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    • 1. 发明公开
    • FEEDING SYSTEM FOR A LIME REBURNING KILN
    • 石灰回炉的喂料系统
    • EP0480960A1
    • 1992-04-22
    • EP90909734.0
    • 1990-06-28
    • A. AHLSTROM CORPORATION
    • AHVENAINEN, Arto
    • C04B2F27B7F27D13
    • C04B2/10F27B7/3205F27B2007/163F27B2007/2008C04B2/005
    • Procédé et appareil pour le traitement à chaud de boues résiduaires de chaux comprenant le séchage desdites boues devant être introduites dans le four de cuisson de la chaux (5) dans un séchoir pneumatique (3) à l'aide de gaz de fumées déchargés dudit four de manière à régénérer la teneur en chaux des boues résiduaires. Les boues que l'on a épaissies à une teneur en matière sèche supérieure à 75 %, et de préférence à 80 %, sont amenées depuis un filtre de séchage (6) à une chambre d'alimentation (2) à travers laquelle est conduite une partie réglable des gaz de fumées. Selon la quantité de gaz, 100% ou moins des boues résiduaires de chaux sont entraînés avec ledit gaz dans le séchoir (3); la portion qui reste tombe dans la partie inférieure (14) de la chambre d'alimentation, d'où on la transfère ensuite au four (5) de cuisson de la chaux.
    • 用于石灰泥的热处理的方法和设备包括:使用从所述炉排出的烟气在气动干燥器(3)中将待引入到石灰烘箱(5)中的所述污泥进行干燥 以便再生废污泥的石灰含量。 已经增稠至固体含量大于75%,优选80%的污泥从干燥过滤器(6)进料到进料室(2),通过该进料室 一个可调整的烟气部分。 根据气体的量,100%或更少的石灰泥与气体在干燥器(3)中夹带; 剩余部分落入进料室的下部(14),然后将其转移到窑(5)烹制石灰。
    • 2. 发明授权
    • FEEDING SYSTEM FOR A LIME REBURNING KILN
    • 石灰回炉的喂料系统
    • EP0480960B1
    • 1995-03-01
    • EP90909734.7
    • 1990-06-28
    • A. AHLSTROM CORPORATION
    • AHVENAINEN, Arto
    • C04B2/10F27B7/32
    • C04B2/10F27B7/3205F27B2007/163F27B2007/2008C04B2/005
    • A method and apparatus for heat treatment of lime mud comprises drying of the lime mud to be introduced into the lime reburning kiln (5) in a pneumatic dryer (3) by means of flue gases discharged from the lime reburning kiln in order to regenerate the lime content of the lime mud. From a drying filter (6), the lime mud thickened to a dry solids content of over 75 %, preferably to 80 %, is introduced into a feed chamber (2) through which an adjustable portion of the flue gas is conducted. Depending on the gas amount, 100 % or less of the lime mud is entrained with the gas into the dryer (3), the remaining portion falling into the lower section (14) of the feed chamber, wherefrom it is further transferred into the lime reburning kiln (5).
    • 用于石灰泥热处理的方法和设备包括通过从石灰再燃烧窑排出的烟道气干燥待引入石灰再燃窑(5)中的石灰泥(5)以便再生 石灰泥的石灰含量。 从干燥过滤器(6)中将浓缩至超过75%,优选至80%的干固体含量的石灰泥引入进料室(2)中,烟道气的可调节部分通过该进料室传导。 取决于气体量,100%或更少的石灰泥与气体一起夹带到干燥器(3)中,其余部分落入进料室的下部(14),从那里进一步转移到石灰 再烧窑(5)。
    • 3. 发明授权
    • Heat treatment of expansible materials to form lightweight aggregate
    • 可膨胀材料的热处理形成轻骨料
    • US5482458A
    • 1996-01-09
    • US244046
    • 1994-05-23
    • Robin A. Kyffin
    • Robin A. Kyffin
    • C04B20/06F27B7/20F27B7/34F27B15/00
    • C04B20/061F27B7/2016F27B7/34F27B2007/2008F27M2003/09
    • A rotary kiln (10) is employed which is inclined downwardly from its charge end (12) to its discharge end (14) and has a maximum length to breadth ratio of 5:1. The interior space of the kiln (10) is heated by means of at least one burner (B1, B2) directed into the kiln from one end thereof to a substantially constant elevated process temperature. Material is fed into the kiln (10) so that it occupies a maximum of 10% of the cross-sectional area of the internal space of the kiln (10) at the charge end (12). Upon entering the kiln the material is subjected almost immediately to the required process temperature. As it moves along the bottom of the kiln (10) from the charge to the discharge end (14), heat transfer to the material is primarily by radiation from the combustion space and from the lining of the kiln (10).
    • PCT No.PCT / GB92 / 02188 Sec。 371日期1994年5月23日 102(e)日期1994年5月23日PCT提交1992年11月26日PCT公布。 公开号WO93 / 11084 日期:1993年6月10日。采用从其充电端(12)向下倾斜到其排出端(14)的回转窑(10),其最大长度与宽度比为5:1。 窑(10)的内部空间借助至少一个从其一端引导到窑炉中的燃烧器(B1,B2)被加热到基本上恒定的升高的过程温度。 材料被输送到窑(10)中,使得其在充电端(12)处占据窑(10)的内部空间的横截面面积的最大值的10%。 进入窑后,材料几乎立即进入所需的工艺温度。 当其沿着窑(10)的底部从电荷移动到排放端(14)时,对材料的热传递主要是来自燃烧空间和来自窑(10)的衬里的辐射。
    • 4. 发明授权
    • Method for processing colemanite ore
    • 石英矿石加工方法
    • US3865541A
    • 1975-02-11
    • US40831873
    • 1973-10-23
    • TENNECO OIL CO
    • WILSON DAVIDBURWELL BLAIR T
    • B01J6/00F27B7/00F27B7/16F27B7/20F27B7/14
    • C01B35/10B01J6/002C01B35/06C01B35/12F27B7/00F27B7/162F27B7/2016F27B2007/2008
    • In the method, a hot gas is flowed linearly through a slightly inclined treating area. Colemanite ore particles are repeatedly elevated and dropped substantially vertically through the gas while they are simultaneously advanced countercurrent to the gas flow. This movement is continued until the ore particles are heated to the point of decrepitation at which they relatively suddenly break into a large number of relatively fine particles of substantially sure colemanite which are carried out of the treating area by the gas stream. The gas carried colemanite particles are then separated from the gas stream to provide an upgraded and classified product. Gas velocity and temperature and the path and rate of movement of the ore through the gas are varied as required to obtain a given grade or size in the recovered colemanite product. The apparatus used in practicing the method includes, in a preferred form, a tubular calcining drum which is inclined slightly with respect to the horizontal. Lifters are positioned along the internal wall of the calcining drum and the drum is rotated between two stationary end assemblies. Ore particles are introduced into the upper end of the drum and a stream of hot gas is introduced through the lower end of the drum. Rotation of the drum causes the ore to be repeatedly lifted and dropped across the gas stream while the ore simultaneously advances from the upper toward the lower end of the drum. The temperature of the advancing ore increases to the point required to cause decrepitation of the ore, and the gas stream flowing through the drum carries the particles of decrepitation to the upper end of the drum where they are removed and separated from the gas stream. In the preferred form, gas leaving the drum is conveyed to a second rotating, inclined drum which functions as a preheater for ore being introduced into the calcining drum.
    • 在该方法中,热气体直线地流过稍微倾斜的处理区域。 钴黑矿石颗粒被重复地升高并基本垂直地流过气体,同时它们与气流逆流地同时进行。 这一运动继续进行,直到矿石颗粒被加热到爆炸点,在这一点,它们相对突然地分解成大量由气流从处理区域进行的基本上可靠的煤灰岩的相对细小的颗粒。 然后将携带的煤烟气颗粒与气流分离,以提供升级和分类的产品。 气体速度和温度以及矿石通过气体的运动路径和速率根据需要而变化,以在回收的煤le石产品中获得给定的等级或尺寸。
    • 7. 发明授权
    • Rotary kiln for shock sintering
    • 旋转刀具用于冲击烧结
    • US3584850A
    • 1971-06-15
    • US3584850D
    • 1969-07-02
    • UNITED STATES STEEL CORP
    • BRANDVOLD WILLIAM WTRESOUTHICK STEWART W
    • C22B1/24F27B7/02F27B7/04F27B7/20F27B7/32F27B7/38F27B7/42F27B7/00
    • C22B1/2406C22B1/2413F27B7/32F27B7/386F27B7/42F27B2007/022F27B2007/025F27B2007/046F27B2007/2008F27B2007/327
    • This invention relates to a method of and apparatus for pyroprocessing raw material having a reaction temperature and containing moisture into sinter. The apparatus has a rotary kiln adapted to receive the raw material pellets at one end of the rotary kiln and to move the raw material pellets along a path of movement in the rotary kiln to the other end of the rotary kiln. Heating means are adjacent the other end of the rotary kiln for directing a heated fluid through the rotary kiln, the rotary kiln having a drying means adjacent the one end of the rotary kiln for heating the raw material pellets by the heated fluid to substantially remove the moisture in the raw material pellets. Cooling means communicate with the drying means for mixing a cooling fluid with the heated fluid to limit the temperature in the drying means below the temperature at which the raw material pellets explode due to rapid heating to a deleteriously high temperature. The rotary kiln has a preheating zone adjacent the drying means further along the path of movement for heating the raw material pellets to a temperature below the reaction temperature. The rotary kiln has a reaction zone adjacent the other end of the rotary kiln for heating the raw material pellets above the reaction temperature to pyroprocess the raw material pellets into the sinter. Restriction means are between the preheating zone and the reaction zone for damming a reservoir of the raw material pellets adjacent the restriction means so that the reservoir of the raw material pellets is protected from the direct radiation of the heated fluid and the temperature of the reservoir of raw material pellets remains unaffected by instantaneous changes in the temperature of the heated fluid, the restriction means being operable to meter minimum layers of the raw material pellets into the reaction zone so that the minimum layers of the raw material pellets are individually and rapidly heated to the reaction temperature by the heated fluid and the raw material pellets are converted into sinter. The method includes the steps of receiving the raw material pellets at one end of a rotary kiln and moving the raw material pellets along a path of movement in the rotary kiln to the other end of the rotary kiln; directing a heated fluid through the rotary kiln; heating the raw material pellets by the heated fluid adjacent the one end of the rotary kiln to substantially remove the moisture in the raw material pellets; mixing a cooling fluid with the heated fluid to limit the temperature (during the removal of the moisture) below the temperature at which the raw material pellets explode due to rapid heating to a deleteriously high temperature; heating the raw material pellets in a preheating zone of the rotary kiln further along the path of movement to a temperature below the reaction temperature; damming a reservoir of the raw material pellets adjacent the preheating zone and further along the path of movement so that the reservoir of the raw material pellets is protected from the direct radiation of the heated fluid and the temperature of the reservoir of the raw material pellets remains unaffected by instantaneous changes in the temperature of the heated fluid; metering minimum layers of the raw material pellets adjacent the preheating zone and further along the path of movement into a reaction zone of the rotary kiln adjacent the other end of the kiln; and heating raw material pellets individually and rapidly in the reaction zone of the rotary kiln to indivIdually and rapidly heat the raw material pellets to the reaction temperature by the heated fluid, thus converting the raw material pellets into the sinter.
    • 9. 发明申请
    • FEEDING SYSTEM FOR A LIME REBURNING KILN
    • 饲养系统用于跛行
    • WO1991000251A1
    • 1991-01-10
    • PCT/FI1990000172
    • 1990-06-28
    • A. AHLSTROM CORPORATIONAHVENAINEN, Arto
    • A. AHLSTROM CORPORATION
    • C04B02/10
    • C04B2/10F27B7/3205F27B2007/163F27B2007/2008C04B2/005
    • A method and apparatus for heat treatment of lime mud comprises drying of the lime mud to be introduced into the lime reburning kiln (5) in a pneumatic dryer (3) by means of flue gases discharged from the lime reburning kiln in order to regenerate the lime content of the lime mud. From a drying filter (6), the lime mud thickened to a dry solids content of over 75 %, preferably to 80 %, is introduced into a feed chamber (2) through which an adjustable portion of the flue gas is conducted. Depending on the gas amount, 100 % or less of the lime mud is entrained with the gas into the dryer (3), the remaining portion falling into the lower section (14) of the feed chamber, wherefrom it is further transferred into the lime reburning kiln (5).
    • 用于石灰泥的热处理的方法和装置包括通过从石灰再生窑排出的烟道气在气动干燥器(3)中干燥待引入石灰再生窑(5)中的石灰泥,以便再生 石灰泥的石灰含量。 从干燥过滤器(6)中,将加到干燥固体含量超过75%,优选至80%的石灰泥浆引入进料室(2)中,通过该进料室可以调节烟道气的一部分。 取决于气体量,100%以下的石灰泥被气体引入干燥器(3)中,其余部分落入进料室的下段(14),从而进一步转移到石灰 再烧窑(5)。
    • 10. 发明申请
    • HEAT TREATMENT OF EXPANSIBLE MATERIALS TO FORM LIGHTWEIGHT AGGREGATE
    • 可膨胀材料的热处理形成轻型聚合物
    • WO1993011084A1
    • 1993-06-10
    • PCT/GB1992002188
    • 1992-11-26
    • KYFFIN, Robin, Anthony
    • C04B20/06
    • C04B20/061F27B7/2016F27B7/34F27B2007/2008F27M2003/09C04B14/10C04B20/068
    • A rotary kiln (10) is employed which is inclined downwardly from its charge end (12) to its discharge end (14) and has a maximum lenght to breadth ratio of 5:1. The interior space of the kiln (10) is heated by means of at least one burner (B1, B2) directed into the kiln from one end thereof to a substantially constant elevated process temperature. Material is fed into the kiln (10) so that it occupies a maximum of 10 % of the cross-sectional area the interior space of the kiln at the charge end. Upon entering the kiln the material is subjected almost immediately to the required process temperature. As it moves along the bottom of the kiln from the charge to the discharge end, heat transfer to the material is primarily by radiation from the combustion space and from the lining of the kiln.
    • 使用从其充电端(12)向下倾斜到其排出端(14)的回转窑(10),并且具有最大长度与宽度之比为5:1。 窑(10)的内部空间借助至少一个从其一端引导到窑炉中的燃烧器(B1,B2)被加热到基本上恒定的升高的过程温度。 将材料进料到窑炉(10)中,使其在充电端占据窑内部空间的横截面积的最大值的10%。 进入窑后,材料几乎立即进入所需的工艺温度。 当它从窑的底部从充电器移动到排出端时,材料的热传递主要是来自燃烧空间和窑内衬的辐射。