CN110252156B - Metal composite ceramic membrane and preparation method thereof - Google Patents

Metal composite ceramic membrane and preparation method thereof Download PDF

Info

Publication number
CN110252156B
CN110252156B CN201910616011.5A CN201910616011A CN110252156B CN 110252156 B CN110252156 B CN 110252156B CN 201910616011 A CN201910616011 A CN 201910616011A CN 110252156 B CN110252156 B CN 110252156B
Authority
CN
China
Prior art keywords
layer
ceramic
composite ceramic
powder
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201910616011.5A
Other languages
Chinese (zh)
Other versions
CN110252156A (en
Inventor
谢志成
黄德友
曾胜彬
袁年武
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hunan Zhong Tian Yuan Environmental Engineering Ltd
Original Assignee
Hunan Zhong Tian Yuan Environmental Engineering Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hunan Zhong Tian Yuan Environmental Engineering Ltd filed Critical Hunan Zhong Tian Yuan Environmental Engineering Ltd
Priority to CN201910616011.5A priority Critical patent/CN110252156B/en
Publication of CN110252156A publication Critical patent/CN110252156A/en
Application granted granted Critical
Publication of CN110252156B publication Critical patent/CN110252156B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0039Inorganic membrane manufacture
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0039Inorganic membrane manufacture
    • B01D67/0041Inorganic membrane manufacture by agglomeration of particles in the dry state
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12Composite membranes; Ultra-thin membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • B01D71/022Metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • B01D71/024Oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • B01D71/024Oxides
    • B01D71/025Aluminium oxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/02Inorganic material
    • B01D71/024Oxides
    • B01D71/027Silicium oxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/02Details relating to pores or porosity of the membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/04Characteristic thickness
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/22Thermal or heat-resistance properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/24Mechanical properties, e.g. strength

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Filtering Materials (AREA)

Abstract

A metal composite ceramic membrane and a preparation method thereof, wherein the ceramic membrane sequentially comprises a substrate layer, a transition layer and a precision layer; the substrate layer is sintered by elemental metal or alloy powder; the transition layer is a composite layer sintered by elemental metal or alloy powder and composite ceramic or mixed ceramic powder; the precision layer comprises a porous ceramic filter layer sintered by composite ceramic or mixed ceramic powder. The method comprises the following steps: (1) adding a forming agent into the elemental metal or alloy powder, mixing, casting and sintering to obtain a substrate layer; (2) mixing simple substance metal or alloy powder with composite ceramic or mixed ceramic powder, casting the mixture onto a substrate layer, and sintering to form a transition layer; (3) and spraying the composite ceramic or the mixed ceramic powder on the transition layer, and sintering to obtain the ceramic material. The ceramic membrane has the advantages of high filtration precision, large flux, uniform aperture, high toughness, good thermal shock resistance, high mechanical strength and easy back flushing and cleaning. The method is simple, low in cost and suitable for industrial production.

Description

Metal composite ceramic membrane and preparation method thereof
Technical Field
The invention relates to a ceramic membrane and a preparation method thereof, in particular to a metal composite ceramic membrane and a preparation method thereof.
Background
The requirements of the filtration and separation industry on the filtration material are that the filtration flow is improved as much as possible, and the filtration resistance of the filter is reduced, so that the production energy consumption is reduced. However, for filters, there is often a contradiction: the filter material gap of the filter element is large, so that high filtering flux can be obtained, but the filtering precision is relatively reduced. The high-precision filter material needs to improve the filtering precision of the filter material to submicron or even nanometer level, and the filtering flux is inevitably reduced.
In the prior art, a nano-grade precision ceramic filter element obtained by sintering a ceramic material is adopted to obtain a high-precision filter element. However, such a filter element has the characteristics of large brittleness, poor thermal shock resistance and low mechanical strength of porous ceramics. Traditional ceramic filter core is very high because the filter fineness of superficial layer, very easily by the colloidal particle in the solution because of the relatively compact cake layer of bridging effect formation, in case form the permanent cake layer of colloidal property, can lead to periodic blowback washing to become invalid, finally arouses that filtration system can't normally filter.
CN102659447A and CN105693276A disclose a method for producing pure silicon carbide ceramic, and the filter element produced by the method belongs to the traditional method for producing ceramic filter elements, and still has the problems of large brittleness, thermal shock resistance and easy breakage of the traditional ceramic filter element.
CN102500245A discloses a preparation method of a metal-based ceramic composite filter membrane, which is to anodically oxidize a porous metal membrane in electrolyte to obtain a transition layer, and then prepare ceramic powder into slurry to be coated on the transition layer to obtain the composite filter element. In fact, the transition layer obtained by oxidation and the subsequent ceramic layer are used as oxide layers, the micro interface of the product after high-temperature sintering belongs to metal and is directly transited to the ceramic coating, and thus the filter element with the structure can directly cause the peeling failure of the ceramic coating due to the inconsistent expansion coefficients of the metal and the ceramic in the variable-temperature environment. The filter element product is a process from high temperature to normal temperature in the sintering process, and the qualified product can hardly be produced in large batch by adopting the method. Therefore, the method does not completely solve the problem of peeling of the metal layer and the ceramic layer under temperature stress.
CN109364583A discloses a Ti-Ti for industrial purification6Si4The preparation method of the external wall light type metal filtering membrane pipe material comprises the step of co-sintering metal titanium powder and metal silicon powder to obtain metal titanium/Ti6Si4A metal ceramic composite filter element. However, this method has a problem that the application range is limited: first, the method is applicable only to metallic titanium and Ti6Si4The compounding of metal compounds is not effective for the compounding of other metal and ceramic powder, and particularly when a filtering system contains fluoride ions and a strong alkaline medium, the filter element is easy to corrode and damage; secondly, the raw materials of metallic titanium powder and metallic silicon powder for producing the filter element are difficult to obtainWhen the nano-precision raw material is required to be prepared, the method is difficult to solve the problem of high precision; thirdly, the method adopts an isostatic pressing process to prepare the composite filter element, and the thickness of the filter element, particularly the thickness of a precision filter layer, cannot be very thin, so that the filtering flux of a product is small, and the back blowing effect is poor.
In summary, a metal ceramic composite filter membrane technology is needed to overcome the defects of the traditional ceramic filter core, such as high brittleness, poor thermal shock resistance, low mechanical strength, poor back flushing performance and the like.
Disclosure of Invention
The technical problem to be solved by the invention is to overcome the defects in the prior art and provide a metal composite ceramic membrane which has high filtration precision, large filtration flux, uniform pore diameter, thin thickness, high toughness, good thermal shock resistance, high mechanical strength, easy back flushing and cleaning, complete elimination of thermal stress damage and wide application range.
The invention further aims to solve the technical problem of overcoming the defects in the prior art and provide a preparation method of the metal composite ceramic membrane, which has simple process and low cost and is suitable for industrial production.
The technical scheme adopted by the invention for solving the technical problems is as follows: a metal composite ceramic membrane sequentially comprises a substrate layer, a transition layer and a precision layer; the substrate layer is formed by sintering elemental metal or alloy powder; the transition layer is a composite layer formed by sintering elemental metal or alloy powder and composite ceramic or mixed ceramic powder; the precision layer comprises a porous ceramic filter layer sintered by composite ceramic or mixed ceramic powder. The metal substrate layer mainly plays a role in improving the mechanical strength and toughness of the filter membrane and preventing the filter element from being broken; the transition layer plays a role in smoothing the bonding stress between the metal substrate layer and the ceramic layer, and the thermal shock resistance of the filter element is improved; the precision layer is a ceramic layer and mainly provides high filtration precision of the filter membrane, and the filtration precision of the precision layer is equal to that of the ceramic filter membrane.
Preferably, the mass ratio of the base layer to the transition layer to the precision layer is 40-90: 30-80: 0.2-20. If the mass of the substrate layer is too large or too thick, the filtration resistance of the filter membrane is increased, and if the mass of the substrate layer is too small or too thin, the strength of the filter membrane is insufficient and the filter membrane is easy to break; if the mass of the transition layer is too large or too thick, the number of layers is too large, so that the production cost is increased, and if the mass of the transition layer is too small or too thin, the number of layers is too small, so that the stress between the metal layer and the ceramic layer is difficult to effectively eliminate; if the mass of the precision layer is too large or too thick, the resistance of the filter membrane is increased, and if the mass of the precision layer is too small or too thin, the sintering defects therein are difficult to completely eliminate.
Preferably, in the transition layer, the mass ratio of the simple substance metal or alloy powder to the composite ceramic or mixed ceramic powder is 95-5: 5-95. The metal filter membrane has the characteristics of high strength, good toughness and the like, but the filtering precision of the filter element is not easy to improve; the ceramic filter element has large brittleness and low thermal shock resistance, and the filter element with nanometer precision can be easily prepared. If the two are combined, the advantages of the two can be effectively exerted, and the defects of the two can be avoided.
Preferably, the thickness ratio of the base layer to the transition layer to the precision layer is 0.5-2.0: 0.1-1.5: 0.01-0.10 (more preferably 0.8-1.8: 0.3-1.3: 0.02-0.08).
Preferably, the transition layer consists of 1-10 layers (more preferably 2-6 layers). If the number of layers of the transition layer is too small, it is difficult to effectively eliminate the bonding stress, and if the number of layers of the transition layer is too large, the production cost is greatly increased.
Preferably, in each layer of the transition layer, the mass ratio of the simple substance metal or the alloy to the composite ceramic or the mixed ceramic is reduced from the base layer to the precision layer by layer. The design principle of the transition layer of the invention is as follows: through multilayer preparation to make metal content as high as possible in the transition layer near metal substrate layer, the transition layer ceramic content that is close to accurate porous ceramic filter layer simultaneously is as high as possible, makes the metal composition and the ceramic composition of filter core all be gradient distribution in both sides, and the proportion change of content is smooth between metal and the pottery, and structural component is more close the bonding stress just lower, thereby effectively reduces the bonding stress of metal substrate layer and accurate ceramic layer.
Preferably, the thickness of each layer in the transition layer is 10 to 1500 μm (more preferably 100 to 1000 μm). If the transition layer is too thick, the production cost may be increased, and if the transition layer is too thin, it may be difficult to effectively eliminate the stress between the metal layer and the ceramic layer.
Preferably, in the precision layer, the thickness of the porous ceramic filter layer is 1-100 μm. If the precision layer is too thick, the resistance of the filter membrane increases, and if the precision layer is too thin, the sintering defects therein are difficult to completely eliminate.
Preferably, the average pore size of the porous ceramic filter layer is 5-100 nm.
Preferably, in the base layer and the transition layer, the elemental metal is elemental iron, elemental nickel, elemental copper, elemental titanium, or the like.
Preferably, in the base layer and the transition layer, the alloy is stainless steel, hastelloy or iron-chromium-aluminum alloy or the like.
Preferably, in the base layer, the average particle size of the elemental metal or alloy powder is 30-800 meshes. If the metal particle size of the base layer is too small, the sintered product has large voids and high flux, but the mechanical strength is too low, and if the metal particle size of the base layer is too large, the sintered product has high strength, but the voids are small and the filtration flux is too low.
Preferably, in the transition layer, the average particle size of the elemental metal or alloy powder is 30-2000 meshes. Since the melting point of the ceramic is higher than that of the metal, in order to match the temperature at which the metal powder and the ceramic powder are sintered together in the transition layer, the ceramic powder needs to be finer, and the corresponding particles of the metal powder need to be coarser.
Preferably, in the transition layer and the precision layer, the composite ceramic is one or more of oxide ceramic, nitride ceramic, carbide ceramic, boride ceramic, silicide ceramic or metal crystal compound. More preferably, the composite oxide ceramic is an alumina/silica composite ceramic, an alumina/zirconia composite ceramic, a zirconia/yttria composite ceramic, or the like.
Preferably, in the transition layer and the precision layer, the mixed ceramic is one or a mixture of several of oxide ceramic, nitride ceramic, carbide ceramic, boride ceramic, silicide ceramic, metal crystal compound and the like. More preferably, the mixed oxide ceramic is an aluminum nitride-silicon nitride mixed ceramic, a zirconia-alumina mixed ceramic, a silica-zirconia mixed ceramic, or the like.
Preferably, in the transition layer, the average particle size of the composite ceramic or mixed ceramic powder is 300-10000 meshes (more preferably 800-8000 meshes).
Preferably, in the precision layer, the average grain diameter of the composite ceramic or mixed ceramic powder is 2000-10000 meshes. The porous ceramic filter layer is required to have the highest filtering accuracy, and therefore, the selected ceramic particle size is also finer.
Preferably, the precision layer further comprises a ceramic particle modifying layer arranged outside the porous ceramic filter layer. The porous ceramic filter layer sintered by the composite ceramic or the mixed ceramic powder has certain sintering defects, and the gel is soaked in the ceramic particle modification layer formed on the surface of the ceramic layer, so that partial gel is absorbed by local sintering cracks of the porous ceramic filter layer under the capillary action, the sintering defects disappear, and finally the filtering precision of the filter membrane is improved.
Preferably, the mass ratio of the ceramic particle modification layer to the porous ceramic filter layer is 0.04-0.45: 1. The ceramic particle modification layer has the main function of repairing sintering defects generated in the preparation process of the porous ceramic filter layer, if the mass is too large or the thickness is too thick, the filtering flux can be reduced, and if the mass is too small or the thickness is too thin, the effect of eliminating the sintering defects of the ceramic layer is difficult to achieve.
Preferably, the ceramic particle modification layer is composed of 1-4 layers.
Preferably, the thickness of each layer in the ceramic particle modification layer is 1-30 μm.
Preferably, the ceramic particle modification layer is formed by sintering a gel made of composite ceramic or mixed ceramic powder.
Preferably, the composite ceramic or mixed ceramic powder for preparing the gel has an average particle size of 5-100 nm. The ceramic particle modifying layer has the highest filtering precision, so the selected ceramic particle size is also finer.
The technical scheme adopted for further solving the technical problems is as follows: a preparation method of a metal composite ceramic membrane comprises the following steps:
(1) adding a forming agent into the elemental metal or alloy powder, mixing, heating, casting, and sintering in vacuum to obtain a substrate layer;
(2) mixing simple substance metal or alloy powder with composite ceramic or mixed ceramic powder, heating and casting to the substrate layer obtained in the step (1), and performing vacuum sintering to form a transition layer to obtain an intermediate product;
(3) and (3) spraying composite ceramic or mixed ceramic powder on the transition layer of the intermediate product obtained in the step (2), and sintering in vacuum to form a porous ceramic filter layer, thereby obtaining the metal composite ceramic membrane.
Preferably, in the step (1), the amount of the forming agent is 0.1-20.0% (more preferably 0.5-15.0%) of the mass of the elemental metal or alloy powder. If the amount of the forming agent is too small, the tape casting technology is difficult to be normally applied, and if the amount of the forming agent is too large, the production cost is increased, and the carbon content of the product exceeds the standard. The forming agent can be completely volatilized or decomposed in the sintering process, and the base layer does not contain the forming agent.
Preferably, in the step (1), the forming agent is one or more of polyethylene glycol, polyolefin, paraffin, polyacrylamide, polyurethane, methyl cellulose and the like.
Preferably, in the step (1), the mixing temperature is normal temperature-150 ℃ and the mixing time is 1-3 h. If the mixing time is too short, it is difficult to mix uniformly and, if the mixing time is too long, it wastes equipment resources and energy.
Preferably, in the step (1), the temperature of the heating casting is 60-150 ℃, and the casting speed is 0.5-30 m/min (more preferably 1-15 m/min). The adoption of the tape casting method is more beneficial to the batch preparation of qualified base layer blanks, and the prepared base layer has uniform thickness, thus being easy to realize industrial production. If the casting temperature is too high or the casting speed is too fast, the viscosity of the slurry is low, the casting thickness is not easy to control, and if the casting temperature is too low or the casting speed is too slow, the discharging of the casting equipment is not uniform, and the production efficiency is influenced.
Preferably, in the step (1), the temperature of the vacuum sintering is 1000 to 1500 ℃ (more preferably 1200 to 1400 ℃), and the vacuum degree is 1 × 10-1~1×10-4Pa, the time is 2-8 h. During the vacuum sintering process, bonding between the metal particles occurs, so that the substrate layer has a corresponding mechanical strength. If the temperature of the vacuum sintering is too low or the time is too short, effective sintering is difficult to complete, and if the temperature of the vacuum sintering is too high or the time is too long, the porous metal layer is densified, even the metal substrate layer is completely in a molten state, and finally the steel plate is obtained by sintering.
Preferably, in the step (2), the temperature of the heating casting is 60-150 ℃ (more preferably 80-120 ℃), and the casting speed is 0.5-30 m/min (more preferably 1-15 m/min). The adoption of the tape casting method is more beneficial to the batch preparation of the qualified transition layer, and the prepared transition layer has uniform thickness, thus being easy to realize industrial production. If the casting temperature is too high or the casting speed is too fast, the viscosity of the slurry is low, the casting thickness is not easy to control, and if the casting temperature is too low or the casting speed is too slow, the discharging of the casting equipment is not uniform, and the production efficiency is influenced.
Preferably, in the step (2), the temperature of the vacuum sintering is 1000-1500 ℃, and the vacuum degree is 1 × 10-1~1×10-4Pa, for 2-12 h (preferably 2-10 h). The bonding between the metal particles, the bonding between the ceramic particles and the metal powder, and the bonding between the ceramic particles and the ceramic particles occur during the vacuum sintering process, so that the transition layer has corresponding mechanical strength. If the temperature of the vacuum sintering is too low or the time is too short, it is difficult to achieve effective sintering, and if the temperature of the vacuum sintering is too high or the time is too long, the metal particles therein are densified.
Preferably, in the step (2), the operations of powder mixing, heating casting and vacuum sintering are repeated for more than or equal to 1 time to obtain a multi-layer transition layer.
Preferably, in the step (3), the temperature of the vacuum sintering is 1200-1600 ℃ (more preferably 1300-1500 ℃), and the vacuum degree is 1 × 10-1~1×10-4Pa, for 2-14 h (more preferably 8-12 h). Ceramic particles may occur during vacuum sinteringAnd the ceramic particles, and form a porous ceramic structure. If the temperature of the vacuum sintering is too low, the ceramic layer is difficult to achieve effective sintering, and if the temperature of the vacuum sintering is too high, the metal components in the already formed base layer and transition layer may be densified and even melted.
Preferably, in the step (3), the composite ceramic or the gel made of mixed ceramic powder is impregnated on the outer side of the porous ceramic filter layer in the obtained metal composite ceramic membrane, and the ceramic particle modification layer is formed by vacuum sintering.
Preferably, the dipping temperature is 50-80 ℃ and the time is 0.5-15 min (more preferably 6-12 min). If the temperature for impregnation is too low or the time for impregnation is too short, the gel has a high viscosity and is not easily impregnated uniformly, and if the temperature for impregnation is too high or the time for impregnation is too long, the gel is easily dehydrated in the air and loses stability.
Preferably, the mass fraction of the gel is 1 to 50% (more preferably 5 to 30%). If the mass fraction of the gel is too low, the number of required dipping times increases, and if the mass fraction of the gel is too high, the gel becomes unstable.
Preferably, the temperature of the vacuum sintering is 1200-1600 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, for 2-14 h (more preferably 4-10 h). During vacuum sintering, sintering between ceramic particles occurs due to the gel preferentially impregnated into the defects of the ceramic layer and the gel deposited on the porous ceramic filter layer by the capillary principle. If the temperature of the vacuum sintering is too low, the ceramic gel is difficult to achieve effective sintering, and if the temperature of the vacuum sintering is too high, the metal components in the already formed base layer and transition layer may be densified and even melted.
Preferably, the operations of dipping and vacuum sintering are repeated for more than or equal to 1 time to obtain the multilayer ceramic particle modification layer.
The invention has the following beneficial effects:
(1) the filtering precision of the metal composite ceramic membrane can reach 1-50 nm, and the filtering flux can reach 500-3000L/h; the aperture is uniform, and the precision and aperture uniformity indexes are far higher than those of a metal filter membrane;
(2) the metal composite ceramic membrane has the characteristics of thin thickness and continuous change of metal and ceramic phase components in structural design, so that the metal composite ceramic membrane has the advantages of high toughness of metal and ceramic phases, good thermal shock resistance, high mechanical strength and easiness in back flushing and cleaning, and can effectively resist damage caused by temperature change when used in a variable-temperature environment;
(3) the metal composite ceramic membrane can be widely applied to the fields of industrial wastewater, high-temperature corrosive flue gas purification and the like, and can also be applied to various filtering systems with severe temperature changes;
(4) the method has simple process and low cost, and is suitable for industrial production.
Detailed Description
The present invention will be further described with reference to the following examples.
The mass ratio of aluminum nitride to silicon nitride in the aluminum nitride-silicon nitride mixed ceramic powder used in the embodiment of the invention is 72:27, the mass ratio of alumina to silicon oxide in the alumina/silicon oxide composite ceramic powder is 73:24, and the mass ratio of zirconia to alumina in the zirconia-alumina mixed ceramic powder is 10: 90; the starting materials or chemicals used in the examples of the present invention are, unless otherwise specified, commercially available in a conventional manner.
Metal composite ceramic film example 1
The metal composite ceramic membrane sequentially comprises a 90kg basal layer, a 30kg transition layer and a 0.5kg precision layer;
the base layer is formed by sintering simple substance titanium powder with the average grain diameter of 50 meshes; the thickness of the substrate layer is 1800 mu m;
the transition layer is composed of 1 layer, and is a composite layer formed by sintering simple substance titanium powder with the average grain diameter of 800 meshes and aluminum nitride and silicon nitride mixed ceramic powder with the average grain diameter of 3000 meshes according to the mass ratio of 70: 30; the thickness of the transition layer is 750 mu m;
the precision layer is a porous ceramic filter layer formed by sintering aluminum nitride and silicon nitride mixed ceramic powder with the average grain diameter of 5000 meshes; the thickness of the porous ceramic filter layer is 20 μm; the average pore size of the porous ceramic filter layer is 50 nm.
Example 2 of Metal composite ceramic film
The metal composite ceramic membrane sequentially comprises a 50kg basal layer, a 45kg transition layer and a 2kg precision layer;
the base layer is formed by sintering stainless steel 310S powder with the average grain size of 400 meshes; the thickness of the substrate layer is 1200 mu m;
the transition layer consists of 3 layers from the base layer to the precision layer, wherein the 1 st layer is a composite layer sintered by stainless steel 310S powder with the average grain size of 500 meshes and alumina/silicon oxide composite ceramic powder with the average grain size of 5000 meshes in a mass ratio of 90:10, the 2 nd layer is a composite layer sintered by stainless steel 310S powder with the average grain size of 750 meshes and alumina/silicon oxide composite ceramic powder with the average grain size of 5000 meshes in a mass ratio of 50:50, and the 3 rd layer is a composite layer sintered by stainless steel 310S powder with the average grain size of 800 meshes and alumina/silicon oxide composite ceramic powder with the average grain size of 8000 meshes in a mass ratio of 10: 90; each layer of the transition layer is 350 μm thick;
the precision layer comprises a porous ceramic filter layer and a ceramic particle modification layer, wherein the porous ceramic filter layer is formed by sintering alumina/silicon oxide composite ceramic powder with the average particle size of 1.9kg and 10000 meshes, and the ceramic particle modification layer is arranged on the outer side of the porous ceramic filter layer and is formed by sintering gel made of the alumina/silicon oxide composite ceramic powder with the average particle size of 100 nm; the thickness of the porous ceramic filter layer is 45 μm; the average pore size of the porous ceramic filter layer is 10 nm; the ceramic particle modification layer is composed of 1 layer, and the thickness is 25 mu m.
Example 3 of Metal composite ceramic film
The metal composite ceramic membrane sequentially comprises a 40kg basal layer, a 60kg transition layer and a 0.5kg precision layer;
the substrate layer is formed by sintering Hastelloy powder with the average grain size of 300 meshes; the thickness of the substrate layer is 1100 mu m;
the transition layer consists of 2 layers from the base layer to the precision layer, wherein the 1 st layer is a composite layer sintered by Hastelloy powder with the average grain size of 200 meshes and zirconia-alumina mixed ceramic powder with the average grain size of 3000 meshes according to the mass ratio of 70:30, and the 2 nd layer is a composite layer sintered by Hastelloy powder with the average grain size of 800 meshes and zirconia-alumina mixed ceramic powder with the average grain size of 3000 meshes according to the mass ratio of 20: 80; each layer of the transition layer is 650 mu m in thickness;
the precision layer comprises a porous ceramic filter layer and a ceramic particle modification layer, wherein the porous ceramic filter layer is formed by sintering zirconia-alumina mixed ceramic powder with the average particle size of 0.45kg and 10000 meshes, and the ceramic particle modification layer is arranged on the outer side of the porous ceramic filter layer and is formed by sintering gel made of zirconia-alumina mixed ceramic powder with the average particle size of 20 nm; the thickness of the porous ceramic filter layer is 30 μm; the average pore size of the porous ceramic filter layer is 5 nm; the ceramic particle modification layer consists of 2 layers, and the thickness of the ceramic particle modification layer is 5 micrometers and 3 micrometers from inside to outside in sequence.
Preparation method of metal composite ceramic membrane example 1
(1) Adding 0.45kg of methylcellulose into 90kg of simple substance titanium powder, mixing at normal temperature for 3h, heating at 90 deg.C and 4m/min for tape casting, and heating at 1300 deg.C and 3 × 10-3Vacuum sintering for 6 hours under Pa to obtain a substrate layer;
(2) mixing 21kg of simple substance titanium powder and 9kg of aluminum nitride and silicon nitride mixed ceramic powder, heating and casting the mixture on the substrate layer obtained in the step (1) at 90 ℃ and 4m/min, and heating and casting the mixture at 1400 ℃ and 3 multiplied by 10-3Under Pa, vacuum sintering for 10h to form a transition layer to obtain an intermediate product;
(3) spraying 0.5kg of aluminum nitride and silicon nitride mixed ceramic powder on the transition layer of the intermediate product obtained in the step (2), and carrying out spray coating at 1400 ℃ and 5 multiplied by 10-3And (3) sintering for 8 hours in vacuum under Pa to form a porous ceramic filter layer, thus obtaining the metal composite ceramic membrane 1.
Through detection, the filtering precision of the metal composite ceramic membrane 1 obtained in the embodiment of the invention is 50nm, and the filtering flux is 2000L/h; the aperture is uniform, and the precision and aperture uniformity indexes are far higher than those of the metal filter element; and the toughness is high, the mechanical strength is high, and the back flushing cleaning is easy.
Preparation method of metal composite ceramic membrane example 2
(1) Adding 7.5kg of polypropylene/paraffin (1: 1 by mass) into 50kg of stainless steel 310S powder, mixing at 150 deg.C for 2 hr, and mixing at 130 deg.C and 5m/min, heat casting at 1320 deg.C, 5X 10-2Vacuum sintering for 3 hours under Pa to obtain a substrate layer;
(2) mixing 13.5kg stainless steel 310S powder and 1.5kg alumina/silica composite ceramic powder, heating and casting at 120 deg.C and 5m/min to the substrate layer obtained in step (1), and heating and casting at 1450 deg.C and 5 × 10-2Under Pa, vacuum sintering for 4h to form a 1 st transition layer;
mixing 7.5kg of stainless steel 310S powder and 7.5kg of alumina/silicon oxide composite ceramic powder, heating and casting to the first transition layer at 120 ℃ and 5m/min, and heating and casting at 1450 ℃ and 5 x 10-2Under Pa, vacuum sintering for 5h to form a 2 nd transition layer;
mixing 1.5kg stainless steel 310S powder and 13.5kg alumina/silica composite ceramic powder, heating and casting to the 2 nd transition layer at 120 deg.C and 5m/min, and casting at 1450 deg.C and 5 × 10-2Under Pa, vacuum sintering for 6h to form a 3 rd transition layer to obtain an intermediate product;
(3) spraying 2kg of alumina/silica composite ceramic powder on the transition layer of the intermediate product obtained in the step (2) at 1500 ℃ and 5 multiplied by 10-2Under Pa, vacuum sintering for 10h to form a porous ceramic filter layer;
soaking 30% gel of alumina/silica composite ceramic powder at 80 deg.C for 6min at 1500 deg.C and 5 × 10-2And (4) sintering for 4 hours in vacuum under Pa to form a ceramic particle modification layer, thus obtaining the metal composite ceramic membrane 2.
Through detection, the filtering precision of the metal composite ceramic membrane 2 obtained in the embodiment of the invention is 10nm, and the filtering flux is 800L/h; the aperture is uniform, and the precision and aperture uniformity indexes are far higher than those of the metal filter element; and the toughness is high, the mechanical strength is high, and the back flushing cleaning is easy.
Preparation method of metal composite ceramic membrane example 3
(1) Adding 0.3kg polyacrylamide into 40kg Hastelloy powder, mixing at room temperature for 1 hr, heating at 80 deg.C and 8m/min for tape casting, and heating at 1400 deg.C and 1 × 10-2Under Pa, vacuum sintering for 2h to obtain a substrate layer;
(2) Mixing 21kg of Hastelloy powder and 9kg of zirconia-alumina mixed ceramic powder, heating and casting the mixture on the substrate layer obtained in the step (1) at 80 ℃ and 8m/min, and carrying out casting at 1100 ℃ and 4 multiplied by 10-2Under Pa, vacuum sintering for 4h to form a 1 st transition layer;
mixing 6kg of Hastelloy powder and 24kg of zirconia-alumina mixed ceramic powder, heating and casting to the 1 st transition layer at 80 ℃ and 8m/min, and performing 4 multiplied by 10 casting at 1300 ℃-2Under Pa, vacuum sintering for 8h to form a 2 nd transition layer to obtain an intermediate product;
(3) spraying 0.5kg of zirconia-alumina mixed ceramic powder on the transition layer of the intermediate product obtained in the step (2), and carrying out the step (2) of spraying at 1300 ℃ and 4 multiplied by 10-2Under Pa, vacuum sintering for 12h to form a porous ceramic filter layer;
soaking gel with 10% mass fraction prepared from zirconia-alumina mixed ceramic powder at 60 deg.C at 1500 deg.C for 12min, and treating at 6 × 10-2Under Pa, vacuum sintering for 8h to form a 1 st ceramic particle modification layer;
soaking gel with mass fraction of 6% prepared from zirconia-alumina mixed ceramic powder at 60 deg.C for 10min at 1400 deg.C and 6 × 10-2And (3) sintering for 5 hours in vacuum under Pa to form a 2 nd ceramic particle modification layer and obtain the metal composite ceramic membrane 3.
Through detection, the filtering precision of the metal composite ceramic membrane 3 obtained in the embodiment of the invention is 5nm, and the filtering flux is 1500L/h; the aperture is uniform, and the precision and aperture uniformity indexes are far higher than those of the metal filter element; and the toughness is high, the mechanical strength is high, and the back flushing cleaning is easy.
Thermal shock resistance comparison experiments are carried out on the metal composite ceramic membranes 1-3 and the ceramic membranes sold in the market, the low temperature point of the thermal shock cycle is 20 ℃, the high temperature point of the thermal shock cycle is 800 ℃, the number of the filter membrane samples is 100, the damage number of the filter membrane after 10 times, 20 times and 50 times of cycle is calculated respectively, and the results are shown in table 1.
TABLE 1 comparison table of thermal shock resistance of the metal composite ceramic films 1-3 of the present invention and commercially available ceramic films
Figure BDA0002123963630000091
As can be seen from Table 1, none of the metal composite ceramic membranes 1-3 of the invention is damaged in the thermal shock resistant cycle, and after 50 cycles from low temperature to high temperature, 25% of the filter membranes of the commercially available ceramic filter elements are cracked, which finally leads to failure and damage of the filter membranes.

Claims (17)

1. A metal composite ceramic membrane, characterized by: the device sequentially comprises a substrate layer, a transition layer and a precision layer; the substrate layer is formed by sintering elemental metal or alloy powder; the transition layer is a composite layer formed by sintering elemental metal or alloy powder and composite ceramic or mixed ceramic powder; the precision layer comprises a porous ceramic filter layer sintered by composite ceramic or mixed ceramic powder; the mass ratio of the base layer to the transition layer to the precision layer is 40-90: 30-60: 0.5-2; in the transition layer, the mass ratio of the simple substance metal or alloy powder to the composite ceramic or mixed ceramic powder is 90-10: 10-90; in each layer of the transition layer, the mass ratio of the simple substance metal or the alloy to the composite ceramic or the mixed ceramic is reduced from the substrate layer to the precision layer by layer; the precision layer also comprises a ceramic particle modification layer arranged outside the porous ceramic filter layer; the mass ratio of the ceramic particle modification layer to the porous ceramic filter layer is 0.04-0.45: 1; the thickness ratio of the base layer to the transition layer to the precision layer is 0.8-1.8: 0.3-1.3: 0.02-0.08; the transition layer consists of 2-6 layers; the thickness of each layer in the transition layer is 350-750 mu m; in the precision layer, the thickness of the porous ceramic filter layer is 20-45 μm; in the base layer, the average particle size of the simple substance metal or alloy powder is 50-400 meshes; in the transition layer, the average particle size of the simple substance metal or alloy powder is 200-800 meshes; in the transition layer and the precision layer, the composite ceramic is alumina/silicon oxide composite ceramic, alumina/zirconia composite ceramic or zirconia/yttria composite ceramic; in the transition layer and the precision layer, the mixed ceramic is aluminum nitride and silicon nitride mixed ceramic, zirconia and alumina mixed ceramic or silica and zirconia mixed ceramic; in the transition layer, the average grain diameter of the composite ceramic or mixed ceramic powder is 800-8000 meshes; in the precision layer, the average grain diameter of the composite ceramic or mixed ceramic powder is 5000-10000 meshes; the ceramic particle modification layer consists of 1-2 layers; the thickness of each layer in the ceramic particle modification layer is 3-25 mu m; the ceramic particle modification layer is formed by sintering gel made of composite ceramic or mixed ceramic powder;
the preparation method of the metal composite ceramic membrane comprises the following steps:
(1) adding a forming agent into the elemental metal or alloy powder, mixing, heating, casting, and sintering in vacuum to obtain a substrate layer;
(2) mixing simple substance metal or alloy powder with composite ceramic or mixed ceramic powder, heating and casting to the substrate layer obtained in the step (1), and performing vacuum sintering to form a transition layer to obtain an intermediate product;
(3) spraying composite ceramic or mixed ceramic powder on the transition layer of the intermediate product obtained in the step (2), and sintering in vacuum to form a porous ceramic filter layer to obtain the metal composite ceramic membrane; the temperature of the vacuum sintering is 1300-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 8-12 h;
in the step (3), the outer side of the porous ceramic filter layer in the obtained metal composite ceramic membrane is soaked in gel prepared by composite ceramic or mixed ceramic powder, and the gel is sintered in vacuum to form a ceramic particle modification layer; the dipping temperature is 50-80 ℃, and the time is 0.5-15 min; the mass fraction of the gel is 5-30%.
2. The metal composite ceramic membrane of claim 1, wherein: the average pore size of the porous ceramic filter layer is 5-100 nm.
3. A metal composite ceramic membrane according to claim 1 or 2, wherein: in the base layer and the transition layer, the elementary metal is elementary iron, elementary nickel, elementary copper or elementary titanium; the alloy is stainless steel, hastelloy or iron-chromium-aluminum alloy.
4. A metal composite ceramic membrane according to claim 1 or 2, wherein: the average particle size of the composite ceramic or mixed ceramic powder for preparing the gel is 5-100 nm.
5. A metal composite ceramic membrane according to claim 3, wherein: the average particle size of the composite ceramic or mixed ceramic powder for preparing the gel is 5-100 nm.
6. A metal composite ceramic membrane according to claim 1 or 2, wherein: in the step (1), the amount of the forming agent is 0.1-20.0% of the mass of the elemental metal or alloy powder; the forming agent is one or more of polyethylene glycol, polyolefin, paraffin, polyacrylamide, polyurethane or methyl cellulose; the mixing temperature is normal temperature-150 ℃, and the mixing time is 1-3 h; the heating casting temperature is 60-150 ℃, and the casting speed is 0.5-30 m/min; the temperature of the vacuum sintering is 1000-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-8 h.
7. A metal composite ceramic membrane according to claim 3, wherein: in the step (1), the amount of the forming agent is 0.1-20.0% of the mass of the elemental metal or alloy powder; the forming agent is one or more of polyethylene glycol, polyolefin, paraffin, polyacrylamide, polyurethane or methyl cellulose; the mixing temperature is normal temperature-150 ℃, and the mixing time is 1-3 h; the heating casting temperature is 60-150 ℃, and the casting speed is 0.5-30 m/min; the temperature of the vacuum sintering is 1000-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-8 h.
8. The metal composite ceramic membrane of claim 4, wherein: in the step (1), the amount of the forming agent is 0.1-20.0% of the mass of the elemental metal or alloy powder;the forming agent is one or more of polyethylene glycol, polyolefin, paraffin, polyacrylamide, polyurethane or methyl cellulose; the mixing temperature is normal temperature-150 ℃, and the mixing time is 1-3 h; the heating casting temperature is 60-150 ℃, and the casting speed is 0.5-30 m/min; the temperature of the vacuum sintering is 1000-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-8 h.
9. A metal composite ceramic membrane according to claim 1 or 2, wherein: in the step (2), the temperature of heating and casting is 60-150 ℃, and the casting speed is 0.5-30 m/min; the temperature of the vacuum sintering is 1000-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-12 h; repeating the operations of powder mixing, heating tape casting and vacuum sintering for more than or equal to 1 time to obtain a multi-layer transition layer.
10. A metal composite ceramic membrane according to claim 3, wherein: in the step (2), the temperature of heating and casting is 60-150 ℃, and the casting speed is 0.5-30 m/min; the temperature of the vacuum sintering is 1000-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-12 h; repeating the operations of powder mixing, heating tape casting and vacuum sintering for more than or equal to 1 time to obtain a multi-layer transition layer.
11. The metal composite ceramic membrane of claim 4, wherein: in the step (2), the temperature of heating and casting is 60-150 ℃, and the casting speed is 0.5-30 m/min; the temperature of the vacuum sintering is 1000-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-12 h; repeating the operations of powder mixing, heating tape casting and vacuum sintering for more than or equal to 1 time to obtain a multi-layer transition layer.
12. The metal composite ceramic membrane of claim 6, wherein: in the step (2), the temperature of heating and casting is 60-150 ℃, and the casting speed is 0.5-30 m/min; the shoe soleThe temperature of air sintering is 1000-1500 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-12 h; repeating the operations of powder mixing, heating tape casting and vacuum sintering for more than or equal to 1 time to obtain a multi-layer transition layer.
13. A metal composite ceramic membrane according to claim 1 or 2, wherein: in the step (3), after the gel prepared by the composite ceramic or the mixed ceramic powder is impregnated, the temperature of the vacuum sintering is 1200-1600 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-14 h; repeating the operations of dipping and vacuum sintering for more than or equal to 1 time to obtain the multilayer ceramic particle modification layer.
14. A metal composite ceramic membrane according to claim 3, wherein: in the step (3), after the gel prepared by the composite ceramic or the mixed ceramic powder is impregnated, the temperature of the vacuum sintering is 1200-1600 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-14 h; repeating the operations of dipping and vacuum sintering for more than or equal to 1 time to obtain the multilayer ceramic particle modification layer.
15. The metal composite ceramic membrane of claim 4, wherein: in the step (3), after the gel prepared by the composite ceramic or the mixed ceramic powder is impregnated, the temperature of the vacuum sintering is 1200-1600 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-14 h; repeating the operations of dipping and vacuum sintering for more than or equal to 1 time to obtain the multilayer ceramic particle modification layer.
16. The metal composite ceramic membrane of claim 6, wherein: in the step (3), after the gel prepared by the composite ceramic or the mixed ceramic powder is impregnated, the temperature of the vacuum sintering is 1200-1600 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-14 h; repeating the operations of dipping and vacuum sintering for more than or equal to 1 time to obtain the multilayer ceramic particle modification layer.
17. A metal composite ceramic membrane according to claim 9, wherein: in the step (3), after the gel prepared by the composite ceramic or the mixed ceramic powder is impregnated, the temperature of the vacuum sintering is 1200-1600 ℃, and the vacuum degree is 1 multiplied by 10-1~1×10-4Pa, the time is 2-14 h; repeating the operations of dipping and vacuum sintering for more than or equal to 1 time to obtain the multilayer ceramic particle modification layer.
CN201910616011.5A 2019-07-09 2019-07-09 Metal composite ceramic membrane and preparation method thereof Active CN110252156B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910616011.5A CN110252156B (en) 2019-07-09 2019-07-09 Metal composite ceramic membrane and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910616011.5A CN110252156B (en) 2019-07-09 2019-07-09 Metal composite ceramic membrane and preparation method thereof

Publications (2)

Publication Number Publication Date
CN110252156A CN110252156A (en) 2019-09-20
CN110252156B true CN110252156B (en) 2022-04-05

Family

ID=67925272

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910616011.5A Active CN110252156B (en) 2019-07-09 2019-07-09 Metal composite ceramic membrane and preparation method thereof

Country Status (1)

Country Link
CN (1) CN110252156B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112569803B (en) * 2019-09-30 2022-08-05 成都易态科技有限公司 Preparation method of composite porous film
CN110893324A (en) * 2019-12-06 2020-03-20 北京工业大学 Method for preparing hydrophobic porous cordierite ceramic membrane for desalination by taking high-silicon solid waste as raw material through tape casting
CN111039472A (en) * 2020-02-18 2020-04-21 胡日中 Multifunctional tap water terminal water purifier
CN111437726A (en) * 2020-04-24 2020-07-24 佛山市中国科学院上海硅酸盐研究所陶瓷研发中心 Tin oxide ultrafiltration membrane and preparation method and application thereof
CN114618316B (en) * 2022-03-30 2023-04-18 西部宝德科技股份有限公司 Porous metal-ceramic composite membrane material and preparation method thereof

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62129104A (en) * 1985-11-28 1987-06-11 Ngk Insulators Ltd Ceramic tubular filter and its manufacturing process
CN1548586A (en) * 2003-05-22 2004-11-24 中南大学 Ceramet material with gradient function for electrolyzing Al
CN101234296A (en) * 2008-02-29 2008-08-06 南京工业大学 Preparation technique of porous stainless steel-ceramic compound film
CN102500245A (en) * 2011-12-01 2012-06-20 西北有色金属研究院 Preparation method of metal-base ceramic composite filter membrane
CN102794053A (en) * 2012-08-21 2012-11-28 韶关市贝瑞过滤科技有限公司 Powder-sintered filter core with gradient multilayer composite structure and production method thereof
CN103079339A (en) * 2013-01-28 2013-05-01 深圳市泓亚光电子有限公司 Metal ceramic composite substrate and manufacturing method for same
CN104437112A (en) * 2014-10-11 2015-03-25 南京工业大学 Method for preparing porous metal supporting ceramic membrane based on static induced type nanometer particle coating
CN105215365A (en) * 2014-06-05 2016-01-06 中国科学院上海硅酸盐研究所 A kind of metal-cermic coating and preparation method thereof
CN105983349A (en) * 2015-02-16 2016-10-05 中国科学院大连化学物理研究所 Method for producing ceramic membrane through adopting suspension particle sintering technology
CN107305953A (en) * 2016-04-18 2017-10-31 汕头大学 A kind of SOFC composite base plate and its preparation technology
CN108144457A (en) * 2016-12-02 2018-06-12 北京有色金属研究总院 A kind of preparation method of porous ceramic material graded composite film

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62129104A (en) * 1985-11-28 1987-06-11 Ngk Insulators Ltd Ceramic tubular filter and its manufacturing process
CN1548586A (en) * 2003-05-22 2004-11-24 中南大学 Ceramet material with gradient function for electrolyzing Al
CN101234296A (en) * 2008-02-29 2008-08-06 南京工业大学 Preparation technique of porous stainless steel-ceramic compound film
CN102500245A (en) * 2011-12-01 2012-06-20 西北有色金属研究院 Preparation method of metal-base ceramic composite filter membrane
CN102794053A (en) * 2012-08-21 2012-11-28 韶关市贝瑞过滤科技有限公司 Powder-sintered filter core with gradient multilayer composite structure and production method thereof
CN103079339A (en) * 2013-01-28 2013-05-01 深圳市泓亚光电子有限公司 Metal ceramic composite substrate and manufacturing method for same
CN105215365A (en) * 2014-06-05 2016-01-06 中国科学院上海硅酸盐研究所 A kind of metal-cermic coating and preparation method thereof
CN104437112A (en) * 2014-10-11 2015-03-25 南京工业大学 Method for preparing porous metal supporting ceramic membrane based on static induced type nanometer particle coating
CN105983349A (en) * 2015-02-16 2016-10-05 中国科学院大连化学物理研究所 Method for producing ceramic membrane through adopting suspension particle sintering technology
CN107305953A (en) * 2016-04-18 2017-10-31 汕头大学 A kind of SOFC composite base plate and its preparation technology
CN108144457A (en) * 2016-12-02 2018-06-12 北京有色金属研究总院 A kind of preparation method of porous ceramic material graded composite film

Also Published As

Publication number Publication date
CN110252156A (en) 2019-09-20

Similar Documents

Publication Publication Date Title
CN110252156B (en) Metal composite ceramic membrane and preparation method thereof
US7699903B2 (en) Porous ceramic body and method for production thereof
CN105727755B (en) A kind of gradient-porosity silicon nitride combined silicon carbide membrane tube and preparation method thereof
CN106187297A (en) A kind of preparation method of composite silicon carbide ceramic filter membrane material
CN102659446B (en) Pure SiC membrane tube support and preparation method thereof
CN103691330B (en) A kind of preparation technology of porous stainless steel membrane
EP1934156A1 (en) Ceramic from preceramic paper or board structures, process for producing it and its use
JP2007532778A (en) Method for producing sintered metal fiber
CN105622079A (en) Preparing method for molecular sieving membrane support
CN110252157B (en) Reinforced metal composite ceramic membrane and preparation method thereof
MX2011002827A (en) Process for manufacturing a porous sic material.
JPH07247188A (en) Production of article made of functional gradient material
CN105693276A (en) Silicon carbide filtering film and low temperature preparation method thereof
JP2600105B2 (en) Method for forming SiC film
US20230074526A1 (en) Fe-al-based metal membrane and preparation method thereof
JP5132176B2 (en) Multilayer porous material and method for producing the same
CN110981453B (en) Preparation method of light ceramic filtering membrane
EP1421042A1 (en) Filter for molten metal filtration and method for producing such filters
CN100393400C (en) Asymmetric porous ceramic micro filter film and its preparing method
JP2004089838A (en) Separation membrane module and its manufacturing method
US20030035901A1 (en) Silicon carbide-based, porous, lightweight, heat-resistant structural material and manufacturing method therefor
JP2672545B2 (en) Method for manufacturing silicon carbide honeycomb filter
WO2022068109A1 (en) High-flux anti-pollution ceramic filter membrane and preparation method therefor
CN220478548U (en) Porous metal-based ceramic composite membrane
KR101595541B1 (en) Setter for manufacturing ceramic and manufacturing method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant