Process for producing (meth)acrylic acid or (meth)acrolein
View Patent ↗A method for producing (meth)acrylic acid or (meth)acrolein, comprising a catalytic gas phase oxidation process for producing (meth)acrylic acid or (meth)acrolein by supplying propylene, propane, or isobutylene and a gas containing molecular oxygen to a reactor which contains a catalyst filled therein, wherein a gas containing molecular oxygen is supplied to the reactor having the catalyst filled therein during shutdown of the catalytic gas phase oxidation process does not lower the reaction activity of the catalyst and the selectivity of target products when re-starting the running after shutdown of the catalytic gas phase oxidation process.
1. A method for producing (meth)acrylic acid or (meth)acrolein, comprising:
(a) supplying propylene, propane, or isobutylene and a first gas comprising molecular oxygen to a reactor which contains a catalyst, to effect catalytic gas phase oxidation of said propylene, propane, or isobutylene, to obtain (meth)acrylic acid or (meth)acrolein; and
(b) shutting down said reactor by reducing said supplying of said propylene, propane, or isobutylene;
wherein a second gas comprising molecular oxygen is supplied to said reactor during said shutting down of said reactor, to maintain said catalyst in an oxidized state.
2. A method according to claim 1 , wherein said second gas comprising molecular oxygen is supplied to said reactor by using a compressed gas holder or a compressor connected to a failure-free power source.
3. A method according to claim 1 , wherein said reactor is a tube reactor.
4. A method according to claim 3 , wherein said tube reactor comprises 10,000 to 30,000 reactor tubes.
5. A method according to claim 4 , wherein said second gas comprising molecular oxygen is supplied to said reactor during said shutting down of said reactor in an amount of 0.2 to 50 NL per hour per reactor tube.
6. A method according to claim 1 , wherein said second gas comprising molecular oxygen is air.
7. A method according to claim 1 , wherein said catalytic gas phase oxidation of said propylene, propane, or isobutylene, to obtain (meth)acrylic acid or (meth)acrolein is carried out at a temperature of at least 300° C. and said shutting down of said reactor comprises cooling said temperature to about room temperature.
8. A method according to claim 7 , wherein said reactor is a tube reactor.
9. A method according to claim 8 , wherein said tube reactor comprises 10,000 to 30,000 reactor tubes.
10. A method according to claim 9 , wherein said second gas comprising molecular oxygen is supplied to said reactor during said shutting down of said reactor in an amount of 0.2 to 50 NL per hour per reactor tube.
11. A method according to claim 7 , wherein said second gas comprising molecular oxygen is air.
12. A method according to claim 1 , further comprising: (c) restarting said reactor after said shutting down of said reactor.
13. A method according to claim 12 , wherein said restarting of said reactor comprises re-supplying said propylene, propane, or isobutylene and said first gas comprising molecular oxygen to said reactor and raising the temperature of said reactor to at least 300° C.
14. A method according to claim 12 , wherein said reactor is a tube reactor.
15. A method according to claim 14 , wherein said tube reactor comprises 10,000 to 30,000 reactor tubes.
16. A method according to claim 15 , wherein said second gas comprising molecular oxygen is supplied to said reactor during said shutting down of said reactor in an amount of 0.2 to 50 NL per hour per reactor tube.
17. A method according to claim 12 , wherein said second gas comprising molecular oxygen is air.
18. A method according to claim 1 , wherein said second gas comprising molecular oxygen is supplied to said reactor until said reactor is restarted.