DE2103060C - Device for importing kor mgen bulk goods in a pressurized conveying line - Google Patents
Device for importing kor mgen bulk goods in a pressurized conveying lineInfo
- Publication number
- DE2103060C DE2103060C DE19712103060 DE2103060A DE2103060C DE 2103060 C DE2103060 C DE 2103060C DE 19712103060 DE19712103060 DE 19712103060 DE 2103060 A DE2103060 A DE 2103060A DE 2103060 C DE2103060 C DE 2103060C
- Authority
- DE
- Germany
- Prior art keywords
- funnel
- pipe
- tube
- conveying
- feed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000463 material Substances 0.000 claims description 17
- 239000007787 solid Substances 0.000 claims description 4
- 230000003068 static Effects 0.000 claims description 3
- 230000001413 cellular Effects 0.000 claims 3
- 210000003800 Pharynx Anatomy 0.000 claims 1
- 210000001138 Tears Anatomy 0.000 claims 1
- 238000005299 abrasion Methods 0.000 claims 1
- 238000003780 insertion Methods 0.000 claims 1
- 238000009423 ventilation Methods 0.000 claims 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 239000010431 corundum Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
Description
und 32, weiche die Rohre überragen. Wenn Material in den Trichter 32 eingeführt wird, entweicht das Gas nur noch durch den Zwischenraum zwischen den beiden Trichtern, ohne jedoch den Zulauf und die Geschwindigkeitszunahme des unter der Wirkung der Schwerkraft im Rohr 3 abwärts bewegten Materials zu behindern. Am unteren Ende 31 dieses Rohres reicht die Geschwindigkeit des Gutes für die Erzeugung eines Gegendrucks im Rohr 2 aus, der den Aufstieg von Luft in diesem Rohr praktisch zum Verschwinden bringt: Das Material setzt also seine Abwärtsbewegung fort und tritt längs der Pfeile 30 in die Leitung 1 ein. Es wird dann durch den Pfeil 10 angedeuteten Gasstrom mitgenommen.and 32, which protrude beyond the tubes. When material is introduced into hopper 32, the gas escapes only through the space between the two funnels, but without the inlet and the increase in speed to hinder the material moved downward under the action of gravity in the pipe 3. At the lower end 31 of this tube is enough the speed of the material for the generation of a back pressure in the pipe 2, which causes the ascent of air practically disappears in this pipe: The material thus continues its downward movement continues and enters line 1 along arrows 30. It is then indicated by the arrow 10 Gas stream taken.
Wenn die Beaufschlagung mit Feststoff zu hoch ist, füllen sich die Rohre 2 und dann 3 vollständig mit Material. Der von der Geschwindigkeit des Materials herrührende Gegendruck nimmt ab; er wird nun jedoch durch einen statischen Gegendruck ersetzt, der gleich der Höhe der Materialsäule istIf the loading of solids is too high, pipes 2 and then 3 fill completely with material. The back pressure resulting from the speed of the material decreases; he will now but replaced by a static counterpressure that is equal to the height of the column of material
Unabhängig von der Matenalbeauf schlagung ergeben sich also in der Vorrichtung Bedingungen einerRegardless of the material impact, there are conditions in the device
dichten Einführung ohne Aufstau von Gas oder Mate-τι ill tight introduction without accumulation of gas or material τι ill
Die Vorrichtung ist sehr einfach, bfflig und nicht
anfällig in bezug auf Pannen und Abneb.
Sie wird abgewandt für die Einspeisung von ge-The device is very simple, simple and not prone to breakdowns and loss.
It is turned away for the infeed of
körntem Korund einer Korngröße unter 5 mm m eine pneumatische Förderleitung mit einem horizontalen Abschnitt von 10 m Länge, an den sich ein vertikaler Abschnitt von 12 m Länge anschließt. Das Rohr 2 hat einen Innendurchmesser von 50 mm bei einer Hohegranular corundum with a grain size of less than 5 mm m a pneumatic conveying line with a horizontal section of 10 m in length, to which a vertical section of 12 m in length is connected. The pipe 2 has an inner diameter of 50 mm at a height
von 800 mm (ohne den Trichter). Das Rohr 3 hat einen Innendurchmesser von 40 mm. Der Druck m der Leitung 1 beträgt 0,08 bar. Der Durchsatz an Material beträgt 3,5 t/Std.of 800 mm (without the funnel). The tube 3 has an inside diameter of 40 mm. The pressure m in line 1 is 0.08 bar. The throughput of material is 3.5 t / hour.
Hierzu 1 Blatt Zeichnungen1 sheet of drawings
Claims (2)
Rohr (3) anschließt. Aus der britischen Patentschrift 736 207 ist1. Device for introducing granular Mas pipe ends immediately above the cell edge and surrounded by senguts in a pressurized form 5 a weiderleitung connected to the cellular wheel housing, consisting of a vertical pipe in th, which is in the upper area with the delivery line protruding, is provided there in ventilation openings. Through this supply direction opening feed pipe, the top order of which is supposed to merge into a funnel shape due to leaks at the end of the meter, the air passing by without disturbing the air that flows into the io grain inflow via the openings into the atmosphere conveying line (1) protruding section of the discharged. If, however, the bulk material inlet feed pipe (2) is flat transversely to the conveying direction, it is occasionally transported away through the cellular wheel and squeezed, so that a thin opening gap (21) exceeds the pressure pipe, collects in the annular space for the bulk material, and that remains inside between the funnel pipe and in the vent pipe of the funnel (22) a second funnel (32) with excess grain material, which is then immediately sorted, to which a second funnel can be blown downwards.
Pipe (3) connects. From British Patent 736 207 is
gierenden-divergierenden Düsen, statischen Schleusen Gemäß einer bevorzugten Ausführungsform derThe introduction of granular bulk goods in 40 remains for the bulk goods, and that a second funnel is arranged within the space with air circulation or blower overpressure funnel, to which, according to the prior art, a second tube is connected with the help of a convergent downward,
yawing-diverging nozzles, static locks According to a preferred embodiment of the
Diese Vorrichtung hat zum einen den Mangel, daß nur 50 In der Zeichnung ist ein Ausführungsbeispiel der geringe Durchsätze möglich sind und zum anderen Ausbildung gemäß der Erfindung im Schnitt dargetritt am divergierenden Teil der Anordnung wegen der stellt.The converging or the junction between the outer funnel and the diverging nozzle connected in a conduit is designed so that at its and the feed tube, with a negative pressure prevailing between the end of the throat, which feeds the second tube and the inner wall of the outer of solids into close to the neck. An annular gap remains in the funnel.
On the one hand, this device has the shortcoming that only 50. In the drawing, an embodiment of the low throughputs is possible and, on the other hand, the training according to the invention is shown in section on the diverging part of the arrangement because of the.
vor allem beim Fördern von Feststoffen auf, die einen Wenn die Vorrichtung leer ist, entweicht DruckgasIn the case of static locks, the lock chamber has a funnel 22 at the end. The feed pipe 2 is at the top and bottom a valve or a slide, which is squeezed flat at its lower end in such a way that an alternating filling of the lock space with a thin opening gap 21 running in the direction of flow of the compressed gas (arrow atmospheric pressure and emptying into the transport 10) forms. In line made possible. Such a device 6 ° the funnel 22 of the feed pipe 2 is a second one is generally provided twice, so that a funnel 32 is introduced, which can be ensured continuous operation at its lower end, a second pipe 3 with an end 31 open at the bottom each of the one lock chamber has material, the end open at the bottom receiving above the, while the other is emptied into the transport line connecting point 23 between the outer funnel. In this device 65 occur 22 and its feed pipe 2 is located. The path of the disturbance due to wear of the valves or slides for bulk goods is marked by the arrows 30,
Especially when conveying solids, which have a When the device is empty, pressurized gas escapes
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7002225A FR2096386B1 (en) | 1970-01-22 | 1970-01-22 | |
FR7002225 | 1970-01-22 |
Publications (2)
Publication Number | Publication Date |
---|---|
DE2103060A1 DE2103060A1 (en) | 1971-07-29 |
DE2103060C true DE2103060C (en) | 1973-04-26 |
Family
ID=
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE3003919C2 (en) | ||
DE3115125C2 (en) | ||
DE4414233A1 (en) | Device for measuring powdered or granular material to be weighed | |
DE964463C (en) | Device for sorting and discharging pneumatically conveyed bulk material | |
DE3012065A1 (en) | Bulk material vessel pneumatic discharge equipment - has separate supply system for top nozzles and bottom nozzles | |
DE69102812T2 (en) | Device for controlling the grinding process of roasted coffee. | |
DE2103060C (en) | Device for importing kor mgen bulk goods in a pressurized conveying line | |
DE2443552A1 (en) | Filling unit for sand bunkers on tram cars - with pressurized containers between hopper and filling hoses | |
DE1642918B2 (en) | Method and device for dosing a powdery! Good | |
DE2616430B2 (en) | Device for collapsing chimneys in the case of a conically narrowing discharge funnel for pneumatically conveyable bulk material | |
DE2363505A1 (en) | Feeder for pneumatic conveying plant - has portion of clean air diverted on discharge end of cell wheel | |
EP0247235B1 (en) | Pressurized-air conveyor and metering device | |
DE2623705A1 (en) | DISCHARGE DEVICE FOR SCHUETTGUETER | |
DE2103060A1 (en) | Static device for the continuous feeding of pressure rooms | |
DE2252870A1 (en) | METHOD AND DEVICE FOR PNEUMATIC CONVEYING | |
DE898109C (en) | Device for circulating or mixing floury, powdery or grainy substances | |
DE834450C (en) | Dosing scales for continuous and constant weight feeding of pourable materials | |
DE2206763C3 (en) | ||
DE1182594B (en) | Device for the uniform discharge of dust-like goods from a closed container into a conveyor line via a material discharge pipe | |
DE738601C (en) | Connecting chute between a sieve and a conveyor belt | |
DE1586083C (en) | Device for removing air oxygen from debris to be packed good | |
DE455929C (en) | Device for conveying dry, fine sand, especially for filling the sand cans of locomotives | |
DE426838C (en) | Device for emptying containers with dust-like material | |
DE442121C (en) | Discharge device for compressed air conveying systems with discharge of the conveying air from the line in front of the discharge end of the conveyed material | |
DE959266C (en) | Feed container for dosing a grainy solid into a gas stream |