Elliptical and funnel-shaped jet nozzle structure
10913078 ยท 2021-02-09
Assignee
Inventors
Cpc classification
F25D13/067
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
A23L3/361
HUMAN NECESSITIES
F25D2500/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
A23L3/001
HUMAN NECESSITIES
International classification
A23L3/00
HUMAN NECESSITIES
Abstract
An elliptical and funnel-shaped jet nozzle structure includes a plurality of elliptical tapered diversion channels, a plurality of elliptical jet nozzles and a conveyer belt. A wall thickness of each of the elliptical tapered diversion channels is 1-5 mm. A wall thickness of each of the elliptical jet nozzles is 1-5 mm. A thickness of the conveyer belt is 1-5 mm. The elliptical tapered diversion channel is a hollow elliptical truncated cone and it includes an upper opening and a lower opening. The upper opening of the elliptical tapered diversion channel is connected to an elliptical opening, and the lower opening of the elliptical tapered diversion channel is connected to an inlet of the elliptical jet nozzle. The elliptical jet nozzle is a hollow elliptical cylinder.
Claims
1. An elliptical and funnel-shaped jet nozzle structure, comprising: a plurality of elliptical tapered diversion channels; a plurality of elliptical jet nozzle; and a conveyer belt; wherein a wall thickness of each of the elliptical tapered diversion channels is 1-5 mm; a wall thickness of each of the elliptical jet nozzles is 1-5 mm; and a thickness of the conveyer belt is 1-5 mm; the elliptical tapered diversion channel is a hollow elliptical truncated cone comprising an upper opening and a lower opening; wherein the upper opening of the elliptical tapered diversion channel is connected to an elliptical opening of an orifice plate of a plenum chamber, and the lower opening of the elliptical tapered diversion channel is connected to an inlet of the elliptical jet nozzle; and the elliptical jet nozzle is a hollow elliptical cylinder; the plurality of elliptical tapered diversion channels are in a linear arrangement, and a distance between two adjacent elliptical tapered diversion channels is 70-90 mm, the distance being a distance between geometric centers of two elliptic sections of the two adjacent elliptical tapered diversion channels; the upper opening of the elliptical tapered diversion channel has an elliptical section with a major axis of 55-65 mm and a minor axis of 40-50 mm; and a height of the elliptical tapered diversion channel is 30-50 mm; an outlet of the elliptical jet nozzle has an elliptical section with a major axis of 15-25 mm and a minor axis of 4-6 mm; and a height of the elliptical jet nozzle is 20-40 mm; the conveyer belt is arranged just below the elliptical jet nozzle, and a distance between the conveyer belt and the elliptical jet nozzle is 20-40 mm.
2. The elliptical and funnel-shaped jet nozzle structure of claim 1, wherein the wall thickness of each of the elliptical tapered diversion channels is 1-3 mm; the wall thickness of each of the elliptical jet nozzles is 1-3 mm; and the thickness of the conveyer belt is 1-3 mm.
3. The elliptical and funnel-shaped jet nozzle structure of claim 1, wherein the wall thickness of each of the elliptical tapered diversion channels is 2 mm; the wall thickness of each of the elliptical jet nozzles is 2 mm; and the thickness of the conveyer belt is 2 mm.
4. The elliptical and funnel-shaped jet nozzle structure of claim 1, wherein the distance between the two adjacent elliptical tapered diversion channels is 80 mm.
5. The elliptical and funnel-shaped jet nozzle structure of claim 1, wherein the upper opening of the elliptical tapered diversion channel has an elliptical section with a major axis of 60 mm and a minor axis of 45 mm; and the height of the elliptical tapered diversion channel is 40 mm.
6. The elliptical and funnel-shaped jet nozzle structure of claim 1, wherein the outlet of the elliptical jet nozzle has an elliptical section with a major axis of 20 mm and a minor axis of 5 mm; and the height of the elliptical jet nozzle is 30 mm.
7. The elliptical and funnel-shaped jet nozzle structure of claim 1, wherein the distance between the conveyer belt and the elliptical jet nozzle is 30 mm.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
(3)
(4) In the drawings: 1, elliptical tapered diversion channel; 11, upper opening; 12, lower opening; 2, elliptical jet nozzle; 21, inlet; 22, outlet; 3, conveyer belt; 4, orifice plate of plenum chamber; 41, elliptical opening.
DETAILED DESCRIPTION OF THE PRESENT INVENTION
(5) The present invention will be further described below in conjunction with specific embodiments to make the process and features clearer.
(6) As shown in
(7) The low-temperature air from an evaporator is drawn by the air blower of the freezer, and then is boosted to flow out. The boosted low-temperature air enters the jet nozzle 2 via the plenum chamber. After being ejected through the jet nozzle 2, the low-temperature air flows out of the outlet 22 of the nozzle structure and enters the evaporator for heat transfer, and then is drawn into the air blower for next cycle.
(8) The present jet nozzle structure can greatly improve the heat transfer on the surface of the conveyor belt 3 and increase the freezing rate of the frozen products as compared to the conventional circular orifice plate structure. Meanwhile, with the significant increase of the flow rate at the nozzle outlet, the flow in the freezing area is improved, leading to the improved evenness during cooling of the frozen products and the improved quality of the frozen products.
(9) Numerical simulation has been performed on the elliptical and funnel-shaped nozzle structure with a plenum chamber of the quick freezer having a size of 600*600*600 mm and an orifice plate 4 having a size of 600*600*2 mm. An conventional orifice plate structure with an elliptical opening is used as a control. Using air as a simulated fluid, assumptions are made as follows: (1) the air is an incompressible fluid; (2) the internal flow field is in a steady state during the normal operation of the model; and (3) the wall of the plenum chamber is insulated. A k-E turbulence model is employed allowing for the energy equations due to a temperature change during impact. Pressure at the boundary of the inlet is P.sub.in=250 Pa and pressure at the boundary of the outlet is P.sub.out=0 Pa. An inlet temperature and an outlet temperature in the freezing area are set as 230 K and 235 K, respectively. The conveyor belt has a thermal conductivity of 16.3 W/(m* C.).
(10) Through numerical simulation, it is preferred that the wall thickness of the elliptical tapered diversion channel 1 is 2 mm; a wall thickness of the elliptical jet nozzle 2 is 2 mm; a thickness of the conveyer belt 3 is 2 mm. The elliptical tapered diversion channels 1 are preferably in a linear arrangement, and the distance between two adjacent elliptical tapered diversion channels 1 is preferably 80 mm. It is preferred that the upper opening 11 of the elliptical tapered diversion channel 1 has an elliptical section with a major axis a.sub.1 of 60 mm and a minor axis b.sub.1 of 45 mm, and the height H.sub.1 of the elliptical tapered diversion channel is 40 mm. It is preferred that the outlet 22 of the elliptical jet nozzle 2 preferably has an elliptical section with a major axis a.sub.2 of 20 mm and a minor axis b.sub.2 of 5 mm, and the height H.sub.2 of the elliptical jet nozzle is 30 mm. The conveyor belt 3 is preferably arranged just below the elliptical jet nozzle 2, and the distance between the conveyer belt 3 and the outlet 22 of the elliptical jet nozzle 2 is preferably 30 mm.
(11) Results of the numerical simulation to the freezing area of the quick freezer indicate that in the case of same area of the nozzle outlet, the surface of the conveyor belt of the elliptical and funnel-shaped nozzle structure has an average Nusselt number of 158.13, and the elliptical nozzle of the conventional orifice plate has an average Nusselt number of 145.31. It can be seen that the average Nusselt number of the elliptical and funnel-shaped nozzle structure is increased by about 8.82%. The elliptical and funnel-shaped nozzle structure can significantly increase the flow area in the cross-flow direction and reduce the cross-flow effect.
(12) The embodiments are merely used to exemplarily illustrate but not to limit the principles and effects of the present invention. Modifications or variations to the above embodiments may be made by those skilled in the art without departing from the spirit and scope of the invention. Therefore, all of the equivalent modifications or variations also fall within the scope of the claims.