GB1075907A - A method of and an apparatus for separating a constituent from a stream of media - Google Patents
A method of and an apparatus for separating a constituent from a stream of mediaInfo
- Publication number
- GB1075907A GB1075907A GB11845/66A GB1184566A GB1075907A GB 1075907 A GB1075907 A GB 1075907A GB 11845/66 A GB11845/66 A GB 11845/66A GB 1184566 A GB1184566 A GB 1184566A GB 1075907 A GB1075907 A GB 1075907A
- Authority
- GB
- United Kingdom
- Prior art keywords
- region
- auxiliary medium
- chamber
- flow
- inlet
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/08—Housing; Encapsulation
- H01G9/10—Sealing, e.g. of lead-in wires
-
- 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
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
- B04C5/04—Tangential inlets
Abstract
1,075,907. Centrifugal separators. SIEMENS-SCHUCKERTWERKE A.G. March 17, 1966 [March 20, 1965], No. 11845/66. Heading B2P. In an apparatus for separating solid and/or liquid particles from gases, particle-laden gas 4 fed to a vortex chamber 1 through an inlet 2 is imparted a rotary flow 5 by means of vanes 3. A continuous flow of gaseous auxiliary medium as represented by the dotted lines 10 is set up in the chamber in such manner that a helical flow 8 of the auxiliary medium having an axial component and an angular component of velocity in the same directions as those of the rotary flow 5 extends in a first annular region of the chamber surrounding the rotary flow and that a potential flow 9 of the auxiliary medium having an axial component of velocity oppositely directed to that of the rotary flow and an angular component of velocity in the same direction as that of the rotary flow extends in a second annular region of the chamber surrounding the first region. The auxiliary medium passes from the first region to the second region at their ends adjacent an outlet 6 for the purified gas 7 and from the second to the first region at their ends adjacent the inlet 2. The particles are separated radially of the rotary flow and are discharged with a branch of the potential flow in the direction of arrows 11. The auxiliary medium may be sucked from the first region of the chamber through a conduit 15 by a fan 16 and returned to the second region via a passage 17 which may be provided with guide means or nozzles, or which may be of nozzlelike construction, for imparting a preliminary spin to the auxiliary medium. In another embodiment, Fig. 3 (not shown) the auxiliary medium is removed through a duct (18) adjacent the inlet 2 and returned via a duct (19) which has an annularly disposed extension around the inlet (2). In a further modification, Fig. 4 (not shown), a portion only of the auxiliary medium is removed through an annular opening (18) in the wall of the chamber adjacent the inlet (2) and is reintroduced in the upper region of the chamber through obliquely tangential nozzles (20).
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DES0096072 | 1965-03-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1075907A true GB1075907A (en) | 1967-07-19 |
Family
ID=7519805
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB11845/66A Expired GB1075907A (en) | 1965-03-20 | 1966-03-17 | A method of and an apparatus for separating a constituent from a stream of media |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US3396511A (en) |
| JP (1) | JPS529870B1 (en) |
| AT (1) | AT267481B (en) |
| BE (1) | BE677303A (en) |
| CH (1) | CH432204A (en) |
| DK (1) | DK125571B (en) |
| GB (1) | GB1075907A (en) |
| NL (1) | NL147650B (en) |
| SE (1) | SE333919B (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1229212A (en) * | 1967-05-03 | 1971-04-21 | ||
| DE1619920B1 (en) * | 1967-09-27 | 1970-10-01 | Siemens Ag | Swirl device for pre-cleaning the raw gas flow of a three-phase vortex |
| US3643800A (en) * | 1969-05-21 | 1972-02-22 | Bo Gustav Emil Mansson | Apparatus for separating solids in a whirling gaseous stream |
| US3595392A (en) * | 1969-06-13 | 1971-07-27 | Reynolds Submarine Services Co | Method of and apparatus for separating fluids having different densities |
| FI56037C (en) * | 1975-10-30 | 1979-11-12 | Enso Gutzeit Oy | HYDROCYCLON |
| GB1583730A (en) * | 1978-05-31 | 1981-01-28 | Nat Res Dev | Cyclone separator |
| JPS62261842A (en) * | 1986-05-09 | 1987-11-14 | Nippon Air Curtain Kk | Artificial tornado generating mechanism and utilization thereof |
| GB2239191B (en) * | 1989-11-28 | 1993-04-14 | Orkney Water Test Centre Limit | A method of coalescing a disperse phase within a continuous phase of a fluid mixture |
| US5262046A (en) * | 1991-12-27 | 1993-11-16 | Amoco Corporation | In-line cyclone separator and method of solid/gas separation |
| CN104949231A (en) * | 2014-03-25 | 2015-09-30 | 欣兴电子股份有限公司 | Dehumidification equipment and dehumidification method |
| US20150362198A1 (en) * | 2014-06-15 | 2015-12-17 | Unimicron Technology Corp. | Dehumidification apparatus and dehumidification method |
| CN112521993A (en) * | 2020-11-13 | 2021-03-19 | 重庆科技学院 | Natural gas foam separation device, control method and application |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2664966A (en) * | 1949-01-15 | 1954-01-05 | Raymond H Moore | Dust arrester |
| US3064411A (en) * | 1959-08-14 | 1962-11-20 | Jr Joseph Breslove | Separator |
| NL261844A (en) * | 1960-03-25 |
-
1966
- 1966-02-07 DK DK60666AA patent/DK125571B/en unknown
- 1966-02-18 CH CH237166A patent/CH432204A/en unknown
- 1966-02-22 AT AT162166A patent/AT267481B/en active
- 1966-02-28 NL NL666602569A patent/NL147650B/en not_active IP Right Cessation
- 1966-03-03 BE BE677303D patent/BE677303A/xx unknown
- 1966-03-14 SE SE03353/66A patent/SE333919B/xx unknown
- 1966-03-17 GB GB11845/66A patent/GB1075907A/en not_active Expired
- 1966-03-21 US US535799A patent/US3396511A/en not_active Expired - Lifetime
- 1966-03-22 JP JP41017298A patent/JPS529870B1/ja active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| DE1507847B1 (en) | 1972-06-08 |
| SE333919B (en) | 1971-04-05 |
| US3396511A (en) | 1968-08-13 |
| BE677303A (en) | 1966-07-18 |
| NL147650B (en) | 1975-11-17 |
| DK125571B (en) | 1973-03-12 |
| CH432204A (en) | 1967-03-15 |
| NL6602569A (en) | 1966-09-21 |
| AT267481B (en) | 1968-12-27 |
| JPS529870B1 (en) | 1977-03-18 |
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