DE2220290B2 - DEVICE FOR CONTINUOUS CRYSTALLIZATION CLEANING OF ORGANIC COMPOUNDS FROM CONTRIBUTIONS RELEASABLE IN THE MELT - Google Patents
DEVICE FOR CONTINUOUS CRYSTALLIZATION CLEANING OF ORGANIC COMPOUNDS FROM CONTRIBUTIONS RELEASABLE IN THE MELTInfo
- Publication number
- DE2220290B2 DE2220290B2 DE19722220290 DE2220290A DE2220290B2 DE 2220290 B2 DE2220290 B2 DE 2220290B2 DE 19722220290 DE19722220290 DE 19722220290 DE 2220290 A DE2220290 A DE 2220290A DE 2220290 B2 DE2220290 B2 DE 2220290B2
- Authority
- DE
- Germany
- Prior art keywords
- nozzle
- admixtures
- cleaning
- melt
- cleaned
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/004—Fractional crystallisation; Fractionating or rectifying columns
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Cleaning In General (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
2?2?
die auf eine nahe der Kristallisationstemperatur liegende Temperatur vorgekühlt ist. Die Verbindung kristallisiert wenn sie auf die Kristallisationsfläche 6 des Blocks 7 gelangt. Der Strom der zirkulierenden Verbindung erfaßt die Beimengungen und entfernt sie von der Kristallisationsfläche 6 über den Stutzen 3. Hierbei erwärmt der Wärmeaustauscher 5 die Schmelzfläche 8 des Blocks 7 bis auf eine Temperatur, bei der die Geschwindigkeit, mit der die gereinigte geschmolzene Verbindung abgeleitet wird, gleich der Geschwindigkeit ist, mit der die kristalline Phase wächst. Während seines Schmelzens von unten her senkt sich der Block langsam unter dem Einfluß seines Eigengewichts, wobei er den gereinigten geschmolzenen Stoff aus dem Spalt zwischen dem Block 7 und der Wand des Kegels 1 über den Stutzen 4 verdrängt.which is pre-cooled to a temperature close to the crystallization temperature. The connection crystallizes when it reaches the crystallization surface 6 of the block 7. The stream of circulating The compound detects the admixtures and removes them from the crystallization surface 6 via the nozzle 3. Here, the heat exchanger 5 heats the melting surface 8 of the block 7 to a temperature at which the rate at which the purified molten compound is discharged is equal to that Is the rate at which the crystalline phase grows. While it was melting from below the block slowly descends under the influence of its own weight, removing the purified molten Substance is displaced from the gap between the block 7 and the wall of the cone 1 via the connecting piece 4.
Es kann, um das Verschmutzen der gereinigten Verbindung zu verhindern, an der Innenfläche des Kegels 1 eine ringförmige Rinne9 (Fig. 2) ausgeführt werden, welche einen Stutzen 10 zum Ableiten der Beimengungen enthält und sich von der Kristallisationsfront in einem Abstand befindet, der von der Struktur der Kristalle der gereinigten Verbindung abhängt.To prevent contamination of the cleaned connection, it can be attached to the inner surface of the Cone 1 an annular groove9 (Fig. 2) executed which contains a nozzle 10 for discharging the admixtures and is removed from the crystallization front located at a distance equal to the structure of the crystals of the purified compound depends.
Die Vorrichtung arbeitet in diesem Falle analog der in F i g. 1 dargestellten Vorrichtung. Der einzige Unterschied besteht darin, daß während des Schmelzens der Schmelzfläche 8 von unten her der Block 7 unter dem Einfluß seines Eigengewichts sich langsam senkt, wobei er die gereinigte geschmolzene Verbindung aus dem Spalt zwischen dem Block 7 und der Wand des Kegels 1 verdrängt. Hierbei wird die Verbindung in zwei Ströme unterteilt.In this case, the device works analogously to that in FIG. 1 shown device. One and only The difference is that during the melting of the melting surface 8 from below the block 7 slowly descends under the influence of its own weight, thereby removing the purified molten compound displaced from the gap between the block 7 and the wall of the cone 1. This is where the connection divided into two streams.
Der erste Strom (der Hauptstrom), der die Produktivität der Vorrichtung und den Reinheitsgrad der gereinigten Verbindung bestimmt, besteht aus der gereinigten geschmolzenen Verbindung, die durch Schmelzen des Teils des Blocks 7 erhalten wird, der sich unterhalb der ringförmigen Rinne 9 befindet. Der Hauptstrom der gereinigten geschmolzenen Verbindung fließt während des Schmelzens des Blocks 7 über den Stutzen 4 herab.The first stream (the main stream), which affects the productivity of the device and the degree of purity of the Purified compound, determined, consists of the purified molten compound produced by Melting of the part of the block 7 which is below the annular channel 9 is obtained. The main stream of the purified molten compound flows during the melting of the ingot 7 down over the nozzle 4.
Der zweite Strom (der Hilfsstrom) besteht aus der gereinigten geschmolzenen Verbindung, die durch Schmelzen des Teils des Blocks 7 erhalten wird, der sich oberhalb der ringförmigen Rinne 9 befindet.The second stream (the auxiliary stream) consists of the purified molten compound passed through Melting of the part of the block 7 which is located above the annular channel 9 is obtained.
Der Hilfsstrom der gereinigten geschmolzenen Ausgangsverbindung fließt während des Schmelzens des Blocks 7 über den Stutzen 10 herab.The auxiliary stream of the purified molten starting compound flows during the melting of the Blocks 7 down over the nozzle 10.
F i g. 3 zeigt eine der in F i g. 2 abgebildeten Vorrichtung analoge Vorrichtung, bei der die ringförmige Rinne ein anderes Profil hat.F i g. 3 shows one of the in FIG. 2 device is an analog device in which the ring-shaped Rinne has a different profile.
Diese Vorrichtung arbeitet analog der der Fig. 2.This device works analogously to that of FIG. 2.
Hierzu 1 Blatt Zeichnungen1 sheet of drawings
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19722220290 DE2220290C3 (en) | 1972-04-25 | Device for the uninterrupted crystallization cleaning of organic compounds from additions that are soluble in the melt |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19722220290 DE2220290C3 (en) | 1972-04-25 | Device for the uninterrupted crystallization cleaning of organic compounds from additions that are soluble in the melt |
Publications (3)
Publication Number | Publication Date |
---|---|
DE2220290A1 DE2220290A1 (en) | 1973-11-15 |
DE2220290B2 true DE2220290B2 (en) | 1976-02-12 |
DE2220290C3 DE2220290C3 (en) | 1976-09-30 |
Family
ID=
Also Published As
Publication number | Publication date |
---|---|
DE2220290A1 (en) | 1973-11-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE2752308A1 (en) | DEVICE FOR GROWING SINGLE CRYSTALS FROM A MELT WHEN FEEDING CRUSHED BATCH MATERIAL | |
DE1235528B (en) | Method and device for preheating, charging and melting a batch in a glass melting furnace | |
EP0250355A1 (en) | Method of manufacturing a rotationally symmetrical hollow body | |
DE750301C (en) | Method and device for casting metal bars | |
EP0488953B1 (en) | Apparatus for separating material from a liquid mixture by cristallization | |
DE2220290B2 (en) | DEVICE FOR CONTINUOUS CRYSTALLIZATION CLEANING OF ORGANIC COMPOUNDS FROM CONTRIBUTIONS RELEASABLE IN THE MELT | |
DE60320551T2 (en) | METHOD, SYSTEM AND FORM FOR MANUFACTURING MOLDED ICE CREAMS | |
DE2801117C2 (en) | Glass melting furnace | |
DE881344C (en) | Method and device for separating and purifying at least one of the components of a liquid organic mixture containing several components | |
DE2220290C3 (en) | Device for the uninterrupted crystallization cleaning of organic compounds from additions that are soluble in the melt | |
EP0492149B1 (en) | Process and apparatus for cleaning chemical substances | |
DE557598C (en) | Method and device for operating smelting furnaces, in particular Siemens-Martin-OEfen | |
EP0707508B1 (en) | Process and device for the separation of substances by crystallization of molten material | |
DE3540889A1 (en) | METHOD AND LANCE FOR FORMING A FIRE-RESISTANT MATERIAL UNDER SPRAYING PARTICLE-SHAPED EXOTHERM OXIDIZABLE MATERIALS | |
DE202012008388U1 (en) | Tempering and coating machine for chocolate masses | |
DE391240C (en) | Device for removing individual glass loads from the container | |
AT110340B (en) | Method and device for delivering measured glass gobs. | |
DE554026C (en) | Process for the continuous excavation of cylindrical glass bodies from the melt | |
DE319798C (en) | Process for the continuous production of calcium cyanamide | |
DE519797C (en) | Rotary kiln for the production of molten cement | |
DE1176976B (en) | Device for the production of protrusions and indentations having powder from relatively easily fusible metals | |
DE1771523B2 (en) | FLOATING CHAMBER FOR THE MANUFACTURE OF FLAT GLASS BY THE FLOATING PROCESS | |
DE552333C (en) | Method and apparatus for delivering measured gobs of glass from a container to a mold | |
DE566715C (en) | Methods and devices for casting metals or alloys directly from the molten state | |
DE938585C (en) | Device for coating and treating body surfaces, in particular for the photomechanical production of printing forms, mainly printing rollers |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C3 | Grant after two publication steps (3rd publication) | ||
E77 | Valid patent as to the heymanns-index 1977 | ||
EHJ | Ceased/non-payment of the annual fee |