This application is entitled to and hereby claims the priority to co pending U.S. application Serial No. 15/293,927, filed October 14, 2016.

TECHNICAL FIELD

The present disclosure generally relates to pellet dryer and more particularly relates to a pellet dryer with a pellet outlet.

BACKGROUND

Centrifugal pellet dryers of both vertical and horizontal type are well known in the state of the art and include an outer housing, a screen oriented in the housing and a bladed rotor mounted in the screen for moving a slurry of fluid and pellets within the screen, to enable a discharge of fluid through the screen. A slurry inlet is provided along with two outlets for fluid and dried pellets. Centrifugal pellet dryers of the vertical type are disclosed in U.S. Pat. Nos . 3,458,945; 4,565,015; 4,896,435; 5,245,347 commonly owned by Gala Industries, Inc. In the operation of such dryers an exhaust fan as a blower at the upper end of the housing communicates directly with the interior of the dryer with the dryer rotor shaft extending upwardly from the dryer and being connected with the bladed rotor, so that the fan of the blower and the bladed rotor are driven by the same motor. The blower produces a countercurrent flow of drying air through the pellet discharge outlet duct. One problem of such pellet dryer is to optimize the pellet discharge through said outlet duct since a varying amount of pellets are bounced back in an transition area between the end of the screen and an outlet opening in a side surface of the inner wall close to the vertical end of the housing in respect to the main rotational speed of the motor of the bladed rotor optimized in respect to an upward accelerating of the pellets by the blades of the rotor, which dictates contemporary the amount of the countercurrent flow of drying air provided by the main blower in a countercurrent direction to the upward accelerated pellets which is difficult to balance in an optimized way for both, the optimization of upward acceleration of pellets and optimization of drying the pellets by an optimized air flow. Actually there is an amount of pellets which has to be recycled since the pellets have not reached the outlet opening close to the vertical end of the housing .

SUMMARY OF THE INVENTION

An object of the present invention is to improve the output of dried pellets of a pellet dryer of vertical type. Another object of the present invention is to avoid any stacking of pieces of pellets in a transition region between the end of the screen and an outlet opening in a side surface of the inner wall close to the vertical end of the housing followed by an agglomeration of pellets in the transition region for pellets from the screen toward a pellet outlet of the pellet dryer. A further object of the invention is to minimize the bouncing back of pellets into the drying area of the pellet dryer. Still another object is to provide a centrifugal pellet dryer in accordance with the preceding objects, so that this pellet dryer does not require any additional floor space, any additional supporting structure thereby reducing overall cost. A further object of the invention is to decrease maintenance cost and elongate maintenance intervals of the pellet dryer. Still a further object of the invention is to provide an additional guidance of counter-current air in counter direction of the main flowing direction of the pellets, in particular counter-current of air entering a pellet outlet to be passed downward in the dryer housing. These objects are solved by the subject matter of independent claim 1 and features of dependent clams. Furthermore, other desirable features and characteristics of the present invention will be apparent from the subsequent detailed description and the appended claims, taken in conjunction with the accompanying drawings and the foregoing technical field and background.

In accordance with an exemplary embodiment a pellet dryer comprising: a housing, an inlet for feeding fluid flushed pellets and two separate outlets for discharging the dried pellets and the fluid, a vertical bladed rotor for centrifugal separation of the fluid by a screen surrounding the bladed rotor and for a vertical acceleration and separation of the pellets by the blades of the rotor, wherein the outlet for dried pellets is provided above the upper end of the screen comprising an opening toward the top of the housing at an inner cylindrical side surface of the housing distant from the screen in a radially outward direction and an outlet duct connected to the opening, wherein the outlet duct is attached to the opening by an acute angle in respect to the central axis of the rotor, wherein an outlet guidance plate of curved shape is provided close to the top of the housing inside the housing in a transition region between the end of the screen and the outlet duct wherein the outlet guidance plate extents from a central position above the screen through the outlet opening into the outlet duct.

SHORT DESCRIPTION OF THE DRAWINGS

The present disclosure will be hereafter be described in conjunction with the following drawing figures, wherein like numerals denote like elements, and wherein: FIG, 1 is a cross sectional view of the pellet dryer according to an embodiment of the invention;

FIG. 2 is a side view of the pellet dryer according to the embodiment of the invention shown in FIG. 1. DETAILED DESCRIPTION OF THE PREFERED EMPODIMENTS

Referring now to the drawings FIGS, 1 and 2 illustrate two different views of a centrifugal pellet dryer 1 of the vertical type according to an embodiment of the invention. The pellet dryer 1 comprises a vertical housing 2 of generally cylindrical configuration and supported in any suitable manner. A slurry of pellets and fluid enters the pellet dryer 1 through a slurry inlet 30 shown in FIG. 2 for feeding fluid flushed pellets and impinges against a fluid separator 31 in the form of an inclined and partially screened tube 32 which deflects the pellets with most of the fluid passing through the screen 33 of the tube 32 and out through a first outlet 3 of the housing 2 for the fluid. The remaining moisture and fluid is separated from the pellets by centrifugal force applied to the remaining moisture and fluid by a vertically arranged bladed rotor 4 and a separating central screen 5 shown in FIG. 1 surrounding the bladed rotor 4 inside the housing 2. Blades 6 of the bladed rotor 4 accelerate the pellets upwards contrary to a continuously drying downwards air flow of a suction blower 18 attached to an lateral outer top 15 of the housing 2, so that the dried pellets could be accelerated to a second outlet 10 close to an inner top 9 of the housing 2 for discharging the dried pellets whilst the centrifugally separated fluid is discharged through the screen 5 toward outside the screen 5 to the first outlet 3 of the housing 2. The bladed rotor 4 is driven by one motor 11 attached centrally on the outer top 8 of the housing 2 comprising one central axis 12 for the bladed rotor 4 to provide a rotational speed.

As shown in FIG. 2 an outlet guidance plate 40 of curved shape is provided close to the inner top 9 of the housing 2 inside the housing in a transition region 41 between the end 37 of the screen 5 shown in FIG.l and the outlet duct 36 wherein the outlet guidance plate 40 extents from a central position above the screen 5 through the outlet opening 35 into the outlet duct 36. The guidance plate 40 is provided at the second outlet 10 of the housing 2 for dried pellets above an upper end 37 of the screen 5. Since an outlet duct 36 is attached to the opening 35 by an acute angle β in respect to the vertical central axis 12 of the rotor 4 the guidance plate 40 smoothes the transition region 41 between the end 37 of the screen 5 and the outlet duct 36 for guiding the pellets smoothly toward the outlet duct 36.

Accordingly any stacking of pieces of pellets in the transition region 41 between the end 37 of the screen 5 and an outlet opening 35 in a side surface 16 of the inner wall close to the vertical end of the housing 2 followed by an agglomeration of pellets in the transition range 41 for pellets from the screen 5 toward the pellet outlet duct 36 of the pellet dryer 1 is avoided. Further, the bouncing back of pellets into the drying area of the pellet dryer 1 is minimized. Furthermore, this pellet dryer 1 does not require any additional floor space, any additional supporting structure thereby reducing overall cost. Still further, the maintenance intervals of the pellet dryer 1 can be elongated and accordingly the maintenance cost will decrease. The outlet guiding plate furthermore influences the direction of flow of the counter current of air entering into the outlet duct 36 and moving further into the dryer housing 2.

In another embodiment of the invention the cross section of the outlet guidance plate 40 in the length direction comprises in a center part a flattened contour and toward the outlet duct 36 a gradually increasing curved profile. This gradually increasing curved profile toward the outlet duct 36 supports an avoidance on bouncing back of pellets toward the drying region of the pellet dryer 1.

In a further embodiment of the invention the cross section of the outlet guidance plate 40 in width direction comprises in a center part a flattened contour and toward the outlet opening 35 a smoothly curved profile. This smoothly curved profile toward the outlet opening 35 supports an avoidance on bouncing back of pellets toward the drying region of the pellet dryer 1.

Furthermore, the outlet guidance plate 40 is made of a metal alloy especially aluminum bronze which is resistive against corrosion. Another embodiment of the invention applies stainless steel for the outlet guidance plate 40 which is resistive against corrosion and erosion,

The outlet guidance plate 40 can be equipped with a wear protection at least on the inner concave surface thereof. Furthermore, the outlet guidance plate 40 can be fixed by quick disconnect features, allowing for easy exchange thereof. The foregoing detailed description of embodiments of the invention has been presented for purposes of illustration and description, but it is not intended to be exhaustive or limited to the invention as disclosed. Many modifications and variations will be apparent to those of ordinary skill in the art without departing from the scope and spirit of the invention defined by the claims, which includes known equivalents and foreseeable equivalents at the time of filing the application. The embodiments were chosen and described in order to best explain the principles of the invention and then practical application, and to enable others of ordinary skill in the art to understand the invention for various embodiments with various modifications as are suited to the particular use contemplated.

LIST OF REFERENCE SIGNS

1 centrifugal pellet dryer

2 vertical housing

3 first outlet of housing for fluid

4 bladed rotor

5 central screen

6 blades of bladed rotor

7 sleeve

8 outer top of housing

9 inner top of housing

10 second outlet of housing for pellets

11 motor

12 central axis of the rotor

13 housing for rotor coupling

16 inner surface of the housing

30 slurry inlet

31 separator

32 partially screened tube

33 inclined screen of the tube

35 outlet opening

36 outlet duct of pellets

37 end of screen

40 guidance plate

41 transition region

β acute angle of outlet duct