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Operation Conditions of Iron Ore Sintering Process Combined with
                                                                                 Oxygen Enrichment and Exhaust Gas Recirculation   System
                                             Hidetoshi NODA, Noboru SAKAMOTO,
                                                                            Koichi ICHIKAWA,
                                                                                           Satoshi MACHIDAand Shoichi ROKUGAWA




Synopsis        : An        advanced                sintering                process                   was     proposed                     on      the     basis        of mathematical                           models            and         was          verified             by        pot        tests          . This               process              is characterized

                   by      combining                    exhaust              gas        recirculation                           with        oxygen            enrichment               in    order             to      meet        the          future            environmental                          regulations                           as     well            as to        keep              the

                   productivity.                   The         main          results                  obtained                 are     as follows                 :

                         ( 1 )         The        models               clarify              that        the        introduction                     of the            oxygen       enrichment                       in the         first        half         and        the    exhaust                   gas            recirculation                           in    the        latter         half

                   of the          sintering             process              gives               better           coke          combustion                   rate      and      sinter      quality                than         other          possible               alignments                   .

                         ( 2 ) The                models              also         show               that     with             the    constant O2                    quantity         provided,                   the     concentrated O2                              supply               in a short                      time           helps          reduce                the      sinter-

                   ing      time       because                 of the        balance                    between                 combustion                   rate       and      cooling           rate        of the           sinter          bed      .

                         ( 3 ) The                pot     test         results              were             in good             agreement                  with        the      models.           The          suitable O2                     content                of 28•`30%                        and O2                   injection                time            of 2•`3              min

                   were       consequently                       obtained.

                         ( 4 )       The          proposed                 process                    did     not        cause          the      deterioration                   of sinter          qualities                 such         as reducibility                         although                       the        change                 in O2            content              would

                   affect        the    occurrence                      of hematite/magnetite                                          phase          in sinter           microstructures                      .

Key words       : sintering             process;               oxygen                  enrichment;                       exhaust              gas     recirculation;                 iron         are        sinter;          productivity;                       sinter       qualities;                     coke                combustion;                         mathematical

                   model.




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                                                                                                                                                                                                                                                                                                                                                     ,Ž_             ‘f    •x ‰» ‚Æ ”r

  •Ä Œ‹ ƒv         ƒ• ƒZ ƒX ‚É ‚¨                   ‚¯         ‚é ”r         ƒK ƒX •z                   ŠÂ •û        –@ ‚É ‚ ‚¢                    ‚Ä ‚Í ŠD ’J                              ƒK ƒX •z               ŠÂ ‚Ì          “¯      Žž ‘g •‡               ‚í    ‚¹    ƒv ƒ• ƒZ ƒX ‚ª •¶ ŽY –Ê,ŠÂ                                                             ‹«    –Ê ‚Ì          •”     ‰Û




   •½•¬ 12”N 8ŒŽ 31“ú Žó •t•@ •½ •¬ 13”N 1ŒŽ 30“ú Žó —• (Received on Aug. 31, 2000; Accepted on Jan. 30, 2001)
* NKK‘• •‡ •Þ—¿Z•p Œ¤ •Š (Materials & Processing Research Center, NKK Corp., 1 Kokan-cho Fukuyama 721-8510)
                 ‹       ‹†
*2NKK‘• •‡•Þ—¿Z•p Œ¤ •Š(Œ»:•|
                 ‹       ‹†              ŠÇƒhƒ‰ ƒ€(Š”)) (Materials & Processing Research Center,NKK Corp., now Kokan Drum Co., Ltd.)



                                                                                                                                                                                 101
Fig.   1. Mass   transfer   model   in a quasi-particle.




102
Fig.   2. Temperature   distribution   in sintering   bed evaluated      by the simulation      model.




                                                      Case      1 : Oxygen   and exhaust     gas are mixed before     injection




                                                       Case 2: Oxygen injection before exhaust gas recycling




                                                       Case 3: Exhaust       gas recycling     before oxygen    injection




                                                         Fig.    3. Typical sintering  processes  supposing             oxygen      en-
                                                                    richment  and exhaust gas recirculation.




                                                      ‘f •x ‰»”Z “x ‚ð26vol%(‘å              ‹C ‘g •¬ ‚æ ‚è+5vol%)‚Æ              •Ý ’è ‚µ

                                                      ‚½ •B ‚È ‚¨,•ã,’†,‰º             ‘w ‚Ì ‰· “x,”r     ƒKƒX‘g •¬ “™‚Ì ŒvŽZ ƒ| ƒC

                                                      ƒ“ ƒg‚Í Še •X •ã –Ê ‚æ ‚è1/3,2/3,3/3(Œ´              —¿‘w ‚Æ•° •~ ‚Ì ‹« ŠE –Ê)

                                                      ‚Æ ‚µ ‚½ •B

                                                         Fig.4‚É      ‚± ‚ê ‚ç3ƒP     •[ ƒX ‚Ì ƒv ƒ• ƒZ ƒX ƒV ƒ~ ƒ…ƒŒ•[ ƒV ƒ‡ ƒ“ Œ‹

                                                      ‰Ê‚𠎦 ‚· •BFig.4‚Ì          ƒV ƒ~ ƒ…ƒŒ•[ ƒV ƒ‡ ƒ“ Œ‹ ‰Ê‚æ ‚è,ƒx           ƒb ƒhŠe

                                                      ‘w ‚Ì ƒq •[    ƒgƒp ƒ^ •[ ƒ“ ‚© ‚ç3ƒP     •[ ƒX‚Ì –â ‚Å Œ°’˜ ‚È •· ‚Í Œ©‚ç ‚ê

                                                      ‚È ‚¢ ‚ª,•²       ƒR •[ ƒNƒX‚Ì ”R •Ä ‘¬ “x ‚É ‚Í •· ‚ª ”F ‚ß ‚ç ‚ê ‚é •B ‚· ‚È

                                                      ‚í ‚¿,Šî      •€ ‚Æ‚È ‚é ƒP •[ ƒX1‚É ”ä ‚×,ƒP          •[ ƒX2‚Ì       •² ƒR •[ ƒNƒX

                                                      ”R •Ä ‘¬ “x ‚Í ‘¬ ‚-,Ž_        ‘f •x ‰»400s‚Ì      Šú ŠÔ‚É ‰º ‘w •” ‚Ì •² ƒR •[

                                                      ƒNƒX ‚Ü‚Å Š® ‘S ‚É ”R •Ä ‚ª Š® —¹‚· ‚é •B ‚± ‚Ì ‚½ ‚ß,Œã              ”¼ ‚É Ž_ ‘f ”Z

                                                      “x ‚Ì ’á ‚¢ ”r ƒKƒX ‚ð •• ‚« •ž ‚ñ ‚Å ‚à •² ƒR •[ ƒNƒX‚Ì ”R •Ä ‚Ì ’x ‰„‚É

                                                      ‚Í ŽŠ ‚ç ‚È ‚¢ •B ‚± ‚ê ‚É ‘Î ‚µ,ƒP        •[ ƒX3‚Å ‚Í Œã”¼ ‚Ì Ž_ ‘f •x ‰»‚É

                                                      ‚æ ‚Á‚Ä ‰º‘w •” ‚Ì •² ƒR •[ ƒNƒX‚Ì ”R •Ä ‘¬ “x ‚Í ƒP •[ ƒX1,2‚É                ”ä Šr



                                               103
Fig. 4. Simulation results showing influence of injection gas conditions on the sintering process.




                                               104
Fig. 5. Experimental   apparatus   for the sintering   test.


Table   1. Raw material conditions   of pot tests     and target
           CaO/SiO2 and SiO2 of sinter products.


                                                                         Fig.   6. Effect of O, content   on characteristics      of the sinter-
                                                                                   ing process.




                                                                         Fig.   7. Influence of O2 content    on JIS-RI,       RDI and FeO of
                                                                                   sinter products.




                                                                   105
Fig.    10. Mineral    composition                and porosity   of the            sinter
                                                                                                                        structures  measured                by an image analyzer.




   (a) Base(02=21vol%)                    (b) 02=35vo1%             (c) 02=11vo1%
  Fig. 8. Effect of 0, content in injection gas on the exhaust
          gas composition.




                                                                                                            Fig.    11. Effect        of 0, content on             Flame        Front   Speed       ob-
                                                                                                                        tained        from the pot tests.




                                                                                                       4.      •l   Ž@




                                                                                                       4•E1         Ž_ ‘f ”Z “x ‚Ì •²      ƒR •[ ƒN ƒX ”R •Ä •« ‚É ‹y ‚Ú ‚· ‰e‹¿

                                                                                                            Ž_ ‘f •x ‰» Žž ‚Ì •Ä Œ‹ ”r ƒK ƒX ‚Ì ‘g •¬ •ª •Í Œ‹ ‰Ê(•Ä                     Œ‹ ŠJ Žn ‚© ‚ç

                                                                                                       •I    —¹ ‚Ü ‚Å ‚Ì      •½ ‹Ï ‘g •¬)‚ðFig.10‚É               Ž¦ ‚· •B ”r      ƒK ƒX ’†co”Z          “x

                                                                                                       ‚Í Ž_ ‘f ”Z “x ‚É ‚æ ‚ç ‚¸ ‚Ù ‚Ú ˆê ’è ‚Å ‚                 ‚é ‚ª,”r        ƒK ƒX ’†CO2‚¨          ‚æ

                (a) Base(02=21vo1%)         (b) 02=35vo1%     (c) 02=11vo1%                            ‚Ñ Ž_ ‘f(02)”Z           “x ‚Í ‹¤ ‚É ‘• ‰Á ‚µ ‚Ä ‚¢ ‚é •B ‚½ ‚¾ ‚µ ‚» ‚Ì ‘• ‰Á •‡
                                                                                                                                                                                     Š„

                Fig.     9. Microstructure        of sinter    products.                               ‚Í,02‚É           ”ä Šr ‚µCO2‚Í           ”÷ ‘• ‚É —¯ ‚Ü ‚Á ‚Ä ‚¢ ‚é •B •Å ‹ß ‚Ì              Ž– ‘O

                                                                                                       •ˆ —• ‚ð ‹- ‰» ‚µ ‚½ •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚Å ‚Í,•Ä                         Œ‹ ƒx ƒb ƒh “à ‚Å ‚Ì •²

‚è “¾ ‚ç ‚ê ‚½ Še •Ä Œ‹ ƒP •[ ƒL ‚Ì          ’† ‘w •” ‚æ ‚è •Ì Žæ ‚µ ‚½ •BFig.8‚É                      ƒR •[ ƒN ƒX ‚Í         ’P “Æ ‚É ‘¶ •Ý ‚·      ‚é ‚± ‚Æ ‚Í •- ‚È ‚-,‚»             ‚Ì   ‘å •” •ª    ‚Í

‚× •[ ƒX(‘å      ‹C ’† ’Ê •í •Ä Œ‹:ƒP           •[ ƒX1‚É      ŠY “– ‚µ,Ž_      ‘f •x ‰» ”r             Fig.1‚É        Ž¦ ‚·     ‚æ ‚¤ ‚É ‹[    Ž——± Žq “à •” ‚É ‘¶ •Ý ‚·            ‚é •B ‚± ‚Ì     ‚½ ‚ß,

ƒK ƒX •z ŠÂ ‚È ‚µ)‚¨             ‚æ ‚Ñ Ž_ ‘f ”Z “x –ñ35volo/•B,llvo1%•ð               Œ•F              ‹[ Ž——± Žq “à •²            ƒR •[ ƒN ƒX ‚Í ’… ‰Î ’¼ Œã ‚É ‚Í ‰»Šw ”½ ‰ž—¥‘¬ ‚Æ‹[ Ž—

(ƒP •[ ƒX2,3‚É          ŠY “–)‚Å        ‚Ì •Ä •¬ ŽŽ Œ± ‚Å “¾ ‚ç ‚ê ‚½ •Ä Œ‹ •z ‚Ì           ƒ~         —±Žq ŠO • –Ê ‹« –Œ “à Šg ŽU —¥‘¬ ‚É ‚æ ‚Á ‚Ä ”R •Ä ‚ª •i •s ‚·                        ‚é ‚ª,’†

ƒN ƒ• ‘g •D ŽÊ •^ ‚𠎦 ‚·        •B ‚Ü ‚½,“¯     ˆê •E —¿ ‚Å ‚Ì ‰æ‘œ •ˆ —• ‘• ’u
                                                      ŽŽ                                    ‚É         Šú ˆÈ •~ ‚Í ‹[ Ž——±Žq “à •”              ‚ð Ž_ ‘f ‚ª Šg ŽU ‚·          ‚é Šg ŽU —¥‘¬ ‚É ˆÚ •s ‚·

‚æ ‚é ‘g •D ’è —Ê‚à ŽÀ Ž{ ‚µ,‚±             ‚Ì Œ‹ ‰Ê‚ðFig.9‚É        Ž¦ ‚·    •B                       ‚é •B ‚± ‚Ì       ‚½ ‚ß,Ž_       ‘f •x ‰»‚É ‚æ ‚è Ž_ ‘f ”Z “x ‚ð             ƒq‚° ‚Ä ‚à • •ª ‚É

   Fig.8‚æ      ‚è,Ž_       ‘f    ”Z “x ‚ª35volo/•B    ‚Ì   •ð Œ• ‰º ‚Å •Ä •¬      ‚µ ‚½(b)            ”R •Ä ‚¹      ‚¸,Fig.10‚É          Ž¦ ‚· ”r ƒK ƒX ’† ‚Ì Ž_ ‘f ”Z “x ‚Ì•ã               •¸ ‚É ŽŠ ‚Á

‚Å ‚Í ƒx •[ ƒX(a)‚É        ”ä ‚× ƒw ƒ} ƒ^ ƒC ƒg ‘Š ‚ª ‘• ‰Á ‚µ ‚Ä ‚¢ ‚é ‚ª,”ì                          ‚½ ‚à ‚Ì      ‚Æ •„ ’è ‚³ ‚ê ‚é •B ‚µ ‚© ‚µ Ž_ ‘f ”Z “x ‚Ì•ã                •¸ ‚É ‚æ ‚è,”r         ƒK

‘å ‰» ‚µ ‚½2ŽŸ         ƒw ƒ} ƒ^ ƒC ƒg—± Žq ‚Í     ‚   ‚Ü ‚è Œ©‚ç ‚ê ‚¸ ‰ß —n—Z‘g •D                    ƒX ’† ‚ÌCO2‚à            •ã •¸    ‚µ ‚Ä ‚¨   ‚è,•²       ƒR •[ ƒN ƒX ‚Ì ”R •Ä ‘¬ “x Œü•ã ‚Ö

‚à •- ‚È ‚¢ •B(c)‚Å        ‚Í Ž_ ‘f ”Z “x ‚ª ’á ‰º ‚µ ‘g •D ’† ‚Ì Ž_ ‰» “S ‚ª ƒw                       ‚Ì Šñ —^ ‚Í •         •ª ”F ‚ß ‚ç ‚ê ‚é •BFig.11‚É           Ž_ ‘f ”Z “x ‚ÆFFS(Flame

ƒ} ƒ^ ƒC ƒg ‚æ ‚è ƒ} ƒO ƒl ƒ^ ƒC ƒg ‚É •Ï ‰» ‚µ ‚Ä ‚à,‚»               ‚Ì    ƒ} ƒO ƒl ƒ^ ƒC            FrontSpeed:•Ä                Œ‹ ƒx ƒb ƒh •‚ ‚³ ‚ð •Ä Œ‹ Š® —¹ Žž ŠÔ ‚·             ‚È ‚í ‚¿,“_

 ƒg—± Žq‚Í •‚ ƒV ƒŠ ƒJ •Ä Œ‹ •z ’† ‚É Œ©‚ç ‚ê ‚é ‘e ‘å2ŽŸ                    ƒw ƒ} ƒ^ ƒC ƒg            ‰Î ‚© ‚ç ƒ| ƒb ƒg ƒO ƒŒ•[              ƒg˜F ’¼ ‰º ‚Ì     ”r ƒK ƒX •Å •‚ ‰· “x “ž ’B ‚Ü ‚Å ‚Ì

‚© ‚ç •Ï ‰» ‚µ ‚½2ŽŸ         ƒ} ƒO ƒl ƒ^ ƒC ƒg23)‚É ”ä Šr ‚µ —± Œa ‚Í •¬ ‚³ ‚¢ ‚Ì                      Žž ŠÔ ‚Å •œ ‚µ ‚½ ’l ‚Å,‰Î               ‰Š ‘O –Ê ‚Ì •½ ‹Ï ˆÚ “® ‘¬ “x ‚Æ ’è ‹`)‚Ì                 ŠÖ

‚ª “Á ’¥ ‚Å ‚     ‚é •A,                                                                               ŒW‚𠎦 ‚· •B ‚± ‚ê ‚æ ‚è,Ž_                  ‘f     ”Z “x ‚ª ‘• ‰Á‚·       ‚é ‚É ‚µ ‚½ ‚ª ‚Á ‚Ä

                                                                                                       FFS‚Í        ‘• ‰Á ‚µ ‚Ä ‚¢ ‚é ‚± ‚Æ ‚ª •ª ‚© ‚é •B ‚± ‚ê ‚Í Ž_ ‘f •x ‰»‚É ‚æ ‚è,




                                                                                                 106
Fig.   12.   Effect    of   02   content   on   the   holding   time   above
             1100•Ž.




                                                                                     Fig.   13.   Comparison   of simulation   results on coke com-
                                                                                                  bustion time under a constant    oxygen enrichment
                                                                                                  condition.




                                                                               107
Fig. 14. Pot test conditions under a constant amount of in-
         jecting oxygen.




Fig.   15.   Influence     of oxygen enrichment     conditions   on the
             sintering   time and productivity    at pot test.




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Oxygen in sintering

  • 1. Operation Conditions of Iron Ore Sintering Process Combined with Oxygen Enrichment and Exhaust Gas Recirculation System Hidetoshi NODA, Noboru SAKAMOTO, Koichi ICHIKAWA, Satoshi MACHIDAand Shoichi ROKUGAWA Synopsis : An advanced sintering process was proposed on the basis of mathematical models and was verified by pot tests . This process is characterized by combining exhaust gas recirculation with oxygen enrichment in order to meet the future environmental regulations as well as to keep the productivity. The main results obtained are as follows : ( 1 ) The models clarify that the introduction of the oxygen enrichment in the first half and the exhaust gas recirculation in the latter half of the sintering process gives better coke combustion rate and sinter quality than other possible alignments . ( 2 ) The models also show that with the constant O2 quantity provided, the concentrated O2 supply in a short time helps reduce the sinter- ing time because of the balance between combustion rate and cooling rate of the sinter bed . ( 3 ) The pot test results were in good agreement with the models. The suitable O2 content of 28•`30% and O2 injection time of 2•`3 min were consequently obtained. ( 4 ) The proposed process did not cause the deterioration of sinter qualities such as reducibility although the change in O2 content would affect the occurrence of hematite/magnetite phase in sinter microstructures . Key words : sintering process; oxygen enrichment; exhaust gas recirculation; iron are sinter; productivity; sinter qualities; coke combustion; mathematical model. 1.•@ •• Œ¾ ‚ç7),ŽR “c ‚ç4)‚ª “ç ŽŽ Œ± ‚É ‚æ ‚è •Ú •× ‚È ŒŸ “¢ ‚ð •s ‚Á ‚Ä ‚¨ ‚è, ƒO ƒŒ •[ ƒg Œã ”¼ •” ‚Ì ”r •o ‘z ’è ƒK ƒX ‚ð •Ä Œ‹ ‹@ ‘O ”¼ •” ‚Ö •z ŠÂ ‚³ ‚¹ •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚Í ‘å ‹C ’† ‚Ö ‚Ì ”r •o ƒK ƒX —Ê ‚ª ”œ ‘å ‚Å ‚ ‚é ‚± ‚Æ ‚½ •ê •‡,•Ä Œ‹ Žž ŠÔ ‚Í ‰„ ’· ‚· ‚é ‚ª,•¬ •i •à —¯ ‚ª Œü •ã ‚· ‚é ‚½ ‚ß ‚© ‚ç,‰¢ •B Še •‘ ‚Å ‚Í Œn ŠO ”r •o ƒK ƒX •í Œ¸ ‚ð –Ú “I ‚Æ ‚µ ‚½ ”r ƒK ƒX •¶ ŽY •« ‚Í ’Ê •í •Ä Œ‹ –@ ‚Æ •Ï ‰» ‚ª ‚È ‚¢ ‚± ‚Æ,‚Ü ‚½,‹z ˆø ƒK ƒX ’† •z ŠÂ ƒv ƒ• ƒZ ƒX1,2)‚ª ŠJ ”- ‚³ ‚ê ‚Ä ‚¢ ‚é •B •‘ “à ‚É ‚¨ ‚¢ ‚Ä ‚à ŒË ”¨3 Ž_ ‘f ”Z “x ‚Ì ŒÀ ŠE ‚Í16•`17vol%‚Å ‚ ‚é ‚± ‚Æ ‚ð Žw “E ‚µ ‚Ä ‚¢ ‚é •B •† •Ä Œ‹ ‹@3)‚ð Žn ‚ß,”r ƒK ƒX •z ŠÂ •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚ª Šù ‚É “± “ü ŽÀ ‚³ ‚ç ‚É •z ŠÂ •û Ž® ‚É ‚ ‚¢ ‚Ä ‚Í,ˆÀ –{ ‚ç8-10)‚ª Ž_ ‘f ”Z “x ‚Ì ’á ‚¢ Ž{ ‚³ ‚ê ‚Ä ‚¢ ‚é •B ‚µ ‚© ‚µ ”r ƒK ƒX •z ŠÂ ƒv ƒ• ƒZ ƒX ‚Å ‚Í Ž_ ‘f ”Z “x ‚Ì ƒO ƒŒ •[ ƒg ‘O ”¼ •” ‚Ì ”r •o ƒK ƒX ‚ð Œã ”¼ •” ‚É •z ŠÂ —˜ —p ‚· ‚é ‚¢ ‚í ‚ä ’á ‰º ‚É ‚æ ‚è ‹[ Ž— —± Žq “à •² ƒR •[ ƒN ƒX ‚Ì ”R •Ä ‘¬ “x ‚ª ’x ‚ê,•¶ ŽY ‚é,‘O ”¼ ‘å ‹C/Œã ”¼ ”r ƒK ƒX •z ŠÂ •Ä Œ‹ ‚É ‚¨ ‚¢ ‚Ä ‚à,’Ê •í ‚Ì •Ä •« ‚Ì ’á ‰º ‚ª ‹N ‚± ‚é ‚± ‚Æ ‚ª ”F ‚ß ‚ç ‚ê ‚Ä ‚¢ ‚é4,5)•B ˆê •û,•‚ ˜F Œ‹ –@ ‚Æ •Ï ‚í ‚ç ‚È ‚¢ •i Ž¿ ‚ª “¾ ‚ç ‚ê,”r •o ƒK ƒX —Ê ‚à –ñ40vol% Œ´ —¿ ‚Æ ‚µ ‚Ä “K ‚· ‚é •Ä Œ‹ •z ‚Ì ”z •‡ —¦ ˆÛ Ž• ‚Ì ‚½ ‚ß ‚É ‚Í •Ä Œ‹ ‹@ ‚Ì •í Œ¸ ‚Å ‚« ‚é ‰Â” •« ‚ª ‚ ‚é ‚± ‚Æ ‚ð •ñ •• ‚µ ‚Ä ‚¢ ‚é •B •¶ ŽY —¦ ˆÛ Ž• ‚ª •K —v ‚Å ‚ ‚è,‚» ‚Ì ‘Î •ô ‚Ì ˆê ‚ ‚É Ž_ ‘f •x ‰» ƒv ƒ• ‚± ‚± ‚Å,•Ä Œ‹ Žž ŠÔ ‚Í “ç ŽŽ Œ± ‚É ‚¨ ‚¢ ‚Ä ‚Í “_ ‰Î ‚æ ‚è ”r ƒK ƒX ‚ª ƒZ ƒX ‚ª ‚ ‚° ‚ç ‚ê ‚é6)•B •Å •‚ ‰· “x ‚𠎦 ‚· “_(BTP:Burn Through Point)‚Ü ‚Å ‚Ì Žž ŠÔ ‚ð ‚» ‚± ‚Å –{ Œ¤ ‹† ‚Å ‚Í,”r ƒK ƒX •z ŠÂ ‚Æ Ž_ ‘f •x ‰» ‚Ì —¼ŽÒ ‚ð ‘g •‡ Žw ‚· ‚Ì ‚ª ˆê ”Ê “I ‚Å,•² ƒR •[ ƒN ƒX(ƒJ •[ ƒ{ ƒ“)‚Ì ”R •Ä ‚ª ‚Ù ‚Ú ‚í ‚¹ ‚½ •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚Ì ‰Â” •« ‚¨ ‚æ ‚Ñ “K •³ ‚È ‘€ ‹Æ •ð Œ• ‚ð –¾ ‚ç Š® —¹ ‚µ ‚Ä ‚¢ ‚é •ó ‘Ô ‚Æ •l ‚¦ ‚ç ‚ê ‚é •B ŽÀ ‹@ ƒv ƒ• ƒZ ƒX ‚Ì •ê •‡,Šî ‚© ‚Æ ‚µ,•‚ •¶ ŽY —¦ ‰º ‚Å Œn ŠO ”r •o ƒK ƒX —Ê ‚ð —} •§ ‰Â ” ‚È ŽŸ •¢ ‘ã –{ “I ‚É ‚ÍBTP‚ª ‚Ù ‚Ú,•Ä Œ‹ ‹@ ‚Ì ‹@ ’· •û Œü ‚Å92%‚Ì ˆÊ ’u ‚Æ •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚ð ’ñ Œ¾ ‚· ‚é •B ‚È ‚Á ‚Ä ‚¨ ‚è,‚± ‚Ì Žž “_ ‚Å ‚Í ƒJ •[ ƒ{ ƒ“ ”R •Ä ‚ª Š® —¹ ‚µ ‚Ä ‚¢ ‚é ‚Æ •„ Ž@ ‚³ ‚ê,‚± ‚Ì •ó ‘Ô ‚ð •Ä Œ‹ Š® —¹,‚· ‚È ‚í ‚¿,“_ ‰Î ‚© ‚ç ‚± ‚Ì 2.•@ Ž_ ‘f •x ‰» ”r ƒK ƒX •z ŠÂ •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚Ì ŒŸ “¢ ŠÔ ‚Ì Žž ŠÔ ‚ð •Ä Œ‹ Žž ŠÔ ‚Æ ’è ‹` ‚· ‚ê ‚Î •¶ ŽY •« “™ ‚Ö ‚Ì ‰e ‹¿ Œø ‰Ê ‚É ‘Î ‚µ ‚Ä ‚Í,—¼ ŽÒ ‚Í “¯ “™ ‚É •] ‰¿ ‚Å ‚« ‚é ‚à ‚Ì ‚Æ •l ‚¦ ‚ç ‚ê ‚é •B 2•E1•@ Ž_ ‘f •x ‰» ”r ƒK ƒX •z ŠÂ ƒv ƒ• ƒZ ƒX ‚Ì •l ‚¦ •û ‚± ‚ê ‚ç ‚Ì ’m Œ© ‚¨ ‚æ ‚Ñ •¶ ŽY •« ‚ð •l —¶ ‚· ‚é ‚Æ ,Ž_ ‘f •x ‰» ‚Æ ”r •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚É ‚¨ ‚¯ ‚é ”r ƒK ƒX •z ŠÂ •û –@ ‚É ‚ ‚¢ ‚Ä ‚Í ŠD ’J ƒK ƒX •z ŠÂ ‚Ì “¯ Žž ‘g •‡ ‚í ‚¹ ƒv ƒ• ƒZ ƒX ‚ª •¶ ŽY –Ê,ŠÂ ‹« –Ê ‚Ì •” ‰Û •½•¬ 12”N 8ŒŽ 31“ú Žó •t•@ •½ •¬ 13”N 1ŒŽ 30“ú Žó —• (Received on Aug. 31, 2000; Accepted on Jan. 30, 2001) * NKK‘• •‡ •Þ—¿Z•p Œ¤ •Š (Materials & Processing Research Center, NKK Corp., 1 Kokan-cho Fukuyama 721-8510) ‹ ‹† *2NKK‘• •‡•Þ—¿Z•p Œ¤ •Š(Œ»:•| ‹ ‹† ŠÇƒhƒ‰ ƒ€(Š”)) (Materials & Processing Research Center,NKK Corp., now Kokan Drum Co., Ltd.) 101
  • 2. Fig. 1. Mass transfer model in a quasi-particle. 102
  • 3. Fig. 2. Temperature distribution in sintering bed evaluated by the simulation model. Case 1 : Oxygen and exhaust gas are mixed before injection Case 2: Oxygen injection before exhaust gas recycling Case 3: Exhaust gas recycling before oxygen injection Fig. 3. Typical sintering processes supposing oxygen en- richment and exhaust gas recirculation. ‘f •x ‰»”Z “x ‚ð26vol%(‘å ‹C ‘g •¬ ‚æ ‚è+5vol%)‚Æ •Ý ’è ‚µ ‚½ •B ‚È ‚¨,•ã,’†,‰º ‘w ‚Ì ‰· “x,”r ƒKƒX‘g •¬ “™‚Ì ŒvŽZ ƒ| ƒC ƒ“ ƒg‚Í Še •X •ã –Ê ‚æ ‚è1/3,2/3,3/3(Œ´ —¿‘w ‚Æ•° •~ ‚Ì ‹« ŠE –Ê) ‚Æ ‚µ ‚½ •B Fig.4‚É ‚± ‚ê ‚ç3ƒP •[ ƒX ‚Ì ƒv ƒ• ƒZ ƒX ƒV ƒ~ ƒ…ƒŒ•[ ƒV ƒ‡ ƒ“ Œ‹ ‰Ê‚𠎦 ‚· •BFig.4‚Ì ƒV ƒ~ ƒ…ƒŒ•[ ƒV ƒ‡ ƒ“ Œ‹ ‰Ê‚æ ‚è,ƒx ƒb ƒhŠe ‘w ‚Ì ƒq •[ ƒgƒp ƒ^ •[ ƒ“ ‚© ‚ç3ƒP •[ ƒX‚Ì –â ‚Å Œ°’˜ ‚È •· ‚Í Œ©‚ç ‚ê ‚È ‚¢ ‚ª,•² ƒR •[ ƒNƒX‚Ì ”R •Ä ‘¬ “x ‚É ‚Í •· ‚ª ”F ‚ß ‚ç ‚ê ‚é •B ‚· ‚È ‚í ‚¿,Šî •€ ‚Æ‚È ‚é ƒP •[ ƒX1‚É ”ä ‚×,ƒP •[ ƒX2‚Ì •² ƒR •[ ƒNƒX ”R •Ä ‘¬ “x ‚Í ‘¬ ‚-,Ž_ ‘f •x ‰»400s‚Ì Šú ŠÔ‚É ‰º ‘w •” ‚Ì •² ƒR •[ ƒNƒX ‚Ü‚Å Š® ‘S ‚É ”R •Ä ‚ª Š® —¹‚· ‚é •B ‚± ‚Ì ‚½ ‚ß,Œã ”¼ ‚É Ž_ ‘f ”Z “x ‚Ì ’á ‚¢ ”r ƒKƒX ‚ð •• ‚« •ž ‚ñ ‚Å ‚à •² ƒR •[ ƒNƒX‚Ì ”R •Ä ‚Ì ’x ‰„‚É ‚Í ŽŠ ‚ç ‚È ‚¢ •B ‚± ‚ê ‚É ‘Î ‚µ,ƒP •[ ƒX3‚Å ‚Í Œã”¼ ‚Ì Ž_ ‘f •x ‰»‚É ‚æ ‚Á‚Ä ‰º‘w •” ‚Ì •² ƒR •[ ƒNƒX‚Ì ”R •Ä ‘¬ “x ‚Í ƒP •[ ƒX1,2‚É ”ä Šr 103
  • 4. Fig. 4. Simulation results showing influence of injection gas conditions on the sintering process. 104
  • 5. Fig. 5. Experimental apparatus for the sintering test. Table 1. Raw material conditions of pot tests and target CaO/SiO2 and SiO2 of sinter products. Fig. 6. Effect of O, content on characteristics of the sinter- ing process. Fig. 7. Influence of O2 content on JIS-RI, RDI and FeO of sinter products. 105
  • 6. Fig. 10. Mineral composition and porosity of the sinter structures measured by an image analyzer. (a) Base(02=21vol%) (b) 02=35vo1% (c) 02=11vo1% Fig. 8. Effect of 0, content in injection gas on the exhaust gas composition. Fig. 11. Effect of 0, content on Flame Front Speed ob- tained from the pot tests. 4. •l Ž@ 4•E1 Ž_ ‘f ”Z “x ‚Ì •² ƒR •[ ƒN ƒX ”R •Ä •« ‚É ‹y ‚Ú ‚· ‰e‹¿ Ž_ ‘f •x ‰» Žž ‚Ì •Ä Œ‹ ”r ƒK ƒX ‚Ì ‘g •¬ •ª •Í Œ‹ ‰Ê(•Ä Œ‹ ŠJ Žn ‚© ‚ç •I —¹ ‚Ü ‚Å ‚Ì •½ ‹Ï ‘g •¬)‚ðFig.10‚É Ž¦ ‚· •B ”r ƒK ƒX ’†co”Z “x ‚Í Ž_ ‘f ”Z “x ‚É ‚æ ‚ç ‚¸ ‚Ù ‚Ú ˆê ’è ‚Å ‚ ‚é ‚ª,”r ƒK ƒX ’†CO2‚¨ ‚æ (a) Base(02=21vo1%) (b) 02=35vo1% (c) 02=11vo1% ‚Ñ Ž_ ‘f(02)”Z “x ‚Í ‹¤ ‚É ‘• ‰Á ‚µ ‚Ä ‚¢ ‚é •B ‚½ ‚¾ ‚µ ‚» ‚Ì ‘• ‰Á •‡ Š„ Fig. 9. Microstructure of sinter products. ‚Í,02‚É ”ä Šr ‚µCO2‚Í ”÷ ‘• ‚É —¯ ‚Ü ‚Á ‚Ä ‚¢ ‚é •B •Å ‹ß ‚Ì Ž– ‘O •ˆ —• ‚ð ‹- ‰» ‚µ ‚½ •Ä Œ‹ ƒv ƒ• ƒZ ƒX ‚Å ‚Í,•Ä Œ‹ ƒx ƒb ƒh “à ‚Å ‚Ì •² ‚è “¾ ‚ç ‚ê ‚½ Še •Ä Œ‹ ƒP •[ ƒL ‚Ì ’† ‘w •” ‚æ ‚è •Ì Žæ ‚µ ‚½ •BFig.8‚É ƒR •[ ƒN ƒX ‚Í ’P “Æ ‚É ‘¶ •Ý ‚· ‚é ‚± ‚Æ ‚Í •- ‚È ‚-,‚» ‚Ì ‘å •” •ª ‚Í ‚× •[ ƒX(‘å ‹C ’† ’Ê •í •Ä Œ‹:ƒP •[ ƒX1‚É ŠY “– ‚µ,Ž_ ‘f •x ‰» ”r Fig.1‚É Ž¦ ‚· ‚æ ‚¤ ‚É ‹[ Ž——± Žq “à •” ‚É ‘¶ •Ý ‚· ‚é •B ‚± ‚Ì ‚½ ‚ß, ƒK ƒX •z ŠÂ ‚È ‚µ)‚¨ ‚æ ‚Ñ Ž_ ‘f ”Z “x –ñ35volo/•B,llvo1%•ð Œ•F ‹[ Ž——± Žq “à •² ƒR •[ ƒN ƒX ‚Í ’… ‰Î ’¼ Œã ‚É ‚Í ‰»Šw ”½ ‰ž—¥‘¬ ‚Æ‹[ Ž— (ƒP •[ ƒX2,3‚É ŠY “–)‚Å ‚Ì •Ä •¬ ŽŽ Œ± ‚Å “¾ ‚ç ‚ê ‚½ •Ä Œ‹ •z ‚Ì ƒ~ —±Žq ŠO • –Ê ‹« –Œ “à Šg ŽU —¥‘¬ ‚É ‚æ ‚Á ‚Ä ”R •Ä ‚ª •i •s ‚· ‚é ‚ª,’† ƒN ƒ• ‘g •D ŽÊ •^ ‚𠎦 ‚· •B ‚Ü ‚½,“¯ ˆê •E —¿ ‚Å ‚Ì ‰æ‘œ •ˆ —• ‘• ’u ŽŽ ‚É Šú ˆÈ •~ ‚Í ‹[ Ž——±Žq “à •” ‚ð Ž_ ‘f ‚ª Šg ŽU ‚· ‚é Šg ŽU —¥‘¬ ‚É ˆÚ •s ‚· ‚æ ‚é ‘g •D ’è —Ê‚à ŽÀ Ž{ ‚µ,‚± ‚Ì Œ‹ ‰Ê‚ðFig.9‚É Ž¦ ‚· •B ‚é •B ‚± ‚Ì ‚½ ‚ß,Ž_ ‘f •x ‰»‚É ‚æ ‚è Ž_ ‘f ”Z “x ‚ð ƒq‚° ‚Ä ‚à • •ª ‚É Fig.8‚æ ‚è,Ž_ ‘f ”Z “x ‚ª35volo/•B ‚Ì •ð Œ• ‰º ‚Å •Ä •¬ ‚µ ‚½(b) ”R •Ä ‚¹ ‚¸,Fig.10‚É Ž¦ ‚· ”r ƒK ƒX ’† ‚Ì Ž_ ‘f ”Z “x ‚Ì•ã •¸ ‚É ŽŠ ‚Á ‚Å ‚Í ƒx •[ ƒX(a)‚É ”ä ‚× ƒw ƒ} ƒ^ ƒC ƒg ‘Š ‚ª ‘• ‰Á ‚µ ‚Ä ‚¢ ‚é ‚ª,”ì ‚½ ‚à ‚Ì ‚Æ •„ ’è ‚³ ‚ê ‚é •B ‚µ ‚© ‚µ Ž_ ‘f ”Z “x ‚Ì•ã •¸ ‚É ‚æ ‚è,”r ƒK ‘å ‰» ‚µ ‚½2ŽŸ ƒw ƒ} ƒ^ ƒC ƒg—± Žq ‚Í ‚ ‚Ü ‚è Œ©‚ç ‚ê ‚¸ ‰ß —n—Z‘g •D ƒX ’† ‚ÌCO2‚à •ã •¸ ‚µ ‚Ä ‚¨ ‚è,•² ƒR •[ ƒN ƒX ‚Ì ”R •Ä ‘¬ “x Œü•ã ‚Ö ‚à •- ‚È ‚¢ •B(c)‚Å ‚Í Ž_ ‘f ”Z “x ‚ª ’á ‰º ‚µ ‘g •D ’† ‚Ì Ž_ ‰» “S ‚ª ƒw ‚Ì Šñ —^ ‚Í • •ª ”F ‚ß ‚ç ‚ê ‚é •BFig.11‚É Ž_ ‘f ”Z “x ‚ÆFFS(Flame ƒ} ƒ^ ƒC ƒg ‚æ ‚è ƒ} ƒO ƒl ƒ^ ƒC ƒg ‚É •Ï ‰» ‚µ ‚Ä ‚à,‚» ‚Ì ƒ} ƒO ƒl ƒ^ ƒC FrontSpeed:•Ä Œ‹ ƒx ƒb ƒh •‚ ‚³ ‚ð •Ä Œ‹ Š® —¹ Žž ŠÔ ‚· ‚È ‚í ‚¿,“_ ƒg—± Žq‚Í •‚ ƒV ƒŠ ƒJ •Ä Œ‹ •z ’† ‚É Œ©‚ç ‚ê ‚é ‘e ‘å2ŽŸ ƒw ƒ} ƒ^ ƒC ƒg ‰Î ‚© ‚ç ƒ| ƒb ƒg ƒO ƒŒ•[ ƒg˜F ’¼ ‰º ‚Ì ”r ƒK ƒX •Å •‚ ‰· “x “ž ’B ‚Ü ‚Å ‚Ì ‚© ‚ç •Ï ‰» ‚µ ‚½2ŽŸ ƒ} ƒO ƒl ƒ^ ƒC ƒg23)‚É ”ä Šr ‚µ —± Œa ‚Í •¬ ‚³ ‚¢ ‚Ì Žž ŠÔ ‚Å •œ ‚µ ‚½ ’l ‚Å,‰Î ‰Š ‘O –Ê ‚Ì •½ ‹Ï ˆÚ “® ‘¬ “x ‚Æ ’è ‹`)‚Ì ŠÖ ‚ª “Á ’¥ ‚Å ‚ ‚é •A, ŒW‚𠎦 ‚· •B ‚± ‚ê ‚æ ‚è,Ž_ ‘f ”Z “x ‚ª ‘• ‰Á‚· ‚é ‚É ‚µ ‚½ ‚ª ‚Á ‚Ä FFS‚Í ‘• ‰Á ‚µ ‚Ä ‚¢ ‚é ‚± ‚Æ ‚ª •ª ‚© ‚é •B ‚± ‚ê ‚Í Ž_ ‘f •x ‰»‚É ‚æ ‚è, 106
  • 7. Fig. 12. Effect of 02 content on the holding time above 1100•Ž. Fig. 13. Comparison of simulation results on coke com- bustion time under a constant oxygen enrichment condition. 107
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