EP2562506A1 - Rohrbündelwärmeübertrager - Google Patents

Rohrbündelwärmeübertrager Download PDF

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Publication number
EP2562506A1
EP2562506A1 EP11178395A EP11178395A EP2562506A1 EP 2562506 A1 EP2562506 A1 EP 2562506A1 EP 11178395 A EP11178395 A EP 11178395A EP 11178395 A EP11178395 A EP 11178395A EP 2562506 A1 EP2562506 A1 EP 2562506A1
Authority
EP
European Patent Office
Prior art keywords
shell
tube
spurting
heat exchanger
inlet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP11178395A
Other languages
English (en)
French (fr)
Inventor
Yung-Sho Yang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yu Shen Machinery Co Ltd
Original Assignee
Yu Shen Machinery Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yu Shen Machinery Co Ltd filed Critical Yu Shen Machinery Co Ltd
Priority to EP11178395A priority Critical patent/EP2562506A1/de
Publication of EP2562506A1 publication Critical patent/EP2562506A1/de
Withdrawn legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus

Definitions

  • 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.
  • a conventional shell-and-tube heat exchanger 90 comprises a shell assembly, a front cover 92, a rear cover 93 and a safety valve 95.
  • 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.
  • Condensate formed in the shell 91 is drained to the seam trap 94 through the condensate outlet 917 of the shell 91.
  • 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.
  • the heating surfaces on one heat transfer tube 916 differ with positions.
  • 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.
  • the shell side fluid has to flow downwardly and upwardly and the heat transfer tubes 916 hinder the shell side fluid, the shell side fluid tends to flow along a side channel 918 defined around an inner surface of the shell 91. Therefore, the conventional shell-and-tube heat exchanger 90 has low heat transfer efficiency.
  • 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.
  • a shell-and-tube heat exchanger in accordance with the present invention comprises a shell assembly, a front cover 20, a rear cover 30, a first guiding panel 41 and a second guiding panel 42.
  • 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.
  • the spurting tube 15 is axially mounted in the shell 10, may be disposed at a bottom of the shell 10, is mounted through the tube panels 11 and the partition panels 12 and has a first end, a second end, multiple spurting holes 151 and a drain hole 153.
  • the first end of the spurting tube 15 is connected to and communicates with the inner end of the inlet tube 14.
  • the spurting holes 151 are separately formed through the spurting tube 15.
  • the drain hole 153 is formed through the spurting tube 15 and is disposed adjacent to the second end of the spurting tube 15.
  • the lower guiding panel 152 is mounted on an inner wall of the spurting tube 15, is disposed adjacent to the first end of the spurting tube 15 and protrudes inwardly and downwardly.
  • 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.
  • the tube side outlet 301 of the rear cover 30 is disposed higher than the tube side inlet 201 of the front cover 20.
  • the first guiding panel 41 is mounted in the front cover 20, curves outward toward the tube side inlet 201 of the front cover 20 and has multiple guide holes 411 separately formed through the first guiding panel 41.
  • 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.
  • the shell-and-tube heat exchanger may further comprise a steam inlet valve 511, a cooling water inlet valve 512, a pressure release valve 513, a cooling water outlet valve 52, a pressure gauge 53, a vacuum breaker 54, a safety valve 55, a steam trap 56 and multiple temperature sensors 571, 572, 573, 574.
  • the steam inlet valve 511 and the cooling water inlet valve 512 are connected to the shell side inlet 101 of the shell 10.
  • the pressure release valve 513 is connected to the steam inlet valve 511 to control the shell side fluid.
  • the cooling water outlet valve 52 is connected to the shell side outlet 102.
  • the pressure gauge 53, the vacuum breaker 54 and the safety valve 55 are mounted on the shell 10 to detect and control pressure of the shell side fluid in the shell 10.
  • the steam trap 56 is connected to the drain tube 18 of the shell 10 via a pipeline so condensate formed in the shell 10 can be drained via the steam trap 56.
  • the temperature sensors 571, 572, 573, 574 are respectively mounted on the front cover 20, the rear cover 30, the pipeline that connects the steam trap 56 to the drain tube 18 of the shell 10 and the cooling water outlet valve 52 to detect temperatures of the tube side fluid, the condensate and the shell side fluid.
  • 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.
  • 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.
  • the condensate accumulated in the spurting tube 15 is drained out of the spurting tube 15 via the drain hole 153.
  • humidity of the shell side fluid is lowered so less condensate is formed in the shell 10.
  • the shell-and-tube heat exchanger as described has the following advantages.
  • shell side fluid in the shell 10 is steam
  • the spurting tube 15 since the spurting tube 15 is disposed at the bottom of the shell 10, the shell side fluid always flows upwardly toward a top of the shell 10.
  • the shell side fluid does not become turbulent, no air film occurs in the shell 10 and lower surfaces of the heat transfer tubes 13 act as heating surfaces. Consequently, the shell-and-tube heat exchanger has high heat transfer efficiency.
  • the tube side fluid flows equally into each heat transfer tubes 13. Therefore, the tube side fluid in different heat transfer tubes 13 has equal heat transfer efficiencies.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
EP11178395A 2011-08-23 2011-08-23 Rohrbündelwärmeübertrager Withdrawn EP2562506A1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP11178395A EP2562506A1 (de) 2011-08-23 2011-08-23 Rohrbündelwärmeübertrager

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP11178395A EP2562506A1 (de) 2011-08-23 2011-08-23 Rohrbündelwärmeübertrager

Publications (1)

Publication Number Publication Date
EP2562506A1 true EP2562506A1 (de) 2013-02-27

Family

ID=44508977

Family Applications (1)

Application Number Title Priority Date Filing Date
EP11178395A Withdrawn EP2562506A1 (de) 2011-08-23 2011-08-23 Rohrbündelwärmeübertrager

Country Status (1)

Country Link
EP (1) EP2562506A1 (de)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117989898A (zh) * 2024-04-03 2024-05-07 安徽省信邦化工工程装备有限公司 一种高效循环加氢换热器

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE273452C (de) *
US3173480A (en) * 1958-10-13 1965-03-16 Kenneth O Parker Heat exchanger assembly
EP1498678A1 (de) * 2003-07-12 2005-01-19 Borsig GmbH Wärmetauscher mit einem Bypassrohr

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE273452C (de) *
US3173480A (en) * 1958-10-13 1965-03-16 Kenneth O Parker Heat exchanger assembly
EP1498678A1 (de) * 2003-07-12 2005-01-19 Borsig GmbH Wärmetauscher mit einem Bypassrohr

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117989898A (zh) * 2024-04-03 2024-05-07 安徽省信邦化工工程装备有限公司 一种高效循环加氢换热器

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