US2017297113A1PendingUtilityA1

Gas atomization of molten materials using by-product off-gases

Assignee: HATCH LTDPriority: Sep 21, 2014Filed: Sep 21, 2015Published: Oct 19, 2017
Est. expirySep 21, 2034(~8.2 yrs left)· nominal 20-yr term from priority
B22F 2009/0832B22F 9/082F27D 17/302B01J 2/04Y02P10/10
33
PatentIndex Score
0
Cited by
0
References
0
Claims

Abstract

Metallurgical processes and systems for gas atomization of molten slag and/or molten metals from a metallurgical furnace are integrated with off-gas handling processes and equipment, such that the off-gases are fed to the gas atomization plant for atomizing the molten slag and/or molten metal. The use of by-product off-gases for atomizing molten slag and/or molten metals provides a number of benefits, including elimination of off-gas handling and treatment equipment, centralization and upgrading of heat via atomization to improve heat recovery, prevention of oxidation of granular products of atomization, and reduction of CO 2 emissions. A process for preparing a granular product comprises: feeding a molten material and a by-product off-gas to a dispersion apparatus; and contacting the gas with the molten material in the dispersion apparatus, whereby the molten material is dispersed and solidified by contact with the gas to form the granular product.

Claims

exact text as granted — not AI-modified
1 . A process for preparing a granular product, comprising:
 (a) providing a molten material;   (b) feeding the molten material to a dispersion apparatus;   (c) feeding a gas to the dispersion apparatus, wherein the gas is a by-product off-gas;   (d) contacting the gas with the molten material in the dispersion apparatus, whereby the molten material is dispersed and solidified by contact with the gas to form said granular product.   
     
     
         2 . The process of  claim 1 , wherein the molten material is molten metal or molten slag produced by a metallurgical process conducted in a metallurgical furnace. 
     
     
         3 . The process of  claim 2 , wherein the molten material is molten metal and wherein the granular product comprises metal granules. 
     
     
         4 . The process of  claim 2 , wherein the molten material is molten slag and wherein the granular product comprises slag granules. 
     
     
         5 . The process of  claim 2 , wherein the dispersion apparatus comprises a gas atomization plant. 
     
     
         6 . The process of  claim 5 , further comprising an induced draft (ID) fan for blowing the by-product off-gas to the dispersion apparatus. 
     
     
         7 . The process of  claim 6 , wherein the metallurgical furnace includes a furnace cooling system, wherein the by-product off-gas comprises air exhausted by the furnace cooling system, and whereby the ID fan extracts the air from the furnace cooling system. 
     
     
         8 . The process of  claim 6 , wherein the by-product off-gas comprises a furnace off-gas from an interior of the metallurgical furnace, and whereby the ID fan extracts the furnace off-gas from the metallurgical furnace. 
     
     
         9 . The process of  claim 6 , wherein the gas atomization plant produces a hot off-gas, and wherein the hot off-gas is used in downstream process equipment for energy transfer. 
     
     
         10 . The process of  claim 9 , wherein the downstream process equipment comprises a drying unit or a pre-heating unit. 
     
     
         11 . The process of  claim 10 , wherein the by-product off-gas supplied to the gas atomization plant is laden with particulates. 
     
     
         12 . The process of  claim 3 , wherein the off-gas supplied to the gas atomization plant is substantially oxygen-free. 
     
     
         13 . The process of  claim 1 , wherein the by-product off-gas is substantially oxygen-free and is enriched in one or more gases selected from the group consisting of N 2 , H 2 O, CO 2 , CO, H 2  and SO 2 . 
     
     
         14 . The process of  claim 12 , wherein the molten material atomized using the by-product off-gas becomes less oxidized than material that would have otherwise been atomized by air. 
     
     
         15 . The process of  claim 1 , wherein the dispersion apparatus comprises a gas atomization plant;
 wherein the gas atomization plant produces a hot off-gas;   wherein the off-gas supplied to the gas atomization plant includes an undesirable component; and   wherein the undesirable component contained in the off-gas supplied to the gas atomization plant is contacted with the molten material during the formation of said granular product, such that a concentration of the undesirable component in the hot off-gas is less than a concentration of the undesirable component in the off-gas supplied to the gas atomization plant.   
     
     
         16 . The process of  claim 15 , wherein the undesirable component is a gas or a particulate solid. 
     
     
         17 . The process of  claim 15 , wherein the undesirable component is CO 2 , a sulphur-containing species such as SO 2 , SO 3 , and H 2 S; a nitrogen oxide selected from NO and NO 2 , a phosphorus-containing gas; a gaseous organic species; fluorides (such as HF and SiF 4 ), and combinations of one or more thereof; and
 wherein at least a portion of the undesirable component is dissolved in the molten material during formation of said granular product.   
     
     
         18 . The process of  claim 17 , wherein the gaseous organic species is selected from furans and dioxins, and combinations thereof; and
 wherein at least a portion of the gaseous organic species is combusted and/or dissolved in the molten material during formation of said granular product.   
     
     
         19 . The process of  claim 15 , wherein the undesirable component is a particulate solid. 
     
     
         20 . The process of  claim 19 , wherein the particulate solid is dust; and wherein the dust becomes incorporated into the granular product during the formation of the granular product. 
     
     
         21 . The process of  claim 15 , wherein the undesirable component is CO 2 ; and wherein a portion of the CO 2  in the off-gas supplied to the gas atomization plant is captured in the granular product. 
     
     
         22 . The process of  claim 21 , wherein the hot off-gas produced by the gas atomization plant is converted to synthetic gas in a downstream reformer. 
     
     
         23 . A system for preparing a granular product, comprising:
 (a) a metallurgical furnace containing a molten material selected from one or more of molten metal and molten slag;   (b) a gas atomization plant located proximate to the metallurgical furnace;   (c) a gas supply system for supplying a by-product off-gas to the gas atomization plant;   (d) a molten material supply system for transporting the molten material from the metallurgical furnace to the gas atomization plant.   
     
     
         24 . The system of  claim 23 , wherein the molten material comprises slag, and wherein the molten material supply system comprises a slag vessel or launder. 
     
     
         25 . The system of  claim 23 , further comprising an ID fan for blowing the by-product off-gas to the gas atomization apparatus. 
     
     
         26 . The system of  claim 25 , wherein the system further comprises an air cooling system for cooling the metallurgical furnace. 
     
     
         27 . The system of  claim 26 , wherein the by-product off-gas comprises air exhausted by the furnace air cooling system, and wherein the system further comprises a conduit for conveying the by-product off-gas from the furnace to the gas atomization plant. 
     
     
         28 . The system of  claim 23 , wherein the by-product off-gas comprises off-gases exhausted from the metallurgical furnace, and wherein the system further comprises a conduit for conveying the by-product off-gas from the metallurgical furnace to the gas atomization plant. 
     
     
         29 . The system of  claim 28 , further comprising a fume and dust capture hood for collecting the off-gases exhausted from the metallurgical furnace, wherein the conduit for conveying the by-product off-gas to the gas atomization plant is adapted to receive the off-gases from the fume and dust capture hood. 
     
     
         30 . The system of  claim 23 , wherein the molten material atomized using the by-product off-gas becomes less oxidized than material that would have otherwise been atomized by air. 
     
     
         31 . A product from off-gas atomization that is less oxidized than the same product atomized through an air atomization plant.

Join the waitlist — get patent alerts

Track US2017297113A1 — get alerts on status changes and closely related new filings.

We store only your email — no account needed. See our privacy policy.