EP3675987A1 - Procédé de traitement d'effluents gazeux contenant des oxydes de soufre - Google Patents

Procédé de traitement d'effluents gazeux contenant des oxydes de soufre

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Publication number
EP3675987A1
EP3675987A1 EP18807308.4A EP18807308A EP3675987A1 EP 3675987 A1 EP3675987 A1 EP 3675987A1 EP 18807308 A EP18807308 A EP 18807308A EP 3675987 A1 EP3675987 A1 EP 3675987A1
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EP
European Patent Office
Prior art keywords
exhaust gas
exhaust
gas treatment
injection
range
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Application number
EP18807308.4A
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German (de)
English (en)
Inventor
Bernd Morun
Paul-Udo Schmidt
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Drysotec GmbH
Original Assignee
Drysotec GmbH
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Publication date
Application filed by Drysotec GmbH filed Critical Drysotec GmbH
Publication of EP3675987A1 publication Critical patent/EP3675987A1/fr
Withdrawn legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/48—Sulfur compounds
    • B01D53/50—Sulfur oxides
    • B01D53/508—Sulfur oxides by treating the gases with solids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/06—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
    • B01D53/10—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds with dispersed adsorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26—Drying gases or vapours
    • B01D53/265—Drying gases or vapours by refrigeration (condensation)
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75—Multi-step processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/81—Solid phase processes
    • B01D53/83—Solid phase processes with moving reactants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/30—Alkali metal compounds
    • B01D2251/304—Alkali metal compounds of sodium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/40—Alkaline earth metal or magnesium compounds
    • B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/602—Oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/604—Hydroxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/60—Inorganic bases or salts
    • B01D2251/606—Carbonates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/112—Metals or metal compounds not provided for in B01D2253/104 or B01D2253/106
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/30—Physical properties of adsorbents
    • B01D2253/302—Dimensions
    • B01D2253/304—Linear dimensions, e.g. particle shape, diameter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/30—Physical properties of adsorbents
    • B01D2253/302—Dimensions
    • B01D2253/306—Surface area, e.g. BET-specific surface
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/30—Physical properties of adsorbents
    • B01D2253/302—Dimensions
    • B01D2253/311—Porosity, e.g. pore volume
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/30—Sulfur compounds
    • B01D2257/302—Sulfur oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/025—Other waste gases from metallurgy plants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/12—Methods and means for introducing reactants
    • B01D2259/122—Gaseous reactants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/12—Methods and means for introducing reactants
    • B01D2259/128—Solid reactants

Definitions

  • the present invention relates to the technical field of treating exhaust gases containing sulfur oxides (SO x ), in particular exhaust gases from industrial incinerators, the so-called flue gases, or exhaust gases from industrial processes, such as steelmaking (eg blast furnace gases, etc.).
  • SO x sulfur oxides
  • the present invention relates to a method for the treatment of exhaust gases containing sulfur oxides, in particular from technical incinerators, such as flue gases, or from technical processes, for the purpose of removing and / or separating the sulfur oxides or for the purpose of reducing the sulfur oxide content and an apparatus for carrying out the process.
  • the proportion of carbon monoxide in the flue gases is kept low by targeted control of the combustion.
  • carbon monoxide produced can be returned to the combustion chamber or converted into carbon dioxide in a subsequent burner stage.
  • the proportion of nitrogen oxides in the flue gases is kept low by targeted control of the conditions under which the combustion takes place.
  • a reduction of the nitrogen oxides with nitrogen oxide-containing compounds, such as ammonia or urea, to elemental nitrogen by spraying or injecting the nitrogen-containing substances in the combustion chamber at about 900 ° C or by a downstream, catalytically activated reaction.
  • Particulate matter, soot and fly ash can be separated from the flue gases by a filtration system, such as bag filters or electrostatic precipitators, while volatile organic compounds (VOCs) can be removed by adsorption on activated carbon or by condensation.
  • a filtration system such as bag filters or electrostatic precipitators
  • VOCs volatile organic compounds
  • a regenerative process for flue gas desulfurization is, for example, the Wellmann-Lord process, which converts the sulfur dioxide from the flue gas with a sodium sulfite solution to sodium hydrogen sulfite. Later heating of the sodium hydrogen sulphite releases the sulfur dioxide again and the sodium sulphite can subsequently be used for the renewed absorption of sulfur dioxide.
  • the non-regenerative processes all aim to bind sulfur oxides by chemical reaction as sulfates.
  • ammonia REA process has no great industrial significance, as it combines the disadvantages of the aforementioned methods.
  • the recovered ammonium sulfate can be used as a fertilizer.
  • exhaust gases from technical processes such as steel production (for example, exhaust gases from the chemical roasting or Sinterbandher too, blast furnace gases from the blast furnace process, etc.), may contain significant amounts of sulfur oxides. So far, however, no efficient method for the separation of sulfur oxides from the relevant exhaust gases of these technical processes are known in this context.
  • the separation efficiency can be improved under certain conditions, after which the economics of the dry sorption process can be increased.
  • These include, above all, the increase in the relative exhaust gas humidity or an increase in the water vapor content in the exhaust gases. This can increase the efficiency of the dry sorption process.
  • the influence of the flue gas moisture is particularly noticeable in the deposition of sulfur dioxide. This can be achieved, for example, by adding or adding lime milk - a suspension of hydrated lime in the water - to the flue gas.
  • an exhaust gas treatment reagent which is, for example, calcareous.
  • the flue gas cools down.
  • the water content or the steam content of the flue gas or the exhaust gases can be increased. Both ultimately leads to the fact that the relative humidity and / or the water vapor content of the exhaust gases increases and a more effective separation of the pollutants of the exhaust gases is possible.
  • the disadvantage here is that when the exhaust gas is cooled to its taut, it comes to a condensation.
  • the condensates can cause corrosion damage in the flue gas duct, so that a sufficient temperature difference to the dew point of the exhaust gases should be maintained.
  • the pollutant separation improves as a result of the increased humidity of the exhaust gas, but also increases the risk of corrosion for the system components in the entire flue gas path and accordingly increase the investment costs and also the technical complexity.
  • the subsequently supplied exhaust treatment reagent causes caking or caking of system components.
  • the caking or caking thus caused can cause damage, so that water and / or water vapor can be supplied to the exhaust gas only within a small time frame or period of time relative to the actual service life of a dry sorption system.
  • the caking or caking prevent, although with an increasing pollutant separation and an increased efficiency of the dry sorption process, an increase in the humidity in the flue gas duct is technically usually not implemented.
  • the investment costs and downtimes caused for example due to a jagged nozzle exceed the temporary reduction in operating costs due to the saving of the exhaust gas treatment reagent due to the improved efficiency.
  • the laws on the emission of pollutants have been rigorously tightened in recent years, and it is expected in the future with even stricter rules, so that there is a great need for efficient and economical and environmentally sound treatment of the exhaust gases.
  • the present invention is based on the object, a method for the desulfurization of flue gases or other exhaust gases containing sulfur oxides or a method for the treatment of exhaust gases containing sulfur oxides, in particular exhaust gases from technical incinerators or exhaust gases from technical processes (such as steel production), for purposes of Removal and / or deposition of the sulfur oxides or for purposes of reducing the sulfur oxide content available to provide, which at least largely avoids or at least mitigates the disadvantages of the methods of the prior art previously described.
  • the invention has for its object to provide such an exhaust treatment process, which has a high degree of efficiency and / or high separation efficiency of sulfur oxides in a dry sorption, but prevents caking or caking of system components or at least significantly reduced.
  • the present invention proposes - according to a first aspect of the present invention - a process for the treatment of exhaust gases containing sulfur oxides (SO x ) from industrial processes for the purpose of removing and / or separating the sulfur oxides and / or for purposes of Reduction of the sulfur oxide content (exhaust gas treatment process) according to claim 1 before;
  • exhaust gas treatment process a process for the treatment of exhaust gases containing sulfur oxides (SO x ) from industrial processes for the purpose of removing and / or separating the sulfur oxides and / or for purposes of Reduction of the sulfur oxide content (exhaust gas treatment process) according to claim 1 before;
  • SO x sulfur oxides
  • the present invention - according to a second aspect of the present invention - a system for the treatment of sulfur oxides (SO x ) containing exhaust gases from technical processes according to the relevant independent plant claim; Further, in particular special and / or advantageous embodiments of the system according to the invention are the subject of the relevant sub-systems.
  • SO x sulfur oxides
  • the present invention relates to the use (s) of the system according to the invention and / or of the method according to the invention in accordance with the claim for use thereof.
  • the present invention - accordingly provides a process for the treatment of sulfur oxides (SO x) -containing flue gases from industrial processes for the purpose of removal and / or deposition of the sulfur oxides and / or for the purpose of reducing the Schwefeloxidgehalts,
  • exhaust gases containing the sulfur oxides are subjected to exhaust gas treatment, in particular desulfurization, by means of at least one particulate sulfur dioxide-reactive exhaust gas reaction reagent, in particular desulfurization reagent,
  • sulfur oxides are oxides of the chemical element sulfur to understand.
  • the sulfur oxides include any possible sulfur oxide compound, in particular sulfur dioxide (S0 2 ) and sulfur trioxide (SO 3 ).
  • the correlating acids of the sulfur oxides are also to be understood by the general term "sulfur oxides", so that the correlating acids which are formed in aqueous solutions are also regarded as sulfur oxides in the context of the present invention.
  • sulfur oxide reactive is to be understood as meaning that a reagent-in this case the exhaust gas treatment reagent-can react with sulfur oxides in a chemical and / or physical manner.
  • the reagent reacts in a chemical reaction with the sulfur oxides to react the sulfur oxides.
  • An implementation of the sulfur oxides can be carried out for example by means of reduction, hydrolysis and decomposition or the like.
  • a significantly increased separation efficiency, in particular sulfur oxides is ensured by the process according to the invention for the treatment of exhaust gas.
  • the effectiveness of the pollutant removal can be increased by producing a liquid phase (hydrate shell) on the surfaces of the particulate waste gas treatment reagents, the hydrate shell favoring the conversion of the sulfur oxide and the kinetics of the chemisorptive reaction of the aqueous region increased dramatically and significantly compared to dry particles.
  • the particulate, dry exhaust gas treatment reagent in process step (a) reacts in a significantly lower ratio compared to the reaction in process step (b) and / or has a significantly lower separation efficiency of the sulfur oxides.
  • nents for example, due to aggressive condensates avoided.
  • the exhaust gas treatment process according to the invention can purpose and purpose for the deposition and / or reduction of sulfur oxides from exhaust gases from technical processes apply, ensuring the efficiency of the exhaust gas treatment process while ensuring a long service life and / or service life of the exhaust treatment plant can be.
  • the maintenance and repair costs are significantly reduced due to the avoided caking or caking of the system components, in particular by at least 30% and the period of use of the system according to the invention can therefore significantly, preferably increased by at least 50%.
  • a conversion into existing plants can be carried out very easily, with no great technical effort, since ultimately the desulfurization to a very small area within the exhaust treatment room, in particular the exhaust gas and / or flue gas channel extends.
  • the operating costs, investment costs and repair and maintenance costs are reduced or saved in comparison to the dry sorption methods known from practice, whereby at least 20% of the amount of exhaust gas treatment reagent can be saved.
  • the aforementioned costs are reduced by more than 60%, preferably more than 80%, more preferably between 60% to 90%, wherein an increase in the efficiency by at least 5%, preferably from 10% to 50%, compared to which takes place from the dry sorption method known in the art.
  • a reduction in the consumption of the exhaust gas treatment reagent is not only relevant with regard to the operating costs, but also with regard to environmental aspects, there is a positive effect from the exhaust gas treatment process according to the invention.
  • the ecological compatibility is increased by the fact that during the exhaust gas treatment, the consumption of the required exhaust gas treatment reagent by increasing the water vapor content of the Exhaust gas can be significantly reduced - in such a way that also caking or caking of system components are avoided.
  • these caking or caking finally led to an increase in the water vapor content of the exhaust gases never being able to be integrated efficiently and permanently in an exhaust gas treatment process; and that although the theoretically positive effect of increasing the separation efficiency due to increased humidity and the associated reactions - theoretically - have been known in principle.
  • the exhaust treatment process is a dry sorption process.
  • the exhaust gas treatment reagent in its particulate form and / or in powder form is introduced into the flue gas or into the exhaust gases containing the sulfur oxides, in particular sprayed, blown in and / or injected.
  • various sulfur oxide-reactive exhaust gas treatment reagents are conceivable in the dry sorption process, with, for example, the calcium hydroxide or hydrated lime (Ca (OH) 2 ) competing with sodium bicarbonate (NaHCOs).
  • the dry sorption method it is further provided that, after introduction of the exhaust gas treatment reagent, deposition is provided on a fabric filter, also referred to as a bag filter. Due to a chemical reaction between the exhaust gas treatment reagent and the gaseous pollutants, in particular sulfur dioxide, the pollutants are bound to the exhaust gas treatment reagent. Accordingly, this form of sorption process is also referred to as chemisorption.
  • the dry sorption method according to the invention is characterized in that very dry exhaust gases are subjected to exhaust gas treatment at comparatively low exhaust gas temperatures by means of the exhaust gas treatment reagent.
  • the objective of a dry sorption method is to enable a reaction between the exhaust gas treatment reagent and the pollutants contained in the exhaust gases by introducing, preferably dry, particulate or pulverulent exhaust gas treatment reagent, and then to carry out a separation of the pollutants bound to the exhaust gas treatment reagent into a fabric filter ,
  • the pure dry sorption methods are rather associated with disadvantages, since in the practice known dry sorption method a very high Contain consumption of lime compounds, which is ultimately due to the fact that the lime particles or the exhaust gas treatment reagent does not fully react / Wegreagiert.
  • the subsequent introduction of water vapor into the exhaust gas stream and thus the guarantee of improved reaction kinetics significantly reduced the consumption of the exhaust gas treatment reagent, so that the ongoing operating costs can likewise be reduced.
  • the exhaust gas treatment reagent is used as a solid or solid mixture, in particular in the form of a, preferably finely divided, powder.
  • the particulate sulfur oxide reactive exhaust gas treatment reagent is useful as a solid or solid mixture especially for use in a dry sorption process.
  • the storage or the availability of the exhaust gas treatment reagent is procedurally and economically significantly improved compared to the prior art, since the solid or the solid mixture can be stored for a longer period without the sulfur oxide-reactive properties of the exhaust gas treatment reagent is lost or A precipitation of the exhaust gas treatment reagent in a solution can be avoided according to the invention by the particulate or particulate form of the exhaust gas treatment reagent formed as a solid or solid mixture.
  • the finely divided powder is particularly suitable for being introduced into the exhaust gas flow, so that the exhaust gas treatment reagent can absorb the entire exhaust gas stream, so that the exhaust gas treatment reagent is at least substantially evenly distributed in the exhaust gas flow or exhaust gases in process step (a) can be introduced.
  • the finely divided powder is suitable for injection or injection; and without a clogging of the injection and / or Einsprüh Surprise would be feared.
  • the exhaust gas treatment reagent is brought into fine distribution with the exhaust gases in contact and / or introduced into the exhaust gases.
  • the exhaust gas treatment reagent is injected into the exhaust gases in fine distribution and / or sprayed, preferably by means of at least one, preferably lance-shaped, first injection and / or Einsprüh sensible.
  • Particularly preferred is a plurality of preferably lancetike first Injection and / or Einsprüh prepareden provided.
  • the exhaust gas treatment reagent can be introduced into the exhaust gases by means of at least one, preferably lance-shaped, first injection and / or injection device, particularly preferably by means of a plurality of preferably lance-shaped first injection and / or injection devices.
  • the exhaust gas treatment reagent is injected into the exhaust gases and / or sprayed, preferably in fine distribution.
  • the contacting or the entry, in particular the injection and / or spraying, of the exhaust gas treatment reagent into the exhaust gases by two to eight preferably lanceous injection and / or Einsprüh realizeden, preferably from two to four first lances for introducing the exhaust gas treatment reagent.
  • the exhaust gas treatment reagent is introduced into the exhaust gas flow or into the exhaust gases at least substantially uniformly distributed.
  • the fine distribution of the exhaust gas treatment reagent in the exhaust gases can be achieved by the plurality of preferably lance-shaped injection and / or Einsprüh drivenen, as adapted to the exhaust treatment room, in particular the smoke and / or exhaust duct, the introduction of the exhaust gas treatment reagent can be performed.
  • the exhaust gas treatment reagent is introduced into the exhaust gases in a flow or in a conveying air flow, so that a conveying air flow can form the carrier for the exhaust gas treatment reagent. It can be provided that the conveying air flow can be introduced by means of the first lance in the flue gas duct.
  • the lance-shaped formation of the first injection and / or Einsprüh founded the exhaust treatment reagent in the central region of the exhaust stream - that is ultimately in the central region of the flue gas and / or exhaust gas passage through which the exhaust gases flow - are introduced and so can target - And purposely impacting or hitting the Abgas harmonysreagenzes on the walls of the exhaust gas treatment room, in particular the exhaust gas and / or flue gas duct, at least substantially avoided.
  • the exhaust gas treatment reagent can not be incorporated in the center of the exhaust stream, especially at the edge.
  • the exhaust gas treatment reagent is entrained with the exhaust gas stream after introduction into process step (a), wherein now the exhaust gas flow or the exhaust gases form the carrier for the sulfur-oxide-reactive exhaust gas treatment reagent.
  • the exhaust gas treatment reagent supply can also be carried out and / or carried out by means of pneumatic conveying. From the pneumatic Promotion can come from the conveying air flow used as a carrier for the exhaust gas treatment reagent.
  • the exhaust gas treatment reagent is at least one reagent reactive from the group of alkali metal and / or alkaline earth metal hydroxides, oxides, carbonates and bicarbonates and mixtures thereof and combinations thereof, in particular from the group of calcium hydroxide, sodium bicarbonate and sodium bicarbonate Sodium carbonate (soda) and their mixtures and combinations.
  • the exhaust treatment reagent contains and / or consists of calcium hydroxide, more preferably in the form of hydrated lime. More preferably, the exhaust gas treatment reagent contains or consists of (hydrated) hydrated lime, sodium bicarbonate, sodium carbonate or mixtures thereof or combinations thereof.
  • the exhaust gas treatment reagent is particularly preferably hydrated lime and / or a reagent having a hydrated lime.
  • a lime hydrate-containing reagent with at least 50% by weight of hydrated lime preferably with at least 75% by weight of hydrated lime, more preferably with at least 90% by weight of hydrated lime, based on the reagent containing kalkhydrate.
  • both lime hydrate-containing reagents and also lime-containing residual products can be used as the sulfur-oxide-reactive waste gas treatment reagent, preferably wherein the lime-containing residual products have more than 50% by weight of alkaline earth hydrate.
  • the exhaust gas treatment reagent may also have at least one adsorptive reagent, in particular a reagent having activated carbon.
  • the adsorptive reagent can allow adsorption of, in particular toxic, pollutants, in particular dioxins.
  • the exhaust gas treatment reagent comprises a mixture and / or combination of the adsorptive reagent and the sulfur oxide-reactive reagent, in particular of the reagent containing a hydrated lime, in particular from 5 to 40% by weight, preferably from 10 to 30% by weight, more preferably from 15 to 25% by weight of the exhaust treatment reagent is the adsorptive reagent.
  • the adsorptive reagent may also have absorptive properties for the reduction and / or separation of pollutants, in particular dioxins.
  • the adsorptive reagent may preferably be activated carbon; Further possible adsorptive reagents are selected from the group of zeolites, aluminum oxides, silicon oxides, silicic acids and silica gels, clathrates, molecular sieves and mixtures and combinations thereof.
  • the disadvantage of the sodium bicarbonate compared to the hydrated lime is the comparatively high material costs.
  • sodium bicarbonate also requires a higher reaction temperature than hydrated lime.
  • bicarbonate is regarded as a lime hydrate as an energy and resource-saving additive
  • the short-term increase in the humidity or the water vapor content of the exhaust gas in process step (b) take place, whereby a reaction between the exhaust gas treatment reagent and the sulfur oxides contained in the exhaust gases can be ensured.
  • bicarbonate or sodium bicarbonate may also be used in further embodiments, preferably if it would be activated in advance, in particular at temperatures in the range from 200 to 1 000 ° C., preferably in the range from 250 to 450 ° C.
  • the sodium bicarbonate can also be moistened and / or moistened, so that it can be used in particular at exhaust gas temperatures of 40 to 60 ° C. and in method step (b) contributes to the reduction or separation of the sulfur oxides in the exhaust gases.
  • sodium carbonate is also conceivable as an exhaust gas treatment reagent, although the comparatively high costs for the sodium carbonate would have to be weighed in relation to the separation efficiency, wherein the exhaust gas treatment reagent can be selected depending on the exhaust gas composition.
  • a reaction with the sulfur oxides contained in the exhaust gases takes place only in process step (b) by increasing the humidity of the exhaust gas and the formation of a hydrate shell around the particulate or particulate Abgas harmonysreagenz, which is present in fine distribution in the exhaust gas.
  • the basic reactions between the hydrated lime and the sulfur oxides can be indicated by the following reaction formulas:
  • step (a) is so slow that activation is required.
  • sulfur trioxide has a much higher reactivity than sulfur dioxide and also as carbon dioxide.
  • the hydrogen fluoride By adding water vapor into the exhaust stream, the hydrogen fluoride can react with calcium hydroxide to form calcium chloride.
  • the deposition of sulfur dioxide in the coexistence of hydrogen chloride and sulfur dioxide in the exhaust gas stream may improve as compared to the separate separation in the sole presence of sulfur oxide.
  • the intermediate calcium hydroxychloride - from the reaction of hydrated lime with hydrogen chloride - also reacts with sulfur dioxide.
  • Calcium hydroxychloride may also arise as a residual product in the tissue filter as a result of a reaction between excess hydrated lime with calcium chloride. It is believed that the calcium hydroxychloride with the Sulfur oxides can react, as the following reaction equations illustrate:
  • a “hydration shell” is to be understood as an addition of water molecules around an ion.
  • the effective forces here are the ion-dipole interactions.
  • the hydrate shell can ensure the mass transfer of the gas / particle surface and the pore diffusion by certain solubility effects, which enable rapid ionic reactions in the molecular range. Therefore, the presence of HCl or CaCl 2 is an important parameter for a high S0 2 separation efficiency since the formation of the hydrate shell can exploit the hygroscopic properties of the calcium chloride.
  • the particles of the exhaust gas treatment reagent in particular the hydrated lime particles, particularly preferably serve and / or function as condensation nuclei and / or condensation nuclei.
  • the condensation nuclei and / or nuclei can facilitate the nucleation and the subsequent condensation of the water vapor.
  • the exhaust gas treatment reagent has particle sizes, in particular particle diameters, below 500 ⁇ m, in particular below 250 ⁇ m, preferably below 100 ⁇ m, particularly preferably below 50 ⁇ m, very particularly preferably in the range of 1 to 50 pm.
  • the aforementioned particle sizes, in particular particle diameters can be determined by means of a sieve analysis.
  • the methods for determining particle sizes, in particular particle diameters are standardized by means of sieve analysis, for example in DIN 66165 (DIN 66165-1: "Particle size analysis sieve analysis - Part 1: Basics” and DIN 66165-2: “Particle size analysis sieve analysis - Part 2: Execution”).
  • the exhaust gas treatment reagent preferably has average particle sizes D50, in particular particle diameter D50, in the range from 1 to 50 gm.
  • the mean particle size D50 is in the range from 1 to 30 gm, preferably in the range from 2 to 20 gm, preferably in the range from 2 to 15 gm.
  • the mean grain size, in particular the particle diameter D50 can be determined by sieve analysis, preferably by means of a sieve analysis Sieve analysis according to DIN 66165, to be determined.
  • the aforementioned particle sizes and / or average particle sizes D50 can ensure finely divided injection and a good reaction between the exhaust gas treatment reagent and the sulfur oxides contained in the exhaust gases. Due to the particulate or particulate exhaust gas treatment reagent, which preferably has a fine distribution, and which has the abovementioned particle sizes and / or mean particle sizes D50, good overall humidification of all particles of the exhaust gas treatment reagent is possible. Furthermore, a rapid reaction between the sulfur oxides and the humidified or surrounded by a hydrate shell exhaust treatment reagent in step (b) can be ensured.
  • the above-mentioned grain sizes and / or average particle sizes D50 have optimal properties in terms of humidification and / or wetting, preferably all particles of the exhaust gas treatment reagent, and also cause a high deposition rate of sulfur oxides. Furthermore, they can be introduced by the first injection and / or Einsprüh founded in fine distribution in the exhaust gas flow, that the exhaust gas treatment reagent at least substantially uniformly distributed in the exhaust gas stream in step (a) results. Also, an advantageous ratio between the reaction of the sulfur oxides, which ultimately causes a deposition of the sulfur oxides on the particles of the exhaust gas treatment reagent, and the total amount of exhaust gas treatment reagent used can be ensured while the economic process management is still present.
  • the exhaust gas treatment reagent has a BET surface area in the range from 5 to 100 m 2 / g, preferably in the range from 10 to 75 m 2 / g, preferably in the range from 15 to 50 m 2 / g.
  • the aforementioned BET surfaces relate in particular to the sulfur-oxide-reactive surface of the exhaust gas treatment reagent.
  • the BET surface area relative to the sulfur oxide reactive and / or acid adsorption active hydrated lime surface in the case of use of hydrated lime and / or a calchydrate-containing reagent specified as exhaust gas treatment reagent.
  • lime hydrate and / or a product containing a kalkhydrate is used as the exhaust gas treatment reagent, after which the BET surface area ultimately relates to the hydrated lime or the reagent of the exhaust gas treatment reagent containing kalkhydrate.
  • the abovementioned BET surfaces enable a high separation efficiency in process step (b) of the sulfur oxides.
  • the BET surface area can be determined by means of a BET measurement in an analytical method for determining the size of surfaces, in particular porous solids, by means of gas adsorption. With this surface chemistry analysis method, a mass-related specific surface can be calculated from experimental data.
  • the measurement of the BET surface area (measuring devices required for this purpose) are described in detail in DIN-ISO 9277 and DIN 66131 (withdrawn).
  • the BET surface area indicates, in particular, the surface of the exhaust gas treatment reagent available for the reaction with respect to the quantity or mass of exhaust gas treatment reagent required for this purpose. Accordingly, the preferred range shows that, in relation to the mass, a surface which is large for a preferably hydrated product may be provided to form the hydrate shell.
  • the exhaust gas treatment reagent has a total pore volume in the range of 0.01 to 0.95 m 3 / g, preferably in the range of 0.02 to 0.75 m 3 / g, preferably in the range of 0.05 to 0.5 m 3 / g, on.
  • the abovementioned total pore volumes result in a good separation efficiency of the exhaust gas treatment reagent in process step (b) after contact with the steam or the already condensed water vapor for the separation or reduction of the sulfur oxides contained in the exhaust gases.
  • the aforementioned total pore volumes are particularly suitable for introduction into the exhaust gas stream in process step (a) in fine distribution and also for uniform distribution within the exhaust gas stream. In tests carried out it was found that with a total pore volume in the range of 0.05 to 0.5 m 3 / g, the best results could be achieved in terms of process economy and efficiency.
  • the exhaust gas treatment reagent in a stoichiometric excess, based on the sulfur oxides is used.
  • An excess of the exhaust gas treatment reagent ensures that the, in particular legal, prescribed degree of separation of sulfur oxides can be ensured.
  • the excess of the exhaust gas treatment reagent is due to the fact that in carried out experiments that not the entire exhaust treatment reagent, as mentioned above, with the sulfur oxides contained in the exhaust gases, but only a certain proportion of the exhaust gas treatment reagent.
  • the exhaust gas treatment reagent is calculated in a stoichiometric excess of at least 1.05, preferably at least 1.1, preferably at least 2, more preferably at least 3, even more preferably at least 5, calculated as the stoichiometric ratio of exhaust gas treatment reagent used to reduced and / or precipitated sulfur oxides. the exhaust gases provided.
  • the stoichiometric ratio of exhaust gas treatment reagent to sulfur oxides is preferably in the range from 1:05 to 1 to 50: 1, in particular in the range from 1.1: 1 to 25: 1, preferably in the range from 5: 1 to 20: 1, particularly preferably in the range from 8: 1 to 12: 1, calculated as the stoichiometric ratio of exhaust gas treatment reagent used to reduced and / or precipitated sulfur oxides.
  • the abovementioned relationships between the exhaust gas treatment reagent and the sulfur oxides contained in the exhaust gases ensure that the required proportion of sulfur oxides can be removed or removed from the exhaust gases.
  • the stoichiometric ratio is due to the fact that only a certain proportion of the exhaust gas treatment reagent reacts with the sulfur oxides in process step (b), so that an excess of exhaust gas treatment reagent is necessary in particular if a high proportion of sulfur oxides is separated from the exhaust gases or to be separated.
  • the amount of water vapor in process step (b) is increased into the exhaust gases having the exhaust gas treatment reagent-that is, ultimately in the exhaust gas flow.
  • An increase in the amount of steam and / or the relative humidity of the exhaust gases in process step (b) is ensured by the supply of water vapor and concomitantly the condensation on the exhaust gas treatment reagent.
  • the water vapor content of the exhaust gases increases in the region of the supply of water vapor in the exhaust gases. However, this increase is in particular only for a very short period of time and also only in the range of Introduction, in particular injection and / or spraying, of the steam provided in the exhaust gases.
  • a condensation on the exhaust gas treatment reagent occurs in that an increase in the water vapor content of the exhaust gases in step (b) is caused by supplying the water vapor, wherein due to the temperature difference between the, in particular colder, exhaust gases and, in particular hotter, steam condensation of the water vapor conditional.
  • the condensation is reflected here on the particles contained in the exhaust gases and thus also on the particulate or particulate exhaust gas treatment reagent, which has been previously introduced into process step (a) in the exhaust gas stream.
  • a condensation on the exhaust gas treatment reagent according to the invention is particularly advantageous with regard to the separation efficiency of the exhaust gas treatment reagent, since - as already explained - hydrate sheath forms around the exhaust gas treatment reagent due to the condensation of water vapor on the exhaust gas treatment reagent.
  • the hydrate shell formed around the exhaust gas treatment reagent allows a reaction between the sulfur oxides and the exhaust gas treatment reagent, so that a condensation of water vapor in process step (b) by increasing the water vapor content of the exhaust gases can ultimately lead to a higher separation efficiency of the process.
  • the amount of water vapor in process step (b) may preferably be increased into the exhaust gases having exhaust gas treatment - that is, in the exhaust gas stream in process step (b), such that the water vapor content in the exhaust gases (exhaust gas flow) containing exhaust gas treatment reagent is at least 0.1 vol .-%, in particular by at least 0.2 vol .-%, preferably by at least 0.5 vol .-%, preferably by at least 0.8 vol .-%, most preferably by at least 1 vol .-%, is increased ,
  • the aforementioned increases or the possible ranges of the increase in the water vapor content in the exhaust gases in process step (b) relate in particular to the location of the contact between the steam and the exhaust gases.
  • the location of the contacting is particularly in the area of introduction, preferably injection and / or spraying, of the water vapor in process step (b).
  • the increase in the water vapor content of the exhaust gases can also be provided only for a very short time frame or period and ultimately lead in particular purposeful and purposive for higher separation efficiency of sulfur oxides due to condensation on the exhaust gas treatment reagent.
  • An increase in the moisture or the water vapor content in the exhaust gases can also be indicated by an increase in the relative humidity of the exhaust gas. Increasing the amount of water vapor in the given ranges is ultimately an increase in relative humidity. At 100% by volume of water vapor in the exhaust gases, saturation is reached and no additional water vapor can be taken up in the carrier stream.
  • the abovementioned water vapor contents relate in particular to a measurement at the temperature of the exhaust gases present in process step (b).
  • the relative humidity is the quotient of the absolute humidity and the maximum possible humidity at saturation temperature (saturation vapor density) or the ratio of the partial pressure of the water vapor and the temperature-dependent saturation vapor pressure.
  • the relative humidity can be determined, for example, with an absorption hygrometer, an aspiration psychrometer, a dew point hygrometer and / or a hair hygrometer. In general, devices for measuring the humidity are called hygrometers.
  • the amount of water vapor in process step (b) is increased in the exhaust gas treating the exhaust gas - that is ultimately in the exhaust gas stream - such that the water vapor content of the resulting, with steam contacted, the exhaust gas treatment reagent having exhaust gases (exhaust stream) at least 2% by volume, in particular at least 3% by volume, preferably at least 4% by volume, preferably at least 5% by volume.
  • the aforementioned values include the inventive increase in the water vapor content of the exhaust gases having the exhaust gas treatment reagent in process step (b).
  • the aforementioned relative humidity or the water vapor content of the exhaust gases refers only to the location of the contact with the water vapor, that is, ultimately to a locally limited area; and in particular limited in time to the time of contacting.
  • exhaust gases with the aforementioned relative humidities or the aforementioned water vapor content can be classified as dry exhaust gases.
  • comparatively very dry exhaust gases are treated with water vapor.
  • a very dry exhaust gas is still present, but it can be ensured that it comes to the condensation on the exhaust gas treatment reagent, so that a reaction of the exhaust gas treatment reagent can be ensured with the sulfur oxides contained in the exhaust gases.
  • the amount of steam in the exhaust gas treatment reagent having exhaust gas (exhaust stream) is increased in step (b) such that the water vapor content of the resulting, contacted with water vapor, the exhaust gas treatment reagent having exhaust gases (exhaust gas flow) Range of 2 to 25 vol .-%, in particular in the range of 3 to 20 vol .-%, preferably in the range of 3.5 to 10 vol .-%, particularly preferably in the range of 4 to 8% by volume ,
  • the abovementioned value ranges of the relative humidity and / or the water vapor content in the exhaust gases having the exhaust gas treatment reagent characterize in particular a dry exhaust gas, which is treated with water vapor.
  • a drastic increase in the relative humidity and / or the water vapor content in process step (b) does not necessarily have to take place, but it should preferably be ensured that a condensation of the invention takes place on the exhaust gas treatment reagent and / or that a hydrate shell surrounds the particles of the exhaust gas treatment reactor - Genzes can form, so that a reaction between the exhaust gas treatment reagent and the sulfur oxides can be ensured.
  • water vapor in an amount in the range of 5 to 250 kg / h, in particular an amount in the range from 6 to 125 kg / h, preferably in an amount of from 10 to 75 kg / h, preferably in an amount in the range of from 18 to 50 kg / h.
  • a relative indication of the supply of water vapor, preferably saturated steam, in relation to the amount of exhaust gas results from the fact that a different total amount of exhaust gases is obtained, depending on the technical process to be carried out, which ultimately produces the exhaust gases and / or the combustion process.
  • the amount of steam that is supplied to the exhaust gases is ultimately designed so that an increase of the water vapor content and / or the relative humidity according to the invention can be ensured, so that a hydrate shell can form around the exhaust gas treatment reagent.
  • the exhaust gas quantity of 10,000 standard cubic meters / h (Nm 3 / h) is related back to the standard volume and a volume unit used in process engineering. After measuring the amount of gas, a conversion to the respective same standard state, so a comparison of amounts of exhaust gas having different pressures and / or temperatures can be made possible.
  • the standard physical state is, in particular according to DIN 1343, a standard pressure of 101 .325 Pa at a standard temperature of 273.15 K.
  • the aforementioned standard volume in standard cubic meters can refer to the physical standard state according to DIN 1343.
  • the water vapor in process step (b) at a temperature in the range of 1 10 ° C to 185 ° C, in particular in the range of 120 ° C to 170 ° C, preferably in the range of 125 ° C to 160 ° C, fed.
  • the steam in process step (b) can be supplied at a temperature of at least 120 ° C., preferably of at least 130 ° C., preferably of at least 135 ° C., particularly preferably of at least 140 ° C.
  • the aforementioned temperatures may be determined due to the saturated steam properties of the water vapor.
  • the steam in process step (b) can be supplied at a pressure in the range of more than 1 bar to 10 bar, in particular in a range of 2 bar to 8 bar, preferably in the range of 3 bar to 6 bar.
  • the steam can alternatively or additionally in process step (b) with a pressure of more than 1 bar, preferably of at least 2 bar, preferably of at least 3 bar, more preferably at least 4 bar, are supplied.
  • the pressure of the steam can be selected as a function of the pressure in the exhaust-gas treatment space, in particular in the area where the water vapor is brought into contact with the exhaust gases. Accordingly, compared to the atmospheric pressure, the steam is preferably introduced with overpressure.
  • a purposeful and purposeful addition of exhaust gas treatment reagent and / or water vapor is particularly advantageous in that, depending on the prevailing conditions, a targeted addition is made possible.
  • the supply of exhaust gas treatment reagent can be increased, so that the required separation efficiency of the sulfur oxides can be ensured.
  • the supply of exhaust treatment reagent can be reduced, for example, if a low sulfur oxide content is present in the exhaust gases. Accordingly, the amount of the provided exhaust treatment reagent can be selectively employed, so that an unnecessary excess of the exhaust treatment reagent is avoided.
  • the abovementioned parameters either have an influence on the separation efficiency of sulfur oxides and / or on the supply of steam and / or exhaust gas treatment reagent.
  • it is advantageous in the supply of saturated steam to have knowledge of the prevailing pressure in the exhaust gas treatment room, in particular in process step (b), so that depending on that pressure, the saturated steam temperature and the pressure of the steam can be adjusted and / or regulated.
  • the deposition rate can be improved, while at the same time the running operating costs, in particular by a targeted supply of exhaust gas treatment reagent, can be reduced.
  • the water vapor in fine distribution in process step (b) is brought into contact with the exhaust gases and / or introduced into the exhaust gases, in particular injected into the exhaust gases and / or sprayed.
  • This can take place by means of at least one, preferably lance-shaped, second injection and / or injection device, particularly preferably by means of a plurality of preferably lance-shaped second injection and / or injection devices.
  • the water vapor can be separated by means of 2 to 10, preferably 2 to 4, preferably lance-shaped injection and / or Einsprüh sensibleen be introduced into the exhaust gases.
  • the steam is introduced into the exhaust gases, in particular into the exhaust gases, by means of at least one preferably lance-shaped second injection and / or injection device, preferably by means of a plurality of, preferably lance-shaped, second injection and / or injection devices / or sprayed, preferably in fine distribution.
  • the second injection and / or Einsprüh shark is formed such that condensation on the exhaust gas treatment reagent can be ensured, so that the necessary for the reaction between the exhaust gas treatment reagent and the sulfur oxides hydrate sheath on the surface of the exhaust gas treatment reagent can form.
  • the steam is introduced as possible over the entire cross section of the exhaust gas treatment room, in particular the flue gas and / or exhaust duct, in the exhaust gas stream.
  • the fine distribution of the water vapor is characterized in particular by the fact that the largest possible cross section of the exhaust gas stream can be mixed with water vapor or that the water vapor at least 50%, preferably from 50% to 95%, more preferably from 60% to 70%, the particle of the exhaust treatment reagent can condense.
  • the preferably lance-shaped second injection and / or spraying device can have a plurality of openings for the water vapor to the outlet and / or outlet, so that every second injection and / or spraying device can provide the exhaust individual partial flows of water vapor.
  • the speed is designed or selected such that a condensation of the water vapor is not only caused in the region of the outlet openings of the preferably lance-shaped second injection and / or spraying device, but that the water vapor can be introduced over a large area of the cross section of the exhaust gas flow as far as possible so that condensation of water vapor on the exhaust treatment reagent can be at least substantially ensured.
  • the steam can be introduced at a much higher speed in the exhaust gas flow, so that ultimately an entry of the water vapor can be ensured in the exhaust gas flow due to the increased speed. If the steam would escape at too low a speed from the preferably lance-shaped second injection and / or spraying device, the high separation efficiency according to the invention could not be guaranteed due to the reaction of the sulfur-oxide-reactive exhaust gas treatment reagent with the sulfur oxides.
  • the steam is at a rate of at least twice, preferably at least three times, more preferably from 4 times to 10 times, in particular at least 6 times to 7 times as fast as the speed of Exhaust gases and / or the exhaust gas stream supplied to the exhaust gases or the exhaust gas stream.
  • a higher velocity of the water vapor compared to the velocity of the exhaust stream can ensure that the water vapor, preferably in fine distribution, at least substantially evenly over the cross section of the exhaust stream, in particular in the flue gas and / or exhaust duct, can be introduced.
  • the water vapor is not introduced into the exhaust gases in the flow direction, so that an entry into the, preferably microturbulent, flow of the exhaust gas flow can be ensured at an increased velocity of the water vapor.
  • the water vapor is at an angle of at least 20 °, in particular at an angle of at least 30 °, preferably at an angle in the range of 20 ° to 160 ° , Particularly preferably at an angle in the range of 40 ° to 150 °, based on the direction of the exhaust stream, supplied, in particular injected and / or sprayed, is.
  • the aforementioned angles make it clear that the steam is preferably introduced into the exhaust gases or fed to the exhaust gases at least substantially transversely to the flow direction of the exhaust gas flow.
  • the exhaust gases and / or the exhaust gas flow are at least substantially without backflow and / or at least substantially without backmixing in the region of the, preferably lancet, second injection and / or Einsprüh observed for the water vapor along /becomes.
  • the outlet region of the second injection and / or injection device for the steam is at least substantially without a backflow of the exhaust gases and / or the exhaust gas flow and / or at least substantially without backmixing.
  • the exhaust gas treatment process according to the invention can be configured in such a way that in process step (b) the steam is supplied in an area of the exhaust gases which is at least substantially free of exhaust gas treatment reagent.
  • the, preferably lanceous, second injection and / or Einsprüh adopted for the steam of waste gas treatment reagent is kept free and / or sealed off, in particular by means of at least one Verdränger stressess, in particular in the form of a diaphragm, in particular pinhole, or a sheet, in particular baffle or baffle.
  • the outlet region for the water vapor of the second injection and / or injection device of exhaust gas treatment reagent is kept free.
  • the clearing ultimately leads to caking or caking on the second injection and / or spraying device and / or other system components can be at least substantially avoided.
  • exhaust gas treatment reagent already brought into contact with water vapor can lead to caking or caking of plant components and thus cause considerable damage to the entire exhaust gas treatment plant.
  • the exhaust gases and / or the exhaust gas flow between process step (a) and process step (b), in particular between the supply of the exhaust gas treatment reagent and the water vapor can be diverted and / or swirled.
  • the turbulence and / or deflection can be provided for better mixing of the exhaust gas stream with the exhaust gas treatment reagent, so that the exhaust gas treatment reagent can be provided evenly in fine distribution in the exhaust stream.
  • at least one displacement body for deflecting and / or swirling the Exhaust gases and / or the exhaust stream used.
  • the displacement body in the form of a diaphragm, in particular pinhole, or a sheet, in particular guide or deflection plate, on.
  • the displacement body preferably serves for the mixing of the exhaust gases (the exhaust gas stream) containing the exhaust gas treatment reagent and the exhaust gas treatment reagent.
  • the displacement body is provided for generating an exhaust gas treatment reagent at least substantially free area of the exhaust gases for supplying the water vapor.
  • the displacement body can preferably be arranged such that the outlet of the water vapor is carried out in an at least substantially particle-free and / or dust-free region so that caking or caking in the region of the outlet of the water vapor in process step (b) can be avoided.
  • the amount of steam and / or the relative humidity in the exhaust gases-that is, in the exhaust gas stream- is subsequently lowered to process step (b) and / or after the supply of steam.
  • a short-term increase of the water vapor in process step (b) may preferably be provided, which may ultimately result in the water vapor condensing on the exhaust gas treatment reagent, the condensation of which causes the water vapor content of the exhaust gas to drop again.
  • the proportion of water vapor in the exhaust gases decreases such that the water vapor content of the exhaust gases (exhaust gas stream) at least 1 vol .-%, in particular at least 2 vol .-%, preferably at least 3 vol .-%, more preferably at least 4 vol. %, is.
  • the amount of water vapor in the exhaust gases (exhaust stream) is lowered, in particular such that the water vapor content of the exhaust gases (exhaust gas flow) Range of 1 to 24 vol .-%, in particular in the range of 2 to 19 vol .-%, preferably in the range of 2.5 to 9 vol .-%, particularly preferably in the range of 3 to 7 vol .-%, is located , It is very particularly preferred that the water vapor content of the exhaust gases is lowered in such a way that it at least substantially corresponds to the water vapor content of the exhaust gases in process step (a).
  • a low moisture content of the exhaust gases after process step (b) is advantageous for the subsequent treatment of the exhaust gases, in particular the filtering or mechanical separation of the pollutants.
  • the abovementioned proportions of the water vapor in the exhaust gas stream ultimately characterize a very dry exhaust gas, so that the supply of water vapor to a desired condensation on the particles of the exhaust gas treatment reagent is particularly advantageous since otherwise condensation due to the water vapor already present in the exhaust gas would be relatively unlikely is and / or only less than 5% of the particles of the exhaust gas treatment reagent.
  • the water vapor content of the exhaust gases to be treated at least 1 vol .-%, in particular at least 2 vol .-%, preferably at least 3 vol .-%, particularly preferably at least 4 vol .-%.
  • the water vapor content of the exhaust gases to be treated is preferably in the range of 1 to 24% by volume, especially in the range of 2 to 19% by volume, preferably in the range of 2.5 to 9% by volume, more preferably in the range Range from 3 to 7% by volume.
  • waste gases to be treated means the original waste gases that originate from the technical process step and / or from the combustion.
  • the exhaust gases to be treated are accordingly supplied to process step (a) and therefore the exhaust gases before process step (a) to the aforementioned water vapor content.
  • the abovementioned ranges and minimum details of the water vapor content show that, preferably after process step (b) and / or after the supply of steam, the water vapor content of the exhaust gases can ultimately drop to the level which it already had before carrying out the exhaust gas treatment, in particular before carrying out process step (a).
  • the exhaust gases to be treated are from smelters, in particular copper smelters and / or iron smelters, cement works,
  • the exhaust gases to be treated can be from the pig iron and / or steel production by sintering iron ores and subsequent pig iron production in the blast furnace process.
  • the waste gases to be treated can be obtained from smelters, in particular copper smelters and / or iron smelters, cement plants,
  • the abovementioned exhaust gases can have a large proportion of sulfur oxides or pollutants to be separated in the exhaust gases, so that they are particularly suitable for the exhaust gas treatment process according to the invention.
  • the abovementioned exhaust gases preferably have a very low proportion of water vapor, in particular in the range from 1 to 10% by volume, so that without the supply of water vapor according to the invention in one of the feeds of the exhaust gas treatment reagent downstream process step no condensation on the particles of the exhaust gas treatment reagent Formation of a hydrate shell would occur.
  • the temperature of the exhaust gases (exhaust stream) at least 15 ° C, in particular at least 20 ° C, preferably at least 30 ° C. , particularly preferably at least 40 ° C, is.
  • the exhaust gases have a comparatively low temperature in comparison to exhaust gases which originate from a technical process step.
  • the original or exhaust gases to be treated may have a temperature in the range of 40 to 60 ° C at a, preferably very low, water vapor content of less than 15 vol .-%.
  • the inventive method is particularly advantageous because without a heating of the exhaust gases and without a long-term increase of the water vapor content - the water vapor is only briefly formed in process step (b) a Hydrathülle on the particles of the exhaust gas treatment reagent increased - a high separation efficiency of sulfur oxides can be ensured.
  • the exhaust stream in step (b) has a velocity of at least 1 m / s, preferably in the range of 2 m / s to 100 m / s, preferably in the range of 2 m / s to 20 m / s, more preferably in the range from 10 m / s to 20 m / s, up.
  • the aforementioned speed depends in particular on the respective process control and likewise also on the origin of the exhaust gases, for example the combustion process and / or the technical process step.
  • the aforementioned velocities make it clear that the introduction of the vapor according to the invention preferably takes place at a much higher speed than the velocity of the exhaust gas stream.
  • the speed is also designed in particular such that in method step (a) introduction of the exhaust gas treatment reagent can be ensured, in which the exhaust gas treatment reagent is present at least substantially uniformly distributed within the exhaust gas flow.
  • the steam can also be introduced into the exhaust gas stream in process step (b) or supplied thereto, so that a condensation on the particles of the exhaust gas treatment reagent is produced.
  • the exhaust gases having the exhaust gas treatment reagent are passed through at least one swirling section, in particular a Venturi section, before the steam is supplied in process step (b) and / or after the exhaust gas treatment reagent has been brought into contact with the exhaust gases in process step (a).
  • the Venturi path and / or the Verwirbelungsrange between the method step (a) and the method step (b) is arranged.
  • the Verwirbelungsrange is preferably designed such that a thorough mixing of the exhaust gas stream is carried out with the exhaust gas treatment reagent, in particular so that the exhaust gas treatment reagent is at least substantially uniformly distributed in the exhaust gas stream.
  • the swirling section can be designed such that the outlet and / or outlet opening and / or the outlet and / or outlet openings for the water vapor of the second injection and / or spraying device are at least substantially free of dust-like particles and / or free from the exhaust treatment reagent is / are kept.
  • a narrowing and / or narrowing of the flue gas and / or exhaust gas channel cross section of the exhaust gas treatment space can be used as Venturi path.
  • the pollutant emissions can likewise be greatly reduced, since the exhaust gas treatment reagent is finely and uniformly distributed in the exhaust gas stream and can accordingly also react in process step (b) with the sulfur oxides contained in the exhaust gases in process step (b).
  • the exhaust gas treatment in process step (a) and process step (b) is carried out in the presence of oxygen.
  • the oxygen does not have to be removed in advance from the exhaust gases in advance, which would ultimately increase both the energy costs and the operating costs.
  • an air flow (containing oxygen) can be used as a flow for the exhaust gas treatment reagent.
  • the exhaust gases are subjected to filtration after feeding the water vapor in process step (b) and / or after process step (b).
  • the filtering is used in particular for the separation of the reaction products of the reacted exhaust gas treatment reagent and / or unreacted exhaust gas treatment reagent and further, contained in the exhaust gases, pollutants and / or dust-like or particulate components.
  • the exhaust gases of a filter device preferably a fabric filter, are supplied.
  • the solids and / or pollutants contained in the exhaust gas in particular solid and / or dust-like particles, preferably unreacted exhaust gas treatment reagent and / or reaction products of the reacted exhaust gas treatment reagent, can be separated and / or separated from the exhaust gases.
  • calcium hydroxychloride may arise as a residual product from the tissue filter as a result of a reaction between excess hydrated lime with calcium chloride.
  • the fabric filter and / or the filter device is cleaned in particular at cyclic intervals, so that the deposited on the fabric filter components of the exhaust gases as so-called "filter cake" separated from the filter device become.
  • the fundamental task of the filter device and / or the fabric filter can ultimately be to separate the dust particles from the exhaust gases, for example the flue gases.
  • the separated components of the exhaust gases can be deposited on the filter material and thus produce the filter cake, which then ultimately can act as a separator.
  • a regular regeneration is required in particular to ensure the required pressure conditions, for example, by an introduced against the flow direction of compressed air pulse, which leads to the discharge of the filter cake.
  • the flow of the filter can be selected and / or adjusted so that optimum sorption conditions are present. Likewise, this also applies to the cleaning cycle of the fabric filter, within which the filter cake is deposited.
  • the unreacted exhaust gas treatment reagent and / or the reacted exhaust gas treatment reagent is / are recycled, preferably after filtering in the filter device and / or the fabric filter.
  • a recycle allows reuse of the exhaust gas treatment reagent, preferably the unreacted exhaust treatment reagent, thus reducing the amount of exhaust treatment reagent required by the process of the present invention which subsequently can not be further used in the process of the present invention, followed by operating costs can be reduced significantly.
  • the exhaust gas treatment process according to the invention for the treatment of exhaust gases from smelters, especially copper smelters and / or ironworks, cement works, steel mills or power plants, preferably hard coal power plants, and / or for the treatment of pig iron and / or steel production by sintering iron ores and subsequent pig iron production in Blast furnace process originating exhaust gases are used.
  • the exhaust gas treatment process can be integrated very easily into already existing smelters and / or power plants in the already existing exhaust gas treatment plant, usually the exhaust gas treatment plant already includes a fabric filter as well as a spraying and / or injection device for an additive of the dry sorption process.
  • the introduction according to the invention and / or the supply of the substance according to the invention provided downstream of the supply of the exhaust gas treatment reagent Water vapor can thus lead to a significant improvement in the separation efficiency with respect to the sulfur oxides without complex conversion measures for carrying out the method according to the invention would be present.
  • the already existing flue gas and / or exhaust gas duct of the exhaust gas treatment space can be used for the arrangement of the first and / or second injection and / or spraying device.
  • the water vapor now introduced into process step (b) in the exhaust gas can be made to have a hydrate shell around the exhaust gas treatment reagent particles which are preferably formed as solids, whereby the reaction kinetics is greatly favored over pure dry sorption.
  • Another object of the present invention - according to a second aspect of the present invention - is a plant for the treatment of sulfur oxides (SO x ) containing exhaust gases (exhaust treatment plant) from technical processes for the purpose of removal and / or deposition of sulfur oxides and / or for purposes of reduction Sulfur oxide content, in particular a plant for carrying out a process for the treatment of sulfur oxides (SO x ) containing exhaust gases from industrial processes for the purpose of removal and / or deposition of sulfur oxides and / or for the purpose of reducing the sulfur oxide content, preferably for carrying out a method according to one the previously described embodiments and / or according to the first aspect of the present invention,
  • the plant having a device for carrying out a process containing sulfur oxide containing exhaust gases, wherein the device is associated with an exhaust gas treatment device for the exhaust gas treatment of the sulfur oxide-containing exhaust gases generated in the device and / or wherein the device is followed by an exhaust gas treatment device for the exhaust gas treatment of the sulfur oxide-containing exhaust gases generated in the device and / or is provided in the process direction downstream of the device,
  • the exhaust gas treatment device has a, preferably channel-shaped, exhaust gas treatment space
  • the exhaust treatment space has at least one first section and, downstream of the first section and / or in the process direction downstream of the first section, a second section and / or subdivided, wherein the exhaust gas treatment device comprises:
  • the introduction and / or supply of the water vapor via the second injection and / or injection device which is provided in the process direction downstream and / or subsequently to the introduction and / or supply of the exhaust gas treatment reagent via the first injection and / or injection device, makes the formation possible a hydrate shell around the particles of the exhaust treatment reagent.
  • a higher reaction kinetics of the reaction of the, preferably calcareous, particles of the exhaust gas treatment reagent with the sulfur oxides contained in the exhaust gases can be made possible.
  • the particles of the exhaust gas treatment reagent can act as condensation nuclei.
  • the exhaust gas treatment device can accordingly ensure a high separation efficiency of the sulfur oxides; in that the second injection and / or Einsprüh adopted in the second section, which is in the process direction downstream and / or downstream of the first section, is arranged. Accordingly, the exhaust treatment space is separated and / or divided into at least two regions, wherein initially a supply of the exhaust gas treatment reagent and then a supply of water vapor is provided; in each case by injection and / or injection devices provided for this purpose.
  • the exhaust gas treatment device according to the invention is characterized in particular by the fact that it can be integrated with little effort and low investment costs into an already existing exhaust gas treatment device, in particular for the exhaust gas treatment of huts. Consequently, the system according to the invention can be obtained by a simple retrofitting and, consequently, a high separation efficiency of sulfur oxides and a significant reduction in operating costs can be achieved.
  • the exhaust gas treatment device is designed such that the exhaust gases containing the sulfur oxides are subjected to exhaust gas treatment, in particular desulfurization, by means of at least one particulate sulfur dioxide-reactive exhaust gas treatment reagent, in particular desulfurization reagent.
  • the first injection and / or injection device for contacting and / or recording, in particular for injection and / or spraying, the exhaust gas treatment reagent in fine distribution with and / or in the exhaust gases (s) may be formed.
  • a fine distribution of the exhaust gas treatment reagent in the exhaust gas stream is advantageous, in particular, for uniform distribution of the particles of the exhaust gas treatment reagent in the exhaust gas stream, whereby an increased separation efficiency of the sulfur oxides can be ensured. Therefore, a high proportion of the exhaust treatment agent particles may react with the sulfur oxides in the second section.
  • first injection and / or Einsprüh drove at least one, preferably 2 to 8, first lance (s) for entry, in particular injection and / or spraying, the exhaust gas treatment reagent in the exhaust gases containing the sulfur oxides.
  • a first lance is particularly advantageous in that a supply of Abgas accompanimentsreagenzes can be specifically provided in the exhaust stream and thus the distribution of Abgas secretsreagenzes in the exhaust stream through the first lance can be specified target and purpose.
  • the first lance is designed such that it can provide the exhaust gas treatment reagent by means of a flow rate, in particular a conveying air flow available, the conveying air flow acts as a carrier for the Abgasgeschsreagenz and the first lance in the first section of the exhaust treatment room, preferably in the flue gas and / or exhaust duct, can be initiated.
  • the first lance can be designed in such a way that the particles of the exhaust gas treatment reagent leaving the first lance can be deflected and, together with the exhaust gas flow, flow through the first section.
  • the second injection and / or injection device preferably has at least one, preferably 2 to 8, second lance (s) for introduction, in particular injection and / or spraying, of the water vapor into the exhaust gases.
  • the second lance is in particular designed such that the water vapor can penetrate as deeply as possible into the exhaust gas flow and / or via a As large as possible range of the cross section of the second section of the exhaust treatment chamber, in particular the channel cross-section, can distribute.
  • the steam may be at least 20%, preferably from 20% to 80%, more preferably from 30% to 50%, of the cross section of the exhaust treatment space in the second section, preferably in the region of the second injection and / or Einsprüh adopted, in the exhaust gases be introduced.
  • the second lance may have a plurality of openings, preferably in the range of 2 to 8 openings, preferably in the range of 2 to 4 openings, for discharging and / or discharging the water vapor.
  • a plurality of openings results in a plurality of partial streams of water vapor, which can be introduced into the exhaust gases.
  • a multiplicity of partial flows a larger area of the second section of the exhaust gas treatment space can be brought into contact with the steam.
  • a greater proportion of the exhaust gas-containing particles of the exhaust gas treatment reagent can thus have a hydrate shell and / or act as condensation nuclei, wherein the formation of the hydrate shell can be initiated by the water vapor.
  • the first injection and / or injection device in particular the first lance, be designed and / or arranged such that the exhaust gas treatment reagent at an angle in the range of -30 ° to 30 °, in particular at an angle in Range of -20 ° to 20 °, more preferably at an angle in the range of -10 ° to 10 °, relative to the direction of the exhaust stream, preferably at least substantially in the flow direction, supplied in the first section of the Abgas accompaniments- space, in particular injected and / or sprayed.
  • the aforementioned angle can ultimately relate to the flow direction of the exhaust gas flow.
  • the flow direction relates in particular to the main flow direction and / or main flow direction of the exhaust gas flow.
  • the flow direction in particular the main flow direction and / or the main flow direction, can be arranged in the 0 ° position.
  • a negative angle of -20 ° can also be given as 340 °.
  • the introduction and / or supply of the exhaust gas treatment reagent at least substantially in the flow direction ensures that the particles of the exhaust gas treatment reagent can be "carried away" by the exhaust gas flow so that they are conveyed by the exhaust gas flow through the exhaust gas treatment chamber.
  • the second injection and / or injection device in particular the second lance, is designed and / or arranged such that the water vapor is at an angle of at least 20 °, in particular in one Angle of at least 30 °, preferably at an angle in the range of 20 ° to 160 °, more preferably at an angle in the range of 40 ° to 150 °, based on the direction of the exhaust gas flow, supplied in the second section of the exhaust treatment chamber, in particular injected and / or sprayed.
  • the second lance of the second injection and / or Einsprüh founded is arranged such that the outlet opening and / or the outlet openings at least substantially transversely, that is in a 90 ° -angle position, to the flow direction, in particular the Main flow direction and / or main flow direction, the exhaust stream are arranged.
  • An introduction of the water vapor provided at least substantially transversely to the flow direction has the advantage that the steam can penetrate into the exhaust gas stream due to its preferably higher velocity, so that ultimately a large proportion of the cross section of the exhaust gas treatment space can be brought into contact with water vapor. This would be difficult to achieve and / or executable upon introduction and / or delivery in the flow direction of the exhaust gas stream.
  • the water vapor When introduced in the direction of flow of the water vapor, it would not be possible, as provided for by the invention, for the water vapor to be distributed over a large proportion of the cross section of the exhaust gas treatment space. It is understood that in the case of a plurality of second injection and / or injection devices, these can each be arranged above and below the flow device, in particular the main flow direction and / or the main flow device, in the aforementioned angular ranges.
  • second injection and / or injection devices and / or first injection and / or injection devices may be arranged opposite one another, in particular wherein the respective adjacent devices are at an angle of preferably 100 ° to 250 °, more preferably 150 ° ° to 200 °, with each other.
  • At least one displacement body in particular in the form of a diaphragm, in particular pinhole, or a sheet, in particular guide or deflecting plate, and / or a Verwirbelungsrange, preferably a Venturi route arranged.
  • the displacer and / or the Verwirbelungsrange, in particular the Venturi route, are designed for deflecting and / or turbulence of the exhaust gases and / or the exhaust gas stream.
  • a filter device downstream and / or downstream in the direction of the second injection and / or spraying device and / or the second section of the exhaust treatment chamber is arranged.
  • a fabric filter can be used as a filter device, which is designed such that the products of the reacted exhaust gas treatment reagent and / or the unreacted exhaust gas treatment reagent and further dust-like particles can be deposited on it.
  • the filter device can undergo cleaning at cyclic intervals, which can be predetermined in particular by a control device which is coupled to the filter device.
  • the filter device for filtering the exhaust gases preferably for the separation and / or separation of the solids contained in the exhaust gas and / or pollutants, in particular solid and / or dust-like particles, preferably unreacted Abgas harmonysreagenz and / or reaction products of the converted exhaust gas treatment reagent may be formed.
  • the sulfur oxides can be at least substantially separated and / or separated from the exhaust gases through the filter device, whereby a subsequent disposal and / or utilization of the deposited on the filter device substances can be provided.
  • a so-called filter cake deposits on the filter device which is embodied in the exhaust gas treatment process according to the invention cyclic distances should be separated from the filter device and / or removed. This filter cake can then be disposed of properly.
  • a recycling device in particular downstream and / or in the process direction downstream of the filter device, a recycling device is provided.
  • the recycle device may be configured to recycle the unreacted exhaust treatment reagent and / or the reacted exhaust treatment reagent, preferably after filtering in the filter device and / or the fabric filter.
  • a recycle allows a reuse of the exhaust gas treatment reagent, preferably the unreacted exhaust gas treatment reagent, resulting in a reduction of the operating costs.
  • a first storage container device for storing and / or storing the exhaust gas treatment reagent.
  • the first storage tank device can be fed recycled waste gas treatment reagent from the recycling device.
  • the first storage container device can be provided in particular for the supply of exhaust gas treatment reagent to the first injection and / or Einsprüh observed.
  • the first reservoir device can preferably be assigned to the first injection and / or injection device, preferably wherein the first reservoir device is connected to the first injection and / or injection device.
  • the exhaust gas treatment reagent can be stored safely in the first storage container device, in particular in the dry state of the exhaust gas treatment reagent.
  • the storage container device can be coupled to a control device for the targeted and purposeful feeding of the exhaust gas treatment reagent, wherein the control device can control and / or regulate the supply of the exhaust gas treatment reagent, preferably also of the water vapor.
  • a second storage container device may preferably be provided for storage and / or storage of water and / or water vapor, in particular for supplying water and / or water vapor to the second injection and / or Einsprüh observed.
  • the second storage container device can be assigned to the second injection and / or injection device, preferably wherein the second storage container device is connected to the second injection and / or injection device.
  • a heating device for generating the water vapor may be connected to the second reservoir device and / or the second injection and / or injection device, in particular if water is stored in the second reservoir device.
  • the heating device can be designed such that its water can be supplied through the second storage container means and they can heat this water to saturated steam.
  • This saturated steam can then provide the heating device the second injection and / or Einsprüh worn.
  • the second storage container device and / or the heating device and / or the second injection and / or spraying device can be coupled to a control device for controlling and / or regulating, in particular for supplying the water vapor, in particular wherein Control device, the temperature, the pressure and the amount to be supplied water vapor can be specified.
  • a targeted and purposeful supply of water vapor can be carried out, preferably in view of the formation of the hydrate shell and / or increasing the separation efficiency, an optimization of the system according to the invention and / or the inventive exhaust gas treatment method.
  • system according to the second aspect of the present invention in particular according to one of the embodiments described above, is characterized by the features of the first aspect of the present invention, in particular the preferred embodiments of the exhaust gas treatment method according to the first aspect of the present invention.
  • Another object of the present invention - according to a third aspect of the present invention - is the use of the method (exhaust gas treatment method), in particular according to the first aspect of the present invention, and / or the plant, in particular according to the second aspect of the present invention, for the purification of Sulfur oxide-containing waste gases from smelters, in particular copper smelters and / or iron smelters, cement works, steelworks or power plants, preferably hard coal power plants, and / or for treatment from pig iron and / or steel production by means of Sintering of iron ores and, subsequently, the production of pig iron in the blast furnace process.
  • Fig. 1 is a schematic representation of a system according to the invention according to a particular embodiment of the present inven tion;
  • Fig. 2 is a schematic representation of an inventive
  • Fig. 3 is a schematic representation of a system according to the invention according to a particular embodiment of the present inven tion;
  • FIG. 1 shows an inventive plant 6 for the treatment of sulfur oxides (SO x ) containing exhaust gases from industrial processes for the purpose of removal and / or deposition of sulfur oxides and / or for purposes of reducing the sulfur oxide content.
  • the plant 6 has a device 7 for carrying out a sulfur oxide-containing exhaust gases generating technical process.
  • the technical process can be, for example, a metallurgical process or can be carried out as part of smelting and / or contain combustion.
  • the device 7 is associated with an exhaust gas treatment device 8, wherein the exhaust gas treatment device 8, the sulfur oxide-containing exhaust gases generated in the device 7 are supplied.
  • the exhaust gas treatment device 8 is connected downstream in the illustrated embodiment and provided in the process direction downstream of the device 7.
  • the exhaust gas treatment device 8 can also be assigned to the device 7.
  • the exhaust gas treatment device has a channel-shaped exhaust gas treatment chamber 9.
  • the exhaust gas treatment chamber 9 is subdivided into a first section 10 and a second section 11 arranged downstream of the first section 10 and / or arranged downstream of the first section 10 in the process direction.
  • the first injection and / or injection device 1 is designed in such a way that an exhaust gas stream containing the exhaust gas treatment reagent is obtained, which is not shown in the illustrated exemplary embodiments.
  • a second injection and / or injection device 2 is arranged downstream of the first injection and / or injection device 1 in the second section 11 of the exhaust treatment chamber 9 and downstream of the process.
  • the second injection and / or injection device 2 is provided for contacting and supplying water vapor with the exhaust gas stream containing the exhaust gas treatment reagent.
  • the supply of water vapor can be carried out in such a way that the exhaust gas treatment reagent is reacted with the sulfur oxides contained in the exhaust gases.
  • first injection and / or injection device 1 has two first lances 1 1 and the second injection and / or injection device 2 has two second lances 13.
  • the second lance 13 may have a plurality of openings.
  • the second lance 13 may have two to eight openings for discharging and / or for discharging the water vapor.
  • the first injection and / or injection device 1 in the illustrated embodiment also the first lance 12, is arranged at an angle ⁇ of at least substantially 10 ° to the direction of the exhaust gas flow.
  • the direction of the exhaust gas flow is predetermined by the flow direction and, consequently, the main flow direction or main flow direction of the exhaust gas flow.
  • the angle ⁇ may vary within a range of -30 ° to 30 °.
  • a negative angle indicates that the lance 12 instead of facing upwards, so that ultimately an angle ß of -20 ° also indicates an angle of 340 ° in analogy to the positive angle ß to the main flow direction or to the main flow direction of the exhaust gas flow ,
  • two first lances 12 can each be arranged at an angle ⁇ of at least substantially 10 ° to the flow direction, wherein the two first lances 12 lie opposite one another and enclose an angle of at least substantially 160 ° with one another.
  • the second injection and / or injection 2 in the illustrated embodiment, in each case the two second lances 13, is arranged such that the water vapor at an angle a of at least 20 °, in the illustrated embodiment of an angle a of at least substantially 90 °, based on the direction of the exhaust gas stream, is supplied.
  • the direction of the exhaust gas flow is in the illustrated embodiment, the main flow direction and the main flow direction of the exhaust gas flow.
  • the angle a may be provided in the range of 20 ° to 160 °.
  • two second lances 13 each at an angle a of 90 ° to the flow direction of Arranged exhaust gas flow, wherein the two second lances 13 with each other enclose an angle of at least substantially 180 °.
  • the exhaust gas treatment reagent can be introduced centrally into the first section 10 and / or at the edge into the exhaust gas treatment chamber 9 and / or in the first section 10 via the first injection and / or injection device 1.
  • FIG. 1 shows that a swirling section 4 is arranged between the first section 10 and the second section 11 of the exhaust-gas treatment chamber 9 of the exhaust-gas treatment device 8.
  • the Verwirbelungsrange 4 is formed for turbulence and / or deflection of the exhaust stream.
  • a turbulence of the exhaust gas stream for example, a good mixing of the exhaust gas stream with the particles of the exhaust gas treatment reagent can be caused.
  • the displacer 3 is formed as a pinhole.
  • the pinhole diaphragm can be designed in such a way that it has, for the second injection and / or injection device 2, an area for the outlet and / or outlet of the water vapor which is at least substantially free of the particles of the exhaust gas treatment reagent.
  • the second lances 13 of the second injection and / or injection device 2 are arranged in a region which is at least substantially free of the particles of the exhaust gas treatment reagent of the exhaust gas stream, so that caking or caking on the second lance 13 can be avoided.
  • FIGS. 1 and 3 show that downstream of the second section 11 and the second injection and / or injection device 2 a filter device 5 can be arranged.
  • the filter device 5 is formed as a fabric filter.
  • the filter device 5 is also designed such that dust-like particles can be deposited on it.
  • the solids contained in the exhaust gases and / or pollutants, in particular solid and / or dust-like particles, preferably of unreacted exhaust gas treatment reagent and / or reaction products of the reacted exhaust gas treatment reagent can be deposited.
  • the first injection and / or injection device 1 is assigned a first storage container device 14, so that the exhaust gas treatment reagent of the first injection and / or Spraying device 1 can be supplied via the first storage tank device 14.
  • FIG. 3 shows that a second storage container device 15 can be associated with the second injection and / or injection device 2.
  • a heating section 16 is connected downstream of the second storage tank device 15.
  • the heating section 16 is designed for heating water, which can be fed to it via the second Vorratsge conceptioner observed 15.
  • the steam thus produced, in other embodiments saturated steam, can then be supplied to the second injection and / or injection device 2, in particular the second lance 13.
  • the water vapor of the second injection and / or spraying device 2 in particular the second lances 13, from the device 7 and / or from steam-carrying and / or steam-generating components or Anlagenkompenenten the system 6 to Is made available.
  • process flow diagram for the treatment of sulfur oxides (SO x) -containing flue gases from industrial processes for the purpose of removal and / or deposition of the sulfur oxides and / or reduction of the Schwefeloxidgehalts the successive process steps or process steps are shown schematically, wherein the steps the generation of the SO x -containing exhaust gas and the supply to the filter device 5 and the filter are optional.
  • the optional method step of turbulence and / or deflection is provided between the non-optional method steps (a) and (b).
  • process step (a) the exhaust gas treatment reagent is supplied.
  • process step (b) which is downstream of the process step (a)
  • water vapor, preferably saturated steam, is fed.
  • the exhaust gas treatment process ultimately serves to desulphurise and concomitantly reduce the proportion of sulfur oxides in the exhaust gases.
  • the following embodiments show the exhaust gas treatment process according to the invention and, consequently, the deposition of sulfur oxides (SO x ) from exhaust gases which originate from industrial processes.
  • the exhaust gas is supplied in a first process step (a) the exhaust gas treatment reagent.
  • the exhaust gas through a pinhole, which acts as a displacer, out.
  • This is followed by an addition of water vapor.
  • the dry sorption not according to the invention without the addition of steam or with the preceding addition of steam ie addition of steam before the addition of the exhaust gas treatment reagent
  • the steam has a pressure of at least substantially 4 bar at a temperature of at least substantially 143 ° C.
  • the exhaust gas treatment reagent is introduced into the exhaust gas flow by means of a conveying air flow in method step (a).
  • the process sequence of the exhaust gas treatment process according to FIG. 5 is carried out.
  • the exhaust gas treatment device according to the invention is shown in FIG. 3.
  • the sulfur oxides or the proportion of sulfur oxides in the exhaust gas is indicated in the experiments carried out by the measurement of sulfur dioxide.
  • Exhaust gases having a temperature of at least substantially 40 ° C and with a
  • the added waste gas treatment reagent has at least substantially 75% by weight hydrated lime (slaked lime).
  • the exhaust gas treatment reagent has particle sizes of at least substantially 35 .mu.m, which have been determined by means of a sieve analysis according to DIN 66165.
  • the mean particle size D50 is at least substantially 10 to 15 pm and was likewise determined by sieve analysis in accordance with DIN 66165.
  • the exhaust gas treatment reagent furthermore has a BET surface area of at least substantially 35 m 2 / g, the BET surface area being based on the sulfur-oxide-reactive surface of the exhaust gas treatment reagent, in particular of the hydrated lime.
  • the total pore volume of the exhaust treatment reagent is further at least substantially 0.35 cm 3 / g.
  • the stoichiometric ratios of the addition of the exhaust gas treatment reagent are given in the following table, wherein the stoichiometric ratio is calculated as the ratio of exhaust gas treatment reagent used to reduced and / or precipitated sulfur oxides.
  • the stoichiometric ratio refers to the exhaust gas treatment reagent to the sulfur oxides.
  • the exhaust gas flow is identical and is in each case at about 70,000 standard cubic meters / h, the sulfur oxide loading of the exhaust gas stream before exhaust gas treatment (measured or evaluated as S0 2 ) is about 700 mg / standard cubic meter of exhaust gas.
  • the separation performance of the sulfur oxides can be significantly increased by the addition of water vapor according to the invention at an equal stoichiometric ratio of the exhaust gas treatment reagent. Even when lowering the stoichiometric ratio, the separation efficiency can be increased by the addition of steam, wherein the addition of the exhaust gas treatment reagent correlates at least in certain areas with the separation efficiency.
  • the exhaust gas treatment process according to the invention shows very good results both with regard to the separation efficiency and to the reduction of the stoichiometric ratio.
  • exhaust gases are treated from zinc smelter, wherein the exhaust gases have an exhaust gas temperature of 60 ° C and a water vapor content of at least substantially 3 vol .-%.
  • the exhaust gases in the Example 2 series have a higher proportion of sulfur oxides in comparison to the exhaust gases from Example Series 1.
  • the exhaust gas treatment reagent used in Example 2 has at least substantially 93% by weight (purity) of hydrated lime and, moreover, a particle size of at least substantially 30 ⁇ m, which is determined by means of a
  • Sieve analysis has been determined according to DIN 66165.
  • the mean particle size D50 of the hydrated lime is in the range from 5 to 8 ⁇ m (determined by sieve analysis according to DIN 66165).
  • the BET surface area is between 40 and 60 m 2 / g.
  • the total pore volume is between 0.2 to 0.4 cm 3 / g.
  • the exhaust gas treatment reagent has also been finely ground and spotted and also dry quenched and coarse from existing ones
  • the exhaust gas flow is identical and is in each case at about 70,000 standard cubic meters / h, the sulfur oxide loading of the exhaust gas stream before exhaust treatment (measured or evaluated as S0 2 ) is about 1000 mg / standard cubic meter of exhaust gas.
  • experiment 1 of example 2 (not according to the invention) and experiment 2 of example 2 (according to the invention) are repeated, but with the difference that the amount of exhaust gas treatment reagent used was identical in both experiments at 405 kg / h.
  • experiment 2 of the example series 2A was repeated, but with the difference that the addition of the steam already takes place before the addition of the exhaust gas treatment reagent.
  • the separation performance for the sulfur oxides is initially within the first hour at only 53%, which already due to caking or caking on the system components in the exhaust treatment room, especially in the second section of the exhaust treatment room, the separation efficiency in this approach not according to the invention after 3 h was below 40%.
  • the six experiments of the example series 2 were repeated, but with the deviation that the addition of the water vapor does not take place after supply of the exhaust gas treatment reagent but before and / or upstream and / or upstream. Accordingly, the steam is first introduced into the exhaust gas flow in the first section of the exhaust treatment chamber, in particular injected and / or sprayed, and then introduced in process step (b) in the second section of the exhaust treatment room, the exhaust treatment reagent, in particular sprayed and / or injected.
  • a plant downtime due to a failed Abgas adaptations- device took place after 2 to 3 days of operation.
  • the shutdown is due to the arrival and / or caking of the second injection and / or Einsprüh coupled, in particular the steam lance, due.
  • the separation efficiency of the method according to the invention could not be achieved.
  • the separation efficiency dropped significantly, in particular due to the reduced supply of steam, and the separation efficiency only caused sufficient results after 2 to 3 h. After a day is the
  • Example Series 3 Separation performance of sulfur oxides had been unacceptable.
  • the separation efficiency of Example Series 3 was subject to the results of the method according to the invention in each of the six experiments both at the beginning of the operation and after several hours of operation. LIST OF REFERENCE NUMBERS

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Abstract

L'invention concerne le domaine technique de traitement d'effluents gazeux contenant des oxydes de soufre, notamment des effluents gazeux issus d'installations d'incinération techniques, dits gaz de fumée, ou de gaz d'échappement issus de procédés techniques comme, par exemple, la fabrication d'acier (par exemple gaz de haut fourneaux, etc.). L'invention concerne en particulier un procédé de traitement d'effluents gazeux contenant des oxydes de soufre, notamment issus d'installations d'incinération techniques, comme des gaz de combustion ou issus de procédés techniques, en vue de l'élimination et/ou de la séparation des oxydes de soufre ou en vue de la réduction de la teneur en oxyde de soufre, ainsi qu'un dispositif pour la mise en œuvre du procédé.
EP18807308.4A 2017-12-20 2018-11-21 Procédé de traitement d'effluents gazeux contenant des oxydes de soufre Withdrawn EP3675987A1 (fr)

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DE102018105892.6A DE102018105892A1 (de) 2017-12-20 2018-03-14 Verfahren zur Behandlung von Schwefeloxide enthaltenden Abgasen
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Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI78401B (fi) * 1985-04-24 1989-04-28 Tampella Oy Ab Foerfarande och anordning foer att bringa roekgasernas gasformiga svavelfoereningar saosom svaveldioxid att reagera till fasta foereningar som separeras fraon roekgaserna.
DE3526008A1 (de) * 1985-07-20 1987-01-22 Metallgesellschaft Ag Verfahren zur entfernung von schadstoffen aus rauchgas
FI88681C (fi) * 1990-10-18 1993-06-28 Sf Cleanair Oy Foerfarande och anordning foer rening av roekgaser vid oljepannor
DE19609966A1 (de) * 1996-03-14 1997-09-25 Intensiv Filter Gmbh Verfahren zur Reinigung SO¶2¶-haltiger Abgase
DE19711529A1 (de) * 1997-03-19 1998-09-24 Sueddeutsche Kalkstickstoff Verfahren zur Entfernung von sauren Schadstoffen aus Abgasen
DE10133991B4 (de) * 2001-07-12 2012-08-02 Doosan Lentjes Gmbh Vorrichtung zur Reinigung von Verbrennungsabgasen
DE102009048370A1 (de) * 2009-07-24 2011-01-27 Drysotec Gmbh Verfahren zur Behandlung von Abgasen, insbesondere aus der Stahlherstellung
US20180250628A1 (en) * 2015-08-31 2018-09-06 Mobotec Uk Ltd Sorbent injection system and method for treating flue gases

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DE102018105892A1 (de) 2019-06-27
US20200368680A1 (en) 2020-11-26
CL2020001121A1 (es) 2020-10-09

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