• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
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  • 优先权
    • 专利摘要:
    A method for making silver nanowires is provided, wherein the recovered silver nanowires have a high aspect ratio; and where the total glycol concentration is <0.001 wt% at any time during the process.
    公开号:FR3027539A1
    申请号:FR1560275
    申请日:2015-10-28
    公开日:2016-04-29
    发明作者:Robin P Ziebarth；Richard A Patyk；Wei Wang；Patrick T Mcgough；George L Athens；Janet M Goss；Jonathan D Lunn
    申请人:Dow Global Technologies LLC；
    IPC主号:
    专利说明:

    [0001] The present invention relates generally to the field of manufacturing silver nanowires. In particular, the present invention relates to a method for producing silver nanowires having a high aspect ratio for use in a variety of applications. [0002] High conductivity films with high transparency are of great value for use as electrodes or coatings in a wide range of electronic applications, including, for example, touchscreen displays and cells. PV. Current technology for these applications involves the use of films containing tin-doped indium oxide (ITO) that are deposited by physical vapor deposition processes. The high capital cost of physical vapor deposition processes has led to the desire to find other transparent conductive materials and other coating approaches. The use of dispersed silver nanowires in the form of a percolation network has emerged as a promising alternative to films containing ITO. The use of silver nanowires has the potential advantage that they can be implemented using roll-to-roll techniques. Thus, silver nanowires have the advantage of low cost manufacturing with the potential to provide higher transparency and conductivity than conventional ITO containing films. The "polyol process" has been disclosed for the manufacture of silver-based nanostructures. The polyol process utilizes ethylene glycol (or other glycol) both as a solvent and as a reducing agent in the production of silver nanowires. The use of glycols, however, has several inherent disadvantages. Specifically, the use of a glycol as both a reducing agent and a solvent leads to a decrease in the control of the reaction because the main species of reducing agent (glycolaldehyde) is produced in situ and its presence and concentration are dependent on the extent of exposure to oxygen. Also, the use of a glycol introduces the possibility of formation of combustible glycol / air mixtures in the free space of the reactor used to produce the silver nanowires. Finally, the use of large volumes of glycol creates waste problems, which increases the cost of marketing such operations. [0004] An approach constituting an alternative to the polyol process for making silver nanowires has been disclosed by Miyagishima, et al. in U.S. Patent Application Publication No. 20100078197. Miyagishima, et al. disclose a method for producing metal nanowires, comprising: adding a solution of a metal complex to an aqueous solvent containing at least one halide as a reducing agent, and heating the resulting mixture to 150 ° C or less, wherein the metal nanowires comprise metal nanowires having a diameter of 50 nm or less and a major axis length of 5 nm or more in an amount of 50% by mass or more in terms of the amount of metal relative to the total metal particles. [0005] Another approach constituting an alternative to the polyol process for making silver nanowires has been disclosed by Lunn, et al. in U.S. Patent Application Publication No. 20130283974. Lunn, et al. disclose a method for making silver nanowires having a high aspect ratio, wherein the recovered silver nanowires have an average diameter of 25 to 80 nm and an average length of 10 to 100 μm; and where the total glycols concentration is <0.001% by weight at any time during the process. However, while producing silver nanowires having a desirable high aspect ratio, the manufacturing method described by Lunn, et al. Also leads to the formation of silver nanowire populations having an extended diameter distribution which can lead to a lack of uniformity in the electrical properties of the films produced therewith. [0007] Thus, there remains a need for other methods for manufacturing silver nanowires. In particular, processes for manufacturing silver nanowires which do not involve the use of a glycol, wherein the produced silver nanowires have a high aspect ratio (preferably> 500) in combination with a narrow distribution of diameters of silver nanowires. The present invention provides a method for manufacturing silver nanowires having a high aspect ratio, comprising: providing a container; the supply of water; the supply of a reducing sugar; supply of a reducing agent; providing a polyvinylpyrrolidone (PVP), wherein the polyvinylpyrrolidone (PVP) provided is divided into a first portion of the polyvinylpyrrolidone (PVP) and a second portion of the polyvinylpyrrolidone (PVP); providing a source of copper (II) ions; providing a source of halide ions; providing a source of silver ions, wherein the supplied silver ion source is divided into a first portion of the silver ion source and a second portion of the silver ion source; adding water, reducing sugar, copper ion source (II) and the halide ion source to the container to form a combination; heating the combination at 110 to 160 ° C; adding the first portion of the polyvinylpyrrolidone (PVP), the first portion of the silver ion source and the reducing agent to the combination in the vessel to form a creation mixture; then adding to the vessel the second portion of the polyvinylpyrrolidone (PVP) and the second portion of the silver ion source to form a growth mixture; maintaining the growth mixture at 110 to 160 ° C for a holding period of 2 to 30 hours to provide a product mixture; and recovering a plurality of silver nanowires having a high aspect ratio from the product mixture; where the concentration of total glycols in the container is <0.001% by weight at any time. According to a particular characteristic, the first part of the polyvinylpyrrolidone (PVP) and the first part of the silver ion source are added to the container simultaneously. According to another particular feature, the first part of the silver ion source is added to the combination under a surface of the combination in the container. In a particular embodiment, the method of the present invention further comprises: a delay period, wherein the delay period is disposed between the addition of the first portion of the silver ion source to form the mixture of creating and adding the second portion of the silver ion source to form the growth mixture. According to a particular characteristic, the first part of the polyvinylpyrrolidone (PVP) represents 10 to 40% by weight of the polyvinylpyrrolidone (PVP) supplied, and the first part of the source of silver ions represents 10 to 40% by weight of the silver ion source supplied. According to another particular characteristic, the reducing agent is chosen from ascorbic acid; borohydride salts; hydrazine; salts of hydrazine; hydroquinone; C1-5 alkylaldehydes and benzaldehyde. According to another particular feature, the reducing sugar provided is glucose, and the reducing agent provided is at least one of ascorbic acid and sodium borohydride. In another particular embodiment, the method of the present invention further comprises: providing a pH adjusting agent; and adding the pH adjusting agent to the combination, wherein the combination has a pH of 2.0 to 4.0 as a result of the addition of the pH adjusting agent. In another particular embodiment, the method of the present invention further comprises: purging a gas space from the container in contact with the combination into the container to provide a reduced oxygen gas concentration in the gas space of the container. container; bubbling into the silver ion source provided with an inert gas to extract entrained oxygen gas from the supplied silver ion source and to give a low concentration of oxygen gas in a silver ion gas space in contact with the silver ion source provided; purging a PVP gas space in contact with the polyvinylpyrrolidone (PVP) provided to provide a dilute oxygen gas concentration in the PVP gas space; maintaining the low oxygen gas concentration in the silver ion gas space and the dilute oxygen gas concentration in the PVP gas space; and maintaining the reduced oxygen gas concentration in the container gas space during formation of the creation mixture, during formation of the growth mixture and during the holding period. In yet another particular embodiment, the reducing sugar provided is glucose; the reducing agent provided is selected from ascorbic acid; borohydride salts; hydrazine; salts of hydrazine; hydroquinone; C1-5 alkylaldehydes and benzaldehyde; the polyvinylpyrrolidone (PVP) provided has a weight average molecular weight, Mw, of 40,000 to 150,000 Daltons; the copper (II) ion source supplied is copper (II) chloride; The source of halide ions supplied is sodium chloride; the silver ion source supplied is silver nitrate; the first part of the polyvinylpyrrolidone (PVP) represents 10 to 40% by weight of the polyvinylpyrrolidone (PVP) supplied; and the first part of the silver ion source is 10 to 40% by weight of the silver ion source supplied. The present invention provides a method for making silver nanowires having a high aspect ratio, comprising: providing a container; the supply of water; the supply of a reducing sugar; providing a reducing agent, wherein the reducing agent is selected from the group consisting of ascorbic acid, sodium borohydride (NaBH4), hydrazine, hydrazine salts, hydroquinone, C1- -5 alkylaldehydes and benzaldehyde; providing a polyvinylpyrrolidone (PVP), wherein the polyvinylpyrrolidone (PVP) provided is divided into a first portion of the polyvinylpyrrolidone (PVP) and a second portion of the polyvinylpyrrolidone (PVP); providing a source of copper (II) ions; providing a source of halide ions; providing a source of silver ions, wherein the supplied silver ion source is divided into a first portion of the silver ion source and a second portion of the silver ion source; adding water, reducing sugar, copper ion source (II) and the halide ion source to the container to form a combination; heating the combination at 110 to 160 ° C; adding the first portion of the polyvinylpyrrolidone (PVP), the first portion of the silver ion source and the reducing agent to the combination in the vessel to form a creation mixture; then adding to the vessel the second portion of the polyvinylpyrrolidone (PVP) and the second portion of the silver ion source to form a growth mixture; maintaining the growth mixture at 110 to 160 ° C for a holding period of 2 to 30 hours to provide a product mixture; and recovering a plurality of silver nanowires having a high aspect ratio from the product mixture; where the concentration of total glycols in the container is <0.001% by weight at any time. The present invention provides a method for manufacturing silver nanowires having a high aspect ratio, comprising: providing a container; the supply of water; the supply of a reducing sugar; supply of a reducing agent; providing a polyvinylpyrrolidone (PVP), wherein the polyvinylpyrrolidone (PVP) provided is divided into a first portion of the polyvinylpyrrolidone (PVP) and a second portion of the polyvinylpyrrolidone (PVP); providing a source of copper (II) ions; providing a source of halide ions; providing a source of silver ions, wherein the supplied silver ion source is divided into a first portion of the silver ion source and a second portion of the silver ion source; providing a pH adjusting agent; adding water, reducing sugar, copper ion source (II), halide ion source and pH adjusting agent to the container to form a combination; wherein the combination has a pH of 2.0 to 4.0; heating the combination at 110 to 160 ° C; adding the first portion of the polyvinylpyrrolidone (PVP), the first portion of the silver ion source and the reducing agent to the combination in the vessel to form a creation mixture; then adding to the vessel the second portion of the polyvinylpyrrolidone (PVP) and the second portion of the silver ion source to form a growth mixture; maintaining the growth mixture at 110 to 160 ° C for a holding period of 2 to 30 hours to provide a product mixture; and recovering a plurality of silver nanowires having a high aspect ratio from the product mixture; where the concentration of total glycols in the container is <0.001% by weight at any time. DETAILED DESCRIPTION [0011] A method for making silver nanowires having a high aspect ratio has been found which surprisingly provides silver nanowires having an average diameter of 20. at 60 nm and an average length of 20 to 100 μm, while avoiding the inherent disadvantages that are associated with the use of glycols and while providing silver nanowires having a high degree of uniformity of diameters. Silver nanowire populations having a narrow diameter distribution as provided by the method of the present invention provide an advantage in the preparation of films having more uniform conductive properties and transparency in the film. The term "total glycol concentration" as used herein for the contents of the container means the combined total of the concentration of all glycols (eg, ethylene glycol, propylene glycol, butylene glycol, poly (ethylene glycol), poly (propylene glycol)) present in the container. The term "high aspect ratio" as used herein about recovered silver nanowires means that the average aspect ratio of recovered silver nanowires is> 500. [0014] The term "silver nanoparticle fraction" or IINPF "used herein is the silver nanoparticle fraction of a silver nanowire sample determined according to the following equation: NPF = NPA / TA where TA is the surface area total of a substrate that is occluded by a given deposited sample of silver nanowires; and, NPA is the portion of the total occluded surface area attributable to silver nanoparticles having an aspect ratio <3 included in the deposited sample of silver nanowires. Preferably, the method for manufacturing silver nanowires having a high aspect ratio of the present invention comprises: providing a container; the supply of water; the supply of a reducing sugar; supply of a reducing agent; providing polyvinylpyrrolidone (PVP), wherein the polyvinylpyrrolidone (PVP) provided is divided into a first portion of the polyvinylpyrrolidone (PVP) and a second portion of the polyvinylpyrrolidone; providing a source of copper (II) ions; providing a source of halide ions; providing a source of silver ions, wherein the supplied silver ion source is divided into a first portion of the silver ion source and a second portion of the silver ion source; adding water, reducing sugar, copper ion source (II) and the halide ion source to the container to form a combination; heating the combination at 110 to 160 ° C (preferably at 120 to 150 ° C, more preferably at 125 to 140 ° C, particularly preferably at 130 ° C); adding (preferably stirring) the first portion of the polyvinylpyrrolidone (PVP), the first portion of the silver ion source and the reducing agent to the combination into the vessel to form a creation mixture; then (preferably, following a delay period) adding to the creating mixture the second part of the polyvinylpyrrolidone (PVP) and the second part of the silver ion source to form a growth mixture ; maintaining the growth mixture at a temperature of 110 to 160 ° C (preferably 120 to 150 ° C, more preferably 125 to 135 ° C, particularly preferably 130 ° C) for a period of holding for 2 to 30 hours (preferably 4 to 20 hours, more preferably 6 to 15 hours) to provide a product mixture; and recovering a plurality of silver nanowires having a high aspect ratio from the product mixture; where the concentration of total glycols in the container is <0.001% by weight at any time during the process. Preferably, wherein the weight ratio of polyvinylpyrrolidone (PVP) to silver ions added to the container is 4: 1 to 10: 1; and wherein the weight ratio of halide ions to copper (II) ions added to the container is 1: 1 to 5: 1. Preferably, wherein the plurality of silver nanowires having a high aspect ratio recovered have a mean diameter of 5.40 nm (preferably 20 to 40 nm, more preferably 20 to 35 nm; preferably from 20 to 30 nm) and an average length of 10 to 100 μm. Preferably, wherein the plurality of silver nanowires having a high aspect ratio recovered have an average aspect ratio of> 500. [0016] Preferably, the water provided in the process for producing silver nanowires having a high aspect ratio of the present invention is at least one of deionized water and distilled water to limit accidental impurities. More preferably, the water provided in the process for making silver nanowires having a high aspect ratio of the present invention is deionized and distilled. Most preferably, the water provided in the process for making silver nanowires having a high aspect ratio of the present invention is ultrapure water which meets or exceeds the requirements for Type 1 water according to ASTM D1193-99e1 (Standard Specification for Reagent Grade Water) ("Standard Specification for Reagent Water"). Preferably, the reducing sugar provided in the process for making silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of at least one of the aldoses (e.g., glucose). glyceraldehyde, galactose, mannose); disaccharides with a free hemiacetal unit (eg, lactose and maltose); and sugars carrying a ketone (eg, fructose). More preferably, the reducing sugar provided in the process for making silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of at least one of an aldose, lactose, maltose and fructose. More preferably, the reducing sugar provided in the process for making silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of at least one of glucose, glyceraldehyde, galactose , mannose, lactose, fructose and maltose. Most preferably, the reducing sugar provided in the process for making silver nanowires having a high aspect ratio of the present invention is D-glucose. [0018] Preferably, the polyvinylpyrrolidone (PVP) provided in the process for producing silver nanowires having a high aspect ratio of the present invention has a weight average molecular weight, Mw, of 20000 to 300000 Daltons. More preferably, the polyvinylpyrrolidone (PVP) provided in the process for making silver nanowires having a high aspect ratio of the present invention has a weight average molecular weight, Mw, of 30,000 to 200,000 Daltons. Particularly preferably, the polyvinylpyrrolidone (PVP) provided in the process for producing silver nanowires having a high aspect ratio of the present invention has a weight average molecular weight, Mw, of from 40000 to 150,000 Daltons, preferably still from 40000 to 60000 Daltons. Preferably, the polyvinylpyrrolidone (PVP) supplied is divided into a first part of the polyvinylpyrrolidone (PVP) and a second part of the polyvinylpyrrolidone (PVP). Preferably, the first part of the polyvinylpyrrolidone (PVP) is 10 to 40% by weight (more preferably 10 to 30% by weight, particularly preferably 15 to 25% by weight) of the polyvinylpyrrolidone (PVP) provided. . Preferably, the copper (II) ion source provided in the process for producing silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of at least one of CuCl2 and Cu (NO3) 2. More preferably, the copper (II) ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of CuCl 2 and Cu (NO3) 2. Particularly preferably, the copper (II) ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is CuCl 2, where CuCl 2 is a copper (II) chloride. ) di hydrated. [0021] Preferably, the halide ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of at least one of a source chloride ion source, fluoride ion source, bromide ion source and iodide ion source. More preferably, the halide ion source provided in the process for producing silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of at least one of a source of chloride ions and a source of fluoride ions. More preferably, the halide ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is a source of chloride ions. Most preferably, the halide ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is a source of chloride ions, where the source of chloride ions is an alkali metal chloride. Preferably, the alkali metal chloride is selected from the group consisting of at least one of sodium chloride, potassium chloride and lithium chloride. More preferably, the alkali metal chloride is selected from the group consisting of at least one of sodium chloride and potassium chloride. Particularly preferably, the alkali metal chloride is sodium chloride. [0022] Preferably, the silver ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is a silver complex. More preferably, the silver ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is a silver complex, wherein the silver complex is selected from the group consisting of at least one of silver nitrate (AgNO3) and silver acetate (AgC2H302). Most preferably, the silver ion source provided in the process for making silver nanowires having a high aspect ratio of the present invention is silver nitrate (AgNO 3). Preferably, the silver ion source provided in the process for producing silver nanowires having a high aspect ratio of the present invention has a silver concentration of 0.005 to 1 molar (M) (more preferably from 0.01 to 1 M, particularly preferably from 0.4 to 1 M). Preferably, the provided silver ion source is divided into a first part of the silver ion source and a second part of the silver ion source. Preferably, the first part of the silver ion source is 10 to 40% by weight (more preferably 10 to 30% by weight, particularly preferably 15 to 25% by weight) of the ion source. money provided. [0024] Preferably, the reducing agent provided in the process for making high aspect ratio silver nanowires of the present invention is selected from the group consisting of ascorbic acid; borohydride salts (e.g., NaBH4, KBH4, LiBH4, Ca (BH4) 2); hydrazine; salts of hydrazine; hydroquinone; C1-5 alkylaldehydes and benzaldehyde. More preferably, the reducing agent provided in the process for making silver nanowires having a high aspect ratio of the present invention is selected from the group consisting of ascorbic acid, sodium borohydride (NaBH4), potassium borohydride (KBH4), lithium borohydride (LiBH4), calcium borohydride (Ca (BH4) 2), hydrazine, hydrazine salts, hydroquinone, acetaldehyde, propionaldehyde and benzaldehyde. Most preferably, the reducing agent provided in the process for making silver nanowires having a high aspect ratio of the present invention is at least one of ascorbic acid and sodium borohydride. Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the water, the reducing sugar, the source of copper (II) ions, the source of halide ions and the pH adjusting agent, if any, are added to a vessel (preferably, where the vessel is a reactor, more preferably, where the vessel is a reactor equipped with a stirrer ) to form a combination; then, the silver ion source is added to the combination in the container (preferably, with stirring) to form a growth mixture while maintaining the combination at a temperature of 110 to 160 ° C (preferably 120 to 160 ° C). 150 ° C, more preferably from 125 to 135 ° C, particularly preferably from 130 ° C) during the addition of the silver ion source and after the addition of the silver ion source during a holding period of 2 to 30 hours (preferably 4 to 20 hours, more preferably 6 to 15 hours) to provide the product mixture. Preferably, the water, the reducing sugar, the source of copper (II) ions, the source of halide ions and the pH adjusting agent, if any, are added to the container in any order in an individual succession (ie, one at a time), simultaneously (ie, all at the same time), or semi-simultaneously (ie, some individually a at the same time, some simultaneously at the same time or in the form of sub-combinations) to form a combination. More preferably, at least two of the water, the reducing sugar, the copper (II) ion source, the halide ion source and the pH adjusting agent, if any, are mixed together to form a sub-combination prior to addition to the container to form the combination. Preferably, the method for producing silver nanowires having a high aspect ratio of the present invention further comprises: a delay period, wherein the delay period is disposed between the addition of the first portion of the silver ion source to form the creation mixture and the addition of the second part of the silver ion source to form the growth mixture. Preferably, the delay period between additions is 5 seconds to 60 minutes (more preferably 1 to 20 minutes, particularly preferably 5 to 15 minutes). Preferably, in the method of the present invention: the supplied silver ion source is divided into a first part of the silver ion source and a second part of the silver ion source, where the first part of the source The amount of silver ion is 10 to 30% by weight of the silver ion source provided (preferably, where the first part of the silver ion source is 15 to 25% by weight of the silver ion source supplied. more preferably, where the first part of the silver ion source is 20% by weight of the supplied silver ion source). The method for producing silver nanowires having a high aspect ratio of the present invention preferably further comprises: providing a pH adjusting agent; and adding the pH adjusting agent to the container. The pH adjusting agent may be added to the container together with the water, the reducing sugar, the copper ion source (II) and the halide ion source as part of the combination; wherein the combination has a pH of 2.0 to 4.0 (preferably 2.0 to 3.5, more preferably 2.4 to 3.3, particularly preferably 2.6). The pH adjusting agent may be added to the container simultaneously with the polyvinylpyrrolidone (PVP). Preferably, when the pH adjusting agent is added simultaneously with the polyvinylpyrrolidone (PVP), the pH adjusting agent is added to the polyvinylpyrrolidone (PVP) prior to addition to the container. ; wherein the polyvinylpyrrolidone (PVP) has a pH of 2.0 to 4.0 (preferably 2.0 to 3.5, more preferably 2.3 to 3.3, most preferably 3.1 to 3.3). Preferably, the pH adjusting agent is added to the polyvinylpyrrolidone (PVP) supplied before the division of the polyvinylpyrrolidone (PVP) provided in a first portion of the polyvinylpyrrolidone (PVP) and a second portion of the polyvinylpyrrolidone (PVP) wherein the polyvinylpyrrolidone (PVP) provided has a pH of 2.0 to 4.0 (preferably 2.0 to 3.5, more preferably 2.3 to 3.3, most preferably , from 3.1 to 3.3). [0029] Preferably, the pH adjusting agent provided in the process for making high aspect ratio silver nanowires of the present invention is an acid. More preferably, the pH adjusting agent provided in the process for producing silver nanowires having a high aspect ratio of the present invention is an acid, wherein the acid is selected from the group consisting of at least one of the inorganic acids (eg, nitric acid, sulfuric acid, hydrochloric acid, fluorosulfuric acid, phosphoric acid, fluoroantimonic acid) and organic acids (eg for example, methanesulfonic acid, ethanesulphonic acid, benzenesulphonic acid, acetic acid, fluoroacetic acid, chloroacetic acid, citric acid, gluconic acid, lactic acid). Preferably, the pH adjusting agent provided in the process for making silver nanowires having a high aspect ratio of the present invention has a pH value. <2.0. More preferably, the pH adjusting agent provided in the process for making silver nanowires having a high aspect ratio of the present invention includes nitric acid. Most preferably, the pH adjusting agent provided in the process for making silver nanowires having a high aspect ratio of the present invention is aqueous nitric acid. [0030] Preferably, the method for producing silver nanowires having a high aspect ratio of the present invention further comprises: purging a gas space of the container in contact with the combination in the container to give a reduced oxygen gas concentration in the gas space of the vessel. Preferably, the step of purging the gas space of the container in contact with the combination in the container to give the reduced oxygen gas concentration in the gas space of the container, includes: (i) the isolation of the gas space of the container of a surrounding atmosphere outside the container; (ii) then pressurizing the vessel gas space with an inert gas (preferably, wherein the inert gas is selected from the group consisting of argon, helium, methane, and nitrogen (more preferably argon, helium and nitrogen, more preferably argon and nitrogen, particularly preferably nitrogen); and (iii) thereafter purging the gas space of the vessel to provide the reduced oxygen gas concentration in the gas space of the vessel. Preferably, the gas space of the vessel is vented to a pressure in the vessel which is> the atmospheric pressure of the surrounding atmosphere) to give the reduced oxygen gas concentration in the gas space of the vessel. Preferably, the reduced oxygen gas concentration is 2000 ppm (more preferably 400 ppm, particularly preferably 5. 20 ppm). More preferably, the step of purging the gas space of the container in contact with the combination in the container to give the reduced oxygen gas concentration in the gas space of the container, includes: (i) isolation the gas space of the container of a surrounding atmosphere outside the container; (ii) then pressurizing the vessel gas space with an inert gas (preferably, wherein the inert gas is selected from the group consisting of argon, helium, methane, and nitrogen (more preferably argon, helium and nitrogen, more preferably argon and nitrogen, particularly preferably nitrogen); and (iii) thereafter purging the gas space of the vessel to provide the reduced oxygen gas concentration in the gas space of the vessel (preferably, where the gas space of the vessel is vented to a pressure in the container which is> the atmospheric pressure of the surrounding atmosphere outside the container); and (iv) repeating steps (ii) and (iii) at least three times to give the reduced oxygen gas concentration in the container gas space (preferably, where the reduced oxygen gas concentration is 2000 ppm). (more preferably, 400 ppm, particularly preferably 20 ppm)). Preferably, the method for making silver nanowires having a high aspect ratio of the present invention further comprises: maintaining a reduced oxygen gas concentration in the container gas space during formation of the mixture during the formation of the growth mixture and during the maintenance period. [0031] Preferably, the method for producing silver nanowires having a high aspect ratio of the present invention further comprises: bubbling into the silver ion source provided with an inert gas to extract the oxygen gas driven from the silver ion source and to give a low oxygen gas concentration in a silver ion gas space in contact with the silver ion source. Preferably, the bubbling step in the silver ion source provided with an inert gas comprises (preferably consists of): bubbling into the supplied silver ion source of an inert gas (preferably, where the inert gas is selected from the group consisting of argon, helium, methane, and nitrogen (more preferably argon, helium and nitrogen, more preferably argon and nitrogen, particularly preferably nitrogen) during a bubbling time. 5 minutes (more preferably 5 minutes to 2 hours, particularly preferably 5 minutes to 1.5 hours) prior to addition to the vessel to extract entrained oxygen gas from the supplied silver ion source and give a low concentration of oxygen gas in the silver ion gas space. Preferably, the low oxygen gas concentration in the silver ion gas space is 10000 ppm (preferably 1000 ppm, more preferably 400 ppm, particularly preferably 5 ppm). Preferably, the method for making silver nanowires having a high aspect ratio of the present invention further comprises: maintaining a low concentration of oxygen gas in the silver ion gas space up to the supplied silver ion source is added to the container. Preferably, the method for producing silver nanowires having a high aspect ratio of the present invention further comprises: purging a PVP gas gap in contact with the polyvinylpyrrolidone (PVP) provided for give a dilute oxygen gas concentration in the PVP gas space. Preferably, the step of purging the PVP gas space to provide the dilute oxygen gas concentration in the PVP gas space includes: (i) isolating the polyvinylpyrrolidone (PVP) supplied; (ii) then pressurizing the PVP gas space with an inert gas (preferably, wherein the inert gas is selected from the group consisting of argon, helium, methane, and nitrogen (more preferably argon, helium and nitrogen, more preferably argon and nitrogen, particularly preferably nitrogen); and (iii) thereafter purging the PVP gas space to give the dilute oxygen gas concentration in the PVP gas space. Preferably, the PVP gas space is purged to a pressure that is> atmospheric pressure of the surrounding atmosphere to give the dilute oxygen gas concentration in the PVP gas space. More preferably, the step of purging the PVP gas space to provide the dilute oxygen gas concentration in the PVP gas space includes: (i) isolating the polyvinylpyrrolidone (PVP) provided; (ii) then pressurizing the PVP gas space with an inert gas (preferably, wherein the inert gas is selected from the group consisting of argon, helium, methane, and nitrogen (more preferably argon, helium and nitrogen, more preferably argon and nitrogen, particularly preferably nitrogen); (iii) then purging the PVP gas space to give the concentration of dilute oxygen gas in the PVP gas space (preferably, where the PVP gas space is purged to a pressure of inert gas which is> atmospheric pressure); and (iv) repeating steps (ii) and (iii) at least three times to provide the dilute oxygen gas concentration in the PVP gas space. Preferably the dilute oxygen gas concentration in the PVP gas space is 5000 ppm (preferably 1000 ppm, more preferably 400 ppm, particularly preferably ppm). Preferably, the method for making silver nanowires having a high aspect ratio of the present invention further comprises: maintaining the dilute oxygen gas concentration in the PVP gas space until the Polyvinylpyrrolidone (PVP) provided is added to the container. Preferably, the method for producing silver nanowires having a high aspect ratio of the present invention further comprises: bleeding a gas space from the container in contact with the combination in the container to give a reduced oxygen gas concentration in the container gas space; bubbling into the silver ion source provided with an inert gas to extract the entrained oxygen gas from the supplied silver ion source and to give a low concentration of oxygen gas in a silver ion gas space in contact with the silver ion source provided; purging a PVP gas gap in contact with the polyvinylpyrrolidone (PVP) provided to provide a dilute oxygen gas concentration in the PVP gas space; maintaining the low oxygen gas concentration in the silver ion gas space and the dilute oxygen gas concentration in the PVP gas space; and maintaining the reduced oxygen gas concentration in the container gas space during formation of the creation mixture, during formation of the growth mixture and during the holding period. [0034] Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the polyvinylpyrrolidone (PVP) supplied and a certain amount of the water are supplied in the form of a sub-combination of polyvinylpyrrolidone (PVP). Preferably, the polyvinylpyrrolidone (PVP) supplied is divided into a first portion of the polyvinylpyrrolidone (PVP) and a second portion of the polyvinylpyrrolidone (PVP) as a result of the formation of a polyvinylpyrrolidone (PVP) sub-combination with the water. Preferably, the first part of the polyvinylpyrrolidone (PVP) and the second part of the polyvinylpyrrolidone (PVP) are separately added to the container simultaneously with the first part of the silver ion source and the second part of the silver ion source. , respectively. When the polyvinylpyrrolidone (PVP) and the silver ion source are added to the vessel simultaneously, but separately (i.e., through separate entry points); at least one of polyvinylpyrrolidone (PVP) and the silver ion source is added at a point beneath a surface of the combination in the container (preferably, where the first part of the silver ion source and the second part of the silver ion source are introduced into the container at a point below the surface of the combination in the container and where the first part of the polyvinylpyrrolidone (PVP) and the second part of the polyvinylpyrrolidone (PVP) are introduced in the container at a point above the surface of the combination in the container). [0035] Preferably, the water is divided into at least two volumes of water (more preferably at least three volumes of water, particularly preferably at least four volumes of water). ) to facilitate formation of at least two sub-combinations which include water prior to addition to the container. More preferably, the water is divided into at least five volumes of water, wherein a first volume of water is combined with the reducing sugar to form a sub-combination of reducing sugar, wherein a second volume of water is combined with the copper (II) ion source to form a sub-combination of copper (II) ions, wherein a third volume of water is combined with the halide ion source to form a sub-ionic combination halide, where a fourth volume of water is combined with the polyvinylpyrrolidone (PVP) provided to form a polyvinylpyrrolidone (PVP) sub-combination, where a fifth volume of water is combined with the silver ion source to form a sub-combination of - 15 combination of silver ions. Preferably, the reducing sugar sub-combination, the copper (II) ion sub-combination, the halide ion sub-combining and the pH adjusting agent, if any, are added. to the container in any order in an individual succession (i.e., one at a time), simultaneously (i.e. all at the same time), or semi-simultaneously (i.e., some individually one at a time, some simultaneously at the same time or in the form of additional sub-combinations) to form the combination. More preferably, the reducing sugar sub-combination is added to the vessel, followed by the addition to the vessel of the copper (II) ion sub-combination, the halide ion sub-combination and the pH adjusting agent, if any, in any order in an individual succession (i.e., one at a time), simultaneously (i.e. all at the same time), or serni-simultaneously (that is, some individually one at a time, some simultaneously simultaneously or as additional sub-combinations) to form the combination. Particularly preferably, the reducing sugar sub-combination is added to the vessel, followed by the addition of the copper (II) ion sub-combination to the vessel, followed by the addition of the ion sub-combination. halide to the vessel, followed by the addition of the pH adjusting agent, if any, to form the combination. The polyvinylpyrrolidone (PVP) sub-combination, the silver ion sub-combination and the reducing agent are then added to the combination in the container. Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the reducing agent and a certain amount of water are provided in the form of a sub-combination. reducing agent. Preferably, the reducing agent is added to the vessel following the addition of the first portion of the silver ion source. More preferably, the reducing agent is added to the vessel following the addition of the first portion of the silver ion source and the first portion of the polyvinylpyrrolidone (PVP). Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the total glycol concentration in the container is <0.001% by weight at any time during the process. Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the polyvinylpyrrolidone (PVP) and the silver ion source are added to the container at a ratio by weight of silver ion polyvinylpyrrolidone (PVP) of 4: 1 to 10: 1 (more preferably 5: 1 to 8: 1, most preferably 6: 1 to 7: 1). [0039] Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the halide ion source and the copper (II) ion source are added to the container. a weight ratio of the halide ions to copper (II) ions of from 1: 1 to 5: 1 (more preferably from 2: 1 to 4: 1, particularly preferably from 2.5: 1 to 3.5 : 1). Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the reducing agent is provided in an amount sufficient to convert 0.01 to 5.0 mol% (of more preferably, from 0.025 to 1 mol%, particularly preferably from 0.04 to 0.6 mol%, of AgNO 3 to metallic Ag. [0041] Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the recovered silver nanowires have an average diameter of 40 nm (preferably 20 to 40 nm). more preferably from 20 to 35 nm, particularly preferably from 20 to 30 nm). More preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the recovered silver nanowires have a mean diameter of 40 nm (preferably 20 to 40 nm; more preferably, from 20 to 35 nm, particularly preferably from 20 to 30 nm) and an average length of 10 to 100 μm. Preferably, the recovered silver nanowires have an average aspect ratio of> 500. [0042] Preferably, in the process for producing high aspect ratio silver nanowires of the present invention, the nanowires of Recovered silver has a standard deviation of diameters 5 to 35 nm (preferably 1 to 32 nm, more preferably 1 to 25 nm, particularly preferably 5 to 20 nm). More preferably, in the process for making silver nanowires having a high aspect ratio of the present invention, the recovered silver nanowires have a mean diameter of 40 nm (preferably 20 to 40 nm; more preferably, from 20 to 35 nm, particularly preferably from 20 to 30 nm) with a standard deviation of diameters of 5. 35 nm (preferably from 1 to 32 nm, more preferably from 1 to 25 nm). particularly preferably from 5 to 20 nm). Particularly preferably, in the process for making silver nanowires having a high aspect ratio of the present invention, the recovered silver nanowires have a mean diameter of 40 nm (preferably 20 to 40 nm; more preferably from 20 to 35 nm, particularly preferably from 20 to 30 nm) with a standard deviation of diameters of 35 nm (preferably from 1 to 32 nm, more preferably from 1 to 25 nm, particularly preferably 5 to 20 nm) and an average length of 10 to 100 μm. Preferably, in the process for producing silver nanowires having a high aspect ratio of the present invention, the plurality of silver nanowires having a high aspect ratio recovered from the product mixture have a fraction of silver nanoparticles, NPF, <0.2 (preferably <0.17; preferably again, <0.15; particularly preferably, <0.13) (as determined by the method described herein in the examples). Some embodiments of the present invention will now be described in detail in the following examples. The water used in the following examples was obtained by means of a Barnstead NANOPure ThermoScientific purification system with a 0.2 μm pore size hollow fiber filter positioned downstream of the purification unit. the water. Example Si: sub-combination of halide ions The halide ion sub-combination used here in some examples was prepared by dissolving sodium chloride (0.2104 g, available from Sigma Aldrich) in water (900 mL).
    [0002] Example 52: Sub-combination of copper (II) ions [0047] The sub-combination of copper (II) ions used here in certain examples was prepared by dissolving copper (II) chloride dihydrate (0.6137 g available from Sigma Aldrich) in water (900 mL). Example 53: Reducing sugar / Polvvinylpyrrolidone (PVP) sub-combination [0048] The reducing sugar / polyvinylpyrrolidone (PVP) sub-combination used here in some examples was prepared by combining polyvinylpyrrolidone (PVP) (5.14 g; Sokalan® K30 P available from BASF having a weight average molecular weight of 50000 g / mol) and D-glucose (1.33 g,> 99% from Sigma-Aldrich) in water (250 mL). Example S4: Combination The combination used herein in some examples was prepared by combining a reducing sugar / polyvinylpyrrolidone (PVP) sub-combination prepared according to Example S3; a sub-combination of halide ions (2.1 mL) prepared according to Example Si; and a copper (II) ion sub-combination (2.1 mL) prepared according to Example S2. Example 55: silver ion sub-combination [0050] The silver ion sub-combination used herein in some examples was prepared by addition of AgNO 3 (1.25 g, ACS reagent grade, 99.0%). % available from Sigma Aldrich) to water (30 mL). Example 56: Reducing sugar sub-combination [0051] The reducing sugar sub-combination used herein in some examples was prepared by dissolving D-glucose (1.33 g,> 99% from Sigma-Aldrich) in water (250 mL).
    [0003] Example S7: Polyvinylpyrrolidone (PVP) Sub-Combination The polyvinylpyrrolidone (PVP) sub-combination used here in some examples was prepared by addition of polyvinylpyrrolidone (PVP) (5.14 g, Sokalan® K30 P available from BASF having a weight average molecular weight of 50000 g / mol) to water (25 mL). Example S8: silver ion sub-combination The silver ion sub-combination used here in some examples was prepared by addition of AgNO 3 (1.25 g, reagent grade ACS, 99.0% available). from Sigma Aldrich) to water (25 mL). Example S9: Reducing Agent Sub-combination [0054] The reducing agent sub-combination used herein in some examples was prepared by adding ascorbic acid (3.2 mg) to water (10 mL). ). Example S10: Reducing Agent Sub-combination [0055] The reducing agent sub-combination used herein in some examples was prepared by adding ascorbic acid (6 mg) to water (20 mL). Example S11: Reducing Agent Sub-combination [0056] The reducing agent sub-combination used herein in some examples was prepared by adding sodium borohydride (NaBH4) (6 mg) to water (71). mL).
    [0004] Example S12: Reducing Agent Sub-combination [0057] The reducing agent sub-combination used herein in some examples was prepared by adding sodium borohydride (NaBH4) (12 mg) to water (70 mL) ).
    [0005] Example S13: Reducing agent sub-combination [0058] The reducing agent sub-combination used herein in some examples was prepared by adding hydrazine dihydrochloride (H2NNH2.2HCl) (2 mg) to water (10 mL).
    [0006] Comparative Example C1: Preparation of Silver Nanowires A 600 mL Parr reactor with a teflon jacket, mixing means and a temperature control system was used. A combination prepared according to Example S4 was added to the reactor. The reactor was then sealed and purged with nitrogen. The combination in the reactor was then heated to 150 ° C. Then 1 / 5th of a silver ion sub-combination prepared according to Example S5 was charged to the reactor in 1 minute to form a creation mixture. The creation mixture was then mixed for ten minutes while the setting point of the temperature control device was maintained at 150 ° C. Then for the next ten minutes, the set point of the temperature control device was decreased linearly to 130 ° C. Then the remaining 4 / 5ths of the silver ion sub-combination prepared according to Example S5 were charged into the reactor in ten minutes to form a growth mixture, the growth mixture was then mixed for twelve hours while that the set point of the temperature control device was maintained at 130 ° C to form a product mixture, the product mixture was then cooled to room temperature, and the reactor was vented to the atmosphere. to relieve any accumulated pressure in the vessel and the product mixture was collected Comparative Example C2: Preparation of aruent nanowires A 600 mL Parr reactor with a Teflon liner, mixing means and a system A sub-combination of reducing sugar prepared according to Example S6, a sub-combination of halide ions (2.1 ml) prepared according to the example of Si, and a sub-combination of copper (II) ions (2.1 mL) prepared according to Example S2 were added to the reactor to form a combination. The reactor was then sealed and purged with nitrogen. The combination in the reactor was then heated to 130 ° C. Then a silver ion sub-combination prepared according to Example S8 and a polyvinylpyrrolidone (PVP) sub-combination prepared according to Example S7 were fed into the reactor simultaneously, through separate conduits, at a rate of 1 mL / min to form a growth mixture. The growth mixture was then mixed for eight hours while the set point of the temperature control device was maintained at 130 ° C to form a product mixture. The product mixture was then cooled to room temperature. The reactor was then vented to release any accumulated pressure in the vessel and the product mixture was collected.
    [0007] Examples 1-6: Preparation of silver nanowires [0061] A 600 ml Parr reactor with a teflon jacket, mixing means and a temperature control system was used. A sub-combination of reducing sugar prepared according to Example S6; a sub-combination of halide ions (2.1 mL) prepared according to Example Si; and a sub-combination of copper (II) ions (2.1 mL) prepared according to Example 52 were added to the reactor to form a combination. The reactor was then sealed and purged with nitrogen. The combination in the reactor was then heated to 130 ° C. Then 1 / 5th of a sub-combination of silver ions prepared according to Example S8 and 1 / 5th of a polyvinylpyrrolidone (PVP) sub-combination prepared according to Example S7 were loaded into the reactor simultaneously, through separate conduits, at a flow rate of 1 mL / min Then a sub-combination of reducing agent prepared according to the example noted in Table 1 was added in the amount noted in Table 1 in the reactor. Then the remaining 4 / 5ths of the silver ion sub-combination prepared according to Example S8 and the remaining 4/5 of the polyvinylpyrrolidone (PVP) sub-combination prepared according to Example S7 were loaded into the reactor simultaneously. , through separate conduits, at a rate of 1 mL / min to form a growth mixture, the growth mixture was then mixed for a holding time, as noted in Table 1, while the set point of the temperature control device The temperature was maintained at 130 ° C to form a product mixture. The product mixture was then cooled to room temperature. The reactor was then vented to release any accumulated pressure in the vessel and the product mixture was collected.
    [0008] TABLE 1 Ex Sub-combination Reducing agent sub-time volume combination of (AR) AR (mL) holding (h) 1 S9 1.0 8 2 510 1.0 12 3 S9 2.0 12 4 S11 0.3 12 S12 0.68 6 S13 2.0 8 Analysis of the silver nanowires collected Silver nanowires recovered from the product mixtures obtained in each of the comparative examples C1-C2 and examples 1-6 were then analyzed with a FEI Nova Nano SEM Field Emission Scanning Electron Microscope (SEM) using the Automated Image Acquisition (AIA) program from FEI. A drop of purified dispersion was taken from the UV / Vis cuvette and applied to a sample holder of SEM coated with a silica wafer before being dried under vacuum. The backscattering electronic images were collected with a FEI Nova Nano SEM Field Emission Scanning Electron Microscope. FEI's Automated Image Acquisition (AIA) program was used to move the deck, focus, and collect images. Eighteen images of each sample were acquired at a horizontal field width of 6 μm. Semi-automatic image analysis using the Image] software classified the objects as threads or particles based on an aspect ratio of 3. The yarn widths were measured automatically as well as the total area of wires in the pictures. Particles were classified with respect to the individual size and the total area of particles in the images. The Image] software was also used to determine the diameter of the silver nanowires in Table 3. It was observed that the average length of the silver nanowires exceeded 20 μm, based on the SEM images obtained for the analysis. diameters. The Image software) was used to analyze the SEM images of the silver nanowires produced in each of the comparative examples C1-C2 and Examples 1-6 to give a relative measure of the silver nanoparticles having a ratio of appearance <3 in product samples. The statistic used for this measurement is the fraction of nanoparticles, NPF, determined according to the following expression: N PF = N PA / TA; Where TA is the total surface area of the substrate that is occluded by a given deposited sample of silver nanowires; and, NPA is the portion of the total occluded surface area attributable to silver nanoparticles having an aspect ratio <3, UV / Vis spectral analysis of the silver nanowires produced in each of the Comparative examples C1-C2 and Examples 1-6 were carried out using a Shimadzu UV 2401 spectrophotometer. The raw UV / Vis absorption spectra were normalized so that the local minimum near 320 nm and the local maximum in the vicinity of 375 nm cover the range from 0 to 1. The maximum absorption wavelength, λmax, and the normalized absorption at 500 nm, Abs500, are shown in Table 1 302 75 3 9 33 TABLE 2 Ex Diameter of nanowires NPF Silver analysis (nm) spectral Median Mov Ecart-Amax Abs500 type (nm) enne Cl 41.4 59.4 49.0 0.54 378 0.77 C2 33.8 44.7 37, 6 0.29 378 0.47 1 27.1 29.9 10.0 0.28 372 0.45 2 26.7 31.5 17.5 0.36 372 0.41 3 27.4 31.0 12 , 6 0.23 373 0.33 4 26.3 27.4 8.0 0.19 373 0.26 5 34.4 43.1 30.3 0.45 377 0.54 37.9 45.9 27.2 0.32 376 0.34
    权利要求:
    Claims (10)
    [0001]
    REVENDICATIONS1. A process for producing silver nanowires having a high aspect ratio, characterized by comprising: providing a container; the supply of water; the supply of a reducing sugar; supply of a reducing agent; providing a polyvinylpyrrolidone (PVP), wherein the polyvinylpyrrolidone (PVP) provided is divided into a first portion of the polyvinylpyrrolidone (PVP) and a second portion of the polyvinylpyrrolidone (PVP); providing a source of copper (II) ions; providing a source of halide ions; providing a source of silver ions, wherein the supplied silver ion source is divided into a first portion of the silver ion source and a second portion of the silver ion source; adding water, reducing sugar, copper ion source (II) and the halide ion source to the vessel to form a combination; heating the combination at 110 to 160 ° C; adding the first portion of the polyvinylpyrrolidone (PVP), the first portion of the silver ion source and the reducing agent to the combination in the vessel to form a creation mixture; Then adding to the vessel the second portion of the polyvinylpyrrolidone (PVP) and the second portion of the silver ion source to form a growth mixture; maintaining the growth mixture at 110 to 160 ° C for a holding period of 2 to 30 hours to provide a product mixture; andrecovering a plurality of silver nanowires having a high aspect ratio from the product mixture; where the total glycol concentration in the container is <0.001% by weight at any time.
    [0002]
    2. Method according to claim 1, characterized in that the first part of the polyvinylpyrrolidone (PVP) and the first part of the silver ion source are added to the container simultaneously.
    [0003]
    3. Method according to any of the preceding claims, characterized in that the first part of the silver ion source is added to the combination under a surface of the combination in the container.
    [0004]
    4. Method according to any one of the preceding claims, characterized in that it further comprises: a delay period, wherein the delay period is arranged between the addition of the first part of the silver ion source to form the creation mixture and adding the second part of the silver ion source to form the growth mixture.
    [0005]
    5. Process according to any one of the preceding claims, characterized in that the first part of the polyvinylpyrrolidone (PVP) represents 10 to 40% by weight of the polyvinylpyrrolidone (PVP) supplied, and the first part of the source of Silver ions represent 10 to 40% by weight of the silver ion source supplied. 25
    [0006]
    6. Process according to any one of the preceding claims, characterized in that the reducing agent is chosen from ascorbic acid; borohydride salts; hydrazine; salts of hydrazine; hydroquinone; C1-5 alkylaldehydes and benzaldehyde.
    [0007]
    7. A process according to any one of the preceding claims characterized in that the reducing sugar provided is glucose, and the reducing agent provided is at least one of ascorbic acid and sodium borohydride.
    [0008]
    The method according to any one of the preceding claims, characterized in that it further comprises: providing a pH adjusting agent; and adding the pH adjusting agent to the combination, wherein the combination has a pH of 2.0 to 4.0 following the addition of the pH adjusting agent.
    [0009]
    9. A method according to any one of the preceding claims, characterized in that it further comprises: purging a gas space of the container in contact with the combination in the container to give a reduced oxygen gas concentration in the container. gas space of the container; bubbling into the silver ion source provided with an inert gas to extract the entrained oxygen gas from the supplied silver ion source and to give a low concentration of oxygen gas in a silver ion gas space in contact with the silver ion source provided; purging a PVP gas space in contact with the polyvinylpyrrolidone (PVP) provided to provide a dilute oxygen gas concentration in the PVP gas space; maintaining the low oxygen gas concentration in the silver ion gas space and the dilute oxygen gas concentration in the PVP gas space; and maintaining the reduced oxygen gas concentration in the container gas space during formation of the creation mixture, during formation of the growth mixture and during the holding period.
    [0010]
    10. A process according to any one of the preceding claims characterized in that: the reducing sugar provided is glucose, the reducing agent provided is selected from ascorbic acid; borohydride salts; hydrazine; salts of hydrazine; hydroquinone; C1-5 alkylaldehydes and benzaldehyde; the polyvinylpyrrolidone (PVP) provided has a weight average molecular weight, Mw, of 40,000 to 150,000 Daltons; the copper (II) ion source supplied is copper (II) chloride; the source of halide ions provided is sodium chloride; the silver ion source supplied is silver nitrate; the first part of the polyvinylpyrrolidone (PVP) represents 10 to 40% by weight of the polyvinylpyrrolidone (PVP) supplied; and the first part of the silver ion source is 10 to 40% by weight of the silver ion source supplied.
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    同族专利:
    公开号 | 公开日
    KR20160049983A|2016-05-10|
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    US10081059B2|2018-09-25|
    DE102015013220A1|2016-04-28|
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    CN105537609A|2016-05-04|
    TW201615550A|2016-05-01|
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