Patent Application
20130048258
1. Field of the Invention
The present invention relates to a shell-and-tube heat exchanger, especially to a shell-and-tube heat exchanger that has good heat exchange efficiency.
2. Description of the Prior Art(s)
With reference to
The shell assembly has a shell 91, two tube panels 913, multiple upper baffles 914, multiple lower baffles 915 and multiple heat transfer tubes 916. The shell 91 is tubular and has a front opening, a rear opening, a shell side inlet 911, a shell side outlet 912 and a condensate outlet 917. The condensate outlet 917 is connected to and communicates with a steam trap 94. The tube panels 913 are respectively mounted at and cover the front opening and the rear opening of the shell 91. Each tube panel 913 has multiple through holes. The upper baffles 914 are semilunar, are mounted on an inner top wall of the shell 91 and are separately arranged in the shell 91 and between the front and rear openings of the shell 91. The lower baffles 915 are semilunar, are mounted on an inner bottom wall of the shell 91 and are separately arranged in the shell 91 and between the front and rear openings of the shell 91. Each lower baffle 915 is disposed between two adjacent upper baffles 914. Thus, a curved channel is formed between the upper and lower baffles 914, 915. The heat transfer tubes 916 are axially mounted in the shell 91 and are mounted through the tube panels 913 and the upper and/or lower baffles 914, 915.
The front cover 92 is securely mounted on the front opening of the shell 91 and has a tube side inlet 921. The rear cover 93 is securely mounted on the rear opening of the shell 91 and has a tube side outlet 931. The safety valve 95 is mounted on the shell 91, protrudes into the shell 91, and detects and controls fluid pressure in the shell 91.
Tube side fluid that needs to be heated or cooled flows into the conventional shell-and-tube heat exchanger 90 from the tube side inlet 921 of the front cover 92 and through the heat transfer tubes 916, and then flows out of the conventional shell-and-tube heat exchanger 90 from the tube side outlet 931 of the rear cover 93. Shell side fluid such as steam or cooling water flows into the conventional shell-and-tube heat exchanger 90 from the shell side inlet 911 of the shell 91 and along the curved channel formed between the upper and lower baffles 914, 915, and then flows out of the conventional shell-and-tube heat exchanger 90 from the shell side outlet 912 of the shell 91. Thus, the tube side fluid and the shell side fluid exchange heat. Condensate formed in the shell 91 is drained to the seam trap 94 through the condensate outlet 917 of the shell 91.
However, for example, when shell side fluid in the shell 91 is steam to transfer heat to the tube side fluid in the heat transfer tubes 916, where the shell side fluid flows downwardly, top surfaces of the heat transfer tubes 916 act as heating surfaces; where the shell side fluid flows upwardly, lower surfaces of the heat transfer tubes 916 act as the heating surfaces. Thus, the heating surfaces on one heat transfer tube 916 differ with positions. Furthermore, since the shell side fluid also transversely flows toward the shell side outlet 912 of the shell 91, the shell side fluid bumps against the upper and lower baffles 914, 915, becomes turbulent and air films occur at nooks in the shell 91. Therefore, heat transfer efficiency between the shell side fluid and the heat transfer tubes 916 is affected.
With further reference to
Moreover, according to the principle of inertia force, when the tube side fluid flows through the tube side inlet 921 of the front cover 92, most of the tube side fluid flows into the heat transfer tubes 916 that directly correspond to the tube side inlet 921 of the front cover 92 and only few of the tube side fluid flows into the heat transfer tubes 916 that do not directly correspond to the tube side inlet 921 of the front cover 92. Therefore, the heat transfer tubes 916 have different quantities of tube side fluid flowing therein, and the tube side fluid in different heat transfer tubes 916 have different flow rates. Consequently, heat transfer efficiencies in different heat transfer tubes 916 differ.
To overcome the shortcomings, the present invention provides a shell-and-tube heat exchanger to mitigate or obviate the aforementioned problems.
The main objective of the present invention is to provide a shell-and-tube heat exchanger. The shell-and-tube heat exchanger has a tubular shell, two tube panels mounted in the shell, multiple heat transfer tubes axially mounted on and between the tube panels, an inlet tube mounted in the shell and connected to a shell side inlet of the shell, a spurting tube axially mounted in the shell and connected to the inlet tube, and a front cover and a rear cover respectively mounted on a front opening and a rear opening of the shell.
Shell side fluid spurts into the shell from the spurting tube toward a specific direction. The shell side fluid does not become turbulent, no air film occurs in the shell and lower surfaces of the heat transfer tubes act as heating surfaces so the shell-and-tube heat exchanger has high heat transfer efficiency.
Other objectives, advantages and novel features of the invention will become more apparent from the following detailed description when taken in conjunction with the accompanying drawings.
With reference to
The shell assembly has a shell 10, two tube panels 11, multiple partition panels 12, multiple supporting rods 16, multiple heat transfer tubes 13, an inlet tube 14, an upper guiding panel 141, a spurting tube 15, a lower guiding panel 152 and a drain tube 18.
The shell 10 is tubular and has a front opening, a rear opening, a shell side inlet 101 and a shell side outlet 102. The shell side inlet 101 is formed through the shell 10 and is disposed adjacent to the rear opening of the shell 10. The shell side outlet 102 is formed through the shell 10 and is disposed adjacent to the front opening of the shell 10.
The tube panels 11 are respectively mounted at and cover the front opening and the rear opening of the shell 10. Each tube panel 11 has multiple through holes separately formed through the tube panel 11. The partition panels 12 are separately arranged in the shell 10 and between the tube panels 11. Each partition panel 12 has multiple through holes separately formed through the partition panel 12. The supporting rods 16 are axially mounted in the shell 10 and through the through holes of the partition panels 12 to support and hold the partition panels 12. The heat transfer tubes 13 are axially mounted in the shell 10 and through the through holes of the partition panels 12. Each heat transfer tube 13 has two ends respectively mounted through the through holes of the tube panels 11 and corresponding to the front opening and the rear opening of the shell 10. The inlet tube 14 is mounted in the shell 10, may be disposed between the rear opening of the shell 10 and the tube panel 11 that is mounted at the rear opening of the shell 10, and has an inner end and an outer end. The outer end of the inlet tube 14 is connected to and communicates with the shell side inlet 101 of the shell 10. The upper guiding panel 141 is mounted on an inner wall of the inlet tube 14, is disposed adjacent to the inner end of the inlet tube 14 and protrudes inwardly and downwardly.
With further reference to
The drain tube 18 is mounted on and through a bottom of the shell 10.
The front cover 20 is securely mounted on the front opening of the shell 10 and has a tube side inlet 201 formed through the front cover 20 and communicating with the heat transfer tubes 13.
The rear cover 30 is securely mounted on the rear opening of the shell 10 and has a tube side outlet 301 formed through the rear cover 30 and communicating with the heat transfer tubes 13. Preferably, the tube side outlet 301 of the rear cover 30 is disposed higher than the tube side inlet 201 of the front cover 20.
With further reference to
The second guiding panel 42 is flat, is mounted between the first guiding panel 41 and the tube panel 11 that is mounted at the front opening of the shell 10, is connected to the first guiding panel 41 via multiple fasteners 43, and has multiple guide holes 421 separately formed through the second guiding panel 42.
With reference to
Tube side fluid flows into the shell-and-tube heat exchanger from the tube side inlet 201 of the front cover 20 and flows along the curved first guiding panel 41 to distribute to the guide holes 411 of the first guiding panel 41. Then the tube side fluid flows through the guide holes 411, 421 of the first guiding panel 41 and the second guiding panel 42, into the heat transfer tubes 13 and through the tube side outlet 301 of the rear cover 30 to flow out of the shell-and-tube heat exchanger. Shell side fluid flows through the shell side inlet 101 of the shell 10 to flow into the inlet tube 14 and the spurting tube 15. Then the shell side fluid flows through the spurting holes 151 of the spurting tube 15 to spurt into the shell 10 and exchanges heat with the tube side fluid in the heat transfer tubes 13.
When the shell side fluid is steam, the steam flows through the inlet tube 14 and the spurting tube 15, and bumps against the upper guiding panel 141 and the lower guiding panel 152, and condensate is formed on the upper and lower guiding panels 141, 152. Then the condensate accumulated in the spurting tube 15 is drained out of the spurting tube 15 via the drain hole 153. Thus, humidity of the shell side fluid is lowered so less condensate is formed in the shell 10.
With further reference to
Even though numerous characteristics and advantages of the present invention have been set forth in the foregoing description, together with details of the structure and features of the invention, the disclosure is illustrative only. Changes may be made in the details, especially in matters of shape, size, and arrangement of parts within the principles of the invention to the full extent indicated by the broad general meaning of the terms in which the appended claims are expressed.
