GB1572003A - Pneumatic suction conveying plant - Google Patents
Pneumatic suction conveying plant Download PDFInfo
- Publication number
- GB1572003A GB1572003A GB13181/77A GB1318177A GB1572003A GB 1572003 A GB1572003 A GB 1572003A GB 13181/77 A GB13181/77 A GB 13181/77A GB 1318177 A GB1318177 A GB 1318177A GB 1572003 A GB1572003 A GB 1572003A
- Authority
- GB
- United Kingdom
- Prior art keywords
- suction
- conveying
- separator
- line
- separators
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/24—Gas suction systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/60—Devices for separating the materials from propellant gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92228—Content, e.g. percentage of humidity, volatiles, contaminants or degassing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
- B29C2948/9259—Angular velocity
Description
(54) PNEUMATIC SUCTION CONVEYING PLANT
(71) We, AZO-MACHINEN
FABRIK ADOLF ZIMMER
MANN GMBH. a German Company, of D-6960 Osterburken, Federal Republic of Germany, do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement:
The invention relates to pneumatic suction conveying plant for supplying a plurality of consumers with particulate material from at least one storage container.
In a known plant of this kind (DE-OS 2,136,328) the pneumatic conveying line leads axially and vertically into the product chamber of a separator having a product chamber and a clean air chamber. Between the delivery pipe of the conveying line and the wall of the separator a filter is held in a slack condition. Upon charging from the supply container, that is to say when there is a depression in the clean air chamber, the filter bulges into the clean air chamber. The material arriving through the delivery pipe of the conveying line is separated in its gravity descent. whilst the conveying air passes into the suction line through the filter. The filter is so designed that all the solid particles are separated from the conveying stream.
Such suction conveying plants are used, for example, in the synthetic plastics processing industry for supplying a plurality of processing machines from one or more silos containing, for example. a synthetic plastics granulate. In the processing of synthetic plastics material it is possible for dust contained in the granulate to impair the mechanical and optical properties of the end product.
The present invention takes as its basic purpose the provision of a suction conveying plant which can be so designed that dustfree material will be delivered to the consumer.
According to the invention there is provided a suction conveying plant as defined in claim 1 of the appended claims.
With this arrangement of a separate dust separator before the blower the result can be achieved, by giving the filter in each particulate material separator a mesh dimension which is only slightly smaller than the smallest grain size of the material required by the consumer, that any dust contained originally in the particulate material, or perhaps created during conveyance, is not retained by the filters in the separators. On the contrary the dust passes through these filters and is only separated immediately in front of the blower. On the other hand the particulate material precipitating at the separator is absolutely free of dust.As contrasted with known plants, the construction of the suction conveying plant according to the invention has the further advantage that the filter resistance in the individual separators is materially reduced, and that it is only necessary to have a single dust separator with a suitably high filter resistance for all of the separators. Not only is an improvement in the technical functioning of the plant achieved thereby, but a reduction in cost is also possible.
In a preferred construction according to the invention the filter in each separator is so designed that its flow cross-section (i.e.
its open area, that is the total area of the apertures therein) is substantially greater than the free cross-section of the suction line. The filter resistance is therefore not greater than the resistance of the line, and consequently there is an unrestricted flow through the filter, which entrains the dust particles.
The filter arranged upstream of the suction connection of the blower is advantageously designed as a conventional battery of pocket-type filters, which is distinguished by its high degree of separation. By the design of the plant in accordance with the invention its efficiency is materially improved.
The invention will now be described, by way of example. with reference to the accompanying drawing, the single Figure of which shows a practical form of the invention as a flow diagram.
In the drawing there are shown three supply hoppers 1, 2 and 3 belonging to storage containers not shown. To each of these supply hoppers 1, 2 and 3 there is connected a pneumatic conveying line 4, which is taken to a plurality of consumers in the present example three consumers not shown in the drawing. To each consumer there is allocated a delivery hopper 5, upstream of each of which is a separator 6.
The suction conveying plant furthermore includes a suction blower 7, to which each separator 6 is connected through a suction line 8 and a branch line 9.
Each separator 6, and therefore each consumer, can be connected when necessary to any of the three conveying lines 4, and therefore to any of the three supply hoppers 1, 2 and 3 for the purpose of conveying into the separators 6 various products, for example. which are stored in the various storage containers. Thus, the separator 6 shown at the left hand side of the drawing is shown connected to the Iower supply hopper 3, the centre separator is shown connected to the upper supply hopper 1 and the separator at the right hand side is shown connected to the middle supply hopper 2.In the operating condition shown in the drawing the right hand consumer is being supplied with particulate material, the flap 10 being closed at the exit of the separator 6 and the three valves in the valve block VB (shown diagrammatically) being set as shown to open the connection between the clean air chamber 13 and the suction branch line 9, to open the connection between the product chamber 12 and a branch line 11 mentioned below, and to close a ventilation opening to the atmosphere. On the other hand the flaps 10 of the two other separators are open, so that the product enters the delivery hoppers 5 of the consumers.
The separators 6 are in communication with the conveying lines 4 through respective branch lines 11. For the sake of clarity the drawing has been simplified by omitting two of the branch lines 11 to each separator 6 from the stub pipes shown in the other two conveying lines 4. The branch lines 11 lead in each case into the lower chamber. namely the product chamber 12 of the separator. By
means of a filter 14, the product chamber 12 is separated from the clean air chamber 13 connected to the branch line 9 of the suction line 8, the filter having a relatively large mesh dimension. The mesh dimension is so selected that the particles of the material having the smallest grain size which is desired for the processing are retained and therefore fall into the product chamber 12 and can be transferred into the delivery hopper 5.All smaller particles, in particular dust, pass through the filter 14 and travel through the branch line 9 and the suction line 8 to the blower 7.
Upstream of the blower 7, in fact upstream of its suction pipe 15, there is arranged a separator 16 having a plurality of pocket-type filters 17, through which the clean air flows from the outside. The mesh dimension is so selected that the pockettype filters 17 retain any dust still present in the clean air. Consequently, only a single dust separator is necessary for all of the consumers, whilst the filters 14 for the individual separators retain no dust and moreover have a flow cross-section (as hereinbefore defined) which is equal to or greater than the free or conveying crosssection of the suction line 8, including the branch lines 9.
WHAT WE CLAIM IS:
1. A pneumatic suction conveying plant for supplying a plurality of consumers with particulate material from at least one storage container; said plant comprising at least one storage container for such material, a plurality of consumers, a pneumatic conveying line or respective pneumatic conveying lines between the storage container or the respective storage containers and the consumers, respective separators situated above the respective consumers for separating said material from conveying air, and a suction line connected to each of the separators and to a blower for causing the conveying air to flow by suction, wherein each of the separators includes a product chamber and a clean air chamber, the product chamber being connected to the pneumatic conveying line, or to at least one such line where the plant has a plurality of such lines, and being arranged for discharging material accumulated therein to the consumer, the clean air chamber being connected to the suction line, and said chambers being separated from each other by a filter for separating the particulate material from its conveying air, and a finer mesh filter for separating the dust contained in the stream of clean air from the separators is provided in the suction line downstream of the clean air chambers and upstream of the suction connection of the blower.
2. A suction conveying plant according to claim 1 wherein the filter in each of the separators has a flow cross-section (as hereinbefore defined) substantially greater than the free cross-section of the suction
**WARNING** end of DESC field may overlap start of CLMS **.
Claims (5)
1. A pneumatic suction conveying plant for supplying a plurality of consumers with particulate material from at least one storage container; said plant comprising at least one storage container for such material, a plurality of consumers, a pneumatic conveying line or respective pneumatic conveying lines between the storage container or the respective storage containers and the consumers, respective separators situated above the respective consumers for separating said material from conveying air, and a suction line connected to each of the separators and to a blower for causing the conveying air to flow by suction, wherein each of the separators includes a product chamber and a clean air chamber, the product chamber being connected to the pneumatic conveying line, or to at least one such line where the plant has a plurality of such lines, and being arranged for discharging material accumulated therein to the consumer, the clean air chamber being connected to the suction line, and said chambers being separated from each other by a filter for separating the particulate material from its conveying air, and a finer mesh filter for separating the dust contained in the stream of clean air from the separators is provided in the suction line downstream of the clean air chambers and upstream of the suction connection of the blower.
2. A suction conveying plant according to claim 1 wherein the filter in each of the separators has a flow cross-section (as hereinbefore defined) substantially greater than the free cross-section of the suction
line.
3. A suction conveying plant according to claim 1 or claim 2, wherein the finer mesh filter comprises a battery of pocket-type filters.
4. A pneumatic suction conveying plant substantially as herein described with reference to the accompanying drawling.
5. A particulate material processing installation including a pneumatic suction conveying plant according to any one of the preceding claims.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2614713A DE2614713B2 (en) | 1976-04-06 | 1976-04-06 | Pneumatic suction conveyor system to supply several consumers |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1572003A true GB1572003A (en) | 1980-07-23 |
Family
ID=5974507
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB13181/77A Expired GB1572003A (en) | 1976-04-06 | 1977-03-29 | Pneumatic suction conveying plant |
Country Status (7)
Country | Link |
---|---|
JP (1) | JPS52123085A (en) |
DE (1) | DE2614713B2 (en) |
DK (1) | DK141684C (en) |
FR (1) | FR2347289A1 (en) |
GB (1) | GB1572003A (en) |
NL (1) | NL7702154A (en) |
SE (1) | SE7703510L (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110027134A (en) * | 2019-04-10 | 2019-07-19 | 中国寰球工程有限公司 | Polyolefine powder multifunctional comprehensive processing system and method |
CN110150730A (en) * | 2019-06-24 | 2019-08-23 | 湖南核三力技术工程有限公司 | Free-standing blower Pneumatic Feeding System |
CN111620128A (en) * | 2019-02-27 | 2020-09-04 | 韦尔特·克拉默 | Suction conveying system for bulk material |
CN110027134B (en) * | 2019-04-10 | 2024-05-10 | 中国寰球工程有限公司 | Multifunctional comprehensive treatment system and method for polyolefin powder |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8327832D0 (en) * | 1983-10-18 | 1983-11-16 | Nihot Bv | Waste and dust handling system |
DE3637701C2 (en) * | 1986-11-05 | 1997-06-19 | Motan Plast Automation Ag | Suction conveyor system |
DE3900173C1 (en) * | 1989-01-05 | 1990-07-12 | Azo Gmbh & Co, 6960 Osterburken, De | Pneumatic suction conveyor system for the volumetric apportioning of bulk material components |
DE3934910A1 (en) * | 1989-10-20 | 1991-04-25 | Azo Gmbh & Co | PNEUMATIC SUCTION CONVEYOR FOR GRAVIMETRICALLY ALLOCATING SCHUETTGUT COMPONENTS |
DE10024428A1 (en) * | 2000-05-19 | 2001-11-22 | Mann & Hummel Protec Gmbh | Filter-free plastic granule and fine powder pneumatic feed for multi-station activated by compressed air cylinder |
FI128263B (en) * | 2016-11-18 | 2020-01-31 | Jari Jokila | System and method of moving construction waste |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1081407A (en) * | 1952-07-28 | 1954-12-20 | Gebru Der Bu Hler | Pneumatic transport installation |
US3494460A (en) * | 1968-02-14 | 1970-02-10 | Calvin Lee Scott | Pneumatic conveyor and dust separator systems |
DE2136328B2 (en) * | 1971-07-21 | 1981-05-07 | Azo-Maschinenfabrik Adolf Zimmermann Gmbh, 6960 Osterburken | Pneumatically feeding multiple extruders with granulate - system meters supply to hoppers by cutting off air when filled |
DE2303011A1 (en) * | 1973-01-22 | 1974-07-25 | Meyer Maschinen Und Wiegeappar | Volumetric recording of components of a mixture - by feeding components to separate storage containers and measuring vessels under vacuum |
-
1976
- 1976-04-06 DE DE2614713A patent/DE2614713B2/en active Granted
-
1977
- 1977-02-28 NL NL7702154A patent/NL7702154A/en not_active Application Discontinuation
- 1977-03-28 SE SE7703510A patent/SE7703510L/en not_active Application Discontinuation
- 1977-03-29 GB GB13181/77A patent/GB1572003A/en not_active Expired
- 1977-03-30 FR FR7709567A patent/FR2347289A1/en active Granted
- 1977-04-01 JP JP3744477A patent/JPS52123085A/en active Pending
- 1977-04-05 DK DK150977A patent/DK141684C/en not_active IP Right Cessation
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111620128A (en) * | 2019-02-27 | 2020-09-04 | 韦尔特·克拉默 | Suction conveying system for bulk material |
CN110027134A (en) * | 2019-04-10 | 2019-07-19 | 中国寰球工程有限公司 | Polyolefine powder multifunctional comprehensive processing system and method |
CN110027134B (en) * | 2019-04-10 | 2024-05-10 | 中国寰球工程有限公司 | Multifunctional comprehensive treatment system and method for polyolefin powder |
CN110150730A (en) * | 2019-06-24 | 2019-08-23 | 湖南核三力技术工程有限公司 | Free-standing blower Pneumatic Feeding System |
Also Published As
Publication number | Publication date |
---|---|
DK141684B (en) | 1980-05-27 |
JPS52123085A (en) | 1977-10-15 |
DE2614713B2 (en) | 1981-01-08 |
DE2614713C3 (en) | 1987-07-09 |
FR2347289A1 (en) | 1977-11-04 |
NL7702154A (en) | 1977-10-10 |
FR2347289B1 (en) | 1983-11-18 |
DK141684C (en) | 1980-10-27 |
SE7703510L (en) | 1977-10-07 |
DK150977A (en) | 1977-10-07 |
DE2614713A1 (en) | 1977-10-27 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 19940329 |