlOg, CaCoj, CaClj, kaolin. FesOg, aluminum hydroxide, kaolin ,, color pigments based on aceto-teto base, activated carbon, superabsorber materials, Fnaase®, MateriaSi®, flame retardants, siozides, chitosarrs and expanded polymers and biopolymers.
    Further, the molded articles of the present invention have a babies water repellency (WRV) capability. The WRV, for example, after two hours in VSWaaser for typical cellulosic dried cellulosic typically in the range of 70 * 90% by weight and supercritically CO * dried or freeze-dried celleiosepeden, is typically in the range of 12% to 10% by weight.
    The subject of the present invention is further a process for the preparation of the abovementioned three-membered aelulasiotic vegetable body having an optically detectable core structure according to the invention, characterized in that it comprises the following preparation: a, dissolution of the cellulose csmäE a Lyoceli process to obtain a solution with 10 to 15 wt .-% to obtain cellulose; b. Bvtrusion of the pure solution obtained in Sehnrt a without air-pass directly into a precipitation bath; c, regeneration process, wherein at the onset of ceiMoselösung inPolifsad the difference of NyyO-fonzentratienen of Celfutosetösimg and Fälibad IS ~ s wt.%, Preferably 40 »» g wt.%, and 'the difference in temperature of Ceiiuiosaidsuno and Fälibad SO - 120 K, preferably 70 ~ 120 K, particularly preferably 80-120 K in amount; d, washing process gamin the Perkoiatsonsprinzlp with at least one alkaline Wasehschrifi prefers hot pH 9-13; e, optionally, a drying process by which the exterior of the mold body is not damaged abruptly; wherein the laundry referred to in item d <) is preferably multi-stage and countercurrent-containing and contains at least one alkaline step
    Possible dissolving processes are, for example, the viscose *, the lyocell or the copper ammonium process; also, lautering the cellulose In NaOH or suitable ionic liquids is possible. In general, the invention is not restricted to specific solvents or processes, but the use of different methods can additionally influence the structure of the particles obtained. However, preference is given to the lyocel FVerfahrao which is generally known to the person skilled in the art, described inter alia in EP 03BS419. In denepthnmeeae men "during their nomdation, in jodom fail but ver-and Kimien ien, in addition substances are incorporated, as already described above. Starting from the Ceiluloselösung takes place the shaping, in which - especially in the Fäliungsprozess ~ care must be taken This is not a trivial requirement because celululose tends to form fibrous domains because of its macromolecular structure. This problem is alleviated by first rendering the cellulose solution into the desired shape without significant shearing and, also, the regeneration conditions be selected accordingly. It is imperative that the cellulose solution be directly, d, h, without air gap, in a Pllbädeztrydiert and the reduction of the solution strand on a Waisestattet that results in substantially equal particles, Suitable aggregates for this step are about underwater * or Btranggramriaforen, which next
    Lending AG, PL0S48 spherical particles also cylinders, Dreheiiipsoide and Ovoide eräugen sa§§ ^ n &gt;
    The aggregates mentioned above fulfill the obligations of making changes to the process of division. The particles produced are said to have a maximum of almost 100% of their size, allowing them to be controlled via the feeds. At the same time, the process should have a throughput. Granules can be produced from tyoöeii * losnnmaesa beispieiÄlseml an underwater granulator Eeon type BUPSO, depending on the execution of toshplafte and osenisch high throughputs of 2 to 30 kg / h - calculated on 100% cellulose , NMMCMrei washed and dried finished product ~ are possible. In the alternative, such solid-liquid separations z, S &lt; &numsp; &numsp; &numsp; &numsp; and &numsp; &numsp; &numsp;, may be separated from the process vessel by a mechanical centrifugal oroknar. By means of hyperpicyclopters, by-products, or also by way of demonstration, erenulators are available from various sources on the market, and due to the simplicity of the method of granulation of particle size, the emphasis on large-scale species is relative. So only one
    Gfenuiator ümType IUP 3000 about 5000 tons of pellets are produced per year. Furthermore, much larger machines are available from other Nemfeliefh ncdi; in a walteran branch, geliyiosestrands can also be made with special lyoceii nozzles with oxy-silhodorshrnesse Vbh 0, ssls, mm, which are, according to a series of measures, a sintering frangipr ^ in this respect; washing, feeding and feeding of the individual rods into the stiffener, the strands being very flexible. Cylindrical granules have been obtained on these catfish.
    ROLLING INFLUENCES IN THE PROPERTIES OF © rhÄR®nFlrÜkei haf aur ^ dp ^ skoai ^ oof the egg-infiltration. since these also have a normal viscosity or difference in viscosity between the gel solution and the fat bath, the precipitation bath is preferably aqueous (with a viscosity in the range of 1 Fa, s), however
    (Polymers) the viscosity of the felibody increases significantly. The lower the difference in viscosity results in a thinner küantei. In accordance with the invention, CefWose solution and precipitation db of mind, 600Fa, s, preferably in the range 7§0-T2O, Ps, $. parogen syf the NullvisköÄ).
    The presence of the Msntsl is decisively influenced by the N.MMO in the precipitation bath when the celulose sols enter into the precipitation bath, the greater this is, the more the mentet is formed in accordance with the invention, the maximum difference is when Pure water is used as the precipitation bath and the fifting bath is thoroughly mixed at the point of entry of the carbon dioxide solution so that all the exiting NMMO is immediately transported away.
    The thickness of the coat will also be affected by the camouflage on entering the cellulosic solution. The coarser it is, the more coarse the coat of the granules made according to the invention becomes,
    Hubs of Unfewaasargranuiiereng in a liquid * Fllfbade you are the Mögilohte the coagulation in a gaseous medium,
    In the large-scale Mafktsb is the Gegenstromwäsehe to adhere to the necessary amount of wash water and the Rückückungatesten in order to achieve the required © purity of the moldings, 10 to 12 washing steps are necessary for this. In addition, if there is an increase in the washing temperature, it is preferable to have a washing water temperature of from 60 * 0 to less. In order to remove even small amounts of the growing agent of the solvent, an alkaline step is additionally necessary, preferably pH of 9-13 being used.
    In particular, all types of FesbFiössig extractions in Continuous or File & eMeb are suitable as methods for the industrial laundry according to the invention. However, preference is given to methods according to the invention of the peroxidase pnnzip, d, h, with a cross-countercurrent wash. Suitable apparatuses for this are, inter alia, koulusseliextraktoran or Eztraktoren the type Pe ^ Smst, Crown or Bellmann. Also, cascades are suitable for this purpose. Such extractors are also used in the treatment of maceration, pusher joints would also be suitable in principle, but it is important for the method of the invention that shearing or crushing of the granules be avoided as far as possible, so that centrifuge "© H® Might come question. Weilars suitable columns nachdemionaafauseherpnnaig, wherein the solvent for cellulose preferably above the column votvoben down vardringiwird, these can also be tu cascade ordered »
    In view of the multiple uses of the products of this invention, it is important to remove the MM MO as completely as possible so that MMO may have an oxidizing effect on some of the active ingredients that are later incorporated into the products.
    After being soaked, the excess in-moistening moisture should be removed from the particles to minimize the trocar coagulation and render the granule drizeable. Suitable aggregates for this purpose are centrifuges and decanters as well as Bendfier which can be operated continuously or dsskonflnuieriteh »
    As additional Prozesssohnit can also follow the wiping of the granules also a Pampfsferislerung. The steam recovery rate reduces the water retention of the never-dried ceflufe beads and pre-drying before drying can be more efficient this invention. As a result, the very open pore structure present after regeneration and washing out of the solvent is retained and the cellulose particles are visually receptive and accessible. "
    Furthermore, the coagulation of the dope with the aid of the above-mentioned aggregates produces a cognac / manganese dioxide. This © Karn / Mania structure is evidenced by a compact transparent shell and a spongy white interior (core) of the beads.
    This structure is responsible for the controlled release properties of the molded articles of the invention in the delivery of cosmetic or pharmaceutical agents, since the active ingredients which are readily available in the spongy interior of FL0546 must be able to overcome the very compact appearance of the delivery aMibistobi is thereby delayed. Thickness and structure can not be changed in the future.
    Between writing d. and step e. For example, an enhancement action may be performed to describe in detail the functional properties corresponding to the form-hearing function according to the invention. For this purpose, one or more enzymes, selected from the group consisting of Sxo ~ and inde-1 sd-b ^ lucenaseb, giueosiases and xylans, are preferably used. The uranium-doroid is 'smoothed' by an idless, which is attacked in the middle of the surface, but also the porous structure in the interior. From this, it can be shown that enzymes can intervene in the interior of the radical, so that the enzymes of the particles can penetrate by means of an ensiphoning action, enzymes or proteins can penetrate into the interior of the beads, and a loading of the orphan more accessible to the orphan With these dandruffing is possible.Dt © inzymbehanniung the beads shows: that both enzymes and proteins can be taken up by the beads, these can also be used as encapsulated immobilized bm immobilized.
    On the one hand, the eggshell of the cervical nerves can be dramatically altered by the variably deformed shape of the aura, but on the other hand, both the interior of the globule ice can be changed Outer skin by chemical upper enzymatic modification, which changes the precipitating fluid parameters. that the Küptehon are already pressurizing between their fingers and thus balling up their in-bedded cbelsgie way of training an idydrogei). The resulting by the AufpiaizersKügejchen © Nydrögdf has very inleressaoto cosmetic properties, oo is kainedel stickiness, greasiness or oiliness of this hydrogel detectable; Also its Pardkeigmia and granularity can be adjusted individually by the duration of chemical treatment, an anteptive treatment or even change of the hydration parameters. As a result, the beads can be used as a turmeric in cosmetics.
    This StimuikResponse effect is for the Kosmotik »or Prtsrmosiktof of particular importance, since z3, cosmetic or pharmaceutical active ingredients, in addition color pigments or, colors of decorative cosmetics, which were brought into the beads ©, ges gesielt fraigesetzi can be. Furthermore, the beads may be used as a peeling or exfoliants with StsmulFResponsedlffekt, These beads may contain inside abrasive particles or even standards that can be released by the Aüfplateen in triturating the beads and thereby achieve the desired peeling effect, the StimulPRospohose " Beads can be individually adjusted by the duration of the chemical modification, the enzymatic treatment, or also by changing the fluid medium.
    For certain applications, particles with only low moisture gel! of advantage, the particles according to the invention can be dried by means of different drying varnish. In a preferred embodiment of the invention, the drying process is carried out by normal pressure drying drying, drying, freeze-drying or super dry COI drying. Drying is a challenge in that the product moisture is very high. In the case of celulose beads, moisture contents of T0 »T5 oaw.»% Must be allowed, up to the equilibrium values of 10 -13% wgt%. for some applications must be dried to <% by weight. To protect the product, the drying should take place according to the invention as kontakilos possible. Surprisingly, the drying in the fluidized bed process has proven to be particularly gentle and efficient. Due to the permanent circulation and loosening of the material, it promotes the expulsion of the humidity of the city. In addition, the drying is very product-friendly with regard to abrasion. In addition, high throughputs and short drying times can be achieved. This, in turn, causes the yellowing, as manifested by the action of elevated temperatures, to be low in Europe, and the process can also be operated continuously. Heap densities of the material, as they sometimes occur in other drying processes, would cause the moisture to dwell very long between the grains, thereby increasing the drying time immensely and adding to the long term temperature increase the risk of yellowing. Examples of such were conical crookers or crystallizers In addition, in these aggregates, through the tubing: a high degree of product orientation, which rubs off the outer skin and creates a great deal of dust. Furthermore, this abrasion also changes the pitch of the Mentslschfcht Om which destroys the Centroiied-relesee properties of the product. These aggregates are therefore not suitable for the process according to the invention,
    As an alternative to the invention, vibratory scanners have been seen to provide similar drying benefits. These may be advantageous for certain incorporated products since they are dried under vacuum at low temperatures.
    A further advantage of the alcohol layer method is that it can be both dried and coated with additional material in a process document. The possibilities in the coating process are manifold. For example, the oranges can be colored or functional substances can be applied, for example biopeiymer © (xB Chüosan etc.), Synthetic polymers, active cosmetic or pharmaceutical active substances, enzymes, protein and separating agents as well as grinding agents. Also a chemical modification of the surface of the birds in the fluidized bed is possible. Through the coet in the fluidized bed, the distribution of the coating over the boulders and the top of the individual particles is very homogeneous. Surprisingly, it has been found that the coated, fluidized-bed, dried form-drums continue to have very good oil-yielding properties.
    By selecting appropriate drying methods, the pore structure and density of the effervescent Porm bodies can also be significantly influenced. However, when subjected to an 80X hormone compression in an ultrafine rock tube, the sponge-like structure of the never-dried beads collapse completely to give a nearly transparent, compact, much smaller bead, but retain its ellipsoidal shape. However, this effect of collapsing the structure inside the beads is in part reversible the beads swell again in water. At atmospheric pressure, fluid bed drying showed that the sponge structure of the never-dried beads was best reproducible by subsequent dueling in water, as previously outlined
    The sponge structure, however, could be obtained much better when the leaves were dried by stinging jellyfish in liquid
    Nitrogen and subsequent defrosting Hetgestei were. In doing so, © shows that these dried beads are no longer transparent, but white. This is an ingredient in preserving the pore structure. However, the surface and shape of the beads changed very much during drying. Daserhakena was mainly true of its eipsoid ferms, but harbor formed on the surface like dents and craters, similar to a lunar landscape. The kaheohene thus gave a rather peculiar appearance, and the density of these cows was lower than that of water.
    In addition, the water in the beads was launched against AeMon by the supercrossing coarse drying. In this dressing, the original shape and porosity of the never-dried yeast beads were the best become. These had a poisonous Bonn with gtafer Dbariadhe, The fine fine structure was shown by the white color of the beads. Also these beads had a low density than water.
    Another object of the present invention is also to use oils of the present invention; due to their unique structure, they can be with you much better Widisföllsn Mieden,
    Inventively, the molded articles may be used to make an active ingredient carrier styrene, with the solution being warmed with a solution of the active ingredient and then washed and dried. In addition, they may be used in the manufacture of effective heliacal adhesions with controlled release properties for cosmetic and pharmaceutical applications. For this purpose, a prior grinding of the shaped articles according to the invention may be necessary.
    The following applications are better preferred: aromatic amyl ions, gel emulsions, heat-treated products, saturated spfproduct, sunscreens, cosmetic serums, deodorizing appliqués, mock-uj ^ gfursdlage and FarbKosmotlk. The active ingredients may be, for example, enzymes and peptides for cosmological and technical applications, such as coenzyme QI®.
    According to the invention, the fenakobodies can also be used as abrasive material in cosmetic products, such as, for example, Feelings or * xföiiatof * Means, wherein the average size of the shaped bodies is ISO ~ 80 $ pm, preferably 200 - $ 09 pm. especially preferably SSO - $ 80 pm
    Likewise, the body bodies can be used as optical effect sheets for cosmetic products, preferably shampoos and creams.
    Pie formers have been used both in the never-dried ice and in the dried state to produce algae powders for producing spherical candy powders such as Sensorio-Sooster shadows in oil-water miststones. The molds are preferably used on various grounds by various methods preferably d 'o * spm ground, you will then fö Their main advantages are that the end products have less stickiness and greasiness, as well as improved absorption of solder into the skin. Particular preference is given to natural eye creams, men's care products, cosmetic products, sunscreen products, cosmetic serums, pesodorising preparations, yake «« p » Grendiagen and Fsrbkosmetik,
    In the technical field, the above-described molded articles can be used as silver matehal in chromatography, especially in the polymeric, reverse, ionic, affinity, and silica biosomatographs. For this, the molded articles can also be chemically modified, for example, by acetylation, mathoxyation, or similar methods.
    Furthermore, the forerunners described in Öberi initiate the mobilization. of enzymes, or peptides may be used to increase theiranalytical activity or stability. Particularly useful for this is the safe in cosmetics &quot; and technical field, Likewise, the odes described Eormkdrper invention are known to be used for the immobilization of Teilmemdiiichen, animal or pflan & ichan origin (bacteria, Pifee, tissue, Aigen, etc.),
    Examples
    The following examples are given to illustrate and better understand the particles of the invention and their inhibitory properties, but the invention is not intended to be limited to these exemplary embodiments.
    Example 1 - * Production of Cellulose Peden
    The starting materials used in the preparation of the Ceilutoseparltn a standard Lyoeeilspinnmasso was used with the following composition; 13% by weight of pulp {100% Saiecork TS, 3% by weight,% NMMG, 11,7% water and traces m
    Stabilizer, Dia dope was kept at 12 ° C and processed by means of underwater gramer EGON EUP SO. It was consistently usedochpiattan with 12 holes and 4 better. Anfahrvenffff and sohpiaftewurden to a constant 120 * 0 tempered, the water tank to 20 * 0, Table 1 summarizes those parameters that were varied during the experiments V1 to ¥ 6,
    Tak «ks 1
    The underwater ampules of haricic acid celulose were precipitated in pure yoiianisafete.n water (FVE * water) and subjected to an 8-bit filter with 8C * C hot-water of a wash in a column. The delicates were washed with caustic soda (pH 11). After the caustic soda, the birds were washed neutral with VE water at a temperature of SOX and boiled to a residual yield of about 70% by weight.
    Pie Structure of Never-Dried Particles from Experiments V1 to VE was examined under an optical microscope (Type 2eiss Discovery, VI2, Olympus PP-1). All of the particles showed a pronounced Kem-HMe structure. Figure 1 shows ice cream sample! © in particles from VI.
    Vitts is the software ÄnsfyStS S, Ö of Olympus was the disks of hell, where five measurements were conducted and averaged. The results are also summarized in Table 1. A significant dependency of fdameidisk © was found by the Repfterafiensbadlngoftgan, increasing the NA ^ O concentration in the bath taw, with elevation of the tamparade the thickness decreases beyond the outer layer,
    Walter's m realize that the outer skin traps i $! &Gt; while the inner sphere is 8! This clearly shows the different structuring of the material. Dia transparent # layer is very dense whereas the white and the lighter the Cellutase pentane has a sponge-like structure 6ifta detailed characterization of the KermHüile structure can be found in example S
    Example 2 * »Loading with Active Rescue 20 g of never-dried cellulose beads VT from Example 1 (68.3 s.c.) were treated with 40 ml of a 3% wt.% Paracetamol (Merck) in ethanol ρ A solution This suspension was stirred at 100 rpm for 120 minutes. The loaded Calluiöseperien were filtered off with suction and washed with 10ml voiientsalztem (VE ~) water and then dried in Vacuumtrocktnsohrank at 40oC, 150 mbar for ea * 8 h, The Auswasga of the dried Cetlutosepeflen was 5.8016 g, loading the Celuleseperien with
    As reference substances, felgende materials were used; Teneeli) CP 4 (spherical Cefiuicsaputver, manufacturer Lenzing AG), TonesI® Gei
    From this were also suspensions with paracetamol, prepared in ethanol analogue according to the invention CeiMoseperlen, weave! the ratio of cellulose to paracetamol was always kept constant. The Vergieionsrnaterialien, however, were not dried in Vakuumtroekensohrenk because this would have led to clumping due to the fine particles, but by means of spray dryer Buch! i2S0, Table 2 summarizes the properties of the loaded particles.
    TsfeÄ 3
    Bösspal 3 - RalaaseA / ereuohe
    The release rate of paracetamol from the charged particles prepared in Example 2 was readily determined using the method described below. To this was added 100 mg of the particles in 30 ml of aqueous hydrochloric acid (0.1 ml of pH 1.2) and 100 at 37 ° C stirred (stirrer: Eiweks Dfe & okitionTester DT 820). At regular intervals, primes were released and the absorbance at 243 nrrs was measured against a reference (pure aqueous hydrochloric acid) (Perkin Elmer Lambda 050 UV / VtS spectrometer). "In Figure 2, the tracers are dargaaiatii of various particles
    It clearly shows that the cellulose beads according to the invention show a significant anti-catabolic effect on the active substance paracetamol. This retarding effect is very strong in comparison to powdery particles which are loaded by spray-drying. For the particles which have been taken from the Celutose-CSefberg, the highest loading can be achieved due to the even more open structure. However, also here the release takes place abruptly Only the causal pearls show their inherent structural slowness properties.
    Example 4 - Drying (inki, Coating)
    The never-dried Caltulosaperian VI from Example 1 (residual feucbia 83.13%) was spiked with different drying cycles to investigate its influence on the structure of the dried particles:
    * YrockensabrardLbm6ö''C «Wirbalsehiehttroeknung (in a yvirbeisehichfesseskner DMR WFF-8) böi100 * 0« &gt; Drying with supercritical COj {5 Habcranisge Natex) - heat-exchanging to acetone {"soCQyT roeknyrsg · *) * freeze drying Cisbeancb Fteeeöhöh 2.5 liters, vacuum 0 mbar) after freezing in liquid Mg
    Beside the swirling dryings were carried out still more Coailnguarsuebefore. In the meantime, aqueous dye solutions (Wae © blad, Waec pink, SaptCcst 3013 Yeitow * Sepiflim Gloss, Sepicosl 3404 Green + SepifltniGloss, Gspiccaf 5001 Brown * Sepifslm Gloss) have been used in the vertebrate salivary. Old exposed particles showed a homogeneous coloration on the surface.
    In all vaccine vectors, no shrinkage could occur in the particles. For example, after elution, celulose pads have a dry consistency & bulk density of 0.74 g / ml, while the never-dried oalluiase beads adhere to a bulk density of 0.22 g / ml. The increase in bulk density directly indicates a decrease in the particle size, Figure 3 shows typical structures obtained from the various drying tubes: * Left oven * Transparent to slightly opaque oeufuioseperie with rough surface * Middle: ss ^ CGrlcation - »white and co-egglose with smooth surface * Right; GroWing * white Geiluiosepsrle with smooth, oberformed surface
    However, the drying process has not only an influence on the appearance of the particles, but also on their internal structure. Dacu has determined the surface area of the particles by means of adsorption of BELsorp mini II). For this purpose, no cepe- Oberfläohe be determined, which means that the inner pore structure is completely collapsed For the se ~ Cös "§etr0cknefe sample a BET Oberfiähehe te» 174 m * / g was requested, which. With Sggr ™ 46ma / g, the freeze-dried pattern is as expected from the other two methods; in Figure 3a, the pomegranate distribution of 6 * C0g * geftödknetan Caiyoseperlan is determined by means of a BJ, H, Pieta (FIG. calculated from theNrAdVOaserption), which sets mainly sm range of 2S nm «
    Furthermore could by Heliumpyknomatris (Pycnomatlc ATC of the company ThermeFssher / Porotec), it is proved that the coextruded carbonization episodes produce an offanporous structure, whereas the freeze-dried ceïsseous perteol fills a closed-triangular structure,
    Example S '"* Characterization of the core-hats structure
    On the never-dried samples V4 and Vf of Example 1, which have a well-behaved thickening (TS pm bm, 182 pm), C15 CP-MAS-HMR measurements were rotated (Spectrometer Broker Avance DPX 300 NMR, 7, OST magnetic field strength Uffrahaiefd (SB), 2 rf channels, 100 / 30Ö W 'HBB amplifier, 4mm' N / B8 Festkdfpef CF-MAS Pfobankopf). From these measurements, according to the "G. Zuckersiltter et, Novel Insight into cellulose sypmmotecular structurethrough 'SC OP-MAS, NMR spectroscopy and paramagnetic relaxation enhancement, Carbohydrate Polymers 83 (2013), p. 122-128 &quot; The methods described are intrinsic tristain (IC), whether or not related to tumoral (SC) and disordered (DIS)
    From the results presented in Figure 4, it can be clearly seen that by decreasing the precipitation temperature of SOX (V4) to 10 * C (V6) and lowering the NMMQ rate in the precipitation bath of 44.8 Oew <»% NMMO (at V4) to 0% w *% NMMO (at VS) increase the disordered areas from 37.4% to29.3%. »Therefore, the innextile part must decrease accordingly, so that the obarflichenkristailine Artel remains constant. Therefore one can say that the
    Dick's skin with the disorganized share The Au &amp;, clearly identifies the globule as amorphan tali, and DurahCemputedcmographia-Maturity clearly indicates that it • orders amorphous outer skin of denser material than the nucleus,
    These measurements were carried out with a Sarai GSßheeniv ix ~ ray nanotome and a VoxsigrdSe of 4, S um dumhgafühft, the measurement duration was 121 min and a total of 1700 projections were recorded, whole cellulose preparations were measured (not comminuted ): Piegafoergetfoekheten and medium ac cokerettes Ceiiuioseperien from Example 4, and as a reference commercially available compact Ceilylese ^ Kögetehen (Sprayephefes-SE Whte, Umang), A measurement of moister Ceiiiiioseperien not meaningful possible, using the software VG Studio MAX 2.2 were (virtual) cuts made by the particles! and evaluated according to the coarse grades (corresponds to the density of the densities). A relative density of δ% was defined for the particle size and for compact cellulose (spray spheres) a relative density of 100%, and the value of the values shown in Table 3 for the dried "fence ! # * Parian revealed
    Table s
    Example 6 - Oil-Dependent Dried Celiacose Particles
    The fluidized-bed dried (uncoated) GeiMoseperlan sue Example 4 was tested for water balance in water. Pefemnzmafedai were again used with commercial spray-granulated cellulose beads (CSsprayspberes * 8β White, ümang).
    Water was added and allowed to swell without any extensive movement (tubes a, a.), Thereby establishing an equilibrium. in Table-4 are the results of these experimental semisfaasfaasi T & hsks 4
    It shows. " that the TenoahSegds are a much better source of currency than commercial Greek partisans. Deskann turn on oils previously described in the previous examples
    Example 7 * - Variation of particle strength by enzymatic and chemical treatment
    Pieces of never ciliated Oeilulpsepehen V1 from Example 1 were subjected to both an enzymatic and an oxidative treatment, with the following parameters being used:
    In smsr buffer solution (pH 4), a solution of the enzymes Ceilydast UL and EOnease HC 400 (Movozyme) in a ratio of 2: 1 was prepared. A further blast-raising enzyme treatment results from the use of Ndvozyme FIParCar® 8 or FiserCam D in a pH 8 buffer solution , p. Each of the cellulosic dpeads was given a call (40X0) and, in turn, the respective enzyme solution was added in a dosage equal to 1 ml per gram of dry cellulose pulp. The reaction tent was 10 minutes and 80 minutes. The resident-enzyme digestion was then stopped and the cellulases washed several times with VB-Wasssr. The oxidation was via the known TEMPO reaction, with the reactants being 4 ti bet 80s C. After quenching the reaction by EiQH addition and thorough washing of the glucoses with deionized water, there was a further 48 h of post-oxidation in 0.1 M Ns-acetate buffer (ρΗ * 4, δ). After the reaction, the particles were filtered off with suction, washed thoroughly and stored in the refrigerator
    The firmness of the gel-lysis beads was examined by means of different stamps of different weights placed on a defined amount of csiolinase beads. Furthermore, micropanoscopic images of the particles were again made to analyze changes in morphology
    Enzymatically treated, never dried Cellolosepeflen (10 min and 8ö minReakbenszeit) are crushed by the own weight of a 100 g heavy stamp. Untreated Oeüuioseperien women by the weight of this stamp only reversibly deformed, untreated Celluteseperlen (blank) amt amt from a stamp with a weight of 3 kg irreversible deformed and from 5 kg hydrogah-like consistency and are neither sticky nor greasy. Similar to the enzymatic treatment, the structural integrity of the beads has also been greatly reduced by the effects of the ozone. Thus, these beads can be irreversibly cracked with a 1 kg punch, except for a 2 kg ~ Stempe! shows a strong crack formation and with a $ kg ~ stamp the Gepulosepeden are already completely crushed,
    In addition to these simple tests to determine the shepherd, the microhardness was also determined by means of a ShimadzuEZ Test X tarsal instrument. The test was marked with a 10. mm. Stamp and the deformation against the applied force was recorded. Figure S shows the deformation curves for enzyme treated and TEMPO oxidized samples,
    The enzymatically treated samples have undergone a dramatic change in morphology, vines of smoothing the QberHiche have been shown to erode the core / hell structure, Oil shows that both the dense outer and the inside of the cellulase are accessible to the enzymes and afegafeaut There was no longer any difference between the outer skin and the inner part of the cellulose sponges; both are part of a hydrogel,
    These mor- piologic changes in TSMPO oxydases hm, EneymbeHandiunii can be confirmed by NMR spectroscopy (see Figure 0) as described in Example 8, Thus, the disordered cellulosic part decreases in the enzyme treatment, and the innocardial portion increases inevitably, thereby decreasing the TEMP oxidation obanlächsnknstaine share is strongly ad, increasing the share of employment.
    Example 8 Incorporation of Inorganic Pigments
    A 33% w / w ZnO suspension (type © Pherrna 4, $ m * 1.2 pm) in Bulk Qmi% aqueous solution was used for heme division of a tyoceilepine pulp. Unsupported dope consisted of 12.2 Gow% pulp ( Type Baseil), 73.9% by wt.% NMMO / 11 lbs. G w / w% water, ZA Oew.% ZnO, as well as traces of stabilizer, This bpinnmasse were now Celiuiosepanen as in Example 1, V1 &gt; The outer appearance of cellulose was equal to that of cellulose without ZnO addition. OreZnO content of the particles was determined to be 16.7Gm, A3 (ashlar 0804¾ and gravimetrically scored blank on a bead without ZnO) and distributed by SEM (Hitachi S * 40O 'Field Emission SEM) with an embedded EDX (Oxford BOX Detector), Figure 7 shows the very similar ZnA / distribution in such a halved Tencel-Beed
    权利要求:
    Claims (10)
    [1]
    Paientanapriche 1. Three-dimensional Caltufesian form-body, by which it can be visually ascertained, "Kam" y®ofei "Stiykiur" yfWsist, whereby the mantle © inthéher © dense © and a lower Kdstafmtil than the kernel exhibiting and Karnam® sehwammihnliche The structure has a pot body according to claim 1, wherein the shell has a relative density of 86% to 86% and the chamber has a relative density of from 20% to 80% - corresponding tocomplex cellulose, i, pormkörpaf each claim 1, wherein dl® Manteidiok ® between SO prrt and 200 pm
    [2]
    4, shaped body according to claim 1, wherein the ratio of yantetdloka to Gesamfdyrohmesser de® shaped body «wipe 1: 6 and 1:60
    [3]
    5. Shaped body according to claim 1, wherein the ratio of the semi-axes of the elilpaoiden shaped body 3: 1 not Öbersfoigi
    [4]
    The fermkdrper of claim 1, wherein the never-dried variant of the celiac peri fi ces has a fruity content of 28-300% by weight, based on the lotfulose amount, of the polymer body of claim 1, wherein the shaped body contains additive particles incorporated during its manufacture and these additive branches are selected from the group containing ZnO; TIÖ &amp; CaCOs, kaolin, f & nos, color pigments based on plastics, activated carbon, superabsorbent materials, phase »changa» yateriaifent flame retardants, biocides, chilosan, as well as wetterePolymer® or biopolymers,
    [5]
    8, a process for producing a three-dimensional cellulosic shaped body with optically detectable Kom-Mentel structure, characterized pkennzeiehfiet * that takes place Heretetlungsschni®; a, dissolution of the column residue according to a tyccetipimsss to obtain a solution with 10 to 18 6aw>% cellulose: b, .Extrusion of the cellulosic solution obtained in step a, directly from the air gap into a precipitate; e, Regenemtiortsprozess, wherein at the entrance of Cellutesafdsung in Fäffhaddis difference of UMMO concentrations of Celluloselbeung and FillbadiS * 78 wt% s preferably 40 - TO Gew.4i, and the difference between the temperature of CeflulbselOsung and Pilibad §0 ** 120 K, preferably TO -120 K, particularly preferably $ 0 -120 K; d. Washing process according to the percolation principle with at least one alkaline wash, preferably at pH 9~~ 13: e. optionally a drying process », which does not damage the AuEenhaui derFormkOrpar abrasively; wherein dl © in point d.) Preferably, multi-stage and countercurrent and contains at least one efkaiisdhen step.
    [6]
    8. The method according to claim 8, wherein the Trooknungepfozzess by normal pressure drying, Strämungstroeknung, Sandtrooknung, WlfbelsehiehhroknungGafhertrooknune or supercritical COrDrocknung takes place. 1S, method according to. Claim 8, wherein between step d, and font e. an enzyme treatment takes place »11 Process according to claim 8, weave! one or more enzyme selected: from the group containing Ezo »and Endb ~ l, 4-h ~ glucanasen, Giucosidasen andXyianasen used.
    [7]
    12. Use of Pormkörper according to claim 1 for Herateilung wi ^ a material-loaded carrier material, wherein the Pormkärper is soaked with a solution of the drug and then washed and dried "Lenzing AG, PL0546 13, V" rv "# enäung 'the Pormkörpar according to claim 1 tm production Use of the molded bodies according to claim 1 as abrasive material In cosmetic products such as gassplel peelings or escrofillosis, the average size of the shaped bodies 180 - 800 pm, preferably 2ÖÖ ~ 800 pm, more preferably 300 - SSO is around.
    [8]
    15, use of the Femikdrper according to claim 1 as optical Effektkügalchen incosmetic products, preferably shampoos and creams,
    [9]
    16, use of the moldings according to claim 1 as Ausphgsmafada! For the preparation of sphSdscfien oailufoslsehen powders, the sensorimbooster * Bigensetwffen for cosmetically © products In öiAh / asser «Emuision © n up, by Mehlung, t , Use of the moldings according to claim 1 as Äuspnpmstehal for the preparation of« phyton cellubsischen powders, which for Control Belass © Particles © that can be used as a core for control release particles
    [10]
    18, use of the moldings according to claim 1 as Säulenmetena! in chromatography, in particular in the normal phase, phase-to-phase ion expression, affinity and particle sensitivity,
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    同族专利:
    公开号 | 公开日
    ES2639807T3|2017-10-30|
    US10093790B2|2018-10-09|
    PL3058022T3|2017-11-30|
    WO2015054711A2|2015-04-23|
    DK3058022T3|2017-10-02|
    WO2015054711A3|2015-07-16|
    CN105829351A|2016-08-03|
    EP3058022B1|2017-06-14|
    CN105829351B|2019-05-10|
    AT515180B1|2016-06-15|
    EP3058022A2|2016-08-24|
    KR20170071444A|2017-06-23|
    JP6511441B2|2019-05-15|
    JP2016538367A|2016-12-08|
    US20160257806A1|2016-09-08|
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    JPWO2020022524A1|2018-07-26|2021-07-01|株式会社日本触媒|A method for producing a cellulose monolith and a cellulose monolith obtained by the method.|
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    申请号 | 申请日 | 专利标题
    ATA794/2013A|AT515180B1|2013-10-15|2013-10-15|Three-dimensional cellulosic molding, process for its preparation and its use|ATA794/2013A| AT515180B1|2013-10-15|2013-10-15|Three-dimensional cellulosic molding, process for its preparation and its use|
    DK14838769.9T| DK3058022T3|2013-10-15|2014-11-14|THREE-DIMENSIONAL CELLULOSE EMBODIMENT, PROCEDURE FOR PREPARING THE SAME AND USING THE SAME|
    KR1020167012437A| KR20170071444A|2013-10-15|2014-11-14|Three-dimensional cellulose moulded body, method for the production thereof and use of the same|
    EP14838769.9A| EP3058022B1|2013-10-15|2014-11-14|Three-dimensional cellulose moulded body, method for the production thereof and use of the same|
    US15/027,923| US10093790B2|2013-10-15|2014-11-14|Three-dimensional cellulose molded body, method for the production thereof and use of the same|
    CN201480056149.XA| CN105829351B|2013-10-15|2014-11-14|Three-dimensional fiber element formed body, Its Preparation Method And Use|
    JP2016524151A| JP6511441B2|2013-10-15|2014-11-14|Three-dimensional cellulose molded body, method for producing the same, and use thereof|
    PCT/AT2014/000202| WO2015054711A2|2013-10-15|2014-11-14|Three-dimensional cellulose moulded body, method for the production thereof and use of the same|
    ES14838769.9T| ES2639807T3|2013-10-15|2014-11-14|Three-dimensional cellulosic molded body, procedure for its manufacture and use|
    PL14838769T| PL3058022T3|2013-10-15|2014-11-14|Three-dimensional cellulose moulded body, method for the production thereof and use of the same|
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