Method for preparing high-purity dimethyl ether free from extraneous odour
A technology of dimethyl ether and no peculiar smell is applied in the field of preparing high-purity dimethyl ether without peculiar smell, which can solve the problems of peculiar smell and high manufacturing cost, and achieve the effects of low manufacturing cost, simple preparation process and saving production cost.
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Embodiment 1
[0017] Raw material GZ 01 50 tons, measure the raw material methanol content of 75%, PH value ≈ 6.5, add 150.0 kg of NaOH or KOH solution with a concentration of 2%, adjust the pH value of the methanol raw material to 7-8, and use the raw material pump to transport the methanol raw material to the raw material evaporator Evaporate into methanol vapor, enter the synthesis reactor, and use r-AL at a temperature of 250.0°C and a pressure of 0.5MPa 2 o 3 The catalyst is dehydrated in the gas phase to produce dimethyl ether gas. The dimethyl ether gas is input into the condenser to condense into dimethyl ether liquid and stored in the storage tank, and then the dimethyl ether liquid is transported to the first-stage rectification tower by the raw material pump. In the process, under the conditions of tower bottom temperature: 135.0°C, tower top temperature: 37.0°C, and pressure: 0.7MPa, the primary rectification is carried out. When the purity of dimethyl ether in the reflux liqu...
Embodiment 2
[0019] Raw material YN 02 150 tons, measure the raw material methanol content to 85%, PH ≈ 6.8, add 400.0 kg of NaOH or KOH solution with a concentration of 2%, adjust the pH value of the methanol raw material to 7-8, and use the raw material pump to transport the methanol raw material to the raw material evaporator for evaporation into methanol vapor, enter the synthesis reactor, and use r-AL at a temperature of 283.3°C and a pressure of 0.6MPa 2 o 3 The catalyst is dehydrated in the gas phase to produce dimethyl ether gas. The dimethyl ether gas is input into the condenser to condense into dimethyl ether liquid and stored in the storage tank, and then the dimethyl ether liquid is transported to the first-stage rectification tower by the raw material pump. In the process, the primary rectification is carried out at the temperature of the tower bottom of 138.3°C, the temperature of the top of the tower is 37.7°C, and the pressure is 0.7MPa. When the purity of dimethyl ether ...
Embodiment 3
[0021] Raw material SC 03 200 tons, measure the methanol content of the raw material to 90.0%, PH value ≈ 6.8, add 500.0 kg of NaOH or KOH solution with a concentration of 1%, adjust the pH value of the methanol raw material to 7-8, and use the raw material pump to transport the methanol raw material to the raw material evaporator Evaporate into methanol vapor, enter the synthesis reactor, and use r-AL at a temperature of 316.7°C and a pressure of 0.7MPa 2 o 3 The catalyst is dehydrated in the gas phase to produce dimethyl ether gas. The dimethyl ether gas is input into the condenser to condense into dimethyl ether liquid and stored in the storage tank, and then the dimethyl ether liquid is transported to the first-stage rectification tower by the raw material pump. In the process, the primary rectification is carried out at the temperature of the tower bottom of 141.7°C, the temperature of the top of the tower is 38.3°C, and the pressure is 0.8MPa. When the purity of dimeth...
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