Modified nanocomposite material, method for its production and its application
10174457 ยท 2019-01-08
Assignee
Inventors
- Joanna Lojewska (Cracow, PL)
- Tomasz Lojewski (Cracow, PL)
- Jacob L. Thomas (Gothenburg, SE)
- Roman J. Jedrzejczyk (Cracow, PL)
- Dominika Pawcenis (Cracow, PL)
- Barbara Gil (Cracow, PL)
- Jakub M. Milczarek (Lodz, PL)
- Katarzyna Turnau (Cracow, PL)
- Andrzej Kolodziej (Czekanow, PL)
Cpc classification
B65D65/38
PERFORMING OPERATIONS; TRANSPORTING
D21H17/69
TEXTILES; PAPER
D21H21/36
TEXTILES; PAPER
International classification
D21H17/69
TEXTILES; PAPER
D21H21/36
TEXTILES; PAPER
B65D65/38
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A nanocomposite material with antimicrobial properties, based on cellulose packed with a mineral filler (zeolite) exchanged with silver, characterised in that the mineral filler is made up of Y-type zeolites, while silver occurs in a form bound with the zeolite matrix in the form of cations and, optionally, nanoparticles of reduced silver, as well as a method for preparation of such a material and its application for the wrapping of plants, works of art, archives and antique objects, as well as food, pharmaceuticals and animal fodder.
Claims
1. A composite material comprising cellulose packed with silver-containing zeolite of a Y-type, which is a mineral filler, whereas silver occurs in a form that is entirely bound to the zeolite and in the form of both silver cations and reduced silver, wherein the silver content not exceeding 2 wt. %, and the material exhibits antimicrobial, sorptive, and catalytic properties, wherein the reduced silver is silver having an oxidation state of zero.
2. A material according to claim 1 characterised in that the silver cations are introduced to the zeolite by ion exchange.
3. A material according to claim 1 characterised in that the reduced silver occurs in the zeolite as a result of sonication.
4. A material according to claim 1 characterised in that the zeolite has exclusively exchanged silver and no silver in a non-bound form.
5. A material according to claim 1 characterised in that the material exhibits sorptive properties towards volatile organic compounds or gaseous impurities, or both.
6. A material according to claim 1 characterised in that the material exhibits catalytic properties in oxidation of volatile organic compounds at room temperature in air and at a temperature of above 60 C. without air access.
7. A material according to claim 1 characterised in that the material exhibits bactericidal properties against Escherichia coli, Serratia marcescens, Bacillus subtilis or Bacillus megatherium bacteria.
8. A material according to claim 1 characterised in that the material exhibits fungicidal properties against Trichoderma viride, Chaetomium globosum, Aspergillus Niger, Cladosporium cladosporides and Morterella alpinum fungi.
9. A packaging material comprising the composite material of claim 1.
10. The packaging material according to claim 9, wherein said packaging material is for plants, works of art, archives or antique objects.
11. The packaging material according to claim 9, wherein said packaging material is for food, pharmaceuticals or animal fodder.
12. The material of claim 1, wherein said silver cations and said reduced silver are present in a ratio of 1:1.
13. A method for production of a composite material of claim 1, said method comprising the substitution of a zeolite with both silver(I) ions and a reduced form of metallic silver to obtain a modified zeolite, addition of said modified zeolite to a cellulose suspension with cellulose fibres, formation of the paper pulp into a desired shape and drying said paper pulp, wherein the modified zeolite is rinsed with an aqueous solution of disodium salt of ethylenediaminetetraacetic acid (EDTA).
14. The method according to claim 13 characterised in that before rinsing with EDTA, said method comprising sonication of the modified zeolite.
15. The method of claim 14, wherein said sonication comprises sonicating for at least 10 minutes in a suspension of the modified zeolite, and at a temperature of below 60 C.
16. The method of claim 13, wherein said rinsing with EDTA comprises the following steps: a) rinsing of the zeolite with 0.01 M EDTA at room temperature; b) washing for one hour at boiling temperature with the 0.01 M EDTA; c) rinsing of the zeolite with of 0.1 M EDTA solution and d) flushing of the zeolite with deionised water.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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(16) The goal of the invention is to provide packaging material with high biocidal activity and sorption and catalytic properties, with a minimum content of silver introduced into the zeolite, the silver being in a dispersed state in the channels and cavities of the zeolite in the form of clusters or atoms of metallic silver particles and silver cations in order to prevent their migration. The formation of silver in two oxidation states in the zeolite is to ensure the catalytic activity of the material. The goal of the invention is also to provide a method for obtaining of such a material having the aforementioned features.
(17) The present invention relates to a method for manufacturing of a nanocomposite packaging material, comprising the substitution of a zeolite matrix with silver(I) ions, addition of an active material in the form of a zeolite matrix containing silver to a cellulose suspension and its deposition on cellulose fibres, formation of the paper pulp into a desired shape and drying, characterised in that before the addition of the zeolite matrix exchanged with silver ions to the cellulose suspension, the zeolite is rinsed with an aqueous solution of disodium salt of ethylenediaminetetraacetic acid (EDTA), wherein the rinsing with EDTA preferably comprises the following steps: a) rinsing of the zeolite with 0.01 M EDTA at room temperature; b) washing with 0.01 M EDTA for one hour at boiling temperature; c) rinsing of the zeolite with 0.1 M EDTA solution and d) flushing of the zeolite with deionised water.
(18) Preferably, the zeolite matrix is treated with a silver nitrate solution in order to introduce silver into it.
(19) In a preferred variant, sonication of the zeolite matrix exchanged with silver ions is additionally carried out before washing with EDTA, preferably for 10 minutes in a suspension of the zeolite with an average power of 90 W and at a temperature of the solution below 60 C.
(20) A further object of the invention is a nanocomposite material comprising cellulose packed with the silver-containing zeolite, characterised in that a Y-type zeolite is the mineral filler, whereas silver occurs in a form bound with the zeolite matrix in the form of silver cations, silver content is in the range of 1-2% by wt., and the material also exhibits sorptive and catalytic properties apart from antimicrobial properties. Such a material is obtained using a variant of the method according to the invention carried out without sonication.
(21) A further object of the invention is a nanocomposite material containing cellulose packed with the silver-containing zeolite, characterised in that a Y-type zeolite is the mineral filler, whereas silver occurs in a form bound with the zeolite matrix in the form of silver cations and metallic silver nanoparticles, preferably in a ratio of 1:1, whereas the total silver content in the zeolite does not exceed 1% by wt. Preferably, metallic silver occurs in the zeolite beside silver cations in the result of application of a sonication procedure.
(22) Preferably, the silver ions were introduced into the structure of the zeolite by ion exchange. Preferably, the zeolite matrix does not contain silver in its non-bound form in the form of silver oxide clusters. Preferably, the material according to the invention exhibits sorptive properties towards volatile organic compounds and gaseous impurities, and catalytic properties in the oxidation of volatile organic compounds at room temperature in air and at a temperature of 60 C. without air access. Equally preferably, the material according to the invention exhibits bactericidal and fungicidal properties, particularly against Escherichia coli, Serratia marcescens, Bacillus subtilis and Bacillus megatherium bacteria, and/or Trichoderma viride, Chaetomium globosum, Aspergillus niger, Cladosporium cladosporides and Morterella alpinum fungi.
(23) A further object of the invention is the application of the nanocomposite material according to the invention, defined above, for wrapping, particularly for wrapping of plants, works of art, archives and antique objects or for the wrapping of food, pharmaceuticals and animal fodder.
(24) In a particular embodiment, the present invention relates to a nanocomposite material with sorptive, catalytic and antimicrobial properties. The material is obtained from paper pulp packed with a Y-type zeolite, having clusters or atoms of metallic silver trapped in its structure, so as they do not migrate to the exterior of the material. Moreover, the present invention relates to a method for production of the modified zeolite exchanged with silver cations, and then flushed with an EDTA solution in order to remove silver not bound with the zeolite matrix, using sonication, leading to a reaction of silver and a refinement of the zeolite while preserving its structure. The material being the subject of the invention may find application as a packaging material for the storage of works of art, archives and antique objects, as well as plants, food, pharmaceuticals and animal fodder.
(25) The first aspect of the invention is a multifunctional nanocomposite material based on cellulose packed with a zeolite with clusters or atoms of metallic silver and silver cations trapped in the structure of the zeolite's channels and cavities, the material exhibiting antimicrobial, sorptive and catalytic properties, which may be used, among others, for the wrapping of plants (living and cut flowers), food and pharmaceuticals, animal fodder, works of art and antique objects or as an insulation material.
(26) Another aspect of the invention relates to a method for production of the material according to the invention. According to the invention, a Y-type zeolite (a mesoporous material- with a faujasite structure), used as a carrier for silver, is applied for the modification of cellulose. During the ion exchange of the sodium zeolite form, sodium cations are exchanged with silver cations (bound state of silver); however, the deposition of silver oxide crystallites on the external surface of the zeolite (non-bound state of silver) is also possible. In the first step, after treatment with the solution of a silver salt, both the bound state of silver in the form of cations and the non-bound state in the form of crystallites (clusters) of its oxide occur in the zeolite. Elimination of silver in the form of clusters from the surface of the zeolite is then carried out until a pure zeolite exchanged with silver cations is obtained, i.e. a material with silver in its bound form, with minimum silver content. In the next step, sonication of the so-prepared material is carried out in order to reduce silver cations to metallic silver in the form of atoms or clusters, so as to obtain defined contents of both forms of silver in the final product. Considering the fact that this process is carried out in the interior of the zeolite, the obtained silver atoms or nanoparticles are trapped in it, resulting in a reduced risk of contamination of the packed products and the external environment with silver.
(27) Sonicators are commonly used in the chemical industry for modification of chemical properties of materials or for chemical synthesis. The approach to the engineering of the materials shown in the invention enables uniform distribution and high dispersion of the zeolite in the paper material for the sake of i) application of the zeolite exchanged with silver on an atomic scale, permanently bound with the zeolite matrix thanks to flushing with EDTA, ii) sonication leading to a dispersion of the zeolite and reduction of the silver cations contained in it, as well as iii) a method for manufacturing of paper sheets with zeolite packing.
(28) The modified zeolite used in the present invention exhibits the ability to absorb gases, and it has proved useful as a component of other products, performing as a material reducing the concentration of volatile organic compounds (VOC) and other gases connected with unpleasant odours, e.g. forming as the result of degradation of the materials being stored. Moreover, silver in its dispersed state inside zeolites is a catalyst of VOC oxidation, which has been proven in the example of acetic aldehyde oxidation. Surprisingly, it was found that in order to obtain catalytic activity of silver at low temperatures, particularly room temperature, the presence of both a reduced form of metallic silver and that of its cations is necessary. Catalytic activity of the material is observed at low temperatures even without air access to the material. Thus, the present invention is a novelty when compared to other cellulose materials containing zeolites, because of the fact that while using it, undesirable organic gases may be removed both by their sorption and catalytic decomposition.
(29) The basic component for production of the material according to the invention is made up of paper pulp, which may be easily prepared in large amounts and formed into two- and three-dimensional objects, such as: paper, paperboard, containers, etc., using known industrial processes, or suspended in a liquid and applied as a spray, as well as dried and blown into isolated spaces. Cellulose fibres have micro- and mesopores and voids, as well as a polar surface, thanks to which they may bind and hold the zeolite particles.
(30) Paper packed with the prepared zeolite, constituting a particular embodiment of the invention, has proven biostatic and biocidal properties both against bacteria and fungi. Moreover, it is characterised by sorptive properties towards both VOC and gaseous impurities such as SO.sub.2 or NO.sub.x. Catalytic activity of the obtained material in oxidation of VOC at low temperatures without air access was also demonstrated.
(31) The invention has a series of unexpected advantages in comparison to similar solutions known from the state of art.
(32) Particularly, in the present invention, silver occurs not only in the form of cations exchanged in the zeolite, but also in the form of atoms or nanoparticles trapped in the structure of the zeolite. Thanks to this fact, the catalytic properties of the material were improved, and the material oxidises volatile organic compounds already at room temperature, and even partially without air access. A high dispersion of the material was also obtained, additionally contributing to the improvement of catalytic activity. On the other hand, the silver content was reduced to an amount below 1% by wt.
(33) Application of zeolites has a stabilising influence on silver, being the active component of the entire material. In particular, one should take into account the reduction of migration of the silver nanoparticles (contained in the packaging material) to objects or substances stored in this packaging.
(34) The invention described in this application differs fundamentally from the products of the state of art, because of the fact that the proposed material is a multifunctional paper product adsorbing impurities and exhibiting antimicrobial and catalytic properties thanks to the application of zeolites with silver in two oxidation states. In the present embodiment, zeolite aggregates with silver cations and atoms or clusters of silver trapped in their structure are immobilised on purified cellulose fibres using chemical and physical sorption methods in order to form the composite zeolite-fibre material. Using filtration and sedimentation methods, it is possible to produce a composite material consisting of a zeolite-fibre component enriched with a layer of functionalised zeolites.
(35) The invention should find application in the field of preservation of works of art and antique objects. The developed material may be a part of paperboard elements in contact with a work of art, particularly in the case of mounts which will be in contact with the external walls of buildings. In winter, the external walls, particularly in poorly insulated buildings, such as historic houses or churches, may have a low temperature, leading to the formation of a humid microclimate inside the building. This is a particularly dangerous situation in spaces behind and between the objects of interest, where the risk of growth of mould increases. The present invention, prepared in the form of paperboard and used as a mounting support or rear wall for an object in a frame, may serve as a prophylactic tool inhibiting the growth of mould. As a result of increased humidity, water bridges between the paperboard and the object in question will form, which should additionally improve the biostatic effect. Another application in this group may consist in a material for wrapping materials of organic origin (cloth, leather, parchment, paper, wood, fossils, etc.), which are also susceptible to microbial attack. Absorbent paper may also be prepared and delivered as a system ready to use in the case of disasters such as flood or inundation. In the case of such disasters or malfunctions, wet objects are often wrapped in absorbent paper and tissues prior to vacuum packing. In the next step, the objects are stored at a low temperature, stopping or significantly hindering microbial growth. In such a case, the present invention would provide a possibility for additional antimicrobial protection. In all described cases, the sorptive properties of the present invention are of importance, too. For storage of archival materials or library collections, boxes or envelopes with such catalytic, sorptive and biocidal properties may be used.
(36) While preserving works of cultural importance, it is necessary to separate them from the influence of harmful gaseous air impurities, e.g. acidic gases present in urban agglomerations at high concentrations (NO.sub.x, SO.sub.2, CO.sub.2), as well as to remove gaseous products of degradation of the object, often having a destructive influence on the object, from the atmosphere surrounding the object. The undesirable influence of microbes (fungi and bacteria) on works of art is known and has been repeatedly described in literature.
(37) As a packaging protecting antique and archival objects, the present invention is currently the only known product having fungicidal and bactericidal properties, as well as biostatic and sorptive properties, simultaneously. Stabilising properties, multifunctionality, application of renewable materials, simple and scaleable production methods and a green chemistry-consistent approach differentiate the presented invention from other products commercially available on the market.
(38) The developed packaging material was subjected to comprehensive physicochemical studies. It was shown in their results that, among others, both silver cations and metallic silver in the form dispersed in the zeolite are permanently bound with the zeolite and do not penetrate into the environment, and this fact is of high importance because of the stability of the biostatic properties of the material and safety of its use. Tests for the presence of silver in the aqueous filtrate which was in contact with the developed material (the sample denoted as P_ZAgO was used) yielded a negative resultboth at low and high temperatures, neither silver ions nor silver nanoparticles were extracted to water, which was confirmed by chloride ions test and XRF analyses.
(39) The transfer of silver nanoparticles and silver ions during contact with model food may be checked using proper analytical techniques. In the investigations carried out by the authors using the XRF technique, no presence of silver was found in nutrient agar remaining in prolonged contact with silver-containing paper disks.
(40) Moreover, it was proven that thanks to use of sonication and obtaining silver at two oxidation states in the zeolite matrix, the material exhibits catalytic activity in combustion of volatile organic compounds at room temperature even without air access, and this has a significant biocidal activity. This was confirmed using sorption and catalytic tests carried out in situ with the analysis of the intermediate products by DRIFT/FTIR. Thanks to sonication, a high granularity of the material was obtained, possibly also contributing to its exceptional catalytic activity. The silver content in the material was reduced below 1%.
(41) The results of microbiological tests confirm the high activity of the material against the strains of bacteria and fungi typically occurring in food or archives, however this activity is comparable to that of the non-sonicated material containing silver cations only.
(42) The results of physicochemical and microbiological analyses of the invention are presented in
(43) The invention is described in more detail in the following embodiment; however, the embodiment should not be considered the full scope of the invention.
EXAMPLE 1
Preparation of the Material According to the Invention Ion Exchange of the Zeolite
(44) A Y-type zeolite was the basic zeolite used for the studies, and the full optimisation of the ion exchange procedure presented below was carried out for it. Samples of ZSM-5 and MCM-56 reference zeolites were also used in the studies. The ion exchange procedure was as follows: 50 mg of the zeolite were introduced into 10 cm.sup.3 of 0.1 M aqueous solution of AgNO.sub.3, and the so-prepared suspensions were shaken at a rate of 300 rpm. The shaking was carried out without access of light. After the assumed sorption time, the suspension was centrifuged at a rate of 2.000 rpm. According to the optimisation carried out, the centrifugation was done 5 times. After washing, the precipitates were dried at a temperature of 120 C. Dried precipitates were conditioned for 24 h and weighed with an accuracy up to 0.1 mg. The samples were placed in a beaker, and 5 cm.sup.3 of 65% solution of nitric acid was added. The suspension was heated to boiling and maintained at this temperature for 15 minutes. After cooling, the suspension was centrifuged (2,000 rpm), and the supernatant was quantitatively transferred to a graduated flask with a volume of 25 cm.sup.3. The precipitate remaining on the bottom of the test tube was treated with deionised water and shaken until a suspension formed anew; this suspension was centrifuged. The supernatant was transferred to a graduated flask containing the solution after the first centrifugation. This procedure was repeated 5 times in total. The precipitate was dried and tested on the optionally remaining silver contents. The solution in the flask was made up to 25 cm.sup.3 with deionised water. The so-prepared solution of silver (corresponding to the initial silver content in the zeolite) was analysed with XRF using the calibration curve method.
(45) Determination of Silver in the Zeolite by X-ray Fluorescence Spectroscopy (XRF)
(46) The measurements were carried out using an ED-XRF spectrometer (Quant'x-Thermo). Parameters of the measurement: t=60 s, air atmosphere, thin copper filter, large measurement cup. K emission line for silver was selected for the assay (integrated with the background cut-off in the range 21.46-22.60 keV). The determination of silver was carried out in HNO.sub.3 solutions with the dissolved zeolite, and the results are shown in Table 1. The determination of silver content is burdened with an error of 5%, determined based on the reference to the blank test. The error is a consequence of the scatter of resultsthe correlation coefficient for fit of the curve developed based on the analyses of AgNO.sub.3 standard solutions (see Table 1) amounts to R.sup.2=0.9819. Incomplete leaching of silver from the zeolite by hot HNO.sub.3 also contributes to the error. The silver content in the non-dissolved zeolite in the form of precipitate was also checked; however, the amount of silver in precipitates did not exceed 1% by wt. Thus, the assays of the silver content in the zeolite were based on analyses of the solubilised material.
(47) The sorption isotherm determined with XRF indicated that half-exchange of the zeolite with silver ions under the described conditions is obtained after approx. 1 h (
(48) TABLE-US-00001 TABLE 1 Results of studies of the silver content in solutions after washing of the zeolite after the ion exchange using hot HNO.sub.3. The penultimate position in the sample name (0.1) denotes the concentration of silver in the AgNO.sub.3 solution used for the exchange, the last position - time of the ion exchange. Silver content Ion exchange Count [mg Ag/g of the Assay time [h] number zeolite] YAg_0.1_1 1 280,000 94.0 YAg_0.1_2 2 429,500 263 YAg_0.1_3 3 422,800 253 YAg_0.1_20 20 396,006 246 YAg_0.1_29 29 423,700 265 YAg_0.1_39 39 374,800 225 YAg_0.1_92 92 439,200 254 Calibration curve data Concentration of the AgNO.sub.3 solution [mol/dm.sup.3] 0.1 681,900 0.05 430,100 0.033 365,600 0.025 298,100 Determined concentration [mol/dm.sup.3] Blank test 0.05 424,900 0.0475 Preparation of a zeolite matrix
(49) Based on the determined ion exchange isotherm, 1 hour was selected as the optimal ion exchange time. Three portions of 5.00 g each were weighed out. The first portion was placed in a beaker and treated with 100 cm.sup.3 of 0.1 M aqueous solution of silver nitrate(V). The suspension was shaken for 1 hour at a rate of 300 rpm. The precipitate was filtered, and the recovered nitrate solution was used again for sorptions with portions two and three. The precipitates were rinsed with 500 cm.sup.3 of distilled water in order to flush the excess silver nitrate. After drying of the precipitates at temperature of 60 C., they were combined and mixed, yielding a homogeneous sample. From the so-prepared base material, a representative sample was collected in order to carry out physico-chemical analyses (the results are presented later). The base material (zeolite exchanged with silver) was used as a filler of paper sheets in further preparations.
(50) Modification of Structure and Composition of the Zeolite Matrix
(51) The final prepared sample was washed with EDTA in order to remove the silver non-bound to the zeolite. Therefore, in the case of sonicated samples, it was carried out after sonication. However, for the sake of comparison of the sonicated samples with the non-sonicated reference samples, the washing procedure is described as in the first sequence. Optimisation of the washing procedure was developed for the non-sonicated samples and used further in the same way for the sonicated samples described in the invention.
(52) Leaching of the Non-Bound Silver with an EDTA Salt Solution
(53) Before application of the procedure of silver ions removal from the external surfaces of the zeolite crystallites, the influence of rinsing on the dealumination of the sample was tested. To this end, reference samples of the raw zeolite were rinsed with an aqueous solution of disodium salt of ethylenediaminetetraacetic acid (EDTA). The procedure consisted of three steps: a) rinsing of the zeolite in a funnel (paper filter) with 150 ml of 0.01 M EDTA solution (room temperature), b) flushing at boiling temperature with 150 ml of 0.01 M EDTA solution (maintaining time1 hour), c) rinsing with 150 ml of 0.1 M EDTA solution.
(54) The flushing was carried out in a plain funnel using qualitative paper filters. Proper solutions were dosed so that the precipitate was immersed in the solution for the entire washing process. The precipitate was rinsed with a fresh portion of the complexone each timethe solutions were not recirculated. In the case of hot rinsing, the material being modified was placed in a beaker and treated with 0.01 M EDTA solution. The solution was mixed using a magnetic stirrer and maintained at boiling temperature for 1 hour.
(55) Exclusion of Dealumination of the Zeolite
(56) The filtrates were centrifuged (4,000 rpm, 4 min) and then characterised by atomic absorption spectrometry ASA (a Z 2000 atomic absorption spectrometer with Zeeman polarisation, HITACHI) in order to eliminate the possibility of dealumination of the zeolite during flushing. NMR analyses using a Bruker 400 MHz spectrometer with an attachment for solids was also performed. In Table 2, the results of the studies carried out for filtrates after treating the zeolites with Na.sub.2EDTA are shown. The results presented in Table 2 prove that treating the zeolites with cold 0.01 M EDTA solution does not cause leaching of aluminium from the structure. A zeolite heated in an aqueous EDTA solution for 1 hour was selected as a reference sample; in the case of this zeolite, dealumination occurred.
(57) In this case, aluminium was detected in the filtrates by ASA. However, not detecting aluminium in the other solutions is not an unequivocal confirmation of a lack of dealumination in the zeolite lattice; therefore, analyses of the material were supplemented with the 27A1 MAS NMR method, used for determination of dealumination degree. To this end, dried precipitates after rinsing with an aqueous EDTA solution were tested on changes in the aluminium NMR signal. A standardisation of NMR spectra in relation to the surface area of the main signal for tetrahedral aluminium of the non-modified initial Y-type zeolite (A=1.0000) was carried out. Values for the measured samples are collected in Table 2. The obtained results indicate that the selected flushing method does not cause dealumination, proving the thesis that the zeolite does not change its crystal structure after chemical treatment (rinsing with 0.01 M EDTA). It should be noted that in the case of heating of the zeolite in the EDTA solution or application of a higher EDTA concentration, structural changes do occur. In the case of washing with 0.1 M EDTA, the loss amounted to 6%.
(58) TABLE-US-00002 TABLE 2 The results of determination of aluminium in the filtrates after rinsing with EDTA. NMR method percentage loss ASA method of aluminium Assay Treatment method [c.u.] from the lattice* ZAg+_0.01_T25 150 cm.sup.3 of cold 1 (not 0.05 0.01M EDTA detected) ZAg+_0.01 Heating for 1 hour 33 3.80 T100 in 0.01M EDTA ZAg+_0.1 T25 Rinsed with 150 1 (not 6.10 cm.sup.3 of 0.1M EDTA detected) *the results related to the dry precipitates of the zeolites standardised in relation to their mass, collected after the process described in the second column of the table. T25 and T100 assays relate to temperatures of 25 and 100 C., respectively.
Optimisation of Zeolite Rinsing
(59) In order to optimise the time and multiplicity of the washing of the zeolite materials exchanged with silver using EDTA in order to complex the silver ions present on the external surfaces of the zeolite crystallites, an XRF analysis of the filtrates after rinsing (or solutions after centrifugation of suspensions) was performed.
(60) TABLE-US-00003 TABLE 3 XRF quantitative analysistransition line intensities for silver after consecutive washings with EDTA for a ZAg+ sample of the Y-type zeolite after ion exchange (shaking). Number of washings Analytical signal (solution volume V = number .Math. 10 cm.sup.3) for silver [keV] 1 1,710,009 2 224,776 3 13,700 4 3,134 5 2,215 6 2,731
(61) The above results were obtained for a freshly prepared sample of the zeolite after ion exchange. As is shown by the analysis of the results collected in Table 3, a sufficient leaching of ions non-bound with the structure from the zeolite is obtained after five washings, when the signal of silver reaches a constant minimum level (studies on the influence of washing on the ions bound in the matrix were not carried out). The degree of elution of silver from the zeolite amounts to almost 100% when compared to the first washing, whereas the degree of elution between the 4.sup.th and 5.sup.th washing is lower than 0.1%. Thus, practically, there is no loss of the active material (with some approximation, as in the case of fresh materials, it is very hard to obtain a structure which would be completely resistant to washing with water). Taking this result into account, it was assumed that 5-fold rinsing with water is sufficient from the point of view of silver leaching. At the same time, this is consistent with the assumption for the optimisation of washing, which was to ensure a well-defined structure of materials with minimum amount of silver bound solely to the zeolite matrix.
(62) Moreover, similar analyses were carried out for increasing volumes of the used EDTA solution. To this end, the same mass of the zeolite exchanged with silver ions was rinsed with consecutive portions of water (50 cm.sup.3 each). From the so-prepared filtrate, 2 cm.sup.3 of the solution was collected and analysed by XRF. As results from the data in Table 4, in this case, low values of the signal originating from silver were also obtained (the ratio of the last result to the first amounts to 0.13%).
(63) TABLE-US-00004 TABLE 4 XRF quantitative analysis - rinsing of the sample of ZAg+ Y-type zeolite exchanged with silver ions using water. Total volume of water portions [cm.sup.3] Analytical signal for silver* [keV] 0 1,047,293 50 51,722 100 3,019 150 1,393 *signal standardised in relation to the mass of the sample and the volume of the examined filtrate.
(64) Application of an EDTA solution is, as proven, a good method for minimisation of the amount of silver in the samples to the level of silver bound with the zeolite matrix. The premise is that it prevents migration of silver to the environment, particularly to food, which is often characterised by high humidity. It is also noteworthy that after washing with 40 cm.sup.3 of EDTA, a stable leaching level is obtained (Table 3). However, the degree of elution does not decrease as in the case of water. Obviously, after complexing all ions weakly bound with the structure of the zeolite, the EDTA solution may have access to bound silver ions exchanged in the zeolite.
(65) In the next optimisation stage, the stability of final zeolites exchanged with silver ions in aqueous solutions was investigated (this time, after prior drying of the samplesthe starting material). The degrees of elution of silver ions by water and EDTA were compared. The results are gathered in Table 5.
(66) The results presented in Table 5 indicate that the zeolite packing loses negligible amounts of silver in an aqueous medium. Besides this, the silver content in post-extraction solutions after washing with 50 cm.sup.3 of water falls below the limit of detection. The so-washed sample was then washed with an EDTA solutionconsecutive portions of 10 cm.sup.3 each (coloured part of Table 5). The efficiency of elution of silver ions with an EDTA solution is significantly higher than that of water (150-200 times) and increases together with an increase in the solution volume. When water was not able to leach the silver ions further, a high signal of silver was obtained for the EDTA solution.
(67) TABLE-US-00005 TABLE 5 Rinsing of the same sample of the Y-type zeolite exchanged with silver ions (ZAg+) using water and then EDTA. In the results presented in Tables 3 and 4, the same sample divided into parts was used. Analytical XRF signal for silver [] Total volume of water in consecutive washing with 10 cm.sup.3 portions [cm.sup.3] 10 2,129 20 737 30 561 40 399 50 <LOD Total volume of EDTA in consecutive washing with 10 cm.sup.3 portions 10 EDTA 150,045 20 EDTA 55,039 30 EDTA 23,001 40 EDTA 22,100
(68) Moreover, the optimisation of concentration and amount of the EDTA solution used for rinsing of samples of the zeolites substituted with 4.sup.+ cations was carried out based on analyses of the surface by XPS for Ag.sup.+ band with a bond energy of 432 eV in the spectrum. In Table 6, the results of quantitative analysis of samples of the modified zeolite are shown (the symbols denote, respectively: ZAg+non-washed zeolite substituted with silver ions, ZAg+_H.sub.2Ozeolite exchanged with silver ions washed with deionised water, ZAg+_0.01M_EDTA_150zeolite exchanged with silver ions washed with 150 cm.sup.3 of 0.01 M EDTA and water, ZAg+_0.01M_EDTA_150zeolite exchanged with silver ions washed with 150 cm.sup.3 of 0.1 M EDTA and water, ZAg+_0.01M_EDTA_300zeolite exchanged with silver ions washed with 300 cm.sup.3 of 0.01 M EDTA and water.
(69) The results show that increasing the EDTA concentration from 0.01 M to 0.1 M for ZAg+_0.01M_EDTA_150 and _ZAg+_0.1M_EDTA_150 samples, respectively, causes further leaching of silver from the surface of the zeolite crystallites. In order to minimise the amount of silver, a more concentrated EDTA solution was used for further washing tests. In turn, an increase in the amount of the solution used for rinsing from 150 to 300 cm.sup.3 for ZAg+_0.1M_EDTA_150 and ZAg+_0.1M_EDTA_300 samples, respectively, does not cause further leaching of silver, and the differences between the determined amounts of Ag.sup.+ are within the limits of measurement error. The results of the XPS analysis are consistent with those obtained by XRF. After leaching ions weakly bound with the structure (approx. 40-50 cm.sup.3), EDTA is still able to leach silver from the structure; however, the degree of leaching remain at a low constant level.
(70) TABLE-US-00006 TABLE 6 Quantitative results of XPS for silver on the surface of the zeolite crystallites after rinsing with EDTA. EDTA Signal for concen- silver after tration Rinsing [cm.sup.3] normalisation Sample [mol/dm.sup.3] 1 2 [a.u.] ZAg+ 1.05 ZAg.sup.+_H.sub.2O 150 150 1.19 H.sub.2O H.sub.2O ZAg.sup.+_0.01M_EDTA_150 0.01 150 150 1.25 EDTA H.sub.2O ZAg.sup.+_0.1M_EDTA_150 0.1 150 150 0.29 EDTA H.sub.2O ZAg.sup.+_0.1M_EDTA_300 0.1 300 150 0.31 EDTA H.sub.2O
(71) The performed optimisation of flushing of samples of the starting materials showed that the applied preparation method allowed for the obtaining of stable materials with a minimum amount of silver strongly bound with the zeolite matrix, which was used for further modification of the material.
(72) Sonication
(73) Sonicated samples of the zeolites exchanged with silver cations were prepared as reference samples containing nanoparticles of metallic silver dispersed in the zeolite matrix. These samples were necessary for a comparison of the biocidal properties of silver cations and those of reduced silver. Below, a method for the sonication of samples is presented.
(74) Procedure of Sonication in Solutions
(75) Synthesis of metallic nanoparticles as reference samples was carried out in an aqueous AgNO.sub.3 solution (0.1 M). The first step consisted in checking whether nanoparticles form in the process, what are their sizes and if they are stable. An ultrasound generator with a power of 20,000 kHz was used for synthesis. In the first step, a possibility for synthesis of silver nanoparticles in an AgNO.sub.3 solution without additives was examined. In subsequent steps, the procedure was modified in such a way that increasing amounts of ethanol (max. 5 cm.sup.3) were added to the solution. The last step consisted in the application of a blowthrough of an inert gas (argon) for 60 minutes before turning on the ultrasound, as well as a reducing mixture (H.sub.2/He5/95%.sub.vol.) during the sonication process.
(76) Procedure of Sonication in a Suspension of the Zeolite
(77) Silver nanoparticles were also synthesised in the zeolite matrix. To this end, 1.00 g weighouts of the Y zeolite were prepared and placed in a beaker. The zeolite was treated with 150 cm.sup.3 of distilled water and flushed with argon (15 minutes). The sonication process was carried out using an ultrasound generator (QSonica S-4000, diameter head, P.sub.short-term=90 W, E.sub.total=approx. 97,000 J) (after 30 min) for a time consistent with the data in Table 18. Conditions of sonicationaverage power 90 W, temperature of the solutionbelow 60 C. In the final phase, a blowthrough of the zeolite suspension with the reducing mixture for 1 hour and during sonication was applied.
(78) TABLE-US-00007 TABLE 7 Time of sonication of the zeolite samples. No. Assay* Time of sonication [min] 1 Z 0 2 Z_son_10 10 3 Z_son_20 20 4 Z_son_30 30
Influence of Sonication on the Structure of the Zeolites
(79) Studies on the influence of sonication on dispersion of the zeolite were carried out using atomic force microscopy (AFM, Park Systems, model XE100). The images shown in
(80) Studies on the influence of sonication on the zeolite structure by X-ray diffraction (XRD) were carried out for starting (not listed) samples of the Y-type zeolite subjected to sonication (Table 7). There were no differences found in the diffractograms (
(81) Form and Amount of Silver in the Zeolite
(82) The goal of this part of the research consisted in determination of the composition of the zeolite and the form of silver occurring in it. The studies also enabled determination of the sorptive capacity of the zeolite for the CO molecule. A technique of in situ infrared spectroscopy (in situ FTIR) was used in the studies, with a probe molecule for Ag.sup.+ cations (the band from vibrations of CO adsorbed on Ag.sup.+ occurs at 2,170 cm.sup.1). The measurements were carried out using two methods:
(83) Sorption of carbon monoxide at room temperature was carried out in order to define the quantitative ratio between the silver atoms in the first and zero oxidation state. The results are presented in
(84) Activation of the zeolite samples using conditioning in a vacuum was carried out at two temperaturesroom temperature, as well as at 80 C. and 450 C. Measurements at a temperature of 80 C. were carried out in order to check whether a removal of water from the zeolite by evaporation is possible, while preserving the intensity of the band originating from carbon monoxide being adsorbed, enabling an analysis of the samples. For the Y-type zeolite, this band is located at 2,175 cm.sup.1 and is attributed to an Ag.sup.+(CO) monocarbonyl group. As is shown in
(85) The results obtained after activation of the zeolite samples exchanged with silver at room temperature indicate that there is a high probability of occurrence of silver(I) in hexagonal prisms, because of the number of OH groups lower than in unexchanged zeolites. Activation at an elevated temperature (80 C.) allows for ascertaining that migration and reduction of silver occur in the zeolite, being in turn connected with formation of OH groups, which now have to balance the negative charge of the lattice. Metallic silver particles cannot perform this function.
(86) The degree of reduction of silver is higher in the case of the sample sonicated for a shorter time. In the case of the sample sonicated for 30 min and additionally washed with EDTA (ZAg+_son_30_EDTA), leaching of silver cations is observed, with an effect comparable to the non-sonicated sample (ZAg+_EDTA).
(87) TABLE-US-00008 TABLE 8 Number of silver ions per unit cell in the zeolite. Number of ions Ag.sup.+/unit Fraction of Ag.sup.+ in Atomic ratio Sample cell the sample Ag.sup.+/Ag.sup.0 ZAg+ 15.5 1 1:0 ZAg+_EDTA 6.4 1 1:0 ZAg0_son_10 8.5 0.6 3:2 ZAg0_son_10_EDTA 3.0 0.5 1:1 ZAg0_son_30 14.0 0.9 9:1 ZAg0_son_30_EDTA 5.0 0.8 4:1
(88) The presented results of the studies are complementary with XPS and XRF studies. Rinsing with an EDTA solution causes a decrease in the amount of silver ions (approx. 3-fold). In turn, the sonication process leads to a reduction of silver ions (formation of OH groups) only, however, when a short sonication time is used (10 min). Longer sonication results in repeated oxidation of silver.
(89) Using the results presented in Table 8, the degree of reduction of silver in a given sample (rinsed or non-rinsed series) may also be calculated. While calculating, it is assumed that a maximum amount of silver cations for the non-rinsed series is present in the ZAg+ sample, and for the series rinsed with EDTAin ZAg+_EDTA. Therefore, the fraction of the amount of silver cations in the sample amounts to 1 for reference samples. One should note that by proper selection of sonication time and application of the washing procedure, one may select the Ag.sup.+:Ag.sup.0 ratio in the obtained material. As for the operation of the material as a catalyst, the ZAg0_son_10 _EDTA sample was selected as an optimal material. This sample has a balance of oxidised and reduced silver, being important from the point of view of catalytic activity. This sample will be hereinafter referred to as ZAg0_EDTA.
EXAMPLE 2
Development of a Method for Shaping Paper Sheets Packed with the Zeolite
(90) Samples of paper sheets were prepared by disintegration of 4.00 g of Whatman filter paper in 400 cm.sup.3 of distilled water using a dispersing instrument (IKA T18 Ultra-Turrax). Depending on the type of the prepared sample, the properly prepared active material in the form of the zeolites (Table 9) was added to this paper pulp.
(91) TABLE-US-00009 TABLE 9 A method for preparation of model samples of the packaging material. Method for preparation of active material - Assay* Active material addition to the paper pulp P none not applicable PAg+ Ag.sup.+ 0.51 g of silver nitrate(V), corresponding to 0.003 mole of Ag in the material volume PZ0 Y 1.77 g of the Y-type zeolite in the paper pulp PAg0 Ag.sup.0 0.51 g of silver nitrate(V), sonicated in a suspension together with the paper pulp for 10 minutes (A = 100%) PZAg+ AgY 1.77 g of the Y-type zeolite exchanged with Ag.sup.+. PZAg0 AgY and Ag.sup.+ 1.77 g of the Y-type zeolite exchanged with Ag.sup.+, sonicated for 10 minutes (A = 100%) PZAg+_EDTA Y-type zeolite 1.77 g of the Y-type zeolite exchanged with Ag.sup.+, exchanged with silver rinsed with 300 cm.sup.3 of 0.1M EDTA solution ions - rinsed with and 150 cm.sup.3 of distilled water EDTA PZAg0_EDTA Y-type zeolite 1.77 g of the Y-type zeolite exchanged with Ag.sup.+, exchanged with silver rinsed with 300 cm.sup.3 of 0.1M EDTA solution ions, rinsed with and 150 cm.sup.3 of distilled water and sonicated for EDTA and subjected 10 minutes (A = 100%) to sonication
(92) The paper pulp was prepared according to the description shown in Table 9. The pulp was formed into paper sheets using a Bchner funnel or a vacuum plate. A hydrophobic cloth was used as a supporting element for the paper pulp being filtered. Drying of the sheets was carried out on a glass pane at room atmosphere. From the dried sheets, samples in the form of discs with a diameter of 6 mm were cut out. The samples were protected by placing them in paper envelopes. Disinfection of the samples was carried out in the stage of microbiological studies.
(93) Apart from the ion exchange of silver of the zeolites selected as the active material added to the paper sheets, it was necessary to develop proper procedures for preparation of sheets packed with the zeolite.
(94) Original Procedure
(95) In the original procedure for preparation of sheets in an aqueous medium, the active material (here the Y-type zeolite) was mixed with paper pulp dispersed in deionised water. In the beginning of the procedure's optimisation, a Bchner funnel was used to form the paper discs. Such a mode of operation required that the paper mass (with a volume of 400 cm.sup.3) was filtered off on an area with a diameter of approx. 25 mm. Therefore, it was necessary to pour the paper pulp slowly through a tube specially adapted to this purpose. After drying, the discs varied in their appearance depending on the side (bottom or top on the filtrating cloth). For the sake of these differences, the discs were tested for homogeneity of distribution of the active material in the volume of the sheet. The paper discs were examined by XRF spectroscopy, on each side, determining the silver content. The results obtained for all tested sheets proved that there are significant differences (up to 10%) in the amount of silver, depending on the side of the sample. Such a difference might affect the analysis of microbiological activity, because its results would depend on the arrangement of the paper disc on the nutrient medium. Most probably, the observed differences in the distribution of the zeolite material resulted from separation of the material components as a result of filtration. Moreover, it is noteworthy that in the case of thick paper samples, with the thickness of the order of 3 mm, a mass attenuated coefficient of X-rays penetrating the sample begins to be of significance, which is connected with attenuation of the XRF signal. In such a case, only the layer of the material reached by X-radiation is analysed. Considering the fact that during filtering and forming of the sheets, a segregation of silver occurs (the zeolite sediments faster than the paper pulp); the silver content may be measured only in the paper layer enriched with silver and not in the entire sample. Thus, the method for preparation of the paper sheets had to be changed so as to guarantee uniform distribution of the active material.
(96) Modified Procedure
(97) In the modified procedure, a vacuum plate was used, enabling the forming of paper sheets with a size of approx. 15-20 cm. Filtration time on such a large surface, with the same suction power, was reduced incomparably. The sheets were devoid of water practically at the instant the paper pulp landed on the filtration cloth. The sheets were then removed from the filtration cloth and placed on a glass pane (flat surface) for drying. From the so-prepared sheets, samples for tests were collected (now with a diameter of approx. 6 mm). In order to determine whether there were any changes in the silver content depending on the side of the sheet, an XRF analysis was carried out as in the previous case. The obtained results proved that there is no difference in the amount of silver depending on the side of the sample (differences below standard deviation of silver content measuremets). The paper sheets prepared using the new method were treated as model samples in physico-chemical studies and determination of the sorptive, catalytic and microbiological activity.
(98) Loss of the Active Material during Forming of the Sheets
(99) In spite of the optimisation of the procedure for preparation of the paper sheets aimed to ensure their homogeneity, it was necessary to determine the degree of loss of the active material. This indicated that the exchanged zeolite was placed in an aqueous medium in which leaching of silver from the zeolite structure could occur. Moreover, a concern arose that a part of the zeolite (particularly in the case of sonicated samplescomp. the influence of sonication on the zeolite structure described in a further part of the document) could be leached during filtering. Such a possibility occurs particularly in the first moments of filtering, when the zeolite had direct contact with the filtration paper and was able to penetrate through it. In order to verify this, the system for shaping of the sheets was equipped with a washer collecting the filtrate. The filtrate was then analysed with XRF in order to detect silver ions. The obtained results indicate that forming of the sheets was connected with a loss of silver. The analysis was based on the K line for silver. However, it should be emphasised that it was a semi-quantitative analysis. For the sake of the size of the system and the problem with quantitative collection of the entire filtrate, quantitative analysis made no sense. In connection with the detection of silver in the filtrates and the problem with quantitative measurements of the silver content, the final paper sheets were examined for silver content separately. The determination procedure was identical as in the case of the zeolites, but a sample of the paper was solubilised instead of the zeolite.
(100) Determination of the Silver Concentration in the Paper Sheets
(101) During the optimisation of the silver content in the final material, quantitative analysis was synchronised with the microbiological analysis in order to define the minimum silver content in the paper which would yield a satisfying biocidal activity. In Table 10, microbiological activity against the tested model organisms is shown.
(102) TABLE-US-00010 TABLE 10 Microbiological activity of the paper materials with various silver contents against selected test organisms. Silver content mg Ag/g of the paper Bacteria Fungi 87 + + 71 + + 46 + + 10 + + 1 + +/
(103) The silver content was determined according to the following procedure:
(104) 0.02 g of the paper was weighed out, approx. 7.5 ml of 65% nitric(V) acid was added to it, and the mixture was brought to boiling. The suspension was maintained at boiling temperature for 15 minutes while stirring. The suspension was transferred quantitatively to a test tube and centrifuged at a rate of 4,000 rpm. The supernatant was transferred quantitatively to a graduated flask with a volume of 25 ml. Distilled water was added to the precipitate in the test tube; the content was mixed, obtaining a suspension, and then centrifuged again. The procedure was repeated five times. The solution in the flask (after the procedure was finished) was made up to the mark. These solutions constituted the basis for the determination of silver with XRF.
(105) The concentration of silver in the prepared samples was determined with XRF from the calibration curve. The results are shown in
(106) TABLE-US-00011 TABLE 11 Percentage of silver in the final material and in the reference samples. Silver % of content silver mg Ag/g content of the in the Sample paper paper PAg+ 2.69 0.3 PZAg+ 14.9 1.5 PZAg+_EDTA 10.9 1.1 PZAg0 31.1 3.1 PZAg0_EDTA 5.9 0.6
(107) In the final material subjected to sonication and then washing with EDTA based on the developed procedure, the silver content is below 1% by wt. and amounts to 0.6% by wt.
EXAMPLE 3
Properties of the Obtained Paper Material
(108) Stability of the Obtained Paper Material
(109) Acidity of the Paper
(110) The parameters defining the stability of the paper include its acidity determined by the pH measurements. Measurements of the pH of the paper samples were carried out using a flat plate electrode (Flatrode Hamilton, 809 TitrandoMetrohm). Samples were cut out from the prepared paper sheets, and a drop of water was placed on each of them. A flat plate electrode was then applied to the sample, and the pH was measured until a stable value was obtained (however, for not less than 120 s). The measured pH values are presented in
(111) Another parameter defining the stability of the paper may consist in its degree after ageing tests. Conditioning of the samples was carried out according to the D685 ASTM standard at 23 C. and RH=50%. A procedure described in the D6819-02(2007) ASTM standard was used for the ageing tests. Ageing was carried out in a climatic chamber at 90 C. and a relative humidity of 59%. The ageing time of the samples amounted to 12 days. Both the paper made of pure cellulose and the paper with the zeolite were aged.
(112) Degree of Polymerisation of Cellulose
(113) The weight-averaged degree of polymerisation (DP.sub.w) of cellulose in the form of cellulose triphenylcarbamate (CTC) was determined. Analysis of molecular mass distributions was carried out in tetrahydrofurane, with double detection: by multiple angle laser light scattering (MALLS, Waters) and refractive index (RI). Both detectors worked at a light wavelength of 658 nm. In the measurements, a value of the specific increment of the refractive index equal to 0.162 cm.sup.3/g was used, determined experimentally on the chromatographic system used later for measurements of molecular mass distributions of the material.
(114) The cellulose material with zeolite was subjected to a standard procedure of the preparation of samples. The zeolite was separated from the CTC solution by filtration of the solution through a Teflon syringe filter with pore diameter of 0.45 m. The filtered solution was subjected to further SEC analysis.
(115) The paper with silver ions/nanoparticles and with silver ions/nanoparticles and the zeolite was washed before derivatisation in order to remove the silver ions/nanoparticles to avoid contamination of the chromatographic column. Samples of the paper containing Ag.sup.0, Ag.sup.+ and zeolite were defibered in a beaker in 50 cm.sup.3 of water (the process was aided by an ultrasound bath).
(116) TABLE-US-00012 TABLE 11 Weight polymerisation degrees DP.sub.w of model paper samples (SDstandard deviation), ageing - 12 days. Assay Type of the material DP.sub.w SD P Non-aged cellulose 1,228 8 P_S12 Cellulose aged for 12 days 918 95 PZ0 Cellulose with the zeolite - 1,238 82 non-aged PZ0_S12 Cellulose with the Y-type 1,285 44 zeolite - aged PAg+ Cellulose with silver ions - 1,288 7 non-aged PAg+_S12 Cellulose with silver ions - aged 115 3 PZAg+ Cellulose with the AgY zeolite - 1,077 38 non-aged PZAg+_S12 Cellulose with the AgY 423 14 zeolite - aged PAg0 Cellulose with Ag.sup.0 sonicated for 1,357 61 10 min - non-aged PAg0_S12 Cellulose with Ag.sup.0 sonicated 190 5 for 10 min - aged PZAg+_EDTA Cellulose with AgY, rinsed with 1,362 33 EDTA - non-aged PZAg+_EDTA_S12 Cellulose with AgY, 591 13 rinsed with EDTA - aged PZAg0 Cellulose with AgY and 1,341 17 Ag.sup.0 sonicated for 10 min - non-aged PZAg0_S12 Cellulose with AgY and 287 6 Ag.sup.0 sonicated for 10 min -aged PZAg0_EDTA Cellulose with z AgY and 1,259 28 Ag.sup.0 sonicated for 10 min,rinsed with EDTA - non-aged PZAg0_EDTA_S12 Cellulose with AgY and 514 37 Ag.sup.0 sonicated for 10 min, rinsed with EDTA - aged
(117) The weight-averaged degree of polymerisation was calculated based on the molecular mass distributions of the studied samples, obtained by SEC using a multiple angle laser light scattering (MALLS) detector.
(118) When comparing the samples before ageing in relation to DP.sub.w, one may ascertain that in spite of some decrease in the degree of polymerisation, resulting from the addition of a filler containing silver ions, the PZAg+_EDTA sample exhibits the lowest decrease in polymerisation in relation to the non-aged sample, significantly lower than the sonicated PZAg0 sample. Moreover, a slight increase in DP.sub.w was observed for the non-aged PZAg+_EDTA in comparison to the initial sample of the paper.
(119) In order to improve the structural parameters of the paper, the procedure of development of the final material was extended with an additional step of washing the paper packed with the zeolite and sonicated (PZAg0) with an EDTA salt solution, in the manner described in previous sections. Thus, the formed paper material (PZAg0_EDTA sample) had structural properties close to those of the PZAg.sup.+_EDTA material.
(120) A correlation of DP.sub.w and pH results may be noticed. The sheet exhibited a more basic reaction (PZ0) than the reference sample (P) only in the case of the paper packed with the zeolite. Therefore, it may be concluded that the increase in the degree of polymerisation of samples of the paper packed with the zeolite, sonicated and then rinsed with EDTA is connected with the decrease in acidity of the paper.
(121) Mechanical Properties
(122) As is shown in
(123) Sorptive and Catalytic Properties
(124) A part of the studies on sorption using carbon monoxide was presented in the previous section. In order to define the sorption and catalytic potential of the materials, acetic aldehyde was used for the studies as a representation of volatile organic compounds and, simultaneously, a possible product of degradation of various products (food, paper), as well as for the sake of its undesirable influence on human health. Samples of the sonicated zeolite ZAg0.sub. EDTA (sample sonicated for 10 min) and the non-sonicated zeolite ZAg.sup.+_EDTA were used for the comparison.
(125) The experiments were carried out in a flow system in situ in a reaction chamber (Harrick) inserted into the DRIFT attachment of an infrared spectrometer (Thermo Nicolet 6700). Before the tests, the samples of the zeolite placed in the reactor were heated at 110 C. under He flow in order to desorb part of the water present in the zeolite. Sorption of the aldehyde dosed from a saturator was carried out in the reactor under He flow at a rate of 20 cm.sup.3/min for 30 min at 25 C. After the sorption, and before turning the thermal programme on, the sample was blowed with He at 25 C. Analyses of transformations of the formaldehyde adsorbed on the zeolite surface were carried out at various temperatures under He flow.
(126) The results presented in
(127) Moreover, in the range of carbonyl group vibrations of the aldehyde, a band at 1,642 cm.sup.1 occurs, originating from bending vibrations of H.sub.2O molecules bound in the zeolite. The band at 1,680 cm.sup.1 is characteristic for stretching vibrations from carboxylic groups. Depending on the local potential around the adsorbed molecule, these bands may shift.
(128) A comparison of spectra for the presented material ZAg0_EDTA and the reference material ZAg.sup.+_EDTA indicates differences in the sorptive capacity and the catalytic activity of the materials (
(129) In an analogous experiment carried out in air as the carrier gas used instead of helium, in the thermal programme, acetic acid forms in the zeolite in a large amount already at room temperature, being a fundamental difference in comparison to the non-sonicated reference sample. The latter does not starts to oxidise acetic aldehyde to a significant degree before 100 C. (similar traces are also observed at room temperature) (comp. spectra
(130) A quantitative interpretation of the observed changes is shown in
(131) Acetic aldehyde is also adsorbed on samples of the final paper material (PZAg0_EDTA), shown in
(132) Definition of Microbiological Activity
(133) The studies were carried out using the following test organisms:
(134) Bacteria: 1. Escherichia coli 2. Serratia marcescens 3. Bacillus subtilis 4. Bacillus megatherium Fungi: 5. Trichoderma viride 6. Chaetomium globosum 7. Aspergillus niger 8. Cladosporium cladosporioides 9. Mortierella alpinum
(135) The above strains are stored on nutrient media in the laboratory of the Plant-Microbial Interactions team, Institute of Environmental Sciences and the Malopolska Centre of Biotechnology, Jagiellonian University (Krakw), and are used for comparative studies after inoculating onto proper nutrient media. A part of these strains was isolated from paper, and another part was obtained during other research.
(136) Comparison of Various Zeolite Materials
(137) The first step of quantitative analysis of microbiological activity consisted in the testing of a series of the zeolites which could be possibly used in nanocomposite packaging. Y-type (faujasite), ZSM-5 (pentozil) zeolites and MCM-56 molecular sieves (a mesoporous material) were used for the tests. These materials were exchanged with silver cations, similarly as described for the Y-type zeolite in previous sections.
(138) All tested materials exhibited antibacterial activity (
(139) Tests of the Paper Materials with the Y-type Zeolite
(140) The next step in determination of activity consisted in tests on finished paper sheets. Samples of the materials prepared at the Faculty of Chemistry of the Jagiellonian University were used for this test. Before the samples were used in the experiment, they were sterilised on Whatman paper in Petri dishes.
(141) Bacteria (strains 1-4) were placed onto the surface of agar (NA) and spread using a disposable spreader (a single spreader was used for a given strain). Every strain and every type of the paper sample was tested 3-5 times (some tests were rejected because of a non-uniform spreading of the material, which is visible several days after preparation; min. N=3). Onto each Petri dish with bacteria, a single paper disk was placed. The cultures were placed at a temperature of 32 C. for three days, and then the temperature was decreased to 25 C. for the next several days. Growth of the microorganisms was observed every day. No formation of a no-growth zone around the discs of the material was found in any tested sample, proving that silver did not propagate from the tested material.
(142) A further part of the experiment was transferred into a laminar chamber (sterile conditions). A significant decrease in bacteria growth under the discs with an addition of silver (in every form) was found. Every Petri dish was opened, and on the reverse side of its upper part, a paper disc was placed using a sterile pincette by turning it upside-down and thus exposing the part which was adjacent to the agar. A LuciPac Pen (ATP+AMP Hygiene Monitoring test kit from Kikkoman Corp. code 60331) was used for evaluation of bacterial populations, following recommendations, with minute innovations. The swab was positioned perpendicularly to the disc in its central part, and by leaning its tip against the disk in a screwdriver position, it was turned by 360. The result defining a relative ATP+AMP content was then read from the lumitester reader.
(143) Fungi (strains 5-9) were introduced onto Petri dishes containing a PDA nutrient medium, and three filters of each type were placed centrally onto each dish. In each case, the test was carried out in triplicate. The strains were introduced in the form of an agar disc with mycelium at a distance of 2 cm from the central disc. Due to the various rate of mycelium growth, it was necessary to carry out the test for a prolonged time (approx. 2 weeks). Each of the tested strains exhibited slightly different problems during observation.
(144) Trichoderma virideformed colonies with spores in a circular area of the colony's exterior; in some cases, the disc was found in the wrong place, hindering observations. In some cases, a delay in maturation of conidia was observed, manifested with their lighter colourlight green or yellow (outside this area, the conidia were blue-green).
(145) Chaetomium globosumformation of fruit bodies was generally delayed on the surface of the paper samples used, wherein the activity of the mycelium was probably focused on decomposition of the paper, while fructification constitutes a sign of lack of nutritive compounds.
(146) Aspergillus nigeris suitable for rapid tests, although spores freed from the surrounding conidiophores appeared on the surface of the discs with silver during the test, slightly hindering the analyses; however, no such conidia grew in such places, although they probably maintained their viability.
(147) Cladosporium cladosporioidesa species characterised by relatively slow growth; it was necessary to place the inoculum on the dishes again in order to accelerate the mycelium reaching the discs; formation of black mycelium (visible within the paper discs in cases when colonisation of the paper occurred) is an advantage of this species.
(148) Mortierella alpinalight mycelium with conidia containing no dark pigments.
(149) The results presented in
(150) Summary Relating to the Developed Material
(151) Taking into account such parameters as: silver content in paper preparations, stability of the paper, sorptive and catalytic properties, the PZAg0_EDTA paper material with the sonicated Y-type zeolite exchanged with silver significantly enriches the expected assumptions for packaging. Based on optimisation of the silver content, a material containing less than 1% by wt. of silver was chosen for physico-chemical studies. This is the lowest value for which biocidal activity against all tested organisms was observed. The proposed material has a hybrid character, in which the active agent is in the form containing both cations and reduced silver bound in the zeolite matrix. The sorptive properties of the material confirmed for carbon monoxide and acetic aldehyde are noteworthy. Another advantage of the material consists in its ability to catalyse oxidation reactions at room temperature without the access of air, which has been ascertained in the example of acetic aldehyde oxidation. High biocidal activity was confirmed in tests with selected strains of microorganisms typically occurring in food and archival materials. A relatively lower microbiocidal capacity was found for Bacillus megaterium bacteria and Aspergillus fungi.