|Publication number||US3866432 A|
|Publication date||Feb 18, 1975|
|Filing date||Mar 29, 1973|
|Priority date||Mar 29, 1973|
|Publication number||US 3866432 A, US 3866432A, US-A-3866432, US3866432 A, US3866432A|
|Inventors||Harrison Donald I|
|Original Assignee||Cryo Chem Inc|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (31), Classifications (13)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent (191 Harrison [451 Feb. 18,1975
1 1 HELICAL CONVEYOR HEAT EXCHANGE SYSTEM  Inventor: Donald 1. Harrison. Santa Monica,
 Assignee: Cryo-Chem, lnc.. Gardena. Calif.
 Filed: Mar. 29, 1973 21 Appl. No.: 345,990
 US. CL... 62/208, 62/375, 62/381  Int. Cl. F25b 41/00  Field of Search 62/381, 374, 375, 376, 62/380, 63, 208
 References Cited UNITED STATES PATENTS 3.412.476 11/1968 Astrom 62/381 X 3.412.573 11/1968 Pauliukonis 62/374 3.609.987 10/1971 Waldin 62/63 3,733,848 5/1973 Duron et al 62/381 Primary ExaniinerMeyer Perlin Assistant ExamincrRonald C. Capossela Attorney, Agent. or FirmChristie. Parker & Hale  ABSTRACT Food is frozen in a high temperature gradient environment by moving the food along a helical conveyor countercurrently to a fan-driven stream of cold nitrogen gas produced by contacting liquid nitrogen with the food near the discharge end of the conveyor. The food at the discharge end of the conveyor is subjected to about 320 F, the boiling point of nitrogen at atmospheric pressure. Before leaving the freezer, the nitrogen gas is warmed substantially above that temperature by contact with the food on the helical conveyor.
10 Claims, 4 Drawing Figures PATENTEHFEB 1 81975 SHEET 3 BF 4 I I I I I I I I HELICAL CONVEYOR HEAT EXCHANGE SYSTEM BACKGROUND OF THE INVENTION zles to atmospheric pressure. expands to a mixture of 55 percent gas and 45 percent solid carbon dioxide. which is in the form of very small particles. Both the gas and the solid'material are exhausted frotn the nozzles 5 at about 109" l. The light solid particles are entrained h e t lhvehtmh in the gas flow and circulate more or less evenly tlhls 'hvehtleh relates to an endless heheill Conveyor throughout the compartment, subliming to gas as latent helt heat exehtthget y m l there partleularly to heat is added from the product moving through the inh Systems t eeehhg thhtt 1h two phasesv terior of the enclosure. The gas-solid mixture is essenhqutd and gaseous h tially homogeneous, and the entire enclosure volume is State of the h Art kept at a relatively constant temperature of l()0 F. h e h heheal Conveyor System teed tteezthg CO gas is constantly exhausted from the enclosure at apphcattons 1s a well established practice as shown in US t 3,348,659 The use of liquid nitrogen in In the carbon dioxide system, the refrigeration effect heheal Conveyor System is Shown in 15 is obtained almost totally from the latent heat of subli- 3141;573- mation contained in the 45 percent of the injected car- It PP that the lower the temperature of the bon dioxide which has expanded to the solid particle eoohhg medium Within a freezer, the higher the Fate of state. Since the amount of refrigeration available in the heat transfer from the product, the shorter the transit gas f -109 to i BTUS per pound, Carbon time through the freezer to achieve the required cool 20 dioxide gas exhausted atl00 f. results in a substantial line the higher the Productivity of the q p loss of refrigeration. For example, uniform temperature as expressed in PoundS p hour of Product throughput operation in the enclosure results in a loss of 15 percent lt is also pp that to mtlihtath the pressure within of the available refrigeration effect of the liquid carbon the freezer ht essentially htmosphettewhich is P dioxide. In large systems this loss is prohibitive, and ehtly required for Practical Commercial Operation the carbon dioxide recoverey and reliquification systems cooling medium must be removed from the enclosure are i d to t h Operation economicat HOW at the same rate it is introduced. At the present time, ever, h advantage f hi System i h h bi there are three principal refrigeration systems used in temperature f 1()() F i h freezer results i faster Commercial treeZerS- llrei transit time than can be employed with the air blast sysl. Air blast" freezer system. using closed cycle me t Chu l CZl f g i The use of liquid nitrogen as a refrigerant creates 2. Car on di x p n cycle r f g rati and substantially lower ambient tetnperatures in the Liquid hlttegeh P eyele refrigeration freezer, which result in even faster transit time for the In an air blast freezer, the refrigerant, which is chilled p od ct, Despite the reduced freezing times and inby conventional closed-cycle mechanical equipment, is creased productivity obtained in a helical convey circulated through an evaporative cO ocated t n freezer using liquid nitrogen as a refrigerant, its use has the insulated enclosure or freezer box. Air is drawn been severely limited by the inefficient utilization of through ducts and directed by fans ac the e p r the refrigeration effect available in the liquid nitrogen, tor coils, and chilled to the desired temperature usuwith resulting uneconomic operating costs. When operally about 40 F. The cold air is then circulated past 40 ating the freezer with a substantially constant temperathe food product, and then exhausted by a blower and tore throughout the enclosure, as in US. Pat. No. recycled past the evaporator coil. In this system the in- 3,412,573, the thermodynamic characteristics of nitroterior of the insulated chamber is kept essentially at a gen result in a large waste of refrigeration. This is due constant temperature throughout. The atmosphere of to the fact that the liquid nitrogen, which enters the the chamber is constantly recirculated, so only sufichamber at a temperaturue of 320 V., has a latent cient refrig eration is ad ded t o the at? to halarfce the heat of vaporization of 86 BTUs per pound. The resultheat load of the product throughput. This system is ecing gas at -320 F. has a refrigeration capacity of 80 onomical in terms of refrigeration energy, but the rela- BTUs per pound between 320 and 0 F. Therefore, tively high temperature freezing environment of only if the chamber is operated at a constant low tempera- 40 F. requires much longer transit times and slower ture, 200 F. for example. the liquid nitrogen being speeds for a given amount heat transfer than is required added to mix with the gas to maintain that temperature, by the other two refrigerant systems. exhaust gas is constantly discharged at a temperature The carbon dioxide open cycle refrigeration system of200 F. This results in a loss of 50 BUTs per pound injects pressurized liquid at 300 psig and 0 F. through of-refrigerant as compared to an exhaust temperature nozzles directly into the enclosure. This flow is usually of 0 F. The following table shows the percent loss of directed into a suction plenum behind circulation fans. refrigerant at various internal operating temperatures The liquid carbon dioxide, in passing through the nozas compared to a gas exhaust temperature of 0 F. H
Total Total Internal Latent Ht.of Refrig. Refrig. Refrig. Ambient Vaporization of Gas Used Available 7c 7r Temp.F. BTU/LB BTU/LB BTU/LB BTU/LB Utilized L051 The preceding table shows that the production rate advantage which can be obtained from the use of liquid nitrogen by operating at low internal temperatures is offset by the economic loss involved in non-utilization of available refrigeration capacity in the exhaust gas.
SUMMARY OF THE INVENTION This invention provides novel apparatus and method to introduce, control, and circulate nitrogen refrigerant so as to utilize the maximum refrigeration capability and enable economical refrigeration use, while at the same time providing the benefit of improved quality and increased productivity obtainable from a low temperature environment in a freezere using a helical conveyor.
Briefly, the apparatus includes a thermally insulated enclosure with an inlet and outlet for material to be cooled or frozen. A helical conveyor in the enclosure carries the material from the inlet toward theoutlet. Means are provided for introducing a liquid coolant, say, nitrogen, into the enclosure to contact the material on the conveyor adjacent the enclosure outlet so the liquid coolant absorbs sufficient heat to vaporize. Fan means in the enclosure blow the vaporized coolant around the helical conveyor in the direction opposite to that in which material is moved on the conveyor to effect countercurrent cooling of material with the vaporized coolant. Means are also provided for removing vaporized coolant from the enclosure after a substantial amount ofthe heat has been absorbed by the vaporized coolant from the product.
Preferably, an annular upright baffle adjacent the helical conveyor forces the vaporized coolantto flow in a helical path countercurrent to the product carried by the conveyor. The liquid coolant is preferably injected through two manifold systems, one of which is on con: tinuously. and the other of which is cycled on and off in response to the temperature of the vaporized coolant leaving the enclosure.
In the presently preferred embodiment ofthe apparatus, the helical conveyor moves around an upright axis and carries the product from a lower to an upper portion of the enclosure. Nozzles mounted over the upper end of the conveyor spray liquid nitrogen onto the product near the discharge end of the helical conveyor. The liquid nitrogen is vaporized or else spills down onto the product carried by lower loops of the conveyor and is vaporized there. The cylindrical baffle is preferably within the helical conveyor, and is open at its bottom and closed at its top except for an exhaust duct connected to a blower, which exhausts vaporized nitrogen gas from the inside of the baffle. One of more fans in the enclosure, and outside the baffle, impart a tangen tial component to theh vaporized nitrogen gas and cause it to swirl around the baffle and helical conveyor in a direction opposite to the movement of the product on the conveyor. In an alternate embodiment, the baffle is on the outside of the helical conveyor, and the fans are inside the baffle. A core in the center of the heelical conveyor confines the gas to a helical path countercurrent to the movement of the product.
A sump in the floor of the enclosure collects any liquid nitrogen which may not be vaporized, and a liquid nitrogen level sensor in the sump generates an alarm signal and stops the injection of liquid nitrogen into the enclosure if the level of liquid nitrogen in the sump rises above a desired level. g
In terms of method for effecting rapid heat transfer. the invention includes the steps of moving material to be cooled on a conveyor in a freezer from an inlet to an outlet for the material. A portion of a coolant liquid, say, liquid nitrogen, is introduced into the enclosure at a first location near the is introduced into the enclosure at a first location near the outlet for the material, and a second portion of the cooling liquid is introduced into the enclosure at a second location spaced farther from the inlet than the first location. Thellquid coolant is supplied to the enclosure to contact the material to be cooled at a rate which causes the liquid coolant to be vaporized into gaseous form. The gas is then forced by fans to flow thro ugh the enclosure countercurrently to the movement of the material on the conveyor.
Preferably, the temperature of the gasified coolant is sensed as it is removed from the enclosure, and the injection of the cooling liquid into the enclosure at the second location is varied in response to the temperature of the gas leaving the enclosure.
BRIEF DESCRIPTION OF THE DRAWINGS The invention will be more fully understood from the following detailed description and the accompanying drawings, in which:
FIG. 1 is a fragmentary perspective view, partially broken away, of the heat exchanger system using liquid nitrogen as a coolant;
FIG. 2 is a sectional elevation of the system of FIG. 1;
FIG. 3 is a view taken on staggered line 3-3 of FIG. 2; and
FIG. 4 is a diagrammatic sectional elevation of an alternate embodiment of the invention in which the product to be cooled is passed down a helical conveyor into a pool of liquid coolant.
Referring to FIGS. 13, a freezer 10 includes a boxlike enclosure 11 with four insulated side walls 12, a bottom wall 14, and a top wall 16. An endless conveyor 20 in the enclosure carries food packages 22 (FIG. 2) from an inlet 24 in the lower corner of one of the side walls of the enclosure, around an ascending helical path 25 in the central portion of the enclosure, and to an outlet 26 in the upper corner of a side wall opposite from that which includes the inlet.
The helical conveyor is of the type described in U.S. Pat. No. 3,348,659. Its helical portion includes nine loops 27 disposed around an upright cylindrical and hollow baffle 30 secured by bolts 32 (FIG. 2 to the inside surfaces of equally spaced vertical ribs 33 in an upright rotatable drum 34, which includes at its lower end a downwardly extending stub shaft 36 mounted to revolve in a thrust bearing 38 supported by the bottom 40 ofa cage 42, which surrounds the helical portion of the conveyor.
The bottom of the drum includes eight radially extending and horizontally drum spokes 44 secured at their respective inner ends in the center of the drum to the upper end of the stub shaft 36, and at their respective outer ends to a lower horizontal drum hoop 46.
The vertical drum ribs 33 are secured at their lower ends to the lower drum hoop 46 and at their upper ends to an upper horizontal drum hoop 50.
Eight horizontal and radially extending top drum spokes 52 are secured at equally spaced intervals at their respective outer ends to the upper hoop, and at their respective inner ends to a stabilizing bearing 54, which receives the lower end of a stub shaft 56 secured in a socket S8 of a hub 60 secured to the inner ends of six horizontal and radially extending cage spokes 62, which are each secured at their respective outer ends to a respective downwardly extending cage rib 64. The lower ends of the cage ribs are secured to pads 66 on the floor of the enclosure. The upper and lower ends of the cage ribs are braced by horizontal struts 68.
The upper end of the baffle is covered by an outwardly extending flange or baffle cover 70 secured to the lower end of an exhaust stack 72, which extends up through the center of the enclosure top wall. The exhaust stack is connected by a duct 74 to a blower 76 driven by an electric motor 78.
The helical portion of the conveyor slides on a pair of laterally-spaced, helical tracks 80 mounted on top of a helical shalf 82 secured at its outer periphery to the inner portions of the cage ribs. The inner edges of the loops in the helical portion of the conveyor belt are frictionally engaged by the vertical drum ribs, which maintain proper tension in the conveyor (as described in US. Pat. No. 3,348,659), when the drum is rotated by a chain 84 secured around a sprocket 86 mounted on the periphery of the lower end of the drum. Chain 84 also extends around a drive sprocket 88 mounted on the upper end of a vertical shaft 90, which is driven through a conventional gear train (not shown) in synchronization with a horizontal conveyor drive shaft 92, the outer end of which extends through a side wall of the enclosure and carries a drive sprocket 94 driven by conventional chain drive 96. The inner end of horizontal shaft 92 carries a drive sprocket 98, which engages the conveyor to apply the proper tension to cause the belt to move over a system of idler sprockets 100 in a tension take-up mechanism 102 (FIG. 1), which forms no part of the present invention, and therefore is not described in detail.
Liquid nitrogen is supplied to the enclosure from a cryogenic storage tank (not shown) through a supply line 104, which is connected through a main control solenoid-operated valve 106 and a first manifold valve 107 to a first or upper manifold line 107A, and through a second manifold valve 108, which is solenoid operated, to a second or lower manifold valve 108, which is solenoid operated, to a second or lower manifold line 109. The solenoid operated valve 108 is controlled by a temperature sensor 110 mounted in the exhaust stack.
The first liquid nitrogen manifold line extends down through the top wall of the enclosure, and is connected to an upper circular distributor pipe 111 disposed around the outside of the cage just below the second loop from the top of the helical portion of the conveyor. A first set of six separate horizontal and radially extending spray nozzle lines 112 are connected at their respective outer ends to the circular distributor at equally spaced intervals. Each spray nozzle line extends inwardly through a respective cage rib, and terminates at its inner end just short of the drum. Four radially spaced and downwardly directed nozzles 114 in each nozzle line spray liquid nitrogen onto the food product supported by the third loop from the top of the helical portion of the conveyor. A second set of six horizontal and radially extending spray nozzle lines 116 (FIGS. 1 and 2) are located at equally spaced intervals around the space between the cage and the drum just below the fourth loop from the top of the helical portion of the conveyor. The outer end of each of the second set of spray lines extends through a respective cage rib and is connected to a lower circular distributor pipe 117 secured around the outside of the cage and connected to the lower end of the second manifold line which extends down through the top of the enclosure. A set of fourth nozzles 118 is secured to the underside of each of the spray lines in the second set to direct a stream of liquid nitrogen onto the food product carried by the fifth loop in the helical conveyor.
As shown in FIGS. 1 and 3, a separate pair of vertically spaced fans 119 are mounted in diametrically opposed corners of the enclosure to rotate on respective horizontal shafts 120 extending to the exterior of the enclosure where each shaft is connected to and driven by an electric motor 121. The fans blow nitrogen gas around the helical portion of the conveyor in a counterclockwise (as viewed in FIG. 3) direction, which is opposite to the direction of the travel of the helical portion of the conveyor.
The insulaE d floor of the enclosure slopes down from left to right (as viewed in FIG. 2) to an elongated gutter 122 in the floor of the enclosure along the lowest edge in the enclosure. The gutter slopes downwardly, in the direction perpendicular to the floor slope, from one end to another so that any excess liquid nitrogen which might each the enclosure floor is collected in a sump 123 at the lower end of the gutter. A liquid nitrogen level control system 24 is mounted in the lower portion of the sump to prevent the accumulation of an excessive amount of liquild nitrogen. The control sys' tem includes a lower thermocouple contact 126 mounted in the bottom of the sump and connected to a control box 127 by a lead 128. An upper thermocouple contact 130 is mounted in the sump above the first contact and connected to the control box through a lead 132. An electrical heating element 134 is connected by leads 135, 136 to the control box, which is supplied power from a conventional source (not shown). If sufficient liquid nitrogen collects in the sump to rise to the level of the lower contact 126, a conventional control circuit in the control box energizes the electrical heating element until the liquid nitrogen is evaporated to the level below that of the lower thermocouple contact sensor. If the capacity of the heater is insufficient to evaporate the liquid nitrogen as fast as it accumulates, the level of the liquid nitrogen rises to the upper contact 130, which causes the control circuit to generate an alarm signal, closes the main valve in the liquid nitrogen supply line to shut off the supply of liquid nitrogen to the enclosure, and turns off the motors for the conveyor, fans and blower.
In using the equipment shown in FIGS. l-3, the product to be cooled or frozen enters at the bottom of the enclosure on the conveyor, moves in an ascending helical path around the rotatable drum, and exits at the top of the enclosure through the outlet. The drum and conveyor are driven synchronously through a conventional gear train (not shown) by power supplied to the horizontal shaft 92 (FIG. 1). Liquid nitrogen is sprayed onto the ascending product through both manifolds, and is vaporized into gaseous nitrogen, which is blown in a counterclockwise direction (as viewed in FIG. 3) by the fans around the helical portion of the conveyor. The blower connected to the exhaust duct creates a reduced pressure inside the rotating drum so the gaseous nitrogen is drawn 56m and into the open lower end of the drum and is discharged from the drum through the exhaust stack and blower. The upper end of the cylindrical baffle makes a close sliding fit against the stationary baffle cover, so there is negligible leakage of nitrogen gas between the cover and the baffle.
When the temperature of the nitrogen gas leaving through the exhaust stack reaches a desired value, F. for example, indicating that sufficient liquid nitrogen has been supplied to the enclosure for the rate of prod uct being conveyed through the enclosure, the temperature sensor in the exhaust stack actuates solenoid valve 108 to close it, thus interrupting the supply of liquid nitrogen to the lower set of spray nozzles. Valve 107 stays open so the upper nozzles continue to spray liquid nitrogen in an amount which supplies about 75 percent of the required cooling. Valve 108 stays closed until the temperature of the nitrogen gas in the exhaust stack exceeds a desired value, +5 F. for example, indicating that insufficient nitrogen is being introduced into the system. The temperature controller then opens solenoid valve 108, permitting liquid nitrogen to flow through the nozzles in the lower manifold, whichsupplies about 50 percent of the required cooling.
As the liquid nitrogen is discharged from the nozzles, part of it comes in direct contact withi the product on the conveyor. Heat is transferred from the product, which is at a substantially higher temperature than the liquid nitrogen, and the liquid nitogen is vaporized to nitrogen gas as it absorbs the latent heat of vaporization. Liquid nitrogen which is not vaporized at the level where it is injected flows over the product and drips through the conveyor onto warmer product below, so the liquid nitrogen is vaporized at lower levels as it absorbs latent heat. The gas generated by the vaporizing of the liquid nitrogen is circulated in a tangential direction by the fans in the enclosure. They provide a substantial horizontal velocity vector to the gas flow. The negative pressure induced in the cylindrical baffle by the exhaust blower causes the nitrogen gas to have a downward velocity component from the manifold spray nozzles to the bottom of the enclosure, then a horizontal radial inward component into the bottom opening of the cylindrical baffle. The gas circulation past the product on the conveyor thus has a horizontal tangential component imparted by the circulation fans, and a vertically downward component due to the exhaust suction. This results in a substantially helical flow path of the circulating gas in a direction countercurrent to the direction of the product moving on the helical portion of the conveyor.
Thus, the nitrogen gas which is generated from the liquid nitrogen at a temperature of 320 F., is warmed as it transfers heat from the product by convection. As indicated above, when the exhaust gas temperature exceeds a pre-set value, indicating that insufficient liquid nitrogen is being introduced into the system, the temperature controller causes the opening of the solenoid valve for the lower liquid nitrogen manifold, permitting additional liquid nitrogen to flow through the orifice nozzles in the manifolds. The spray manifolds are located on different levels to disperse the liquid nitrogen for more complete vaporization. All of the nozzles are located at an elevation above the middle loop of the helical portion ofthe conveyor to permit sufficient length of travel of the resultant vaporized nitrogen gas to absorb a substantial amount of sensible heat from the product to the gas.
The lower set of nozzles being sized to permit a total liquid nitrogen flow about 25 percent greater than that required by the product heat load insures proper on-off cycling of the solenoid valve in the lower manifold to maintain control of the exhaust temperature within close limits. Even closer control is obtained by using a conventional proportional control valve in the supply line to the lower manifold. The valve position is controlled by the temperature sensor monitoring the exhaust gas temperature. In such a system the proportional control valve controls flow, even with changing input product load, to maintain within very close limits the required temperature of the output gas.
Although substantially all of the liquid nitrogen introduced through the manifolds is vaporized, either by direct contact with the product, or by convection from the circulating gas, some small quantity of nitrogen may remain in the liquid state as it falls to the sloped floor of the enclosure. If so, it drains into the gutter and then into the sump where it is vaporized by the electrical heating element. If the equipment should malfunction and supply an excess amount of liquid nitrogen to the enclosure, causing the level of liquid nitrogen to rise in the sump above the desired value, the liquid level control in the sump shuts off all liquid nitrogen supplied to the enclosure, and stops the motors for the conveyor belt, blower, andfans An alternate embodiment of the invention is shown in FIG. 4. An enclosure has an inlet opening 152 at its upper portion, and a discharge opening 154 in its lower portion on the side of the enclosure opposite from the inlet. An endless conveyor 156 carries a product (not shown) to be frozen in a descending helical path in a counterclockwise direction (as viewed from above) around an upright imperforate drum 158, which is suspended above the floor of the enclosure by a vertical shaft 159 secured to the upper end of the drum and extending up through an exhaust opening 160 covered by an exhaust duct 162 connected to a blower 163. The upper end of the shaft 159 is supported in a thrust bearing 164 mounted in the exhaust duct.
A cylindrical baffle 166, secured by flanges 168 to the roof of the enclosure, surrounds the helical portion of the conveyor, and hangs down so that its open lower end terminates just below a pool of liquid nitrogen 169 in the bottom of the enclosure. A plurality of fans 170 are mounted within the baffle to direct a circular flow of gas in the annular space between the baffle and the drum in a clockwise direction (as viewed from above) so the gas flows countercurrently to the product moving down the helical portion of the conveyor.
The liquid nitrogen in the bottom of the enclosure is vaporized as it is contacted by the product carried by the lower portion of the helical conveyor. This causes nitrogen to be vaporized and rise in the annular space between the cylindrical baffle and the imperforate drum. The nitrogen gas is given an upward velocity component by the blower reducing the pressure within the exhaust duct, and the fans cause the nitrogen gas to siwrl in a clockwise direction in the annular space while the product moves in a counterclockwise direction. The product is removed from the liquid nitrogen by an endless transfer belt 172 and carried out through the enclosure discharging opening.
The level of the liquid nitrogen in the enclosure, and the temperature of the exhaust gas, is controlled as described with the embodiment shown in FIGS. l-3.
From the foregoing description, it will be apparent that this invention provides an improved cooling or freezing apparatus which substantially increases the product throughput because of the large temperature gradient imposed by liquid nitrogen at -320 F., and which obtains high efficiency by using a substantial portion of the sensible heat in the vaporized nitrogen gas before it leaves the cooling enclosure.
1. Cooling apparatus comprising a thermally insulated enclosure with an inlet and an outlet for material to be cooled, the inlet being below the outlet, a helical conveyor having upper and lower ends disposed in the enclosure about an upright axis to carry the material upwardly from the inlet to the outlet of the enclosure, an upright annular and imperforate baffle disposed within the helical convevyor, means for introducing liquid nitrogen into the enclosure to contact the material on the conveyor at a point nearer the enclosure outlet than the inlet so the liquid nitrogen absorbs sufficient heat to vaporize to nitrogen gas, fan means in the enclosure arranged to impart a horizontal velocity vector component to the nitrogen gas thus blowing it around the helical conveyor in the direction opposite to that in which the material is moved on the conveyor, means for creating a lower pressure at the lower end of the helical conveyor than at the upper end so that a vertical velocity vector component is imparted to the gas so that substantially all the nitrogen gas flows down the helical conveyor, the net flow of the gas being to spiral downwardly around the helix to effect countercurrent cooling ofmaterial with the nitrogen gas, and means for removing nitrogen gas from the enclosure.
2. Apparatus according to claim 1 which includes a first manifold for spraying a portion of the liquid nitrogen on the product on the conveyor at the point nearer the enclosure outlet than the inlet, and a second manifold for spraying the balance of the liquid nitrogen onto the product at another point farther from the enclosure outlet than where the first manifold is located, but closer to the enclosure outlet than the inlet.
3. Apparatus according to claim 2 which includes means for varying the amount of liquid nitrogen supplied through the second manifold while maintaining substantially constant flow of liquid nitrogen through the first manifold.
4. Apparatus according to claim 3 which includes means responsive to the temperature of the vaporized nitrogen removed from the enclosure for controlling the amount of liquid nitrogen flowing through the sec ond manifold.
5. Apparatus according to claim I which includes a sump in the floor of the enclosure for collecting excess liquid nitrogen, and vaporizing means in the sump for vaporizing liquid collected there.
6. Apparatus according to claim 5 which includes a sensor in the sump for detecting the presence of liquid nitrogen, and means responsive to the sensor for shutting off the flow of liquid nitrogen into the enclosure.
7. Apparatus according to claim 5 which includes means responsive to the sensor for stopping the conveyor.
8. Apparatus according to claim 5 which includes a sensor in the sump for detecting the present of liquid nitrogen, and means responsive to the sensor for energizing the vaporizing means.
9. Apparatus according to claim 8 which includes a first sensor at one level in the sump for developing a signal when liquid accumulates in the sump, means responsive to the signal from the first sensor for energizing the vaporizer, a second sensor disposed about the first sensor for detecting the presence of liquid in the sump at a level above that of the first sensor, and means responsive to the signal from the first sensor for stopping the flow of liquid nitrogen into the enclosure.
10. Apparatus according to claim 9 which includes means responsive to the sensor for stopping the conveyor.
mg UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3,866,432 Dated February 18, 1975 Invent0 (s) Donald I. Harrison It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
Col. 2, line 20 -"-'1o0f." should be -100F--;
Col. 2, line 25 "recogerey" should be --re overy-;
Col. 2, line '45 "-320 V" should be 320 F.;
Col. 2, line 53 "BUT's" should be BTU's-;
Col. 3, line 16 "freezere" should be -freezer--;
Col. 3, line 54 "of" (second occurrence) should be -or-;
Col. 3, line 56 "theh" should be -the-; Col. 3, line 62 "heelical" should be --helical--; Col. 4, lines 8 "is introduced into the enclosure at a and 9 first location near the" should be deleted (repetition) Col. 4, line 60 "horizontally" should be "horizontal- Col. 5, lines 46)- "valve. 108, which is solenoid operated, to
' and 47 a second or lower manifold" should be I deleted (repetition) Col. 6, line 29 "each" should be reach-; Col. 6, line 31 "24" should be -l24; Col. 6, line 46 "electrical" should be -electric-; Col. 7, line 27 "withi" should be -with---; C01. 8, line 63 "siwrl" should be -swirl-;
Col. 8, line 68 "discharging" should be -discharge Col. 10, line 26 "present" should be -presence-;
Col. 10, line 39 before "sensor" insert signal from the second-.
Signed and sealed this 13th day of May 1975.
C. MARSHALL DANN RUTH C. MASON Commissioner of Patents Attesting Officer and Trademarks
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US3412476 *||Mar 13, 1967||Nov 26, 1968||Frigoscandia Ab||Plant for treating products with air as a treating agent|
|US3412573 *||Sep 21, 1966||Nov 26, 1968||Richard S. Pauliukonis||Cryogenic quick freezing apparatus|
|US3609987 *||Apr 1, 1970||Oct 5, 1971||Du Pont||Method and apparatus for extracting heat from articles with an ebullient liquid freezant|
|US3733848 *||Aug 9, 1971||May 22, 1973||Airco Inc||Freezing system|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4023376 *||Jul 31, 1975||May 17, 1977||Hirohumi Onodera||Food refrigerating method|
|US4078394 *||Jun 29, 1976||Mar 14, 1978||J. W. Greer, Inc.||Cryogenic freezer|
|US4103507 *||Jun 17, 1977||Aug 1, 1978||Airco, Inc.||High speed freezing system|
|US4124997 *||Oct 22, 1976||Nov 14, 1978||Linde Ag||Apparatus for the cooling and embrittlement of tires|
|US4189047 *||Oct 12, 1977||Feb 19, 1980||Alto Corporation||Endless conveyor|
|US4324110 *||Oct 22, 1980||Apr 13, 1982||Air Products And Chemicals, Inc.||Spiral-type heat exchanger|
|US4363263 *||Jul 26, 1979||Dec 14, 1982||Hester Industries, Inc.||Efficient high humidity food processing system with sanitizing improvements|
|US4370861 *||Dec 21, 1981||Feb 1, 1983||Air Products And Chemicals, Inc.||Spiral-type heat exchanger|
|US5020330 *||Mar 20, 1990||Jun 4, 1991||Liquid Carbonic Corporation||CO2 food freezer|
|US5170631 *||May 23, 1991||Dec 15, 1992||Liquid Carbonic Corporation||Combination cryogenic and mechanical freezer apparatus and method|
|US5205135 *||Nov 13, 1991||Apr 27, 1993||Liquid Carbonic Corporation||Helical conveyor freezer|
|US5247810 *||Jul 14, 1992||Sep 28, 1993||Liquid Carbonic Corporation||Freezer conveyor|
|US5277301 *||Jun 14, 1993||Jan 11, 1994||Liquid Carbonic Corporation||Freezer conveyor|
|US5343714 *||May 20, 1992||Sep 6, 1994||Air Products And Chemicals, Inc.||Spiral freezer|
|US6615592||Dec 28, 2001||Sep 9, 2003||Supachill Technologies Pty. Ltd.||Method and system for preparing tissue samples for histological and pathological examination|
|US6619069 *||Nov 17, 1999||Sep 16, 2003||Aga Aktiebolag||Flexible conveyor belt and a climate chamber comprising a belt of that kind|
|US6656380||Oct 16, 2001||Dec 2, 2003||Supachill Technologies Pty. Ltd.||Super-coolable composition having long-duration phase change capability, process for preparation of same, process for super-cooling same and articles comprising same|
|US6681581||Nov 20, 2001||Jan 27, 2004||Supachill Technologies Pty. Ltd.||Pre-conditioned solute for use in cryogenic processes|
|US9453684 *||Dec 29, 2011||Sep 27, 2016||Eni S.P.A.||Heat exchanger for the cooling of hot gases and heat exchange system|
|US20040221587 *||Nov 25, 2003||Nov 11, 2004||Cassell Allan J.||Pre-conditioned solute for use in cryogenic processes|
|US20130313482 *||Dec 29, 2011||Nov 28, 2013||Eni S.P.A.||Heat exchanger for the cooling of hot gases and heat exchange system|
|USRE33510 *||Apr 15, 1988||Jan 1, 1991||Hester Industries, Inc.||High humidity steam cooker with continuously running conveyor|
|USRE35259 *||Jun 21, 1990||Jun 4, 1996||Hester Industries, Inc.||High humidity steam cooker with continuously running conveyor|
|EP0050372A2 *||Oct 21, 1981||Apr 28, 1982||Air Products And Chemicals, Inc.||Spiral-type heat exchanger|
|EP0050372A3 *||Oct 21, 1981||Dec 15, 1982||Air Products And Chemicals, Inc.||Spiral-type heat exchanger|
|EP0128270A2 *||Oct 21, 1981||Dec 19, 1984||Air Products And Chemicals, Inc.||Spiral-type heat exchanger|
|EP0128270A3 *||Oct 21, 1981||Oct 23, 1985||Air Products And Chemicals, Inc.||Spiral-type heat exchanger|
|EP0570833A1 *||May 12, 1993||Nov 24, 1993||Air Products And Chemicals, Inc.||Spiral freezer|
|WO2001055654A1 *||Jan 24, 2001||Aug 2, 2001||Frigoscandia Equipment Ab||Spiral conveyor cooling apparatus|
|WO2002022470A2 *||Sep 14, 2001||Mar 21, 2002||Supachill Technologies Pty. Ltd.||Spiral immersion conveyor, system, and method for use|
|WO2002022470A3 *||Sep 14, 2001||Feb 13, 2003||Supachill Internat Pty Ltd||Spiral immersion conveyor, system, and method for use|
|U.S. Classification||62/208, 198/778, 62/381, 62/375|
|International Classification||F25D25/00, F25D25/04, F25D3/11, F28D11/00, F25D3/10|
|Cooperative Classification||F25D25/04, F25D3/11|
|European Classification||F25D3/11, F25D25/04|