DE541564C - Device for the concentration of sulfuric acid - Google Patents
Device for the concentration of sulfuric acidInfo
- Publication number
- DE541564C DE541564C DEB150305D DEB0150305D DE541564C DE 541564 C DE541564 C DE 541564C DE B150305 D DEB150305 D DE B150305D DE B0150305 D DEB0150305 D DE B0150305D DE 541564 C DE541564 C DE 541564C
- Authority
- DE
- Germany
- Prior art keywords
- acid
- concentration
- sulfuric acid
- heating
- department
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/69—Sulfur trioxide; Sulfuric acid
- C01B17/88—Concentration of sulfuric acid
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
Vorrichtung zur Konzentration von Schwefelsäure Der vorliegende Eindampfapparat, bei dem in bekannter Weise heiße Gase zwecks Verdampfung des Wassers der Säure auf diese zur Einwirkung gebracht werden, ist, wie aus folgendem ersichtlich, eingerichtet: Die zu konzentrierende Säure tritt durch die Öffnung A (s. Abbildung) in die von einer Anzahl Heizröhren Bin vertikaler Richtung durchzogene Abteilung C ein, füllt diese wie auch das am Fuße mit Durchlässen D - versehene Steigrohr E vollständig aus und fließt aus diesem in die Abteilung F. In letzterer Abteilung bildet sich eine durch die aus dem Boden einheitlich hervorragenden Heizrohrenden B1 bedingte Säureschicht, von deren Oberfläche ab ein gleichmäßiger Überlauf in sämtliche Heizröhren erfolgt. Aus diesen Röhren gelangt die Säure in die Abteilung G, bildet hier ebenfalls eine Schicht, von welcher die überschüssige Menge durch die Öffnung H in ein Kühlgefäß abgegeben wird.Device for the concentration of sulfuric acid The present evaporator, in which in a known manner hot gases for the purpose of evaporation of the water of the acid these are brought into effect, is set up, as can be seen from the following: The acid to be concentrated enters the from opening A (see illustration) a number of heating tubes this as well as the riser pipe E, which is provided with passages D at the foot, is complete from and flows out of this into department F. In the latter department forms one caused by the heating pipe ends B1 protruding uniformly from the ground Acid layer, from the surface of which an even overflow into all heating tubes he follows. The acid reaches compartment G from these tubes, where it also forms a layer from which the excess amount through the opening H into a cooling vessel is delivered.
Die Heizgase strömen durch den Kanal J in die Abteilung G, wo sie sich, auf der Säureoberfläche ausbreitend, in die Heizröhren verteilen, in welchen sie mit der Säure in innige Berührung geraten. Die Heizgase sättigen sich mit Wasserdampf und werden bei ihrem Übertritt aus den Heizröhren in die Abteilung F mittels der Kalotten K nochmals in enge Berührung mit der Säure gebracht. Endlich entweichen die Gase, das aus der Säure ausgetriebene Wasser mit sich führend, durch die Saugleitung L nach einem Kondensator.The heating gases flow through channel J into department G, where they spreading on the surface of the acid in the heating tubes, in which they come into intimate contact with the acid. The heating gases are saturated with water vapor and when they pass from the heating pipes into compartment F, they are Calottes K brought into close contact with the acid again. Escape at last the gases, carrying the water expelled from the acid, through the suction line L after a capacitor.
Da bei dem Prozeß die in der Abteilung C befindliche Säure bereits stark vorgewärmt wird, so könnten bei etwaiger Verschlammung der Durchlässe D Druckspannungen entstehen, die aber durch die von der Abteilung C in die Abteilung F führenden Entlastungsstutzen M vermieden werden.Since in the process the acid in department C is already present If the passages D are heavily preheated, compressive stresses could occur if the passages D become silted up which arise, however, through the relief nozzles leading from department C to department F. M to be avoided.
Die Vorteile des Apparates lassen sich in besonders günstigen Leistungsmöglichkeiten bei verhältnismäßig sehr geringen Anschaffungs-und Betriebskosten erblicken.The advantages of the apparatus can be seen in particularly favorable performance options behold at relatively very low acquisition and operating costs.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB150305D DE541564C (en) | Device for the concentration of sulfuric acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB150305D DE541564C (en) | Device for the concentration of sulfuric acid |
Publications (1)
Publication Number | Publication Date |
---|---|
DE541564C true DE541564C (en) | 1932-01-13 |
Family
ID=7002158
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEB150305D Expired DE541564C (en) | Device for the concentration of sulfuric acid |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE541564C (en) |
-
0
- DE DEB150305D patent/DE541564C/en not_active Expired
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE2133807C3 (en) | Multi-stage spray film evaporator for obtaining service water from raw water | |
DE541564C (en) | Device for the concentration of sulfuric acid | |
DE1771810A1 (en) | Method and device for cleaning metal parts | |
DE1097449B (en) | Thermal deaerator with vapor condenser for liquids, especially for boiler feed water | |
DE604450C (en) | Surface feed water deaerator, especially for ship operation | |
DE710797C (en) | Method and device for the continuous recovery of alcohol from impure alcoholic liquids, in particular raw alcohol | |
DE603684C (en) | Process for the production of a uniform heat carrier layer using curtain nozzles for evaporation systems | |
DE707155C (en) | Process for increasing the performance of steam-loaded heat exchangers | |
DE567338C (en) | Process for reducing the gas content in the condensate to be discharged from surface condensers of steam power plants | |
DE436985C (en) | Method for heat transfer from a heating source to a liquid to be evaporated by means of a third heat-transferring medium | |
DE738121C (en) | Process and device for corrosion protection in steam heating systems | |
DE548363C (en) | Device on multiple evaporators | |
AT71146B (en) | Process for the continuous concentration of dilute nitric acid. | |
DE370297C (en) | Process for the production of high grade alcohol | |
DE967006C (en) | Method and device for evaporating milk and other emulsions, suspensions or similar liquids | |
DE621110C (en) | Process and device for increasing the performance of evaporators | |
DE633722C (en) | Method and device for the evaporation of liquids in rotary tubes | |
AT229344B (en) | Condenser for precipitating vapors | |
DE249236C (en) | ||
DE574995C (en) | Multi-stage evaporator system | |
DE1619697C (en) | Falling film evaporator | |
DE413832C (en) | Method and device for the concentration of dilute volatile substances from water by evaporation | |
DE556002C (en) | Process and device for obtaining a cooking acid with a high SO content in the production of cellulose by the sulfite process | |
AT148480B (en) | Device for the distillation of raw resin. | |
DE129737C (en) |