Crosslinkable polytetrafluoroethylene composition, cross-linked polytetrafluoroethylene powder, polytetrafluoro-ethylene moldings, resin blend compositions, and resin blend moldings
A technology of polytetrafluoroethylene and composition, which is applied in the field of polytetrafluoroethylene resin and polytetrafluoroethylene composition, can solve problems such as wrinkles, lack of improved performance, difficult compression molding, etc., and achieve the effect of not being easily deformed
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[0215] [Preparation method of PTFE cross-linked powder]
[0216] The powder of the PTFE cross-linked body of the present invention can be obtained by treating under suitable and appropriate conditions. For example, in the case of oxazole cross-linking, the powder of the cross-linkable PTFE composition or cross-linked PTFE is put into an air circulation furnace and kept at 120-320° C. for 1-300 minutes to obtain a cross-linked PTFE. Furthermore, in the case of imidazole crosslinking, a crosslinked PTFE body with good physical properties can be obtained at a relatively low crosslinking temperature (for example, 120 to 280° C., preferably 120 to 250° C.). In addition, the heating temperature may be changed stepwise without being fixed. For example, a method may be considered in which the crosslinking agent is kept at a temperature near the melting point of the crosslinking agent, the crosslinking agent is sufficiently impregnated with PTFE, and then the temperature is raised to ...
Embodiment
[0258] (1) Manufacturing method of PTFE having reactive functional groups
Synthetic example 1
[0260] 3560 g of deionized water, 94 g of paraffin wax and 5.4 g of perfluorooctanoic acid ammonium dispersant were added to a stainless steel reactor with an internal capacity of 6 L and a stirrer. Next, while heating the contents of the reactor to 70° C., while evacuating, purging with TFE monomer was performed to remove oxygen in the reactor. Then, 0.17 g of ethane gas and 16.6 g of perfluorobutenoic acid (PFBA) were added to the reactor, and the contents were stirred at a speed of 280 rpm. TFE monomer was added to the reactor until the pressure was 0.73 MPa. 0.36 g of ammonium persulfate (APS) initiator dissolved in 20 g of deionized water was injected into the reactor so that the pressure of the reactor was 0.83 MPa. After injection of the initiator, a drop in pressure was observed and polymerization started. Add TFE monomer into the reactor, and keep the pressure to continue polymerization until about 1.1Kg of TFE monomer has reacted completely. Then, the reactor was ...
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