GB711554A - Improvements relating to regenerators for coke ovens and other industrial furnaces - Google Patents

Improvements relating to regenerators for coke ovens and other industrial furnaces

Info

Publication number
GB711554A
GB711554A GB20503/52A GB2050352A GB711554A GB 711554 A GB711554 A GB 711554A GB 20503/52 A GB20503/52 A GB 20503/52A GB 2050352 A GB2050352 A GB 2050352A GB 711554 A GB711554 A GB 711554A
Authority
GB
United Kingdom
Prior art keywords
apertures
channels
flue
regenerator
gas
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
Application number
GB20503/52A
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.)
Didier Kogag Hinselmann Koksofenbau und Gasverwertung AG
Original Assignee
Didier Kogag Hinselmann Koksofenbau und Gasverwertung AG
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 Didier Kogag Hinselmann Koksofenbau und Gasverwertung AG filed Critical Didier Kogag Hinselmann Koksofenbau und Gasverwertung AG
Publication of GB711554A publication Critical patent/GB711554A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B5/00Coke ovens with horizontal chambers
    • C10B5/10Coke ovens with horizontal chambers with heat-exchange devices
    • C10B5/12Coke ovens with horizontal chambers with heat-exchange devices with regenerators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D17/00Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles
    • F28D17/02Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles using rigid bodies, e.g. of porous material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Coke Industry (AREA)

Abstract

711,554. Regenerators for coke ovens &c. D IDIER-KOGAG-HINSELMANN, KOKSOPENBAU UND GASVERWERTUNG AKT.-GES. Aug. 14, 1952 [Aug. 14, 1951; Dec. 29, 1951; Feb. 2, 1952; Feb. 26, 1952], No. 20503/52. Class 64(1) In a regenerator for a coke oven or other industrial furnace, a bottom flue extending over the whole length of the regenerator is divided by longitudinal partitions 16-19 into separate longitudinal channels 20-24, each communicating with one cell or section 1-5 of the regenerator, and means are provided for separately regulating the flow of gas through each channel. Air or gas flowing into the regenerator passes through one set of regulating apertures by which the flow through each channel is controlled, and the waste gases discharged from the regenerator through the same or different flue channels pass through a second set of regulating apertures. In the form shown in Figs. 1 and 2, the bottom flue is divided by a vertical wall 9 into two flue chambers each divided into longitudinal channels. Each cell or section of the regenerator communicates with one channel in each flue chamber through a pasage in the wall 9. The regulating means comprise obstructing bricks or guide vanes in the mouths of the channels. Air or gas to be heated enters the regenerator from an inlet through the channels in one flue chamber, and t h e waste heating gases leave it through the channels in the other flue chamber. In a modified arrangement, the air or gas and the waste gases flow through the channels in both flue chambers. All the channels are connected through separate ducts such as 98, 99, 100, Fig. 12, to a common air or gas supply chamber 101 and a common waste gas exhaust chamber 105. The outlet from the latter is controlled by a flap 104. The outlets from the ducts to the chamber 105 may be similarly controlled. The longitudinal channels and the ducts are of different cross-sectional area. In a form in which the bottom flue is not divided by a vertical wall, two sets of regulating apertures are carried by two separate doors hinged on opposite sides of the mouth of the flue. One door is closed over the mouths of all the channels when the air or gas is flowing in, and the other in place of the first when waste gas is being discharged. Each door has two openings, adjustable by slides, for each channel. In a modification the mouth of the flue is divided by a central pillar into two parts each provided with two apertured doors. In both forms the doors are operated automatically by means which open and close the exhaust valve for the exhaust gases. In another form, Fig. 17, the difference between the rates of inflow and outflow through the channels is obtained by the association of a fixed apertured plate 107 with a vertically slidable plate 108 having two sets of apertures 130-139 which are adjustable by slides. The apertures of one set alternate with those of the other. When the apertures in one set are opposite the apertures in the plate 107, the apertures in the other set are closed by the plate. The plate 108 may be moved simultaneously with the exhaust damper 155 and air damper 153. Alternatively, the two sets of apertures may be provided in a rotatable damper, Fig. 20, comprising rings 168 supported from a hollow shaft 161 by radial arms 166. The rings are connected at 90 degrees intervals by vertical sealing strips which form the apertures. The sizes of the apertures in two adjacent sectors are controlled by plates 170 slidable in grooves in the rings.
GB20503/52A 1951-08-14 1952-08-14 Improvements relating to regenerators for coke ovens and other industrial furnaces Expired GB711554A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE711554X 1951-08-14

Publications (1)

Publication Number Publication Date
GB711554A true GB711554A (en) 1954-07-07

Family

ID=6620759

Family Applications (1)

Application Number Title Priority Date Filing Date
GB20503/52A Expired GB711554A (en) 1951-08-14 1952-08-14 Improvements relating to regenerators for coke ovens and other industrial furnaces

Country Status (1)

Country Link
GB (1) GB711554A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1078994B (en) * 1956-05-28 1960-04-07 Otto & Co Gmbh Dr C Throttle device for distribution channels in regenerative ovens, especially for chamber ovens for the production of coke and gas
DE1084689B (en) * 1957-03-16 1960-07-07 Koppers Gmbh Heinrich Reversing device for regenerative coke oven batteries
DE1119820B (en) * 1958-11-14 1961-12-21 Koppers Gmbh Heinrich Regenerative coke oven battery
US4257476A (en) * 1979-03-29 1981-03-24 Ppg Industries, Inc. Manifold regeneration flues for regenerative furnaces
EP2522636A3 (en) * 2011-05-10 2013-04-24 Beteiligungen Sorg GmbH & Co. KG Regenerative chamber for a glass melt assembly
WO2013068003A1 (en) * 2011-11-07 2013-05-16 Get Glass Engineering Gmbh Process and device for improving the performance of the regenerators in glass melting and refining processes in cross-fired furnaces with regenerative heaters
CN113462402A (en) * 2021-07-29 2021-10-01 黑龙江省建筑安装集团有限公司 Dead processing apparatus of board card is turned over in coke oven flue regulation of coke-oven plant

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1078994B (en) * 1956-05-28 1960-04-07 Otto & Co Gmbh Dr C Throttle device for distribution channels in regenerative ovens, especially for chamber ovens for the production of coke and gas
DE1084689B (en) * 1957-03-16 1960-07-07 Koppers Gmbh Heinrich Reversing device for regenerative coke oven batteries
DE1119820B (en) * 1958-11-14 1961-12-21 Koppers Gmbh Heinrich Regenerative coke oven battery
US4257476A (en) * 1979-03-29 1981-03-24 Ppg Industries, Inc. Manifold regeneration flues for regenerative furnaces
EP2522636A3 (en) * 2011-05-10 2013-04-24 Beteiligungen Sorg GmbH & Co. KG Regenerative chamber for a glass melt assembly
US9919942B2 (en) 2011-05-10 2018-03-20 Beteiligungen Sorg Gmbh & Co. Kg Regenerative chamber for a glass melting furnace
WO2013068003A1 (en) * 2011-11-07 2013-05-16 Get Glass Engineering Gmbh Process and device for improving the performance of the regenerators in glass melting and refining processes in cross-fired furnaces with regenerative heaters
CN113462402A (en) * 2021-07-29 2021-10-01 黑龙江省建筑安装集团有限公司 Dead processing apparatus of board card is turned over in coke oven flue regulation of coke-oven plant

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