as noted above , raw licorice extract is generally received by a licorice processor in 5 to 10 kilogram blocks . this licorice extract generally arrives with varying glycyrrhizin levels , typically ranging from about 12 % to about 30 %, depending upon the geographic area from which it was received . referring to fig1 in accordance with the present invention , the raw extract is preferably reduced to randomly sized particles , typically less than about one inch ( 1 &# 34 ;) [ 25 . 4 mm ] in diameter . ( such reduction facilitates the blending of the licorice extract to achieve a desired flavor pattern or glycyrrhizin level .) this is accomplishes by placing the raw extract blocks into , for example , a lump breaker 2 or a fitz mill . preferably , the extract lumps are then further reduced in size by the use of a commercial blender or mixer 4 to achieve a more homogeneous blend . following blending , the mixture is transferred at a substantially fixed velocity to an extruder assembly 6 via a cleated belt or the like ( not shown ). in accordance with a preferred embodiment of the invention , the extruder assembly 6 is a bausano tr2 / 140 / 15 counter - rotating twin screw extruder . however , it is believed that one of skill in the art could successfully employ other extruder assemblies including co - rotating twin screw extruders , single screw or ram extruders . the extruder temperature is regulated to maintain the temperature of the licorice extract at less than about 80 ° c . throughout substantially the entire extrusion process . at the end of the main extruder assembly 6 , a conditioning head 8 is preferably employed to allow the licorice extract to cool to about 70 ° c .± 1 ° c . before being forced through the die 10 . the die 10 preferably has one or more orifices ranging in diameter from about 2 mm to about 8 mm . the throughput of the extruder 6 varies with the size of the die orifice , with a typical value of about 150 kg / hr when a 5 mm orifice is employed . upon exiting the die 10 , the extruded licorice extract is picked up by a conditioning belt 12 , preferably in the form of a perforated conveyor . the extruded extract is cooled on the conditioning belt 12 by exposure to ambient or desiccated air to a preferred temperature in the range of about 34 ° c . to about 41 ° c . the conditioning belt 12 carries the extruded extract to a cutting device 14 , preferably of the guillotine variety . the cutter 14 severs the extruded extract into pieces with preferably ranging from about 2 mm to about 150 mm . if the temperature of the extruded extract under a guillotine cutter is in excess of 41 ° c ., it is likely that no cut will be achieved . if the temperature of the extruded extract under a guillotine cutter is below 34 ° c ., it is likely that fracturing will occur such that fines and other irregularly shaped pieces will be created . after cutting , the pieces of licorice extract are placed in perforated holding trays 16 for curing . they are maintained in these trays , in moving , conditioned air ( i . e ., air which is temperature and humidity controlled ), for a period of time in excess of 12 hours , preferably for a period of time between 5 and 7 days . in this regard , either ambient or desiccated air may be used to cure the pieces , depending upon the current atmospheric conditions and the composition of the licorice extract . if the licorice extract is insufficiently cured , it will block or otherwise coalesce as with licorice extract prepared in accordance with prior art processes . after curing , the severed pieces are sorted as to size by passing the pieces through a sorting assembly 18 such as a vibratory sifter . those skilled in the art will recognize that the pieces can also be sized by other means . the cured licorice extract product is ultimately packaged via conventional packaging equipment 20 in multi - walled paper bags , polylined corrugated boxes , fiber drums , bulk totes or the like for shipment to makers of licorice candy , cigarettes , pharmaceuticals etc . in accordance with the present invention , the licorice extract remains free - flowing under virtually all regularly encountered environmental conditions , including extreme heat and humidity . this is in a manner wholly distinct from that of any prior processed licorice extract . approximately 250 pounds of block - type licorice having glycyrrhizin levels in the range of about 12 - 30 %, by weight , was supplied to a fitz mill where it was reduced to randomly shaped particles having a size of less than 1 inch ( 25 . 4 mm ) in diameter . the treated licorice was then supplied to a commercial blender where it was thoroughly mixed and then loaded directly into the holding hopper of a bausano tr2 / 140 / 15 counter - rotating twin screw extruder . the extruder assembly was set at a throughput speed of approximately 150 kg / hr and further was adjusted to maintain the licorice extract at a temperature not to exceed 80 ° c . a conditioning head was attached to the end of the main extruder assembly , to cool the extruded licorice to a temperature of approximately 70 ° c . a 5 mm diameter die hole was employed in the die through which the extruded licorice extract was forced . the extruded licorice was carried from the die by a conditioning belt where it was exposed to a stream of moving air which further cooled the extract to a temperature of about 35 °- 40 ° c . a rotary cutter was then employed to reduce the licorice to pieces having lengths of approximately 2 mm - 15 mm . the resulting licorice pieces were sorted as to size using a vibratory sifting bed and then stored in perforated trays to cure by exposure to dehumidified air for a period of time of at least 12 hours . following packaging in polylined corrugated boxes , and storage under normal warehouse conditions , the licorice was inspected for any signs of blocking , caking , or other conditions which would impede its flowability . none was found . in accordance with the present invention , processed licorice extract does not adhere or cake to itself under ordinary storage conditions . moreover , the invention provides an effective means by which a normally sticky , and difficult to handle product can be quickly , easily , and economically converted to a flowable food product while simultaneously preserving its flavor and other essential characteristics . although the present invention has been shown and described with reference to particular equipment , components and processing conditions , one of skill in the art may deviate from these particular elements without departing from the spirit or intent of the invention .
a free - flowing , non - blocking licorice extract is achieved by breaking raw licorice extract into pieces , transferring the pieces of licorice extract to an extruder assembly , processing the licorice extract through said extruder assembly in accordance with a predetermined temperature profile , forcing the licorice extract through a die , cooling the extruded licorice extract to within a predetermined temperature range , severing the extruded licorice extract into pieces of predetermined length and curing the cut pieces for period of time in excess of 12 hours by exposing the cut pieces to moving air .