• 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:
    Shaft arrangement for thermal and/or material transfert processes between a gas and a flowing bulk material, wherein the shaft is divided by grates (2) into chambers (3) which are partly filled with plane heaps (4) of material. In the wall of the shaft (1) there are provided free passage openings (12, 13 respectively 14, 15) for the gas to be entered into at least certain chambers and to be evacuated from other chambers. The heaps traverse the shaft (1) in a discontinuous way. To this effect, all the grates are formed at least partially with moving grate bars which may be taken out temporarily from the plane of fixed bars by a drive device so as to generate a uniform dripping flow and to form on the following grate (2) a heap (4) having the same thickness with respect to the section surface of the shaft. The grates (2) may also be comprised of fixed bars parallel between each other with slit lamellae arranged on top and inclined with respect to each other in a roof configuration, and of which one is fixed and the other one may pivot.
    公开号:SU1450760A3
    申请号:SU853979505
    申请日:1985-11-22
    公开日:1989-01-07
    发明作者:Зендерманн Эрих；Лаурин Ганно；Вальбраук Вольфганг；Рейе Ганс
    申请人:Перфлуктив-Консульт Аг (Фирма)；
    IPC主号:
    专利说明:


    The invention relates to a device for carrying out physical processes, in particular to an apparatus for heat exchange between a gas and a bulk material.
    The aim of the invention is to intensify heat transfer.
    FIG. 1 shows the proposed apparatus, a longitudinal section; FIG. 2 Q Part of the apparatus at the height of one lattice; in fig. 3 is the same, top view in FIG. 4 and 5 - the position of the rods) of the lattice; in fig. 6 - lattice rods with fitted reiter-like elec-15 cops; in fig. 7 - the same, top view; in fig. 8 - zone of the lower part of the apparatus, longitudinal section; figure 9- distributed over the cross section of the apparatus of the valve, bottom view, nafig. flap, cross section} in Fig. 11 is an apparatus with longitudinal section gratings inserted from the side; FIG. 12 is an embodiment of the grid, a slit.
    The proposed apparatus is made in the form of a shaft 1, which can be made with a square or rectangular cross section. In mine 1, grids 2 are installed one above the other in the walls at a distance with chambers 3, with a layer 4 of bulk material located on each grid 2. The distance between layers 4 is 0.8 - 8 times the thickness of an individual layer.
    The shaft consists of annularly closed and stacked modular elements 5 with a grid 2 located in each of them, so that the shaft can be made with different heights and different numbers of floors by selecting the appropriate number of modular elements 5. At the lower end of the shaft there are 25
    thirty
    35
    40
    45

    the wife of the valve 6 is closed by an opening 7 for the release of material in the mine. Under the shaft there is a conveyor 8, by means of which the material coming out of the shaft is fed for further processing or processing.
    The shaft is closed from above with the housing 9, which is filled as an inlet slurry. In the side part of the housing 9, the dosing-distribution device 10 is schematically depicted to receive the amount of material necessary for one layer 4, from which it is transferred as a flat layer with a uniform forming cross-section box 11, which is closed from the bottom by a grid, is made in the same way as grid 2 in modular elements 5 of mine 1, and is equipped with a drive (not shown). From the molding box 11, the layer is transferred to the uppermost chamber located in the mine, i.e. on the grille bounding this camera as the bottom.
    In the wall of the shaft 1 are provided in the chambers 3 or in the free intermediate spaces formed by the chambers inlet holes 12-14 and outlets. openings 15-18, which are connected to the respective pipelines (not shown) for supplying and discharging gas, which are connected to transport devices or devices for the preparation of gas or steam, depending on whether they are treated with gases or vapors. layer x 4 material.
    In the shaft 1 between the two uppermost gratings 2, a partition formed from the rotary plates 19 is provided, which can be inserted into the closed position and opened by appropriately moving the plates. A similar partition of the plates 19 is also located between the two lowest gratings 2. In addition, an insert 20 in the form of a grating is installed below the lowest grating 2 located in the shaft, which serves to form parallel channels 21 in which flaps 22 are installed, which can be rotated around horizontal axes 23 and 24. These dampers can take both a closing and an opening position.
    The lattice 2 installed in the shaft 1 (Figs. 2 and 3) consists of stationary rods 25 and movable rods 26, the rods 26 being relatively stationary 25 rods capable of moving upwards from the plane of the lattice in order to temporarily increase the free intermediate spaces between adjacent rods. In the left part of FIG. 2 shows the position of the rods 25 and 26 in the grid plane, while on the right side the rods 26 are depicted in different positions relative to the grid plane. To lift the slider rods 26 mounted in the recesses 27 on the inner side of the shaft 1, the levers 28 are made with the possibility of rotation around the axis 29. The movable rods 26 are made elongated with respect to the fixed legs 25 and combined into a knot that can be lifted and opus Cani, and the elongation of the rods 26 (Fig. 2) has the shape of the bends 30 of various lengths. As a consequence, it is achieved that when rotating {{of the cuts 28 around the axis 29, the rods 26 are transferred to different heights, as shown in the right-hand part of Fig. 2.
    Instead of lifting, the movable rods 26 can also be lowered, so that depending on the direction of movement, the rods 26 can occupy a different position relative to one another (Fig. 4 and 5). The rods of the lattice can have the shape shown in Fig.6 and 7. In this case, the rods can be made as solid rods or hollow rods. They have an occipital profile 31 in cross section in the upper part and are equipped with replaceable rater-like elements 32 mounted on this profile. Reiter-like elements 32. are horseshoe-shaped and have protrusions 33 serving as stops for adjacent riter-like elements 32. When the riter-shaped elements 32 are tightly placed, the rods 32 are shaped as shown in FIG. 7
    Reservoir elements 32 ensure that the lower layer of particles in each individual layer 4 cannot block the intermediate spaces between adjacent rods, even if the bulk material is in the form of cylindrical particles. At a given distance of the rods, the riter-shaped elements 32 can have a different diameter, so that as a result of this, the free cross section of the flow can be adjusted or changed accordingly by means of the grids 2,
    In addition, the use of Reiter-32differential elements 32 of different cross-sections allows influencing the amount of free spaces for the flow of gases between the rods in places or across the entire cross-section of the lattice.
    - In FIG. 8-11 show the details of the implementation of the rotary valves around the horizontal axes 22 installed in the channels 21 of the insert 20. The valves 22 are installed in the channels in a checkerboard pattern so that the valves located next to each other occupy a different position. For the joint adjustment of the dampers 22 of each row located in the same position, two horizontal axes 23 and 24 arranged one above the other (Fig. 10) are provided on which the shutters 22 of each row are arranged alternately. According to FIG. 8, in the grooves of the shutters 22 installed on the axis 23, an axis 24 of the corresponding shutters is located, and the axis 24 does not interfere with the rotation of the shutters located on the axis 23. Thus, it is possible to move all the dampers to the closed position or to the open position or to move the adjacent dampers to different positions.
    Instead of a modular design, mine 1 can also be made with
    solid wall or (Fig. II) to have holes 34, in which the side can enter the grating 2 in the form of separate nodes. In this case, the grids, consisting of fixed and movable rods, are installed in the grooved grooves 35, which are made in the side wall, with the aid of a supporting device
    plates 41 and to be installed in the modular construction of the corresponding shty.
    The device works as follows.
    The apparatus can be used, for example, to heat or cool the treated material. For
    36, to close the opening 34 in the wall of this target, the openings 12 and 13 can
    ke use the correspondingly made insert 37, as well as the overlapping plate 38, which is screwed to the wall of the shaft 1 after the placement of the insert 37. The described form of the implementation allows simple and quick replacement of the grid assembly.
    Instead of the one shown in FIG. 2-11 of the embodiment of the lattice 2, the latter can also be carried out in accordance with the image in FIG. 12. At the same time using parallel bearing rods 39, mounted in a fixed -. a bearing carrier, configured as shown in FIG. 11 to the carrier device 36. In this case, the carrier rods 39 can be made hollow. Above each carrier rod 39, plates 40 and 41 arranged in a cap-like manner are provided, having passageways 42 arranged transversely to the longitudinal direction. In this case, the plate 40 is rigidly attached, for example welded, to the corresponding carrier rod 39, while each plate 41 is rigidly connected to a pivot axis 43 mounted above the supporting rod. In this case, the pivot axes are mounted in a frame bearing device and are connected to pivoting levers 44 that are located outside the plane of the lattice. with the connecting rod 45 connected to the drive, so that it can reciprocate in the direction of the double boom 46, and thus the levers 44 can be rotated in the direction of the double boom 47. As a result, the turn plates 41 (Fig. 12) can be moved from the position depicted by the solid line to the position depicted by the dashed line.
    The grid according to FIG. 12 it is possible: also to produce as a prefabricated unit, to connect with the corresponding crank-connecting rod mechanisms for turning
    be connected to the co-venter while opening. 17 are connected to a joint pipe for the removal of gas, which is
    15 to be part of the circulation duct and connected to the fan, for example, through a heat exchanger. The lowermost layer 4 located in the shakt can be processed by
    20 dachas and withdrawal through openings 14 and 18 of another gas or with a different gas temperature. In this case, the transmission through the aforementioned lowest layer of the medium can be adjusted by
    25 of the insert 20 and the shutters 22. In addition, by setting the gas flow rate appropriately, it is possible to achieve the desired degree of control of the material in the layer, so
    30 that, in the zone of the open channels 21, a partial movement of the particles of material takes place, which, due to loosening and creation, flow into areas that are not straight
    25 start up fluid: By changing the position of the shutters 22, it is possible to achieve recirculation and reverse movement of the material particles. This is particularly advantageous if, when processing the lowermost layer, the particles should have a tendency to clumping. Due to the presence of a layer above
     plates 19 are created separately
    45 per treatment for the lower layer. At the same time, the layer located above the lower plates and 1 9 forms an additional: locking element through which the city does not flow. In contrast to this, connecting the connections 12 and 13 to the pipeline for supplying gas through the subsequent in the upward direction, four layers in the direction of the arrows shown skip ha
    55 partially upwards and partially upwards. In this case, the gas is vented from the outlet openings 15-17. These outlet openings can be connected to a joint pipe.
    plates 41 and installed in the modular construction of the corresponding shaft.
    The device works as follows.
    The apparatus can be used, for example, to heat or cool the material to be treated. For
    For this purpose, holes 12 and 13 can
    to be connected to a joint fan, while openings 15-17 are connected to a joint pipeline for venting gas, which can be part of a circulation pipe and connected to the fan, for example, through a heat exchanger. The lowermost layer 4 located in the shakt can be processed by inlet and outlet through openings 14 and 18 of a different or different gas temperature. In this case, the transmission through the aforementioned lowest layer of the medium can be controlled by
    the inserts 20 and the shutters 22; In addition, by setting the appropriate gas flow rate, it is possible to achieve the desired degree of control of the material in the layer, so
    that in the zone of the open channels 21 a partial movement of material particles takes place which, due to loosening and creation, flows into areas that do not allow the fluid to pass through: By changing the position of the shutters 22, it is possible to achieve recirculation and reverse movement of the material particles. This is particularly advantageous if, when processing the lowermost layer, the particles should have a tendency to clumping. Due to the presence of a layer
    The plates 19 create a separate treatment zone for the lower layer. At the same time, the layer located above the lower plastids 1 9 forms an additional: locking element through which the city does not flow, in contrast to this, when the holes 12 and 13 are connected to the pipeline for supplying gas through the subsequent ones in the upward direction four layers in the direction of the arrows shown allow gas to flow
    partially from top to bottom and partially from bottom to top. At the same time, the gas is vented through the outlets 15-17. The said outlets may be connected to a common pipeline for venting. By means of suitable adjusting devices, the direction of the gas flow indicated by the arrows shown can be changed, so that without any difficulties it is possible to change the direction of flow during the stay of the layers at different stages.
    The apparatus located in the mine (Fig. 1), the second layer on top also constitutes a locking element, as above this layer there is a partition formed by the swivel plates 19, which is from the IB closed position during the passage of the medium through the layers. This layer is formed while the medium is being passed in the manner described above through other layers.
    When the lowermost layer located in the mine reaches its final state as a result of medium treatment, by moving the movable rods of this lattice to the open position and moving the valve 6 to the open position, the layers are transferred to the conveyor 8. After moving the movable rods back into the plane of the fixed rods the rotary plates 19 above this grating are turned to the open position and by temporarily moving the rods of the gratings located above these plates the free layer on them deniem transmitted to the lowermost grille so that achieved uniformly over the cross section of the mine layer thickness, this process is repeated with the grating on the grating as long as the uppermost grille in the shaft will not be free of particulate material. In the closed position of the lamella 19 provided in the upper part of the shaft, material is formed into the shaft by means of movable molding machines II to form the uppermost layer.
    Drives of various types, such as hydraulic electric or electromechanical drives with appropriate control capabilities, can be used to control the moving rods to control both the degree of movement and the time of movement of the rods.
    eight
    ten
    Thus, in the proposed mine apparatus, it is possible to carry out drying, heating, cooling of the chemical material of the material, depending on the type of material and the gases or vapors used to process it.
    权利要求:
    Claims (5)
    [1]
    Invention Formula
    I. Apparatus for heat exchange and / or mass transfer between gas and bulk material, containing a shaft with a grating placed in it, billowed in a vertical direction movable in a vertical direction from the drive and fixed rods, loading and unloading devices, holes for supplying and expelling heat carrier, characterized by that, in order to intensify heat exchange, it is provided with additional gratings with movable and fixed rods evenly spaced along the height of the shaft, and the openings for supply and discharge of heat transfer fluid are placed in ovyh the walls of the mine.
    five
    0
    five
    [2]
    2. The device according to claim 1, differs - 30 10 u and in that it is supplied
    lamellar partitions placed under the top and above the bottom gratings.
    [3]
    3. The device on PP. I and 2, that is, it is equipped with an insert in the form of a grid with rotary valves installed in it, located under the lower grid.
    35
    40
    45
    [4]
    4. The device on PP. 1-3, characterized in that the lattice rods in cross section have an occipital profile and are provided with the possibility of replacing the horseshoe-shaped reiter elements with projections in the longitudinal direction.
    [5]
    5. The device on the PP. 1-4, which is based on the fact that the lattice is complete in the form of stationary parallel support rods with overhead and recessed plates with passage slots across the longitudinal direction, and one of the plates is fixed still rotation over the bearing rod.
    26 26
    II
    Tl
    I /
    ZS
    Z7
    X
    qptit.l
    25
    26 25
    e.J
    25
    Faeb

    Have
    M
    M
    ;
    -one-(

    t
    Fia. 7
    9
    FIG, Yu
    H
    J7
    D
    58
    FIG. //
    33
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1450760A3|1989-01-07|Apparatus for heat and/or mass exchange between gas and loose material
    KR910002215B1|1991-04-08|Fluidized bed boilers
    MXPA02006871A|2004-12-13|Cfb with controllable in-bed heat exchanger.
    DE3322119A1|1983-12-29|COMBUSTION PLANT WITH REGENERATIVE HEAT EXCHANGER
    US20120322016A1|2012-12-20|Roller hearth calcining furnace and method of use
    DK157808B|1990-02-19|PROCEDURE FOR SUPPLY OF COMBUSTION AIR TO REGENERATORS IN A GLASS MOLD OVEN AND REGENERATIVE GLASS MOLD OVEN FOR EXECUTING THE PROCEDURE
    AU652248B2|1994-08-18|Partition wall for a multi-compartment furnace
    US20030170582A1|2003-09-11|Method in connection with a pipe grate for fluidized bed boiler and a pipe grate
    US5005272A|1991-04-09|Process in setting a web, and a heat setting plant for setting webs
    US4664623A|1987-05-12|Process and apparatus for the thermal treatment of trickling material swellable or rendered swellable, and containing aluminosilicates
    US4619606A|1986-10-28|Vertical maltdrying kiln
    US4708642A|1987-11-24|Process for the thermal and/or chemical treatment of grained, granular or lump material
    US1359301A|1920-11-16|Drying apparatus
    WO2002023112A1|2002-03-21|A grate cooler for granular material
    US2812592A|1957-11-12|Heat treatment of finely-divided solids
    CH421162A|1966-09-30|Apparatus working with movable mass particles, in particular a regenerator, in which a gaseous medium is passed in countercurrent through a layer of mass particles
    US3549135A|1970-12-22|Regenerative furnaces
    US3215125A|1965-11-02|Sectional boiler construction
    US2759710A|1956-08-21|Cooling device
    US4752359A|1988-06-21|Method of producing active form coke
    SU890057A1|1981-12-15|Gas distributing grill
    JP5528344B2|2014-06-25|Staircase burning grate
    SU575463A1|1977-10-05|Apparatus for drying loose materials in fluidized bed
    SU724897A2|1980-03-30|Plant for drying capillary-porous materials
    DE1056081B|1959-04-30|Grain mill
    同族专利:
    公开号 | 公开日
    ES8706376A1|1987-07-01|
    BR8506055A|1986-03-25|
    EP0174970B1|1988-10-12|
    IT1187649B|1987-12-23|
    DD233411A5|1986-02-26|
    ZA852152B|1985-12-24|
    ES541451A0|1987-07-01|
    JPS61501522A|1986-07-24|
    US4764107A|1988-08-16|
    IT8520056D0|1985-03-25|
    EP0174970A1|1986-03-26|
    AU4153085A|1985-11-01|
    DK518685A|1985-11-11|
    DE3410894A1|1985-10-03|
    WO1985004469A1|1985-10-10|
    DK518685D0|1985-11-11|
    DE3565597D1|1988-11-17|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2626360C1|2016-05-25|2017-07-26|Федеральное государственное бюджетное образовательное учреждение высшего образования "Тихоокеанский государственный университет"|Vertical adsorber for butane fraction separation|DE31932C|A. DUFOUR in Dole, Jura, Frankreich|Shaft furnace with two-part partition walls for the continuous burning of lime, cement and the like|
    GB157194A|1915-11-05|1921-07-14|Pfeiffer Fa Geb|Mechanical disintegrating and discharging apparatus for shaft furnaces|
    DE328807C|1919-04-17|1920-11-05|Felix Fuchs|Emptying device for shaft ovens for burning cement, lime, magnesite u. like|
    US1533572A|1922-10-02|1925-04-14|Robert H Richards|Furnace|
    DE618207C|1930-02-28|1935-09-05|Ernst Curt Loesche|Shaft furnace for burning cement and similar goods|
    DE607786C|1930-10-14|1935-01-08|Arno Andreas|Device and method for burning cement|
    DE848172C|1949-01-14|1952-09-01|Peter Steinbuechel|Discharge grate for shaft ovens|
    FR1139777A|1954-11-26|1957-07-04|Device for preheating powdery materials|
    US2948521A|1956-07-14|1960-08-09|Roechlingsche Eisen & Stahl|Process and apparatus for heating a cross stream shaft furnace in view of heating solid materials, particularly for the calcination of limestone|
    US2996292A|1958-06-12|1961-08-15|Ernst G Graf|Gravity-fed combustion equipment applying crossfeed ignition principle|
    DE1243827B|1959-09-07|1967-07-06|Erich Heidelmeyer|Shaft furnace for the production of porous aggregates from blue-able material|
    FR1424099A|1964-03-26|1966-01-07|Polysius Gmbh|Method and device for the manufacture of blown or expanded clay|
    DE2364626A1|1973-12-24|1975-06-26|Kloeckner Humboldt Deutz Ag|PROCESS FOR THE HEAT TREATMENT OF GRAINY AND / OR LITTLE GOODS, IN PARTICULAR FOR BURNING LIME, DOLOMITE, MAGNESITE OR THE GLOBE.|
    DE2707953C2|1977-02-24|1986-12-11|Hugo Dipl.-Phys. Dr. 5757 Wickede Balster|High temperature grate|
    US4334859A|1978-07-20|1982-06-15|Susumu Minegishi|Method and apparatus for melting matrix materials|DE3540068A1|1985-11-12|1987-05-14|Babcock Anlagen Ag|METHOD AND PLANT FOR PRODUCING CONCRETE ADDITIVES FROM WASHING MOUNTAINS|
    US5044942A|1990-01-18|1991-09-03|Gas Research Institute|Cement shaft suspension furnace and process|
    US4975046A|1990-01-18|1990-12-04|Gas Research Institute|Cement shaft suspension furnace and process|
    DE102005052753A1|2005-11-04|2007-05-10|Polysius Ag|Plant and process for the production of cement clinker|
    DE102006052416A1|2006-11-07|2008-05-08|Polysius Ag|Process and apparatus for calcining solids or sludges|
    CN101726168B|2009-11-30|2011-03-16|广西大学|Bagasse tower-type multi-layer dryer|
    CN102368016A|2011-10-20|2012-03-07|洛阳市谱瑞慷达耐热测试设备有限公司|Granular material calcining furnace and calcining method|
    US9512950B1|2011-12-29|2016-12-06|Arthur M. Squires Irrevocable Trust|Method and apparatus for uniformity of spills from fluid-entry faces of a panel bed|
    WO2019050777A1|2017-09-08|2019-03-14|A.J. Antunes & Co.|Conveyor belt for use within a toaster appliance for preventing the pinching of food buns|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19843410894|DE3410894A1|1984-03-24|1984-03-24|SHAFT ARRANGEMENT FOR THERMAL AND / OR MATERIAL TRANSFER PROCESSES BETWEEN A GAS AND A BULK MATERIAL|
    [返回顶部]