Abstract:
A process for producing dry α-L-aspartyl-L-phenylalanine methyl ester having an improved solubility from wet crystals of α-L-aspartyl-L-phenylalanine methyl ester having a water content of at least 20% by weight, which comprises drying the wet crystals at a temperature of higher than 50°C to obtain moist crystals having a water content of less than 20 and more than l5% by weight, then drying the moist crystals at a temperature of not higher than 50°C to obtain semi-dry crystals having a water content of less than 5% by weight, and further drying the semi-dry crystals at a temperature of higher than 50°C to obtain dry crystals of α-L-aspartyl-L-phenylalanine methyl ester.
Abstract:
A process for producing stable α-L-aspartyl-L-phenylalanine methyl ester, which comprises heat-treating crystals of α-L-aspartyl-L-phenylalanine methyl ester having a water content of from 5 to l5% by weight based on wet crystals, at a temperature of higher than 50°C and lower than 80°C for at least 30 minutes.
Abstract:
An ion-exchanger is provided which comprises zirconium hydroxide supported on active carbon. A process for producing the ion-exchanger, and a process for removing a multiply charged anion by using the ion-exchanger are also provided. The ion-exchanger of the present invention has high chemical resistance, high heat resistance, high mechanical strength, and excellent ion exchange characteristics.
Abstract:
An ion-exchanger is provided which comprises zirconium hydroxide supported on active carbon. A process for producing the ion-exchanger, and a process for removing a multiply charged anion by using the ion-exchanger are also provided. The ion-exchanger of the present invention has high chemical resistance, high heat resistance, high mechanical strength, and excellent ion exchange characteristics.
Abstract:
A process for producing dry α-L-aspartyl-L-phenylalanine methyl ester having an improved solubility from wet crystals of α-L-aspartyl-L-phenylalanine methyl ester having a water content of at least 20% by weight, which comprises drying the wet crystals at a temperature of higher than 50°C to obtain moist crystals having a water content of less than 20 and more than l5% by weight, then drying the moist crystals at a temperature of not higher than 50°C to obtain semi-dry crystals having a water content of less than 5% by weight, and further drying the semi-dry crystals at a temperature of higher than 50°C to obtain dry crystals of α-L-aspartyl-L-phenylalanine methyl ester.
Abstract:
A process for producing stable α-L-aspartyl-L-phenylalanine methyl ester, which comprises heat-treating crystals of α-L-aspartyl-L-phenylalanine methyl ester having a water content of from 5 to l5% by weight based on wet crystals, at a temperature of higher than 50°C and lower than 80°C for at least 30 minutes.