The present invention relates generally to deep-fat fryers and, more particularly, to a deep-fat fryer heat exchange system.
A typical deep-fat fryer will include a fryer vat containing a heated bath of cooking oil. The cooking oil is adapted to receive baskets of food products such that the food products will be immersed within and cooked by the heated cooking oil. Such fryers include a heat exchanger, which may take the form of one or more in vat heat exchange tubes through which combusted gases pass to deliver heat to the oil through the tube walls.
It would be desirable to provide a fryer and associated heat exchange tube and system that effectively and efficiently heats oil in the fryer vat.
In one aspect, a baffle is utilized as primary heat transfer device installed within one or more burner tubes of a fryer. The baffle(s) restrict the flow of heated combustion gases deflecting the gases within the tube(s) which are in direct contact with the cooking substrate (oil). The objective is to increase the thermal transfer of the combustion gas heat energy into the tube walls to increase the cooking efficiency of the fryer. The baffle configuration may include multi angled profiled fins which also have air pass holes on each fin to enhance airflow and maximize heat transfer.
In another aspect, a fryer unit includes a fryer vat defining a volume for receiving oil to be heated for cooking. A heating system is provided for heating oil in the volume. The heating system includes at least one gaseous fuel burner and at least one heat exchange tube, the heat exchange tube passing through the volume such that an external surface of the heat exchange tube will be in contact with oil in the volume. The heat exchange tube defines an internal passage through which heated combustion gases of the gaseous fuel burner can pass, and a baffle is positioned within the internal passage for enhancing heat transfer from the combustion gases to the external surface of the heat exchange tube.
In one implementation the fryer vat includes three burner tubes and there is one baffle per burner tube.
In one implementation the baffle is inserted from the rear of the fryer unit or rear of the baffle tube, which baffle tube extend from a front side of the vat to a rear side of the vat. Two fingers/flanges on the rear of the baffle catch the rear of the burner tube and a front finger/flange is pulled over to catch a flange face on the front of the burner tube.
In one implementation, flow through the tube is primarily a spiral throughout the tube.
In one implementation, each burner tube profile is oval-shaped or elongated slot-shaped with end curves and linear side sections, and the longer dimension of the profile is oriented substantially vertically in the vat. Each burner may be formed by two like burner segments, each with a curved end and a straight side, that are welded together.
In one implementation each baffle has a plurality of fin sets arranged sequentially along a flow path of the internal passage of the heat exchange tube. The fin sets may include a progressively increasing angle of departure from an elongated axis of the heat exchange tube. At least one or more initial sets of fins may be angled in a direction with the flow direction from front to rear of the heat exchange tube. At least one or more downstream sets of fins may be oriented perpendicular to the flow direction.
In one implementation each baffle has a plurality of fin sets arranged sequentially along a flow path of the internal passage of the heat exchange tube. Each fin set may include an upper fin and a lower fin, both of which angle away from a central plate portion of the baffle. Each fin set may further include a left fin and a right fin, each of which departs from a common axial position along a length of the central plate portion. In one implementation, each fin set includes one upper fin at one side of the central plate portion and one lower fin at an opposite side of the plate portion.
In one implementation each baffle is formed by a single piece of plate material cut/stamped and bent to final baffle shape.
In one implementation a bottom edge part of a central plate portion of the baffle contacts a lower internal surface of the internal passage of the heat exchange tube.
Referring to
The fryer housing structure to which the vat is attached may include edge portions extending upward from the right and left sides of the vat, a front portion 15 extending laterally forward of the front of the vat to an upwardly extending front edge portion, and a back portion including an upwardly extending rear wall 34 formed by part of the chimney shell 32. Here, the rear wall 34 extends upward to a height well above the height of the left, right and front edge portions. Additional housing structure and/or support frame structure may be associated with the bottom portion of the fryer vat as well.
The oil heating system 20 includes one or more (here three) heat exchange tubes 22, each with an associated gaseous fuel burner 24. The heat exchange tubes 22 extend from a front side of the fryer vat to a read side of the fryer vat, and may be integrated with the fryer vat as a unit, such as where a front edge of each heat exchange tube is welded to the front wall of the fryer vat and a rear edge of each heat exchange tube is welded to the rear wall of the fryer vat. The heat exchange tubes 22 are immersed in oil within the vat and therefore heat exchange occurs between combustion gasses in the heat exchange tubes and the oil in the vat through the walls of heat exchange tubes. A burner casing 26 covers the burners. During frying operations, when oil in the vat is being heated, gaseous fuel is fed to the burners and combusted at the front of each heat exchange tube, and the combustion gases then traverse the length of the tubes (e.g., from left to right in the side view of
Referring to
As shown, in the case of each fin set, one of the upper fin or the lower fin extends to one side of the central plate portion 42 and the other of the upper fin or the lower fin extends to the other side of the central plate portion 42. Here, fin extension direction alternates from opening to opening (i.e., the upper fin of any given opening extends to one side of the central plate portion 42 but the upper fin(s) of the adjacent opening(s) in the opening sequence extend to the other side of the central plate portion, and similarly for the lower fins).
Generally, fin sets toward the rear of the baffle plate structure 52 (e.g., fin sets 46E and 46F) depart from the plane or axis 52 defined by the central plate structure 52 with a higher departure angle than fin sets toward the front of the plate structure 52 (e.g., fin sets 46A and 46B). Here, fin sets 46A and 46B have the same angle of departure angle (e.g., about forty-five degrees, such as between thirty-five and fifty degrees), fin sets 46C-46E have the same departure angle (e.g., about seventy degrees, such as between sixty-five degrees and seventy-five degrees) and fin set 46F has the highest departure angle (e.g., about eight degrees, such as between seventy-five and eighty-five degrees). Here, an additional fin set 46G is located at the rear edge of the central plate structure 52 and includes fins with a departure angle that is the same as that of fin set 46F.
In the illustrated embodiment, the baffles 40 are inserted into the respective tubes 22 from a rear of the tube. In this regarding, each baffle 40 includes an upper finger or flange 56 and a lower finger or flange 58 that extend laterally from the rear edge of the central plate 52. Each finger or flange extends in a direction substantially perpendicular to the central plate plane or axis 52 and includes a respective end segment 60, 62 that is turned forward to run substantially parallel to the plane or axis 52. As best seen in
As mentioned above, the baffle 40 of each tube is configured to promote a flow within the tube that enhances heat exchange from the combustion gases to the oil within the vat. With the baffle configuration described above, combustion gas flow through the heat exchange tube 22 is primarily a spiral flow throughout the heat exchange tube. In this regard, reference is made to
It is to be clearly understood that the above description is intended by way of illustration and example only, is not intended to be taken by way of limitation, and that other changes and modifications are possible.
This application claims the benefit of U.S. provisional application No. 62/579,410, filed Oct. 31, 2017, which is incorporated herein by reference in its entirety.
Number | Date | Country | |
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62579410 | Oct 2017 | US |