EP0209463B1 - Anlage zum Heizen von Flüssigkeiten auf unterschiedlichen Temperaturstufen - Google Patents

Anlage zum Heizen von Flüssigkeiten auf unterschiedlichen Temperaturstufen Download PDF

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Publication number
EP0209463B1
EP0209463B1 EP86401579A EP86401579A EP0209463B1 EP 0209463 B1 EP0209463 B1 EP 0209463B1 EP 86401579 A EP86401579 A EP 86401579A EP 86401579 A EP86401579 A EP 86401579A EP 0209463 B1 EP0209463 B1 EP 0209463B1
Authority
EP
European Patent Office
Prior art keywords
liquid
exchanger
installation
vat
temperature
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
EP86401579A
Other languages
English (en)
French (fr)
Other versions
EP0209463A1 (de
Inventor
Georges Austruy
François Cagnon
Denis Di Paola
André Vinchon
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.)
Engie SA
Original Assignee
Gaz de France SA
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 Gaz de France SA filed Critical Gaz de France SA
Priority to AT86401579T priority Critical patent/ATE46569T1/de
Publication of EP0209463A1 publication Critical patent/EP0209463A1/de
Application granted granted Critical
Publication of EP0209463B1 publication Critical patent/EP0209463B1/de
Expired legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/18—Water-storage heaters
    • F24H1/20—Water-storage heaters with immersed heating elements, e.g. electric elements or furnace tubes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/10—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium
    • F24H1/107—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium using fluid fuel

Definitions

  • the present invention essentially relates to an installation for heating industrial liquids at different temperature levels.
  • liquids are at a high temperature , for example greater than 60 ° C, or at an average temperature, for example less than or equal to 60 ° C, is very often necessary.
  • heating methods and installations comprising a tank containing a liquid heated by an exchanger or tube immersed in this liquid and connected to the outlet of a burner, and in which the outlet of the exchanger or tube is connected to a second enclosure containing a second liquid heated by bubbling the hot gases leaving the exchanger , in this second liquid.
  • the object of the present invention is to propose an installation which overcomes the above drawbacks and has a high efficiency, in particular with regard to the heating efficiency and that of bringing the heated liquids to the required temperature.
  • the subject of the invention is a heating installation comprising a first tank containing a first liquid, a second tank containing a second liquid, a partition separating the first liquid from the second liquid, an exchanger or tube immersed in the liquid of the first tank and connected to the outlet of a burner, this exchanger also being connected to a means for diffusing the hot gases leaving the exchanger, said diffusing means being immersed in the liquid, contained in the second tank, characterized in that the first and second tanks each comprise a supply and withdrawal line for the first liquid and the second liquid which is heated to a temperature lower than that of the first liquid, and in that a pump provided with a supply line inlet and outlet immersed in the two tanks allows the transfer of liquid from one tank to another to make the energy need topping up of the two tanks and thus regulate the temperature of the two x liquids in these tanks.
  • an installation in accordance with the principles of the invention essentially comprises two tanks 1 and 2, and immersed and connected heating means for heating the liquids L, and L respectively to different temperatures. 2 contained in tanks 1 and 2 respectively.
  • These tanks 1 and 2 can be constituted by two tanks separated from each other or else directly adjacent, or else formed from a single tank separated by a partition shown diagrammatically in 3.
  • This exchanger 5, which can be a simple submerged tube, is connected by a pipe portion 7 to a diffuser system shown diagrammatically at 8 and immersed in the liquid L 2 of the second tank 2.
  • a pump P provided with an inlet and outlet pipe 9 and 10 plunging into the tanks 1 and 2 allows the transfer of the liquid from one tank to the other.
  • This liquid transfer can be carried out without a pump, that is to say simply by overflowing the liquid from one tank into the other.
  • the combustion products from the burner 4 pass through the exchanger 5 and by heat exchange with the liquid L 1 , the latter is heated to a temperature level above 60 ° C. for example.
  • the fumes leaving at 7 from the exchanger 5 are diffused by bubbling into the tank 2 where the liquid L 2 is heated to a temperature level less than or equal to 60 ° C. for example.
  • the overall heating efficiency of the assembly is conditioned by the reference temperature of the tank 2.
  • the yield varies from 110 to 96% on the lower calorific value for temperatures ranging from 20 ° C to 60 ° C in the tank 2.
  • the dimensioning of the exchanger 5, the volume of the two tanks 1 and 2, and the quantities of liquid to be transferred are to be optimized as a function of the rise in temperature of the tanks and of the withdrawal methods.
  • An installation was therefore carried out according to the invention allowing the heating of liquids at two different temperature levels with a single heating equipment, the heating efficiency of this installation, based on the lower calorific value, being greater than 100% than that either in the case where it is desired to use a single liquid at a temperature above 60 ° C, or in the case where it is desired to use two liquids at respectively different temperatures, one being greater than 60 ° C and the other less than 60 ° C.

Landscapes

  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Frying-Pans Or Fryers (AREA)
  • Catching Or Destruction (AREA)

Claims (1)

  1. Heizungsanlage mit einer ersten, eine erste Flüssigkeit (L1) enthaltenden Wanne (1), einer zweiten, eine zweite Flüssigkeit (L2) enthaltenden Wanne (2), einer die erste Flüssigkeit von der zweiten Flüssigkeit trennenden Wand (3), einem in der Flüssigkeit (L1) der ersten Wanne (1) eingetauchten und am Auslaß (6) eines Brenners (4) angeschlossenen Austauscher oder Rohr (5), wobei dieser Austauscher mit einem Diffusor (8) für die aus dem Austauscher (5) kommenden warmen Gase auch angeschlossen ist, und der besagte Diffusor in der in der zweiten Wanne (2) enthaltenen Flüssigkeit (L2) eingetaucht ist, dadurch gekennzeichnet, daß die erste und zweite Wanne (1, 2) jeweils eine Zufuhr(11) und Abfuhrleitung (12, 13) für die erste Flüssigkeit (L1) und für die zweite Flüssigkeit (L2), die auf eine niedrigere Temperatur als die der ersten Flüssigkeit (L1) erwärmt ist, aufweist, und daß eine eine in den beiden Wannen (1, 2) eingetauchte Einlaß-und Auslaßleitung (9, 10) aufweisende Pumpe (P) die Versetzung der Flüssigkeit von einer Wanne in die andere ermöglicht, um die Ernergiebedarfergänzung der beiden Wannen (1, 2) durchzuführen und um damit die Temperatur der beiden Flüssigkeiten (L1, L2) in diesen Wannen zu regulieren.
EP86401579A 1985-07-17 1986-07-15 Anlage zum Heizen von Flüssigkeiten auf unterschiedlichen Temperaturstufen Expired EP0209463B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT86401579T ATE46569T1 (de) 1985-07-17 1986-07-15 Anlage zum heizen von fluessigkeiten auf unterschiedlichen temperaturstufen.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8510974A FR2585112B1 (fr) 1985-07-17 1985-07-17 Procede de chauffage de liquides a des niveaux de temperature differents, et installation pour la mise en oeuvre de ce procede
FR8510974 1985-07-17

Publications (2)

Publication Number Publication Date
EP0209463A1 EP0209463A1 (de) 1987-01-21
EP0209463B1 true EP0209463B1 (de) 1989-09-20

Family

ID=9321396

Family Applications (1)

Application Number Title Priority Date Filing Date
EP86401579A Expired EP0209463B1 (de) 1985-07-17 1986-07-15 Anlage zum Heizen von Flüssigkeiten auf unterschiedlichen Temperaturstufen

Country Status (9)

Country Link
US (1) US4719878A (de)
EP (1) EP0209463B1 (de)
JP (1) JPS6217564A (de)
KR (1) KR870001450A (de)
AT (1) ATE46569T1 (de)
CA (1) CA1268087C (de)
DE (1) DE3665765D1 (de)
ES (1) ES2000688A6 (de)
FR (1) FR2585112B1 (de)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6338337B1 (en) * 1999-09-30 2002-01-15 Inproheat Industries Ltd. Two-stage heat recovery for submerged combustion heating system
US6293277B1 (en) * 1999-09-30 2001-09-25 Inproheat Industries Ltd. Sludge treatment system using two-stage heat recovery submerged combustion

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2594063A (en) * 1952-04-22 norman
US2611362A (en) * 1946-04-03 1952-09-23 Swindin Norman Submersible burner
US2981250A (en) * 1958-02-07 1961-04-25 Richard M Stewart Submerged combustion heating apparatus
US3716045A (en) * 1969-05-03 1973-02-13 Siegener Ag Heat exchanger
ES437211A1 (es) * 1974-04-29 1977-02-01 Thurley Ltd John Aparato de intercambio termico.
US4393815A (en) * 1981-04-16 1983-07-19 Pedersen Niels R Heating plant
FR2550614A2 (fr) * 1983-06-14 1985-02-15 Deleage Pierre Chaudiere a condensation

Also Published As

Publication number Publication date
EP0209463A1 (de) 1987-01-21
JPS6217564A (ja) 1987-01-26
DE3665765D1 (en) 1989-10-26
FR2585112A1 (fr) 1987-01-23
FR2585112B1 (fr) 1987-11-27
CA1268087A (en) 1990-04-24
KR870001450A (ko) 1987-03-13
ES2000688A6 (es) 1988-03-16
CA1268087C (en) 1990-04-24
ATE46569T1 (de) 1989-10-15
US4719878A (en) 1988-01-19

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