Field of the Invention
[0001] The invention concerns an apparatus to reduce size of material, particularly of light
material, preferably raw materials for panels.
Background of the Invention
[0002] An apparatus to reduce size of material typically transforms material, material pieces
and/or material chips in flakes and/or fibers. Examples of such apparatuses include
knife ring flakers, hammer mills, refiners or defibrators. These types of said apparatus
all comprise a supply unit and a size reduction unit. Materials for processing like
for example pieces of wood, plants, non-woody lignocelluloses and/or recycling materials
such as polymer, packaging fabrics, paper and cardboard waste are inserted in the
supply unit. Typically, the material is directly supplied from the supply unit to
the size reduction unit. The size reduction unit comprises means to reduce the size
of the material through cutting, shredding or grinding. In said machines, the size
reduction unit is mainly of the type of a knife ring where the material is carried
in a rotating impeller and pushed to the blades of a fixed ring with blades under
the influence of centrifugal force. Typically, the feed system of said machines is
driven by gravity force of the material. Therefore, particularly light material may
often lead to problems such as reduced throughput or clogging in the size reduction
unit. Examples for said light material include light wooden chips or flakes, straw,
flax, corn, grass, rice stalks, leaves, bamboo, shrubs, algae, seaweed and recycling
material such as polymer films, protective packaging fabrics, solve packaging, paper
and cardboard waste.
[0003] DE 02702338 A1 discloses an apparatus of the type of a knife ring flaker to reduce size of material
with a blade ring around a rotor characterized by a radial fan to reduce the problem
of material clogging at the blades by means of a cyclic air flow between knife ring
and housing. An air flow supports the transportation of materials.
Summary of the Invention
[0004] The present invention is set forth and characterized in the independent claims, while
the dependent claims describe other characteristics of the invention
[0005] The purpose of the invention is to achieve an improved apparatus for size reduction
of material, particularly of light material, preferably raw materials for panels.
[0006] The device according to the invention comprises an apparatus to reduce size of material,
particularly of light material, with a material supply unit and a size reduction unit
as well as a suction unit for sucking material, particularly light material, through
the size reduction unit.
[0007] Suction unit means a unit to generate depression, for example with a fan. In the
presence of gas, said depression enables a gas flow to the suction unit. Sucking of
material by said suction unit means that a gas, for example air, transfers forces
to the pieces and/or particles of said material, so that the material can move and
follow the direction of said gas flow to the suction unit.
[0008] The sucking of the material, particularly light material, through the size reduction
unit by a suction unit enables high material throughput and little clogging in an
improved manner especially compared with other gas flow techniques in order to transport
materials through a size reduction unit. In addition, by overcoming the problem of
clogging of particularly light material, the invention allows processing of material
that otherwise could not or only under great difficulties be processed.
[0009] One favorable embodiment of the invention comprises a gas source connected with the
entrance of the size reduction unit and/or with the outlet of the size reduction unit.
[0010] A gas source is a defined access to gas. A defined access is an access designed to
supply gas to the apparatus. A defined access does not mean areas where by some reason
gas may be sucked into the apparatus for example leaky pipes or connection as well
as connected units such as the supply unit where gas may enter the apparatus through
the material or when the supply unit runs out of material. A simple example for a
gas source could be an open end of a pipe leading to the environmental air. A complex
example for a gas source could be a chamber with gas supply and/or a conditioning
unit to condition the gas.
[0011] Connecting the gas source with the entrance of the size reduction unit enables feeding
with high feed rates of the material into the size reduction unit and also treating
the material with conditioned gas from the gas source prior to the size reduction
process. Connecting the gas source with the outlet of the size reduction unit leads
to reduced clogging in the size reduction unit and also allows treating the size reduced
material with conditioned gas from the gas source. The combination of both said connections
brings both described advantages.
[0012] One favorable embodiment of the invention comprises one or more flow channels for
guiding a gas flow and/or material flow. Flow channels can connect to other flow channels
or units, i.e. gas source or sucking unit, in a sealed manner. The cross-sectional
shape of a flow channel can be a polygon or round shape for example a rectangle or
a cycle. A flow channel can also branch off other flow channels. Said flow channels
for guiding a gas flow and/or material flow enable the targeted transport of material,
particularly driven by the suction unit.
[0013] One preferred embodiment comprises for example a flow channel starting from the gas
source, taking up a branch flow channel from the material supply unit, branch off
a flow channel or chamber for a separation unit and connecting to entrance of the
size reduction unit as well as another flow channel starting from the gas source,
taking up a branch flow channel from the outlet of the size reduction unit and connecting
to the suction unit.
[0014] One preferred embodiment of the invention comprises a gas source connected to the
entrance of the size reduction unit by a flow channel running above the size reduction
unit. This flow channel arrangement enables gravity force to support the material
flow to the size reduction unit.
[0015] One favorable embodiment of the invention comprises a supply unit placed above the
size reduction unit, preferably connected to the vertical part of the flow channel
leading to the entrance of the size reduction unit, particularly with a connection
in form of a down slope flow channel. Arranging the material supply unit in the described
way has the advantages, that gravity force supports the suction unit with the material
transport, thus reducing energy consumption. The connection of a flow channel to another
flow channel, particularly vertical downwards oriented flow channel, enables an additional
sucking effect that improves the material flow from the material supply unit. A down
slope flow channel for connection of the material supply unit with another flow channel
as the advantage, that heavy impurities or material pieces are moving on the bottom
of the flow channel instead of simply falling down as it would be the case in a vertical
flow channel.
[0016] One favorable embodiment of the invention comprises a separation unit for separating
heavy impurities in the material, particularly in form of a branched off chamber,
preferably branched off in a curve and/or in the direction of gravity forces, particularly
branched off from a flow channel for guiding a gas and material flow to the entrance
of the size reduction unit.
[0017] One favorable embodiment of the invention comprises a separation unit for separating
heavy impurities in the material. Said separation unit removes impurities that would
otherwise impurify the processed material and could damage the size reduction unit.
A separation unit arranged as branched off chamber is a very simple way of realizing
such separation unit. Branching off such chamber in a curve and/or in the direction
of gravity forces bring the advantage that heavy impurities can be separated in the
chamber due to their difference in weight, thus no complex separation devices are
needed. Said separation unit can be particularly branched off from a flow channel
for guiding a gas and material flow to the entrance of the size reduction unit to
assure that all material for processing in the size reduction unit passes the separation
unit. Thanks to such integrated separation unit, there is not need for an additional
work step for separation prior to the processing in the apparatus to reduce size of
material.
[0018] One preferred embodiment of the invention comprises a separation unit with means
for removal of separated heavy impurities by an operator for example through a removal
flap. Means for removal of the separated impurities by an operator can be realized
very simple and have the advantage of being very flexible and reliable compared to
complex automated solutions. For example a simple removal flap can be used.
[0019] One preferred embodiment of the invention comprises a size reduction unit, particularly
comprising a knife ring, arranged in a way that the entrance of the size reduction
unit is oriented horizontally and/or away from the gas source and/or the outlet of
the size reduction unit is oriented vertically and/or downward. The described orientation
of the entrance and outlet of the size reduction unit helps to reduce the space needed
to arrange the material supply unit and separation unit while taking advantage of
gravity forces to support the material transport, thus allowing the design of a smaller
dimensioned apparatus
[0020] One favorable embodiment of the invention comprises a outlet of the size reduction
unit and/or of the connected flow channel with a cross-section area smaller than the
cross-section area of the entrance of the size reduction unit and/or of the connected
flow channel to the suction unit, particularly connected in form of a T-shape, preferably
connected to a flow channel running from the gas source to the suction unit. The difference
in said cross-section areas enables an improved gas and material flow through the
size reduction unit and thereby boosts the favorable effects of the innovation. Same
benefits arise when connecting the outlet of the size reduction unit or a flow channel
connected to the outlet of the size reduction unit with a flow channel that connect
the gas source with the suction unit, for example with a T-shaped connection. Because
the gas flow in said flow channel leads to additional suction force at the outlet
of the size reduction unit and thereby improves the suction of material through the
size reduction unit.
[0021] One favorable embodiment of the invention comprises a suction unit with a greater
cross-section area compared to the entrance of the suction unit and/or with means
for separating gas and material. The greater cross-section area within the suction
unit compared to the entrance of the suction unit allows the implementation of a suction
driver, for example fan, adapted to the material that shall be processed in the apparatus
without imposing close restrictions for the dimensions of said suction driver. Furthermore,
said cross-section area different leads to improved flow characteristics of the gas
and/or material for separating gas and material in the suction unit. Said separation
of gas and material in the suction unit brings the advantages that small particles
or additives, which were added to the gas, can be extracted for environmentally safe
removal or recycling, thus eliminating the release of harmful particles and dusk to
the environment and thereby increase operating safety or obviating the need for additional
particle and/or dusk sucking devices.
[0022] One favorable embodiment of the invention comprises a distributer for distributing
a gas flow in two or more separated gas flows. Distribution of a gas flow in separated
gas flows means that the gas flow of the supplying flow channel is distributed in
branch flow channels in a way that the flow rate in each channel can be adjusted.
A simple way of implementing said distributer is to place a turnable flap particularly
inside of the supply flow channel with for example the pivot bearing positioned in
the center point of a Y-, T- or t-shaped duct branch. Seen from the pivot gearing,
the flap can be placed in or against the direction of the gas flow. The advantage
of said distributer is that the process outcome of the apparatus can be improved by
adapting the flow rate in each flow channel to the processed material.
[0023] One favorable embodiment of the invention comprises a gas source comprises a gas
inlet with a mesh or filter and/or an outlet with distributer, preferably with a cross-section
area of the outlet smaller than the cross-section area of the inlet of said gas source,
Intake of material or dusk is avoided by mesh or filter at the inlet of the gas source
that otherwise would impurify the processed material. Particularly for a gas source
with integrated hazardous conditioning unit such as a heat exchanger, a mesh also
increases operating safety. The distributer at the outlet allows adaption of the flow
rates in the supplied flow channels to the currently processed material to improve
process outcome. A gas source with greater cross-section area of inlet than of the
outlet brings the advantage of reduced flow rate at the inlet, thus improving operational
safety as well as increased efficiency for favorable embodiments with integrated heat
exchangers.
[0024] In another aspect of the invention, an apparatus to reduce size of material, particularly
of light material, with a material supply unit and a size reduction unit comprises
a conditioning unit for treatment of material before and/or after size reduction preferably
by means of conditioned gas. The advantage of the invention is that additional working
steps prior or after the working step of size reduction are obviated. Preferably conditioned
gas, meaning gas conditioned by the conditioning unit, can be used for said material
treatment in order to achieve homogeneous treatment of the entire material surface.
[0025] One favorable embodiment of the invention comprises a conditioning unit that allows
adjusting the gas temperature and/or adding additives to the gas, particularly liquids,
other gases, and/or powders. Adjusting the gas temperature enables to improve the
process. High gas temperature leads for example to dry material pieces that typically
reveal reduced clogging. Adding additives enables various beneficial effects to the
size reduction process, the operating safety and the characteristics of the treated
material. There are for example additives that increase fire resistance and thereby
improved operating safety. Additives in form of for example powers can particularly
reduce clogging. Other additives such as for example disinfectants, perfumes, colorants,
neutralizers and antioxidants as well as waterproof, anti-aging and anti-rot agents
enable value addition to the material without additional, subsequent process steps.
Furthermore, addition of other gases or liquids enables to adjust the humidity of
the gas leading to wetting or drying the material.
[0026] One favorable embodiment of the invention comprises an injector for adding additives
particularly to gas for example within the gas source, preferably arranged with a
nozzle shaped injector particularly placed in the middle area of a chamber or flow
channel for guiding a gas flow and/or directed towards the outlet of said chamber
or flow channel. Nozzle shape means that the cross-section area of the injector opening
is narrowing down from a wide to a smaller cross-section area in the direction of
the flow of additives. The described placement and orientation of said injector enables
favorable distribution of the additives in the gas flow.
[0027] One favorable embodiment of the invention comprises a an additives supply unit for
supplying additives to the injector preferably in the shape of a funnel, particularly
placed above the injector and/or outside of a chamber or flow channel, and preferably
connected to the injector with a L-shaped supply channel. The described additives
supply unit with connection to the injector is a very simple but reliable way of supplying
the injector with additives while offering an easy access for the operator to refill
additives.
[0028] One favorable embodiment of the invention comprises a heat exchanger for cooling
and/or heating gas, preferably placed directly in a chamber or flow channel for containing
or guiding a gas flow, particularly at the gas inlet of the gas source. A heat exchanger
of such kind and arranged in the proposed manner is a simple and effective way to
heat up or cool down gas.
[0029] One favorable embodiment of the device according to the invention comprises an improved
apparatus with a size reduction unit comprising a knife ring and impeller for example
as used in a knife ring flaker.
The features described in the main, dependent and independent claims can be implemented
in an apparatus with a size reduction unit comprising a knife ring and impeller very
easily while delivering the described advantages of the innovation particularly well.
Brief description of the drawings
[0030] These and other characteristics of the invention will be clear from the following
description of a preferential form of embodiment, given as a non-restrictive example,
with reference to the attached drawings wherein:
Fig. 1 shows an apparatus to reduce size of material according to the invention with
a size reduction unit comprising a knife ring.
Detailed description of a preferential embodiment
[0031] With reference to the attached drawing, an apparatus to reduce size of material 1,
particularly light material, comprises a gas source 2, flow channels 3 for guiding
a gas flow and/or material flow between connected units or other flow channels, a
material supply unit 4, a separation unit 5, a size reduction unit 6, a conditioning
unit 7 and a suction unit 8.
[0032] The suction unit 8 causes depression and thereby drives a gas flow consisting of
environmental air 18 and originating at the gas source 2 with integrated conditioning
unit 7.
[0033] The gas source 2 comprises a chamber with an inlet to allow environment air 18 from
outside the apparatus to enter into the chamber. In order to reduce the incoming flow
rate of the environment air 18, the cross-section area of the inlet 9 of said gas
source 2 is designed greater than the cross-section area of the outlet 10, The cross-section
area of the inlet 9 is covered by a mesh 11, At the outlet of said gas source 2, a
turnable flap 12 with pivot bearing 13 placed in the center point of a T-shaped duct
branch 14 works as distributer to distribute the gas flow at the outlet of the gas
source 2 to the two branched off flow channels 3 and to adjust the gas flow rate in
each flow channel.
[0034] The conditioning unit 7 for adjusting the temperature and adding additives to the
gas 2 is integrated in the gas source 2. A heat exchanger 15 is placed inside of the
chamber of the gas source 2 directly behind the mesh 11 and running over the entire
cross-section area of the inlet 9 of the gas source 2. Additives 16 including liquids
or powders are supplied from outside the chamber of the gas source 2 to a nozzle shaped
injector 17 in the center the gas flow in said chamber by an additives supply unit
with a funnel (33) and L-shaped supply channel 34.
[0035] At the outlet of the gas source 2, said distributer distributes the gas flow from
the gas source 2 into two separated gas flows 19, 20.
[0036] One gas flow 19 is guided by means of flow channels 3 from the gas source 2 above
the size reduction unit 6 to the intersection with the material flow 21 from the material
supply unit 4 that is connected through a down sloped branch flow channel. The depression
in that flow channel, the passing gas flow 19 and the gravity forces all facilitate
the material flow 21 of the material 1 into the flow channel 3 with the gas flow 19,
[0037] After that intersection, the gas flow 19 and the material flow 21 combined to one
gas material flow 22. A curve of the flow channel 3 between said intersection and
the entrance of the size reduction unit 6 caused the gas material flow 22 to follow
that curve. Heavy impurities 23 are diverted into the branched off separation unit
5 in direction of and due to gravity forces and can be removed through a flap 32.
[0038] After passing the separation unit 5, the gas material flow 22 runs through the size
reduction unit 6 comprising a knife ring 24 and a rotating impeller 25 for pressing
the material against the blades of the knife ring 24 in order to facilitate size reduction
of the material.
[0039] After the gas material flow 22 passed the size reduction unit 6, the gas flow with
size reduced material 26 run into the gas flow 20 at a T-shape intersection of the
respective flow channels 3. The cross-section area of the outlet of the size reduction
unit 28, which is equal to the connected flow channel 3, is smaller than the cross-section
area of the entrance of the size reduction unit 27 and the cross-section area of the
connected flow channel to the entrance of the suction unit 29. The difference in said
cross-section areas enables an improved gas material flow through the size reduction
unit with increased suction force as well as improved material distribution in the
gas flow with size reduced material heading the suction unit 8 for improved separation
of gas and material in the suction unit 8.
[0040] The suction unit cross-section area 30 is again greater than the cross-section areas
of the entrance of the suction unit 29 to enable usage of bigger dimensioned fans
31,
[0041] It is obvious however that modifications and/or additions can be made to the apparatus
as described heretofore, but these shall remain within the field and scope of the
invention. For example, the size reduction unit can have different components from
those shown and described here or the conditioning unit can be replaced by another,
functionally equivalent element.
1. An apparatus to reduce size of material (1), particularly of light material, preferably
raw materials for panels, comprising a material supply unit (4) and a size reduction
unit (6), characterized by a suction unit (8) for sucking material (1), particularly light material, through
the size reduction unit (6).
2. Apparatus as in Claim 1, characterized by a gas source (2) connected with the entrance of the size reduction unit (6) and/or
with the outlet of the size reduction unit (6).
3. Apparatus as in the preceding Claim, characterized by one or more flow channels (3) for guiding a gas flow and/or material flow.
4. Apparatus as in at least one of the preceding Claims, characterized in that the material supply unit (4) is placed above the size reduction unit (6), preferably
connected to the vertical part of the flow channel (3) leading to the entrance of
the size reduction unit (6), particularly with a connection in form of a down slope
flow channel.
5. Apparatus as in at least one of the preceding Claims, characterized by a separation unit (5) for separating heavy impurities (23) in the material (1), particularly
in form of a branched off chamber, preferably branched off in a curve and/or in the
direction of gravity forces, particularly branched off from a flow channel (3) for
guiding a gas and material flow to the entrance of the size reduction unit (6).
6. Apparatus as in at least one of the preceding Claims, characterized in that the cross-section area of the outlet of the size reduction unit (28) and/or of the
connected flow channel are smaller than the cross-section area of the entrance of
the size reduction unit (27) and/or of the connected flow channel to the suction unit
(29), particularly connected in form of a T-shape, preferably connected to a flow
channel (3) running from the gas source (2) to the suction unit (8).
7. Apparatus as in at least one of the preceding Claims, characterized by a suction unit (8) with a greater cross-section area (30) compared to the entrance
of the suction unit (29) and/or with means for separating gas and material.
8. Apparatus as in at least one of the preceding Claims, characterized by a distributer for distributing a gas flow in two or more separated gas flows (19,
20), preferably by means of a turnable flap (12) particularly inside of a flow channel
with for example the pivot bearing (19) placed in the center point of a Y-, T- or
t-shaped duct branch (14),
9. Apparatus as in at least one of the preceding Claims, characterized in that the gas source (2) comprises a gas inlet with a mesh [11] or filter and/or an outlet
with distributer, preferably with a cross-section area of the outlet (10) smaller
than the cross-section area of the inlet (9) of said gas source (2).
10. An apparatus to reduce size of material (1), particularly of light material, preferably
raw materials for panels, comprising a material supply unit (4) and a size reduction
unit (6), characterized by a conditioning unit (7) for treatment of material before and/or after size reduction
preferably by means of conditioned gas.
11. Apparatus as in the preceding Claim, characterized in that said conditioning unit (7) allows adjusting the gas temperature and/or adding additives
(16) to the gas, particularly liquids, other gases, and/or powders.
12. Apparatus as in the preceding Claim, characterized by an injector (17) for adding additives (16) particularly to gas for example within
the gas source (2), preferably arranged with a nozzle shaped injector (17) particularly
placed in the middle area of a chamber or flow channel for guiding a gas flow and/or
directed towards the outlet of said chamber or flow channel.
13. Apparatus as in the preceding Claim, characterized by an additives supply unit for supplying additives to the injector (17) preferably
in the shape of a funnel (33), particularly placed above the injector (17) and/or
outside of a chamber or flow channel, and preferably connected to the injector (1
7) with a L-shaped supply channel (34).
14. Apparatus as in at least one of the preceding Claims, characterized by a heat exchanger (15) for cooling and/or heating gas, preferably placed directly
in a chamber or flow channel for containing or guiding a gas flow, particularly at
the gas inlet of the gas source (2).
15. Apparatus as in at least one of the preceding Claims, characterized by a size reduction unit (6) comprising a knife ring (24) and impeller (25).