WO1999058005A1 - Methods and apparatus for applying coating material - Google Patents

Methods and apparatus for applying coating material Download PDF

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Publication number
WO1999058005A1
WO1999058005A1 PCT/GB1999/001524 GB9901524W WO9958005A1 WO 1999058005 A1 WO1999058005 A1 WO 1999058005A1 GB 9901524 W GB9901524 W GB 9901524W WO 9958005 A1 WO9958005 A1 WO 9958005A1
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WO
WIPO (PCT)
Prior art keywords
coating
coating material
batches
batch
product
Prior art date
Application number
PCT/GB1999/001524
Other languages
French (fr)
Inventor
Kim Brent Jan David
Original Assignee
Rospen Industries Limited
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 Rospen Industries Limited filed Critical Rospen Industries Limited
Priority to AU39412/99A priority Critical patent/AU3941299A/en
Publication of WO1999058005A1 publication Critical patent/WO1999058005A1/en

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Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23PSHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P20/00Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
    • A23P20/10Coating with edible coatings, e.g. with oils or fats
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23PSHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P20/00Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
    • A23P20/10Coating with edible coatings, e.g. with oils or fats
    • A23P20/12Apparatus or processes for applying powders or particles to foodstuffs, e.g. for breading; Such apparatus combined with means for pre-moistening or battering
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23PSHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P20/00Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
    • A23P20/10Coating with edible coatings, e.g. with oils or fats
    • A23P20/15Apparatus or processes for coating with liquid or semi-liquid products
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01GWEIGHING
    • G01G11/00Apparatus for weighing a continuous stream of material during flow; Conveyor belt weighers
    • G01G11/08Apparatus for weighing a continuous stream of material during flow; Conveyor belt weighers having means for controlling the rate of feed or discharge
    • G01G11/086Apparatus for weighing a continuous stream of material during flow; Conveyor belt weighers having means for controlling the rate of feed or discharge of the loss-in-weight feeding type

Definitions

  • the present invention relates to materials handling and treatment apparatus .
  • a preferred application of the invention is to application of flavouring compositions to foods, particularly particulate foods or snack foods e.g. potato crisps
  • flavouring composition may be salt, or other more complex flavouring compounds. Whatever flavouring is to be used, there is a need to control the amount of flavouring composition which is applied to ensure that the strength of flavour on the finished product is within acceptable limits .
  • potato crisps are made in large batches.
  • the batches are each weighed, and then tumbled in a processing drum with an amount of flavouring composition appropriate to the weight of the batch.
  • the intention is that tumbling will cause the flavouring composition to be coated evenly onto the crisps .
  • the coated crisps are weighed into small batches and packaged as a product for sale.
  • flavouring composition there is a tendency for some of the flavouring composition to fall from the crisps before they are packaged. This results in wastage, because an extra quantity of flavouring composition must be added to the processing drum to 2 compensate for this loss . This also causes a variation in the flavour of the final product. Also, apparatus which processes the crisps following coating will become contaminated with the flavouring composition. This is particularly problematic when the flavouring composition is to be changed because such apparatus must be thoroughly cleaned to avoid contamination of the new flavouring composition with the old.
  • the coating material such as a powdered flavouring to batched product such as a snackfood consisting of loose, discrete articles, which is to be packaged.
  • the coating material is presented as charges of controlled size by dividing a uniform feed, e.g. from a weigher by means of a rotary valve.
  • An injector or other suitable applicator applies the charges of coating material successively to respective batches of product, in-line downstream of the batch formation apparatus which is e.g. a multihead or linear weigher, and directly upstream of or at packaging apparatus such as a bagging machine. This minimises contamination by the coating material.
  • a control unit may synchronise the applications with the production of the batches and control the coating material supply.
  • material handling and processing apparatus for multiple articles comprising batch formation apparatus for receiving articles in bulk and for producing relatively smaller batches of articles, a coating apparatus for applying a coating material to articles, and a packaging apparatus for packaging a batch of articles into a discrete package; the apparatus being arranged such that the coating apparatus operates on individual batches of articles produced by the batch formation apparatus, before packaging of the batch by the packaging apparatus .
  • This arrangement of apparatus ensures that the batch formation apparatus cannot become contaminated by the coating material. This is of particular advantage because the batch formation apparatus is commonly a component which presents particular difficulties when cleaning is required.
  • Articles processed by apparatus embodying the invention may be discrete articles such as potato crisps or other snack foods. Alternatively, it can be used to process articles in the form of particulate, granular or powdered material in applications where there is a requirement to coat a product with a coating composition.
  • the batch formation apparatus may operate on the basis of generating batches of constant weight or of constant volume.
  • apparatus as described in UK Patent Specification No. 2127158 may be used.
  • a loss-in-weight feeder, a batch weigher or a multi-head weigher could alternatively to provide batches of known weight . It will be recognised by those skilled in the art that many other types of weight-based or volumetric batch production apparatus could be used, as appropriate for the particular application of the apparatus .
  • the invention may use batch or charge formation apparatus comprising a continuous feeder for generating a flow of material from a reservoir at a constant weight or a constant volume per unit time, a diverter for generating a batch by diverting that flow to an output for a predetermined time, and a recovery system for returning to the reservoir any material not diverted to the output .
  • This apparatus has the advantage of being able to produce a batch of material of known weight or volume, as the case may be, on demand. No difficulty is encountered in the event that a demand for batches of material temporarily ceases .
  • the coating apparatus is most preferably arranged to minimise the distance travelled by the articles following coating and before packaging. This minimises the opportunity for coating composition to be lost from the articles.
  • the coating apparatus comprises a coating chamber within which can be created an "atmosphere" of coating composition, the articles becoming coated with the coating composition as they fall through the chamber.
  • An electrostatic charge may be applied to the coating material and/or to the articles to reduce the tendency for them to separate .
  • the coating composition may be introduced into the coating chamber by an injector.
  • an injector may carry the coating composition entrained in a fluid stream, especially a gas such as air.
  • coating composition into the coating apparatus in synchronism 5 with operation of the batch production apparatus . This can ensure that the articles and the coating composition arrive at the coating apparatus with a relative timing to ensure proper coating of the articles.
  • Measures may be taken during operation of apparatus embodying the invention to ensure that the batch production apparatus does not deliver batches of articles when either the coating apparatus or the packaging apparatus is not ready to receive them. If this were to happen then articles might potentially accumulate within the apparatus, or be mishandled, with generally undesirable consequences .
  • the coating apparatus preferably generates controlled size charges by means of a divider arrangement acting on a uniform feed e.g. from a weighing feeder.
  • the divider arrangement may have an interrupter construction traversing the material path and having relatively movable parts with respective openings, a drive being provided - stepped or continuous - controllable to bring the respective openings into register with one another (allowing or causing onward flow of a charge of material) at a controlled frequency.
  • Figure 1 is a schematic diagram of apparatus for batch weighing, flavouring and packaging potato crisps
  • Figure 2 shows in more detail a diagrammatic cross-section of a depositor valve being part of the embodiment of Figure 1
  • Figures 3 and 4 are schematic diagrams of apparatus for batch weighing, flavouring and packaging potato crisps being second and third embodiments of the invention.
  • apparatus embodying the invention includes a batch formation apparatus comprising a multihead weigher 10.
  • the multihead weigher 10 is conventional and widely used in production of potato crisps and of many other articles and will therefore not be described further, other than to say that it has a control input 20 upon which a signal can be placed in order to instruct the weigher to measure and release a batch of potato crisps (shown generally at 12) of a predetermined weight.
  • This signal can be initiated from other apparatus, such as a packaging apparatus or a control unit .
  • the batches 12 which are produced by the multihead weigher fall from it, through a coating chamber at 14, into a packaging apparatus at 16.
  • the packaging apparatus 16 comprises a tube 22 in which bags are formed and a sealing arrangement 24; again both of these are entirely conventional.
  • the multihead weigher 10, the coating chamber 14, and the packaging apparatus 16 are all arranged in a vertical alignment . This arrangement allows batches 12 to drop through the apparatus, so avoiding the need to provide complex handling equipment to transport them. However, if it is deemed necessary or desirable, offsets can be accommodated between components by providing suitable conveyors .
  • the coating chamber 14 forms part of coating apparatus of this embodiment of the invention, which 7 coating apparatus will now be described in greater detail .
  • the coating apparatus operates to deliver into the coating chamber 14 an amount of flavouring to be coated onto a batch of crisps 12.
  • the flavouring is in the form of a fine powder.
  • a loss-in-weight feeder 30 generates a continuous supply of flavouring at a constant weight per unit time .
  • the supply of flavouring is carried by a conveyer 32 to be deposited into a depositor valve 34.
  • the depositor valve 34 operates to transform the continuous feed produced by the loss-in-weight feeder 30 into a regular succession of batches of flavouring.
  • Each batch is collected from the output of the loss-in-weight feeder 30 during a fixed time period, with the consequence that the batches are of substantially uniform weight, in a manner substantially as described in GB-A-2127158 , which is hereby incorporated by reference .
  • a deflector valve 36 is positioned between the loss-in-weight feeder 30 and the depositor valve 34.
  • the deflector valve 36 can be selectively operated to allow flavouring to enter the depositor valve 34, or to be diverted from it into a collection vessel (not shown) . The intention behind this will become apparent in due course .
  • Batches of flavouring leaving the depositor valve 34 are received by an input hopper 38 of a blowing line eductor.
  • the eductor causes the flavouring to be carried from the hopper rapidly along a pipe 40 to an injector 42. From the injector 42, the flavouring is injected directly into the coating chamber 14.
  • the depositor valve 34 comprises a housing 70 having an upwardly open inlet port 62 and a downwardly open outlet port 66.
  • the housing has a cylindrical valve chamber 68, having a horizontal axis .
  • the inlet and the outlet ports 62,66 extend from the valve chamber 68.
  • Within the valve chamber there is a rotor 72 having a shaft 74 extending coaxially of the chamber 68 and being rotatable within it.
  • a plurality of vanes 78 extend from the shaft 74, spaced at equal angles around it. The vanes 78 extend to approach closely an inner wall
  • Cells A to D are defined between adjacent vanes and the inner wall 80.
  • the shaft 74 is connected to a stepper motor by means of which it can be rotated. Suitable seals are provided where the shaft passes out of the housing 70.
  • cell A is open to the inlet port 62 and is being filled, at a constant mass-flow rate, by a flow of flavouring powder from the conveyer 32.
  • Cell B is filled with flavouring awaiting release.
  • the contents of cell C are being deposited into the outlet port 66.
  • Cell D is empty.
  • the weight of flavouring in cell A can be deduced from the amount of time for which it has been receiving flavouring from the inlet port 62. After such a time as is required to fill the cell with a desired weight, the rotor is rotated by the stepper motor through an angle identical to the angle between adjacent vanes 78, such that cell A moves to the position formerly occupied by cell B, and the other cells are moved likewise. This causes the contents of cell B to be deposited into the output port 66 in a batch. This process can be repeated indefinitely to produce a succession of batches of flavouring powder of approximately equal weight .
  • the amount of time for which the uppermost cell is filled with flavouring powder is fixed by the requirement for it to contain an amount of powder of a known weight . Under normal operation, this period is fixed by periodic rotation of the rotor 72. From time to time, it may happen that the multihead weigher 10 is unable to deliver a batch of crisps 12, or that the packaging apparatus 16 is not ready to receive a batch of crisps 12 by the time that the uppermost cell has been filled with the required amount of flavouring. If this happens, the rotor 72 is preferably not advanced because it would deposit a batch of flavouring that cannot be put to use. In this event, the deflector valve 36 is operated to prevent overfilling of the uppermost cell.
  • the rotor 72 can be rotated and the deflector valve 36 can be deactivated to allow normal operation to recommence.
  • Flavouring powder which has been diverted to the collection vessel can be returned to the loss-in-weight feeder 30.
  • a control unit 1 is provided which is programmed to control operation of the apparatus .
  • the control unit 1 can (a) initiate release of a batch of crisps 10 from the multihead weigher by placing a suitable signal on its control input 20; (b) initiate release of a batch of flavouring powder by activating the stepper motor in order to rotate the rotor 72; and (c) activate and deactivate the deflector valve 36 as appropriate. 10
  • control unit 1 is set by an operator to specify the amount of additive (in this case, flavouring powder) to be added to each batch of product (in this example, crisps) to be dropped into each bag. Additionally, the operator sets a default bag filling rate which should preferably be achieved. From these two figures, the control unit can calculate the rate of operation of the loss-in-weight feeder 30.
  • additive in this case, flavouring powder
  • the control unit can calculate the rate of operation of the loss-in-weight feeder 30.
  • the operator could specify that 2g of additive should be added to each batch with a default bag- filling rate of 60 bags per minute.
  • the loss-in-weight feeder should achieve 120 g/minute (7.20 kg/hour) .
  • the control unit 1 monitors (e.g. via conventional sensors) the frequency at which batches are actually being generated. If this frequency deviates from that expected, the control unit re-calculates the rate at which the loss-in-weight feeder should operate and adjusts its operation accordingly. In the above example, if the rate were observed to be 70 per minute, the control unit would re-calculate the required flow to be 140 g/min.
  • the control unit is configured such that time elapsing during operation of the diverter valve is not taken, into account when calculating a flow rate, since such diversions are normally temporary, and should not be allowed to effect a long-term influence on the calculated flow rate.
  • the control unit 1 can also be programmed to raise alarms in the event that the flow rate exceeds or falls below threshold levels, or in the event that the total amount of product or additive dispensed is such that a refill of additional product or additive is likely to 11 be needed .
  • FIG. 3 an alternative batch formation apparatus is shown. This apparatus is suitable for use within the first aspect of the invention, to deliver batches of flavouring, and in many other applications .
  • the apparatus comprises a constant rate feeder 100 which delivers material at a constant rate to an output 102.
  • the rate may be constant in volume or constant in weight, as appropriate to a particular application.
  • the feeder comprises a hopper 104 as a reservoir for the material .
  • Material is delivered from the output 102 to an intake 108 of a diverter 106.
  • the diverter 106 delivers material received on its input 108 to one of two outputs 110 or 112.
  • An electrical control signal is applied to the diverter 106 to determine which of the two outputs 110,112 receives the material e.g. by means of a pivotable vane or sliding gate.
  • Material delivered to a first of the two outputs 110 is deposited in a receptacle 114 at a delivery point for subsequent processing.
  • a continuous supply of such receptacles 114 may proceed along a conveyer 116.
  • Sensors are provided to indicate to a control unit the presence of a receptacle 114 at the delivery point, whereupon the control unit operates the diverter
  • the amount of material delivered to the receptacle is determined by the amount of time that the 12 diverter 106 delivers material to its first output 110.
  • Material delivered to the second output 112 of the diverter 106 is received by a fixed receptacle 120 from which it is carried back to the hopper 104. In this embodiment, this is achieved by an air conveyor 122, but many other conveying systems (mechanical or otherwise) could be used. Thus, material delivered by the feeder 100 is either delivered as a batch to an output for use, or is eventually returned to the feeder 100. This allows batches to be generated on demand with no waste of material, nor is there a need to ensure that the demand for batches is regular and periodic .
  • the feeder 100 delivers material into an input 140 of an air conveyor 142.
  • the air conveyor 142 has a diverter valve 144 which has two outputs .
  • a first of the outputs delivers material to an injector nozzle 146 which injects the material into a coating chamber for application to a product .
  • a second of its outputs delivers material to a return line 150 which feeds the material back to the hopper 104 of the feeder 100.
  • nozzle is not an essential feature of the embodiment of Figure 4.
  • the material might be delivered to any other receiving apparatus .

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Formation And Processing Of Food Products (AREA)

Abstract

Apparatus and methods for applying coating material such as a powdered flavouring to batched, packaged product such as a snackfood consisting of loose, discrete articles. The coating material is presented as charges of controlled size by dividing a uniform feed, e.g. from a weigher (30) by means of a rotary valve (34). An injector (40, 42) or other suitable applicator applies the charges of coating material successively to respective batches of product, in-line downstream of the batch formation apparatus (10) which is e.g. a multihead or linear weigher, and directly upstream of or at packaging apparatus (16) e.g. a bagging machine. This minimises contamination by the coating material. A control unit (1) may synchronise the applications and control coating material supply.

Description

1 METHODS AND APPARATUS FOR APPLYING COATING MATERIAL
FIELD OF THE INVENTION
The present invention relates to materials handling and treatment apparatus . A preferred application of the invention is to application of flavouring compositions to foods, particularly particulate foods or snack foods e.g. potato crisps
BACKGROUND
Potato crisps, like other snack foods, are typically coated with a flavouring composition. The flavouring composition may be salt, or other more complex flavouring compounds. Whatever flavouring is to be used, there is a need to control the amount of flavouring composition which is applied to ensure that the strength of flavour on the finished product is within acceptable limits .
Conventionally, potato crisps are made in large batches. The batches are each weighed, and then tumbled in a processing drum with an amount of flavouring composition appropriate to the weight of the batch. The intention is that tumbling will cause the flavouring composition to be coated evenly onto the crisps .
Subsequently, the coated crisps are weighed into small batches and packaged as a product for sale.
This system has disadvantages. First, there is a tendency for some of the flavouring composition to fall from the crisps before they are packaged. This results in wastage, because an extra quantity of flavouring composition must be added to the processing drum to 2 compensate for this loss . This also causes a variation in the flavour of the final product. Also, apparatus which processes the crisps following coating will become contaminated with the flavouring composition. This is particularly problematic when the flavouring composition is to be changed because such apparatus must be thoroughly cleaned to avoid contamination of the new flavouring composition with the old.
SUMMARY OF THE INVENTION
It is an aim of the present invention to ameliorate these problems and analogous problems which occurs when processing other coated products .
We disclose herein apparatus and methods for applying coating material such as a powdered flavouring to batched product such as a snackfood consisting of loose, discrete articles, which is to be packaged. The coating material is presented as charges of controlled size by dividing a uniform feed, e.g. from a weigher by means of a rotary valve. An injector or other suitable applicator applies the charges of coating material successively to respective batches of product, in-line downstream of the batch formation apparatus which is e.g. a multihead or linear weigher, and directly upstream of or at packaging apparatus such as a bagging machine. This minimises contamination by the coating material. A control unit may synchronise the applications with the production of the batches and control the coating material supply.
Particular aspects of the invention are set out in the claims .
According to one aspect herein there is provided material handling and processing apparatus for multiple articles comprising batch formation apparatus for receiving articles in bulk and for producing relatively smaller batches of articles, a coating apparatus for applying a coating material to articles, and a packaging apparatus for packaging a batch of articles into a discrete package; the apparatus being arranged such that the coating apparatus operates on individual batches of articles produced by the batch formation apparatus, before packaging of the batch by the packaging apparatus .
This arrangement of apparatus ensures that the batch formation apparatus cannot become contaminated by the coating material. This is of particular advantage because the batch formation apparatus is commonly a component which presents particular difficulties when cleaning is required.
Articles processed by apparatus embodying the invention may be discrete articles such as potato crisps or other snack foods. Alternatively, it can be used to process articles in the form of particulate, granular or powdered material in applications where there is a requirement to coat a product with a coating composition.
The batch formation apparatus may operate on the basis of generating batches of constant weight or of constant volume. As an example, apparatus as described in UK Patent Specification No. 2127158 may be used. A loss-in-weight feeder, a batch weigher or a multi-head weigher could alternatively to provide batches of known weight . It will be recognised by those skilled in the art that many other types of weight-based or volumetric batch production apparatus could be used, as appropriate for the particular application of the apparatus . The invention may use batch or charge formation apparatus comprising a continuous feeder for generating a flow of material from a reservoir at a constant weight or a constant volume per unit time, a diverter for generating a batch by diverting that flow to an output for a predetermined time, and a recovery system for returning to the reservoir any material not diverted to the output . This apparatus has the advantage of being able to produce a batch of material of known weight or volume, as the case may be, on demand. No difficulty is encountered in the event that a demand for batches of material temporarily ceases .
The coating apparatus is most preferably arranged to minimise the distance travelled by the articles following coating and before packaging. This minimises the opportunity for coating composition to be lost from the articles.
In particularly advantageous embodiments, particularly suitable for use with coating material in powder form, the coating apparatus comprises a coating chamber within which can be created an "atmosphere" of coating composition, the articles becoming coated with the coating composition as they fall through the chamber. An electrostatic charge may be applied to the coating material and/or to the articles to reduce the tendency for them to separate .
The coating composition may be introduced into the coating chamber by an injector. Such an injector may carry the coating composition entrained in a fluid stream, especially a gas such as air.
It has been found preferable to introduce coating composition into the coating apparatus in synchronism 5 with operation of the batch production apparatus . This can ensure that the articles and the coating composition arrive at the coating apparatus with a relative timing to ensure proper coating of the articles.
Measures may be taken during operation of apparatus embodying the invention to ensure that the batch production apparatus does not deliver batches of articles when either the coating apparatus or the packaging apparatus is not ready to receive them. If this were to happen then articles might potentially accumulate within the apparatus, or be mishandled, with generally undesirable consequences .
The coating apparatus preferably generates controlled size charges by means of a divider arrangement acting on a uniform feed e.g. from a weighing feeder. The divider arrangement may have an interrupter construction traversing the material path and having relatively movable parts with respective openings, a drive being provided - stepped or continuous - controllable to bring the respective openings into register with one another (allowing or causing onward flow of a charge of material) at a controlled frequency.
BRIEF DESCRIPTION OF THE DRAWINGS
Embodiments of the invention will now be described in detail, by way of example, and with reference to the accompanying drawings in which:
Figure 1 is a schematic diagram of apparatus for batch weighing, flavouring and packaging potato crisps; Figure 2 shows in more detail a diagrammatic cross-section of a depositor valve being part of the embodiment of Figure 1 ; and Figures 3 and 4 are schematic diagrams of apparatus for batch weighing, flavouring and packaging potato crisps being second and third embodiments of the invention.
DESCRIPTION OF PREFERRED EMBODIMENTS
With reference to Figure 1, apparatus embodying the invention includes a batch formation apparatus comprising a multihead weigher 10. The multihead weigher 10 is conventional and widely used in production of potato crisps and of many other articles and will therefore not be described further, other than to say that it has a control input 20 upon which a signal can be placed in order to instruct the weigher to measure and release a batch of potato crisps (shown generally at 12) of a predetermined weight. This signal can be initiated from other apparatus, such as a packaging apparatus or a control unit .
The batches 12 which are produced by the multihead weigher fall from it, through a coating chamber at 14, into a packaging apparatus at 16. The packaging apparatus 16 comprises a tube 22 in which bags are formed and a sealing arrangement 24; again both of these are entirely conventional. The multihead weigher 10, the coating chamber 14, and the packaging apparatus 16 are all arranged in a vertical alignment . This arrangement allows batches 12 to drop through the apparatus, so avoiding the need to provide complex handling equipment to transport them. However, if it is deemed necessary or desirable, offsets can be accommodated between components by providing suitable conveyors .
The coating chamber 14 forms part of coating apparatus of this embodiment of the invention, which 7 coating apparatus will now be described in greater detail .
The coating apparatus operates to deliver into the coating chamber 14 an amount of flavouring to be coated onto a batch of crisps 12. The flavouring is in the form of a fine powder. In the coating apparatus, a loss-in-weight feeder 30 generates a continuous supply of flavouring at a constant weight per unit time . The supply of flavouring is carried by a conveyer 32 to be deposited into a depositor valve 34. The depositor valve 34 operates to transform the continuous feed produced by the loss-in-weight feeder 30 into a regular succession of batches of flavouring. Each batch is collected from the output of the loss-in-weight feeder 30 during a fixed time period, with the consequence that the batches are of substantially uniform weight, in a manner substantially as described in GB-A-2127158 , which is hereby incorporated by reference .
A deflector valve 36 is positioned between the loss-in-weight feeder 30 and the depositor valve 34. The deflector valve 36 can be selectively operated to allow flavouring to enter the depositor valve 34, or to be diverted from it into a collection vessel (not shown) . The intention behind this will become apparent in due course .
Batches of flavouring leaving the depositor valve 34 are received by an input hopper 38 of a blowing line eductor. The eductor causes the flavouring to be carried from the hopper rapidly along a pipe 40 to an injector 42. From the injector 42, the flavouring is injected directly into the coating chamber 14.
With reference now to Figure 2, the depositor valve 34 comprises a housing 70 having an upwardly open inlet port 62 and a downwardly open outlet port 66. The housing has a cylindrical valve chamber 68, having a horizontal axis . The inlet and the outlet ports 62,66 extend from the valve chamber 68. Within the valve chamber, there is a rotor 72 having a shaft 74 extending coaxially of the chamber 68 and being rotatable within it. A plurality of vanes 78 extend from the shaft 74, spaced at equal angles around it. The vanes 78 extend to approach closely an inner wall
80 of the chamber 68. Cells A to D are defined between adjacent vanes and the inner wall 80.
Externally of the housing 70, the shaft 74 is connected to a stepper motor by means of which it can be rotated. Suitable seals are provided where the shaft passes out of the housing 70.
As shown in Figure 2, cell A is open to the inlet port 62 and is being filled, at a constant mass-flow rate, by a flow of flavouring powder from the conveyer 32. Cell B is filled with flavouring awaiting release. The contents of cell C are being deposited into the outlet port 66. Cell D is empty.
The weight of flavouring in cell A can be deduced from the amount of time for which it has been receiving flavouring from the inlet port 62. After such a time as is required to fill the cell with a desired weight, the rotor is rotated by the stepper motor through an angle identical to the angle between adjacent vanes 78, such that cell A moves to the position formerly occupied by cell B, and the other cells are moved likewise. This causes the contents of cell B to be deposited into the output port 66 in a batch. This process can be repeated indefinitely to produce a succession of batches of flavouring powder of approximately equal weight .
It will be understood that the amount of time for which the uppermost cell is filled with flavouring powder is fixed by the requirement for it to contain an amount of powder of a known weight . Under normal operation, this period is fixed by periodic rotation of the rotor 72. From time to time, it may happen that the multihead weigher 10 is unable to deliver a batch of crisps 12, or that the packaging apparatus 16 is not ready to receive a batch of crisps 12 by the time that the uppermost cell has been filled with the required amount of flavouring. If this happens, the rotor 72 is preferably not advanced because it would deposit a batch of flavouring that cannot be put to use. In this event, the deflector valve 36 is operated to prevent overfilling of the uppermost cell. Once the multihead weigher 10 or the packaging apparatus 16 is ready to deliver or receive a batch of crisps, the rotor 72 can be rotated and the deflector valve 36 can be deactivated to allow normal operation to recommence. Flavouring powder which has been diverted to the collection vessel can be returned to the loss-in-weight feeder 30.
A control unit 1 is provided which is programmed to control operation of the apparatus . Most particularly, the control unit 1 can (a) initiate release of a batch of crisps 10 from the multihead weigher by placing a suitable signal on its control input 20; (b) initiate release of a batch of flavouring powder by activating the stepper motor in order to rotate the rotor 72; and (c) activate and deactivate the deflector valve 36 as appropriate. 10
In operation, the control unit 1 is set by an operator to specify the amount of additive (in this case, flavouring powder) to be added to each batch of product (in this example, crisps) to be dropped into each bag. Additionally, the operator sets a default bag filling rate which should preferably be achieved. From these two figures, the control unit can calculate the rate of operation of the loss-in-weight feeder 30.
For example, the operator could specify that 2g of additive should be added to each batch with a default bag- filling rate of 60 bags per minute. Thus, the loss-in-weight feeder should achieve 120 g/minute (7.20 kg/hour) .
During operation of the apparatus, the control unit 1 monitors (e.g. via conventional sensors) the frequency at which batches are actually being generated. If this frequency deviates from that expected, the control unit re-calculates the rate at which the loss-in-weight feeder should operate and adjusts its operation accordingly. In the above example, if the rate were observed to be 70 per minute, the control unit would re-calculate the required flow to be 140 g/min. The control unit is configured such that time elapsing during operation of the diverter valve is not taken, into account when calculating a flow rate, since such diversions are normally temporary, and should not be allowed to effect a long-term influence on the calculated flow rate.
The control unit 1 can also be programmed to raise alarms in the event that the flow rate exceeds or falls below threshold levels, or in the event that the total amount of product or additive dispensed is such that a refill of additional product or additive is likely to 11 be needed .
With reference now to Figure 3 , an alternative batch formation apparatus is shown. This apparatus is suitable for use within the first aspect of the invention, to deliver batches of flavouring, and in many other applications .
The apparatus comprises a constant rate feeder 100 which delivers material at a constant rate to an output 102. The rate may be constant in volume or constant in weight, as appropriate to a particular application. The feeder comprises a hopper 104 as a reservoir for the material .
Material is delivered from the output 102 to an intake 108 of a diverter 106. The diverter 106 delivers material received on its input 108 to one of two outputs 110 or 112. An electrical control signal is applied to the diverter 106 to determine which of the two outputs 110,112 receives the material e.g. by means of a pivotable vane or sliding gate.
Material delivered to a first of the two outputs 110 is deposited in a receptacle 114 at a delivery point for subsequent processing. A continuous supply of such receptacles 114 may proceed along a conveyer 116. Sensors are provided to indicate to a control unit the presence of a receptacle 114 at the delivery point, whereupon the control unit operates the diverter
106 to deliver material to the first output 110 for a predetermined time, and after that time has elapsed, to revert delivery to the second output 112. Given that the rate at which material is delivered to the diverter is known, the amount of material delivered to the receptacle is determined by the amount of time that the 12 diverter 106 delivers material to its first output 110.
Material delivered to the second output 112 of the diverter 106 is received by a fixed receptacle 120 from which it is carried back to the hopper 104. In this embodiment, this is achieved by an air conveyor 122, but many other conveying systems (mechanical or otherwise) could be used. Thus, material delivered by the feeder 100 is either delivered as a batch to an output for use, or is eventually returned to the feeder 100. This allows batches to be generated on demand with no waste of material, nor is there a need to ensure that the demand for batches is regular and periodic .
The embodiment of Figure 4 operates in accordance with the same general principles of that of Figure 3. In this embodiment, the feeder 100 delivers material into an input 140 of an air conveyor 142. The air conveyor 142 has a diverter valve 144 which has two outputs . A first of the outputs delivers material to an injector nozzle 146 which injects the material into a coating chamber for application to a product . A second of its outputs delivers material to a return line 150 which feeds the material back to the hopper 104 of the feeder 100. By operating the valve 144 to deliver material to the first output for a predetermined time, a batch of material of known weight or volume is delivered to the nozzle 146.
It will be clear that the nozzle is not an essential feature of the embodiment of Figure 4. The material might be delivered to any other receiving apparatus .
For example, suppose that batches of 2g of 13 material are required at a rate of 60 per minute, and that at least half a second must elapse between delivery of batches. A theoretical limit would be for the feeder to operate at a rate of 240 g/min (4 g/s) with batches being generated by diverting flow from the feeder for periods of half a second.

Claims

14 CLAIMS :
1. Handling and processing apparatus comprising batch formation apparatus (10) to receive a bulk supply of product and divide it into relatively smaller batches (12) of predetermined size for packaging; coating apparatus (30-42) adapted to divide a coating material into charges of predetermined size and apply the charges of coating material to respective said product batches (12) downstream of the batch formation apparatus (10) , and packaging apparatus (16) which receives and encloses the product batches (12) in discrete packages,- the coating apparatus (30-42) being disposed to apply said coating material at a coating location (14) which is at or directly upstream of the packaging apparatus (16) .
2. Apparatus according to claim 1 in which the batch formation apparatus (10) comprises a weigher for controlling batch size by weight.
3. Apparatus according to claim 2 in which the batch formation apparatus (10) comprises a multi-head or linear weigher.
4. Apparatus according to any one of the preceding claims in which the packaging apparatus (16) is a bagging machine .
5. Apparatus according to any one of the preceding claims in which the coating location (14) is on a product batch conveyor path leading directly to receipt of the product batches (12) in their packages.
6. Apparatus according to claim 5 in which said 15 conveyor path is an enclosed chute into which the coating apparatus injects the successive charges of coating material.
7. Apparatus according to claim 5 or 6 in which product batches pass under gravity along said batch conveyor path past the coating location (14) .
8. Apparatus according to any one of the preceding claims in which a control processor (1) is programmed to synchronise said operation of the coating apparatus to apply coating material with passage of batches (12) from the batch formation apparatus (10) .
9. Coating apparatus for use in handling and processing apparatus according to any one of claims 1 to 8, comprising a divider arrangement (34) for dividing a controlled feed of coating material into said charges and an applicator (38,40,42) for transferring the charges successively onto the product batches (12) .
10. Apparatus according to any one of claims 1 to 8 in which the coating apparatus is as defined in claim 9 and in which the applicator is an injector (40,42) arranged to inject the charges of coating material at the coating location (14) .
11. Apparatus according to claim 9 or 10 in which the applicator comprises a fluid-pressure device for injecting the coating material at the coating location (14) .
12. Apparatus according to claim 11 in which the applicator provides a gas stream to entrain particles of coating material . 16
13. Apparatus according to any one of the preceding claims, the coating apparatus including a continuous feeder (30) for generating a controlled feed of the coating material at a constant volume or constant weight per unit time.
14. Apparatus according to any one of the preceding claims in which a control processor (1) is programmed to adjust a rate of feed of the coating material in dependence on variations in rate of production of said batches (12) .
15. Apparatus according to any one of the preceding claims comprising a diverter arrangement (36,106) which is switchable from a control processor (1) to interrupt the feed of coating material.
16. A method comprising the operation of apparatus according to any one of claims 1 to 15 to apply coating material to batches of product
17. A method according to claim 16 in which the product is a food.
18. A method according to claim 16 or 17 in which the product is loose discrete articles, and each batch (12) contains multiple articles.
19. A method according to any one of claims 16 to 18 in which the coating material is a flowable material, preferably either liquid or powder.
PCT/GB1999/001524 1998-05-13 1999-05-13 Methods and apparatus for applying coating material WO1999058005A1 (en)

Priority Applications (1)

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AU39412/99A AU3941299A (en) 1998-05-13 1999-05-13 Methods and apparatus for applying coating material

Applications Claiming Priority (2)

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GBGB9810249.4A GB9810249D0 (en) 1998-05-13 1998-05-13 Materials handling and treatment apparatus
GB9810249.4 1998-05-13

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Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0009888D0 (en) * 2000-04-20 2000-06-07 United Biscuits Ltd Improvements in and relating to the processing and packaging of food items
JP4529022B2 (en) * 2001-05-08 2010-08-25 株式会社イシダ Weighing seasoning system
DE60114445T2 (en) * 2000-11-27 2006-07-27 Ishida Co., Ltd. DEVICE FOR FLAVORING
GB2385810B (en) * 2002-03-01 2005-03-09 Spice Applic Systems Ltd Product coating method and apparatus
AU2002301940B9 (en) * 2002-11-06 2009-09-17 Ishida Co., Ltd. Flavouring system and method
US8051795B2 (en) * 2006-04-28 2011-11-08 Restaurant Technology, Inc. Storage and packaging of bulk food items and method
US9055767B2 (en) 2012-01-22 2015-06-16 John Bean Technologies Corporation Food coating apparatuses, systems, and methods

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2303608A1 (en) * 1975-03-11 1976-10-08 Gervais Danone Sa Spraying of fine coatings onto prods. in a tank - without wasting coating material or spoiling coating
US4264634A (en) * 1977-10-26 1981-04-28 J. E. Grote Pepp-A-Matic Co., Inc. Method for applying grated cheese to pizza shells
US5287801A (en) * 1991-07-31 1994-02-22 Clark Gordon A Flavoring food products
WO1995001105A1 (en) * 1993-07-02 1995-01-12 General Mills, Inc. Reduced fat microwave popcorn and method of preparation
US5620519A (en) * 1994-08-19 1997-04-15 Sunkist Growers, Inc. Controller and method for selectively controlling the amount of wax applied to fruit

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61173756A (en) * 1985-01-25 1986-08-05 Nissin Food Prod Co Ltd Preparation of instant noodle
US5353959A (en) * 1992-12-11 1994-10-11 Recot, Inc. Apparatus for dispensing powdered or granular seasoning materials
GB9620228D0 (en) * 1996-09-27 1996-11-13 Itw Ltd An electronic flavouring system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2303608A1 (en) * 1975-03-11 1976-10-08 Gervais Danone Sa Spraying of fine coatings onto prods. in a tank - without wasting coating material or spoiling coating
US4264634A (en) * 1977-10-26 1981-04-28 J. E. Grote Pepp-A-Matic Co., Inc. Method for applying grated cheese to pizza shells
US5287801A (en) * 1991-07-31 1994-02-22 Clark Gordon A Flavoring food products
WO1995001105A1 (en) * 1993-07-02 1995-01-12 General Mills, Inc. Reduced fat microwave popcorn and method of preparation
US5620519A (en) * 1994-08-19 1997-04-15 Sunkist Growers, Inc. Controller and method for selectively controlling the amount of wax applied to fruit

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AU3941299A (en) 1999-11-29
GB9810249D0 (en) 1998-07-08
GB9911120D0 (en) 1999-07-14
GB2337191A (en) 1999-11-17

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