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DE1519569A1 - Horizontal countercurrent evaporator - Google Patents

Horizontal countercurrent evaporator

Info

Publication number
DE1519569A1
DE1519569A1 DE19651519569 DE1519569A DE1519569A1 DE 1519569 A1 DE1519569 A1 DE 1519569A1 DE 19651519569 DE19651519569 DE 19651519569 DE 1519569 A DE1519569 A DE 1519569A DE 1519569 A1 DE1519569 A1 DE 1519569A1
Authority
DE
Germany
Prior art keywords
chamber
countercurrent evaporator
patent application
horizontal countercurrent
separating funnel
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Withdrawn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
DE19651519569
Other languages
German (de)
Inventor
Alfred Winkler
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.)
Cwielong & Winkler
Original Assignee
Cwielong & Winkler
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 Cwielong & Winkler filed Critical Cwielong & Winkler
Publication of DE1519569A1 publication Critical patent/DE1519569A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D3/00—Halides of sodium, potassium or alkali metals in general
    • C01D3/04—Chlorides
    • C01D3/06—Preparation by working up brines; seawater or spent lyes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Cyclones (AREA)

Description

CWIILONO AWIN KLIR- IN OENI EU R- BÜROCWIILONO AWIN KLIR- IN OENI EU R- OFFICE

Expl.Expl.

lorizontal-Gegenstromverdampferhorizontal countercurrent evaporator

Zusatz zur Patentanmeldung C 54- 14-5 IVc/12aAddition to patent application C 54-14-5 IVc / 12a

Die Erfindung bezweckt eine Verbesserung des Horizontal-Gegenstromverdampfers nach obiger Patentanmeldung G 34 / 12a.The invention aims to improve the horizontal countercurrent evaporator according to the above patent application G 34 / 12a.

Die Neuerung bezieht sich auf die Gestaltung der Kammer -Figo 1 - im Besonderen auf deren unteren Ausgang 11 und das Rohrleitungsachlangen-Ende 8.The innovation relates to the design of the chamber -Fig o 1 - in particular to its lower outlet 11 and the pipe runner end 8.

Es hat sich bei der ursprünglichen Ausführung als Nachteil herausgestellt, dass das sich an der Kammerwand 6 bildende Kondensat in die abgeschiedenen Feststoffbestandteile läuft, da die Abscheideleistung dadurch herabgemindert wird.In the original embodiment, it has been found to be a disadvantage that this occurs on the chamber wall 6 The condensate that forms runs into the separated solid components, as this reduces the separation efficiency will.

Einer Verbesserung der ,Virkungs weite dient auch die neuartige Ausbildung des Rohrleitungsschlangen-Sndes 8 der Rohrschlange 1. Bei der alten Ausführung spritzten die Feststoffbestandteile des Mediums gegen die Behälterwand 6, das Mantelrohr 5 und bildeten feste Verkrustungen.The new type also serves to improve the effect width Formation of the pipe coil end 8 of the pipe coil 1. In the old version, the sprayed Solid components of the medium against the container wall 6, the jacket pipe 5 and formed solid incrustations.

O Ein Ausführungsbeispiel zeigt die neue Zeichnung, anhand dieser eine genaue Beschreibung folgt.The new drawing shows an exemplary embodiment, with the aid of which a detailed description follows.

«* Ib unteren abnehmbaren Teil 6" der Kammer 6 befindet sich M ein Abscheidetrichter 11', dessen grösster Durchmesser die Kammerwand 6 nicht berührt und der mit dem unteren"* Ib lower detachable part 6" of the chamber 6 is a separating funnel 11 ', the largest diameter of which does not touch the chamber wall 6 and the one with the lower one

■ - ■ .2 - BAD ORIGINAL■ - ■ .2 - BAD ORIGINAL

CWIILONO * WINKLIR -I NOENIIU R- BUtOj 5 19569CWIILONO * WINKLIR -I NOENIIU R- BUtOj 5 19569

Ausgang 11 verbunden ist, der nur zum Sammeln und Ablassen der Feststoffbestandteile dient. Das sich an der Behälterwand 6 bildende Kondensat« sammelt sich um den Abseheidetrichter 11' und wird durch den separaten Ablaßstutzen Λ\ " abgeleitet.Output 11 is connected, which is only used to collect and drain the solid components. The condensate forming on the container wall 6 collects around the separating funnel 11 'and is drained off through the separate drainage connection Λ \ ".

Erfindungsgemäss wird das Rohrleitungsschlangen-Bnde 8' konisch erweitert, bis zur Mittel der Kammer 6 geführt und hier vertikal nach unten gebogen. Durch die l^ierschnittserweiterung wird die Austrittsgeachwindigkeit des Mediums vermindert und dadurch die ADScheidung der Feststoffbestandteile verbessert.According to the invention, the pipeline serpentine band 8 ' widened conically, guided to the middle of the chamber 6 and here bent vertically downwards. Through the cross-sectional enlargement becomes the exit speed of the medium and thereby improves the separation of the solid constituents.

009827/1432009827/1432

Claims (1)

CWIILONO & WINKLIft-!NGENIIUR-BÜRO*! 5 I 9569CWIILONO & WINKLIft-! NGENIIUR OFFICE *! 5 I 9569 P a t e nt a η s ρ r ü eheP a t e nt a η s ρ r ü ehe Zusatz zur Patentanmeldung G $4 145 IVc / 12aAddition to patent application G $ 4 145 IVc / 12a 1.) Horizontal-Gegenstromverdampfer nach obiger Patentanmeldung dadurch gekennzeichnet, dass in der Kammer, in die die Rohrschlange mündet, sich im unteren Teil ein Äbscheidetrichter befindet, der mit dem unteren Feststoff-Ausgang verbunden ist.1.) Horizontal countercurrent evaporator according to the above patent application characterized in that in the chamber into which the pipe coil opens, in lower part is a separating funnel, which is connected to the lower solids outlet. 2.) Horizontal-Gegenstromverdanipfer nach Anspruch 1, dadurch gekennzeichnet, dsss das sich um den Adscheidetrichter sammelnde Kondensat einen separaten Ausgan.: hat.2.) Horizontal countercurrent evaporator according to claim 1, characterized in that it is around the separating funnel collecting condensate has a separate outlet. 5.) Horisontal-Gegenscroinverdampfer nach Anspruch Ί und 2, daämch gekennzeicimet, dass das Rohr-3chlangen-ände in der Kammer konisch erweitert, bis zur Eitte der Kammer reicht ;nd nier mit der grossen Öffnung nach unten ^eborr^n ist, se dass die AustriitsgesciiwindijTke it des Mediums vermindert wird.5.) Horisontal Gegenenscroinverdampfer according to claim Ί and 2, because it is marked that the pipe-3-snake-ends in the chamber widened conically, reaching up to the middle of the chamber; nd nier with the large opening downward ^ eborr ^ n is that se that the outlet flow of the medium is reduced will. Cwielc/rig & WinklerCwielc / rig & Winkler / b-.genie^rbjr / b-.genie ^ rbjr r Ahee 67, Tel. I 4720/1 31 30 --■-■«,r Ahee 67, Tel. I 4720/1 31 30 - ■ - ■ «, / BAD ORIGINAL/ BAD ORIGINAL 009827/U32 ~009827 / U32 ~ Le ers ei teBlank page
DE19651519569 1964-10-20 1965-08-21 Horizontal countercurrent evaporator Withdrawn DE1519569A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEC0034145 1964-10-20
DEC0036704 1965-08-21

Publications (1)

Publication Number Publication Date
DE1519569A1 true DE1519569A1 (en) 1970-07-02

Family

ID=25969957

Family Applications (2)

Application Number Title Priority Date Filing Date
DE19641519564 Withdrawn DE1519564A1 (en) 1964-10-20 1964-10-20 Horizontal countercurrent evaporator
DE19651519569 Withdrawn DE1519569A1 (en) 1964-10-20 1965-08-21 Horizontal countercurrent evaporator

Family Applications Before (1)

Application Number Title Priority Date Filing Date
DE19641519564 Withdrawn DE1519564A1 (en) 1964-10-20 1964-10-20 Horizontal countercurrent evaporator

Country Status (9)

Country Link
US (1) US3321002A (en)
AT (1) AT257663B (en)
BE (1) BE671071A (en)
CH (1) CH429610A (en)
DE (2) DE1519564A1 (en)
GB (1) GB1128659A (en)
IL (1) IL24472A (en)
NL (1) NL6513531A (en)
SE (1) SE320046B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3405509A (en) * 1966-11-08 1968-10-15 Combustion Eng Means for conserving heat and regulating temperature in a stack
GB1317121A (en) * 1971-01-01 1973-05-16 Churchill Instr Co Ltd Oil heating systems and oil heater units therefor
US4294199A (en) * 1979-10-26 1981-10-13 Combustion Engineering, Inc. Steam generating magnetohydrodynamic diffuser
HU193336B (en) * 1985-07-19 1987-09-28 Fegyver Es Gazkeszuelekgyar Heat exchanger first for gas-heating equipment

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US263316A (en) * 1882-08-29 browne
US2599451A (en) * 1952-06-03 Vacuum bodying process
FR667359A (en) * 1928-04-16 1929-10-16 Process for extracting salts from a liquid
US1831121A (en) * 1930-01-23 1931-11-10 Buffalo Foundry & Machine Comp Evaporating apparatus
US2150860A (en) * 1937-09-15 1939-03-14 Zaremba Company Evaporator
FR1060544A (en) * 1952-07-23 1954-04-02 Krebs & Co Ag Installation for the continuous concentration of alkaline and other solutions

Also Published As

Publication number Publication date
NL6513531A (en) 1966-04-21
GB1128659A (en) 1968-10-02
AT257663B (en) 1967-10-25
CH429610A (en) 1967-01-31
BE671071A (en) 1966-02-14
US3321002A (en) 1967-05-23
IL24472A (en) 1969-11-12
SE320046B (en) 1970-02-02
DE1519564A1 (en) 1970-03-12

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Legal Events

Date Code Title Description
E77 Valid patent as to the heymanns-index 1977
EHJ Ceased/non-payment of the annual fee