Method and apparatus for flue-gas cleaning

Abstract: A method of flue-gas cleaning comprising the separa­ tion of water-soluble substances from flue gases containing water vapour. The invention is characterized in that the flue gases are caused to be cooled by direct contact between flue gas and atomized water in two or more separation steps, where in a separation step (2) subsequent in the flow direc­ tion of the flue gases the flue gases are cooled by atomized water to a temperature, at which the water in the flue gases is condensed out, which water is collected and thereafter both recirculated for utilization in said subsequent separa­ tion step (2) and introduced into a separation step (1) prior in the flow direction of the flue gases. In said prior separation step the water is atomized and meets uncleaned flue gases, the water-soluble and potentially water-soluble substances of which thereby are solved in the atomized water. The water thus impurified is collected for further treatment.

Description: This invention relates to a method and an apparatus for the cleaning of flue gases, especially of flue gases containing compounds soluble in acid aqueous solutions. The present invention is intended particularly to be used for cleaning flue gases resulting from the combustion of household refuse, bulky waste, industrial waste or other fuel with a high water content, in respect of hydrochloric acid gas and heavy metals, such as mercury. Flue gases often are cleaned by using various types of mechanical filters and precipitators. More scarcely, such methods are combined with wet ones, at which the washing medium is supplied externally to the system as a separate material flow. In DE-B-24 49 057 a gas cleaning method is shown where impurified water collected from a washer is introduced in a heat exchanger located prior to the washer in the flow direction of the flue gases. However, according to DE-B-24 49 057 a washing liquid is continuously fed into the washer and there is not disclosed to use the water contained in the flue gases. In FR-A-2,283,719 a gas cleaning method is used where in a last step the flue-gases are cooled so that water vapour in the flue-gases is condensed out. Flue-gases are cooled in a precooling tower and are further cooled in an intermediate cooler. Downstream of said cooler the flue-gases are introduced in a washing tower where the flue-gases are washed. The washing liquid is water or an alcaline solution. The water condensed out is used in said water spray tower, said intermediate cooler or in said washing tower. No liquid water is collected in said precooling tower or in said intermediate cooler. US-A-2,598,116 refers to a process for cooling sulphur burner gases. There is a precooling column and a main cooling column. External water is continuously introduced into the process in a subsequent step. Further, water collected in the subsequent step, a part of which is introduced into precooling column, is not cooled by a cooler before it is fed into said precooling column. SE-A-130 603 describes a process for recovering valuable substances from flue-gases. The gas is cooled by passing screens and a water bed. In a first step liquid is recirculated to obtain a concentrated end product fraction. In addition a comparatively diluted end product fraction is withdrawn from a subsequent step. DE 2 708 919 shows a gas cleaning method where a reaction column and a cooling tower are used, where a washing liquid is injected into the reaction column. The washing liquid from the reaction column is injected into the cooling tower. An apparatus is shown where there is a common container for collected washing liquid from the column and the tower, which container is a part of two flow circuits, namely a first comprising the reaction column and a second containing the cooling tower. In both flow circuits the washing liquid is recirculated via said container. According to the present invention, however, the water inherent in the flue-gas is utilized for cleaning the flue-gases, thereby achieving the separation of water-soluble compounds. These compounds are concentrated in a later step by precipitation and thereafter are removed from the system. The present invention, thus, relates to a method of flue-gas cleaning, comprising the separation of water-soluble substances from flue-gases containing water vapour, where the flue-gases are caused to directly contact atomized water in two or more separation steps, where in a subsequent one of said separation steps in the flow direction of the flue-gases, the flue-gases are cooled by atomized water to a temperature at which the water in the flue-gases is condensed out, so that the water content in the flue-gases leaving the subsequent step is less than the water content in the flue-gases entering a first of the separation steps, which water is collected and cooled. The invention is characterized in that said collected and cooled water is partly recirculated in said subsequent separation step and partly introduced into a prior one of said separation steps in the flow direction of the flue-gases, in which prior separation step the water is caused to be atomized and to meet uncleaned flue-gases, the water-soluble substances of which thereby are solved in the atomized water, and where the water thus impurified is collected without recirculation and withdrawn from the prior separation step to be further treated in a separate means, and where no water is added to the separation steps in addition to the water required for initially starting the cleaning process. The invention further relates to an apparatus for the cleaning of flue gases according to said method, which apparatus is of the type and has the main characterizing features as defined in the attached claim 4. The invention is described in greater detail in the following, with reference to an embodiment shown in the accompanying drawing of an apparatus according to the invention, the drawing Figure showing an apparatus, of which a first and a second separation step are illustrated partially cut open. In the Figure, a first separation step 1 and a second separation step 2 are shown, which are interconnected to a pipe 3. An inlet pipe 4 for flue gases is located in the lower portion of the first separation step, and an outlet pipe 5 for cleaned flue gases is located at the upper portion of the second separation step 2. The numerals 6, 7, 8 designate control valves, the numerals 9 and 10 designate pumps, 11 is a water and/or vapour seal, and 12 is a separation tank. The arrows in the Figure indicate flow directions. Flue gases 13 from a combustion plant are intended to be fed into the apparatus via the inlet pipe 4. Prior to their feed-in, the flue gases preferably are cooled in a cooler (not shown) to a temperature of 200-250°C. The flue gases thus fed-in rise through the first separation step 1. The first separation step 1 comprises a cylindric vessel, in which a tube system 14 is located. The tube system 14 comprises a plurality of substantially vertically arranged tubes 15, which are connected directly or indirectly to one or more feed pipes 16, 17. Each tube 15, 16 is provided with a great number of apertures acting as spray nozzles for water. For reason of clearness, only a small number of apertures have been marked in the Figure by outflowing water 18. In operation, water is pumped by a pump 10 in the feed pipe 17 to the tube system 14 whereby atomized water flows out through said apertures. The upward flowing flue gas is hereby mixed effectively with water droplets. The second separation step 2 also comprises a cylindric vessel, in which a tube system 19 is located, which corresponds to the one described with reference to the first separation step. The tube system 19 has the same object and function. In operation it is supplied with water from a feed pipe 20 by means of a pump 9. The second separation step is formed at its lower end with an upward convex portion 21. The said pipe 3 connects the upper portion of the first separation step to the lower portion of the second separation step 2. The pipe 3 is connected to the highest point of the convex portion 21, and an annular cup 22 is formed in the lower portion of the second separation step. An outlet pipe 23 is connected at the bottom of said cup 22. A flow circuit for the second separation step 2 comprises-marked by the screws 24 in the flow direction-the outlet pipe 23, a pump 37, a cooler 25 such as a heat pump, a possible device 26 for adjusting the pH-value of the water and the content of suspended substances, said pump 9, a control valve 6 and, finally, said feed pipe 20, which is connected to the tube system 19. The said feed pipe 17 to the tube system 14 of the first separation step 1 is connected to said flow circuit via a control valve 8. In the lower portion of the first separation step 1, a discharge pipe 27 is located which opens into a tank 12 and is provided with a water and/or vapour seal. The tank 12 is provided with one or several sections or may consist of separate units connected in series for the neutralisation and/or precipitation of different substances in the water coming from the lower separation step. For this purpose, the tank 12 is provided with one or more nozzles 30, 31, 32 or the like for adding chemicals for the precipitation of desired substances and with means for stirring and mixing as well as for separating resulting precipitates. As mentioned above in the introductory portion, the object of the invention is to neutralize and/or separate water-soluble or potentially water-soluble substances from gases and flue gases with a high water vapor content. The separation of the substances is effected by cooling the gas or flue gas by direct contact between gas and atomized water in two or more separation steps connected in series. The necessary water amount is obtained by lowering the gas temperature to a desired level below its dew point. The second separation step 2 has the object primarily by cooling the gas to condense-out the water amount, which is desired in the first separation step 1. It is thereby possible to use simple structural material in the second separation step. The condensing-out of water from the gases proceeds in such a manner, that the gases are cooled by water flowing out of the tube system 19 to a temperature below the dew point at the pressure in question. For the gases flowing into the second separation step 2 an inlet temperature of e.g. 60-70°C and an outlet temperature of the gases of about 35°C are chosen. The separation water is circulated in said flow circuit. The water is cooled in the cooler 25, which preferably comprises a heat pump. Heated medium can pass out through a pipe 28. As mentioned above, a device 26 not described in detail can be provided for adjusting the properties, for example the pH-value, of the water. When the water or separated suspended substances must be drained off from the flow circuit, the aforesaid valve 7 is used together with an associated pump 38 and a discharge pipe 29. The main part of all of the water which had been condensed out in the second separation step. However, is passed via the valve 8 from the flow circuit to said feed pipe 17 and via the pump 10 to the tube system 14 of the first separation step 1. The valve 8 is located after the cooler 25, and therefore cooled water is caused to be atomized and sprayed via the system in the first separation step 1. In the first separation step 1 incoming flue gases, which have a temperature of e.g. 215-230°C, are cooled to the aforesaid temperature of 60-70°C, whereby the water in the gas to some part can be condensed out, and water-soluble substances are washed out of the gas. The part of the water which is not evaporated thereby, is removed from the system through the discharge pipe 27 to the tank 12. The apparatus and the method are especially suitably used for separating hydrochloric acid gas from flue gases and for substances forming complex substances with chlorine with a low volatality. Thus, hydrochloric acid, HCl gas and water-soluble mercury compounds and other water-soluble substances are solved and separated. Especially valuable is the separation of mercury out of flue gases from the combustion of e.g. household refuse. Due to the presence of HCl in the flue gases, complex ions between mercury and chlorine are formed, which are not volatile but remain in aqueous phase. The cleaning in the first separation phase 1, of course, is not 100 per cent, but the second separation step 2 acts as final cleaning step as well as cooler. The contact between gas and liquid, thus, is intended to take place in a combination of counter-current and cross-current apparatuses, where liquid is sprayed-in on different levels in the separation steps, whereby both a low pressure drop for the gas and a high washing-out effect are obtained. As has appeared from the aforesaid, no washing water has to be added in addition to the water required for initially starting the process. The process, thus, is carried out with a relatively small amount of water. Thus is of advantage for the further treatment of the water enriched with impurities. The water injected in the first separation step 1, as mentioned, flows out through the discharge pipe 27 in the tank 12. As the washing-out proper takes place in a system with no re-circulation of liquid, a high and specific separation of the substance in question is obtained. These substances can be neutralized in the tank and, respectively, be separated from the water by combinations of reaction and filtering steps. The water collected in the tank system 12 is treated with chemicals, which are specific for the impurities desired to be separated from the water or be further treated. Lime (CaO) e.g. is added for neutralizing hydrochloric acid (HCl). Preferably also mercury is to be separated, for which purpose the water-soluble sulphide Na 2 S is added. CaO and Na 2 S are added in a suitable way, for example through the nozzles 30, 31, 32. The present invention is not restricted to the separation of hydrochloric acid and mercury, which are of interest when household refuses are combusted, but every comopund desired can be separated in the tank system 12 by adding known chemicals reacting with the substance to be separated. Precipitates resulting therefrom can be collected in different separate sections 33, 34, 35 in the tank system 12. Purified water can thereby be discharged through a discharge pipe 36. Resulting residue products, such as precipitates, can thereafter be stored finally or be utilized for other purposes. The method and the apparatus, thus, render it possible to extremely effectively separate impurities in flue gases by using only the water contained in the flue gases. This implies, that the water collected has a high content of impurities, which facilitiates their further treatment. The method and the apparatus, furthermore, are extremely simple to carry out and, respectively, to manufacture, so that the flue-gas cleaning costs can be kept very low compared to conventional art. The apparatus, of course, must be dimensioned according to the demand in respect of flue-gas volume and temperature, impurities to be separated, etc. As an example can be mentioned, however, that when the vessel of the separation steps has a diameter of about 2 m and a height of 6 m, the vertical tubes have a total of about 100 apertures with a diameter of 2,5 mm. At such a design and a flue-gas volume of 9 m 3 /s, 0,6 litre water/s are generated, which is sufficient for substantially separating HCl and Hg from flue gases from normal household refuse.

Claims: A method of flue-gas cleaning, comprising the separation of water-soluble substances from flue-gases containing water vapour, where the flue-gases are caused to directly contact atomized water in two or more separation steps, where in a subsequent one of said separation steps in the flow direction of the flue-gases, the flue-gases are cooled by atomized water to a temperature at which the water in the flue-gases is condensed out, so that the water content in the flue-gases leaving the subsequent step is less than the water content in the flue-gases entering a first of the separation steps, which water is collected and cooled, wherein said collected and cooled water is partly recirculated in said subsequent separation step and partly introduced into a prior one of said separation steps in the flow direction of the flue-gases, in which prior separation step the water is caused to be atomized and to meet uncleaned flue-gases, the water-soluble substances of which thereby are solved in the atomized water, and where the water thus impurified is collected without recirculation and withdrawn from the prior separation step to be further treated in a separate means, and where no water is added to the separation steps in addition to the water required for initially starting the cleaning process. A method as defined in claim 1, characterized in that in each of the separation steps water is introduced by a pump in a tube system comprising a great number of apertures or nozzles for atomizing the water, and that atomized water is caused to flow out to the greater part of the volume of a vessel enclosing the separation step. A method as defined in claim 1 or 2, characterized in that at said further treatment of collected impurified water chemicals are added, which together with the impurity in question form a water-insoluble compound, which is separated from the water. An apparatus for flue-gas cleaning comprising the separation of water-soluble substances from flue-gases containing water vapour, where two or more separation stages (1,2) are comprised, each of which is provided with means (14,19) for injecting atomized water into a vessel and each of which is provided with an inlet and an outlet pipe (4,3,5) for passing flue-gases through the vessel, where the subsequent one of the separation stages (2) in the flow direction of the flue-gases is provided with a flow circuit for water comprising an outlet pipe (23) from said subsequent stage, a cooler (25), a pump (9) and an inlet pipe (20) to a tube system (19) comprising water atomizing means in said subsequent stage for recirculation only the water separated from the flue-gases in said subsequent separation stage (2) in order to continously separate water from the flue-gases, wherein the water recirculated in said subsequent separation stage is cooled by a cooler, which is located in the flow direction after the vessel of the subsequent separation stage but before a connection pipe (17) connected between said flow circuit and a prior one of said separation stages (1) in the flow direction of the flue-gases to provide said prior separation stage with water thus separated, whereby water-soluble substances in the flue-gases are separated in said prior separation stage, which prior separation stage (1) is connected to a collecting means (12) for collecting the water fed to the prior step without recirculation and for further treatment of water thus impurified, and wherein the apparatus is arranged such that, in use of the apparatus, no water is added to the separation steps in addition to the water for initially starting the cleaning process. An apparatus as defined in claim 4, characterized in that each of the separation stages (1,2) comprises a vessel provided with said means (14,19), which comprise a tube system (14,19) consisting of a plurality of tubes (15,16) with a great number of apertures or nozzles, so that at the pumping of water into the tube system (14,19) atomized water meets flowing flue-gases, and that the tube system (14,19) is arranged so that atomized water can be caused to flow out to the greater part of the volume of said vessel. An apparatus as defined in claim 4 or 5, characterized in that the subsequent separation stage (2) is cylindric and formed with an upward convex bottom (21), in the highest point of which an inlet pipe (3) for flue-gases is located, and that an annular cup (23) thus formed about the bottom for collecting separated water is connected via a connecting pipe (23) to the remaining part of the flow circuit (25,20,6,9). An apparatus as defined in claim 4, 5 or 6, characterized in that said vessels are arranged for vertical upward directed transport of flue-gases, and that said tubes (15) with apertures or nozzles are arranged vertically in the vessel.

Inventors: HOVSENIUS GUNNAR, LINDAHL ERIK, HOVSENIUS, GUNNAR, LINDAHL, ERIK
Applicants: HOVSENIUS GUNNAR, LINDAHL ERIK, HOVSENIUS, GUNNAR, LINDAHL, ERIK
Application year: 1984
Main classification: B01D53
IPC codes: B01D53