초록 ▼

A reactor for steam reforming of hydrocarbon fuel to produce hydrogen having an inner cylindrical wall and outer cylindrical wall which provide an annular reaction chamber within which solid particles such as catalysts are disposed. During operation of the reactor, the reactor goes through temperatu

A reactor for steam reforming of hydrocarbon fuel to produce hydrogen having an inner cylindrical wall and outer cylindrical wall which provide an annular reaction chamber within which solid particles such as catalysts are disposed. During operation of the reactor, the reactor goes through temperature cycles in which the temperature of the reactor is increased and decreased, such as, during start up and shut down and the volume within the annular reaction chamber increases during heating a greater amount than the volume of the solid particles due to different coefficients of expansion of the inner and outer walls and of the solid particles. This differential expansion allows the solid particles to slump when the temperature of the reactor is elevated and results in pressure being exerted by the walls of the reactor against the solid particles when the temperature of the reactor is reduced. This pressure may result in crushing of the solid particles. The reactor incorporates a design which eliminates or reduces crushing of the solid particles.

대표청구항 ▼

An annular reactor for steam reforming hydrocarbon fuel comprising: a generally cylindrical inner wall, said inner wall having a thickness t1 in the range of 0.02 to 0.25 inches, said inner wall being capable of a limited degree of yielding in the radial inward direction in response to applied force

An annular reactor for steam reforming hydrocarbon fuel comprising: a generally cylindrical inner wall, said inner wall having a thickness t1 in the range of 0.02 to 0.25 inches, said inner wall being capable of a limited degree of yielding in the radial inward direction in response to applied forces, said inner wall having an outer diameter D1 in the range of 1 to 11 inches and a coefficient of thermal expansion a5×10-6 to 12×10-6°F.-1, said inner wall having a modulus of elasticity E in the range of 27×10-6 to 32×10-6 psi; an intermediate wall, said intermediate wall being coextensive in length with said inner wall and being coaxial therewith to define a first annular chamber, said intermediate wall having a thickness t2 in the range of 0.1 to 1.0 inches and an inner diameter D2 in the range of 2 to 12 inches, the coefficient of thermal expansion and modulus of elasticity of said intermediate wall being chosen to be the same as those of said inner wall, said intermediate wall always being thicker than said inner wall; catalyst particles disposed in said first annular chamber between said inner and intermediate walls, said catalyst particles having a coefficient of thermal expansion ac in the range of 3×10-6 to 8×10-6°F.-1; a generally cylindrical outer wall, said outer wall being coaxial with said inner and intermediate walls to define a second annular chamber between a portion of said intermediate and outer walls, said outer wall having a thickness t3 in the range of 0.02 to 0.25 inches, the thickness of the outer wall always being less than the thickness of the intermediate wall, said outer wall having an inner diameter D3 in the range of 4 to 16 inches, said outer wall being chosen to have a coefficient of thermal expansion and a modulus of elasticity commensurate with those of the inner and intermediate walls; a particulate heat exchange material disposed in said second annular chamber between said outer and intermediate walls, said heat transfer material being pervious to fluid flow and having a coefficient of thermal expansion ap in the range of 3×10-6 to 8×10-6°F.-1, said inner wall, intermediate wall, catalyst particles, outer wall and heat transfer material respectively being subjected to thermal cycles D2, D1, Dc, D3 and Dp, said thermal cycles being between about 400°F. and about 2000°F., said reactor meeting the following constraint equations: [Figure] and [Figure] where the mechanical pressure Pc on the solid particle bed after cooling of the walls defining the first annular chamber and the mechanical pressure Pp on the heat transfer material after cooling of the walls defining the second annular chamber do not exceed 7500 psi and wherein B is the bulk modulus of the catalyst particles and B′is the bulk modulus of the heat transfer material; and means delivering a gaseous fuel to the base of said first annular chamber for flow upwardly through said catalyst particles.