IP Library Granted Patent US 10,758,853
Granted Patent B2
US 10,758,853 · App. 15/881,599 · Granted Sep 1, 2020

Combined briquetting and cyclonic separation device and process capable of removing particles from a fluid stream and converting directly into briquettes

Inventor: Martin Scaife (Singapore, SG)
Assignee: MOBIAIR PTE. LTD.
B01D45/18A61F13/15617B01D45/12B01D45/16B01D46/0005B01D46/0086B01D46/10B01D46/4254F24F11/39
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Quick Facts
Patent No.
US 10,758,853
App. No.
15/881,599
Granted
Sep 1, 2020
Kind
B2
Abstract

Process and apparatus capable to remove particles from a fluid stream (such as air or water) and directly convert the removed particles into a solid compact format commonly known as briquettes in a standalone combined single unit operation. The outlined process and equipment operates without the need for rotary valve technology and uses air versus hydraulics offering a cost competitive equipment solution for the end user. Active processes within the apparatus actively control the dust thereby allowing a variety of particles to be processes irrespective of moisture content and surface adhesive characteristics. Having the low-cost capability to convert explosive air/dust mixtures into briquettes significantly enhances safety and also reduces the associated manhandling effort required with disposing of collected dust with many briquettes typically having 100-500× the density of the incoming particles. In many regions the produced briquettes have a second hand value thereby creating a value stream from a zero value dust stream.

Claims (30)

1. An equipment ( 600 ) for separating a plurality of particles from a fluid stream and briquetting said plurality of particles, said equipment comprising:

a cyclonic separator ( 610 ) capable of accumulating particles of said plurality of particles loaded fluid in a particle outlet zone; and

a particle compactor ( 615 ) capable of forming briquettes comprising one or more pre-compaction means and a final briquetting means;

said particle compactor ( 615 ) being essentially unitary with a cyclonic separator by being directly connected thereto and being directly underneath said cyclonic separator along the direction of gravity; and

said one or more pre-compaction means is a mechanical press compactor that comprises a multi stage air cylinder ( 665 ) adapted to be driven by pressurized air wherein said one or more pre-compaction means and said final briquetting means are actuated by said multi stage air cylinder.

2. The equipment according to claim 1 , wherein at least one of said one or more pre-compaction means is a low air-pressure actuated mechanical press compactor.

3. The equipment according to claim 1 , wherein said cyclonic separator and said one or more pre-compaction means are in an air-tight closed housing, optionally comprising a pressure sensor.

4. The equipment according to claim 3 , wherein said step is adapted to receive a sensing means to allow surveillance and control of said cyclonic separator, said sensing means comprising one or more elements selected from the group consisting of a camera system, a lighting system, and a cleaning air jet system.

5. The equipment according to claim 1 , wherein said cyclonic comprises a first section and second section positioned downwards towards said particle outlet zone,

wherein said second section exhibits a diameter that is smaller than the diameter of said first section, and

wherein said first section and said at least one further section are positioned such that a step is created in a wall of said cyclotronic separator.

6. A manufacturing equipment comprising equipment for separating a plurality of particles from a fluid stream and briquetting said plurality of particles according to claim 1 .

7. A process for separating a plurality of particles from a particle loaded fluid stream and briquetting said plurality of particles, said process comprising the steps of:

providing a stream of particle loaded liquid or gaseous fluid and air;

accumulating a plurality of particles of said particle loaded fluid stream in a particle outlet zone for sending to a cyclonic separator ( 610 );

forming briquettes in a particle compactor ( 615 ) comprising one or more pre-compaction device(s), comprising a mechanical press compactor having a multi stage air cylinder, and a final briquetting device wherein said multi stage air cylinder is adapted to be driven by pressurized air wherein said one or more pre-compaction devices and said final briquetting device are actuated by said multi stage air cylinder;

feeding said particle loaded fluid stream into a cyclonic separator ( 610 );

accumulating a plurality of particles in a particle accumulating zone of said cyclonic separator;

transferring said accumulated plurality of particles through an outlet zone ( 810 ) of said cyclonic separator ( 610 ) directly to said particle compactor;

submitting said plurality of particles to a pre-compacting step in said pre-compaction device(s);

transferring said plurality of particles from said pre-compaction step to one or more further pre-compaction steps, and to said final briquetting step by employing no other transport means than said one or more pre-compaction devices;

actuating said final briquetting device for forming a plurality of briquettes by said multi stage air cylinder that concurrently drives said one or more pre-compaction devices, and using pressurized air for actuating said multi stage air cylinder, wherein said pressurized air is less than 10 bar.

8. The process according to claim 7 , wherein said plurality of particles of said particle loaded fluid stream exhibit differing properties selected from the group consisting of composition, size, and density.

9. The process according to claim 8 , wherein said fluid particle loaded stream is air, and said plurality of particles result from a manufacturing process of hygiene articles, comprising particles selected from the group consisting of cellulose fibers, dust, and superabsorbent polymer particles.

10. The process according to claim 7 , wherein said briquettes exhibit a size selected from the group consisting of less than 125 000 cm 3 , less than 1000 cm 3 , less than 1 cm 3 but more than 0.001 cm 3 , and more than 0.008 cm 3 .

11. A process according to claim 7 , wherein said plurality of briquettes exhibit a density selected from the group consisting of more than 100 kg/m 3 , more than 800 kg/m 3 , and more than 1000 kg/m 3 .

12. A manufacturing process comprising a process according to claim 7 , further comprising the steps of:

providing an automated briquette transport system, said automated briquette transport system being a continuous transport system, selected from the group consisting of a screw conveyor, a belt conveyor, a bucket conveyor, a pneumatic transfer conveyor, a vibrating conveyor, and a continuous flow conveyor;

providing a briquette storage or disposal system selected from the group consisting of a plurality of bags exhibiting a volume of at least 1001, or more than 1 m 3 , a plurality of drums that are moveable drums, a plurality of silos exhibiting a volume of more than 1 m 3 , a storage space adapted to allow heaps of briquettes being formed, said heaps exhibiting a volume of 1 m 3 , or more than 10 m 3 , and a continuous transport system connected to a downstream processing step, said downstream processing step selected from the group consisting of thermal recuperation and waste treatment system; and

transporting said briquettes by said transport system to said briquette storage or said disposal system.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 19, 2018
From: SCAIFE, MARTIN
To: MOBIAIR PTE.LTD.
Reel/Frame 045279/0030 →
Priority Claims (1)
SG 10201506050T · Aug 2, 2015 · national
Continuity (2)
Continuation PCTSG2016050368 · Jul 29, 2016
Related Publication 20180147516A1 · May 31, 2018