SELF-REGULATING POROUS HEATER DEVICE

Abstract: A self-regulating porous heater (100) solves the problem of regulating the temperature of a fluid passing through the heater (100) by using the skin effect. The heater (100) has a layer of porous material (102) which has a magnetic permeability inversely related to temperature over a given range. Due to conductor skin effects, changes in permeability cause changes in the depth of penetration of a.c. current passing through the magnetic layer (102). Changes in the depth of penetration, in turn, result in changes in resistance --the less the depth the greater the resistance-- and in I<2>R Joule heat. The combined result of these effects is to provide more heat where the temperature of the fluid and the porous layer (102) is below a specified temperature that is related to the layer's Curie temperature. In another embodiment, the heater (200) is a laminate structure made of a low resistance porous material layer (202) and a porous thermally conductive magnetic layer (204). By properly defining the pore dimensions, the porous layers (102, 202, and 204) can filter contaminants from a fluid as it flows through the heater.

Description: SELF-REGULATING POROUS HEATER DEVICE BACKGROUND OF THE INVENTION The present application is related to patent applications Serial No. 243,777 filed on March 16, 1981 entitled "Shielded Heating Element Having Intrinsic Temperature Control"; Serial No. 430,317 filed on September 30, 1982 entitled "Autoregulating Electrically Shielded Heater"; Serial No. 445, 863 filed on December 1, 1982 entitled "Improved Autoregulating Heater"; and Serial No. 498,282 filed on even date herewith. TECHNOLOGICAL CONTEXT OF THE INVENTION Various devices and methods have been suggested over the years for controlling the temperature of a heater. Generally, such devices and methods have relied on positive temperature coefficient of resistance materials in some type of separate feedback network in which temperature variations detected by a sensor serve as input to a control system. The major problem with techniques that rely on the positive temperature coefficient of resistance for a material is that such materials can control temperature over only a limited temperature range. Prior techniques employing feedback networks have proved to be inappropriate in various applications— for example, in an environment where the response time is short, or where the heater must provide various amounts of heat along its cross-section, or where the addition of extra heating elements is not desired. A heater that improves on such prior devices and methods has been proposed by Carter and Krumme in U.S. Patent No. 4,256,945. Referred to as an autoregulating electric heater, the Carter-Krumme heater does not employ separate sensors or feedback elements. Instead, the heater temperature—which is to be regulated—directly affects the amount of heat generated by the heater. Specifically, Carter and Krumme disclose a lami¬ nate structure ' in which one layer comprises a material ot high magnetic permeability and a second layer comprises a low resistance, non-magnetic material. The two layers have a common interface and are in thermal and electrical contact. Connected at opposite ends along the magnetic layer is an a.c. source. The magnetic layer and non-mag¬ netic layer are in parallel across the source. Because of the skin effect, the application of alternating current to the magnetic layer initially results in a " current path substantially confined to a depth in the magnetic layer extending inward from the surface adjacent the current return path of the circuit; i.e. opposite the interface with the low resistance layer. The depth of penetration of the current is defined by the well-known Steinmetz expression; skin depth = constant ; p/μf where p is the resistivity and μ is the magnetic permea¬ bility of the magnetic material and where f is the fre¬ quency of the current. Because the field falls off exponentially in accordance with the expression e where x = thickness/skin depth- it should be realized that approximately 63.2% of the current flows in one skin depth. As is well known, resistance to current is pro¬ portional to p/A where "A" is the cross-section through which current flows. Accordingly, if the skin depth is increased, the cross-section A increases and the resistance correspondingly decreases. Where the Joule heat generated by a material is equal to I R, it is noted that by increas¬ ing skin depth the area A increases; the resistance decreases; and thus the heat generated decreases. O PI Carter and Krumme in the above-referenced patent have coupled this relation of depth versus generated heat with their awareness of magnetic materials which have permeabilities which, at least over a range of tempera- tures, increase with decreasing temperatures. In partic¬ ular, certain magnetic materials provide a large increase in permeability with a small decrease in temperature between two predefined temperatures (one of which may be referred to as the Curie temperature) . When these certain materials undergo this small decrease in temperature, the value of the permeability greatly increases and, all other factors being equal, the depth of penetration of a major portion of the a.c. current in the material decreases. This depth of penetration is not necessarily the skin depth.. Rather this depth of penetration may reflect the depth at which 95% (or some other percentage) rather than the theoretical 63.2% of the current flows. This select¬ able depth is inversely related to permeability, increas¬ ing with decreasing permeability. Moreover, the resis- 2 tance increases resulting in an increased I R generation of heat for a constant current passing through a device. By combining these various effects and material properties, as discussed above, a first measure of self- regulation (or autoregulation) is achieved. That is, within the magnetic material itself, the heat generated thereby is affected by the depth of current penetration and the depth of current penetration has been shown to depend on the temperature of the magnetic material. As taught by Carter and Krumme, a second measure of self-regulation is also achieved as the current totally penetrates the magnetic layer and follows a path that also includes the "parallel" low resistance layer. When this occurs, it is as if a constant current passes through a high resistance and a low resistance in parallel rather than through just a high resistance. OM?I_ This change in resistance translates into a sharp variation in generated heat. With a constant cur- rent of I, I = K (where K is a constant) . When the current flows only through the magnetic layer of high re- sistance R, , the corresponding value for generated heat is KR, . When the current flows through along the layer of low resistance R_ (where << R. ) , the generated heat is approximately KR 2 * generated heat KR_ is significantly lower than the heat KR.. Accordingly, it is noted that as the depth of the current into the mag¬ netic layer increases, the resistance and, hence, the generated heat decreases. In addition, as the current penetrates the low resistance layer, resistance drops .even more drastically to further decrease the generated heat. . _ By employing the two layer laminate structure, Carter and Krumme achieved a highly effective autoregula¬ ting or self-regulating heater useful in various applica¬ tions, such as soldering irons. In addition to the teachings of U.S. Patent No. 4,256,945, related inventions have been set forth in co- pending patent applications. Such inventions have pertained, inter alia, to features including: (a) the prevention of high frequency fields generated in the heater from being radiated into regions adjacent to the heater; (b) the generation of autoregulated heat with a relatively low constant current source; (c) the formation of a laminar structure of two high magnetic permeability layers one of which has a higher Curie point than the other; (d) the use of an autoregulating heater in raising the temperature of a fusible material to a condition of molten flow; and (e) the formation a laminate structure in which a low resistance layer is interposed between two magnetic layers having differing Curie temperatures. OMPI ; The advances in the heating art achieved by the various inventions relating to autoregulation have been useful and significant in numerous fields of application and environments. The present invention expands the utili- ty of these prior advances into new applications and new environments as well as providing new features and useful articles. SUMMARY OF THE INVENTION The present invention relates to an autoregula- ting heater which is porous and is used primarily in the heating of fluids. As a porous, self-regulating heater, the present invention has the various advantages achieved in the above- mentioned autoregulating heaters. For example, the inven- tion does not require additional, often elaborate sensors and control systems. Also, various areas along the heater can provide different levels of generated heat in response to the temperature of the heater at each such area. The generating of heat can thus be localized to effect either a uniform or a predefined variation or gradient of tem¬ peratures along the heater. In addition, however, the present invention features uses and advantages which underscore the signi¬ ficance and synergistic nature of the porous self-regula- ting heater device of the present invention. First, the heater of the invention can serve as a filter as well as a heater. By applying a pressure differential across the porous heater, fluid and contami¬ nants entrained therein can be directed toward the pores. The contaminants can then be trapped and the fluid allowed to pass through. The invention, in such an embodiment, may be used to purify liquids by both filtering and heat¬ ing at the same time. A second and perhaps more notable application of such a device is in a diesel fuel line. When attempt- ing to cold start a diesel engine, a build-up of paraffin, particularly in a fuel filter, may often prevent the flow of fuel and the starting of the engine. The present in¬ vention can alleviate such a problem. When energized, the filter-heater will generate heat, the amount of heat being related to the temperature of the heater device at each given area. Cold or solidified paraffin resting against the filter-heater is then heated in the normal operation of the filter-heater, which results in melting the paraffin. Because the heat tends to concentrate on the cold spots, the device of course realizes thermal efficiency by directing heat where it is most needed. If the heat of normal operation is insufficient, means for internally generating greater levels of heat in the device in order to melt or burn-off paraffin or contaminants may be provided by increasing frequency or current density. The significance of this invention in a fuel line for aircraft is particularly" oteworthy since such a fuel line may undergo severe temperature decreases as the aircraft increases its elevation. The clogging of a fuel filter screen with ice crystals is a long known, serious problem which can be substantially alleviated by the present fil¬ ter-heater. A third context in which a multiple temperature heater-filter may be used is in oceanography. Where sea water is to be collected and/or heated as it passes through a filter, a filter may become clogged with bio- fouling. By heating the filter beyond a normally regu¬ lated temperature to a biocidal level, marine growth may be vaporized or burned off so that the filter can resume normal operation. Additional uses contemplated by the invention include the purification of used motor oil and polymer stripping. it is further contemplated that a porous heater be used in separating, for example, low molecular weight amorphous polypropylene from a polypropylene poly- O mer, amorphous polypropylene having a lower melt transi¬ tion than isotactic polypropylen . The devices of this invention can be used as porous heaters through which fluids flow; porous heaters which filter contaminants from a fluid as it " flows through the device; porous heaters which can be fabricated to regulate fluids at several temperatures; porous heaters which heat local areas to effect either a desired uniform or a variable temperature profile across a fluid; porous heaters that can be switched between at least two temper¬ atures, the higher of which is sufficient to remove con¬ taminants which may be trapped at the pores; or other such porous heaters and combinations thereof which feature autoregulation, or self-regulation. .. The device that achieves these various ends includes at least one thermally conductive layer of a porous magnetic material that has a defined magnetic per¬ meability (μ) versus temperature (T) response wherein, at least over a given temperature range, μ increases as T decreases. The μ versus T response is a function of the- magnetic material employed and the magnetic field to which the layer is exposed. That is to say that over a predefined temperature range, the variation in μ may also be considerably affected by changing the magnetic field. it is preferred that the change of permeability over the predefined temperature range be large in order to enhance the regulation of temperature. In the absence of fluid the device autoregulates at a prescribed temperature. As fluid comes in contact with such a magnetic layer, the fluid comes in thermal equilibrium with the surface of the layer where contact is made. That area of contact decreases in temperature in response to fluid temperature below the autoregulating temperature and (assuming the temperature variation is within the given range) the value of μ will increase. As O PI RN \ μ increases, the skin depth, which represents the depth of current penetration, decreases, resulting in a de¬ crease in current cross-section and an increase in resis¬ tance. When a constant a.c. current is applied across two spaced points on the magnetic layer, the decrease in temperature which leads to an increase in resistance re¬ sults in an appreciable increase in heat generation. That is, the devices of this invention generate more heat when in contact with lower temperature fluids than with higher temperature fluids over the self-regulating temperature range of the heater. Accordingly, this simplest form of the invention permits a fluid to be heated by a heater in an authothermic, self-regulating manner as the fluid pas¬ ses through it. By adding another layer to form a laminate struc¬ ture, the characteristics of the invention are further enhanced. If the added layer has a low resistance, a sharp or well defined cut off temperature can be provided, above which considerably less heat energy is transferred to the fluid. In such an embodiment, current is normally and substantially confined to the skin depth or some other defined depth of penetration of current in the magnetic layer. When the thermal equilibrium induced in the magne¬ tic layer is high, the permeability μ is correspondingly low, resulting in a large depth of penetration. If the depth of penetration becomes larger than the thickness of the magnetic layer, substantial current then also passes through the low resistance, added layer. Once current flow enters this added layer, the heat generated is dras- tically reduced. That is, where the "parallel" resistance 2 of the added layer is relatively small, I R heat is great¬ ly diminished. Hence, at and above the temperature at which the depth of penetration exceeds the thickness of the magnetic layer, comparatively little heat is genera- ted. In this embodiment, the heater assures that the temperature of the fluid (at least over a given ran^f£^ j ^ O PI ►.. wIiPfOu , a is raised to at least a predefined minimum level. A third alternative embodiment or device inclu¬ des at least two magnetic layers that form a laminate structure, each layer having different μ versus T res- ponse. In this embodiment, different fluid temperatures produce different relative responses. Within a single layer, it is recalled, the change in skin depth with respect to temperature depends on changes mainly in μ (the resistivity of the single layer remaining substanti- ally relatively constant) . In this laminate device, when and a.c. current penetrates the first layer and enters a second layer, however, the permeability and resistivity of the second layer also ' affect the heat generated. If the second layer has the same resistivity and a higher permeability than the first layer at a specific tempera¬ ture, the depth of this added current penetration into the second layer is smaller than if the current was to penetrate further into m'aterial of the first layer. A gradient in the heat generation profile thus results as the current penetrates the second layer. If the second layer differs in resistivity as well, the heat generation profile may also exhibit a calculable—although more com¬ plicated—gradient. Moreover, by stacking more than two magnetic layers to form a laminate structure, various heat generation gradients may result corresponding to de¬ termined temperature ranges. A fourth embodiment of the heater which can also vary the heat generation response includes at least one magnetic layer having a thickness, resistivity, or magnetic permeability that varies at different areas within the device. In this embodiment, it is envisioned that the thickness of the magnetic layer may gradually increase from one end of the magnetic layer toward the other. The effect of this change in thickness is readily noted if a low resistance layer of uniform thickness is laminated to one surface of the magnetic layer and a con- OMPI stant a.c. current applied to the magnetic layer. The temperature required for the current to penetrate the mag¬ netic layer and to substantially cut off heat generation thus varies from one end of the magnetic layer to the other. This embodiment can serve to permit a fluid to pass through the device while effecting a progressive thermal gradient across the fluid cross-section. The heating devices of this invention may com¬ prise flat, cylindrical, conical or other such structural configurations comprising at least one porous layer or a plurality of laminated, porous layers. Accordingly, the invention may be shaped for use as a fuel filter-heater, or a hot air gun to precisely heat a given flow rate of gas, or a chemical reaction chamber in which reactants and flow rate can be precisely controlled as to tempera¬ ture, or a fractionation or stripping column for polymers. In addition/ since the heater itself is an in¬ tegral structure, removal and replacement from a support structure can be simplified. A further mode of this invention contemplates the heating of a fluid that is electrically conductive, wherein such fluid passes through at least one porous layer of thermally conductive material encircled by a non- porous magnetic, thermally conductive layer. An a.c. cur- rent is supplied so that it follows a path about the outer surface of the encircling magnetic layer. When the encir¬ cling magnetic layer is below a given temperature, the current is confined to a narrow depth and significant heat is directed to the fluid passing through the porous inner layer or layers. When the encircling layer exceeds the given temperature, the a.c. current spreads inwardly. When the current reaches the conductive fluid, the resis- 2 tance and the related I R heat drop. Thermal control is thereby achieved. In addition, it is noted that the mag- netic layer may be encircled, rather than encircle, the porous layer. That is, a.c. current may then move out- wardly from the inner surface of an encircled magnetic layer until it reaches the conductive fluid, whereat the generation of heat drops. The employment of either or both an encircling and an encircled magnetic layer may be provided. In considering these various embodiments, it is noted that there may be limiting factors such as (a) mate¬ rials and temperature ranges which must be used; (b) con¬ taminants which do not vaporize or burn off in the heater- filter embodiments; (c) flow rate limits (although the invention may be designed to regulate fluid temperature over a wide range of flow rates) ; and (d) the thermal con¬ ductivity of different layers and fluids. In practicing the various embodiments and realizing the sundry advanta- ges and benefits of this invention, these factors should be considered. In any case, regardless of the embodiment, it is preferred that the maximum heat obtained at a minimum power, or maximum I 2R heat, be transferred to a fluid. Specifically, it is preferred that the heater device pro¬ vide several times more heat to the fluid when cold and thus requiring maximum heating rather than to attempt to heat a fluid above a desired level at which little or no heat is required. Proper selection of the material of construction of the heating device can achieve this end. One significant application for the heating devices of this invention is in the area of chemical reaction chambers. In a number of chemical reactions, tight and strict control of the variables in the equation PV = nRT is of significance. Specifically, in the disciplines of polymer synthesis, of organic and inorganic chemistry, and of biochemistry, there are reactions in which tempe¬ rature (as well as other variables) must be closely con- trolled. By proper selection of chamber dimensions and flow rates, together with the employment of heating de¬ vices taught herein, exquisite and explicit control reaction conditions can be attained. Controlled reaction chambers are used in in¬ dustrial applications. Reactions such as large-scale polymerization may be practiced simply and economically when both polymer molecular weight and molecular weight distribution can be controlled and reaction yields maxi¬ mized. Such polymerization reactions include, but are not limited to, free radical initiated, chain propagation reaction polymerization and stepwise condensation reac¬ tion polymerization. By way of example, polymer classes formed by the former type of polymerization include: 1-polyolefins, poly vinyl halides, polyaromatics, poly- alkyl ethacrylates, polyaσrylonitrile, and the like. Examples of the latter type of polymerization include: polyepoxy resins, phenol-formaldehyde resins, polyamides, polyesters, Urea- ' formaldehyde resins, etc. Siliσone poly¬ mers represent yet another example of a material that may be manufactured using th.e heating devices of this inven¬ tion. Furthermore, controlled co-polymerization, alter- nating co-polymerization, block co-polymerization and polymer grafting may employ these porous heating devices. Large-scale industrial applications obviously would involve the use of large reaction units and large heaters; however, the present invention may be employed on smaller scales as well. Such smaller units would find use in organic and in biochemical synthesis. Reaction chambers made using heaters of this invention can feature multiple zones of tightly controlled temperature, as well as pressure, volume, and concentration control. As a result, most any endothermic or exothermic reaction may be carried out resulting in nearly complete reactions and consequently excellent yields by merely selecting optimal reaction conditions. One or more reaction heating zones may be e - ployed in a serial manner in order to sustain biochemical synthesis. Specific amino acid chains, proteins, poly- sachamides, nucleic acid chains, and the like may be pr__. duced by arranging the heating zones (or portions thereof) serially with sequential feedstock inputs. In a preferred embodiment, a reaction chamber would include a heater device that extends entirely along the path length of flow through the chamber. By forming the heater device either as (a) a single layer of alloy having varied permeability versus temperature response along the direction of flow or as (b) a plurality of stacked layers, different levels of heat may be imparted at various locations along the length of the chamber. For example, two reactants A and B may be combined at a first location along the chamber with a heater device raising both reactants to a temperature as they combine to form a mixture M. As mixture M flows through the cha - ber,.it may be raised in temperature by the single or mul¬ tiple layers of the heater device. At a second location along the chamber at which the mixture M reaches a tem¬ perature T / a third reactant C may be entered to combine with the mixture * M. This serial combining or mixing may be necessary since reactant .C must be kept at a tempera¬ ture above T-. or since reactants A and B may combine opti¬ mally at T , with their resultant mixture M combining optimally with reactant C at temperature T to promote a chemical reaction. Thus reaction chambers based on heating devices of this invention permit tightly control¬ led temperature regulation of fluids therein before, during and after a reaction occurs. The term "fluid", it is noted, includes liquids, gases, mixtures, suspen¬ sions, powders, and generally any substance that will flow under sufficient heat and pressure. To enhance the temperature control and safety aspects of such reactions chambers, zones of cooling,— preferably constant cooling,—can also be provided. The cooling zone, if needed or desired, extracts heat from the chamber along at least part of the chamber length. Together with the heater devices, cooling zones permit even tighter thermal control over a reaction than can be OMPI achieved with more traditional methods. The pairing of a cooling zone and a heater de- vice may be needed when an exothermic reaction is to be considered. The heater device may raise the temperature of reactant E to T-.-., and the combine E with a reactant F already at temperature T-J-JJ to yield product N plus heat. Where the heat generated is of an excessive level, two effects occur to reduce the heat level. First, the heater itself automatically, —by self-regulation,—cur- tails the heat transferred to a minimal level. Second, the cooling zone withdraws heat from the reaction stream. In addition, the cooling zone can withdraw sufficient heat to prevent serious overheating. If necessary, a ca¬ talyst coating can be provided within the interior of the chamber to promote a desired reaction. BRIEF DESCRIPTION OF THE DRAWINGS Figure I is a side-view illustration showing one embodiment of a self-regulating fluid heating device comprising a single porous layer of magnetic material. Figure 11(a) is a side-view illustration showing another embodiment of a self-regulating fluid heating de¬ vice comprising two porous layers, one being magnetic and one being low resistance and nonmagnetic. Figure 11(b) illustrates the sharp break in heat generated versus depth of current penetration attainable with such a two layer heating device. Figure III is a side-view illustration showing another embodiment of a self-regulating fluid heating de¬ vice comprising three porous layers-, amely one low resis- tance nonmagnetic layer sandwiched between two magnetic layers. Figure IV is a side-view illustration showing another embodiment of a self-regulating fluid heating device comprising at least two magnetic layers of conical shape. OMPI Figure V illustrates the dependence of perme¬ ability, μ, on temperature, T, for different materials. Figure VI is top-front perspective of a tubular embodiment of a heating device of this invention. Figure VII is a cutaway view of a heater-filter made according to this invention, used in a fuel line environment. Figure VIII is a side-view illustration of another embodiment of a self-regulating fluid heating device having a magnetic layer with a conductive fluid forming a low resistance "layer" against it. Figure IX is a front-top perspective of a cylindrical dual-temperature heating device. Figure X is a cutaway view of one embodiment of a reaction chamber with a self-regulating heater zone within it. Figure XI is a cutaway view of another embodi¬ ment of a reaction chamber with a self-regulating heater within it. Figure XII is an illustration of an embodiment of a reaction chamber having self-regulating heating and controlled presence and volume. DESCRIPTION OF THE INVENTION Referring to Figure I, a heater device 100 is shown comprising of a single layer 102 which is made of a porous, thermally conductive material having a magnetic permeability which, over a given temperature range, de¬ creases with increasing temperature. Such a material preferably has a relatively high effective permeability (μ _> 200) below a first given temperature (T, ) and a per¬ meability of approximately one (μ s 1) above a second higher given temperature (T..) , where T„ > T, . As the temperature of the layer 102 drops in the range between the second temperature (T- and the first temperature (T.) , the permeability increases. When the material of construction of layer 102 is selected such that its resis- "ξfϋREX OMPI tivity does not undergo any appreciable change over the given temperature range (T 2 - T_) , a change in permeabi¬ lity results in a change in skin depth. This fact is readily recognized when one notes the definition of skin depth (S.D.) : S.D. = 5030 p/μfcm. (1) where and are the resistivity and permeability of a material through which an a.c. current at the frequency f passes. With the frequency f and the resistivity p main- tained constant, the skin depth becomes solely dependent on changes in the permeability of the material. More spe¬ cifically, under these conditions: S.D. α 1/ ^μ~ (2) Accordingly, as temperatures increase (within the given range) , permeability μ decreases and the skin depth in¬ creases. Because the current density falls off at a rate equal to e *' , where t is the thickness being con¬ sidered, it is noted that all but (1-1/e) x 100% of the current is theoretically confined to a skin depth. In this description, the term "depth of penetration" of the current is used to represent that thickness beyond which no substantial current flows. This depth of penetration may equal one skin depth or some other thickness at which a predefined theoretical percentage of current flows. When the depth of penetration is the skin depth, expres¬ sion (1) applies. Where the depth of penetration is other than skin depth, expression (1) would require some minor modification although the general principles would remain the same. This change in the depth of penetration beyond which no significant current passes takes on special meaning when a.c. current is, in fact, applied to the layer 102 by a source 104 connected to two points 106 and 108. The contact points 106 and 108, it is noted, OMPI may be located on either surface of the layer 102 with a similar effect being achieved. As shown in Figure I, a fluid 110 flows against the layer 102. The temperature of the fluid 110 varies at different areas along the layer. Along one area on the surface 111 of the layer 102, the temperature of the fluid 110 is T __; at another area the temperature of the fluid 110 is T a-,; and at a third area the temperature of the fluid 110 is T_,. The temperature T_ is lower than temperature T A which, in turn, is lower than temperature T C_, i.e. TJ_B < TA A < TC_,. Because the resistivity p of the layer is considered constant and the frequency f of the a.c. current is held constant, the depth of penetration of the current, represented by the shaded portion 112,- " varies with the temperature-induced changes in permeabi¬ lity of the material as reflected in the permeability μ versus temperature- response curve for the given magnetic material. That is, where the fluid 100 induces the low temperature T_ in the layer 102, the permeability remains high and the depth of penetration remains low. Similar¬ ly, where the higher temperature T Ά is induced in a dif- * ferent area of the layer 102, the permeability is corres¬ pondingly less and the depth of penetration is greater. At the highest temperature T , the permeability is even lower and the depth of current penetration even greater. These variations of the depth of current pene¬ tration with variations in the fluid temperature repre¬ sents one basic aspect of a self-regulating heater. In this regard, it is recognized that the resistance (R) to a current (I) is a function of the cross-sectional area (A) through which the current flow is confined. Speci¬ fically, resistance is inversely proportional to A. The cross-sectional area A is approximately equal to the width (transverse to current flow) multiplied by the depth of penetration. Hence, as shown by the following expressions, a decrease (increase) in depth of penetration causes a decrease (increase in area A, which results in increased (decreased) resistance. For a current I of 2 constant frequency, the value of I — oule heat—trans¬ ferred by the layer 102 to the fluid is greater where the fluid temperature is low and less where the fluid tem¬ perature is high. In Figure I, resistance R is large where the temperature T is low and the depth of current penetration is small. At this area, the Joule heat provided to the fluid 110 is relatively large. On the other hand, where the temperature is high at T , the depth of current pene¬ tration is great, the resistance is relatively low, and the Joule heat generated and transferred to the fluid 110 is relatively low. Accordingly, with reference to Figure I, it is observed that the heating can be localized within layer 102 to provide heat as required to raise the temperature at cold spots while providing little heat where it is not required. Finally, with regard to Figure I, it is noted that the layer 102 is porous. The pores 116 permit the fluid 110 to flow through the layer 102. This aspect is significant not in providing a flow-through heater that is self-regulating; but by properly dimensioning the pores 116, contaminants entrained in the fluid 110 can be en- trapped. The heater device 100 thereby also serves as a filter. The same layer 102 thus ^ fa) senses the fluid temperature, (b) automatically provides heat to the fluid 110 in accordance with where it is needed, and (c) filters the fluid 110 as it flows through the layer 102 if so de¬ sired. In the Figure I embodiment,it is noted that the return path is located opposite the surface 111 which first comes in contact with the fluid 110. Alternatively, the return path in this single layer embodiment may be positioned on the same side of the layer 102 as the fluid 110 itself. According to this alternative embodiment, the surface 111 closest to the fluid 110 is directly hea¬ ted with portions away from the surface 111 being heated by conduction and to a lesser degree. Hence, although both techniques achieve the desired heating, this latter embodiment is more efficient. It should be recognized that the principles underlying the operation of the device in Figure I also apply, for the most part, to the subsequent embodiments which are discussed below. In this regard, however, it will be noted that the location of the ground return path is generally not optional as in the Figure I device. Turning now to Figure 11(a), a two layer embo¬ diment of a heater device 200 according to this invention is shown. The first layer 202 is made of a low resistance, preferably porous, material. The second layer 204 is porous, thermally conductive, and magnetic. That is, the second layer 204 has a relatively high permeability below a first given temperature (T, ) , and a permeability of approximately one above a second given temperature (T_, where T_ > T, ) . (The second given temperature may be referred to as the Curie point) . As discussed relative to Figure I, the material of layer 204 has a permeability which is inversely related to temperature between the first (T- ) and second (T_) given temperatures. The ma¬ terial of layer 204 is also of high resistivity relative to layer 202. The thickness of the low resistivity layer 204 is preferably on the order of one to two skin depths. Layer 202 is laminated to layer 204 to form an interface 206 between them. The layers 202 and 204 are thereby in physical as well as electrical contact-. Connected at two points 208 and 210 on surface 220 of the layer 204 are leads from a source 212, which applies an a.c. current. The current follows a path the depth of which is measured from the surface 220 of the layer 204; that is the surface opposite the interface 206. When the temperature of a fluid 222 is at relative- OMPI ly low (T_ , the depth of penetration of the current is small. However, when the temperature of the fluid 222 is at a high T_, the depth of penetration is large (T_. >> T_) . In fact, the current totally penetrates the magnetic layer 204 and enters the low resistance layer 202. Along this portion of the current path, the two layers appear to be electrically in parallel. Because the layer 202 has low resistance, the parallel combination also has low resistance. The Joule heat generated (where 2 I is constant) thus almost completely drops off because of this severe change in resistance. Hence, where the temperature of the fluid 222 is T_i_, much Joule heat is generated, whereas little heat is generated where the temperature of the fluid 222 is T . - * In the Figure II embodiment, two effects contri¬ bute to self-regulation. First, as in Figure I, an in¬ creased depth of penetration of current into the layer 204 from surface 220 results in decreased resistance and Joule heat. In addition, however, when the current enters layer 202, the resistance drops drastically resulting in a corresponding drop in heat generation. This dual effect is depicted in Figure II(b) which graphically shows how the generated heat (a) is at a maximum where the depth of current penetration is the least; (b) gradually de- creases as the depth of penetration increases; and (c) drops to a minimum when the current enters the low resis¬ tivity layer 202. The graph, Figure 11(b), is provided to show general relationships and is not intended to set forth precise, quantitative relationship between the heat generated and the depth of current penetration. In this regard, the thickness of the layer 204 is defined so that as a predefined temperature T, , e.g. the Curie point for the material of composition of layer 204, the current totally penetrates layer 204 and enters layer 202. That is, at the temperature T,, the depth of penetration exceeds the thickness of the layer 204. Layer 204 is preferably one or several skin depths thick and may be defined as desired. As with the Figure I embodiment, the heater device 200 can also function as a filter as well as a self-regulating, flow-through heater. To achieve filtra¬ tion, the pores in layer 202 or layer 204 or both may be small enough to trap contaminants entrained in the fluid 222. Currently, there are sintered bronze and other porous metal filters. Such filters may comprise the low resistance layer 202 and may be laminated to a magnetic layer 204. The layer 202 in such case would already have an appropriate porosity for a given end use. The magne¬ tic layer 204 should have pores that are preferably grea¬ ter than or equal to the size of the pores in the layer 202 since contaminated and cool fluid would first come in contact with layer 204. Whether used in a heater-filter application or not, there may be a problem with particles clogging the pores of the heating devices 100 or 200. To address this problem this invention further contemplates a multi-level heating feature in which a device can be operated at any of several selectable, self-regulating temperatures. A dual-level heating device 300 is shown in Figure III. The device 300 has a laminate structure which permits the device 300 to effect heating at two different levels. Specifically a low resistance, thermally con¬ ductive layer 302 is sandwiched between two magnetic layers 304 and 306. Coupled to each magnetic layer 304 and 306 is a respective contact 310 and 314. Either con- tact 310 or 314 is selectively connected to one terminal of a two-terminal source of current 316 by the action of a switch 318. The switch 318 also selectively connects the other terminal of the source 316 to a contact 320 or 322. Contact 320 is connected to an electrical conductor layer 324; contact 322 is connected to an electrical con¬ ductor layer 326. Sandwiched between the conductor layer 324 and the magnetic layer 304, is an electrical insula- tor layer 330. Similarly, sandwiched between the con¬ ductor layer 326 and the magnetic layer 306 " is an elec¬ trical insulator layer 332. The switch 318 in a first (up) position creates a current path through contact 310, magnetic layer 304, insulator layer 330, conductor layer 324, and contact 320. In this switch position current penetrates a thin depth of the magnetic layer 304 proxi¬ mate the interface with the insulator layer 330 when the temperature of the magnetic layer 304 is low. When the temperature is high, the depth of penetration increases, eventually reaching the low resistance layer 302 which results in a substantially cut-off of heating. Moving the switch 318 to a second (down) position creates an alternate current path through contact 314; layers 306, 332, and 326; and contact 322. By choosing the materi¬ als of construction of layers 304 and 306 with the appro¬ priate resistivities and permeabilities, the switching of the a.c source 316 to one of the layers {e.g. 304) can result in considerably more heat being generated than if the source 316 were connected to the other layer (e.g. 306) . The level at which less heat is generated may re¬ present the normal operating level for raising a fluid to a desired temperature. The level at which greater heat is generated may represent a level at which elements which clog the pores and must be removed either vaporize or burn-off. By switching the source 316 to one set of con¬ tacts, the fluid heating level is achieved; by switching the source to the other pair of contacts, unclogging is performed by pyrolyzing contaminants. This dual-level embodiment would be particularly useful where organic fouling or contaminants (such as biofouling in an oceano- graphic context or paraffin in a diesel filter context) are to be removed from the pores. By way of example, assume that the two magnetic layers 304 and 306 have the same resistivity, but layer 304 has an effective permeability of 1000. The skin depth of layer 304 is proportional to 1/ j 200 whereas the OMPI skin depth of layer 306 is proportional to 1/ 1000. When switched to the contacts 312 and 314 (on layer 306) the a.c. current encounters high resistance resulting in large I R heat generation. This heat is conducted throughout the laminate structure of device 300 and is preferably sufficient to vaporize or burn-off the removable elements deposited on the pores of any of the layers 302, 304 and 306. When connected back between contacts 308 and 310 (on layer 304) , the current encounters less resistance and sufficient heat is provided to only raise the tempera¬ ture of the fluid. As in the Figure 11(a) mode, the heat is substantially reduced if the depth of penetration total¬ ly penetrates either magnetic layer 304 or 306 and enters the low resistivity layer 302. A similar multi-level thermal effect is achiev¬ able in the Figure I embodiment by stacking a layer of a second magnetic material, with differing resistivity and/ or permeability characteristics, against it. Two pairs of contacts would likewise be provided to switch the σur- rent between the alternative paths. One path or layer would provide sufficient heat for raising the fluid tem¬ perature; the other path or layer would generate enough heat to burn off or vaporize the clogging contaminants. Figure IV illustrates a conically-shaped heater device 400 that has an inner porous magnetic layer 402 _of conical shape against and within an outer porous magnetic layer 404 also of conical shape. Fluid 406 flows into . the large diameter opening 407 of the device 400 and to¬ ward the apex 412 of the cone of the device 400. An a.c. current source 408 is connected to substantially confine current to a narrow depth along the inner surface 410 of layer 402 of the device 400 when the temperature of the fluid 406 at a given area on the device 400 is below a desired level. When the fluid 406 at an area within the cone is at or above the desired temperature, the depth of current penetration is great. As a result, resistivity is reduced and I 2R heating diminished. It is notable that in the Figure IV embodiment heat is concentrated at the apex 412 of the device 400. This effect is due to an increase in resistance as the apex 412 is approached. Resistance, as previously noted, is inversely proportional to the cross-sectional area A through which current flows. The area A is equal to (depth of current penetration) X (width of current path) . It is observed that for a conical element the width of the current path corresponds to the circumf rence. As the circumference decreases toward the apex 412, the area A decreases and resistance tends to increase. Hence, at low temperatures where the permeabi¬ lity of layer 402 remains at a high effective level, the application of a.c. current to the layer 402 results in a large concentration of heat being provided at the apex 412. When used as a filter, such as in a diesel fuel filter, this feature of this invention is particularly significant. If fuel, for example, is contained by the device 400 at a low temperature before an a.c. current from the source 408 is applied, the device 400 may be clogged with paraffin or the like. When the a.c. current is switched on, heat is concentrated at the apex 412 which will melt the paraffin next to it. Fuel is then able to at least flow through the apex 412 and easier diesel start-up is achieved. Heat spreads out to other regions on the device 400 away from the apex 412. As the fluid approaches a desired temperature,, the inverse relationship between μ and T dominates and autoregulation over a given temperature range is achieved. That is, the depth of current penetration varies with changes in permeability to thereby affect the heat ge¬ nerated at each area of the d ' evice 400. Still referring to Figure IV, it is noted that the conical shape is similarly applicable to embodiments generally suggested in Figures I, II and III, such as an embodiment comprising a single porous magnetic layer of OMPI a conical shape or an embodiment comprising a porous mag¬ netic layer and a porous low resistance layer shaped and positioned to form a conical, laminate structure. The principles of (a) concentrating heat at the apex, espe- cially at temperatures well below a desired level, and (b) autoregulating at or near the desired temperature still apply. Referring now to Figure V, the permeability versus temperature response for several magnetic materials which may be used as magnetic layers in the present inven¬ tion are shown. This graph shows how the permeability (μ) for these various materials is inversely related to temperature (T) over a given range; that is, μ increases when T decreases. The graph,- Figure V, may be supplemen- ted with similar curves for other magnetic materials shown in the following Table 1. TABLE 1 MAGNETIC RESISTIVITY EFFECTIVE MATERIAL CURIE POINT P PERMEABILITY * 30% Ni 70% Fe 100° C 80 X 10 " ^ 100 - 300 36% Ni 64% Fe 279° C 82 X 10 J 100 - 300 42% Ni 58% Fe 325° C 71 X 10 " 200 - 400 46% Ni 54%. . Fe -460° C 46 X 10~ 200 - 400 52% Ni 48% Fe 565° C 43 X 10 " 200 - 400 80% Ni 20% Fe 460° C 58 X lo "" ;? 400 - 1000 Kovar 435° C 49 X 10~ 400 - 1000 Low Carbon Steel 760° C 10 X 10- 1000 Cobalt 1120° C 9.8 X 10 " >1000 Nickel 353° C 6.8 X 10~ b > 500 * below Curie point As noted in Table 1, these materials vary in Curie point, resistivity, and effective permeability (at temperatures below the Curie point) . The choice of materials of con¬ struction for use in the embodiments set forth in Figures I, 11(a), III, and IV can provide the sundry properties and characteristics needed in tailoring the heater device to a particular application. Figure VI illustrates a cylindrical or tubular structure device 600. This device 600 is particularly amenable to use as a filter, such as a diesel fuel filter. The device 600 is shown having two concentric cylindrical porous layers 602 and 604 laminated as in the two layer embodiment of Figure II. A solid end plug 618 forces the fluid 606 to flow through the pores of the layers 602 and 604. As in Figure II, layer 602 is of magnetic material as described above and layer 604 is a low resistance ma¬ terial, such as porous copper or bronze. Fluid, shown by arrows 606, flows through the device 600 and is heated and, optionally, filtered at the same time. The heating is achieved by a.c. current which passes between contacts 610 and 612 from a source 614. The contacts 610 and 612 are preferably, but not necessarily, located as shown in Figure VI attached to the magnetic layer 602. In this regard, a.c. current follows a path along the inner surface of layer 602 bet¬ ween the contacts " 610 and 612. The a.c. current is con¬ fined in depth of current penetration due to the skin effect. AS previously discussed, the two layers 602 and 604 provide the two effects of a self-regulating heater. If the temperature of the fluid is at the autoregulating temperature and the permeability, μ, is low, the depth of current penetration extends from the inner surface of layer 602 outward into layer 604. Under this set of con¬ ditions, little heat is transferred to the fluid 606. If the fluid 606 falls to a temperature below the desired temperature, e.g. Curie point of the material of layer 602, the current recedes from the layer 604 and follows a narrower path within the layer 602 itself. As the skin depth decreases, both the effect of decreased depth and the effect of current receding from the layer 604 cause increased resistance and thus increased heating. To force fluid 606 through the device 600 to effect heating and filtering, a pressure differential is provided by con¬ ventional means, e.g. a pump, gravity, etc. O PI In Figure VII, a tubular device 700 like that of Figure VI is shown in a fuel line. The fuel line has an inner tube 702 coupled to a larger overlappping tube 704. The fuel shown by arrows 706 passes through the pores in the device 700. Self-regulated heating is, again, affected by sending an a.c. current from source 710 to the tubular device 700 so that current normally travels mainly along the surface 711 of a magnetic layer 712 that is opposite the interface 714 between the mag- netic layer 712 and a low resistance layer 716. At higher temperatures, a.c. current spreads outward and into layer 716, resulting in little heat ge¬ neration. With regard to Figure VII, it should be realized that the device 700 may serve as a heating device and as an optional filter with the pressure differential in the opposite direction as well. That is, fluid forced from tube 704 to tube 702 would also be heated andfiltered. Reference is now made to Figure VIII in which a cylindrical heater device 800 is shown having a porous cylindrical layer 802 encircled by a solid tubular magnet¬ ic layer 804. An a.c- source 806 is connected so that current flows along the outer surface of solid magnetic layer 804. As the temperature decreases, current spreads inwardly and eventually enters the cylindrical porous inner layer 802. By passing an electrically conductive fluid 808 through the- layer 802, the layer 802 acts as a low resistance layer. That is, when current spreads into layer 802 with conductive fluid 808 in its pores, the current follows a low resistance path through the fluid 808 and along the outer surface of layer 802. If the layer 802 is also low resistance, the layer 802 with conductive fluid 808 flowing through it simulates a solid layer for purposes of heat generation and transfer. Similar to Figure VIII it should be recognized that a dual-temperature device 850 based on Figure III O P1 may be readily envisioned as shown in Figure IX. In Figure IX, a tubular nonporous magnetic layer 852 encir¬ cles a cylindrical electrical conductor 854 with a tubular electrical insulator 856 being interposed therebetween. Coaxial with and encircling this magnetic layer 852 is a porous layer 858. Coaxial with and encircling the porous layer 858 is an outer nonporous magnetic layer 860 which, preferably, has a different permeability and, optionally, resistivity response relative to temperature than layer 852. The porous layer 858 is preferably of low resistance but, in any case, becomes low resistance as an electric-r¬ ally conductive fluid 862 flows through it. The porous layer 858 is in contact with the inner magnetic layer 852 and with the outer magnetic layer 860 to permit electrical and thermal conduction between them. Because of their proximity, layers 852, 858, and 860 are thermally conduc¬ tive. As in Figure III a switch 864 is provided to initially confine current from an a.c. source 866 to either the outer surface of layer 860—with the switch 864 in the lower position—or the inner surface of layer 852— with the switch 864 in the upper position. In either case, current spreads toward the porous layer 858 as the depth of current penetration increases. The thickness of the porous layer 858 is preferably on the order of five skin depths—as it is also in low resistance layers of the Figure III and Figure VIII devices. Referring to Figure X, a reaction chamber 900 is shown. The reaction chamber 900 includes a pre-reac- tion zone 901 into which reactants A, B, and C are intro- duced and a reaction zone 902. Along a length of the pre- reaction zone 901 is a self-regulating heater 904 compris¬ ing two porous layers 906 and 908. Layer 906 is a ther¬ mally conductive, preferably high resistance magnetic material. Across points 910 and 912 an a.c. current is applied. Due to the skin effect, the a.c. current is substantially confined to a thickness defined by the above noted expression As the layer 906 increases in temperature (over a predefined ' range) , the permeability μ for layer 906 decreases causing the a.c. current to spread into layer 908. In one form of the invention, the layer 908 is a thermally conductive, low resistance, nonmagnetic material. In this embodiment, the resistance heating drops off sharply when the current begins to flow through the layer 908. That is, above a temperature of T__ at which the a.c. current enters the layer 908, little heat is provided. Hence, both reactants A and B will be raised to temperature T _, as they enter the pre-reaction zone 901. As a result of normal or induced mixing, the reactants A and B combine to form a mixture M that enters the reaction zone 902 to chemically react with another reactant C which can be introduced directly into the reaction zone 902. Either or both reactants A and B can enter upstream of layer 906 or tangential to the surface of layer 906 to cause mixing. Mixture M and reactant C each flow through another heater device 916 comprised of a single porous, magnetic layer and having contacts 918 and 920 which are connected to a source (not shown) . The device 916 provides more and less heat depending on how deeply a.c. current penetrates it. If the initial temperature (T ) of the mixture M is too low, the depth of current penetration in layer 908 decreases or termi¬ nates and the amount of heat generated increases to raise the mixture M to temperature T__. Reactant C is also raised to temperature T , which represents the optimal reaction temperature. At temperature T__, maximum yield, for example, can be achieved. In order to permit reactants which exceed the optimal temperature T__. to be cooled down, cooling pipes 924 can be used to withdraw heat from the reaction zone 902. The cooling pipes 924, or other such cooling mechanisms, serve at least two purposes. First, the cooling pipes 924 can provide constant cooling which may prevent reaction runaway or the reaction zone overheating in a highly exothermic reaction. Secondly, the cooling pipes 924 may lower the temperature in the reaction zone 902 while the heater device 916 generates heat to raise the temperature. The combined effects of the cooling pipes 924 and heater device 916 can thus very narrowly define the temperature range in reaction zone 902 and also increase the speed of response to slight changes in re¬ actant temperatures. As an alternative, the layer 908 may comprise another layer of magnetic material. In this alternative embodiment, layer 906 and 908 have preferably, distinct and different μ versus T responses. Accordingly, a spe- cific heat versus temperature profile can be defined along the length of the heater device 904. Referring now to Figure XI, a cylindrical reac¬ tion chamber 1000 is shown having a pre-reaction zone 1002, a reaction zone 1004, and a post-reaction zone 1006. Along the length of the chamber 1000 is an elongated, cylindrical porous layer 1008 made of a magnetic material with high permeability, μ. Distributed at various loca¬ tions along the length and within the chamber 1000 are cooling pipes 1010, 1012, 1014 and 1016. Each of these cooling pipes, 1010, 1012, 1014 and 1016, have separate controls. Reactant E enters pre-reaction zone 1002 and passes through the porous layer 1008. An a.c. current is supplied to layer 1008 through contacts 1020 and 1022. The current flows along the outer surface of this cylin¬ drical layer 1008, the depth of penetration being depen¬ dent on the value of μ at a given time and location along the layer 1008. If the temperature of reactant E is below a desired temperature, cooling pipes 1010 and 1012 may be shut off. However, it is within the teachings of this invention that the cooling be maintained continuously. OMPI Also if the temperature of reactant E is below in desired level, the depth of current penetration along the pre- reaction zone 1002 is small—the μ versus T response for layer 1008 along the pre-reaction zone having been de- fined to achieve this result. The amount of Joule heat thus increases as the depth of current decreases, with heat being transferred to reactant E. Reactant F, which may already be at a desired temperature is fed directly into the reaction zone 1004. Reactants E and F may, optionally, pass through a sheet 1026 of catalyst. Catalytic pellets, coatings, or other elements can be provided within the reaction zone to pro¬ mote the desired reaction. After E and F react, a pro¬ duct N then flows through the post reaction zone 1006. For exothermic reactions which are to be run und ' er tight thermal control, the embodiment in Figure XI is especially noteworthy. First, the cooling pipe 1014 will withdraw heat from the reaction zone 1004. Second, as the reaction zone 1004 heats up, the current will pene- trate the entire layer 1008—the current will spread from the outer surface inward toward the center of the layer 1008—to minimize the generation of heat. If the dia¬ meter of the layer 1008 is large, the difference in heat generated either when the layer 1008 is barely penetra- ted and/or when it is totally penetrated will be large. Third, the amount of cooling is preferably gauged to the maximum heat which can be generated in the reaction. It should also be realized that the depth of penetration may be affected by varying the composition of the layer 1008 along its length. For example, if layer 1008 is an alloy, the μ versus T characteristic along the length and/or cross-section can be varied as desired. If the alloying is varied in discrete steps along its length, a laminate structure can be simulated. By proper selection of material along the length of layer 1008, it is contemplated that a fluid passing through the pre-reaction zone at a given tempe- rature will be heated while a fluid passing through the reaction zone at the same given temperature will see lit¬ tle heating within the layer 1008. It should be noted that the resistivity of the layer 906 and of the layer of device 916 (in Figure X) and of the layer 1008 {in Figure XI) may also affect the measure of heat generated—although to a lesser extent than permeability. In addition, the frequency f and amplitude of the a.c. current may also affect the level of heating. Finally, the magnetic field to which a mag¬ netic material is exposed also affects the μ versus T response and thus represents another parameter for ad¬ justing heat transfer. All of these factors may be con¬ sidered in controlling the temperature of a liquid, gas, suspension, or other flowing substance passing through a reaction chamber. Referring again to Figures X and XI, it should be realized that the pores of the layers 906, 908, 916, and/or 1008 may be dimensioned small enough to entrap contaminant particles. The filtering of such particles may not only enhance yield but may also reduce the for¬ ming of undesired by-products such as gel. To free the pores of such particles, a layer may be raised in tempera¬ ture high enough to vaporize the particles or burn them off. This elevated temperature may, of course, be achieved by increasing the current amplitude or frequency, by increasing μ or otherwise increasing the resistance to current, by directing a high d.c. current across the layer, by switching the current between either of two laminated layers one of which provides more heat for a given current, or by other means. Turning now to Figure XII, a particularly sig¬ nificant aspect of this invention is depicted. A tape¬ red reaction chamber 1100 is shown having circumference which varies along its length. The pre-reaction zone 1102 has a funnel shape the small end of which leads in¬ to the reaction zone 1104. The reaction zone 1104 has a constant cross-section which leads into a bell-shaped cross-section of the post-reaction zone 1106. In this embodiment, a reactant H enters the pre-reaction zone 1102, the flow rate being controlled by a valve 1108. It is readily noted that the pressure and the volume of the reactant H enroute to the reaction zone 1104 is determined mainly by the dimensions of the pre-reaction zone 1102 and the flow rate of the reactant H. A heater device 1110 (comprising one or more layers as described above) is positioned within the pre-reaction zone 1102. A cooling pipe 1112 is also included within this zone. By noting that, at least for a gas: PV = nRT where P is pressure, V is volume, R is a constant, and T is., emperature (n being moles) , it is recognized that the embodiment of Figure XII reflects desired control over P, V, and T. Accordingly, precise control of a reaction can be achieved. With regard to the chamber dimensions shown in Figure XII, it should of course be realized that any of several shapes may be employed at each zone as a particu¬ lar reaction may require. It should also be understood, that any and all zones may include cooling pipes or self- regulating heater devices or both as desired. There are of course numerous ways of controlling temperature along the length of a reaction chamber. In the pre-reaction zone, e.g. zone 1102 of Figure XII, a reactant H may be either { a) lowered in temperature due to the withdrawal of heat by the cooling pipe 1112; or (b) maintained at its entry temperature; or (c) elevated in temperature by the heater device 1110. Fluids in the reaction zone and in the post-reaction zone may similarly be lowered, maintained, or raised in temperature since cooling pipes and heater devices are included in each zone. The temperature control across the reactor need not, of course, be constant but can be varied depending on the fluid being heated, its flow rate, the dimensions of the chamber, variations in p or μ along the chamber length, and other factors. In accordance with the invention, reactions might include controlled temperature variations within one reactor zone. For example, a reactant J at a high temperature may be cooled along a first length of the pre-reaction zone so that it may be mixed at a certain temperature with a reactant K. The mixture may then be further elevated in temperature in the pre-reaction zone enroute to the reaction zone. Other such combinations are also contemplated and within the scope of this in¬ vention. By way of example and not limitation, the fol- lowing examples suggest how the present invention might be employed in controlling chemical reactions. The present invention is capable of broad use in controlling chemical reactions since it permits tight control of various reaction conditions, before, during and after a reaction takes place. It is well known that some reactions use batch processing techniques; however, the present invention is more useful in continuous pro¬ cessing. Some polymerization reactions requiring the conditions listed have been selected as illustrative exam- pies. Strict temperature control during and after the reaction are required for processes disclosed in: 1) U.S. Patent No. 2,518,388 issued to Simon for urea-formalde¬ hyde adhesives; 2) Silicon resin formation as in Polymer Synthesis II. Chapter 4, pg. 114, ed. Sandier, Karo; Academic Press, New York, NY (1977) ; 3) Poly Epoxy for¬ mation using the method of Ravey et al, J. Polym. Sci. S Polym. Chem. 12, 2821 (1974) . Strict temperature con¬ trols of the pre-reaction stages are required for alkyd resins formation using the method of Martens in Alkyl Re- sins, pp. 71-73, Van Nostrand, Princeton, NJ (1961). Narrowly defined temperature and pressure con¬ trols must be used for the following reactions: 1) Ferrocene using the method found in Organic Polymeric Semiconductors, Chapt. 4, Paushkin et al ed., John Wiley & Sons, NY (1974); and 3) Block Copolymerization ' (tetra- hydrofuran method) using the method of Saegusa et al in Block Polymers pg. 293 Plenum Press, NY (1970) . In addition to the above embodiments, it should be noted that this invention also encompasses other as¬ pects. First, it should be noted that skin depth and depth of current penetration are functions of current - frequency as well as the resistivity and permeability of the material of construction. It is within the scope of this invention to select any of these parameters to provide additional means for decreasing the depth of cur¬ rent penetration to increase the heat generated for con- taminant vaporization or burn-off. Similarly, the inven¬ tion has suggested above that current amplitude (I) re¬ mains constant. By permitting this factor to vary in a prescribed fashion, the heat response can further be ad¬ justed. Second, in the Figures the various embodiments show each layer having uniform thickness and apparently uniform composition. Additional modes of this invention could provide for tapered thicknesses and/or varying the alloy compositions of a layer along the current path. By these techniques, thermal gradients may be readily pro¬ duced. For example in Figure II if the magnetic layer 204 were to be tapered so that it was thicker toward one end, the current would totally penetrate the less thick portion before penetrating the thicker end of the layer 204. The thicker end would still be generating consider¬ able heat while the thinner end would generate much less, although both ends and the entire layer will still be in contact with fluid at a single given temperature. Similar effects can be achieved by varying the alloying along the layer, thereby varying the permeability versus temperature response at different areas along the current path. Third, it should be realized that this invention suggests that a differential pressure may or may not be applied to force fluid through any of the heater devices or heater-filters. Fluid may thus, optionally, diffuse or be forced through the pores in the various layers. Fourth, the heat generated by a device of this invention may vary between a maximum and mini-mum, the ratio of which depends on the various factors discussed above and their interrelation. Ratios minimum to maximum heat output of 6:1 or 45:1, for example, may be achieved. Fifth, especially with regard to the device 700 of Figure VII, it is within the scope of this invention to provide a mechanism for inserting these heating devices in other systems such as the fuel line 702. That is, the device 700, for example, may be inserted or removed from such a system by means of conventional coupling techniques. Sixth, in embodiments employing a low resistance layer it is usually preferred that such a layer be non¬ magnetic and thermally conductive although not necessarily so. Seventh, it is noted that this invention is directed toward an autoregulating heater that is porous so that fluid can pass through it. This generic concept includes further embodiments characterized by having at least one porous layer and at least one non-porous layer, and at least one layer which is magnetic so as to provide an autoregulating effect. This effect may be achieved by passing the fluid through a porous magnetic layer or by passing the fluid through a porous low resistance, non¬ magnetic layer in thermal contact with a porous or non¬ porous magnetic layer. Eighth, according to this invention, heater de¬ vice can be designed to autoregulate the temperature of a fluid so as to achieve a maximum flow rate. At or below this maximum flow rate, in other words, the heater device raises the temperature of the fluid to a desired level. Finally, it should be recognized that features and elements of any one embodiment may be included in OMP other embodiments. For example, dual-level temperature control for eliminating contaminants may be used with any heater which may be clogged; diffuse or pressurized fluid flow may be employed with the various embodiments; and the use of a plurality of magnetic layers with one or more low resistance layers may form a laminate struc¬ ture according to this invention. The term "ground" in the illustration of ground in the drawings although basically applicable only to a d.c. circuitry, are employed for purposes of clarifying the location of the concentration of current in the vari¬ ous conductors. In RF systems, a coaxial cable is nor¬ mally connected between the power supply and the heater. In such circuits the so-called "ground" connection is'made to the shield of the cable and the "ungrounded" connec¬ tion is made to the cable center conductor. It should be noted that preferably fluid should flow first through the layer remote from the current re¬ turn path and then through the layer of ferromagnetic ma- terial adjacent the current return path. This assumed that fluid flows at a constant flow rate through the de¬ vice. In the vast majority of cases the remote layer is at least two to three times thicker than the adjacent layer. Thus by flowing fluid in the recommended direc- tion the fluid may be raised to autoregulating tempera¬ ture over a greater period of time and the heat input may be less than in the case when fluid flows in the opposite direction. Finally, if such reverse flow is used, suf¬ ficient heat must be applied to raise the fluid to auto- regulating temperature well before the fluid exits the adjacent layer or autoregulating cannot be achieved. The additional heat dissipates into the remote layer and may cause the fluid temperature to raise above the auto¬ regulating temperatures in the remote (uncontrolled) layer. Moreover, it is noted that the source of cur¬ rent may be an ohmic source, an inductive source, other desired source of current at a selectable amplitude and frequency. Other improvements, modifications, and embodi¬ ments will become apparent to one of ordinary skill in the art upon review of this disclosure. Such improve¬ ments, modifications and embodiments are considered to be within the scope of this invention as defined by the following claims. ^JRE ^ OMPI

Claims: I Claim: 1. A device for regulating the temperature of a fluid, the device comprising: a laminar structure having (a) a first therm- ally conductive layer comprising a low resistance material and (b) a second, thermally conductive layer comprising a high resistance magnetic material the permeability μ~ of which is inversely related to temperature over a given temperature range, at least said first layer or said second layer being porous and at least a ' portion of a porous layer being adapted to have the fluid flow in the pores thereof; and an interface between said first layer and said second layer which permits good electrical and thermal conduction between said first layer and said second layer. 2. A device as in claim 1 further comprising: means for passing an a.c. current through said laminar structure so that the depth of penetration of a major portion of the current is measured from the surface of said second layer opposite said interface, the depth of penetration d2 into said second layer being defined accord¬ ing to the expression: the magnitude I of the current through and the resistance R of each area on said second layer determining the quantity of I 2R heat transferred to the fluid at each said area; the quantity of heat transferred to the fluid by each such area in contact with the fluid being inversely related to the temperature of the fluid at such area over said range of temperature, thereby providing a self-regula¬ ting control of fluid temperature over said range of fluid temperatures. OMPI 3. A device as in claim 2 wherein said second layer has a thickness which is totally penetrated by the current when the temperature thereon exceeds a predefined level T, . 4. A device as in claim 3 wherein the depth of penetration d, of current into said first layer when said second layer is totally penetrated (a) is measured from said interface into said first layer and (b)is determined by the formula: d ι α ^/^r where μ_ is the magnetic permeability of said first layer along-the current path. 5. A device as in claim 2 wherein said current source means provides current of a fixed amplitude and constant frequency. 6. A device as in claim 3 wherein said current source means provides current of a fixed amplitude and constant frequency. 7. A device as in claim 4 wherein the depth of penetration d, , if any, into said first layer and the depth of penetration d 2 into said second layer is variable along said laminar structure, the depths of penetration d. and d 2 aligned with each area on said second layer increas¬ ing in accordance with the temperature of the fluid in contact with each said area; and 2 wherein the I R heat applied to each said area is greater when the fluid in contact with said each area induces a temperature below T, , than when the fluid in contact with said each area induces a temperature of at least T-. O PI 8. A device as in claim 3 wherein the permea¬ bility versus temperature characteristic differs at differ¬ ing areas on said second layer. 9. A device as in claim 2. wherein the permea- bility μ of the magnetic layer varies inversely with temperature between (a) an effective permeability and (b) a permeability of substantially one, the Joule heat gen¬ erated in response to the application of a constant a.c. current being at least great enough to raise the fluid to a desired autoregulation temperature when the layer has said effective permeability. 10. A device as in claim 1 wherein the fluid has contaminants therein, wherein said first layer is porous, and wherein the fluid is forced under pressure through the pores in said first layer, the pores in said first layer being sufficiently small- to prevent the flowing of contaminants therethrough; said laminar structure layer thereby filtering contaminants from the fluid. 11. A device as in claim 3 wherein the fluid has contaminants therein, wherein said first layer and said second layer are porous, and wherein the fluid is forced under pressure through the pores in said first layer and in said second layer; and wherein the pores in said first layer and the pores in said second layer are sufficiently small to pre¬ vent the flowing of contaminants therethrough; said laminar structure thereby filtering contaminants from the fluid. 12. A device as in claim 9 wherein the fluid has contaminants therein, wherein said first layer and said second layer are porous, and wherein the fluid is forced -.. under pressure through the pores in said first layer and in said second layer; and wherein the pores in said first layer and the pores in said second layer are sufficiently small to pre- vent the flowing of contaminants therethrough; said laminar structure thereby filtering contaminants from the fluid. 13. A device as in claim 10 further comprising: means for heating the laminar structure to a temperature T 2 at which pores are freed of filtered con¬ taminants. 14. A device as in claim 12 further comprising: means for heating the laminar structure to a temperature 2 at- which pores are freed of filtered contaminants. 15. A device as in claim 1 wherein the heating means comprises: a third layer comprising a magnetic material having a permeability μ 3 and a resistivity p 3 , the third layer (a) being in electrical and thermal contact with the surface of the first layer opposite the interface; and (b) being characterized in that the resistance to current therethrough is relatively greater than the resistance to current through said second layer, under similar conditions; means for selectively switching the a.c. cur¬ rent to be applied either between (a) two points spaced along said second layer or (b) two points spaced along said third layer; the I 2R heat generated when the current is applied between two points spaced along said third layer being greater than when switched between two points spaced along said second layer. 16. A device as in claim 14 wherein the laminar structure forms a multilayered tubular structure, the first layer encircling the second layer. 17. A device as in claim 15 wherein the laminar structure forms a multilayered tubular structure, the first layer encircling the second layer and the third layer encircling the first layer. 18. A device as in claim 14 wherein the pressure on the fluid within the tubular structure is greater than the pressure outside the tubular structure; and wherein the fluid is forced through the pores in the first layer and the second layer effectuating fil¬ tration and self-regulated heating simultaneously. 19. A device as in claim 1 wherein the laminar structure forms a multilayered tubular structure, the first layer encircling the second layer. 20. A device as in claim 2 wherein the thickness of the second layer is uniform. 21. A device as in claim 3 further comprising: at least one additional layer of magnetic material, each additional layer having a corresponding resistivity .p. and temperature versus permeability μ. characteristic, all the layers of magnetic material being stacked, each pair of adjacent magnetic layers being in electrical and thermal contact along a corresponding common surface, a surface of one of the additional layers lying against and in electrical contact with the surface of the second layer opposite the interface. OMPI 22. A device as in claim 2 wherein the temperature of the fluid is regulated to be at a level substantially at ' or above the temperature T,. 23. A device as in claim 7 wherein the temperature of the fluid is regulated to be at a level substantially at or above the temperature T- . 24. A device as in claim 11 wherein the temperature of the fluid is regulated to be at a level substantially at or above the temperature T, . 25. A self-regulating heater which filters con¬ taminants from a fluid, the heater comprising: a laminar structure having (a) a first layer comprising a porous, low resistance, nonmagnetic material and (b) a thermally conductive second layer electrically and thermally sealedly interfaced with said first layer, said second layer comprising a porous, magnetic material, the permeability of said magnetic material varying inversely between two identifiable temperatures, and; means for directing an a.c. current to pass between two points on the surface of said second layer opposite the interface with the first layer; wherein Joule heat is transferred to the fluid from each area on said second layer in a quantity inversely related to the temperature, in a given range, of the fluid flowing through the pores at said each area; wherein fluid flows through the pores in the first layer and the second layer; and wherein the pores in the first layer are smaller in cross-section than the cross-section of the contaminants. 26. A device as in claim 25 wherein the pores defined in the second layer are smaller in cross-section than the cross-section of the contaminants. 27. A device as in claim 25 wherein the laminar structure comprises a multilayered tubular structure, the first layer circumscribing the second layer. 28. A device as in claim 27 further comprising: a cap which closes off one end of the tubular structure. 29. A device as in claim 27 wherein the first layer is thermally conductive and the device further com¬ prising: means for heating the laminar structure to a temperature T-, at which pores are freed of filtered con¬ taminants. 30. A device as in claim 3 wherein the magnetic layer along the path of current provides differing resis- tances and levels of heat generation therealong when all areas therealong are subjected to the same temperature level and current amplitude. 31. A device as in claim 12 wherein the magnetic layer along the path of current provides differing resis¬ tances and levels of heat generation therealong when all areas therealong are subjected to the same temperature level and current amplitude. 32. A device as in claim 22 wherein the magnetic layer along the path of current provides differing resistances and levels of heat generation therealong when all areas therealong are subjected to the same temperature level and current amplitude. 33. A device as in claim 30 wherein the magnetic layer has a tapering thickness along the path of the current. 34. A device as in claim 31 wherein the magnetic layer comprises alloy material which has a different per¬ meability versus temperature characteristic at different - areas along the current path. 35. A device for regulating the temperature of a fluid under pressure flowing along a path, the device comprising: a first layer of thermally conductive, porous magnetic material having a defined temperature T vs. μ permeability characteristic wherein the permeability of the magnetic material is inversely related to temperature over a range of temperatures; the fluid being in contact with and passing through the pores in the magnetic layer. 36. A device as in claim 35 wherein the thermally conductive layer comprises a conical magnetic layer the axis of which is at least substantially aligned with the flow path of the fluid. 37. A device as in claim 36 further comprising: means for applying an a.c. current between the apex and circumferential ridge of the conical first layer, he depth of penetration of a.c. current in the con¬ ical first layer increasing and decreasing with respective increases and decreases in temperature. 38. A device as in claim 37 wherein the fluid has contaminants therein; and wherein the pores in the magnetic layer are sufficiently small to filter the contaminants from the fluid as the fluid passes through the pores. 39. A device as in claim 36 further comprising: a second thermally conductive, porous conical layer in contact with and coaxial with said first layer. 40. A device as in claim 39 wherein said second conical layer is electrically conductive and disposed around said first layer; and wherein the a.c. applying means has a ground return path whereby a.c. current flows (a) along the inner conical surface of said layer of porous magnetic material at temperatures below a predefined level and (b) spreads into said conical layer at temperatures above a predefined level. 41. A device as in claim 40 further comprising: a third conical layer; wherein the third conical layer comprises " a porous magnetic material having a different μ versus T characteristic than the first layer; the second layer being (a) sandwiched between the first layer and third layer and (b) in thermal and electrical contact therewith; and wherein the a.c. applying means further com¬ prises: means for selectively directing a.c. current along either the inner surface of the first layer or the outer surface of the third layer, the a.c. current spread¬ ing into the second layer (a) from the first layer at temperatures above a first level when a.c. current is directed therethrough and (b) from the second layer at temperatures above a second level when a.c. current is directed therethrough. 42. A device as in claim 41 wherein at least the first temperature level or the second temperature level is high enough to free pores in the layers of contaminants thereon. 43. A device as in claim 2 wherein the current applying means includes two contacts across which an a.c. current signal is supplied; the two contacts being coupled to the magnetic layer at two respective points on the surface of the mag¬ netic layer opposite the interface. 44. A device as in claim 12 wherein the current applying means includes two contacts across which a.c. current signal is supplied; the two contacts being coupled to the mag¬ netic layer at two respective points on the surface of the magnetic layer opposite the interface. 45. A device as in claim 39 wherein the current applying means includes two contacts across which a.c. current signal is supplied; the ' two contacts being coupled to the ag- netic layer at two respective points on the surface of the magnetic layer opposite the interface. 46. A device for regulating the temperature of a fluid, the device comprising: a thermally conductive layer of porous, high resistance magnetic material, the permeability μof each incremental area of which is inversely related to its temperature over a given temperature range; said layer being adapted to have at least a portion of fluid to be heated located in said pores and in contact with said magnetic material. 47. A device as in claim 46 further comprising: .n additional layers of porous magnetic material, each additional layer having a permeability versus temperature characteristic corresponding to said thermally conductive layer; all said layers of magnetic material being stacked,with each pair of adjacent magnetic layers being OM?l in electrical contact along a corresponding- common surface, and wherein n is any integer. 48. A device as in claim 47 further comprising: means for applying an a.c. current between at least two points on of one of said magnetic layers, said current applying means directing current through a circuit having a return path adjacent a surface of said one mag¬ netic layer, such that said current is confined to flow along said adjacent surface. 49. A device as in claim 48 wherein the pores in at least one layer are sufficiently small to trap contam¬ inants entrained in the fluid. 50. A device as in claim 49 further comprising: means for raising the temperature of each layer that traps contaminants to a level sufficient to free the pores therein of trapped contaminants. 51. A device in accordance with claim 46 further comprising: means for applying an a.c. current which follows a path along a surface of said layer, the depth of penetration d of a major portion of the current into the layer being defined^according to the expression: the quantity of heat provided to the fluid at each incremental area of said layer to be in contact with a fluid being inversely related to the temperature of the fluid at each said area over the given range of temperatures, thereby providing a self-regulating control of fluid temperature over at least the given range of temperatures. 52. A device as in claim 51 wherein the fluid has contaminants therein and wherein the fluid is forced under pressure through the pores in said layer; and wherein the pores in said layer are suffic¬ iently small to prevent the flowing of contaminants there¬ through; the layer thereby filtering contaminants from the fluid. 53. A device as in claim 52 wherein the layer forms a tubular structure. 54. A device as in claim 51 wherein there is a pressure differential which forces fluid through the pores of the layer. 55. In a chemical reaction chamber having at least one fluid therein, a heater device as in claim 1 the heater device transferring an amount of heat to at least one of the fluids in the chamber to direct the temperature thereof to a desired level. 56. In a reaction chamber having at least one fluid therein, a heater device as in claim 13 the heater device transferring an amount of heat to at least one of the fluids in the chamber to direct the temperature thereof to a desired level. 57. In a reaction chamber having at least one fluid therein, a heater device as in claim 22 the heater device transferring an amount of heat to at least one of the fluids in the chamber to direct the temperature there¬ of to a desired level. 58. In a reaction chamber having at least one fluid therein, a heater device as in claim 26 the heater device transferring an amount of heat to at -least one of the fluids in the chamber to direct the temperature there¬ of to a desired level. 59. In a reaction chamber having at least one fluid therein, a heater device as in claim 37 the heater device transferring an amount of heat to at least one of the fluids in the chamber to direct the temperature thereof to a desired level. 60. In a reaction chamber having at least one fluid therein, a heater device as in claim 43 the heater device transferring an amount of heat to at least one of the fluids in the chamber to direct the temperature there¬ of to ' a desired level. 61. In a reaction chamber having at least one fluid therein, a heater device as in claim 45 the heater device transferring an amount of heat to at least one of the fluids in the chamber to direct the temperature thereof to a desired level. 62. In a reaction chamber having at least one fluid therein, a heater device as in claim 54 the heater device transferring an amount of heat to at least one of the fluids in the chamber to direct the temperature there¬ of to a desired level. 63. In a chemical reaction chamber as in claim 60 wherein at least one of the fluids comprises a reactant that enters the chamber at a first respective temperature and wherein the chamber has a reaction zone into which said at least one reactant flows at a second temperature, said at least one reactant reacting with at least one other substance in the reaction zone, the heater device transferring an amount of heat to each reactant to direct the temperature thereof to said second temperature. 64. In a chemical reaction chamber as in claim 63, wherein a plurality of reactants enter the reaction zone to generate at least one fluid product, the heater device being disposed along the reaction zone, the reactants and the at least one fluid product each (a) flowing through the heater device and (b) being directed to a desired temperature by the self- regulated transfer of heat. 65. In a chemical reaction chamber as in claim 64, " the heater device further being disposed to receive from the reaction zone outflow of at least one fluid product, each fluid product flowing through the heater device being directed to a desired temperature by the self-regulating transfer of heat. 66. In a chemical reaction chamber as in claim 55, wherein the chemical reaction chamber has a cooling source for withdrawing heat from the fluid in the chamber, the heater device transferring heat to fluid in the chamber to raise the temperature thereof. 67. In a chemical reaction chamber as in claim 66 wherein the cooling source withdraws heat from and the heater device transfers heat to fluid at the same location within the chamber at the same time. 68. In a chemical reaction chamber as in claim 66 wherein there is at least one location whereat heat is only transferred thereto. 69. In a chemical reaction chamber as in claim 63 wherein one of the substances with which the at least one reactant reacts is a catalyst which is disposed within the reaction zone of the chamber. 70. In a chemical reaction chamber as in claim 46 wherein the permeability of each magnetic layer varies inversely with temperature between (a) an effective per¬ meability and (b) a permeability of substantially one, each layer generating, in response to a con¬ stant a.c. current applied thereto, a first quantity of Joule heat when operating at its effective permeability and a second significantly lower quantity of Joule heat when -operating at a permeability of one, the first quan¬ tity divided by the second quantity representing a power ratio for said each layer; at least one layer having a sufficiently high power ratio such that the first quantity of cleans con¬ taminants. 71. A chemical reaction chamber having a fluid moving therein the temperature of which is to be controlled, the chamber comprising: a first porous layer of thermally conductive magnetic material through which the fluid moves; said first porous layer, in response to the application of an a.c. current thereto, generating more Joule heat when the fluid moving therethrough is at a low temperature in a predefined range than when the fluid is at a high temperature in the predefined range. 72. A chemical reaction chamber as in claim 71 wherein the difference in heat generation for different fluid temperatures is dependent primarily on the magnetic permeability versus temperature characteristic of said first layer (a) over the predefined range and (b) with O PI said first layer subject to a magnetic field of predefined intensity. 73. A chemical reaction chamber as in claim 72 wherein the resistivity of said first porous layer is relatively constant over the predefined temperature range. 74. A chemical reaction chamber as in claim 72 further comprising: means for directing an a.c. current along a surface path of said first porous layer, at least a segment of the path being transverse to the direction of fluid motion. 75. A chemical reaction chamber as in claim 74 further comprising: means for adjusting the frequency and ampli- tude of the a.c. current to a desired level, the adjusting means being coupled to the a.c. current directing means. 76. A chemical reaction chamber as in claim 74 further comprising: at least one other thermally conductive porous layer, said first porous layer and said other porous layers being stacked to form a laminar structure; the laminar structure being disposed so that fluid moves through each porous layer. 77. A chemical reaction chamber as in claim 71 further comprising: at least one other thermally conductive porous layer, said first porous layer and said other porous layers being stacked to form a laminar structure; the laminar structure being disposed so that fluid moves through each porous layer. 78. A chemical reaction chamber as in claim 76 wherein at least one of said other layers comprises a • .nonmagnetic low resistance material. 79. A chemical reaction chamber as in claim 76 wherein at least one of said other layers comprises a magnetic material of high resistance. 80. A chemical reaction chamber as in claim 78 wherein at least one of said other layers comprises a magnetic material of high resistance. 81. A chemical reaction chamber as in claim 7.6 wherein the magnetic material of said first layer comprises an alloy of differing compositions and permeability versus temperature characteristics at differing cross-sectional vicinities thereof. 82. A chemical reaction chamber as in claim 74 wherein (a) the chamber has a pre-reaction zone and a reaction zone and (b) each of at least one fluid represents a corresponding reactant flowing through the pre-reaction zone; said first porous layer being disposed within the pre-reaction zone along the path of flow of at least one reactant enroute to the reaction zone. 83. A chemical reaction chamber as in claim 74 wherein (a) the chamber has a pre-reaction zone and a reaction zone and (b) each of at least one fluid represents a corresponding reactant flowing through the pre-reaction zone; said first porous layer being disposed within the pre-reaction zone along the path of flow of at least one reactant enroute to the reaction zone. OϊfPI 84. A chemical reaction chamber as in claim 79 wherein (a) the chamber has a pre-reaction zone and a reaction zone and (b) each of at least one fluid represents a corresponding reactant flowing through the pre-reaction zone; at least one of the porous layers being dis¬ posed within the pre-reaction zone along the path of flow of at least one reactant enroute to the reaction zone. 85. A chemical reaction chamber as in claim 81 0 wherein (a) the chamber has a pre-reaction zone and a reaction zone and (b) each of at least one fluid represents a corresponding reactant flowing through the pre-reaction zone;., at least one of the porous layers being dis- - posed within the pre-reaction zone along the path of flow of at least one reactant enroute to the reaction zone. 86. A chemical reaction chamber as in claim 83 further comprising: means for introducing reactants into said 0 first porous layer at any of various locations along the length of the pre-reaction zone, the heat applied to each reactant enroute to the reaction zone being dependent On the location at which said each reactant is introduced. 87. A chemical reaction chamber as in claim 84 5 further comprising: means for introducing reactants into said first porous layer at any of various locations along the length of the pre-reaction zone, the heat applied to each reactant enroute to the reaction zone being dependent on 0 the location at which said each reactant is introduced. 88. A chemical reaction chamber as in claim 85 further comprising: OMPI means for introducing reactants- into said first porous layer at any of various locations along the • length of the pre-reaction zone, the heat applied to each reactant enroute to the reaction zone being dependent on the location at which said each reactant is introduced. 89. A chemical reaction chamber as in claim 76 wherein (a) the chamber has a reaction zone and (b) each of at least one fluid flows through the reaction zone; said first porous layer being disposed within the reaction zone along the path of flow of at least one fluid flowing in the reaction zone. 90. A chemical reaction chamber as in claim 78 wherein (a) the chamber has a reaction zone and (b) each of at least one fluid flows through the reaction zone; said first porous layer being disposed within the reaction zone along the path of flow of at least one fluid flowing in the reaction zone. 91. A chemical reaction chamber as in claim 79 wherein (a) the chamber has a reaction zone and (b) each of at least one fluid flows through the- reaction zone; at least one of the porous layers being disposed within the reaction zone along the path of flow of at least one fluid flowing in the reaction zone. 92. A chemical reaction chamber as in claim 81 wherein (a) the chamber has a reaction zone and (b) each of at least one fluid flows through the reaction zone; at least one of the porous layers being dis¬ posed within the reaction zone along the path of flow of at least one fluid flowing in the reaction zone. 93. A chemical reaction chamber as in claim 75 further comprising: cooling means for withdrawing heat from the chamber. 94. A chemical reaction chamber as in claim 89 further comprising: cooling means for selectively withdrawing heat from the reaction zone, the cooling means and the at least one porous layer through which a.c. current passes together controlling fluid temperature along the reaction zone. 95. A chemical reaction chamber as in claim 9.0 further comprising: cooling means for selectively withdrawing heat from the reaction zone, the cooling means, and the at least one porous layer through which a.c. current passes together controlling fluid temperature along the reaction zone. 96. A chemical reaction chamber as in claim 91 further comprising: cooling means for selectively withdrawing heat from the reaction zone, the cooling means and the at least one porous layer through which a.c. current passes together controlling fluid temperature along the reaction zone. 97. A chemical reaction chamber as in claim 92 further comprising: cooling means for selectively withdrawing heat from the reaction zone, the cooling means and the at least one porous layer through which a.c. current passes together controlling fluid temperature along the reaction zone. 98. A chemical reaction chamber as in claim 74 wherein (a) the chamber has a reaction zone and a post reaction zone and (b) each of at least one fluid flows out I _. OOMMPPII from the reaction zone and through the post reaction zone; a porous layer being disposed within the post reaction zone along the path of flow of at least one fluid flowing in the post reaction zone. 99. A chemical reaction chamber as in claim 78 wherein (a) the chamber has a reaction zone and a post reaction zone and (b) each of at least one fluid flows out from the reaction zone and through the post reaction zone; a porous layer being disposed within the post reaction zone along the path of flow of at least one fluid flowing in the post reaction zone. 100. A chemical reaction chamber as in claim 79 wherein (a) the chamber has a reaction zone and a post reaction zone and (b) each of at least one fluid flows out from the reaction zone and through the post reaction zone; at least one of the porous layers being dis¬ posed within the post reaction zone along the path of flow of at least one fluid flowing in the post reaction zone. 101. A chemical reaction chamber as in claim 81 wherein (a) the chamber has a reaction zone and a post reaction zone and (b) each of at least one fluid flows out from the reaction zone and through the post reaction zone; at least one of the porous layers being dis- posed within the post reaction zone along the path of flow of at least one fluid flowing in the post reaction zone. 102. A chemical reaction chamber as in.claim 76 wherein the chamber has a pre-reaction zone, a reaction zone, and a post reaction zone, fluids flowing through the zones; one porous layer extending along a length of the pre-reaction zone; one porous layer extending along a length of the reaction zone; one porous layer extending along a length of the post reaction zone; fluid flowing through the zones being heated by said porous layers in a self-regulated manner; and wherein the chamberfurther includes: cooling means for withdrawing heat from the zones in the chamber in a predefined manner: said a.c. current directing means providing current along a surface of each layer, the current pene¬ trating each vicinity of each layer by a depth determined by the temperature at said each portion, said porous layers with.a.c. current passing therethrough and said cooling means together regulating the temperature of the fluid in each zone. 103. A chemical reaction chamber as in claim 78 wherein the chamber has a pre-reaction zone, a reaction zone, and a post reaction zone, fluids flowing through the. zones; one porous layer extending along a length of the pre-reaction zone; one porous layer extending along a length of the reaction zone; one porous layer extending along a length of the post reaction zone; fluid flowing through the zones being heated by said porous layers in a self-regulated manner; and where the chamberfurther includes: cooling means for withdrawing heat from the zones in the chamber in a predefined manner; said a.c. current directing means providing current along a surface of each layer, the current pene¬ trating each vicinity of each layer by a depth determined by the temperature at said each portion, said porous layers with a.c. current passing therethrough and said cooling means together regulating the temperature of the fluid in each zone. 104. A chemical reaction chamber as in claim 79 wherein the chamber has a pre-reaction zone, a reaction zone, and a post reaction zone, fluids flowing through the zones; at least one of the porous layers extending along a length of the pre-reaction zone; at least one of theporous layers extending along a length of the post reaction zone; fluids flowing through the zones being heated by the porous layers in a self-regulated manner; and wherein the chamber further includes: cooling means for withdrawing heat from the zones in the chamber in a predefined manner; the porous layers with a.c. current passing therethrough and the cooling means together regulating the temperature of the fluid in each zone. 105. A chemical reaction chamber as in claim 81 wherein the chamber has a pre-reaction zone, a reaction zone, and a post reaction zone, fluids flowing through the zones; ' at least one of the porous layers extending along a length of the pre-reaction zone; at least one of the porous layers extending along a length of the post reaction zone; fluids flowing through the zones being heated by the porous layers in a self-regulated manner; and wherein the chamber further includes: cooling means for withdrawing heat from the zones in the chamber in a predefined manner; the porous layers with a.c. current passing therethrough and the cooling means together regulating the temperature of the fluid in each zone. 106. A chemical reaction chamber as in claim 102 wherein the (a) chamber is so dimensioned and (b) the chamber further comprises means for controlling fluid flow rate into the chambers; the fluid rate control means and the chamber dimensions together controlling the pressure and volume of the fluid in each zone in a prescribed manner. 107. A chemical reaction chamber as in claim 103 wherein the (a) chamber is so dimensioned and (b) the chamber further comprises means for controlling fluid flow rate into the chambers; the fluid rate control means and the chamber dimensions together controlling the pressure and volume of the fluid in each zone in a prescribed manner. 108. A chemical reaction chamber as in claim 104 wherein the (a) chamber is so dimensioned and (b) the chamber further comprises means for controlling fluid flow rate into the chambers; the fluid rate control means and the chamber dimensions together controlling the pressure and volume of the fluid in each zone in a prescribed manner. 109. A chemical reaction chamber as in claim 105 wherein the (a) chamber is so dimensioned and (b) the chamber further comprises means for controlling fluid flow rate into the chambers; the fluid rate control means and the chamber dimensions together controlling the pressure and volume of the fluid in each zone in a prescribed manner. 110. A chemical reaction chamber as in claim 75 wherein the fluid has contaminant particles entrained therein; and wherein the pores of the layer are dimen- 5 sioned small enough to entrap the contaminant particles. 111. A chemical reaction chamber as in claim 110 further comprising: means for heating the porous layer to an ele¬ vated temperature at which the pores are freed of the 0 entrapped contaminant particles, the elevated temperature being high enough (a) to vaporize some contaminant parti¬ cles and (b) to burn off other contaminant particles. ' " 112. A chemical reaction chamber as in claim 89 further comprising: _5 a catalyst provided within the reaction zone of the chamber, the catalyst promoting a reaction among reactants entering the reaction zone. 113. A chemical reaction chamber as in claim 90 further comprising: o a catalyst provided within the reaction zone of the chamber, the catalyst promoting a reaction among reactants entering the reaction zone. 114. A chemical reaction chamber as in claim 91 further comprising: 5 a catalyst provided within the reaction zone of the chamber, the catalyst promoting a reaction among reactants entering the reaction zone. 115. A chemical reaction chamber as in claim 92 further comprising: 0 a catalyst provided within the reaction zone of the chamber, the catalyst promoting a reaction among reactants entering the reaction zone. 116. A device for regulating the temperature of an electrically conductive fluid, the device comprising: a porous layer through which the fluid flows; and a first thermally conductive, nonporous mag- netic layer having (a) a high resistance relative to the fluid and said porous layer and (b) a magnetic permeabil¬ ity which varies inversely with temperature over a given range, one surface of said first magnetic layer forming an interface with a first surface of said porous layer; and first means for connecting a first source of a.c. current to said first magnetic layer, said first means being positioned to direct a.c. current along the surface of said first magnetic layer opposite said inter- face between said first magnetic layer and said porous layer. 117. A device as claimed in claim 116 wherein said porous layer comprises a thermally conductiv layer. 118. A device as claimed in claim 117 wherein said first magnetic layer comprises a cylindrical layer which encircles said porous layer; said first connecting means being positioned to direct the current along the outer surface of said first magnetic layer; the depth of penetration of the current flowing along the outer surface being inversely related to the temperature of the fluid in the given range. 119. A device as claimed in claim 117 wherein said first magnetic layer comprises a cylindrical layer which is encircled by said porous layer; said first connecting means being positioned to direct the current along the inner surface of said first magnetic layer; the depth of penetration of the current flowing along the outer surface being inversely related to the temperature of the fluid in the given range. 120. A device as claimed in claim 117 further comprising: a second cylindrical thermally conductive, nonporous magnetic layer having (a) a high resistance relative to the fluid and said porous layer, and (b) a magnetic permeability which varies inversely with tem- perature over a characteristic range; said porous layer being sandwiched between said first magnetic layer and said second magnetic layer; said.first magnetic layer encircling said porous layer and said porous layer encircling said second magnetic layer; and wherein the device further comprises: second means for connecting a second source of a.c. current to said second magnetic layer, said second means being positioned to direct: a.c. current from said second source along the inner surface of said second magnetic layer.

Inventors: DERBYSHIRE RODNEY L, DERBYSHIRE, RODNEY, L.
Applicants: METCAL INC, METCAL, INC.
Application year: 1984
Main classification: B01D35
IPC codes: B01D35, H05B3, H05B6