Design and Control of Glycerol-tert-Butyl Alcohol Etherification Process

Table 1

Equilibrium constants and rate constants [19].

Equilibrium constant	Rate constant/(mol s^−1 kg^−1)
𝐾eq1=exp(2.581−754.8/𝑇)	𝑘1=exp(17342−6835/𝑇)
𝐾eq2=exp(1.228−942.1/𝑇)	𝑘2=exp(26953−10382/𝑇)
𝐾eq3=exp(1.779−2212/𝑇)	𝑘3=exp(26953−10382/𝑇)
—	𝑘4=exp(23.358−12480/𝑇)