Process for the production of syngas
A process for the production of syngas comprising the steps of providing a feed gas comprising a hydrocarbon, carbon dioxide and optionally steam, contacting a flow of said feed gas with a metal oxide to form syngas, wherein the mole fraction of carbon dioxide or in the case the feed gas comprises steam, the sum of the mole fractions of carbon dioxide and steam, in the feed gas is between 0.3 and 0.7; and/or wherein the mole fraction of the hydrocarbon in the feed gas is between 0.3 to 0.5, wherein the feed gas is contacted with the metal oxide at a temperature of between 1050K and 1600K.
1 . A process for the production of syngas comprising the steps of
a. providing a feed gas consisting of a hydrocarbon, carbon dioxide, and steam,
b. contacting a flow of said feed gas with ceria (CeO 2 ) to form syngas, wherein
the sum of the mole fractions of carbon dioxide and steam, in the feed gas, is between 0.5 and 0.7; and wherein the mole fraction of carbon dioxide in the feed gas is 0.1 and 0.55 and the mole fraction of steam in the feed gas is between 0.15 and 0.6,
wherein the mole fraction of the hydrocarbon in the feed gas is between 0.3 to 0.5,
wherein the feed gas is contacted with the metal oxide at a temperature of between 1200 K and 1400 K and wherein the feed gas has a pressure of from 2 bar to 20 bar,
wherein the flow of feed gas simultaneously reduces the ceria in a first non-stoichiometric state CeO 2-α towards a second non-stoichiometric state CeO 2-β and oxidizes the ceria in a second non-stoichiometric state CeO 2-β towards a first non-stoichiometric state Ceo 2-α , wherein β is in the range of 0.10 and 0.25, and α is in the range of 0.05 and 0.2 and β-α is in the range of 0.01 and 0.2.
2 . The process for the production of syngas according claim 1 , wherein the hydrocarbon comprises or consists of methane, ethane, propane, butane, pentane or mixtures thereof.
3 . The process for the production of syngas according to claim 1 , wherein the feed gas is obtained by the addition of carbon dioxide, steam, or steam and carbon dioxide to a biogas.
4 . The process for the production of syngas according to claim 1 , wherein the feed gas is a biogas.
5 . The process for the production of syngas according to claim 1 , wherein the feed gas is obtained by the addition of carbon dioxide, steam, or steam and carbon dioxide to a natural gas.
6 . The process for the production of syngas according to claim 1 , wherein the metal oxide is in the form of a packed bed of irregular particles of metal oxide.
7 . The process for the production of syngas according to claim 1 , wherein the mole fraction of carbon dioxide in the feed gas is 0.25 and 0.45 and the mole fraction of steam in the feed gas is between 0.15 and 0.45.
8 . A device for the production of syngas, configured to carry out the process according to claim 1 , comprising at least
a. a reaction chamber comprising ceria (CeO 2 ),
b. a heat source capable of heating and maintaining the reaction chamber at a temperature of from 1200 K to 1400 K, and controlled by a heat source control device,
c. a first mass flow controller capable of controlling the mass inflow of feed gas into the reaction chamber, and controlled by a first mass flow controller control device,
d. an analytic device capable of determining the mole fraction of methane, carbon dioxide and steam in the inflow of feed gas and capable of communicating with, and controlling, a second mass flow controller capable of controlling the addition of either carbon dioxide, steam or both to the flow of feed gas such as to adjust the mole fraction of hydrocarbon, carbon dioxide and steam in the feed gas towards a mole fraction of carbon dioxide and steam, in the feed gas of between 0.5 and 0.7 and towards a mole fraction of the hydrocarbon in the feed gas of between 0.3 to 0.5 when the mole fraction of carbon dioxide and steam, in the feed gas is not between 0.5 and 0.7 or when the mole fraction of the hydrocarbon in the feed gas is not between 0.3 to 0.5, such as to adjust the mole fraction of carbon dioxide in the feed gas towards a mole fraction of 0.1 and 0.55 and the mole fraction of steam in the feed gas towards a mole fraction of 0.15 and 0.6, when the mole fraction of the carbon dioxide in the feed gas is not between 0.1 to 0.55 when the mole fraction of the steam in the feed gas is not between 0.15 to 0.6.
9 . The device for the production of syngas according to claim 8 , wherein the reaction chamber comprises a tubular reactor chamber.
10 . The device for the production of syngas according to claim 8 , wherein the reaction chamber is delimited by a tubular structure having an inner diameter corresponding to the diameter of the reaction chamber.
11 . The device for the production of syngas according to claim 10 , wherein a heat transfer fluid emanating from the heat source is guided along the longitudinal dimension of the tubular reaction chamber such as to transfer thermal energy into the reaction chamber across the tubular structure delimiting the reaction chamber.
12 . The process for the production of syngas according to claim 1 , wherein the mole fraction of the hydrocarbon in the feed gas is between 0.45 and 0.5.
13 . The device for the production of syngas according to claim 8 , wherein the reaction chamber comprises a tubular reactor chamber having a diameter of from about 0.02 m to about 0.2 m or a length of at least 5 times the diameter.