Co-production of methanol and ammonia

1. A process for co-producing methanol and ammonia from a hydrocarbon feedstock, said process comprising the steps of:

a) from a first methanol process, comprising a first reforming step and first methanol conversion step, obtaining a first effluent comprising methanol and a first gas effluent comprising hydrogen, nitrogen and unconverted carbon oxides, and

from a second methanol processes, comprising a second reforming step and a second methanol conversion step, obtaining a second effluent comprising methanol and a second gas effluent comprising hydrogen, nitrogen and unconverted carbon oxides;

b) producing an ammonia synthesis gas from the first and second gas effluent in a common catalytic methanation stage and withdrawing said ammonia synthesis gas having a H 2 :N 2 molar ratio of 3:1; and

c) catalytically converting the nitrogen and hydrogen of the ammonia synthesis gas in a common ammonia synthesis stage and withdrawing an effluent comprising ammonia and a purge-gas stream comprising hydrogen, nitrogen and/or methane.

2. The process according to claim 1 , wherein in each of the first and second methanol processes, the following steps are carried out:

1) producing a methanol synthesis gas containing hydrogen, carbon oxides and nitrogen by steam reforming the hydrocarbon feedstock in a reforming section comprising a primary and a secondary reforming stage;

2) catalytically converting the carbon oxides and hydrogen of the methanol synthesis gas in a once-through methanol synthesis stage and withdrawing an effluent comprising methanol and a gas effluent comprising nitrogen, hydrogen and unconverted carbon oxides.

3. The process according to claim 2 , wherein the secondary reforming stage is an air-blown secondary reforming stage.

4. The process according to claim 1 , wherein the hydrocarbon feedstock is natural gas or substitute natural gas (SNG) or a gas comprising >80% methane.

5. The process according to claim 1 , wherein the methanol conversion of the first and second once-through methanol synthesis stage of the first and the second methanol processes are controlled at least by controlling the amount of syngas from the first and/or second reforming step fed to the first and/or second methanol production stage.

6. The process according to claim 1 , wherein the methanol synthesis is conducted by passing the synthesis gas through one or more boiling water reactor and subsequently through one or more adiabatic fixed bed reactors.

7. The process according to claim 1 , wherein the methanol synthesis is conducted by passing the synthesis gas through one or more boiling water reactor and subsequently through one or more gas cooled reactors.

8. The process according to claim 7 , wherein the boiling water reactor is a single condensing-methanol reactor which comprises within a common shell a fixed bed of methanol catalyst particles and cooling means adapted to indirectly cooling the methanol synthesis gas with a cooling agent.

9. The process according to claim 7 , further comprising cooling the synthesis gas withdrawn from each methanol reactor to condense methanol and passing the gas through a separator, withdrawing a bottom fraction from the separator containing the raw methanol, withdrawing an overhead fraction containing synthesis gas which is passed to the subsequent methanol reactor, and forming a single liquid effluent containing methanol by combining the bottom fractions of the separators of each reactor containing the raw methanol.

10. The process according to claim 1 , further comprising withdrawing a hydrogen-rich stream from the purge-gas stream comprising hydrogen, nitrogen and methane and adding this stream to step (a).

11. The process according to claim 1 , further comprising withdrawing an off gas from the purge-gas stream comprising hydrogen, nitrogen and methane and adding this stream to step (a) as fuel.

12. The process according to claim 1 , further comprising further parallel methanol processes.