Abstract This invention relates to apparatus for carrying out physical and/or chemical processes, more specifically a heat exchanger (10) of the continuous type, comprising a large number of vertical heat exchanger tubes (18) mounted between a lower chamber (17) and an upper chamber (16) within a jacket (15). Within the tubes (18) small solid particles are kept in a fluidized condition by the fluid medium passing up from the lower chamber (17) through the tubes (18), so as to achieve a good heat transfer, whereas also any deposit will be removed from the inner tube walls. For the downward flow of the granular mass at least one return tube (21) is provided. Downward circulation of the fluid medium through the return tube (21) should be minimal, however, which can be achieved by an increase of the pressure difference between the upper and lower chamber (16; 17), which increase of the pressure difference can be achieved by fitting several distribution plates (24; 42) at a level above the return tube (21) outlet into the lower chamber (17), preferably so that the apertures in the various distribution plates (24; 42) of the multiple design are not vertically in line. The second distribution plate (42) also serves to minimize excessive wear of the material of the jacket (15) due to the eddying motion of the granules.
Apparatus for carrying out physical and/or chemical processes, in particular a heat exchanger of the continuous type, comprising a bundle of parallel vertical riser tubes, an upper chamber, a lower chamber, an upper pipe plate and a lower pipe plate for open connection of the pipe bundle to the upper and lower chambers respectively, a granular mass that can be kept in a fluidised condition at least in the riser tubes by a fluid medium that flows during operation upwardly through the lower chamber, the riser tubes and the upper chamber, a distribution plate for the granular mass in the lower chamber, and at least one return tube with an outlet below the distribution plate for return of an overflow of granules above the upper pipe plate from the upper chamber to the lower chamber, wherein each riser tube is provided with an inflow element extending into the lower chamber from the lower pipe plate to a level above the distribution plate through which the return tube or return tubes projects or project, and the lower chamber is provided with a device that prevents the granules from reaching the lower chamber inlet for the fluid medium at standstill characterized in that a constriction (32) is provided in the ends of the riser tubes (18) that open into the upper chamber (16).
Claim 2
Dependent Claim
221 words
Apparatus for carrying out physical and/or chemical processes, in particular a heat exchanger of the continuous type, comprising a bundle of parallel vertical riser tubes, an upper chamber, a lower chamber, an upper pipe plate and a lower pipe plate for open connection of the pipe bundle to the upper and lower chambers respectively, a granular mass that can be kept in a fluidised condition at least in the riser tubes by a fluid medium that flows during operation upwardly through the lower chamber, the riser tubes and the upper chamber, a distribution plate for the granular mass in the lower chamber, and at least one return tube with an outlet below the distribution plate for return of an overflow of granules above the upper pipe plate from the upper chamber to the lower chamber, wherein each riser tube is provided with an inflow element extending into the lower chamber from the lower pipe plate to a level above the distribution plate through which the return tube or return tubes projects or project, and the lower chamber is provided with a device that prevents the granules from reaching the lower chamber inlet for the fluid medium at standstill characterized in that a constriction (32) is provided in the ends of the riser tubes (18) that open into the upper chamber (16).
Claim 3
Dependent Claim
28 words
Apparatus according to claim 1, characterised by an upper pipe plate (19) with apertures (32) for the riser tubes (18) having smaller cross-section than the riser tubes themselves.