DE360283C - Dephlegmator and preheater for ammonia abortion devices - Google Patents

Dephlegmator and preheater for ammonia abortion devices

Info

Publication number
DE360283C
DE360283C DET24638D DET0024638D DE360283C DE 360283 C DE360283 C DE 360283C DE T24638 D DET24638 D DE T24638D DE T0024638 D DET0024638 D DE T0024638D DE 360283 C DE360283 C DE 360283C
Authority
DE
Germany
Prior art keywords
ammonia
abortion
dephlegmator
preheater
liquid
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
DET24638D
Other languages
German (de)
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.)
DR JOHANN TERWELP
Original Assignee
DR JOHANN TERWELP
Publication date
Priority to DET24638D priority Critical patent/DE360283C/en
Application granted granted Critical
Publication of DE360283C publication Critical patent/DE360283C/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01CAMMONIA; CYANOGEN; COMPOUNDS THEREOF
    • C01C1/00Ammonia; Compounds thereof
    • C01C1/02Preparation, purification or separation of ammonia
    • C01C1/10Separation of ammonia from ammonia liquors, e.g. gas liquors

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

Dephlegmator und Vorwärmer für Ammoniak-Abtreibeapparate. Beire Verarbeiten von Ammoniakwasser tritt mit dem abgetriebenen Ammoniak eine große Menge Dampf aus dem Abtreibapparat. Dieser Begleitdampf spielt eine große Rolle beim Dampfverbrauch des Abtreibapparates. Er beträgt bei gut geleiteten Betrieben (las i- bis 8fache des Ammoniaks, meistens ist er aber bedeutend höher, so daß er über 50 Prozent der ganzen zur Abtreibung benötigten Dampfmenge betragen kann. Außer den großen direkten Kosten für diesen Dampf verursacht derselbe je- nach der Verwendung des Ammoniaks auch noch Betriebsschwierigkeiten und indirekte Kosten.Dephlegmator and preheater for ammonia abortion machines. When ammonia water is processed, a large amount of steam escapes from the stripping apparatus with the ammonia that is driven off. This accompanying steam plays a major role in the steam consumption of the stripping apparatus. In well-managed establishments it is (1 to 8 times as much as ammonia, but it is usually much higher, so that it can amount to over 50 percent of the total amount of steam required for abortion. In addition to the large direct costs for this steam, it causes the same, depending on the situation) the use of ammonia also adds operational difficulties and indirect costs.

Mit Hilfe der vorliegenden Erfindung ist es nun möglich, ohne jede Wartung den Dampf von dem Ammoniak bis auf die der Tension des Wasserdampfes bei der Temperatur des Ammoniaks entsprechende Menge zu trennen und die Verdampfungswärme des niedergeschlagenen Dampfes voll auszunutzen, wobei man es ganz genau in der Hand hat, die Temperatur des Ammoniaks beliebig einzustellen.With the help of the present invention it is now possible without any Maintain the vapor from the ammonia except for the tension of the water vapor to separate the amount corresponding to the temperature of the ammonia and the heat of vaporization to take full advantage of the precipitated steam, being very precise in the Hand has to adjust the temperature of the ammonia as desired.

Eine zweckmäßige Ausführungsform der vorliegenden Erfindung ist auf der Zeichnung dargestellt. 21 ist ein allseitig geschlossener Behälter, welcher durch Platte B in zwei Teile getrennt ist. D ist ein Rohrsystem, oben (bei B) offen, unten (bei C) geschlossen. E ist eine im oberen Teil (Dampfraum) des Behälters befindliche Rohrschlange. In den Rohren D befindet sich eine Flüssigkeit, deren Siedepunkt den Arbeitsbedingungen angepaßt zweckmäßig zwischen 70 und 95° liegt.An expedient embodiment of the present invention is shown in the drawing. 21 is a container which is closed on all sides and which is separated into two parts by plate B. D is a pipe system, open at the top (at B), closed at the bottom (at C). E is a coil located in the upper part (vapor space) of the container. In the pipes D there is a liquid, the boiling point of which, adapted to the working conditions, is expediently between 70 and 95 °.

Beirr Betrieb des Apparates leitet man durch F die aus denn Abtreibapparat kommenden Dämpfe ein. Diese treten durch Öffnungen L zwischen die Rohre D und erhitzen die Flüssigkeit in denselben zum Sieden. Es wird nun alles Ammoniak auf den Siedepunkt dieser Flüssigkeit äbgekühlt, und es verläßt den Apparat bei G mit nur' so viel Wasser, als der Tension desselben bei der betreffenden Temperatur entspricht, während durch k das niedergeschlagene Wasser abläuft. Bei H wird das zum Abtreibapparat laufende Rohwasser in die Schlange E ein- und bei I zum Abtreibappar at weitergeführt. An der Schlange E werden die aus der in den Rohren befindlichen Flüssigkeit entweichenden -Dämpfe niedergeschlagen und. die Wärme an das Rohti#asser abgegeben, so daß die gesamte Wärme zur Vorwärmung des Rohwassers ausgenutzt wird.When the apparatus is in operation, F is used to introduce the vapors coming from the abortion apparatus. These pass through openings L between the tubes D and heat the liquid in them to boiling. All the ammonia is then cooled down to the boiling point of this liquid, and it leaves the apparatus at G with only as much water as corresponds to its tension at the temperature in question, while the precipitated water runs off through k. At H the raw water running to the abortion apparatus is fed into the queue E and at I to the abortion apparatus at. The vapors escaping from the liquid in the pipes are precipitated at the snake E and. the heat is transferred to the raw water, so that the entire heat is used to preheat the raw water.

Claims (1)

PATE NT-ANSPRtiCHE: i. Dephlegmator und Vorwärmer für Ammonialc-A1>triibapparate, gekennzeichnet durch eine doppelte Wärineaustauschvorrichtung, derart, daß in der einen Vorrichtung eine Flüssigkeit durch die abgetriebenen Dämpfe zum Sieden erhitzt wird, so (laß sich die zurückzuhaltenden Wasserdämpfe niederschlagen, während das zu gewinnende Ammoniak entweicht, worauf sich in einer zweiten Vorrichtung die Dämpfe aus der zum Sieden erhitzten Flüssigkeit wieder niederschlagen, indem sie dabei (las dem Abtreibapparat zuzuführende Ammoniakwasser vorwärmen. z. Dephlegmator und Vorwärmer nach Anspruch i, bestehend in einem Behälter mit einem mit einer niedriger siedenden Flüssigkeit gefüllten Rohrsystem in seinem unteren Teil und einer im zugehörigen Dampfraum liegenden Rohrschlange für das vorzuwärmende Ammoniakwasser.PATE NT CLAIMS: i. Dephlegmator and preheater for ammonia-A1> triibapparate, characterized by a double heat exchange device such that in the a device heated a liquid to boiling by the expelled vapors so (let the water vapor to be retained precipitate while the ammonia to be recovered escapes, whereupon the vapors are in a second device from the boiling liquid to precipitate again by doing it (read to preheat the ammonia water to be fed to the abortion apparatus, e.g. dephlegmator and A preheater according to claim i, consisting of a container with a lower one boiling liquid-filled pipe system in its lower part and one in the associated Coiled pipe lying in the vapor space for the ammonia water to be preheated.
DET24638D Dephlegmator and preheater for ammonia abortion devices Expired DE360283C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DET24638D DE360283C (en) Dephlegmator and preheater for ammonia abortion devices

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DET24638D DE360283C (en) Dephlegmator and preheater for ammonia abortion devices

Publications (1)

Publication Number Publication Date
DE360283C true DE360283C (en) 1922-09-30

Family

ID=7551563

Family Applications (1)

Application Number Title Priority Date Filing Date
DET24638D Expired DE360283C (en) Dephlegmator and preheater for ammonia abortion devices

Country Status (1)

Country Link
DE (1) DE360283C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2493723A1 (en) * 1980-11-12 1982-05-14 Uss Eng & Consult PROCESS FOR REMOVING AMMONIA AND HYDROGEN SULFIDE FROM A VAPOR STREAM

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2493723A1 (en) * 1980-11-12 1982-05-14 Uss Eng & Consult PROCESS FOR REMOVING AMMONIA AND HYDROGEN SULFIDE FROM A VAPOR STREAM

Similar Documents

Publication Publication Date Title
DE360283C (en) Dephlegmator and preheater for ammonia abortion devices
EP0046876A1 (en) Process for the treatment of the bottom product of extractive-distillation processes for obtaining pure hydrocarbons
DE347278C (en) Process for the gradual smoldering of fuels by means of hot gases or superheated steam
DE504337C (en) Process for the processing of waste water resulting from the treatment of coal distillation gases using the direct ammonia process
DE642749C (en) Method and device for driving off the light oil from washing oil enriched with it
DE891318C (en) Separating column for the treatment of the abortion plumes of ammoniacal washing fluids
AT109459B (en) Process and device for cleaning boiler feed water.
DE510940C (en) Process for the direct production of road tar in a coke oven plant with by-product recovery plant
DE1567942C2 (en) Method and device for evaporation of a NaCl sol containing Na deep 2 SO deep 4
DE509584C (en) Method and device for distilling hydrocarbons, in particular crude petroleum or tar, by means of steam
DE1653002A1 (en) Hot plate press
AT133645B (en) Process for the production of amino alcohols from the aqueous solutions resulting from the production thereof.
DE349079C (en) Apparatus for separating liquid mixtures into two components
DE457230C (en) Process for the complete removal of ammonia from distillation gases
DE601198C (en) DEVICE FOR RECOVERING FEED WATER CONDENSATE AND HEAT FROM DUSTY VAPOR
DE439804C (en) Process for breaking down tars or tea oils into pitch substances and oils without distillation
DE591317C (en) Device for cooling steam
DE454893C (en) Siphoning ammonium sulfate from the saturation bath
DE437796C (en) Process for the continuous distillation of crude petroleum u. like
DE527008C (en) Device for utilizing the condensate heat in evaporators to obtain additional feed water
DE552963C (en) Fatty acid distillation column
DE656308C (en) Process and device for the distillation of high-boiling substances
AT132544B (en) Method for operating absorption refrigeration machines with cooker absorbers.
DE494109C (en) Process for treating coal tar
DE401159C (en) Device for preheating and dehairing of water, e.g. for the treatment of textile goods