Non-hazardous water-based polyurethane dispersion
US-12110373-B2 · Oct 8, 2024 · US
US10294198B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10294198-B2 |
| Application number | US-201515302724-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 13, 2015 |
| Priority date | Apr 11, 2014 |
| Publication date | May 21, 2019 |
| Grant date | May 21, 2019 |
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The invention relates to a method for producing the isomers 1,3- and/or 1,4-xylylene diisocyanates by reacting the corresponding 1,3- and/or 1,4-xylylene diamines with phosgene in the gaseous phase.
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The invention claimed is: 1. A method for producing 1,3- and/or 1,4-xylylene diisocyanate (XDI) by phosgenation of 1,3- and/or 1,4-xylylenediamine (XDA) with phosgene in the gas phase in a reactor connected to a vaporizer circuit, the method comprising: vaporizing xylylenediamine/xylylenediamines in a vaporizer in the vaporizer circuit, optionally with addition of stabilizers and/or an inert gas, at a pressure of <1000 mbar, with a mean residence time in the vaporizer circuit of 5 to 90 minutes and at a temperature in a pumping circuit connected to the vaporizer circuit of 40 to 190° C., wherein the temperature is maintained by cooling in a first heat exchanger in the pumping circuit, heating XDA vapors a further 10-100° K. above the vaporization temperature of the XDA at prevailing pressure in a second heat exchanger in the pumping circuit, and reacting the vapors from the second heat exchanger connected to the reactor with phosgene by gas-phase phosgenation in the reactor. 2. The method according to claim 1 , wherein the xylylenediamine/ xylylenediamines is vaporized at 350 to 900 mbar. 3. The method according to claim 1 , wherein the xylylenediamine/ xylylenediamines is vaporized at 500 to 800 mbar. 4. The method according to claim 1 , wherein the mean residence time in the vaporizer circuit is 10 to 60 minutes. 5. The method according to claim 1 , wherein the mean residence time in the vaporizer circuit is 10 to 45 minutes. 6. The method according to claim 1 , wherein the temperature in the pumping circuit of the vaporization is 60 to 170° C. 7. The method according to claim 1 , wherein the temperature in the pumping circuit of the vaporization is 60 to 150° C. 8. The method according to claim 1 , wherein the XDA vapors are heated by a further 20 to 50 K above the vaporization temperature of the XDA under prevailing pressure, and then reacted with phosgene via gas-phase phosgenation. 9. The method according to claim 1 , wherein the XDA is admixed prior to vaporization with one or more stabilizers in concentrations of 50-2000 ppm based on XDA. 10. The method according to claim 9 , wherein the stabilizers are sterically hindered phenols and/or alkyl-substituted benzosulfonic acids. 11. The method according to claim 1 , wherein XDA droplets are separated by a droplet separator between the steps of vaporization of the XDA in the vaporizer circuit and superheating of the XDA vapors in the pumping circuit and/or after superheating of the XDA vapors in the pumping circuit. 12. The method according to claim 11 , wherein the apparatus used for the superheating also functions as droplet separator(s).
containing at least two isocyanate or isothiocyanate groups linked to the aromatic ring by means of an aliphatic group having a primary carbon atom next to the isocyanate or isothiocyanate groups, e.g. xylylene diisocyanate or homologues substituted on the aromatic ring · CPC title
containing two or more cycloaliphatic rings · CPC title
Lenses · CPC title
Compounds containing carbon-to-nitrogen triple bonds · CPC title
containing mercapto groups · CPC title
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