GB600326A - Improvements in and relating to the separation of particulate materials - Google Patents
Improvements in and relating to the separation of particulate materialsInfo
- Publication number
- GB600326A GB600326A GB1569945A GB1569945A GB600326A GB 600326 A GB600326 A GB 600326A GB 1569945 A GB1569945 A GB 1569945A GB 1569945 A GB1569945 A GB 1569945A GB 600326 A GB600326 A GB 600326A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- vessel
- pipe
- entrained
- mixture
- 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
- 239000011236 particulate material Substances 0.000 title abstract 2
- 238000000926 separation method Methods 0.000 title 1
- 239000000463 material Substances 0.000 abstract 6
- 239000002245 particle Substances 0.000 abstract 6
- 239000007789 gas Substances 0.000 abstract 4
- 239000000203 mixture Substances 0.000 abstract 4
- 238000004519 manufacturing process Methods 0.000 abstract 3
- 239000001257 hydrogen Substances 0.000 abstract 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 2
- 238000005054 agglomeration Methods 0.000 abstract 1
- 230000002776 aggregation Effects 0.000 abstract 1
- 230000003247 decreasing Effects 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 150000002431 hydrogen Chemical class 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 229910052742 iron Inorganic materials 0.000 abstract 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 abstract 1
- 229910000460 iron oxide Inorganic materials 0.000 abstract 1
- 230000004048 modification Effects 0.000 abstract 1
- 238000006011 modification reaction Methods 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
-
- 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
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B4/00—Separating by pneumatic tables or by pneumatic jigs
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
<PICT:0600326/III/1> <PICT:0600326/III/2> A process for separating particulate material of desired particle size from a mixture containing material of larger particle size, which process may be used in the production of hydrogen as described in Specification 578,323, comprises passing a gas and/or vapour through a bed of the mixture contained in a stationary vessel with a conical bottom, at a velocity sufficient to maintain the material of desired size in the fluid state, avoiding the production of an entrained stream, but insufficient to prevent the larger particles from moving to the conical bottom of the vessel where they distribute the gas across the bed. The velocity of the gas may, however, be increased at the upper surface of the bed for the purpose of removing the desired particle size in an entrained stream. In the production of hydrogen, the mixture is metallic iron, iron oxide and larger particles due to agglomeration of the smaller particles. In the arrangement shown in Fig. 1, the mixture is fed through a pipe 2 to a vessel 1 through which is forced a gas from a ring main 9 and tuyeres 10. Larger material is removed from the bottom under the control of a slide valve 8. The smaller material is entrained through a pipe 3. In a modification, the top of the vessel is conical, decreasing in cross-section to that of a narrow outlet. In a further arrangement, the smaller material flows over a weir to an outlet. In the arrangement shown in Fig. 4, the smaller material flows through a channel 3 to an outlet pipe 15 where it is entrained upwardly by steam passed through a pipe 16. Specification 582,055, [Group XII], also is referred to.
Publications (1)
Publication Number | Publication Date |
---|---|
GB600326A true GB600326A (en) | 1948-04-06 |
Family
ID=1731713
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1569945A Expired GB600326A (en) | 1945-06-20 | Improvements in and relating to the separation of particulate materials |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB600326A (en) |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2643219A (en) * | 1949-06-21 | 1953-06-23 | Standard Oil Dev Co | Fluidized distillation of oil-shale |
US2654665A (en) * | 1950-02-21 | 1953-10-06 | Consolidation Coal Co | Gasification of carbonaceous solids |
US2699421A (en) * | 1950-09-26 | 1955-01-11 | Sinclair Refining Co | Coking reactor |
US2711387A (en) * | 1949-11-30 | 1955-06-21 | Exxon Research Engineering Co | Treating subdivided solids |
US2717694A (en) * | 1954-05-26 | 1955-09-13 | Standard Oil Co | Elutriation of fines from powdered solids having agglomerating tendencies |
DE934473C (en) * | 1950-04-15 | 1955-10-27 | Basf Ag | Process for the production of gases containing sulfur dioxide |
US2725348A (en) * | 1949-12-30 | 1955-11-29 | Exxon Research Engineering Co | Fluidized distillation of oil-bearing minerals |
US2774661A (en) * | 1951-08-07 | 1956-12-18 | Dorr Co | Method of heat-treating fines in a coarse solids fluidized bed |
US2870001A (en) * | 1952-06-26 | 1959-01-20 | Texas Gulf Sulphur Co | Method of fluidization |
US2870002A (en) * | 1952-06-26 | 1959-01-20 | Texas Gulf Sulphur Co | Method of fluidization |
DE973866C (en) * | 1951-03-04 | 1960-06-30 | Metallgesellschaft Ag | Process for roasting sulfidic ores |
US2954288A (en) * | 1960-09-27 | Ore beneficiahon | ||
US3002805A (en) * | 1957-03-07 | 1961-10-03 | Socony Mobil Oil Co Inc | Method for contacting fluids with solid contact materials |
US3251677A (en) * | 1963-04-19 | 1966-05-17 | Exxon Research Engineering Co | Fluid bed process |
US3332853A (en) * | 1962-06-22 | 1967-07-25 | Coal Industry Patents Ltd | Apparatus for effecting dense phase fluidisation of particulate material |
US3341014A (en) * | 1964-01-29 | 1967-09-12 | Laporte Titanium Ltd | Process of particulate matter separation |
-
1945
- 1945-06-20 GB GB1569945A patent/GB600326A/en not_active Expired
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2954288A (en) * | 1960-09-27 | Ore beneficiahon | ||
US2643219A (en) * | 1949-06-21 | 1953-06-23 | Standard Oil Dev Co | Fluidized distillation of oil-shale |
US2711387A (en) * | 1949-11-30 | 1955-06-21 | Exxon Research Engineering Co | Treating subdivided solids |
US2725348A (en) * | 1949-12-30 | 1955-11-29 | Exxon Research Engineering Co | Fluidized distillation of oil-bearing minerals |
US2654665A (en) * | 1950-02-21 | 1953-10-06 | Consolidation Coal Co | Gasification of carbonaceous solids |
DE934473C (en) * | 1950-04-15 | 1955-10-27 | Basf Ag | Process for the production of gases containing sulfur dioxide |
US2699421A (en) * | 1950-09-26 | 1955-01-11 | Sinclair Refining Co | Coking reactor |
DE973866C (en) * | 1951-03-04 | 1960-06-30 | Metallgesellschaft Ag | Process for roasting sulfidic ores |
US2774661A (en) * | 1951-08-07 | 1956-12-18 | Dorr Co | Method of heat-treating fines in a coarse solids fluidized bed |
US2870001A (en) * | 1952-06-26 | 1959-01-20 | Texas Gulf Sulphur Co | Method of fluidization |
US2870002A (en) * | 1952-06-26 | 1959-01-20 | Texas Gulf Sulphur Co | Method of fluidization |
US2717694A (en) * | 1954-05-26 | 1955-09-13 | Standard Oil Co | Elutriation of fines from powdered solids having agglomerating tendencies |
US3002805A (en) * | 1957-03-07 | 1961-10-03 | Socony Mobil Oil Co Inc | Method for contacting fluids with solid contact materials |
US3332853A (en) * | 1962-06-22 | 1967-07-25 | Coal Industry Patents Ltd | Apparatus for effecting dense phase fluidisation of particulate material |
US3251677A (en) * | 1963-04-19 | 1966-05-17 | Exxon Research Engineering Co | Fluid bed process |
US3341014A (en) * | 1964-01-29 | 1967-09-12 | Laporte Titanium Ltd | Process of particulate matter separation |
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