Process for the preparation of methanol in parallel reactors
In a process for the preparation of methanolin parallel reactors, comprising the steps of (a) reacting carbon oxides and hydrogen in the presence of a methanol catalyst in a first methanol reactor to obtain a first methanol-containing effluent, (b) introducing and reacting unconverted synthesis gas in a second methanol reactor in the presence of a methanol catalyst to obtain a second methanol-containing effluent, the first methanol reactor and the second methanol reactor being connected in parallel, (c) combining the first and second effluent, and (d) cooling and separating the combined and cooled effluent into a methanol-containing liquid phase and unconverted synthesis gas, the methanol catalyst in the first methanol reactor is indirectly cooled by boiling water and the methanol catalyst in the second methanol reactor is either directly or indirectly cooled by the unconverted synthesis gas prior to conversion into the second effluent.
1. Process for the preparation of methanol, comprising the steps of
a) reacting carbon oxides and hydrogen in the presence of a methanol catalyst in a first methanol reactor to obtain a first methanol-containing effluent;
b) introducing and reacting unconverted synthesis gas in a second methanol reactor in the presence of a methanol catalyst to obtain a second methanol-containing effluent, the first methanol reactor and the second methanol reactor being connected in parallel;
c) combining the first and second effluent, and
d) cooling and separating the combined and cooled effluent into a methanol-containing liquid phase and unconverted synthesis gas,
wherein the first methanol reactor is a boiling-water reactor and the second methanol reactor is a gas-cooled reactor or a multistage packed-bed reactor.
2. The process of claim 1 , wherein the methanol catalyst in the first methanol reactor is indirectly cooled by boiling water and the methanol catalyst in the second methanol reactor is indirectly cooled by the unconverted synthesis gas prior to conversion into the second effluent.
3. The process of claim 1 , wherein the carbon oxides and hydrogen in the boiling-water reactor and the gas-cooled reactor are provided by a mixture of fresh synthesis gas and a part of the unconverted synthesis gas.
4. The process of claim 3 , wherein the gaseous phase is contacted with the methanol catalyst after having directly or indirectly cooled the methanol catalyst in the second reactor.
5. The process of claim 1 , wherein the carbon oxides and hydrogen in the boiling-water reactor are provided by a mixture of fresh synthesis gas and the gaseous phase from step d).
6. The process of 1 , wherein the carbon oxides and hydrogen in the gas-cooled reactor are provided by a mixture of the gaseous phase from step d) and the fresh synthesis gas.
7. Process for the preparation of methanol, comprising the steps of
a) reacting a methanol free feed gas comprising carbon oxides and hydrogen in the presence of a methanol catalyst in a first methanol reactor to obtain a first methanol-containing effluent;
b) introducing and reacting unconverted synthesis gas in a second methanol reactor in the presence of a methanol catalyst to obtain a second methanol-containing effluent, the first methanol reactor and the second methanol reactor being connected in parallel;
c) combining the first and second effluent, and
d) cooling and separating the combined and cooled effluent into a methanol-containing liquid phase and unconverted synthesis gas,
wherein the first methanol reactor is a boiling-water reactor and the second methanol reactor is a gas-cooled reactor or a multistage packed-bed reactor.
8. The process of 7 , wherein separated and cooled synthesis gas is recycled to at least one of the first and second rectors.