Abstract:
A method and device for removing scaling from the interior of a conduit used in a heat transfer device, the method comprising the steps of diverting a portion of the fluid from the conduit, passing the diverted portion through a filter, passing the filtered portion through a magnetic field, and reintroducing the fluid into the conduit. The method of the present invention can also be used with chillers to control bacterial growth therein.

Description:
[0001]    This application is a continuation in part application of application Ser. No. 12/148,450 filed Apr. 18, 2008. 
     
    
     FIELD OF THE INVENTION 
       [0002]    The present invention relates to a method for treating water and a system for treating water, particularly industrial water used in heat exchangers and chillers. 
       BACKGROUND OF THE INVENTION 
       [0003]    Numerous heating and cooling systems using water circulation in closed loops age prematurely. In many buildings and industrial plants, these CVC systems show signs of deterioration and weakening performance signs after only a few years. This loss of efficiency is not always quickly detected right away, because it is not very apparent if one does not pay close and regular attention to it. Eventually, this will translate in pumping difficulties and poor performance of the thermo-exchange equipments. This loss in performance is usually caused by corrosion and scaling of the piping system. 
         [0004]    If no preventive action against corrosion and limestone deposits is taken, they have to be dissolved in an acid solution, which is costly and damaging to the environment. This must be repeated regularly since it does not prevent any ulterior limestone deposits in the circuits. 
         [0005]    Furthermore, each acid treatment will cause corrosion of the metal installations, therefore reducing their durability. 
         [0006]    The deterioration of these systems always seem surprising since, in theory, they are insulated, without possible evaporation, without any need to be purged or changing the water. At first, this characteristic seems advantageous because the relative waterproofness limits the addition of water contaminants. Unfortunately, the limitation in water changing does not immediately eliminate all contaminants and a prolonged stay of the fluid inside the circuit is not always an advantage. The reality is quite different. 
         [0007]    The water circulating through the closed loops usually contains fine particles in suspension which can cause many problems like scaling and abrasion. This invariably results in abnormally quick wear of the components et loss of efficiency. These particles come from various sources, including manufacturing debris cause by construction or contaminants introduced during repair or maintenance work on the network. However, the most part of the particles in suspension contained the water of these networks are caused by corrosion. The presence of oxygen, the different metals and microbiological activity are the main causes of this corrosion. The presence of oxygen is not surprising and it can be brought into the water in different ways: supply of new water, the pump fittings, the fans, pressure variations, etc. Oxygen, even in low concentration, always causes corrosion. Without suitable preventive measures, this dissolved gas will be responsible for stringing degradation, the most frequent type of corrosion of water circulation systems. 
         [0008]    Contact between different metals is not unusual in these loops and this can cause corrosion of galvanized pipes. Finally, the presence of bacteria, mainly silt causing bacteria and sulfate reduction bacteria (SRB), are a significant element in terms of the problems of fouling and corrosion. 
         [0009]    The presence of residue on the metallic surfaces is always a source of problems and it is always best to take preventive measures against this. However, when residue has already started accumulating inside the piping network, any preventive effort will have little effect and deterioration will continue to progress. In such a situation, the catalytic treatment we proposed herein to remove scale becomes essential. 
         [0010]    Another factor which should be considered is the efficiency of the prevention treatment program. It is in fact impossible to obtain a reasonable protection if the surfaces to be protected are not in the right condition for it. On one hand, the corrosion inhibitors cannot be efficient on blocked surfaces and on the other hand, residue accumulation is a good place for microbic growth. Letting a blocked piping system stay that way will only make things worse and will lead to corrosion and gradual deterioration of the surfaces. 
       SUMMARY OF THE INVENTION 
       [0011]    It is an object of the present invention to provide a system suitable for chillers or other heat exchangers and which system can prevent scaling and where scaling has occurred, can remove the scale. 
         [0012]    It is a further object of the present invention to provide a method for the removal of scale from pipes or other conduits such as are used in heat exchangers. 
         [0013]    According to one aspect of the present invention, there is provided a method for removing scale from the interior of a conduit in a heat exchanger wherein a fluid passes through the conduit, the method comprising the steps of diverting a portion of the fluid from the conduit, passing the diverted portion through a filter to remove particles above a predetermined size while permitting smaller particles to pass through the filter, passing the portion from the filter through a magnetic field in a spiral direction to cut lines of flux such that the direction of water flow and the direction of the flux lines are set at an angle and the water is treated for a longer period of time, and reintroducing the fluid into the conduit at a point downstream of a point where the fluid is diverted whereby the smaller particles will act to remove the scale from the conduit. 
         [0014]    According to a further aspect of the present invention, there is provided a method for removing bacteria from a heat transfer system having a chiller and wherein a fluid is circulated through a conduit, the method comprising the steps of diverting a portion of the fluid from the conduit, passing the diverted portion through a filter, passing the portion from the filter through a magnetic field in a direction to cut lines of flux such that the direction of water flow and the direction of the flux lines are set at an angle, and reintroducing the fluid into the conduit at a point downstream of a point where the fluid is diverted. 
         [0015]    In the first aspect of the present invention, it is believed that the changing morphology of the solids as they are subjected to the magnetic field is changed and they will then act as an abrasive while circulating through the conduits to remove deposits from therein. The removed deposits are then picked up by the filter. Naturally, one can control the removal to a certain extent by the particle sizes permitted to pass through the filter. Since the removed deposits will accumulate in the filter, it is advisable to monitor the pressure drop across the filter to signal when a change of the filter is required. 
         [0016]    The problem of corrosion can effect many metals although pipes of iron of steel are most common. With iron pipes, the oxide formed by oxidation does not firmly adhere to the surface of the metal and flakes off relatively easily causing pitting. Extensive pitting eventually causes structural weakness and disintegration of the metal. With aluminum, a different problem occurs in that a very tough oxide coating is formed which strongly bonds to the surface of the metal. 
         [0017]    The formation of rust in metal pipes could occur at some distance away from the actual pitting or erosion of the iron. This is possibly because electrons produced by the initial oxidation of iron can be conducted through the metal and the ions can defuse through the water layer to another point on the metal surface where oxygen is available. This process essentially results in an electrical chemical cell in which iron serves as an anode, oxygen gas as a cathode and the aqueous solution of ions serving as a salt bridge therebetween. 
         [0018]    A still further problem with industrial water is in microbiological control. Microbiological activity in a closed loop system can degrade performance and needs to be prevented. Generally, in a closed loop system, biocides are not suitable since each of them has side effects limiting their overall utility. Thus, oxidizing biocides such as chlorine or bromine are rarely effective at eliminating all microbes due to the fact that the biocides are catalystically decomposed by iron and copper corrosion products and even the metal surfaces. This means that the system can be readily reinnoculated from zones that did not “see” the biocide. Also, oxidizing biocides produced by products which build up over repeated treatments and will increase the corrosiveness of the water. 
         [0019]    When passing through the magnetic device, the fluid is passed in a manner such that the direction of the flow of the fluid cuts the magnetic flux lines created by the magnetic field at an angle with respect thereto. It is the angle of the flow of the water with respect to the flux lines that permits efficient operation of the invention. The speed of the water flow is also important with relatively high speeds being preferred. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0020]    Having thus generally described the invention, reference will be made to the accompanying drawings illustrating an embodiment thereof, in which: 
           [0021]      FIG. 1  is a schematic view of a system according to one embodiment of the present invention; 
           [0022]      FIGS. 2 to 5  are schematic views of other types of systems according to the present invention; 
           [0023]      FIG. 6  is a schematic view of the overall system and heat exchanger; 
           [0024]      FIG. 7  is a photograph of the crystal structure in water without treatment; and 
           [0025]      FIG. 8  is a photograph of crystal structure following treatment with the magnetic device. 
       
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
       [0026]    Referring to the drawings in greater detail and by reference characters thereto, there is illustrated a treatment system  80  according to an embodiment of the present invention. The system is designed to be used with a closed circuit heat exchanger  70  which includes a pipe  10  having fluid circulating in the direction indicated by arrow  12 . Heat exchanger  70  may be any known type including boilers, chillers, thermopumps, etc. 
         [0027]    The system will include a conduit  14  which is tapped into pipe  10  such that a certain portion of the water within the heat transfer circulation will be diverted thereto. Preferably, the amount is between 5 and 15 percent and even more preferably between 8 and 10 percent of the total flow. 
         [0028]    Conduit  14  includes a valve  16  thereon, and is provided a pump  17  on the line, depending upon the desired pressures. 
         [0029]    A system inlet  20  has a bypass conduit  22  located thereat. On bypass conduit  22  there are provided pressure gages  24  and  25  with a valve  26  therebetween. 
         [0030]    Treatment line  28  has a valve  30  thereon. A filter  32  having the desired filtering media therein filters the water to be treated. From filter  32 , there is provided a conduit  34 . On conduit  34 , there is provided a discharge line  36  and associated valve  38 . A magnetic treatment device  40  is of the type shown in U.S. Pat. No. 5,149,438, the teachings of which are hereby incorporated by reference. After magnetic treatment device  40 , there is also provided a discharge line  42  with associated valve  44 . On conduit  45 , there is provided a valve  46  and this is connected to a return line  48  feeding back into main pipe  10 . 
         [0031]    In operation, the filter size can be of great importance. Thus, when the system is installed in pipes suffering from scaling, the size of particles permitted to pass through the filter can be slightly larger than normal. It has been found that allowing these particles to pass through and then treating these particles with magnetic treatment device  40 , that the particles will tend to “scrub” the scale from the pipes. As the scale is removed, the filter can be changed to further limit the size of particles passing therethrough. 
         [0032]    In a preferred embodiment, the filter is designed to remove all particles above 5 microns. With the treatment of the present invention, these small particles will scrub the walls of the conduits to remove the scale. 
         [0033]    During the process iron oxide is picked up within the magnetic treatment device and retained therein. These iron oxide particles can be removed through discharge line  42  when required. 
         [0034]      FIGS. 2 to 5  illustrate other arrangements which may be utilized. It is believed that the circuits are self-explanatory with reference numeral  52  designating the pipe through which the liquid is circulated and from where the liquid to be treated is taken. Reference numeral  54  designates the magnetic treatment unit while reference numeral  56  is utilized for gauges. The ball valves are designated by reference numeral  58  while cartridge filters are designated by reference numeral  60 . As an alternative to cartridge filters  60 , bag filters  62  may be employed. The pumps are designated by reference numeral  64 . Reference numeral  66  designates a manifold which may be utilized in cases of limited space. While water is conventionally used in heat exchange systems, a glycol mix may also be employed. 
         [0035]    One large advantage of the system of the present invention is its ability to remove deposits already formed on conduits. In this regard, it is believed that a micro abrasion technique is responsible for removal of the deposits. With treatment according to the system of the present invention, it is believed that the morphology of the solids is changed and they become of a form which, while circulating through the pipes, acts as an abrasive to remove deposits. These deposits are subsequently picked up by the filter. 
         [0036]    It has been found that the geometrical morphology of the crystals changes with treatment. Generally, they may be of an orthorhombic, triangular or cubic structure which will not adhere to wall surfaces. The microscopic clusters will generally travel at 3 to 7 feet per second in water circuits and will initiate a microscopic sandblasting of the conduits. The released particles and the larger clusters will be captured in the filter system. 
         [0037]    The passing of the water in a spiral direction ensures that the water is treated for a substantially longer period of time than would be the case when the water would flow directly past the magnet. It has been found that one need only treat a portion of the water and reintroduce it into the system. 
         [0038]    It will be understood that the above described embodiments are for purposes of illustration only and that changes and modifications may be made thereto without departing from the spirit and scope of the invention.