Plant for the production of methanol from synthesis gas rich in inerts
During the production of methanol from inert-rich syngas, a catalytic pre-reactor is installed upstream of the single- or multi-stage synthesis loop, a first part of the syngas being converted to methanol in the catalytic pre-reactor. An inert gas separation stage, for example a pressure swing adsorption system or a membrane system, can be connected downstream of the synthesis loop, whereby a hydrogen-enriched syngas stream can be returned to the synthesis loop. In the processing of methane-rich syngas, the inert gas separation stage may also have an autothermal reformer in which methane is converted to carbon oxides and hydrogen, which are also returned into the synthesis loop.
1. A plant for the production of methanol from a synthesis gas containing hydrogen, one or more carbon oxides, and one or more inert components, the plant comprising:
a methanol pre-reactor in which a first part of the carbon oxides is catalytically converted to methanol;
a methanol main reactor in which a second part of the carbon oxides is catalytically converted to methanol;
a first separator, downstream of the methanol pre-reactor, configured to separate the methanol from the synthesis gas;
a second separator, downstream of the methanol main reactor, configured to separate further methanol from the synthesis gas;
a conduit configured to recirculate a synthesis gas cycle stream to the methanol main reactor;
an inert gas separation stage;
a conduit configured to supply synthesis gas from the methanol main reactor to the inert gas separation stage;
a conduit configured to discharge a purge stream from the inert gas separation stage; and
a conduit configured to recirculate a recirculation stream, depleted of one or more inert components, to the methanol main reactor.
2. The plant of claim 1 , comprising:
the methanol pre-reactor as a first methanol pre-reactor; and
a second methanol pre-reactor.
3. The plant of claim 1 , comprising:
the methanol main reactor as a first methanol main reactor; and
a second methanol main reactor.
4. The plant of claim 3 , wherein the first methanol main reactor in flow direction is operated in a water-cooled manner, and
wherein the second methanol main reactor in flow direction is operated in a gas-cooled manner.
5. The plant of claim 1 , wherein the inert gas separation stage comprises a pressure swing adsorption system.
6. The plant of claim 5 , wherein the inert gas separation stage comprises an autothermal reformer.
7. The plant of claim 5 , wherein the inert gas separation stage comprises an autothermal reformer and a pressure swing adsorption system.
8. The plant of claim 5 , further comprising:
a natural gas gasification stage, configured to provide the first synthesis gas stream.
9. The plant of claim 5 , further comprising:
a biomass gasification stage, configured to provide the first synthesis gas stream.
10. The plant of claim 5 , further comprising:
a coal gasification stage, configured to provide the first synthesis gas stream.
11. The plant of claim 5 , wherein the methanol main reactor is operated in a water-cooled manner.
12. The plant of claim 5 , wherein the methanol main reactor is operated in an adiabatic manner.
13. The plant of claim 5 , wherein the methanol main reactor is operated in a gas-cooled manner.
14. The plant of claim 1 , wherein the inert gas separation stage comprises a membrane system.
15. The plant of claim 1 , comprising:
the methanol pre-reactor as a first methanol pre-reactor;
a second methanol pre-reactor;
the methanol main reactor as a first methanol main reactor; and
a second methanol main reactor.
16. A method for retrofitting an existing plant for producing methanol with one or more methanol main reactors within an inner synthesis cycle from an operation with synthesis gas low in inerts to an operation with synthesis gas rich in inerts, in the plant of claim 1 , the method comprising
providing, upstream of the methanol main reactor, the methanol pre-reactor;
providing, downstream of a last methanol main reactor, the inert gas separation stage, and
recirculating the synthesis gas cycle stream, depleted of one or more inert components, to the methanol main reactor, thereby forming an outer synthesis cycle,
wherein the methanol pre-reactor and the inert gas separation stage are located outside the inner synthesis cycle.
17. The method of claim 16 , wherein the methanol obtained is supplied to the further product processing.