EP0148360A2 - Procédé pour compacter et/ou remplir des matières pulvérulentes - Google Patents
Procédé pour compacter et/ou remplir des matières pulvérulentes Download PDFInfo
- Publication number
- EP0148360A2 EP0148360A2 EP84113391A EP84113391A EP0148360A2 EP 0148360 A2 EP0148360 A2 EP 0148360A2 EP 84113391 A EP84113391 A EP 84113391A EP 84113391 A EP84113391 A EP 84113391A EP 0148360 A2 EP0148360 A2 EP 0148360A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- container
- filling
- separating device
- tube
- gas
- 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.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B39/00—Nozzles, funnels or guides for introducing articles or materials into containers or wrappers
- B65B39/04—Nozzles, funnels or guides for introducing articles or materials into containers or wrappers having air-escape, or air-withdrawal, passages
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B1/00—Packaging fluent solid material, e.g. powders, granular or loose fibrous material, loose masses of small articles, in individual containers or receptacles, e.g. bags, sacks, boxes, cartons, cans, or jars
- B65B1/20—Reducing volume of filled material
Definitions
- the invention relates to a method for compacting and / or filling powdery substances in rigid or flexible containers.
- Powdered substances are placed in flexible or rigid containers, e.g. Drums or sacks, filled.
- Some powdery substances in particular pyrogenic oxides or mixed oxides of metals and / or metalloids, such as pyrogenic silicon dioxide, have a low bulk density and / or are heavily permeated with air. These properties require large containers for filling and transport, which inevitably result in high packaging and transport costs.
- the known filling method by means of a flow compressor has the disadvantage that the powdery material is loosened again on the way into the container after the compression. If a specific density is to be achieved in the container, this can only be achieved by over-compressing the pulverulent substance in the compacting device. There is a risk that the application properties of the powdery substance, such as e.g. the dispersibility, could be changed in an undesirable manner.
- the object of the invention when filling powdery substances is to achieve a homogeneous consistency in the entire container volume range and an increase in the mean consistency in the Containers without undesired changes in the application properties, e.g. Dispersibility and thickening effect.
- the invention relates to a method for compacting and / or filling powdery substances in rigid or flexible containers, which is characterized in that the powdery substance by means of at least a tube which can carry out a filling movement relative to the container, fills the container and the pulverulent substance by means of a separating device which surrounds the tube and is optionally flush with the open end of the tube and which is suitable for gas / solid separation and has an essentially dustproof surface adapted to the cross-section of the container, is separated from the fluidizing medium which may be present or is retained in the container, while the fluidizing medium which may be present is allowed to escape from the container through the gas-permeable surface of the separating device by means of a suitable pressure gradient, and the fill level and thus, if appropriate determines the degree of compaction of the powdery substance in the container by means of the respective position of the separating device.
- the pulverulent substance for filling can be removed from a storage container by means of a fluidizing medium, in particular fluidiser air, and optionally also conveyed in a line to the filling device by means of a transport device.
- a fluidizing medium in particular fluidiser air
- the pipe with the separating device can first be led to the bottom or near the bottom of the container and then moved to the opening of the container in the form of a filling movement.
- the filling movement can be brought about by the pressure of the pulverulent substance or gas / solid mixture in the container, a counterforce possibly being less than or equal to the compressive force of the pulverulent in the container on the pipe and thus also on the separating device Substance, or gas / solid mixture.
- the filling movement can also be driven mechanically, pneumatically or hydraulically.
- the separating device can be used to allow the tube to perform an oscillating movement in the direction of its longitudinal axis, which overlaps the actual filling movement.
- the oscillating movement can take place periodically or non-periodically with different strokes.
- the amount of powdery substance can be metered volumetrically over the variable volume of the space remaining between the tank bottom, tank walls and separating device or gravimetrically using a scale.
- any commercially usable gaseous substance such as air, nitrogen or carbon dioxide, can be used as the fluidizing medium.
- Air is preferably used as the fluidizing medium.
- a diaphragm pump such as a gear pump or a progressing cavity pump may be used.
- Another transport device for conveying the gas / solid mixture can be a pressure vessel.
- a suitable operating pressure is applied to this pressure vessel.
- Fluidizing air can be applied to the bottom of the pressure vessel during emptying.
- the filling of the powdery substance can also be carried out simultaneously with several, for example two or three pipes. It is essential that these pipes on their open end, optionally connected flush with the same separating device.
- the pressure gradient at the geeineten for gas / solid separation area of the cutting device can by means of overpressure keeps opening-e in the fluidizing medium and / or by negative pressure on the B or the separating device are generated.
- an excess pressure is created in the fluidizing medium by the transport device, e.g. by means of a diaphragm pump or an overpressure container.
- the pressure drop can be constant over time or intermittent.
- the area suitable for gas / solid separation can e.g. consist of sintered metal or porous ceramic.
- the surface of the separation device can consist of a gas-permeable fabric or felt made of wire or natural or synthetic organic or inorganic fibers, which are arranged on stable, gas-permeable supports.
- a perforated plate can be used as a stable support.
- the surface suitable for gas / solid separation can be flat or curved. If the surface is curved, the tube or the tubes with the open end can be arranged on the concave side or on the convex side of the hollow body formed by the curved surface.
- the surface suitable for gas / solid separation should be largely dust-tightly adapted to the container wall.
- To Ab Seal can be used, for example, brushes or a ring with a suitable, for example round, cross section made of elastic hollow or solid material. It is essential that the surface suitable for gas / solid separation can slide sealingly in the container.
- the interior of the rigid or flexible container should have a constant congruent cross-sectional area perpendicular to the longitudinal axis of the container, which is identical to the axis of the filling movement, along its longitudinal axis. This provides an adequate seal between the container wall and the separating device over the entire fill level.
- the completion of the filling can take place in such a way that the gas / solid mixture conveyance and the relative movement from container to tube with separating device are ended at the same time, or that the relative movement from container to pipe with separating device is terminated before the gas / solid mixture conveyance has ended completed.
- the container preferably in the case of flexible containers, e.g. Sacks, enclosed by a support structure that can absorb the mechanical stress that occurs during filling.
- An advantage of the process according to the invention is that a higher average and more uniform density of the pulverulent substance is obtained in the container, the good application properties being retained. It allows greater flexibility in adjusting the average density of the powder in the container. Simpler and therefore cheaper containers can be used. A particular advantage is that largely gas or moisture-tight containers can be used. This means greater freedom in the choice of the material of the container.
- the process according to the invention is suitable for filling carbon black, color pigments and / or silicas, e.g. precipitated or pyrogenic silicas.
- the method according to the invention is preferably suitable for filling pyrogenically produced oxides or mixed oxides of metals and / or metalloids, in particular of pyrogenically produced silicon dioxide.
- the tube 1 is arranged on the separating device 2 on the convex side, the opening of which with the con the side of the surface is flush.
- This consists of the perforated plate 3 on which the separating surface 4 for the separation of the gas / solid mixture is arranged.
- the separating device 2 is surrounded by the ring 5 made of elastic material, whereby a largely dust-tight seal between the separating device 2 and the flexible wall of the container 6 is given.
- the flexible wall of the container 6 is fastened in the frame 7 by means of the bracket 8.
- the pulverulent substance mixed with air is conveyed through the pipe 1 into the space 9 between the separating device 2 and the flexible wall of the container 6.
- the pulverulent substance is retained in this space 9 by the separating device 2, while the air escapes through the opening 10 of the separating device 2.
- the separation device 2 is flat.
- the pipe 1 ' is arranged flush on the separating device 2.
- the wall of the container 6 is made of rigid material, so that a support structure is not required. To increase the stability, the container 6 is placed on the platform 11.
- the separating device 2 is curved, the tube 1 projecting beyond the separating device 2 into the space 9.
- the tube 1 is arranged on the concave side of the separating device 2. Furthermore, the same arrangement as in FIG. 1 is used.
- the pipe 1 with the separating device 2 moves in a guided relative movement due to the force relationships on the separating device 2 from those to be filled Container 6 out.
- a cross-bottom bag with the dimensions 550 x 220 x 1300 mm is attached to the bracket 8 and then slid over the separating device 2 by raising the frame 7 with the bracket 8 until the separating device 2, which has a needle felt surface, on the bag bottom or in whose proximity has reached.
- the fluidized, pyrogenically produced silicon dioxide with a surface area of approx. 200 m 2 / g and a tamped density according to DIN 53 194 of 35 g / 1 is pumped through a pipe 1 into the space 9 by means of a membrane pump, the filling pressure being approx. Is 0.5 bar.
- the frame 7 with the bag 6 is lowered at a lifting speed of approximately 0.6 m / min until the separating device reaches the filling end position.
- the gas / solid mixture delivery is stopped by switching off the pump and the separating device is moved out of the cross-bottom bag by further lowering the frame 7.
- the cross bottom sack is filled to a height of approx. 1100 mm with 10 kg of pyrogenic silicon dioxide.
- the average density of this product is 75 g / 1 with a density fluctuation of + 5 / -10 g / l.
- the separation device 2 at the lower end of the tube 1, consists of a perforated plate on which a filter fabric LAINYL M9 / S5 / HCa .. is attached as a separation surface 4.
- the separating pre-seal is sealed against the container 6 by means of an O-ring 5.
- the fluidized, pyrogenically produced silicon dioxide with a surface of approx. 200 m 2 / g and a tamped density according to DIN 53 194 of approx. 35 g / 1 is pumped through a tube 1 through the pipe 1 into the room 9, the filling pressure approx 0.5 bar.
- the container 6 is lowered at a stroke speed of approximately 0.6 m / min until the separating device reaches the filling end position.
- the gas / solid mixture delivery is stopped by switching off the pump and the separating device is moved out of the container 6 by further lowering the frame 7.
- the container is filled to a height of approx. 250 mm with pyrogenic silicon dioxide.
- the silicon dioxide has an average density of approx. 67 g / 1 with a fluctuation range of the average density in the individual ring elements of the container of + 3 / - 5 g / l.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Basic Packing Technique (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19843400415 DE3400415A1 (de) | 1984-01-07 | 1984-01-07 | Verfahren zum verdichten und/oder befuellen von pulverfoermigen stoffen |
DE3400415 | 1984-01-07 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0148360A2 true EP0148360A2 (fr) | 1985-07-17 |
EP0148360A3 EP0148360A3 (en) | 1986-10-01 |
EP0148360B1 EP0148360B1 (fr) | 1988-10-12 |
Family
ID=6224491
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP84113391A Expired EP0148360B1 (fr) | 1984-01-07 | 1984-11-07 | Procédé pour compacter et/ou remplir des matières pulvérulentes |
Country Status (5)
Country | Link |
---|---|
US (1) | US4770214A (fr) |
EP (1) | EP0148360B1 (fr) |
JP (1) | JPS60158001A (fr) |
BR (1) | BR8500026A (fr) |
DE (2) | DE3400415A1 (fr) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4985143A (en) * | 1988-06-06 | 1991-01-15 | The University Of Maryland | Method for packing chromatographic beds |
WO1991014632A2 (fr) * | 1990-03-23 | 1991-10-03 | Celcommerz High-Chem.-Produkte Gmbh & Co. Kg | Sac auto-desaerant et procede pour son remplissage |
US5479968A (en) * | 1993-08-16 | 1996-01-02 | Xerox Corporation | Ink filling apparatus and method for filling ink cartridges |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6193795B1 (en) | 1993-08-02 | 2001-02-27 | Degussa Corporation | Low structure pyrogenic hydrophilic and hydrophobic metallic oxides, production and use |
JP5070120B2 (ja) * | 2008-05-08 | 2012-11-07 | 紀伊産業株式会社 | 粉体充填装置および粉体充填方法 |
KR200452742Y1 (ko) | 2009-05-08 | 2011-03-17 | (주)아모레퍼시픽 | 개선된 구조를 갖는 건식 파우더 화장품의 에어제거용 성형치구 |
DE102011103876B3 (de) * | 2011-06-10 | 2012-03-15 | Leibinger Smb Technik Gmbh | Vorrichtung zum Befüllen eines Behältnisses mit einer insbesondere zum Verzehr bestimmten Flüssigkeit |
US9845169B2 (en) * | 2011-11-01 | 2017-12-19 | Altria Client Services Llc | Apparatus and method of packaging loose product |
PL3184971T3 (pl) * | 2015-12-21 | 2019-04-30 | Fydec Holding Sa | Urządzenie do dozowania najmniejszych ilości, w szczególności do zastosowań farmaceutycznych, a także sposób dozowania najmniejszych ilości proszku |
JP6834249B2 (ja) * | 2016-02-18 | 2021-02-24 | 大同特殊鋼株式会社 | 粉末充填装置及び焼結磁石製造装置 |
JP6848544B2 (ja) * | 2017-03-09 | 2021-03-24 | 大同特殊鋼株式会社 | 粉末充填装置、焼結磁石製造装置及び焼結磁石製造方法 |
CN110871271B (zh) * | 2018-08-29 | 2022-02-25 | 大同特殊钢株式会社 | 粉末填充装置、烧结磁体制造装置以及烧结磁体制造方法 |
US10960995B2 (en) * | 2019-07-24 | 2021-03-30 | Ford Global Technologies, Llc | Methods and apparatuses for filling adsorbent powder in a hydrogen or natural gas tank |
CN113134990A (zh) * | 2021-04-26 | 2021-07-20 | 洛阳景瑞工业科技有限公司 | 一种细粉容器的细粉装填方法 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE176156C (fr) * | ||||
US2350438A (en) * | 1940-10-02 | 1944-06-06 | Crown Can Company | Plunger pad for container closing machines |
US2352663A (en) * | 1941-02-07 | 1944-07-04 | Sowden Alfred | Packing machine for containers and the like |
US3181575A (en) * | 1961-11-09 | 1965-05-04 | Paktronic Machine Corp | Filling machines |
US3716081A (en) * | 1971-03-29 | 1973-02-13 | Dow Chemical Co | Apparatus and method for tamping particulate materials into a container |
GB1535757A (en) * | 1976-11-15 | 1978-12-13 | Vita Int Ltd | Bag filling nozzle |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US494979A (en) * | 1893-04-04 | Lead-packer | ||
US367857A (en) * | 1887-08-09 | Flour-packer | ||
FR2377937A1 (fr) * | 1977-01-20 | 1978-08-18 | Alfa Laval Ag | Procede et dispositif pour la desaeration des poudres, telles que poudres de lait |
-
1984
- 1984-01-07 DE DE19843400415 patent/DE3400415A1/de not_active Withdrawn
- 1984-11-07 DE DE8484113391T patent/DE3474535D1/de not_active Expired
- 1984-11-07 EP EP84113391A patent/EP0148360B1/fr not_active Expired
-
1985
- 1985-01-04 BR BR8500026A patent/BR8500026A/pt unknown
- 1985-01-07 JP JP60000253A patent/JPS60158001A/ja active Pending
-
1987
- 1987-09-17 US US07/097,263 patent/US4770214A/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE176156C (fr) * | ||||
US2350438A (en) * | 1940-10-02 | 1944-06-06 | Crown Can Company | Plunger pad for container closing machines |
US2352663A (en) * | 1941-02-07 | 1944-07-04 | Sowden Alfred | Packing machine for containers and the like |
US3181575A (en) * | 1961-11-09 | 1965-05-04 | Paktronic Machine Corp | Filling machines |
US3716081A (en) * | 1971-03-29 | 1973-02-13 | Dow Chemical Co | Apparatus and method for tamping particulate materials into a container |
GB1535757A (en) * | 1976-11-15 | 1978-12-13 | Vita Int Ltd | Bag filling nozzle |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4985143A (en) * | 1988-06-06 | 1991-01-15 | The University Of Maryland | Method for packing chromatographic beds |
WO1991014632A2 (fr) * | 1990-03-23 | 1991-10-03 | Celcommerz High-Chem.-Produkte Gmbh & Co. Kg | Sac auto-desaerant et procede pour son remplissage |
WO1991014632A3 (fr) * | 1990-03-23 | 1991-12-26 | Celcommerz High Chem Produkte | Sac auto-desaerant et procede pour son remplissage |
US5479968A (en) * | 1993-08-16 | 1996-01-02 | Xerox Corporation | Ink filling apparatus and method for filling ink cartridges |
Also Published As
Publication number | Publication date |
---|---|
EP0148360A3 (en) | 1986-10-01 |
BR8500026A (pt) | 1985-08-13 |
US4770214A (en) | 1988-09-13 |
EP0148360B1 (fr) | 1988-10-12 |
DE3400415A1 (de) | 1985-07-18 |
JPS60158001A (ja) | 1985-08-19 |
DE3474535D1 (en) | 1988-11-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0148360B1 (fr) | Procédé pour compacter et/ou remplir des matières pulvérulentes | |
DE3040003A1 (de) | Verfahren und vorrichtung zum beschicken der verkokungskammer eines koksofens | |
DE3540505C1 (de) | Sackfuellmaschine | |
DE2063935C3 (de) | Verpackungsvorrichtung für pulverförmiges Gut | |
DE2722720C2 (fr) | ||
DE2553879A1 (de) | Packmaschine zum fuellen von schuettfaehigem gut in einen behaelter | |
EP2683874A2 (fr) | Dispositif vibrateur pour la fabrication de colonnes de matière de remplissage | |
DE3520492C2 (fr) | ||
DE10261276B4 (de) | Vorlagebehälter für pulverförmige Medien | |
EP0903440B1 (fr) | Procédé et dispositif pour amélioration des sols avec un liant a poudre | |
DE3936761C1 (en) | Ventilator for fine granular material - has vibrating elastically suspended probe with porous walls | |
DE2714903C2 (de) | Verfahren und Vorrichtung zur kontinuierlichen Verwiegung bzw. kontinuierlichen volumetrischen Dosierung von unverdichtetem, auf pyrogenem Wege hergestelltem Siliciumdioxid | |
DE3414218A1 (de) | Vorrichtung zum befuellen von ventilsaecken mit insbesondere pulverfoermigem schuettgut | |
EP1099104A1 (fr) | Appareil de mesure d'imbibition pour determiner la mouillabilite de poudres | |
DE602005003855T2 (de) | Vorrichtung und Verfahren zum Verdichten eines fliessfähigen festen Materials | |
DE2243156A1 (de) | Verfahren und vorrichtung zum einspeisen von pulverfoermigen additivstoffen in verbrennungsraeume | |
DE2829149A1 (de) | Verfahren und vorrichtung zur herstellung von puderzucker | |
DE10246659A1 (de) | Verfahren und Vorrichtung zum dosierten Befüllen von Behältnissen mit mikronisiertem Pulver | |
DE3231070A1 (de) | Vorrichtung zur austragung von in silos gelagerten stoffen | |
DE3827676C1 (en) | Arrangement for transporting powdery or granular material - construction-material mixtures (material to be conveyed) - for use in underground mining or tunnelling | |
AT201508B (de) | Vorrichtung zum Entleeren und Fördern von staub- oder pulverförmigem Gut aus Behältern | |
DE1085091B (de) | Verfahren zum Fuellen von Ventilsaecken mit pulverfoermigen oder koernigen Stoffen | |
DE1786412C (de) | Verpackungsvorrichtung für pulverfbrmi ges GuL | |
DE1511688C (de) | Verfahren und Vorrichtung zur Förderung und Verpackung feinkörniger und sauerstoffempfindlicher Füllgüter | |
DE3520498A1 (de) | Einrichtung zur verteilung eines fluidisierbaren pulverisierten schuettgutes in einer speicherungsanlage |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19841107 |
|
AK | Designated contracting states |
Designated state(s): BE DE FR GB IT |
|
PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): BE DE FR GB IT |
|
17Q | First examination report despatched |
Effective date: 19870424 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): BE DE FR GB IT |
|
ITF | It: translation for a ep patent filed |
Owner name: JACOBACCI & PERANI S.P.A. |
|
REF | Corresponds to: |
Ref document number: 3474535 Country of ref document: DE Date of ref document: 19881117 |
|
ET | Fr: translation filed | ||
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Effective date: 19891107 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Effective date: 19891130 |
|
BERE | Be: lapsed |
Owner name: DEGUSSA A.G. Effective date: 19891130 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Effective date: 19900731 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Effective date: 19900801 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |