REDUCTION OF HEAT TRANSFER BETWEEN A BODY AND ITS ENVIRONMENT

Abstract: Heat transfer between a body located above ground and a surrounding gaseous environment is reduced by placing at least one baffle-insulator adjacent to the body, such that the baffle-insulator which has a thermal conductivity of less than about 5 watts/meter- DEG K, disturbs, modifies, and/or wakens flow of the gaseous environment about the body, thus reducing heat transfer between the body and the gaseous environment.

Description: REDUCTION OF HEAT TRANSFER BETWEEN A BODY AND ITS ENVIRONMENT BACKGROUND OF THE INVENTION Heat transfer between a body and its surrounding gaseous environment is an inherent response to a non-uniform temperature distribution between the body and the gaseous environment. Lim¬ iting heat transfer between a body and its gaseous environment is highly desirable in many situations. Such heat transfer is the result of conduction, convection, and radiation. Heat trans¬ fer by convection occurs when natural forces such as gravity and buoyancy (either positive or negative) due to a temperature gra¬ dient between a body and its gaseous environment, and possibly external forces such as a fan, causes the gaseous environment to flow about the body and transfer heat to or from that body. Heretofore, conductive heat transfer was the primary means of control and it was sought by placing one or more layers of an insulating material around the body. Insulation, however, is often expensive, not intended nor effective at dealing with con¬ trolling convective heat transfer, difficult to install, and can deteriorate over time. Moreover, some insulation materials, e.g. asbestos, have proven harmful to the environment and man. Jaber et al., Optimal Location of a District-Heating Pipe¬ line Within a Rectangular Duct , Applied Energy, 40, pp. 101-109 (1991) , considered the problem of heat transfer in natural con¬ vection flow over an insulated horizontal hot-water pipe embedded within an air filled, relatively cold, rectangular air-filled duct. The data suggest an optimal configuration in terms of pipe location relative to the cavity walls which could result in a minimum rate of heat loss from the pipe. Similarly, Jaber et al, Optimal Thermal-Insulation Placement of District-Heating Pipes and Their Support Baffles in Air Filled Trenches, Applied Energy, 40, pp. 111-118 (1991), investigated the steady state heat- transfer across a cold, horizontal, rectangular cavity enclosing two relatively hot horizontal pipes. The data suggest that the minimum steady-state heat loss occurs when the two pipes were placed one above the other. The analysis suggests that effective thermal resistance can further be enhanced by physically sup¬ porting each pipe with a pair of low-conductivity physical sup¬ port structures which are termed baffles. The support structures form isolated air spaces in a closed environment. Jaber et al only deals with heated pipes located within cold ducts. Neale et al, Steady State Heat Transfers Across an Obstruct¬ ed Air-Filled Rectangular Cavity, Chem. Eng. Res. Des., 66, pp. 458-462 (1988) considered the problem of heat transfer from a hot horizontal pipe embedded inside a cold, horizontal, rectangular, air-filled duct. The pipe was assumed to be supported by two, low-conductivity, symmetrically-placed spacers that completely bridge the gap between the pipe and the walls of the duct and extend the length of the pipe. The article suggests that the presence of such spacers could improve the thermal resistance of the air-filled cavity over an unobstructed one. The article is limited to pipes located in a closed environment, i.e. an air- filled duct. Lai, Jjπproving Effectiveness of Pipe Insulation By Using Radial Baffles to Suppress Natural Convection , Int. J. Mass Heat Transfer, 36, pp. 899-906 (1993) discloses the use of baffles solely as an integral part of porous media insulation, i.e. located within the insulation. There is no suggestion of extend¬ ing the baffles beyond the insulation to further reduce heat loss from the pipe. Accordingly, there remains a need for improved control or reduction of heat transfer between a body located above ground and the surrounding gaseous environment without the need of bulky, expensive layers of insulating materials. There is a need to minimize heat transfer between a body, e.g. a pipe, and its gaseous environment, e.g. air, without going to the extreme of placing the body in an air-filled cavity or isolated duct or for relocating the body. SUMMARY OF THE INVENTION The present invention is directed to products and methods for reducing heat transfer between a body located above ground and the surrounding gaseous environment which are at different temperatures. This is done by placing at least one baffle-in¬ sulator adjacent a body extending into the gaseous environment. The baffle-insulator preferably has a thermal conductivity of less than about 5 watts/meter-"K, extends into the gaseous en¬ vironment sufficiently to modify or weaken the flow of that gas¬ eous environment around the body to cause a reduction in convec- tive heat transfer between the body and the gaseous environment. DESCRIPTION OF THE DRAWINGS Fig. 1 is a plot of uniformly spaced isotherms (left side) and streamlines (right side) of the convective fluid flow outside a prior art horizontal pipe with no baffle-insulators. Fig. 2 is a detailed streamline plot of the fluid flow around a single baffle-insulator attached to a horizontal pipe in accordance with this invention. Fig. 3 is a cross-sectional schematic view of a horizontal pipe having ten baffle-insulators extending substantially perpen¬ dicularly from the pipe showing isotherms and streamlines. Fig. 4 is a partial schematic view of a prior art vertical pipe with no baffle-insulator attached and showing streamlines of convective fluid flow about the pipe and the velocity profile of the air flow adjacent to the pipe. Fig. 5 is a partial schematic view of a vertical pipe with a single radial baffle-insulator attached in accordance with this invention, showing streamlines of the convective fluid flow and the velocity profile of the air flow adjacent to the pipe. Fig. 6 is a partial schematic view of a vertical pipe with four radial baffle-insulators attached in accordance with this invention and showing streamlines of the convective fluid flow. Fig. 7 is a side view of air flow traveling along a prior art L-shaped surface with a heated vertical wall. Fig. 8 is a side view of air flow traveling along an embodi¬ ment of the invention wherein a horizontal planar baffle-insula¬ tor is attached to the vertical wall of Fig. 7. Fig. 9 is a side view of air flow traveling along the heated vertical wall of Fig. 7 having four horizontal planar baffle- insulators attached thereto. Fig. 10 is a cross-sectional view of an embodiment of the invention having three curvilinear baffle-insulators attached to a horizontal pipe. Fig. 11 is a side view of the air flow about a heated verti¬ cal wall having a curvilinear baffle-insulator attached thereto. Fig. 12 is a side view of the air flow along a heated verti¬ cal wall having two complex curvilinear baffle-insulators attach¬ ed thereto. Fig. 13 is a cross-sectional view of a horizontal pipe with three complex baffles, each having an articulated secondary sur¬ face or vane, attached thereto. Fig. 14 is a partial side view of a pleated structure where¬ in each pleat forms a baffle-insulator. Fig. 15 is a cross-sectional schematic view of a horizontal pipe with planar baffle-insulators attached to a pipe with snap- on connectors. Fig. 16 is a side view of a stiffened wire frame structure with four baffle-insulator holding places for use with and in place about a portion of a horizontal pipe. Fig. 17 is a partial side view of a vertical pipe showing a radial baffle-insulator in place and a strap for supporting a second radial baffle-insulator about the pipe. Fig. 18 is a partial side view of two curved baffle-insul¬ ators intended for use with horizontal bodies. Fig. 19 is a partial side view of a curved radial baffle- insulator intended for use with vertical bodies and placed out¬ side a vertical pipe. DETAILED DESCRIPTION OF THE INVENTION Heat transfer between a body located above ground and its gaseous environment occurs by conduction, convection, and radia¬ tion. Since radiative heat transfer is relatively low, the total resistance to heat transfer from a body insulated with conven¬ tional insulation can be considered to be the sum of the thermal resistance due to the conventional insulation (conductive resis¬ tance) and the thermal resistance due to the convection of fluid flow. The total thermal resistance can be increased by either increasing the conductive resistance provided by conventional insulation or by increasing the convective resistance. The con¬ ductive thermal resistance can be increased by (i) increasing the thickness of the insulation or (ii) utilizing a more effective insulation. The present invention deals with increasing the resistance to heat transfer between a body located above ground and its gaseous environment by increasing the thermal resistance due to convective heat transfer. This is accomplished by associating, generally attaching, a body at one temperature with one or more low thermal conductivity baffle-insulators which extend into the gaseous environment which is at a different temperature (either higher or lower) . The baffle-insulators modify the hydrodynamic and thermal characteristics of the flow of the gaseous environ- ment near the body such that the strength of that flow is reduced and heat transfer between the body and that gaseous environment is reduced. As used herein unless otherwise stated, "gaseous environ¬ ment" refers to a gas such as air, oxygen, helium, and argon which flows about or within a body being insulated. Convective heat transfer, i.e. convection, between the environment and the body occurs when the two are at different temperatures. Convec¬ tion as used herein includes natural, forced, and mixed convec¬ tion. As used herein unless otherwise stated, "wall" refers to a surface, either inner or outer, of a body which is at a differ¬ ent temperature than its gaseous environment and to which a baf¬ fle-insulator is adjacent. A baffle-insulator of the present invention is a generally thin extended surface, vane, or the like of a low thermal conduc¬ tivity material which extends out from a wall of a body into the gas which flows about the body, either inside, outside, or both. The baffle-insulator disturbs, diverts, alters, or weakens the flow of the environment in the area of the body wall, thus reduc¬ ing convective heat transfer to or from the body. Although sometimes physically shaped like fins which are made of high thermal conductivity materials and are used to enhance heat transfer between a body and its environment, a baffle-insulator is made from different materials and functions in a fundamentally different manner. Baffle-insulators are prepared from materials having thermal conductivity too low to function effectively as a fin. One end of a baffle-insulator is adjacent to a wall of the body being insulated and the other end extends freely into the gaseous environment. Preferably, the first end will directly or indirectly contact the body. While less desirable, a baffle- insulator may be placed a short distance away from the body wall provided that it is sufficiently close to divert the gaseous environment flow in the immediate vicinity of the body including between the wall and the baffle-insulator. The portion of the baffle-insulator furthermost from the body must be open to flow of the gaseous environment around it, i.e. it must not contact any structure. A baffle-insulator functions by minimizing gase¬ ous environment flow close to the surface of the body being insulated and thereby reducing heat transfer by convection. A baffle-insulator generates regions of relatively stagnant flow, i.e. gaseous barriers, along the body, between the body and its gaseous environment. While the baffle-insulators of this invention will most com¬ monly be placed outside a heated fluid conduit, e.g. a pipe located above ground which transports a heated liquid or gas, they may also be adjacent any body which is at a different tem¬ perature than that of its gaseous environment and wherein heat transfer by convection is occurring. The body may extend hori¬ zontally, vertically, or any angle therebetween. The body may be spherical. The body may be warmer or colder than its gaseous environment. The gaseous environment will most commonly be air. Most commonly the baffle-insulators will extend outwardly from a wall of a body being insulated into the gaseous envi¬ ronment, i.e. air. There may be situations in which the reverse location of the baffle-insulators is advantageous, at least from an aesthetic point of view. In such a situation the baffle insulators are located inside the body and extend from an inner wall of the body into a fluid contained within the body, e.g. oil or a distillate thereof, a process liquid such as a chemical reactant, a food substance, milk, brine, acid, pulp slurry, and the like. In this circumstance, the term "gaseous environment" in intended to include the liquids within the body. The baffle-insulators are made from materials having thermal conductivities sufficiently low to prevent a baffle-insulator from functioning as heat transfer-enhancing fins. The thermal conductivity of suitable baffle-insulator materials is generally less than about 5 Watts/meter- β K (W/m- β K) , preferably less than about 1.5 W/m-"K, and most commonly in the range of about 0.05 /m-'K to about 1 W/m-'K. The performance of a baffle-insulator material increases as the emissivity decreases. The baffle- insulator should also be sufficiently durable to withstand the conditions of the anticipated gaseous environment for an extended period, preferably the projected life of the body. It should also be non-toxic. It should also be sufficiently temperature resistant to withstand the expected operating conditions. Exam¬ ples of suitable materials include: polymers such as polyeth¬ ylene, polypropylene, polystyrene (both foamed and unfoamed) , polyimide, polytetrafluoroethylene, polytrifluorochloroethylene, polyurethane, acrylate and methacrylate polymers and copolymers, polyadipamide, polyester, polyvinyl chloride polymers and copol¬ ymers; non-polymeric materials such as wood, glass, paper, rub¬ ber, leather, wallboard, gypsum, ceramic, cement, conventional insulation materials such as fiberglass, cellulosics, silicates and the like; fabric; and combinations such as plastic-coated fabric, metal coated plastic, and the like. Preferably, the bar¬ rier is a polymeric material, either a flat or pleated sheet or fabric thereof which can form multiple baffle-insulators or a sheet or a pre-formed fixed shape which is sufficiently rigid to be self-supporting. Also, conventional building or insulation materials may be produced with external ridges which extend into the gaseous environment sufficiently to break-up the convective flow along the material, perpendicular to the ridges, to reduce heat transfer and serve as "built-in" baffle-insulators. The baffle-insulators reduce heat transfer by at least 1%, preferably at least about 2%, more preferably by at least about 5%. Typically, a baffle-insulator has generally smooth outer surfaces. If desired, however, the surfaces may be roughened so as to provide additional resistance against gaseous environment flow to divert and weaken that gaseous environment flow around the baffle-insulators. The baffle-insulators of this invention modify the gaseous environment flow traveling about a body by extending across the predominant direction of the gaseous environment flow, preferably substantially perpendicular thereto, such that the gaseous envi- ronment flow is diverted around the baffle-insulator away from the body. In the absence of the baffle-insulators, the path of a gaseous environment flow about a body will be influenced by factors such as the shape of the body, the physical and thermal properties of the fluid of the gaseous environment, constant nat¬ ural driving forces (e.g. buoyancy and gravity) , variable natural driving forces (e.g. wind) and external driving forces (i.e. man- generated) . In operation, a baffle-insulator preferably causes a barrier to gaseous environment flow to form along the wall of the body and the barrier reduces the rate of convective heat transfer between the wall and its gaseous environment. General¬ ly, the effectiveness of a specific baffle-insulator system will depend upon (i) the number of baffle-insulators used, (ii) the distance the baffle-insulators extend into the gaseous environ¬ ment and away from the body being insulated, (iii) the temper¬ ature differential between the body and the gaseous environment, (iv) the materials used to form the baffle-insulators, (v) the specific position, orientation, and shape of the baffle-insula¬ tor, and (vi) the spacing, if any, between the body and the baf¬ fle-insulators. As indicated, the insulating effect of a baffle-insulator system is dependent upon many variables. Therefore, each specif¬ ic installation should be separately evaluated to determine an optimum number, shape, and placement of baffle-insulators while considering the economics of manufacture and installation. The evaluations can be performed by simple trial and error in a lab¬ oratory setting or by mathematical analysis while considering the well-known governing equations relating to conservation of mass, conservation of momentum, and conservation of energy, i.e. the continuity equation and the Navier-Stokes and energy equations. In the case of natural convection, the Boussinesq approximation may be used to approximate the bouyancy effect. The governing set of partial non-linear differential equations can be solved numerically using an iterative scheme such as the well-known Gauss-Seidel method. The baffle-insulator length or distance it extends away from a body being insulated is a well-defined, controllable variable in a system. The greater the distance a baffle-insulator ex¬ tends, the greater the heat transfer reduction, all other varia¬ bles being constant. The distance can be as small as a few millimeters or as large as a meter or more, depending upon the selection of the other variables, including the extent of insul¬ ation desired. For a small cylindrical body, e.g. a pipe, with a radius up to about 6" (15.2 cm), the distance will generally be at least about 0.1R, preferably at least about 0.2R, more preferably at least about 0.4R, where R is the radius of the pipe. For a large cylindrical body, i.e. with a radius of 10 ft (3 m) or more, the distance is generally at least about 1-2" (2.5 to 5.1 cm) , though it may be smaller or larger, even 1-2 ft (0.3- 0.6 m) or more. For relatively flat bodies, e.g. vertical or horizontal wall surfaces or spherical bodies, the distance will often be at least about 1-2" (2.5 to 5.1 cm). However, very small distances, such as those generated by forming substantially parallel ripples in the outer surface of conventional insulation or building materials may be adequate in some situations. The thickness of a baffle-insulator is generally not of con¬ cern provided that it is sufficient to permit the desired shape and placement of the baffle-insulator to be maintained. Thus, for applications in air, a suitable thickness for a self-support¬ ing baffle insulator structure will generally be at least about 0.005" (0.13 mm) . Thinner baffle-insulators may be used provided that an adequate support structure is provided. A baffle-insul¬ ator may be solid or hollow so long as its weight is such that it retains its placement in use. One end of the baffle-insulator will be associated with the body being insulated and the other end will extend into the gase¬ ous environment in such a manner that there are no restrictions to flow of the gaseous environment about the end furthermost from the body. Most commonly, the end of the baffle-insulator closest to the body will be in direct contact with a wall of the body. Alternatively, although generally only if required for a partic¬ ular installation, a baffle-insulator may be placed a short dis¬ tance away, e.g. up to about 0.1" (0.3 cm) from the body. This will reduce the effect of a baffle-insulator system, but it can be compensated for, at least in part, by increasing the distance a baffle-insulator extends into the fluid and/or increasing the number of baffle-insulators. In determining the number of baffle-insulators to be used, (i) the temperature difference between the body and its gaseous environment, (ii) the distance the baffle-insulators will extend into the gaseous environment, (iii) the shape of the body being insulated, (iv) the body size, and (v) the fluid type, are the most significant physical factors typically considered for an application. The number will also depend on the extent of reduc¬ tion of heat transfer which is desired or economically warranted since the more individual baffle-insulators present used for a particular system, the greater the benefit. The baffle-insula¬ tors are commonly spaced relatively uniformly around or on the body. The specific optimal distribution will depend, at least partially, upon the shape of the body and the above factors. Increasing the number of baffle-insulators will generally provide enhanced performance. As the total number of baffle-insulators increases, the greater the diversion of the gaseous environment flow and the greater the reduction in heat transfer between the body and its environment. In each of the following situations, it is assumed that all other parameters are held constant: the greater the temperature difference, the greater the number of baffle-insulators to obtain a particular reduction in heat transfer; the shorter the distance each baffle-insulator extends into the gaseous environment, the greater the number of baffle-insulators; the longer a vertical body, the greater the number of baffle-insulators; the larger the pipe diameter, the greater the number of baffle-insulators; the less the kinematic viscosity of a fluid transported within a body, and the greater the number of baffle-insulators. For vertically disposed bodies, the baffle-insulators should normally extend substantially horizontally and the number of baf¬ fle-insulators will generally be such that the distance between successive baffle-insulators is generally less than about 30.5 cm, preferably less than about 15.2 cm, more preferably less than about 7.6 cm. Except under a most extreme temperature differ¬ ence, e.g. more than about 300°C, or when very short-baffle-in¬ sulators are used, vertical baffle-insulators are rarely placed closer together than about 0.6 cm. Specific non-limiting application areas which will benefit by the heat transfer reduction resulting from this invention in¬ clude such as (i) local heating district systems, (ii) plumbing systems, (iii) refrigeration systems, (iv) pipelines used for transporting crude oil, (v) chilled water lines, (vi) energy storage systems, (vii) boiler surfaces, (viii) transportation systems of hot industrial liquids and gases, (ix) storage tanks containing fluids, (x) vertical surfaces or walls of homes or other buildings, (xi) all steam pipes and hot water pipes, whether previously insulated or not, and the like. The invention will now be described further with particular reference to the various embodiments shown in the figures. Fig. 1 shows the flow of a gaseous environment around a hot horizontal pipe 10 which has no baffle-insulator associated with it and the flow 14 traveling around the surface of the pipe 10 converging as it rises. In the absence of a gaseous barrier, the gaseous environment flow 14 about the pipe is unrestricted and heat will transfer to a gaseous environment by convection at a rate proportional to the temperature difference. The isotherm 13 about the pipe 10 is also shown. In Fig. 2 an uninsulated hot horizontal pipe 10 in a gaseous environment 11 is shown with a single baffle-insulator 12 placed outside the pipe. A streamline plot of the gaseous environment flow 14 around the baffle-insulator 12 is also shown. The streamline plot assumes the pipe to be surrounded by a gaseous environment with only gravity and the buoyancy force affecting the direction of gaseous environment flow about the pipe. For the hot horizontal pipe 10 of Fig. 2, the predominant direction of gaseous environment flow 14 is vertical and therefore when a single baffle-insulator is used, as shown, it will generally ex¬ tend along the entire length of the pipe 10 to maximize the re¬ duction of heat transfer. Similarly, when two baffle-insulators 12 are used, each will commonly extend horizontally to either side of the body. As the number of baffle-insulators increases beyond two, the additional ones are placed around the body, most commonly but not necessarily, uniformly. It may not always be possible to extend the baffle-insulators the full length of a pipe due to the physical location of a pipe or some other reason and thus multiple short sections of baffle-insulator may be used with some unmodified areas between the sections. Fig. 3 shows the flow of a gaseous environment due to grav¬ ity and bouyancy around a hot horizontal pipe 10 which has ten baffle-insulators 12 associated with it and with the flow 14 traveling around the surface of the pipe 10 and converging as it rises. The isotherm 15 about the pipe 10 is also shown. Figs. 4, 5, and 6 show a second embodiment of the invention in which gaseous environment flow is substantially vertical along the length of a vertical pipe. Fig. 4 shows the gaseous environ¬ ment flow 18 outside a prior art hot vertical pipe 20 having no baffle-insulators attached. The gaseous environment flow 18 travels upward parallel to the hot surface of vertical pipe 20. In the absence of any gaseous barriers associated with the pipe, there is no resistance to gaseous environment flow and heat will transfer to or from the gaseous environment at a rate dependent predominantly upon the temperature differential. Fig. 4 also includes a velocity profile 19 of the rate of flow versus dis¬ tance from the outer surface of the vertical pipe 20. Fig. 5 shows a single radial baffle-insulator 21 placed around a hot vertical pipe 20 in which the gaseous environment flow 18 is parallel to, i.e. along the length of the vertical pipe 20. When a vertical pipe 20 is surrounded by a gaseous environment such as air and no forces other than gravity and the buoyancy force affect the direction of the gaseous environment flow, horizontally extending radial baffle-insulators 21 are used to enhance resistance to heat transfer. The radial baffle- insulators 21 along the length of a vertical pipe 20, as shown in Fig. 6, create gaseous barriers 24 that reduce the rate of convective heat transfer to or from the vertical pipe 20. Fig. 7 shows the flow of a gaseous environment at the base of a heated vertical wall 64 which has no baffle-insulator asso¬ ciated with it. The flow 62 travels along the vertical surface of the wall 64 as it rises due to bouyancy. In the absence of any gaseous barriers, the gaseous environment flow 62 along the wall 64 is unrestricted and heat will transfer to the gaseous environment by convection at a rate proportional to the tempera¬ ture difference. Figs. 8 and 9 show the flow of the gaseous environment when one (Fig. 8) and four (Fig. 9) horizontal baf¬ fle-insulators 66 are placed on the heated vertical wall 64. As shown, the hot ascending gaseous environment flow 62 is diverted away from the wall by the baffle-insulators and mixes with cooler gaseous environment flow 69 drawn from the side, thereby reducing heat transfer. As best seen in Fig. 9, relatively stagnant gase¬ ous areas form between between successive wall baffle-insulators. Although Figs. 2, 3, 5, and 6 show the baffle-insulators 12 and 18 outside uninsulated pipes 10 and 20, the baffle-insulators may also be used in combination with conventional insulation. When such insulation is present, the baffle-insulators will generally be placed atop the insulation, extending from the out¬ side of the insulation into the gaseous environment flow. Also, the baffle-insulators may be placed around a body and then par¬ tially covered by the insulation. When insulation is present, the distance a baffle-insulator extends into the gaseous envi¬ ronment is the distance from the outside of the insulation to the farthermost point. When baffle-insulators are associated with an insulated body, the baffle-insulators will preferably be attached to the outside of the insulation. A baffle-insulator may also be formed as an extension of the insulation surface. When an uninsulated hot body is protected only by baffle-in¬ sulators of this invention, it is preferable that a low emissiv- ity jacket be used to cover the body either before attaching the baffle-insulators or as part of the baffle-insulator attaching mechanism to minimize radiative heat transfer from the body. While Fig. 2 shows a planar baffle-insulator 12 and Fig. 5 a radial baffle-insulator 21, the baffle-insulators may be of any shape which will retard gaseous environment flow around a body. The specific shape will generally be a simple plane but, depend¬ ing on the fluid resistance desired and the likelihood of varia¬ tion in the direction of expected gaseous environment flow, more complex shapes may be used. Fig. 10 shows three curvilinear baffle-insulators 26 associated with a horizontal pipe 10. Such curvilinear baffle-insulators may be particularly useful when a significant portion of the gaseous environment flow originates from beside, as compared to below, the baffle-insulator. This is best seen by comparing Figs. 8 and 11 in which the flow is shown around a planar baffle-insulator 66 and a curvilinear baf¬ fle-insulator 26, each attached to a heated vertical wall 64. When a horizontal baffle-insulator 66 is placed on the vertical wall 64 as shown in Fig. 8, a hot ascending gaseous environment flow 62 is diverted away from the wall by the baffle-insulator and mixes with cooler gaseous environment flow 69 drawn from the side. When an upwards-facing curvilinear baffle-insulator 26 is attached to a heated wall as in Fig. 11, the curvature of the baffle-insulator 26 will help limit the amount of cooler gaseous environment flow stream 68 which reaches the hotter wall 64 just immediately above the baffle-insulator 26, thus increasing the thermal resistance and reducing the heat transfer rate. Other curvilinear baffle-insulators may face downward as shown in Fig. 20 or be a complex structure having portions facing in two directions, e.g. both up and down, as shown in Fig. 12 in which two complex curvilinear baffle-insulators 26 are attached to a heated vertical wall 64 and the air flow is indicated by lines 62. Such a baffle-insulator structure may be molded from a suit¬ able low thermal conductivity polymer. In Fig. 13, three complex-shape baffle-insulators 28 are at¬ tached to a horizontal pipe 10. In this embodiment, a planar baffle 30 has been modified by attaching thereto a perpendicular baffle-modifier unit 32. Such complex baffle-insulators are particularly suitable for use with bodies having complex geome¬ tries or in gaseous environments wherein the flow will not solely be due to gravity and bouyancy. Complex shape baffle-insulators may lead to enhanced overall performance, although the increased manufacturing cost may not always be economically justified. Suitable procedures for forming a particular baffle-insul¬ ator structure and associating that structure with a body will generally depend upon the number of baffle-insulators which are to be used with a particular body and the physical location of that body, i.e. horizontal or vertical. For horizontal bodies and vertical walls, a particularly convenient method of preparing a baffle-insulator structure when there will be a plurality of individual baffle-insulators is to use a sheet of baffle-insula¬ tor material and fold it to form suitably sized pleats as shown in Fig. 12, wherein the pleats are in fact the baffle-insulators. Specifically, in Fig. 14 a multiple baffle-insulator structure 38 is prepared from a continuous, preferably plastic, sheet with pleats 42 formed therein. The individual pleats/baffle-insula¬ tors may be formed to have any desired size and/or distance be¬ tween successive ones. As shown in Fig. 14, the two surfaces which form each pleat are not connected. However, depending upon the baffle-insulator structure desired and/or the physical char¬ acteristics of the specific material, it will likely be advantag¬ eous to join them together to form planar baffle-insulators. When a sheet is used which is rigid enough so that each pleat will be self-supporting, the sheet can be folded to form pleats/- baffle-insulators and the pleats then held in place, if needed, temporarily or permanently, by means such as glue, stitching, heat and the like. Alternatively, external physical male-female connectors, e.g. snaps or Velcro* material, can be inserted at suitable points along a pleat. If the material is such that the pleats are not adequately self-supporting, stiffener means may be inserted into each pleat. In either case, such a baffle-in¬ sulator structure can be attached to a horizontal body 10 as shown in Fig. 15 by wrapping it once around the body 10 and connecting the two ends 74 with means such as glue, male-female connectors, or the like. It can be attached to a vertical wall by suspending it from the top of the wall. An alternative method for generating multiple baffle-insula¬ tors in a single structure is shown in Fig. 16 in which a frame 78 is preshaped to have the desired number, in this case four, of baffle-insulator holding means 76. Individual pieces of baf¬ fle-insulator material may be inserted into one or more of the holding positions. Alternatively, a sheet of baffle-insulator material may be attached to the outside of the structure, i.e. around, rather than in, each holding position 76. A third possi¬ bility is to insert individual rigid pleats from a pleated sheet of baffle-insulator material into one or more of the holding means. The frame may be formed as a single unified structure or as two separate pieces which will serve as end-caps. Such frames can be formed from such as thin metal wire, molded from low ther¬ mal conductivity plastics, and the like. In all such cases, the structures can be attached to the horizontal bodies by any suit¬ able means, e.g. a strap. For small vertical cylindrical bodies the baffle-insulators will be generally flat bodies with a central cut-out in the shape of the body, e.g. a pipe, as needed. Such structures may be at¬ tached to a pipe by wrapping a belt-like structure having a small radial lip around the pipe as shown in Fig. 17 in which a radial baffle-insulator 21 is associated with a body by means of a belt¬ like strap 58 having baffle-insulator supports 60 projecting out- ward therefrom. After a strap 58 is placed around the outer sur¬ face of the body, a baffle-insulator disc 18 can be supported by the projections 60 on strap 58. Alternatively, multiple radial baffle-insulators may be connected by string or the like in the manner of Venetian blinds and then suspended from a point above the vertical body. For planar vertical, large cylindrical, and spherical bodies, e.g. flat walls, large cylindrical and spherical storage tanks, the baffle-insulators may be individually attached to the bodies by any suitable attachment means. Alternatively, a series of baffle-insulators may be connected by string or the like in the manner of Venetian blinds and then suspended from above the planar vertical body. Similarly, the baffle-insulators may be prefabricated into a body wall by intentionally forming a series of ripples or the like which are present in sufficient numbers and extend into the gaseous environment sufficiently to disrupt the gaseous environment flow and reduce the rate of heat transfer between the body and the gaseous environment. Generally the rip¬ ple-insulators will extend very short distances, e.g. 1-5 mm, although it may be possible to form larger ripple-insulators, e.g. up to about 0.5" or more. Figs. 18 and 19 show additional baffle-insulator structures. Specifically, in Figs. 18 two curved baffle-insulators 44 are at¬ tached to the upward side of a horizontal pipe 10. In Fig. 19, a single radial baffle-insulator 45 is shown attached to a verti¬ cal pipe 20. While the direction of expected gaseous environment flow is generally substantially vertical due to gravity and the buoyancy force, the direction can be readily determined for situations in which other forces alter it. Determining the expected predomi¬ nant direction of the gaseous environment flow outside a body will be helpful in optimumizing a system by determining specific shape, number, and placement of the baffle-insulators. Specifi¬ cally, the primary direction of the gaseous environment flow may be determined by consideration of the geometry and the forces which effect the gaseous environment flow. In the case of natur¬ al convection only, the direction of the gaseous environment flow may be determined from the temperature gradients of a body in its gaseous environment. If a body is warmer than its gaseous envi¬ ronment, the buoyancy force acts upwardly and the gaseous envi¬ ronment flow will move upward. If a body is cooler than its gas¬ eous environment, the buoyancy force acts downwardly and the gas¬ eous environment flow moves downward. When the gaseous environ¬ ment flow is effected by a combination of natural convection and forced convection induced by a mechanical device, e.g. a fan, then the effective direction of the gaseous environment flow can be calculated based upon the relative strengths and directions of the various forces using conventional vector analysis. The present invention will now be described with reference to the following Examples. It is understood that these Examples are for illustrative purposes only and should not be deemed as limiting this invention. EXAMPLE 1 In this example, heat transfer rates are determined for a horizontal pipe suspended in air and having a temperature greater than its gaseous environment for (i) a prior art uninsulated pipe, (ii) a prior art insulated pipe, and (iii) four insulated pipes of this invention having 2, 6, 10, or 22 baffle-insulators attached to the pipe. A pipe 2.54 cm in diameter is used and the pipe is suspended horizontally in air. The insulated pipe is covered with 1.27 cm fiberglass insulation. When the insulated pipe is modified in accordance with this invention at a range of pipe surface temper¬ atures T of 26, 32 and 95"C, and 2, 6, 10, or 22 baffle-insul¬ ators are attached thereto, the baffle-insulators are formed by pleating a sheet of polypropylene by attaching multiple male- female connectors suitable distances apart that each pleat ex¬ tends a distance of 1.27 cm beyond the outside of the insulation. The baffle-insulators have a simple planar shape and are attached to the pipe by wrapping the pleated sheet around the pipe and joining the ends. Polypropylene has a thermal conductivity of about 0.14 watts/meter/"K. When an insulated pipe is at a tem¬ perature of 675'C, the outer surface of the insulation is about 120°C and polypropylene baffle-insulators are formed as above. The heat transfer per unit length (watts per meter) from the various pipes is evaluated at four different temperature gradi¬ ents wherein the temperature of the air outside the pipe is room temperature, 25°C, and the temperature T of the pipe is 26, 32, 95 or 675"C. The heat transfer, in watts/meter, along with those of the two prior art systems of (i) an uninsulated pipe and (ii) an insulated pipe having no baffle-insulators attached, are given in Table I. N is the number of baffle-insulators used. TABLE I Heat Transfer (watts/meter) N τ°c Uninsulated None 2 6 10 22 26 0.28 0.23 0.21 0.19 0.18 0.17 32 3.16 2.03 1.95 1.69 1.55 1.40 95 53.21 24.81 24.29 22.07 20.79 17.76 675 840.76 269.22 267.27 255.33 253.85 237.16 The placing of multiple baffle-insulators outside the pipe is highly effective in reducing heat transfer from the pipe. For example, when the temperature of the pipe is 95"C, the addi¬ tion of the fiberglass insulation 1.27 cm (0.5") thick around the entire pipe reduces heat loss by 53%. By adding 2 baffle-insul¬ ators to the insulated pipe, the total reduction in heat loss in¬ creases to 54%. By using 6 baffle-insulators, the total reduc¬ tion is to 59%. By using 10 baffle-insulators, the total reduc¬ tion becomes 61%, and when the number of baffle-insulators is in¬ creased to 22, the total reduction in heat loss increases to 67%. Another way to evaluate the effect of the baffle-insulators is to determine the percent reduction in heat loss starting with the insulated pipe. Based thereon, the % reduction in heat loss in view of the number of baffles with a 95'C pipe is: Number of Baffle-Insulators % Reduction Heat Transfer 2 2.1 6 11.0 10 16.2 22 28.4 Similar substantial reductions in heat transfer are evident for temperatures of 26 and 32°C. When the temperature of the pipe increases to 675"C, the effectiveness of the baffle-insula¬ tors, although still present, is lower due to the hydrodynamic and thermal characteristics of the system. Generally as the tem¬ perature difference between the body and its surrounding gaseous environment increases, the length of the baffle should also in¬ crease to retain the same overall effectiveness. Thus if longer baffle-insulators were used at 675 β C, similar performance results could be obtained as at lower temperature gradients. Perhaps a better way to consider the enhanced reduction in heat transfer is to determine the total thickness of fiberglass insulation that would be required to obtain comparable rates of total heat transfer for a body at various temperatures. The data in Table II indicate the total insulation thickness in centi¬ meters which would be required to produce the enhanced heat loss rates of the combination of insulation and the various number N of baffle-insulators. TABLE II Eσuivalent Insulation Thickness in Centimeters T"C N = 0 N = 2 N = 6 N = 10 N = 22 26 1.27 1.91 3.56 4.47 5.16 32 1.27 1.49 2.35 3.09 4.18 95 1.27 1.36 1.74 1.98 3.0 675 1.27 1.3 1.45 1.46 1.68 The results indicate that substantial amounts of convention¬ al insulation can be replaced by very inexpensive and safe poly¬ propylene baffle-insulators and yield the same insulation effect, i.e. produce the same heat loss. For example, when the tempera¬ ture is 95"C, the heat loss achieved by attaching 2 baffle- insulators to a pipe insulated with 1.27 cm of insulation is 24.29 W/m. To achieve this heat loss with only insulation, 7% more insulation would be needed. To achieve the heat transfer results obtained with 1.27 cm of insulation and 10 baffle-insul¬ ators, 56% more insulation (a total of 1.98 cm) is required. And 136% more insulation is needed to achieve the heat loss rate ob¬ tained with 1.27 cm of insulation and 22 baffle-insulators. EXAMPLE 2 To determine the effect of varying the distance that the baffle-insulators extend away from a horizontal heated body in room temperature air, the procedure of Example 1 is repeated. The heat transfer rates are determined for (i) insulated pipes of the prior art (without baffle-insulators) with (ii) uninsul¬ ated pipes of this invention with baffle-insulators prepared as in Example 1, extending 0.64 or 1.27 cm from the surface of the pipe, uniformly distributed about the pipe. The results are presented in Table III at three heated body temperatures, T=26, 32 and 95'C. The numbers in parentheses are the heat losses that occur in watts per meter. The lower the rate of heat loss, the better the insulating effect. Table III Rates of Heat Loss (Watts/Meter) Baffle Distance into Air, cm 0.64 1.27 T-C Insulated Uninsulated Uninsulated Pipe Pipe Pipe 26 0.23 N = 6 (0.22) N = 6 (0.18) 32 2.03 N = 10 (3.0) N - 6 (1.79) 95 24.81 N = 22 (24.2) N =22 (16.82) The results indicate that baffle-insulators can totally eliminate the use of conventional insulation in certain circum¬ stances. For example, when the temperature of the heated body is 95 β C and 22 baffle-insulators are used which extend outwardly 0.64 cm, a heat loss rate 24.2 W/m which is lower than the heat loss rate 24.81 W/m achieved when the pipe has conventional 1.27 cm layer of fiberglass insulation. EXAMPLE 3 In this example, heat transfer rates are determined for a vertical wall having a temperature greater than its gaseous air environment for four planar baffle-insulators of various lengths. An L-shaped heated vertical wall as in Fig. 7 about 0.3 m high is exposed to air which is 5°C cooler. The heat transfer loss per unit depth-length from the wall is about 3.9 W/m. An insulated structure as in Fig. 9 has four baffle-insulators, each extending about 3 cm from the wall. The baffle-insulators are perpendicular to the vertical wall, extend the width of the wall, and are uniformly spaced. Each baffle-insulator is an acrylic polymer sheet having a simple planar shape and a thermal conduc¬ tivity of about 0.2 W/m-'K. The baffle-insulators are joined and form mini-blinds which are attached atop the wall. The heat loss from the wall having four baffle-insulators extending 3 cm from the wall is 3.5 W/m, a 10 % reduction. The decrease in heat transfer rate as the distance the baf¬ fle-insulators extend from the wall increases is shown in Table IV. Table IV Distance (cm) Heat Transfer Rate (W/m) 3.9 3.0 3.5 4.0 3.2 6.0 2.9

Claims: What is claimed is: 1. A method for reducing heat transfer between a body at a first temperature and its gaseous environment at a second temperature which comprises placing at least one baffle-insulator adjacent to a wall of said body such that flow of the gaseous environment about the wall is diverted by the baffle-insulator away from the wall, wherein the baffle-insulator has a thermal conductivity of less than about 5 watts/meter-"K, wherein the baffle-insulator extends from a first end adjacent to the wall to a second end in the gaseous environment, wherein the gaseous environment flows around the second end. 2. The method of Claim 1, wherein the baffle-insulator has surfaces which are substantially planar or curved. 3. The method of Claim 1, wherein the baffle-insulator has a complex shape. 4. The method of Claim 1, wherein the first end of the baffle-insulator contacts the body. 5. The method of Claim 1, wherein there are at least six baffle-insulators adjacent to the body. 6. The method of Claim 1, wherein there are at least twenty baffle-insulators adjacent to the body. 7. The method of Claim 1, wherein the baffle-insulator is the only means of insulating the body. 8. The method of Claim 1, wherein the baffle-insulator is used in combination with other insulation and the baffle- insulator is attached to said other insulation and not to said body. 9. The method of Claim 1, wherein the baffle-insulator ex- tends substantially perpendicular across the predominant direction of the flow of the gaseous environment. 10. The method of Claim 1, wherein the body is a horizontally disposed cylinder having a radius R less than about 15.2 cm and the second end of the baffle-insulator extends away from the cylinder a distance of at least about 0.1R. 11. The method of Claim 1, wherein the body is a horizontally disposed cylinder having a radius R greater than about 3 m and the second end of the baffle-insulator extends away from the cylinder by at least about 2.5 cm. 12. The method of Claim 1, wherein the body is a vertically disposed flat wall. 13. The method of Claim 1, wherein the body is a vertically disposed pipe and the baffle-insulator extends radially around said pipe. 14. The method of Claim 1, wherein there is more than one baffle-insulator and each is formed from a sheet of baffle-insul¬ ator material which is folded into pleats, wherein each pleat has two surfaces which form a single baffle-insulator. 15. The method of Claim 1, wherein there is more than one baffle-insulator and each is formed by attaching a sheet of baffle-insulator material to a pre-formed structure. 16. The method of Claim 1, wherein the body is spherical. 17. The method of Claim 1, wherein the gaseous environment is outside, inside, or both outside and inside the body. 18. An insulated body produced by the method of any of Claims 1-17.

Inventors: BROWN HARRY, FACAS GEORGE, BROWN, HARRY, FACAS, GEORGE
Applicants: POWERMASS
Application year: 1995
Main classification: F16L59
IPC codes: F16L59