# Patent

## Title
Air guide box for stabilizing the run of a web, for instance a paper web

## Abstract

This is a continuation of Ser. No. 008,463, filed Jan. 29, 1987, abandoned, which is a continuation of application Ser. No. 701,775, filed Feb. 14, 1985, now U.S. Pat. No. 4,676,007.

## Background
The present invention relates to heat exchangers and, more particularly, to heat exchangers for preheating heated air flowing into and drawn from grain bins.

It is well known and accepted that grain in storage may not contain more than a certain minimum moisture content or else discoloration and spoilage will likely occur. To bring grain to the requisite minimum moisture content, various procedures have been developed. In U.S. Pat. No. 4,253,825, there is described a conveyor belt system for transporting grain past a hot air generator to dry the grain prior to storage. U.S. Pat. No. 4,086,708 is directed to a concurrent counter-current flow grain dryer in the form of a tower with side walls, a top and a bottom. This tower has a wet grain receiving bin at the top and wet grain is delivered from the receiving bin into a drying chamber in response to gravity. Thereafter, the grain is subjected to both hot and cool air to dry the grain at a controlled rate to prevent stress cracking. U.S. Pat. No. 2,876,557 describes a recirculation system for fluidisation of grain.

An air flow system incorporating a pair of heat exchangers for preheating the air is described in U.S. Pat. No. 4,091,547. Herein, a first heat exchanger is located at the outlet of a flow of heated air and a second heat exchanger located at the inlet. A refrigerant flowing between the first and second heat exchangers transports heat from the first to the second heat exchanger to preheat the air flowing into the inlet. U.S. Pat. No. 4,132,011 is directed to a device for transporting fresh air past hot exhaust tubes and thence to a predrier to recover a quantity of heat from the exhaust air. U.S. Pat. No. 4,380,126 is directed to apparatus for drawing air from an exhaust pipe to recover heat and into a hot air chamber.

Drying apparatus used to dry tobacco leaves is described in U.S. Pat. No. 4,114,288 wherein the air to be heated is drawn adjacent the heating chamber to become preheated; moreover, the use of an adjacent solar roof further warms the preheated air. U.S. Pat. No. 4,263,721 describes a counterflow heat exchanger for reclaiming heat from air directed past tobacco leaves.

In the devices described above pertaining to grain, the drying apparatus and heat recovery processes used therewith are intended for use prior to storage of the grain. Moreover, such apparatus is used in conjunction with grain under transport which permits certain facility in ducting the drying air flow, whether it be concurrent or countercurrent and whether different segregable air flows are employed. None of such apparatus are particularly suitable for nor readily adaptable to the drying of grain which has been deposited in a grain bin.

The present invention is directed to a heat recovery system for use in conjunction with heated air blown into a grain bin to remove moisture and preheat the inflowing air.

It is therefore a primary object of the present invention to provide apparatus for drying grain in a grain bin and for recovering heat from the exhausted air.

Another object of the present invention is to provide apparatus for permitting filling of a grain bin during operation of inflow and exhaustion of heated air flow through the grain bin.

Still another object of the present invention is to provide a heat recovery system for use with a grain bin which precludes reintroduction of drawn off moisture.

Still another object of the present invention is to provide a heat exchanger which reduces the back pressure to lessen the load imposed on a forced air drier for grain bins and which preheats the inflowing air.

A further object of the present invention is to provide a heat exchanger for use in conjunction with hot air drying apparatus for grain bin which does not reintroduce drawn-off moisture.

A yet further object of the present invention is to provide a process for drying grain in storage.

A still further object of the present invention is to provide a process for filling a grain bin during operation of a forced air grain drying apparatus.

These and other objects of the present invention will become apparent to those skilled in the art as the description thereof proceeds.

The present invention will be described with greater specificity and clarity with reference to the following drawings, in which:

FIG. 1 is a perspective view of the present invention;

FIG. 2 is a top view of the present invention and including a partial cut away view;

FIG. 3 is a partial cross-sectional view of the heat recovery unit;

FIG. 4 is a cross-sectional view taken along lines 4--4, as shown in FIG. 3;

FIG. 5 is a cross-sectional view taken along lines 5--5, as shown in FIG. 3;

FIG. 6 is a side view illustrating the grain feed mechanism; and

FIG. 7 is a detailed view illustrating the introduction of grain into the grain bin.

Referring to FIG. 1, there is shown a grain bin 10 having a turret 12 located at the apex of roof 14. The turret serves a combined purpose of receiving the grain to be stored and of collecting the exhaust air. A conventional blower and heating unit 20 draws air through conduit 22, heats it and blows the heated air into the grain bin. As shown in FIG. 2, the grain bin may include circumferential passageways or ducts 24 to distribute the heated air vertically through the grain stored in the bin. Additionally, radially oriented ducts, represented by arrows 26, may be incorporated at the bottom of the grain bin to distribute the heated air introduced by blower and heating unit 20.

As jointly illustrated in FIGS. 1, 2, 6 and 7, an outlet conduit 30 extends from turret 12 to collect and convey the exhaust air from within the grain bin. To aid the flow rate of the exhaust air and reduce the amount of back pressure within the grain bin, a blower 32 is employed in conjunction with duct 30 to draw the air from within the turret. It has been found that an air flow rate in the range of 5,000 to 25,000 cubic feet per minute imposed by blower 68 in combination with a similar flow rate imposed by blower 32 provides an air flow rate commensurate with economical drying of the grain within the grain bin. Down stream of blower 32, the exhaust air is conveyed through conduit 34 to heat recovery unit 36. The heat recovery unit is operatively associated with duct 22 to heat the fresh air flowing into the duct but preclude mixing therewith. The moisture ladden exhaust air passing through the heat recovery unit is discharged to the atmosphere to preclude re-entry of the moisture into the grain bin.

Referring particularly to FIGS. 3, 4 and 5, heat recovery unit 36 will be described in detail. A plurality of pipes 40 are penetrably secured to and extend intermediate of upper plate 42 and lower plate 44. Upper plate 42 and the associated open ends of pipes 40 are circumscribed by a shroud 46 interconnecting the plate with the terminal end of conduit 34. The function of the shroud is that of directing the air exhausting from conduit 34, as represented by arrows 48, into and through pipes 40. The terminal ends of pipes 40, extending through plate 44, exhausts the heated moisture ladden air into the atmosphere, as represented by arrows 50. To avoid back pressure or other restrictive force upon the air exhausting from pipes 40, heat recovery unit 36 may be mounted upon a pedestal or legs 52 to provide a substantial open space beneath plate 44; it is contemplated that the exhausted air can be directed laterally instead of downwardly.

Fresh air, depicted by arrows 56, enters heat recovery unit 36 through opening 58 defined by the edges of plates 42, 44 and side walls 60, 62. The fresh air flowing through chamber 64, defined by plates 42, 44 and side walls 60, 62 flows in a circuitous and turbulent path around and about all of pipes 40. From chamber 64, the air flow enters a further shroud 66 and is drawn into duct 22 in response to the operation of blower 68 of blower and heater unit 20.

The air exhausted from conduit 34 has a certain heat content as a result of the heating performed upon this air upon introduction to the grain bin. It is obviously preferable to recover a portion of the heat if such recovery can be performed at a cost less than the cost of generating the heat equivalent to the heat recovered. Due to the simplicity of construction and lack of significant air flow impediments presented by heat recovery unit 36, such heat recovery has been found to be sufficiently efficient to warrant installation by providing a reduction in overall costs.

The heated moist air, flowing through pipes 40, will transfer a quantum of heat to these pipes. The quantum of heat transferred is a function of both the flow rate and the temperature differential between the heated exhaust air and the pipes. To slow the air flow rate through pipe 40 will increase the heat transfer rate but create backpressure for both blower 68 and blower 32. The additional work load imposed upon these two blowers must be considered with respect to the amount of back pressure tolerable in order to obtain a better heat transfer. The flow rate through pipes 40 can be slowed to some extent by configuring the pipes to be undulating or serpentine, as depicted by pipe 70. Alternatively, an undulating or serpentine membrane 72, extending partially or diametrically across pipe 74, which may replace one or more of pipes 40, as illustrated in FIG. 5, may be employed. Such membrane, tending to induce a lateral flow of air through the pipe, will somewhat impede the flow rate and yet establish little back pressure. The selection and use of either of the configurations represented by pipes 70 and 74 is a function of economics, flow rates and temperature differentials which must be considered for any given installation.

One of the detriments of many heat recovery systems is that of producing a mixing of the exhaust air with the inflowing air. With respect to the drying of grain, such mixing is counter-productive as moisture would be reintroduced into the grain bin. With the configuration of heat recovery unit 36, such transfer of moisture is precluded. The turbulent circuitous flow of fresh air through the heat recovery unit assures substantial heat transfer from pipes 40 to the inflowing air. Accordingly, the air drawn in by blower 68 is preheated to an extent which is a function of the relevant temperature differentials and flow rates. Heater 76 of blower and heating unit 20, illustrated in FIG. 4, is generally of the thermostat controlled type. The amount of heating performed by such heater is a function of the temperature of the impinging air; the greater the temperature of the impinging air the less heating need be done and the lower are the costs associated with the drying of the grain in the grain bin.

Conventionally, grain bins are filled by a conveyor transporting grain from a source to an opening in turret 12. Were turret 12 open to permit essentially unrestricted airflow through the opening, operation of heater and blower unit 20 would impede filling of the grain bin. Moreover, effective operation of heat recovery unit 36 would be essentially precluded as the heat recovery unit is of limited use unless it is used in conjunction with an essentially closed system. To avoid these problems and permit ongoing drying of the grain within the grain bin during fill, the grain transport apparatus depicted in FIGS. 1, 6 and 7 was developed.

A conventional conveyor 80 transports grain from a source of grain or another conveyor 82 to a hopper 84. The hopper directs grain deposited therein through an inlet 86 of housing 88 for an auger 90. The auger is actuated through energization of a motor 92. The auger transports the grain from inlet 86 through discharge port 94. The discharge port is located internal of turret 12 and in general vertical alignment with a conventional rotating grain dispersing device 96 located within the grain bin.

While a certain amount of air flow through housing 88 from discharge port 94 to inlet 86 may occur in response to the air pressure within turret 12, the volume thereof is relatively insignificant with respect to the volume of air flow through the grain bin in response to operation of heater and blower unit 20. The grain bin, even with the grain introducing auger, remains essentially a closed system and operation of the heater and blower unit in combination with the heat recovery unit may be operated during fill of the grain bin.

While the principles of the invention have now been made clear in an illustrative embodiment, there will be immediately obvious to those skilled in the art many modifications of structure, arrangement, proportions, elements, materials, and components, used in the practice of the invention which are particularly adapted for specific environments and operating requirements without departing from those principles.

## Claims

1. Apparatus for recovering heat energy generated to remove moisture from, and thereby dry, an agricultural product contained in a bin and using air as a medium for the heat exchange without changing its gaseous state, said apparatus including: to aid in evaporating the moisture in the agricultural products and in removing at least some of the moisture from the agricultural products; conduit means including means for forcing air flow in and about the agricultural products within the bin; air from within the bin which air has flowed in and about at least some of the agricultural products in the bin, said exhaust means being operable independently of said heating and blowing means; means to a remote location; venting to the atmosphere the air flowing through said further conduit means; and means to said heating and blowing means to preheat the fresh air flowing into said heating and blowing means; whereby, a quantity of the generated heat energy is recovered from the exhaust air to preheat the fresh air flowing into the bin.

2. The apparatus set forth in claim 1 wherein said heat exchange means includes a plurality of pipes for venting the exhaust air to the atmosphere, means for channeling the received exhaust air into said pipes and a chamber for directing the flow of fresh air in and around said plurality of pipes to draw heat therefrom.

3. The apparatus as set forth in claim 2 wherein at least some of said plurality of pipes are serpentine in configuration to increase the rate of heat transfer to the fresh air.

4. A method for recovering some of the heat energy generated to remove moisture from agricultural products stored in a bin and using air as a medium for the heat exchange without changing its gaseous state, said method comprising the steps of: the moisture from the agricultural products and in removing at least some of the moisture from the agricultural products; products in the bin; of drawing out and exhausting being exercisable independently of said step of heating the fresh air; the conveyed exhausted air; the fresh air to be heated during said step of heating; and exercise of said step of preheating whereby, the fresh air to be heated is preheated by the exhausted air to recover some of the heat energy generated and imparted to the inflowing fresh air.