Continuous production method of furandicarboxylic acid with furan as raw material
A technology of furandicarboxylic acid and production method, applied in the chemical field, can solve the problems of long FDCA reaction route, poor atom economy and high raw material cost, and achieve the effects of high atom utilization rate, high total yield and lower production cost
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Embodiment 1
[0039] Embodiment 1, a kind of continuous production method of furandicarboxylic acid, take furan and carbon dioxide as raw material, carry out following steps successively:
[0040]1), preparation of Pd / 4A type molecular sieve catalyst by impregnation method: dissolve 3.732g palladium potassium chlorate (containing palladium 1.01g) in 100mL water, fully disperse and dissolve; at the same time fully disperse 100g 4A type molecular sieve in 1000mL water, mix the two Thoroughly stir (about 600r / min) and mix for 3 hours, let it stand for 2 hours, conventionally dry (dry at 40°C for 12 hours), and then calcinate at 400°C for 5 hours to obtain about 101g of Pd / 4A molecular sieve catalyst.
[0041] 2) Fix 100 g of the Pd / 4A molecular sieve catalyst obtained in step 1) in the fixed bed reactor 2, add 1.0 kg of furan into the furan gas generator 1, control the gaseous furan and carbon dioxide to mix according to the molar ratio of 1:3 (as fresh mixed raw material gas) enters the fixed...
Embodiment 2
[0042] Embodiment 2, a kind of continuous production method of furandicarboxylic acid, take furan and carbon dioxide as raw materials, carry out the following steps successively:
[0043] 1) Preparation of Ni / Y-type molecular sieve catalyst by impregnation method: Dissolve 2.665g of nickel chloride (containing 1.21g of nickel) in 100mL of water, fully disperse and dissolve; Mix well for 6 hours, let stand for 1 hour, dry and roast at 600°C for 3 hours to obtain about 101.2 g of Ni / Y molecular sieve catalyst;
[0044] 2), fix 75g of the Ni / Y type molecular sieve catalyst obtained in step 1) in the fixed bed reactor 2, add 1.0kg of furan into the furan gas generator 1, control the gaseous furan and carbon dioxide to mix according to the molar ratio of 1:5 Enter the fixed bed reactor 2, and the reaction temperature in the fixed bed reactor 2 is set to 120°C. The unreacted furan gas and carbon dioxide are discharged from the gas outlet 22 at the bottom of the fixed-bed reactor 2,...
Embodiment 3
[0045] Embodiment 3, a kind of continuous production method of furandicarboxylic acid, take furan and carbon dioxide as raw material, carry out the following steps successively:
[0046] 1), preparation of Rh / X type molecular sieve catalyst by impregnation method: 3.059g rhodium trichloride (containing rhodium 1.51g) is dissolved in the water of 100mL, fully disperses and dissolves; The X type molecular sieve of 100g is fully dispersed in 1000mL water at the same time, will The two are fully mixed for 4 hours, left to stand for 1.5 hours, dried and calcined at 500°C for 4.5 hours to obtain about 101.5g of Rh / X molecular sieve catalyst;
[0047] 2) Fix 50 g of the Rh / X molecular sieve catalyst obtained in step 1) in the fixed bed reactor 2, add 1.0 kg of furan into the furan gas generator 1, and control the gaseous furan and carbon dioxide to mix according to the molar ratio of 1:4 Enter the fixed-bed reactor 2, and the reaction temperature in the fixed-bed reactor 2 is set to ...
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