CN1072621C - Ceramic thick membrane assembling process - Google Patents

Ceramic thick membrane assembling process Download PDF

Info

Publication number
CN1072621C
CN1072621C CN98122879A CN98122879A CN1072621C CN 1072621 C CN1072621 C CN 1072621C CN 98122879 A CN98122879 A CN 98122879A CN 98122879 A CN98122879 A CN 98122879A CN 1072621 C CN1072621 C CN 1072621C
Authority
CN
China
Prior art keywords
biscuit
film
static pressure
density
preparation technology
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.)
Expired - Fee Related
Application number
CN98122879A
Other languages
Chinese (zh)
Other versions
CN1226534A (en
Inventor
陈铭
温廷琏
吕之奕
王大千
屠恒勇
杨勇杰
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.)
Shanghai Institute of Ceramics of CAS
Original Assignee
Shanghai Institute of Ceramics of CAS
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 Shanghai Institute of Ceramics of CAS filed Critical Shanghai Institute of Ceramics of CAS
Priority to CN98122879A priority Critical patent/CN1072621C/en
Publication of CN1226534A publication Critical patent/CN1226534A/en
Application granted granted Critical
Publication of CN1072621C publication Critical patent/CN1072621C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Compositions Of Oxide Ceramics (AREA)

Abstract

The present invention relates to a novel ceramic thick film combination forming preparation technology which belongs to the field of a material preparation technology. Firstly, a ceramic biscuit film with certain thickness is prepared by a flow casting method, the biscuit film is isostatically pressed after being dried for certain time, and the biscuit film is sintered. The present invention has the maximum advantage that the advantages of flow casting and isostatic pressing are combined, the present invention not only can prepare thin type large-area ceramics but also can cause the forming density of the biscuit to be increased by 8 to 11% by isostatic pressing to the biscuit, and the relative density of film material sintering can be increased by 5 to 10% under the condition of non-pressure sintering. A film material can be more uniform, smoother and denser, a technological process is not complex, and the present invention is suitable for ceramic preparation in a large scale.

Description

A kind of ceramic thick membrane assembling process
The present invention relates to the assembling process of ceramic thick film, belong to the material preparation process field.
As everyone knows, the moulding process of stupalith is very important in a ceramic material process link.The new moulding process of nearly one, 20 year stupalith occurs in succession, has promoted the development of stupalith, has enriched the intension of ceramic material science.But there is shortcoming in every kind of moulding process inevitably when giving its new advantage.For example, the casting method moulding is a kind of important processing method of the slim big area pottery of preparation, the thin ceramic that makes in this way has the quality height, advantages such as biscuit film machining process performance is good, and be adapted to large-scale commercial production, produce ceramic condenser and ic substrate with the domestic doctor-blade casting process that adopts maturely in the world, it also is the important process of a series of novel thick film ceramic functional devices of development preparation, as the solid electrolyte material YSZ film (8mol%Y in Solid Oxide Fuel Cell (SOFC) 2O 3Stable ZrO 2) very ripe with curtain coating technology preparation technology.But because the preparation technology's of casting films restriction own; its slurry solid content is lower; thereby though can improve the slurry solid content to increase particle diameter by means such as granulation or thermal treatment powders; improve biscuit density, but can cause sintered membrane material density to descend on the contrary if excessive then its sintering character of powder particle particle diameter descends.About 400~600nm, and require uniform particle diameter for its powder optimum grain-diameter of curtain coating legal system film, so comparatively complicated with the technological process that improves casting films sintered membrane material density by handling powder.On the other hand in casting films biscuit drying process, volatilization because of solvent, plastic agent and binding agent are difficult to fill the pore that solvent evaporates stays before dry, thereby leave many pits and hole on biscuit surface and inside, make the biscuit film short texture, density is lower, and the individual layer casting films is because thinner thickness, can not adopt some unconventional sintering means (as hot pressed sintering), can only adopt pressureless sintering, add the burn off of a large amount of organic additives in the sintering process, be difficult to obtain fine and close casting films sintered membrane material, all about 80~90%, difficulty reaches more than 95% the relative density of general casting films sintered membrane material.And for example, the characteristics of cold isostatic compaction are that powder is stressed evenly, can prepare the higher goods of all even biscuit density of shape density, add that its moulding stock is again latex, rubber etc., but thereby with the dry-pressing formed complicated or large-sized plate product of machining shape of comparing, if the thick film of casting method moulding is passed through cold isostatic compaction again, its biscuit density is further improved, improve the sintered density of casting films material, thereby improve the quality of thick film, this has just derived design of the present invention.
The object of the present invention is to provide a kind of novel ceramic thick film combination forming preparation technology, by curtain coating membranogen base is waited static pressure, not only can improve forming of green body density, and can improve sintered membrane material density, and technological process is uncomplicated.
Specifically, implementation process of the present invention is as follows, at first makes certain thickness biscuit film by casting method, treat its drying after, be cut to definite shape (unitary film or biscuit laminated material) and wait static pressure, and then carry out pressureless sintering.
Below in conjunction with concrete used for high-temperature fuel cell YSZ thick-film material, further comment intension of the present invention, but limit the present invention absolutely not.
Selecting median size for use is yttria-stabilized zirconia (YSZ) powder of 350nm and uniform particle diameter, in ceramic powder, added solvent and dispersion agent ball milling 24 hours earlier, add binding agent and plastic agent ball milling again and obtained to be uniformly dispersed stable slurry in 24 hours, on casting machine, make certain thickness biscuit film then by scraper.After treating the dry certain hour of biscuit film, its punch die is become the biscuit of desired size, wait static pressure, both can also can wait static pressure when waiting static pressure unitary film to laminated material with the pressure of 200MPa.During Deng static pressure its thickness and shape all there is not particular requirement.For simplifying sintering process, adopt " sandwich style " porous clamping plate (void content is 50~60%) agglomerating plant, the burn off of organic phase and the sintering of film material are once finished.The size and the variable density of biscuit film material before and after the static pressure such as mensuration, measure the density of sintered membrane material under the different sintering temperatures with drainage, and the microstructure of biscuit film surface and section and sintered membrane material section carried out scanning electron microscope (SEM) observation, with static pressure such as understandings to biscuit film and sintered membrane material density and the microstructural rule that influences.Casting films biscuit to the moulding of above-mentioned employing casting method is used isostatic pressing again, biscuit density can improve 8%~11%, the contraction of biscuit film thickness direction reaches 0~6%, area is contracted in about 5%, and under same sintering temperature (as 1550 ℃) sintering, the relative density of sintered membrane material can improve 5%~10%.
Scanning electronic microscope (SEM) photo of Fig. 1 for waiting same casting films biscuit microstructure in static pressure front and back to change.(a) and (b) are without the upper surface and the fracture photo that wait the static pressure biscuit, (c), (d) be through etc. the upper surface and the fracture photo of biscuit behind the static pressure (200MPa).
As seen from Figure 1, casting films because the volatilization of solvent will inevitably stay a large amount of holes on biscuit surface and inside, makes the biscuit short texture in drying process, and compact density is low, and this will inevitably influence the sintered density of casting films material.By biscuit being waited static pressure post forming compression biscuit, can eliminate biscuit surface and inside holes greatly, make between the particle, air vent aperture and distribute more even in conjunction with tightr, forming of green body density improves, for the raising of sintered membrane material density is laid a solid foundation.In addition, even can not eliminate dry biscuit surface, back and inside holes, so the static pressure post forming that waits of casting films biscuit is of universal significance by organic reagent consumption in means such as the granulation minimizing slurry.
Fig. 2 waits static pressure to the lifting of YSZ thick film firing film material density and the relation of casting films biscuit density, and sintering temperature is 1550 ℃, and X-coordinate is the biscuit density of thick film, and unit is (g/cm 3), ordinate zou is a sintered membrane material density, unit is (g/cm 3).Curve 1 is without the lifting of the thick film firing film material density of isostatic pressing and the relation of biscuit density, and curve 2 is through the lifting of the thick film firing film material density of 200MPa pressure isostatic pressing and the relation of biscuit density.
As seen from Figure 2, different biscuit film are under identical sintering temperature, the relative density of its biscuit sintered membrane material after waiting static pressure generally all can improve 5%~10%, its reason just is that the volatilization of solvent in the casting films drying process will inevitably stay hole in the surface and the inside of biscuit, make biscuit fine and close inadequately, and obviously can eliminate the biscuit inside holes to a certain extent after waiting static pressure, make between the particle in conjunction with tightr.In addition, from figure, also can find out, wait the amplitude that sintered membrane material density improves behind the static pressure also relevant with the former density of film material, obviously as former density low then biscuit density is low, more remarkable effect behind the static pressure is more then waited in its compressible leeway.Also is limited Deng static pressure to the ability that film material density improves, because it can not eliminate pore left in the sintering process, sintered membrane material density also waits other factors relevant with the powder particle size in addition.
Fig. 3 is the SEM photo of same casting films corresponding to the sintered membrane material section of curve among Fig. 21,2, and sintering temperature is 1550 ℃, (a) does not wait static pressure, (b) static pressure such as 200MPa.As can be seen, do not wait the sintered membrane material section of static pressure casting films biscuit that many gross blow holes are arranged, and diameter is all about a few μ m, sintering under the same conditions after waiting static pressure, the aperture of pore and quantity all have obvious reduction, and have only a spot of spilehole to exist.Obviously its surface is relevant with inside holes after the gross blow hole that does not wait static pressure casting films sintered membrane material section and the biscuit drying, biscuit through etc. eliminated the existence of hole behind the static pressure, be left a spot of spilehole in the sintered membrane material.
Under the different as can be seen sintering temperatures of the densimetric curve of sintered membrane material under the different sintering temperatures, the lifting of sintered membrane material relative density is all greater than 5% after waiting static pressure (200MPa) from same biscuit film, and its result as shown in Figure 4.Among the figure X-coordinate be sintering temperature (℃), ordinate zou is the density (g/cm of sintered membrane material 3).Curve 1 and 2 be respectively without isostatic pressing and behind isostatic pressing the sintering temperature of YSZ casting films material and the relation curve of sintered membrane material density.
The feature of ceramic thick membrane assembling process provided by the invention not only is flow casting molding and two kinds of moulding processs of cold isostatic compaction are combined, and is that biscuit of ceramics film that (1) makes flow casting molding is all unrestricted to the thickness and the shape of biscuit when waiting static pressure; (2) when the biscuit of ceramics film is waited static pressure, both can wait static pressure, also can carry out isostatic cool pressing curtain coating membranogen base laminated material to unitary film.
This shows and the invention has the advantages that:
(1) wait static pressure that biscuit film is shunk to the curtain coating biscuit film, and reduce its surface and inside holes, make more even compact of its internal structure, forming of green body density can improve 8%~11%.
(2) after waiting static pressure, the relative density of casting films sintered membrane material generally all can improve 5%~10%, and the aperture of film material internal porosity and quantity all have obvious reduction.
(3) static pressure post forming such as casting films can improve film material forming of green body density and burn till density, and technological process is uncomplicated, is applicable to the scale preparation of ceramic membrane.
Embodiment 1: selecting median size for use is the YSZ powder of the uniform particle diameter of 350nm, added dispersion agent and solvent ball milling 24 hours, add binding agent and plastic agent ball milling again and obtained to be uniformly dispersed stable slurry in 24 hours, on casting machine, make certain thickness biscuit film (table 1:1 film) then by scraper.After treating the dry certain hour of biscuit film, its punch die is become the biscuit of desired size, wait static pressure with the pressure of 200MPa.Deng being contracted in about 5% of biscuit film two dimensional surface direction behind the static pressure, it is about 8% that biscuit density improves, wait static pressure before and after the biscuit film microstructure change as shown in Figure 1, in the raising of 1550 ℃ of sintering temperature film material relative densities greater than 5%.Table 1: wait the influence of static pressure to curtain coating membranogen base
No. 2 films of No. 1 film
Area/mm 2Thickness/mm density/g.cm -3Area/mm 2Thickness/mm density/g.cm -3Without waiting static pressure 400 0.09 2.92 375 0.31 2.87 through waiting static pressure (200MPa) 380 0.09 3.16 355 0.29 3.20 area contraction/% 5.0 5.3 thickness contraction/%~0 5.9 variable density/% 8.2 11.5
Embodiment 2: the biscuit film that flow casting molding makes, unitary film mean thickness are 0.31mm, and area is 375mm 2, behind the static pressure such as 200MPa, the biscuit film area is punctured into 5.3%, and thickness is punctured into 5.9%, and biscuit density has improved 11.5%, and concrete data see Table the 1:2 film, and all the other are with embodiment 1.
Embodiment 3: the biscuit film that flow casting molding makes, and become the disk of diameter 40mm to wait static pressure towards film it, at 1550 ℃ of sintering, not waiting static pressure casting films sintered membrane material density is 5.4g/cm 3, the density of casting films sintered membrane material is 5.7g/cm behind static pressure such as 200MPa 3, relative density rises greater than 5%.
Embodiment 4: the biscuit film that flow casting molding makes becomes 20 * 20mm with it towards film 2Square sheet and lamination wait static pressure (200MPa), at 1550 ℃ of sintering.Not waiting static pressure casting films sintered membrane material density is 5.2g/cm 3, 14 layers and 16 laminar flows prolong membranogen base lamination and etc. behind the static pressure, at same sintering temperature, sintered density is respectively 5.7g/cm 3And 5.8g/cm 3, the rising of relative density reaches 8~10%.

Claims (4)

1. ceramic thick film combination forming preparation technology, it is characterized in that flow casting molding and two kinds of ceramic moldings of cold isostatic compaction are combined, adopt earlier casting method to make certain thickness biscuit of ceramics film, treat its dry certain hour after, biscuit film is waited static pressure.
2. by the described ceramic thick film combination forming of claim 1 preparation technology, when it is characterized in that biscuit of ceramics film that described flow casting molding makes waits static pressure, all unrestricted to the thickness and the shape of biscuit.
3. by the described ceramic thick film combination forming of claim 1 preparation technology, it is characterized in that static pressure such as described biscuit of ceramics film individual layers.
4. by the described ceramic thick film combination forming of claim 1 preparation technology, it is characterized in that static pressure such as curtain coating biscuit film laminated materials.
CN98122879A 1998-12-28 1998-12-28 Ceramic thick membrane assembling process Expired - Fee Related CN1072621C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN98122879A CN1072621C (en) 1998-12-28 1998-12-28 Ceramic thick membrane assembling process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN98122879A CN1072621C (en) 1998-12-28 1998-12-28 Ceramic thick membrane assembling process

Publications (2)

Publication Number Publication Date
CN1226534A CN1226534A (en) 1999-08-25
CN1072621C true CN1072621C (en) 2001-10-10

Family

ID=5227927

Family Applications (1)

Application Number Title Priority Date Filing Date
CN98122879A Expired - Fee Related CN1072621C (en) 1998-12-28 1998-12-28 Ceramic thick membrane assembling process

Country Status (1)

Country Link
CN (1) CN1072621C (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105503182A (en) * 2015-12-18 2016-04-20 珠海市香之君科技股份有限公司 Cutter blank forming technology of ceramic surgical blade
CN106242567A (en) * 2016-07-13 2016-12-21 西安科技大学 A kind of lanthanum molybdate-based thick-film material of high oxide ion conduction and preparation method thereof
CN107658230A (en) * 2017-08-30 2018-02-02 广东风华高新科技股份有限公司 A kind of regulation and control method of ceramic chips and ltcc substrate surface roughness
CN107602114B (en) * 2017-10-26 2022-05-20 贵州大学 Barium calcium zirconate titanate BCZT piezoelectric ceramic and texturing preparation method thereof
CN109160809A (en) * 2018-08-29 2019-01-08 厦门朝瓷科技有限公司 A kind of submicrometer structure ultrathin alumina ceramic substrate and preparation method
CN108947504A (en) * 2018-08-29 2018-12-07 厦门朝瓷科技有限公司 Submicrometer structure ultrathin alumina ceramic substrate and preparation method
CN114800775B (en) * 2022-05-23 2023-04-18 江苏方达正塬电子材料科技有限公司 GSPL-SNST silicon nitride tape casting biscuit and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1126132A (en) * 1995-01-06 1996-07-10 侯伟华 Isostatic pressing method for ceramic powder
CN2233929Y (en) * 1995-11-09 1996-08-28 河北邢台晶牛玻璃股份有限公司 Pressing machine by flowing out method for slag nucleated glass

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1126132A (en) * 1995-01-06 1996-07-10 侯伟华 Isostatic pressing method for ceramic powder
CN2233929Y (en) * 1995-11-09 1996-08-28 河北邢台晶牛玻璃股份有限公司 Pressing machine by flowing out method for slag nucleated glass

Also Published As

Publication number Publication date
CN1226534A (en) 1999-08-25

Similar Documents

Publication Publication Date Title
CN101061596B (en) Process for solid oxide fuel cell manufacture
JP2604592B2 (en) Molding method of metal, ceramic powder, etc. and composition therefor
CN108794033A (en) A kind of self toughening fibrous monolithic ceramic structural ceramics and preparation method thereof
CN1176874C (en) Ceramic locator and its manufacturing method
CN100519475C (en) Method of preparing zirconium oxide ceramic by curtain coating method and product obtained by using the method
CN108249952A (en) A kind of preparation method of porous ceramics load bearing board
US20090159853A1 (en) Colloidal templating process for manufacture of highly porous ceramics
CN110128115A (en) A kind of method that flash burning prepares oxide eutectic ceramics
CN1072621C (en) Ceramic thick membrane assembling process
CN1151094C (en) Method and special mold for preparing unfired ceramic element sheet
CN105459515A (en) Ceramic substrate and preparation method thereof, and power module
CN1212289C (en) Method for preparing functional gradient material by adopting doctor-blade casting process
CN108947504A (en) Submicrometer structure ultrathin alumina ceramic substrate and preparation method
CN111509251A (en) Bipolar plate for hydrogen fuel cell and preparation method thereof
KR101222867B1 (en) Anode support using spherical pore former and solid oxide fuel cell and the fabrication method therefor
JPH064502B2 (en) Ceramics manufacturing method
CN109160809A (en) A kind of submicrometer structure ultrathin alumina ceramic substrate and preparation method
US5834108A (en) Multi-layered ceramic porous body
CN104803686A (en) Solid oxide fuel cell multi-layer ceramic structure body sintering method
US20080232996A1 (en) Method for Fabricating Parts by PIM or MICROPIM
CN110862260B (en) Electronic product shell, preparation method thereof and mobile phone rear cover
CN110759731B (en) Mobile phone rear cover and preparation method thereof
CN115124328B (en) Selective laser melting preparation method of high-density massive eutectic composite ceramic
WO2017142121A1 (en) Method for preparing ceramic thick film by using water-based binder, and molten carbonate fuel cell and solid oxide fuel cell using same
CN102140953B (en) Method for manufacturing oxygen sensor chip

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee