Preparation method of fiber-grade PTFE spinning emulsion
A fiber grade and emulsion technology, which is applied in the fields of fiber chemical characteristics, textiles and papermaking, single-component synthetic polymer rayon, etc., can solve the problems of weak affinity between PTFE and fiber-forming carrier, fiber defects, etc. Emulsion stability, increase in emulsion viscosity, and the effect of solving the occurrence rate of fiber defects
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[0018] The present invention provides a kind of preparation method of fiber grade PTFE spinning emulsion, it is characterized in that it comprises the following steps: Step 1, at first prepare raw material: take deionized water as medium, perfluoropolyether ammonium carboxylate as the first emulsifier, Paraffin is a stabilizer, ammonium persulfate is an initiator, sodium bisulfite is a reducing agent, sodium dodecylsulfonate is a second emulsifier, acrylic acid is a pH regulator, isopropanol is a chain transfer agent, tetrafluoroethylene For polymerization monomer, polymerization makes dispersed polytetrafluoroethylene emulsion; Step 2, then take the add-on of deionized water as the basis by weight, when deionized water is 100 parts, perfluoropolyether ammonium carboxylate is 1.43×10 -1 ~4.3×10 -1 parts, paraffin is 5 parts, ammonium persulfate is 1.14×10 -2 parts, sodium bisulfite 2.28×10 -2 Parts, sodium dodecyl sulfate is 2.14×10 -2 parts, acrylic is 2.14 x 10 -2 parts...
Embodiment 1
[0022]Example 1. When the volume of the reactor in this example is 100L, add 65L of deionized water and 3.5kg of liquid paraffin into the reactor with a volume of 100L, and perform vacuum replacement treatment. The temperature is controlled at 60°C, and tetrafluoroethylene is added to the The reaction pressure in the reactor was adjusted to 2.0MPa and maintained throughout the process. Add 7.4g of ammonium persulfate, 15g of acrylic acid, 120g of perfluoropolyether ammonium carboxylate, and 7.5g of isopropanol into the reactor with a metering pump; Concentration is 1% sodium bisulfite solution and mixing, continuously add to step reaction kettle with metering pump at 0.7L / h; Ammonium acid solution and 0.72L of sodium dodecylsulfonate solution with a mass percentage concentration of 2% were added to the reaction kettle; the reaction was terminated when the gas mass flow meter display reached 21kg; the polymerization kettle was cooled to below 40°C, and the emulsion was transferr...
Embodiment 2
[0023] Example 2, when the volume of the reactor in this example is 100L, add 65L of deionized water and 3.5kg of liquid paraffin into the reactor with a volume of 100L, and perform pumping and replacement treatment. The temperature is controlled at 60°C, and tetrafluoroethylene is added to the The reaction pressure in the reactor was adjusted to 1.6MPa and maintained throughout the whole process. Add 7.4g ammonium persulfate, 15g acrylic acid, 90g perfluoropolyether ammonium carboxylate, and 7.5g isopropanol into the reactor with a metering pump; Concentration is 1% sodium bisulfite solution and mixing, continuously add to step reaction kettle with metering pump at 0.7L / h; Ammonium acid solution and 0.72L of sodium dodecylsulfonate solution with a mass percentage concentration of 2% were added to the reaction kettle; the reaction was terminated when the gas mass flow meter display reached 12kg; the polymerization kettle was cooled to below 40°C, and the emulsion was transferre...
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