DE659452C - Procedure for heating liquids - Google Patents

Procedure for heating liquids

Info

Publication number
DE659452C
DE659452C DED68008D DED0068008D DE659452C DE 659452 C DE659452 C DE 659452C DE D68008 D DED68008 D DE D68008D DE D0068008 D DED0068008 D DE D0068008D DE 659452 C DE659452 C DE 659452C
Authority
DE
Germany
Prior art keywords
steam
heating
boiler
engine
heat
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
DED68008D
Other languages
German (de)
Inventor
Anonyme La Distillatio Societe
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.)
DISTILLATION DYNAMIQUE Ste
Original Assignee
DISTILLATION DYNAMIQUE Ste
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 DISTILLATION DYNAMIQUE Ste filed Critical DISTILLATION DYNAMIQUE Ste
Application granted granted Critical
Publication of DE659452C publication Critical patent/DE659452C/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/28Evaporating with vapour compression
    • B01D1/284Special features relating to the compressed vapour
    • B01D1/2856The compressed vapour is used for heating a reboiler or a heat exchanger outside an evaporator
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/28Evaporating with vapour compression
    • B01D1/289Compressor features (e.g. constructions, details, cooling, lubrication, driving systems)

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Description

PATENTANSPRUCII : Verfahren zum Beheizen von Flüssigkeiten nach Patent 639 408, dadurch gekennzeichnet, daß der durch Thermokompression beheizte Teil des Apparates eine zusätzliche Beheizungseinrichtung enthält, in die ein Teil des Abdampfes des Motors, der den Kompressor antreibt, eingeleitet wird, und der Motor so betrieben wird, daß sein Abdampf ausreicht, um die benötigte zusätzliche Wärmemenge der mit Thermokompression beheizten Kolonne zu liefern. PATENT CLAIM: Process for heating liquids according to patent 639 408, characterized in that the part of the heated by thermocompression Apparatus contains an additional heating device into which part of the exhaust steam of the engine driving the compressor is initiated, and the engine is operated is that its exhaust steam is sufficient to the required additional amount of heat with Supply thermocompression heated column.

Claims (1)

Verfahren zum Beheizen von Flüssigkeiten Zusatz zum Fatent 639 408 Das Hauptpatent 639 408 bezieht sich auf die Anwendung der mechanischen Thermokompression. auf Konzentrations-, D estillations-und Rektifikaüonsverfabren und findet vorzugsweise Anwendung bei denjenigen Industrien, bei denen große Heizdampfmengen verbraucht werden. Nach dem Hauptpatent erfolgt ein Teil der Beheizung durch mechanische Theimokompression, während der andere Teil mit Hilfe von Niederdruckdampf durchgeführt wird, der durch Entspannung desjenigen Hochdruckdampfes entsteht, der die Thermokompressionsarbeft geleistet hat.Method for heating liquids Addition to Fatent 639 408 The main patent 639 408 relates to the application of mechanical thermocompression. on concentration, distillation and rectification processes and is preferred Application in those industries in which large amounts of heating steam are consumed will. According to the main patent, part of the heating is done by mechanical thimokompression, while the other part is done with the help of low pressure steam passing through The high-pressure steam that does the thermocompression work is released has done. Die Flüssigkeit wird nachfolgend in verschiedenen Apparaten nach der ersten und zweiten Methode beheizt.The liquid is subsequently in various apparatus according to the first and second method heated. Blei der vorliegenlden Erfindung soll der durch Tbermokompression beheizte Teil des Apparates eine zusätzliche Beheizung erfahren, und zwar durch einen Teil des Abdampfes des Motors, der den Kompressor antreibt. Um diesen Dampf zur Verfügung zu hauben, ist es erforderlich, die Leistung des Motors so zu berechnen, daß sein Abdampf in solcher Menge vorhanden ist, daß er zum Teil dem mit Tbermokompression beheizten Apparat zugeführt werden kann. One of the main features of the present invention is that of hypermocompression heated part of the apparatus experienced additional heating, namely by part of the exhaust steam from the engine that drives the compressor. To that steam available hood, it is necessary to calculate the power of the engine so that its exhaust vapor is present in such an amount that it is partly that with tbermocompression heated apparatus can be fed. Die Durchführung des Verfahrens soll an Hand von zwei Beispielen erläutert werden, die in der beiliegenden Zeichnung dargestellt sind. The implementation of the procedure should be based on two examples explained, which are shown in the accompanying drawing. In der Abb. list eine kombinierte Destillations- und Entwässerungsanlage für alkoholische Maischen dargestellt. Wenn bei einer solchen Anlage die bei 3 in die Kolonne ! eintretende Flüssigkeit kalt ist, so reicht die Thermokompression zur Beheizung der Kolorine unter Umständen nicht aus. In diesem Fall soll die Leistung oder der Druck des Hochdruckdampfes, der den Kompressor 4 speist, so bemessen werden, daß der Abdampf ausreicht, um nicht nur in der Schlange 7 die Beheizung der Entwäss, erungskolonne 2 zu bewirken, sondern auch in der Schlange 8 der Kolonne I eine zusätzliche Wärmemenge zuzuführen. In the Fig. List a combined distillation and dewatering system shown for alcoholic mashes. If the 3 in the column! incoming liquid is cold, thermocompression is sufficient to heat the Kolorine under certain circumstances. In this case, the performance is intended or the pressure of the high-pressure steam that feeds the compressor 4 can be measured in such a way that that the exhaust steam is sufficient to not only heat the drainage in line 7, erungskolonne 2 to effect, but also in the queue 8 of the column I an additional Supply amount of heat. Je nach den besonderen Umständen wird man den Kompressor mit einem Motor von hoher Ausbeute oder im Gegenteil mit einem Motor, der sehr viel Dampf verbraucht, betreiben. In diesem letzteren Falle ist es möglich, einen Motor zu wählen, der Abdampf mit ziemlich hohlem Druck liefert, so daß er eine einfach oder doppelt wirksame Konzentrierung in in der Zeichnung nicht dargestellten Gefäßen bewirken kann, bevor die Beheizung der Kolonne 2 durchgeführt wird. Depending on the particular circumstances, one will use the compressor with one Engine of high yield or, on the contrary, with an engine that has a lot of steam consumed, operate. In this latter case it is possible to use a motor choose that delivers exhaust steam at a fairly hollow pressure, so that it is a simple or double effective concentration in vessels not shown in the drawing can cause before the heating of the column 2 is carried out. Man kann auch aus dem Motor Dampf mit zwei verschiedenen Drucken entweichen lassen und so mehr Treibdampf verbrauchen, wenn man viel Heizdampf braucht. You can also get steam from the engine with two different pressures let it escape and thus use more motive steam if you need a lot of heating steam. Bei der Abb. 2 handelt es sich um eine einfache Konzentrierung einer Flüssigkeit. Diese wird bei 3 dem Kessel 1- zugeführt. Der aus dem Kessel 1 entweichende Brüdendampf wird in dem Kompressor 5, der von der Maschine 4 angetrieben wird, kondensiert und in dem Wärmeaustauscher 1a verdichtet. Bei 1b entweicht das Kondensat. Die konzentrierte Flüssigkeit wird in dem zweiten Kessel von neuem behandelt und durch die Leitung 9 abgezogen. Dler zur Beheizung des zweiten Kessels dienende Niederdruckdampf erfährt eine Abzweigung über den Hahn 1c in Richtung auf den Kessel I, der durch diesen abgezweigten Teil des Niederdruckdampfes zusätzlich beheizt wird. Fig. 2 is a simple concentration of a Liquid. This is fed to boiler 1 at 3. The one escaping from boiler 1 Evaporative vapor is condensed in the compressor 5 driven by the engine 4 and compressed in the heat exchanger 1a. At 1b the condensate escapes. The concentrated Liquid is re-treated in the second kettle and through the line 9 deducted. The low-pressure steam used to heat the second boiler experiences a branch via the tap 1c in the direction of the boiler I, which through this branched off part of the low-pressure steam is additionally heated. Gegebenenfalls kann auch der für die Beheizung des Kessels I verwendete Niederdruckdampf am Austritt 2b des Wärmeaustauschers 2a des zweiten Kessels entnommen werden. If necessary, the one used for heating the boiler I can also be used Low pressure steam taken at outlet 2b of the heat exchanger 2a of the second boiler will.
DED68008D 1932-03-16 1934-05-04 Procedure for heating liquids Expired DE659452C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR747788T 1932-03-16
FR45169T 1934-03-09

Publications (1)

Publication Number Publication Date
DE659452C true DE659452C (en) 1938-05-04

Family

ID=33454446

Family Applications (1)

Application Number Title Priority Date Filing Date
DED68008D Expired DE659452C (en) 1932-03-16 1934-05-04 Procedure for heating liquids

Country Status (2)

Country Link
DE (1) DE659452C (en)
FR (1) FR45169E (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2509136A (en) * 1949-06-17 1950-05-23 Gulf Oil Corp Process and apparatus for concentrating dilute solutions
DE884630C (en) * 1948-10-02 1953-07-27 Ewald Krombach Multi-stage evaporator, especially for sugar juices
DE3016406A1 (en) * 1980-04-29 1981-11-05 Maschinenfabrik Buckau R. Wolf Ag, 4048 Grevenbroich MULTI-STAGE EVAPORATOR SYSTEM WITH COMBINED VAPOR COMPRESSOR AND HEAT TRANSFORMER FOR RECOVERY OF THE HEAT CONTAINED IN THE VOM

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE884630C (en) * 1948-10-02 1953-07-27 Ewald Krombach Multi-stage evaporator, especially for sugar juices
US2509136A (en) * 1949-06-17 1950-05-23 Gulf Oil Corp Process and apparatus for concentrating dilute solutions
DE3016406A1 (en) * 1980-04-29 1981-11-05 Maschinenfabrik Buckau R. Wolf Ag, 4048 Grevenbroich MULTI-STAGE EVAPORATOR SYSTEM WITH COMBINED VAPOR COMPRESSOR AND HEAT TRANSFORMER FOR RECOVERY OF THE HEAT CONTAINED IN THE VOM

Also Published As

Publication number Publication date
FR45169E (en) 1935-07-06

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