Aqueous Polymerization of Fluorinated Monomer Using a Mixture of Fluoropolyether Acids or Salts
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examples 1-7
TFE / HFP / PEVE
[0125]Examples 1 through 7 are performed in a manner similar to comparative example 1, with the polymerization agent mixture employed having a PFPEA in accordance with the invention, PFPEA 3 or PFPEA 4, and / or varying amounts of PFPEA and DA used as shown in Table 2A. Results are reported in Table 2B. Using similar quantities of PFPEA in the polymerization agent, Examples 1 and 3 illustrate the invention by showing improved performance of polymerization as compared to Comparative Examples 1 and 3 as indicated by smaller RDPS and less coagulum. Using similar quantities of PFPEA in the polymerization agent, Examples 2 and 4 also illustrate the invention by showing improved performance of polymerization as compared to Comparative Examples 2 and 4 as indicated by smaller RDPS and less coagulum. Using significantly less PFPEA in the polymerization agent, Examples 5, 6, and 7 show equal or improved performance of polymerization as compared to Comparative Examples 1-4.
TABLE 2AP...
examples 8-9
TFE / HFP
[0128]Examples 8 and 9 are performed in a manner similar to Comparative Example 5, but the polymerization agent mixtures employed have a PFPEA in accordance with the invention, PFPEA3, and in significantly decreased amounts as shown in Table 3A. The DA amount is varied. Several other minor changes are also made including using a single fresh initiator solution produced with 3.74 wt % of ammonium persulfate (APS) that is pumped to the reactor at 3.4 mL / min during reaction, increasing the HFP pressure to 466 psig (3.31 MPa), and increasing the TFE pressure before the reaction starts to 650 psig (4.58 MPa). Results are reported in Table 3B. Examples 8 and 9 demonstrate the invention by achieving smaller RDPS and acceptable coagulum with significantly less PFPEA than Comparative Examples 5 and 6, respectively.
example 10
TFE / HFP
[0129]Example 10 is performed in a manner similar to Example 8, but the polymerization agent mixture 16 is added to the reactor while the reactor is paddle agitated at 93 rpm. The polymerization agent mixture 16 is shown in Table 3A. Results are reported in Table 3B. Example 10 illustrates the invention by producing significantly smaller particle size and less coagulum than Comparative Example 6 with only 12% of the PFPEA.
[0130]The process of the invention is illustrated in Examples 11, 12 and 13 in the polymerization of PTFE homopolymer and compared with Comparative Examples 7 and 8.
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