A method of preparing caffeine
A technology of caffeine and theophylline sodium salt is applied in the methylation of theophylline sodium salt to obtain caffeine. Uneven mixing and other problems, to achieve the effect of eliminating VOCs emissions, saving manpower, and eliminating batch differences
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0025] Embodiment 1: prepare crude product caffeine with the inventive method
[0026] Preparation of tea sodium feed solution with a mass content of 15%. The sodium tea solution at a flow rate of 24 mL / min and the dimethyl sulfate at a flow rate of 1.6 ml / min were simultaneously fed into the continuous mixing reactor, and the molar ratio of dimethyl sulfate to theophylline sodium salt was controlled to be 1.1:1. Adjust the pH value to between 8 and 10 with 30% sodium hydroxide solution. The reaction temperature was controlled to be 50°C. The effluent enters the crystallization tank for cooling and crystallization. When the temperature dropped below 20°C, solid-liquid separation was carried out, followed by drying to obtain 127.4 g of crude caffeine. The yield of crude caffeine was 98.8%.
Embodiment 2
[0028] The tea sodium feed solution with a mass content of 13% was prepared. The tea sodium solution with a flow rate of 24mL / min and the dimethyl sulfate with a flow rate of 1.82ml / min were simultaneously fed into the continuous mixing reactor, and the molar ratio of dimethyl sulfate to theophylline sodium salt was controlled to be 1.2:1. Adjust the pH value to between 8 and 10 with 30% potassium hydroxide solution. The reaction temperature was controlled to be 50°C. The effluent enters the crystallization tank for cooling and crystallization. When the temperature dropped below 20°C, solid-liquid separation was carried out, followed by drying to obtain 126.9 g of crude caffeine. The yield of crude caffeine was 98.4%.
Embodiment 3
[0030] The tea sodium feed solution with a mass content of 12% was prepared. The sodium tea solution with a flow rate of 24mL / min and the dimethyl sulfate with a flow rate of 2.18ml / min were simultaneously fed into the continuous mixing reactor, and the molar ratio of dimethyl sulfate to theophylline sodium salt was controlled to be 1.3:1. Adjust the pH value to between 8 and 10 with 30% sodium hydroxide solution. The reaction temperature was controlled to be 45°C. The effluent enters the crystallization tank for cooling and crystallization. When the temperature dropped below 20°C, solid-liquid separation was carried out, followed by drying to obtain 127.01 g of crude caffeine. The yield of crude caffeine was 98.5%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
