Dimethyl phthalate production process
A technology of dimethyl phthalate and phthalic anhydride, applied in the field of production technology of dimethyl phthalate, can solve the problem of low product yield and purity, high production cost, raw materials and water resources Waste and other problems, to achieve the effect of improving the catalytic efficiency of esterification, high esterification rate and good selectivity
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Embodiment 1
[0032] A kind of production technology of dimethyl phthalate, wherein: comprise the following steps:
[0033] S1. Put phthalic anhydride and methanol into the esterification reaction tower through the reaction pump, and add a catalyst to carry out the esterification reaction to obtain the crude product of dimethyl phthalate, the molar ratio of phthalic anhydride and methanol is 1 : 2.6; the catalyst consumption is 0.05% of the total mass of phthalic anhydride and methanol, and the reaction time is 2h; the temperature in the esterification tower is 160°C, and the reflux feed ratio is 1.8:1;
[0034] S2. adding the dimethyl phthalate crude product to an alkali washing tank for alkali washing;
[0035] S3. the dimethyl phthalate crude product after alkali washing is added in the washing tank and washed;
[0036] S4. adding the crude product of dimethyl phthalate after washing to the dehydration tower for dehydration;
[0037] S5. the dimethyl phthalate crude product after dehydra...
Embodiment 2
[0047] A kind of production technology of dimethyl phthalate, wherein: comprise the following steps:
[0048] S1. Put phthalic anhydride and methanol into the esterification reaction tower through the reaction pump, and add a catalyst to carry out the esterification reaction to obtain the crude product of dimethyl phthalate, the molar ratio of phthalic anhydride and methanol is 1 : 2.7; the catalyst consumption is 0.1% of the total mass of phthalic anhydride and methanol, and the reaction time is 3h; the temperature in the esterification reaction tower is 180°C, and the reflux feed ratio is 2:1;
[0049] S2. adding the dimethyl phthalate crude product to an alkali washing tank for alkali washing;
[0050] S3. the dimethyl phthalate crude product after alkali washing is added in the washing tank and washed;
[0051] S4. adding the crude product of dimethyl phthalate after washing to the dehydration tower for dehydration;
[0052] S5. the dimethyl phthalate crude product after...
Embodiment 3
[0062] A kind of production technology of dimethyl phthalate, wherein: comprise the following steps:
[0063] S1. Put phthalic anhydride and methanol into the esterification reaction tower through the reaction pump, and add a catalyst to carry out the esterification reaction to obtain the crude product of dimethyl phthalate, the molar ratio of phthalic anhydride and methanol is 1 : 2.8; the catalyst consumption is 1.0% of the total mass of phthalic anhydride and methanol, and the reaction time is 4h; the temperature in the esterification reaction tower is 200 ° C, and the reflux feed ratio is 2.4: 1;
[0064] S2. adding the dimethyl phthalate crude product to an alkali washing tank for alkali washing;
[0065] S3. the dimethyl phthalate crude product after alkali washing is added in the washing tank and washed;
[0066] S4. adding the crude product of dimethyl phthalate after washing to the dehydration tower for dehydration;
[0067] S5. adding the dimethyl phthalate crude p...
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