Method for separating 1-chloro-3,3,3-trifluoropropene and hydrogen fluoride, and method for producing 1-chloro-3,3,3-trifluoropropene by using same
US-9221732-B2 · Dec 29, 2015 · US
US10759725B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10759725-B2 |
| Application number | US-201916562483-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 6, 2019 |
| Priority date | Apr 27, 2012 |
| Publication date | Sep 1, 2020 |
| Grant date | Sep 1, 2020 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
To provide a method for stably storing tetrafluoropropene filled in a container for e.g. storage or transportation, without occurrence of reaction such as polymerization. A method for storing tetrafluoropropene in a gaseous-liquid state composed of a gas phase and a liquid phase in a closed container, wherein the oxygen concentration (content) in the above gas phase is adjusted to at least 3 vol ppm and less than 3,000 vol ppm at a temperature of 25° C.
Opening claim text (preview).
What is claimed is: 1. A method for storing tetrafluoropropene, the method comprising storing the tetrafluoropropene in a gaseous-liquid state comprising a gas phase and a liquid phase in a closed container, wherein the gas phase has an oxygen concentration ranging from 3 vol ppm to less than 3,000 vol ppm at 25° C. and a total content of non-condensable gas of 15,000 vol ppm or less at 25° C. 2. The method according to claim 1 , wherein the oxygen concentration in the gas phase is adjusted to at least 5 vol ppm and less than 1,000 vol ppm at 25° C. 3. The method according to claim 1 , wherein the tetrafluoropropene is 2,3,3,3-tetrafluoropropene. 4. A closed container for storing tetrafluoropropene in a gaseous-liquid state of comprising a gas phase and a liquid phase, wherein the gas phase has an oxygen concentration ranging from 3 vol ppm to less than 3,000 vol ppm at 25° C. and a total content of non-condensable gas of 15,000 vol ppm or less at 25° C., and the closed container is made of at least one material selected from the group consisting of a carbon steel, a manganese steel, a chromium-molybdenum steel, a stainless steel, and an aluminum alloy. 5. The closed container according to claim 4 , wherein the oxygen concentration in the gas phase is at least 5 vol ppm and less than 1,000 vol ppm at 25° C. 6. The closed container according to claim 4 , wherein the tetrafluoropropene is 2,3,3,3-tetrafluoropropene.
Separation; Purification; Stabilisation; Use of additives · CPC title
Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures (adding propellants to aerosol containers B65B31/00) · CPC title
Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge (pressurised apparatus for purposes other than storage, see the relevant subclasses such as A62C, B05B; associated with vehicles, see the appropriate subclass of classes B60 - B64; pressure vessels in general F16J12/00 {; autoclaves B01J3/04; tank vehicles B60P3/22; railway tank wagons for carrying fluent materials B61D5/00; accumulators for supplying fluid under pressure F15B1/04; liquefied gas stoves F24C3/00}) · CPC title
Stainless steels · CPC title
containing fluorine · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.