APPARATUS FOR MULTI-TUBE HEAT EXCHANGER WITH TURBULENCE PROMOTERS
An apparatus is provided employing multi-tube heat exchangers that include turbulence promoters, which are easy to clean, thus maintaining sanitary conditions; prevent catching or trapping of product flowing or pumping through the tubes; and aid in maximizing heating and cooling efficiency of flowable or pumpable product flowing within the apparatus.
This application claims priority under 35 U.S.C. 119(e) and 37 C.F.R. 1.78(b) based upon copending U.S. Provisional Application Ser. No. 60/902,449 for Apparatus for Multi-tube Heat Exchanger with Turbulence Promoters filed Feb. 21, 2007 and which is incorporated herein by reference.
FIELD OF THE INVENTIONThe present invention relates to multi-tube heat exchangers, and more particularly to multi-tube heat exchangers having turbulence promoter fins that promote turbulence for passing liquid or flowable product thus increasing heating or cooling efficiency.
BACKGROUNDCurrently, multi-tube heat exchangers are used in various industries to heat or cool products passing through tubes. For example, the food and beverage, pharmaceutical and chemical industries use such devices because of a basic and important need to subject products to varying temperatures. Multi-tube heat exchangers provide an efficient and effective means to accomplish such needs. Typically, a multi-tube heat exchanger is configured so that a first concentric tube is placed within the hollow section of a second concentric tube. Hot or cold media flows within the hollow section of the first concentric tube in a direction counter to the flow of product. Product flows in the annular space created between the outer surface of the first concentric tube and the inner surface of the second concentric tube. In this way, product and heating or cooling medium do not come in contact with each other thus preserving the purity and sanitation of the product. A third concentric tube may enclose the second concentric tube to create yet another temperature gradient for the product. Multi-tube heat exchangers and their use is well known in the art. Previously, as in U.S. Pat. No. 5,174,369, product would pass through tubes relatively undisturbed. Except for the occasional bend or curve brought about by connecting joints or fittings, the product path through a multi-tube heat exchanger was relatively straight, smooth and undisturbed. One major reason for this design was to facilitate the product's movement through the tube. The movement of semi-solid product may be problematic if a tube surface is rough or partially occluded by obstacles. In addition, another reason for this smooth tube design was to prevent the tubes from “catching” or accumulating residue of the product within the hollow section of the tubes. The accumulation of product residue is undesirable, especially in the food and beverage industry, because it causes unsanitary conditions. Bacterial and mold growth within the hollow section of the tubes are just two of the possible problems caused by the accumulation of product.
Although the smooth tube design of multi-tube heat exchangers holds many advantages, it also possess disadvantages. For example, since the hollow section of the tubes are linear and smooth, product passes along the tubes mostly undisturbed in laminar flow. As such, product initially traveling closer to the surface of the tube containing the heating or cooling media remains closer to the heating or cooling tube throughout the path of the tube. The product traveling closer to the heating or cooling tube is thus heated or cooled more so than product traveling further away from such tube as it is exposed for a prolonged period of time and distance to the heating or cooling tube. Since there is little to no product turnover within the tubes, this causes a temperature gradient across the flow path of the product. To address this problem, several improvements have been made to the multi-tube heat exchanger. One such improvement is the inclusion of turbulence promoters within the hollow section or outer surfaces of the tubes. Turbulence promoters are structures disposed on the outer or inner surface of concentric tubes which disrupt the laminar flow of product or media.
For example, U.S. Pat. No. 4,258,782 discloses a heat exchange device with a cylinder having “turbulators” arranged helically around the cylinder. The turbulators are used to improve heat transfer to viscous liquid flowing in a tube. However, a disadvantage of the turbulators is that “raised fins” create numerous areas where product may catch and is difficult to dislodge or clean. This type of design is extremely difficult to remove trapped product and moreover causes the unsanitary conditions previously discussed above.
U.S. Pat. No. 5,375,654 attempts to address the shortcomings of U.S. Pat. No. 4,258,782 by disclosing smooth raised “dimples” disposed along the path of product. The dimples are smooth raised surfaces and create turbulence for product placed within the tube. In addition, no dimples are placed along the bottom or six o'clock drainage path of the product. This allows easy clean-up of the tube and prevents product from catching. However, despite the improvements made by U.S. Pat. No. 5,375,654, there is still a need for a more efficient turbulence structure which allows for maximum heat transfer to the product while maintaining sanitary conditions and facilitating easy cleaning of the inside of the tubes.
SUMMARY OF THE INVENTIONThe present disclosure describes a greatly improved apparatus for increasing heat exchange when using multiple tubes. An embodiment of the multi-tube heat exchanger has a first tube for receiving a heating or cooling medium. The first tube has a first end and a second end wherein the first end and the second end provide a medium inlet and a medium outlet, an outer surface, and a plurality of turbulence inducers wherein a single turbulence inducer is a smooth raised fin disposed on the outer surface of the first tube and further wherein the plurality of turbulence inducers are disposed in rows around the outer surface of the first tube with the rows arranged perpendicular to a laminar flow direction of a flowable or pumpable product.
A second tube is disposed about and concentric with the first tube for receiving a flowable or pumpable product. The second tube has a first end and a second end wherein the first end and the second end provide a product inlet and a product outlet, a securing clamp adjacent the first end of the second tube wherein the securing clamp secures the first end of the second tube to the first tube, a seal assembly adjacent the second end of the second tube wherein the seal assembly seals the second end of the second tube to the first tube.
The product outlet of the second tube is in tubular form and has an angled outlet portion extending toward the securing clamp adjacent the first end of the second tube and the product inlet of the second tube is in tubular form and has an angled inlet portion extending toward the seal assembly adjacent the second end of the second tube, with each of the product inlet and the product outlet having a portion extending radially outward of the angled outlet portion and the angled inlet portion.
Various objects and advantages of this invention will become apparent from the following description taken in conjunction with the accompanying drawings wherein are set forth, by way of illustration and example, certain embodiments of this invention.
The drawings, including
As required, detailed embodiments of the present invention are disclosed herein; however, it is to be understood that the disclosed embodiments are merely exemplary of the invention, which may be embodied in various forms. Therefore, specific structural and functional details disclosed herein are not to be interpreted as limiting, but merely as a basis for the claims and as a representative basis for teaching one skilled in the art to variously employ the present invention in virtually any appropriately detailed structure.
Referring to
Referring now to
In the foregoing description, certain terms have been used for brevity, clearness and understanding; but no unnecessary limitations are to be implied therefrom beyond the requirements of the prior art, because such terms are used for descriptive purposes and are intended to be broadly construed. Moreover, the description and illustration of the inventions is by way of example, and the scope of the inventions is not limited to the exact details shown or described.
Certain changes may be made in embodying the above invention, and in the construction thereof, without departing from the spirit and scope of the invention. It is intended that all matter contained in the above description and shown in the accompanying drawings shall be interpreted as illustrative and not meant in a limiting sense.
Claims
1. A sanitary concentric tube heat exchanger comprising:
- a first tube for receiving a heating or cooling medium, the first tube comprising a first end and a second end wherein the first end provides a medium inlet and the second end provides a medium outlet, an outer surface, and a plurality of turbulence inducers wherein a single turbulence inducer is a smooth raised fin disposed on the outer surface of the first tube and further wherein the plurality of turbulence inducers are disposed in rows around the outer surface of the first tube with the rows arranged perpendicular to a laminar flow direction of a flowable or pumpable product;
- a second tube disposed about and concentric with the first tube for receiving a flowable or pumpable product, the second tube having a first end and a second end wherein the first end provides a product inlet and the second end provides a product outlet;
- a securing clamp adjacent the first end of the second tube wherein the securing clamp secures the first end of the second tube to the first tube;
- a seal assembly adjacent the second end of the second tube wherein the seal assembly seals the second end of the second tube to the first tube; and
- wherein the product outlet of the second tube is in tubular form and having an angled outlet portion extending toward the securing clamp adjacent the first end of the second tube and the product inlet of the second tube is in tubular form and having an angled inlet portion extending toward the seal assembly adjacent the second end of the second tube, with each of the product inlet and the product outlet having a portion extending radially outward of the angled outlet portion and the angled inlet portion.
2. The sanitary concentric tube heat exchanger of claim 1 wherein the plurality of turbulence inducers are further configured in sets of adjacent rows around the outer surface of the first tube, a set comprising a first row of turbulence inducers wherein a leading product contact side of the fin of each turbulence inducer in the first row is oriented at a first angle relative to the laminar flow direction of the flowable or pumpable product and a second row of turbulence inducers adjacent the first row of turbulence inducers wherein a leading product contact side of the fin of each turbulence inducer in the second row is oriented at a second angle relative to the laminar flow direction of the flowable or pumpable product.
3. The sanitary concentric tube heat exchanger of claim 2 wherein the first angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of the flowable or pumpable product is 135 degrees and the second angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of flowable or pumpable product is 225 degrees.
4. The sanitary concentric tube heat exchanger of claim 2 wherein the first angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of the flowable or pumpable product is 225 degrees and the second angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of flowable or pumpable product is 135 degrees.
5. The sanitary concentric tube heat exchanger of claim 1 wherein the plurality of turbulence inducers are forged into the outer surface of the first tube during the formation of the first tube.
6. The sanitary concentric tube heat exchanger of claim 1 further comprising a round o-ring protector wherein the o-ring protector receives the second end of the first tube.
7. The sanitary concentric tube heat exchanger of claim 1 further comprising a triangular protector with a round opening through a middle section of the triangular protector wherein the round opening receives the second end of the first tube.
8. The sanitary concentric tube heat exchanger of claim 1 further comprising a third tube disposed about and concentric with the second tube, the third tube having a first end and a second end, the first end providing a medium inlet and the second end providing a medium outlet, wherein the medium inlet and the medium outlet of the third tube is tubular and extends perpendicular to a longitudinal axis of the third tube.
9. The sanitary concentric tube heat exchanger of claim 1 wherein the securing clamp comprises a pair of ring members having an O-ring inserted therebetween and an outer clamp member which is removable without tools for inspection or cleaning of the outer surface of the first tube and an inner surface of the second tube.
10. The sanitary concentric tube heat exchanger of claim 1 wherein the seal assembly permits relative movement between the first rube and the second tube to accommodate thermal effects which may occur between the first tube and the second tube.
11. The sanitary concentric tube heat exchanger of claim 1 wherein the seal assembly comprises an inner ring member secured to the first tube, the inner ring member having a cavity on an outer surface of the inner ring member wherein an O-ring may be installed, and an outer ring member secured to the second tube and sealingly engaged to the O-ring.
12. The sanitary concentric tube heat exchanger of claim 1 wherein angles of the product inlet and the product outlet relative to a longitudinal axis of the second tube is about 45 to 60 degrees.
13. The sanitary concentric tube heat exchanger of claim 1 wherein a plurality of the sanitary concentric tube heat exchangers are interconnected to provide a heat exchange system.
14. A sanitary concentric tube heat exchanger comprising:
- a first tube for receiving a heating or cooling medium, the first tube comprising a first end and a second end wherein the first end provides a medium inlet and the second end provides a medium outlet, an outer surface, and a plurality of turbulence inducers wherein a single turbulence inducer is a smooth raised fin disposed on the outer surface of the first tube and further wherein the plurality of turbulence inducers are disposed in rows around the outer surface of the first tube with the rows arranged perpendicular to a laminar flow direction of a flowable or pumpable product;
- a second tube disposed about and concentric with the first tube for receiving a flowable or pumpable product, the second tube having a first end and a second end wherein the first end provide a product inlet and the second end provides a product outlet;
- a third tube disposed about and concentric with the second tube, the third tube having a first end and a second end, the first end providing a medium inlet and the second end providing a medium outlet, wherein the medium inlet and the medium outlet of the third tube is tubular and extends perpendicular to a longitudinal axis of the third tube;
- a securing clamp adjacent the first end of the second tube wherein the securing clamp secures the first end of the second tube to the first tube;
- a seal assembly adjacent the second end of the second tube wherein the seal assembly seals the second end of the second tube to the first tube; and
- wherein the product outlet of the second tube is in tubular form and having an angled outlet portion extending toward the securing clamp adjacent the first end of the second tube and the product inlet of the second tube is in tubular form and having an angled inlet portion extending toward the seal assembly adjacent the second end of the second tube, with each of the product inlet and the product outlet having a portion extending radially outward of the angled outlet portion and the angled inlet portion, and wherein the medium inlet of the third tube and the product inlet of the second tube are located on a same side of a longitudinal axis of the sanitary concentric tube heat exchanger and with the medium outlet of the third tube and the product outlet of the second tube are located on an opposite side of the longitudinal axis of the concentric tube heat exchanger, thus providing a symmetrical shape to facilitate interconnection of a plurality of the sanitary concentric tube heat exchangers in series.
15. The sanitary concentric tube heat exchanger of claim 14 wherein the plurality of turbulence inducers are further configured in sets of adjacent rows around the outer surface of the first tube, a set comprising a first row of turbulence inducers wherein a leading product contact side of the fin of each turbulence inducer in the first row is oriented at a first angle relative to the laminar flow direction of the flowable or pumpable product and a second row of turbulence inducers adjacent the first row of turbulence inducers wherein a leading product contact side of the fin of each turbulence inducer in the second row is oriented at a second angle relative to the laminar flow direction of the flowable or pumpable product.
16. The sanitary concentric tube heat exchanger of claim 14 wherein the first angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of the flowable or pumpable product is 135 degrees and the second angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of flowable or pumpable product is 225 degrees.
17. The sanitary concentric tube heat exchanger of claim 14 wherein the first angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of the flowable or pumpable product is 225 degrees and the second angle of the leading product contact side of the fin of each turbulence inducer relative to the laminar flow direction of flowable or pumpable product is 135 degrees.
18. The sanitary concentric tube heat exchanger of claim 14 wherein the plurality of turbulence inducers are forged into the outer surface of the first tube during the formation of the first tube.
19. The sanitary concentric tube heat exchanger of claim 14 further comprising a triangular protector with a round opening through a middle section of the triangular protector wherein the round opening receives the second end of the first tube.
20. The sanitary concentric tube heat exchanger of claim 14 wherein the seal assembly permits relative movement between the first rube and the second tube to accommodate thermal effects which may occur between the first tube and the second tube.
21. The sanitary concentric tube heat exchanger of claim 14 wherein the securing clamp comprises a pair of ring members having an O-ring inserted therebetween and an outer clamp member which is removable without tools for inspection or cleaning of the outer surface of the first tube and an inner surface of the second tube.
22. The sanitary concentric tube heat exchanger of claim 14 wherein the seal assembly comprises an inner ring member secured to the first tube, the inner ring member having a cavity on an outer surface of the inner ring member wherein an O-ring may be installed, and an outer ring member secured to the second tube and sealingly engaged to the O-ring.
23. The sanitary concentric tube heat exchanger of claim 14 further comprising corrugated bellows which extend circumferentially around the third tube for accommodation of thermal effects which may occur between the second and the third tube.
24. The sanitary concentric tube heat exchanger of claim 14 wherein angles of the product inlet and the product outlet relative to a longitudinal axis of the second tube is about 45 to 60 degrees.
25. The sanitary concentric tube heat exchanger of claim 14 wherein a plurality of the sanitary concentric tube heat exchangers are interconnected to provide a heat exchange system.
Type: Application
Filed: Nov 12, 2007
Publication Date: Nov 6, 2008
Inventor: Gerald Glass (Springfield, MO)
Application Number: 11/938,333
International Classification: F28F 13/12 (20060101);