Patent Abstract:
An improved method and apparatus for recovering metal values from Electric Arc Furnace dust, particularly zinc and iron values, by mixing EAF dust and carbonaceous fines to form a particulate mixture; heating the mixture at a sufficient temperature and for a sufficient time to reduce and release volatile metals and alkali metals in a flue gas; collecting the released metals, and removing the metal values from the process as product.

Full Description:
FIELD OF THE INVENTION 
     The present invention relates to a method and apparatus for recovering metal values from particulate metal-containing dust, and more particularly to a method and apparatus for recovering metal from electric arc furnace dust. 
     BACKGROUND OF THE INVENTION 
     Rotary Hearth Furnace processes such as the Midrex FASTMET™ Process, INMETCO process, and Maumee process, and Rotary Kiln processes such as Horse Head and BUS Waelz Kiln, have been developed, marketed, and sold as methods of recovering iron units, zinc and other valuable metallics from large integrated steel mill waste streams. Economical plant capacity for these processes is in the range of 100,000 to 200,000 tonnes of waste processed per year. Mini mills, based on Electric Arc Furnace technology, are typically smaller in capacity than integrated steels mills and produce significantly less waste, ranging from 5,000 to 30,000 tonnes per year. The specific dust waste from Electric Arc Furnace (EAF) operations has been classified by the US Environmental Protection Agency (US EPA) as K061, a hazardous waste requiring special handling, inventory control and approved disposal by US EPA. These special handling requirements and implied liabilities make operation of a large capacity centralized EAF Dust Processing facility cumbersome and undesirable. High Temperature Metals Recovery (HTMR) processing of wastes classified as K061 has been identified by US EPA as the preferred method of treating and delisting. 
     It is therefore desirable to provide an economical method of thermal treatment of as-generated mini-mill waste located at the site at which such waste is produced. 
     In 1998, Midrex International BV received U.S. Pat. No. 5,730,775, that teaches an improved method known by the trade name or trademark of FASTMET™, and apparatus for producing direct reduced iron from dry iron oxide and carbon compacts that are layered no more than two layers deep onto a rotary hearth, and are metallized by heating the compacts to temperatures of approximately 1316° to 1427° C., for a short time period. For a general understanding of the recent art, U.S. Pat. No. 5,730,775 is herein incorporated by reference. 
     In existing rotary hearth and rotary kiln HTMR processes, most of the capital cost is associated with feed preparation equipment necessary to feed the processing furnace, with the fabrication and erection of the furnace itself, and with product handling equipment. 
     SUMMARY OF THE INVENTION 
     The invention provides a method and apparatus for recovering principally iron and zinc values from EAF dust. The method of recovering metal values from metal-containing dust, comprises the steps of: 
     a. mixing metal-containing dust and carbonaceous fines to form a particulate mixture; 
     b. heating the metal-containing dust and carbonaceous fines mixture on a moving bed horizontal tunnel furnace at a sufficient temperature and for a sufficient time to reduce and release volatile metals and alkali metals therefrom along with gaseous products; 
     c. collecting the released metals and gases, and reoxidizing the metals; and 
     d. separating the metal values from the gases and removing the metal values, principally zinc and iron, from the process as product. 
     The furnace is sealed to prevent the intrusion of ambient air. A baghouse is provided to collect the volatile metals. 
     The invented process feeds a simple “as is” mixture of EAF dust and carbon fines (coal dust, charcoal, pet coke. etc.) through a feed leg onto a horizontal stroke conveyor. Motion of the conveyor controls the feed rate and distributes the feed evenly across the conveyor pan. Since the pan is not a “moving hearth” the feed area is always cold,. i.e., at ambient temperature. This eliminates the complicated and expensive feed and leveling systems associated with rotary hearth processes. 
     OBJECTS OF THE INVENTION 
     The principal object of the present invention is to provide an improved method of achieving rapid and efficient reduction of metal oxide fines and recovery of metal values therefrom. 
     Another object of the invention is to provide a simple, low-cost method and apparatus for the processing of EAF dust. 
     Another object of the invention is to provide a reduction furnace apparatus which can be installed on site, or can be fully portable. 
     A further object of the invention is to provide a fines reduction furnace capable of operating at variable speed 
     Another object of the invention is to provide means for recovering useable zinc oxide from EAF dust. 
     Another object of the invention is to provide a method which requires no hazardous waste water treatment. 
     Another object of the invention is to provide a method which produces no hazardous solid waste. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     The foregoing and other objects will become more readily apparent by referring to the following detailed description and the appended drawings in which: 
     FIG. 1 is a schematic diagram of the invented process. 
     FIG. 2 is a schematic top view of the furnace, feed, and discharge. 
     FIG. 3 is side view of the invented processing furnace mounted on a truck. 
     FIG. 4 is side view of the filter equipment of the invention mounted on a truck. 
     FIG. 5 is a side view of an EAF Dust silo or bin mounted on a truck. 
     FIG. 6 is a side view of a pulverized reductant bin mounted on a truck. 
     FIG. 7 is a side view of the invented tunnel furnace and associated equipment and supports. 
     FIG. 8 is a cross-section of the tunnel kiln taken along line  8 — 8  of FIG.  7 . 
     FIG. 9 is an enlarged detail view of the portion of FIG. 7 indicated by oval  90 . 
    
    
     DETAILED DESCRIPTION 
     As shown in FIG. 1 an elongated reduction furnace  10  has a charging or feed end  12  and a discharge end  14 . A feed hopper  16  communicates with the charging end  12  of the furnace which can advantageously be by a seal leg  18  controlled by a sliding gate  20 . A horizontal stroke conveyor  22  is positioned in the lower part of the furnace to move the feed material from the charging end through the furnace at a controlled rate. Burners  24  are positioned as shown in the side wall of the reduction furnace to provide the necessary heat for the reduction process. A flue gas offtake  26  is provided in the top wall of the refractory lined furnace. 
     The furnace  10  is a tunnel furnace and has a suitable side seal  28  such as a flexible connector which provides a seal between the sides of the furnace and the conveyor  22 . 
     Product is discharged from the furnace into a transport vessel  92 , the discharge of which product may be controlled by a slide gate  94 . 
     EAF dust is collected in bin  40  and fed to a mixing conveyor  42  along with pulverized reductant from bin  44 . The reductant is pulverized or powdered coal, petroleum coke, or charcoal. 
     Flue gas from offtake  26  has dilution air A provided thereto and the diluted flue gas moves through line  48  to a filter  50 . Particulates drop out from the filter which may be a bag filter and are collected in vessel  52 . The filtered diluted offgas may then be exhausted to the air through exhaust stack  54 . 
     The reduction furnace can not only be mounted on the ground as shown in FIGS. 1 and 7, but can be truck mounted as shown in FIG.  3 . The additional components of the process can also be truck mounted, ie, the offgas treating vessel comprising a bag filter  50  and a fan  56  shown in FIG.  4  and EAF silo or bin  40 A shown in FIG.  5  and reductant bin  44 A shown in FIG.  6 . 
     The speed of the material flowing through the furnace is controlled by thermocouple  88 . 
     The invention is a low cost plant specifically designed for efficient EAF Dust thermal processing. The invented reduction process utilizes a horizontal motion conveyor  22  in a high temperature tunnel furnace  10  for thermal processing of EAF Dust. The primary goal is recovery of high quality crude zinc oxide. Metallic iron product that is produced may be recycled to an EAF as injectable fines, or it may be briquetted in a briquetting facility, or it may be landfilled, depending on local requirements. 
     The horizontal conveyor  22  is shop fabricated and installed at the site with minimal foundations and field erection. The horizontal stroke conveyor transports the EAF dust and carbon mixture from the cold feed area through a heated “tunnel kiln” or furnace  10  maintained at 1100 to 1200° C. by a system of burners. Retention time in the heated zone is 10 to 20 minutes. 
     A thermocouple  88  located under the conveyor pan at the end of the heating zone monitors the temperature of the bottom layer of the dust and carbon mixture and maintains a setpoint by controlling by the frequency of the conveyor stroke. Since the action of the conveyor does not mix the dust mixture, monitoring the temperature of the bottom layer indicates when the reduction and volatile metals release is complete, which is when the lowermost part of the mixture reaches a temperature of about ˜1100° C., and this also protects the conveyor pan from damage due to overheating. 
     Volatile metals (zinc, lead, cadmium, etc.) and alkali metals (sodium and potassium) are released from the dust upon heating, are reoxidized in the flue gas, exhausted from the furnace with the flue gas, and captured by the bag filter. The volatile metals strip sulfur compounds from the flue gas and form metal sulfides that are also captured by the bag filter, thus controlling and limiting SO 2  emissions. The flue is quickly cooled from furnace temperatures (˜1150° C.) to acceptable bag filter inlet temperature by introducing dilution air (at about a 5:1 air to flue gas ratio). This quick cooling prevents formation of dioxin compounds. The fuel burners are low NO x  by design and are operated with minimum excess oxygen to minimize NO x  generation. No additional emission control devices are required to meet EPA requirements. The particulate captured by the bag filter is rich in zinc oxide (more than 70%) and is sold to zinc refiners as a valuable source of zinc. 
     Reduced iron product is discharged from the furnace, preferably into a sealed container  92 . When the container is full, the sliding gate  94  is closed, the container is removed and replaced with another. The reduced iron product collected in the container may be reintroduced by injectoin into the EAF, or briquetted and fed to the EAF with scrap, or in some cases simply disposed of in land fill. The filled container may be cooled by simply setting it aside under ambient conditions for 12 to 18 hours, or it may be more rapidly cooled by immersion in a water bath. 
     Plant equipment may be skid mounted for easy erection (and minimum engineering) on a simple, concrete slab foundation. 
     Bench scale testing has shown that reduction of EAF Dust and release of zinc is feasible under the conditions described by this process. The following table shows recovery of iron units from EAF dust in this process: 
     
       
         
               
               
               
               
               
               
             
               
               
               
               
               
               
             
           
               
                   
               
               
                 Sam- 
                   
                   
                   
                   
                   
               
               
                 ple 
                 Description 
                 Total Iron 
                 Metallic Iron 
                 % MET 
                 % C 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 A 
                 MET #2 Residue 
                 52.72 
                 41.55 
                 78.8 
                 2.13 
               
               
                 B 
                 MET Dust Mix 
                 30.23 
                 — 
                 — 
                 13.07 
               
               
                 C 
                 MET (10 min.) CSM 
                 45.57 
                 35.04 
                 76.9 
                 3.34 
               
               
                 D 
                 MET (12.5 min.) CSM 
                 53.48 
                 43.54 
                 81.4 
                 2.03 
               
               
                 E 
                 MET (15 min.) CSM 
                 49.95 
                 32.18 
                 64.4 
                 1.52 
               
               
                   
               
               
                 Notes:  
               
               
                 A = 7.3 grams of mix heated at 1100° C. for 15 minutes  
               
               
                 B is unheated mix-mixing ratio is 84% EAF Dust with 16% Charcoal (ground and dry)  
               
               
                 C thru E9 grams of mix heated at 1150° C. Furnace Temperature  
               
             
          
         
       
     
     Alternative Embodiments 
     Alternatively the furnace and related equipment may be truck mounted on a series of trucks as shown in FIGS. 3 through 6, which are then connected with appropriate conduits. 
     Summary of the Achievement of the Objects of the Invention 
     From the foregoing, it is readily apparent that I have invented an improved method and apparatus for achieving rapid and efficient reduction of metal oxide fines and recovery of metal values therefrom; a simple, low-cost method and apparatus for the processing of EAF dust, which can be installed on site, or can be fully portable, a fines reduction furnace which is capable of operating at variable speed; which recovers useable zinc oxide from EAF dust; which requires no hazardous waste water treatment; and which produces no hazardous solid waste. 
     It is to be understood that the foregoing description and specific embodiments are merely illustrative of the best mode of the invention and the principles thereof, and that various modifications and additions may be made to the apparatus by those skilled in the art, without departing from the spirit and scope of this invention, which is therefore understood to be limited only by the scope of the appended claims.

Technology Classification (CPC): 8