WO2019227872A1 - Formaldehyde purification fiber and preparation method therefor - Google Patents

Formaldehyde purification fiber and preparation method therefor Download PDF

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WO2019227872A1
WO2019227872A1 PCT/CN2018/116866 CN2018116866W WO2019227872A1 WO 2019227872 A1 WO2019227872 A1 WO 2019227872A1 CN 2018116866 W CN2018116866 W CN 2018116866W WO 2019227872 A1 WO2019227872 A1 WO 2019227872A1
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fiber
polymer
formaldehyde
solution
formaldehyde purification
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PCT/CN2018/116866
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French (fr)
Chinese (zh)
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杜冰
赫法贵
陈家枢
高福
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深圳大学
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/83Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with metals; with metal-generating compounds, e.g. metal carbonyls; Reduction of metal compounds on textiles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8668Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/18Synthetic fibres consisting of macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/22Polymers or copolymers of halogenated mono-olefins
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/18Synthetic fibres consisting of macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/24Polymers or copolymers of alkenylalcohols or esters thereof; Polymers or copolymers of alkenylethers, acetals or ketones
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/18Synthetic fibres consisting of macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/26Polymers or copolymers of unsaturated carboxylic acids or derivatives thereof
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/18Synthetic fibres consisting of macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/26Polymers or copolymers of unsaturated carboxylic acids or derivatives thereof
    • D06M2101/28Acrylonitrile; Methacrylonitrile

Definitions

  • the invention relates to the technical field of formaldehyde removal, in particular to a formaldehyde purification fiber and a preparation method thereof.
  • Formaldehyde is one of the most common indoor pollutants. Prolonged inhalation of formaldehyde can cause great harm to human health.
  • Existing formaldehyde purification methods mainly include adsorption method, photocatalytic oxidation method, and catalytic combustion method. Among them, the adsorption method cannot degrade formaldehyde. When the temperature changes, the adsorbed formaldehyde will desorb and cause secondary pollution; the photocatalytic technology requires a specific light source, and the light utilization rate is low, which can cause secondary pollution during the removal process, and The cost of catalytic equipment is high and it is difficult to popularize and apply it on a large scale. Therefore, the currently used formaldehyde purification method is mainly catalytic combustion.
  • Catalytic combustion is also known as flameless combustion.
  • the essence of catalytic combustion is to decompose formaldehyde into water and carbon dioxide by catalytic oxidation reaction. There is no secondary pollution of the product, and formaldehyde can be removed.
  • the key is to build a suitable catalyst.
  • the catalyst is composed of two main components: an active component and a support.
  • the active component is mostly a noble metal and is supported on the support.
  • the support is the backbone of the entire catalyst and has the function of supporting and dispersing the active component. It gives the catalyst certain strength and heat resistance Sex. Proper treatment of the support can also improve some physical properties of the catalyst and thus affect the performance of the catalyst. Appropriate support can reduce the amount of active components, improve catalyst performance, and reduce catalyst cost.
  • the commonly used carriers for the catalyst include magnesium oxide, alumina, silica, transition metal oxides, etc.
  • some carriers prepared by special methods such as preparing carriers into nanorods, nanospheres, or nanoporous materials.
  • the above-mentioned carriers all exist in the form of powder or nanoparticles, which are easy to cause dust pollution in daily life, have a heavy weight, and need to carry more active components. Therefore, there is a need for a formaldehyde removal catalyst that can avoid dust pollution, is light in weight and low in cost.
  • the present invention provides a formaldehyde purification fiber as a catalyst for catalyzing the conversion of formaldehyde into water and carbon dioxide, avoiding dust pollution caused by powdery catalysts, and at the same time, the formaldehyde purification fiber is environmentally friendly, light in weight, good in permeability and stable. High performance, high loading capacity, high formaldehyde conversion can be achieved by adsorbing a small amount of active components, and the preparation cost is low. It has a wide application prospect in the removal of methanol.
  • the present invention provides a method for preparing formaldehyde purification fibers, including:
  • the second polymer is dissolved in an organic solvent to prepare a second spinning solution, and the second polymer fiber is obtained after electrostatic spinning and ultraviolet light; wherein the first polymer includes polymethyl methacrylate, At least one of polyacrylonitrile and polyvinylidene fluoride, and the second polymer includes polyvinylpyrrolidone;
  • first polymer fiber and / or the second polymer fiber Immersing the first polymer fiber and / or the second polymer fiber in a solution containing noble metal ions, so that the first polymer fiber and / or the second polymer fiber are combined with the noble metal Ion, and then immersing the first polymer fiber and / or the second polymer fiber in a sodium borohydride solution to convert the noble metal ion into a noble metal element or a noble metal compound, and then take out and wash to obtain formaldehyde Purify the fiber.
  • a polymer containing at least one of polymethyl methacrylate, polyacrylonitrile, and polyvinylidene fluoride is dissolved in an organic solvent to prepare a first spinning solution, it is necessary to undergo electrostatic spinning. After vacuum drying and soaking the dopamine modified solution, a first polymer fiber is obtained.
  • the second spinning solution may be, but is not limited to, a polyvinylpyrrolidone solution, or a mixed solution of polyvinylpyrrolidone and polyacrylonitrile, or a mixed solution of polyvinylpyrrolidone and polyvinylidene fluoride, or polyvinylpyrrolidone and polymethacrylic acid.
  • ultraviolet light is required after electrospinning to obtain a second polymer fiber.
  • the organic solvent includes at least one of dimethyl sulfoxide, chloroform, N, N-dimethylformamide, and N, N-dimethylacetamide.
  • the mass concentration of the first polymer in the first spinning solution is 15% -40%. Further optionally, the mass concentration of the first polymer in the first spinning solution is 20% -35%. Specifically, the mass concentration of the first polymer in the first spinning solution may be, but is not limited to, 20%, 27%, 30%, or 35%.
  • the mass ratio of the two or more polymers is not limited, and two or more The total mass concentration of the polymer is 15% -40%.
  • the electrostatic spinning includes dry spinning, wet spinning, or dry-wet spinning.
  • the spinning temperature of the electrostatic spinning is 20 ° C-35 ° C
  • the humidity is 20% -80%
  • the injection speed is 0.4mL / h-1.8mL / h.
  • the anode voltage of the electrostatic spinning is 8kV-25kV
  • the cathode voltage is (-4) kV-(-2) kV
  • the rotation speed of the roller is 50 revolutions / min-200 revolutions / min.
  • the vacuum drying temperature is 40 ° C-80 ° C, and the time is 6h-24h.
  • the modified dopamine solution includes an aqueous solution containing anhydrous ethanol, ammonia, and dopamine hydrochloride. Further optionally, the modified dopamine solution contains 5 mL-15 mL of absolute ethanol, 0.3 mL-0.8 mL of ammonia water, 0.05 g-0.25 g of dopamine hydrochloride, and 15 mL-25 mL of distilled water.
  • the immersion temperature in the dopamine modified solution is 15 ° C-35 ° C, and the immersion time is 6h-24h.
  • the immersion in the dopamine modification solution further includes immersion in a dopamine modification solution at a rotation speed of 50 rpm to 150 rpm.
  • the fiber obtained by electrospinning the first spinning solution when placed in a dopamine modification solution, dopamine self-polymerizes on the fiber surface, and the first polymer fiber is a polydopamine-encapsulated fiber, polydopamine
  • the surface has a large number of oxygen and nitrogen coordination atoms for chelating precious metal ions.
  • the first polymer fiber obtained after washing includes: washing multiple times with water until the aqueous solution is colorless, and immersing in an isopropanol solution for 10min-30min, and washing with water for 3-5 times, The first polymer fiber is obtained. Further optionally, the mass concentration of isopropanol in the isopropanol solution is 15% -30%. In the present invention, an isopropanol solution is used to remove unreacted dopamine on the fibers.
  • the mass concentration of the second polymer in the second spinning solution is 15% -40%. Further optionally, the mass concentration of the second polymer in the second spinning solution is 15% -35%. Specifically, the mass concentration of the second polymer in the second spinning solution may be, but is not limited to, 15%, 20%, 27%, or 30%.
  • the second polymer is a mixture of polyvinylpyrrolidone and one or more other polymers
  • the mass ratio of polyvinylpyrrolidone to other one or more polymers is not limited, and polyvinylpyrrolidone and other one or more polymers are not limited.
  • the total mass concentration of this polymer is 15% -40%.
  • the fibers obtained by electrospinning the second spinning solution are crosslinked under ultraviolet light to obtain the second polymer fibers.
  • the concentration of the precious metal ion in the precious metal ion-containing solution is 0.01 mol / L to 2 mol / L, and the pH of the precious metal ion-containing solution is 2-6.
  • the precious metal ion-containing solution includes a precious metal cation-containing solution and / or a precious metal salt anion-containing solution.
  • the precious metal may be, but is not limited to, platinum, nickel, gold, palladium, ruthenium, rhodium, and silver.
  • the precious metal-containing ion may be, but is not limited to, a nickel ion, a platinum ion, and / or a cobalt ion.
  • the solution of the active component contains platinum ions and / or nickel ions
  • the molar concentration of the platinum ions is 0.03mol / L-0.05mol / L
  • the molar concentration of the nickel ions is 0.03mol / L-1mol / L.
  • the first polymer fiber and / or the second polymer fiber are immersed in a solution containing platinum ions and nickel ions and reduced by sodium borohydride
  • the first polymer fiber And / or the surface of the second polymer fiber is platinum-nickel composite nanoparticles
  • the platinum-nickel composite nanoparticles have nickel as the core and platinum as the shell.
  • the noble metal ion-containing solution may further include a transition metal ion.
  • the transition metal can be, but is not limited to, manganese, zinc, and iron.
  • the first polymer fiber and / or the second polymer fiber may be placed in a solution containing two or more precious metal The ions are immersed in the solution, or the first polymer fiber and / or the second polymer fiber are sequentially immersed in a solution containing a single precious metal ion.
  • the immersion temperature in the solution containing noble metal ions is 15 ° C-35 ° C, and the immersion time is 24h-144h. Further optionally, the immersion in the solution containing noble metal ions further includes immersion in the solution containing noble metal ions under the condition of a rotation speed of 50 rpm-150 rpm.
  • the molar concentration of the sodium borohydride solution is 0.0001 mol / L-0.1 mol / L.
  • the immersion temperature of the immersion in the sodium borohydride solution is 15 ° C-35 ° C, and the immersion time is 0.5h-7h.
  • the immersion in the sodium borohydride solution further includes immersion in a sodium borohydride solution at a rotation speed of 50 rpm to 150 rpm.
  • the method for preparing formaldehyde purification fiber uses electrostatic spinning to prepare light-weight and air-permeable fibers, and then increases the original fiber characteristics by vacuum drying, dopamine modification, or ultraviolet light.
  • the adsorption of noble metal ions by the fiber can be carried, so that the noble metal ions can be loaded with a high load.
  • the formaldehyde purification fiber can be prepared, which can be used as a catalyst for decomposing formaldehyde.
  • the preparation process is simple and the cost is low, which is beneficial to industrial production .
  • the present invention provides a formaldehyde purification fiber, which is prepared by the method for preparing a formaldehyde purification fiber according to the first aspect.
  • the diameter of the formaldehyde purification fiber is 700 nm-1300 nm.
  • the linear density of the formaldehyde purification fiber is 1.01dtex-1.44dtex
  • the breaking strength is 7.3cN / dtex-7.9cN / dtex
  • the breaking elongation is 5% -30%.
  • the conversion rate of the formaldehyde purification fiber to formaldehyde is higher than 93%.
  • the formaldehyde purification fiber can be used in, but not limited to, civil or industrial air filtering equipment, including masks, air conditioners, air purifiers, and filter elements thereof.
  • the formaldehyde purification fiber provided by the second aspect of the present invention can be used as a catalyst for catalyzing the decomposition of formaldehyde, so that methanol is converted into water and carbon dioxide, thereby removing formaldehyde, and the product is not polluted.
  • the formaldehyde purification fiber avoids dust pollution caused by the dust catalyst. Green environmental protection, light weight, good air permeability, high stability, high load capacity, and efficient absorption of formaldehyde can be achieved by adsorbing a small amount of precious metals.
  • the present invention provides a method for preparing formaldehyde-purified fibers.
  • Light-weight and air-permeable fibers are prepared by electrostatic spinning, followed by vacuum drying, dopamine modification, or ultraviolet light.
  • the basis for maintaining the original fiber characteristics It increases the fiber's adsorption of noble metal ions, so that it can carry noble metal ions, and finally it is reduced by sodium borohydride solution to obtain formaldehyde purified fiber.
  • the preparation process is simple and the cost is low, which is conducive to industrial production;
  • the formaldehyde purification fiber provided by the present invention can be used as a catalyst for catalyzing the decomposition of formaldehyde, so that methanol is converted into water and carbon dioxide, thereby removing formaldehyde, and the product is not polluted; at the same time, the formaldehyde purification fiber avoids dust pollution caused by dust catalyst, green Environmental protection, light weight, good air permeability, high stability, high load capacity, adsorption of a small amount of precious metals can achieve efficient formaldehyde conversion efficiency, and has broad application prospects in the removal of formaldehyde.
  • FIG. 1 is an electron micrograph of a formaldehyde purification fiber prepared in Example 1 of the present invention
  • FIG. 2 is a transmission electron microscope image of the formaldehyde-purified fiber prepared in Example 1 of the present invention.
  • FIG. 2 (a) is a transmission electron microscope image at a scale of 0.2 ⁇ m
  • FIG. 2 (b) is a transmission electron microscope at a scale of 50 nm.
  • Example 3 is a diameter analysis chart of surface nanoparticles of the formaldehyde purification fiber prepared in Example 1 of the present invention
  • FIG. 5 is a diagram showing the stability test results of the formaldehyde purification fiber prepared in Example 1 of the present invention.
  • FIG. 6 is a diagram of the efficiency of formaldehyde decomposition of the formaldehyde purification fiber prepared in Example 1 of the present invention at different gas flow rates.
  • a method for preparing formaldehyde purification fiber includes:
  • Polymethyl methacrylate was dissolved in N, N-dimethylformamide (DMF) to prepare a spinning solution.
  • the mass concentration of polymethyl methacrylate in the spinning solution was 30%. Spinning and drying under vacuum for 6 h to obtain white polymethyl methacrylate fibers.
  • Chloroplatinic acid and nickel nitrate were dissolved in water and mixed to prepare a solution.
  • the molar concentration of platinum ions was 0.0494 mol / L
  • the molar concentration of nickel ions was 0.12 mol / L
  • the pH of the solution was 3.5
  • the polydopamine-coated The polymethyl methacrylate fiber was placed therein, soaked in a shaker at room temperature for 72 hours, and then immersed in a 0.0005mol / L sodium borohydride solution for 3 hours, washed and dried to obtain formaldehyde-purified fibers.
  • the obtained formaldehyde purification fiber was scanned by an electron microscope, and the result is shown in FIG. 1.
  • the diameter of the formaldehyde purification fiber is 1100 nm-1200 nm.
  • Polydopamine particles are attached to the surface of the fiber, and the surface is rough. Polydopamine is evenly wrapped on the surface of the fiber to form a layer of polydopamine. The particles on the surface of the fiber are polydopamine particles that have not yet grown along the fiber.
  • platinum and nickel nanoparticles were uniformly attached to the surface of the formaldehyde purification fiber. Transmission electron microscopy was performed on the prepared formaldehyde-purified fibers. The results are shown in Figure 2.
  • Nanoparticles ((b) in Figure 2)
  • the attached nanoparticles were analyzed and found to be composite nanoparticles with nickel as the core and platinum as the shell.
  • the diameters of 200 nanoparticles were measured. The results are shown in Figure 3.
  • the average diameter of the nanoparticles is 2.14 nm, and the diameter is very small, which makes the nanoparticles have higher catalytic activity.
  • a method for preparing formaldehyde purification fiber includes:
  • Polymethyl methacrylate and polyvinylidene fluoride are dissolved in N, N-dimethylformamide (DMF) to prepare a spinning solution, wherein the mass concentration of polymethyl methacrylate in the spinning solution is 15%, The mass concentration of polyvinylidene fluoride is 20%.
  • Spinning was performed on an electrostatic spinning machine. Electrostatic spinning parameters were: anode voltage 8 kV, cathode voltage-4 kV, injection speed 0.4 ml / h, rotation speed 60 rpm, spinning temperature 20 ° C, humidity 40%. The spun fibers were dried under vacuum at 50 ° C. for 7 hours to obtain polymethyl methacrylate fibers.
  • Nickel nitrate was dissolved in water and mixed to prepare a solution, wherein the molar concentration of nickel ions was 0.03 mol / L.
  • the polydopamine-coated polymethyl methacrylate fiber was placed therein, and after soaking at room temperature for 96 hours, it was soaked in a 0.003mol / L sodium borohydride solution, and the formaldehyde purified fiber was obtained after washing and drying. After testing, the linear density of the formaldehyde-purified fiber was 1.3 dtex, the breaking strength was 7.8 cN / dtex, and the elongation at break was 20%.
  • a method for preparing formaldehyde purification fiber includes:
  • the polyvinylpyrrolidone and polyvinylidene fluoride are mixed at a ratio of 3: 2 by mass and dissolved in chloroform to prepare a spinning solution, wherein the mass concentration of the polyvinylpyrrolidone in the spinning solution is 10%.
  • Spinning was performed on an electrostatic spinning machine.
  • the electrostatic spinning parameters were: anode voltage 25 kV, cathode voltage-2 kV, injection speed 1 ml / h, rotation speed 180 rpm, spinning temperature 30 ° C, humidity 60%.
  • the fiber was irradiated with ultraviolet light at 50 ⁇ W / cm 2 for 4 hours, and then subjected to a crosslinking reaction to obtain a second polymer fiber.
  • a chloroplatinic acid solution was prepared, in which the molar concentration of platinum ions was 0.035 mol / L.
  • the second polymer fiber was placed therein, soaked in a shaker at room temperature for 80 hours, and then soaked in a 0.03mol / L sodium borohydride solution. After washing and drying, formaldehyde-purified fibers were obtained. After testing, the linear density of the formaldehyde purification fiber was 1.2 dtex, the breaking strength was 7.4 cN / dtex, and the breaking elongation was 10%.
  • Polymethyl methacrylate was dissolved in N, N-dimethylformamide (DMF) to prepare a spinning solution.
  • the mass concentration of polymethyl methacrylate in the spinning solution was 30%.
  • Spinning and drying under vacuum for 6 h to obtain white polymethyl methacrylate fibers.
  • the obtained polymethyl methacrylate fiber was scanned by an electron microscope, and the result is shown in FIG. 4.
  • the surface of the prepared polymethyl methacrylate fiber was smooth, and the fiber morphology was uniform and stable, with a diameter of 700 nm-850 nm.
  • the formaldehyde purification fiber prepared in Example 1 it can be seen that after the polymethyl methacrylate fiber is coated with dopamine, the fiber diameter increases and the surface becomes rough.
  • the formaldehyde purification fiber prepared in Example 1 was tableted and pulverized into particles. After passing through a 50-mesh sieve, 0.03 g was filled into a quartz tube with an inner diameter of 7 mm, and a small amount of quartz cotton was fixed at the position. The quartz tube was fixed in the reactor. .
  • a 200mg / L formaldehyde solution was prepared and transferred to a bubbler in an ice-water bath incubator. N 2 was used as a carrier gas, and the formaldehyde gas was taken out by the bubbling. It was mixed with the diluent air into the quartz tube in the reactor. Measure the concentration of formaldehyde in the gas before and after passing through the quartz tube, and calculate the efficiency of the formaldehyde purification fiber to convert formaldehyde according to formula (1).
  • the method for measuring the concentration of formaldehyde refers to the national standard "Method for measuring formaldehyde in air in public places" (GB / T18204.26- In the phenol reagent spectrophotometry in 2000), C 0 is the concentration of formaldehyde in the mixed gas passed into the quartz tube, and C 1 is the concentration of formaldehyde in the mixed gas after passing through the quartz tube.
  • the quartz tube containing the formaldehyde purification fiber was continuously fed with a mixed gas, and the stability of the formaldehyde purification fiber was measured.
  • the results are shown in Fig. 5.
  • the mixed gas was continuously introduced (the content of formaldehyde was 3mg / L and the air flow rate was 30ml / min).
  • the conversion rate of formaldehyde remained above 95%, and the overall conversion level remained high. It is shown that the formaldehyde purification fiber prepared by the present invention has high stability and can be reused.
  • the formaldehyde purification fiber provided by the present invention is environmentally friendly, light in weight, good in breathability, high in stability, has excellent ability to remove formaldehyde, and has a broad application prospect in the removal of formaldehyde.

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  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Biomedical Technology (AREA)
  • Health & Medical Sciences (AREA)
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  • General Chemical & Material Sciences (AREA)
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Abstract

Provided is a method for preparing a formaldehyde purification fiber, the method involving dissolving a first polymer in an organic solvent to formulate a first spinning solution, and carrying out electrostatic spinning and vacuum drying on same, and then placing same in a dopamine modification solution for soaking, and washing same so as to obtain a first polymer fiber; or, dissolving a second polymer in an organic solvent to formulate a second spinning solution, and carrying out electrostatic spinning and UV irradiation on same so as to obtain a second polymer fiber; and placing the first polymer fiber and/or the second polymer fiber into a solution containing noble metal ions for soaking so as to combine the first polymer fiber and/or the second polymer fiber with the noble metal ions; then placing same into a sodium borohydride solution for soaking so as to convert the noble metal ions into a noble metal elementary substance or a noble metal compound, subsequently removing same and washing same to obtain the formaldehyde purification fiber. The fiber has a light mass, good air permeability, high stability, and a high loading capacity, and can be used as a catalyst for catalyzing the conversion of formaldehyde, and can achieve a high formaldehyde conversion rate by means of absorbing a small amount of active components.

Description

一种甲醛净化纤维及其制备方法Formaldehyde purification fiber and preparation method thereof
本发明要求2018年5月31日递交的发明名称为“一种甲醛净化纤维及其制备方法”的申请号201810551037.1的在先申请优先权,上述在先申请的内容以引入的方式并入本文本中。The present invention claims the priority of an earlier application with an application number of 201810551037.1 with the invention name “A formaldehyde purification fiber and a preparation method thereof” submitted on May 31, 2018, and the contents of the foregoing earlier application are incorporated into this text by way of introduction. in.
技术领域Technical field
本发明涉及除甲醛技术领域,特别涉及一种甲醛净化纤维及其制备方法。The invention relates to the technical field of formaldehyde removal, in particular to a formaldehyde purification fiber and a preparation method thereof.
背景技术Background technique
甲醛是最常见的室内污染物之一,长时间吸入甲醛给人体健康带来极大损害。现有的甲醛净化方法主要有吸附法、光催化氧化法、催化燃烧法等。其中,吸附法无法使甲醛降解,当温度变化时,吸附的甲醛会发生脱附,引发二次污染;光催化技术需要特定光源,光利用率较低,去除过程中能造成二次污染,且催化设备成本高昂,难以大规模推广应用。因此,目前比较常用的甲醛净化方法主要是催化燃烧法。Formaldehyde is one of the most common indoor pollutants. Prolonged inhalation of formaldehyde can cause great harm to human health. Existing formaldehyde purification methods mainly include adsorption method, photocatalytic oxidation method, and catalytic combustion method. Among them, the adsorption method cannot degrade formaldehyde. When the temperature changes, the adsorbed formaldehyde will desorb and cause secondary pollution; the photocatalytic technology requires a specific light source, and the light utilization rate is low, which can cause secondary pollution during the removal process, and The cost of catalytic equipment is high and it is difficult to popularize and apply it on a large scale. Therefore, the currently used formaldehyde purification method is mainly catalytic combustion.
催化燃烧法也称为无火焰燃烧,其实质是催化氧化反应将甲醛分解成为水和二氧化碳,产物不存在二次污染,并且可以将甲醛去除,其关键在于构建合适的催化剂。催化剂由活性组分和载体两个主要组成部分构成,活性组分多为贵金属,负载于载体上;载体是整个催化剂的骨架,具有支撑和分散活性组分的作用,赋予催化剂一定强度和耐热性。适当的处理载体还可以改善催化剂的一些物理性质从而影响催化剂的性能。合适载体可以减少活性组分的用量,提升催化剂性能,降低催化剂的成本。催化剂常用的载体包括氧化镁、三氧化二铝、氧化硅、过渡金属氧化物等,近年来也有一些特殊方法制备的载体,例如将载体制备成纳米棒、纳米微球或者纳米多孔材料等。然而,上述的载体都以粉末或纳米颗粒的形式存在,在日常生活中容易造成粉尘污染、质量较重,需要负载较多的活性组分。因此,需要一种可以避免粉尘污染,质量轻、成本低的除甲醛催化剂。Catalytic combustion is also known as flameless combustion. The essence of catalytic combustion is to decompose formaldehyde into water and carbon dioxide by catalytic oxidation reaction. There is no secondary pollution of the product, and formaldehyde can be removed. The key is to build a suitable catalyst. The catalyst is composed of two main components: an active component and a support. The active component is mostly a noble metal and is supported on the support. The support is the backbone of the entire catalyst and has the function of supporting and dispersing the active component. It gives the catalyst certain strength and heat resistance Sex. Proper treatment of the support can also improve some physical properties of the catalyst and thus affect the performance of the catalyst. Appropriate support can reduce the amount of active components, improve catalyst performance, and reduce catalyst cost. The commonly used carriers for the catalyst include magnesium oxide, alumina, silica, transition metal oxides, etc. In recent years, there have also been some carriers prepared by special methods, such as preparing carriers into nanorods, nanospheres, or nanoporous materials. However, the above-mentioned carriers all exist in the form of powder or nanoparticles, which are easy to cause dust pollution in daily life, have a heavy weight, and need to carry more active components. Therefore, there is a need for a formaldehyde removal catalyst that can avoid dust pollution, is light in weight and low in cost.
发明内容Summary of the Invention
有鉴于此,本发明提供了一种甲醛净化纤维,作为催化甲醛转化为水和二氧化碳的催化剂,避免了粉末状催化剂造成的粉尘污染,同时甲醛净化纤维绿色环保、质量轻、透气性好、稳定性高、负载量高,吸附少量活性组分即可达到高的甲醛转化率,制备成本低,在去除甲醇方面具有广泛应用前景。In view of this, the present invention provides a formaldehyde purification fiber as a catalyst for catalyzing the conversion of formaldehyde into water and carbon dioxide, avoiding dust pollution caused by powdery catalysts, and at the same time, the formaldehyde purification fiber is environmentally friendly, light in weight, good in permeability and stable. High performance, high loading capacity, high formaldehyde conversion can be achieved by adsorbing a small amount of active components, and the preparation cost is low. It has a wide application prospect in the removal of methanol.
第一方面,本发明提供了一种甲醛净化纤维的制备方法,包括:In a first aspect, the present invention provides a method for preparing formaldehyde purification fibers, including:
将第一聚合物溶于有机溶剂中配制成第一纺丝液,进行静电纺丝、真空干燥后置于多巴胺改性液中浸泡,经洗涤后得到第一聚合物纤维;Dissolving the first polymer in an organic solvent to prepare a first spinning solution, subjecting it to electrostatic spinning, vacuum drying, and soaking in a dopamine modified solution to obtain a first polymer fiber after washing;
或将第二聚合物溶于有机溶剂中配制成第二纺丝液,进行静电纺丝、紫外光照后得到第二聚合物纤维;其中,所述第一聚合物包括聚甲基丙烯酸甲酯、聚丙烯腈和聚偏氟乙烯中的至少一种,所述第二聚合物包括聚乙烯吡咯烷酮;Or the second polymer is dissolved in an organic solvent to prepare a second spinning solution, and the second polymer fiber is obtained after electrostatic spinning and ultraviolet light; wherein the first polymer includes polymethyl methacrylate, At least one of polyacrylonitrile and polyvinylidene fluoride, and the second polymer includes polyvinylpyrrolidone;
将所述第一聚合物纤维和/或所述第二聚合物纤维置于含贵金属离子的溶液中浸泡,使所述第一聚合物纤维和/或所述第二聚合物纤维结合所述贵金属离子,再将所述第一聚合物纤维和/或所述第二聚合物纤维置于硼氢化钠溶液中浸泡,使所述贵金属离子转变为贵金属单质或贵金属化合物,随后取出,经洗涤得到甲醛净化纤维。Immersing the first polymer fiber and / or the second polymer fiber in a solution containing noble metal ions, so that the first polymer fiber and / or the second polymer fiber are combined with the noble metal Ion, and then immersing the first polymer fiber and / or the second polymer fiber in a sodium borohydride solution to convert the noble metal ion into a noble metal element or a noble metal compound, and then take out and wash to obtain formaldehyde Purify the fiber.
在本发明中,当包含有聚甲基丙烯酸甲酯、聚丙烯腈和聚偏氟乙烯中的至少一种的聚合物溶于有机溶剂中配制出第一纺丝液时,需要经过静电纺丝、真空干燥和浸泡多巴胺改性液后,得到第一聚合物纤维。In the present invention, when a polymer containing at least one of polymethyl methacrylate, polyacrylonitrile, and polyvinylidene fluoride is dissolved in an organic solvent to prepare a first spinning solution, it is necessary to undergo electrostatic spinning. After vacuum drying and soaking the dopamine modified solution, a first polymer fiber is obtained.
在本发明中,当聚乙烯吡咯烷酮或聚乙烯吡咯烷酮与其他聚合物一起溶于有机溶剂中配制出第二纺丝液时,需要经过静电纺丝以及紫外光照,发生交联反应,得到第二聚合物纤维。具体的,可以但不限于第二纺丝液为聚乙烯吡咯烷酮溶液、或聚乙烯吡咯烷酮和聚丙烯腈混合溶液、或聚乙烯吡咯烷酮和聚偏氟乙烯混合溶液、或聚乙烯吡咯烷酮和聚甲基丙烯酸甲酯混合溶液时,在静电纺丝后需要进行紫外光照,得到第二聚合物纤维。In the present invention, when polyvinylpyrrolidone or polyvinylpyrrolidone is dissolved in an organic solvent together with other polymers to prepare a second spinning solution, it needs to undergo electrostatic spinning and ultraviolet light to undergo a crosslinking reaction to obtain a second polymerization.物 材料。 Fibers. Specifically, the second spinning solution may be, but is not limited to, a polyvinylpyrrolidone solution, or a mixed solution of polyvinylpyrrolidone and polyacrylonitrile, or a mixed solution of polyvinylpyrrolidone and polyvinylidene fluoride, or polyvinylpyrrolidone and polymethacrylic acid. In the case of a methyl ester mixed solution, ultraviolet light is required after electrospinning to obtain a second polymer fiber.
可选的,所述有机溶剂包括二甲基亚砜、氯仿、N,N-二甲基甲酰胺和N,N-二甲基乙酰胺中的至少一种。Optionally, the organic solvent includes at least one of dimethyl sulfoxide, chloroform, N, N-dimethylformamide, and N, N-dimethylacetamide.
可选的,所述第一纺丝液中所述第一聚合物的质量浓度为15%-40%。进 一步可选的,所述第一纺丝液中所述第一聚合物的质量浓度为20%-35%。具体的,所述第一纺丝液中所述第一聚合物的质量浓度可以但不限于为20%、27%、30%或35%。当所述第一聚合物为聚甲基丙烯酸甲酯、聚丙烯腈和聚偏氟乙烯中的两种或多种时,两种或多种聚合物的质量比不作限定,两种或多种聚合物的总质量浓度为15%-40%。Optionally, the mass concentration of the first polymer in the first spinning solution is 15% -40%. Further optionally, the mass concentration of the first polymer in the first spinning solution is 20% -35%. Specifically, the mass concentration of the first polymer in the first spinning solution may be, but is not limited to, 20%, 27%, 30%, or 35%. When the first polymer is two or more of polymethyl methacrylate, polyacrylonitrile, and polyvinylidene fluoride, the mass ratio of the two or more polymers is not limited, and two or more The total mass concentration of the polymer is 15% -40%.
可选的,所述静电纺丝包括干法纺丝、湿法纺丝或干湿法纺丝。Optionally, the electrostatic spinning includes dry spinning, wet spinning, or dry-wet spinning.
可选的,所述静电纺丝的纺丝温度20℃-35℃,湿度为20%-80%,进样速度为0.4mL/h-1.8mL/h。Optionally, the spinning temperature of the electrostatic spinning is 20 ° C-35 ° C, the humidity is 20% -80%, and the injection speed is 0.4mL / h-1.8mL / h.
可选的,所述静电纺丝的阳极电压为8kV-25kV,阴极电压为(-4)kV-(-2)kV,滚轴转速为50转/min-200转/min。Optionally, the anode voltage of the electrostatic spinning is 8kV-25kV, the cathode voltage is (-4) kV-(-2) kV, and the rotation speed of the roller is 50 revolutions / min-200 revolutions / min.
可选的,所述真空干燥的温度为40℃-80℃,时间为6h-24h。Optionally, the vacuum drying temperature is 40 ° C-80 ° C, and the time is 6h-24h.
可选的,所述多巴胺改性液包括含有无水乙醇、氨水和盐酸多巴胺的水溶液。进一步可选的,所述多巴胺改性液含有5mL-15mL无水乙醇、0.3mL-0.8mL氨水、0.05g-0.25g盐酸多巴胺以及15mL-25mL蒸馏水。Optionally, the modified dopamine solution includes an aqueous solution containing anhydrous ethanol, ammonia, and dopamine hydrochloride. Further optionally, the modified dopamine solution contains 5 mL-15 mL of absolute ethanol, 0.3 mL-0.8 mL of ammonia water, 0.05 g-0.25 g of dopamine hydrochloride, and 15 mL-25 mL of distilled water.
可选的,所述置于多巴胺改性液中浸泡的浸泡温度为15℃-35℃,浸泡时间为6h-24h。进一步可选的,所述置于多巴胺改性液中浸泡还包括在转速50转/min-150转/min条件下置于多巴胺改性液中浸泡。Optionally, the immersion temperature in the dopamine modified solution is 15 ° C-35 ° C, and the immersion time is 6h-24h. Further optionally, the immersion in the dopamine modification solution further includes immersion in a dopamine modification solution at a rotation speed of 50 rpm to 150 rpm.
在本发明中,第一纺丝液经静电纺丝得到的纤维置于多巴胺改性液中时,多巴胺在纤维表面发生自聚,所述第一聚合物纤维为聚多巴胺包裹的纤维,聚多巴胺表面具有大量氧、氮配位原子,用于螯合贵金属离子。In the present invention, when the fiber obtained by electrospinning the first spinning solution is placed in a dopamine modification solution, dopamine self-polymerizes on the fiber surface, and the first polymer fiber is a polydopamine-encapsulated fiber, polydopamine The surface has a large number of oxygen and nitrogen coordination atoms for chelating precious metal ions.
可选的,所述经洗涤后得到第一聚合物纤维,包括:经水洗涤多次至水溶液无色,并在异丙醇溶液中浸泡10min-30min后,在经水洗涤3-5次,得到所述第一聚合物纤维。进一步可选的,所述异丙醇溶液中异丙醇的质量浓度为15%-30%。在本发明中,异丙醇溶液用于去除纤维上未反应的多巴胺。Optionally, the first polymer fiber obtained after washing includes: washing multiple times with water until the aqueous solution is colorless, and immersing in an isopropanol solution for 10min-30min, and washing with water for 3-5 times, The first polymer fiber is obtained. Further optionally, the mass concentration of isopropanol in the isopropanol solution is 15% -30%. In the present invention, an isopropanol solution is used to remove unreacted dopamine on the fibers.
可选的,所述第二纺丝液中所述第二聚合物的质量浓度为15%-40%。进一步可选的,所述第二纺丝液中所述第二聚合物的质量浓度为15%-35%。具体的,所述第二纺丝液中所述第二聚合物的质量浓度可以但不限于为15%、20%、27%或30%。当所述第二聚合物为聚乙烯吡咯烷酮和其他一种或多种聚合物混合时,聚乙烯吡咯烷酮与其他一种或多种聚合物的质量比不作限定,聚 乙烯吡咯烷酮与其他一种或多种聚合物的总质量浓度为15%-40%。Optionally, the mass concentration of the second polymer in the second spinning solution is 15% -40%. Further optionally, the mass concentration of the second polymer in the second spinning solution is 15% -35%. Specifically, the mass concentration of the second polymer in the second spinning solution may be, but is not limited to, 15%, 20%, 27%, or 30%. When the second polymer is a mixture of polyvinylpyrrolidone and one or more other polymers, the mass ratio of polyvinylpyrrolidone to other one or more polymers is not limited, and polyvinylpyrrolidone and other one or more polymers are not limited. The total mass concentration of this polymer is 15% -40%.
可选的,所述紫外光照为在10μW/cm 2-100μW/cm 2紫外光强度下照射2h-12h。在本发明中,第二纺丝液经静电纺丝后得到的纤维在紫外光照下进行交联,得到所述第二聚合物纤维。 Alternatively, the UV irradiation under irradiation 2h-12h / cm 2 intensity of ultraviolet light at 10μW / cm 2 -100μW. In the present invention, the fibers obtained by electrospinning the second spinning solution are crosslinked under ultraviolet light to obtain the second polymer fibers.
可选的,所述含贵金属离子的溶液中所述贵金属离子的浓度为0.01mol/L-2mol/L,所述含贵金属离子的溶液的pH为2-6。所述含贵金属离子的溶液包括含贵金属阳离子的溶液和/或含贵金属盐阴离子的溶液。具体的,贵金属可以但不限于为铂、镍、金、钯、钌、铑、银。具体的,所述含贵金属离子可以但不限于为镍离子、铂酸根离子和/或钴离子。当所述活性组分的溶液含有铂离子和/或镍离子,所述铂离子的摩尔浓度为0.03mol/L-0.05mol/L,所述镍离子的摩尔浓度为0.03mol/L-1mol/L。在本发明中,当所述第一聚合物纤维和/或所述第二聚合物纤维在含铂离子和镍离子的溶液中浸泡,并经硼氢化钠还原后,所述第一聚合物纤维和/或所述第二聚合物纤维的表面为铂镍复合纳米颗粒,所述铂镍复合纳米颗粒以镍为核心,铂为外壳。在本发明中,所述含贵金属离子溶液中还可以包括含过渡金属离子。过渡金属可以但不限于为锰、锌、铁。在本发明中,若所述含贵金属离子的溶液中含有两种及以上贵金属离子时,可以将所述第一聚合物纤维和/或所述第二聚合物纤维置于含两种及以上贵金属离子的溶液中进行浸泡,或将所述第一聚合物纤维和/或所述第二聚合物纤维置于含单一的贵金属离子的溶液中依次进行浸泡。Optionally, the concentration of the precious metal ion in the precious metal ion-containing solution is 0.01 mol / L to 2 mol / L, and the pH of the precious metal ion-containing solution is 2-6. The precious metal ion-containing solution includes a precious metal cation-containing solution and / or a precious metal salt anion-containing solution. Specifically, the precious metal may be, but is not limited to, platinum, nickel, gold, palladium, ruthenium, rhodium, and silver. Specifically, the precious metal-containing ion may be, but is not limited to, a nickel ion, a platinum ion, and / or a cobalt ion. When the solution of the active component contains platinum ions and / or nickel ions, the molar concentration of the platinum ions is 0.03mol / L-0.05mol / L, and the molar concentration of the nickel ions is 0.03mol / L-1mol / L. In the present invention, when the first polymer fiber and / or the second polymer fiber are immersed in a solution containing platinum ions and nickel ions and reduced by sodium borohydride, the first polymer fiber And / or the surface of the second polymer fiber is platinum-nickel composite nanoparticles, the platinum-nickel composite nanoparticles have nickel as the core and platinum as the shell. In the present invention, the noble metal ion-containing solution may further include a transition metal ion. The transition metal can be, but is not limited to, manganese, zinc, and iron. In the present invention, if the noble metal ion-containing solution contains two or more precious metal ions, the first polymer fiber and / or the second polymer fiber may be placed in a solution containing two or more precious metal The ions are immersed in the solution, or the first polymer fiber and / or the second polymer fiber are sequentially immersed in a solution containing a single precious metal ion.
可选的,所述置于含贵金属离子的溶液中浸泡的浸泡温度为15℃-35℃,浸泡时间为24h-144h。进一步可选的,所述置于含贵金属离子的溶液中浸泡还包括在转速50转/min-150转/min条件下置于含贵金属离子的溶液中浸泡。Optionally, the immersion temperature in the solution containing noble metal ions is 15 ° C-35 ° C, and the immersion time is 24h-144h. Further optionally, the immersion in the solution containing noble metal ions further includes immersion in the solution containing noble metal ions under the condition of a rotation speed of 50 rpm-150 rpm.
可选的,所述硼氢化钠溶液的摩尔浓度为0.0001mol/L-0.1mol/L。Optionally, the molar concentration of the sodium borohydride solution is 0.0001 mol / L-0.1 mol / L.
可选的,所述置于硼氢化钠溶液中浸泡的浸泡温度为15℃-35℃,浸泡时间为0.5h-7h。进一步可选的,所述置于硼氢化钠溶液中浸泡还包括在转速50转/min-150转/min条件下置于硼氢化钠溶液中浸泡。Optionally, the immersion temperature of the immersion in the sodium borohydride solution is 15 ° C-35 ° C, and the immersion time is 0.5h-7h. Further optionally, the immersion in the sodium borohydride solution further includes immersion in a sodium borohydride solution at a rotation speed of 50 rpm to 150 rpm.
本发明第一方面提供的甲醛净化纤维的制备方法,利用静电纺丝制备质量轻、透气性好的纤维,再通过真空干燥、多巴胺改性或紫外光照,在保持原有纤维特性的基础上增加了纤维对贵金属离子的吸附性,从而可以负载贵金属离 子,负载量高,经过硼氢化钠溶液还原,制得甲醛净化纤维,可以作为分解甲醛的催化剂,制备工艺简单、成本低,有利于工业化生产。The method for preparing formaldehyde purification fiber provided by the first aspect of the present invention uses electrostatic spinning to prepare light-weight and air-permeable fibers, and then increases the original fiber characteristics by vacuum drying, dopamine modification, or ultraviolet light. The adsorption of noble metal ions by the fiber can be carried, so that the noble metal ions can be loaded with a high load. After the reduction of sodium borohydride solution, the formaldehyde purification fiber can be prepared, which can be used as a catalyst for decomposing formaldehyde. The preparation process is simple and the cost is low, which is beneficial to industrial production .
第二方面,本发明提供了一种甲醛净化纤维,由第一方面所述的甲醛净化纤维的制备方法制得。In a second aspect, the present invention provides a formaldehyde purification fiber, which is prepared by the method for preparing a formaldehyde purification fiber according to the first aspect.
可选的,所述甲醛净化纤维的直径为700nm-1300nm。Optionally, the diameter of the formaldehyde purification fiber is 700 nm-1300 nm.
可选的,所述甲醛净化纤维的线密度为1.01dtex-1.44dtex,断裂强度为7.3cN/dtex-7.9cN/dtex,断裂拉伸率为5%-30%。Optionally, the linear density of the formaldehyde purification fiber is 1.01dtex-1.44dtex, the breaking strength is 7.3cN / dtex-7.9cN / dtex, and the breaking elongation is 5% -30%.
可选的,所述甲醛净化纤维对甲醛的转化率高于93%。Optionally, the conversion rate of the formaldehyde purification fiber to formaldehyde is higher than 93%.
具体的,所述甲醛净化纤维可以但不限用于民用或工业用空气过滤设备,包括口罩、空调、空气净化器及其滤芯。Specifically, the formaldehyde purification fiber can be used in, but not limited to, civil or industrial air filtering equipment, including masks, air conditioners, air purifiers, and filter elements thereof.
本发明第二方面提供的甲醛净化纤维可以用作催化甲醛分解的催化剂,使得甲醇转变为水和二氧化碳,从而去除甲醛,并且产物没有污染;同时,甲醛净化纤维避免了粉尘催化剂造成的粉尘污染,绿色环保、质量轻、透气性好、稳定性高、负载量高,吸附少量贵金属就可达到高效的甲醛转化效率。The formaldehyde purification fiber provided by the second aspect of the present invention can be used as a catalyst for catalyzing the decomposition of formaldehyde, so that methanol is converted into water and carbon dioxide, thereby removing formaldehyde, and the product is not polluted. At the same time, the formaldehyde purification fiber avoids dust pollution caused by the dust catalyst. Green environmental protection, light weight, good air permeability, high stability, high load capacity, and efficient absorption of formaldehyde can be achieved by adsorbing a small amount of precious metals.
本发明的有益效果:The beneficial effects of the present invention:
(1)本发明提供了一种甲醛净化纤维的制备方法,通过静电纺丝制备质量轻、透气性好的纤维,再经过真空干燥、多巴胺改性或紫外光照,在保持原有纤维特性的基础上增加了纤维对贵金属离子的吸附性,从而使其可以负载贵金属离子,最后经过硼氢化钠溶液还原,制得甲醛净化纤维,制备工艺简单、成本低,有利于工业化生产;(1) The present invention provides a method for preparing formaldehyde-purified fibers. Light-weight and air-permeable fibers are prepared by electrostatic spinning, followed by vacuum drying, dopamine modification, or ultraviolet light. The basis for maintaining the original fiber characteristics It increases the fiber's adsorption of noble metal ions, so that it can carry noble metal ions, and finally it is reduced by sodium borohydride solution to obtain formaldehyde purified fiber. The preparation process is simple and the cost is low, which is conducive to industrial production;
(2)本发明提供的甲醛净化纤维可以作为催化甲醛分解的催化剂,使得甲醇转变为水和二氧化碳,从而去除甲醛,并且产物没有污染;同时,甲醛净化纤维避免了粉尘催化剂造成的粉尘污染,绿色环保、质量轻、透气性好、稳定性高、负载量高,吸附少量贵金属就可达到高效的甲醛转化效率,在去除甲醛方面具有广泛的应用前景。(2) The formaldehyde purification fiber provided by the present invention can be used as a catalyst for catalyzing the decomposition of formaldehyde, so that methanol is converted into water and carbon dioxide, thereby removing formaldehyde, and the product is not polluted; at the same time, the formaldehyde purification fiber avoids dust pollution caused by dust catalyst, green Environmental protection, light weight, good air permeability, high stability, high load capacity, adsorption of a small amount of precious metals can achieve efficient formaldehyde conversion efficiency, and has broad application prospects in the removal of formaldehyde.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍。此处所描述的具体实施 例仅仅用以解释本发明,并不用于限定本发明。In order to explain the technical solutions in the embodiments of the present invention or the prior art more clearly, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. The specific embodiments described here are only used to explain the present invention, and are not intended to limit the present invention.
图1为本发明实施例1制得的甲醛净化纤维的电镜扫描图;FIG. 1 is an electron micrograph of a formaldehyde purification fiber prepared in Example 1 of the present invention; FIG.
图2为本发明实施例1制得的甲醛净化纤维的透射电镜图,图2中(a)是在标尺0.2μm下的透射电镜图,图2中(b)是在标尺50nm下的透射电镜图;FIG. 2 is a transmission electron microscope image of the formaldehyde-purified fiber prepared in Example 1 of the present invention. FIG. 2 (a) is a transmission electron microscope image at a scale of 0.2 μm, and FIG. 2 (b) is a transmission electron microscope at a scale of 50 nm. Figure;
图3为本发明实施例1制得的甲醛净化纤维的表面纳米颗粒直径分析图;3 is a diameter analysis chart of surface nanoparticles of the formaldehyde purification fiber prepared in Example 1 of the present invention;
图4为对比例1制得的聚甲基丙烯酸甲酯纤维的电镜扫描图;4 is an electron micrograph of a polymethyl methacrylate fiber prepared in Comparative Example 1;
图5为本发明实施例1制得的甲醛净化纤维稳定性检测结果图;FIG. 5 is a diagram showing the stability test results of the formaldehyde purification fiber prepared in Example 1 of the present invention; FIG.
图6为本发明实施例1制得的甲醛净化纤维在不同气体流速下的分解甲醛效率图。FIG. 6 is a diagram of the efficiency of formaldehyde decomposition of the formaldehyde purification fiber prepared in Example 1 of the present invention at different gas flow rates.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In the following, the technical solutions in the embodiments of the present invention will be clearly and completely described with reference to the drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, but not all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by a person of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
实施例1Example 1
一种甲醛净化纤维的制备方法,包括:A method for preparing formaldehyde purification fiber includes:
将聚甲基丙烯酸甲酯溶解于N,N-二甲基甲酰胺(DMF)中制备纺丝液,其中纺丝液中聚甲基丙烯酸甲酯的质量浓度为30%,在静电纺丝机上进行纺丝,再于真空干燥6h,得到白色的聚甲基丙烯酸甲酯纤维。Polymethyl methacrylate was dissolved in N, N-dimethylformamide (DMF) to prepare a spinning solution. The mass concentration of polymethyl methacrylate in the spinning solution was 30%. Spinning and drying under vacuum for 6 h to obtain white polymethyl methacrylate fibers.
将22.5mL蒸馏水、10mL无水乙醇、0.5mL氨水,0.125g盐酸多巴胺混合均匀,配制出多巴胺改性液,将聚甲基丙烯酸甲酯纤维置于多巴胺改性中,放置在摇床上室温浸泡12h,碱性条件下多巴胺在纤维上发生氧化自聚,用水进行洗涤,至水溶液无色后,再用质量分数15%的异丙醇水溶液浸泡20min,去除未反应的多巴胺,水漂洗3-5次,冻干机冻干即可得到黑色的聚多巴胺包覆的聚甲基丙烯酸甲酯纤维。Mix 22.5mL of distilled water, 10mL of absolute ethanol, 0.5mL of ammonia, and 0.125g of dopamine hydrochloride to prepare a dopamine modified solution. Put the polymethyl methacrylate fiber in the dopamine modification, and soak it in a shaker at room temperature for 12h. Under alkaline conditions, dopamine undergoes oxidative self-polymerization on the fibers, washed with water until the aqueous solution is colorless, and then immersed in a 15% isopropyl alcohol aqueous solution for 20 minutes to remove unreacted dopamine, and rinsed with water 3-5 times The lyophilizer can be lyophilized to obtain black polydopamine-coated polymethyl methacrylate fibers.
将氯铂酸和硝酸镍溶于水中混合均匀配制成溶液,其中,铂离子的摩尔浓度为0.0494mol/L,镍离子的摩尔浓度为0.12mol/L,溶液pH为3.5,聚多巴胺包覆的聚甲基丙烯酸甲酯纤维置于其中,并放置在摇床上室温浸泡72h后,再置 于0.0005mol/L硼氢化钠溶液中浸泡3h,经洗涤、干燥得到甲醛净化纤维。对制得的甲醛净化纤维进行电镜扫描,结果如图1所示,可以看出甲醛净化纤维的直径为1100nm-1200nm。纤维表面附着有聚多巴胺颗粒,表面粗糙,聚多巴胺均匀的包裹在纤维表面,形成一层聚多巴胺外壳,纤维表面的颗粒是还未沿纤维生长的聚多巴胺颗粒。同时经过能谱扫描发现甲醛净化纤维表面均匀的附着铂、镍纳米颗粒。对制得的甲醛净化纤维进行透射电镜检测,结果如图2所示,发现聚甲基丙烯酸甲酯纤维表面被一层黑色的多巴胺包裹(图2中(a)),并且多巴胺外壳上附着有纳米颗粒(图2中(b))。对附着的纳米颗粒进行分析,发现其为以镍为核,铂为壳的复合纳米颗粒。对200个纳米颗粒的直径进行测量,结果如图3所示,纳米颗粒平均直径为2.14nm,直径非常小,使得纳米颗粒具有较高的催化活性。Chloroplatinic acid and nickel nitrate were dissolved in water and mixed to prepare a solution. The molar concentration of platinum ions was 0.0494 mol / L, the molar concentration of nickel ions was 0.12 mol / L, the pH of the solution was 3.5, and the polydopamine-coated The polymethyl methacrylate fiber was placed therein, soaked in a shaker at room temperature for 72 hours, and then immersed in a 0.0005mol / L sodium borohydride solution for 3 hours, washed and dried to obtain formaldehyde-purified fibers. The obtained formaldehyde purification fiber was scanned by an electron microscope, and the result is shown in FIG. 1. It can be seen that the diameter of the formaldehyde purification fiber is 1100 nm-1200 nm. Polydopamine particles are attached to the surface of the fiber, and the surface is rough. Polydopamine is evenly wrapped on the surface of the fiber to form a layer of polydopamine. The particles on the surface of the fiber are polydopamine particles that have not yet grown along the fiber. At the same time, through energy spectrum scanning, it was found that platinum and nickel nanoparticles were uniformly attached to the surface of the formaldehyde purification fiber. Transmission electron microscopy was performed on the prepared formaldehyde-purified fibers. The results are shown in Figure 2. It was found that the surface of the polymethyl methacrylate fiber was covered with a layer of black dopamine ((a) in Figure 2), and the dopamine shell was attached to the shell. Nanoparticles ((b) in Figure 2). The attached nanoparticles were analyzed and found to be composite nanoparticles with nickel as the core and platinum as the shell. The diameters of 200 nanoparticles were measured. The results are shown in Figure 3. The average diameter of the nanoparticles is 2.14 nm, and the diameter is very small, which makes the nanoparticles have higher catalytic activity.
实施例2Example 2
一种甲醛净化纤维的制备方法,包括:A method for preparing formaldehyde purification fiber includes:
将聚甲基丙烯酸甲酯和聚偏氟乙烯溶解于N,N-二甲基甲酰胺(DMF)中制备纺丝液,其中纺丝液中聚甲基丙烯酸甲酯的质量浓度为15%,聚偏氟乙烯的质量浓度为20%。在静电纺丝机上进行纺丝,静电纺丝参数为:阳极电压8kV,阴极电压-4kV,进样速度0.4ml/h,转速60转/min,纺丝温度20℃,湿度40%。经纺丝后的纤维在50℃下真空干燥7h,得到聚甲基丙烯酸甲酯纤维。Polymethyl methacrylate and polyvinylidene fluoride are dissolved in N, N-dimethylformamide (DMF) to prepare a spinning solution, wherein the mass concentration of polymethyl methacrylate in the spinning solution is 15%, The mass concentration of polyvinylidene fluoride is 20%. Spinning was performed on an electrostatic spinning machine. Electrostatic spinning parameters were: anode voltage 8 kV, cathode voltage-4 kV, injection speed 0.4 ml / h, rotation speed 60 rpm, spinning temperature 20 ° C, humidity 40%. The spun fibers were dried under vacuum at 50 ° C. for 7 hours to obtain polymethyl methacrylate fibers.
将15mL蒸馏水、5mL无水乙醇、0.3mL氨水,0.05g盐酸多巴胺混合均匀,配制出多巴胺改性液,将聚甲基丙烯酸甲酯纤维置于多巴胺改性中,室温浸泡24h后用水进行洗涤,至水溶液无色后,再用质量分数20%的异丙醇水溶液浸泡30min,去除未反应的多巴胺,水漂洗3-5次,冻干机冻干即可得到聚多巴胺包覆的聚甲基丙烯酸甲酯纤维。Mix 15 mL of distilled water, 5 mL of absolute ethanol, 0.3 mL of ammonia, and 0.05 g of dopamine hydrochloride to prepare a dopamine modified solution. Put the polymethyl methacrylate fiber in the dopamine modification, soak it in room temperature for 24 hours, and wash it with water. After the aqueous solution is colorless, immerse it in a 20% isopropyl alcohol aqueous solution for 30 minutes to remove unreacted dopamine, rinse with water for 3-5 times, and freeze dry with a lyophilizer to obtain polydopamine coated polymethacrylic acid Methyl ester fiber.
将硝酸镍溶于水中混合均匀配制成溶液,其中,镍离子的摩尔浓度为0.03mol/L。聚多巴胺包覆的聚甲基丙烯酸甲酯纤维置于其中,室温浸泡96h后,再置于0.003mol/L硼氢化钠溶液中浸泡,经洗涤、干燥后得到甲醛净化纤维。经检测,该甲醛净化纤维的线密度为1.3dtex,断裂强度为7.8cN/dtex,断裂拉伸率为20%。Nickel nitrate was dissolved in water and mixed to prepare a solution, wherein the molar concentration of nickel ions was 0.03 mol / L. The polydopamine-coated polymethyl methacrylate fiber was placed therein, and after soaking at room temperature for 96 hours, it was soaked in a 0.003mol / L sodium borohydride solution, and the formaldehyde purified fiber was obtained after washing and drying. After testing, the linear density of the formaldehyde-purified fiber was 1.3 dtex, the breaking strength was 7.8 cN / dtex, and the elongation at break was 20%.
实施例3Example 3
一种甲醛净化纤维的制备方法,包括:A method for preparing formaldehyde purification fiber includes:
将聚乙烯吡咯烷酮和聚偏氟乙烯以质量比3:2比例混合,并溶解于氯仿中制成纺丝液,其中纺丝液中聚乙烯吡咯烷酮的质量浓度为10%。在静电纺丝机上进行纺丝,静电纺丝参数为:阳极电压25kV,阴极电压-2kV,进样速度1ml/h,转速180转/min,纺丝温度30℃,湿度60%。经纺丝后的纤维在50μW/cm 2紫外光强度下进行光照4h,进行交联反应制得第二聚合物纤维。 The polyvinylpyrrolidone and polyvinylidene fluoride are mixed at a ratio of 3: 2 by mass and dissolved in chloroform to prepare a spinning solution, wherein the mass concentration of the polyvinylpyrrolidone in the spinning solution is 10%. Spinning was performed on an electrostatic spinning machine. The electrostatic spinning parameters were: anode voltage 25 kV, cathode voltage-2 kV, injection speed 1 ml / h, rotation speed 180 rpm, spinning temperature 30 ° C, humidity 60%. After spinning, the fiber was irradiated with ultraviolet light at 50 μW / cm 2 for 4 hours, and then subjected to a crosslinking reaction to obtain a second polymer fiber.
配制氯铂酸溶液,其中,铂离子的摩尔浓度为0.035mol/L。将第二聚合物纤维置于其中,并放置在摇床上室温浸泡80h后,再置于0.03mol/L硼氢化钠溶液中浸泡,经洗涤、干燥后得到甲醛净化纤维。经检测,该甲醛净化纤维的线密度为1.2dtex,断裂强度为7.4cN/dtex,断裂拉伸率为10%。A chloroplatinic acid solution was prepared, in which the molar concentration of platinum ions was 0.035 mol / L. The second polymer fiber was placed therein, soaked in a shaker at room temperature for 80 hours, and then soaked in a 0.03mol / L sodium borohydride solution. After washing and drying, formaldehyde-purified fibers were obtained. After testing, the linear density of the formaldehyde purification fiber was 1.2 dtex, the breaking strength was 7.4 cN / dtex, and the breaking elongation was 10%.
对比例1Comparative Example 1
将聚甲基丙烯酸甲酯溶解于N,N-二甲基甲酰胺(DMF)中制备纺丝液,其中纺丝液中聚甲基丙烯酸甲酯的质量浓度为30%,在静电纺丝机上进行纺丝,再于真空干燥6h,得到白色的聚甲基丙烯酸甲酯纤维。对制得的聚甲基丙烯酸甲酯纤维进行电镜扫描,结果如图4所示,制得的聚甲基丙烯酸甲酯纤维表面光滑,纤维形貌均匀稳定,直径为700nm-850nm。与实施例1制得的甲醛净化纤维比较可知,聚甲基丙烯酸甲酯纤维经过多巴胺包覆后,纤维直径增加,表面变粗糙。Polymethyl methacrylate was dissolved in N, N-dimethylformamide (DMF) to prepare a spinning solution. The mass concentration of polymethyl methacrylate in the spinning solution was 30%. Spinning and drying under vacuum for 6 h to obtain white polymethyl methacrylate fibers. The obtained polymethyl methacrylate fiber was scanned by an electron microscope, and the result is shown in FIG. 4. The surface of the prepared polymethyl methacrylate fiber was smooth, and the fiber morphology was uniform and stable, with a diameter of 700 nm-850 nm. Compared with the formaldehyde purification fiber prepared in Example 1, it can be seen that after the polymethyl methacrylate fiber is coated with dopamine, the fiber diameter increases and the surface becomes rough.
为了证明本发明的有益效果,进行以下效果实施例:In order to prove the beneficial effects of the present invention, the following effect examples are performed:
效果实施例1Effect Example 1
将实施例1制备的甲醛净化纤维进行压片并研磨粉碎成颗粒,过50目筛后取0.03g填充于内径7mm的石英管中,并少量石英棉固定位置,将石英管固定在反应器中。The formaldehyde purification fiber prepared in Example 1 was tableted and pulverized into particles. After passing through a 50-mesh sieve, 0.03 g was filled into a quartz tube with an inner diameter of 7 mm, and a small amount of quartz cotton was fixed at the position. The quartz tube was fixed in the reactor. .
配制200mg/L的甲醛溶液并转移至处于冰水浴保温箱的鼓泡机中,通入N 2作为载气,鼓泡带出甲醛气体,与稀释气体空气混合进入反应器中的石英管,取样测定通过石英管前后气体中甲醛的浓度,按照公式(1)计算甲醛净化纤维转化甲醛的效率,其中,甲醛浓度测定方法参照国家标准《公共场所空气中甲醛测定方法》(GB/T18204.26-2000)中的酚试剂分光光度法,C 0为通入石英管的混合气体中甲醛浓度,C 1为通过石英管后的混合气体中甲醛浓度。 A 200mg / L formaldehyde solution was prepared and transferred to a bubbler in an ice-water bath incubator. N 2 was used as a carrier gas, and the formaldehyde gas was taken out by the bubbling. It was mixed with the diluent air into the quartz tube in the reactor. Measure the concentration of formaldehyde in the gas before and after passing through the quartz tube, and calculate the efficiency of the formaldehyde purification fiber to convert formaldehyde according to formula (1). Among them, the method for measuring the concentration of formaldehyde refers to the national standard "Method for measuring formaldehyde in air in public places" (GB / T18204.26- In the phenol reagent spectrophotometry in 2000), C 0 is the concentration of formaldehyde in the mixed gas passed into the quartz tube, and C 1 is the concentration of formaldehyde in the mixed gas after passing through the quartz tube.
Figure PCTCN2018116866-appb-000001
Figure PCTCN2018116866-appb-000001
经测定通入石英管的混合气体中甲醛的含量为3mg/L,当空气流速为30ml/min时,最终甲醛的转化率达到了99.8%。It was determined that the content of formaldehyde in the mixed gas flowing into the quartz tube was 3 mg / L. When the air flow rate was 30 ml / min, the final formaldehyde conversion rate reached 99.8%.
效果实施例2Effect Example 2
与效果实施例1的条件相同,对含有甲醛净化纤维的石英管持续通入混合气体,对甲醛净化纤维的稳定性进行测定。结果如图5所示,在408h中持续通入混合气体(甲醛的含量为3mg/L,空气流速为30ml/min),甲醛的转化率保持在95%以上,整体保持较高的转化水平,表明本发明制备的甲醛净化纤维具有高的稳定性并且能够进行重复利用。Under the same conditions as in Effect Example 1, the quartz tube containing the formaldehyde purification fiber was continuously fed with a mixed gas, and the stability of the formaldehyde purification fiber was measured. The results are shown in Fig. 5. In 408h, the mixed gas was continuously introduced (the content of formaldehyde was 3mg / L and the air flow rate was 30ml / min). The conversion rate of formaldehyde remained above 95%, and the overall conversion level remained high. It is shown that the formaldehyde purification fiber prepared by the present invention has high stability and can be reused.
效果实施例3Effect Example 3
与效果实施例1的条件相同,对含有甲醛净化纤维的石英管持续通入混合气体(甲醛的含量为3mg/L),改变通入气体的流速,观察其对甲醛净化纤维性能的影响。结果如图6所示,气体流速低于70ml/min时,甲醛的转化率保持在97%以上,当高于70ml/min时,甲醛转化率略有降低,但仍然保持在93%以上,表明本发明制备的甲醛净化纤维在多种气流条件下均可以保持较高的甲醛转化率,具有广泛的应用前景。Same conditions as in Effect Example 1, a mixed gas (formaldehyde content of 3 mg / L) was continuously introduced into the quartz tube containing the formaldehyde purification fiber, the flow rate of the gas was changed, and the influence on the performance of the formaldehyde purification fiber was observed. The results are shown in Figure 6. When the gas flow rate is lower than 70ml / min, the conversion rate of formaldehyde remains above 97%. When the gas flow rate is higher than 70ml / min, the conversion rate of formaldehyde decreases slightly, but still remains above 93%, indicating that The formaldehyde purification fiber prepared by the invention can maintain a high formaldehyde conversion rate under various air flow conditions, and has a wide application prospect.
因此,基于上述效果实施例的结果,可以看出本发明提供的甲醛净化纤维绿色环保、质量轻、透气性好、稳定性高,具有优异的去除甲醛能力,在除甲醛方面的应用前景广。Therefore, based on the results of the above-mentioned effect examples, it can be seen that the formaldehyde purification fiber provided by the present invention is environmentally friendly, light in weight, good in breathability, high in stability, has excellent ability to remove formaldehyde, and has a broad application prospect in the removal of formaldehyde.
以上所述是本发明的优选实施方式,但并不能因此而理解为对本发明专利范围的限制。应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也视为本发明的保护范围。The above is a preferred embodiment of the present invention, but it cannot be understood as a limitation on the scope of the patent of the present invention. It should be noted that, for those of ordinary skill in the art, without departing from the principle of the present invention, several improvements and retouches can be made, and these improvements and retouches are also considered as the protection scope of the present invention.

Claims (10)

  1. 一种甲醛净化纤维的制备方法,其特征在于,包括:A method for preparing formaldehyde purification fiber, comprising:
    将第一聚合物溶于有机溶剂中配制成第一纺丝液,进行静电纺丝、真空干燥后置于多巴胺改性液中浸泡,经洗涤后得到第一聚合物纤维;Dissolving the first polymer in an organic solvent to prepare a first spinning solution, subjecting it to electrostatic spinning, vacuum drying, and soaking in a dopamine modified solution to obtain a first polymer fiber after washing;
    或将第二聚合物溶于有机溶剂中配制成第二纺丝液,进行静电纺丝、紫外光照后得到第二聚合物纤维;其中,所述第一聚合物包括聚甲基丙烯酸甲酯、聚丙烯腈和聚偏氟乙烯中的至少一种,所述第二聚合物包括聚乙烯吡咯烷酮;Or the second polymer is dissolved in an organic solvent to prepare a second spinning solution, and the second polymer fiber is obtained after electrostatic spinning and ultraviolet light; wherein the first polymer includes polymethyl methacrylate, At least one of polyacrylonitrile and polyvinylidene fluoride, and the second polymer includes polyvinylpyrrolidone;
    将所述第一聚合物纤维和/或所述第二聚合物纤维置于含贵金属离子的溶液中浸泡,使所述第一聚合物纤维和/或所述第二聚合物纤维结合所述贵金属离子,再将所述第一聚合物纤维和/或所述第二聚合物纤维置于硼氢化钠溶液中浸泡,使所述贵金属离子转变为贵金属单质或贵金属化合物,随后取出,经洗涤得到甲醛净化纤维。Immersing the first polymer fiber and / or the second polymer fiber in a solution containing noble metal ions, so that the first polymer fiber and / or the second polymer fiber are combined with the noble metal Ion, and then immersing the first polymer fiber and / or the second polymer fiber in a sodium borohydride solution to convert the noble metal ion into a noble metal element or a noble metal compound, and then take out and wash to obtain formaldehyde Purify the fiber.
  2. 如权利要求1所述的甲醛净化纤维的制备方法,其特征在于,所述多巴胺改性液包括含有无水乙醇、氨水和盐酸多巴胺的水溶液。The method of claim 1, wherein the dopamine modification liquid comprises an aqueous solution containing anhydrous ethanol, ammonia, and dopamine hydrochloride.
  3. 如权利要求2所述的甲醛净化纤维的制备方法,其特征在于,所述多巴胺改性液包括5mL-15mL无水乙醇、0.3mL-0.8mL氨水、0.05g-0.25g盐酸多巴胺和15mL-25mL蒸馏水。The method for preparing formaldehyde-purified fiber according to claim 2, wherein the dopamine modified solution comprises 5mL-15mL of absolute ethanol, 0.3mL-0.8mL of ammonia, 0.05g-0.25g of dopamine hydrochloride, and 15mL-25mL Distilled water.
  4. 如权利要求1所述的甲醛净化纤维的制备方法,其特征在于,所述置于多巴胺改性液中浸泡的浸泡温度为15℃-35℃,浸泡时间为6h-24h。The method for preparing formaldehyde purification fiber according to claim 1, wherein the soaking temperature in the dopamine modified solution is 15 ° C-35 ° C, and the soaking time is 6h-24h.
  5. 如权利要求1所述的甲醛净化纤维的制备方法,其特征在于,所述含贵金属离子的溶液中所述贵金属离子的浓度为0.01mol/L-2mol/L,所述含贵金属离子的溶液的pH为2-6;所述硼氢化钠溶液的摩尔浓度为0.0001mol/L-0.1mol/L。The method for preparing formaldehyde purification fiber according to claim 1, wherein the concentration of the precious metal ions in the precious metal ion-containing solution is 0.01 mol / L-2 mol / L, The pH is 2-6; the molar concentration of the sodium borohydride solution is 0.0001mol / L-0.1mol / L.
  6. 如权利要求1所述的甲醛净化纤维的制备方法,其特征在于,所述第一纺丝液中所述第一聚合物的质量浓度为15%-40%,所述第二纺丝液中所述第二聚合物的质量浓度为15%-40%,所述有机溶剂包括二甲基亚砜、氯仿、N,N-二甲基甲酰胺和N,N-二甲基乙酰胺中的至少一种。The method of claim 1, wherein the mass concentration of the first polymer in the first spinning solution is 15% -40%, and the concentration of the first polymer in the second spinning solution is 15% -40%. The mass concentration of the second polymer is 15% -40%, and the organic solvent includes dimethyl sulfoxide, chloroform, N, N-dimethylformamide, and N, N-dimethylacetamide. At least one.
  7. 如权利要求1所述的甲醛净化纤维的制备方法,其特征在于,所述静电纺丝的纺丝温度为20℃-35℃,湿度为20%-80%,进样速度为0.4ml/h-1.8ml/h;所述真空干燥的温度为40℃-80℃,时间为6h-24h;所述紫外光照为在10μW/cm 2-100μW/cm 2紫外光强度下照射2h-12h。 The method for preparing formaldehyde purification fiber according to claim 1, wherein the spinning temperature of the electrostatic spinning is 20 ° C-35 ° C, the humidity is 20% -80%, and the injection speed is 0.4ml / h -1.8ml / h; the vacuum drying temperature of 40 ℃ -80 ℃, time 6h-24h; the UV irradiation is irradiation 2h-12h at 10μW / cm 2 -100μW / cm 2 ultraviolet light intensity.
  8. 一种甲醛净化纤维,其特征在于,由权利要求1-7任一项所述的甲醛净化纤维的制备方法制得。A formaldehyde purification fiber, which is prepared by the method for preparing a formaldehyde purification fiber according to any one of claims 1-7.
  9. 如权利要求8所述的甲醛净化纤维,其特征在于,所述甲醛净化纤维的直径为700nm-1300nm。The formaldehyde purification fiber according to claim 8, wherein the formaldehyde purification fiber has a diameter of 700nm-1300nm.
  10. 如权利要求8所述的甲醛净化纤维,其特征在于,所述甲醛净化纤维对甲醛的转化率高于93%。The formaldehyde purification fiber according to claim 8, wherein the conversion rate of formaldehyde purification fiber to formaldehyde is higher than 93%.
PCT/CN2018/116866 2018-05-31 2018-11-22 Formaldehyde purification fiber and preparation method therefor WO2019227872A1 (en)

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