FR2788513A1 - Limewash preparation for injecting in a stream of fumes, comprises mixing water and quicklime in order to obtain a limewash with specified amount of dry material and grinding the limewash - Google Patents
Limewash preparation for injecting in a stream of fumes, comprises mixing water and quicklime in order to obtain a limewash with specified amount of dry material and grinding the limewash Download PDFInfo
- Publication number
- FR2788513A1 FR2788513A1 FR9900525A FR9900525A FR2788513A1 FR 2788513 A1 FR2788513 A1 FR 2788513A1 FR 9900525 A FR9900525 A FR 9900525A FR 9900525 A FR9900525 A FR 9900525A FR 2788513 A1 FR2788513 A1 FR 2788513A1
- Authority
- FR
- France
- Prior art keywords
- limewash
- lime
- milk
- quicklime
- mixing water
- 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.)
- Pending
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Classifications
-
- 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
- B01D53/38—Removing components of undefined structure
- B01D53/40—Acidic components
-
- 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
- B01D53/80—Semi-solid phase processes, i.e. by using slurries
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2/00—Lime, magnesia or dolomite
- C04B2/02—Lime
- C04B2/04—Slaking
- C04B2/045—After-treatment of slaked lime
Abstract
Description
-Jl La présente invention est relative à un procédé pour préparer un laitThe present invention relates to a process for preparing a milk.
deof
chaux en vue de son injection dans un flux de fumées. lime for injection into a smoke stream.
On connaît déjà des produits et des procédés pour traiter des fumées tels que ceux décrits dans le document WO-97/14650-A, dans lequel est notamment décrit un procédé pour obtenir des particules d'hydroxyde de calcium séchées pré- Products and methods are already known for treating fumes such as those described in document WO-97/14650-A, in which is described in particular a method for obtaining pre-dried calcium hydroxide particles.
sentant en particulier une teneur en humidité inférieure à 2 % en poids. feeling in particular a moisture content of less than 2% by weight.
Selon ce procédé de l'art antérieur, on éteint des particules de chaux vive According to this process of the prior art, quicklime particles are quenched
(CaO) au moyen d'une quantité d'eau suffisante pour obtenir un hydroxyde de cal- (CaO) with sufficient water to obtain a cal-
cium [Ca(OH)2 présentant une humidité résiduelle comprise entre 15 et 30 % en poids; puis on sèche cet hydroxyde au moyen d'un gaz présentant une température inférieure à 500 0C et une teneur en gaz carbonique (CO2) inférieure à 500 mg/Nm3 pour abaisser son humidité résiduelle à moins de 2 % et on broie le produit séché pour obtenir une première fraction de particules présentant une granulométrie inférieure à 32 zim et une seconde fraction de particules présentant une granulométrie supérieure à 32 pim, le pourcentage en poids de refus à 32 lm étant compris entre 10 et 90. Un tel produit broyé peut être utilisé pour traiter des cium [Ca (OH) 2 having a residual humidity of between 15 and 30% by weight; then this hydroxide is dried by means of a gas having a temperature of less than 500 ° C. and a carbon dioxide (CO2) content of less than 500 mg / Nm3 in order to reduce its residual humidity to less than 2% and the dried product is ground to obtaining a first fraction of particles having a particle size less than 32 μm and a second fraction of particles having a particle size greater than 32 μm, the percentage by weight of refusal at 32 μm being between 10 and 90. Such a ground product can be used to deal with
fumées par injection des particules dans le flux de fumées. smoke by injecting particles into the smoke stream.
Un tel procédé conduit à un produit pulvérulent qui présente les inconvé- Such a process leads to a pulverulent product which has the disadvantages
nients inhérents aux poudres et est grand consommateur d'énergie notamment nents inherent in powders and is a large consumer of energy in particular
pendant la phase de séchage.during the drying phase.
Aussi un des buts de la présente invention est-il de fournir un procédé pour préparer un lait de chaux qui permet d'obvier les inconvénients de l'art antérieur One of the aims of the present invention is therefore to provide a process for preparing a whitewash which overcomes the drawbacks of the prior art.
tels que ceux cités ci-dessus.such as those cited above.
Un autre but de la présente invention est de fournir un tel procédé qui peut Another object of the present invention is to provide such a method which can
être mis en ceuvre in situ.be implemented in situ.
Ces buts, ainsi que d'autres qui apparaîtront par la suite, sont atteints par un procédé pour préparer un lait de chaux qui est caractérisé, selon la présente invention, par le fait que l'on prépare un lait de chaux ayant une teneur en chaux de à 600 g de matière sèche par litre de lait de chaux en mélangeant de l'eau et These aims, as well as others which will appear subsequently, are achieved by a process for preparing a milk of lime which is characterized, according to the present invention, by the fact that a milk of lime having a content of lime from to 600 g of dry matter per liter of milk of lime by mixing water and
de la chaux vive (CaO) et que l'on broie ce lait de chaux. quicklime (CaO) and grind this milk of lime.
De préférence, la teneur en chaux du lait de chaux est comprise entre 100 et Preferably, the lime content of milk of lime is between 100 and
250 g de matière sèche par litre de lait de chaux. 250 g of dry matter per liter of lime milk.
Avantageusement, on additionne l'eau ou la chaux d'un retardateur de réac- Advantageously, water or lime is added to a reaction retarder.
tivité tel que l'éthylène-glycol, la mono-, bi- ou tri-éthanolamine, à raison d'au plus activity such as ethylene glycol, mono-, bi- or tri-ethanolamine, at a rate of at most
2 % en poids de celui-ci par rapport au poids de chaux. 2% by weight thereof relative to the weight of lime.
2 27885132 2788513
De préférence, on crible auparavant la chaux vive pour en éliminer les fines Preferably, the quicklime is screened beforehand to remove the fines.
particules de granulométrie inférieure à 2 mm. particle size less than 2 mm.
Avantageusement, les particules de chaux éteintes [Ca(OH)2J dans le lait de chaux ont une granulométrie inférieure à 200 pm et préférentiellement inférieure à 20 pm. Selon le procédé de la présente invention, on crible de la chaux vive (CaO) afin d'en éliminer les fines particules incuites et/ou surcuites, c'est-à-dire celles constituées de carbonate de chaux (CaCO3), qui ne pourront être éliminées par la Advantageously, the slaked lime particles [Ca (OH) 2J in the milk of lime have a particle size less than 200 μm and preferably less than 20 μm. According to the process of the present invention, quicklime (CaO) is screened in order to remove the fine particles which have been induced and / or overcooked, that is to say those made up of lime carbonate (CaCO3), which do not may be eliminated by the
suite: ces particules ont en général une grande granulométrie inférieure à 2 mm. continued: these particles generally have a large particle size of less than 2 mm.
Puis, on ajoute de l'eau qui peut être additionnée d'un retardateur de réactivité à une concentration d'au plus 2 % en poids par rapport au poids de chaux, tel que par exemple de l'éthylène-glycol, la mono-, bi- ou tri-éthanolamine sans que cette énumération soit limitative. L'additif est ajouté dans l'eau d'hydratation ou même à la chaux vive. La concentration de l'additif peut être inférieure à 1% et de Then, water is added which can be added with a reactivity retarder at a concentration of at most 2% by weight relative to the weight of lime, such as for example ethylene glycol, the mono- , bi- or tri-ethanolamine without this list being limiting. The additive is added to the water of hydration or even to quicklime. The concentration of the additive may be less than 1% and
préférence de 0,5 % en poids par rapport au poids de chaux vive. preferably 0.5% by weight relative to the weight of quicklime.
Dans le lait de chaux ainsi obtenu, le volume poreux total de la chaux éteinte In the milk of lime thus obtained, the total pore volume of the slaked lime
[Ca(OH)j est supérieur à 0,15 cm3/g et même à 0,25 cm3/g. [Ca (OH) j is greater than 0.15 cm3 / g and even more than 0.25 cm3 / g.
Le mélange ainsi obtenu, ou lait de chaux, comprend de 100 à 600 g de matière sèche par litre de lait de chaux, et de préférence de 150 à 250 g de matière sèche par litre de lait de chaux. On agite l'ensemble pendant au moins 10 mn, et, The mixture thus obtained, or milk of lime, comprises from 100 to 600 g of dry matter per liter of milk of lime, and preferably from 150 to 250 g of dry matter per liter of milk of lime. The whole is stirred for at least 10 min, and,
si nécessaire, pendant 20 minutes.if necessary, for 20 minutes.
Puis on broie ce lait de chaux de telle sorte que les particules de chaux éteintes [Ca(OH)2] ont une granulométrie inférieure à 200 pm; en fait 80 % des particules présentent une granulométrie inférieure à 20 pm et même inférieure à Then this milk of lime is ground so that the slaked lime particles [Ca (OH) 2] have a particle size less than 200 μm; in fact 80% of the particles have a particle size less than 20 μm and even less than
10 pm selon l'intensité du broyage réalisé dans un broyeur du type broyeur à cou- 10 pm depending on the intensity of the grinding carried out in a grinder of the neck mill type
teaux par exemple.for example.
Le lait de chaux broyé peut être directement injecté dans un flux de fumées The ground lime milk can be directly injected into a smoke stream
afin de neutraliser les particules acides en suspension. in order to neutralize the acidic particles in suspension.
Le procédé selon la présente invention permet d'utiliser des chaux vives ayant une granulométrie supérieure à 2 mm, ce qui, comme le notera l'homme du métier, présente un avantage économique important. En effet, I'utilisation de telles chaux permet l'élimination par criblage à 500 pum ou 200 pm des particules incuites ou surcuites. Ainsi on peut obtenir un lait de chaux d'excellente qualité ayant une teneur élevée en chaux éteinte [Ca(OH)J, c'est à dire d'au moins 95 % en poids par rapport à la matière sèche, et une faible teneur en carbonate de calcium The method according to the present invention makes it possible to use quicklime having a particle size greater than 2 mm, which, as will be appreciated by those skilled in the art, has an important economic advantage. Indeed, the use of such lime allows elimination by screening at 500 pum or 200 pm of the incised or overcooked particles. Thus, it is possible to obtain an excellent quality lime milk having a high content of slaked lime [Ca (OH) J, that is to say at least 95% by weight relative to the dry matter, and a low content in calcium carbonate
3 27885133 2788513
(CaC03) c'est à dire d'au plus 1 % en poids par rapport à la matière sèche, à partir (CaC03) that is to say at most 1% by weight relative to the dry matter, from
d'une chaux vive plus fortement carbonatée. of a more strongly carbonated quicklime.
4 27885134 2788513
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9900525A FR2788513A1 (en) | 1999-01-19 | 1999-01-19 | Limewash preparation for injecting in a stream of fumes, comprises mixing water and quicklime in order to obtain a limewash with specified amount of dry material and grinding the limewash |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9900525A FR2788513A1 (en) | 1999-01-19 | 1999-01-19 | Limewash preparation for injecting in a stream of fumes, comprises mixing water and quicklime in order to obtain a limewash with specified amount of dry material and grinding the limewash |
Publications (1)
Publication Number | Publication Date |
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FR2788513A1 true FR2788513A1 (en) | 2000-07-21 |
Family
ID=9541000
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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FR9900525A Pending FR2788513A1 (en) | 1999-01-19 | 1999-01-19 | Limewash preparation for injecting in a stream of fumes, comprises mixing water and quicklime in order to obtain a limewash with specified amount of dry material and grinding the limewash |
Country Status (1)
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FR (1) | FR2788513A1 (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE965688C (en) * | 1951-07-14 | 1957-06-13 | Erich Kanert Dr Ing | Process for extinguishing quicklime with the recovery of purified hydrated lime |
DE3620024A1 (en) * | 1986-06-13 | 1987-12-17 | Fels Werke Peine Salzgitter | Process for preparing finely divided calcium hydroxide |
EP0313483A1 (en) * | 1987-10-23 | 1989-04-26 | Coatex S.A. | Grinding agent for lime to enhance its reactivity |
EP0327902A1 (en) * | 1988-02-11 | 1989-08-16 | Rheinische Kalksteinwerke GmbH. | Process for the production of dry highly disperse calcium hydroxide |
EP0367148A1 (en) * | 1988-10-28 | 1990-05-09 | FTU GmbH Forschung und technische Entwicklung im Umweltschutz | Agents and method for purifying gases and waste gases from heavy metals, and method of producing these agents |
WO1992009528A1 (en) * | 1990-11-21 | 1992-06-11 | Lhoist Recherche Et Developpement S.A. | Method for preparing calcium and/or magnesium hydroxide, and use thereof |
DE19542159A1 (en) * | 1995-11-11 | 1997-05-15 | Fels Werke Gmbh | Preparation of dry highly reactive calcium hydroxide |
-
1999
- 1999-01-19 FR FR9900525A patent/FR2788513A1/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE965688C (en) * | 1951-07-14 | 1957-06-13 | Erich Kanert Dr Ing | Process for extinguishing quicklime with the recovery of purified hydrated lime |
DE3620024A1 (en) * | 1986-06-13 | 1987-12-17 | Fels Werke Peine Salzgitter | Process for preparing finely divided calcium hydroxide |
EP0313483A1 (en) * | 1987-10-23 | 1989-04-26 | Coatex S.A. | Grinding agent for lime to enhance its reactivity |
EP0327902A1 (en) * | 1988-02-11 | 1989-08-16 | Rheinische Kalksteinwerke GmbH. | Process for the production of dry highly disperse calcium hydroxide |
EP0367148A1 (en) * | 1988-10-28 | 1990-05-09 | FTU GmbH Forschung und technische Entwicklung im Umweltschutz | Agents and method for purifying gases and waste gases from heavy metals, and method of producing these agents |
WO1992009528A1 (en) * | 1990-11-21 | 1992-06-11 | Lhoist Recherche Et Developpement S.A. | Method for preparing calcium and/or magnesium hydroxide, and use thereof |
DE19542159A1 (en) * | 1995-11-11 | 1997-05-15 | Fels Werke Gmbh | Preparation of dry highly reactive calcium hydroxide |
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