The present invention relates to a rotary steam blancher for cooking food product, and in particular, a steam recirculation system for maintaining a uniform temperature pattern within the blancher.
In mass processing of food product, food product is often heated by cooking or blanching the food product in a food processing apparatus having a tank holding a heat transfer medium into which the food product is immersed. After cooking or blanching of the food product occurs, the food product is cooled or chilled by immersing the food product in a cool transfer medium so that the food product may be packaged, stored and/or shipped.
In a rotary blancher, food product is introduced into an inlet end of an elongate drum, which is rotatably mounted in a generally cylindrical, open-top tank. The tank is fitted with a cover for minimizing heat loss and for enclosing the drum for safety reasons, and which can be opened for maintenance and cleaning. The drum includes an auger therein for advancing food product from the inlet end of the drum to an outlet end of the drum and through the heat transfer medium.
Typically, rotary blanchers use hot water, or a combination of hot water injected with steam as the heat transfer medium. Until recently, it has been impractical to blanch or cook only using steam because substantial steam leakage from the blancher would be too costly. Current seals prevent steam leakage through sidewall and endwall interfaces between the cover and the tank, openings for the drum journals in the tank and tank cover endwalls, and the drum inlet and outlet openings. However, steam within the rotary blancher is not evenly distributed throughout the blancher, which results in a non-uniform temperature pattern within the blancher and inefficient or non-uniform heat transfer to the food product. Further, as compared to rotary hot water blanchers, high density pockets of food product develop in rotary steam blanchers and draw a disproportionate amount of heat from the heat transfer medium, which results in non-uniform heat transfer to the food product.
In one embodiment, the invention provides a food processing apparatus including a tank defining a heat compartment having an inlet end for receiving food product and an outlet end for discharging food product, and an inlet for introducing a non-liquid heat transfer medium to the heat compartment. A drum is rotatably mounted within the inner compartment and has an auger therein. The auger advances food product within the tank from the inlet end toward the outlet end and through the non-liquid heat transfer medium. The food processing apparatus also includes a recirculation mechanism configured and adapted to create a uniform temperature pattern within the heat compartment and to transfer non-liquid heat transfer medium from the outlet end of the heat compartment to the inlet end of the heat compartment.
In another embodiment, the invention provides a rotary cooker and cooler including a tank having an inlet end and a discharge end, a baffle that divides the tank into a first compartment and a second compartment, a first inlet for introducing a non-liquid heat transfer medium to the first compartment, and a second inlet for introducing a cool transfer medium to the second compartment. A first drum is rotatably mounted within the first compartment of the tank and has an auger therein, wherein the auger advances food product from the inlet end of the tank toward the baffle and through the non-liquid heat transfer medium. A second drum is rotatably mounted within the second compartment of the tank, and has an auger therein, wherein the auger advances food product toward the discharge end the tank and through the cool transfer medium. The rotary cooker and cooler also includes a recirculation mechanism configured and adapted to create a uniform temperature pattern within the first compartment and to transfer non-liquid heat transfer medium from an outlet end of the first compartment to an inlet end of the first compartment.
In yet another embodiment, the invention provides a steam recirculation system for use with a food processing apparatus including a tank and a cover defining a first compartment having an inlet end for receiving food product and an outlet end for discharging food product, and an inlet for introducing steam to the first compartment. The steam recirculation system includes a conduit positioned external to the tank and defining a passageway. The conduit has a first end in fluid communication with the outlet end of the first compartment and a second end in fluid communication with the inlet end of the heat compartment. A fan is positioned within the conduit to facilitate transfer of steam from the outlet end to the inlet end.
Other aspects of the invention will become apparent by consideration of the detailed description and accompanying drawings.
Before any embodiments of the invention are explained in detail, it is to be understood that the invention is not limited in its application to the details of construction and the arrangement of components set forth in the following description or illustrated in the following drawings. The invention is capable of other embodiments and of being practiced or of being carried out in various ways. Also, it is to be understood that the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting. The use of “including,” “comprising,” or “having” and variations thereof herein is meant to encompass the items listed thereafter and equivalents thereof as well as additional items. Unless specified or limited otherwise, the terms “mounted,” “connected,” “supported,” and “coupled” and variations thereof are used broadly and encompass both direct and indirect mountings, connections, supports, and couplings. Further, “connected” and “coupled” are not restricted to physical or mechanical connections or couplings.
The rotary blancher 10 includes an open-top tank 26 that is supported by a frame 30 having legs 34 that rest upon a support surface and space the tank 26 above the support surface. The tank 26 defines in part an inner compartment 38 of the blancher 10. The tank 26 is preferably made of stainless steel or another suitable material for food processing applications. The tank 26 includes an inlet endwall 42 at the inlet end 22 of the tank 26 and an outlet endwall (not shown) at the outlet end 18 of the tank 26. Each endwall defines an arcuate or semicircular opening 46 that communicates with the inner compartment 38 of the tank 26.
A drum 50 is rotatably mounted in the inner compartment 38 of the tank 26 and is configured to transport food product received in the blancher 10 from the inlet end 22 to the outlet end 26 of the tank 26. The drum 50 includes an inlet end (not shown) proximate the inlet opening 46 of the tank 26 and an outlet end 54 proximate the outlet opening (not shown) of the tank 26 with a generally cylindrical and perforate sidewall 58 that substantially extends between the drum ends. The perforations in the sidewall 58 of the drum 50 consist of a plurality of small diameter bores that extend completely through the sidewall 58 to allow steam to pass from the inner compartment 38, through the sidewall 58 and into the drum 50. In another embodiment, the drum 50 is formed from a wire screen.
A helical auger 62 is disposed within the drum 50 and rotates with the drum 50 for advancing food product from the inlet end 22 of the tank 26 toward the outlet end 18 of the tank 26. To further support the auger 62, the inner compartment 38 carries a trunnion (not shown). The auger 62 includes a plurality of axially spaced apart and interconnected flights 66 that spiral substantially the length of the interior of the drum 50. As the auger 62 rotates, the flights 66 move food product from the inlet end (not shown) of the drum 50 to the outlet end 54 of the drum 50. Typically, the auger 62 rotates with the drum 50, however, in another embodiment, the auger 62 may rotate relative to or independently from the drum 50. In the illustrated embodiment, the auger 62 is of coreless construction, however, in further embodiments, the auger flights 66 can be carried by a support core. The drum 50 includes circumferentially spaced apart elongate struts 70 that extend from the inlet end to the outlet end of the drum 50 to help strengthen and rigidify the drum 50 and the respective auger 62. Portions of the outer radial peripheral edge of at least some of the auger flights 66 are coupled to the support struts 70, which provide support to the auger 62 from the support struts 70, the drum 50 and end plates (not shown) of the drum.
An elongated vaulted cover 74 mates with the tank 26 and covers the tank 26 to substantially enclose the inner compartment 38 and provide an enclosure for the steam. In the illustrated embodiment, the cover 74 includes an inlet endwall 78 for positioning at the inlet end 22 of the tank 26 and an outlet endwall (not shown) for positioning at the outlet end 18 of the tank 26. Each cover endwall includes an arcuate or semicircular opening 82 that communicates with the inner compartment 38 and is positioned above the opening 46 in the respective tank endwall. The cover 74 of the tank 26 is generally attached to the tank 26 in such a manner as to allow the cover 74 to move relative to the tank 26 and permit access to the inner compartment 38 of the blancher 10. In one embodiment, the cover 74 is hingedly connected to the tank 26 so the cover 74 can be swung away from the drum 50 to permit access to the drum 50 and the inner compartment 38.
Steam is supplied to the inner compartment 38 of the tank 26 from a supply source (not shown) by manifolds 86 disposed in the inner compartment 38, and steam is supplied to each manifold 86 from a steam header. Generally, steam is delivered to the manifolds 86 under the control or one or more valves 88 (
The rotary blancher 10 includes the steam recirculation system 14 for transferring steam from the outlet end 18 of the tank 26 to the inlet end 22 of the tank 26. Although a mixture of steam and air is supplied to the inner compartment 38, because steam is lighter than air, primarily steam is recirculated through the steam recirculation system 14. Recirculation of steam from one end of the tank 26 to another creates an even distribution of steam throughout the blancher 10 and maintains a substantially uniform temperature throughout the blancher 10. The steam recirculation system 14 constantly agitates and stirs the steam and air mixture within the inner compartment 38 and prevents localized cool spots within the tank 26. Uniformity of temperature within the blancher 10 improves efficiency of cooking food product as greater masses of food product can be processed.
Referring to
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The rotary steam blancher 10 has a short blanch cycle time of approximately 5 minutes, therefore, it is important for the temperature sensors 138, 142 to obtain accurate, instantaneous temperature readings within the inner compartment 38. In conventional rotary blanchers, high density areas of food product gather at the bottom of the drum, which absorb a disproportional amount of heat from the steam and results in non-uniform heat transfer to the food product. The present invention rotary blancher 10 includes a plurality of lifters 146 to agitate food product and break up the high density areas of food product within the drum 50. Thereby, more uniform heat transfer to food product occurs.
Referring to the rotary blancher 10 in
In the present embodiment steam rotary blancher 10, the steam recirculation system 14, the temperature sensors 138, 142, and the lifters 146 work together to ensure a uniform heat transfer to food product. The steam recirculation system 14 transfers steam from the outlet end 18 of the tank 26 to the inlet end 22 of the tank 26 to provide a uniform distribution of steam throughout the inner compartment 38. Thus, a substantially uniform temperature within the blancher 10 is achieved and the recirculation of steam prevents localized cold spots within the blancher 10. The temperature sensors 138, 142 read the average steam and air temperature within the inner compartment 38. Based upon the sensed average temperatures, the amount of steam introduced into the inner compartment 38 is increased or decreased to maintain an average temperature within the blancher 10. Finally, the lifters 146 break up areas of high density food product, which draws a disproportionate amount of steam and air mixture and results in non-uniform heat transfer to the food product. Therefore, the steam recirculation system 14, the temperature sensors 138, 142, and the lifters 146 all contribute to provide a substantially uniform temperature within the blancher 10 such that a uniform heat transfer to the food product occurs and thereby a short blanch cycle time is achieved.
A first baffle 188 and a second baffle 192 divide the tank 164 into the first compartment 168, an intermediate compartment 196, and the second compartment 172, with the intermediate compartment 196 defined between the first baffle 188 and the second baffle 192. The first compartment 168 is positioned between an inlet end 200 of the tank 164 and the first baffle 188, and the second compartment 172 is positioned between an outlet end 204 of the tank 164 and the second baffle 192.
The tank 164 has an open top and is supported by a frame 208 that includes legs 212, which rest upon a support surface and space the tank 164 above the support surface. A first drum 216, or cylinder, is rotatably mounted in the first compartment 168. The first drum 216 includes an inlet end plate 220 approximate the inlet end 200 of the tank 164, and an outlet end plate 224 approximate the first baffle 188 with a generally cylindrical and perforate sidewall 228 that substantially extends between the end plates 220, 224. Each end plate 220, 224 includes a food product opening (not shown) for receiving or discharging food product, generally defined by an axially outwardly extending flange 232. The inlet end 184 of the first compartment 168 is located proximate the inlet end plate 220 and the inlet end 200 of the tank 164, and the outlet end 180 of the first compartment 168 is located adjacent the outlet end plate 224 and the first baffle 188. A helical auger 236 is disposed within the first drum 216 and rotates with the drum 216 for advancing food product from the inlet end 200 of the tank 164 toward the first baffle 188 and the outlet end 180 of the first compartment 168.
A second drum 240, or cylinder, is rotatably mounted in the second compartment 172. The second drum 240 includes an inlet end plate 244 proximate the second baffle 192 and an outlet end plate 248 proximate the outlet end 180 of the tank 164 with a generally cylindrical and perforate sidewall 252 that substantially extends between the end plates 244, 248. Each end plate 244, 248 includes a food product opening (not shown) for receiving or discharging food product. A helical auger 256 is disposed within the second drum 240 and rotates with the drum 240 for advancing food product through the second drum 240 toward the outlet end 204 of the tank 164. In the illustrated embodiment, the first and second drums 216, 240 are driven independently of each other. In another embodiment, the first and second drums 216, 240 are formed from a wire screen.
An elongated vaulted cover 260 mates with the tank 164 and covers the tank 164 to substantially enclose the drums 216, 240 and other components within the tank 164 and provide an enclosure for the steam. The cover 260 of the tank 164 is generally attached to the tank 164 in such a manner as to allow the cover 260 to move relative to the tank 164 and permit access to the inner compartments. In one embodiment, the cover 260 is hingedly connected to the tank 164 so the cover 260 can be swung away from the drums 216, 240 to permit access to the tank interior.
As discussed above with respect to the rotary steam blancher 10, perforations in the sidewall 228, 252 of each drum 216, 240 consist of a plurality of small diameter bores that extend completely through the sidewall 228, 252 to allow heat transfer medium or a cool transfer medium to pass from the respective tank compartment, through the sidewall and into the drum. A heat transfer medium, which in the preferred embodiment is steam, is supplied to the first compartment 168 of the tank 164 from the supply source (not shown) by one or more manifolds or steam headers (not shown) disposed in the first compartment 168. The first drum 216 is constructed and arranged to receive the steam such that the steam can surround and contact the food product within the first drum 216. In the first drum 216, the steam blanches or cooks the food product as the food product is advanced through the drum 216 by an auger 236. In one embodiment, compressed air is discharged from the manifold with the steam to better effect heat transfer.
A cool transfer medium is supplied to the second compartment 172 of the tank 164 from a supply source (not shown) by one or more manifolds or headers (not shown) disposed in the second compartment 172. The second drum 240 is constructed and arranged to receive the cool transfer medium such that the cool transfer medium can surround and contact the food product within the drum 240. In the second drum 240, the cool transfer medium cools the food product as the food product is advanced through the drum 240 by an auger (not shown). In the illustrated embodiment, the cool transfer medium comprises a liquid, such as water. In another embodiment, compressed air is discharged from the manifold with the liquid cool transfer medium to better effect cooling. Other examples of the cool transfer medium include a combination of liquid and a gaseous cool transfer medium, such as water and air, or a gaseous cool transfer medium such as air.
Each auger 236 includes a plurality of axially spaced apart and interconnected flights 264 that spiral substantially the length of the interior of the respective drum. It should be noted that in
Similar to the rotary blancher 10 discussed above, the rotary cooker-cooler 160 includes the steam recirculation system 176 for transferring steam from the outlet end 180 of the first heat compartment 168 to the inlet end 184 of the first compartment 168. Recirculation of steam from one end of the first compartment 168 to another creates an even distribution of steam within the first compartment 168 of the cooker-cooler 160 and maintains a substantially uniform temperature within the first compartment 168. The steam recirculation system 176 constantly agitates and stirs the steam and air mixture within the first compartment 168 and prevents localized cool spots within the first compartment 168.
Referring to
A fan 300 is positioned within the passageway 276 of the conduit 272 to facilitate transfer of steam from the outlet end 180 of the first compartment 168 to the inlet end 184 of the first compartment 168. The fan 300 draws steam from the outlet end 180 of the first compartment 168 into the conduit 272, through the conduit 272, and propels the steam to the inlet end 184 of the first compartment 168. A motor box 304 is attached to an outer surface of the conduit 272 and stores a fan motor (not shown). In other embodiments, the fan 300 may be positioned anywhere within the conduit 272 of the steam recirculation system 176 and the conduit 272 may have other configurations.
The first compartment 168 of the tank 164 defines a heat zone for the cooker portion of the rotary cooker-cooler 160 in which steam cooks food product as it passes through the first drum 216. Similar to the rotary steam blancher 10 discussed above, in the illustrated embodiment approximately 50% of the steam within the first compartment 168 is located in a first portion 308, or zone, of the first compartment 168. The first portion 308 of the first compartment 168 is defined by the first one-third of the first compartment 168 relative to the inlet end 184. The remaining portion of the steam is located in a second portion 312, or zone, of the first compartment 168. The second portion 312 of the first compartment 168 is defined by the last two-thirds of the first compartment 168 relative to the inlet end 184.
Referring to
Each temperature sensor 316, 320 is electrically connected with a steam controller (not shown). Based upon the sensed average temperature, the controller signals the steam valves (not shown) interconnected with the manifold(s) to increase or decrease the amount of steam introduced into the first compartment 168. The controller and steam valves function similar to those discussed above with respect to
The present invention rotary cooker-cooler 160 includes a plurality of lifters 324 to agitate food product and break up high density areas of food product within the first drum 216. Therefore, more uniform heat transfer to the food product occurs. Referring to
Various features and advantages of the invention are set forth in the following claims.