DE749635C - Process for the production of pure carbon according to the foam swimming process, in which the foam products are floated in several stages with a constant supply of fresh water - Google Patents
Process for the production of pure carbon according to the foam swimming process, in which the foam products are floated in several stages with a constant supply of fresh waterInfo
- Publication number
- DE749635C DE749635C DEE55110D DEE0055110D DE749635C DE 749635 C DE749635 C DE 749635C DE E55110 D DEE55110 D DE E55110D DE E0055110 D DEE0055110 D DE E0055110D DE 749635 C DE749635 C DE 749635C
- Authority
- DE
- Germany
- Prior art keywords
- foam
- fresh water
- floated
- production
- pure carbon
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
- B03D1/06—Froth-flotation processes differential
Landscapes
- Physical Water Treatments (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Description
Verfahren zur Herstellung von Reinstkohle nach dem Schaumschwimmverfahren, bei dem die Schaumerzeugnisse in mehreren Stufen unter ständiger Frischwasserzufuhr nachgeschwommen werden Die Erfindung betrifft ein Verfahren zur Herstellung von Reinstkohle nach dem Schaumschwimmverfahren, bei dem die Schaumerzeugnisse in mehreren Stufen unter ständiger Fri.schwasserzufuhr nachgeschwommen werden, wie es in dein Hauptpatent 746 179 beschrieben ist. Gemäß dem Hauptpatent werden die Schaumerzeugnisse vor jeder Nachreinigungsstufe auf Vakuumfiltern entwässert, anschließend daran in Frischwasser aufgeschlämmt und ein- oder mehrfach nachgeschwommen. Das Verfahren nach dem Hauptpatent, d. h. die Zwischenentwässerung der Schaumerzeugnisse auf Vakuumfiltern, wird im allgemeinen dann anzuwenden sein, wenn eine gröbere Zerkleinerung der Kohle vor der Schaumschwimmaufbereitung, z. B. auf unter o,6 mm ausreicht. In weiterer Ausgestaltung des Gedankens des Hauptpatents wird gemäß der Erfindung vorgeschlagen, die Entwässerung .der Schaumerzeugnisse vor jeder Nachreinigungsstufe auf einer Schleuder vorzunehmen. Eine solch;. Zwischenentwässerung wird vorzugsweise für feiner aufgeschlossene Kohle von beispielsweise unter o,2 mm anzuwenden sein. Die -Verwendung von Schleudern zum Entwässern ist an sich bekannt. Ihre Anwendung im Rahmen der im Hauptpatent unter Schutz gestellten Kombination im Austausch gegen Vakuumfilter ergibt eine wesentliche Verbesserung und Vereinfachung der bisher bekannten Verfahren, da durch die zwischengeschaltete Entwässerung das in der Trübe emulgierte Schwimmittel sowie auch die kolloidalen Bestandteile und gegebenenfalls auch gelöste Salze entfernt werden. Es ist dabei weiter von Vorteil, wenn die Gewebespannungen der Schleuder so gewählt werden, dar die aschenreicheren Feinstschlämme mit dem Filtrateva'sser'-abgelien. -Process for the production of pure carbon according to the foam swimming process, in which the foam products in several stages with a constant supply of fresh water The invention relates to a method for producing Pure carbon according to the foam swimming process, in which the foam products in several Steps can be swum under constant supply of fresh water, as it is in your Main patent 746 179 is described. According to the main patent, the foam products dehydrated on vacuum filters before each post-cleaning stage, then in Fresh water slurried and swum once or several times. The procedure according to the main patent, d. H. intermediate drainage of foam products on vacuum filters, will generally be used when a coarser crushing of the coal before the foam swim preparation, e.g. B. is sufficient to less than 0.6 mm. In further Development of the idea of the main patent is proposed according to the invention, the dewatering of the foam products before each post-cleaning stage on one To make a sling. One such ;. Intermediate drainage is preferred for finer digested coal of, for example, less than 0.2 mm must be used. The usage from centrifuging to dewatering is known per se. Your application within the Combination protected in the main patent in exchange for vacuum filter results in a significant improvement and simplification of the previously known processes, as the floating agent emulsified in the sludge due to the interposed dewatering as well as the colloidal components and possibly also solved Salts are removed. It is also advantageous when the tissue tension the centrifuge can be chosen so that the ash-rich fine sludge with the Filtratevasser'-drained. -
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEE55110D DE749635C (en) | 1941-07-20 | 1941-07-20 | Process for the production of pure carbon according to the foam swimming process, in which the foam products are floated in several stages with a constant supply of fresh water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEE55110D DE749635C (en) | 1941-07-20 | 1941-07-20 | Process for the production of pure carbon according to the foam swimming process, in which the foam products are floated in several stages with a constant supply of fresh water |
Publications (1)
Publication Number | Publication Date |
---|---|
DE749635C true DE749635C (en) | 1944-11-28 |
Family
ID=7082021
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEE55110D Expired DE749635C (en) | 1941-07-20 | 1941-07-20 | Process for the production of pure carbon according to the foam swimming process, in which the foam products are floated in several stages with a constant supply of fresh water |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE749635C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE864833C (en) * | 1948-12-31 | 1953-01-29 | Erich Dr-Ing Noetzold | Extraction of ultra-pure coal with the least ashes by flotation |
-
1941
- 1941-07-20 DE DEE55110D patent/DE749635C/en not_active Expired
Non-Patent Citations (1)
Title |
---|
None * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE864833C (en) * | 1948-12-31 | 1953-01-29 | Erich Dr-Ing Noetzold | Extraction of ultra-pure coal with the least ashes by flotation |
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