Process for Injection of Fluid, e.g. Slurry in e.g. Flue Gases and a Nozzle Device for the Accomplishment of the Process

This invention relates to a process for injection of fluid e.g. slurry in e.g. flue gases and a nozzle device for the accomplishment of the process.

By flue gas cleaning, especially by cleaning of flue gas from sulphuric gases like SO.sub.2 and SO.sub.3, basic substances are often injected, e.g. CaO, Na.sub.2 CO.sub.3 or MgO in the flue gas.

To reach an acceptable reaction of these substances with the sulphuric flue gases, this should be done together with water in the state of a slurry. The reaction with SO.sub.2, which is the main part of the sulphuric substances, is easier accomplished when the flue gas temperature is lowered and gets close to the dew point of the flue gas. Before the slurry comes out into the flue gas, it should, however, be disintegrated as much as possible, so that (a) the reactive surface, which is exposed to the flue gas, gets as large as possible and (b) the slurry manages to evaporate before it reaches the following dust collector.

To obtain the above mentioned disintegration, another medium, e.g. steam or compressed air, is caused to act upon the injected slurry in a special nozzle device according to the invention. This device is characterized by the claims submitted herewith. This general idea itself is already known, but the nozzle device according to the invention shows a simple way of accomplishing this result, which makes it easier to use this technique also for small coal- and oilfired boilers.

The invention will now be further described with reference to the drawing enclosed, where

FIG. 1 shows a cross section of the device seen from the side and

FIG. 2 shows a view of intakes 2 and 3 illustrating the manner in which the streams of slurry and steam or compressed air are mixed in the nozzle.

FIG. 1 shows a flue gas duct 1, in which a particle distributor or a nozzle device 4 is placed. To the nozzle are connected (a) an intake 2 of basic slurry, preferably slaked lime and/or fly-ash suspended and/or dissolved in water and (b) an intake 3 of compressed air or steam. The principle is, that the slurry is injected as a thin stream into a wider stream of e.g. compressed air, after which the fine drops obtained from the slurry are prevented from agglomerating into bigger drops, when the flue gas is spreading these at the passage through the nozzle 4. The forming of the fine drops of slurry is best shown in FIG. 2. The slurry comes in through intake 2, after which it comes into a wear-resistant part 5 of e.g. ceramic or hard metal. In the wear-resistant part there is a smaller opening 2', in which the slurry is accelerated to a high speed. The wear-resistant part 5 is used, since lime stone slurry and fly-ash, which also can be mixed in the slurry, is very abrasive. The slurry opening 2' is centred in relation to an opening of the compressed air pipe 3', at which the slurry and compressed air meet at very high relative speeds. The slurry stream is then "peeled off" on its way into the compressed air stream, after which the slurry drops, now formed, make a 180.degree. turn and accelerate against the sheet created by said air stream, which is in the front of the wear-resistant part 5. The slurry drops hit this sheet at a high speed, after which another disintegration of the drops occurs explosively.

The invention is of course not restricted to this design but can be varied within the scope of the invention.