AT79023B - Process for the preparation of pure, high-grade nitric acid from gases containing nitrogen oxides. - Google Patents

Process for the preparation of pure, high-grade nitric acid from gases containing nitrogen oxides.

Info

Publication number
AT79023B
AT79023B AT79023DA AT79023B AT 79023 B AT79023 B AT 79023B AT 79023D A AT79023D A AT 79023DA AT 79023 B AT79023 B AT 79023B
Authority
AT
Austria
Prior art keywords
nitric acid
pure
preparation
nitrogen oxides
containing nitrogen
Prior art date
Application number
Other languages
German (de)
Original Assignee
Oesterreichischer Ver Fuer Che
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 Oesterreichischer Ver Fuer Che filed Critical Oesterreichischer Ver Fuer Che
Application granted granted Critical
Publication of AT79023B publication Critical patent/AT79023B/en

Links

Landscapes

  • Removal Of Specific Substances (AREA)

Description

  

   <Desc/Clms Page number 1> 
 



  Ver Sahren zur Darstellung reiner, hochgradiger Salpetersäure aus Stickstoffoxyde ent- haltenden Gasen. 



   Nach der englischen Patentschrift Nr. 25632/1907 wird   Kalziumcyanamid   in Form von Kalkstickstoff mit nitrosen Gasen, wie sie z. B. bei der katalytischen Oxydation von Ammoniak erhalten werden   können, behandelt,   also mit Gaser, welche Stickstoffoxyde, Luft und Wasserdampf enthalten wobei sich ein Gemenge von Kalzium- und Ammoniumnitrat 
 EMI1.1 
 ausgelaugt, die Lauge abgedampft, der Rückstand mit Schwefelsäure versetzt und der Destillation unterworfen werden. Hiebei wird zweifellos ein Destillat von Salpetersäure nebst Ammoniumsulfat als Rückstand erhalten. 



   Die Patentschrift enthält keine Angabe über die Menge der aufzuwendenden Schwefelsäure im Verhältnis zum zersetzten Ammoniumnitrat. Nimmt man auch an, es sei das im folgenden angegebene Verhältnis richtig getroffen, so ist es doch zweifellos, dass bei dieser Destinlation nur eine unreine Salpetersäure erhalten werden kann. da im Ammoniumnitrat alle, im Kaikstickstoff enthaltenen, nicht zersetzten, löslichen Verunreinigungen vorhanden sein werden.   namentlich   auch alle Chlor- und Schwefelverbindungen.

   Diese bewirken. dass das erhalten Salpetersäuredestillat sehr unrein, namentlich stark untersalpetersäurehaltig sein wird, und   dass   nach Massgabe der Mengen dieser Verunreinigungen auch das Ausbringen an Salpeter säure ein schlechtes sein muss. 
 EMI1.2 
 Doch kann Pelouze noch nicht die Absicht gehabt haben und   auch nicht   daran gedacht haben. mittels dieser Reaktion aus nitrosen Gasen, z. B. von der Ammoniakoxydation usw. reine.   hochkonzentrierte Salpetersäure   darzustellen, da damals weder die Ammoniakoxydation.   noch     andere technische Methoden   der Darstellung nitroser Gase   aus Luftstichtofi, wie   sie im vor liegenden Falle in Betracht kommen, bekannt waren. 



   Nach der Erfindung wird beabsichtigt, aus den nitrosen Gasen solcher Verfahren konzen- 
 EMI1.3 
   wärtigen wären. 

**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.



   <Desc / Clms Page number 1>
 



  Process for the preparation of pure, high-grade nitric acid from gases containing nitrogen oxides.



   According to the English patent specification No. 25632/1907 calcium cyanamide is in the form of calcium cyanamide with nitrous gases, such as are used, for. B. can be obtained in the catalytic oxidation of ammonia, treated, so with gases which contain nitrogen oxides, air and water vapor with a mixture of calcium and ammonium nitrate
 EMI1.1
 leached, the liquor evaporated, the residue mixed with sulfuric acid and subjected to distillation. A distillate of nitric acid and ammonium sulfate are undoubtedly obtained as residue.



   The patent does not contain any information about the amount of sulfuric acid to be used in relation to the decomposed ammonium nitrate. If one also assumes that the relationship given below is correct, there is no doubt that only impure nitric acid can be obtained in this destinlation. since in ammonium nitrate all non-decomposed, soluble impurities contained in quay nitrogen will be present. including all chlorine and sulfur compounds.

   These effect. that the nitric acid distillate obtained will be very impure, namely with a high content of subnitric acid, and that, depending on the quantities of these impurities, the amount of nitric acid must also be poor.
 EMI1.2
 But Pelouze could not have had the intention and could not have thought of it. by means of this reaction from nitrous gases, e.g. B. from ammonia oxidation, etc. pure. To represent highly concentrated nitric acid, since at that time neither the ammonia oxidation. Other technical methods for the preparation of nitrous gases from air pollution, as they come into consideration in the present case, were known.



   According to the invention it is intended to concentrate from the nitrous gases of such processes
 EMI1.3
   would be waiting.

** WARNING ** End of DESC field may overlap beginning of CLMS **.

 

Claims (1)

PATENT ANSPRUCH : EMI1.4 **WARNUNG** Ende CLMS Feld Kannt Anfang DESC uberlappen**. PATENT CLAIM: EMI1.4 ** WARNING ** End of CLMS field may overlap beginning of DESC **.
AT79023D 1917-06-30 1917-06-30 Process for the preparation of pure, high-grade nitric acid from gases containing nitrogen oxides. AT79023B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT79023T 1917-06-30

Publications (1)

Publication Number Publication Date
AT79023B true AT79023B (en) 1919-11-10

Family

ID=3600563

Family Applications (1)

Application Number Title Priority Date Filing Date
AT79023D AT79023B (en) 1917-06-30 1917-06-30 Process for the preparation of pure, high-grade nitric acid from gases containing nitrogen oxides.

Country Status (1)

Country Link
AT (1) AT79023B (en)

Similar Documents

Publication Publication Date Title
DE892587C (en) Process for the production of aqueous ammonium nitrite solutions
DE2262754A1 (en) METHOD OF TREATMENT OF WASTEWATER
AT79023B (en) Process for the preparation of pure, high-grade nitric acid from gases containing nitrogen oxides.
DE739176C (en) Process for the production of a fertilizer containing phosphoric acid
DE334014C (en) Process for the production of carbonate of lime
DE553985C (en) Process for the production of a concentrated fertilizer
DE243892C (en)
DE662445C (en) Process for the production of gases with a high content of sulfur trioxide
DE1064935B (en) Process for the production of lithium sulfate from spodumene
AT70783B (en) Process for the production of organic acid anhydrides or mixtures of anhydrides with their acids.
DE598773C (en) Process for the production of coarse-grain ammonium sulphate from evaporating liquid ammonia and sulfuric acid
AT118009B (en) Process for the purification of wastewater containing cyanide.
DE391011C (en) Process for converting alkali chlorides into alkali nitrates using nitric acid
DE261027C (en)
AT68167B (en) Process for the preparation of nitric acid guanidine from cyanamide.
DE833489C (en) Process for the production of analytically pure ammonium sulfate from coking ammonium sulfate
DE429722C (en) Process for the preparation of ammonium chloride from final liquors containing magnesium chloride in potash production
DE329591C (en) Process for the preparation of oxalic acid from carbohydrates by oxidation with nitric acid
DE2136303B2 (en) Process for the production of iron (III) chloride from iron (H) chloride
AT103899B (en) Process for the separation of zirconium and hafnium compounds.
DE367768C (en) Process for the production of solid potassium dichromate
DE484000C (en) Process for the production of acetone from stillage or similar products
AT10741B (en) Process for decolorizing sugar juices.
DE422074C (en) Process for the production of urea salts, in particular urea nitrate, from cyanamides
DE535725C (en) Process for the production of thiourea from metal cyanamides and sulfides by the action of carbonic acid