EP1715989A1 - Process and plant for dehumidification, heating and injection moulding of granulated plastics materials - Google Patents

Process and plant for dehumidification, heating and injection moulding of granulated plastics materials

Info

Publication number
EP1715989A1
EP1715989A1 EP04804179A EP04804179A EP1715989A1 EP 1715989 A1 EP1715989 A1 EP 1715989A1 EP 04804179 A EP04804179 A EP 04804179A EP 04804179 A EP04804179 A EP 04804179A EP 1715989 A1 EP1715989 A1 EP 1715989A1
Authority
EP
European Patent Office
Prior art keywords
dehumidification
granules
temperature
moulding
injection
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP04804179A
Other languages
German (de)
French (fr)
Inventor
Rinaldo Piva
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Plastic Systems SpA
Original Assignee
Plastic Systems SpA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Plastic Systems SpA filed Critical Plastic Systems SpA
Publication of EP1715989A1 publication Critical patent/EP1715989A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • B29B13/00—Conditioning or physical treatment of the material to be shaped
    • B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
    • B29B13/065—Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
    • 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
    • B29B13/00—Conditioning or physical treatment of the material to be shaped
    • B29B13/02—Conditioning or physical treatment of the material to be shaped by heating
    • B29B13/021—Heat treatment of powders
    • 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
    • B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58—Component parts, details or accessories; Auxiliary operations
    • B29B7/60—Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
    • 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
    • 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
    • B29B9/00—Making granules
    • B29B9/16—Auxiliary treatment of granules
    • 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
    • B29C31/00—Handling, e.g. feeding of the material to be shaped, storage of plastics material before moulding; Automation, i.e. automated handling lines in plastics processing plants, e.g. using manipulators or robots
    • B29C31/02—Dispensing from vessels, e.g. hoppers
    • 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
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17—Component parts, details or accessories; Auxiliary operations
    • B29C45/18—Feeding the material into the injection moulding apparatus, i.e. feeding the non-plastified material into the injection unit
    • 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
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/285—Feeding the extrusion material to the extruder
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/12—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
    • F26B17/14—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas
    • F26B17/1408—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the gas being supplied and optionally extracted through ducts extending into the moving stack of material
    • F26B17/1425—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the gas being supplied and optionally extracted through ducts extending into the moving stack of material the ducts being perforated and arranged vertically
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/06—Controlling, e.g. regulating, parameters of gas supply
    • F26B21/08—Humidity
    • F26B21/083—Humidity by using sorbent or hygroscopic materials, e.g. chemical substances, molecular sieves
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00—Heating arrangements
    • F26B23/001—Heating arrangements using waste heat
    • F26B23/002—Heating arrangements using waste heat recovered from dryer exhaust gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • 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
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C2045/0096—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor drying the moulding material before injection, e.g. by heating
    • 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
    • B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
    • 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
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/022—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • 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
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • 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
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/285—Feeding the extrusion material to the extruder
    • B29C48/286—Raw material dosing
    • 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
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/285—Feeding the extrusion material to the extruder
    • B29C48/295—Feeding the extrusion material to the extruder in gaseous form
    • 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
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/78—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/80—Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
    • 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
    • B29K2067/00—Use of polyesters or derivatives thereof, 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
    • B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
    • B29K2067/006—PBT, i.e. polybutylene terephthalate
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
    • F26B2200/08—Granular materials

Definitions

  • the present invention relates to a process of dehumidification and of injection and moulding for granulated plastics materials according to the characteristics set forth in the preamble to independent Claim 1.
  • the invention is also directed towards a plant arranged to operate in accordance with the process, according to the preamble to independent Claim 10.
  • Technological background In the field of methods for the processing of granulated plastics materials by injection and moulding, it is known that the granules have to reach the injection and moulding press with a moisture level which is as low as possible (or in any case is controlled in dependence on the type of final product to be produced). For this purpose, the granules are normally subjected to a dehumidification step immediately upstream of the injection and moulding step.
  • the step of dehumidification of the granules is carried out in a hopper by stripping of the moisture contained in the granules with air which is caused to flow as a counter-current.
  • the air admitted to the hopper has an extremely low moisture content and a relatively high temperature.
  • the need is known to maintain the temperature as high as possible, not only in view of possible improvements in terms of the drying of the granules but also in view of a reduction in the cycle times of the injection and moulding press which is typically disposed immediately downstream of the dehumidification step.
  • this apparatus in fact, before the granules are injected into the mould, they have to be brought to the melting point of the polymer in a suitable heating chamber, requiring a certain amount of time which forms part of the overall cycle time of the press.
  • the increase in temperature within the dehumidification step is limited, however, by the fact that high temperature promotes undesired oxidative degradation reactions of the polymer, compromising the final quality of the product.
  • a range of temperature values which is normally used as an optimal compromise between the requirements set out above is between 180°C and 190°C.
  • the PET granules are supplied to the injection and moulding apparatus which brings them to a temperature of about 280°C - 290°C, ready to be injected into the mould.
  • the problem underlying the present invention is that of providing a process of dehumidification and of injection and moulding for granulated plastics materials, as well as a plant arranged to operate in accordance with the process, which are designed structurally and functionally to respond to the requirements set out above, overcoming the limitations of the prior art mentioned.
  • This problem is solved by the present invention by means of a process of dehumidification and of injection and moulding, as well as a plant operating in accordance with the process, according to the appended claims.
  • the plant 1 is intended for the dehumidification of polyethylene terephthalate (PET) granules and comprises, as a whole, a dehumidification unit la for dehumidifying the granules, and an injection and moulding unit lb disposed downstream of the dehumidification unit la.
  • the dehumidification unit la in turn comprises a hopper 2, a granule-loading system 3 for loading the granules into the hopper 2, as well as a circuit 4 for the admission and treatment of the process air for removing moisture from the granules inside the hopper 2.
  • the hopper 2 is loaded with granules from above by means of the loading system 3 which comprises a suction line 5 for the pneumatic transportation of the granules.
  • the suction line 5 opens at a first end in a granule storage tank 6 and is connected to a cyclone 7, which is disposed at the top of the hopper 2 and in which the granules are separated from the transportation air and are allowed to fall into the hopper, and then to a vacuum pump 8.
  • the granules come into contact with process air which is admitted from the bottom 2a of the hopper 2 as a counter- current relative to the granules, at a dehumidification temperature.
  • the process-air admission and treatment circuit 4 comprises a dehumidifier 10, for example, of the type with molecular sieves, which is connected downstream to a heater 11 and then to a line 12 for admitting the air to the hopper 2.
  • the circuit 4 is completed by a line 13 for recovering the process air from the hopper; the line 13 connects the top of the hopper 2 to a pair of filters 14 and then to a heat recovery unit 15 and finally to the dehumidifier 10.
  • the operation of the dehumidifier 10 is controlled by a control unit 16.
  • the above-mentioned components are dimensioned and controlled in accordance with procedures known in the technical field in question and will not therefore be described in greater detail.
  • the bottom 2a of the hopper 2 is connected downstream to the injection and moulding unit lb which comprises, for example, an injection and moulding press arranged for the manufacture of PET-based articles or semi-finished products.
  • the injection and moulding press in turn comprises a heating chamber for bringing the granules to a moulding temperature which, in the case of PET, is between 280°C and 290°C, and a mould into which the molten plastics material is admitted.
  • granule- heating means are interposed between the dehumidification unit la and the injection and moulding unit lb.
  • the granule-heating means 20 comprise a hopper 21 and a circuit
  • the hopper 21 is connected at its top to the bottom of the hopper 2 by means of a duct 23 and at its bottom to the injection and moulding unit lb by means of a duct 24 and is preferably provided with stirring means 21b for keeping the granules inside it in motion.
  • the circuit 22 comprises gas-movement means, for example, a blower 25 which is connected by means of a line 26 to a heater 27, preferably of an electric type, and to the bottom 21a of the hopper 21, where the gas is put in contact with the granules, flowing as a counter- current relative thereto, towards the top of the hopper 21. From there, the gas is led back to the blower 25 by means of the return line 28, after passing through a filter 29.
  • the gas used in the circuit 22 is a substantially oxygen-free gas, that term being intended to indicate generally a presence of less than about 5% of oxygen.
  • the gas is preferably technical nitrogen and can be introduced into the circuit 22, for example for operations for the replenishment thereof, by means of a coupling 30 provided in the line 26.
  • the granule-heating means 20 further comprise a control unit 35 which is arranged for the control and overall management of that step of the process, as described in greater detail in the following paragraphs.
  • the process according to the present invention comprises a first step for the dehumidification of the granules with process air.
  • the granules are loaded into the hopper 2 at the top thereof by means of the loading system 3 and the process air is admitted from the bottom 2a as a counter-current, at a temperature such that the granules inside the hopper are at a dehumidification temperature of between 180°C and 190°C.
  • the process air output from the hopper 2 preheats the process air output from the dehumidifier 10 in the heat recovery unit 15 and is sent to the dehumidifier 10 in order to be treated in the molecular sieves thereof.
  • the process air has a very low moisture level with a dew point typically of between -50°C and -60 O C.
  • the process air is admitted to the hopper 2, it is then preheated in the heat recovery unit 15 and is brought to the final temperature by the heater 11.
  • the granules are then supplied, by falling through the duct 23, into the hopper 21 where they are heated by contact with the gas admitted through the circuit 22 to a supply temperature between the dehumidification temperature and the moulding temperature.
  • the granules are preferably brought to a supply temperature of between 200°C and 250°C, even more preferably between 220°C and 230°C. It should be noted that the granules are heated to a supply temperature lower than the softening point of the granules which, for PET, is of the order of 270°C, so as not to create problems when they pass from the hopper 21 to the injection and moulding press due to sticking of the granules. In any case, the mixing to which the granules are subjected by virtue of the action of the stirring means 21b is such as to prevent the establishment of local hot spots which could lead to the above-mentioned sticking problems.
  • the granule-heating means 20 are of dimensions such that the granules remain in the hopper 21 for sufficient time to reach the supply temperature indicated above. Granules are thus supplied to the injection and moulding unit at a higher temperature and the unit thus requires less time to bring them to the moulding temperature.
  • the heating step thus promotes the process of the plasticization of the granules within the injection and moulding press, also leading to less thermal degradation of the PET and a lower energy consumption for the operation of the press.
  • the gas is preferably technical nitrogen. It is found that undesired degradation reactions of the PET are thus not triggered, in spite of the high temperature reached. Although the use of technical nitrogen remains the greatly preferred option, the gas may be constituted by air with a low oxygen content.
  • the gas may even result from the use, in closed circuit for a suitable period of time, of process air drawn from the circuit 4 (variant shown in Figure 1 by means of the discontinuous connecting line 31). If the process air is recirculated continuously in the hopper 21, the fraction of oxygen therein will in fact reduce over time because of oxidative reactions with the plastics material present therein until it reaches the percentages indicated above which enable further possible degradation reactions to be prevented. Naturally, during this recirculation stage in which the oxygen fraction is still high, a lower temperature of the gas will have to be maintained unless a generally lower quality of the granules output from the hopper 21 is acceptable.
  • the present invention thus solves the problem discussed above with reference to the prior art mentioned, at the same time offering many further advantages, amongst which is an increase in the productivity of the dehumidification and injection and moulding plants without compromising the quality of the final product.
  • Another advantage is that operation in an environment that is substantially free of oxygen also minimizes degradative reactions which might lead to the undesired formation of aldehydes, particularly formaldehyde and acetaldehyde which, with their strong and pungent odours, can adversely affect the flavour of any beverage contained in bottles produced from the granules of plastics material.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • Sustainable Development (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Robotics (AREA)
  • Manufacturing & Machinery (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

A process of dehumidification and of injection and moulding for granulated plastics materials comprises a dehumidification step (1a) in which the granules are dehumidified by contact with air at a dehumidification temperature, and a subsequent injection and moulding step (1b) in which the granules coming from the dehumidification step are heated to a moulding temperature higher than the dehumidification temperature and are then injected into a mould. Between the dehumidification step and the injection and moulding step, a heating lo step (20) is provided, in which the granules are heated, in a substantial absence of oxygen, to a supply temperature between the dehumidification temperature and the moulding temperature. A plant (1) operating in accordance with the process is also described.

Description

PROCESS AND PLANT FOR DEHUMIDIFICATION, HEATING AND INJECTION MOULDING OF GRANULATED PLATSTICS MATERIALS
Description Technical field The present invention relates to a process of dehumidification and of injection and moulding for granulated plastics materials according to the characteristics set forth in the preamble to independent Claim 1. The invention is also directed towards a plant arranged to operate in accordance with the process, according to the preamble to independent Claim 10. Technological background In the field of methods for the processing of granulated plastics materials by injection and moulding, it is known that the granules have to reach the injection and moulding press with a moisture level which is as low as possible (or in any case is controlled in dependence on the type of final product to be produced). For this purpose, the granules are normally subjected to a dehumidification step immediately upstream of the injection and moulding step. This requirement is particularly necessary for plastics materials which have a high hygroscopic capacity such as, for example, polyethylene terephthalate (PET), to the processing of which the present invention is preferably but not exclusively applied. In known processes, the step of dehumidification of the granules is carried out in a hopper by stripping of the moisture contained in the granules with air which is caused to flow as a counter-current. To promote the dehumidification process, the air admitted to the hopper (process air) has an extremely low moisture content and a relatively high temperature. With regard to this latter characteristic, the need is known to maintain the temperature as high as possible, not only in view of possible improvements in terms of the drying of the granules but also in view of a reduction in the cycle times of the injection and moulding press which is typically disposed immediately downstream of the dehumidification step. In this apparatus, in fact, before the granules are injected into the mould, they have to be brought to the melting point of the polymer in a suitable heating chamber, requiring a certain amount of time which forms part of the overall cycle time of the press. The increase in temperature within the dehumidification step is limited, however, by the fact that high temperature promotes undesired oxidative degradation reactions of the polymer, compromising the final quality of the product. It is therefore necessary to carry out the dehumidification process at a temperature adapted to the conflicting requirements for quick and effective drying of the granules and for maintenance of the qualitative integrity of the polymer. A range of temperature values which is normally used as an optimal compromise between the requirements set out above is between 180°C and 190°C. At these temperatures, the PET granules are supplied to the injection and moulding apparatus which brings them to a temperature of about 280°C - 290°C, ready to be injected into the mould.
Description of the invention The problem underlying the present invention is that of providing a process of dehumidification and of injection and moulding for granulated plastics materials, as well as a plant arranged to operate in accordance with the process, which are designed structurally and functionally to respond to the requirements set out above, overcoming the limitations of the prior art mentioned. This problem is solved by the present invention by means of a process of dehumidification and of injection and moulding, as well as a plant operating in accordance with the process, according to the appended claims. Brief description of the drawings The characteristics and the advantages of the invention will become clearer from the detailed description of a preferred embodiment thereof which is described by way of non-limiting example with reference to the appended drawing in which the sole Figure 1 is a schematic view of a plant for the dehumidification and the injection and moulding of granulated plastics materials, arranged to operate in accordance with the process of the present invention. In the appended drawing, a plant for the dehumidification of granulated plastics materials and for the injection and moulding thereof, formed in accordance with the present invention, is generally indicated 1. In the preferred embodiment described herein, the plant 1 is intended for the dehumidification of polyethylene terephthalate (PET) granules and comprises, as a whole, a dehumidification unit la for dehumidifying the granules, and an injection and moulding unit lb disposed downstream of the dehumidification unit la. The dehumidification unit la in turn comprises a hopper 2, a granule-loading system 3 for loading the granules into the hopper 2, as well as a circuit 4 for the admission and treatment of the process air for removing moisture from the granules inside the hopper 2. The hopper 2 is loaded with granules from above by means of the loading system 3 which comprises a suction line 5 for the pneumatic transportation of the granules. The suction line 5 opens at a first end in a granule storage tank 6 and is connected to a cyclone 7, which is disposed at the top of the hopper 2 and in which the granules are separated from the transportation air and are allowed to fall into the hopper, and then to a vacuum pump 8. Inside the hopper 2, the granules come into contact with process air which is admitted from the bottom 2a of the hopper 2 as a counter- current relative to the granules, at a dehumidification temperature. The process-air admission and treatment circuit 4 comprises a dehumidifier 10, for example, of the type with molecular sieves, which is connected downstream to a heater 11 and then to a line 12 for admitting the air to the hopper 2. The circuit 4 is completed by a line 13 for recovering the process air from the hopper; the line 13 connects the top of the hopper 2 to a pair of filters 14 and then to a heat recovery unit 15 and finally to the dehumidifier 10. The operation of the dehumidifier 10 is controlled by a control unit 16. The above-mentioned components are dimensioned and controlled in accordance with procedures known in the technical field in question and will not therefore be described in greater detail. The bottom 2a of the hopper 2 is connected downstream to the injection and moulding unit lb which comprises, for example, an injection and moulding press arranged for the manufacture of PET-based articles or semi-finished products. The injection and moulding press in turn comprises a heating chamber for bringing the granules to a moulding temperature which, in the case of PET, is between 280°C and 290°C, and a mould into which the molten plastics material is admitted. These presses are also known in the technical field in question and a detailed description thereof will therefore be omitted. According to a principal characteristic of the invention, granule- heating means, generally indicated 20, are interposed between the dehumidification unit la and the injection and moulding unit lb. The granule-heating means 20 comprise a hopper 21 and a circuit
22 for the heating and admission of a hot gas into the hopper 21 in order to heat the granules contained therein to a supply temperature for supply to the injection and moulding unit. The hopper 21 is connected at its top to the bottom of the hopper 2 by means of a duct 23 and at its bottom to the injection and moulding unit lb by means of a duct 24 and is preferably provided with stirring means 21b for keeping the granules inside it in motion. The circuit 22 comprises gas-movement means, for example, a blower 25 which is connected by means of a line 26 to a heater 27, preferably of an electric type, and to the bottom 21a of the hopper 21, where the gas is put in contact with the granules, flowing as a counter- current relative thereto, towards the top of the hopper 21. From there, the gas is led back to the blower 25 by means of the return line 28, after passing through a filter 29. The gas used in the circuit 22 is a substantially oxygen-free gas, that term being intended to indicate generally a presence of less than about 5% of oxygen. The gas is preferably technical nitrogen and can be introduced into the circuit 22, for example for operations for the replenishment thereof, by means of a coupling 30 provided in the line 26. The granule-heating means 20 further comprise a control unit 35 which is arranged for the control and overall management of that step of the process, as described in greater detail in the following paragraphs. The process according to the present invention comprises a first step for the dehumidification of the granules with process air. The granules are loaded into the hopper 2 at the top thereof by means of the loading system 3 and the process air is admitted from the bottom 2a as a counter-current, at a temperature such that the granules inside the hopper are at a dehumidification temperature of between 180°C and 190°C. The process air output from the hopper 2 preheats the process air output from the dehumidifier 10 in the heat recovery unit 15 and is sent to the dehumidifier 10 in order to be treated in the molecular sieves thereof. At the output from the dehumidifier 10, the process air has a very low moisture level with a dew point typically of between -50°C and -60OC. Before the process air is admitted to the hopper 2, it is then preheated in the heat recovery unit 15 and is brought to the final temperature by the heater 11. The granules are then supplied, by falling through the duct 23, into the hopper 21 where they are heated by contact with the gas admitted through the circuit 22 to a supply temperature between the dehumidification temperature and the moulding temperature. The granules are preferably brought to a supply temperature of between 200°C and 250°C, even more preferably between 220°C and 230°C. It should be noted that the granules are heated to a supply temperature lower than the softening point of the granules which, for PET, is of the order of 270°C, so as not to create problems when they pass from the hopper 21 to the injection and moulding press due to sticking of the granules. In any case, the mixing to which the granules are subjected by virtue of the action of the stirring means 21b is such as to prevent the establishment of local hot spots which could lead to the above-mentioned sticking problems. The granule-heating means 20 are of dimensions such that the granules remain in the hopper 21 for sufficient time to reach the supply temperature indicated above. Granules are thus supplied to the injection and moulding unit at a higher temperature and the unit thus requires less time to bring them to the moulding temperature. The heating step thus promotes the process of the plasticization of the granules within the injection and moulding press, also leading to less thermal degradation of the PET and a lower energy consumption for the operation of the press. As stated above, the gas is preferably technical nitrogen. It is found that undesired degradation reactions of the PET are thus not triggered, in spite of the high temperature reached. Although the use of technical nitrogen remains the greatly preferred option, the gas may be constituted by air with a low oxygen content. The gas may even result from the use, in closed circuit for a suitable period of time, of process air drawn from the circuit 4 (variant shown in Figure 1 by means of the discontinuous connecting line 31). If the process air is recirculated continuously in the hopper 21, the fraction of oxygen therein will in fact reduce over time because of oxidative reactions with the plastics material present therein until it reaches the percentages indicated above which enable further possible degradation reactions to be prevented. Naturally, during this recirculation stage in which the oxygen fraction is still high, a lower temperature of the gas will have to be maintained unless a generally lower quality of the granules output from the hopper 21 is acceptable. The present invention thus solves the problem discussed above with reference to the prior art mentioned, at the same time offering many further advantages, amongst which is an increase in the productivity of the dehumidification and injection and moulding plants without compromising the quality of the final product. Another advantage is that operation in an environment that is substantially free of oxygen also minimizes degradative reactions which might lead to the undesired formation of aldehydes, particularly formaldehyde and acetaldehyde which, with their strong and pungent odours, can adversely affect the flavour of any beverage contained in bottles produced from the granules of plastics material.

Claims

CLAIMS 1. A process of dehumidification and of injection and moulding for granulated plastics materials, comprising a dehumidification step (la) in which the granules are dehumidified by contact with air at a dehumidification temperature, and a subsequent injection and moulding step (lb) in which the granules coming from the dehumidification step are heated to a moulding temperature higher than the dehumidification temperature and are then injected into a mould, characterized in that, between the dehumidification step and the injection and moulding step, a heating step (20) is provided, in which the granules are heated, in a substantial absence of oxygen, to a supply temperature between the dehumidification temperature and the moulding temperature. 2. A method according to Claim 1 in which, in the heating step (20), the granules are heated by contact with a substantially oxygen- free inert gas. 3. A method according to . Claim 2 in which the inert gas is technical nitrogen. 4. A method according to Claim 1 or Claim 2 in which the gas is oxygen-impoverished air obtained by means of a step of recirculation of the air in closed circuit at high temperature, in which the air is put in contact with the granules. 5. A method according to Claim 4 in which the air is derived from the air which is used in the step for the dehumidification of the granules. 6. A method according to one or more of the preceding claims in which the supply temperature is lower than the softening point of the granules. 7. A method according to one or more of the preceding claims in which the plastics material is based on polyethylene terephthalate. 8. A method according to Claim 7 in which the supply temperature is between 200°C and 250°C. 9. A method according to Claim 8 in which the supply temperature is between 220°C and 230°C. 10. A plant (1) for the dehumidification and the injection and moulding of granulated plastics materials, comprising a unit (la) for dehumidifying the granules by means of process air, in which the granules are heated to a dehumidification temperature, and a unit (lb) for injecting and moulding the granules coming from the dehumidification unit, in which the granules are brought to a moulding temperature higher than the dehumidification temperature, characterized in that, between the dehumidification unit and the injection and moulding unit, granule-heating means (20) are provided for heating the granules in a substantial absence of oxygen, to a supply temperature between the dehumidification temperature and the moulding temperature. 11. A plant according to Claim 10 in which the granule-heating means (20) comprise a hopper (21) and a circuit (22) for the heating and admission of a hot inert gas into the hopper (21) in order to heat the granules contained therein to the supply temperature. 12. A plant according to Claim 11 in which a connection (31) is provided between a circuit (4) of the process air used in the unit (la) for dehumidifying the granules and the circuit (22) for heating and admitting the gas to the hopper (21). 13. A plant according to Claim 11 or Claim 12 in which the hot inert gas is admitted to the hopper (21) as a counter-current relative to the granules.
EP04804179A 2004-02-16 2004-12-22 Process and plant for dehumidification, heating and injection moulding of granulated plastics materials Withdrawn EP1715989A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT000037A ITPD20040037A1 (en) 2004-02-16 2004-02-16 DEHUMIDIFICATION AND INJECTION AND MOLDING PROCESS OF PLASTIC MATERIALS IN GRANULES AND PLANT PREPARED TO OPERATE ACCORDING TO SUCH PROCESS
PCT/EP2004/014583 WO2005077628A1 (en) 2004-02-16 2004-12-22 Process and plant for dehumidification, heating and injection moulding of granulated plastics materials

Publications (1)

Publication Number Publication Date
EP1715989A1 true EP1715989A1 (en) 2006-11-02

Family

ID=34856949

Family Applications (1)

Application Number Title Priority Date Filing Date
EP04804179A Withdrawn EP1715989A1 (en) 2004-02-16 2004-12-22 Process and plant for dehumidification, heating and injection moulding of granulated plastics materials

Country Status (4)

Country Link
EP (1) EP1715989A1 (en)
CA (1) CA2555611A1 (en)
IT (1) ITPD20040037A1 (en)
WO (1) WO2005077628A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022111514A1 (en) * 2020-11-27 2022-06-02 湖南连心科技有限公司 Environment-friendly powder paint extrusion device

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1393078B1 (en) * 2009-01-26 2012-04-11 Plastodidattica Commerciale S R L METHOD FOR THE PRODUCTION OF PRESENTATION LENSES.
JP2012180999A (en) * 2011-03-03 2012-09-20 Kawata Mfg Co Ltd Drying system and drying method
JP6076820B2 (en) * 2013-04-24 2017-02-08 株式会社カワタ Powder and particle metering device
IT201800011013A1 (en) * 2018-12-12 2020-06-12 Pegaso Ind S P A Processing process of polymeric granular material and plant operating according to this process
CN110631328A (en) * 2019-10-15 2019-12-31 昆山森驰机械设备有限公司 Dehumidifying dryer
CN110893661B (en) * 2019-12-27 2020-07-17 江苏惠利隆塑业集团有限公司 Processing apparatus of injection moulding raw materials
IT202000007147A1 (en) * 2020-04-03 2021-10-03 Piovan Spa Apparatus and Method of Treatment of Inconsistent Material
CN218504963U (en) * 2022-07-05 2023-02-21 摩丹智能制造(太仓)有限公司 Integrated intelligent drying device with plastic particle mixing and drying functions

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1226101A (en) * 1958-12-20 1960-07-08 Inventa Ag Method and apparatus for drying granular polyamides
JPS5949881B2 (en) * 1978-01-31 1984-12-05 ユニチカ株式会社 Continuous countercurrent drying method for synthetic resin chips
JPS62201204A (en) * 1986-03-01 1987-09-04 Konishiroku Photo Ind Co Ltd Manufacture of thermoplastic resin sheet and device thereof
DE4314345A1 (en) * 1993-04-30 1994-11-17 Reinhard Dr Unger Process and apparatus for the recycling of solid polyester material
DE19957664A1 (en) * 1999-11-30 2001-05-31 Basf Ag Device for drying granulates, especially polyamide-6, has granulate inlet at top and outlet at bottom, inert gas inlet and outlet in opposite walls and perforated metal partitions across these walls to slow down and distribute gas

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2005077628A1 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022111514A1 (en) * 2020-11-27 2022-06-02 湖南连心科技有限公司 Environment-friendly powder paint extrusion device

Also Published As

Publication number Publication date
WO2005077628A1 (en) 2005-08-25
CA2555611A1 (en) 2005-08-25
ITPD20040037A1 (en) 2004-05-16

Similar Documents

Publication Publication Date Title
JP3718470B2 (en) Method and apparatus for recycling PET material
EP1156914B1 (en) Process for upgrading plastic material
KR101298818B1 (en) Method and device for increasing the limiting viscosity of polyester materials by solid phase polycondensation
JP2895235B2 (en) Method of operating a dryer for powdered and granular, bulkable materials and dryers operating according to this method
RU2556929C2 (en) Method of increasing molecular weight using residual heat of granular polyester
EP1715989A1 (en) Process and plant for dehumidification, heating and injection moulding of granulated plastics materials
US8877107B2 (en) Method for increasing the molecular weight of a polyester granulate by using its residual heat
US20230166428A1 (en) Process for deodorization of recycled polyolefin pellets
US20230158713A1 (en) Process for drying granular polymeric material and plant operating according to said process
EP1922195B1 (en) Apparatus and process for drying plastic material for a machine used to produce plastic containers
US11241665B2 (en) Method for producing a plastic granulate
EP1316770A2 (en) Method and apparatus for drying plastics
EP1133384B1 (en) Method and installation for making a preform, using improved drying means
US11203133B2 (en) Method and apparatus for polymer drying using inert gas
KR20050095081A (en) Method of manufacturing recycle synthetic resin pellet adopting hot cutting and plant therefor
US20070130791A1 (en) Dehumidification process for granulated plastic materials and a plant operating in accordance with the process
CN114986743A (en) Continuous drying method and processing method for plastic particles
JP2023013988A (en) Method for reprocessing plastic waste, in particular pet waste, and reprocessing system
CA2766364A1 (en) Method and device for providing a raw material for the production of pet containers

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20060808

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU MC NL PL PT RO SE SI SK TR

DAX Request for extension of the european patent (deleted)
17Q First examination report despatched

Effective date: 20070904

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20080115