Bimesogenic compounds and mesogenic media
US-2017342324-A1 · Nov 30, 2017 · US
US9353030B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9353030-B2 |
| Application number | US-201514737530-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 12, 2015 |
| Priority date | Jul 25, 2014 |
| Publication date | May 31, 2016 |
| Grant date | May 31, 2016 |
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Disclosed is a one step process for making of 1,1,1,4,4,4-hexafluoro-2-butene. More specifically, the present invention provides a process for making hexafluoro-2-butene, continuously, from 2-chloro-3,3,3-trifluoropronene using Fe 2 O 3 /NiO impregnated carbon catalyst at 600° to 650° C.
Opening claim text (preview).
What is claimed is: 1. A process for making 1,1,1,4,4,4-hexafluoro-2-butene (HFO-1336) from 2-chloro-3,3,3-trifluoropropene (HCFC-1233xf) comprising reacting HCFC-1233xf with a selected catalyst, at a reactive temperature, to produce HFO-1336. 2. The process of claim 1 , which is conducted in the vapor phase. 3. The process of claim 2 , which is conducted in a continuous manner. 4. The process of claim 2 , wherein the catalyst comprises Fe 2 O 3 /NiO. 5. The process of claim 4 , wherein the catalyst comprises a ratio of about 95-99 wt % Fe 2 O 3 to about 5-1 wt % NiO. 6. The process of claim 4 , wherein the catalyst comprises a ratio of about 98 wt % Fe 2 O 3 to 2 wt % NiO. 7. The process of claim 2 , wherein the catalyst is selected from the group consisting of RuO 2 , RuO 4 , and OsO 4 in combination with oxides of Pd or Pt. 8. The process of claim 2 , wherein the catalyst is impregnated on carbon. 9. The process of claim 8 , wherein the carbon is activated carbon. 10. The process of claim 9 , wherein the activated carbon is granular with a mesh size of 4-14. 11. The process of claim 9 , wherein the activated carbon is pelletized. 12. The process of claim 2 , wherein the reaction temperature ranges from 600° to 650° C. 13. The process of claim 1 , wherein both the trans and cis isomers of HFO-1336 are formed. 14. The process of claim 13 , wherein the predominant isomer of HFO-1336 formed is the trans isomer. 15. The process of claim 14 , wherein the ratio of the trans isomer to the cis isomer of HFO-1336 is about 88:12. 16. The process of claim 15 , wherein the trans isomer is converted into the cis isomer by reaction with an isomerization catalyst. 17. The process of claim 16 , wherein the isomerization catalyst comprises a fluorinated chromia catalyst. 18. The process of claim 1 , further comprising the step of using 1,1,1,4,4,4 hexafluoro-2-butene as a foam blowing agent.
Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
by reactions involving an increase in the number of carbon atoms in the skeleton · CPC title
Carbon · CPC title
by reactions involving a decrease in the number of carbon atoms · CPC title
Drying, e.g. preparing a suspension, adding a soluble salt and drying · CPC title
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