CA2245330A1 - Process for producing batches of rubber-based composition - Google Patents
Process for producing batches of rubber-based composition Download PDFInfo
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- CA2245330A1 CA2245330A1 CA 2245330 CA2245330A CA2245330A1 CA 2245330 A1 CA2245330 A1 CA 2245330A1 CA 2245330 CA2245330 CA 2245330 CA 2245330 A CA2245330 A CA 2245330A CA 2245330 A1 CA2245330 A1 CA 2245330A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J11/00—Recovery or working-up of waste materials
- C08J11/04—Recovery or working-up of waste materials of polymers
- C08J11/06—Recovery or working-up of waste materials of polymers without chemical reactions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/0026—Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
- B29B17/0042—Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting for shaping parts, e.g. multilayered parts with at least one layer containing regenerated plastic
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/002—Methods
- B29B7/005—Methods for mixing in batches
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
- B29B7/06—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
- B29B7/10—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
- B29B7/12—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with single shaft
- B29B7/16—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with single shaft with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/02—Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
- B29B7/22—Component parts, details or accessories; Auxiliary operations
- B29B7/28—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control
- B29B7/286—Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control measuring properties of the mixture, e.g. temperature, density
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
- B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
- B29B7/7495—Systems, i.e. flow charts or diagrams; Plants for mixing rubber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/82—Heating or cooling
- B29B7/823—Temperature control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/82—Heating or cooling
- B29B7/826—Apparatus therefor
-
- 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
- B29C2791/00—Shaping characteristics in general
- B29C2791/001—Shaping in several steps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2021/00—Use of unspecified rubbers as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/26—Scrap or recycled material
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Processes for the batch production of rubber-based compositions capable of being shaped and shaped articles made thereof. They include a step of high intensity mixing cured rubber particles with other selected compounds into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades. Through high speed rotation of the shaft, blade tip speed above about 20 meter/s are obtained to intensively mix and thermokinetically heat the batch of mixable material, whose temperature is continuously monitored.
Discharge of the batch from the mixing chamber takes place when the temperature is considered to have reached a reference value ensuring a substantially uniform mix of the rubber material and added compounds, to produce the rubber-based composition. According to a first preferred embodiment, cured rubber is fed into the mixing chamber with a resinous material, and discharge occurs at a temperature ensuring a substantially uniform mix of the rubber material in a matrix of resinous material to produce the rubber-based composition, which can be then shaped without any further heating. According to a second preferred embodiment, a curing agent is added to the cured rubber particles, and the batch is discharged from the mixing chamber when the temperature reaches a reference value ensuring a substantially uniform mix of the cured rubber material with the curing agent without causing a significant further curing, to produce a rubber-based composition capable of being heat-shaped. Other preferred embodiments using a reactive polymeric binding agent and a bonding agent are described.
Discharge of the batch from the mixing chamber takes place when the temperature is considered to have reached a reference value ensuring a substantially uniform mix of the rubber material and added compounds, to produce the rubber-based composition. According to a first preferred embodiment, cured rubber is fed into the mixing chamber with a resinous material, and discharge occurs at a temperature ensuring a substantially uniform mix of the rubber material in a matrix of resinous material to produce the rubber-based composition, which can be then shaped without any further heating. According to a second preferred embodiment, a curing agent is added to the cured rubber particles, and the batch is discharged from the mixing chamber when the temperature reaches a reference value ensuring a substantially uniform mix of the cured rubber material with the curing agent without causing a significant further curing, to produce a rubber-based composition capable of being heat-shaped. Other preferred embodiments using a reactive polymeric binding agent and a bonding agent are described.
Description
Process for producing batches of rubber-based composition The present invention relates to processes for producing batches of rubber-based composition and articles made thereof, and more 5 particularly to processes for producing batches of rubber-based composition and shaped made thereof.
Since the creation of the rubber industry over more than a century ago, rubber materials have been essentially produced through processes based on dimes vulcanization. In the early stages, dimes-based 10 materials were produced through plant-latex obtained from particular tropical trees such as Para rubber-plant (Hevea). Synthetic rubbers have first been introduced during the second world war to obviate a shortage in natural rubber supply. Dimes-based rubbers, either natural or synthetic, are made of macromolecular compounds exhibiting significant 15 flowing characteristic under tensile stress. Actually, such basic materials do not present great interest for industrial applications. To prevent macromolecular slipping for the purpose of providing a material capable of sustaining deformation while recovering its initial state after stressing, blocking of the macromolecular chains to one another is 20 required. Such molecular chains blocking is obtained through a process known as vulcanization or curing, which typically consists of cross-linking macromolecular chains at double bond sites which are present along the chains, using sulfur as the linking element or an organic peroxide. Typically, curing occurs through heating diene-based rubber 25 materials at a temperature between about 130°C to 150°C in the presence of about 7 - 10% of sulfur. Mechanical properties of sulfur-cured rubbers vary with cross-linking density which is proportional to the initial sulfur concentration. In practice, compositions of various virgin (uncured) rubber types, such as natural rubber, butyl rubber, 30 polybutadiene and neoprene, with specific additives such as curing starting agents and curing accelerators, have been developed to obtain, after curing, rubber-based material exhibiting various mechanical properties such as tensile strength, maximum tensile elongation, tear strength, embrittlement temperature and resilience.
35 During the past years, due to the generally high cost of uncured rubbers, reclaimed cured rubber in the form of particles or dust has been used as raw material to form a variety of manufactured articles.
Essentially, the technique usually consists of mixing rubber particles with 1% - 5% sulfur and curing the obtained mix in a suitable mold heated at a temperature of about 180°C while applying a pressure 5 between 500 pound/sq.in. to 2000 pound/sq.in. with a conventional hydraulic press. Processes using such technique are generally known to be more cost effective than processes using uncured rubber as raw material, which is significantly more expensive than reclaimed rubber.
However, the mechanical properties exhibited by such reclaimed 10 materials are generally inferior, typically characterized by a maximum tensile strength of about 300 pound/sq.in., a maximum tensile elongation of about 50%, and maximum tear strength of about 100 pound/in., which properties are significantly inferior than those exhibited by uncured rubber-based compositions. Such inferior mechanical behavior is mainly 15 due to porosity characteristics and cross-linking level. Materials made of rubber particles or dust are characterized by a porosity which is generally responsible for the appearance of microfissures under mechanical strength. Furthermore, effective contact areas between adjacent particles of a reclaimed rubber material are reduced as 20 compared to those observed in virgin raw material. Under such conditions, cross-linking between macromolecules of adjacent particles are reduced accordingly, since most free double links of adjacent particles are not in sufficiently close proximity to be bound, and accordingly the non-reacted curing agent rapidly becomes in excess.
25 Microfissures appearing within the rubber material initiate flaws therein which rapidly grow toward material rupture, due to the weakness of internal forces binding rubber particles together, observed at low cross-linking level.
A known technique to reduce the inherent porosity of a material 30 made of reclaimed rubber particles consists in adding a resin, preferably a thermoplastic resin, to bind the rubber particles and therefore reduce porosity. A certain amount of uncured rubber material can also be added to increase the number of free double bond available for curing.
Additives such as compatibility agents may also be added. The resultant 35 composition is used to produce rubber materials which have been found to exhibit improved mechanical properties in the range of 400 pound/sq.in. for tensile strength, 250% for maximum tensile elongation and 180 pound/in for maximum tear strength. However, such improved reclaimed rubber materials still exhibit lower mechanical properties as compared to materials essentially made of virgin rubber, since the cross-5 linking level remains substantially unchanged when a thermoplastic binding resin is used, and because the electrostatic forces acting between rubber particles and thermoplastic resin are also weak. Such an improved technique is disclosed in U.S. Patent No. 5,510,419 issued April 13, 1996, to Burgoyne et al., and it teaches to produce a polymer-10 modified rubber composition comprising reclaimed cured styrene-butadiene rubber particles, uncured rubber, a styrene-based thermoplastic resin, a homogenizing agent, to form a blend wherein the thermoplastic resin is substantially homogeneously mixed with the cured and uncured rubbers. Additives including plasticizers, lubricants, mold 15 release agent or viscosity modifiers such as traps-polyoctanamer rubber may also be added. Use of a batch mixer such as the well known Moriyama or Bandbury high intensity mixers is proposed to produce a moldable composition showing a temperature between 120°C and 150°C, which is then transferred to a mold which is preheated at a 20 temperature above a vulcanizing temperature of about 120°C. Another similar process is disclosed in U.S. Patent No. 5,425,904 issued June 20, 1995, to Smits, which uses rubber latex to treat cured waste rubber particles with a curing agent to produce an activated moldable composition. Another similar approach is taught in U.S. Patent No.
25 4,257,925 issued March 24, 1981, to Freeguard, which consists of swelling reclaimed tire rubber with a monomer and then causing polymerization thereof.
In order to further improve mechanical properties of reclaimed rubber materials, the addition of various reactive cross-linking resin 30 binders to the curing agent has been proposed. In U.S. Patent No.
Since the creation of the rubber industry over more than a century ago, rubber materials have been essentially produced through processes based on dimes vulcanization. In the early stages, dimes-based 10 materials were produced through plant-latex obtained from particular tropical trees such as Para rubber-plant (Hevea). Synthetic rubbers have first been introduced during the second world war to obviate a shortage in natural rubber supply. Dimes-based rubbers, either natural or synthetic, are made of macromolecular compounds exhibiting significant 15 flowing characteristic under tensile stress. Actually, such basic materials do not present great interest for industrial applications. To prevent macromolecular slipping for the purpose of providing a material capable of sustaining deformation while recovering its initial state after stressing, blocking of the macromolecular chains to one another is 20 required. Such molecular chains blocking is obtained through a process known as vulcanization or curing, which typically consists of cross-linking macromolecular chains at double bond sites which are present along the chains, using sulfur as the linking element or an organic peroxide. Typically, curing occurs through heating diene-based rubber 25 materials at a temperature between about 130°C to 150°C in the presence of about 7 - 10% of sulfur. Mechanical properties of sulfur-cured rubbers vary with cross-linking density which is proportional to the initial sulfur concentration. In practice, compositions of various virgin (uncured) rubber types, such as natural rubber, butyl rubber, 30 polybutadiene and neoprene, with specific additives such as curing starting agents and curing accelerators, have been developed to obtain, after curing, rubber-based material exhibiting various mechanical properties such as tensile strength, maximum tensile elongation, tear strength, embrittlement temperature and resilience.
35 During the past years, due to the generally high cost of uncured rubbers, reclaimed cured rubber in the form of particles or dust has been used as raw material to form a variety of manufactured articles.
Essentially, the technique usually consists of mixing rubber particles with 1% - 5% sulfur and curing the obtained mix in a suitable mold heated at a temperature of about 180°C while applying a pressure 5 between 500 pound/sq.in. to 2000 pound/sq.in. with a conventional hydraulic press. Processes using such technique are generally known to be more cost effective than processes using uncured rubber as raw material, which is significantly more expensive than reclaimed rubber.
However, the mechanical properties exhibited by such reclaimed 10 materials are generally inferior, typically characterized by a maximum tensile strength of about 300 pound/sq.in., a maximum tensile elongation of about 50%, and maximum tear strength of about 100 pound/in., which properties are significantly inferior than those exhibited by uncured rubber-based compositions. Such inferior mechanical behavior is mainly 15 due to porosity characteristics and cross-linking level. Materials made of rubber particles or dust are characterized by a porosity which is generally responsible for the appearance of microfissures under mechanical strength. Furthermore, effective contact areas between adjacent particles of a reclaimed rubber material are reduced as 20 compared to those observed in virgin raw material. Under such conditions, cross-linking between macromolecules of adjacent particles are reduced accordingly, since most free double links of adjacent particles are not in sufficiently close proximity to be bound, and accordingly the non-reacted curing agent rapidly becomes in excess.
25 Microfissures appearing within the rubber material initiate flaws therein which rapidly grow toward material rupture, due to the weakness of internal forces binding rubber particles together, observed at low cross-linking level.
A known technique to reduce the inherent porosity of a material 30 made of reclaimed rubber particles consists in adding a resin, preferably a thermoplastic resin, to bind the rubber particles and therefore reduce porosity. A certain amount of uncured rubber material can also be added to increase the number of free double bond available for curing.
Additives such as compatibility agents may also be added. The resultant 35 composition is used to produce rubber materials which have been found to exhibit improved mechanical properties in the range of 400 pound/sq.in. for tensile strength, 250% for maximum tensile elongation and 180 pound/in for maximum tear strength. However, such improved reclaimed rubber materials still exhibit lower mechanical properties as compared to materials essentially made of virgin rubber, since the cross-5 linking level remains substantially unchanged when a thermoplastic binding resin is used, and because the electrostatic forces acting between rubber particles and thermoplastic resin are also weak. Such an improved technique is disclosed in U.S. Patent No. 5,510,419 issued April 13, 1996, to Burgoyne et al., and it teaches to produce a polymer-10 modified rubber composition comprising reclaimed cured styrene-butadiene rubber particles, uncured rubber, a styrene-based thermoplastic resin, a homogenizing agent, to form a blend wherein the thermoplastic resin is substantially homogeneously mixed with the cured and uncured rubbers. Additives including plasticizers, lubricants, mold 15 release agent or viscosity modifiers such as traps-polyoctanamer rubber may also be added. Use of a batch mixer such as the well known Moriyama or Bandbury high intensity mixers is proposed to produce a moldable composition showing a temperature between 120°C and 150°C, which is then transferred to a mold which is preheated at a 20 temperature above a vulcanizing temperature of about 120°C. Another similar process is disclosed in U.S. Patent No. 5,425,904 issued June 20, 1995, to Smits, which uses rubber latex to treat cured waste rubber particles with a curing agent to produce an activated moldable composition. Another similar approach is taught in U.S. Patent No.
25 4,257,925 issued March 24, 1981, to Freeguard, which consists of swelling reclaimed tire rubber with a monomer and then causing polymerization thereof.
In order to further improve mechanical properties of reclaimed rubber materials, the addition of various reactive cross-linking resin 30 binders to the curing agent has been proposed. In U.S. Patent No.
3,489,710 issued January 13, 1970, to Bonotto et al., ethylene-based flexible resins reactive with a curing agent such as sulfur are mixed with reclaimed rubber particles in the presence of the curing agent using a high intensity batch mixer such as a Bandbury mixer. Similarly, in U.S.
35 Patent No. 4,481,335 issued November 6, 1984 to Stark, a liquid sulfur-curable polymeric binder, namely a homopolymer or copolymer of 1,4-butadiene and substituted butadiene, is blended with cured rubber scrap and sulfur to produce a treated rubber material which can be used in large proportion as a filler or extender for uncured rubbers. Although known prior art processes employing reclaimed rubber have heretofore 5 proved to be capable of producing, at lesser cost, shaped rubber-based products of various quality in terms of mechanical properties, in order to be practiced on an industrial basis, these processes generally require the use of large and expensive high intensity mixing equipment, generally limited to long production cycles to provide a composition homogeneity 10 which is required to obtain uniformity of physical properties, which requirement may affect the effective productivity of the process.
Furthermore, known processes for mixing curable rubber-based compositions may not provide proper reduction of humidity within a batch to be formed, which may cause dangerous high pressure steam 15 discharge upon removal from the mold. Therefore, there is still a need for a process for producing batches of rubber-based composition and articles made therefrom which overcome the foregoing drawbacks of the prior art.
It is therefore an object of the present invention to provide 20 economic and safe processes for the production of moldable rubber based compositions and shaped products made therefrom, which affords short production cycle for a large range of shaped product quality requirements in terms of mechanical characteristics.
According to the above object, from a broad aspect, there is 25 provided a process for producing a batch of rubber-based composition capable of being formed into an article, comprising the steps of:
feeding a batch of mixable material comprising from about 40%
to about 90% by weight of particles of cured rubber material with from about 60% to about IO% ;;;;;;by weight of a resinous material into a 30 closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meters to about 35 meters under conditions effective to intensively mix and thermokinetically heat the batch of mixable material;
35 continuously monitoring one of temperature and temperature related parameter of the batch;
35 Patent No. 4,481,335 issued November 6, 1984 to Stark, a liquid sulfur-curable polymeric binder, namely a homopolymer or copolymer of 1,4-butadiene and substituted butadiene, is blended with cured rubber scrap and sulfur to produce a treated rubber material which can be used in large proportion as a filler or extender for uncured rubbers. Although known prior art processes employing reclaimed rubber have heretofore 5 proved to be capable of producing, at lesser cost, shaped rubber-based products of various quality in terms of mechanical properties, in order to be practiced on an industrial basis, these processes generally require the use of large and expensive high intensity mixing equipment, generally limited to long production cycles to provide a composition homogeneity 10 which is required to obtain uniformity of physical properties, which requirement may affect the effective productivity of the process.
Furthermore, known processes for mixing curable rubber-based compositions may not provide proper reduction of humidity within a batch to be formed, which may cause dangerous high pressure steam 15 discharge upon removal from the mold. Therefore, there is still a need for a process for producing batches of rubber-based composition and articles made therefrom which overcome the foregoing drawbacks of the prior art.
It is therefore an object of the present invention to provide 20 economic and safe processes for the production of moldable rubber based compositions and shaped products made therefrom, which affords short production cycle for a large range of shaped product quality requirements in terms of mechanical characteristics.
According to the above object, from a broad aspect, there is 25 provided a process for producing a batch of rubber-based composition capable of being formed into an article, comprising the steps of:
feeding a batch of mixable material comprising from about 40%
to about 90% by weight of particles of cured rubber material with from about 60% to about IO% ;;;;;;by weight of a resinous material into a 30 closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meters to about 35 meters under conditions effective to intensively mix and thermokinetically heat the batch of mixable material;
35 continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said rubber material in a matrix of said resinous material to produce said rubber-based composition.
5 Preferred embodiments of the present invention will now be explained in detail with reference to the accompanying drawing in which:
Fig. 1 is a perspective view of a high intensity batch mixer used to practice the 10 process according to the present invention;
Fig. 2 is a partially cross-sectional perspective view of a front end of the batch mixer shown in Fig.l; and Fig. 3 is a graph showing the variation of a mixer motor load current measured as a function of time, and related thresholds used to 15 control a process according to the present invention.
Referring now to the drawings, a high intensity mixer 10 which could be used to carry out the process according to the present invention is depicted, which mixer 10 comprises a base frame 12 including a pair of longitudinal beams 14 secured to upper ends of front and rear pairs of 20 floor mounted pillars 16 rigidly secured by transverse members 18 and bracing plates 20. On the rear portion of the beams 14 is secured a motor base 22 having a mounting plate 24 on which is secured lower parts of legs 26 supporting an electric industrial motor 28, preferably of a self cooling type. As shown in Fig. 2, motor 28 is provided with an output 25 shaft 30 connected to a driving end of a flexible coupling 13 of known construction, which has a driven end connected to a driving shaft 15 extending through a cantilever bearing unit 17 permanently lubricated with a pumped oil circuit (not shown). The flexible coupling is covered fox protection with a casing 19 (Fig. 1) provided with an aperture 21 30 giving required clearance for the main driving shaft 15. The cantilever bearing unit 17 is rigidly mounted through rear and front supports 29 (only rear support being shown in Fig. 2) on an horizontal plate 19 as part of a sub-frame assembly 21 secured to the front portions of the beams 14, and having a vertical mounting plate 23 further secured to the 35 horizontal plate 19 through a pair of opposed bracing plates 27.
As shown in Fig. 2, apparatus 10 further comprises a cylindrical mixing chamber 32 having outer double peripheral wall 34 and provided with cooling fluid ports 35 (Fig. 1) to be connected to a cooling circuit line (not shown} as will be later explained in more detail. Wall 34 is 5 further provided with and optional temperature probe 37. Mixing chamber 32 further has a circular double end wall 36 defining a mixing cavity 38. Mixing chamber 32 is secured to the body of a feeding unit 42 having an outer double peripheral wall 39 provided with cooling fluid ports 41 as better shown in Fig. l, and an input tubular portion 44 in 10 communication with an output annular portion 46 defining a feeding cavity 48 therebetween, as better shown in Fig. 2. The inner edge of peripheral double wall 34 of the mixing chamber 32 defines an annular channel adapted to receive an annular rib protruding from the outer surface of a first collar 52, which is then rigidly welded or otherwise 15 secured to the double wall 34. The inner surface of first collar 52 is in turn joined to the outer mating surface of a second collar 54. Collars 52 and 54 are rigidly bolted together. Output annular portion 46 of the feeding unit 42 tightly engages with an inner opening formed in collar 54, to form an annular inner end wall opposed to circular end wall 36.
20 Input tubular portion 44 defines with the inner rear surface of collar 54 an internal space 33 in fluid communication through a fluid line (not shown) with internal space 31 within double walls 34 and 36, to form a cooling cavity as part of the cooling fluid circuit filled with a cooling fluid such as cold water, for limiting the temperature of the feeding 25 cavity and mixing chamber to a level providing desired process continuity.
Centrally extending through the output annular portion 46 is a two-part driven shaft 56 having a forward bladed portion 58 contained in the mixing chamber 32 and being opposed to a rearward threaded 30 portion 60 contained in the feeding cavity 48 and acting as a conveyor screw. The cantilever bearing unit 17 provides axial and radial stability for shaft 56 while allowing rotation thereof about axis 66. Rearward shaft portion 60 is rigidly secured to the driven end of the driving shaft 15 using a key screw (not shown}, to impart rotation to the rearward 35 shaft portion 60. The outer end of forward shaft portion 58 is formed with a threaded hole 62 for receiving an aligned bolt 64 securing the forward shaft portion 58 to the driven end of the driving shaft 15, to impart rotation to the forward shaft portion 58. An optional aeration port 65 is provided at the outer surface of double end wall 36.
Alternatively, instead of using a cantilever arrangement, port 65 may be 5 replaced by a bearing for receiving a rotating rod (not shown) to be secured to the outer end of the forward shaft portion 58. The outer diameter of threads 66 provided on the driven shaft 56 is chosen to closely fit within output annular portion 46, mixing cavity 38 thereby becoming substantially enclosed. Input tubular portion 44 of feeding unit 10 42 is coupled with a corresponding lower flange 68 of a feeding column 40 provided with a feeding hopper 70 at an upper portion thereof. In the example shown, a feeding door mechanism 72 provided with a hand-held actuating arm 74 allows an operator to dump raw materials previously discharged in the hopper into feeding cavity 48. Ra.dially 15 extending from the surface of the forward shaft portion 58 are a plurality of mixing blades 75 each having a tip portion maintained in substantially close proximity to the inner surface of the double wall 34. Located in a lower portion of the peripheral double wall 34 is a discharge opening 76 delimited by a peripheral sealing edge surface adapted to tightly mate 20 with the corresponding inner surface of a displaceable door 78. Door 78 is rigidly secured to an outer end of a pivoting arm 77 having an inner end rigidly attached to a clamping sleeve 79 receiving an output shaft 80 of a rotary actuator 81 mounted on the sub-frame assembly 21 and being driven through a pneumatic cylinder 84 coupled to a linear-to-rotary 25 converting mechanism of a known construction (not shown). Using set screws 80a, the output shaft 80 is caused to rigidly engage the clamping sleeve, to selectively displace the door away from a discharge opening 76 to provide discharge of mixed material out of the mixing chamber upon rotation of the shaft in a first direction, or to displace the door 30 toward discharge opening 76 and maintain door 78 against it in an opposite direction to tightly obstruct the opening 76 during the feeding and mixing steps. To cover the discharge area there is provided a chute 82, which comprises front and rear wall 85, 86 as better shown in Fig. 2 and side walls 88, 90 as better shown in Fig. 1, which walls define a 35 discharge outlet for dumping a mixed batch to be transferred to a forming station.
Fig. 1 is a perspective view of a high intensity batch mixer used to practice the 10 process according to the present invention;
Fig. 2 is a partially cross-sectional perspective view of a front end of the batch mixer shown in Fig.l; and Fig. 3 is a graph showing the variation of a mixer motor load current measured as a function of time, and related thresholds used to 15 control a process according to the present invention.
Referring now to the drawings, a high intensity mixer 10 which could be used to carry out the process according to the present invention is depicted, which mixer 10 comprises a base frame 12 including a pair of longitudinal beams 14 secured to upper ends of front and rear pairs of 20 floor mounted pillars 16 rigidly secured by transverse members 18 and bracing plates 20. On the rear portion of the beams 14 is secured a motor base 22 having a mounting plate 24 on which is secured lower parts of legs 26 supporting an electric industrial motor 28, preferably of a self cooling type. As shown in Fig. 2, motor 28 is provided with an output 25 shaft 30 connected to a driving end of a flexible coupling 13 of known construction, which has a driven end connected to a driving shaft 15 extending through a cantilever bearing unit 17 permanently lubricated with a pumped oil circuit (not shown). The flexible coupling is covered fox protection with a casing 19 (Fig. 1) provided with an aperture 21 30 giving required clearance for the main driving shaft 15. The cantilever bearing unit 17 is rigidly mounted through rear and front supports 29 (only rear support being shown in Fig. 2) on an horizontal plate 19 as part of a sub-frame assembly 21 secured to the front portions of the beams 14, and having a vertical mounting plate 23 further secured to the 35 horizontal plate 19 through a pair of opposed bracing plates 27.
As shown in Fig. 2, apparatus 10 further comprises a cylindrical mixing chamber 32 having outer double peripheral wall 34 and provided with cooling fluid ports 35 (Fig. 1) to be connected to a cooling circuit line (not shown} as will be later explained in more detail. Wall 34 is 5 further provided with and optional temperature probe 37. Mixing chamber 32 further has a circular double end wall 36 defining a mixing cavity 38. Mixing chamber 32 is secured to the body of a feeding unit 42 having an outer double peripheral wall 39 provided with cooling fluid ports 41 as better shown in Fig. l, and an input tubular portion 44 in 10 communication with an output annular portion 46 defining a feeding cavity 48 therebetween, as better shown in Fig. 2. The inner edge of peripheral double wall 34 of the mixing chamber 32 defines an annular channel adapted to receive an annular rib protruding from the outer surface of a first collar 52, which is then rigidly welded or otherwise 15 secured to the double wall 34. The inner surface of first collar 52 is in turn joined to the outer mating surface of a second collar 54. Collars 52 and 54 are rigidly bolted together. Output annular portion 46 of the feeding unit 42 tightly engages with an inner opening formed in collar 54, to form an annular inner end wall opposed to circular end wall 36.
20 Input tubular portion 44 defines with the inner rear surface of collar 54 an internal space 33 in fluid communication through a fluid line (not shown) with internal space 31 within double walls 34 and 36, to form a cooling cavity as part of the cooling fluid circuit filled with a cooling fluid such as cold water, for limiting the temperature of the feeding 25 cavity and mixing chamber to a level providing desired process continuity.
Centrally extending through the output annular portion 46 is a two-part driven shaft 56 having a forward bladed portion 58 contained in the mixing chamber 32 and being opposed to a rearward threaded 30 portion 60 contained in the feeding cavity 48 and acting as a conveyor screw. The cantilever bearing unit 17 provides axial and radial stability for shaft 56 while allowing rotation thereof about axis 66. Rearward shaft portion 60 is rigidly secured to the driven end of the driving shaft 15 using a key screw (not shown}, to impart rotation to the rearward 35 shaft portion 60. The outer end of forward shaft portion 58 is formed with a threaded hole 62 for receiving an aligned bolt 64 securing the forward shaft portion 58 to the driven end of the driving shaft 15, to impart rotation to the forward shaft portion 58. An optional aeration port 65 is provided at the outer surface of double end wall 36.
Alternatively, instead of using a cantilever arrangement, port 65 may be 5 replaced by a bearing for receiving a rotating rod (not shown) to be secured to the outer end of the forward shaft portion 58. The outer diameter of threads 66 provided on the driven shaft 56 is chosen to closely fit within output annular portion 46, mixing cavity 38 thereby becoming substantially enclosed. Input tubular portion 44 of feeding unit 10 42 is coupled with a corresponding lower flange 68 of a feeding column 40 provided with a feeding hopper 70 at an upper portion thereof. In the example shown, a feeding door mechanism 72 provided with a hand-held actuating arm 74 allows an operator to dump raw materials previously discharged in the hopper into feeding cavity 48. Ra.dially 15 extending from the surface of the forward shaft portion 58 are a plurality of mixing blades 75 each having a tip portion maintained in substantially close proximity to the inner surface of the double wall 34. Located in a lower portion of the peripheral double wall 34 is a discharge opening 76 delimited by a peripheral sealing edge surface adapted to tightly mate 20 with the corresponding inner surface of a displaceable door 78. Door 78 is rigidly secured to an outer end of a pivoting arm 77 having an inner end rigidly attached to a clamping sleeve 79 receiving an output shaft 80 of a rotary actuator 81 mounted on the sub-frame assembly 21 and being driven through a pneumatic cylinder 84 coupled to a linear-to-rotary 25 converting mechanism of a known construction (not shown). Using set screws 80a, the output shaft 80 is caused to rigidly engage the clamping sleeve, to selectively displace the door away from a discharge opening 76 to provide discharge of mixed material out of the mixing chamber upon rotation of the shaft in a first direction, or to displace the door 30 toward discharge opening 76 and maintain door 78 against it in an opposite direction to tightly obstruct the opening 76 during the feeding and mixing steps. To cover the discharge area there is provided a chute 82, which comprises front and rear wall 85, 86 as better shown in Fig. 2 and side walls 88, 90 as better shown in Fig. 1, which walls define a 35 discharge outlet for dumping a mixed batch to be transferred to a forming station.
Apparatus 10 further comprises a control device such as parogrammable logic controller (PLC) 92 which receives from line 98 a current load indicating signal generated by an electrical current measuring device such as ammeter 96 as part of the motor drive unit 94, 5 or located at a remote location, to derive the estimated temperature of the mix, as will be explained later in more detail. Alternatively, the PLC
may receive via line 102 and optional temperature probe 3 7, a signal representing the temperature directly measured within mixing cavity 38.
Due to the generally short time cycle of the process, the temperature 10 within the batch of material being mixed could be significantly different from the temperature of walls 34 or 36 of mixing chamber 32.
Therefore, a remote temperature sensor should preferably be used, such as optical infrared sensor as disclosed in U.S. Patent No. 4,332,479 issued June l, 1882, to Crocker et al. PLC 92 also sends to motor drive 15 unit 94 through line 100, a command signal to control the rotation of motor 28 according to a preset RPM value. The motor drive unit 94 incorporates a feedback device to substantially maintain the preset RPM, whatever the load current variation may be. PLC 92 sends a command signal to pneumatic cylinder 84 via line 97 according to a selected 20 predetermined program stored in the PLC, as will be discussed later in more detail. It should be understood that discharge can also be manually operated a through manual control mode available on the PLC. Lines 106 and 108 are used to send control signals to a lubricating oil pump for bearing unit 17 and a valve (not shown) which controls the cooling 25 circuit. Optionally, the hand-held arm 74 of the feeding door mechanism 72 can be replaced by a rotary actuator which can be coupled to the feeding door mechanism and activated through the PLC via line 104.
The principles underlying the process according to the present invention will now be explained with reference to the operation of the 30 apparatus described above with respect to Figs. l and 2, and also in conjunction with Fig. 3. Mixing and heating of the raw material present in mixing cavity 38 of mixing chamber 32 are simultaneously achieved as a result of the high speed of blades 75 obtained by rotation of shaft 56. Under centrifugal forces resulting from the rotation of the blades, 35 particles of material are violently projected against the inner surface of the peripheral wall 34 and the shaft or against one another, such friction converting kinetic energy into thermal energy resulting in material temperature increase at a fast rate toward a target maximum temperature, typically within 30 to 60 seconds for a target temperature above 180°C, without any need for further extraneous heat source. The rotation speed 5 in RPM of shaft 56 is preset to a value ensuring that sufficient mixing and friction energy is provided to the mix, in a short processing time while still providing the stability required for efficient process control.
The composition homogeneity which is required to obtain uniform physical properties is also obtained. Such results can be obtained when 10 the blade tip speed is above about 17 meter/sec, and preferably between about 25 and 30 meter/sec. Experience has shown that with blade tip speeds above 35 meter/sec, a fast temperature rising rate observed may render the process difficult to control. Since the blade tip speed is directly related to the RPM value as a tangential speed at the 15 corresponding radius, the RPM as a standard parameter, is preferably chosen as a reference control parameter for the process. To substantially maintain a preset RPM, electrical power or energy required will depend on the inherent properties of the formulation such as volume of the batch, density and viscosity of the material, as well as characteristics of 20 the mixer such as mixing cavity radial section and volume, design of shaft 56 and configurations of blades 75, torque requirement without load, etc. While the latter characteristics can be considered as substantially constant, the parameters characterizing properties of the material to be mixed such as density and viscosity vary during the 25 mixing process, altering load current or energy required to maintain a preset RPM.
Referring now to Figs. 2 and 3, the process control according to a preferred embodiment of the present invention will be explained through a series of examples, wherein a load current measurement to monitor 30 the temperature of the batch material under mixing is used.
Example 1 Referring to Fig. 3, curve 101 which is shown, represents the variation of load current (in amp) shown on vertical reference axis 102, and as a function of time (in sec.) on horizontal reference axis 104, 35 measured during mixing of a 1 kg batch of material, from the initial material feeding step to a final state where the 3 liter mixing chamber 32 of the high intensity mixer 10 is empty after discharge of the mixed batch. In this example, 63% by weight of vulcanized (cured) rubber crumb of either natural or synthetic type were previously pre-mixed with 32% of a thermoplastic polymer resin, selected from polyethylenes 5 (from low to high density) or ethyl-vinyl acetates, optionally with 5 by weight of an additive such as acrylic acid. The rubber crumbs were selected to pass through a 8 mesh sieve in the instant example.
However, depending on the raw rubber crumb grain size and desired composition quality, any sieve size between 8 to 60 mesh, and 10 preferably between about 20 to 30 mesh may be used. Depending on the desired mechanical properties for the formed material, experience has shown that from about 40% to about 90% by weight of cured rubber crumbs may be added to from about 60 to about 10 % by weight of thermoplastic resin. Before feeding the raw material into feeding cavity 15 48 upon activation of feeding door mechanism 72, the load current drawn by motor 28 running idle at a preset speed of about 3200 RPM
was measured to be about 15 amp. For the composition of this example, the rotation speed of shaft 56 may be typically set from about 2800 to about 3600 RPM, which limit values correspond to a blade tip speed 20 from about 22 to 29 meterls, respectively. Once the material is introduced, friction of the material carried along the path of feed thread 66 upon rotation of shaft 56, creates a counter-torque producing an initial increase of the load current which rises to a preset feeding value of about 19 amp in the example shown, which roughly corresponds to an 25 effective introduction of the material into mixing cavity 38.
Conveniently, the timing of the process was chosen to begin as the measured load current reaches, associated with an initial temperature for the input material which generally corresponds to ambient storage temperature. Thereafter, the intensity of the load current increases 30 according to a first substantially linear gradient until the whole batch of material has been introduced within the mixing cavity 38, which corresponds to a substantially flat intermediate curve part showing an average load current value of about 35 amp in the example shown. That temporary load current stability is associated with a constant mixing 35 behavior exhibited by the batch material as the temperature is rising toward a first transition temperature where the material enters into a viscous state progressively adding to counter-torque, requiring further increase of the load current above to maintain the RPM at the preset level of 3200. The increase in viscosity is associated with a melting of the thermoplastic resin which encapsulates the rubber crumbs which 5 remain in a solid state at that temperature range. In the example shown, the transition temperature was obtained in about 9 sec. Then, the load current rises according to a second substantially linear gradient, passing through a minimum value the purpose of which will be explained later, to substantially stabilize at a maximum level of about 56 amp in about 10 15 sec for the example shown, which maximum corresponds to a second transition temperature where the mixed material gradually enters into a fluidized state requiring less energy to abe mixed. Thereafter, the load current begins to drop accordingly, while the temperature of the fluidized matter still increases, until the desired batch temperature is 15 considered to have been reached, corresponding to a predetermined discharge load current, which parameter can be derived in various ways.
A first way consists in causing PLC 92 to open discharge door 78 for a preset time following the moment where the load current reaches through a numerical analysis method programmed in PLC 92. It should 20 be understood that can be set at zero. The preset value for can be chosen experimentally by a direct measurement of the temperature of the discharge material using successive test values for. In the example shown in Fig. 3, was given a value of 2 sec. An alternate way would consist in programming PLC 92 to open the discharge door 78 for a 25 preset time following the moment where the load current reaches, both current values being experimentally set while ensuring that the derived has a value equal to or under. In the example shown in Fig. 3, was given a value of 8 sec, to correspond to a target discharge temperature for the mixed matter, of about 170°C. For the composition of this example, a 30 target temperature within a range from about 160°C to about 190°C
ensures the production of a substantially uniform mix of cured rubber material in a matrix of resinous material to produce a rubber-based composition which could be later formed into an article. A third way would consist in causing PLC 92 to open discharge door 78 for a preset 35 time following the start of the mixing, which corresponds to. In the example shown in Fig. 3, was given a value of 19 sec. It should be understood that any combination of the foregoing conditions for discharge control can be used alternatively, whichever is met first. It should also be understood that any other practical way using any other appropriate temperature-related parameter can be used to control batch 5 discharge after mixing. Optionally, the material discharge may be caused to occurs in case where the load current as measured reaches a predetermined critical value, indicating a possible malfunction of the apparatus. As mentioned before, the mixed matter discharge can also be under the control of the operator using manual functions available on 10 PLC 92, based on manual timing carried out after the introduction of the material into feeding cavity 48. If the process control is based on direct temperature measurement through temperature probe 37 as shown in Fig. 1 rather than being indirectly based on load current measurement, PLC 92 can be programmed to monitor a temperature signal coming 15 from probe 37, and to command activation of discharge door 78 whenever a target discharge temperature is measured. The discharged material which was in a viscous state was then ready to be transferred to a shaping station to be shaped into an article. For a rubber-thermoplastic composition used in the example described with reference to Fig. 3, a 20 conventional cold-molding press on which is mounted a two-part mold was used to form the article, the latter being allowed to cool into the mold under pressure until mold removal temperature was attained.
Example 2 In this example, from about 90% and 99% by weight of cured 25 rubber crumbs of either natur al or synthetic type were previously pre mixed with from about 10% to 1% of a curing agent such as sulfur, which is characterized by a minimum curing temperature of about 110°C, and then introduced into 3 liter mixing chamber 32 of high intensity mixer 10. The rubber crumbs were selected to pass through a 8 30 mesh sieve in the instant example. For the composition of this example, the rotation speed of shaft 56 may be set from about 2200 to about 3600 RPM, which limit values correspond to a blade tip speed from about 17 to 29 meters, respectively. PLC 92 was programmed to monitor the temperature as previously explained, to command activation of discharge 35 door 78 whenever a target discharge temperature was considered to have been reached, corresponding to a temperature for the mixed matter selected within a range from about 115°C to about 140°C, ensuring the production of a substantially uniform mix of cured rubber with the curing agent without causing significant further curing to produce a rubber-based composition which could be later heat-shaped into an 5 article.
Typically, the mixing cycle is completed within about 30 sec. The discharged composition in the form of a mass of hot particles was then ready to be transferred to a shaping station to be shaped into an article, the mold being pre-heated to a molding temperature substantially above 10 a minimum curing temperature. The batch of heat-moldable composition is maintained within the pre-heated mold for a sufficient period of time to allow further curing of the composition to produce the shaped article. For the rubber of the present example, a conventional hot-molding press on which is mounted a two-part mold pre-heated to a 15 temperature from about 140°C or about 200°C was be used to shape the article, the latter being allowed to further cure under heat into the mold under pressure and then allowed to chill until mold removal temperature was attained. Pre-heating of the composirion in the mixing stage followed by molding at a temperature well above minimum curing 20 temperature has been found more energetically effective than known processes using one-step heating while shaping. Typically, curing is completed within about 60 min., which is more than twice faster than the curing time required by known one-step heating shaping processes.
The humidity which remained in the molded batch was sufficiently 25 reduced during mixing to ensure safe removal from the mold.
Example 3 In this example, from about 40% to 90% by weight of cured rubber crumbs of either natural or synthetic type were previously pre-mixed with from about 0.1% to about 5% of a bonding agent, such as 30 acrylic acid, Primacor 3460 (Dow Chemicals) a silane or a titanate, and are first introduced into 3 liter mixing chamber 32 of high intensity mixer 10. T'he rubber crumbs were selected to pass through a 20 mesh sieve. In a first step, the rotation speed of shaft 56 was maintained for about 30 sec to a value of about 3000 RPM corresponding to a blade tip 35 speed of about 24 meters, to cause a substantially uniform distribution of the bonding agent through the rubber particles to form a coating.
may receive via line 102 and optional temperature probe 3 7, a signal representing the temperature directly measured within mixing cavity 38.
Due to the generally short time cycle of the process, the temperature 10 within the batch of material being mixed could be significantly different from the temperature of walls 34 or 36 of mixing chamber 32.
Therefore, a remote temperature sensor should preferably be used, such as optical infrared sensor as disclosed in U.S. Patent No. 4,332,479 issued June l, 1882, to Crocker et al. PLC 92 also sends to motor drive 15 unit 94 through line 100, a command signal to control the rotation of motor 28 according to a preset RPM value. The motor drive unit 94 incorporates a feedback device to substantially maintain the preset RPM, whatever the load current variation may be. PLC 92 sends a command signal to pneumatic cylinder 84 via line 97 according to a selected 20 predetermined program stored in the PLC, as will be discussed later in more detail. It should be understood that discharge can also be manually operated a through manual control mode available on the PLC. Lines 106 and 108 are used to send control signals to a lubricating oil pump for bearing unit 17 and a valve (not shown) which controls the cooling 25 circuit. Optionally, the hand-held arm 74 of the feeding door mechanism 72 can be replaced by a rotary actuator which can be coupled to the feeding door mechanism and activated through the PLC via line 104.
The principles underlying the process according to the present invention will now be explained with reference to the operation of the 30 apparatus described above with respect to Figs. l and 2, and also in conjunction with Fig. 3. Mixing and heating of the raw material present in mixing cavity 38 of mixing chamber 32 are simultaneously achieved as a result of the high speed of blades 75 obtained by rotation of shaft 56. Under centrifugal forces resulting from the rotation of the blades, 35 particles of material are violently projected against the inner surface of the peripheral wall 34 and the shaft or against one another, such friction converting kinetic energy into thermal energy resulting in material temperature increase at a fast rate toward a target maximum temperature, typically within 30 to 60 seconds for a target temperature above 180°C, without any need for further extraneous heat source. The rotation speed 5 in RPM of shaft 56 is preset to a value ensuring that sufficient mixing and friction energy is provided to the mix, in a short processing time while still providing the stability required for efficient process control.
The composition homogeneity which is required to obtain uniform physical properties is also obtained. Such results can be obtained when 10 the blade tip speed is above about 17 meter/sec, and preferably between about 25 and 30 meter/sec. Experience has shown that with blade tip speeds above 35 meter/sec, a fast temperature rising rate observed may render the process difficult to control. Since the blade tip speed is directly related to the RPM value as a tangential speed at the 15 corresponding radius, the RPM as a standard parameter, is preferably chosen as a reference control parameter for the process. To substantially maintain a preset RPM, electrical power or energy required will depend on the inherent properties of the formulation such as volume of the batch, density and viscosity of the material, as well as characteristics of 20 the mixer such as mixing cavity radial section and volume, design of shaft 56 and configurations of blades 75, torque requirement without load, etc. While the latter characteristics can be considered as substantially constant, the parameters characterizing properties of the material to be mixed such as density and viscosity vary during the 25 mixing process, altering load current or energy required to maintain a preset RPM.
Referring now to Figs. 2 and 3, the process control according to a preferred embodiment of the present invention will be explained through a series of examples, wherein a load current measurement to monitor 30 the temperature of the batch material under mixing is used.
Example 1 Referring to Fig. 3, curve 101 which is shown, represents the variation of load current (in amp) shown on vertical reference axis 102, and as a function of time (in sec.) on horizontal reference axis 104, 35 measured during mixing of a 1 kg batch of material, from the initial material feeding step to a final state where the 3 liter mixing chamber 32 of the high intensity mixer 10 is empty after discharge of the mixed batch. In this example, 63% by weight of vulcanized (cured) rubber crumb of either natural or synthetic type were previously pre-mixed with 32% of a thermoplastic polymer resin, selected from polyethylenes 5 (from low to high density) or ethyl-vinyl acetates, optionally with 5 by weight of an additive such as acrylic acid. The rubber crumbs were selected to pass through a 8 mesh sieve in the instant example.
However, depending on the raw rubber crumb grain size and desired composition quality, any sieve size between 8 to 60 mesh, and 10 preferably between about 20 to 30 mesh may be used. Depending on the desired mechanical properties for the formed material, experience has shown that from about 40% to about 90% by weight of cured rubber crumbs may be added to from about 60 to about 10 % by weight of thermoplastic resin. Before feeding the raw material into feeding cavity 15 48 upon activation of feeding door mechanism 72, the load current drawn by motor 28 running idle at a preset speed of about 3200 RPM
was measured to be about 15 amp. For the composition of this example, the rotation speed of shaft 56 may be typically set from about 2800 to about 3600 RPM, which limit values correspond to a blade tip speed 20 from about 22 to 29 meterls, respectively. Once the material is introduced, friction of the material carried along the path of feed thread 66 upon rotation of shaft 56, creates a counter-torque producing an initial increase of the load current which rises to a preset feeding value of about 19 amp in the example shown, which roughly corresponds to an 25 effective introduction of the material into mixing cavity 38.
Conveniently, the timing of the process was chosen to begin as the measured load current reaches, associated with an initial temperature for the input material which generally corresponds to ambient storage temperature. Thereafter, the intensity of the load current increases 30 according to a first substantially linear gradient until the whole batch of material has been introduced within the mixing cavity 38, which corresponds to a substantially flat intermediate curve part showing an average load current value of about 35 amp in the example shown. That temporary load current stability is associated with a constant mixing 35 behavior exhibited by the batch material as the temperature is rising toward a first transition temperature where the material enters into a viscous state progressively adding to counter-torque, requiring further increase of the load current above to maintain the RPM at the preset level of 3200. The increase in viscosity is associated with a melting of the thermoplastic resin which encapsulates the rubber crumbs which 5 remain in a solid state at that temperature range. In the example shown, the transition temperature was obtained in about 9 sec. Then, the load current rises according to a second substantially linear gradient, passing through a minimum value the purpose of which will be explained later, to substantially stabilize at a maximum level of about 56 amp in about 10 15 sec for the example shown, which maximum corresponds to a second transition temperature where the mixed material gradually enters into a fluidized state requiring less energy to abe mixed. Thereafter, the load current begins to drop accordingly, while the temperature of the fluidized matter still increases, until the desired batch temperature is 15 considered to have been reached, corresponding to a predetermined discharge load current, which parameter can be derived in various ways.
A first way consists in causing PLC 92 to open discharge door 78 for a preset time following the moment where the load current reaches through a numerical analysis method programmed in PLC 92. It should 20 be understood that can be set at zero. The preset value for can be chosen experimentally by a direct measurement of the temperature of the discharge material using successive test values for. In the example shown in Fig. 3, was given a value of 2 sec. An alternate way would consist in programming PLC 92 to open the discharge door 78 for a 25 preset time following the moment where the load current reaches, both current values being experimentally set while ensuring that the derived has a value equal to or under. In the example shown in Fig. 3, was given a value of 8 sec, to correspond to a target discharge temperature for the mixed matter, of about 170°C. For the composition of this example, a 30 target temperature within a range from about 160°C to about 190°C
ensures the production of a substantially uniform mix of cured rubber material in a matrix of resinous material to produce a rubber-based composition which could be later formed into an article. A third way would consist in causing PLC 92 to open discharge door 78 for a preset 35 time following the start of the mixing, which corresponds to. In the example shown in Fig. 3, was given a value of 19 sec. It should be understood that any combination of the foregoing conditions for discharge control can be used alternatively, whichever is met first. It should also be understood that any other practical way using any other appropriate temperature-related parameter can be used to control batch 5 discharge after mixing. Optionally, the material discharge may be caused to occurs in case where the load current as measured reaches a predetermined critical value, indicating a possible malfunction of the apparatus. As mentioned before, the mixed matter discharge can also be under the control of the operator using manual functions available on 10 PLC 92, based on manual timing carried out after the introduction of the material into feeding cavity 48. If the process control is based on direct temperature measurement through temperature probe 37 as shown in Fig. 1 rather than being indirectly based on load current measurement, PLC 92 can be programmed to monitor a temperature signal coming 15 from probe 37, and to command activation of discharge door 78 whenever a target discharge temperature is measured. The discharged material which was in a viscous state was then ready to be transferred to a shaping station to be shaped into an article. For a rubber-thermoplastic composition used in the example described with reference to Fig. 3, a 20 conventional cold-molding press on which is mounted a two-part mold was used to form the article, the latter being allowed to cool into the mold under pressure until mold removal temperature was attained.
Example 2 In this example, from about 90% and 99% by weight of cured 25 rubber crumbs of either natur al or synthetic type were previously pre mixed with from about 10% to 1% of a curing agent such as sulfur, which is characterized by a minimum curing temperature of about 110°C, and then introduced into 3 liter mixing chamber 32 of high intensity mixer 10. The rubber crumbs were selected to pass through a 8 30 mesh sieve in the instant example. For the composition of this example, the rotation speed of shaft 56 may be set from about 2200 to about 3600 RPM, which limit values correspond to a blade tip speed from about 17 to 29 meters, respectively. PLC 92 was programmed to monitor the temperature as previously explained, to command activation of discharge 35 door 78 whenever a target discharge temperature was considered to have been reached, corresponding to a temperature for the mixed matter selected within a range from about 115°C to about 140°C, ensuring the production of a substantially uniform mix of cured rubber with the curing agent without causing significant further curing to produce a rubber-based composition which could be later heat-shaped into an 5 article.
Typically, the mixing cycle is completed within about 30 sec. The discharged composition in the form of a mass of hot particles was then ready to be transferred to a shaping station to be shaped into an article, the mold being pre-heated to a molding temperature substantially above 10 a minimum curing temperature. The batch of heat-moldable composition is maintained within the pre-heated mold for a sufficient period of time to allow further curing of the composition to produce the shaped article. For the rubber of the present example, a conventional hot-molding press on which is mounted a two-part mold pre-heated to a 15 temperature from about 140°C or about 200°C was be used to shape the article, the latter being allowed to further cure under heat into the mold under pressure and then allowed to chill until mold removal temperature was attained. Pre-heating of the composirion in the mixing stage followed by molding at a temperature well above minimum curing 20 temperature has been found more energetically effective than known processes using one-step heating while shaping. Typically, curing is completed within about 60 min., which is more than twice faster than the curing time required by known one-step heating shaping processes.
The humidity which remained in the molded batch was sufficiently 25 reduced during mixing to ensure safe removal from the mold.
Example 3 In this example, from about 40% to 90% by weight of cured rubber crumbs of either natural or synthetic type were previously pre-mixed with from about 0.1% to about 5% of a bonding agent, such as 30 acrylic acid, Primacor 3460 (Dow Chemicals) a silane or a titanate, and are first introduced into 3 liter mixing chamber 32 of high intensity mixer 10. T'he rubber crumbs were selected to pass through a 20 mesh sieve. In a first step, the rotation speed of shaft 56 was maintained for about 30 sec to a value of about 3000 RPM corresponding to a blade tip 35 speed of about 24 meters, to cause a substantially uniform distribution of the bonding agent through the rubber particles to form a coating.
During that step, the temperature of the mix did not significantly raise.
In a second step, a thermoplastic polymer resin selected from polyethylene (from low to high density) or ethyl-vinyl-acetates, from about 60 to about 10 % by weight, was introduced into the mix, while 5 shaft 56 was rotated at a speed set from about 2800 to about 3600 RPM, which correspond to a blade tip speed from about 22 to 29 meters, respectively. PLC 92 was programmed to monitor the temperature as previously explained, to command activation of discharge door 78 whenever a target discharge temperature was considered to have been 10 reached, corresponding to a temperature for the mixed matter from about 160°C to about 190°C to yield a ready to shape matter exhibiting improved mechanical properties due to the bound rubber-thermoplastic matter as compared to material wholly made of cured rubber crumbs.
The discharged material in a viscous state was then ready to be 15 transferred to a shaping station to be formed into an article, using a cold molding press as explained before in conjunction with example 1.
Example 4 In this example, from about 20% to 99% by weight of cured rubber crumbs of either natural or synthetic type were previously pre 20 mixed with from about 10% to 1% of a curing agent such as sulfur, with from about 80% to 1% of a low molecular weight polymeric binder which reacts with the curing agent, such as traps-polyoctenamer (supplied by Huls AG) with from about 40% to 1% of natural or synthetic uncured rubber such as a styrene-butadiene. Other polymeric 25 binder such as styrene-1,4-butadiene, a copolymer of 1,4-butadiene and acrylonitrile or 1,2-polybutadiene may also be used. Known activators such as zinc oxide or stearic acid, and a curing accelerator such as tetramethyl thiuran disulfide (TMTD) or benzothiazyldisulfide (MBTS) were added to control curing of the uncured rubber. This pre-mix was 30 then introduced into 3 liter mixing chamber 32 of the high intensity mixer 10. The rubber crumbs were selected to pass through a 20 mesh sieve. For the composition of the present example, the rotation speed of shaft 56 may be set from about 2200 to about 3600 RPM, which correspond to a blade tip speed from about 17 to 29 meters, 35 respectively. PLC 92 can be programmed to monitor the temperature as previously explained, to command activation of discharge door 78 whenever a target discharge temperature was considered to have been reached, corresponding to a temperature for the mixed material from about 115°C to about 140°C, at which temperature fw-ther curing is substantially prevented, thereby producing a rubber-based composition 5 which can be later heat-shaped into an article. The discharged composition in the form of a mass of hot particles was then ready to be transferred to a shaping station to be shaped into an article, in the same manner as explained in conjunction with Example 2.
10 It is to be understood that any variant of the preferred embodiments described above should be considered within the ambit of the present invention, provided it falls within the scope of the appended claims.
In a second step, a thermoplastic polymer resin selected from polyethylene (from low to high density) or ethyl-vinyl-acetates, from about 60 to about 10 % by weight, was introduced into the mix, while 5 shaft 56 was rotated at a speed set from about 2800 to about 3600 RPM, which correspond to a blade tip speed from about 22 to 29 meters, respectively. PLC 92 was programmed to monitor the temperature as previously explained, to command activation of discharge door 78 whenever a target discharge temperature was considered to have been 10 reached, corresponding to a temperature for the mixed matter from about 160°C to about 190°C to yield a ready to shape matter exhibiting improved mechanical properties due to the bound rubber-thermoplastic matter as compared to material wholly made of cured rubber crumbs.
The discharged material in a viscous state was then ready to be 15 transferred to a shaping station to be formed into an article, using a cold molding press as explained before in conjunction with example 1.
Example 4 In this example, from about 20% to 99% by weight of cured rubber crumbs of either natural or synthetic type were previously pre 20 mixed with from about 10% to 1% of a curing agent such as sulfur, with from about 80% to 1% of a low molecular weight polymeric binder which reacts with the curing agent, such as traps-polyoctenamer (supplied by Huls AG) with from about 40% to 1% of natural or synthetic uncured rubber such as a styrene-butadiene. Other polymeric 25 binder such as styrene-1,4-butadiene, a copolymer of 1,4-butadiene and acrylonitrile or 1,2-polybutadiene may also be used. Known activators such as zinc oxide or stearic acid, and a curing accelerator such as tetramethyl thiuran disulfide (TMTD) or benzothiazyldisulfide (MBTS) were added to control curing of the uncured rubber. This pre-mix was 30 then introduced into 3 liter mixing chamber 32 of the high intensity mixer 10. The rubber crumbs were selected to pass through a 20 mesh sieve. For the composition of the present example, the rotation speed of shaft 56 may be set from about 2200 to about 3600 RPM, which correspond to a blade tip speed from about 17 to 29 meters, 35 respectively. PLC 92 can be programmed to monitor the temperature as previously explained, to command activation of discharge door 78 whenever a target discharge temperature was considered to have been reached, corresponding to a temperature for the mixed material from about 115°C to about 140°C, at which temperature fw-ther curing is substantially prevented, thereby producing a rubber-based composition 5 which can be later heat-shaped into an article. The discharged composition in the form of a mass of hot particles was then ready to be transferred to a shaping station to be shaped into an article, in the same manner as explained in conjunction with Example 2.
10 It is to be understood that any variant of the preferred embodiments described above should be considered within the ambit of the present invention, provided it falls within the scope of the appended claims.
Claims (20)
1. Process for producing a batch of rubber-based composition capable of being formed into an article, comprising the steps of:
feeding a batch of mixable material comprising from about 40 %
to about 90% by weight of particles of cured rubber material with from about 60 % to about 10 % by weight of a resinous material into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s under conditions effective to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said rubber material in a matrix of said resinous material to produce said rubber-based composition.
feeding a batch of mixable material comprising from about 40 %
to about 90% by weight of particles of cured rubber material with from about 60 % to about 10 % by weight of a resinous material into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s under conditions effective to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said rubber material in a matrix of said resinous material to produce said rubber-based composition.
2. Process according to claim 1, wherein the blade tip speed is from about 25 meters to about 30 meters.
3. Process for producing a shaped article made from a rubber-based material comprising the steps of:
feeding a batch of mixable material comprising from about 40 %
to about 90% by weight of particles of cured rubber material with from about 60 % to about 10 % by weight of a resinous material into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s under conditions effective under conditions effective to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said rubber material in a matrix of said resinous material to produce a rubber-based composition; and shaping the discharged batch of rubber-based composition to produce said shaped article.
feeding a batch of mixable material comprising from about 40 %
to about 90% by weight of particles of cured rubber material with from about 60 % to about 10 % by weight of a resinous material into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s under conditions effective under conditions effective to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said rubber material in a matrix of said resinous material to produce a rubber-based composition; and shaping the discharged batch of rubber-based composition to produce said shaped article.
4. Process according to claim 3, wherein the blade tip speed is from about 25 meter/s to about 30 meter/s.
5. Process for producing a batch of rubber-based composition capable of being heat-formed into an article, comprising the steps of:
feeding a batch of mixable material comprising from about 90%
to about 99% by weight of particles of cured rubber material with from about 10% to about 1% by weight of a curing agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said cured rubber material with said curing agent without causing significant further curing to produce said rubber-based composition.
feeding a batch of mixable material comprising from about 90%
to about 99% by weight of particles of cured rubber material with from about 10% to about 1% by weight of a curing agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said cured rubber material with said curing agent without causing significant further curing to produce said rubber-based composition.
6. Process according to claim 5, wherein the blade tip speed is from about 25 meter/s to about 30 meter/s.
7. Process according to claim 5, wherein said batch of mixable material further comprises from about 40% to about 1% by weight of a polymeric binder which is reactive with the curing agent.
8. Process according to claim 7, wherein said polymeric binder is a low molecular weight polymeric binder.
9. Process according to claim 7, wherein said batch of mixable material further comprises from about 40% to about 1% by weight of virgin rubber.
10. Process according to claim 7, wherein said batch of mixable material further comprises at least one of a curing starting agent and a curing accelerator.
11. Process for producing a molded article made of a rubber-based material comprising the steps of:
feeding a batch of mixable material comprising from about 90 %
to about 99 % by weight of particles of cured rubber material with from about 10% to about 1% by weight of a curing agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said cured rubber material with said curing agent without causing significant further curing to produce a rubber-based composition capable of being shaped; and molding the discharged batch of rubber-based composition at a molding temperature substantially above a minimum curing temperature for a sufficient period of time to allow further curing of the rubber-based composition to produce said molded article.
feeding a batch of mixable material comprising from about 90 %
to about 99 % by weight of particles of cured rubber material with from about 10% to about 1% by weight of a curing agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed of from about 17 meter/s to about 35 meter/s to intensively mix and thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of said cured rubber material with said curing agent without causing significant further curing to produce a rubber-based composition capable of being shaped; and molding the discharged batch of rubber-based composition at a molding temperature substantially above a minimum curing temperature for a sufficient period of time to allow further curing of the rubber-based composition to produce said molded article.
12. Process according to claim 11, wherein the blade tip speed is from about 25 meter/s to about 30 meter/s.
13. Process according to claim 11, wherein said batch of mixable material further comprises from about 40% to about 1% by weight of a polymeric binder which is reactive with said curing agent.
14. Process according to claim 13, wherein said polymeric binder is a low molecular weight polymeric binder.
15. Process according to claim 13, wherein said batch of mixable material further comprises from about 80% to about 1% by weight of virgin rubber.
16. Process according to claim 13, wherein said batch of mixable material further comprises at least one of a curing starting agent and a curing accelerator.
17. Process for producing a batch of rubber-based composition capable of being shaped into an article, comprising the steps of:
feeding from about 40 % to about 90 % by weight of particles of cured rubber with from about 0.1 % to about 5 % by weight of a bonding agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed from about 17 meter/s to about 35 meter/s for a sufficient period of time to substantially uniformly distribute the bonding agent onto the cured rubber particles to form a coating;
feeding from about 60 % to about 10 % by weight of a resinous material into the closed mixing chamber to form a batch of mixable material;
rotating the shaft to provide a blade tip speed above about 17 meter/s under conditions effective to intensively mix the resinous material with the cured rubber particles coated with the bonding agent and to thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of the coated particles bound to a matrix of said resinous material to produce said rubber-based composition.
feeding from about 40 % to about 90 % by weight of particles of cured rubber with from about 0.1 % to about 5 % by weight of a bonding agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed from about 17 meter/s to about 35 meter/s for a sufficient period of time to substantially uniformly distribute the bonding agent onto the cured rubber particles to form a coating;
feeding from about 60 % to about 10 % by weight of a resinous material into the closed mixing chamber to form a batch of mixable material;
rotating the shaft to provide a blade tip speed above about 17 meter/s under conditions effective to intensively mix the resinous material with the cured rubber particles coated with the bonding agent and to thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of the coated particles bound to a matrix of said resinous material to produce said rubber-based composition.
18. Process according to claim 17, wherein the blade tip speed is from about 25 meter/s to about 30 meter/s.
19. Process for producing a shaped article made of a rubber-based material comprising the steps of:
feeding from about 40 % to about 90 % by weight of particles of cured rubber material with from about 0.1 % to about 5 % by weight of a cross linking agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed from about 17 meter/s to about 35 meter/s for a sufficient period of time to substantially uniformly distribute the cross linking agent into the cured rubber particles to form a coating thereon;
feeding from about 60 % to about 10 % by weight of a resinous material into the closed mixing chamber to form a batch of mixable material;
rotating the shaft to provide a blade tip speed above about 17 meter/s under conditions effective to intensively mix the resinous material with the cured rubber particles which are coated with the cross linking agent and to thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of the cross-linking agent coated particles in a matrix of said resinous material to produce a rubber-based composition capable of being shaped; and shaping the discharged batch of rubber-based composition to produce said shaped article.
feeding from about 40 % to about 90 % by weight of particles of cured rubber material with from about 0.1 % to about 5 % by weight of a cross linking agent into a closed mixing chamber provided on a high intensity mixer including a central shaft having mixing blades;
rotating the shaft to provide a blade tip speed from about 17 meter/s to about 35 meter/s for a sufficient period of time to substantially uniformly distribute the cross linking agent into the cured rubber particles to form a coating thereon;
feeding from about 60 % to about 10 % by weight of a resinous material into the closed mixing chamber to form a batch of mixable material;
rotating the shaft to provide a blade tip speed above about 17 meter/s under conditions effective to intensively mix the resinous material with the cured rubber particles which are coated with the cross linking agent and to thermokinetically heat the batch of mixable material;
continuously monitoring one of temperature and temperature related parameter of the batch;
discharging the batch from the mixing chamber when said one of temperature and temperature related parameter reaches a reference value ensuring a substantially uniform mix of the cross-linking agent coated particles in a matrix of said resinous material to produce a rubber-based composition capable of being shaped; and shaping the discharged batch of rubber-based composition to produce said shaped article.
20. A process according to claim 19, wherein the blade tip speed is from about 25 meter/s to about 30 meter/s.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA 2245330 CA2245330A1 (en) | 1998-08-19 | 1998-08-19 | Process for producing batches of rubber-based composition |
| US09/149,859 US6224796B1 (en) | 1998-08-19 | 1998-09-09 | Process for producing batches of rubber-based composition |
| PCT/CA1999/000696 WO2001008862A1 (en) | 1998-08-19 | 1999-07-29 | Process for producing batches of rubber-based composition |
| AU51427/99A AU5142799A (en) | 1998-08-19 | 1999-07-29 | Process for producing batches of rubber-based composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA 2245330 CA2245330A1 (en) | 1998-08-19 | 1998-08-19 | Process for producing batches of rubber-based composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2245330A1 true CA2245330A1 (en) | 2000-02-19 |
Family
ID=29409769
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA 2245330 Withdrawn CA2245330A1 (en) | 1998-08-19 | 1998-08-19 | Process for producing batches of rubber-based composition |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA2245330A1 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110815622A (en) * | 2019-11-15 | 2020-02-21 | 黄志贤 | Mixer for plastic processing |
| CN112123613A (en) * | 2020-09-10 | 2020-12-25 | 衡阳市衡山科学城科技创新服务有限公司 | Production equipment for negative template structured ultrathin heat management material |
| CN112123826A (en) * | 2020-09-08 | 2020-12-25 | 浙江中天能橡胶股份有限公司 | Manufacturing method of high-performance conveying belt |
| CN112428471A (en) * | 2020-10-30 | 2021-03-02 | 福建永荣锦江股份有限公司 | Spinning plastic particle blending and metering system |
| CN112590044A (en) * | 2020-12-07 | 2021-04-02 | 高宾 | Button shaping machine capable of preventing colloid from solidifying |
-
1998
- 1998-08-19 CA CA 2245330 patent/CA2245330A1/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110815622A (en) * | 2019-11-15 | 2020-02-21 | 黄志贤 | Mixer for plastic processing |
| CN112123826A (en) * | 2020-09-08 | 2020-12-25 | 浙江中天能橡胶股份有限公司 | Manufacturing method of high-performance conveying belt |
| CN112123613A (en) * | 2020-09-10 | 2020-12-25 | 衡阳市衡山科学城科技创新服务有限公司 | Production equipment for negative template structured ultrathin heat management material |
| CN112428471A (en) * | 2020-10-30 | 2021-03-02 | 福建永荣锦江股份有限公司 | Spinning plastic particle blending and metering system |
| CN112590044A (en) * | 2020-12-07 | 2021-04-02 | 高宾 | Button shaping machine capable of preventing colloid from solidifying |
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