Process for conversion of natural gas to liquid hydrocarbons and a plant for carrying out the process
A process and plant for conversion of a feed hydrocarbon stream to liquid hydrocarbon products in a small scale GTL plant, comprising the use of a cryogenic air separation unit (ASU), optionally together with vacuum pressure swing adsorption (VPSA), an autothermal reformer (ATR) or catalytic partial oxidation (CPO), and pressure swing adsorption (PSA) unit to produce a synthesis gas for downstream Fischer-Tropsch (FT) synthesis for production of liquid hydrocarbons.
1. A process for the conversion of a feed hydrocarbon stream into liquid hydrocarbons comprising:
(a) producing oxygen with a purity of at least 80% vol. in at least a vacuum pressure swing adsorption (VPSA) unit;
(b) mixing steam to the feed hydrocarbon stream to form a hydrocarbon-steam stream;
(c1) adding the oxygen of step (a) and the hydrocarbon-steam stream of step (b) to an autothermal reformer (ATR), or catalytic partial oxidation (CPO) unit,
or
(c2) combining the oxygen of step (a) with the resulting stream of step (b) and then adding to an autothermal reformer (ATR), catalytic partial oxidation (CPO) unit;
(d) withdrawing from the ATR or CPO a raw synthesis gas which is first dewatered and then split into a first and second raw synthesis gas stream;
(e) removing hydrogen from the second raw synthesis gas stream without any water-gas-shift pre-treatment, and withdrawing a hydrogen-rich stream and an off gas stream;
(f) converting the first raw synthesis gas stream from step (d) into liquid hydrocarbons through Fischer-Tropsch synthesis and a tail-gas;
(g) recycling tail gas from the Fischer-Tropsch synthesis to the feed hydrocarbon stream prior to step (b), to step (b), to step (c1), to step (c2), or combinations thereof.
2. The process according to claim 1 , wherein, prior to step (b), the feed hydrocarbon stream is subjected to a desulphurization step.
3. The process according to claim 1 , wherein the hydrocarbon-steam stream is pre-reformed in one or more pre-reformers.
4. The process according to claim 1 , wherein said producing oxygen with a purity of at least 80% vol. includes cryogenic separation unit.
5. The process according to claim 1 , wherein the second raw synthesis gas is fed to a PSA unit to produce said hydrogen-rich stream.
6. The process according to claim 1 , wherein the feed hydrocarbon stream is natural gas, associated gas, or combinations thereof.
7. The process according to claim 1 , wherein steam is added to the oxygen of step (a).
8. A process for the conversion of a feed hydrocarbon stream into liquid hydrocarbons comprising:
(a) producing oxygen with a purity of at least 80% vol. in at least a vacuum pressure swing adsorption (VPSA) unit;
(b) mixing steam to the feed hydrocarbon stream to form a hydrocarbon-steam stream;
(c1) adding the oxygen of step (a) and the hydrocarbon-steam stream of step (b) to an autothermal reformer (ATR), or catalytic partial oxidation (CPO) unit,
or
(c2) combining the oxygen of step (a) with the resulting stream of step (b) and then adding to an autothermal reformer (ATR), catalytic partial oxidation (CPO) unit;
(d) withdrawing from the ATR or CPO a raw synthesis gas which is first dewatered and then split into a first raw synthesis gas stream, and a second raw synthesis gas stream;
(e) removing hydrogen from the second raw synthesis gas stream without any water-gas-shift pre-treatment, and withdrawing a hydrogen-rich stream and an off gas stream;
(f) converting the first raw synthesis gas stream from step (d) into liquid hydrocarbons through Fischer-Tropsch synthesis and a tail-gas;
(g) recycling tail gas from the Fischer-Tropsch synthesis to the feed hydrocarbon stream prior to step (b), to step (b), to step (c1), to step (c2), or combinations thereof.