Process and reaction system for the preparation of methanol
Process and reaction system for the preparation of methanol comprising two reaction units, wherein a first unit is operated on a mixture of fresh synthesis gas and unconverted synthesis gas and a second unit solely with unconverted synthesis gas.
1. Process for the preparation of methanol comprising the steps of
(a) providing a fresh methanol synthesis gas containing hydrogen, carbon monoxide and carbon dioxide;
(b) providing a recycle gas stream containing unconverted methanol synthesis gas from a first reaction unit and a second methanol reaction unit, wherein the recycle stream is pressurized by a common circulator, and mixing a part of the recycle stream with the fresh synthesis gas to form a process gas stream;
(c) introducing and reacting the process gas stream from (b) in the first methanol reaction unit in presence of a methanol catalyst and obtaining a first effluent stream containing methanol and a part of the unconverted synthesis gas contained in the recycle stream; and
(d) introducing and reacting at least another part of the recycle gas stream in the second methanol reaction unit in presence of a methanol catalyst and obtaining a second effluent stream containing methanol and another part of the unconverted synthesis gas contained in the recycle stream.
2. The process of claim 1 , wherein the unconverted synthesis gas in the first and second effluent stream is separated from the methanol by cooling and condensing methanol in each effluent stream separately or by combining the first or second effluent stream prior to the cooling and condensing methanol.
3. The process of claim 1 , wherein the recycle stream is obtained by
(i) cooling the first effluent stream from the first methanol reaction unit and separating the methanol contained in the first effluent from the unconverted synthesis;
(ii) cooling the second effluent stream from the second methanol reaction unit and separating the methanol contained in the second effluent stream from the unconverted synthesis gas; and
(iii) combining the unconverted synthesis gas separated from the first and second effluent stream to the recycle stream.
4. The process of claim 1 , wherein the recycle stream is obtained by
(i) mixing the first effluent stream from the first methanol reaction unit with the second effluent stream from the second methanol reaction unit;
(ii) cooling the mixed effluent stream and separating the unconverted synthesis gas from the methanol contained in the mixed first and second effluent stream.