• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    This reactor (1) comprises an elongated trough (10), which defines a reactivation chamber (C) extending in a longitudinal direction (D) from a first end of the trough to a second end (10B) of the trough. trough. The reactor also comprises two shafts (20), which are arranged in the reactivation chamber and extend parallel thereto in the longitudinal direction, each of the two shafts comprising, successively, a first portion (20C) , provided with a propeller (21) conveying solids, a second portion (20D) provided with blades (23) for stirring solids, the length of the first portion (20C) representing between 10% and 33% of the sum of the respective lengths of the first and second parts. The reactor also comprises a chute (40) for distributing a gaseous reactivation fluid, which is arranged in the reactivation chamber at the bottom of the trough, which extends in the longitudinal direction from below the current. less the second portion of the two shafts, and which is provided with one or more orifices (42) for admission of the fluid into the reactivation chamber. This reactor is simple, economical and efficient, in particular for reactivating solids from the flue gas treatment.
    公开号:FR3060417A1
    申请号:FR1662483
    申请日:2016-12-15
    公开日:2018-06-22
    发明作者:Frank TABARIES；Bernard Siret
    申请人:LAB SA；
    IPC主号:
    专利说明:

    ® FRENCH REPUBLIC
    NATIONAL INSTITUTE OF INDUSTRIAL PROPERTY © Publication number:
    (to be used only for reproduction orders)
    ©) National registration number
    060 417
    62483
    COURBEVOIE © Int Cl 8 : B 01 J 20/34 (2017.01), B 01 J 8/10, B 02 C 4/02, 23/24, B 01 F 7/04, 3/06, B 01 D 53 / 83, 53/40
    A1 PATENT APPLICATION
    ©) Date of filing: 15.12.16.(© Priority: ©) Applicant (s): LAB SA - FR. ©) Date of public availability of the request: 06.22.18 Bulletin 18/25. @ Inventor (s): TABARIES FRANK and SIRET BERNARD. ©) List of documents cited in the preliminary search report: See the end of this booklet (© References to other related national documents: ®) Holder (s): LAB SA. ©) Extension request (s): (© Agent (s): LAVOIX. © SOLID REACTIVATION REACTOR.
    FR 3 060 417 - A1
    This reactor (1) comprises an elongated trough (10) which defines a reactivation chamber (C) extending in a longitudinal direction (D) from a first end of the trough to a second end (10B) of the 'trough. The reactor also comprises two shafts (20), which are arranged in the reactivation chamber and which extend therein parallel to each other in the longitudinal direction, each of the two shafts successively comprising a first part (20C) , provided with a propeller (21) for conveying solids, a second part (20D), provided with blades (23) for mixing solids, the length of the first part (20C) representing between 10% and 33% of the sum of the respective lengths of the first and second parts. The reactor also comprises a chute (40) for distributing a gaseous reactivation fluid, which is arranged in the reactivation chamber at the bottom of the trough, which extends in the longitudinal direction by running below at least minus the second part of the two shafts, and which is provided with one or more orifices (42) for admitting the fluid into the reactivation chamber. This reactor is simple, economical and efficient, in particular for reactivating solids from the treatment of smoke.

    Solid reactivation reactor
    The present invention relates to a reactor for reactivating solids by bringing them into contact with a reactive gas fluid.
    The field of application of the invention is mainly, but not exclusively, the purification of gases and fumes, in particular fumes emitted by combustion units, such as incinerators, power plants from electricity fossil fuels, cement kilns, petroleum refineries, etc.
    Indeed, many industrial activities generate fumes containing sulfur oxides, such as sulfur dioxide SO 2 , hydrochloric acid HCl and other acidic pollutants, which need to be treated before releasing the fumes to the atmosphere. To treat these various acidic pollutants contained in fumes, several methods are known and in common commercial use.
    First of all, there are the wet processes in which the fumes to be purified are brought into contact with a washing liquid which, by absorption, captures the acid pollutants and neutralizes them. Several technologies are available. While these wet processes are extremely efficient and produce comparatively little solid residue, they are rather costly in terms of investment.
    Then there are the dry processes in which an alkaline neutralizing reagent, such as lime, quicklime or sodium bicarbonate, is injected into the fumes to be treated in order to react with the acid pollutants to form salts. The products of this reaction, as well as the excess of reagent, that is to say the part of the reagent which has not reacted with the pollutants to be captured, are collected in a filter, for example a bag filter, or an electrostatic precipitator. These dry processes, which are lighter in investment, can suffer from significantly higher operating costs than those of wet processes, in particular if the reagent is misused. Indeed, an excess of reagent is always necessary for a thorough purification, which results in more costs for this reagent and especially for the treatment and the landfill of the solid residues captured by filtration.
    Attempts have been made to improve this situation with semi-dry processes in which the alkaline reagent is brought into contact with the fumes to be purified not in solid form, but in the form of a liquid or of a slurry, usually a milk of lime. On contact with hot smoke, the water from the aforementioned liquid or the aforementioned slurry evaporates, leaving in the end solid residues which are of a composition similar to that of the residues of dry processes and which are collected on a filter, example a bag filter or an electrostatic precipitator. This situation represents an improvement over dry systems because the temporary existence of a wet phase makes it possible to reduce the necessary excess of reagent, but, on the other hand, it limits the possible energy recovery. The quantity of reagents consumed is less, as is the quantity of residues produced. This also implies greater complexity since an atomization-evaporation device is essential to prepare the reagent to be brought into contact with the fumes to be purified.
    Attempts have also been made to reduce the quantity of reagents and residues produced in dry systems, by humidifying the reagent beforehand, for example by spraying water on lime in a screw or a drum, before contacting with hot fumes. This produces a kind of semi-dry process at low cost, which takes advantage of the surface humidification of the alkaline reagent.
    In all cases, the dry and semi-dry processes result in the collection, by filtration, of solids consisting of a mixture of alkaline reagent, which has not reacted with the acid pollutants of the treated fumes, and residues from the purification of these fumes. Attempts have been made to reactivate these solids with a view to recycling them as a neutralizing reagent in the fumes to be treated. The purpose of reactivating the residues is both to promote solid-solid reactions, to refresh the surface of the grains and to rewet locally, so as to facilitate the subsequent capture of acidic pollutants.
    In practice, it has thus been proposed to reactivate the recycled solids by spraying water. The reactivation process is difficult to carry out as soon as the solids are hygroscopic: if we admit too much water, the solids lump and become not very transportable, while if we do not put enough water, the process is not very effective.
    It has also been proposed to reactivate the recycled solids by exposing them to steam, as described in EP 1 716 910. This reactivation using water vapor is far preferable to reactivation by spraying with water. However, the implementation of a contactor, such as a fluidized bed, to expose the solids to be reactivated to steam poses problems and is quite expensive in terms of investment. From a process point of view, driving such a contactor can be tricky: if the solids are too humidified, they are subject to caking. They are therefore difficult to transport and can cause blockages or jams. Conversely, if the solids are too little humidified by the water vapor, their reactivation becomes insufficient. To address this problem, EP 1 949 956 proposed an improved reactivation reactor, ensuring a sufficient contact time, of at least a few minutes, between the solids to be reactivated and a gaseous reactivation fluid. However, here again, it has been noted that this type of reactor can be subject to blockage, in particular for large units.
    The object of the present invention is to propose a new reactivation reactor for solids by bringing them into contact with a gaseous reactivation fluid, which is both simple, economical and efficient.
    To this end, the subject of the invention is a reactivation reactor for solids, comprising:
    - an elongated trough, which defines a reactivation chamber extending in a longitudinal direction from a first end of the gauge to a second end of the gauge, this reactivation chamber having:
    - an inlet, which is located at the first end of the gauge and through which solids to be reactivated enter the reactivation chamber, and
    - an outlet, which is located at the second end of the gauge and through which the reactivated solids leave the reactivation chamber;
    - two shafts, which are arranged in the reactivation chamber and which extend therein parallel to each other in the longitudinal direction, each of the two shafts successively comprising:
    - a first part, which extends from the first end of the gauge towards the second end of the gauge and which is provided with a propeller for conveying solids, and
    - A second part, which extends from the second end of the trough towards the first end of the trough and which is provided with blades for mixing solids, the length of the first part representing between 10% and 33% of the sum of the respective lengths of the first and second parts; and
    - a chute for distributing a gaseous reactivation fluid, which is arranged in the reactivation chamber at the bottom of the trough, which extends in the longitudinal direction by running below at least the second part of the two shafts, and which is provided with one or more orifices for admitting the fluid into the reactivation chamber.
    When the reactor according to the invention is in service, its chute is supplied with a gaseous reactivation fluid, for example water vapor or a gaseous mixture containing water, so that this reactivation fluid reaches, via the orifice (s) of the chute, the solids contained in the bottom of the reactor trough. At the same time, the two reactor shafts, parallel and adjacent, ensure, thanks to their first part, the conveying of solids from the inlet of the reactivation chamber to the outlet of this chamber, the respective propellers of these first parts trees forming together, in a way, a double screw for transporting solids. The second respective parts of the two trees provide ventilation and a mixture of the solids pushed by the first parts of the trees, by mixing these solids with the respective blades of each of these second parts of the trees: bringing them into contact between these stirred solids and the gaseous fluid distributed by the chute is thus substantially facilitated, thereby significantly improving the reactivation of the solids. This effect is all the more marked since the invention provides that the length of the second parts of the trees represents between 67% and 90% of the sum of the respective lengths of the first and second parts: conversely, if the first part of the trees were extended further, if necessary until reaching the exit from the reactivation chamber, this first part of the trees would tend to compact the solids and therefore limit their contact with the reactive gas fluid, with the additional risks of clumping, this compaction of solids which can become such that the trees become blocked. In other words, the arrangement of the two shafts and the chute of the reactivation reactor according to the invention, which is provided so that the respective second parts of the two shafts, under which the chute runs, are much longer than the respective first parts of these shafts, makes it possible both to reactivate the solids more effectively by the gaseous fluid distributed by the chute at the bottom of the trough and to limit the risk of blocking of the shafts. The reactivation reactor according to the invention thus ensures, in an integrated, simple and economical manner, the following functions: feeding the solids to be reactivated at the inlet of the trough, transporting the solids inside the trough in direction of the exit of the latter, agitation without compaction of the solids with the gaseous reactivation fluid, and evacuation of the reactivated solids for the purpose of their recycling by reintroduction into fumes to be purified.
    According to advantageous additional characteristics of the reactivation reactor according to the invention, taken individually or according to all technically possible combinations:
    - each shaft has a central hub which runs in the longitudinal direction over the entire first part and the entire second part of the shaft,
    - in the first part of each tree, the propeller of the tree is continuously wound around the hub of the tree, and
    - in the second part of each shaft, the blades of the shaft extend individually projecting from the hub of the shaft;
    the two shafts are arranged symmetrically with respect to a geometric plane which is vertical and parallel to the longitudinal direction, and
    - The chute is arranged globally in this geometric plane;
    - At least some of the orifices of the chute are distributed on both sides of the geometric plane, if necessary being associated by pair (s);
    - At least some of the orifices of the chute are distributed in the longitudinal direction, if necessary in a substantially regular manner;
    - the or at least one of the orifices of the chute is a slot, which extends in length in the longitudinal direction and which, if necessary, is located at the base of the chute;
    - the chute is provided with between two and thirty holes plumb with the second part of the trees;
    - The chute consists of a sheet having a cross section which is arranged perpendicular to the longitudinal direction and which has a "V" shape, the top of which is turned away from the bottom of the gauge;
    - the trough comprises a barrier, which is arranged in the reactivation chamber on the side of the outlet facing the first end of the trough, and which rises from the bottom of the trough so as to prevent solids contained in the reactivation chamber to reach the outlet as long as the thickness of the solids is less than the height of the dam relative to the bottom of the trough;
    - The reactor further comprises an engine block designed to drive the two shafts at the same speed, between two and thirty revolutions per minute, in particular in respective directions of rotation which are opposite;
    - The trough is provided with at least one degassing vent, which is arranged above the second part of the two shafts, and / or at least one gas inlet nozzle, which is arranged above of the two trees.
    The invention will be better understood on reading the description which follows, given solely by way of example and made with reference to the drawings in which:
    FIG. 1 is a schematic perspective view of a reactivation reactor according to the invention, certain parts of the reactor being omitted or drawn away for reasons of visibility, and
    - Figures 2 and 3 are schematic sections respectively along plane II and according to plane III of Figure 1.
    In Figures 1 to 3 is shown a reactor 1 for reactivation of solids. This reactor 1 makes it possible in particular to reactivate solids consisting of a mixture of alkaline reagent, which has not reacted with fumes to be purified of their acid pollutants, and of residues which result from the reaction between acid pollutants of fumes and a reagent for neutralizing these acidic pollutants.
    The reactor 1 comprises a trough 10 of elongated shape. The embodiment of the trough 10 is not limiting as long as the trough 10 internally defines a reactivation chamber C inside which solids, once introduced, are reactivated by contacting with a fluid reactivation gas, as explained below.
    The geometry of the reactivation chamber C is not limiting as long as it extends in length in a longitudinal direction D from a first end 10A of the trough 10 to a second end 10B of the trough, opposite the end 10A. As clearly visible in FIGS. 1 and 2, the reactivation chamber C has, at the end 10A of the trough 10, an inlet CE while at the end 10B of the trough, the reactivation chamber has a CS outlet. The inlet CE of the reactivation chamber C is provided to allow the introduction, inside the reactivation chamber, of solids to be reactivated, in particular under the effect of gravity, as indicated by the arrow S1 on the Figure 2. In practice, this CE inlet is delimited through an upper cover 12 of the trough 10 which closes the reactivation chamber from above, the CE inlet can for example be bordered by a drop 13 above above the cover 12. The outlet CS of the reactivation chamber C is, in turn, provided to allow the evacuation of the reactivated solids outside of the chamber C, in particular under the effect of gravity, as indicated by the arrow S2 in FIG. 2. In practice, this outlet CS is delimited by the bottom 14 of the trough 10, being able for example to be bordered by a descent 15 below the bottom 14.
    As shown in Figures 1 to 3, the reactor 1 also comprises two shafts 20 which are arranged, at least for the most part, inside the reactivation chamber C. The two shafts 20 extend, in the chamber reactivation C, parallel to each other in the direction D. In a manner known per se and without limitation, the opposite ends 20A and 20B of each shaft 20 are supported by the trough 10, respectively at the level of the end 10A and at the end 10B of the trough.
    The shafts 20 are provided to be driven each in rotation about a central axis X20 of the shaft. In practice, the shafts 20 are driven in rotation by a motor unit 30 which, in the embodiment considered in the figures, is in drive engagement with the respective ends 20A of the shafts 20. Whatever its As an embodiment, the engine block 30 is advantageously designed to drive the shafts 20 at the same speed, between two and thirty revolutions per minute, if necessary in respective directions of rotation which are opposite to each other.
    As can be clearly seen in FIG. 2, each of the two shafts 20 comprises two parts which follow one another in the direction D and which are jointly arranged between the ends 20A and 20B of the shaft, namely a first part 20C and a second part
    20D. The first part 20C thus connects the end 20A to the second part 20D, the latter connecting the first part 20C to the end 20B of the shaft concerned.
    The part 20C extends from the end 10A of the trough 10 towards the opposite end 10B, having a length, that is to say a dimension in the direction D, which is denoted L1 in FIG. 2 The part 20D of each shaft extends from the end 10B of the trough 10 towards the opposite end 10A, having a length denoted L2. For each shaft 10, the parts 20C and 20D are distinguished, inter alia, by their effect on the solids contained in the reactivation chamber C, as explained below.
    The part 20C of each shaft 20 is designed to essentially, if not exclusively, convey the solids contained in the reactivation chamber C, from the end 10A of the gauge 10 to the end 10B. To this end, this part 20C is provided with a propeller 21 for conveying solids, which, in the embodiment considered in the figures, are wound continuously around a central hub 22 of the corresponding shaft 20, centered on the X20 axis. The part 20C of each tree 20 is thus similar for example to an Archimedes screw.
    The part 20D of each shaft 20 is designed to essentially, or even exclusively, stir the solids contained in the reactivation chamber C, by aerating these solids. To do this, this part 20D is provided with blades 23 for mixing solids, which, in the embodiment considered in the figures, extend individually projecting from the hub 22 of the corresponding shaft, being distributed so regular on this hub in the direction D. These blades 23 are, for example and without limitation, in the form of plates, shovels, etc. and are not necessarily flat. They can optionally be tilted to contribute marginally to the dragging of solids towards the 10B end of gauge 10.
    Even though the part 20D of each shaft 20 can contribute marginally to the transport of the solids in the reactivation chamber C towards the end 10B of the trough 10, it will be noted that the propeller 21 of the part 20C does not extend in part 20D. Likewise, even if certain embodiments of the propeller 21 can optionally contribute to inducing a certain agitation of the solids in the reactivation chamber C, the blades 23 of the part 20D are not found in the part 20C. In practice, in the embodiment considered in the figures, the material continuity of each shaft 20 between its ends 20A and 20B is produced by the central hub 22 which runs in the direction D over both the entire part 20C and the whole part 20D.
    Thus, the parts 20C of the shafts 20 and the parts 20D of the shafts 20 induce the formation of two respective zones within the reactivation chamber C, which follow one another in the direction D and which act with different respective effects on the solids contained respectively in these zones: in a first zone, which is denoted Z1 in FIG. 2 and which corresponds to the respective first parts 20C of the shafts 20, the solids introduced into the reactivation chamber C by the inlet CE which is arranged above respective parts 20C of the shafts 20 are essentially, or even exclusively conveyed by these parts 20C as indicated by an arrow S3 in FIG. 2, and this up to a second area, denoted Z2 and corresponding to the second respective parts 20D of the shafts 20, in which the solids coming from the first zone Z1 are essentially, or even exclusively brewed by these parts 20D of the trees, as indicated by arrows S4 in FIG. 2. At the end of the zone Z2 turned towards the end 10B of the trough 10, the solids are evacuated from this zone Z2 via the outlet CS which is located below the respective parts 20D of the shafts 20, more precisely below the terminal longitudinal portion of these parts 20D, opposite the parts 20C of the shafts.
    According to the invention, the zone Z1 is much shorter, in the direction D, than the zone Z2: according to one of the characteristics of the invention, the length L1 thus represents between 10% and 33% of the sum of the lengths L1 and L2, it being understood that the length L2 therefore necessarily represents between 67% and 90% of the sum of the lengths L1 and L2.
    According to an optional arrangement which is implemented in the exemplary embodiment considered in the figures, the trough 10 comprises a dam 16, arranged in the reactivation chamber C and located on the side of the outlet CS facing towards the end 10A of the trough: as clearly visible in FIG. 2, this barrier 16 rises from the bottom 14 of the trough 10 so as to prevent the solids contained in the reactivation chamber C from reaching the outlet CS as long as the thickness of the solids is less than the height of the dam relative to the bottom of the trough. It is understood that the dam 16 thus makes it possible to maintain a minimum level of solids in the zone Z2 of the reactivation chamber C.
    As clearly visible in Figures 1 to 3, the reactor 1 further comprises a chute 40 for distributing a gaseous reactivation fluid. This chute 40 is designed to distribute, in the reactivation chamber C, a gaseous reactivation fluid which consists of water vapor or which consists of a mixture of air, fumes and water vapor. More generally, the composition of the reactive gas fluid is not limiting.
    The chute 40 is arranged in the reactivation chamber C, being located on the bottom 14 of the trough 10. In addition, the chute 40 extends in the direction D, and this below the shafts 20, more precisely by running below at least the second part 20D of these shafts 20: via orifices 42 of the chute 40, gaseous reactivation fluid, supplying the chute, is admitted into the lower part of the reactivation chamber C, in particular in the lower part of zone Z2, as indicated by the arrows F in FIG. 2. In operation, this gaseous fluid mixes easily with the solids contained in zone Z2 of the reactivation chamber C because these residues are there stirred by the respective parts 20D of the shafts 20: in fact, this gaseous fluid flows easily within the stirred solids, thus promoting the contacting of the latter with the gaseous fluid, which guarantees an effective reactivation of these solids.
    According to a practical, economical and effective embodiment, which is implemented in the embodiment considered in the figures, the chute 40 consists of a sheet having a cross section which is arranged perpendicular to the direction D and which has an inverted "V" shape, that is to say a "V" shape, the apex of which is turned away from the bottom 14 of the trough 10. Of course, other embodiments are possible for chute 40.
    According to a preferred but non-limiting aspect, relating to the arrangement of the chute 40 inside the trough 10, the chute 40 is, as in the example considered in the figures, generally arranged in a geometric plane P, which is vertical and parallel to the direction D, while the two shafts 20 are arranged symmetrically with respect to this geometric plane P, as clearly visible in FIG. 3. In this case, in order to homogenize the distribution of the gaseous fluid reactivation in the chamber C vis-à-vis the two shafts 20, at least some of the orifices 42 of the chute 40 can advantageously be distributed on both sides of the geometric plane P, preferably being associated by pair (s).
    In practice, the shape, the arrangement and the number of the orifices 42 of the chute 40 are not limiting of the invention. Thus, according to a possible embodiment, each or at least some of the orifices 42 are in the form of slots, which each extend in length in the direction D and which are for example located at the base of the chute 40, c 'that is to say at its junction with the bottom 14 of the trough 10. It can also be envisaged that the trough 40 is provided with a single orifice 42, in the form of a long slot which runs at least at below all or part of the parts 20D of the shafts 20. Alternatively, two such long slots can also be envisaged for the orifices 42, being located laterally on either side of the chute. In the embodiments where several orifices 42 are provided, at least some of them can advantageously be distributed in the direction D, preferably in a substantially regular manner. According to a practical and effective embodiment, between two and thirty orifices 42 are provided in the zone Z2 of the reactivation chamber C, that is to say that between two and thirty orifices 42 are provided directly above the parts 20D trees 20.
    Similarly, the embodiment of the means for supplying the chute 40 with the reactivation fluid is not limiting, these means being known per se. By way of example, these means include nozzles and flanges, arranged on the underside of the chute 40.
    Furthermore, optionally, the chute 40 can be segmented so as to control, segment by segment, the flow rate of the reactivation fluid admitted into the chamber C through the orifices 42.
    Finally, various optional arrangements for reactor 1 can be envisaged.
    Thus, not shown in the figures, the trough 10 can be provided with one or more degassing vents, arranged above the second part 20D of the shafts 20. This or these vents make it possible to evacuate a surplus of reactive gas fluid, present in the sky of the reactor 1, in other words in the part of the reactivation chamber C situated above the parts 20D of the shafts 20 and not occupied by the solids.
    Also not shown in the figures, the gauge 10 can be provided with one or more gas inlet nozzles, arranged above the shafts 20, in particular above their second parts 20D. This or these tappings make it possible in particular to supply the headspace of the reactor 1 with a predetermined gas, for example and without limitation of air.
    权利要求:
    Claims (11)
    [1" id="c-fr-0001]
    1.- Reactor (1) for reactivation of solids, comprising:
    - an elongated trough (10), which defines a reactivation chamber (C) extending in a longitudinal direction (D) from a first end (10A) of the trough to a second end (10B) of the trough , this reactivation chamber having:
    - an inlet (CE), which is located at the first end of the gauge and through which solids to be reactivated enter the reactivation chamber, and
    - an outlet (CS), which is located at the second end of the gauge and through which the reactivated solids leave the reactivation chamber;
    - two shafts (20), which are arranged in the reactivation chamber (C) and which extend there parallel to each other in the longitudinal direction (D), each of the two shafts successively comprising:
    - A first part (20C), which extends from the first end (10A) of the trough (10) towards the second end (10B) of the trough and which is provided with a propeller (21) for conveying solids, and
    - a second part (20D), which extends from the second end of the trough towards the first end of the trough and which is provided with blades (23) for mixing solids, the length (L1) of the first part (20C) representing between 10% and 33% of the sum of the respective lengths (L1, L2) of the first and second parts; and
    - a chute (40) for distributing a gaseous reactivation fluid, which is arranged in the reactivation chamber (C) at the bottom of the trough (10), which extends in the longitudinal direction (D) in current below at least the second part (20D) of the two shafts (20), and which is provided with one or more orifices (42) for admitting the fluid into the reactivation chamber.
    [2" id="c-fr-0002]
    2, - Reactor (1) according to claim 1, wherein each shaft (20) has a central hub (22) which runs in the longitudinal direction (D) over the entire first part (20C) and the entire second part (20D ) of the shaft, in which, in the first part (20D) of each shaft (20), the propeller (21) of the shaft is continuously wound around the hub (22) of the shaft, and in which, in the second part (20D) of each shaft (20), the blades (23) of the shaft extend individually projecting from the hub (22) of the shaft.
    [3" id="c-fr-0003]
    3.- Reactor (1) according to one of claims 1 or 2, wherein the two shafts (20) are arranged symmetrically with respect to a geometric plane (P) which is vertical and parallel to the longitudinal direction (D ), and in which the chute (40) is arranged globally in this geometric plane (P) ·
    [4" id="c-fr-0004]
    4. - Reactor according to claim 3, wherein at least some of the orifices (42) of the chute (40) are distributed on both sides of the geometric plane (P), if necessary being associated by pair (s).
    [5" id="c-fr-0005]
    5. - Reactor according to any one of the preceding claims, in which at least some of the orifices (42) of the chute (40) are distributed in the longitudinal direction (D), where appropriate in a substantially regular manner.
    [6" id="c-fr-0006]
    6. - Reactor according to any one of the preceding claims, in which the or at least one of the orifices (42) of the chute (40) is a slot, which extends in length in the longitudinal direction (D) and which, if applicable, is located at the base of the chute.
    [7" id="c-fr-0007]
    7. - Reactor according to any one of the preceding claims, in which the chute (40) is provided with between two and thirty orifices (42) perpendicular to the second part (20D) of the shafts (20).
    [8" id="c-fr-0008]
    8. - Reactor according to any one of the preceding claims, in which the chute (40) consists of a sheet having a cross section which is arranged perpendicular to the longitudinal direction (D) and which has a "V" shape. > the top of which is turned away from the bottom (14) of the trough (10).
    [9" id="c-fr-0009]
    9. - Reactor according to any one of the preceding claims, in which the trough (10) comprises a dam (16), which is arranged in the reactivation chamber (C) on the side of the outlet (CS) facing towards the first end (10A) of the trough, and which rises from the bottom (14) of the trough (10) so as to prevent the solids contained in the reactivation chamber from reaching the outlet as long as the thickness of solids is less than the height of the dam relative to the bottom of the trough.
    [10" id="c-fr-0010]
    10. - Reactor according to any one of the preceding claims, in which the reactor (1) further comprises an engine block (30) provided for driving the two shafts (20) at the same speed, between two and thirty revolutions per minute, especially in respective opposite directions of rotation.
    [11" id="c-fr-0011]
    11. Reactor according to any one of the preceding claims, in which the trough (10) is provided with at least one degassing vent, which is arranged above the second part (20D) of the two shafts (20) , and / or at least one gas inlet nozzle, which is arranged above the two shafts (20).
    1/2
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    同族专利:
    公开号 | 公开日
    PT3554679T|2021-04-05|
    ES2863578T3|2021-10-11|
    WO2018109072A1|2018-06-21|
    DK3554679T3|2021-04-06|
    EP3554679A1|2019-10-23|
    PL3554679T3|2021-06-28|
    EP3554679B1|2021-01-06|
    FR3060417B1|2019-05-24|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE3408047A1|1984-03-05|1985-10-10|Friedrich 4983 Kirchlengern Hellmich|Reactivation apparatus for the sorption material used for purifying industrial waste gases|
    EP1980581A1|2006-01-30|2008-10-15|Kureha Corporation|Process for producing aliphatic polyester|
    FR2911518A1|2007-01-24|2008-07-25|Lab Sa Sa|Conditioning solids returning from a gas-solid separator, comprises introducing solids in an inlet placed at a first end of a reactor, injecting a conditioning gas in a chamber, and counter-currently circulating the gas in the reactor|
    US20100137463A1|2008-11-26|2010-06-03|Cleanaway Pet International Gmbh|Polyester with caustic material mixing methods and mixing reactors|
    US20150016211A1|2013-07-09|2015-01-15|Wenger Manufacturing, Inc.|Steam/water static mixer injector for extrusion equipment|EP3586944A1|2018-06-27|2020-01-01|Lab Sa|Method for removing mercury from gaseous effluents|
    CN111760550A|2020-06-24|2020-10-13|生态环境部南京环境科学研究所|Device and method for preparing porous active biochar adsorbing material|
    WO2021213793A1|2020-04-22|2021-10-28|Soprema|Heatable mixer for composite products|FR2883772B1|2005-03-30|2007-05-11|Lab Sa Sa|METHOD AND INSTALLATION FOR PURIFYING SMOKE CONTAINING ACIDIC POLLUTANTS|CN110756265A|2019-10-30|2020-02-07|徐州宝美工程机械有限公司|Ore raw material crushing, shaping and mixing device for metallurgy|
    CN110918170A|2019-12-12|2020-03-27|杨银龙|Chemical material's crushing stoving sieving mechanism|
    法律状态:
    2017-11-23| PLFP| Fee payment|Year of fee payment: 2 |
    2018-06-22| PLSC| Publication of the preliminary search report|Effective date: 20180622 |
    2019-11-20| PLFP| Fee payment|Year of fee payment: 4 |
    2020-11-18| PLFP| Fee payment|Year of fee payment: 5 |
    2021-11-18| PLFP| Fee payment|Year of fee payment: 6 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1662483|2016-12-15|
    FR1662483A|FR3060417B1|2016-12-15|2016-12-15|SOLID REACTIVATION REACTOR|FR1662483A| FR3060417B1|2016-12-15|2016-12-15|SOLID REACTIVATION REACTOR|
    PL17835616T| PL3554679T3|2016-12-15|2017-12-14|Reactor for reactivating solids|
    PT178356168T| PT3554679T|2016-12-15|2017-12-14|Reactor for reactivating solids|
    PCT/EP2017/082785| WO2018109072A1|2016-12-15|2017-12-14|Reactor for reactivating solids|
    DK17835616.8T| DK3554679T3|2016-12-15|2017-12-14|Reactor for reactivation of solids|
    EP17835616.8A| EP3554679B1|2016-12-15|2017-12-14|Reactor for reactivating solids|
    ES17835616T| ES2863578T3|2016-12-15|2017-12-14|Reactor to reactivate solids|
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