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    • 1. 发明公开
    • Discharge device for particulate material
    • EntleerungsvorrichtungfürSchüttgut。
    • EP0281231A2
    • 1988-09-07
    • EP88300523.3
    • 1988-01-22
    • Westelaken, Christianus Marinus Theresia
    • Westelaken, Christianus Marinus Theresia
    • B65G65/42
    • B65G65/42
    • A device is described for withdrawing particulate material from a series of outlets extending across the bottom of a storage container or bin (10). The outlets are arranged in a row with each outlet having a front wall and a rear wall (16). A discharge channel is positioned beneath the row of outlets and in alignment with the row, the channel having parallel side walls extending downwardly adjacent the sides of the outlets, a platform (15) joining the side walls and an endless conveyor (17) adapted to move longitudinally within the channel along the plat­form. The bottom ends of the outlet front and rear walls (16) are vertically spaced from the conveyor on the platform in progressively increasing amounts in the direction of travel of the conveyor, whereby particulate material can be discharged at a substantially uniform rate across the storage bin.
    • 描述了一种用于从延伸穿过存储容器或垃圾箱(10)的底部的一系列出口排出颗粒材料的装置。 出口布置成一排,每个出口具有前壁和后壁(16)。 排出通道位于出口排下方并与排对齐,通道具有平行的侧壁,邻近出口的侧面向下延伸,连接侧壁的平台(15)和适于 沿着平台沿通道纵向移动。 出口前壁和后壁(16)的底端在平台上与输送机垂直地间隔开,在输送机的行进方向上逐渐增加的量,从而颗粒材料可以以大体均匀的速率排出储存箱 。
    • 2. 发明公开
    • Multi-stage particulate material dryer having channelized discharge
    • 具有通道排放的多级颗粒物料干燥剂
    • EP0206069A3
    • 1987-02-25
    • EP86107817
    • 1982-06-17
    • Westelaken, Christianus Marinus Theresia
    • Westelaken, Christianus Marinus Theresia
    • F26B17/12F26B25/00
    • F26B17/122F26B25/002
    • @ A gravity-flow grain dryer (10) for particulate material comprises first and second generally vertical drying columns (68, 100) spaced apart to provide a plenum chamber (112) therebetween, the drying columns each having opposed spaced walls (20, 70, 108, 110) with perforate portions. Drying air is passed through the perforate portions in a treating zone in the columns (68, 100). First and second inputs (32, 72, 90, 96) are provided for introducing particulate material into top portions of the first and second drying columns (68, 100), respectively. First, second, third and fourth discharge means (84, 82, 126, 124) are also provided for removing particulate material from bottom portions of the first and second drying columns (68, 100), respectively. Associated with the first and second discharge means (82, 84) is a dividing wall (76) which extends between a pair of the spaced walls (20, 70) below the treating zone of the column (68) for dividing a bottom portion of the column into at least two channels (78, 80). The first discharge means (84) is associated with a first of the channels (80) and the second discharge means (82) is associated with a second of the channels (78). The first channel (80) is adjacent the first wall (70) and the first discharge means (84) is adapted to discharge particulate material at a rate faster than the second discharge means (82).
    • 3. 发明公开
    • Discharge device for particulate material
    • 用于颗粒材料的放电装置
    • EP0281231A3
    • 1988-10-26
    • EP88300523
    • 1988-01-22
    • Westelaken, Christianus Marinus Theresia
    • Westelaken, Christianus Marinus Theresia
    • B65G65/42
    • B65G65/42
    • A device is described for withdrawing particulate material from a series of outlets extending across the bottom of a storage container or bin (10). The outlets are arranged in a row with each outlet having a front wall and a rear wall (16). A discharge channel is positioned beneath the row of outlets and in alignment with the row, the channel having parallel side walls extending downwardly adjacent the sides of the outlets, a platform (15) joining the side walls and an endless conveyor (17) adapted to move longitudinally within the channel along the plat­form. The bottom ends of the outlet front and rear walls (16) are vertically spaced from the conveyor on the platform in progressively increasing amounts in the direction of travel of the conveyor, whereby particulate material can be discharged at a substantially uniform rate across the storage bin.
    • 描述了一种用于从延伸穿过存储容器或垃圾箱(10)的底部的一系列出口排出颗粒材料的装置。 出口布置成一排,每个出口具有前壁和后壁(16)。 排出通道位于出口排下方并与排对齐,通道具有平行的侧壁,邻近出口的侧面向下延伸,连接侧壁的平台(15)和适于 沿着平台沿通道纵向移动。 出口前壁和后壁(16)的底端在平台上与输送机垂直地间隔开,在输送机的行进方向上逐渐增加的量,从而颗粒材料可以以大体均匀的速率排出储存箱 。
    • 4. 发明公开
    • Multi-stage particulate material dryer having channelized discharge
    • 具有通道排放的多级颗粒物料干燥剂
    • EP0068734A3
    • 1984-09-12
    • EP82303149
    • 1982-06-17
    • Westelaken, Christianus Marinus Theresia
    • Westelaken, Christianus Marinus Theresia
    • F26B17/12F26B25/00
    • F26B17/122F26B25/002
    • A gravity-flow grain dryer (10) for particulate material comprises first and second generally vertical drying columns (68, 100) spaced apart to provide a plenum chamber (112) therebetween, the drying columns each having opposed spaced perforate walls (26, 70, 108, 110). First and second inputs (32, 72, 90, 96) are provided for introducing particulate material into top portions of the first and second drying columns (68, 100), respectively. First and second discharge means (82, 84, 124, 126) are also provided for removing particulate material from bottom portions of the first and second drying columns (68, 100), respectively. The first discharge means (82, 84) includes a dividing wall (76) which extends between the perforate walls (26, 70) for dividing at least a portion of the column into at least two channels (78, 80), both of the channels containing a discharging mechanism (82, 84) for removing particulate mate- riai from the channel. A first discharge mechanism (84) is associated with a first of the channels (80) and a second discharge mechanism (82) is associated with a second of the channels (78). the first channel (80) being adjacent the first perforate wall (70) and the first discharge mechanism (84) is adapted to discharge particulate material at a rate faster than the second discharge mechanism (82). Conveyor means (90) is provided for receiving the particulate material discharged from the first drying column (68) and for conveying the particulate material to the second input (96). A flow of drying air is directed to the plenum chamber (112), whereby the drying air passes into the first and second drying columns (68, 100) to dry the particulate material, the drying air being subsequently discharged from the drying column.
    • 5. 发明公开
    • Air heating apparatus
    • 一种用于空气加热。
    • EP0068733A2
    • 1983-01-05
    • EP82303148.9
    • 1982-06-17
    • Westelaken, Christianus Marinus Theresia
    • Westelaken, Christianus Marinus Theresia
    • F26B23/02F26B17/12F24H3/08
    • F26B23/02F24H3/087F26B17/122
    • An apparatus (200) is provided for generating heated air, for example, for use in connection with a dryer (10) for particulate material, comprising a base portion (202) having a combustion chamber (204) and a burner (206) for providing a flow of combustion gas. A plurality of open tubes (208) having their first ends communicating with the combustion chamber (204) are provided for receiving the flow of combustion gas. The second ends of the tubes (208) extend beyond the base portion (202) into a tubular structure (210). connected to the base portion (202). The tubular structure (210) has partition means (218) for dividing it into a heat exchange chamber (220) adjacent the base portion (202) and surrounding the tubes (208) and a manifold chamber (222) remote from the base portion (202). The partition means (218) cooperates with the tubes (208) to direct the flow of combustion gas into the manifold chamber (222). Air inlets (223) are provided in one of the chambers (220, 222) and an air exhaust means communicates with the heat exchange chamber (220) via an opening (234) for causing ambient air to flow into the air inlets (223) and through the heat exchange chamber (220) to provide a flow of heated air through the opening (234).
    • 6. 发明公开
    • Air heating apparatus
    • 空气加热装置
    • EP0068733A3
    • 1984-09-19
    • EP82303148
    • 1982-06-17
    • Westelaken, Christianus Marinus Theresia
    • Westelaken, Christianus Marinus Theresia
    • F26B23/02F26B17/12F24H03/08
    • F26B23/02F24H3/087F26B17/122
    • An apparatus (200) is provided for generating heated air, for example, for use in connection with a dryer (10) for particulate material, comprising a base portion (202) having a combustion chamber (204) and a burner (206) for providing a flow of combustion gas. A plurality of open tubes (208) having their first ends communicating with the combustion chamber (204) are provided for receiving the flow of combustion gas. The second ends of the tubes (208) extend beyond the base portion (202) into a tubular structure (210). connected to the base portion (202). The tubular structure (210) has partition means (218) for dividing it into a heat exchange chamber (220) adjacent the base portion (202) and surrounding the tubes (208) and a manifold chamber (222) remote from the base portion (202). The partition means (218) cooperates with the tubes (208) to direct the flow of combustion gas into the manifold chamber (222). Air inlets (223) are provided in one of the chambers (220, 222) and an air exhaust means communicates with the heat exchange chamber (220) via an opening (234) for causing ambient air to flow into the air inlets (223) and through the heat exchange chamber (220) to provide a flow of heated air through the opening (234).
    • 7. 发明公开
    • Multi-stage particulate material dryer having channelized discharge
    • Mehrstufentrocknerfürkörniges材料mit kanalisierterAbführung。
    • EP0068734A2
    • 1983-01-05
    • EP82303149.7
    • 1982-06-17
    • Westelaken, Christianus Marinus Theresia
    • Westelaken, Christianus Marinus Theresia
    • F26B17/12F26B25/00
    • F26B17/122F26B25/002
    • A gravity-flow grain dryer (10) for particulate material comprises first and second generally vertical drying columns (68, 100) spaced apart to provide a plenum chamber (112) therebetween, the drying columns each having opposed spaced perforate walls (26, 70, 108, 110). First and second inputs (32, 72, 90, 96) are provided for introducing particulate material into top portions of the first and second drying columns (68, 100), respectively. First and second discharge means (82, 84, 124, 126) are also provided for removing particulate material from bottom portions of the first and second drying columns (68, 100), respectively. The first discharge means (82, 84) includes a dividing wall (76) which extends between the perforate walls (26, 70) for dividing at least a portion of the column into at least two channels (78, 80), both of the channels containing a discharging mechanism (82, 84) for removing particulate mate- riai from the channel. A first discharge mechanism (84) is associated with a first of the channels (80) and a second discharge mechanism (82) is associated with a second of the channels (78). the first channel (80) being adjacent the first perforate wall (70) and the first discharge mechanism (84) is adapted to discharge particulate material at a rate faster than the second discharge mechanism (82). Conveyor means (90) is provided for receiving the particulate material discharged from the first drying column (68) and for conveying the particulate material to the second input (96). A flow of drying air is directed to the plenum chamber (112), whereby the drying air passes into the first and second drying columns (68, 100) to dry the particulate material, the drying air being subsequently discharged from the drying column.
    • 用于颗粒材料的重力流谷物干燥器(10)包括间隔开以在其间提供增压室(112)的第一和第二大体垂直的干燥塔(68,100),所述干燥塔各自具有相对的隔开的穿孔壁(26,70 ,108,110)。 提供了第一和第二输入(32,72,90,96),用于将颗粒材料分别引入第一和第二干燥塔(68,100)的顶部。 还设置有第一和第二排出装置(82,84,124,126),用于分别从第一和第二干燥塔(68,100)的底部移除颗粒材料。 第一排出装置(82,84)包括在穿孔壁(26,70)之间延伸的分隔壁(76),用于将塔的至少一部分分成至少两个通道(78,80),两个通道 通道包含用于从通道去除颗粒材料的排放机构(82,84)。 第一排出机构(84)与第一通道(80)相关联,第二排放机构(62)与第二通道(78)相关联,第一通道(80)邻近第一穿孔壁 (70)和第一排出机构(84)适于以比第二排出机构(82)更快的速率排放颗粒材料。 提供输送装置(90)用于接收从第一干燥塔(68)排出的颗粒材料并将颗粒材料输送到第二输入(96)。 干燥空气流被引导到增压室(112),由此干燥空气进入第一和第二干燥塔(68,100)以干燥颗粒材料,干燥空气随后从干燥塔排出。