Chemical reactor tower

Apparatus for the production of hydrogen chloride and for its absorption to hydrochloric acid comprises a vertical tower having an upper section serving as an absorption zone which is charged at the top with aqueous absorption liquid and traversed upwardly by gases containing the hydrogen chloride to be absorbed, a middle section containing a burner chamber provided with a burner having inlet means for introducing the gases forming hydrogen chloride and a bell above the burner provided with openings for the exit of hydrogen chloride formed into the upper absorption zone, and a lower section in the form of a heat exchanger into which the hydrochloric acid, produced in the absorption zone flows after passing down over the inner wall of the middle section and the outer wall of the bell which are thereby cooled, the heat exchanger being provided with outlet means for withdrawing the hydrochloric acid from the tower, in which tower the middle and lower sections are connected to one another by a dip seal. Chlorine and hydrogen or a hydrocarbon such as methane, propane, natural gas or domestic consumer gas are introduced into a burner chamber 1 and burnt in burner 3 which is operated through 5 to form hydrogen chloride which exits through openings 6 in bell 5 and is absorbed in water or dilute hydrochloric acid supplied at the top of the tower by unit 12 and flowing down through absorption zone 11 charged with filler bodies, waste gases and water vapour being discharged through 14. After absorption resultant aqueous hydrochloric acid containing 30-32% Hel flows down the tower and is deflected by 7 so as to flow down the outside walls of bell 4 and the inside wall of chamber 1 thereby cooling the burner chamber. Alternatively, member 7 can be omitted and the space between the outer wall of bell 4 and the inner wall of chamber 1 be charged with filler bodies to promote even distribution of the flow of acid. Openings 6 are shielded to prevent liquid flowing through bell 4 on to the burner. Hydrochloric acid flows through chamber 1 and enters heat exchanger 9 through clip seal 8, where it is cooled to the desired temperature and discharged through 10. In order to produce hydrogen chloride containing 100% Hcl by a modification of the above apparatus the heat exchanger 9 may be operated as a heating device so that the entering acid is freed of part of its Hcl content which escapes as a concentrated vapour through 16 and is thereafter freed in a coo