Device for continuously preparing high-purity meta-position aramid fiber resin solution
A technology of resin solution and aramid fiber, which is applied in the field of polymer material production equipment and industrial continuous preparation of high-purity meta-aramid resin solution, which can solve the problem of high production cost and polym-phenylene isophthalamide polymerization Problems such as narrow molecular weight distribution and large engineering investment
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Embodiment 1
[0022]The solid m-phenylenediamine (MPD) raw material is heated and melted at 80°C into a fluid liquid molten state, and placed in the m-phenylenediamine storage tank 2 for standby; the solid isophthaloyl dichloride (IPC) raw material is in Heating and melting at a temperature of 60°C into a liquid molten state with fluidity, and placing it in the isophthaloyl chloride storage tank 9 for standby; the N,N-dimethylacetamide (DMAc) in the solvent storage tank 1 has a water content of 80ppm, measured by the solvent delivery pump 3 and the solvent mass flowmeter 5, enters from an input port of the static mixer 7 at a flow rate of 401.69 mass parts per hour; m-phenylenediamine (MPD) in the m-phenylenediamine storage tank 2 The melt enters from another input port of the static mixer 7 at a flow rate of 27.29 parts by mass per hour after being metered by the m-phenylenediamine delivery pump 4 and the m-phenylenediamine mass flowmeter 6; the m-phenylenediamine coming out of the static m...
Embodiment 2
[0025] The solid m-phenylenediamine (MPD) raw material is heated and melted at 80°C into a fluid liquid molten state, and placed in the m-phenylenediamine storage tank 2 for standby; the solid isophthaloyl dichloride (IPC) raw material is in Heating and melting at a temperature of 60°C into a liquid molten state with fluidity, and placing it in the isophthaloyl chloride storage tank 9 for standby; the N,N-dimethylacetamide (DMAc) in the solvent storage tank 1 has a water content of 120ppm, measured by the solvent delivery pump 3 and the solvent mass flowmeter 5, enters from an input port of the static mixer 7 at a flow rate of 322.44 mass parts per hour; m-phenylenediamine (MPD) in the m-phenylenediamine storage tank 2 The melt enters from another input port of the static mixer 7 at a flow rate of 27.29 parts by mass per hour after being metered by the m-phenylenediamine delivery pump 4 and the m-phenylenediamine mass flowmeter 6; the m-phenylenediamine coming out of the static...
Embodiment 3
[0028] The solid m-phenylenediamine (MPD) raw material is heated and melted at 80°C into a fluid liquid molten state, and placed in the m-phenylenediamine storage tank 2 for standby; the solid isophthaloyl dichloride (IPC) raw material is in Heating and melting at a temperature of 60°C into a liquid molten state with fluidity, and placing it in the isophthaloyl chloride storage tank 9 for standby; the N,N-dimethylacetamide (DMAc) in the solvent storage tank 1 has a water content of 150ppm, measured by the solvent delivery pump 3 and the solvent mass flowmeter 5, enters from an input port of the static mixer 7 at a flow rate of 227.11 parts by mass per hour; m-phenylenediamine (MPD) in the m-phenylenediamine storage tank 2 The melt enters from another input port of the static mixer 7 at a flow rate of 27.29 parts by mass per hour after being metered by the m-phenylenediamine delivery pump 4 and the m-phenylenediamine mass flowmeter 6; the m-phenylenediamine coming out of the sta...
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