US2162871A - Condenser - Google Patents

Condenser Download PDF

Info

Publication number
US2162871A
US2162871A US200344A US20034438A US2162871A US 2162871 A US2162871 A US 2162871A US 200344 A US200344 A US 200344A US 20034438 A US20034438 A US 20034438A US 2162871 A US2162871 A US 2162871A
Authority
US
United States
Prior art keywords
pass
tubes
passes
steam
condenser
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.)
Expired - Lifetime
Application number
US200344A
Inventor
Charles B Tuley
John W Mcnulty
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.)
CBS Corp
Original Assignee
Westinghouse Electric and Manufacturing Co
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 Westinghouse Electric and Manufacturing Co filed Critical Westinghouse Electric and Manufacturing Co
Priority to US200344A priority Critical patent/US2162871A/en
Application granted granted Critical
Publication of US2162871A publication Critical patent/US2162871A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B1/00Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/02Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/184Indirect-contact condenser
    • Y10S165/205Space for condensable vapor surrounds space for coolant
    • Y10S165/207Distinct outlets for separated condensate and gas
    • Y10S165/213Distinct outlets for separated condensate and gas including baffle partially covering a group of coolant tubes

Definitions

  • Our invention relates to surface condensers of the multiple-pass type and it has for an object to provide apparatus of this character wherein the tubes of the respective passes are disposed in such manner that the tubes of the first pass are more widely spaced than the tubes of the second or subsequent passes.
  • the first pass may have a capacity'for condensation of the order, of 60 to 65 percent of the total capacity of the condenser.
  • the tubes of the first pass should have greater spacing or pitch than the second and so on. Therefore, in accordance with our invention, we provide a condenser wherein the tubes of the first pass are spaced further apart or are more widely pitched than those of the subsequent pass, to provide greater flow area for the increased quantity of steam entering the first pass.
  • a further object of our invention is to. provide a condenser of the multiple-pass type with the tubes of each pass directly'exposed to entering steam and with the spacing or pitch of the tubes of the passes a'maximum in the initial pass and a minimum in the final pass.
  • a further object of our invention is to provide a radial flow condenser having the tubes arranged in horizontallyjuxtaposed first and second passes of substantially equal arcuate extent and wherein the tubes of the first pass occupy a relatively larger cross-sectional area of the nest than those of the second pass so that the tubes of the first pass may be more widely spaced.
  • a further object of our invention is to provide a radial flow condenser having the tubes arranged in horizontally juxtaposed first and second passes of substantially equal arcuate extent and the group of tubes of the first pass being so arranged that a central portion protrudes reentrantly within the group of tubes of the second pass, thereby providing greater area for the first pass so that the tubes of the latter may be more widely spaced.
  • a further object of our invention is to provide a radial flow condenser with the tubes arranged in horizontally juxtaposed first and second passes wherein the tubes of the first pass include a central group protruding within the group of tubes of the second pass so that the tubes of the first pass may be more widely spaced and so that a laterally symmetrical air ofitake may be arranged within the confines of the tubes of the first and colder pass.
  • Fig. l is a transverse sectional viewof a coninto inlet'and outlet chambers l1 and I8, respectively.
  • the chamber Ii is provided with an inlet connection i9 while the chamber i8 is provided'with a corresponding outlet connection 2
  • a plurality of tubes 22 extend longitudinally of the shell from the waterbox !3 to the waterbox,
  • the tubes 22 form a radial-flow tube nest 23 of substantially circular cross-section and are so disposed as to define, with respect to the shell, a steam space diminishing in cross sectional area from the steam inlet opening l2 at the top of the condenser to the bottom of the shell.
  • steam may freely enter the tube nest at all points around its periphery.
  • Exhaust pipes 28 and 29 conduct the air and non-condensable gases from the oiftake to the exterior of the condenser, in a well known manner.
  • the tube nest 23, as herein illustrated, consists of a first pass 31 and a second pass 38.
  • the first pass has a greater cross-sectional area than the second pass, as indicated by the dotted line showing of the partition I6 which divides the waterbox l3 into inlet and outlet chambers.
  • Both passes are provided with approximately the same number of tubes of the same size; and, since the first pass has a greater cross-sectional area than the second pass, the tubes of the first pass are spaced farther apart than those of the second pass, as may be seen from Fig. 2. This construction provides more space for flow of steam between the tubes of the first pass than between those of the second pass.
  • the wider spacing of the tubes of the first pass provides greater entrance area to accommodate the relatively greater quantity of steam which may be condensed by the first pass. thermore, if the greater cross-sectional area of the first pass to obtain the wider tube spacing is secured by having a portion of the tubes of the first pass protrude reentrantly into the tubes of the second pass, such protruding portion of tubes is used to enclose the air offtake to advantage, not only for the reason that a symmetrical location of the air offtake is preserved, but for the further reason that such offtake is entirely surrounded by the relatively cooler tubes of the first pass.
  • a condenser a shell, a nest of tubes within the shell and defining a steam space with respect to the latter and the shell having an exhaust steam admission opening communicating with the space, means providing an air offtake, and means cooperating with the tubes to provide for flow of water therethrough in a plurality of passes in succession, each pass having tubes directly exposed to said steam space so that steam fiows from the latter in parallel through the passes toward the ofitake and the tubes of the first pass being more widely spaced than those of the final pass.
  • a shell a nest of tubes within the shell and defining a steam space with respect to the latter and the shell having an exhaust steam admission opening at the top thereof communicating with the space, means cooperating with the tubes to provide for fiow of water therethrough in a plurality of passes in succession, and an air ofitake, said passes being comprised by horizontally juxtaposed groups of tubes and the outermost tubes of each group being directly exposed to said steam space so that steam flows from the latter in parallel among the tubes of the passes toward the air ofitake and said groups being of substantially equal arcuate extent with the tubes of the initial pass occupying a larger cross-sectional area than the tubes of the final pass and with the spacing of the tubes of the first pass greater than that of the final pass.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

June 20, 1939. c. B. TULEY ET AL CONDENSER Filed April 6, I938 INVENTORS f-Zv-uuu-zs B Tin-er m Jenn w. MgNuL-rr. a. 15, M ATTORNEY Patented June 20, 1939 UNITED STATES CONDENSER Charles B. Tuley, Glenolden, and John W. Mc- Nulty, Ridley Park, Pa., assignors to Westinghouse Electric & Manufacturing Company,
East Pittsburgh, Pa. sylvania a corporation of Penn- Application April 6, 1938, Serial No, 200,344
3 Claims.
Our invention relates to surface condensers of the multiple-pass type and it has for an object to provide apparatus of this character wherein the tubes of the respective passes are disposed in such manner that the tubes of the first pass are more widely spaced than the tubes of the second or subsequent passes.
It has been customary, in laying out tube sheets for two or multiple pass condensers, to pitch the tubes closer together in the first Water pass than in the second or subsequent passes; however, because of the lower water temperature in the first pass, the latterhas the greater condensing capacity. Forexample, with a two-pass condenser having substantially equal numbers of tubes in-each pass, the first pass may have a capacity'for condensation of the order, of 60 to 65 percent of the total capacity of the condenser. In order that the passes may be arranged to accommodate steam inproportion to the capacities thereof, the tubes of the first pass should have greater spacing or pitch than the second and so on. Therefore, in accordance with our invention, we provide a condenser wherein the tubes of the first pass are spaced further apart or are more widely pitched than those of the subsequent pass, to provide greater flow area for the increased quantity of steam entering the first pass.
A further object of our invention is to. provide a condenser of the multiple-pass type with the tubes of each pass directly'exposed to entering steam and with the spacing or pitch of the tubes of the passes a'maximum in the initial pass and a minimum in the final pass.
A further object of our invention is to provide a radial flow condenser having the tubes arranged in horizontallyjuxtaposed first and second passes of substantially equal arcuate extent and wherein the tubes of the first pass occupy a relatively larger cross-sectional area of the nest than those of the second pass so that the tubes of the first pass may be more widely spaced.
A further object of our invention is to provide a radial flow condenser having the tubes arranged in horizontally juxtaposed first and second passes of substantially equal arcuate extent and the group of tubes of the first pass being so arranged that a central portion protrudes reentrantly within the group of tubes of the second pass, thereby providing greater area for the first pass so that the tubes of the latter may be more widely spaced.
A further object of our invention is to provide a radial flow condenser with the tubes arranged in horizontally juxtaposed first and second passes wherein the tubes of the first pass include a central group protruding within the group of tubes of the second pass so that the tubes of the first pass may be more widely spaced and so that a laterally symmetrical air ofitake may be arranged within the confines of the tubes of the first and colder pass.
These and other objects are effected by our invention as will be apparent from the following description and claims taken in connection with the accompanying drawing, forming apart of this application, in which:
Fig. l is a transverse sectional viewof a coninto inlet'and outlet chambers l1 and I8, respectively. The chamber Ii, is provided with an inlet connection i9 while the chamber i8 is provided'with a corresponding outlet connection 2|. A plurality of tubes 22 extend longitudinally of the shell from the waterbox !3 to the waterbox,
l4 whereby water entering ,the inlet chamber of the box [3 may. flow through certain of. the tubes 22xto the waterbox it where the flow is reversed. and the water conveyed through the remaining tubes to the outlet chamber I8 of the Water box l3.
The tubes 22 form a radial-flow tube nest 23 of substantially circular cross-section and are so disposed as to define, with respect to the shell, a steam space diminishing in cross sectional area from the steam inlet opening l2 at the top of the condenser to the bottom of the shell. By this arrangement, steam may freely enter the tube nest at all points around its periphery.
At the center of the tube nest 23, is an air oiftake core 25, extending the entire length thereof. Exhaust pipes 28 and 29 conduct the air and non-condensable gases from the oiftake to the exterior of the condenser, in a well known manner.
Steam, entering the condenser through the inlet opening I2 at the top thereof, passes radially among the tubes of the nest 23, and is condensed, air and non-condensable vapors passing into the offtake 2%, the bailies 3| and 32 providing for distribution of steam in the nest. The lowermost portion of the shell has one or more openings 36 for conducting condensate to a suitable hotwell (not shown).
The tube nest 23, as herein illustrated, consists of a first pass 31 and a second pass 38. The first pass has a greater cross-sectional area than the second pass, as indicated by the dotted line showing of the partition I6 which divides the waterbox l3 into inlet and outlet chambers.
Both passes are provided with approximately the same number of tubes of the same size; and, since the first pass has a greater cross-sectional area than the second pass, the tubes of the first pass are spaced farther apart than those of the second pass, as may be seen from Fig. 2. This construction provides more space for flow of steam between the tubes of the first pass than between those of the second pass.
While the passes are of equal peripheral extent, the wider spacing of the tubes of the first pass provides greater entrance area to accommodate the relatively greater quantity of steam which may be condensed by the first pass. thermore, if the greater cross-sectional area of the first pass to obtain the wider tube spacing is secured by having a portion of the tubes of the first pass protrude reentrantly into the tubes of the second pass, such protruding portion of tubes is used to enclose the air offtake to advantage, not only for the reason that a symmetrical location of the air offtake is preserved, but for the further reason that such offtake is entirely surrounded by the relatively cooler tubes of the first pass.
While we have shown herein a condenser having only two passes, it will be clear to those skilled in the art that the same principles of contruction can be applied to condensers having a greater number of passes with equally advantageous results.
While we have shown our invention in but one form, it will'be obvious to those skilled in the art that it is not so limited, but is susceptible of various changes and modifications without departing from the spirit thereof, and we desire, therefore, that only such limitations shall be placed thereupon as are imposed by the prior art or as are specifically set forth in the appended claims.
What we claim is:
1. In a condenser, a shell, a nest of tubes within the shell and defining a steam space with respect to the latter and the shell having an exhaust steam admission opening communicating with the space, means providing an air offtake, and means cooperating with the tubes to provide for flow of water therethrough in a plurality of passes in succession, each pass having tubes directly exposed to said steam space so that steam fiows from the latter in parallel through the passes toward the ofitake and the tubes of the first pass being more widely spaced than those of the final pass.
2. In a condenser, a shell, a nest of tubes within the shell and defining a steam space with respect to the latter and the shell having an exhaust steam admission opening at the top thereof communicating with the space, means cooperating with the tubes to provide for fiow of water therethrough in a plurality of passes in succession, and an air ofitake, said passes being comprised by horizontally juxtaposed groups of tubes and the outermost tubes of each group being directly exposed to said steam space so that steam flows from the latter in parallel among the tubes of the passes toward the air ofitake and said groups being of substantially equal arcuate extent with the tubes of the initial pass occupying a larger cross-sectional area than the tubes of the final pass and with the spacing of the tubes of the first pass greater than that of the final pass.
3. In a condensena shell, a nest of tubes within the shell and defining, with respect to the latter, a steam space which substantially encompasses the nest and the shell having an exhaust steam admission opening communicating with the space, means cooperating with the tubes to provide for flow of water therethrough in first and second passes, the tubes of the passes being arranged in horizontally juxtaposed groups of substantially equal numbers of tubes and of substantially equal peripheral extents, the tube group of the first pass protruding reentrantly into the tube group of the second pass, with the cross-sectional area occupied by the first pass larger than that of the second pass and with the tubes of the first pass more widely spaced than those of the second pass, and an air offtake encompassed by tubes of the first pass and arranged at the region of the protruding tubes thereof, the outermost tubes of each pass being directly exposed to said steam space so that 50 steam fiows from the latter in parallel through the passes toward the ofitake.
CHARLES B. TULEY. JOHN W. MCNUL'I'Y.
US200344A 1938-04-06 1938-04-06 Condenser Expired - Lifetime US2162871A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US200344A US2162871A (en) 1938-04-06 1938-04-06 Condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US200344A US2162871A (en) 1938-04-06 1938-04-06 Condenser

Publications (1)

Publication Number Publication Date
US2162871A true US2162871A (en) 1939-06-20

Family

ID=22741326

Family Applications (1)

Application Number Title Priority Date Filing Date
US200344A Expired - Lifetime US2162871A (en) 1938-04-06 1938-04-06 Condenser

Country Status (1)

Country Link
US (1) US2162871A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4357991A (en) * 1979-11-23 1982-11-09 C-I-L Inc. Heat exchanger having improved tube layout
US6041852A (en) * 1995-12-15 2000-03-28 Kabushiki Kaisha Toshiba Condenser
US20160290723A1 (en) * 2014-01-23 2016-10-06 Mitsubishi Hitachi Power Systems, Ltd. Condenser

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4357991A (en) * 1979-11-23 1982-11-09 C-I-L Inc. Heat exchanger having improved tube layout
US6041852A (en) * 1995-12-15 2000-03-28 Kabushiki Kaisha Toshiba Condenser
US20160290723A1 (en) * 2014-01-23 2016-10-06 Mitsubishi Hitachi Power Systems, Ltd. Condenser
US10502492B2 (en) * 2014-01-23 2019-12-10 Mitsubishi Hitachi Power Systems, Ltd. Condenser for condensing steam from a steam turbine

Similar Documents

Publication Publication Date Title
US2830797A (en) Refrigerant condenser
US2049748A (en) Heat exchanger
US1917595A (en) Heater
US3338052A (en) High recovery condenser
US4165783A (en) Heat exchanger for two vapor media
US2756028A (en) Heat exchange apparatus
US2162871A (en) Condenser
US2180840A (en) Condenser apparatus
US2848197A (en) Condenser
US1855390A (en) Surface condenser
US3193002A (en) Feed water heaters for steam turbine plant
US4047562A (en) Heat exchanger utilizing a vaporized heat-containing medium
US2279552A (en) Heat exchange apparatus
US1780781A (en) Condenser
US3178891A (en) Feedwater heater
US1759011A (en) Reheater
US1941650A (en) Surface condenser
US1764716A (en) Condenser
US2312113A (en) Condenser apparatus
US1845542A (en) Condenser
US1845541A (en) Condenser
US1711332A (en) Surface condenser
US1634903A (en) Surface condenser
US1845549A (en) Condenser
US1626849A (en) Condensing apparatus