Apparatus for creating a substantially uniform temperature across a plastic sheet for delivery to an appliance liner thermoforming device

Information

  • Patent Grant
  • 6443721
  • Patent Number
    6,443,721
  • Date Filed
    Wednesday, May 5, 1999
    25 years ago
  • Date Issued
    Tuesday, September 3, 2002
    21 years ago
Abstract
A sheet of plastic to be thermoformed into an appliance liner is brought to a substantially uniform temperature, preferably to a temperature differential of less than 5° F. throughout, by directing a fluid medium upon opposing side surfaces of the sheet. In the most preferred form of the invention, the fluid medium is constituted by air which is heated, impinged upon the opposing surfaces and recirculated, with the temperature and flow rate of the air being controlled based on sensed operating parameters.
Description




BACKGROUND OF THE INVENTION




1. Field of the Invention




The present invention pertains to the art of thermoforming appliance liners and, more particularly, to a method and apparatus for developing a substantially uniform temperature across a plastic sheet for delivery to an appliance liner thermoforming device.




2. Discussion of the Prior Art




In forming liners for appliances, such as refrigerators and dishwashers, it is known to extrude sheets or billets of thermoplastic material to be delivered to a thermoforming device. Following the extrusion process, the sheets will be at a temperature in the order of 130° F. and are typically stacked for later delivery to the thermoforming device. At times, the sheets can remain in a given stack for a week or more prior to actually being formed into a liner.




The temperature environment in which the sheets are stacked is typically not uniformly regulated. For instance, the sheets can be placed in a 60° F. or less environment in the winter season and subjected to over 100° F. temperatures in the summer. In addition, since the sheets can remain in the stacks for some time, the outer stacked sheets will generally reach the ambient temperature, while the inner sheets will stay fairly hot. Furthermore, the outer edge portions of each inner sheet will assume a lower temperature than the center of the sheet.




Based on at least these reasons, the actual temperatures of the various sheets delivered to the thermoforming device can vary greatly which, in turn, can result in the production of thermoformed articles having varying wall thicknesses and varying amounts of “formed in” stresses. This problem is particularly significant in the field of the present invention wherein an extruded sheet of approximately 5 mm (0.20 inches) thick is stretched to form a liner in the order of two feet deep, with the liner walls being extremely thin, generally in the order of less than 0.7 mm (0.03 inches). With varying temperatures across the sheet, the sheet will unevenly stretch, perhaps resulting in a liner having certain wall portions which are disadvantageously thin and prone to cracking.




In an attempt to compensate for potential product variations, it has been proposed in the art to pre-heat plastic sheets to be thermoformed. For instance, U.S. Pat. No. 4,842,742 is directed to controlling the heating of different portions of a synthetic resin sheet delivered to a vacuum forming device to create a refrigerator liner. The actual purpose of the controlled heating is to provide a desired differential thickness in different portions of the liner. More specifically, an oven is provided to heat a sheet received from a stacked pallet prior to delivery of the sheet to a vacuum forming device. The heating oven includes upper and lower platens for the differential heating of the sheet. Other arrangements have also been proposed to maintain accurate temperature control in the heating of at least one side of a plastic sheet.




Regardless of the prior attempts made in pre-heating plastic sheets, there still exists a need for a method and apparatus for forming a liner of an appliance from an extruded sheet which is delivered at a substantially uniform temperature to a thermoforming device. More specifically, there exists a need for a compact and efficient device and method for providing a consistent and substantially uniform temperature sheet which is to be thermoformed into an appliance liner.




SUMMARY OF THE INVENTION




The present invention is directed to a method and apparatus for developing a substantially uniform temperature across a sheet of plastic, i.e., to a temperature differential of less than 5° F. throughout, prior to delivery of the sheet to an appliance liner thermoforming device. More specifically, a fluid medium flow is directed unto opposing side surface portions of a sheet being delivered to a thermoforming device from a stack of extruded sheets.




In the preferred embodiment of the invention, the fluid medium is constituted by air and at least one blower is used in combination with at least one temperature control unit to develop the flow of air used in creating the uniform temperature of the sheet. The air is directed through nozzles to impinge upon the opposing side surface portions of the sheet. In the most preferred form of the invention, the air flow is heated and recirculated, with the temperature and flow rate of the air being controlled based on sensed operating parameters.











BRIEF DESCRIPTION OF THE DRAWINGS





FIG. 1

is a schematic representation of a system for producing an appliance liner in accordance with a preferred embodiment of the present invention;





FIG. 2

is a top view of a sheet pre-heating unit incorporated in the system of

FIG. 1

;





FIG. 3

is a schematic side view of the sheet pre-heating unit shown in

FIG. 2

;





FIG. 4

is a perspective view of a sheet pre-heating unit constructed in accordance with a second embodiment of the invention;





FIG. 5

is a side view of the pre-heating unit of

FIG. 4

, with various internal structural components being shown in phantom;





FIG. 6

is a top view of one module of the pre-heating unit of

FIG. 4

, with various internal structural components being shown in phantom; and





FIG. 7

is a block diagram of a control system for the pre-heating unit of the invention.











DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT




With initial reference to

FIG. 1

, an appliance liner formation system, generally indicated at


2


, includes a sheet forming unit


6


which functions to produce sheets to be placed in a stack


9


and a temperature control unit


12


to which the sheets are delivered from stack


9


prior to delivery to a thermoforming device


15


. In the most preferred form of the invention, temperature control unit


12


constitutes a pre-heating unit used to uniformly heat the sheets prior to delivery to thermoforming device


15


. Therefore, for purposes of discussing the preferred embodiment, reference will be made to pre-heating unit


12


. In a manner known in the art, thermoforming device


15


is used to create an appliance liner, such as refrigerator liner


18


. The present invention is particularly directed to the construction and operation of pre-heating unit


12


in the overall appliance liner formation system


2


. In any event, for the sake of completeness, further details of appliance liner formation system


2


will be provided below.




Sheet forming unit


6


is provided with a plastic material inlet


26


which directs plastic material into an extruder


28


. Extruder


28


leads into a housing


30


within which the extruded plastic material is forced through one or more dies to form sheets which are cut and delivered out of housing


30


by means of a conveyer


32


in the form of sheets, one of which is indicated at


35


. In practice, the various sheets


35


are stacked for later use, typically in an area which does not have a specifically regulated temperature environment. As discussed above, the sheets in stack


9


can be subjected to temperatures ranging from approximately 60° F. or less to temperatures of over 100° F. depending upon the season of the year and other temperature affecting factors. In any event, it should be readily apparent that liners formed from sheets which vary greatly in temperature when delivered to thermoforming device


15


will also vary in wall thickness and overall durability.




With this in mind, pre-heating unit


12


is adapted to receive each sheet


35


and to preheat the same to a substantially uniform temperature prior to delivery to thermoforming device


15


. In the most preferred embodiment of the invention, the sheet


35


is heated to establish a temperature differential of less than 5° F. throughout the entire sheet


35


. Therefore, a respective sheet


35


will be taken from stack


9


and placed upon a conveyer


39


for use in transporting the sheet


35


through pre-heating unit


12


. In the preferred embodiment, conveyer


39


includes first, second and third transversely spaced and longitudinally extending endless support belts


42


-


44


for supporting and delivering each of the sheets


35


through a passage


47


defined by an enclosure portion


50


of pre-heating unit


12


. In this preferred embodiment, the multiple endless support belts


42


-


44


are constituted by approximately 2.54 cm (1 inch) wide rubber belts which are designed to minimize the contact area with the sheet


35


so as to expose the entire upper surface and the majority of the lower surface of the sheet


35


.




In accordance with the present invention, pre-heating unit


12


achieves an accurate and consistent uniform heating of successive sheets


35


by impinging a flow of heated air upon upper and lower surfaces of the sheet


35


within enclosure


50


. For this purpose, enclosure


50


has attached thereto an upper blower


54


and a lower blower


55


which receive an intake of air from respective return lines


57


-


60


. Additional details of the structure and function of blowers


54


and


55


will be provided below.




Upon exiting from pre-heating unit


12


, the sheet


35


will be directly delivered to thermoforming device


15


. In a manner known in the art, thermoforming device


15


includes a male mold member


64


and a female mold member


65


between which the sheet


35


is positioned. In the preferred embodiment, a vacuum-based thermoforming process is performed. Although the present invention can be utilized to form various types of appliance liners, including liners for dishwashers, in the most preferred embodiment, each sheet


35


is utilized to form a respective refrigerator liner


18


generally provided with a peripheral front flange


69


and a body portion


71


that defines an interior storage area


73


. Although liner


18


can be formed from various polymers, a preferred material is a high impact polystyrene (HIPS). Of course, in forming liner


18


, the material of sheet


35


must be stretched in order to create the interior storage area


73


. Therefore, a sheet


35


having an initial thickness in the range of approximately 5 mm (0.20 inches) is vacuumed formed into liner


18


having a preferred wall thickness of approximately 0.7 mm (0.03 inches) and a depth of approximately 60 cm (2 feet). Of course, the actual thickness and depth of the liner


18


can vary without departing from the present invention and the thickness of sheet


35


will correspondingly change.




Reference will now be made to

FIGS. 2 and 3

in describing a preferred embodiment for pre-heating unit


12


. In the preferred form shown, upper and lower blowers


54


and


55


are identically constructed. Although two separate blowers are shown for directing a flow of air upon the upper and lower surfaces of each sheet


35


, it should be recognized that a larger, single blower unit could be provided. In any event, in the embodiment shown, each blower


54


,


55


includes an intake


77


for drawing in a flow of air to be heated through respective return lines


57


-


60


. Blowers


54


and


55


can take various forms in accordance with the present invention, such as variable speed, centrifugal squirrel cage type fans, and are readily available in the marketplace. Each blower


54


,


55


incorporates a heating unit


80


which, in the preferred embodiment, constitutes an electric, resistance heating element. In this matter, each blower


54


,


55


draws in the air to be heated and directs the air to a respective outlet


83


.




The outlets


83


of upper and lower blowers


54


and


55


lead to a manifold assembly


85


. In the preferred embodiment, manifold assembly


85


includes an upper manifold section


88


and a lower manifold section


89


. Since upper and lower manifold sections


88


and


89


are substantially identically constructed, the preferred construction for upper manifold section


88


will now be described in detail and it is to be understood that a corresponding structure for lower manifold section


89


is provided.




Upper manifold section


88


includes an inlet


92


which directly receives a flow of air from the outlet


83


of upper blower


54


. As shown, upper manifold section


88


includes a closed rear wall


95


and is provided with a plurality of transversely elongated and longitudinally spaced outlet nozzles


97


. As clearly indicated in

FIG. 2

, each nozzle


97


preferably extends transversely within enclosure


50


a distance substantially equal to the transverse dimension of the sheet


35


. Due to the presence of closed rear wall


95


, all of the air expelled from blower


54


and heated by unit


80


is forced into upper manifold section


88


and must flow through the respective nozzles


97


onto the upper surface of one or more sheets


35


concurrently being transported through pre-heating unit


12


. In this manner, upper manifold section


88


represents a common enclosed zone into which the heated air from blower


54


is expelled for distribution to nozzles


97


. Therefore the actual construction of upper manifold section


88


, and manifold assembly


85


as a whole, can take various forms in accordance with the present invention, including simple ductwork or piping, without departing from the invention. In any event, due to the similar construction for lower manifold section


89


, the lower surface of each sheet


35


also has impinged thereon a flow of heated air. Therefore, due to the arrangement of manifold sections


88


and


89


and nozzles


97


, a uniformly distributed flow of heated air impinges upon the upper and lower surfaces of the sheets


35


which, in turn, enables each of the sheets


35


to be heated to the uniform temperature in accordance with the present invention.




In the preferred embodiment, the sheets


35


are heated to a temperature in the order of 130-140° F. for the production of liner


18


, with this temperature being above any expected ambient temperature for stack


9


to assure a heating of sheets


35


in pre-heating unit


12


, with a temperature of approximately 140° F. being preferred. Of course, various factors directly reflect upon the ability of pre-heating unit


12


to uniformly and consistently heat each sheet


35


as it passes through enclosure


50


. For instance, the air flow rate, the slot width (W) for each of the nozzles


97


, the spacing (S) between adjacent nozzles


97


and the distance (H) from the outlet of each nozzle


97


to the respective surface of the impinged sheet


35


are major input parameters which have been optimally designed in accordance with the present invention. Extensive experimental and theoretical research has been devoted over the years to impinging flow and heat/mass transfer resulting in optimal values of W and S which are as follows:








W≈


0.1


H


&


S=


1.4


H








Reduced scale testing in accordance with the present invention was initially done on a sheet having the length of 42 mm (16.5 inches), a width of 20 mm (8 inches) and a thickness of 6 mm (0.24 inches). The arrangement of nozzles


97


were established based on the above formulas utilizing a distance of 76 mm (3 inches) from the exit of the nozzles


97


to the respective centerline of the sheet which resulted in a nozzle spacing of approximately 107 mm (4.2 inches) and a nozzle width of 7.6 mm (0.3 inches).




It is generally desirable in accordance with the present invention to make pre-heating unit


12


rather compact. In accordance with the preferred form of the invention, it is desired to have pre-heating unit


12


sized to simultaneously heat in a range or three to five (3-5) sheets in any given time. In addition, it is desirable to establish a reasonable heating time which, in the preferred embodiment, is approximately 40 seconds. With these established parameters and desired operation characteristics in mind for the reduced scale testing, a flow of heated air at approximately 140° F. was impinged upon the upper and lower surfaces of the sheet of approximately one square foot at a mass flow rate of 610 CFM (cubic feet per minute). Furthermore, through this testing, it was determined that a static pressure range of approximately 0.7-0.9 in. H


2


O within enclosure


50


is practical and economical for the beating of the sheets.




At this point, it should be realized that the pre-heating unit can take various forms in accordance with the present invention. In forming refrigerator liner


18


, each sheet


35


is preferably constituted by a 122 cm×244 cm (4′×8′) high impact polystyrene sheet. To assure uniform heating of each sheet


35


, the pre-heating unit would actually be built on a much larger scale such as represented by the embodiment of

FIGS. 4-6

. More specifically, this preferred embodiment incorporates two modular pre-heating units


12




a


and


12




b


which are arranged back-to-back and secured together for use with an elongated conveyer


39


. Therefore, modular preheating units


12




a


and


12




b


are integrated to form a single unit, with each pre-heating unit


12




a,




12




b


having associated therewith an outer enclosure


105


which is preferably made from galvanized sheet metal and structurally reinforced by a framework


110


. In the preferred embodiment, framework


110


is defined by welded square steel tubing. Within enclosure


105


is provided a layer of insulation


115


, such as approximately 2 cm (0.75 inch) expanded polystyrene (EPS).




As shown, each pre-heating unit module


12




a,




12




b


includes an upper blower


54




a


having an associated electric heating element


80




a


for directing a flow of heated air into a manifold assembly


85




a


that leads to a nozzle array


97




a.


A similar lower blower


55




a


is also provided with a corresponding electric heating element


80




a


opening into manifold assembly


85




a


for distributing heated air to nozzle array


97




b.


In this preferred embodiment, each blower


54




a,




55




a


is capable of producing an output of 15,000 CFM and is driven by a respective electric motor


120


having a preferable power rating of 5 hp. Each heater unit


80




a


is constituted by a 15 kW unit which has an associated low pressure drop. This overall arrangement functions to provide a preferred static pressure head of 0.85 in. H


2


O. Although not clearly shown in the drawings, each of the comers for enclosure


105


is preferably reinforced with steel angle iron or the like.




As clearly shown in

FIG. 5

, enclosure


105


can simply be subdivided by suitable, preferably sheet metal walls to define upper and lower, distinct manifold sections


88




a


and


89




a


of overall manifold assembly


85




a,


as well as to define ducting channels


57




a,




58




a,


and


59




a,




60




a


which function to recirculate air in a manner directly corresponding to return lines


57


-


60


in the embodiment shown and described above with reference to

FIGS. 1-3

. In the fall scale production model, the distances for nozzle spacing, width and height relative to each sheet


35


are carried over from the established reduced scale testing. However, in this embodiment, it is actually preferred to accommodate a total of four (4) sheets


35


simultaneously within the pre-heating units


12




a


and


12




b.


Also preferably incorporated as part of the invention is a system controller generally indicated at


128


in FIG.


7


. In the most preferred form of the invention, a separate system controller is provided for each of the upper and lower blower/heater arrangements. In addition, each system controller


128


preferably includes a PID controller


130


which receives input signals related to the current drawn by a respective blower as indicated at


132


, the current drawn by a respective heater as indicated at


134


and, at


136


, a temperature signal representative of the sensed temperature adjacent at least one of the nozzles


97


as indicated by the presence of a thermistor


138


(see

FIG. 3

or


5


).




In essence, since the individual temperatures of sheets


35


can fluctuate substantially given the particular season of the year and also the environment in which they are stored within stack


9


, the rate at which each blower


54




a,




55




a


is driven and the amount of current supplied to each heating unit


80




a


can be controlled to assure the desired output temperature of the air impinged upon each sheet


35


. In order to reduce the influence of blower assembly heat, the target sheet temperature has been selected substantially above normal ambient temperatures. Under conditions of high ambient temperature and high sheet temperature, it may be come necessary to mitigate the effects of heating due to the inherent inefficiencies of the blower units. While it is recognized that a cooling coil may be placed in the airstream, such as in the return lines or directly in the blowers adjacent to the heater elements, it is desirable to avoid both the initial and operating expenses of such a chiller arrangement. In the most preferred form of the invention, the heat introduced by the blower units is addressed by lowering the rate at which each blower is driven. An alternative method to mitigate the heating effects of the blower assemblies is to place a motor actuated damper on one or more of the return lines. For instance, note FIG.


3


and the presence of damper


150


which is situated so that, when fully opened, damper


150


allows free entry of ambient air into the return lines


57


-


60


. Correspondingly, the PID controller would have an additional output to control damper(s)


150


as indicated in phantom in FIG.


7


.




In any event, as indicated above, it is desirable to provide heated air at a rate and temperature which will uniformly heat the sheet


35


, i.e., to within a 5° F. differential throughout the entire sheet


35


. Knowing the desired resulting sheet temperature, the varying operating conditions can be accounted for through each controller


130


based on the blower current inputted at


132


, the current inputted at


134


and the sensed temperature provided at


136


, assuming a constant speed for conveyor


39


. However, conveyor speed could also constitute an input to be further regulated by controller


130


if desired. Therefore, each controller


130


will output a desired current to both a respective blower


54




a,




54




b


and heater


80




a


to maintain the desired airflow rate and temperature. Any problems in maintaining this operation will result in the activation of indicator lights and/or alarms at signalling device


140


.




Although described with respect to a preferred embodiment of the invention, it should be readily understood that various changes and/or modifications can be made to the invention without departing from the spirit thereof. In particular, it should be readily recognized that the invention deals with creating a substantially uniform temperature of each sheet


35


for delivery to the thermoforming device


15


. Therefore, although the most preferred form of the invention utilizes a pre-heating unit to achieve this result, the sheets


35


could also be cooled to a uniform temperature for delivery to the thermoforming device


15


in accordance with the invention. In addition, the temperature and flow rate of the air, the configuration of nozzles


97


, the material and size for sheets


35


and the temperature control duration associated with the present invention can be altered depending on various factors, including the particular product to be formed, a desired production rate, etc., without departing from the spirit of the invention. Furthermore, although upper and lower manifold sections with separate blowers are provided in the preferred embodiments described, it should be recognized that a single, annular manifold assembly with one or more blowers could be utilized without departing from the spirit of the invention. Therefore, the particular construction and operation of the temperature control unit can be varied while still achieving uniform temperature throughout a sheet preferably by an impinging air flow regardless of the initial temperature of the various sheets entering the temperature control unit in accordance with the present invention. In any event, the invention is only intended to be limited by the scope of the following claims.



Claims
  • 1. An apparatus for creating a substantially uniform temperature across a sheet of plastic prior to delivery of the sheet to an appliance liner thermoforming device comprising:a conveying mechanism for transporting a plastic sheet into a position wherein a fluid medium having a temperature is placed in contact with opposing surface portions of the plastic sheet; and at least one temperature control unit for regulating the temperature of the fluid medium so that the plastic sheet is brought to a substantially uniform temperature prior to delivery to the appliance liner thermoformed device.
  • 2. The apparatus according to claim 1, wherein the substantially uniform temperature constitutes a temperature differential across the entire sheet of less than 5° F.
  • 3. The apparatus according to claim 1, wherein the at least one temperature control unit is adapted to heat the fluid medium to approximately 130°-140° F.
  • 4. The apparatus according to claim 1, further comprising:an enclosure including a longitudinally extending through passage, said conveying mechanism transporting the sheet through the enclosure; a manifold assembly including first and second manifold sections adapted to face opposing surface portions of a sheet transported through the enclosure; and at least one blower for developing a flow of air, which constitutes the fluid medium, into the first and second manifold sections, with the air to be distributed to flow upon the opposing surface portions.
  • 5. The apparatus according to claim 4, wherein each of the first and second manifold sections includes a plurality of spaced nozzles directed toward the opposing surface portions, with the flow of air from the at least one blower being directed through the nozzles to impinge upon the opposing surface portions.
  • 6. The apparatus according to claim 5, wherein the nozzles extend transversely across and are longitudinally spaced within the passage.
  • 7. The apparatus according to claim 5, wherein the plurality of nozzles are spaced approximately 76 mm (3 inches) from a sheet transported through the passage.
  • 8. The apparatus according to claim 4, wherein the manifold assembly further includes recirculation ducting fluidly connecting the passage with an inlet of the at least one blower.
  • 9. The apparatus according to claim 8, wherein the at least one blower includes first and second blowers, with the first blower directing air into the first manifold section and the second blower directing air into the second manifold section.
  • 10. The apparatus according to claim 9, wherein each of the first and second blowers develops an air flow rate of approximately 15,000 CFM.
  • 11. The apparatus according to claim 4, wherein the passage is adapted to receive a sheet having a thickness in the order of 5 mm (0.20 inches) to form an appliance liner having a depth of approximately 61 cm (2 feet).
  • 12. The apparatus according to claim 4, wherein the apparatus has an operating static pressure in the range of 0.7-0.9 in. H2O.
  • 13. The apparatus according to claim 4, further comprising, in combination: a system controller for regulating at least one of the blower and the temperature control unit based on sensed operating parameters of said apparatus.
  • 14. The apparatus according to claim 4, wherein the at least one blower constitutes a variable speed blower, with said temperature control unit regulating an operating speed of the variable speed blower.
  • 15. The apparatus according to claim 4, further comprising: a damper unit for introducing a desired amount of ambient air into said manifold assembly.
  • 16. In an appliance liner forming system wherein a sheet of plastic is thermoformed in an appliance liner thermoforming device into an appliance liner, an apparatus for creating a substantially uniform temperature across the sheet of plastic prior to delivery of the sheet to the appliance liner thermoforming device comprising:a conveying mechanism for transporting the plastic sheet into a position wherein a fluid medium, having a temperature, is placed in contact with opposing surface portions of the plastic sheet; and control means for regulating the temperature of the fluid medium such that the plastic sheet is brought to a substantially uniform temperature prior to delivery to the appliance liner thermoforming device.
  • 17. In an appliance liner forming system incorporating a thermoforming device including means for thermoforming a sheet of plastic into an appliance liner, an apparatus for creating a substantially uniform temperature across the sheet of plastic prior to delivery of the sheet to the thermoforming device comprising:a conveying mechanism for transporting the plastic sheet; means for directing a fluid medium, having a temperature, into contact with opposing surface portions of the plastic sheet; and control means for regulating the temperature of the fluid medium to establish a substantially uniform temperature for the sheet prior to delivery of the sheet to the appliance liner thermoforming device.
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