CA2023322A1 - Process for preparing an inorganic article - Google Patents
Process for preparing an inorganic articleInfo
- Publication number
- CA2023322A1 CA2023322A1 CA 2023322 CA2023322A CA2023322A1 CA 2023322 A1 CA2023322 A1 CA 2023322A1 CA 2023322 CA2023322 CA 2023322 CA 2023322 A CA2023322 A CA 2023322A CA 2023322 A1 CA2023322 A1 CA 2023322A1
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- CA
- Canada
- Prior art keywords
- slurry
- weight percent
- blend
- binder
- water
- 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.)
- Abandoned
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Abstract
ABSTRACT
A process for making an inorganic slurry of an inorganic powder, water, dispersant, thermally gelable polymeric binder and, optionally, a plasticizer. The process includes admixing the inorganic powder, water and dispersant to form a blend. The blend is a ball milled, heated, and admixed with a thermally gelable polymeric binder at a temperature above the gelation point of the polymer to form a slurry mixture, then the mixture is cooled. The slurry mixture can be extruded to form useful articles, such as metal or ceramic tapes.
Additionally, the invention is also a method of final shaping and removing solvents from the formed article.
36,571-F
A process for making an inorganic slurry of an inorganic powder, water, dispersant, thermally gelable polymeric binder and, optionally, a plasticizer. The process includes admixing the inorganic powder, water and dispersant to form a blend. The blend is a ball milled, heated, and admixed with a thermally gelable polymeric binder at a temperature above the gelation point of the polymer to form a slurry mixture, then the mixture is cooled. The slurry mixture can be extruded to form useful articles, such as metal or ceramic tapes.
Additionally, the invention is also a method of final shaping and removing solvents from the formed article.
36,571-F
Description
2~23322 , PROCESS FOR PREPARING AN
INORGANIC ARTICLE
Many forming techniques have been developed for fabricating inorganic powders into, such as metal or ceramic powders, useful shapes. Typical techniques used in the industry include slip casting, tape casting, isostatic pressing, extrusion, roll compacting and others. These processes typically include dispersion of the powder in a solvent medium, use of an organic binder to hold the article together during and after the 0 forming process, thermally decomposing the binder and sintering the article.
There are many difficulties with previously practiced techniques ~or fabricating inorganic powders into useful articles. For instance, when dispersing the powder in the solvent medium, if the powder i3 not uniformly dispersed, then the undispersed powder agglomerates. The undispersed powder typically causes voids in the sintered article. The binder must also be uniformly dispersed due to similar ef~ects. Generally, it is difficult to uniformly disperse the inorganic powder and bincler in the solvent medium.
36,571-F -1-~ . , ; ,, ~ . . . .. .
Another problem with the previously practiced technique is that it is also difficult and expensive to remove the solvent medium. Typically, for roll--compacted substrates, water is removed by an expensive spray drying process. For organic-based tape casting processes~ solvent is removed by heated air, then recovered in an expensive solvent recovery system.
In particular, difficulties arise if the powder, binder and other ingredients are dry blended.
For instance, when the binder is dry blended with the inorganic powder, and water is added to form a slurry, the dry ingredients are incompletely dispersed in the slurry. The resulting article, after sintering, has large variations in density and porosity due to the incomplete dispersion of the powder and/or binder in the slurry mixture. Another blending technique practiced in the industry is to externally solubilize the binder in water and then to add the inorganic powder to the solution. The use of this tschnique results in the need to add additional water, which in turn reduces the total percent solids of the slurry, causing the mixture to have undesirable p~eudoplastic flow characteristics.
Therefore, it would be desirable to provide a process for homogeneously dispersing an inorganic powder and a binder in a solvent medium without negatively affecting the pseudoplastic flow of the mixture. It would also be desirable to have an inexpensive process to rapidly remove the solvent medium from a formed article.
The present invention includes a process for making an organic slurry, forming the slurry into a flexible article and rendering solvent from the formed 36,571-F -2-article. The present invention is directed to a process for preparing an inorganic powder slurry, comprising:
(a) admixing an inorganic powder, water and a dispersant to form a blend; (b) ball milling said blend; (c) heating said blend; (d) admixing said heated blend with a thermally gelable polymer binder to form a slurry mixture, wherein the temperature of said blend is maintained at greater than the gelable point of said binder such that the thermally gelable polymeric binder is dispersed in the slurry, wherein said slurry is of 70 - 90 weight percent solids; and (e) cooling said ~lurry mixture. The inorganic powder may be a metal or a ceramic powder or mixture thereof.
In another aspect of the invention, the slurry is extruded through a tape die to form a flexible article. The extruded tape is formed into a final shape and the solvents are removed by passing the article through a conventional heated calendar roll stack assembly.. The calendar roll stack assembly is heated to a temperature to effectively, thermally gel the binder, thereby shaping said article. Additionally, the slurry mixture could also be vacuùm formed, thereby final forming the said article.
The slurry mixture can be extruded and formed to make a variety of articles. The articles could be rods, tubes, tapes, sheets, films, resistors, plates monoliths and the like. These articles have a variety of uses in many different types of industries.
The process for preparing the slurry mixture enables homogenous dispersion of the inorganic powder and thermally gelling polymeric binder in the solvent medium without substantial agglomeration. The use of 36,571-F -3-, . ~ , .
`` 2023322 heated calendar rolls is an effective way to remove the solvent system while final forming the article. The resulting article is very dense and exhibit~
substantially no voids.
This invention provides a process ~or preparing a homogeneous, aqueous 7 inorganic slurry mixture which is rapidly dried by a process which forms a high green density inorganic article.
The homogeneous, aqueous, inorganic slurry mixture comprises ingredients which include: an inorganic powder, a dispersant, a thermally gelable polymeric binder and water. The inorganic powder used can be a ceramic powder such as an oxide, carbide, nitride, silicide, titinate, boride, sulfide, phosphides and mixtures thereof. The inorganic powder could also be a metal powder such as stainless steel, carbonyl ironi nickel, cobalt, iron, tungsten, molybdenum?
tantalum, titanium, chromium, niobium, boron, zirconium, vanadium, silicon, palladium, ha~nium, aluminum, copper, alloys thereof or mixtures thereof.
The dispersant used can be ammonium salt o~ a polyaorylate or a similar salt. Optionally, a plasticizer could be added to the slurry. The plasticizer is typically glycerine, polyethylene glycol, propylene glycol, or triethanol amine and polypropylene glycol-The thermally gslable polymeric binder can be acellulo~e ether, such as methylcellulose, hydroxypropyl methylcellulose, hydroxybutyl methylcellulose, hydroxyethyl methylcellulose. These polymers are typically insoluble in hot water, but soluble in cold 36,571-F -4-` ~ ~ ' . . ` ' i . ' ' ' ', " ' ` ": . ~ .`
water. By "thermally gelable polymeric binder" is meant that the polymer, when in an aqueous solution, will gel upon application of heat. Such polymers have thermal gelation temperatures which may be modified by adding more binder, or less water, either of which would decrease the temperature needed to reach the thermally gelable temperature.
Thermally gelable polymers employed in this invention are water-soluble. Therefore, to aid in the homogeneous dispersion of the inorganic powder and polymeric binder, an aqueous solvent is used.
Preferably, water is selected as the aqueous solvent, although a solvent which is up to 20 weight percent alcohol can also be used.
To prepare the slurry mixture, the inorganic powder, water, dispersant and optionally the plasticizer are admixed to form a blend. The blend is ball milled for a sufficient time to completely disperse the ingredients in the water and to obtain the desired particle size. Generally, the blend is ball milled for 30 minutes to 24 hours, preferably from 4 to 20 hours.
Typically, the particle size is from 0.5 to 5 micrometers. The blend i3 then heated so that the temperature is greater than the gelation point of a polymeric binder, which is subsequently added.
Generally, the blend is heated to a temperature from 50 to 100C, preferably from 70 to 90C.
The heated blend is admixed with the thermally gelable polymeric binder to form a slurry mixture.
Preferably, the binder is preheated to prevent a temperature drop in the slurry mixture. The binder can be preheated from 50 to 100C, preferably from 70C to 36,571-F _5_ ,,, :.
.: , . . ~
2Q~22 90C. After the addition of the binder, the slurry mixture is cooled to allow complete hydration o~ the thermally gelable polymeric binder in the mixture.
The slurry has high percent solids. More particularly, the slurry has from 70 to 90 weight percent solids. The percent solids of the slurry can be appropriately adjusted to alter the pseudoplastic flow of the slurry mixture if so desired, thereby permitting numerous alternative way~ of fal)ricating the slurry mixture into useful articles. Typical types of fabricating techniques employed include injection molding, vacuum forming, or coextrusion, for example.
Also, standard processing equipment can be u~ed for fabricating a variety of articles. Furthermore, along with adjusting the amount of the water and/or inorganic powder, the pseudoplasticity of the slurry mixture can be adjusted by alternating the type and concentration of the cellulose ether used.
Preferably, the slurry mixture i3 from 80 to 98 weight percent inorganic powder, from 1 to 10 weight percent thermally gelable polymeric binder, from 0.1 to 2 weight percent dispersant, optionally from 1 to 10 weight percent plasticizer, and water is added in an amount sufficient to give from 70 to 90 weight percent solids.
Preferably, the slurry mixture is from 85 to 95 weight percent inorganic powder, from 2 to 8 weight percent thermally gelable polymeric binder, from 0.2 to 1.5 weight percent dispersant, optionally from 2 to 8 weight percent plasticizer, and water is added to give from 75 to 88 weight percent solids.
36,571-F -6-Most preferably, the slurry mixture is Prom 90 to 96 weight percent inorganic powder, from 2 to 5 weight percent thermally gelable polymeric binder, from 0.3 to 0.7 weight percent dispersant, optionally from 2 to 5 weight percent plasticizer, and water is add to glve from 78 to 88 weight percent ~olids.
Th~ slurry mixture can be extruded into a flexible article, which after sintering i9 very de~se.
The inorganic slurry mixture is very viscous and pseudoplastic in character, thereby easily extruded. In order to feed the viscous slurry mixture into an auger or screw extruder, a ~eed system is designed such that the viscous slurry mixture is delivered to the feed end of the extruder at a constant rate.
Typically, the viscous slurry mixture is placed into a cylinder hopper o~ an extruder. A piston is pu~hed with pressurized air into the cylinder hopper. A
vacuum can be applied to the contents of the cylinder in order to remove entrapped air. Air pressure of from 10 to 200 psi (69 to 1,379 kPa) input is applied onto the piston which pushes the viscous mixture into the extruder screw. Various extrusion rate~ can be achieved by varying the screw speed.
The extruder is operated at ambient condition.
It is important that the temperature of the extruder be below the gel point of the thermally gelable polymeric binder, but high enough to preclude sticking to the die.
In general, the temperature range is from room temperature to the on set of gelation. Preferably, the extruder temperature can be from 20 to 30C. As the amount of water, type and concentration of the cellulose ether and plasticizer all affect the gelation 36,571-F _7_ - 2~23322 temperature, the extruding temperature needs to be optimized for any formulation change.
The various thickness and width of an article, in particular a tape, can be made by attaching an adjustable die, tape die, onto the extruder. Although any size tape can be made, generally one inch to 36 inches (2.5 to 91 cm) width and 0.005 to 0.125 (0.01 to 0.3 cm) inches thick are the most commonly preferred.
After the tape has been formed by the tape die, it is passed through a calendar roll stack assembly.
The calendar rolls are heated to a temperature of 50 to 150C. By heating the calendar rolls, the water is easily removed in a single step from the greenware tape composition. This is an inexpensive alternative to expensive spray or recovery systems for emission control. By quickly removing the water and dispersant from the extruded tape, the heated calendar rolls function as a readily assembled drier. The heated rolls can be used in an embossing mode. The surface finish of the heated metal rolls can also be adjusted to impart any desired finish to the tape. The tape can be sintered to high density with uniform porosity.
In addition to the use of a calendar roll system forming a shaped tape article, other thermoplastic processing techniques may be used after extrusion of the tape article. For instancel after extruding the tape, the tape may be vacuum formed with heat so that the formed shape is retained via the thermal gelation phase change of the polymeric binder.
Alternatively, the slurry mixture may be extruded into a parison, then a heated mold is clamped around the 36,571-F -8-_9_ parison. In this process, the polymeric binder is also thermally gelled so that the formed shape is retained.
The following examples are provided to illustrate the present invention.
Example 1 - Preparin~ the Blend The following ingredients were admixed to form a slurry:
Composition A
2760 grams Al203 33 grams triethanolamine 12 grams polyethylene glycol- E 400*
15 grams polypropylene glycol- P 1200*
7 grams ammonium salt of a polyacrylate 839 grams deionized water *Available from The Dow Chemical Company, Midland, Michigan.
The blend was then added to a 1 gallon (3.8 x 10~3 m3) ball mill and was milled for 20 hours. The milled blend was placed into a Hobart mixing bowl with a heating mantel around the bowl and covered with aluminum foil to eliminate water 103s. The blend was continuously mixed until the temperature reached 70C.
120 Grams of hydroxypropyl methylcellulose, preheated to 90C, was added to the blend to form a slurry mixture, the heating mantel was removed and mixing was continued while the mixture was cooling.
The final slurry mixture comprises:
92 weight percent Al203 1.1 weight percent triethanolamine 36,571-F -9----` 2023322 --~o--0.4 weight percent polyethy~ene glycol .5 weight percent polypropylene glycol 2.0 weight percent glycerine 4.0 weight percent hydroxypropyl 5methylcellulose, and deionized water to give 78 p~rcent solids Composition B
103680 gramis Al203 40 grams triethanolamine 80 grams glycerine 9,2 grams ammonium salts of a polyacrylate 990.8 grams water The blend was added to a 1 gallon (3.8 x 10~3 m3) ball mill and was milled for 20 hours. The milled blend was placed into a glass bowl and was microwaved for approximately 20 minutes, until the temperature reached 90C. The heated blend was mixed in a Hobart mixer. 200 Grams of hydroxypropyl methylcellulose was preheated to 90C and was added to the heated blend to form a slurry mixture. The slurry was mixed until it becomes viscous. The mixture was refrigerated overnight.
Final Composition 92 weight percent Al203 1.0 weight percent triethanolamine 2.0 weight percent glycerine 5.0 weight percent hydroxypropyl methylcellulose .25 weight percent ammonium salt of a polyacrylate, and 36,571-F -lO-~2~322 deionized water to give 80 weight percent solids.
Example 2 - Extrudin~ the Slurr~ Mixture into a Ta~e Com~osition In order to feed the viscous slurry into an extruder, the following feed system was designed and operated a~ described below:
A 4-3/4 inch (12 cm) diameter x 8 inches (20 cm) long stainless steel hopper, equipped with a gate valve at the bottom was attached to the feed end of a Haake 3/4 inch (1.9 cm) extruder. The inorganic slurry mixture was placed into the hopper.
A piston equipped with a rubber O-ring for sealing was attached to a double acting air cylinder.
The piston was pushed with low air pressure into the cylinder which contain~ the slurry mixture. A vacuum was applied for 5 minutes to remove entrained air.
165 psi (1.1 MPa) air pressure was applied onto the piston, thereby pushing the slurry mixture ir.to the extruder screw. One may vary the extrusion rates by varying the screw rpm.
Extrudin~ Com~osition Slurry mixture of Example lB was extruded at room temperature, through a 3/4 Haake extruder at 15 rpm with 165 psi (1.1 MPa) air pressure on the feeder piston. A 4 inch (10 cm) adjustable tape die was attached to the extruder and a 4.0 inch (10 cm) wide, 0.02 inch (0.5 cm) thick tape composition was made.
36,571-F -11-:
.~
.
: ,.... ., ~ ., . ~ , .: : :, :; -` 2023322 Example 3 - Drying/Fini~hin~ an Extruded Article The 4.0 inch (110 cm) wide, 0.02 inch (0.05 cm) thick extruded tape from Example II was passed through a heated calendar roll stack assembly. The roll temperature of the roll stack was 80C and had a 0.019 inch (0.05 cm) gap between rolls 1 and 2, with a line speed of 11.1 inch per minute (28 cm/min). After passing through the calendar roll assembly, the tape was analyzed to have the following properties:
Tape after dryin~
Width-3.68 inches (9.3 cm) *Thickness-.0187 inches (0.05 cm) *Tensile Strength (psi), machine direction, =
534 (3.74 MPa) *Tensile Strength (p3i), transverse direction, =
0 434 (3 MPa ) Percent Elongation, machine direction, = 12 Percent Elongation, transverse direction, = 4 *Procedure for measuring thickness and tensile strength was the following: .500 x 2.0 inch (1.3 x 5.1 cm) strips o~ the extruded tape were cut and ` conditioned for 72 hours at 72F, 50 percent ; relative humidity and then the strips were tested with an Instron Tester.
. .
Samples of the extruded tape were sintered in air for 30 minutes at 1550C. The sintered article was analyzed to have the following properties:
, ~ 36,571-F -12--` 2023~22 Sintered Tape Sintered density = 3.78 g/cc.
; Percent shrinkage, machine direction, _ 17.4 percent Percent shrinkage, Transverse direction, =
17.2 percent Processes of Examples I to 3 can also be done as a continuous process.
; .
.
~:
; 30 .' 35 ., .
.".' .
36,571-F -13-:
INORGANIC ARTICLE
Many forming techniques have been developed for fabricating inorganic powders into, such as metal or ceramic powders, useful shapes. Typical techniques used in the industry include slip casting, tape casting, isostatic pressing, extrusion, roll compacting and others. These processes typically include dispersion of the powder in a solvent medium, use of an organic binder to hold the article together during and after the 0 forming process, thermally decomposing the binder and sintering the article.
There are many difficulties with previously practiced techniques ~or fabricating inorganic powders into useful articles. For instance, when dispersing the powder in the solvent medium, if the powder i3 not uniformly dispersed, then the undispersed powder agglomerates. The undispersed powder typically causes voids in the sintered article. The binder must also be uniformly dispersed due to similar ef~ects. Generally, it is difficult to uniformly disperse the inorganic powder and bincler in the solvent medium.
36,571-F -1-~ . , ; ,, ~ . . . .. .
Another problem with the previously practiced technique is that it is also difficult and expensive to remove the solvent medium. Typically, for roll--compacted substrates, water is removed by an expensive spray drying process. For organic-based tape casting processes~ solvent is removed by heated air, then recovered in an expensive solvent recovery system.
In particular, difficulties arise if the powder, binder and other ingredients are dry blended.
For instance, when the binder is dry blended with the inorganic powder, and water is added to form a slurry, the dry ingredients are incompletely dispersed in the slurry. The resulting article, after sintering, has large variations in density and porosity due to the incomplete dispersion of the powder and/or binder in the slurry mixture. Another blending technique practiced in the industry is to externally solubilize the binder in water and then to add the inorganic powder to the solution. The use of this tschnique results in the need to add additional water, which in turn reduces the total percent solids of the slurry, causing the mixture to have undesirable p~eudoplastic flow characteristics.
Therefore, it would be desirable to provide a process for homogeneously dispersing an inorganic powder and a binder in a solvent medium without negatively affecting the pseudoplastic flow of the mixture. It would also be desirable to have an inexpensive process to rapidly remove the solvent medium from a formed article.
The present invention includes a process for making an organic slurry, forming the slurry into a flexible article and rendering solvent from the formed 36,571-F -2-article. The present invention is directed to a process for preparing an inorganic powder slurry, comprising:
(a) admixing an inorganic powder, water and a dispersant to form a blend; (b) ball milling said blend; (c) heating said blend; (d) admixing said heated blend with a thermally gelable polymer binder to form a slurry mixture, wherein the temperature of said blend is maintained at greater than the gelable point of said binder such that the thermally gelable polymeric binder is dispersed in the slurry, wherein said slurry is of 70 - 90 weight percent solids; and (e) cooling said ~lurry mixture. The inorganic powder may be a metal or a ceramic powder or mixture thereof.
In another aspect of the invention, the slurry is extruded through a tape die to form a flexible article. The extruded tape is formed into a final shape and the solvents are removed by passing the article through a conventional heated calendar roll stack assembly.. The calendar roll stack assembly is heated to a temperature to effectively, thermally gel the binder, thereby shaping said article. Additionally, the slurry mixture could also be vacuùm formed, thereby final forming the said article.
The slurry mixture can be extruded and formed to make a variety of articles. The articles could be rods, tubes, tapes, sheets, films, resistors, plates monoliths and the like. These articles have a variety of uses in many different types of industries.
The process for preparing the slurry mixture enables homogenous dispersion of the inorganic powder and thermally gelling polymeric binder in the solvent medium without substantial agglomeration. The use of 36,571-F -3-, . ~ , .
`` 2023322 heated calendar rolls is an effective way to remove the solvent system while final forming the article. The resulting article is very dense and exhibit~
substantially no voids.
This invention provides a process ~or preparing a homogeneous, aqueous 7 inorganic slurry mixture which is rapidly dried by a process which forms a high green density inorganic article.
The homogeneous, aqueous, inorganic slurry mixture comprises ingredients which include: an inorganic powder, a dispersant, a thermally gelable polymeric binder and water. The inorganic powder used can be a ceramic powder such as an oxide, carbide, nitride, silicide, titinate, boride, sulfide, phosphides and mixtures thereof. The inorganic powder could also be a metal powder such as stainless steel, carbonyl ironi nickel, cobalt, iron, tungsten, molybdenum?
tantalum, titanium, chromium, niobium, boron, zirconium, vanadium, silicon, palladium, ha~nium, aluminum, copper, alloys thereof or mixtures thereof.
The dispersant used can be ammonium salt o~ a polyaorylate or a similar salt. Optionally, a plasticizer could be added to the slurry. The plasticizer is typically glycerine, polyethylene glycol, propylene glycol, or triethanol amine and polypropylene glycol-The thermally gslable polymeric binder can be acellulo~e ether, such as methylcellulose, hydroxypropyl methylcellulose, hydroxybutyl methylcellulose, hydroxyethyl methylcellulose. These polymers are typically insoluble in hot water, but soluble in cold 36,571-F -4-` ~ ~ ' . . ` ' i . ' ' ' ', " ' ` ": . ~ .`
water. By "thermally gelable polymeric binder" is meant that the polymer, when in an aqueous solution, will gel upon application of heat. Such polymers have thermal gelation temperatures which may be modified by adding more binder, or less water, either of which would decrease the temperature needed to reach the thermally gelable temperature.
Thermally gelable polymers employed in this invention are water-soluble. Therefore, to aid in the homogeneous dispersion of the inorganic powder and polymeric binder, an aqueous solvent is used.
Preferably, water is selected as the aqueous solvent, although a solvent which is up to 20 weight percent alcohol can also be used.
To prepare the slurry mixture, the inorganic powder, water, dispersant and optionally the plasticizer are admixed to form a blend. The blend is ball milled for a sufficient time to completely disperse the ingredients in the water and to obtain the desired particle size. Generally, the blend is ball milled for 30 minutes to 24 hours, preferably from 4 to 20 hours.
Typically, the particle size is from 0.5 to 5 micrometers. The blend i3 then heated so that the temperature is greater than the gelation point of a polymeric binder, which is subsequently added.
Generally, the blend is heated to a temperature from 50 to 100C, preferably from 70 to 90C.
The heated blend is admixed with the thermally gelable polymeric binder to form a slurry mixture.
Preferably, the binder is preheated to prevent a temperature drop in the slurry mixture. The binder can be preheated from 50 to 100C, preferably from 70C to 36,571-F _5_ ,,, :.
.: , . . ~
2Q~22 90C. After the addition of the binder, the slurry mixture is cooled to allow complete hydration o~ the thermally gelable polymeric binder in the mixture.
The slurry has high percent solids. More particularly, the slurry has from 70 to 90 weight percent solids. The percent solids of the slurry can be appropriately adjusted to alter the pseudoplastic flow of the slurry mixture if so desired, thereby permitting numerous alternative way~ of fal)ricating the slurry mixture into useful articles. Typical types of fabricating techniques employed include injection molding, vacuum forming, or coextrusion, for example.
Also, standard processing equipment can be u~ed for fabricating a variety of articles. Furthermore, along with adjusting the amount of the water and/or inorganic powder, the pseudoplasticity of the slurry mixture can be adjusted by alternating the type and concentration of the cellulose ether used.
Preferably, the slurry mixture i3 from 80 to 98 weight percent inorganic powder, from 1 to 10 weight percent thermally gelable polymeric binder, from 0.1 to 2 weight percent dispersant, optionally from 1 to 10 weight percent plasticizer, and water is added in an amount sufficient to give from 70 to 90 weight percent solids.
Preferably, the slurry mixture is from 85 to 95 weight percent inorganic powder, from 2 to 8 weight percent thermally gelable polymeric binder, from 0.2 to 1.5 weight percent dispersant, optionally from 2 to 8 weight percent plasticizer, and water is added to give from 75 to 88 weight percent solids.
36,571-F -6-Most preferably, the slurry mixture is Prom 90 to 96 weight percent inorganic powder, from 2 to 5 weight percent thermally gelable polymeric binder, from 0.3 to 0.7 weight percent dispersant, optionally from 2 to 5 weight percent plasticizer, and water is add to glve from 78 to 88 weight percent ~olids.
Th~ slurry mixture can be extruded into a flexible article, which after sintering i9 very de~se.
The inorganic slurry mixture is very viscous and pseudoplastic in character, thereby easily extruded. In order to feed the viscous slurry mixture into an auger or screw extruder, a ~eed system is designed such that the viscous slurry mixture is delivered to the feed end of the extruder at a constant rate.
Typically, the viscous slurry mixture is placed into a cylinder hopper o~ an extruder. A piston is pu~hed with pressurized air into the cylinder hopper. A
vacuum can be applied to the contents of the cylinder in order to remove entrapped air. Air pressure of from 10 to 200 psi (69 to 1,379 kPa) input is applied onto the piston which pushes the viscous mixture into the extruder screw. Various extrusion rate~ can be achieved by varying the screw speed.
The extruder is operated at ambient condition.
It is important that the temperature of the extruder be below the gel point of the thermally gelable polymeric binder, but high enough to preclude sticking to the die.
In general, the temperature range is from room temperature to the on set of gelation. Preferably, the extruder temperature can be from 20 to 30C. As the amount of water, type and concentration of the cellulose ether and plasticizer all affect the gelation 36,571-F _7_ - 2~23322 temperature, the extruding temperature needs to be optimized for any formulation change.
The various thickness and width of an article, in particular a tape, can be made by attaching an adjustable die, tape die, onto the extruder. Although any size tape can be made, generally one inch to 36 inches (2.5 to 91 cm) width and 0.005 to 0.125 (0.01 to 0.3 cm) inches thick are the most commonly preferred.
After the tape has been formed by the tape die, it is passed through a calendar roll stack assembly.
The calendar rolls are heated to a temperature of 50 to 150C. By heating the calendar rolls, the water is easily removed in a single step from the greenware tape composition. This is an inexpensive alternative to expensive spray or recovery systems for emission control. By quickly removing the water and dispersant from the extruded tape, the heated calendar rolls function as a readily assembled drier. The heated rolls can be used in an embossing mode. The surface finish of the heated metal rolls can also be adjusted to impart any desired finish to the tape. The tape can be sintered to high density with uniform porosity.
In addition to the use of a calendar roll system forming a shaped tape article, other thermoplastic processing techniques may be used after extrusion of the tape article. For instancel after extruding the tape, the tape may be vacuum formed with heat so that the formed shape is retained via the thermal gelation phase change of the polymeric binder.
Alternatively, the slurry mixture may be extruded into a parison, then a heated mold is clamped around the 36,571-F -8-_9_ parison. In this process, the polymeric binder is also thermally gelled so that the formed shape is retained.
The following examples are provided to illustrate the present invention.
Example 1 - Preparin~ the Blend The following ingredients were admixed to form a slurry:
Composition A
2760 grams Al203 33 grams triethanolamine 12 grams polyethylene glycol- E 400*
15 grams polypropylene glycol- P 1200*
7 grams ammonium salt of a polyacrylate 839 grams deionized water *Available from The Dow Chemical Company, Midland, Michigan.
The blend was then added to a 1 gallon (3.8 x 10~3 m3) ball mill and was milled for 20 hours. The milled blend was placed into a Hobart mixing bowl with a heating mantel around the bowl and covered with aluminum foil to eliminate water 103s. The blend was continuously mixed until the temperature reached 70C.
120 Grams of hydroxypropyl methylcellulose, preheated to 90C, was added to the blend to form a slurry mixture, the heating mantel was removed and mixing was continued while the mixture was cooling.
The final slurry mixture comprises:
92 weight percent Al203 1.1 weight percent triethanolamine 36,571-F -9----` 2023322 --~o--0.4 weight percent polyethy~ene glycol .5 weight percent polypropylene glycol 2.0 weight percent glycerine 4.0 weight percent hydroxypropyl 5methylcellulose, and deionized water to give 78 p~rcent solids Composition B
103680 gramis Al203 40 grams triethanolamine 80 grams glycerine 9,2 grams ammonium salts of a polyacrylate 990.8 grams water The blend was added to a 1 gallon (3.8 x 10~3 m3) ball mill and was milled for 20 hours. The milled blend was placed into a glass bowl and was microwaved for approximately 20 minutes, until the temperature reached 90C. The heated blend was mixed in a Hobart mixer. 200 Grams of hydroxypropyl methylcellulose was preheated to 90C and was added to the heated blend to form a slurry mixture. The slurry was mixed until it becomes viscous. The mixture was refrigerated overnight.
Final Composition 92 weight percent Al203 1.0 weight percent triethanolamine 2.0 weight percent glycerine 5.0 weight percent hydroxypropyl methylcellulose .25 weight percent ammonium salt of a polyacrylate, and 36,571-F -lO-~2~322 deionized water to give 80 weight percent solids.
Example 2 - Extrudin~ the Slurr~ Mixture into a Ta~e Com~osition In order to feed the viscous slurry into an extruder, the following feed system was designed and operated a~ described below:
A 4-3/4 inch (12 cm) diameter x 8 inches (20 cm) long stainless steel hopper, equipped with a gate valve at the bottom was attached to the feed end of a Haake 3/4 inch (1.9 cm) extruder. The inorganic slurry mixture was placed into the hopper.
A piston equipped with a rubber O-ring for sealing was attached to a double acting air cylinder.
The piston was pushed with low air pressure into the cylinder which contain~ the slurry mixture. A vacuum was applied for 5 minutes to remove entrained air.
165 psi (1.1 MPa) air pressure was applied onto the piston, thereby pushing the slurry mixture ir.to the extruder screw. One may vary the extrusion rates by varying the screw rpm.
Extrudin~ Com~osition Slurry mixture of Example lB was extruded at room temperature, through a 3/4 Haake extruder at 15 rpm with 165 psi (1.1 MPa) air pressure on the feeder piston. A 4 inch (10 cm) adjustable tape die was attached to the extruder and a 4.0 inch (10 cm) wide, 0.02 inch (0.5 cm) thick tape composition was made.
36,571-F -11-:
.~
.
: ,.... ., ~ ., . ~ , .: : :, :; -` 2023322 Example 3 - Drying/Fini~hin~ an Extruded Article The 4.0 inch (110 cm) wide, 0.02 inch (0.05 cm) thick extruded tape from Example II was passed through a heated calendar roll stack assembly. The roll temperature of the roll stack was 80C and had a 0.019 inch (0.05 cm) gap between rolls 1 and 2, with a line speed of 11.1 inch per minute (28 cm/min). After passing through the calendar roll assembly, the tape was analyzed to have the following properties:
Tape after dryin~
Width-3.68 inches (9.3 cm) *Thickness-.0187 inches (0.05 cm) *Tensile Strength (psi), machine direction, =
534 (3.74 MPa) *Tensile Strength (p3i), transverse direction, =
0 434 (3 MPa ) Percent Elongation, machine direction, = 12 Percent Elongation, transverse direction, = 4 *Procedure for measuring thickness and tensile strength was the following: .500 x 2.0 inch (1.3 x 5.1 cm) strips o~ the extruded tape were cut and ` conditioned for 72 hours at 72F, 50 percent ; relative humidity and then the strips were tested with an Instron Tester.
. .
Samples of the extruded tape were sintered in air for 30 minutes at 1550C. The sintered article was analyzed to have the following properties:
, ~ 36,571-F -12--` 2023~22 Sintered Tape Sintered density = 3.78 g/cc.
; Percent shrinkage, machine direction, _ 17.4 percent Percent shrinkage, Transverse direction, =
17.2 percent Processes of Examples I to 3 can also be done as a continuous process.
; .
.
~:
; 30 .' 35 ., .
.".' .
36,571-F -13-:
Claims (12)
1. A process for preparing an inorganic powder slurry, comprising:
(a) admixing an inorganic powder, water and a dispersant to form a blend;
(b) ball milling said blend;
(c) heating said blend;
(d) admixing said heated blend with a thermally gelable polymer binder to form a slurry mixture, wherein the temperature of said blend is maintained at greater than the gelation point of said binder such that the thermally gelable polymeric binder is effectively dispersed in the slurry; and (e) cooling said slurry mixture.
(a) admixing an inorganic powder, water and a dispersant to form a blend;
(b) ball milling said blend;
(c) heating said blend;
(d) admixing said heated blend with a thermally gelable polymer binder to form a slurry mixture, wherein the temperature of said blend is maintained at greater than the gelation point of said binder such that the thermally gelable polymeric binder is effectively dispersed in the slurry; and (e) cooling said slurry mixture.
2. The process of in Claim 1, wherein the blend is heated to a temperature of 50 to 100°C.
3. The process of Claim 1, wherein the inorganic slurry also contains a plasticizer. comprising glycerine, polyethylene glycol, propylene glycol, triethanol amine or polypropylene glycol.
36,571-F -14-
36,571-F -14-
4. The process of Claim 19 wherein the inorganic powder is a metal powder or ceramic powder.
5. The process of Claim 4, wherein the metal is stainless steel, carbonyl iron, nickel, cobalt, iron, tungsten, molybdenum, tantalum, titanium, chromium, niobium, boron, zirconium, vanadium, silicon, palladium, hafnium, aluminum, copper, alloys thereof or mixtures thereof.
6. The process of Claim 4, wherein the ceramic powder is oxide, carbide, nitride, silicide, boride, titinate, sulfide, phosphide and mixtures thereof.
7. The process of Claim 19 wherein the dispersant is an ammonium salt of a polyacrylate.
8. The process of Claim 1, wherein the slurry comprises: 80 to 98 weight percent inorganic powder, 1 to 10 weight percent thermally gelable polymeric binder, 1 to 10 weight percent plasticizer, 0.1 to 2 weight percent dispersant, and with a sufficient amount of water to give 70 to 90 weight percent solids.
9. The process of Claim 1, wherein the binder is a cellulose ether.
10. The process of Claim 9, wherein the cellulose ether is methylcellulose, hydroxypropyl methylcellulose, hydroxybutyl methylcellulose or hydroxyethyl methylcellulose.
11. The process of Claim 1, wherein the slurry comprises 70 to 90 weight percent solids.
36,571-F -15-
36,571-F -15-
12. A process for extruding a flexible article, comprising:
(a) extruding an inorganic slurry mixture containing a dispersant, a thermally gelable polymeric binder, and water as claimed in any one of Claims 1 through 4, wherein said slurry mixture comprises 70 to 90 weight percent solids, through a die to form a flexible formed article, and (b) shaping the final configuration of said formed article by passing said article through a heated calendar roll stack assembly, wherein said heated calendar rolls are heated to a temperature effective to thermally gel the binder and remove water or solvents from the article.
36,571-F -16-
(a) extruding an inorganic slurry mixture containing a dispersant, a thermally gelable polymeric binder, and water as claimed in any one of Claims 1 through 4, wherein said slurry mixture comprises 70 to 90 weight percent solids, through a die to form a flexible formed article, and (b) shaping the final configuration of said formed article by passing said article through a heated calendar roll stack assembly, wherein said heated calendar rolls are heated to a temperature effective to thermally gel the binder and remove water or solvents from the article.
36,571-F -16-
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA 2023322 CA2023322A1 (en) | 1990-08-15 | 1990-08-15 | Process for preparing an inorganic article |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA 2023322 CA2023322A1 (en) | 1990-08-15 | 1990-08-15 | Process for preparing an inorganic article |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2023322A1 true CA2023322A1 (en) | 1992-02-16 |
Family
ID=4145737
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA 2023322 Abandoned CA2023322A1 (en) | 1990-08-15 | 1990-08-15 | Process for preparing an inorganic article |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA2023322A1 (en) |
-
1990
- 1990-08-15 CA CA 2023322 patent/CA2023322A1/en not_active Abandoned
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