Method and plant for the production of synthesis gas
A method for producing syngas includes a) splitting a hydrocarbon into carbon and hydrogen using a plasma to obtain a first product including carbon and hydrogen, b) mixing steam and carbon dioxide with at least a portion of the first product to produce a product stream, wherein a first portion of the carbon in the first product is converted in an endothermic reaction with steam to carbon monoxide and hydrogen and a second portion of the carbon in the first product is converted in another endothermic reaction with the carbon dioxide to carbon monoxide, and wherein heat is supplied to the endothermic reaction, and c) quenching the product stream of step b).
1. A method for producing syngas, the method comprising:
a) splitting a hydrocarbon into carbon and hydrogen using a plasma to obtain a first product including carbon and hydrogen;
b) mixing steam and carbon dioxide with at least a portion of the first product to produce a product stream, wherein a first portion of the carbon in the first product is converted in an endothermic reaction with steam to carbon monoxide and hydrogen and a second portion of the carbon in the first product is converted in another endothermic reaction with the carbon dioxide to carbon monoxide, wherein the mixing of the carbon dioxide takes place before the mixing of the steam and wherein heat is supplied to the endothermic reaction; and
c) quenching the product stream of step b).
2. The method according to claim 1 , wherein in step b), the heat is supplied by electric heating and/or co-combustion of hydrocarbons.
3. The method according to claim 1 , wherein in step c), the product stream of step b) is quenched to a temperature at or below 400° C.
4. The method according to claim 1 , wherein the quenching according to step c) is carried out by injection of water, heat dissipation by means of an endothermic reaction, or heat transfer in a heat exchanger wherein the temperature of the product stream after quenching does not drop below the dew point temperature.
5. The method according to claim 1 , wherein a product ratio of hydrogen to carbon monoxide is regulated via a supply ratio of steam to carbon dioxide.
6. The method according to claim 5 , wherein the product ratio of hydrogen to carbon monoxide is set in a range of 1.75:1 to 1.95:1.
7. The method according to claim 1 , wherein in step b, the temperatures are in the range of 900° C. to 1500° C.
8. The method according to claim 1 , wherein step a) is carried out in one or a plurality of hydrocarbon converters at a working pressure in the range of 1 bar to 50 bar.
9. The method according to claim 1 , further comprising:
d) production of synthetic functionalized and/or non-functionalized hydrocarbons from at least a portion of syngas formed in step c).
10. The method according to claim 9 , wherein the functionalized and/or nonfunctionalized hydrocarbons comprise one or more of the following substances: paraffin, diesel fuels, gasoline fuels, kerosene, methanol, methane, liquefied gases.