The invention will be better understood and objects other than those set forth above will become apparent when consideration is given to the following detailed description thereof. Such description makes reference to the annexed drawings wherein:
Referring to
The poppet valve 40 has a valve body 50 that has an inlet 52 where steam 42 is delivered via line 44. The stainless steel poppet valve and housing are coated with a food release coating or may be made of high temperature plastic which will not transmit heat to the surrounding area which could cause product burn-on. This would also eliminate the need for cooling that portion of the cooker. The steam enters the main chamber 54 of the poppet valve which communicates with the valve head 60 via ports 58. The valve head in the preferred embodiment is flat and round with a tapered face that mates and seats perfectly into a round hole 68 with a chamfered edge 69. The same sort of valve closure is common on the intake and exhaust valves in gas engines. The valve is normally closed by a spring 62 located at the base 64 of the valve stem 66. When the pressure of the steam inside the main body of the poppet valve exceeds the retaining force of the spring, the valve stem will move thus allowing steam to enter the cooking chamber 30. The valve opening is designed to allow steam to flare out initially in a conical shape whose vertex is indicated at V (in
The base 70 of the valve 40 is held against the valve body and seal 72 by a ring clamp 74 which is easily accessed and removed by loosening wing nut 76. This design facilitates quick disassembly, inspection and maintenance.
At least two agitators 80 are required in the preferred embodiment of the present invention. The distal ends 82 are rotatably mounted to the inlet side 22 of the cooking chamber 20. The proximal ends 84 go through the outlet end 26 and are coupled and synchronized at gear box 94 which is connected to a transmission 92 that is driven by motor 90.
Depending at regular spaced intervals from the agitators 80 are agitator arms 86. The preferred embodiment can be seen in
Since the agitators are non-conveying, their rotation is independent of the product flow and strictly used for mixing and kneading the product. This is a tremendous advantage because low RPM agitators impart very little shear to the food product.
The product is conveyed in and through the cooking chamber 20 by a positive displacement type pump 100 (
The process variables that effect the cooked food quality are regulated by a controller 110 as shown in the schematic diagram (
The process variables are identified in a flow chart (
In step 126 temperatures and pressure of incoming food, steam and outgoing cooked food are monitored.
In step 128 the cooked food product is assessed. Depending on the assessment will determine the feedback 129 to make changes to the variable parameters in step 124. The particular food product being cooked will determine the variable settings.
A typical target for pH of mozzarella cheese curd being fed into the mozzarella cooker would be 5.08 at a temperature of 80 degrees F. With a production rate of 5000 lbs per hour a typical inlet steam supply pressure would be 120 PSI, the injectors would be set to open in sequence starting with the first injector at the inlet of the cooker and to open as necessary to reach the set point temperature setting with a temperature setting of the outgoing, heated mozzarella cheese set at 140 degrees F. Ideally the agitator RPM would be set at 100 RPM. With the dual intermeshing agitator cooker one would expect these settings to produce excellent mozzarella cheese. If the pH of the cheese curd was 5.20 the set point temperature of the cooker would be raised to 145 degrees F. to compensate for the increased pH and minimize the loss of cheese moisture and milk solids. If the cheese came out of the cooker with evidence of small, unmelted cheese curd lumps the RPM speed of the agitators should be increased 5 RPM at a time until the evidence of the unmelted cheese curd disappeared. If the heated cheese had evidence of moisture and milk solids separation, the temperature setting of the cooker should be raised 1 degree F. at a time until the moisture separation disappeared. The steam pressure differential between the steam source and the product pressure inside of the cooking chamber must be maintained high enough to counteract the steam poppet spring to create a stable flow of steam through the injectors into the product cooking chamber.
In the case of the cooking of ground beef taco meat, the incoming raw meat temperature would be approximately 35 degrees F. At a production rate of 5000 lbs per hour the cooked meat temperature set point would be set at 155 degrees F. and the agitator RPMs set at 250. The steam injector set up recommended is to spread out the heat input the length of the cooking column with the sequence of the opening of the injectors spaced out, opening every third injector until the temperature set point is reached. If the particle size of the cooked ground beef coming out of the cooker is too small the agitator RPM should be reduced 25 RPM at a time until the particle size is correct. If there are uncooked lumps of meat coming out of the cooking chamber the temperature set point should be increased by a few degrees or the agitator RPM increased by 25 RPM. If both the particle size is too small and the meat has uncooked lumps, location of the open steam injectors need to be moved closer to the inlet of the cooking chamber to allow for the heated meat to be exposed to the agitation in the cooking chamber for a longer period by adding the heat energy earlier in the process.
An alternate embodiment of an agitator is shown in
Another alternate embodiment of the agitator is shown in
Agitators 140 are designed to be used with an alternate cooking chamber embodiment shown in
The foregoing description and illustrations should not be construed as limiting the scope of the invention, which is defined by the appended claims.
The present application claims the benefit of U.S. Provisional Patent Application Ser. No. 60/851,654, filed Oct. 12, 2006 (Oct. 12, 2006).
| Number | Date | Country | |
|---|---|---|---|
| 60851654 | Oct 2006 | US |