Continuous process to produce hexafluoroisopropanol
A technology of hexafluoroisopropanol and hexafluoroacetone, which is applied in the continuous field of preparing hexafluoroisopropanol, and can solve the problems of shortening catalyst life
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Embodiment
[0074] The steps for start-up and continuous operation of the preferred method used in the following examples are described. The examples provide the process variables used.
[0075] Said embodiment works with figure 1 performed in a similar reaction system. The mixing equipment 1 is a 1-liter 316 stainless steel autoclave equipped with a stirrer and a heating device, and has a design pressure of 2000 psig (13.9 MPa). HFA was fed to the autoclave with an Isco syringe pump 16, model 1000D. Pump 3 is a Lewa Ecoflow 319 stainless steel diaphragm pump with a design pressure of 1500 psig (10.4 MPa). Reactor 5 was a 16 x 1 inch (40.6 x 2.54 cm) 316 stainless steel Schedule 80 tube. The product was collected in a 17 x 4 inch (43.2 x 10.2 cm) 304 stainless steel gas / liquid separator 25, which had a capacity of 2.25 L. The catalysts used were Engelhard 1 / 16 inch (1.6 mm) 3F Ni-3288E trilobe catalyst (41.5 g) and Johnson Matthey HTC NI500RP trilobe catalyst (39.2 g).
[0076] In t...
Embodiment 2
[0080] Example 2 used the same reactor configuration as above except that the reactor was used in a downflow configuration instead of an upflow configuration. Reactor feed enters at the top of the bed and product exits at the bottom of the bed.
Embodiment 9
[0081] Example 9 used essentially the same upflow reactor configuration, except that a 6 inch (15.2 cm) Johnson Matthey HTC Ni500 1.2RP trilobe catalyst was used, having a total weight of 39.16 g.
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