PL442302A1 - Galvanizing ash collection tank and method of filling the tank in the hot-dip galvanizing process - Google Patents
Galvanizing ash collection tank and method of filling the tank in the hot-dip galvanizing processInfo
- Publication number
- PL442302A1 PL442302A1 PL442302A PL44230222A PL442302A1 PL 442302 A1 PL442302 A1 PL 442302A1 PL 442302 A PL442302 A PL 442302A PL 44230222 A PL44230222 A PL 44230222A PL 442302 A1 PL442302 A1 PL 442302A1
- Authority
- PL
- Poland
- Prior art keywords
- tank
- galvanizing
- chamber
- cyclone
- ash
- Prior art date
Links
- 238000005246 galvanizing Methods 0.000 title abstract 12
- 238000000034 method Methods 0.000 title abstract 4
- 239000002956 ash Substances 0.000 abstract 8
- 235000002918 Fraxinus excelsior Nutrition 0.000 abstract 3
- 230000010349 pulsation Effects 0.000 abstract 2
- 238000000926 separation method Methods 0.000 abstract 2
- 238000001816 cooling Methods 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 239000000428 dust Substances 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 238000007670 refining Methods 0.000 abstract 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/02—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct with heating or cooling, e.g. quenching, means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/04—Multiple arrangement thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/04—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor characterised by the coating material
- C23C2/06—Zinc or cadmium or alloys based thereon
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Coating With Molten Metal (AREA)
Abstract
Zbiornik gromadzenia popiołów cynkowniczych znajdujący się w praktycznej odległości od wanny cynkowniczej, charakteryzuje się tym, że tworzą go dwie komory (4, 6), gdzie pierwsza komora (4) posiada zasyp zbiornika (2) nad wanną cynkowniczą (1), nad którym znajduje się wentylator wysokociśnieniowy (8) połączony z kanałem pneumatycznym (3) dostarczającym popiół do pierwszej komory (4) zbiornika, w której znajduje się cyklon (5) łączący drugą komorę (6) zbiornika z multicyklonem (7) oraz filtr pulsacyjny (9) pieca cynkowniczego. W innej odmianie zbiornik charakteryzuje się tym, że tworzą go dwie komory (4, 6), pozwalające na praktycznie całkowite wydzielenie popiołów ze strumienia powietrza, umożliwiające wydzielenie w pierwszej jego komorze, cięższej, metalicznej frakcji popiołu, która jest w tej samej ocynkowni poddana recyklingowi poprzez rozścielenie na lustrze kąpieli cynkowniczej i poddana rafinacji. Pierwsza komora (4) posiada cyklon (5), a druga komora (6) multicyklon (7) napędzany przez wentylator wysokociśnieniowy (8) odprowadzający strumień powietrza z resztkami pyłów z popiołów do komory filtra pulsacyjnego (9) pieca cynkowniczego. Komory (4, 6) wyposażone w przepustnice i kanały wsypowe (10) umożliwiają pakowanie popiołów. Sposób napełniania zbiornika w procesie cynkowania ogniowego charakteryzuje się tym, że zbiornik jest napełniany w sposób pneumatyczny z jednoczesnym wychłodzeniem, poprzez załadunek zgarniętych na brzeg wanny cynkowniczej (1) popiołów, perforowaną łopatką do zasypu (2), w którym podciśnieniowo podawane są kanałem (3) do pierwszej komory (4) zbiornika, w której cyklon (5) rozdziela frakcje cięższą popiołów, a frakcja lekka jest transportowana do drugiej komory (6) zbiornika, w której multicyklon (7) wydziela frakcje pylistą, która opada w komorze, a prawie oczyszczone powietrze kierowane jest przez wentylator wysokociśnieniowy (8) do komory filtra pulsacyjnego (9) obsługującego piec cynkowniczy.The galvanizing ash collection tank, located at a practical distance from the galvanizing tank, is characterized by the fact that it consists of two chambers (4, 6), where the first chamber (4) has a tank hopper (2) above the galvanizing tank (1), above which there is consists of a high-pressure fan (8) connected to a pneumatic channel (3) supplying ash to the first chamber (4) of the tank, in which there is a cyclone (5) connecting the second chamber (6) of the tank with the multi-cyclone (7) and the pulse filter (9) of the furnace galvanizing. In another version, the tank is characterized by two chambers (4, 6), allowing for virtually complete separation of ashes from the air stream, enabling the separation in the first chamber of a heavier, metallic fraction of ash, which is recycled in the same galvanizing plant by spreading a galvanizing bath on the mirror and refining it. The first chamber (4) has a cyclone (5), and the second chamber (6) has a multi-cyclone (7) driven by a high-pressure fan (8) discharging an air stream with ash dust residues into the pulsation filter chamber (9) of the galvanizing furnace. Chambers (4, 6) equipped with dampers and feed channels (10) enable ash packing. The method of filling the tank in the hot-dip galvanizing process is characterized by the fact that the tank is filled pneumatically with simultaneous cooling, by loading the ashes scraped onto the edge of the galvanizing bath (1) with a perforated shovel into the charge (2), where they are fed under vacuum through the channel (3). ) to the first chamber (4) of the tank, where the cyclone (5) separates the heavier fraction of ashes, and the light fraction is transported to the second chamber (6) of the tank, where the multicyclone (7) releases the dusty fraction, which falls in the chamber and almost the purified air is directed by a high-pressure fan (8) to the pulsation filter chamber (9) serving the galvanizing furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL442302A PL442302A1 (en) | 2022-09-16 | 2022-09-16 | Galvanizing ash collection tank and method of filling the tank in the hot-dip galvanizing process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL442302A PL442302A1 (en) | 2022-09-16 | 2022-09-16 | Galvanizing ash collection tank and method of filling the tank in the hot-dip galvanizing process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL442302A1 true PL442302A1 (en) | 2024-03-18 |
Family
ID=90300715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL442302A PL442302A1 (en) | 2022-09-16 | 2022-09-16 | Galvanizing ash collection tank and method of filling the tank in the hot-dip galvanizing process |
Country Status (1)
| Country | Link |
|---|---|
| PL (1) | PL442302A1 (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100147149A1 (en) * | 2007-02-16 | 2010-06-17 | Peter Evans | Cyclone with classifier inlet and small particle by-pass |
| EP2851126A1 (en) * | 2012-10-15 | 2015-03-25 | Horkos Corporation | Multi-cyclone collector |
-
2022
- 2022-09-16 PL PL442302A patent/PL442302A1/en unknown
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100147149A1 (en) * | 2007-02-16 | 2010-06-17 | Peter Evans | Cyclone with classifier inlet and small particle by-pass |
| EP2851126A1 (en) * | 2012-10-15 | 2015-03-25 | Horkos Corporation | Multi-cyclone collector |
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