WO2001025121A1 - Device, method and container for handling bulk goods - Google Patents

Device, method and container for handling bulk goods Download PDF

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Publication number
WO2001025121A1
WO2001025121A1 PCT/SE2000/001914 SE0001914W WO0125121A1 WO 2001025121 A1 WO2001025121 A1 WO 2001025121A1 SE 0001914 W SE0001914 W SE 0001914W WO 0125121 A1 WO0125121 A1 WO 0125121A1
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WO
WIPO (PCT)
Prior art keywords
volume
gas
container
bulk goods
pressure
Prior art date
Application number
PCT/SE2000/001914
Other languages
French (fr)
Inventor
Thomas Wallin
Original Assignee
Bmh Marine Ab
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Bmh Marine Ab filed Critical Bmh Marine Ab
Priority to AU79783/00A priority Critical patent/AU7978300A/en
Publication of WO2001025121A1 publication Critical patent/WO2001025121A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D88/00Large containers
    • B65D88/54Large containers characterised by means facilitating filling or emptying
    • B65D88/72Fluidising devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • B65G53/16Gas pressure systems operating with fluidisation of the materials
    • B65G53/18Gas pressure systems operating with fluidisation of the materials through a porous wall
    • B65G53/22Gas pressure systems operating with fluidisation of the materials through a porous wall the systems comprising a reservoir, e.g. a bunker

Definitions

  • the present invention relates to a device and a method for handling bulk goods, such as cement powder, and a container for bulk goods. More specifically, the present invention relates to such a device as comprises a container with an inlet means and an outlet means arranged m a bottom region thereof, said container defining a volume which communicates with said inlet means and outlet means, and a gas unit for introducing gas, such as air, into the volume for applying a pressure above atmospheric which prevails therein and which acts to discharge bulk goods in the volume via the outlet means, and a corresponding method.
  • a device comprising an intermediate storage container is frequently used.
  • the bulk goods are fed into the intermediate storage con- tainer during a filling phase by means of a suitable device, such as a feeding hopper, a screw, belt or chain unit or a pneumatic unit for drawing in the bulk goods into the container.
  • a suitable device such as a feeding hopper, a screw, belt or chain unit or a pneumatic unit for drawing in the bulk goods into the container.
  • the container is pressurised. All connections to the con- tainer are closed, after which gas is introduced into the container.
  • an outlet valve is opened, whereby the bulk goods are pressed out of the container via the outlet valve to a conveyor pipe for further transport to, for example, a storage silo. Gas is continuously introduced into the container for maintaining a requisite pressure above atmospheric in the same.
  • the intermediate storage container When the intermediate storage container is being pressurised during the emptying phase, the bulk goods m the container are compressed. As a result, the viscosity of the bulk goods increases, which makes the discharge of the bulk goods via the outlet difficult. For this reason, a number of nozzles are normally arranged m connection with the outlet, through which nozzles gas is introduced into the container.
  • the container can be designed m such manner that all the gas, or only part thereof, which is introduced into the container for pressurising the same, is introduced via the nozzles.
  • the gas introduced into the container via the nozzles counteracts the compression caused by the pressure above atmospheric by the viscosity of the bulk goods being lowered. Consequently, the discharge of the bulk goods from the container is facilitated.
  • devices of the type described above comprise at least two such containers, which operate alternately, i.e. one is being filled as the other is being emptied and vice versa.
  • the con- tamer should be pressurised as quickly as possible. This requires that a fairly large gas flow be introduced into the container through the nozzles to counteract said com- pression of the bulk goods.
  • the high gas flow means that the gas speed through the nozzles becomes high, which m itself causes compression of the bulk goods. Owing to the compression of the bulk goods, the subsequent emptying phase will take a longer time. Consequently, a shortened pressurising phase results m an extended emptying phase .
  • a discharging device differs from the type described above m that it comprises a breakmg-up bottom m the area of the discharge means of the respective containers.
  • the bulk goods located straight above the breakmg-up bottom are fluidised through the same, thereby preventing compression connection with pressurising.
  • each container nozzles are arranged, which act to break up the non-fluidised bulk goods, so that they fall into the fluidised area.
  • the device also comprises pressure control devices, which sense the pressure in each container and, m response to measuring of predetermined pressures, send signals to actuators for opening of outlet valves.
  • This discharging device is well suited for discharging a load of a bulk vehicle to, for example, a silo.
  • the device is not suited for continuous discharging of a shipload where a quick change between filling phase and emptying phase, as well as quick emptying, is required.
  • the reason for this is that quick pressurisation of a container inevitably causes compression of the non-fluidised bulk goods, and that the device operates against predetermined pressure levels for initiating emptying, which pressure levels necessarily are not optimal.
  • an object of the present invention is to provide an improved device for handling bulk goods.
  • a specific object is to provide a device comprising a container which allows a quick change between filling phase and emptying phase as well as quick emptying of bulk goods positioned therein.
  • Another specific object is to provide a method which allows a quicker change between filling and emptying as well as quicker emptying of bulk goods from a container of a device of the type described above.
  • the objects are achieved by a device for handling bulk goods, having the features stated claim 1, a container for bulk goods having the features stated claim 9, and a method for handling bulk goods having the features stated claim
  • a device for handling bulk goods, comprising a container with an inlet means and an outlet means arranged a bottom region thereof, said container defining a volume communicating with said mlet means and outlet means, and a gas unit for introducing gas into the volume for applying a pressure above atmospheric, which prevails therein and which acts to discharge bulk goods m the volume via the outlet means, a bottom surface being arranged at said bottom region of the container, said bottom surface having a gas-permeable portion, and the gas unit acting, m connection with application of a pressure above atmospheric m the volume, to introduce at least part of the gas into the volume via said portion m order to counteract compression, caused by the pressure above atmospheric, of bulk goods m the volume, said device being characterised m that said gas-permeable portion covers essentially the entire bottom surface, and that the outlet means comprises a non-return valve which is movable between an open and a closed position, the non-return valve being arranged to take its open position if the pressure
  • the low speed is due to the fact that the gas-permeable portion provides a large surface through which the gas can be introduced into the volume.
  • the low gas speed efficiently counteracts compression and ensures good fluidisation, i.e. provision of a sufficiently low viscosity of the bulk goods, of the bulk goods m the volume. This enables emptying of the volume as soon as the gas starts to be introduced into the volume, which results a quick change between the filling phase and the emptying phase.
  • the good fluidisation also enables quick emptying of bulk goods from the volume.
  • the gas-permeable portion covers essentially the entire bottom surface. This results a large surface through which the gas can be introduced into the volume, which of course results m the gas speed being advantageously low, thereby allowing introduction of a large gas flow without any risk of compression of the bulk goods m the volume. Moreover fluidisation of all the bulk goods m the container is allowed, which accelerates the subsequent emptying.
  • the non-return valve which is arranged to take its open position if the pressure prevailing the volume exceeds the pressure prevailing m a discharge conduit connected to the outlet means, ensures that the emptying phase m connection with pressurisation of the volume is always initiated m the most optimal pressure condition, which enables a maximum emptying capacity.
  • the inventive device further comprises a first pressure transducer for measuring the pressure prevailing m the volume, a second pressure transducer for measuring the pressure prevailing m the discharge conduit, downstream of the non-return valve, and a valve means, which, if the pressure indicated by the first pressure transducer is equal to the pressure indicated by the second pressure transducer, is adapted to interrupt the supply of gas to the volume and to introduce gas into the discharge conduit m a position downstream of the non-return valve.
  • a valve means which, if the pressure indicated by the first pressure transducer is equal to the pressure indicated by the second pressure transducer, is adapted to interrupt the supply of gas to the volume and to introduce gas into the discharge conduit m a position downstream of the non-return valve.
  • the bottom surface is advantageously angled to guide bulk goods m the volume towards the outlet means connection with discharge of the bulk goods from the volume.
  • the volume is suitably cylindrical and the bottom surface suitably has the form of a truncated cone, where the narrow end faces away from the volume, to which narrow end the outlet means is connected.
  • the angle of the bottom surface relative to a plane which is perpendicular to a longitudinal axis of the container is preferably the range 6°-70° and most preferably m the range 30°-55°. If the angle is the latter range, experiments have demon- strated that an optimal emptying capacity is obtained m the inventive device.
  • the gas-permeable portion is formed of one or more plates made of sintered plastic beads.
  • the gas-permeable portion is advantageously made of a material which is dimensionally stable when subjected to load. This ensures, on every occasion, sufficient guiding of the bulk goods towards the outlet means.
  • a con- tainer for bulk goods which internally defines a volume, comprising an mlet means communicating with said volume and intended for bulk goods, an outlet means which also communicates with said volume and is arranged a bottom region of the container and which is intended for bulk goods, a gas mlet means, via which gas is mtroducible into the volume for applying a pressure above atmospheric therein, and a bottom surface arranged m said bottom region and having a gas-permeable portion which forms part of said gas let means and via which at least part of the gas is mtroducible into the volume, said container being characterised m that said gas- permeable portion covers essentially the entire bottom surface, and that the outlet means comprises a non-return valve which is movable between an open and a closed posi- tion, the non-return valve being arranged to take its open position if the pressure prevailing m the volume exceeds a pressure prevailing m a discharge conduit which is connectable to the outlet means
  • a method for discharging bulk goods from a volume defined by a container, via an outlet means arranged m a bottom region of the container comprising the step of introducing gas into the volume for applying a pressure above atmospheric therein, whereby the bulk goods are discharged from the volume via the outlet means, said method being characterised by the steps of introducing at least part of the gas into the volume via a bottom surface, covered by a gas-permeable portion and arranged m said bottom region, of the container, m order to counteract compression, caused by the pressure above atmospheric, of bulk goods m the volume, and discharging the bulk goods via a non-return valve arranged m the outlet means by opening the non-return valve, which is arranged for opening if the pressure m the volume is higher than or equal to the pressure prevailing m a discharge conduit connected to the outlet means.
  • the pressure prevailing m the volume and the pressure prevailing m the discharge conduit m a position downstream of the non-return valve are measured and, if the pressures are equal, the supply of gas to the volume is interrupted and gas is introduced into the discharge conduit a position downstream of the non-return valve.
  • the fact that the pressures are equal means m fact that the volume is emptied, and by interrupting the supply of gas to the volume and introducing gas into the discharge conduit m a position downstream of the non-return valve, the pressure prevailing the discharge conduit becomes higher than the pressure prevailing m the volume, which makes the non-return valve take its closed position. Subsequently the pressure above atmospheric prevailing m the volume can be evacuated, after which the filling phase can be initiated.
  • Fig. 1 is a schematic, partly sectional side view of a device according to the present invention.
  • Fig. 2 is a partly sectional perspective view of a container of the device m Fig. 1.
  • Fig. 3 is a schematic illustration of an inventive device, whose outlet means comprises a non-return valve. Description of Embodiments
  • a device for handling bulk goods according to a pre- ferred embodiment of the present invention is illustrated m Figs 1 and 2, to which reference is made.
  • the device comprises a container 1 and a gas unit 2 schematically shown m Fig. 1.
  • the container 1 is formed as a cylindrical vessel closed at both ends.
  • An mlet means 3 for bulk goods is arranged m a top region 4 of the container 1 and an outlet means 5 for bulk goods is m the radial direction centrally arranged m a bottom region 6 of the container 1.
  • a gas mlet means 13 is arranged in said bottom region.
  • the outlet means further comprises a non-return valve 15, which will be described below with reference to Fig. 3.
  • the gas mlet means 13 comprises a bottom surface 7 arranged m the container 1 at said bottom region 6.
  • the bottom surface 7 has a gas-permeable portion 8, which allows gas to pass but which prevents particles, i.e. the bulk goods, from passing through.
  • the portion 8 is formed of a plurality of plates 9, which together form a structure which essentially has the form of a truncated cone, where the wide end faces away from the outlet means 5 and connects to the cylindrical inner wall 10 of the container 1 and where the end facing the outlet means 5 connects to the outlet means 5.
  • the plates 9 are made of a gas-permeable material, such as a porous, relatively hard sheet, which is made of sintered plastic beads.
  • the bottom surface 7 internally divides the container 1 into a first VI and a second V2 defined volume.
  • the gas-permeable plates 9 cover essentially the entire bottom surface 7.
  • the bottom surface 7 is arranged so as to be inclined relative to a plane which is perpendicular to a longitudinal axis 11 of the container 1.
  • Each plate 8 can be inclined at an angle ⁇ relative to said longitudinal axis 11 which is the range 6° -70°.
  • the angle ⁇ is m the range 30°-55°.
  • a gas pipe 12 extends from the schematically illustrated gas unit 2 to the second volume V2 , which is comprised by the gas mlet means 13.
  • the gas unit 2 comprises a compressor and is adapted to introduce compressed gas into the second volume V2.
  • the bottom surface 7 is dimensioned so that it carries the bulk goods supplied to the first volume VI and maintains its shape. It is also important for the bottom surface 7 not to have any apertures through which the bulk goods can pass to the second volume V2.
  • the filling of the first volume VI can be carried out m one of several different ways.
  • the bulk goods can, for example, be conveyed to the mlet means 3 by means of a belt conveyor or by means of a screw. It is also pos- sible to arrange a feeding hopper above the container 1, from which the bulk goods are fed to the first volume VI under the action of gravity.
  • an outlet means 14 for gas is arranged the top region 4 of the container 1.
  • the gas unit 2 is activated for mtro- ducmg compressed gas into the second volume V2 of the container 1 via the gas pipe 12.
  • the gas supplied to the second volume V2 will penetrate through the gas-permeable plates 9 of the bottom surface 7 and be introduced into the first volume VI.
  • the pressure will now increase the entire container 1, whereby the bulk goods are pressed out through the outlet means 5.
  • the generated pressure above atmospheric will act to compress the bulk goods m the first volume VI, thereby increasing the viscosity thereof, which renders the emptying of the bulk goods difficult.
  • This compression is counteracted by the gas which is introduced into the first volume VI via the bottom surface 7, which gas acts to fluidise the bulk goods. This ensures satisfactory emptying of the bulk goods from the first volume VI.
  • the gas-permeable plates 9 provide a relatively large flow area for the gas flow, which means that the speed of the gas flow can be kept at an advantageously low level.
  • Practical experiments have shown that the emptying phase can be begun as soon as the gas penetrates into the first volume VI.
  • the reason for this is that the gas introduced into the first volume VI causes an extremely good fluidisation of the bulk goods the first volume VI. It is thus not necessary to delay the beginning of the emptying phase until a requisite pressure above atmospheric has been built up m the container 1. As a result, the change between filling phase and emptying phase occurs very quickly, which of course improves the capacity of the device.
  • the container 1 of the inventive device For satisfactory emptying of conventional containers for handling bulk goods, it is necessary that they have a bottom which is inclined towards an outlet means at an angle which is normally m the range 55° -60°. The reason for this relatively great inclination is that the angle of repose of the bulk goods must be overcome. Thanks to the efficient fluidisation of the bulk goods the container 1 of the inventive device, the inclination of the bottom surface 7 can have such a small angle ⁇ as about 6° while still ensuring satisfactory emptying of the first volume VI. This means that the container 1 with its height retained can define a considerably larger volume than the corresponding volume of conventional containers, which is advantageous from the viewpoint of capacity.
  • the bottom surface 7 of the container 1 is advantageously inclined at an angle ⁇ which is m the range 30° -55°.
  • is m the range 30° -55°.
  • the inventive device consequently allows a very quick change between filling phase and emptying phase. Furthermore also the emptying of the bulk goods from the container 1 can be carried out quickly. More specifically, this is achieved by means of a bottom surface 7 which is arranged m the container 1 and which has a gas-permeable portion 8, for instance m the form of plates 9, which covers the entire bottom surface 7 and via which gas is conducted to a first volume VI of the container 1 while applying a pressure above atmospheric m the container 1. Bulk goods m said volume VI will then be fluidised, thereby counteracting compression thereof caused by the pressure above atmospheric. Thanks to the inclination of the bottom surface 7 to the outlet means 5, the bulk goods are quickly discharged from the first volume VI.
  • the discharge can be initiated lmme- diately m connection with the fluidisation of the bulk goods, which means that the change between filling phase and emptying phase can occur quickly.
  • the emptying if the bottom surface 7 is inclined at an angle ⁇ m the range 30°-55°, is extremely quick. In this case it has been found that the quickness is independent of the degree of filling of the volume VI and of the pressure above atmospheric prevailing m the container 1.
  • the coefficient of friction of the bottom surface 7 has an effect on said quickness, and therefore as low a coefficient of friction as possible is st ⁇ ved for.
  • the inventive device thus has an improved emptying capacity compared with conventional devices for handling of bulk goods. This makes it possible to provide, by means of a reduced effect of the compressor of the gas unit, an emptying capacity which is similar to that of conventional devices with considerably larger compressors .
  • the outlet means 5 of the container 1 for the bulk goods thus comprises the non-return valve 15 connected to the discharge conduit 16.
  • a first pressure transducer 17 is arranged to measure the pressure prevailing m the container 1 and a second pressure transducer 18 is arranged downstream of the nonreturn valve 15 to measure the pressure prevailing m the discharge conduit 16.
  • a valve means 19 is advan- tageously arranged m the gas pipe 12, which extends between the compressor of the gas unit 2 and the second volume V2 of the container 1. This valve 19 allows guiding of the gas flow supplied from the compressor to the second volume V2 of the container 1 and/or to the discharge conduit 16 m a position of the same downstream of the non-return valve 15 via a pipe 21.
  • the compressor is activated for pressurising the container 1.
  • the non-return valve 15 will take its open position, thereby enabling discharge of the bulk goods m the container 1.
  • the two pressure transducers 17, 18 will indicate the same pressure.
  • the valve means 19 is operated so that all gas is supplied to the discharge conduit 16, which makes the non-return valve 15 take its closed position since the pressure prevailing downstream of the nonreturn valve 15 will exceed the pressure prevailing upstream of the non-return valve 15.
  • a ventilation valve 20 which is shown more detail m Fig. 2, can be opened to evacuate the pressure above atmospheric m the container 1. Subsequently the con- tamer can be once more filled with bulk goods.
  • the filling phase proceeds quicker than the time it takes to empty the conduit 16, which is also usually the case since the discharge conduit normally has a considerable extent, the normal case 200-300 m. Thanks to the filling phase being quicker than the time it takes to empty the discharge conduit, a pressure above atmospheric is ensured m the discharge conduit 16 after completion of the filling phase, whereby it is ensured that the non-return valve 15 remains closed during the entire filling phase. Subsequently the container 1 is pressurised, and the non-return valve 15 again takes its open position when the pressure prevailing m the container 1 slightly exceeds the pressure prevailing m the discharge conduit 16. Thus it is en- sured that the non-return valve 15 of the outlet means 5 always opens m the most optimal pressure condition, whereby an optimal emptying capacity of the inventive device is achieved.

Abstract

A device for handling bulk goods, comprising a container (1) with an inlet means (3) and an outlet means (5) arranged in a bottom region (6) thereof, said container (1) defining a volume (V1) communicating with said inlet means (3) and outlet means (5), and a gas unit (2) for introducing gas into the volume (V1) for applying a pressure above atmospheric prevailing therein and acting to discharge bulk goods in the volume (V1) via the outlet means (5). A bottom surface (7) is arranged at said bottom region (6) of the container (1), said bottom surface (7) having a gas-permeable portion (8). In connection with application of a pressure above atmospheric in the volume (V1), the gas unit (2) acts to introduce at least part of the gas into the volume (V1) through said portion (8) in order to counteract compression, caused by the pressure above atmospheric, of bulk goods in the volume (V1). The device is characterised in that said gas-permeable portion (8) covers essentially the entire bottom surface (7), and that the outlet means (5) comprises a non-return valve movable between an open and a closed position. The non-return valve is arranged to take its open position if the pressure prevailing in the volume (V1) exceeds the pressure prevailing in a discharge conduit connected to the outlet means (5). The invention also concerns a container (1) for bulk goods and a method for handling bulk goods.

Description

DEVICE, METHOD AND CONTAINER FOR HANDLING BULK GOODS
Field of the Invention
The present invention relates to a device and a method for handling bulk goods, such as cement powder, and a container for bulk goods. More specifically, the present invention relates to such a device as comprises a container with an inlet means and an outlet means arranged m a bottom region thereof, said container defining a volume which communicates with said inlet means and outlet means, and a gas unit for introducing gas, such as air, into the volume for applying a pressure above atmospheric which prevails therein and which acts to discharge bulk goods in the volume via the outlet means, and a corresponding method. Background Art
For handling, such as discharging, of bulk goods, and above all pulverulent bulk goods, a device comprising an intermediate storage container is frequently used. The bulk goods are fed into the intermediate storage con- tainer during a filling phase by means of a suitable device, such as a feeding hopper, a screw, belt or chain unit or a pneumatic unit for drawing in the bulk goods into the container. During a subsequent emptying phase, the container is pressurised. All connections to the con- tainer are closed, after which gas is introduced into the container. When a requisite pressure above atmospheric has been obtained m the container, an outlet valve is opened, whereby the bulk goods are pressed out of the container via the outlet valve to a conveyor pipe for further transport to, for example, a storage silo. Gas is continuously introduced into the container for maintaining a requisite pressure above atmospheric in the same.
When the intermediate storage container is being pressurised during the emptying phase, the bulk goods m the container are compressed. As a result, the viscosity of the bulk goods increases, which makes the discharge of the bulk goods via the outlet difficult. For this reason, a number of nozzles are normally arranged m connection with the outlet, through which nozzles gas is introduced into the container. The container can be designed m such manner that all the gas, or only part thereof, which is introduced into the container for pressurising the same, is introduced via the nozzles. The gas introduced into the container via the nozzles counteracts the compression caused by the pressure above atmospheric by the viscosity of the bulk goods being lowered. Consequently, the discharge of the bulk goods from the container is facilitated. When the container is empty, the outlet valve is closed and the container is prepared for a new filling phase. In many cases, devices of the type described above comprise at least two such containers, which operate alternately, i.e. one is being filled as the other is being emptied and vice versa.
Devices of the type described above, however, suffer from a number of drawbacks .
It has been found difficult to fully counteract the compression of the bulk goods caused by the pressure above atmospheric. In consequence, the emptying phase takes a long time, which reduces the capacity of the device .
When changing between said filling phase and said emptying phase, a stop period arises during which the container is pressurised. During this stop period, neither emptying nor filling of the container occurs. As a result, the total capacity is of course lowered, with which the device can handle a load of bulk goods.
With a view to minimising this stop period, the con- tamer should be pressurised as quickly as possible. This requires that a fairly large gas flow be introduced into the container through the nozzles to counteract said com- pression of the bulk goods. The high gas flow, however, means that the gas speed through the nozzles becomes high, which m itself causes compression of the bulk goods. Owing to the compression of the bulk goods, the subsequent emptying phase will take a longer time. Consequently, a shortened pressurising phase results m an extended emptying phase .
The above problems have to some extent been solved by means of a discharging device according to DE 38110191. This discharging device differs from the type described above m that it comprises a breakmg-up bottom m the area of the discharge means of the respective containers. The bulk goods located straight above the breakmg-up bottom are fluidised through the same, thereby preventing compression connection with pressurising. Further, m each container nozzles are arranged, which act to break up the non-fluidised bulk goods, so that they fall into the fluidised area. The device also comprises pressure control devices, which sense the pressure in each container and, m response to measuring of predetermined pressures, send signals to actuators for opening of outlet valves.
This discharging device is well suited for discharging a load of a bulk vehicle to, for example, a silo. However, the device is not suited for continuous discharging of a shipload where a quick change between filling phase and emptying phase, as well as quick emptying, is required. The reason for this is that quick pressurisation of a container inevitably causes compression of the non-fluidised bulk goods, and that the device operates against predetermined pressure levels for initiating emptying, which pressure levels necessarily are not optimal.
There is thus a need for a device of the type described above, the container of which allows a quick change between filling phase and emptying phase as well as quick emptying of bulk goods positioned therein. Summary of the Invention
In view of that stated above, an object of the present invention is to provide an improved device for handling bulk goods. A specific object is to provide a device comprising a container which allows a quick change between filling phase and emptying phase as well as quick emptying of bulk goods positioned therein.
Another specific object is to provide a method which allows a quicker change between filling and emptying as well as quicker emptying of bulk goods from a container of a device of the type described above.
Additional objects of the present invention will be evident from the following description and the appended claims.
According to the present invention, the objects are achieved by a device for handling bulk goods, having the features stated claim 1, a container for bulk goods having the features stated claim 9, and a method for handling bulk goods having the features stated claim
11. Preferred embodiments of the inventive device are evident from claims 2-8. A preferred embodiment of the inventive container is defined claim 11, and a preferred embodiment of the inventive method is defined m claim 12.
More specifically, according to the present invention a device is provided for handling bulk goods, comprising a container with an inlet means and an outlet means arranged a bottom region thereof, said container defining a volume communicating with said mlet means and outlet means, and a gas unit for introducing gas into the volume for applying a pressure above atmospheric, which prevails therein and which acts to discharge bulk goods m the volume via the outlet means, a bottom surface being arranged at said bottom region of the container, said bottom surface having a gas-permeable portion, and the gas unit acting, m connection with application of a pressure above atmospheric m the volume, to introduce at least part of the gas into the volume via said portion m order to counteract compression, caused by the pressure above atmospheric, of bulk goods m the volume, said device being characterised m that said gas-permeable portion covers essentially the entire bottom surface, and that the outlet means comprises a non-return valve which is movable between an open and a closed position, the non-return valve being arranged to take its open position if the pressure prevailing the volume exceeds the pressure prevailing m a discharge conduit connected to the outlet means.
This results a device which allows a quick change between the filling phase and the emptying phase as well as quick emptying of bulk goods from the volume during the actual emptying phase. This is achieved by means of the gas-permeable portion of the bottom surface, through which portion a large gas flow can be introduced into the volume at a very low speed. The low speed is due to the fact that the gas-permeable portion provides a large surface through which the gas can be introduced into the volume. The low gas speed efficiently counteracts compression and ensures good fluidisation, i.e. provision of a sufficiently low viscosity of the bulk goods, of the bulk goods m the volume. This enables emptying of the volume as soon as the gas starts to be introduced into the volume, which results a quick change between the filling phase and the emptying phase. Moreover, the good fluidisation also enables quick emptying of bulk goods from the volume.
Further the gas-permeable portion covers essentially the entire bottom surface. This results a large surface through which the gas can be introduced into the volume, which of course results m the gas speed being advantageously low, thereby allowing introduction of a large gas flow without any risk of compression of the bulk goods m the volume. Moreover fluidisation of all the bulk goods m the container is allowed, which accelerates the subsequent emptying.
The non-return valve, which is arranged to take its open position if the pressure prevailing the volume exceeds the pressure prevailing m a discharge conduit connected to the outlet means, ensures that the emptying phase m connection with pressurisation of the volume is always initiated m the most optimal pressure condition, which enables a maximum emptying capacity. According to a preferred embodiment, the inventive device further comprises a first pressure transducer for measuring the pressure prevailing m the volume, a second pressure transducer for measuring the pressure prevailing m the discharge conduit, downstream of the non-return valve, and a valve means, which, if the pressure indicated by the first pressure transducer is equal to the pressure indicated by the second pressure transducer, is adapted to interrupt the supply of gas to the volume and to introduce gas into the discharge conduit m a position downstream of the non-return valve. This results m a device which allows a quick change between emptying phase and filling phase. When the measured pressures are equal, this is an indication that the container is empty, or any case essentially empty. The supply of gas to the con- tainer is interrupted while gas starts to be supplied to the discharge conduit. This, m turn, results the nonreturn valve closing since the pressure m the discharge conduit will exceed the pressure m the container. After that the container can be prepared for filling. To ensure good emptying of the volume, the bottom surface is advantageously angled to guide bulk goods m the volume towards the outlet means connection with discharge of the bulk goods from the volume. The volume is suitably cylindrical and the bottom surface suitably has the form of a truncated cone, where the narrow end faces away from the volume, to which narrow end the outlet means is connected. The angle of the bottom surface relative to a plane which is perpendicular to a longitudinal axis of the container is preferably the range 6°-70° and most preferably m the range 30°-55°. If the angle is the latter range, experiments have demon- strated that an optimal emptying capacity is obtained m the inventive device.
According to a preferred embodiment of the device, the gas-permeable portion is formed of one or more plates made of sintered plastic beads. The gas-permeable portion is advantageously made of a material which is dimensionally stable when subjected to load. This ensures, on every occasion, sufficient guiding of the bulk goods towards the outlet means.
Moreover, according the present invention, a con- tainer for bulk goods is provided, which internally defines a volume, comprising an mlet means communicating with said volume and intended for bulk goods, an outlet means which also communicates with said volume and is arranged a bottom region of the container and which is intended for bulk goods, a gas mlet means, via which gas is mtroducible into the volume for applying a pressure above atmospheric therein, and a bottom surface arranged m said bottom region and having a gas-permeable portion which forms part of said gas let means and via which at least part of the gas is mtroducible into the volume, said container being characterised m that said gas- permeable portion covers essentially the entire bottom surface, and that the outlet means comprises a non-return valve which is movable between an open and a closed posi- tion, the non-return valve being arranged to take its open position if the pressure prevailing m the volume exceeds a pressure prevailing m a discharge conduit which is connectable to the outlet means .
Finally, according to the present invention a method is provided for discharging bulk goods from a volume defined by a container, via an outlet means arranged m a bottom region of the container, comprising the step of introducing gas into the volume for applying a pressure above atmospheric therein, whereby the bulk goods are discharged from the volume via the outlet means, said method being characterised by the steps of introducing at least part of the gas into the volume via a bottom surface, covered by a gas-permeable portion and arranged m said bottom region, of the container, m order to counteract compression, caused by the pressure above atmospheric, of bulk goods m the volume, and discharging the bulk goods via a non-return valve arranged m the outlet means by opening the non-return valve, which is arranged for opening if the pressure m the volume is higher than or equal to the pressure prevailing m a discharge conduit connected to the outlet means. According to a preferred embodiment of the method, the pressure prevailing m the volume and the pressure prevailing m the discharge conduit m a position downstream of the non-return valve are measured and, if the pressures are equal, the supply of gas to the volume is interrupted and gas is introduced into the discharge conduit a position downstream of the non-return valve. The fact that the pressures are equal means m fact that the volume is emptied, and by interrupting the supply of gas to the volume and introducing gas into the discharge conduit m a position downstream of the non-return valve, the pressure prevailing the discharge conduit becomes higher than the pressure prevailing m the volume, which makes the non-return valve take its closed position. Subsequently the pressure above atmospheric prevailing m the volume can be evacuated, after which the filling phase can be initiated.
The invention will now be described by way of example with reference to the accompanying drawings. Brief Description of the Drawings
Fig. 1 is a schematic, partly sectional side view of a device according to the present invention.
Fig. 2 is a partly sectional perspective view of a container of the device m Fig. 1.
Fig. 3 is a schematic illustration of an inventive device, whose outlet means comprises a non-return valve. Description of Embodiments
A device for handling bulk goods according to a pre- ferred embodiment of the present invention is illustrated m Figs 1 and 2, to which reference is made.
The device comprises a container 1 and a gas unit 2 schematically shown m Fig. 1.
The container 1 is formed as a cylindrical vessel closed at both ends. An mlet means 3 for bulk goods is arranged m a top region 4 of the container 1 and an outlet means 5 for bulk goods is m the radial direction centrally arranged m a bottom region 6 of the container 1. In said bottom region, also a gas mlet means 13 is arranged. The outlet means further comprises a non-return valve 15, which will be described below with reference to Fig. 3.
The gas mlet means 13 comprises a bottom surface 7 arranged m the container 1 at said bottom region 6. The bottom surface 7 has a gas-permeable portion 8, which allows gas to pass but which prevents particles, i.e. the bulk goods, from passing through. In the shown embodiment, the portion 8 is formed of a plurality of plates 9, which together form a structure which essentially has the form of a truncated cone, where the wide end faces away from the outlet means 5 and connects to the cylindrical inner wall 10 of the container 1 and where the end facing the outlet means 5 connects to the outlet means 5. The plates 9 are made of a gas-permeable material, such as a porous, relatively hard sheet, which is made of sintered plastic beads. The bottom surface 7 internally divides the container 1 into a first VI and a second V2 defined volume. The gas-permeable plates 9 cover essentially the entire bottom surface 7. The bottom surface 7 is arranged so as to be inclined relative to a plane which is perpendicular to a longitudinal axis 11 of the container 1. Each plate 8 can be inclined at an angle φ relative to said longitudinal axis 11 which is the range 6° -70°. Preferably the angle φ is m the range 30°-55°.
A gas pipe 12 extends from the schematically illustrated gas unit 2 to the second volume V2 , which is comprised by the gas mlet means 13. The gas unit 2 comprises a compressor and is adapted to introduce compressed gas into the second volume V2.
In connection with filling of the container 1, bulk goods are supplied to the first volume VI of the con- tainer 1 through the mlet means 3. The bottom surface 7 is dimensioned so that it carries the bulk goods supplied to the first volume VI and maintains its shape. It is also important for the bottom surface 7 not to have any apertures through which the bulk goods can pass to the second volume V2.
The filling of the first volume VI can be carried out m one of several different ways. The bulk goods can, for example, be conveyed to the mlet means 3 by means of a belt conveyor or by means of a screw. It is also pos- sible to arrange a feeding hopper above the container 1, from which the bulk goods are fed to the first volume VI under the action of gravity. In the shown embodiment, an outlet means 14 for gas is arranged the top region 4 of the container 1. By evacuating gas from the con- tainer 1 through said outlet means 14, a sub-atmospheric pressure can be generated m the container 1, whereby suction arises m a suction conduit (not shown) connected to the mlet means 3. This makes it possible to draw m the bulk goods to the first volume VI through said suc- tion conduit.
In connection with emptying of the bulk goods the first volume VI, the gas unit 2 is activated for mtro- ducmg compressed gas into the second volume V2 of the container 1 via the gas pipe 12. The gas supplied to the second volume V2 will penetrate through the gas-permeable plates 9 of the bottom surface 7 and be introduced into the first volume VI. The pressure will now increase the entire container 1, whereby the bulk goods are pressed out through the outlet means 5. The generated pressure above atmospheric will act to compress the bulk goods m the first volume VI, thereby increasing the viscosity thereof, which renders the emptying of the bulk goods difficult. This compression is counteracted by the gas which is introduced into the first volume VI via the bottom surface 7, which gas acts to fluidise the bulk goods. This ensures satisfactory emptying of the bulk goods from the first volume VI.
To accelerate the change between filling phase and emptying phase, it is desirable to build up, as quickly as possible, a requisite pressure above atmospheric m the first volume VI. This is carried out by introduction of a large gas flow into the volume VI. In conventional containers for bulk goods, introduction of a large gas flow causes the bulk goods m the container to be compressed, which makes the subsequent emptying phase difficult. In the inventive container 1, however, compression of the bulk goods caused by a high gas speed is prevented m spite of introduction of a large gas flow. Owing to the fact that the gas is introduced into the first volume VI via the gas-permeable portion 8, i.e. the plates 9, of the bottom surface 7, introduction of a large gas flow into said volume VI is m fact allowed, while the speed of the gas flow is low. The reason for this is that the gas-permeable plates 9 provide a relatively large flow area for the gas flow, which means that the speed of the gas flow can be kept at an advantageously low level. Practical experiments have shown that the emptying phase can be begun as soon as the gas penetrates into the first volume VI. The reason for this is that the gas introduced into the first volume VI causes an extremely good fluidisation of the bulk goods the first volume VI. It is thus not necessary to delay the beginning of the emptying phase until a requisite pressure above atmospheric has been built up m the container 1. As a result, the change between filling phase and emptying phase occurs very quickly, which of course improves the capacity of the device.
For satisfactory emptying of conventional containers for handling bulk goods, it is necessary that they have a bottom which is inclined towards an outlet means at an angle which is normally m the range 55° -60°. The reason for this relatively great inclination is that the angle of repose of the bulk goods must be overcome. Thanks to the efficient fluidisation of the bulk goods the container 1 of the inventive device, the inclination of the bottom surface 7 can have such a small angle φ as about 6° while still ensuring satisfactory emptying of the first volume VI. This means that the container 1 with its height retained can define a considerably larger volume than the corresponding volume of conventional containers, which is advantageous from the viewpoint of capacity.
It will be appreciated that it is also possible to design the bottom surface 7 of the container 1 so as to be parallel with the plane perpendicular to the longitudinal axis 11 of the container 1. In this case, however, complete emptying of the bulk goods m the first volume VI is not guaranteed. However, the bottom surface 7 is advantageously inclined at an angle φ which is m the range 30° -55°. Experiments that have been carried out m fact demonstrate that the emptying occurs considerably quicker if the bottom surface is inclined at an angle φ this range. Consequently, an optimal emptying capacity is obtained m this range of angle. Compared with a conventional container it is possible to increase the emptying capacity of the inventive container by 200-300% if the bottom surface 7 is inclined at an angle φ m the range 30° -55° .
The inventive device consequently allows a very quick change between filling phase and emptying phase. Furthermore also the emptying of the bulk goods from the container 1 can be carried out quickly. More specifically, this is achieved by means of a bottom surface 7 which is arranged m the container 1 and which has a gas-permeable portion 8, for instance m the form of plates 9, which covers the entire bottom surface 7 and via which gas is conducted to a first volume VI of the container 1 while applying a pressure above atmospheric m the container 1. Bulk goods m said volume VI will then be fluidised, thereby counteracting compression thereof caused by the pressure above atmospheric. Thanks to the inclination of the bottom surface 7 to the outlet means 5, the bulk goods are quickly discharged from the first volume VI. The discharge can be initiated lmme- diately m connection with the fluidisation of the bulk goods, which means that the change between filling phase and emptying phase can occur quickly. Furthermore, experiments have shown that the emptying, if the bottom surface 7 is inclined at an angle φ m the range 30°-55°, is extremely quick. In this case it has been found that the quickness is independent of the degree of filling of the volume VI and of the pressure above atmospheric prevailing m the container 1. On the other hand, it is assumed that the coefficient of friction of the bottom surface 7 has an effect on said quickness, and therefore as low a coefficient of friction as possible is stπved for.
The inventive device thus has an improved emptying capacity compared with conventional devices for handling of bulk goods. This makes it possible to provide, by means of a reduced effect of the compressor of the gas unit, an emptying capacity which is similar to that of conventional devices with considerably larger compressors .
As mentioned above, it is possible to initiate the emptying phase even m connection with the pressurisation of the container 1. However, it is not always advantageous to initiate the emptying immediately m connection with the pressurisation of the container 1. This may be due to the fact that the pressure prevailing a discharge conduit 16 connected to the container 1 does not allow such immediate emptying. This is conventionally solved by letting a predetermined pressure above atmospheric be built up m the container before the emptying is initiated. It goes without saying that this makes the time of changing unfavourably long. This problem has been solved according to the invention by means of the nonreturn valve 15 shown m Fig. 3.
The outlet means 5 of the container 1 for the bulk goods thus comprises the non-return valve 15 connected to the discharge conduit 16. Moreover, advantageously a first pressure transducer 17 is arranged to measure the pressure prevailing m the container 1 and a second pressure transducer 18 is arranged downstream of the nonreturn valve 15 to measure the pressure prevailing m the discharge conduit 16. Finally, a valve means 19 is advan- tageously arranged m the gas pipe 12, which extends between the compressor of the gas unit 2 and the second volume V2 of the container 1. This valve 19 allows guiding of the gas flow supplied from the compressor to the second volume V2 of the container 1 and/or to the discharge conduit 16 m a position of the same downstream of the non-return valve 15 via a pipe 21.
To empty a filled container 1, the compressor is activated for pressurising the container 1. When the pressure the container 1 slightly exceeds the pressure prevailing m the discharge conduit 16, the non-return valve 15 will take its open position, thereby enabling discharge of the bulk goods m the container 1. When the emptying phase is completed, i.e. when the container 1 is empty, or m any case essentially empty, of bulk goods, the two pressure transducers 17, 18 will indicate the same pressure. Now the valve means 19 is operated so that all gas is supplied to the discharge conduit 16, which makes the non-return valve 15 take its closed position since the pressure prevailing downstream of the nonreturn valve 15 will exceed the pressure prevailing upstream of the non-return valve 15. After that, a ventilation valve 20, which is shown more detail m Fig. 2, can be opened to evacuate the pressure above atmospheric m the container 1. Subsequently the con- tamer can be once more filled with bulk goods.
As the bulk goods are being discharged from the discharge conduit 16, the pressure the same will fall. It is ensured, however, that the filling phase proceeds quicker than the time it takes to empty the conduit 16, which is also usually the case since the discharge conduit normally has a considerable extent, the normal case 200-300 m. Thanks to the filling phase being quicker than the time it takes to empty the discharge conduit, a pressure above atmospheric is ensured m the discharge conduit 16 after completion of the filling phase, whereby it is ensured that the non-return valve 15 remains closed during the entire filling phase. Subsequently the container 1 is pressurised, and the non-return valve 15 again takes its open position when the pressure prevailing m the container 1 slightly exceeds the pressure prevailing m the discharge conduit 16. Thus it is en- sured that the non-return valve 15 of the outlet means 5 always opens m the most optimal pressure condition, whereby an optimal emptying capacity of the inventive device is achieved.
It will be appreciated that the present invention is not limited to the shown embodiments. Several modifications and variations are feasible and the invention is thus defined exclusively by the appended claims.

Claims

1. A device for handling bulk goods, comprising a container (1) with an mlet means (3) and an outlet means (5) arranged m a bottom region (6) thereof, said container (1) defining a volume (VI) communicating with said mlet means (3) and outlet means (5) , and a gas unit (2) for introducing gas into the volume (VI) for applying a pressure above atmospheric, which prevails therein and which acts to discharge bulk goods m the volume (VI) via the outlet means (5) , a bottom surface (7) being arranged at said bottom region (6) of the container (1), said bottom surface (7) having a gas-permeable portion (8), and the gas unit (2) acting, in connection with application of a pressure above atmospheric m the volume (VI) , to introduce at least part of the gas into the volume (VI) via said portion (8) m order to counteract compres- sion, caused by the pressure above atmospheric, of bulk goods m the volume (VI) , c h a r a c t e r i s e d m that said gas-permeable portion (8) covers essentially the entire bottom surface (7), and that the outlet means (5) comprises a non-return valve (15) which is movable between an open and a closed position, the non-return valve (15) being arranged to take its open position if the pressure prevailing m the volume (VI) exceeds the pressure prevailing m a discharge conduit (16) connected to the outlet means (5) .
2. A device as claimed m claim 1, further comprising a first pressure transducer (17) for measuring the pressure prevailing m the volume (VI) , a second pressure transducer (18) for measuring the pressure prevailing m the discharge conduit (16) , downstream of the non-return valve (15) , and a valve means (19) , which, if the pressure indicated by the first pressure transducer (17) is equal to the pressure indicated by the second pressure transducer (18) , is adapted to interrupt the supply of gas to the volume (VI) and to introduce gas into the discharge conduit (16) a position downstream of the non-return valve (15) .
3. A device as claimed m claim 1 or 2 , wherein said bottom surface (7) is angled to guide bulk goods m the volume (VI) towards the outlet means (5) m connection with discharge of the bulk goods from the volume (VI) .
4. A device as claimed m claim 3, wherein the volume (VI) is cylindrical and the bottom surface (7) has the form of a truncated cone, where the narrow end faces away from the volume (VI) , to which narrow end the outlet means (5) is connected.
5. A device as claimed m claim 3 or 4 , wherein the angle (φ) of the bottom surface (7) relative to a plane which is perpendicular to a longitudinal axis (11) of the container (1), is m the range 6°-70°.
6. A device as claimed m claim 5, wherein the angle (φ) is m the range 30°-55°.
7. A device as claimed m any one of the preceding claims, wherein one or more plates (9) made of sintered plastic beads form said gas-permeable portion (8) .
8. A device as claimed m any one of the preceding claims, wherein said gas-permeable portion (8) is made of a material which is dimensionally stable when subjected to load.
9. A container (1) for bulk goods, which internally defines a volume (VI) , comprising an let means (3) communicating with said volume (VI) and intended for bulk goods, an outlet means (5) which also communicates with said volume (VI) and is arranged m a bottom region (6) of the container (1) and which is intended for bulk goods, a gas let means (13) , via which gas is mtroducible into the volume (VI) for applying a pressure above atmospheric therein, and a bottom surface (7) arranged m said bottom region (6) and having a gas-permeable portion (8) , which forms part of said gas mlet means (13) and via which at least part of the gas is mtroducible into the volume (VI) , c h a r a c t e r i s e d m that said gas-permeable portion (8) covers essen- tially the entire bottom surface (7), and that the outlet means (5) comprises a non-return valve (15) which is movable between an open and a closed position, the non-return valve (15) being arranged to take its open position if the pressure prevailing m the volume
(VI) exceeds a pressure prevailing m a discharge conduit (16) which is connectable to the outlet means (5) .
10. A container as claimed m claim 9, further comprising a first pressure transducer (17) for measuring the pressure prevailing m the volume (VI) , a second pressure transducer (18) for measuring the pressure prevailing m the discharge conduit (16), downstream of the non-return valve (15) , and a valve means (19) , which, if the pressure indicated by the first pressure transducer (17) , is equal to the pressure indicated by the second pressure transducer (18), is adapted to interrupt the supply of gas to the volume (VI) and to introduce gas into the discharge conduit (16) m a position downstream of the non-return valve (15) .
11. A method for discharging bulk goods from a volume (VI) defined by a container (1), via an outlet means (5) arranged m a bottom region (6) of the container (1) , comprising the step of introducing gas into the volume (VI) for applying a pressure above atmospheric therein, whereby the bulk goods are discharged from the volume (VI) via the outlet means (5) , c h a r a c t e r i s e d by the steps of introducing at least part of the gas into the volume (VI) via a bottom surface (7) , covered by a gas-permeable portion (8) and arranged m said bottom region (6) , of the container (1) order to counteract compression, caused by the pressure above atmospheric, of bulk goods m the volume (VI) , and discharging the bulk goods via a non-return valve (15) arranged m the outlet means (5) by opening the nonreturn valve (15), which is arranged for opening if the pressure m the volume (VI) is higher than or equal to the pressure prevailing m a discharge conduit (16) connected to the outlet means (5) .
12. A method as claimed claim 11, further comprising the steps of measuring the pressure prevailing m the volume (VI) and the pressure prevailing m the discharge conduit (16) m a position downstream of the non-return valve (15) and, if the pressures are equal, interrupting the supply of gas to the volume (VI) and introducing gas into the discharge conduit (16) a position downstream of the non-return valve (15) .
PCT/SE2000/001914 1999-10-05 2000-10-04 Device, method and container for handling bulk goods WO2001025121A1 (en)

Priority Applications (1)

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AU79783/00A AU7978300A (en) 1999-10-05 2000-10-04 Device, method and container for handling bulk goods

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SE9903616A SE515034C2 (en) 1999-10-05 1999-10-05 Device, container and method for handling bulk goods
SE9903616-2 1999-10-05

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Cited By (6)

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FR2846258A1 (en) * 2002-10-26 2004-04-30 Eisenmann Kg Maschbau COLLECTOR AND DOSAGE CONTAINER FOR POWDERY PRODUCTS, ESPECIALLY FOR POWDER PAINT
WO2007004899A1 (en) * 2005-07-01 2007-01-11 Darryl John Sinclair Fluidising apparatus for transfer of particulate material
WO2007142534A1 (en) * 2006-06-09 2007-12-13 Kristian Gerhard Jebsen Skipsrederi A/S System and method for discharge of bulk material from a ship
EP2042371A1 (en) 2007-09-25 2009-04-01 Ernst Graf Outfeed hopper for the silo of a silo vehicle
US8007736B2 (en) * 2007-11-19 2011-08-30 Daikin Industries, Ltd. Particulate material processing apparatus and particulate material processing system
CN112875332A (en) * 2021-01-21 2021-06-01 中车石家庄车辆有限公司 Pneumatic device for powdery bulk material

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DE3716047A1 (en) * 1987-05-14 1988-12-01 Behn Maschf Method and device for operating a filling apparatus for dust-like or granular material
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GB2219784A (en) * 1988-05-27 1989-12-20 Gary Kenneth Busch Discharging a bulk material container
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Publication number Priority date Publication date Assignee Title
DE1272227B (en) * 1967-03-03 1968-07-04 Ludwig Spitzer Sen K G Fahrzeu Bulk goods vehicle with a pressure vessel
US4088373A (en) * 1976-08-11 1978-05-09 Tbw Ind. Inc. High volume pneumatic tank
EP0027909A1 (en) * 1979-10-26 1981-05-06 Krupp Polysius Ag Installation for conveying fine-grained material
EP0190592A1 (en) * 1985-01-24 1986-08-13 Paul Wurth S.A. Process and apparatus for pneumatically injecting dosed quantities of finely divided solids into a vessel under pressure and the application of this process to shaft furnaces
DE3716047A1 (en) * 1987-05-14 1988-12-01 Behn Maschf Method and device for operating a filling apparatus for dust-like or granular material
DE3810191A1 (en) * 1988-03-25 1989-10-12 Linke Hofmann Busch COMPRESSED AIR EMPTYING DEVICE FOR A BOTTLE CONTAINER WITH AT LEAST TWO DRAINING OPENINGS AND A METHOD FOR EMPTYING THE CONTAINER
GB2219784A (en) * 1988-05-27 1989-12-20 Gary Kenneth Busch Discharging a bulk material container
EP0503423A1 (en) * 1991-03-13 1992-09-16 Thyssen Stahl Aktiengesellschaft Process and apparatus for fluidising and the pneumatic transport of finely granulated material

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2846258A1 (en) * 2002-10-26 2004-04-30 Eisenmann Kg Maschbau COLLECTOR AND DOSAGE CONTAINER FOR POWDERY PRODUCTS, ESPECIALLY FOR POWDER PAINT
WO2007004899A1 (en) * 2005-07-01 2007-01-11 Darryl John Sinclair Fluidising apparatus for transfer of particulate material
WO2007142534A1 (en) * 2006-06-09 2007-12-13 Kristian Gerhard Jebsen Skipsrederi A/S System and method for discharge of bulk material from a ship
EP2032426B1 (en) 2006-06-09 2016-03-30 Kristian Gerhard Jebsen Skipsrederi A/S System and method for discharge of bulk material from a ship
EP2042371A1 (en) 2007-09-25 2009-04-01 Ernst Graf Outfeed hopper for the silo of a silo vehicle
US8007736B2 (en) * 2007-11-19 2011-08-30 Daikin Industries, Ltd. Particulate material processing apparatus and particulate material processing system
CN112875332A (en) * 2021-01-21 2021-06-01 中车石家庄车辆有限公司 Pneumatic device for powdery bulk material

Also Published As

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SE9903616L (en) 2001-04-06
SE9903616D0 (en) 1999-10-05
SE515034C2 (en) 2001-06-05

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