Process for producing cellulose ether by directly separating and recovering diluent
A cellulose ether and production process technology, applied in the field of cellulose ether production and preparation, can solve the problems of high energy consumption, slow speed, consumption of sodium hydroxide, etc., shorten the recovery time, improve production efficiency, and reduce the amount of acetic acid or hydrochloric acid Effect
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Embodiment 1
[0013] Add mixed diluent 800kg (component mass ratio is toluene: isopropanol: water=1: 0.3: 0.15) in etherification tank, sodium hydroxide 60kg, after temperature is controlled at 28 ℃, add refined cotton 100kg, carry out The alkalization reaction is timed for 2 hours (1-3 hours are all acceptable), then 80 kg of methyl chloride and 40 kg of ethylene oxide are added, the temperature is raised to 45-85° C., the reaction pressure is controlled at 0.2-0.5 MPa, and the reaction time is 3 hours. After the reaction finishes, the mixed material (slurry) is separated, adopts a decanter centrifuge, and the rotating speed is 3000 rev / min, and the liquid enters the solvent intermediate tank (its composition is mainly toluene 71.1%, isopropanol 18.7%, hydrogen oxidized Sodium content 1.5%, water and others 8.7%), recovery and reuse, the solid enters the washing tank, neutralizes to PH6-7 with acetic acid, heats up to recover the remaining solvent, then adds water to wash, then separates, t...
Embodiment 2
[0015] Add 1000kg of mixed diluent (component mass ratio is toluene: isopropanol: water = 1: 0.2: 0.1) and 80kg of sodium hydroxide in the etherification kettle. After controlling the temperature at 28°C, add 100kg of refined cotton to carry out The alkalization reaction was timed for 2 hours, then 100 kg of methyl chloride and 30 kg of propylene oxide were added, the temperature was raised to 55-95° C., the reaction pressure was controlled at 0.3-0.6 MPa, and the reaction time was 3 hours. After the reaction finishes, the mixed material is separated, adopts a decanter centrifuge, and the rotating speed is 3000 rpm, and the liquid enters the solvent intermediate tank (after testing, its composition is mainly toluene 78.2%, isopropanol 12.7%, sodium hydroxide content 1.6%) , water and other 7.5%), recovery and reuse, the solid enters the washing tank, after being neutralized with acetic acid, the temperature is raised to recover the remaining solvent, then water is added to wash...
Embodiment 3
[0017] Add mixed diluent 900kg (component mass ratio is toluene: isopropanol: water=1: 0.2: 0.2) in etherification tank, sodium hydroxide 90kg, after temperature is controlled at 28 ℃, add refined cotton 100kg, carry out The alkalization reaction was timed for 1 hour, then 120 kg of methyl chloride was added, the temperature was raised to 70-95° C., the reaction pressure was controlled at 0.4-0.6 MPa, and the reaction time was 3 hours. After the reaction finishes, the mixed materials are separated, using a decanter centrifuge with a rotating speed of 3000 rpm, and the liquid enters the solvent intermediate tank (after testing, its composition is mainly toluene 78.5%, isopropanol 12.9%, sodium hydroxide content 1.2%) , water and other 8.4%), recovery and reuse, the solid was washed in the kettle, after being neutralized with acetic acid, the temperature was raised to recover the remaining solvent, then washed with water, dried and pulverized after separation to obtain 116.5kg of...
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