GB278774A - Improvements in rotary chemical furnaces - Google Patents
Improvements in rotary chemical furnacesInfo
- Publication number
- GB278774A GB278774A GB1439726A GB1439726A GB278774A GB 278774 A GB278774 A GB 278774A GB 1439726 A GB1439726 A GB 1439726A GB 1439726 A GB1439726 A GB 1439726A GB 278774 A GB278774 A GB 278774A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oxide
- temperature
- supplied
- withdrawn
- zone
- 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
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/28—Moving reactors, e.g. rotary drums
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B7/00—Rotary-drum furnaces, i.e. horizontal or slightly inclined
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
- B01J2219/00081—Tubes
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00117—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00132—Controlling the temperature using electric heating or cooling elements
- B01J2219/00135—Electric resistance heaters
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/0015—Controlling the temperature by thermal insulation means
- B01J2219/00155—Controlling the temperature by thermal insulation means using insulating materials or refractories
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
278,774. Tocco, L., and Landi, M. June 8, 1926. Resistance furnaces. - A continuously-operating rotary furnace heated by internal resistance elements is divided by partitions into a number of reaction chambers, and means are provided by which materials, can be automatically introduced and withdrawn, and gases &c. resulting from the reactions can be removed. In the plant shown, which is more particularly adapted for the treatment of ores containing lead and zinc, the material passes in series through three rotary drums I, O, Q, of which the first is divided by partitions 27 into three zones Ir, Iz, Iy, while the second and third are separated by a fixed water-cooled head 80. In the first zone Ir the ore is dried at a temperature of about 150‹ C., in the second Iz the lead sulphide is converted to oxide at a temperature of 380‹ C. by air supplied through the pipe 42, and in the third the oxide is reduced by carbon supplied by a screw conveyer 35 and delivered between the second and third zones through a passage in the partition. The third zone is heated to a temperature of about 500‹ C. by resistances 43, which are embedded in zirconia in grooves in the furnace shell and are supplied with current by slip-rings and brushes. The molten lead is withdrawn through a pipe 60, and the remainder of the charge passes through a water-cooled magnetic separator 64 to the chamber 10, where the zinc sulphide is converted to oxide at a temperature of about 600‹ C. In this zone the surplus heat is utilized to generate steam in a stationary boiler O<1>. The oxide then passes through a rotary chamber 84, in which it is mixed with carbon supplied through a pipe 86, and into the chamber where a temperature of 1400‹ C. is maintained by electric resistances. Here the zinc is reduced, and the vapourized metal is reoxidized by air supplied through a passage 92 in the fixed head 80. The oxide is withdrawn through the conduit 103, while the solid residue is discharged through the passage 100 on to the conveyer 101. The ore is supplied to the zone Ir through the shoot 12 and the charging apparatus comprises a hopper 1, crusher 2, and rotary valves 4, 10 driven through gearing from the furnace. Gases are withdrawn from the zones Ir, Iy and O through pipes 22, 56 and 76 respectively.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1439726A GB278774A (en) | 1926-06-08 | 1926-06-08 | Improvements in rotary chemical furnaces |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1439726A GB278774A (en) | 1926-06-08 | 1926-06-08 | Improvements in rotary chemical furnaces |
Publications (1)
Publication Number | Publication Date |
---|---|
GB278774A true GB278774A (en) | 1927-10-10 |
Family
ID=10040447
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1439726A Expired GB278774A (en) | 1926-06-08 | 1926-06-08 | Improvements in rotary chemical furnaces |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB278774A (en) |
-
1926
- 1926-06-08 GB GB1439726A patent/GB278774A/en not_active Expired
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3163520A (en) | Process and apparatus for preheating and pre-reduction of charge to electric furnace | |
US2754197A (en) | Method and a rotary kiln for the manufacture of sponge iron | |
GB278774A (en) | Improvements in rotary chemical furnaces | |
US1403576A (en) | Process of reducing ores | |
US2786747A (en) | Reduction of iron ores by carbon and steam and plant for carrying it into effect | |
US2603561A (en) | Method and apparatus for reducing ores | |
US1917942A (en) | Method and apparatus for heat treatment of materials in rotary furnaces | |
US3197303A (en) | Process for pretreatment of ores in rotary kiln | |
US2235154A (en) | Method for the reduction of metallic oxides | |
US1704029A (en) | Reduction process and apparatus | |
US1160621A (en) | Process of smelting ores. | |
US826742A (en) | Process of reducing metallic compounds and producing carbids. | |
US1277707A (en) | Calcining coal at high temperatures. | |
US1904684A (en) | Method of melting | |
US3180631A (en) | Integrated charring and ore reduction apparatus | |
US1708526A (en) | Rotary chemical furnace | |
US1338439A (en) | Metallurgical method and apparatus | |
US1006876A (en) | Metallurgy of zinc ores and compounds. | |
US1097156A (en) | Process of reducing ores. | |
US826744A (en) | Apparatus for reducing metallic compounds and producing carbids. | |
US1246576A (en) | Apparatus for removing cadmium from zinc ores. | |
US1007990A (en) | Method or process for the reduction and smelting of ore and arrangement therefor. | |
US1338440A (en) | Production of lead | |
US1899161A (en) | Metallurgical apparatus | |
US1804161A (en) | Method of and means for producing molten and refined metal from crude ores |