[0001] The present invention relates to a vacuum-suction degassing apparatus, in which gas-forming
               solute ingredients are removed or recovered from a melt, such as a molten metal, matte,
               or slag, through a porous member.
 
            [0002] Conventionally, the RH method, DH method, and other degassing methods are used to
               remove gas-forming solute ingredients from a molten metal. According to the RH or
               DH method, a large quantity of argon gas is blown into the melt, the surface of which
               is kept at a vacuum or at reduced pressure so that the partial pressure of the gas-forming
               ingredients is lowered, thereby removing these ingredients.
 
            [0003] Requiring the use of argon gas in large quantity, however, the conventional RH or
               DH degassing method entails high running cost. Since much argon gas is blown into
               the melt, moreover, the melt is liable to splash so that many metal drops adhere to
               the wall surface or some other parts of the apparatus, which requires troublesome
               removal work. To cope with this splashing of the melt, furthermore, the apparatus
               is inevitably increased in size, resulting in higher equipment cost.
 
            [0004] The object of the present invention is to provide a vacuum-suction degassing apparatus,
               in which gas-forming ingredients can be easily removed from a melt without using a
               large quantity of argon gas, so that the melt can be degassed at low cost by means
               of a simple apparatus.
 
            [0005] A vacuum-suction degassing apparatus according to the first invention, a vessel containing
               a melt; a porous member made of a porous material permeable to gas and impermeable
               to melts, a portion thereof being immersed in said melt in the vessel; and sucking
               means for sucking gas from said melt or gas produced by a reaction between said melt
               and said porous material through said partitioning member, in a manner such that the
               portion of said porous member which protrude over the surface of said melt is kept
               at a vacuum or at a reduced pressure.
 
            [0006] A vacuum-suction degassing apparatus according to the second invention, a vessel
               containging a melt; a cylindrical non-porous member; a porous member made of a porous
               material permeable to gas and impermeable to melts, being fitted into the lower portion
               of said non-porous member and immersed in said melt in said vessel; and sucking means
               for sucking gas from said melt or gas produced by a reaction between said melt and
               said porous material through said partitioning member, in a manner such that the inside
               of said non-porous member is kept at a vacuum or at a reduced pressure. The partitioning
               member is sucked by said sucking means, thereby the inside of the partitioning member
               being kept at a vacuum or at reduced pressure. Also, the melt is stirred by moving
               said partitioning member in said melt by said stirring means so that gas in the melt
               or gas produced by the reaction between the melt and the porous member can be moved
               to vacuum or reduced pressure space inside the partitioning member through said partitioning
               member made of a porous material with high efficiency. Also, the vacuum suction degassing
               apparatus according to the present invention does not have to use argon gas, so that
               its running cost is low and also it is possible to suppress generation of splashes
               and reduce deposition of base metal onto a wall surface of the apparatus. Thus, according
               to the present invention, it is possible to reduce the equipment cost as well as its
               running cost.
 
            [0007] According to the first invention, a portion of a porous member made of a porous material
               which allows permeation of gases but does not allow permeation of molten materials
               is immersed in a melt, and another portion of said porous member which protrudes above
               the surface of melt is put in vacuum or under reduced pressure. Gases of said melt
               or gases produced by reactions between said melt and said porous material are sucked
               through said porous member by sucking means.
 
            [0008] According to the second invention, a porous member is fitted into the lower portion
               of a cylindrical non-porous member and the porous member is immersed in said melt.
               Inside of said non-porous member is evacuated or depressurized, and gases in said
               melt or gases produced by reactions between said melt and said porous material are
               sucked through said porous member by sucking means.
 
            [0009] Thus, solute components in the melt, which produce a gas phase, can easily be moved
               to the vacuum or reduced pressure atmosphere.
 
            [0010] Different from the conventional degassing method where a large volume of argon gas
               is blown into, in this invention, argon gas is not blown into, or a small volume of
               argon gas only enough to stir the melt is blown, so that an amount of argon gas used
               can remarkably be reduced. Also, as the amount of argon gas is extremely low, generation
               of splashes is suppressed, and deposition of base metal on a wall surface of a device
               can be reduced. For this reason, according to the present invention, equipment cost
               can be reduced by minimizing size of the apparatus, and also running cost can remarkbly
               be reduced.
               
               
Fig. 1 is a diagram for illustrating the principle of the present invention,
               Fig. 2 is a schematic cross-sectional view showing a first embodiment of the invention,
               Fig. 3 is a schematic cross-sectional view showing second embodiment of the invention.
 
            [0011] First, description is made for a principle of this invention with reference to Fig,
               1. Partitioning member 1 is made of a porous material which is permeable to gas, but
               impermeable to melts, such as molten metal, molten matte, or molten slag. If melt
               2 is brought into contact with one side of porous member 1, and if the other side
               of member 1 is kept at a vacuum or at a reduced pressure 3, the pressure on the wall
               surface in contact with the melt drops without regard to the static pressure of melt
               2.
 
            [0012] Accordingly, those impurities or valuables in melt 2 which produce gaseous substances
               easily nucleate on the wall surface of porous member 1 to form gas 4, and resulting
               gas 4 permeates through member 1 and sucked into space 3 at vacuum or reduced pressure
               atmosphere so that the impurities or valuables are removed from the melt and recovered
               into space 3 at vacuum or reduced pressure atmosphere.
 
            [0013] The inventor hereof realized that gas-forming ingredients can be removed from the
               melt on the basis of the principle described above, and brought the present invention
               to completion.
 
            
            [0015] The impurities in the melt may react with the ingredients of the porous member, to
               form gases, and then they may be removed through the porous member.
 
            [0016] If the porous member is an oxide (M
XO
Y), carbon in the melt is removed in the form of a gas as follows:
               
               
 
               
                
            [0017] If the porous member contains carbon, moreover, oxygen in the melt is sucked and
               removed according to the following reaction formula.
               
               
 
               
                
            
            [0019] In this manner, the impurities, such as 
N, 
H, 
C, 
O, and 
S, and the valuable components are sucked and removed or recovered from the melt.
 
            [0020] According to the present invention, by adjusting content of components of the partitioning
               member which react with the impurities or valuable components in a melt, it is possible
               to control a reaction rate between the impurities or valuable components in the melt
               and components of the partitioning member.
 
            [0021] Note that a heating means may be added to heat a porous member or a melt by energizing
               the porous member or burying a resistance wire previously in the porous member and
               energizing the resistance wire, or by heating the melt from outside ( by means of,
               for instance, plasma heating), for the purpose to prevent the decrease of temperature
               of the melt due to heat emission to atmosphere or the vessel or the decrease of temperature
               of the melt which occurs when the porous member is immersed into the melt, or decrease
               of temperature of the melt due to an endothermic reaction between components of the
               porous member and the melt.
 
            [0022] Various materials may be used for porous member, including metal oxides or other
               metallic compounds (non-oxides), carbon and mixtures thereof and metal, such as Al₂O₃,
               MgO, CaO, SiO₂, Fe₂O₃, Fe₃O₄, Cr₂O₃, BN, Si₃N₄, SiC, C, etc.. Preferably, the material
               used should not react with the principal ingredient of melt 2 so that porous member
               in contact with melt 2 can be prevented from erosion loss and melt 2 can be kept clean.
 
            [0023] Also, a material which hardly gets wet with melts must be used for the partitioning
               member so that only gases can pass through the partitioning member but any melt can
               not pass through the partitioning member. Furthermore, it is preferable that a porosity
               of the partitioning member is not more than 40%.
 
            [0024] Furthermore, in order to prevent a melt from entering the vacuum system even if a
               melt goes into the immersed porous tube, it is preferable to allocate a filter with
               small pressure loss in an upper section of the immersed porous tube to solidify the
               invading melt for trapping it.
 
            [0025] The following is a description of a case in which the present invention is applied
               to the removal or recovery of gas-forming ingredients from a melt.
               
               
(1) First, the present invention can be applied to decarburization, denitrogenation,
                  and dehydrogenation processes for removing carbon, nitrogen, or hydrogen from molten
                  iron. 
                  When this method is applied to remove carbon from molten iron, the main component
                  of said partitioning member should be Al₂O₃ or MgO, and such a material as Fe₂O₃,
                  Fe₃O₄, MnO, and SiO₂ etc. should be mixed in as main oxidizing agents for carbon in
                  the molten iron. But if a compounding ratio of the main oxidizing agent is too high,
                  a melting point of the partitioning member goes down, or the mechanical strength thereof
                  becomes lower, and if carbon content in the molten iron is too low, oxygen content
                  in the molten iron goes up, so that a compounding ratio of the main oxidizing agent
                  must be decided according to the purpose and by referring to the phase diagram already
                  established.
                  On the other hand, if this method is applied to removal of nitrogen in molten iron,
                  a stable oxide such as CaO, Al₂O₃, or MgO should be used as said partitioning member.
                  Also, if this invention is applied to simultaneous removal of carbon and nitrogen
                  in molten iron, the compounding ratio of the oxidizing agent should be changed according
                  to target contents of carbon and nitrogen in the molten iron.
               (2) The invention can be also applied to a deoxygenation process for removing oxygen
                  from molten copper.
               (3) Further, the invention can be applied to a dehydrogenation process for removing
                  hydrogen from molten aluminum.
               (4) Furthermore, the invention can be applied to decarburization, and dehydrogenation
                  of molten silicon.
               (5) According to the present invention, zinc can be recovered from molten lead.
               (6) The invention can be also applied to a desulfurization/deoxygenation process for
                  removing sulfur and oxygen from molten copper matte.
               (7) Further, the invention can be applied to the recovery of valuable metals (As,
                  Sb, Bi, Se, Te, Pb, Cd, etc.) from molten copper matte or nickel matte.
               (8) Furthermore, the invention can be applied to the recovery of valuable metals (As,
                  Sb, Bi, Se, Te, Pb, Cd, Zn, etc.) from slag.
 
            [0026] Detailed description is made below for embodiments of this invention.
 
            [0027] Fig.2 is a schematic cross-sectional view showing a vacuum-suction degassing apparatus
               according to an embodiment of the present invention. Melt 2 is stored in vessel 5,
               and a lower half portion of porous member 6 is immersed in this molten material 2.
               Porous member 6 has a form of rod, and is made of a porous material having pores which
               is permeable to gases and impermeable to melts, such as molten metal, molten slag,
               and molten matte. Therefore, melt 2 do not pass through.
 
            [0028] Vessel 5 is placed in a decompression container (not shown), and inside of the decompression
               container is evacuated by the vacuum pump to maintain the inside in vacuum or under
               reduced pressure.
 
            [0029] In the vacuum-suction degassing apparatus thus constructed, although melt 2 does
               not permeate through porous member 6, but as gases contained in pores of porous member
               6 are released to inside of the decompression container, inside of pores of porous
               member 6 are evacuated or depressurized. Therefore, gases in melt 2 or gases produced
               by reactions between components of the porous member 6 and the melt 2 pass through
               the pores of porous member 6, and are released into vacuum or reduced pressure atmosphere
               in the decompression container. And, the gases are sucked by the vacuum pump and removed
               from inside of the decompression container.
 
            [0030] Fig.3 is a schematic cross-sectional view showing a vacuum suction degassing apparatus
               according to an embodiment of the second invention in this application.
 
            [0031] Melt 2 is stored in vessel 5. Porous member 6a has a form of rod, and is fitted into
               the lower portion of cylindrical non-porous member 8 in a liquid-sealing manner. Porous
               member 6a is made of a porous material having pores which gases can permeate through
               but melt 2, such as molten metal, molten slag, or molten matte can not enter and permeate
               through. Also, non-porous member 8 is made of a non-porous material which gases can
               not permeate through, and is linked to a vacuum pump (not shown).
 
            [0032] In the vacuum suction degassing apparatus having the configuration as described above,
               when inside of non-porous member 8 is evacuated or depressurized, inside of pores
               of porous member 6 is evacuated or depressurized. Therefore, gas-forming components
               in molten 2 are exhausted through the pores of porous member 6a into inside of non-porous
               member 8. And, the gas-forming components are sucked by the vacuum pump and recovered
               or exhausted.
 
            [0033] Also in this embodiment, porous member 6a has only to be immersed in molten material
               2, and even if depth of a melt bath is small, degasification of molten materials can
               be performed.