CN103043997B - The manufacture method of powder, molding, cladding and powder - Google Patents

The manufacture method of powder, molding, cladding and powder Download PDF

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CN103043997B
CN103043997B CN201110308254.6A CN201110308254A CN103043997B CN 103043997 B CN103043997 B CN 103043997B CN 201110308254 A CN201110308254 A CN 201110308254A CN 103043997 B CN103043997 B CN 103043997B
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infrared rays
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CN103043997A (en
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饭塚千博
新纳英明
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Asahi Kasei Corp
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Asahi Kasei Chemicals Corp
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Abstract

The present invention relates to the manufacture method of powder, molding, cladding and powder.Problem of the present invention is, provides a kind of powder that can suppress dispersing when being shaped, the generation of forming defects.Described powder is the powder containing silicon-dioxide and sodium, and wherein, the containing ratio of sodium is below more than 0.005 quality % 3 quality %, and BET specific surface area is 10m 2/ more than g 400m 2/ below g, intensity of compression is less than 31%, and the thermal conductivity at 30 DEG C is below 0.05W/mK.

Description

The manufacture method of powder, molding, cladding and powder
Technical field
The present invention relates to the manufacture method of powder, molding, cladding and powder.
Background technology
The mean free path of room temperature in air molecule is about 100nm.Therefore, in the porous insert in space with below diameter 100nm, by air convection current, conduct the heat transfer that causes and be suppressed, such porous insert shows excellent heat insulating function.
Follow the principle of this heat insulating function, the thermal conductivity of known ultra-fine grain is low, is suitable for thermal insulation material.Such as, in following patent documentation 1, describe a kind of ultrafine powder by silicon-dioxide and be configured as porous insert separately and the thermal insulation material obtained, the volume density of this thermal insulation material is 0.2 ~ 1.5g/cm 3, BET specific surface area is 15 ~ 400m 2/ g, median size is 0.001 ~ 0.5 μm, and accumulating total pore volume is 0.3 ~ 4cm 3/ g, the accumulation pore volume of the pore that average pore diameter is less than 1 μm is more than 10% of the accumulation pore volume in molding.A kind of manufacture method of thermal insulation material is described in patent documentation 2, the mode that it utilizes with ring internal diameter is less than 0.1 μm is associated circlewise or the coated particle be made up of radiation absorption scattering material etc. of spiral helicine ultra-fine grain, form porous insert coatedparticles, by this particle and inorganic fibre or and porous insert coatedparticles in the same manner as the porous insert covered fiber that formed mix, as the powder of thermal insulation material precursor, by this precursor press molding, manufacture thermal insulation material.
Prior art document
Patent documentation
Patent documentation 1: Japanese Unexamined Patent Publication 2007-169158 publication
Patent documentation 2: Japanese Patent No. 4367612 specification sheetss
Non-patent literature
Non-patent literature 1: independent administrative corporation's NEDO, Heisei 17 years ~ 18 years achievement Report book energy use rationalization technology strategy develop energy to use rationalization technical application to melt and sends out " having the practical exploitation of the ultralow heat conducting material of nanoporous composite structure "
Summary of the invention
the problem that invention will solve
But in order to obtain the silica shaped bodies described in patent documentation 1, need following operation, that is, by as classification after the SiO 2 powder preliminary shaping of raw material, make median size be greater than the operation of starting silica powder, manufacturing process is complicated.And during by the shaping of the ultrafine powder of silicon-dioxide or preliminary shaping, dropped in the operation of mould by starting silica powder, powder easily disperses, and operating efficiency is poor.In addition, the importance of other compositions such as the Na beyond silicon-dioxide is not recorded.For the thermal insulation material of patent documentation 2, as disclosed in Non-Patent Document 1, when press molding, produce diffract forming defects in the face perpendicular to press face.When thermal insulation material exists such forming defects, not only thermal insulation material may be damaged, and heat-insulating property also can reduce, and therefore, can not become goods, and yield rate reduces, therefore not preferred.
Produce the reason of forming defects as described in non-patent literature 1, by with ultra-fine grain be main component thermal insulation material precursor press molding after, during relief pressure, molding expands larger.This expansion is called as resilience.The situation of the thermal insulation material described in patent documentation 2, by reducing the content of ultra-fine grain contained in precursor, reducing resilience, can suppress the generation of forming defects, but, only merely by reducing the content of ultra-fine grain, heat-insulating property can not be avoided to reduce.
But, press molding comprises such as to the operation of the thermal insulation material of mould supply powdery, but when supplying the thermal insulation material of powdery to mould, according to the difference of thermal insulation material, easily condense, in storage tanks hopper, because of remaining thermal insulation material, volume density changes, and therefore, is sometimes difficult to carry out stable continuous supply.The cohesion of such shaping raw material may cause the lack of fill to mould, and productivity is significantly reduced.
The thermal insulation material of powdery, except carrying out press molding, is sometimes also filled in outer cover material material (bag of such as woven fiber glass or pipe), is rolled into pipe etc. and utilizes.If powder easily disperses, then operating efficiency when being filled in outer cover material material is poor, and therefore, in such use-pattern, dispersing of powder is more serious problem, expects to be resolved.
The problem that the present invention has in view of such prior art is carried out, and its object is to, and provides a kind of powder that can suppress dispersing when being shaped, the generation of forming defects.In addition, the present invention also aims to, the manufacture method of molding, cladding and the powder using described powder is provided.
for the scheme of dealing with problems
The present inventor, in order to solve above-mentioned problem, has carried out wholwe-hearted research, found that, the powder with following characteristics can suppress the generation of dispersing when being shaped, forming defects, thus completes following the present invention.
Powder of the present invention is the powder containing silicon-dioxide and sodium (Na), and the containing ratio of sodium (Na) is below more than 0.005 quality % 3 quality %, and BET specific surface area is 10m 2/ more than g 400m 2/ below g, intensity of compression is less than 31%, and the thermal conductivity at 30 DEG C is below 0.05W/mK.The resilience when press molding of such powder is little, and plasticity is good, and dispersing during process is also inhibited.
The powder of the invention described above preferably contains potassium (K) and the containing ratio of potassium (K) is below more than 0.005 quality % 5 quality %.
The powder of the invention described above preferably contains magnesium (Mg) and the containing ratio of magnesium (Mg) is below more than 0.005 quality % 5 quality %.
The powder of the invention described above preferably contains calcium (Ca) and the containing ratio of calcium (Ca) is below more than 0.005 quality % 2 quality %.
The powder of the invention described above preferably contains iron (Fe) and the containing ratio of iron (Fe) is below more than 0.005 quality % 6 quality %.
The powder of the invention described above preferably contains phosphorus (P) and the containing ratio of phosphorus (P) is below more than 0.002 quality % 1 quality %.
The powder of the invention described above preferably contains sulphur (S) and the containing ratio of sulphur (S) is below more than 0.002 quality % 1 quality %.
The powder of the invention described above preferably contains inorganic fibre further and the containing ratio of inorganic fibre is below more than 0.1 quality % 50 quality %.
The powder of the invention described above be preferably the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further and the containing ratio of infrared rays opacification particle more than 0 quality % and be below 49.5 quality %.
For the powder of the invention described above and the thermal conductivity of powder preferably at 800 DEG C containing infrared rays opacification particle is below 0.15W/mK.
Inorganic fibre contained in the powder of the invention described above preferably has bio-soluble.
Molding of the present invention contains above-mentioned powder.Such molding can suppress the generation of forming defects, and powder when processing can be suppressed to disperse.
Cladding of the present invention possesses outer cover material material, above-mentioned powder and/or above-mentioned molding is accommodated in outer cover material material and forms.Such cladding than powder, molding is easier processes, application property is also excellent.
In the cladding of the invention described above, outer cover material material is preferably containing inorganic fibre.
In the cladding of the invention described above, outer cover material material is preferably resin molding.
The manufacture method of the powder of the invention described above has following operation: will containing silicon-dioxide and median size D sfor more than 5nm and less than 30nm small-particle with containing silicon-dioxide and median size D lfor the operation that the macrobead of more than 30nm less than 50 μm mixes, and at least one in small-particle or macrobead contains sodium.According to this manufacture method, resilience when can obtain press molding is little, plasticity is good and process time the powder be also inhibited that disperses.
the effect of invention
According to the present invention, resilience during a kind of press molding can be provided little and plasticity is good and process time the powder be also inhibited that disperses.In addition, the present invention can also provide the manufacture method of molding, cladding and the powder using above-mentioned powder.
Accompanying drawing explanation
Fig. 1 is an example of the diagrammatic cross-section of the cladding of one embodiment of the present invention.
Fig. 2 is an example of the small-particle that contains of the powder of one embodiment of the present invention and oarse-grained diagrammatic cross-section.
description of reference numerals
1... thermal insulation material, 2... core, 3... outer cover material material, S... small-particle, L... macrobead.
Embodiment
Below, to for implementing mode of the present invention (hreinafter referred to as " present embodiment ".) be described in detail.It should be noted that, the present invention is not limited to following embodiment, can implement various distortion in its main scope.
[1] powder
[1-1] silicon-dioxide
Powder of the present invention contains silicon-dioxide.When the containing ratio of the silicon-dioxide in powder is more than 50 quality %, the heat transfer caused by solid conduction is little, therefore, when thermal insulation material purposes preferably.In addition, when the containing ratio of silicon-dioxide is more than the 75 quality % of powder, the sticking power between powder increases, and dispersing of powder tails off, therefore more preferably.In this specification sheets, so-called silicon-dioxide, refers to by composition formula SiO 2represent composition form particle, containing SiO 2particle, comprise except SiO 2these particles are also called silica dioxide granule by the outer particle also containing metal ingredient etc., other mineral compound sometimes.The salt that silica dioxide granule can be formed containing Si and other element various or composite oxides, can also contain the such hydrous oxide of oxyhydroxide, also can have silanol group.Silica dioxide granule can be crystalline, also can be amorphousness, and can also be their mixture, when thermal insulation material purposes, during for amorphousness, the heat transfer that the solid conduction in thermal insulation material causes be little, and heat-insulating property is high, therefore preferably.
As the concrete example of silica dioxide granule, following substances can be enumerated.Be called as the oxide compound of the silicon of " silicon-dioxide " or " quartz ".The partial oxide of silicon.The composite oxides of aluminosilicate and the such silicon of zeolite.The silicate (glass) of the arbitrary element in Na, Ca, K, Mg, Ba, Ce, B, Fe and Al.The mixture of the oxide compound of the oxide compound of the element beyond silicon, partial oxide, salt or composite oxides (aluminum oxide, titanium oxide etc.) and silicon, partial oxide, salt or composite oxides.The oxide compound of SiC or SiN.
During using powder as thermal insulation material, preferably use temperature under silica dioxide granule to thermally-stabilised.Specifically, preferably under the maximum operation (service) temperature of thermal insulation material, maintenance 1 is constantly little, and the weight of silica dioxide granule does not reduce more than 10%.In addition, silica dioxide granule preferably has water tolerance.Specifically, preferred silica dioxide granule to the meltage of the water 100g of 25 DEG C less than 0.1g, more preferably less than 0.01g.
The proportion of silica dioxide granule is preferably less than more than 2.0 4.0 when using powder as thermal insulation material.When being below more than 2.0 3.0, the volume density of thermal insulation material is little, therefore more preferably, and more preferably less than more than 2.0 2.5.Here, the proportion of silica dioxide granule refers to the true specific gravity utilizing pycnometric method to obtain.
According to the difference of the purposes of powder, powder can containing the material beyond silica dioxide granule.For the material beyond silica dioxide granule, will describe in detail later, when powder contains the material beyond silica dioxide granule, the containing ratio of silica dioxide granule preferably with the total mass of powder for being below more than 50 quality % 99.9 quality % during benchmark.The containing ratio of silica dioxide granule is below more than 50 quality % 97.5 quality % and powder containing inorganic fibre or infrared rays opacification particle shows more excellent minimizing powder disperses and increase effects such as heat-insulating property under high temperature and more preferably.When containing ratio is below more than 60 quality % 97.5 quality %, the volume density of powder is less, therefore further preferably.
Powder only can contain a kind of silica dioxide granule, also can contain two or more silica dioxide granule.Time particularly containing 2 kinds of particles, the small-particle be namely made up of silica dioxide granule and macrobead that particle diameter is different; BET specific area and thermal conductivity are different from situation about only existing with small-particle or macrobead; therefore, can by the proper ratio 2 kinds of particle mixing being adjusted BET specific area and/or thermal conductivity.Such as, median size D lfor more than 30nm less than 50 μm macrobead sometimes BET specific surface area less than 10m 2/ g, but mix wherein median size Ds be more than 5nm and small-particle less than 30nm time, easily make BET specific surface area be 10m 2/ more than g.In addition, oarse-grained solid thermal conduction is large, and therefore, thermal conductivity is more than 0.05W/mK sometimes, by mixing small-particle wherein, there is the tendency suppressing solid thermal to conduct, easily make thermal conductivity be below 0.05W/mK.About intensity of compression, when being only made up of macrobead, intensity of compression is excessive sometimes, by adding small-particle in macrobead, there is the tendency easily intensity of compression being adjusted to less than 31%.
When powder contains two or more silica dioxide granule, with the BET specific surface area of powder for 10m 2/ more than g 400m 2/ below g, thermal conductivity are that the mode of below 0.05W/mK adjusts macrobead and short grained containing ratio; when such as by the mixing of the macrobead of the small-particle of about 10nm and about 5 μm; preferred oarse-grained quality/(short grained quality+oarse-grained quality) be 0.02 ~ 0.95, be more preferably 0.10 ~ 0.90, when being particularly preferably 0.15 ~ 0.85, BET specific surface area becomes 270m 2about/g ~ 40m 2about/g, can adjust BET specific surface area.When oarse-grained mass ratio is in above-mentioned scope, become the heat conducting bottleneck in space by these granuloplastic spaces, easily suppress the thermal conduction in space.
The BET specific surface area of grain diameter influence's powder of silica dioxide granule, when powder is only made up of silica dioxide granule, the particle diameter of silica dioxide granule is 10m 2/ more than g 400m 2/ below g, when powder contains the composition beyond silica dioxide granule, preferably according to the particle diameter of the BET specific surface area setting silicon-dioxide of described composition.Specifically, when powder contains inorganic fibre, the BET specific surface area of general inorganic fibre is less than the BET specific surface area of silicon-dioxide, and therefore, the BET specific surface area of silicon-dioxide is preferably set to 50m 2about/g ~ 400m 2about/g, the particle diameter of silica dioxide granule is preferably set to about 7nm ~ about 50nm.In addition, when powder contains infrared rays opacification particle, the BET specific surface area of general infrared rays opacification particle is less than the BET specific surface area of silicon-dioxide, and therefore, the BET specific surface area of silicon-dioxide is preferably set to 70m 2about/g ~ 450m 2about/g, the particle diameter of silica dioxide granule is preferably set to about 5nm ~ about 40nm.
The particle diameter of silica dioxide granule can by carrying out observing with field emission type scanning electron microscope (FE-SEM) and measuring.Short grained median size D s, oarse-grained median size D lby observing each 1000 small-particles, macrobeads with FE-SEM, its homalographic equivalent circle diameter can be obtained, calculate number average, thus confirming.From the viewpoint of the solid conduction of silica dioxide granule, the median size of silica dioxide granule is preferably more than 3nm and less than 80 μm, is more preferably more than 5nm and less than 50 μm, more preferably more than 5nm and less than 30 μm.
For for macrobead and short grained powder, preferred short grained median size D sfor more than 5nm and less than 30nm.D sduring for more than 5nm, with D ssituation outside above-mentioned numerical range is compared, and has small-particle to become chemically stable tendency, has the tendency that heat-insulating property is easily stable.D sduring less than 30nm, with D ssituation outside above-mentioned numerical range is compared, exist heat transfer that the contact area solid conduction that is little, powder between small-particle causes less, tendency that thermal conductivity is little.
D sduring for more than 5nm below 25nm, be preferred from the viewpoint of thermal conductivity, more preferably more than 5nm below 15nm.
Oarse-grained median size D lpreferably meet D s< D l, and be more than 30nm less than 50 μm.D lcan utilize and above-mentioned D sidentical method is obtained.D lduring for more than 30nm, when being shaped by powder, there is the tendency that the resilience of molding is little.D lwhen being below 50 μm, there is the tendency that thermal conductivity is little.
Oarse-grained median size D lduring for more than 30nm less than 10 μm, when powder contains inorganic fibre, infrared rays opacification particle, powder and their Homogeneous phase mixing become easy, therefore more preferably.D lduring for more than 30nm less than 5 μm, the sticking power of particle is large, and particle is few from coming off of powder, therefore further preferably.
D lfor D smore than 2 times time, when being shaped by powder, resilience diminishes, therefore preferably.D lfor D smore than 3 times time, the bulk density of small-particle and oarse-grained mixed powder is large, and powder volume is little, and at this moment, workability is high, therefore more preferably.D lfor D smore than 4 times time, the difference of small-particle and oarse-grained particle diameter is large, and when mix with macrobead by small-particle, the relative short grained dispersion of macrobead is easy, therefore preferred further.Powder when thermal insulation material purposes, from the viewpoint of the solid heat transfer that the cohesion of particle causes, preferred each Granular composite.
For powder, when suppression water immerses powder or molding, there are operability reduction, molding distortion, be full of cracks etc., preferably containing water-resisting agent.As water-resisting agent, such as, can enumerate: the wax system water-resisting agents such as paraffin, polyethylene wax, acrylic acid ethylene co-polymer wax; The silicon system water-resisting agents such as silicone resin, polydimethylsiloxane, alkylalkoxy silane; The fluorine system water-resisting agents such as perfluoroalkyl carboxylate, perfluoralkyl phosphate, perfluoroalkyl leptodactyline; The silane coupling agents such as the organoalkoxysilane containing alkyl, full-fluorine group; The silylating agents etc. such as trimethylchlorosilane, 1,1,1,3,3,3-hexamethyldisilazane.These water-resisting agents can use one kind or two or more.These water-resisting agents can use with the form of monomer, also can use with the form of solution or emulsion.Wherein, from the viewpoint of raising water tolerance, preferred wax system water-resisting agent, silicon system water-resisting agent.From the viewpoint of the sufficient waterproof effect of imparting, the containing ratio of the water-resisting agent in powder is, the mass ratio of the quality/water-resisting agent of powder entirety is preferably 100/30 ~ 100/0.1, is more preferably 100/20 ~ 100/0.5, more preferably 100/10 ~ 100/1.
[1-2] inorganic fibre
When being shaped by powder, powder is preferably containing inorganic fibre.During containing inorganic fibre, the powder containing fiber especially has the following advantages: in press molding, and particle is few from coming off of molding, and productivity is high.Even if be powder state, dispersing also few, therefore, process is preferred.In this specification sheets, so-called inorganic fibre, refers to that the mean length of inorganic fibre is the fiber of more than 10 with the ratio (length-to-diameter ratio) of average boldness.Length-to-diameter ratio is preferably more than 10, when powder is shaped, from the viewpoint of can with little pressure forming, improve the productivity of molding, be more preferably more than 50, from the viewpoint of the flexural strength of molding, more preferably more than 100.The length-to-diameter ratio of inorganic fibre can be obtained by the rugosity of 1000 inorganic fibres utilizing FE-SEM to measure and the mean value of length.Be blended in powder, but the state that also mutually can be wound around with inorganic fibre or multiple inorganic fibre collect the state mixing of bunchy in same direction the preferred single dispersing of inorganic fibre.In addition, under monodisperse status, also can for inorganic fibre towards the state collected in same direction, but from the viewpoint of reduction thermal conductivity, inorganic fibre is preferably along perpendicular to the direction orientation in direction of conducting heat.
When illustrating the example of inorganic fibre, can enumerate: long glass fiber (long filament) (SiO 2-Al 2o 3-B 2o 3-CaO), glass wool (SiO 2-Al 2o 3-CaO-Na 2o), alkali resistant glass fibre (SiO 2-ZrO 2-CaO-Na 2o), rock wool (basalt wool) (SiO 2-Al 2o 3-Fe 2o 3-MgO-CaO), slag wool (SiO 2-Al 2o 3-MgO-CaO), ceramic fiber (mullite fiber) (Al 2o 3-SiO 2), silica fiber (SiO 2), sapphire whisker (Al 2o 3-SiO 2), potassium titanate fiber, alumina whisker, silicon carbide whisker, silicon nitride crystal whisker, calcium carbonate crystal whisker, alkali magnesium sulfate crystal whisker, calcium sulfate crystal whiskers (gypsum fiber), ZnOw, Zirconium oxide fibre, Carbon fibe, graphite whisker, phosphate fiber, AES (AlkalineEarthSilicate) fiber (SiO 2-CaO-MgO), the existing known inorganic fibre such as wollastonite, sepiolite, attapulgite, brucite of natural mineral.
In inorganic fibre, particularly preferably use the AES fiber (AlkalineEarthSilicateFiber, alkaline earth silicate fibres) of the bio-soluble to human-body safety.As AES fiber, such as, can enumerate: SiO 2the unorganic glass (inorganic polymer) of-CaO-MgO system.
The average boldness of inorganic fibre is preferably more than 1 μm from the viewpoint of preventing from dispersing.The situation of thermal insulation material, from the viewpoint of the heat transfer suppressing to be caused by solid conduction, is preferably less than 20 μm.The average boldness of inorganic fibre can utilize FE-SEM to obtain the rugosity of 1000 inorganic fibres, and it is on average obtained.
The situation of adiabatic purposes, departs from from the viewpoint of the molding suppressing powder to obtain from press molding, and the containing ratio of the inorganic fibre in powder is preferably more than 0.1 quality % relative to the quality of powder entirety, is 10m from making the BET specific surface area of powder 2/ more than g, thermal conductivity are that the viewpoint of below 0.05W/mK is considered, are preferably below 50 quality %.
From the viewpoint of the easy degree mixed with silica dioxide granule, infrared rays opacification particle; the containing ratio of inorganic fibre is more preferably below more than 0.2 quality % 40 quality %; diminish from the viewpoint of volume density, more preferably below more than 0.2 quality % 20 quality %.
The containing ratio of inorganic fibre such as can by obtaining inorganic fibre from particle classifying.
Inorganic fibre also can contain Na, in this case, the containing ratio of the Na in selection powder can be on the basis of the inorganic fibre of the Na containing ratio of below 3 quality %, and the mode that the combined amount of inorganic fibre also meets below 3 quality % with the containing ratio of the Na in powder is determined.In this case, the Na amount that silica dioxide granule can contain tails off according to the Na containing ratio of inorganic fibre.Therefore, the containing ratio of the Na in silica dioxide granule, inorganic fibre is preferably measured in advance.When inorganic fibre is not containing Na, the Na containing ratio of silica dioxide granule (or mixture of silica dioxide granule and infrared rays opacification particle) meets below more than 0.005 quality % 3 quality % (with the total mass of powder for benchmark).
[1-3] infrared rays opacification particle
When requiring the heat-insulating property under high temperature, powder is preferably containing infrared rays opacification particle.So-called infrared rays opacification particle, refers to by reflection, scattering or absorbs the particle that ultrared material forms.In thermal insulation material during mixture of red outside line opacification particle, can suppress radiation-induced heat transfer, therefore, the heat-insulating property under the high-temperature area particularly more than 200 DEG C is high.
As the example of infrared rays opacification particle, can enumerate: charcoal material, Carbon fibe, spinel pigments, aluminum particulate, stainless steel particle, bronze particles, copper/zinc alloy granules, the copper/Chrome metal powder particles such as zirconium white, zirconium silicate, titanium dioxide, iron titanium oxide, ferric oxide, cupric oxide, silicon carbide, gold mine, chromium dioxide, Manganse Dioxide, graphite.Can be used alone at present known as the opaque material of infrared rays above-mentioned metallic particles or non-metallic particle, also two or more kinds may be used described particle.
As infrared rays opacification particle, particularly preferably zirconium white, zirconium silicate, titanium dioxide or silicon carbide.The composition of infrared rays opacification particle can be obtained by FE-SEMEDX.
The median size of infrared rays opacification particle, from the viewpoint of heat-insulating property when more than 200 DEG C, is preferably more than 0.5 μm, from the viewpoint of obtain by suppressing solid conduction less than 200 DEG C time heat-insulating property, preferably less than 30 μm.It should be noted that, the median size of infrared rays opacification particle can utilize the method identical with silica dioxide granule to obtain.The median size of infrared rays opacification particle also depends on the size of inorganic fibre and silica dioxide granule; when silica dioxide granule is 5nm ~ 50 μm; from the viewpoint of the easy degree mixed with silica dioxide granule, the median size of infrared rays opacification particle is more preferably more than 0.5 μm less than 10 μm.
The containing ratio of the infrared rays opacification particle in powder is preferably greater than 0 quality % and be below 49.5 quality %.When the containing ratio of infrared rays opacification particle is greater than 49.5 quality %, the heat transfer caused by solid conduction is large, and therefore, the tendency that heat-insulating property during Shortcomings 200 DEG C is low, in addition, BET specific surface area is little.Heat-insulating property during in order to improve more than 200 DEG C, the containing ratio of infrared rays opacification particle is preferably set to more than 2 quality %.The containing ratio of infrared rays opacification particle from the viewpoint of the easy degree mixed with silica dioxide granule, more preferably below more than 2 quality % 30 quality %.The mixed powder that powder containing silicon-dioxide and sodium and infrared rays opacification particle mix existed the tendency of the tack grow of silica dioxide granule and infrared rays opacification particle.Thus, when preserving for a long time after preparing mixed powder, there is the effect that particle is not easily separated from each other, easily keeps admixture when preparing.
The containing ratio of infrared rays opacification particle such as can be obtained as follows, that is, utilize FE-SEMEDX to measure the composition of infrared rays opacification particle, utilize fluorescent x-ary analysis to carry out quantitatively, obtaining thus to the element that only infrared rays opacification particle contains.
Infrared rays opacification particle also can contain Na.When infrared rays opacification particle contains Na, in the mode that the Na containing ratio in powder entirety is below more than 0.005 quality % 3 quality %, when deducting silica dioxide granule and contain inorganic fibre, the Na of inorganic fibre measures and adjusts Na containing ratio, the combined amount of infrared rays opacification particle.Therefore, the containing ratio of the Na in silica dioxide granule, inorganic fibre is preferably measured in advance.
The containing ratio of [1-4] sodium (Na)
Powder of the present invention contains Na.The containing ratio of Na with the total mass of powder for being below more than 0.005 quality % 3 quality % during benchmark.When the containing ratio of Na is less than 0.005 quality %, there is many tendencies of dispersing of powder, when the containing ratio of Na is more than 3 quality %, there is the tendency that heat-insulating property is low.Its reason is not yet clear and definite, is presumed as follows.That is, the volume density of powder, particle diameter and particle shape, surface-area, water ratio, tack etc. all can affect the intensity of compression of powder.Wherein, mainly water ratio and tack, time in powder containing Na, details is not yet clear and definite, infer, because the electriferous state of silica particles changes, act on water ratio and the such factor of tack, its result, intensity of compression diminishes, and suppresses dispersing of powder.The containing ratio of Na is preferably below more than 0.005 quality % 2 quality %, is more preferably below more than 0.005 quality % 1.5 quality %, more preferably below more than 0.005 quality % 1.0% quality %.The containing ratio of the Na in powder can pass through XRF (x-ray fluorescence analysis) and carry out quantitatively.
Mix multiple silica dioxide granule, such as small-particle and macrobead when preparing powder, preferably measure the containing ratio of respective Na in advance, adjust combined amount in the mode that the containing ratio of the Na of mixed powder is below more than 0.005 quality % 3 quality %.Such as, mixing Na containing ratio be respectively 0.02 quality % small-particle and 5% macrobead time, preferred oarse-grained quality/(short grained quality+oarse-grained quality) is in the scope of 0 ~ 0.99.When using inorganic fibre, infrared rays opacification particle, also preferably measure the containing ratio of respective Na in advance, determine combined amount.Such as, when the containing ratio of Na be the containing ratio that mixes Na in the silicon-dioxide of 0.07 quality % is the inorganic fibre of 1 quality %, the combined amount of inorganic fibre can be determined arbitrarily.Such as, when the containing ratio of Na be the containing ratio that mixes Na in the silicon-dioxide of 0.07 quality % is the infrared rays opacification particle of 0.6 quality %, the combined amount of infrared rays opacification particle can be determined arbitrarily.
[1-5] BET specific surface area
The BET specific surface area of powder of the present invention is 10m 2/ more than g 400m 2/ below g.There is the little tendency of thermal conductivity in the powder with the BET specific surface area within the scope of this, therefore, is preferred for thermal insulation material purposes.It should be noted that, BET specific surface area and intensity of compression are considered to associating to a certain degree, but are not fully echo.The measuring method of BET specific surface area will describe later.
BET specific surface area is 10m 2/ more than g 400m 2when/below g and the containing ratio of Na are below more than 0.005 quality % 3 quality %, exist have excellent formability, few tendency of dispersing of powder.Its reason is not yet clear and definite, infers that as the factor affecting intensity of compression, can enumerate surface-area and water ratio, tack, BET specific surface area is 10m as mentioned above 2/ more than g 400m 2when/below g and the containing ratio of Na are below more than 0.005 quality % 3 quality %, there is the tendency that intensity of compression diminishes, its result, obtain resilience little, have excellent formability, disperse few powder.BET specific surface area is preferably 10m 2/ more than g 300m 2/ below g, is more preferably 10m 2/ more than g 200m 2/ below g, more preferably 10m 2/ more than g 150m 2/ below g.
Mix multiple silica dioxide granule, such as small-particle and macrobead when preparing powder, preferably measuring respective BET specific surface area, take BET specific surface area as 10m 2/ more than g 400m 2the mode of/below g adjusts combined amount.Such as, mix BET specific surface area and be respectively 200m 2the small-particle of/g and 0.3m 2during/g macrobead, preferred oarse-grained quality/(short grained quality+oarse-grained quality) is in the scope of 0 ~ 0.88.When using inorganic fibre, infrared rays opacification particle, also preferably measure respective BET specific surface area in advance, determine combined amount.Such as, be 200m in BET specific surface area 2mixing BET specific surface area in the silicon-dioxide of/g is 0.15m 2during the inorganic fibre of/g, the combined amount of inorganic fibre is preferably 0.1 quality % ~ 90 quality %.In addition, be such as 200m in BET specific surface area 2mixing BET specific surface area in the silicon-dioxide of/g is 2m 2during the infrared rays opacification particle of/g, the combined amount of infrared rays opacification particle is preferably greater than 0 quality % and be below 95 quality %.
[1-6] intensity of compression
The intensity of compression of powder of the present invention is less than 31%.The powder with the intensity of compression of this scope shows the tendency of not easily condensing.Therefore, consider it is particularly preferably as the powder of shaping from easy to handle viewpoint the operation supplied to mould etc.Intensity of compression is preferably less than 29%, is more preferably less than 27%, few from the viewpoint of dispersing of powder, and more preferably less than 25%.The measuring method of intensity of compression will describe later.
Mix multiple silica dioxide granule, such as small-particle and macrobead when preparing powder, preferably described above the containing ratio of Na is below more than 0.005 quality % 3 quality %, BET specific surface area is 10m making 2/ more than g 400m 2the basis of/below g measures intensity of compression.When intensity of compression is more than 31%, preferably maintains below more than 0.005 quality % 3 quality % at the containing ratio of Na, BET specific surface area maintains 10m 2/ more than g 400m 2change small-particle and oarse-grained combined amount in the scope of/below g, determine the combined amount that can meet intensity of compression.Use when inorganic fibre, infrared rays opacification particle and also similarly can determine combined amount.Now, measure small-particle, macrobead intensity of compression separately, when mixing the little particle of intensity of compression in the particle that intensity of compression is large, there is easily adjustment and there is the tendency of the powder of the intensity of compression of above-mentioned scope.Such as, mixing intensity of compression be respectively 15% small-particle and 37% macrobead time, preferred oarse-grained quality/(short grained quality+oarse-grained quality) scope 0.12 ~ 0.85.In addition, be such as that when mixing in the silicon-dioxide of 25% that fiber diameter is 12 μm, mean length is the inorganic fibre of 5mm, the combined amount of inorganic fibre is preferably 0.1 quality % ~ 18 quality % in intensity of compression.And then, be such as that when to mix median size in the silicon-dioxide of 25% be the infrared rays opacification particle of 2 μm, the combined amount of preferred infrared rays opacification particle is 1 quality % ~ 23 quality % in intensity of compression.
[1-7] thermal conductivity
Thermal conductivity at 30 DEG C of powder of the present invention is below 0.05W/mK.From the viewpoint of heat-insulating property, thermal conductivity is preferably below 0.045W/mK, is more preferably below 0.040W/mK, more preferably below 0.037W/mK.When powder of the present invention contains infrared rays opacification particle, particularly the heat-insulating property of high-temperature area of more than 200 DEG C is high, therefore preferably.When powder of the present invention contains infrared rays opacification particle, the thermal conductivity at 800 DEG C is preferably below 0.15W/mK, is more preferably below 0.14W/mK, more preferably below 0.13W/mK.The measuring method of thermal conductivity will describe later.
Mix multiple silica dioxide granule, such as small-particle and macrobead when preparing powder, preferably make that the containing ratio of Na is below more than 0.005 quality % 3 quality %, BET specific surface area is 10m as mentioned above 2/ more than g 400m 2on the basis of/below g, measure thermal conductivity.When thermal conductivity is more than 0.05W/mK, preferably the containing ratio of Na is below more than 0.005 quality % 3 quality %, BET specific surface area is 10m maintaining 2/ more than g 400m 2combined amount is changed in the scope of/below g.When using inorganic fibre, infrared rays opacification particle, also similarly can determine combined amount.When mixing small-particle and macrobead prepare powder, with powder only compared with the situation that macrobead is formed, the tendency that visible thermal conductivity diminishes.Such as, during the macrobead of the mixing small-particle of about 10nm and about 5 μm, oarse-grained quality/(short grained quality+oarse-grained quality) is preferably made to be 0.02 ~ 0.95.When the combined amount of inorganic fibre, infrared rays opacification particle is excessive, heat insulating ability reduces sometimes, and therefore, preferred limit measures and confirms that thermal conductivity limit is appropriately prepared.Such as, mix that fiber diameter is 12 μm in silica, mean length is when being the inorganic fibre of 5mm, the combined amount of inorganic fibre is preferably below 30 quality %.Such as, when mixing median size is the infrared rays opacification particle of 2 μm in silica, the combined amount of infrared rays opacification particle is preferably below 23 quality %.In addition, when the inorganic fibre that choice for use is made up of the material that thermal conductivity is little or infrared rays opacification particle, there is the tendency of the easily mixed powder of preparation thermal conductivity in above-mentioned scope.
The containing ratio of [1-8] K, Mg, Ca, Fe, P, S
For the powder of present embodiment, from the viewpoint of dispersing of the powder that has excellent formability, reduces, preferably with the total mass of powder for benchmark, the containing ratio of K is below more than 0.005 quality % 5 quality %, the containing ratio of Mg is below more than 0.005 quality % 5 quality %, the containing ratio of Ca is below more than 0.005 quality % 2 quality %, the containing ratio of Fe is below more than 0.005 quality % 6 quality %, the containing ratio of P is below more than 0.002 quality % 1 quality %, the containing ratio of S is below more than 0.002 quality % 1 quality %.In addition, it is further preferred that the containing ratio of K be below more than 0.005 quality % 3 quality %, the containing ratio of Mg is below more than 0.005 quality % 3.5 quality %, the containing ratio of Ca is below more than 0.005 quality % 1.5 quality %, the containing ratio of Fe is below more than 0.005 quality % 3 quality %, the containing ratio of P is below more than 0.005 quality % 0.7 quality %, the containing ratio of S is below more than 0.005 quality % 0.8 quality %.And then, further preferably, the containing ratio of K is below more than 0.005 quality % 1.5 quality %, the containing ratio of Mg is below more than 0.005 quality % 2.5 quality %, the containing ratio of Ca is below more than 0.005 quality % 1 quality %, the containing ratio of Fe is below more than 0.005 quality % 2 quality %, the containing ratio of P is below more than 0.005 quality % 0.3 quality %, the containing ratio of S is below more than 0.005 quality % 0.5 quality %.The containing ratio of K, Mg, Ca, Fe, P, S in powder can pass through XRF (x-ray fluorescence analysis) and carry out quantitatively.
[2] manufacture method of powder
The manufacture method of powder preferably has following operation: by containing silicon-dioxide and median size Ds be more than 5nm and less than 30nm small-particle with containing silicon-dioxide and median size D lfor the operation that the macrobead of more than 30nm less than 50 μm mixes.Here, at least one in small-particle or macrobead can contain Na.In addition, the compound containing Na also can be added in the small-particle not containing Na, macrobead or small-particle and macrobead.
[2-1] silica dioxide granule
As silica dioxide granule, preferably use above-mentioned small-particle and/or macrobead.Silica dioxide granule can for being raw material in order to the particle with silica composition manufactured by existing manufacture method, carries out to the containing ratio of sodium, BET specific surface area, intensity of compression or thermal conductivity the particle adjusting gained.Such as, silica dioxide granule can for the particle utilizing the damp process under acidity or alkaline condition silicate ion condensation to be manufactured.Inorganic compound particle containing silicon-dioxide can for the particle utilizing damp process organoalkoxysilane hydrolytic condensation to be manufactured.Silica dioxide granule can also for the particle manufactured utilizing the silica composition of damp process manufacture to burn till.Inorganic compound particle containing silicon-dioxide can for burning the compound of the silicon such as muriate and the particle manufactured in the gas phase.Silica dioxide granule can be the silicon gaseous oxidation burning that heating silicon metal or the raw material containing silicon are obtained and the particle that manufactures.Silica dioxide granule also can for the particle making the meltings such as silica manufacture.
As the composition beyond silica composition contained in silica dioxide granule, the composition be present in as impurity in above-mentioned manufacture method in raw material can be utilized.Also the composition beyond silica composition can be added in the manufacturing process of silicon-dioxide.
For the manufacture method of known silicon-dioxide, there is following methods.
The silicon-dioxide > that < utilizes damp process to synthesize
Take water glass as the gel silica that raw material manufactures in acid condition.Take water glass as the precipitated silica that raw material manufactures in the basic conditions.The silicon-dioxide synthesized by the hydrolytic condensation of organoalkoxysilane.
The silicon-dioxide > that < utilizes drying process to synthesize
The muriate of burning silicon and the aerosil that manufactures.Burning silicon metal gas and the silicon-dioxide that manufactures.The fine silica powder of by-product such as when manufacturing ferrosilicon.Utilize the silicon-dioxide that arc process or plasma method manufacture.Make the SiO 2 powder of pulverizing melting spheroidization and the fused silica manufactured in flame.
In above-mentioned silicon-dioxide, with water glass be raw material manufacture in acid condition gel silica, the silicon-dioxide synthesized by the hydrolytic condensation of organoalkoxysilane, burning silicon muriate manufacture aerosil, silicon-dioxide that burning silicon metal gas manufactures, utilize arc process or plasma method to manufacture the containing ratio of Na of silicon-dioxide less than 0.005 quality %.Therefore, by utilizing method described later to add Na in the silicon-dioxide obtained, can as the raw material of silica dioxide granule.
Be that the intensity of compression of the precipitated silica that raw material makes in the basic conditions is more than 31% with water glass.Can by by the method beyond the precipitator method, the aerosil such as muriate of burning silicon made, burning silicon metal gas and make silicon-dioxide, manufacture ferrosilicon time etc. by-product the mixing of the silica dioxide granule such as fine silica powder and make intensity of compression be less than 31%, use as silica dioxide granule.
When manufacturing ferrosilicon etc. by-product fine silica powder, by the SiO 2 powder of pulverizing in flame melting spheroidization and the thermal conductivity of fused silica that obtains more than 0.05W/mK.Therefore, from the viewpoint of thermal conductivity, be not only preferred mode using the silicon-dioxide utilizing this manufacture method to obtain as the raw material of silica dioxide granule, but be favourable sometimes in composition.By mixing the silicon-dioxide utilizing other manufacture method to obtain, thermal conductivity can be adjusted to below 0.05W/mK, therefore, when being raw material with fine silica powder etc., preferably mix the silica dioxide granule utilizing other manufacture method to obtain.Such as, the aerosil made by the muriate of burning silicon by mixing, burning silicon metal gas and the silicon-dioxide that makes, can reduce the thermal conductivity of fine silica powder etc.
In above-mentioned silicon-dioxide, from the viewpoint of productivity and cost, more preferably use aerosil, burning silicon metal gas and the silicon-dioxide, fine silica powder, the fused silica that make.
As the inorganic compound particle containing silicon-dioxide, natural silicate minerals can be used.As natural mineral, such as, can enumerate: peridotites class, pistacite class, quartz, feldspar, zeolites etc.By implementing the process such as pulverizing to natural silicate minerals, adjustment BET specific surface area, can use as the silica dioxide granule forming powder.The containing ratio of Na insufficient or excessive time, can utilize method described later implement Na interpolation or removing process, the containing ratio of Na is adjusted to arbitrary value, as form powder silica dioxide granule use.
[2-2]Na
In the manufacture method of powder, small-particle or oarse-grained at least one can contain Na.In addition, the compound containing Na can be added in the small-particle not containing Na, macrobead or small-particle and macrobead.In addition, the mode that small-particle or macrobead are preferably below more than 0.005 quality % 3 quality % with the containing ratio of the Na in powder contains Na.For Na, in the manufacturing process of silica dioxide granule, can add with the form of the compound containing Na, also can use the silica dioxide granule of the Na in advance containing q.s.As the compound containing Na, be not particularly limited, such as, can enumerate: the oxide compound of Na, composite oxides, oxyhydroxide, nitride, carbide, carbonate, acetate, nitrate, indissoluble salt and alkoxide etc.These compounds can add separately, also can add their mixture.Using containing the Na as impurity containing the inorganic compound particle of silicon-dioxide as the raw material of powder from the viewpoint of productivity, cost, workability be preferred mode.The inorganic compound particle containing silicon-dioxide so such as the form of fine silica powder of by-product can obtain with the particle in the silica dioxide gel utilizing the precipitator method to obtain source or when manufacturing ferrosilicon etc.
The method of adding the compound respectively containing Na is not particularly limited.Such as, can be added in the above-mentioned silicon-dioxide utilizing damp process or drying process to obtain, also can add in above-mentioned each manufacturing process of silicon-dioxide.Compound containing Na can be water-soluble, also can be water insoluble.Can add with the form of the aqueous solution of the compound containing Na, and carry out drying as required, also the compound containing Na can be added with the state of solid matter or fluent meterial.Compound containing Na can be crushed to the particle diameter of regulation in advance, in addition, also can carry out coarse reduction in advance.
When silica dioxide granule contains excessive Na, some process can be implemented in the manufacturing process of the manufacturing process of silicon-dioxide or powder, the containing ratio of Na is adjusted to specialized range.The method that excessive Na is adjusted to specialized range is not particularly limited.Such as, as the inflation method of the containing ratio of Na, can enumerate and utilize acidic substance or other element to carry out the method etc. of replacing, extracting, removing, can after the inorganic compound particle nitric acid containing silicon-dioxide or chloroazotic acid etc. be processed, carry out drying, the raw material as powder uses.The adjustment of excessive Na can be carried out after the inorganic compound particle containing silicon-dioxide is crushed to target grain size in advance, also after Na is adjusted to specialized range, can pulverize silica dioxide granule again.
[2-3]K、Mg、Ca、Fe、P、S
In the manufacturing process of silicon-dioxide and the manufacturing process of powder, K, Mg, Ca, Fe, P, S can add respectively with the form of the compound containing K, Mg, Ca, Fe, P, S, also can use the inorganic compound particle containing silicon-dioxide of K, Mg, Ca, Fe, P, the S in advance containing q.s.As the compound containing K, Mg, Ca, Fe, P, S, be not particularly limited, such as, can enumerate: the oxide compound of K, Mg, Ca, Fe, P, S, composite oxides, oxyhydroxide, nitride, carbide, carbonate, acetate, nitrate, indissoluble salt and alkoxide etc.These compounds can add separately, also can add their mixture.Using containing K, Mg, Ca, Fe, P, the S as impurity containing the inorganic compound particle of silicon-dioxide as the raw material of powder from the viewpoint of productivity, cost, workability be preferred mode.The inorganic compound particle containing silicon-dioxide so such as the form of fine silica powder of by-product can obtain with the particle in the silica dioxide gel utilizing the precipitator method to obtain source or when manufacturing ferrosilicon etc.
The method of adding the compound respectively containing K, Mg, Ca, Fe, P, S is not particularly limited.Such as, can be added in the above-mentioned silicon-dioxide utilizing damp process or drying process to obtain, also can add in above-mentioned each manufacturing process of silicon-dioxide.Compound respectively containing K, Mg, Ca, Fe, P, S can be water-soluble, also can be water insoluble.Can add with the form of the aqueous solution of the compound respectively containing K, Mg, Ca, Fe, P, S, and carry out drying as required, also the compound respectively containing K, Mg, Ca, Fe, P, S can be added with the state of solid matter or fluent meterial.Compound respectively containing K, Mg, Ca, Fe, P, S can be crushed to the particle diameter of regulation in advance, in addition, also can carry out coarse reduction in advance.
When silica dioxide granule contains excessive K, Mg, Ca, Fe, P, S, some process can be implemented in the manufacturing process of the manufacturing process of silicon-dioxide or powder, the containing ratio of aforementioned elements is adjusted in specialized range.The method that excessive K, Mg, Ca, Fe, P, S adjust to specialized range is not particularly limited.As the inflation method of the containing ratio of K etc., can enumerate and utilize acidic substance or other element to carry out the method etc. of replacing, extracting, removing, can after the inorganic compound particle nitric acid containing silicon-dioxide or chloroazotic acid etc. be processed, carry out drying, the raw material as powder uses.The adjustment of excessive K, Mg, Ca, Fe, P, S can be carried out after the inorganic compound particle containing silicon-dioxide is crushed to target grain size in advance, also after K, Mg, Ca, Fe, P, S are adjusted to specialized range, can pulverize silica dioxide granule again.
[2-4] blending means
In the manufacture method of powder, preferably there is following operation: will containing silicon-dioxide and median size D sfor more than 5nm and less than 30nm small-particle with containing silicon-dioxide and median size D lfor the operation that the macrobead of more than 30nm less than 50 μm mixes.Small-particle and oarse-grained mixing can use the mixing machine recorded in known powder mixer, such as revision six editions chemical engineering handbooks (ball is apt to) to mix.At this moment, also can mixture of red outside line opacification particle, inorganic fibre or the compound mixed respectively containing Na, K, Mg, Ca, Fe, P, S or its aqueous solution.As known powder mixer, can enumerate: as container rotating type (container self rotates, vibration, shake) horizontal circle cartridge type, V-type (can with agitating vane), bicone, cubic type and shake rotary-type; As single shaft banding pattern, multiaxis slurry type, rotation rake, dual shaft planetary stirring-type, circular cone screw type, high-speed stirring type, rotary disk type, band roller rotary container type, band stirring rotary container type, the high speed elliptic rotor type of mechanical stirring (container is fixed, and stirs with blade etc.); As flowing stirring-type (utilize air, gas stir) airflow stirring type, utilize gravity to carry out without stirring-type.Also can combine these mixing machines to use.
The mixing of small-particle and macrobead, infrared rays opacification particle, inorganic fibre can use known pulverizer, such as revise record in six editions chemical engineering handbooks (ball is apt to) pulverizer pulverized particles, severing inorganic fibre, improve particle, inorganic fibre dispersiveness while carry out.At this moment, small-particle and macrobead also can be made to pulverize, disperse or make, and the compound respectively containing Na, K, Mg, Ca, Fe, P, S or its aqueous solution are pulverized, dispersion.As known pulverizer, can enumerate: roller mill (high pressure compressed roller mill, roller rotary grinder), stamp mill, crushing mill (multi-mull mixer, Chile's formula wheel roller), cut off and shear shredder (knife mill etc.), rod mill, autogenous mill (aerofall mill, cascade mill etc.), vertical roll grinder (ring roller mill, roller finishing machine, ball shredder), high-speed rotary is gone round and round a millstone (hammer mill, squirrel cage mill, pulverizer (Disintegrator), screen mill, dials formula grinding machine), grading machine internally-arranged type high-speed rotary is gone round and round a millstone (to be fixed and impacts template shredder, Scroll-type shredder, centrifugal classification type shredder, circular-gap sand mill), container driving medium shredder (rotary mill (mill,pot, tuber grinder, conical bell mill), (circular vibration grinds vibromill, rotational vibration is ground, centrifugal mill), planetary mills, centrifugal flowization is ground), media-agitation type mill (tower mill, stir slot type shredder, horizontal circulation slot type shredder, vertical circulation slot type shredder, circular-gap sand mill), jet mill (air-flow induction type, type is passed through in nozzle, conflict type, fluidised bed sprays blowing-type), (high speed centrifugation roller grinds compacting cutting mill, interior abrasive disc formula (Innerpiece formula)), mortar, grinding stone etc.Also can combine these pulverizers to use.
In these mixing machines and pulverizer, the dispersiveness that powder mixer, the high-speed rotary with agitating vane are gone round and round a millstone, grading machine internally-arranged type high-speed rotary is gone round and round a millstone, container driving medium shredder, compacting cutting mill can improve particle, inorganic fibre, therefore preferably.In order to improve the dispersiveness of particle, inorganic fibre, the circumferential speed preferably making the top of agitating vane, swivel plate, hammer plate, blade, pin etc. is more than 100km/h, is more preferably more than 200km/h, more preferably more than 300km/h.
When mixing small-particle and macrobead, preferably with the order that bulk density is ascending, silica dioxide granule is dropped in stirrer or pulverizer.During containing inorganic fibre, infrared rays opacification particle, preferably add infrared rays opacification particle after mixing small-particle and macrobead and mix, then mix adding inorganic fibre thereafter.
[2-5] manufacturing process
Powder is when for adiabatic purposes, and only can not be filled in the position using powder via operations such as shapings and directly use as molding, the material (molding) that also can obtain being shaped by powder pressing uses as thermal insulation material.It should be noted that, in press molding, powder easily condenses, such as at storage tanks hopper internal cause remaining thermal insulation material, volume density is changed, therefore, be sometimes difficult to carry out stable continuous supply, but, utilize powder of the present invention, the generation of condensing can be suppressed, easily prevent the lack of fill in mould, productivity from reducing.
When being shaped by powder pressing and manufacturing body, the current known ceramic press molding method such as mould press forming method (plunger tpe press molding method), rubber rolling process (hydrostaticpressure moulding method), extrusion molding method can be utilized to be shaped.From the viewpoint of productivity, preferred mold press forming method.
In mould press forming method or rubber rolling process, by powder filled in mould time, by making powder vibration etc. make filling become evenly, the thickness of molding can be made even, therefore preferably.While to reduce pressure in mould degassed limit by powder filled in mould time, can fill at short notice, therefore, be preferred from the viewpoint of productivity.
Molding in powder, press molding or after press molding is carried out heat drying in the condition and range of the sufficient temperature and time of thermotolerance of powder or molding, time after the planar water of removing powder or molding for practical application, thermal conductivity step-down, therefore preferably.And then, can also heat treated be implemented.
Shaping can be only press molding, but preferably carries out heat treated to the molding of press molding gained.When implementing heat treated to the molding of the gained that is shaped by powder pressing, ultimate compression strength improves, and can particularly preferably use in the purposes that load is large.
From the viewpoint of dimensional stability, heat treatment temperature is preferably the temperature also higher than the maximum operation (service) temperature of described powder or molding.Described heat treatment temperature is of all kinds according to the difference of the purposes of powder or molding, specifically, is preferably 400 ~ 1200 DEG C, is more preferably 500 ~ 1200 DEG C, more preferably 600 ~ 1200 DEG C.
The atmosphere of the heat treated of powder or molding can be enumerated in air in (or in air), oxidizing atmosphere in (oxygen, ozone, oxynitride, carbonic acid gas, hydrogen peroxide, hypochlorous acid, inorganic organo-peroxide etc.) and non-active gas atmosphere (helium, argon, nitrogen etc.).Heating treatment time is suitably selected according to the content of heat treatment temperature and thermal insulation material.Heat treated powder filledly implementing above-mentioned behind field of employment, also can be implemented the molding of the gained that is shaped by powder pressing.
[3] cladding
Cladding has powder and/or the molding that is made up of powder and storage powder and/or the outer cover material material of molding that is made up of powder.Cladding has easy process, also easy such advantage of constructing compared with powder and molding.Fig. 1 is an example of the diagrammatic cross-section of the cladding of present embodiment.In addition, Fig. 2 is the small-particle of present embodiment and an example of oarse-grained diagrammatic cross-section.As shown in Figures 1 and 2, the cladding 1 of present embodiment is made up of the outer cover material material 3 of the powder 2 (or molding) containing the large multiple macrobead L of multiple small-particle S and particle diameter ratio small-particle S and storage powder 2 (or molding).In powder 2 (or molding), small-particle S and macrobead L mixes, and there is small-particle S around macrobead L.It should be noted that, sometimes powder and/or the molding that is made up of powder are called core.
[3-1] outer cover material material
As long as outer cover material material can be received core and just be not particularly limited, as an example, can enumerate: woven fiber glass, alumina fibre cloth, the inorganic fibre fabrics such as titanium dioxide silicon cloth, inorganic fibre compiles thing, polyester film, polyethylene film, polypropylene screen, nylon membrane, polyethylene terephthalate film, the resin moldings such as fluorine resin film, plastic-metal film, aluminium foil, stainless steel foil, the tinsels such as Copper Foil, ceramic paper, inorganic fiber nonwoven fabrics, organic fibre non-woven fabrics, glass fiber paper, Carbon fibe paper, rock wool paper, inorganic fill paper, organic fibre paper, ceramic coating, fluor resin coating, the resin coatings etc. such as silicone resin coating.During using cladding as thermal insulation material, from the viewpoint of the thermal capacitance reducing outer cover material material, the preferably thinner thickness of outer cover material material, suitably can select according to behaviour in service and desirable strength etc.Outer cover material material by use core temperature under stable material form time, also for cover the powder of material storage as core or the state of molding outward during use.The situation of the cladding at high temperature used, be easy to viewpoint from using the process of rear core consider, the outer cover material material that preferred thermotolerance is high, in this specification sheets, " outer cover material material ", except receiving the material of core when comprising and use core, is also included in the material receiving core in the carrying of core, working procedure.That is, outer cover material material comprise only when carrying, construction time protection core, in use melting and/or volatilization outer cover material material, therefore, outer cover material material himself, organic composition contained in outer cover material material can melting under the use temperature of core, disappearance.
Be easy to viewpoint from coated operation consider, the sheet that the tinsels such as resin molding, plastic-metal film, aluminium foil, stainless steel foil, Copper Foil such as the inorganic fibre fabrics such as outer cover material material preferred glass cloth, alumina fibre cloth, titanium dioxide silicon cloth, inorganic fibre volume thing, polyester film, polyethylene film, polypropylene screen, nylon membrane, polyethylene terephthalate film, fluorine resin film, ceramic paper, inorganic fiber nonwoven fabrics, organic fibre non-woven fabrics, glass fiber paper, Carbon fibe paper, rock wool paper, inorganic fill paper, organic fibre paper are such.
When at high temperature using cladding, from the viewpoint of thermostability, outer cover material material is the inorganic fibre fabric such as woven fiber glass, alumina fibre cloth, titanium dioxide silicon cloth, inorganic fibre volume thing, ceramic paper, inorganic fiber nonwoven fabrics more preferably.Outer cover material material is from the viewpoint of intensity preferred inorganic fibre fabric further.
[3-2] is by the coated method of outer cover material material
For powder; can using the powder formed containing small-particle and macrobead and according to behaviour in service interpolation infrared rays opacification particle or inorganic fibre as core; be filled in the outer cover material material being processed into bag-shaped or tubulose; also this powder pressing can be shaped and make core, coated with outer cover material material.During using powder as core, the filling ratio of the volume that powder is formed relative to outer cover material material suitably can set according to using the object of powder.During using molding as core, can as described later, by powder press molding together with outer cover material material, also can be coated with outer cover material material after powder pressing is shaped.
The core method that outer cover material material is coated is not particularly limited, can implement simultaneously the preparation of core, shaping and utilize outer cover material material carry out coated, also can be coated with outer cover material material after preparing core or making it be shaped.
When outer cover material material is the lamellar morphologies such as inorganic fibre fabric, resin molding, plastic-metal film, tinsel, ceramic paper, inorganic fiber nonwoven fabrics, organic fibre non-woven fabrics, glass fiber paper, Carbon fibe paper, rock wool paper, inorganic fill paper, organic fibre paper, can by the stitching that such as utilizes inorganic fibre yarn or resin fibre yarn etc. to carry out, being adhesively fixed of outer cover material material, sew up and bonding the two carry out coated.
When the outer cover material material of sheet is resin molding, plastic-metal film, tinsel etc., from the viewpoint of the easy degree of coated operation, preferably vacuum packed, shrink packaging.
When outer cover material material is ceramic coating, resin coating etc., by being coated on core with hairbrush or sprayer, can be coated with outer cover material material by core.
The indenture of wire also can be set on the molding be made up of core and the outer cover material material of press molding gained, be given to body with flexibility.The form of line can select linearity, curve-like, dotted line shape etc. according to the behaviour in service of molding, also can combine wherein two or more.The rugosity of line, the degree of depth of indenture decide according to the thickness of molding, intensity, behaviour in service.
Outer cover material material can the whole surface of coated core, also can the part of coated core.
[4] purposes
The powder containing silica dioxide granule and Na of present embodiment, molding and cladding, except may be used for thermal insulation material, can also be preferred for the carrier, reodorant, deodorant, humidity adjusting material, weighting agent, pigment etc. of the chemical reagent such as sound absorbent material, soundproof material, sound-proof material, anti-noise-reflecting material, quieter material, abrasive, support of the catalyst, sorbent material, absorption perfume compound and sterilant.
[5] mensuration of parameter
The mensuration of the containing ratio of the Na of powder, BET specific surface area mensuration, the mensuration of intensity of compression, the mensuration of thermal conductivity utilize following method to implement.
[mensuration of the containing ratio of Na]
Powder agate mortar is pulverized, is filled in in vinylchlorid ring, carry out press molding with XRF tablet former, make tablet, as working sample.With Co., Ltd. Neo-Confucianism fluorescent x-ray analyzer RIX-3000, it is measured.The situation of molding too, by after making the size that loads in agate mortar, can be pulverized with agate mortar, similarly measures the containing ratio of Na.
[BET specific surface area of thermal insulation material measures]
Utilize gas adsorption amount determining device " Autosorb3MP " (trade(brand)name) of Yuasaionics Inc., use nitrogen as adsorbed gas, measure the specific surface area (nitrogen adsorption method) of powder.Specific surface area adopts BET method.
[mensuration of intensity of compression]
Intensity of compression (%) is by measuring loose packing volume density and fine and close packing volume density and respective measured value being brought in following formula (1) and obtain.
Intensity of compression=100 × (fine and close packing volume density-loose packing volume density)/fine and close packing volume density (1)
The measuring method of loose packing volume density: the loose packing volume density gauge MVD-86 model using cylinder well Physicochemical apparatus Co., Ltd., carry out electric and magnetic oscillation, by the sieve that aperture is 500 μm, make sample dispersion, fall and put in the sampling receptacle of 100mL.After sample load terminates, with striking off doctor blade, gravimetry, bulk density, using the value that obtains as loose packing volume density.
The measuring method of close packing volume density: load onto connection cylinder frame in the sampling receptacle of 100mL, after filling up powder in cylinder frame, be installed on the shaking table of fine and close packing volume density gauge VBD-2 model of well Physicochemical apparatus Co., Ltd., vibration is not until powder sinks.After vibration terminates, with striking off doctor blade sampling receptacle, gravimetry, bulk density, using the value that obtains as fine and close packing volume density.
[mensuration of thermal conductivity]
The central part of the polystyrene foamed of length 30cm, width 30cm, thickness 5cm is cut a hole into the square of length 24cm, width 24cm, form the frame of polystyrene foamed.Attach the aluminium foil of length 30cm, width 30cm in the side of frame, form recess, as sample table.It should be noted that, using the bottom surface of the face of aluminium foil covering as sample table, using the another side relative with the thickness direction of polystyrene foamed as end face.Completely fill recess by flat for powder, then put the aluminium foil of length 30cm, width 30cm at end face, using gained material as working sample.Use working sample, according to JISA1412-2, use heat flowmeter HFM436Lambda (trade(brand)name, NETZSCH Inc.) measures the thermal conductivity at 30 DEG C.Calibration uses density 163.12kg/m 3, thickness 25.32mm NISTSRM1450c calibration standard plate, under the temperature head of high temperature side and low temperature side is the condition of 20 DEG C, implement at 15,20,24,30,40,50,60,65 DEG C in advance.When measuring molding, using be configured as length 30cm, width 30cm, thickness 20mm the molding of shape as working sample.Thermal conductivity at 800 DEG C measures based on the method for JISA1421-1.2 are made diameter 30cm, thickness 20mm discoideus molding as working sample, use protection hot plate method measuring thermal conductivity device (Eko Instruments Trading's system) as determinator.
Embodiment
Below, utilize embodiment to illustrate in greater detail the present invention, but the present invention is not limited to these embodiments.Those skilled in the art can carry out various change to the content comprising embodiment shown below and implement, and the change carried out is also contained in the scope of Patent right requirement of the present invention.It should be noted that, the mensuration of the mensuration of BET specific surface area of the powder in embodiment and comparative example, the mensuration of the containing ratio of Na, thermal conductivity, the mensuration of intensity of compression is as described above respectively carries out.
reference example 1
Be 125m in BET specific surface area 2/ g and Na containing ratio is the NaOH aqueous solution adding 0.5mol/L in the silicon-dioxide powdery of 0 quality %, mixes, makes the containing ratio of the Na of silicon-dioxide powdery be 0.53 quality % in rotary crusher.The intensity of compression of this silicon-dioxide powdery is the thermal conductivity at 11%, 30 DEG C is 0.0203W/mK.Use this silicon-dioxide powdery 407g, with interior dimensions be length 30cm, the mould of width 30cm carries out press molding, obtains the molding of length 30cm, width 30cm, thickness 20mm.Thermal conductivity at 30 DEG C of molding is 0.0201W/mK.It should be noted that, the median size of silicon-dioxide powdery is 22nm.When silicon-dioxide powdery with reference to example 1 drops in hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.It should be noted that so-called silicon-dioxide powdery refers to the powder containing silica dioxide granule, identical below.
embodiment 2
Hammer mill is used to be 364m by BET specific surface area 2/ g and Na containing ratio be 0% silicon-dioxide powdery (small-particle) 90 quality % and BET specific surface area be 0.04m 2/ g and silicon-dioxide powdery (macrobead) the 10 quality % that Na containing ratio is 10% mix, and obtain the silicon-dioxide powdery of embodiment 2.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 0.97 quality %, 327m 2/ g, 12%, the thermal conductivity at 30 DEG C is 0.0200W/mK.Use this silicon-dioxide powdery 421g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.Thermal conductivity at 30 DEG C of molding is 0.0205W/mK.It should be noted that, short grained median size D sfor 7.5nm, oarse-grained median size D lit is 60 μm.When the silicon-dioxide powdery of embodiment 2 is dropped into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
reference example 3
Be 195m in BET specific surface area 2/ g and Na containing ratio is the NaOH aqueous solution adding 0.5mol/L in the silicon-dioxide powdery of 0 quality %, mixes, makes the containing ratio of the Na of the silicon-dioxide powdery in reference example 3 be 2.9 quality % in ball mill.The intensity of compression of this silicon-dioxide powdery is the thermal conductivity at 9%, 30 DEG C is 0.0191W/mK.Use this silicon-dioxide powdery 331g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, the median size of silicon-dioxide powdery is 14nm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0191W/mK.When silicon-dioxide powdery with reference to example 3 drops into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
embodiment 4
Hammer mill is used to be 364m by BET specific surface area 2/ g and Na containing ratio be 0% silicon-dioxide powdery (small-particle) 25 quality % and BET specific surface area be 0.46m 2/ g and silicon-dioxide powdery (macrobead) the 75 quality % that Na containing ratio is 0.1% mix, and obtain the silicon-dioxide powdery of embodiment 4.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 0.074 quality %, 91m 2/ g, 29%, the thermal conductivity at 30 DEG C is 0.0297W/mK.Use this silicon-dioxide powdery 936g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, short grained median size D sfor 7.5nm, oarse-grained median size D lit is 6 μm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0301W/mK.When the silicon-dioxide powdery of embodiment 4 is dropped into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
embodiment 5
Be 195m by BET specific surface area 2/ g and Na containing ratio be 0% silicon-dioxide powdery (small-particle) 50 quality % and BET specific surface area be 18m 2/ g and silicon-dioxide powdery (macrobead) the 50 quality % that Na containing ratio is 0.34 quality % mix in hammer mill, obtain the silicon-dioxide powdery of embodiment 5.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 0.17 quality %, 106m2/g, 15%, the thermal conductivity at 30 DEG C is 0.0214W/mK.Use this silicon-dioxide powdery 576g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, short grained median size D sfor 14nm, oarse-grained median size D lfor 150nm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0211W/mK.When the silicon-dioxide powdery of embodiment 5 is dropped into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
embodiment 6
Hammer mill is used to be 364m by BET specific surface area 2/ g and Na containing ratio be 0% silicon-dioxide powdery (small-particle) 40 quality % and BET specific surface area be 45m 2silicon-dioxide powdery (macrobead) the 60 quality % that/g and Na containing ratio are 0.273%, intensity of compression is 35% mixes, and obtains the silicon-dioxide powdery of embodiment 6.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 0.16 quality %, 172m 2/ g, 27%, the thermal conductivity at 30 DEG C is 0.0281W/mK.Use this silicon-dioxide powdery 594g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, short grained median size D sfor 7.5nm, oarse-grained median size D lfor 80nm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0285W/mK.When the silicon-dioxide powdery of embodiment 6 is dropped into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
embodiment 7
Be 195m by BET specific surface area 2/ g and Na containing ratio are silicon-dioxide powdery (small-particle) the 25 quality % of 0 quality % and BET specific surface area is 0.23m 2after/g and silicon-dioxide powdery (macrobead) the 75 quality % that Na containing ratio is 0 quality % mix in rotary crusher, add the NaOH aqueous solution of 0.5mol/L, mix in rotary crusher again, the containing ratio obtaining Na is 0.009 quality %, BET specific surface area is 49m 2the silicon-dioxide powdery of the embodiment 7 of/g.The intensity of compression of this silicon-dioxide powdery is the thermal conductivity at 26%, 30 DEG C is 0.0313W/mK.Use this silicon-dioxide powdery 1267g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, short grained median size D sfor 14nm, oarse-grained median size D lit is 10 μm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0314W/mK.When the silicon-dioxide powdery of embodiment 7 is dropped into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
reference example 8
Be 0.030 quality % by the containing ratio of Na, BET specific surface area is 9m 2the silicon-dioxide powdery of/g is pulverized in airflow milling, makes BET specific surface area be 13m 2/ g, obtains the silicon-dioxide powdery of reference example 8.The intensity of compression of this silicon-dioxide powdery is the thermal conductivity at 24%, 30 DEG C is 0.0441W/mK.Use this silicon-dioxide powdery 1978g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, the median size of silicon-dioxide powdery is 210nm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0445W/mK.When silicon-dioxide powdery with reference to example 8 drops into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
reference example 9
With nitric acid to the containing ratio of Na be 4.15 quality %, BET specific surface area is 111m 2the silicon-dioxide powdery of/g carries out pickling, and the containing ratio making Na is 2.3%, obtains the silicon-dioxide powdery of reference example 9.The intensity of compression of this silicon-dioxide powdery is the thermal conductivity at 20%, 30 DEG C is 0.0223W/mK.Use this silicon-dioxide powdery 702g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, the median size of silicon-dioxide powdery is 25nm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0225W/mK.When silicon-dioxide powdery with reference to example 9 drops into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
embodiment 10
Be 195m by BET specific surface area 2/ g and Na containing ratio are silicon-dioxide powdery (small-particle) the 20 quality % of 0 quality % and BET specific surface area is 0.46m 2after/g and silicon-dioxide powdery (macrobead) the 60 quality % that Na containing ratio is 0.1% mix in hammer mill, add the zirconium silicate 15 quality % as infrared rays opacification particle that median size is 1 μm, proceed Homogeneous phase mixing, add fiber diameter again and be 11 μm and average fiber length is the glass fibre 5 quality % of 6.4mm, mix in high shear mixers, obtain the silicon-dioxide powdery of embodiment 10.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 0.063 quality %, 39m 2/ g, 10%, the thermal conductivity at 30 DEG C is 0.0315W/mK.Use this silicon-dioxide powdery 491g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.It should be noted that, short grained median size D sfor 14nm, oarse-grained median size D lit is 6 μm.In addition, the thermal conductivity at 30 DEG C of molding is 0.0311W/mK.When the silicon-dioxide powdery of embodiment 10 is dropped into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
reference example 11
The sodium nitrate aqueous solution of 0.5mol/L is slowly added drop-wise to silicon dioxide gel solution (Nissan Chemical Inc., trade(brand)name " Snowtex40 ", the SiO of the colloidal particle size 10 ~ 20nm of the whipped state remaining on 15 DEG C 2containing ratio: 40 quality %) in, obtain the mixed slurry of silicon dioxide gel, SODIUMNITRATE.Thereafter, be set as that the spray drying unit of 130 DEG C carries out spraying dry to mixed slurry by temperature out, obtain solid matter.Then, by the solid matter that obtains in electric furnace with 2 hours after room temperature to 300 DEG C, keep 3 hours at 300 DEG C.After being warming up to 550 DEG C with 2 hours again, after at 550 DEG C, maintenance is burnt till for 3 hours, Slow cooling, obtains the silicon-dioxide powdery of reference example 11.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 1.7 quality %, 132m 2/ g, 29%, the thermal conductivity at 30 DEG C is 0.0339W/mK.Use this silicon-dioxide powdery 990g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.Thermal conductivity at 30 DEG C of molding is 0.0341W/mK.When silicon-dioxide powdery with reference to example 11 drops into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
embodiment 12
Hammer mill is used to be 195m by BET specific surface area 2/ g and Na containing ratio are silicon-dioxide powdery (small-particle) the 21 quality % of 0 quality % and BET specific surface area is 18m 2after/g and silicon-dioxide powdery (macrobead) the 63 quality % that Na containing ratio is 0.34% mix, add the zirconium silicate 16 quality % as infrared rays opacification particle that median size is 1 μm, proceed Homogeneous phase mixing, obtain the silicon-dioxide powdery of embodiment 12.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 0.22 quality %, 52m 2/ g, 17%, the thermal conductivity at 30 DEG C is 0.0273W/mK.Use this silicon-dioxide powdery 1042g, carry out press molding in the same manner as reference example 1, obtain the molding of length 30cm, width 30cm, thickness 20mm.Thermal conductivity at 30 DEG C of molding is 0.0275W/mK.In addition, each this silicon-dioxide powdery of use 819g, uses the round tube type mould that internal diameter is diameter 30cm to carry out press molding, obtains the discoideus molding of 2 diameter 30cm, thickness 20mm.Use this 2 moldinies, the thermal conductivity at measuring 800 DEG C is 0.0851W/mK.It should be noted that, short grained median size D sfor 14nm, oarse-grained median size D lfor 150nm.When the silicon-dioxide powdery of embodiment 12 is dropped into hopper, dispersing of powder is few.When supplying to mould, powder cohesion ground can not occur and stably supply, and there is not forming defects in the molding obtained.
Table 1 represents the containing ratio of K in the powder of reference example 1,3,8,9,11 and embodiment 2,4,5 ~ 7,10,12 etc.
table 1
comparative example 1
The containing ratio of Na is 0 quality %, BET specific surface area is 68m 2/ g, intensity of compression be 37% the thermal conductivity of silicon-dioxide powdery at 30 DEG C be 0.0411W/mK.Use this silicon-dioxide powdery 787g, carry out press molding in the same manner as reference example 1, wish to get the molding of length 30cm, width 30cm, thickness 20mm, but when the silicon-dioxide powdery of comparative example 1 is dropped into hopper, powder disperses seriously.When supplying to mould, powder cohesion occurs, and there is difference in feed rate, forming defects appears in the molding obtained.Further, when taking out from mould, a part for molding is damaged.It should be noted that, the median size of silicon-dioxide powdery is 40nm.
comparative example 2
The containing ratio of Na is 4.15 quality %, BET specific surface area is 111m 2/ g, intensity of compression be 23% the thermal conductivity of silicon-dioxide powdery at 30 DEG C be 0.0252W/mK.Use this silicon-dioxide powdery 702g, carry out press molding in the same manner as reference example 1, wish to get the molding of length 30cm, width 30cm, thickness 20mm, but when the silicon-dioxide powdery of comparative example 2 is dropped into hopper, powder disperses.The molding obtained is highly brittle, damaged when taking out from mould.It should be noted that, the median size of silicon-dioxide powdery is 25nm.
comparative example 3
Be 195m by BET specific surface area 2to be the silicon-dioxide powdery 80 quality % of 0 quality % and median size be for/g and Na containing ratio after the zirconium silicate 15 quality % as infrared rays opacification particle of 1 μm mixes in hammer mill, add fiber diameter again and be 11 μm and average fiber length is the glass fibre 5 quality % of 6.4mm, mix in high shear mixers, obtain the silicon-dioxide powdery of comparative example 3.Measure the containing ratio of the Na of this silicon-dioxide powdery, BET specific surface area, intensity of compression, be respectively 0.003 quality %, 156m 2/ g, 9%, the thermal conductivity at 30 DEG C is 0.0219W/mK.Use this silicon-dioxide powdery 409g, carry out press molding in the same manner as reference example 1, wish to get the molding of length 30cm, width 30cm, thickness 20mm, but when the silicon-dioxide powdery of comparative example 3 is dropped into hopper, powder disperses seriously.There is forming defects in the molding obtained.It should be noted that, the median size of silicon-dioxide powdery is 14nm.
comparative example 4
The containing ratio of Na is 0.27 quality %, BET specific surface area is 45m 2/ g, intensity of compression be 35% the thermal conductivity of silicon-dioxide powdery at 30 DEG C be 0.0313W/mK.Use this silicon-dioxide powdery 614g, carry out press molding in the same manner as reference example 1, wish to get the molding of length 30cm, width 30cm, thickness 20mm, but when the silicon-dioxide powdery of comparative example 4 is dropped into hopper, powder disperses, and powder cohesion, be difficult to stably supply.There is forming defects in the molding obtained.It should be noted that, the median size of silicon-dioxide powdery is 80nm.

Claims (77)

1. a thermal insulation material powder, it contains:
Containing silicon-dioxide and median size D sfor more than 5nm and less than the small-particle of 30nm;
Containing silicon-dioxide and median size D lfor the macrobead of more than 30nm less than 50 μm; With,
Sodium, the containing ratio of described sodium is below more than 0.005 quality % 3 quality %,
BET specific surface area is 10m 2/ more than g 400m 2/ below g, intensity of compression is less than 31%, and the thermal conductivity at 30 DEG C is below 0.05W/mK.
2. powder according to claim 1, wherein, containing potassium, the containing ratio of described potassium is below more than 0.005 quality % 5 quality %.
3. powder according to claim 1, wherein, containing magnesium, the containing ratio of described magnesium is below more than 0.005 quality % 5 quality %.
4. powder according to claim 2, wherein, containing magnesium, the containing ratio of described magnesium is below more than 0.005 quality % 5 quality %.
5. the powder according to any one of Claims 1 to 4, wherein, containing calcium, the containing ratio of described calcium is below more than 0.005 quality % 2 quality %.
6. the powder according to any one of Claims 1 to 4, wherein, containing iron, the containing ratio of described iron is below more than 0.005 quality % 6 quality %.
7. powder according to claim 5, wherein, containing iron, the containing ratio of described iron is below more than 0.005 quality % 6 quality %.
8. the powder according to any one of Claims 1 to 4, wherein, containing phosphorus, the containing ratio of described phosphorus is below more than 0.002 quality % 1 quality %.
9. powder according to claim 5, wherein, containing phosphorus, the containing ratio of described phosphorus is below more than 0.002 quality % 1 quality %.
10. powder according to claim 6, wherein, containing phosphorus, the containing ratio of described phosphorus is below more than 0.002 quality % 1 quality %.
11. powders according to claim 7, wherein, containing phosphorus, the containing ratio of described phosphorus is below more than 0.002 quality % 1 quality %.
12. powders according to any one of Claims 1 to 4, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
13. powders according to claim 5, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
14. powders according to claim 6, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
15. powders according to claim 7, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
16. powders according to claim 8, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
17. powders according to claim 9, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
18. powders according to claim 10, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
19. powders according to claim 11, wherein, containing sulphur, the containing ratio of described sulphur is below more than 0.002 quality % 1 quality %.
20. powders according to any one of Claims 1 to 4, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
21. powders according to claim 5, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
22. powders according to claim 6, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
23. powders according to claim 7, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
24. powders according to claim 8, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
25. powders according to claim 9, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
26. powders according to claim 10, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
27. powders according to claim 11, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
28. powders according to claim 12, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
29. powders according to claim 13, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
30. powders according to claim 14, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
31. powders according to claim 15, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
32. powders according to claim 16, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
33. powders according to claim 17, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
34. powders according to claim 18, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
35. powders according to claim 19, wherein, further containing inorganic fibre, the containing ratio of described inorganic fibre is below more than 0.1 quality % 50 quality %.
36. powders according to any one of Claims 1 to 4, wherein, be the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
37. powders according to claim 5 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
38. powders according to claim 6 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
39. powders according to claim 7 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
40. powders according to claim 8 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
41. powders according to claim 9 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
42. powders according to claim 10 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
43. powders according to claim 11 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
44. powders according to claim 12 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
45. powders according to claim 13 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
46. powders according to claim 14 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
47. powders according to claim 15 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
48. powders according to claim 16 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
49. powders according to claim 17 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
50. powders according to claim 18 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
51. powders according to claim 19 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
52. powders according to claim 20 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
53. powders according to claim 21 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
54. powders according to claim 22 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
55. powders according to claim 23 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
56. powders according to claim 24 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
57. powders according to claim 25 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
58. powders according to claim 26 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
59. powders according to claim 27 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
60. powders according to claim 28 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
61. powders according to claim 29 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
62. powders according to claim 30 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
63. powders according to claim 31 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
64. powders according to claim 32 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
65. powders according to claim 33 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
66. powders according to claim 34 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
67. powders according to claim 35 wherein, are the infrared rays opacification particle of more than 0.5 μm less than 30 μm containing median size further, and the containing ratio of described infrared rays opacification particle is more than 0 quality % and be below 49.5 quality %.
68. powders according to claim 36, wherein, the thermal conductivity at 800 DEG C is below 0.15W/mK.
69. powders according to any one of claim 52 ~ 67, wherein, the thermal conductivity at 800 DEG C is below 0.15W/mK.
70. powders according to claim 20, wherein, described inorganic fibre has bio-soluble.
71. powders according to any one in claim 21 ~ 35 or 52 ~ 67, wherein, described inorganic fibre has bio-soluble.
72. powders according to claim 69, wherein, described inorganic fibre has bio-soluble.
73. 1 kinds of thermal insulation material moldinies, it contains the thermal insulation material powder according to any one of claim 1 ~ 72.
74. 1 kinds of thermal insulation material claddings, it possesses outer cover material material,
Described cladding is accommodated in described outer cover material material the thermal insulation material powder according to any one of claim 1 ~ 72 and/or the thermal insulation material molding described in claim 73.
75. according to the thermal insulation material cladding described in claim 74, and wherein, described outer cover material material contains inorganic fibre.
76. according to the thermal insulation material cladding described in claim 74, and wherein, described outer cover material material is resin molding.
The manufacture method of 77. 1 kinds of thermal insulation material powders, the manufacture method of its thermal insulation material powder according to any one of claim 1 ~ 72, wherein, has following operation: will containing silicon-dioxide and median size D sfor more than 5nm and less than the small-particle of 30nm with containing silicon-dioxide and median size D lfor the operation that the macrobead of more than 30nm less than 50 μm mixes, at least one in described small-particle or macrobead contains sodium.
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* Cited by examiner, † Cited by third party
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CN101193835A (en) * 2005-05-31 2008-06-04 先进玻璃陶瓷公司 Heat insulating composite and methods of manufacturing thereof
CN102040367A (en) * 2009-10-16 2011-05-04 霓佳斯株式会社 Thermal insulation material and method of producing the same

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101193835A (en) * 2005-05-31 2008-06-04 先进玻璃陶瓷公司 Heat insulating composite and methods of manufacturing thereof
CN102040367A (en) * 2009-10-16 2011-05-04 霓佳斯株式会社 Thermal insulation material and method of producing the same

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