A reformer suitable for micro-scale design has horizontal catalyst tube(s) passing through a baffled radiant section for convective and radiant heat transfer to the tube(s). To reduce the footprint and/or to facilitate field assembly a combustion chamber and convection section can be oriented transversely with respect to the radiant section; the tube(s) can be horizontal and/or include structured catalyst; and/or the combustion chamber provides flameless combustion or produces a flame without impinging on the tubes. Also, a skid frame-mountable version of the reformer; and a process for transporting, assembling, and/or operating the steam methane reformer.

A reformer suitable for micro-scale design has horizontal catalyst tube(s) passing through a baffled radiant section for convective and radiant heat transfer to the tube(s). To reduce the footprint and/or to facilitate field assembly a combustion chamber and convection section can be oriented transversely with respect to the radiant section; the tube(s) can be horizontal and/or include structured catalyst; and/or the combustion chamber provides flameless combustion or produces a flame without impinging on the tubes. Also, a skid frame-mountable version of the reformer; and a process for transporting, assembling, and/or operating the steam methane reformer.

A flow reactor or flow reactor component includes a base plate, a first fluid module having first and second major surfaces, an internal process fluid passage, and a heat exchange channel in the first major surface, the first major surface stacked on the base plate; a second fluid module having first and second major surfaces, an internal process fluid passage and a heat exchange channel in the first major surface, the first major surface stacked on the second major surface of the first fluid module, optional additional fluid modules of the same configuration as the first and second fluid modules stacked successively on the second fluid module, and a top plate having a heat exchange channel in a bottom major surface thereof with the bottom major surface stacked on an uppermost fluid module of (1) the second fluid module and (2) the optional additional fluid modules.

A reactor has a heat exchanging body having a heat medium flow channel that a heat medium fluid flows and a reaction flow channel that a reaction fluid flow, and at least one detection part for detecting temperature of a fluid in one or both of the heat medium flow channel and the reaction flow channel. At least one installation hole extends in a skew position to the flow channel and includes an opening portion communicating with the flow channel. The detection part is installed at the opening portion and contacts the flowing fluid. At least one fluid guide hole is formed along the flow channel from the opening portion of the installation hole.

The invention relates to a micro-reactor for carrying out at least one catalytic reaction between two or more reactants in each case, comprising a stacking sequence of reaction surfaces (1) for carrying out at least one exothermic reaction, and a cooling region (6) divided at least into individual fields (6) with feed and discharge devices for the coolant.

A reactor has a heat exchanging body having a heat medium flow channel that a heat medium fluid flows and a reaction flow channel that a reaction fluid flow, and at least one detection part for detecting temperature of a fluid in one or both of the heat medium flow channel and the reaction flow channel. At least one installation hole extends in a skew position to the flow channel and includes an opening portion communicating with the flow channel. The detection part is installed at the opening portion and contacts the flowing fluid. At least one fluid guide hole is formed along the flow channel from the opening portion of the installation hole.

The invention relates to a micro-reactor for carrying out at least one catalytic reaction between two or more reactants in each case, comprising a stacking sequence of reaction surfaces (1) for carrying out at least one exothermic reaction, and a cooling region (6) divided at least into individual fields (6) with feed and discharge devices for the coolant.