公开(公告)号：US4940478A

公开(公告)日：1990-07-10

申请号：US243240

申请日：1988-09-08

申请人： Wilfried Naber ,  Heinz-Jurgen Ungerer ,  Klaus Sistermann

发明人： Wilfried Naber ,  Heinz-Jurgen Ungerer ,  Klaus Sistermann

IPC分类号： B01D46/30 ,  C03B3/02 ,  C03B5/237 ,  F23J15/02 ,  F23L15/00

CPC分类号： C03B3/023 ,  B01D46/30 ,  C03B5/237 ,  F23J15/02 ,  F23L15/00 ,  F23J2215/20 ,  F23J2215/30 ,  F23J2219/60 ,  Y02E20/348 ,  Y02P40/535

摘要： A process of melting silicate raw materials includes the steps of using the tank exhaust gases to heat the combustion air, using the tank exhaust gases to preheat a mixture of raw materials, removing acid gaseous aggressive media from the tank exhaust gases, then using the tank exhaust gases to preheat the combination air. Because the acid gaseous aggressive media are removed from the tank exhaust gases before the tank exhaust gases are used to preheat the combustion air, more heat can be withdrawn from the tank exhaust gases than was heretofore possible, since there is no danger of acid condensation even when the tank exhaust gases are cooled to near ambient temperature.

摘要翻译： 硅酸盐原料的熔化过程包括以下步骤：使用罐废气来加热燃烧空气，使用罐废气来预热原料混合物，从罐废气中除去酸性气体腐蚀性介质，然后使用罐 废气预热组合空气。 因为在罐排气用于预热燃烧空气之前，酸性气体腐蚀性介质被从罐排气中除去，因此即使没有酸冷凝的危险，也可以从罐排气中抽出更多的热量 当油箱废气冷却到接近环境温度时。

公开(公告)号：US4822392A

公开(公告)日：1989-04-18

申请号：US111125

申请日：1987-10-22

申请人： Gaston Fachat ,  Klaus Sistermann ,  Heinz-Jurgen Ungerer

发明人： Gaston Fachat ,  Klaus Sistermann ,  Heinz-Jurgen Ungerer

IPC分类号： C03B37/06 ,  C03C25/02

CPC分类号： C03B37/06

摘要： Apparatus for producing mineral fibres from silicate raw materials such as basalt by blast drawing.When blast drawing is used to produce mineral fibres from basalt, there is arranged between the entry zone (26) of the chute (16) and the exit zone of the nozzle slot (10) of the blast nozzle unit (8), this slot forming the fiberization duct, a guide cell (13). The relative position of the side walls (29) of the guide cell is freely adjustable, so that desired flow conditions can be set and also the exit direction of the exit flow bundle (31) and hence the web formation can be controlled. As a consequence of a lateral distance (a) of the exit orifice (28) of the guide cell (13) relative to the entry flow bundle (27) additional secondary air is sucked in, which has a further cooling effect on the fibres. At the exit orifice (30) from the guide cell (13) the flow is restructured and emerges as a cooled exit flow bundle (31) and is at that point initially subjected to a further cooling with cooling water applied by spray nozzles (14 ) and by further secondary air sucked into this zone before the application of binder from spray nozzles (15). The spray axis (15a) of the spray nozzles (15) forms an acute angle (.alpha.) with the axis (11a) of the exit flow bundle (31) in order to ensure homogeneous incorporation of binder into the flow bundle (31).

摘要翻译： 用于从硅酸盐原料如玄武岩通过喷丸生产矿物纤维的设备。 当用玄武岩生产矿物纤维时，布置在滑槽（16）的进入区（26）和喷嘴单元（8）的喷嘴槽（10）的出口区之间，这个槽 形成纤维化导管，引导单元（13）。 引导单元的侧壁（29）的相对位置是可自由调节的，从而可以设定所需的流动条件，并且还可以控制出口流束（31）的排出方向，从而可以控制卷材的形成。 作为引导单元（13）相对于进入流束（27）的出口孔（28）的横向距离（a）的结果，附加的二次空气被吸入，这对纤维具有进一步的冷却效果。 在来自引导单元（13）的出口孔（30）处，流动被重组并作为冷却的出口流束（31）而出现，并且在该点处最初经由喷嘴（14）施加的冷却水进一步冷却， 并且在从喷嘴（15）施加粘合剂之前通过进一步的二次空气吸入该区域。 喷嘴（15）的喷射轴（15a）与出口流束（31）的轴线（11a）形成锐角（α），以确保粘合剂均匀地结合到流束（31）中。

公开(公告)号：US4698086A

公开(公告)日：1987-10-06

申请号：US839225

申请日：1986-03-13

申请人： Gaston Fachat ,  Klaus Sistermann ,  Heinz-Jurgen Ungerer

发明人： Gaston Fachat ,  Klaus Sistermann ,  Heinz-Jurgen Ungerer

IPC分类号： C03B37/06

CPC分类号： C03B37/06

摘要： To produce basalt wool having a large fibre diameter of if desired 10 .mu.m with high output and low bead formation, the exit cross-section of the exit orifices (6) of the distributor tank (5), the vertical distance (vA) between the exit orifices (6) and the blow-in slits (29) for propellant gas, the horizontal width (hB) of the nozzle slot (10) and the vertical length (vL) of the nozzle slot (10) downstream of the blow-in slits (29) are dimensioned to be unusually large for an apparatus for producing rock fibres by blast drawing. As a result, it is possible to operate at a low melt temperature and a high propellant gas rate combined with a low propellant gas pressure in order, surprisingly, to obtain a coarse-fibered product with low bead formation and high output. In the area of the blow-in slits (29) the airguide lips (28) advantageously form an abruptly terminated slot constriction in order to assist the fiberization therein and to utilize the subsequent long vertical length (vL) of the nozzle slot (10) in full for fiber drawing without thereby incurring marked bead formation.

摘要翻译： 为了生产具有大纤维直径的玄武岩羊毛，如果需要，10米，高产量和低珠粒形成，分配罐（5）的出口孔（6）的出口横截面，垂直距离（vA）在 出口孔（6）和用于推进气体的吹入狭缝（29），喷嘴槽（10）的水平宽度（hB）和喷嘴槽（10）在吹气下游的垂直长度（vL） - 狭缝（29）的尺寸对于通过鼓风拉制生产岩石纤维的装置是非常大的。 结果，可以在低熔体温度和高推进剂气体速率下结合低推进剂气体压力进行操作，令人惊奇的是获得具有低珠粒形成和高输出的粗纤维产品。 在吹入狭缝（29）的区域中，空气引导嘴唇（28）有利地形成突然终止的槽狭窄，以帮助其中的纤维化并利用喷嘴槽（10）的随后的长垂直长度（vL） 完全用于纤维拉伸，而不会引起明显的珠粒形成。

公开(公告)号：US4263034A

公开(公告)日：1981-04-21

申请号：US94168

申请日：1979-11-14

申请人： Klaus Sistermann ,  Hans Gartner

发明人： Klaus Sistermann ,  Hans Gartner

IPC分类号： C03B37/04 ,  C03B37/06

CPC分类号： C03B37/048 ,  C03B37/06

摘要： A process and apparatus for controlling the operating conditions, particularly the temperature and pressure, of attenuating gas employed in the fiberization of thermoplastic materials. The arrangement disclosed provides for temperature and pressure controls of the hot attenuating gas blast used in connection with a centrifugal or spinner type of technique for making fibers from thermoplastic mineral materials such as glass.

摘要翻译： 用于控制在热塑性材料纤维化中使用的减弱气体的操作条件，特别是温度和压力的方法和装置。 所公开的装置提供了与用于从热塑性矿物材料如玻璃制造纤维的离心或旋转式技术相关的热衰减气体鼓风的温度和压力控制。