Method for producing acrolein and/or acrylic acid from glycerol

1. An installation for continuous production of a stream comprising acrolein, said installation comprising:

a unit for converting glycerol to acrolein,

a source of gaseous reaction stream comprising at least glycerol,

a source of gaseous regeneration stream comprising at least oxygen for regeneration of solid acid catalyst,

wherein the converting unit comprises:

a reactor R comprising at least two separated zones each containing said solid acid catalyst, each of the zones being configured to be used simultaneously and alternately as reaction zone and as regeneration zone in cyclical fashion and with reaction mode and regeneration mode being offset from one zone to another, each of the zones having fluid connection by a feeding device to the source “a” of reaction stream and to the source “b” of regeneration stream, wherein the gaseous streams in each of the catalyst zones are separated,

a system adapted to each feeding device allowing sequential alternation of supply with the gaseous reaction stream or with the gaseous regeneration stream,

at least one device for withdrawing a gas mixture c 1 , c 2 , c 3 , with fluidic connection to the reactor,

the reactor zones being controlled thermostatically with a single system of heat-transfer fluid.

2. The installation as claimed in claim 1 comprising a single device for withdrawing gas mixture.

3. The installation as claimed in claim 2 , wherein each of the reactor zones has fluidic connection to a device for withdrawing gas mixture.

4. The installation as claimed in claim 1 , wherein the reactor R is a multiple-tube reactor comprising tubes ( 10 ) fixed by tube plates ( 20 ) and comprising at least one plate ( 40 ) positioned between the reactor dome and the tube plates ( 20 ).