Apparatus for Producing Synthesis Gas
An apparatus ( 1 ) for producing synthesis gas is described, the apparatus comprising a substantially cylindrical shell ( 2 ) closed by opposite bottoms ( 3, 4 ), at least one inlet opening ( 8 ) for feeding a gaseous flow comprising oxygen, at least one inlet opening ( 7 ) for a gaseous flow comprising hydrocarbons and at least one outlet opening for a flow of synthesis gas and at least one burner ( 9 ) in fluid communication with a reaction chamber ( 15 ) for partially oxidising and/or reforming said hydrocarbons obtaining said flow of synthesis gas, and being characterised in that it comprises a pipe ( 12 ) of a ceramic material extended inside said shell ( 2 ), said pipe ( 12 ) of ceramic material internally defining said reaction chamber ( 15 ).
1 . An apparatus for producing synthesis gas comprising:
a substantially cylindrical shell closed by opposite bottoms;
at least one inlet opening for feeding a gaseous flow comprising oxygen;
at least one inlet opening for a gaseous flow comprising hydrocarbons;
at least one outlet opening for a flow of synthesis gas; and
at least one burner in fluid communication with a reaction chamber for partially oxidising and/or reforming said hydrocarbons obtaining said flow of synthesis gas, and a pipe of a ceramic material extended inside said shell, said pipe of ceramic material internally defining said reaction chamber.
2 . The apparatus according to claim 1 , wherein said pipe of ceramic material is substantially coaxial with said shell.
3 . The apparatus according to claim 1 , wherein said pipe of ceramic material has a thickness of between 5 and 50 mm.
4 . The apparatus according to claim 1 , wherein the pipe of ceramic material is obtained through extrusion and sintering of a ceramic material or plasma deposition procedures.
5 . The apparatus according to claim 1 , wherein the ceramic material used to produce said pipe comprises sintered aluminium oxides and/or zirconium oxides and/or carbides, such as silicon carbides and/or rare earth oxides.
6 . The apparatus according to claim 1 , wherein said pipe of ceramic material is formed from modules of pipe pieces fitted together.
7 . The apparatus according to claim 1 , wherein said pipe of ceramic material contains a catalytic bed in a portion thereof so as to divide said reaction chamber into two distinct reaction zones.
8 . The apparatus according to claim 1 , further comprising an interspace between said pipe of ceramic material and said shell, said interspace being substantially filled with an insulating material.
9 . The apparatus according to claim 8 , wherein said insulating material is a fibrous material, a non-fibrous material or a mixture thereof.
10 . The apparatus according to claim 9 , wherein said fibrous or non-fibrous insulating material is chosen from the group comprising refractory oxides, refractory nitrides, refractory carbides and combinations thereof.
11 . The apparatus according to claim 9 , wherein said fibrous or non-fibrous insulating material includes one or more metallic oxides chosen among alumina, silicon oxides such as silica, rare earth (lanthanides) oxides and mixtures thereof.
12 . The apparatus according to claim 8 , wherein said insulating material is in the form of loose fibres, tape, felt, woven or unwoven fabric.
13 . The apparatus according to claim 8 , wherein said insulting material is in the form of ceramic fibres.
14 . The apparatus according to claim 13 , wherein said insulating material comprises ceramic fibres made of alumina and silica.
15 . The apparatus according to claim 1 , wherein said at least one burner is at least partially inserted into a housing formed in a nozzle of the upper bottom and is provided with said at least one inlet opening for feeding a gaseous flow comprising oxygen and with said at least one inlet opening for a gaseous flow comprising hydrocarbons.
16 . The apparatus according to claim 3 , wherein said pipe of ceramic material has a thickness of between 20 and 50 mm.