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    • 专利摘要:
    The invention relates to a composition for the purification of flue gas containing from 35 to 99% by weight of a powder of an alkali metal salt of carbonic acid and from 1 to 65% by weight of a powder of a material absorbent material, wherein the powder of an absorbent material has a specific pore volume that is equal to or greater than 0.1 cm3 / g. The invention also relates to a method for the purification of dry flue gas and the use of an absorbent material for improving the fluidity and / or the storage ability and / or the absorption capacity of the HF. an alkali metal salt of carbonic acid.
    公开号:BE1023883B1
    申请号:E20165973
    申请日:2016-12-23
    公开日:2017-09-05
    发明作者:Martin Sindram；Walter Diethelm；Xavier Pettiau；Christopher Pust
    申请人:Lhoist Rech Et Developpement Sa；
    IPC主号:
    专利说明:

    COMPOSITION FOR THE PURIFICATION OF SMOKE GAS
    The present invention relates to a composition for the purification of dry flue gas, a method of manufacturing said composition, and the use of said composition for the purification of flue gas by the dry route. The invention also relates to a process for the purification of dry flue gas and the use of an absorbent material to improve the fluidity and / or storage ability and / or the HF absorption capacity of a alkali metal salt of carbonic acid.
    Many industrial processes produce flue gases. For example, in the combustion of fossil fuels, for example in power stations such as coal-fired power plants, large quantities of flue gas are produced. Also in the incineration of waste, large quantities of flue gas are produced.
    The flue gases often contain dangerous or even toxic pollutants, for example sulfur oxides, such as sulfur dioxide (SO2) or sulfur trioxide (SO3), and / or hydrogen halides, such as hydrogen fluoride (HF) and / or hydrogen chloride (HCl).
    Attempts have been made to reduce pollutant levels in the air. In particular, processes for the purification of flue gases have been devised to reduce the amounts of pollutants emitted for example by waste incineration plants and by plants fueled by fossil fuels. These methods usually include contacting the flue gas with an absorbent, also known as a sorbent.
    Various processes have been devised for the purification of flue gases, also called flue gas cleaning. In wet scrubbing, an alkaline absorbent such as limestone or a lime material is contacted with the flue gas usually in the form of an aqueous slurry. The disadvantages of wet scrubbing include corrosion of the equipment, need for treatment or reuse of wastewater.
    In dry scrubbing, also known as dry flue gas purification or dry sorbent injection, the absorbent is normally contacted with the flue gas in the dry state. After absorption, the dry reaction products are normally collected downstream in a dedusting unit which usually has a fabric filter or an electrostatic filter. A major advantage of dry flue gas purification is the simplicity of the equipment required to implement dry flue gas purification.
    Lime-based materials, such as hydrated lime (Ca (OH) 2), or alkali metal salts of carbonic acid, such as sodium hydrogencarbonate (NaHCOa) or sodium sesquicarbonate such as trona (Na2CO3 * NaHCO3 * 2H2O), are often used as absorbers in the purification of flue gases by the dry route.
    It has been suggested to use both sodium hydrogencarbonate and hydrated lime for the purification of flue gas. JP Hll-165036 A discloses a method for the purification of flue gas by simultaneous injection of sodium hydrogencarbonate and hydrated lime via two separate injection systems in the. flue gas stream. However, the two separate injection systems increase the cost of the flue gas purification system.
    In addition, improved absorbents have been reported, particularly improved calcium hydroxide particles.
    For example, EP 0 861 209 B1 discloses calcium hydroxide particles having a total pore volume of at least 0.1 cm 3 / g for the capture of acid gases. The calcium hydroxide particles are prepared by quenching quicklime (CaO) particles having a reactivity greater than 30 ° C / minute with sufficient water to obtain calcium hydroxide having residual moisture between 15 and 30% by weight, followed by drying and milling. Particles are reported to be more effective than standard calcium hydroxide particles in capturing sulfur dioxide and hydrogen chloride.
    WO 2007000433 A2 discloses a powdered hydrated lime comprising up to 3.5% by weight of an alkali metal and having a BET specific surface area of 25 m 2 / g or more and a total pore volume B JH of 0 , 1 cm3 / g. Hydrated lime is prepared by slaking lime. The alkali metal is introduced into the hydrated lime by means of an alkali metal salt which is advantageously added to the extinguishing water for quicklime. It is reported that hydrated lime is more effective than other hydrated lime based absorbers in capturing sulfur dioxide and hydrogen chloride. Generally, in order to increase the absorbency of the adsorbents, they are ground into fine powders having a small particle size. The smaller the particle size and the greater the specific surface area of the particle, and therefore the absorbent, which absorbant can react with pollutants in the flue gas. As a characteristic value of the particle size of a powder, the so-called dso value is often used. The dso value of the particles of the powder is normally determined by the particle size distribution of the powder. The size for which 50% of the powder will pass through a theoretical opening of a sieve, determined from the particle size distribution, is commonly called the d50 value. Typically, d50 values of less than 40 μm, or even less than 20 μm, are desirable for absorbents.
    Maintaining a low d50 in a powder of an alkali metal salt of carbonic acid is difficult, particularly for trona and for sodium hydrogen carbonate.
    Although it is possible to prepare by grinding a powder of an alkali metal and carbonic acid, in particular sodium hydrogen carbonate, having a dso of less than 40 μm or even less than 20 μm, the resulting small particle size of the Fine grain powder can not be maintained over long periods of time. Normally, after a few days or even after one day, the particles of the powder of an alkali metal salt of carbonic acid, in particular sodium hydrogencarbonate, begin to reagglomerate, thereby forming larger aggregates. A powder containing larger aggregates is undesirable because of the reduced surface area. For this reason, the alkali metal salts of carbonic acid, particularly sodium hydrogencarbonate, are normally milled to the site immediately prior to use. This necessitates the presence of grinders for the alkali metal salt of carbonic acid, which increases the cost of the flue gas purification system, also because of their maintenance cost. Thus, the storage ability of alkali metal salt powders of carbonic acid, particularly trona or sodium hydrogencarbonate, having a low d50 is difficult.
    In addition to their specific surface, the particles may also contain some porosity, normally specified by the specific pore volume of the material. If the porosity-forming pores are accessible from outside the particles, this usually also increases the particle surface area. Therefore, if the material being studied has a large specific pore volume, it also normally has a high specific surface area. However, the reverse is not necessarily the case. For example, fumed silica, sometimes also called fumed silica, is a particulate material having a surface area of 50 to 600 m 2 / g, the particles of which are non-porous.
    Another problem with the powders of alkali metal salts of carbonic acid, in particular sodium hydrogen carbonate, is their fluidity. When stored for example in silos, powders of alkali metal salts of carbonic acid tend to become denser, presumably by the action of gravity. In this process, the powder loses its fluidity, making it difficult to remove the powder from the silo. In order to make the powder accessible, it must be agitated, for example with air under pressure, so that the fluidity of the powder is restored.
    Yet another problem observed when grinding alkali metal salts of carbonic acid, in particular sodium hydrogencarbonate, is the agglutination of the ground material on the grinding equipment, for example on the walls of the mill. This agglutination effect makes regular maintenance of the grinders necessary. Attempts to overcome this agglutination effect include the addition of stearic acid, calcium stearate, trimethylolpropane, or glycols during milling, particularly to sodium hydrogencarbonate. While this helps to reduce the agglutination effect, the additional additives increase the cost of the process.
    In addition to compositions consisting mainly of a single absorbent, mixtures of absorbents are also known.
    WO 2007031552 A1 discloses a SO3-containing flue gas absorbent composition which contains an additive and a sodium-based absorbent such as sodium hydrogencarbonate or mechanically refined trona. The additive is selected from magnesium carbonate, calcium carbonate, magnesium hydroxide, calcium hydroxide, and mixtures thereof, and is present in the mixture in an amount of preferably between 0.1% and 5%, especially 0.5 to 2% by weight of the sodium-based absorbent.
    DE 202 10 008 U1 describes a composition for the purification of flue gases based on quicklime (CaO). The composition may further contain calcium hydroxide and sodium hydrogencarbonate. Compositions which contain mainly quicklime are preferred.
    US 4,859,438 discloses a method for removing hazardous substances in flue gases using mixtures of dry absorbers based on hydrated oxides, hydroxides or oxides. The dry absorbents may comprise sodium hydrogencarbonate and one or more of NH 4 HCO 3, Al (OH) 3, silica gel, calcium hydroxide, and salts with water of crystallization such as CaCl 2 or Al 2 O 3. It is reported that the removal of hazardous substances in the flue gases is improved with the composition.
    EP 1 004 345 A2 discloses a treating agent for the removal of acidic components in a gas. The treating agent contains sodium hydrogencarbonate in an amount of preferably at least 70% by weight, and may contain another component such as potassium hydrogencarbonate, slaked lime, calcium carbonate, zeolite, activated charcoal, or silica or diatomaceous earth. In order to prevent agglomeration, the treating agent may contain silica powder, fumed silica, white carbon, basic magnesium carbonate, calcium carbonate or diatomaceous earth. The composition of EP 1 004 345 A2 can effectively remove the acidic components in a flue gas.
    The above-mentioned examples of prior art compositions remain silent about the porosity of the absorbents and / or the beneficial effects resulting therefrom.
    In spite of the progress made in maintaining storage ability, solutions are desired that help maintain the particle size distribution, particularly the dso value, of a powder. In addition, it is desired to have absorbent compositions having a good absorption capacity for sulfur oxides and / or hydrogen halides. In addition, it is desired compositions having a good fluidity, especially after a certain storage time.
    An object of the present invention therefore lies in the provision of a composition having a good fluidity, a good storage capacity, and / or a good absorbency of pollutants such as sulfur oxides and / or hydrogen halides. 'hydrogen. In particular, an object of the present invention lies in the provision of a composition for the purification of flue gas having a sulfur oxide absorption capacity as high as possible and at the same time a good fluidity, in particular after a some storage time. This combination of properties is particularly difficult to achieve because compounds with good sulfur oxide adsorbency, such as, for example, sodium hydrogencarbonate, are known for their limited fluidity, especially after a certain storage time.
    Some or all of these objects can be achieved using the present invention. In particular, some or all of these objects can be achieved by the composition of claim 1, the method of manufacture of claim 10, the composition of claim 15, the method of claim 16, the use of the claim 17, and the use of claim 18. Other embodiments are described in the dependent claims and will be discussed in the following. The invention provides a composition for the purification of flue gas, said composition containing, in each case with respect to the total weight of the composition: a. 35 to 99% by weight of a powder of an alkali metal salt of carbonic acid; and B. 1 to 65% by weight of a powder of an absorbent material; wherein said powder of said absorbent material has a specific pore volume which is equal to or greater than 0.1 cm3 / g.
    It has surprisingly been found that as a result of the unique combination of 35 to 99% by weight of a powder of an alkali metal salt of carbonic acid with 1 to 65% by weight of a powder of a absorbent material, wherein said powder of said absorbent material has a specific pore volume which is equal to or greater than 0.1 cm 3 / g, a composition for the purification of flue gas which can be well stored and / or has good fluidity and / or has a good absorbency of pollutants, in particular sulfur oxides. In particular, it has been found that compositions containing 35 to 99% by weight of a powder of an alkali metal salt of carbonic acid and 1 to 65% by weight of a powder of an absorbent material having a porous volume Specifically equal to or greater than 0.1 cm3 / g have good sulfur oxide adsorption capacity and improved fluidity, particularly after some storage time, compared with pure powders of alkali metal salts of carbonic acid.
    Without being willing to be bound by a scientific theory, it turns out that the high specific porosity of the powder of the absorbent material facilitates the storage of the composition and / or the maintenance of a good fluidity, possibly by trapping of moisture and / or liquids within the particles of absorbent material. In this way, an unchanged surface of the particles can be maintained. This can help prevent an aggregation. This can also help maintain fluidity.
    Surprisingly, it has also been found that when using the above composition in flue gas purification, peak concentrations of hydrogen fluoride do not result in a very high consumption of the composition. .
    The absorbency of an absorbent (or an absorbent composition) describes in particular its ability to retain pollutants, in particular sulfur oxides and / or hydrogen halides. Absorbency can for example be expressed in absolute terms, i.e. by the absolute amount of pollutant absorbed by the absorbent (or absorbent composition), or in relative terms, i.e. ie, the amount of pollutant absorbed by the absorbent (or absorbent composition) relative to an absorbent (or absorbent composition) of reference.
    The fluidity of a loose material, in particular a powder, is related to its accessibility from a storage container. Good fluidity can normally be attributed to loose materials, particularly powders, which can easily flow from the storage container, for example from a silo, due to the action of gravity. In particular, for loose materials having good fluidity, no other flow promoting action is required on the material. Uncoated materials, particularly powders, which have a propensity to obstruct the flow out of the silo, for example by forming consolidated "bridges" (for example via liquid droplets) between the particles, can normally be said to have poor fluidity The fluidity of a cohesive material, in particular a powder, can for example be described by means of the FFC value. Higher FFC values indicate better fluidity.
    DLZ
    The methods for determining the FFC value are known to those skilled in the art and are also described for example in the article by Dietmar Schulze "Zur Fließfähigkeit von Schüttgütern - Definition und Meßverfahren", published in the journal "Chemie Ingenieur Technik" by Wiley VCH, 1995, Volume 67, 1st edition, pages 60-68, or in "Powders and Bulk Solids - Behavior, Characterization, Storage and Flow" by Dietmar Schulze, Berlin Springer-Verlag Heidelberg, 2008. The FFC value can for example be determined by a uniaxial compression test. In the uniaxial compression test, normally a hollow cylinder, ideally with frictionless walls, is filled with the loose material, particularly the powder, under study, and a stress SI - the stress of consolidation - is applied in the vertical direction in the first step. The SI constraint can also be called sigmai, σι. Then the consolidation stress SI on the sample is released, and the hollow cylinder is removed. Then, an increasing vertical compressive stress is applied to the sample of consolidated cylindrical cohesionless material, particularly the consolidated powder sample, to the stress Sc at which the cylindrical sample breaks (or becomes defective). The stress Sc can be called compressive force or unconfined elastic limit, and is sometimes also called sigmac, ac. The defect of the consolidated cylindrical sample following the application of the stress Sc indicates the initial flow of the material without consolidated cohesion, in particular of the consolidated powder. The FFC value can then be determined by the ratio FFC = Sl / Sc.
    The fluidity of a loose material, particularly a powder, can also be determined by means of a Jenike shear tester. In this case, the test method for determining the FFC value usually requires the
    DC.Z determination of what is called the elastic limit or the plot of elasticity locus, from which SI and Sc, and thus the FFC value, can be determined. The determination of the elasticity pattern is described in the references of Dietmar Schulze mentioned above and normally requires a pre-shear treatment of the sample (shear of the sample up to the point of constant shear stress, however). a first consolidation force is applied), followed by a measuring step (shearing of the sample up to the maximum shear stress at which the particles begin to move relative to each other while a force of consolidation lower than that in the pre-shear treatment is applied). For each point in the yield curve, a new sample is required which must be subjected to the same pre-shear treatment. From the resulting elastic limit plot, SI and Sc and hence the FFC value can be determined.
    In addition, it is also possible to describe and / or generally determine the fluidity using an annular shear tester, for example an annular shear tester of the RST-XS type. In the annular shear tester, the sample (the unrelated material, particularly the powder) is usually introduced into an annular shear cell of the tester. A lid is normally placed on the top of the sample and secured with a cross member. Then, a normal stress S is usually applied to the sample via the cover of the shear cell. During measurement, the shear cell usually rotates slowly, while the cover and crosshead are prevented from rotating by two tie rods connected from opposite sides of the crosshead. The bottom of the shear cell and the bottom side of the cover are normally rough so that the rotation of the shear cell induces a shear stress that can be measured via the forces acting on the two tie rods. The measurement steps are similar to the steps described above, although it is possible to determine a complete elastic locus plot with a single sample. From the resulting elastic limit plot, SI and Sc, and thus the FFC value, can then be determined.
    According to one embodiment, the composition has a fluidity value, in particular a FFC value, in particular determined by means of an RST-XS annular shear tester, of 0.2 or more, in particular 0.3 or more, or 0.4 or more, or 0.5 or more, or 0.6 or more, or 0.7 or more, or 0.8 or more, or 0.9 or more , or of 1.0 or more, or 1.1 or more, or 1.2 or more, or 1.3 or more.
    According to one embodiment of the invention, the composition contains 35 to 90% by weight, in particular 35 to 80% by weight, or 35 to 70% by weight, or 35 to 60% by weight, or 35 to 50% by weight. % by weight of said powder of an alkali metal salt of carbonic acid, relative to the total weight of the composition. It has been found that the composition absorbs sulfur dioxide particularly well in these ranges. It has also been found that, in these ranges, the fluidity of the composition, in particular the fluidity after a certain storage time, is improved. In addition, it has been found that a composition having a particularly well-balanced property profile can be obtained if the alkali metal salt of carbonic acid is present in an amount of about 35 to 50% by weight based on the weight. total of the composition.
    dti
    According to another embodiment of the invention, the composition contains 10 to 65% by weight, in particular 20 to 65% by weight or 30 to 65% by weight or 40 to 65% by weight or 50 to 65% by weight. weight of said powder of said absorbent material, based on the total weight of the composition. It has been found that a composition having a particularly well-balanced property profile can be obtained if the absorbent material is present in an amount of about 50 to 65% by weight based on the total weight of the composition.
    The particles of the powder of the alkali metal salt of carbonic acid may have various sizes. It is however advantageous that the particles are small. Thus, in accordance with another embodiment of the invention, the alkali metal salt powder of carbonic acid has a d.sub.50 particle size of less than 50 .mu.m, in particular less than 45 .mu.m or less than 40 .mu.m or less than 35 .mu.m. or less than 30 μm or less than 25 μm or less than 20 μm or less than 15 μm or less than 12 μm. It is particularly preferred that the powder of an alkali metal salt of carbonic acid has a d.sub.2 particle size of less than 20 .mu.m, more preferably less than 15 .mu.m or less than 12 .mu.m. Preferably, the powder of the alkali metal salt of carbonic acid has a particle size d97 of less than 180 μm, in particular less than 170 μm or less than 160 μm or less than 150 μm or less than 140 μm or less than 125 μm. It has been found that powders of alkali metal salts of carbonic acid having particle sizes as mentioned above absorb pollutants more efficiently.
    In order to obtain an effective composition for the purification of flue gas, various alkali metal salts of carbonic acid can be used. Preferably, the alkali metal salt of carbonic acid is selected from the group consisting of sodium hydrogencarbonate, sodium carbonate, sodium sesquicarbonate, potassium hydrogencarbonate, potassium carbonate, sodium sesquicarbonate, and the like. potassium, and mixtures thereof. More preferably, the alkali metal salt of carbonic acid is sodium hydrogencarbonate and / or sodium sesquicarbonate. It has been found that with the aforementioned alkali metal carbonic acid salts, the absorbency, particularly the absorption capacity of sulfur dioxide, is very good.
    Sodium sesquicarbonate can for example be used in the form of trona which can be directly extracted from a deposit. The trona extracted from a deposit can thus be used with or without subsequent refining. Sodium hydrogencarbonate may for example be used in the form of nahcolite extracted from a deposit and / or as a product of a chemical process. Nahcolite extracted from a deposit can thus be used with or without subsequent refining.
    The trona extracted from a deposit may contain impurities such as shortite, dolomitic schist, quartz, illite, calcite, feldspar, and / or sodium fluoride. The trona extracted from a deposit may contain up to 20% by weight, preferably up to 15% by weight, more preferably up to 10% by weight, more preferably up to 5% by weight, more preferably up to 5% by weight. 3% by weight of the abovementioned impurities, relative to the total weight of the trona.
    The composition according to the invention may contain different materials serving as absorbent material. Preferably, the absorbent material is an absorber of sulfur oxides, in particular sulfur dioxide, and / or an absorbent of hydrogen halides, in particular hydrogen chloride and / or hydrogen fluoride.
    The materials contained as absorbent material in the composition according to the invention may advantageously be calcium-containing materials, materials containing calcium and magnesium, and / or magnesium-containing materials. Examples of calcium-containing materials include limestone, quicklime, and hydrated lime. Examples of materials containing calcium and magnesium include raw dolomite (dolomite), dolomitic quicklime, and dolomitic hydrated lime. Examples of magnesium-containing materials include magnesium carbonate, magnesium oxide, and magnesium hydroxide.
    Preferably, the absorbent material contained as a powder in the composition according to the invention is chosen from the group consisting of limestone, quicklime, hydrated lime, raw dolomite (dolomite), dolomitic quicklime, dolomitic hydrated lime, magnesium carbonate, magnesium oxide, magnesium hydroxide, and mixtures thereof. More preferably, the absorbent material contained in the form of a powder in the composition according to the invention is selected from the group consisting of quicklime, hydrated lime, dolomitic quicklime, dolomitic hydrated lime, oxide magnesium, magnesium hydroxide, and mixtures thereof. Most preferably, the absorbent material contained as a powder in the composition according to the invention is hydrated lime. The use of the abovementioned materials, alone or in the form of a combination, proves to be advantageous for the
    The fluidity of the resulting composition and / or the absorbency of the composition, in particular for the absorption capacity of HF. These advantageous effects are particularly pronounced for hydrated lime as an absorbent material.
    The hydrated lime used according to the invention is also called slaked lime, and it contains mainly Ca (OH) 2. Preferably, the hydrated lime of the invention contains more than 90% by weight, more preferably more than 93% by weight, more preferably more than 95% by weight, more preferably more than 97% by weight, more preferably more than 99% by weight. % by weight of Ca (OH) 2 relative to the weight of the hydrated lime in the composition. In addition to Ca (OH) 2, the hydrated lime may contain impurities, in particular impurities derived from SiO 2, Al 2 O, Al 2 O 3, iron oxides such as Fe 2 O 3, MgO, MnO, P 2 O 5, K 2 O, CaSO 4, and or S03. Preferably, the hydrated lime according to the invention contains less than 10% by weight, better still less than 7% by weight, better still less than 5% by weight, better still less than 3% by weight, better still less than 1% by weight. % by weight of the impurities listed above, relative to the weight of the hydrated lime in the composition.
    Similarly, calcium-containing materials, in particular limestone and quicklime, materials containing calcium and magnesium, in particular raw dolomite (dolomite), dolomitic quicklime, and dolomitic hydrated lime, and Magnesium-containing materials, especially magnesium carbonate, magnesium oxide, and magnesium hydroxide, may contain the impurities mentioned above in the amounts mentioned above.
    In addition to the impurities of the hydrated lime mentioned above, the hydrated lime according to the invention may also contain impurities containing calcium, in particular CaO and / or CaCO 3. The calcium oxide impurities in the hydrated lime may be due to insufficient hydration of the quicklime as the starting material. The impurities of calcium carbonate type in the hydrated lime can come either from the initial limestone from which the hydrated lime according to the invention is derived, or from a partial carbonation reaction of the hydrated lime with air. The calcium oxide content of the hydrated lime according to the invention is preferably less than 5% by weight, better still less than 3% by weight, better still less than 2% by weight, better still less than 1% by weight. relative to the weight of the hydrated lime in the composition. The calcium carbonate content of the hydrated lime according to the invention is preferably less than 15% by weight, more preferably less than 10% by weight, better still less than 6% by weight, better still less than 4% by weight. relative to the weight of the hydrated lime in the composition.
    The size of the absorbent material particles in the composition, in particular the d 50 value of the absorbent material, should be small. Preferably, the absorbent material has a particle size d50 of less than 50 μm, more preferably less than 40 μm, or less than 30 μm, or less than 20 μm, or less than 10 μm. Optimum results are obtained when hydrated lime having a particle size of less than 50 μm, preferably less than 40 μm, or less than 30 μm, or less than 20 μm, is used as the absorbent material in the composition. or less than 10 μm. As the absorbent material in the composition, a hydrated lime having a d50 value of less than 10 μm is particularly preferred. Advantageously, the absorbent material, in particular the hydrated lime, has a DCi particle size dg7 of less than 150 μπι, in particular less than 140 μπι, or less than 130 μπι, or less than 120 μπι, or less than 110 μπι, or less than 100 μπι, or less than 90 μπι.
    The dso value of the particles of the powder may for example be determined by determining the particle size distribution of the powder. The size for which 50% of the powder will pass through a theoretical opening of a sieve, determined from the particle size distribution, is commonly called the dso value. Therefore, the size for which 97% of the powder will pass through a Theoretical opening of a sieve, determined from the particle size distribution, is commonly referred to as the dg7 value. One skilled in the art knows various methods for determining the particle size distribution. For example, the particle size distribution can be determined by sieving experiments. For example, the particle size distribution can also be determined by laser diffraction, particularly in accordance with ISO 13320: 2009. In the determination of the particle size distribution of a powder by laser diffraction, the powder under study can be suspended in a liquid medium, for example in ethanol, and the suspension can be subjected to at an ultrasound treatment, for example for 120 seconds, followed by a pause for example of 120 seconds. The suspension can also be stirred, for example at 70 rpm. The particle size distribution can then be determined by plotting the measurement results, in particular the cumulative sum of the mass percentage of the measured particle sizes as a function of the measured particle sizes. The dso value and / or the dg7 value can then be determined from the particle size distribution. For the determination of the particle size distribution and / or the dso value and / or
    For example, the dg7 value of a powder by laser diffraction may be employed by a Helos particle size analyzer available from Sympatec, which uses the additional Sucell dispersing equipment.
    It has also been found to be advantageous for the absorbent material to have a large surface area. A composition containing an absorbent material having a specific surface area equal to or greater than 20 m 2 / g, preferably equal to or greater than 30 m 2 / g, or equal to or greater than 40 m 2 / g, equal to or greater than 45 m 2 / g, is particularly effective for the purification of flue gas. Optimum results are obtained in particular in the purification of flue gas when hydrated lime with a specific surface area equal to or greater than 20 m 2 / g, preferably at least 20 m 2 / g, is used as absorbent material in the composition. 30 m2 / g, or equal to or greater than 40 m2 / g, or equal to or greater than 45 m2 / g.
    The specific surface of the materials described here, in particular the absorbent material, refers in particular to the specific surface, more particularly to the BET specific surface (Brunauer, Emmet, Teller). Methods for determining the surface area of a material are known to those skilled in the art. For example, the surface area can be determined by nitrogen adsorption measurements of a preferably dried sample and evacuated to 77 K in accordance with the BET multipoint method. For this purpose, for example, a device of the Micromeritics ASAP 2010 type can be used. In particular, the BET specific surface area can be determined in accordance with DIN ISO 9277, in particular according to DIN ISO 9277: 2014-01, in particular using the static volumetric determination method and in particular the multipoint analysis method. bti
    Also the specific pore volume of the absorbent material is preferably important. This is particularly useful for obtaining compositions having good sulfur oxide uptake and / or good flowability. In addition, this is advantageous for the absorbency of the composition. Therefore, the composition preferably contains an absorbent material having a specific pore volume equal to or greater than 0.11 cm 3 / g or equal to or greater than 0.12 cm 3 / g or equal to or greater than 0.13 cm 3 / g or equal or greater than 0.14 cm3 / g or greater than or equal to 0.15 cm3 / g or greater than or equal to 0.16 cm3 / g or greater than or equal to 0.17 cm3 / g or greater than or equal to 0.18 cm3 / g or equal to or greater than 0.19 cm3 / g or equal to or greater than 0.2 cm3 / g. Optimum results are obtained by using, as absorbent material in the composition, hydrated lime having a specific pore volume equal to or greater than 0.11 cm 3 / g or equal to or greater than 0.12 cm 3 / g or equal to greater than 0.13 cm3 / g or greater than or equal to 0.14 cm3 / g or greater than or equal to 0.15 cm3 / g or greater than or greater than 0.16 cm3 / g or greater than or equal to 0.17 cm3 / g or equal to or greater than 0.18 cm3 / g or equal to or greater than 0.19 cm3 / g or equal to or greater than 0.2 cm3 / g. It has been found that compositions containing an absorbent material having a large pore volume, in particular a pore volume as indicated above, have improved properties especially with respect to their melt flow values, more particularly as regards their FFC values.
    The specific pore volume described herein refers in particular to the total specific pore volume, preferably pore diameter less than 100 nm, determined by BJH (Barrett, Joyner, Halenda), that is, supporting a geometry of cylindrical pores. Advantageously, the specific porous volume DE of the absorbent material, in particular the specific pore volume determined according to BJH, can represent more than 50% by volume, preferably more than 55% by volume, better still more than 60% by volume, relative to the total pore volume, the partial pore volume of pores with a diameter of 10 to 40 nm, determined according to BJH. Methods for determining the specific pore volume of a material are known to those skilled in the art. For example, the specific pore volume can be determined by nitrogen desorption measurements of a preferably dried sample and evacuated to 77 K. The data obtained in this way can preferably be analyzed according to the method BJH, c. i.e. assuming a cylindrical pore geometry. For this purpose, for example, a device of the Micromeritics ASAP 2010 type can be used. In particular, the specific pore volume determined according to BJH can be determined in accordance with DIN 66134, in particular according to DIN 66134: 1998- 02, in particular using the volumetric determination method.
    Methods for making hydrated lime useful in the present invention are known to those skilled in the art. For example, WO 97/14650 A1 discloses processes for the manufacture of hydrated lime usable in the present invention.
    According to another embodiment of the invention, the composition contains clay and / or activated carbon and / or zeolites in an amount of up to 30% by weight relative to the total weight of the composition. This helps in particular to obtain an effective composition in the purification of flue gas, in particular of flue gas also containing metals
    Heavy DEZ and / or organic pollutants such as dioxins.
    In addition to the composition, the invention also provides methods for the manufacture of the composition for the purification of flue gas.
    The processes for the manufacture of the composition for purifying flue gas according to the invention basically comprises the following steps: a. have a composition containing, in each case relative to the total weight of the composition: 35 to 99% by weight of a powder of an alkali metal salt of carbonic acid, and 1 to 65% by weight of a powder of absorbent material; and B. apply mechanical and / or thermal energy to the composition; wherein said powder of said absorbent material has a specific pore volume that is equal to or greater than 0.1 cm3 / g.
    The steps can be performed in any desired order. Preferably, the steps are performed in the order indicated above.
    According to one embodiment of the manufacturing method of the invention, the composition in step a. contains 35 to 90% by weight, in particular 35 to 80% by weight, or 35 to 70% by weight, or 35 to 60% by weight, or 35 to 50% by weight of said alkali metal salt powder of carbonic acid, relative to the total weight of the composition.
    According to another embodiment of the manufacturing method of the invention, the composition in step a. ac.e contains 10 to 65% by weight, in particular 20 to 65% by weight or 30 to 65% by weight or 40 to 65% by weight or 50 to 65% by weight of said powder of said absorbent material, relative to total weight of the composition.
    With regard to the alkali metal salt of carbonic acid and / or the absorbent material of the manufacturing method according to the invention, the above provisions concerning the alkali metal salt of carbonic acid and / or the absorbent material , respectively, will apply. In particular, the provisions concerning the particle size and / or the type of material used for the alkali metal salt of carbonic acid and / or the provisions concerning the type of material used for the absorbent material, the particle size, the specific surface and / or the pore volume of the absorbent material as described above, will apply. In addition, the provisions concerning the fluidity values, in particular the FFC values, of the composition as described above will apply.
    According to one embodiment of the manufacturing method according to the invention, a thermal and / or mechanical energy is applied to said powder of an alkali metal salt of carbonic acid and / or to said powder of an absorbent material. This confers more flexibility in the preparation of the composition according to the invention. The thermal energy may, for example, be applied by heating the powders and / or compositions, for example by heating, for example in an oven, or by irradiation with a suitable irradiation source such as a radiant heater. The mechanical energy can be applied to the powders and / or compositions in different forms. For example, mechanical energy can be applied by fragmentation, grinding and / or grinding. For this purpose, suitable devices such as ball mills, jet mills, grinders, pin mills, or roll mills can advantageously be used. However, the mechanical energy can also be applied to the powders and / or compositions by mixing the powders and / or compositions by means of a mixer. Suitable mixers may include paddle mixers, rotor mixers, paddle mixers, ribbon mixers, jet mixers, and / or screw mixers. The application of mechanical energy may also comprise several steps, for example a first step of fragmentation, grinding and / or grinding, and a second mixing step.
    According to another embodiment of the manufacturing method according to the invention, step b. comprises a step of mixing and / or grinding. In this way, the agglutination of the alkali metal salt of carbonic acid on the grinding equipment can be minimized. In addition, a very homogeneous composition can be obtained.
    Optimum results are obtained in the manufacturing method according to the invention when step b. comprises a grinding step in which the composition is milled to a particle size d50 equal to or less than 50 μm, in particular less than 45 μm or less than 40 μm or less than 35 μm or less than 30 μm or less than 25 μm or less; at 20 pm or less than 15 pm or less than 12 pm. Advantageously, the composition is milled to a particle size dg7 of less than 180 μm, in particular less than 170 μm or less than 160 μm, or less than 150 μm, or less than 145 μm, or less than 140 μm. This can directly give a usable composition that can also be stored. This can also help reduce agglutination of the grinding charge on the grinding equipment.
    In addition, the invention also provides a method for the purification of flue gas. In the process for purifying flue gas according to the invention, the flue gas is brought into contact with the composition according to the invention.
    The composition according to the invention can be used for different purposes. Ideally, the composition according to the invention is used for the purification of flue gases, preferably for the purification of flue gas containing sulfur oxides and / or HF.
    In addition, the invention provides the use of a powder of an absorbent material having a specific pore volume that is equal to or greater than 0.1 cm 3 / g, to improve fluidity, particularly after a certain time. storage, and / or the storage ability and / or the HF absorption capacity of a powder of an alkali metal salt of carbonic acid having a d.sub.2 particle size of less than 50 .mu.m, in particular less than 45. pm or less than 40 pm. Preferably, the alkali metal salt of carbonic acid is sodium hydrogencarbonate and / or sodium sesquicarbonate. The use according to the invention of the absorbent material can give compositions having a particularly balanced property profile with regard to the absorption capacity of the sulfur oxides and the fluidity, in particular after a certain storage time.
    According to one embodiment of the use of the powder of an absorbent material according to the invention, the powder of the absorbent material is used in an amount of 1 to 65% by weight, in particular from 10 to 65% by weight or from 20 to 65% by weight or from 30 to 65% by weight or from 40 to 65% by weight or from 50 to 65% by weight relative to the total weight of the composition.
    As regards the absorbent material for use of the powder of an absorbent material according to the invention, the provisions concerning the absorbent material will apply. In particular, the provisions concerning the type of material used for the absorbent material, the particle size, the specific surface area and / or the pore volume of the absorbent material as described above will apply.
    Figure 1 shows the relative SO2 uptake (referred to as SO2 reduction) as a function of the comminuted sodium hydrogen carbonate fraction for different absorbent compositions having different levels of sodium hydrogencarbonate and hydrated lime.
    Figure 2 shows the dependence of the FFC value of fresh samples of absorbent compositions and 18 hour old samples of absorbent compositions for different fractions of sodium hydrogencarbonate and hydrated lime, respectively.
    In the following, the invention will be further explained by examples which are illustrative only and should not be construed as limiting in any way.
    Used materials
    Btz
    Sodium hydrogencarbonate, NaHCO3 (Bicar, Solvay); hydrated lime Ca (OH) 2, (Sorbacal SP, Lhoist). Sorbacal SP has a BET specific surface area of about 40 m 2 / g, a specific BJH pore volume of about 0.2 cm 3 / g, and a d50 particle size of about 6 μm.
    Example 1
    Preparation of compositions for the purification of flue gas
    Sodium hydrogencarbonate was ground using a pin mill to obtain a powder having a d50 value of 28.9 μm, as determined by laser light scattering in an ethanolic suspension using a Sympatec Helos particle analyzer. . The particle size analyzer has Sucell equipment, and the sample is subjected to sonication for 120 seconds with a pause of 120 seconds, and the suspension is agitated at 70 rpm. The ground sodium hydrogencarbonate is then homogeneously mixed with hydrated lime in the proportions indicated in Table 1 to obtain compositions for the purification of flue gas. The mixing of the powders is carried out using a rotor mixer.
    Table 1
    Proportions of the compositions for the purification of flue gas
    LDi
    Example 2 Determination of SO2 Absorption Potency
    The SO 2 absorption capacity of compositions 4 and 5 and comparative composition 3 is determined in a pilot flue gas treatment plant which is mainly described in WO 2007/000433 A2, pages 10 to 12 on the Figure 2 of this document. The cocurrent flow compositions are injected to purify a model flue gas under the following gas conditions:
    Temperature 220 ° C,
    Concentration of SO2 at the entry 1500 mg / Nm3,
    10% H2O content,
    CO2 concentration 9%,
    Average stoichiometric ratio of the SO 2 absorbent composition (based on entry) of 2.5.
    The results of the SO 2 absorption tests are compiled in Table 2 and presented in FIG. 1 together with the results for the pure hydrated lime and the composition 3 containing 75% by weight of hydrated lime and 25% by weight of hydrogencarbonate. of sodium, serving as comparative examples.
    Table 2
    During the test, there is no abnormal blockage or blockage of the dosing equipment. Thus, the dosing device is not affected by the presence of ground sodium hydrogencarbonate.
    In addition, the absorption capacity of the SO.sub.2 of the compositions 4 and 5 is significantly greater than that of the pure hydrated lime and also of the composition 3 containing 75% by weight of hydrated lime and 25% by weight of sodium hydrogen carbonate.
    Example 3
    Fluidity of the compositions
    The fluidity of compositions 4 and 5 and comparative compositions 1 to 3 and pure hydrated lime as a comparative example are investigated by determining their FFC values using an RST-XS annular shear tester. The results are shown in Figure 2 and using diamonds for the FFC values of samples of the freshly prepared composition and squares for the FFC values of samples measured 18 hours after preparation of the compositions. As already mentioned, higher FFC values indicate better fluidity. From Figure 2, one can see the beneficial effect of hydrated lime mixture to sodium hydrogencarbonate powder on fluidity after 18 hours. For the freshly prepared comparative compositions 1, 2 and 3, no significant trend is observed. For the freshly prepared compositions 4 and 5, the hydrated lime mixture reduces the fluidity, as can be seen from the reduced FFC value of composition 4 containing 50% by weight of hydrated lime, compared with the FFC value. higher of the composition containing 25% by weight of hydrated lime. However, after 18 hours, it is observed that the FFC values of the compositions decrease relative to the FFC values of the corresponding freshly prepared compositions. Surprisingly, it is observed that after 18 hours the FFC value of the composition 4 containing 50% by weight of hydrated lime is greater than the FFC value of the composition containing 25% by weight of hydrated lime. This indicates that the decrease in fluidity of the mixture over time depends on the ratio of hydrated lime to sodium hydrogencarbonate. A composition with a particularly well-balanced property profile is obtained when the sodium hydrogencarbonate is present in an amount of about 35 to 50% by weight based on the total weight of the composition.
    权利要求:
    Claims (20)
    [1]
    1. Composition for the purification of flue gas, said composition containing, in each case with respect to the total weight of the composition: a. 35 to 99% by weight of a powder of an alkali metal salt of carbonic acid; and B. 1 to 65% by weight of a powder of an absorbent material; wherein said powder of said absorbent material has a specific pore volume which is equal to or greater than 0.1 cm3 / g.
    [2]
    2. A composition according to claim 1, which composition contains 35 to 90% by weight, in particular 35 to 80% by weight or 35 to 70% by weight or 35 to 60% by weight or 35 to 50% by weight of said powder. an alkali metal salt of carbonic acid, based on the total weight of the composition; and / or which composition contains 10 to 65% by weight, in particular 20 to 65% by weight or 30 to 65% by weight or 40 to 65% by weight or 50 to 65% by weight of said absorbent material powder, by relative to the total weight of the composition.
    [3]
    The composition of claim 1 or 2, wherein said powder of said alkali metal salt of carbonic acid has a d.sub.50 particle size of less than 50 .mu.m, in particular less than 45 .mu.m or less than 40 .mu.m or less than 35 .mu.m or less. at 30 pm or less than 25 pm or less than 20 pm or less than 15 pm or less than 12 pm; and / or wherein said powder of said alkali metal salt of carbonic acid has a particle size d97 of less than 180 μm, in particular less than 170 μm or less than 160 μm or less than 150 μm or less than 140 μm or less than 125 μm. pm.
    [4]
    4. A composition according to any one of the preceding claims wherein said alkali metal salt of carbonic acid is selected from the group consisting of sodium hydrogencarbonate, sodium carbonate, sodium sesquicarbonate, hydrogen carbonate, and the like. of potassium, potassium carbonate, potassium sesquicarbonate, and mixtures thereof.
    [5]
    A composition according to any one of the preceding claims, wherein said alkali metal salt of carbonic acid is sodium hydrogencarbonate and / or sodium sesquicarbonate.
    [6]
    6. Composition according to any one of the preceding claims, wherein said absorbent material is selected from the group consisting of limestone, quicklime, hydrated lime, raw dolomite (dolomite), dolomitic quicklime, lime. dolomitic hydrate, magnesium carbonate, magnesium oxide, magnesium hydroxide, and mixtures thereof.
    [7]
    The composition of any of the preceding claims, wherein said absorbent material is hydrated lime.
    [8]
    A composition according to any one of the preceding claims, wherein said absorbent material, in particular said hydrated lime, has a particle size d50 of less than 50 μm, in particular less than 40 μm, or less than 30 μm, or less than 20 μm. pm, or less than 10 pm; and / or wherein said absorbent material, in particular said hydrated lime, has a particle size dg7 of less than 150 μm, in particular less than 140 μm, or less than 130 μm, or less than 120 μm, or less than 110 μm, or less than 100 μιη, or less than 90 μιη; and / or wherein said absorbent material, in particular said hydrated lime, has a specific surface area equal to or greater than 20 m 2 / g, in particular equal to or greater than 30 m 2 / g, or equal to or greater than 40 m 2 / g, or equal to or greater than 45 m2 / g; and / or wherein said absorbent material, in particular said hydrated lime, has a specific pore volume equal to or greater than 0.11 cm 3 / g or equal to or greater than 0.12 cm 3 / g or equal to or greater than 0.13 cm 3 / g or greater than or equal to 0.14 cm3 / g or greater than or equal to 0.15 cm3 / g or greater than or equal to 0.16 cm3 / g or equal to or greater than 0.17 cm3 / g or equal to or greater than at 0.18 cm3 / g or equal to or greater than 0.19 cm3 / g or equal to or greater than 0.2 cm3 / g.
    [9]
    9. Composition according to any one of the preceding claims, which composition contains clay and / or activated carbon and / or zeolites in an amount of up to 30% by weight relative to the total weight of the composition.
    [10]
    Composition according to any one of the preceding claims, which composition has a flow value, in particular a FFC value, in particular determined by using an RST-XS ring shear tester, of 0.2 or more, in 0.3 or more, or 0.4 or more, or 0.5 or more, or 0.6 or more, or 0.7 or more, or 0.8 or more, or 0.9 or more, or 1.0 or more, or 1.1 or more, or 1.2 or more, or 1.3 or more.
    [11]
    A process for the manufacture of a composition for the purification of flue gas according to claims 1 to 10, comprising the steps of: a. have a composition containing, in each case relative to the total weight of the composition: 35 to 99% by weight of a powder of an alkali metal salt of carbonic acid, and 1 to 65% by weight of a powder of absorbent material; and B. apply mechanical and / or thermal energy to the composition; wherein said powder of said absorbent material has a specific pore volume that is equal to or greater than 0.1 cm3 / g.
    [12]
    The method of claim 11, wherein the composition in step a. contains 35 to 90% by weight, in particular 35 to 80% by weight or 35 to 70% by weight or 35 to 60% by weight or 35 to 50% by weight of said powder of an alkali metal salt of acid carbonic, based on the total weight of the composition; and / or wherein the composition in step a. contains 10 to 65% by weight, in particular 20 to 65% by weight or 30 to 65% by weight or 40 to 65% by weight or 50 to 65% by weight of said absorbent material powder, relative to the total weight of the composition.
    [13]
    The method of any of claims 11 and 12, wherein said powder of said alkali metal salt of carbonic acid is as defined in any one of claims 3 to 5 and / or said powder of said absorbent material is as defined in any one of claims 6 to 8.
    [14]
    The method according to any one of claims 11 to 13, wherein thermal and / or mechanical energy is applied to said alkali metal salt powder of carbonic acid and / or said absorbent material powder. .
    [15]
    The method of any one of claims 11 to 14, wherein step b. comprises a step of mixing and / or grinding, and possibly in which, in the grinding stage, the composition is milled to a particle size dso equal to or less than 50 μm, in particular less than 45 μm or less than 40 μm, or less than 35 pm or less than 30 pm or less than 25 pm or less than 20 pm or less than 15 pm or less than 12 pm; and / or wherein the composition is milled to a particle size ά less than 180 μm, in particular less than 170 μm or less than 160 μm or less than 150 μm or less than 140 μm or less than 125 μm.
    [16]
    16. A composition for the purification of a flue gas obtainable by the process according to any one of claims 11 to 15.
    [17]
    17. A process for the purification of flue gas, wherein the flue gas is contacted with a composition according to any of claims 1 to 10 and 16.
    [18]
    18. Use of a composition according to any one of claims 1 to 10 and 16 for purifying flue gas, in particular flue gas containing sulfur oxides and / or HF.
    [19]
    19. Use of a powder of an absorbent material having a specific pore volume equal to or greater than 0.1 cm 3 / g to improve fluidity, particularly after a certain storage time, and / or storage ability and / or the HF absorption capacity of a powder of an alkali metal salt of carbonic acid having a particle size d50 of less than 50 μm, in particular less than 45 μm or less than 40 μm.
    [20]
    20. Use according to claim 19, wherein said powder of said absorbent material is used in an amount of 1 to 65% by weight, especially 10 to 65% by weight or 20 to 65% by weight or 30 to 65% by weight. % by weight or from 40 to 65% by weight or from 50 to 65% by weight relative to the total weight of the composition; and / or wherein said powder of said absorbent material is as defined in any one of claims 6 to 8; and / or wherein said alkali metal salt of carbonic acid is sodium hydrogencarbonate and / or sodium sesquicarbonate.
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    同族专利:
    公开号 | 公开日
    EP3397373A1|2018-11-07|
    EP3187243A1|2017-07-05|
    BR112018013255A2|2018-12-04|
    CL2018001751A1|2018-10-05|
    FR3046363B1|2021-06-04|
    SG11201805663RA|2018-07-30|
    JP2019502551A|2019-01-31|
    WO2017114819A1|2017-07-06|
    BE1023883A1|2017-09-04|
    US20190015778A1|2019-01-17|
    CN108602011A|2018-09-28|
    FR3046363A1|2017-07-07|
    KR20180114012A|2018-10-17|
    JP2021035674A|2021-03-04|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    EP0190416A3|1984-11-30|1988-07-27|Waagner-Biro Aktiengesellschaft|Process for separating pollutants from combustion gases|
    BE1009692A3|1995-10-19|1997-07-01|Lhoist Rech & Dev Sa|PARTICLE Ca 2.|
    JP3948075B2|1997-10-01|2007-07-25|旭硝子株式会社|Acid component removal agent and acid component removal method|
    JPH11165036A|1997-12-04|1999-06-22|Abb Kk|Dual alkali treatment of exhaust gas from incinerator|
    US6352653B1|1998-11-26|2002-03-05|Asahi Glass Company Ltd.|Acid component-removing agent, method for producing it and method for removing acid components|
    JP3828008B2|2001-12-20|2006-09-27|上田石灰製造株式会社|Acid gas absorbent|
    DE20210008U1|2002-04-16|2002-10-24|Walhalla Kalk Gmbh & Co Kg|Exhaust gas cleaning reagents|
    JP4581682B2|2004-12-27|2010-11-17|旭硝子株式会社|Reduction method of dioxins in fly ash of garbage incineration equipment|
    WO2006113301A1|2005-04-19|2006-10-26|Carmeuse North America Services, Inc.|Method for producing activated lime for removal of acid gases from a combustion gas|
    BE1016661A3|2005-06-28|2007-04-03|Lhoist Rech & Dev Sa|PULVERULENT LIME COMPOSITION, METHOD FOR MANUFACTURING THE SAME, AND USE THEREOF|
    JP2009507632A|2005-09-15|2009-02-26|ソルベイ・ケミカルズ・インコーポレーテッド|Removal of sulfur trioxide from exhaust gas stream|
    WO2007135823A1|2006-05-19|2007-11-29|Asahi Glass Company, Limited|Method of removing halogen gas and remover for halogen gas|
    CN101773768A|2010-03-16|2010-07-14|长春惠工净化工业有限公司|Dechlorinating agent used for removing HCl from gas by dry method and preparation method thereof|
    JP5691211B2|2010-03-25|2015-04-01|栗田工業株式会社|Combustion exhaust gas treatment method|
    KR20130050668A|2011-11-08|2013-05-16|주식회사 포스코|Method for removal of sulfur oxides in exhausted gas using the high activity calciumhydrooxide|
    JP5991677B2|2012-09-24|2016-09-14|三菱重工環境・化学エンジニアリング株式会社|Exhaust gas treatment equipment|
    CN104707469B|2015-03-18|2016-09-14|华北理工大学|A kind of preparation method of HCl scavenger|EP3678758A1|2017-09-06|2020-07-15|S.A. Lhoist Recherche Et Developpement|Process for treating flue gases in cds flue gas treatment|
    CN109908741A|2019-03-21|2019-06-21|上海环保工程成套有限公司|Inhibit to burn dioxin generating device and its application method in flue gas|
    法律状态:
    2017-12-13| FG| Patent granted|Effective date: 20170905 |
    优先权:
    申请号 | 申请日 | 专利标题
    EP15203138.1A|EP3187243A1|2015-12-30|2015-12-30|Composition for the purification of flue gas|
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