CN114751733B - Production method of spherical ceramic filler with low temperature coefficient - Google Patents
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Abstract
A production method of spherical ceramic filler with low temperature coefficient belongs to the field of electronic materials, and comprises the processes of proportioning, ball milling, stirring, spray drying, ceramic powder preparation and the like of 100 parts of ceramic filler, 0.5-10 parts of modifier, 50 parts of deionized water, 8-12 parts of PVA solution, 3-8 parts of PEG solution and 0.5-3 parts of silane coupling agent. The grain diameter of the prepared ceramic powder is between 8 and 40 mu m. The method solves the problems that in the prior art, large-particle-size ceramic fillers are irregular in appearance and randomly distributed, the ceramic fillers have large temperature coefficient, long-chain ends are easy to soft agglomerate after surface modification, the composite interface of resin and ceramics is poor, the powder thickness is different, the yield of particle size classification screening is not high, and the batch production cost is high. The preparation method has the characteristics of higher dielectric constant, small temperature coefficient, high sphericity, simple production process, capability of batch production and the like. The method is widely applied to the field of high-speed microwave composite medium substrates.
Description
Technical Field
The invention belongs to the field of electronic materials, and further relates to the field of high-frequency electronic materials, in particular to a spherical ceramic filler with high dielectric constant, low temperature coefficient and large particle size for a high-frequency plate and a batch production method thereof.
Background
In high-frequency circuit base materials, one of the main application directions of ceramic powder is as a filler, and the ceramic powder is often used in high frequencyThe copper-clad plate is used as a functional material for adjusting the dielectric constant of the copper-clad plate, increasing the functionality, improving the comprehensive performance, reducing the cost and the like. In high-frequency copper-clad plate production enterprises, the American Rogers company is used as an industry leading unit, a great amount of ceramic fillers are used in the existing copper-clad plates such as RT6000 series and TMM series, the ceramic addition amount is up to 50-90 wt%, and the particle size D50 is between 5 and 30 mu m. The domestic ceramic powder manufacturers mainly produce microwave ceramic powder, MLCC ceramic powder and LTCC powder, the main application directions of the ceramic powder manufacturers are 5G filters, MLCC devices and LTCC devices, the particle size D50 of the powder is basically between 0.2 and 3 mu m, the powder is used in ceramic filling type copper-clad plates, such as Rogers 6000 series and TMM series, the phenomena of easy agglomeration and the like are presented, and the high-frequency loss of the prepared plate is high; and often high dielectric ceramic fillers such as TiO 2 、BaTiO 3 、CaTi0 3 、SrTiO 3 When the dielectric constant temperature coefficient of the materials is negative and is more than 800 ppm/DEG C, and the zero temperature coefficient copper-clad plate is prepared, the positive temperature coefficient ceramic filler such as SiO is often used 2 、Al 2 O 3 The materials being multiphase-compounded, e.g. SiO 2 /TiO 2 Resin, al 2 O 3 /TiO 2 In the preparation process of the composite system such as resin, due to different fillers, the volume density of the composite system is inconsistent, and the layering is easy to occur in the composite process, so that the three-phase composite is not uniform; meanwhile, the inorganic oxide is polar molecules and shows hydrophilicity, and the common resin of the high-frequency copper-clad plate is polytetrafluoroethylene resin, hydrocarbon resin, polyphenyl ether resin and other materials which all show hydrophobicity, so that the composite interface of the two materials is poor.
In the prior art, the main production scheme of the ceramic filler is that inorganic oxides are subjected to high-temperature calcination, crushing and airflow classification to prepare ceramic powder, and then the ceramic powder is subjected to surface treatment by a silane coupling agent to prepare the ceramic filler, the micro-morphology of the ceramic filler prepared by the method is irregular and randomly distributed as shown in figure 1, meanwhile, the process is physically crushed, the powder is different in fineness in the crushing process, a large amount of fine powder is generated, the powder is wide in particle size distribution as shown in figure 2, and although particle size screening can be performed by airflow classification, the yield is not high, and the mass production cost is high. In addition, in subsequent application, a silane coupling agent is used for carrying out surface modification on ceramic powder, media such as alcohol and deionized water are usually used as dispersion liquid in the modification process, dehydration and drying are carried out after the modification is finished, and the phenomenon of soft agglomeration and hardening of the powder is caused because the long chain section of the silane coupling agent is easy to physically wind in the drying process. The filler prepared by the method is combined with resin to prepare the high-frequency microwave dielectric substrate, and the comprehensive performance is poor.
Therefore, according to the invention, the inorganic ceramic powder is doped in a trace manner, the dielectric constant temperature coefficient of the powder is improved, the spherical filler is prepared in a spray granulation and high-temperature sintering manner, the surface of the spherical filler is treated by using the silane coupling agent, and the spherical filler is dried by using the spray tower, so that the long chain end of the silane coupling agent is more prone to winding and wrapping the spherical powder under the action of centrifugal force, and the prepared filler with better flowability is prepared, thereby improving the compounding uniformity of the powder and resin and optimizing the compounding interface.
In view of the above, the present invention is particularly proposed.
Disclosure of Invention
The technical problem to be solved by the invention is as follows: the problems that in the prior art, high dielectric constant and large-particle size ceramic fillers are irregular in appearance and randomly distributed, high in temperature coefficient, easy to agglomerate in a coupling agent modified long chain segment, poor in resin and ceramic composite interface, different in powder thickness degree, low in particle size grading screening output and high in batch production cost are solved.
Therefore, the invention provides a large-particle-diameter spherical ceramic filler with high dielectric constant and low temperature coefficient for a high-frequency plate, which comprises the following components: tiO 2 2 、CaTiO 3 、SrTiO 3 、BaTiO 3 Weighing 100 parts of ceramic filler and 0.5-10 parts of doping modifier which is SiO 2 、Al 2 O 3 、CuO、ZnO、Mn 2 O 3 50 parts of deionized water, 8-12 parts of PVA solution, 3-8 parts of PEG solution and 0.5-3 parts of silane coupling agent.
The invention provides a production method of a spherical ceramic filler with a low temperature coefficient, which comprises the following processes:
(1) Preparing materials: the ceramic filler is TiO 2 、CaTiO 3 、SrTiO 3 One of the materials is 100 parts of ceramic filler, 0.5-10 parts of doping modifier, 50 parts of deionized water, 8-12 parts of PVA solution and 3-8 parts of PEG solution.
(2) Ball milling: and mixing and ball milling the ceramic filler for 4-6 h.
(3) Stirring: after the ball milling is finished, the mixed solution is led into a stirring device for stirring, and the stirring speed is 100 r/min-300 r/min.
(4) And (3) spray drying: in the stirring process, a spray drying device is used for spray drying the mixed solution, the inlet temperature of the spray drying device is 220-260 ℃, the outlet temperature is 110-130 ℃, the rotating speed of an atomizer is 8000-16000 r/min, and the rotating speed of the atomizer is controlled to prepare the granulating powder with different grain diameters.
(5) Preparing ceramic powder: and (3) calcining the spray granulation powder at high temperature, wherein the high-temperature sintering temperature is 1000-1400 ℃, the heat preservation time is 4h +/-11 h, and the grain size of the prepared ceramic powder is 8-40 mu m.
(6) Surface modification: and preparing a mixed solution by using deionized water and alcohol, wherein the mass ratio of the deionized water to the alcohol is 15. Taking 50 parts of the prepared ceramic powder and 75 parts of deionized water/alcohol mixed solution, and stirring and dispersing at a high speed by using a high-speed dispersion machine, wherein the stirring speed is 800 r/min-3000 r/min, and the stirring time is 2 h-6 h. And after stirring, adding 0.5 to 3 parts of silane coupling agent, and stirring for 2 hours.
(7) Secondary spray drying: (6) And (3) carrying out spray drying on the mixed solution by using a spray drying device, wherein the inlet temperature of the spray drying device is 220-260 ℃, the outlet temperature of the spray drying device is 110-130 ℃, and the rotating speed of an atomizer is 8000-16000 r/min, so as to prepare the surface modified ceramic powder.
The large-particle-size ceramic filler has the characteristics of high dielectric constant, low temperature coefficient, high sphericity, centralized particle size distribution, good high-frequency performance, simple production process, capability of batch production and the like. The method is suitable for the field of manufacturing high-speed microwave composite dielectric substrates.
Drawings
FIG. 1 is a schematic diagram of the effect of a large-particle-size filler after air flow classification in the prior art.
FIG. 2 is a schematic diagram of the effect of the crushed large-particle-size filler in the prior art.
FIG. 3 shows TiO of the present invention 2 The granulation effect is shown schematically.
FIG. 4 shows TiO of the present invention 2 The effect of the spherical filler is shown schematically.
FIG. 5 is a view of TiO in accordance with the present invention 2 The contact angle test results after surface modification are shown schematically.
FIG. 6 shows BaTiO of the present invention 3 Schematic diagram of spray granulation effect.
FIG. 7 shows BaTiO of the present invention 3 The effect of the spherical filler is shown schematically.
FIG. 8 shows BaTiO of the present invention 3 The contact angle test results after surface modification are shown schematically.
Detailed Description
A production method of spherical ceramic filler with low temperature coefficient comprises the following specific embodiments:
example 1:
(1) Using TiO 2 As ceramic filler, al 2 0 3 One or more of MnO and CuO as doping modifier, tiO 2 Weighing 50 parts, weighing 3-8 parts of modifier, adding 100 parts of deionized water, 10 parts of PVA solution, 6.4 parts of PEG solution, and ball-milling for 5 hours.
(2) After the ball milling is finished, the mixed solution is led into a stirring tank, and the stirring speed is 100 r/min-300 r/min.
(3) In the stirring process, a spray drying tower is used for spray drying the mixed solution, the inlet temperature of the spray drying tower is 220-260 ℃, the outlet temperature is 110-130 ℃, the rotation speed of an atomizer is 8000 r/min-16000 r/min, and the granulation is shown in figure 3.
(4) Spray granulating powder, and calcining at high temperature, wherein the high-temperature sintering temperature is 1000-1400 ℃, the heat preservation time is 4h +/-11 h, the particle size of the prepared ceramic powder is 10-20 μm, as shown in figure 4, the dielectric constant of the synthesized spherical titanium dioxide is 83, and the temperature coefficient of the dielectric constant is-152 ppm/DEG C.
(5) And (2) taking 30 parts of synthesized spherical titanium dioxide and 45 parts of deionized water/alcohol mixed solution, stirring at a high speed of 2000r/min for 3 hours, adding 2 parts of silane coupling agent after stirring, wherein the silane coupling agent is one or more of Z6214, KH550, KH570 and F8261, and continuously stirring for 2 hours.
(6) And stirring the mixed solution, and performing spray drying, wherein the inlet temperature of a spray drying device is 220-260 ℃, the outlet temperature is 110-130 ℃, the rotating speed of an atomizer is 8000-16000 r/min, the prepared surface modified ceramic powder is hydrophobic, and the test of the surface contact angle is shown in figure 5.
Example 2:
(1) Using BaTiO 3 As ceramic filler, tiO 2 ZnO, cuO as doping modifier, baTiO 3 50 parts of filler, 0.5-10 parts of modifier, 100 parts of deionized water, 11 parts of PVA solution, 5 parts of PEG solution and ball milling for 4 hours.
(2) After the ball milling is finished, the mixed solution is led into a stirring tank, and the stirring speed is 100 r/min-300 r/min.
(3) And in the stirring process, spray drying the mixed solution by using a spray drying tower, wherein the inlet temperature of the spray drying tower is 220-260 ℃, the outlet temperature is 110-130 ℃, the rotating speed of an atomizer is 8000-16000 r/min, and granulating powder is prepared by spray drying, the granulation is shown in figure 5, the grain diameter of the granules is 40-60 mu m, the dielectric constant of the synthesized spherical barium titanate material is 38, and the temperature coefficient of the dielectric constant is 2 ppm/DEG C.
(4) Spraying and granulating the powder, and calcining at high temperature, wherein the high-temperature sintering temperature is 1000-1400 ℃, the heat preservation time is 4h +/-11 h, and the particle size of the prepared ceramic powder is 30-40 mu m, as shown in figure 6.
(5) And (2) taking 30 parts of synthesized spherical barium titanate and 45 parts of deionized water/alcohol mixed solution, stirring at a high speed of 1800r/min for 3 hours, adding 2 parts of silane coupling agent after stirring, wherein the silane coupling agent is one or more of Z6214, KH550, KH570 and F8261, and continuously stirring for 2 hours.
(6) And stirring the mixed solution, and performing spray drying, wherein the inlet temperature of a spray drying device is 220-260 ℃, the outlet temperature is 110-130 ℃, the rotating speed of an atomizer is 8000-16000 r/min, the prepared surface modified ceramic powder is hydrophobic, and the test of the surface contact angle is shown in figure 8.
Finally, it should be noted that: the above examples are given for clarity of illustration only, and the present invention includes but is not limited to the above examples, which are neither exhaustive nor exhaustive of all embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. Embodiments that meet the requirements of the present invention are within the scope of the present invention.
Claims (3)
1. A production method of spherical ceramic filler with low temperature coefficient is characterized by comprising the following processes:
(1) Preparing materials: the ceramic filler is TiO 2 Or BaTiO 3 Weighing 100 parts of ceramic filler, 0.5-10 parts of doping modifier, 50 parts of deionized water, 8-12 parts of PVA solution and 3-8 parts of PEG solution;
(2) Ball milling: mixing and ball milling the ceramic filler for 4-6 h;
(3) Stirring: after the ball milling is finished, introducing the mixed solution into a stirring device for stirring, wherein the stirring speed is 100 r/min-300 r/min;
(4) And (3) spray drying: in the stirring process, a spray drying device is used for spray drying the mixed solution, the inlet temperature of the spray drying device is 220-260 ℃, the outlet temperature is 110-130 ℃, the rotating speed of an atomizer is 8000-16000 r/min, and the rotating speed of the atomizer is controlled to prepare the granulation powder with different grain diameters;
(5) Preparing ceramic powder: carrying out high-temperature calcination on the spray granulation powder, wherein the high-temperature sintering temperature is 1000-1400 ℃, the heat preservation time is 9 hours, and the particle size of the prepared ceramic powder is 8-40 mu m;
(6) Surface modification: preparing a mixed solution by using deionized water and alcohol, wherein the mass ratio of the deionized water to the alcohol is 15;
(7) Secondary spray drying: spray-drying the mixed solution in the step (6) by using a spray-drying tower, wherein the inlet temperature of a spray-drying device is 220-260 ℃, the outlet temperature is 110-130 ℃, and the rotating speed of an atomizer is 8000 r/min-16000 r/min, so as to prepare surface-modified ceramic powder;
the doping modifier is SiO 2 、Al 2 O 3 One or more of ZnO and CuO;
the silane coupling agent is one or more of Z6214, KH550, KH570 and F8261.
2. The method for producing spherical ceramic packing with low temperature coefficient according to claim 1, wherein the stirring device is a stirring tank.
3. The method for producing spherical ceramic packing with low temperature coefficient according to claim 1, wherein the spray drying apparatus is a spray drying tower.
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