A heat exchanger is a device that transfers heat between two mediums. Depending on the type of heat exchanger, the two mediums might be separated by a wall (e.g. tubing, plates, etc.) Other times, there is no such separation and the two mediums are in direct contact. A wide variety of consumer and industrial applications range utilize heat exchangers. Industries that use heat exchangers include the chemical, fertilizer, food & dairy, organic batch processing, pharmaceutical, paper, and petrochemical industries, and oil and gas refineries.
Generally, an industrial system will require a heat exchanger wherever it is necessary to add or remove heat from a particular process or thing. This encompasses many possibilities. Accordingly, a plurality of heat exchangers might be used in a single system or even in a single process within a system. For instance, the oil industry uses heat exchangers for such varied applications as oil stabilization, gas compression, wastewater treatment, gas desulphurization, crude oil desalting, and closed loop cooling. Yet, within any one of these areas, such as oil stabilization, multiple heat exchangers perform a variety of tasks (e.g. crude oil interchanger, crude oil heater, crude oil cooler, etc.) Therefore, heat exchangers are vital to industry because they perform many necessary functions.
Another reason why heat exchangers are vital to industry is that they allow for the reclamation or redirection of energy. In a particular system, one process might require cooling while another process requires heating. Such a system can utilize a heat exchanger to direct heat from the process requiring cooling to the processes requiring heating. Reclaiming or reusing heat in this manner allows industry to save large amounts of money.
For a heat exchanger to provide a maximum benefit, it must operate at maximum efficiency. One key parameter of heat exchanger efficiency is the surface area of the interface between the two mediums that are exchanging heat. In oil and gas applications, too large of a physical interface can cause a significant accumulation of contaminates, which, as will be discussed further, are difficult to remove using conventional cleaning methods, such as high power sprays.
In a shell and tube heat exchanger, there is a plurality of tubes that act as heat transfer elements. The tubes contain the medium to be heated or cooled. A heat transfer medium is passed over the tubes, and heat is either removed or added to the medium within the tubes. By maximizing the surface area of the tubes (subject to the limiting factors discussed above), a maximum amount of heat transfer medium is brought into thermodynamic contact with the medium within the tubes. This leads to one significant problem associated with heat exchangers efficiency: Fouling. Fouling occurs when impurities or scale accumulates on heat exchanger transfer elements (e.g. the tubes or plates, in the case of a plate type heat exchanger). These impurities or scales interpose themselves between the medium within the heat transfer elements and the heat exchange medium and thus reduce the effective surface area of the interface between the mediums.
One example can be taken from the oil industry. Raw oil contains a significant amount of contaminates due to a number of reasons: The long distance oil travels during extraction; the combination of thick oils and thin oils; the sand and tar in the oil; and the transporting process from the well heads to the first stage refineries. In another example, industries that use river water as a cooling medium create fouling problems. River water contains biological impurities that can build up on heat transfer components. Regardless of the cause, heat exchangers need to be cleaned to reduce the effects of scaling and fouling.
For large industrial heat exchangers, however, cleaning is not an easy or inexpensive undertaking. In one method, high pressure washers, with PSI ratings of 5,000 to 10,000 per inch, are used to clean heat exchanger components. In the oil industry, cleaning a 20 foot section of a five foot in diameter heat exchanger with a pressure washer can require up to 11,000,000 gallons of water and eight days to complete the operation. The cost of recycling the water expended in the cleaning operation can be as high as $5,000,000 to $6,000,000 or higher depending on the environmental regulations of the country where the cleaning operation takes place. Furthermore, there is significant opportunity cost associated with the lost time during which the heat exchanger is off line.
Therefore, what is needed is a way to efficiently clean an industrial size heat exchanger while reducing the cost of cleaning associated with water reclamation.
Ultrasonic cleaning, particularly with thickness mode ultrasonic transducers, provides a much more efficient way to clean industrial heat exchangers. Unfortunately, conventional industrial heat exchangers were not designed with ultrasonic cleaning in mind. Accordingly, embodiments herein provide for the immediate application of ultrasonics to clean industrial heat exchangers by the provision of novel tanks designed to accommodate industrial heat exchangers (and heat exchanger components) and apply ultrasonic energy to the heat exchangers through the novel utilization of thickness mode transducers.
In additional embodiments, novel heat exchanger designs are provided in which thickness mode ultrasonics is integrated directly into heat exchangers themselves. These novel heat exchangers effect superior cleaning due to the positioning of thickness mode transducers at optimal locations throughout the heat exchanger shell. The integration of ultrasonics within the heat exchanger design reduces the time between taking a heat exchanger off line and commencement of the cleaning process. The embodiments provided herein will both significantly reduce the industry cost for cleaning heat exchangers and the cost and waste of water in the cleaning process.
In one embodiment, a heat exchanger is provided. A shell defines a space and has a first end, a second end, and at least two opposing sides, wherein the shell is adapted to hold a cleaning media. A heat exchanger component is positioned within the space. At least one thickness mode transducer positioned within the space, wherein when the space holds a cleaning media, and the thickness mode transducer is capable of imparting ultrasonic energy to the heat exchanger component through the cleaning media.
In one embodiment, a method of cleaning a heat exchanger component is provided. A heat exchanger component is selected for cleaning. The heat exchanger component is placed in a tank. The tank is filled with a cleaning media. At least one thickness mode transducer is connected to the cleaning tank. The at least one thickness mode transducer is operated to clean the heat exchanger component.
In one embodiment, a method of cleaning a component through utilization of an ultrasonic cleaning unit is provided. The ultrasonic cleaning unit comprises a frame having a first end and a second end, two opposing sides, an opening positioned between the first side and second opposing sides, and at least one thickness mode transducer connected to the frame within the opening. The method comprises placing a component in a cleaning tank; filling the tank with cleaning media; positioning the frame within the cleaning tank; and operating the at least one thickness mode transducer to clean the component.
In one embodiment, a transducer immersion unit is provided. A frame comprising a sidewall having a first end, a second end, at least two opposing sides, and an axis extending through the first end and the second end is provided. An opening is defined in the sidewall. At least one thickness mode transducer is positioned on the frame within the opening.
In one embodiment, a method of cleaning a heat exchanger component is provided. At least one thickness mode ultrasonic energy generating device including an ultrasonic converter and a horn attached to the ultrasonic converter is selected. The horn is adapted to transmit ultrasonic energy from the converter and is selected to match a surface contour of the heat exchanger component. The heat exchanger component is placed in a cleaning tank filled with cleaning media. The thickness mode ultrasonic energy device is attached to an external shell of a heat exchanger component. The thickness mode ultrasonic energy generating device is actuated such that ultrasonic energy is directed from the horn to at least one portion of the heat exchanger component.
In one embodiment, a method of cleaning a heat exchanger tube is provided. At least one thickness mode ultrasonic energy generating device includes an ultrasonic converter and a horn attached to the ultrasonic converter. The horn is adapted to transmit ultrasonic energy from the converter. The horn is selected to fit within the heat exchanger tube. The heat exchanger tube is placed in a cleaning tank filled with cleaning media. The horn is positioned within the heat exchanger tube. The thickness mode ultrasonic energy generating device is actuated such that ultrasonic energy is directed throughout the heat exchanger tube.
It should be understood that the invention is not limited in its application to the details of the construction and the arrangement of the components set forth in the following description or illustrated in the drawings. The invention is capable of other embodiments and of being practiced or of being carried out in various ways. Also, it is understood that the phraseology and terminology used herein is to describe and should not be regarded as limiting.
The drawings depict various preferred embodiments for purposes of illustration only. One skilled in the art will recognize from the following discussion that alternative embodiments of the structures and methods illustrated herein may be employed without departing from the principles described herein.
The deficiencies outlined above with respect to conventional heat exchanger cleaning processes can be overcome through the novel employment of ultrasonics as set forth herein. Specifically, the inventor has found that employing thickness mode ultrasonics is a particularly novel and effective way to clean industrial heat exchangers. It should be noted, however, that one should not limit the scope of the present application solely to the use of thickness mode ultrasonic cleaning processes, as the present application encompasses the use of both radial mode and thickness mode ultrasonics.
Thickness mode ultrasonics generally refers to imparting ultrasonic energy through utilization of a transducer operating in thickness mode. In thickness mode, a piezoelectric transducer is excited by an alternating current driving signal that causes alternating expansion and contraction of the thickness of the transducer. The resultant ultrasonic energy is discharged as a powerful directional force that can effectively penetrate to the interior of even the most dense and thick heat exchangers and heat exchanger components.
In one embodiment, ultrasonic thickness mode transducers are attached or immersed in a fluid filled tank of sufficient size to accommodate an industrial size heat exchanger or heat exchanger component, such as at tube bundle. The thickness mode transducers are actuated to impart ultrasonic energy to the heat exchanger or heat exchanger component and remove or loosen the contaminants therefrom. In a further application, however, the inventor has discovered that ultrasonics can be utilized to create a new generation of heat exchangers: Heat exchangers that accommodate the integration of transducers within their very structure.
The integration of thickness mode transducers can be effected by redesigning or retrofitting the heat exchanger and either fixing or removably attaching ultrasonic transducers to the heat exchanger shell. It should be noted that removable attachment provides a particular benefit in that thickness mode transducers can be attached to the heat exchanger body at the time of cleaning and removed prior to the heat exchanger's core operational mode. This is significant because thickness mode transducers depolarize at high temperatures (e.g. 190 degrees F.) and have to be rebuilt. Thus, the ability to remove thickness mode transducers prior to high temperature operations increases their life and minimizes maintenance costs. The adoption by industry of the enhanced heat exchanger designs provided herein will impart significant savings, both in real cost and in efficiency. As a consequence, industrial operators will be able to clean their heat exchangers more often and increase corresponding throughput.
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In use, space 14 is filled with fluid 15 that serves as a cleaning medium. Fluid 15 comprises any of a number of cleaning media of different chemistries, including water and alkaline cleaning solvents.
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Piezoelectric transducers typically operate in two modes: One is thickness mode and the other is radial mode. Radial mode is the primary frequency mode for most ultrasonic cleaning and thickness mode is typically employed in ultrasonic welding. Thickness mode is also used for megasonic applications because there is no limitation as to frequency as the piezoelectric crystal elements get thinner. Thickness mode is determined by the frequency calculation of all the parts including the transducer elements that make up the transducer stack as compared to radial mode where the frequency is determined by the relationship between the inside and the outside diameter of a circular transducer crystal. Thickness mode calculations include the frequency of the total parts of the transducer stack. For example, metal has a frequency. One would take in consideration the frequency of the metal and to achieve the correct thickness frequency in metal to match the rest of the stack.
Piezoelectric component 16 in one example comprises a thickness mode transducer. Such a thickness mode transducer can include a number of possible transducer types. Referring to
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In another example, transducer elements 222 are configured in radial mode. Radial frequency in one example is created by configuring a transducer element as a disc with a hole located in its center. The size of the inner diameter relative to the outer diameter of the disc creates the radial frequency. The radius of the disc is inversely proportional to the frequency created. First harmonic radial transducers operate in the range of 15 to 65 kHz. Third harmonic radial transducers operate in the range of 250 to 300 kHz. A further description of radial mode transducers can be found in U.S. Pat. No. 5,748,566, which is hereby incorporated by reference.
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Piezoelectric components 16 can be arranged in a number of different configurations. For instance, in one embodiment, the piezoelectric components 16 can be arranged parallel with respect to a central axis A extending through space 14. In another embodiment, the piezoelectric components 16 can be arranged perpendicular to axis A. Other configurations, such as a combination of horizontally, vertically, and diagonally arranged piezoelectric components 16 are also possible.
The number of piezoelectric components 16 varies according to the application. In the example shown, piezoelectric components 16 are arranged in opposing pairs 161, 162 such that piezoelectric components are present on opposing sides 123 and end sides 129 (defined by first end 121, and second end 122). Alternatively, piezoelectric components 16 could be positioned only on one of opposing sides 123 or end sides 129. As another alternative, piezoelectric components 16 could be positioned only on one of sides 123, 129.
Heat exchanger component 1 in one example comprises an entire industrial shell and tube heat exchanger of the kind used in the chemical, fertilizer, food & dairy, organic batch processing, pharmaceutical, paper, petrochemical industries, and in oil and gas industries. Such heat exchangers can be as large as 24 feet long with a diameter of 2 to 6 feet. In another example, the heat exchanger 1 component comprises a subcomponent of a heat exchanger, such as a tube bundle (assembled or disassembled) or the heat exchanger shell. Tube bundles can comprise as many as 600 or more individual tubes. Accordingly, shell 12 must be large enough to hold such volume. To accommodate 600 heat exchanger tubes, an exemplary tank would have the following dimensions 6′W×7′H×20′L. To optimize the cleaning process of heat exchanger component 1, it is desirable to fill both the tubes and the shell 12 with cleaning media. For such an application, it has also been found to be desirable to provide a watt density of 35 watts per gallon of cleaning media. Although other operating ranges could be used. For instance, as tube diameters increase above 4 feet, it may be desirable to operate in the 55-60 watts per gallon range to reach the inside of the tube bundles or to remove a disproportionate amount of sticky or compacted contaminants. The longer a heat exchanger is in use between cleaning cycles the more desirable it may be to increase the watts per gallon used to operate at a higher cleaning efficiency with respect to a given period of time.
The novel heat exchangers, which are further illustrated herein, efficiently utilize 35 watts per gallon to clean the tube bundles positioned therein. It should be noted, however, that the designers of conventional heat exchangers did not anticipate the novel use of thickness mode ultrasonics to clean heat exchanger components. Hence, with conventional heat exchangers it may be necessary to increase the watts per gallon above 35 watts per gallon in a given cleaning operation. It should be noted that inputting less than 35 watts per gallon could also be utilized. However, such lower input power may not always clean stubborn contaminates.
It should be noted at the outset that the drawing shown in
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PushPull® thickness mode transducers 20 are in one example attached to tank 40 through utilization of bracket mechanisms 42. Bracket mechanisms 42 in one example comprise plate 421 having horizontally projecting portion 422 and vertically projecting portion 423. Horizontally projecting portion 422 includes recess 425 to receive both top portion 22(1) of PushPull® thickness mode transducer 20 and electric cabling which is connected to a generator (not shown). Brackets 45 are attached with screws to vertically projecting portion 423 and bear against top portion 21(1) of PushPull® thickness mode transducer 20 to secure it to the sidewall of tank 40. Bracket mechanisms 42 also secure bottom portion 22(1) of PushPull® thickness mode transducers 20 to sidewall of tank 40. Hinged access doors 48 can be added to tank 40 to aid in the insertion of PushPull® thickness mode transducers 20 prior to operation and the removal of PushPull® thickness mode transducers 20 subsequent to operation. It should be noted that bracket mechanism 42 is depicted and described for exemplary purposes only. Alternate means of attaching PushPull® thickness mode transducers 20 to tank 40 can be utilized without departing from the scope of what is described and claimed herein.
In a further embodiment, tank 40 could be provided with a reflector that would enhance the distribution of sound throughout the tank. Such a reflector would be particularly effective in cases in which there is not a uniform distance between the PushPull® thickness mode transducers 20 and the exterior surface of tank 40. In one embodiment, the reflector is fabricated from 14 gauge steel and includes two opposing sidewalls that are spaced approximately 2 inches apart to form an air gap there between. The reflector in one example is removably or permanently fixed to the tank 40 through conventional connecting mean. For long tanks 40, the reflector could be provided in multiple segments that would be fastened together prior to the cleaning process.
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In the example shown, piezoelectric components 16 comprise PushPull® thickness mode transducers 20, although other transducers, such as immersibles could also be used. In one example, some PushPull® thickness mode transducers 20 are attached to the tank in the following manner: A plurality of recesses are formed at one end 55 of the tank such that one end a PushPull® thickness mode transducers 20 can be seated therein. On the other end 57 of tank 50, PushPull® thickness mode transducers 20 can be secured by inserting interface 225 and projection 227 into a corresponding recess (not shown) on lid 52. On both ends 55, 57 the other end of the piezoelectric transducer 20, i.e., the end not inserted into a recess, can be secured through means, such as bracket mechanism 42 or conventional means. In one example, there are also piezoelectric transducers 20 located in the interior of shell 12 that can be attached through bracket mechanism 42 or conventional means. As an alternative to the embodiment shown in
In operation, a cleaning media is added to the tank 50 and the piezoelectric PushPull® thickness mode transducers 20 are actuated in the manner described with respect to
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While particular embodiments have been shown and described, it will be apparent to those skilled in the art that changes and modifications may be made without departing from the broader aspects of applicants' contribution. The actual scope of the protection sought is intended to be defined in the following claims when viewed in their proper perspective based on the prior art.
This application claims priority to U.S. Provisional Applications 61/267,230, 61/290,091, and 61/290,785, which are hereby incorporated by reference.
Number | Date | Country | |
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61267230 | Dec 2009 | US | |
61290091 | Dec 2009 | US | |
61290785 | Dec 2009 | US |