Process and plant for substitute natural gas
View Patent ↗A process for producing substitute natural gas (SNG) comprising the steps of reacting a fresh syngas ( 11 ) into a methanation section ( 10 ) comprising adiabatic reactors ( 101 - 104 ) connected in series, with heat removal and reacted gas-recirculation, wherein the fresh syngas is fed in parallel to said adiabatic reactors. In a preferred embodiment the reacted gas is recirculated to the first reactor ( 101 ) and further dilution of the fresh gas at the inlet of the first and second reactor is achieved by steam addition.
1. A process for producing SNG from a fresh syngas feedstock, said process comprising at least the steps of:
reacting said fresh syngas into a methanation section comprising at least a first adiabatic reactor and at least one further adiabatic reactor connected in series, so that each of said at least one further reactor(s) is fed with a gas stream taken from the previous reactor of the methanation section;
feeding said fresh syngas feedstock in parallel to each of said reactors; and
re-circulating at least a portion of the reacted gas as input gas to at least one of said reactors, wherein at least a portion of a reacted gas stream taken from said first reactor is used as a re-circulated gas to dilute the fresh syngas feedstock stream fed to said first reactor, obtaining a diluted gas stream at the inlet of said first reactor.
2. The process according to claim 1 , wherein said fresh syngas feedstock is split into a plurality of fresh gas streams, each of said fresh gas streams being fed to a respective one of said reactors.
3. The process according to claim 2 , wherein said methanation section comprises a plurality of said further adiabatic reactors and each of said fresh gas streams is between 15% and 35% molar of the total gas feedstock.
4. The process according to claim 1 , wherein said portion of reacted gas stream is fed to the inlet of the first reactor via a re-circulation loop comprising a compressor for the re-circulated gas stream and a pre-heater for heating said diluted gas stream before entering the first reactor.
5. The process according to claim 1 , wherein the molar ratio between the total diluted gas flow entering the first reactor, and the fresh gas stream fed to said first reactor is around 2.
6. The process according to claim 1 , wherein steam is added at the inlet of at least the first reactor to further dilute the inlet gas.
7. The process according to claim 6 , wherein reacted gas from the first reactor is split into a first gas portion and a second gas portion;
said first gas portion is re-circulated to dilute the fresh gas stream fed to said first reactor, obtaining a diluted gas stream at the inlet of said first reactor;
said diluted gas stream is further diluted by addition of a steam flow before entering the first reactor;
said second gas portion is used to dilute fresh gas fed to a second reactor of the methanation section and the gas flow entering said second reactor is further diluted with steam.
8. The process of according to claim 1 , wherein said reactors operate at around 35 bar pressure.