Patent ID: 8414840

Claim:
An isothermal vertical reactor for a chemical reaction, comprising: a shell with a longitudinal axis; at least a gas inlet for a fresh gas charge and a product outlet; at least a first gas-permeable wall parallel to said longitudinal axis, and a second gas-permeable wall parallel to said longitudinal axis, so that an inlet gas distribution chamber is defined between the first gas-permeable wall and the shell of the reactor, and a product collecting chamber in communication with said product outlet is defined between the second gas-permeable wall and the shell; a catalytic bed accommodated inside the shell, the gas permeable walls of said inlet gas distribution chamber and said product collecting chamber facing said catalytic bed; and a heat exchanger embedded in said catalytic bed, the heat exchanger comprising a bundle of U tubes, each of said U tubes having two straight portions fixed to a bottom tube sheet or manifold and connected by a U-shaped portion, thus forming a U-shaped end portion of the tube bundle, wherein a first straight portion of said U tubes fixed to said bottom tube sheet or manifold is in communication with a fluid distribution chamber while a second straight portion of said U tubes fixed to said bottom tube sheet or manifold is in communication with a fluid collecting chamber, said fluid distribution chamber and said fluid collecting chamber being delimited by a partition wall; wherein said gas inlet is disposed to direct the fresh charge in an upper chamber of the reactor, over the catalytic bed, and wherein the catalytic bed and the inlet gas distribution chamber are in communication with said upper chamber of the reactor, so that during operation of the reactor, a first portion of the fresh charge can enter directly the catalytic bed, passing through the U-shaped portion of the tube bundle, and a second portion of the fresh charge can enter the inlet gas-distribution chamber, the first portion flowing in the catalytic bed and towards the product collecting chamber with a mixed axial-transversal flow, and the second portion flowing in the catalytic bed, from the inlet gas distribution chamber towards said product collecting chamber, with a substantially transversal flow.