Abstract: There is provided a method for producing a beta-alumina solid electrolyte without calcination of starting materials, according to which the step of synthesizing a magnesium-aluminum spinel starting material is not needed and a beta-alumina solid electrolyte of low resistance can be produced at lower cost. According to this method, the beta-alumina solid electrolyte is produced without carrying out calcination of the starting materials by granulating a slurry obtained by milling and mixing starting materials of an aluminum source, a magnesium source and a sodium source in water, molding the granulated product and then firing the molded product. In this method, magnesium hydroxide is used as the magnesium source and an active spinel high in reactivity is synthesized in the course of firing, and citric acid is added to the slurry as a dispersing agent.

Abstract: There is provided a method for producing a beta-alumina solid electrolyte without calcination of starting materials, according to which the step of synthesizing a magnesium-aluminum spinel starting material is not needed and a beta-alumina solid electrolyte of low resistance can be produced at lower cost. According to this method, the beta-alumina solid electrolyte is produced without carrying out calcination of the starting materials by granulating a slurry obtained by milling and mixing starting materials of an aluminum source, a magnesium source and a sodium source in water, molding the granulated product and then firing the molded product. In this method, magnesium hydroxide is used as the magnesium source and an active spinel high in reactivity is synthesized in the course of firing, and citric acid is added to the slurry as a dispersing agent.

Abstract: A beta-alumina solid electrolyte for use in a sodium-sulfur battery is composed of beta-alumina crystals having a degree of orientation toward the C axis thereof, of 0.2-0.4 and an aspect ratio of 4.0 or less. The beta-alumina solid electrolyte is composed of the beta-alumina crystals having a degree of orientation toward the C axis thereof, of 0.2-0.4 and has such a particle diameter distribution that the average particle diameter is 3 .mu.m or less, the proportion of the particles having a particle diameter of 5 .mu.m or less is 90% or more, and the maximum particle diameter is 300 .mu.m or less. A process for producing a beta-alumina solid electrolyte using an alumina source material, a magnesium source material and a sodium source material, uses a magnesium-aluminum spinel as the magnesium source material and subjects all materials to mixing, granulation, molding and firing to obtain a beta-alumina solid electrolyte without subjecting the materials to calcination.

Abstract: A beta-alumina solid electrolyte for use in a sodium-sulfur battery is composed of beta-alumina crystals having a degree of orientation toward the C axis thereof, of 0.2-0.4 and an aspect ratio of 4.0 or less. The beta-alumina solid electrolyte is composed of the beta-alumina crystals having a degree of orientation toward the C axis thereof, of 0.2-0.4 and has such a particle diameter distribution that the average particle diameter is 3 .mu.m or less, the proportion of the particles having a particle diameter of 5 .mu.m or less is 90% or more, and the maximum particle diameter is 300 .mu.m or less. A process for producing a beta-alumina solid electrolyte using an alumina source material, a magnesium source material and a sodium source material, uses a magnesium-aluminum spinel as the magnesium source material and subjects all materials to mixing, granulation, molding and firing to obtain a beta-alumina solid electrolyte without subjecting the materials to calcination.

Abstract: A process for producing high density SiC sintered bodies by primarily firing and then hot isostatic pressing. The process includes the steps of formulating a powder consisting essentially of 90.0 to 99.8% by weight of the SiC powder, boron or a boron-containing compound in an amount of 0.1 to 5.0% by weight when calculated as boron, and carbon or a carbon-producing organic compound in an amount of 0.1 to 5.0% by weight when calculated as carbon, mixing and shaping the formulated powder, firing the shaped bodies in a temperature range from 1,900.degree. to 2,300.degree. C. in vacuum or in an inert gas atmosphere, and then hot isostatically pressing the fired bodies in a temperature range from 1,800.degree. to 2,200.degree. C. under a pressure of not less than 100 atms in an inert gas atmosphere. The SiC powder is an SiC mixed powder consisting essentially of 95.0 to 99.