turning now to the drawings in more detail , numeral 10 designates the inline heating apparatus in accordance with the present invention . as can be seen in fig1 , the apparatus 10 is operationally connected to a transformer 12 and a pulse generator 14 positioned above the surface . the transformer 12 is adapted for connecting to a source of electrical power , for instance a 480 - watt power source . the pulse generator 14 transmits electrical power to the heating elements positioned in the well 16 formed in the ground formation . the power generator 14 receives a signal from a temperature controller 18 that is operationally connected to a temperature sensor 20 . the apparatus 10 is positioned in a selected pre - determined location in the “ cool zone ” 22 of the well 16 wherein paraffin solidification is likely to occur . a hot zone 24 is usually located below the cool zone 22 and thus , it will not be necessary to position the apparatus zone in the zone 24 . as can be seen in fig1 , the apparatus 10 can be connected end - to - end with a well bore string 26 which extends in the well bore 16 toward a production zone 28 . extending through the central opening in the apparatus 10 and through the well bore string 26 is a production line , or production tubing 30 , through which crude oil is pumped from the production zone 28 to the surface . the transformer 12 , the power generator 14 , and the temperature controller 18 are positioned on the surface above a wellhead 32 . the apparatus 10 has distinct portions that for the ease of explanation are designated as “ dry zone ” and “ wet zone .” as can be seen in fig2 a and 2b , three wires 36 , 37 , and 38 positioned in a cable 34 extend into the well 16 from the pulse generator 14 . a cable 35 is a ground wire , and a cable 33 extends from the temperature controller 18 to the temperature sensor 20 . each of the wires 36 , 37 , and 38 is connected to a respective heating element 40 , 41 and 42 . each of the heating elements comprises an elongated heating member extending longitudinally in the elongated hollow body 50 of the apparatus 10 . the body 50 comprises a top plate 52 , that is sealed against the interior of the well bore 16 and carries the connecting wires 36 , 37 and 38 that extend through the plate 52 into the interior of the housing 50 . the wires 36 , 37 and 38 may be kapton - coated wires that are sealed with graphite seals 43 , 44 and 45 that are crimped around the wires to prevent liquid from entering a the body 50 . the plate 52 defines one end of a dry zone 60 , while another transverse plate 54 defines another end of the dry zone 60 . an opposite surface of the plate 54 defines one end of a wet zone 62 , while still another transverse plate 84 separates the wet zone 62 from the next dry zone 86 . the body 50 comprises an outer housing 51 and an inner housing 64 ; the housings 51 and 64 are spaced apart , defining an annular space 66 therebetween . a first insulation layer 56 is located inwardly from the outer housing 51 , and a second insulation layer 58 is located on the outside of the inner housing 64 . the operating wiring and the connectors extending through the dry zone 60 are thereby protected from the heat generated in the well bore and from the heat generated by the heating elements of the apparatus 10 . the inner housing 64 extends formed longitudinally substantially through the entire length of the tool 10 and in a parallel relationship to the outer casing 51 . the inner housing is sized and configured to allow extension of the production tubing 30 through a central opening 63 formed in the inner housing 64 . a bushing 70 is mounted on the plate 52 in fluid communication with the annular space 66 . a valve 72 is connected to the bushing 70 to allow evacuation of oxygen from the space 66 and introduction of a neutral gas into the annular space 66 as shown by arrows in fig8 . the neutral gas , for instance nitrogen prevents flash ignition in the electrical connection environment in the dry zone 60 . the inner housing 64 extends both through the dry zone 60 and the wet zone 62 . the portion of the inner housing 64 located in the wet zone 62 is provided with perforations 74 made through the wall of the inner housing 64 . the perforations 74 allow heat exchange between the well bore liquid , such as salt water and the like , entering annulus 66 from the central opening 63 in the wet zone 62 . the flow of fluids in the wet zones of the body 50 is schematically illustrated in fig7 . the heating elements 40 , 41 and 42 that extend in the wet zone 62 heat the liquid circulating through the perforations 74 and transfer the heat to the flow of crude oil passing through the production tubing 30 . as a result , paraffin suspended in the crude oil flow does not cool to a temperature low enough to cause paraffin to be separated and attaching to the wall of the production line 30 . the wires 36 , 37 and 38 extend from the dry zone 60 to the wet zone 62 by passing through a sleeve 80 positioned in the annulus 66 and subsequently through the entire apparatus 10 between the dry zones and the wet zones . of course , the apparatus 10 can have more than one dry zone and more than one wet zone ; the number of the zones and the number of heating elements will depend on the conditions of the well so that the heating elements are positioned in strategic locations for introducing a heating power to the crude oil . if desired , a guide plate 82 can be positioned in the dry zone 62 for retaining the heating elements 41 , 42 and 43 in alignment in relation to the central axis of the well casing 17 and the body 50 . another wet zone 88 can be formed next to the dry zone 86 and the tool 10 can be thus extended for providing several heating or wet zones in the well bore 16 . the wet zone 88 has separate heating elements 89 that extend through the wet zone 88 . each wet zone has independent heating elements . the top of the body 50 can be connected by a suitable coupling 93 to a well string sub 95 , while a free end 90 of the body 50 can be provided with a threaded connector 92 that allows the apparatus 10 to be connected to another sub ( not shown ) that forms a part of a well string . the temperature sensor 20 detects the temperature in the area near the heating elements and sends a signal to the controller 18 at the surface . the sensor 20 is positioned within a temperature sensor housing 21 , which is secured to the outer housing 51 . the temperature sensor 20 is fittingly engaged in a receiver 23 that is secured at one end of the sensor housing 21 . an opening 94 in the outer housing 51 admits temperature from the body 50 to the end 98 of the sensor 20 thereby allowing the sensor 20 to generate a signal of the current temperature and send the signal to the controller 18 . the controller 18 determines whether the temperature has been raised sufficiently to maintain paraffins in a viscous state as a three - phase electric pulse generator 14 generates an electrical current and transmits it to the heating elements 40 , 41 , and 42 . if the temperature is too high , the transformer generates less electricity . if the temperature is too low , the transformer is activated to supply more electric power to the downhole heating elements . a bleed valve 96 ( fig2 b and 8 ) is set in the casing 51 . a set screw opens the valve 96 to allow bleeding of oxygen from the dry zone and introduction of neutral gas , for instance nitrogen into the dry zones . the bleed valve 96 is removable to allow removal of oxygen . the apparatus of the present invention can be also used for generating steam in a downhole location , which will require connection of the body 50 to a source of water . the heating elements , then activated all across the surrounding areas can be heated , thereby generating steam that would melt paraffin . the length of the tool 10 can be extended by adding multiple stages , dry zones followed by wet zones , followed by dry zones , etc . the number of heating assemblies will be determined by the rate of flow and diameter of the well . the multiple stage system dramatically increases the heat output variable thereby increasing the volume of fluid that can be heated . the use of kapton - coated wires and graphite seals crimped around the wires form a leak - proof seal around the electrical wires where they enter the dry zones 60 . of course , the use of an insulation coating in a hot temperature environment is not limited to the use of polymer kapton , and other suitable insulation coating can be used . the use of 480 - watt 3 - phase heating elements with three heating wires increases the heat output and makes the apparatus 10 more efficient and cost effective . the transformer 12 positioned on the surface eliminates fire hazard problems that can result from the use of a heat source downhole . the fiber optic source or probe 98 monitors downhole temperature and regulates operations at the surface . the system of the present invention , when electrically connected elements are activated , controls electrical currents to the elements within scr or pulse method . the pulse power supply is delivered by processors and through the downhole sensors . the control system 18 prevents the operating wires and heating elements from extending and contracting which extends the lifetime of the elements . additionally , the pulsing system significantly reduces electrical consumption making the apparatus 10 more economical . the present invention is designed to accommodate the insertion and placement of the downhole pump through the hollow inner core of the inner casing . as a consequence , the downhole pump can pass through the body 50 during normal installation . the perforated inner housing 64 prevents “ gas locking ” of the downhole production pump . a particular advantage of the present invention is that it can be used in both horizontal and vertical piping systems and is not limited only to vertical placement . the apparatus 10 is a circulation heater as opposed to a probe heater , which is conventionally used in the field . it is envisioned that once the operator identified the cold zones , the apparatus 10 can be installed with the well bore string at a point approximately 100 to 200 feet below the deepest cold zone . in the flow or fluid lines , the problem areas can be identified by conventional tests and the apparatus 10 be installed within the line 50 to 100 feet before the paraffin build - up can occur . in addition to preventing paraffin problems , the apparatus 10 can be utilized in low gravity heavy hydrocarbon recovery . if the producing zone requires heating to raise the temperature to convert the heavy hydrocarbons to light hydrocarbons , the apparatus 10 can be used as well . rather than using a boiler system on the surface as a steam source , the apparatus 10 provides a tool to produce and deliver steam downhole directly to the producing line . in the injection well , the apparatus 10 can be installed as a production zone . the heating elements 41 , 42 and 43 are single end heat - generating elements ; the apparatus 10 can therefore be safely used in a situation where the power source is electric power . conventional tools utilize heating elements that must be terminated at each end ( double - ended termination ), which does not allow for extension of the heating element when heated . when necessary , the elongated heating elements can be extended to 20 - feet length . the pulse power supply delivered by the transformer 12 and the pulse generator 14 is regulated by processors receiving data from the downhole sensor 20 . this control system prevents the heating elements from expanding and contracting in excess of the optimum operating environment , which extends the life of the elements to a significant degree . many changes and modifications can be made to the apparatus and method of the present invention without departing from the spirit thereof . i therefore pray that my rights to the present invention be limited only by the scope of the appended claims .