{"id":3036,"date":"2026-06-15T09:03:51","date_gmt":"2026-06-15T09:03:51","guid":{"rendered":"https:\/\/regenerative-thermal-oxidation.com\/?p=3036"},"modified":"2026-06-15T09:03:51","modified_gmt":"2026-06-15T09:03:51","slug":"bakir-eritme-tesislerinde-manyetik-duman-azaltma-yontemiyle-alkali-reaktif-veya-ikincil-atik-su-aritimi-olmadan-bakir-elektroliz-tesisinin-buharlastirici-baca-gazindan-cikan-asit-sisi-beyaz-dumanini","status":"publish","type":"post","link":"https:\/\/regenerative-thermal-oxidation.com\/tr\/basvuru\/bakir-eritme-tesislerinde-manyetik-duman-azaltma-yontemiyle-alkali-reaktif-veya-ikincil-atik-su-aritimi-olmadan-bakir-elektroliz-tesisinin-buharlastirici-baca-gazindan-cikan-asit-sisi-beyaz-dumanini\/","title":{"rendered":"Bak\u0131r Eritme \u0130\u015fleminde Manyetik Duman Azaltma: Alkali Reaktif veya \u0130kincil At\u0131k Suya Gerek Kalmadan Bak\u0131r Elektroliz Tesisi Buharla\u015ft\u0131r\u0131c\u0131s\u0131n\u0131n \u00c7\u0131k\u0131\u015f Gaz\u0131ndan Kaynaklanan Asit Sisi Beyaz Duman\u0131n\u0131n Giderilmesi"},"content":{"rendered":"

<\/p>\n

<\/p>\n
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Vaka \u0130ncelemesi \u00b7 End\u00fcstriyel Emisyon Kontrol\u00fc<\/p>\n

Yunnan eyaletindeki bir elektrolitik bak\u0131r \u00fcretim tesisi, g\u00fcnde 170 m\u00b3 s\u00fclf\u00fcrik asitli bak\u0131r elektrolitini, geleneksel alkali y\u0131kama y\u00f6ntemiyle \u00e7al\u0131\u015fan baca gaz\u0131 ar\u0131tma sistemini, grafen kompozit manyetik baca gaz\u0131 azaltma sistemiyle de\u011fi\u015ftirerek, saatte 20.000 Nm\u00b3 asit buhar\u0131 i\u00e7eren buharla\u015ft\u0131r\u0131c\u0131 buhar\u0131n\u0131 nas\u0131l ar\u0131tarak g\u00f6r\u00fcnmez baca gaz\u0131 de\u015farj\u0131, GB 26132\u22122010 standard\u0131na tam uyum ve s\u0131f\u0131r ikincil at\u0131k su \u00fcretimi sa\u011flad\u0131.<\/p>\n

Beyaz T\u00fcylerin Giderilmesi<\/span>
\nBak\u0131r Eritme Asit Buhar\u0131 \u0130\u015flemi<\/span>
\nElektroliz Y\u00f6ntemiyle Gaz \u00c7\u0131k\u0131\u015f\u0131n\u0131n Azalt\u0131lmas\u0131<\/span>
\nIs\u0131 D\u0131\u015f\u0131 Duman Bast\u0131rma<\/span>
\nS\u00fclf\u00fcrik Asit Sisi Manyetik Yakalama<\/span><\/div>\n<\/header>\n

<\/p>\n

\n
\n
20,000<\/div>\n
Nm\u00b3\/h<\/div>\n
Nominal Baca Gaz\u0131 Hacmi<\/div>\n<\/div>\n
\n
\u226597%<\/div>\n
Ar\u0131tma Oran\u0131<\/div>\n
Kar\u0131\u015f\u0131k Kirleticilerin Giderilmesi<\/div>\n<\/div>\n
\n
50\u219210<\/div>\n
mg\/Nm\u00b3<\/div>\n
Giri\u015ften \u00c7\u0131k\u0131\u015fa Kirletici Yo\u011funlu\u011fu<\/div>\n<\/div>\n
\n
S\u0131f\u0131r<\/div>\n
\u0130kincil At\u0131k Su<\/div>\n
Reaktif Madde Yok \u2022 At\u0131k Su Yok<\/div>\n<\/div>\n<\/div>\n

<\/p>\n

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01 \u2014 Sekt\u00f6r Hakk\u0131nda Bilgiler<\/p>\n

Yunnan Ekolojik K\u0131rm\u0131z\u0131 \u00c7izgi Uygulamas\u0131 Kapsam\u0131nda Bak\u0131r Eritme, Elektrolizle Bak\u0131r Elde Etme ve Asit Sisi Uyumluluk Zorlu\u011fu<\/h2>\n

10 Kas\u0131m 2020 tarihinde Yunnan Eyalet H\u00fck\u00fcmeti \u015fu a\u00e7\u0131klamay\u0131 yay\u0131nlad\u0131: \u201c\u00dc\u00e7 \u00c7izgi ve Bir Liste\u201d Ekolojik ve \u00c7evresel B\u00f6lgeleme Y\u00f6netiminin Uygulanmas\u0131na \u0130li\u015fkin G\u00f6r\u00fc\u015fler<\/em> (Yunzhengfa [2020] No. 29). Belge, Yunnan genelindeki 1.164 ekolojik \u00e7evre y\u00f6netim birimini \u00fc\u00e7 s\u0131n\u0131fa ay\u0131rd\u0131: \u00f6ncelikli koruma, kilit y\u00f6netim ve genel y\u00f6netim. Ayr\u0131ca \u015fu konularda ba\u011flay\u0131c\u0131 \u015fartlar belirledi: ekolojik \u00e7evre koruma yasalar\u0131n\u0131n s\u0131k\u0131 bir \u015fekilde uygulanmas\u0131, sabit kaynakl\u0131 kirlilik emisyon izinlerinin kapsaml\u0131 bir \u015fekilde verilmesi, motorlu ta\u015f\u0131t kirlili\u011fi kontrol\u00fcn\u00fcn g\u00fc\u00e7lendirilmesi, toprak kirlili\u011fi risk y\u00f6netiminin g\u00fc\u00e7lendirilmesi ve \u201cda\u011f\u0131n\u0131k, kaotik ve kirletici\u201d i\u015fletmelerin entegre iyile\u015ftirilmesi yoluyla end\u00fcstriyel kirlili\u011fin derinlemesine ar\u0131t\u0131lmas\u0131.<\/p>\n

Bu d\u00fczenleyici \u00e7er\u00e7eve kapsam\u0131nda, \u00f6nemli bir bak\u0131r \u00fcretim b\u00f6lgesi olan Yunnan Eyaleti'ndeki end\u00fcstriyel bak\u0131r eritme i\u015flemleri, atmosferik emisyonlar, su kaynaklar\u0131n\u0131n korunmas\u0131 ve birim \u00e7\u0131kt\u0131 ba\u015f\u0131na enerji t\u00fcketimi a\u00e7\u0131s\u0131ndan yo\u011funla\u015ft\u0131r\u0131lm\u0131\u015f bir incelemeyle kar\u015f\u0131 kar\u015f\u0131ya kalmaktad\u0131r. \u00d6zellikle elektrolizle bak\u0131r elde etme tesisleri i\u00e7in, birincil atmosferik uyumluluk sorunu, elektrolit konsantre etmek i\u00e7in kullan\u0131lan buharla\u015ft\u0131r\u0131c\u0131 sistem taraf\u0131ndan \u00fcretilen asit buhar\u0131d\u0131r. Buharla\u015ft\u0131r\u0131c\u0131, yakla\u015f\u0131k 50\u00b0C'de 20.000 Nm\u00b3\/h buhar \u00fcretir ve bu buhar, 100 mg\/Nm\u00b3 oran\u0131nda ince s\u00fclf\u00fcrik asit buhar\u0131 damlac\u0131klar\u0131 ta\u015f\u0131r; bu de\u011fer, NOx i\u00e7in GB 26132\u22122010 limiti olan 50 mg\/Nm\u00b3 ve genel partik\u00fcl limiti olan 10 mg\/Nm\u00b3'\u00fcn \u00e7ok \u00fczerindedir.<\/p>\n

Bu asit sisi ak\u0131\u015f\u0131n\u0131n geleneksel ar\u0131t\u0131m\u0131nda, s\u00fclf\u00fcrik asit aerosol\u00fcn\u00fc n\u00f6tralize etmek i\u00e7in alkali y\u0131kama y\u0131kay\u0131c\u0131lar\u0131 (NaOH \u00e7\u00f6zeltisi, Ca(OH)\u2082 \u00e7\u00f6zeltisi veya benzeri alkali reaktifler) kullan\u0131l\u0131r. Bununla birlikte, bu yakla\u015f\u0131m \u00f6nemli miktarda kirlenmi\u015f at\u0131k su (elektro kazan\u0131m i\u015fleminden kaynaklanan y\u00fcksek bak\u0131r, arsenik ve a\u011f\u0131r metal i\u00e7eri\u011fine sahip s\u00fclfat bak\u0131m\u0131ndan zengin) \u00fcretir, s\u00fcrekli reaktif tedarik maliyetine yol a\u00e7ar ve genellikle y\u0131kay\u0131c\u0131dan \u00e7\u0131kan doymu\u015f su buhar\u0131n\u0131 ve art\u0131k ince aerosol\u00fc uzakla\u015ft\u0131rmad\u0131\u011f\u0131 i\u00e7in \"g\u00f6r\u00fcn\u00fcr beyaz duman olmamas\u0131\" \u015fart\u0131n\u0131 kar\u015f\u0131layamaz. Manyetik Duman Azaltma teknolojisi, g\u00f6r\u00fcn\u00fcr duman\u0131n \u00fc\u00e7 bile\u015fenini de (partik\u00fcller, asit sisi ve doymu\u015f su buhar\u0131) herhangi bir s\u0131v\u0131 reaktif girdisi olmadan ortadan kald\u0131rd\u0131\u011f\u0131 i\u00e7in \u00f6zellikle se\u00e7ilmi\u015ftir.<\/p>\n

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<\/div>\n

\u201cGeleneksel alkali ar\u0131tma, s\u00fclf\u00fcrik asit buhar\u0131n\u0131 n\u00f6tralizasyon yoluyla ar\u0131t\u0131r; ancak beyaz duman\u0131 ortadan kald\u0131ramaz, \u00e7\u00fcnk\u00fc g\u00f6r\u00fcn\u00fcr duman\u0131 olu\u015fturan doymu\u015f su buhar\u0131 ve art\u0131k mikron alt\u0131 aerosol fraksiyonu, ar\u0131tma dolgusundan do\u011frudan ge\u00e7er. Sadece aerosol faz\u0131n\u0131 e\u015f zamanl\u0131 olarak ortadan kald\u0131ran bir teknoloji beyaz duman sorununu \u00e7\u00f6zebilir. Manyetik yakalama mekanizmas\u0131 tam olarak bunu ba\u015far\u0131r.\u201d<\/p>\n

\u2014 M\u00fchendislik Teknik \u00d6zeti, Bak\u0131r Eritme Manyetik Duman Azaltma Projesi<\/cite><\/p><\/blockquote>\n

\"Manyetik<\/p>\n<\/section>\n

\n

<\/p>\n

\n

02 \u2014 Kirlilik Profili<\/p>\n

Buharla\u015ft\u0131r\u0131c\u0131 Buhar Karakterizasyonu: Bak\u0131r Elektrolizinden Elde Edilen S\u00fclf\u00fcrik Asit Sisi \u0130\u00e7eren At\u0131k Gaz\u0131n Elektrolit Konsantrasyonu<\/h2>\n

Tesis, s\u00fclf\u00fcrik asit bak\u0131r elektrolit buharla\u015ft\u0131rma oran\u0131 170 m\u00b3\/g\u00fcn olan ve 20.000 Nm\u00b3\/saat buhar \u00fcreten bir elektrolitik bak\u0131r i\u015fletmesidir. Buharla\u015ft\u0131rma i\u015fleminde, buhar s\u00fclf\u00fcrik asit bak\u0131r \u00e7\u00f6zeltisinden ge\u00e7er ve \u0131s\u0131t\u0131larak buharla\u015fmaya neden olur. Buhar toplan\u0131r ve bir yo\u011fu\u015fma suyu tank\u0131na y\u00f6nlendirilir ve \u00fcstten bo\u015falt\u0131lan yo\u011fu\u015fma suyu (yakla\u015f\u0131k 1,9 mg\/m\u00b3 asit i\u00e7eri\u011fiyle) 40 mg\/m\u00b3'l\u00fck ulusal de\u015farj standartlar\u0131n\u0131 kar\u015f\u0131lar ve atmosfere de\u015farj edilir.<\/p>\n

Ancak, \u00e7evresel gereksinimler s\u0131k\u0131la\u015ft\u0131k\u00e7a ve \u015firket ye\u015fil kalk\u0131nmay\u0131 hedefledik\u00e7e, egzoz gaz\u0131n\u0131n daha derinlemesine i\u015flenmesi i\u00e7in kapsaml\u0131 bir ar\u0131tma sistemi ba\u015flat\u0131ld\u0131. Birincil asit buhar\u0131 ve yo\u011fu\u015fma suyu toplama yollar\u0131 yeniden tasarland\u0131 ve de\u015farj gazlar\u0131n\u0131n derinlemesine ar\u0131t\u0131lmas\u0131n\u0131 sa\u011flamak i\u00e7in bir su buhar\u0131 y\u00f6netim sistemi eklendi. Reaksiyon tank\u0131 havaland\u0131rma hatlar\u0131ndan gelen asit buhar\u0131, da\u011f\u0131t\u0131m borular\u0131 arac\u0131l\u0131\u011f\u0131yla so\u011fuk yo\u011fu\u015fma kulesine toplanarak asit buhar\u0131 so\u011fuk yo\u011fu\u015fma geri kazan\u0131m\u0131 sa\u011flan\u0131r, ard\u0131ndan cebri \u00e7eki\u015f fan\u0131 taraf\u0131ndan son ar\u0131tma ve de\u015farj i\u00e7in MPA \u00fcnitesine y\u00f6nlendirilir.<\/p>\n

    \n
  • S\u00fclf\u00fcrik asit buhar\u0131 (ba\u015fl\u0131ca kirletici):<\/strong> Elektroliz i\u015flemi, buharla\u015ft\u0131r\u0131c\u0131 buhar\u0131nda ta\u015f\u0131nan ince s\u00fclf\u00fcrik asit sisi damlac\u0131klar\u0131 \u00fcretir. Ba\u015flang\u0131\u00e7 \u200b\u200bkonsantrasyonu, MPA \u00fcnitesi giri\u015finde (so\u011fuk yo\u011fu\u015fma sonras\u0131 geri kazan\u0131m) 50 mg\/Nm\u00b3 olup, hedef \u00e7\u0131k\u0131\u015f konsantrasyonu \u226410 mg\/Nm\u00b3't\u00fcr. Asit sisi hem uyumluluk a\u00e7\u0131s\u0131ndan kirletici bir madde hem de g\u00f6r\u00fcn\u00fcr beyaz duman olu\u015fumunun birincil nedenidir.<\/li>\n
  • SO\u2082 (asit buhar\u0131n\u0131n ta\u015f\u0131nmas\u0131ndan kaynakl\u0131):<\/strong> Ba\u015flang\u0131\u00e7 \u200b\u200b100 mg\/Nm\u00b3; \u00e7\u0131k\u0131\u015f hedefi \u226430 mg\/Nm\u00b3. Hem gaz halindeki SO\u2082 hem de buharla\u015ft\u0131r\u0131c\u0131 buhar ak\u0131\u015f\u0131na kar\u0131\u015fm\u0131\u015f s\u00fclfat aerosol\u00fc olarak mevcuttur.<\/li>\n
  • Partik\u00fcl madde (PM):<\/strong> Ba\u015flang\u0131\u00e7 \u200b\u200b50 mg\/Nm\u00b3; \u00e7\u0131k\u0131\u015f hedefi \u226410 mg\/Nm\u00b3. Asit buhar\u0131 fraksiyonuna ek olarak, buharla\u015ft\u0131r\u0131c\u0131dan gelen ince tuz kristalleri ve aerosol damlac\u0131klar\u0131n\u0131 da i\u00e7erir.<\/li>\n
  • Asit buhar\u0131 boru hatt\u0131 g\u00fczergah\u0131n\u0131n karma\u015f\u0131kl\u0131\u011f\u0131:<\/strong> S\u00fclf\u00fcrik asit reaksiyon sisteminde, aralar\u0131nda uzun boru hatlar\u0131 bulunan \u00e7ok say\u0131da reaksiyon kab\u0131 bulunmaktad\u0131r. Kanal tasar\u0131m\u0131n\u0131n sonland\u0131r\u0131lmas\u0131ndan \u00f6nce ak\u0131\u015f da\u011f\u0131l\u0131m\u0131n\u0131n do\u011fru bir \u015fekilde karakterize edilmesi i\u00e7in gaz ak\u0131\u015f alan\u0131 modellemesi (CFD) gereklidir ve genel hava ak\u0131\u015f\u0131 dengelemesi ve ayarlanmas\u0131 i\u00e7in her asit buhar\u0131 bran\u015fman hatt\u0131na manuel hava damperleri tak\u0131lmal\u0131d\u0131r.<\/li>\n
  • Doymu\u015f buhar\u0131n olu\u015fturdu\u011fu beyaz duman:<\/strong> Buharla\u015ft\u0131r\u0131c\u0131 buhar\u0131 yakla\u015f\u0131k 50\u00b0C'de tamamen doymu\u015f haldedir. So\u011fuk yo\u011fu\u015fma kulesinden ge\u00e7tikten sonra gaz, yakla\u015f\u0131k 40\u00b0C'de, 50% nem oran\u0131 ve 50 mg\/Nm\u00b3 kar\u0131\u015f\u0131k giri\u015f kirletici y\u00fck\u00fc ile MPA \u00fcnitesine girer ve aktif aerosol giderme i\u015flemi yap\u0131lmadan t\u00fcm ortam ko\u015fullar\u0131nda yo\u011fun beyaz bir duman olu\u015fturur.<\/li>\n<\/ul>\n
    \n\n\n\n\n\n\n\n\n\n\n\n\n\n\n
    Parametre<\/th>\nBa\u015flang\u0131\u00e7 \u200b\u200bKonsantrasyonu<\/th>\n\u00c7\u0131k\u0131\u015f (Tasar\u0131m)<\/th>\nD\u00fczenleyici S\u0131n\u0131r<\/th>\n<\/tr>\n<\/thead>\n
    NOx<\/td>\n\u2014<\/td>\n\u226450 mg\/Nm\u00b3<\/td>\n50 mg\/Nm\u00b3<\/td>\n<\/tr>\n
    SO\u2082<\/td>\n100 mg\/Nm\u00b3<\/td>\n\u226430 mg\/Nm\u00b3<\/td>\n30 mg\/Nm\u00b3<\/td>\n<\/tr>\n
    Partik\u00fcl madde (PM)<\/td>\n50 mg\/Nm\u00b3<\/td>\n\u226410 mg\/Nm\u00b3<\/td>\n10 mg\/Nm\u00b3<\/td>\n<\/tr>\n
    S\u00fclf\u00fcrik asit buhar\u0131 (MPA giri\u015fi)<\/td>\n50 mg\/Nm\u00b3<\/td>\n\u226410 mg\/Nm\u00b3<\/td>\n10 mg\/Nm\u00b3<\/td>\n<\/tr>\n
    G\u00f6r\u00fcn\u00fcr beyaz t\u00fcy<\/td>\nMevcut (yo\u011fun asit sisi bulutu)<\/td>\nYok (g\u00f6r\u00fcnmez)<\/td>\nG\u00f6r\u00fcnmez, anormal bir kokusu yok.<\/td>\n<\/tr>\n
    Baca gaz\u0131 hacmi (nominal)<\/td>\n20.000 Nm\u00b3\/sa<\/td>\n\u2014<\/td>\n\u2014<\/td>\n<\/tr>\n
    Baca gaz\u0131 s\u0131cakl\u0131\u011f\u0131 (evaporat\u00f6r \u00e7\u0131k\u0131\u015f\u0131)<\/td>\n50\u00b0C<\/td>\n\u2014<\/td>\n\u2014<\/td>\n<\/tr>\n
    Giri\u015f s\u0131cakl\u0131\u011f\u0131 (MPA \u00fcnitesi, so\u011fuk kondenser sonras\u0131)<\/td>\n\u224840\u00b0C<\/td>\n\u2014<\/td>\n\u2014<\/td>\n<\/tr>\n
    Nem (MPA \u00fcnitesi giri\u015finde)<\/td>\n50%<\/td>\n\u2014<\/td>\n\u2014<\/td>\n<\/tr>\n
    Uygulanabilir emisyon standard\u0131<\/td>\nGB 26132\u22122010 S\u00fclf\u00fcrik Asit End\u00fcstrisi i\u00e7in Hava Kirleticileri Emisyon Standard\u0131<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n<\/section>\n
    \n

    <\/p>\n

    \n

    03 \u2014 M\u00fchendislik Gereksinimleri<\/p>\n

    Bak\u0131r Eritme Elektroliz Gaz\u0131 Uygulamalar\u0131nda Manyetik Duman Azalt\u0131m\u0131 i\u00e7in Tasar\u0131m Kriterleri<\/h2>\n

    Bu bak\u0131r eritme elektroliz uygulamas\u0131n\u0131n asit buhar\u0131 bile\u015fimi, a\u015f\u0131nd\u0131r\u0131c\u0131 \u00e7al\u0131\u015fma ortam\u0131, karma\u015f\u0131k boru hatt\u0131 g\u00fczergah\u0131 ve s\u0131f\u0131r ikincil at\u0131k su gereksinimini yans\u0131tan a\u015fa\u011f\u0131daki ba\u011flay\u0131c\u0131 tasar\u0131m gereksinimleri, teknoloji se\u00e7iminden \u00f6nce belirlenmi\u015ftir.<\/p>\n

    \n
    \n
    \ud83c\udfaf<\/div>\n

    Kan\u0131tlanm\u0131\u015f Teknoloji, Ulusal Standartlar<\/h3>\n

    Yaln\u0131zca ticari olarak olgunla\u015fm\u0131\u015f, sahada kan\u0131tlanm\u0131\u015f ar\u0131tma teknolojileri kabul edilebilir. T\u00fcm ekipman, yard\u0131mc\u0131 malzemeler ve \u00fcretim s\u00fcre\u00e7leri ulusal standart \u015fartnamelerine uygun olmal\u0131d\u0131r. Sistem, s\u00fclf\u00fcrik asit buhar\u0131 yakalamaya uygulanabilir do\u011frulanm\u0131\u015f azaltma teknikleri kullan\u0131larak mevcut temel seviyeye g\u00f6re 30%\u201350%'lik bir iyile\u015fme sa\u011flamal\u0131d\u0131r.<\/p>\n<\/div>\n

    \n
    \u2699\ufe0f<\/div>\n

    Y\u00fck Tolerans\u0131 10%\u2013110%<\/h3>\n

    Sistem, baca gaz\u0131 hacmi tasar\u0131m kapasitesinin 10% ile 110%'si aras\u0131nda de\u011fi\u015fti\u011finde istikrarl\u0131 ar\u0131tma ve duman bast\u0131rma \u00f6zelli\u011fini korumal\u0131d\u0131r. Elektroliz tesisindeki buharla\u015fma oranlar\u0131, katot bak\u0131r \u00fcretim verimi ve elektrolit bile\u015fimindeki de\u011fi\u015fikliklerle birlikte de\u011fi\u015fmekte olup, geni\u015f bir \u00e7al\u0131\u015fma aral\u0131\u011f\u0131 kapasitesi gerektirmektedir.<\/p>\n<\/div>\n

    \n
    \ud83d\udee1\ufe0f<\/div>\n

    S\u00fclf\u00fcrik Asit Sisine Kar\u015f\u0131 Korozyon Direnci<\/h3>\n

    S\u00fclf\u00fcrik asit sisi ak\u0131m\u0131yla temas eden t\u00fcm bile\u015fenler, sertifikal\u0131 korozyon \u00f6nleyici koruma i\u00e7ermelidir. Grafen kompozit emici tabaka, 50 mg\/Nm\u00b3 konsantrasyonda s\u00fclf\u00fcrik asit aerosol\u00fcyle s\u00fcrekli temas i\u00e7in gerekli asit direncini ve periyodik rejeneratif geri y\u0131kama i\u015flemi i\u00e7in termal kararl\u0131l\u0131\u011f\u0131 sa\u011flar.<\/p>\n<\/div>\n

    \n
    \u2668<\/div>\n

    S\u0131f\u0131r \u0130kincil Kirlilik \u2014 Alkali Reaktif Yok<\/h3>\n

    Se\u00e7ilen teknoloji, alkali reaktifler (NaOH \u00e7\u00f6zeltisi, Ca(OH)\u2082 veya benzeri) kullanmamal\u0131 ve at\u0131k su de\u015farj\u0131 veya kullan\u0131lm\u0131\u015f reaktif \u00fcretmemelidir. Bu gereklilik, ortaya \u00e7\u0131kan s\u00fclfatl\u0131 at\u0131k suyun ek ar\u0131tma yap\u0131lmadan mevcut at\u0131k su sistemine de\u015farj edilemeyece\u011fi i\u00e7in geleneksel alkali y\u0131kamay\u0131 a\u00e7\u0131k\u00e7a bir se\u00e7enek olarak d\u0131\u015flamaktad\u0131r.<\/p>\n<\/div>\n

    \n
    \ud83d\udca1<\/div>\n

    Enerji Verimlili\u011fi<\/h3>\n

    Ekipman se\u00e7imi hem sermaye hem de i\u015fletme maliyetlerini en aza indirmelidir. Tasar\u0131m, i\u015fletme maliyetlerini d\u00fc\u015f\u00fcrmek i\u00e7in enerji tasarrufu sa\u011flayan teknolojileri ve cihazlar\u0131 i\u00e7ermelidir. T\u00fcm \u00f6nemli ekipmanlar, ulusal olarak sertifikal\u0131 ve yerle\u015fik yerel tedarik zincirlerine sahip kalite \u00fcreticilerinden temin edilmelidir.<\/p>\n<\/div>\n

    \n
    \ud83d\udd0a<\/div>\n

    G\u00fcr\u00fclt\u00fc Uyumlulu\u011fu<\/h3>\n

    Ekipman g\u00fcr\u00fclt\u00fcs\u00fc, GB 12348\u22122008 S\u0131n\u0131f II limitlerini kar\u015f\u0131layacak \u015fekilde, 1 m mesafede 85 dB(A)'y\u0131 a\u015fmamal\u0131d\u0131r. Bak\u0131r eritme tesisi, Yunnan \u00dc\u00e7 Hat ve Bir Liste d\u00fczenleyici \u00e7er\u00e7evesi kapsam\u0131ndaki t\u00fcm end\u00fcstriyel faaliyetlerle ayn\u0131 topluluk g\u00fcr\u00fclt\u00fc y\u00fck\u00fcml\u00fcl\u00fcklerine tabidir.<\/p>\n<\/div>\n

    \n
    \ud83d\udd27<\/div>\n

    Asit Sisi Boru Hatt\u0131 Ak\u0131\u015f Alan\u0131 Tasar\u0131m\u0131<\/h3>\n

    S\u00fclf\u00fcrik asit reaksiyon tank\u0131 sisteminde, uzun boru hatlar\u0131na sahip \u00e7ok say\u0131da tank bulunmaktad\u0131r. Boru hatt\u0131 tasar\u0131m\u0131n\u0131n sonland\u0131r\u0131lmas\u0131ndan \u00f6nce gaz ak\u0131\u015f alan\u0131 modellemesi (CFD) yap\u0131lmal\u0131d\u0131r. Uzun boru hatt\u0131 a\u011f\u0131ndaki ak\u0131\u015f da\u011f\u0131l\u0131m\u0131 asimetrilerini dengelemek ve genel hava ak\u0131\u015f\u0131n\u0131 sa\u011flamak i\u00e7in her bir asit sisi bran\u015f hatt\u0131na manuel hava damperleri tak\u0131lmal\u0131d\u0131r.<\/p>\n<\/div>\n

    \n
    \ud83d\udd04<\/div>\n

    Mod\u00fcler ve Gelece\u011fe Haz\u0131r<\/h3>\n

    Mod\u00fcler tasar\u0131m, Yunnan'\u0131n g\u00fc\u00e7lenen ekolojik koruma \u00e7er\u00e7evesi kapsam\u0131nda 3-5 y\u0131l i\u00e7inde s\u0131k\u0131la\u015fan emisyon s\u0131n\u0131rlar\u0131n\u0131 kar\u015f\u0131lamal\u0131d\u0131r. Geli\u015fmi\u015f teknoloji, ayn\u0131 zamanda kalan gaz halindeki e\u015f emisyonlar\u0131 da ele almal\u0131 ve tesisin tam sistem de\u011fi\u015fimi gerektirmeden ultra d\u00fc\u015f\u00fck emisyon s\u0131n\u0131fland\u0131rmas\u0131na girmesini sa\u011flamal\u0131d\u0131r.<\/p>\n<\/div>\n<\/div>\n<\/section>\n

    \n

    <\/p>\n

    \n

    04 \u2014 Tedavi \u00c7\u00f6z\u00fcm\u00fc<\/p>\n

    Bak\u0131r eritme elektrolizinden \u00e7\u0131kan at\u0131k gazlar i\u00e7in manyetik duman azaltma sisteminin nas\u0131l yap\u0131land\u0131r\u0131ld\u0131\u011f\u0131<\/h2>\n

    Manyetik Duman Azaltma (MPA) \u2014 di\u011fer ad\u0131yla manyetik duman ar\u0131tma<\/strong>, kuru fazl\u0131 s\u00fclf\u00fcrik asit buhar\u0131 yakalama<\/strong>, termal olmayan duman bast\u0131rma<\/strong>, veya manyetik alan asit buhar\u0131 giderme<\/strong> \u2014 Buharla\u015ft\u0131r\u0131c\u0131 buhar ak\u0131\u015f\u0131ndan ince par\u00e7ac\u0131klar\u0131, asit sisi aerosollerini ve doymu\u015f su buhar\u0131n\u0131 ayn\u0131 anda uzakla\u015ft\u0131rarak g\u00f6r\u00fcn\u00fcr beyaz duman\u0131 ortadan kald\u0131r\u0131r. BLEMG-1KA jenerat\u00f6r\u00fc, paramanyetik molek\u00fcllerin ve y\u00fckl\u00fc aerosol par\u00e7ac\u0131klar\u0131n\u0131n (bak\u0131r eritme elektroliz gaz\u0131na \u00f6zg\u00fc s\u00fclf\u00fcrik asit sisi damlac\u0131klar\u0131 ve ince tuz kristal par\u00e7ac\u0131klar\u0131 dahil) grafen kompozit emici tabakaya do\u011fru hareket etmesine neden olan kontroll\u00fc bir manyetik alan gradyan\u0131 olu\u015fturarak \u00e7\u0131kan gaz\u0131 ger\u00e7ekten g\u00f6r\u00fcnmez hale getirir.<\/p>\n

    \u0130\u015flem dizisi, \u00e7ok dall\u0131 bir manifold ba\u015fl\u0131k sistemi arac\u0131l\u0131\u011f\u0131yla reaksiyon kab\u0131 havaland\u0131rma hatlar\u0131ndan asit buhar\u0131n\u0131n toplanmas\u0131yla ba\u015flar. Toplanan gaz, toplu asit buhar\u0131 yo\u011fu\u015fmas\u0131n\u0131n geri kazan\u0131ld\u0131\u011f\u0131 so\u011fuk bir yo\u011fu\u015fma kulesinden ge\u00e7er. \u00d6n i\u015flemden ge\u00e7irilmi\u015f gaz daha sonra, baca yoluyla de\u015farj edilmeden \u00f6nce, son derin safla\u015ft\u0131rma i\u00e7in ind\u00fcklenmi\u015f \u00e7eki\u015f fan\u0131 arac\u0131l\u0131\u011f\u0131yla MPA \u00fcnitesine girer. Bu iki a\u015famal\u0131 yakla\u015f\u0131m \u2013 so\u011fuk yo\u011fu\u015fma geri kazan\u0131m\u0131 ve ard\u0131ndan MPA ar\u0131tma \u2013 hem yasal uyumluluk hedefine hem de i\u015flem i\u00e7inde potansiyel yeniden kullan\u0131m i\u00e7in maksimum asit buhar\u0131 geri kazan\u0131m\u0131na ula\u015f\u0131r.<\/p>\n

    Proses Ak\u0131\u015f\u0131: Reaksiyon Kaplar\u0131 \u2192 So\u011fuk Kondenser \u2192 MPA \u00dcnitesi \u2192 Baca<\/h3>\n
    \n
    \n
    Tepki
    \nDamar Havaland\u0131rmalar\u0131<\/div>\n
    \u2192<\/div>\n
    \u00c7oklu
    \nBa\u015fl\u0131k<\/div>\n
    \u2192<\/div>\n
    So\u011fuk Yo\u011fu\u015fma
    \nKule<\/div>\n
    \u2192<\/div>\n
    Tetiklenmi\u015f
    \nTaslak Hayran\u0131<\/div>\n
    \u2192<\/div>\n
    MPA Birimi \u2b50
    \n(BLCNXB-2W)<\/div>\n
    \u2192<\/div>\n
    Temiz
    \nY\u0131\u011f\u0131n<\/div>\n<\/div>\n<\/div>\n

    \"Bak\u0131r<\/p>\n

    Sistem Yap\u0131land\u0131rmas\u0131 ve Temel Teknik Parametreler<\/h3>\n

    BLCNXB-2W \u00fcnitesi bir kule-d\u0131\u015ftan, alttan giri\u015fli \/ \u00fcstten egzozlu<\/strong> 3,6\u00d73,6\u00d713,2 m'lik kompakt kare planl\u0131 yap\u0131s\u0131, mevcut elektroliz h\u00fccresi altyap\u0131s\u0131 ile so\u011fuk yo\u011fu\u015fma kulesi aras\u0131nda bulunan s\u0131n\u0131rl\u0131 alanlara kurulum i\u00e7in olduk\u00e7a uygundur.<\/p>\n

    \n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n\n
    Parametre<\/th>\n\u00d6zellikler<\/th>\n<\/tr>\n<\/thead>\n
    \u00dcnite Modeli<\/td>\nBLCNXB-2W<\/td>\n<\/tr>\n
    Yerle\u015fim Tipi<\/td>\nKule d\u0131\u015f\u0131, ba\u011f\u0131ms\u0131z mod\u00fcl<\/td>\n<\/tr>\n
    Hava Ak\u0131\u015f\u0131 Y\u00f6nlendirmesi<\/td>\nAlttan giri\u015fli, \u00fcstten egzozlu<\/td>\n<\/tr>\n
    Ar\u0131tma Verimlili\u011fi<\/td>\n\u226597%<\/td>\n<\/tr>\n
    Giri\u015f Kar\u0131\u015f\u0131k Kirletici Konsantrasyonu<\/td>\n50 mg\/Nm\u00b3<\/td>\n<\/tr>\n
    \u00c7\u0131k\u0131\u015f Kar\u0131\u015f\u0131k Kirletici Konsantrasyonu<\/td>\n\u226410 mg\/Nm\u00b3<\/td>\n<\/tr>\n
    Sistem Direnci<\/td>\n250 Pa<\/td>\n<\/tr>\n
    \u0130\u015flem G\u00f6rm\u00fc\u015f Baca Gaz\u0131 Hacmi<\/td>\n20.000 Nm\u00b3\/sa<\/td>\n<\/tr>\n
    Baca Giri\u015f Gaz\u0131 S\u0131cakl\u0131\u011f\u0131 (MPA birimi)<\/td>\n\u224840\u00b0C<\/td>\n<\/tr>\n
    Emici Katman Malzemesi<\/td>\nGrafen kompoziti<\/td>\n<\/tr>\n
    Ekipman Boyutlar\u0131 (Uzunluk \u00d7 Geni\u015flik \u00d7 Y\u00fckseklik)<\/td>\n3,6 m \u00d7 3,6 m \u00d7 13,2 m<\/td>\n<\/tr>\n
    Manyetik Enerji Jenerat\u00f6r\u00fc Modeli<\/td>\nBLEMG-1KA<\/td>\n<\/tr>\n
    \u00c7al\u0131\u015ft\u0131rma G\u00fcc\u00fc<\/td>\n15 kW<\/td>\n<\/tr>\n
    Y\u0131ll\u0131k \u00c7al\u0131\u015fma G\u00fcnleri<\/td>\n300 g\u00fcn\/y\u0131l<\/td>\n<\/tr>\n
    Y\u0131ll\u0131k Elektrik Maliyeti<\/td>\nYakla\u015f\u0131k 43.200 RMB\/y\u0131l<\/td>\n<\/tr>\n
    Uygulanabilir Emisyon Standard\u0131<\/td>\nGB 26132\u22122010 S\u00fclf\u00fcrik Asit End\u00fcstrisi Emisyon Standard\u0131<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n

    \"Bak\u0131r<\/p>\n<\/section>\n

    \n

    <\/p>\n

    \n

    05 \u2014 Temel Avantajlar<\/p>\n

    Bak\u0131r eritme i\u015flemlerinde asit buhar\u0131 ar\u0131t\u0131m\u0131nda manyetik duman azaltma y\u00f6nteminin alkali ar\u0131tma y\u00f6nteminden neden daha iyi performans g\u00f6sterdi\u011fi<\/h2>\n
      \n
    • \u2713<\/span>
      \nS\u0131f\u0131r Alkali Reaktif \u2014 S\u0131f\u0131r \u0130kincil At\u0131k Su \u2014 Belirleyici Fark Yaratan \u00d6zellik:<\/strong> S\u00fclf\u00fcrik asit buhar\u0131n\u0131n geleneksel NaOH veya Ca(OH)\u2082 ile y\u0131kanmas\u0131, elektroliz i\u015fleminden kaynaklanan y\u00fcksek miktarda bak\u0131r, arsenik, kadmiyum ve di\u011fer a\u011f\u0131r metalleri i\u00e7eren s\u00fclfat a\u00e7\u0131s\u0131ndan zengin at\u0131k su \u00fcretir. Bu at\u0131k su basit\u00e7e de\u015farj edilemez ve ek ar\u0131tma gerektirir veya i\u015fleme geri d\u00f6nd\u00fcr\u00fclerek hem maliyeti hem de operasyonel karma\u015f\u0131kl\u0131\u011f\u0131 art\u0131r\u0131r. MPA kuru i\u015flemi, s\u0131f\u0131r s\u0131v\u0131 reaktif i\u00e7erir ve s\u0131f\u0131r s\u00fcrekli at\u0131k su \u00fcretir, bu da bu ikincil kirlilik sorununu tamamen ortadan kald\u0131r\u0131r. Bu, teknoloji se\u00e7imini belirleyen birincil kriterdi.<\/li>\n
    • \u2713<\/span>
      \nAlkali ile temizlemenin yetersiz kald\u0131\u011f\u0131 durumlarda beyaz duman\u0131n tamamen ortadan kald\u0131r\u0131lmas\u0131:<\/strong> Geleneksel alkali y\u0131kama y\u00f6ntemi s\u00fclf\u00fcrik asit buhar\u0131 konsantrasyonunu yasal s\u0131n\u0131rlar\u0131n alt\u0131na d\u00fc\u015f\u00fcrse bile, y\u0131kay\u0131c\u0131 dolgu malzemesinden ge\u00e7en doymu\u015f su buhar\u0131 ve art\u0131k mikron alt\u0131 aerosol fraksiyonu bacada g\u00f6r\u00fcn\u00fcr beyaz veya gri bir duman olu\u015fturmaya devam eder. MPA sistemi ise partik\u00fclleri, asit buhar\u0131n\u0131 ve doymu\u015f su buhar\u0131 faz\u0131n\u0131 ayn\u0131 anda yakalayarak egzozu ger\u00e7ekten g\u00f6r\u00fcnmez hale getirir. Bu, iki teknoloji aras\u0131ndaki temel fiziksel mekanizma fark\u0131d\u0131r.<\/li>\n
    • \u2713<\/span>
      \nUltra D\u00fc\u015f\u00fck \u00d6zg\u00fcl Enerji \u2014 20.000 Nm\u00b3\/h i\u00e7in 15 kW:<\/strong> BLCNXB-2W, Nm\u00b3\/h ba\u015f\u0131na 0,75 W enerji t\u00fcketimiyle, alkali y\u0131kama, elektrostatik \u00e7\u00f6kt\u00fcr\u00fcc\u00fc veya gaz yeniden \u0131s\u0131tma alternatiflerinden daha d\u00fc\u015f\u00fck \u00f6zg\u00fcl enerji t\u00fcketimine sahiptir. 300 \u00e7al\u0131\u015fma g\u00fcn\u00fc i\u00e7in 0,4 RMB\/kWh elektrik maliyetiyle y\u0131ll\u0131k elektrik maliyeti yakla\u015f\u0131k 43.200 RMB'dir; bu da bak\u0131r eritme sekt\u00f6r\u00fcndeki her \u00f6l\u00e7ekteki ticari bir MPA kurulumu i\u00e7in en d\u00fc\u015f\u00fck y\u0131ll\u0131k i\u015fletme maliyetlerinden biridir.<\/li>\n
    • \u2713<\/span>
      \nSo\u011fuk Yo\u011funla\u015ft\u0131rma \u00d6n A\u015famas\u0131, MPA Y\u00fck\u00fcn\u00fc Azalt\u0131rken Asit Buhar\u0131n\u0131 Yeniden Kullan\u0131m \u0130\u00e7in Geri Kazand\u0131r\u0131r:<\/strong> MPA \u00fcnitesinin \u00f6n\u00fcne kurulan so\u011fuk yo\u011fu\u015fma kulesi, asit buhar\u0131n\u0131n \u00f6nemli bir k\u0131sm\u0131n\u0131 prosese geri kazand\u0131r\u0131labilen s\u0131v\u0131 yo\u011fu\u015fma suyu olarak geri kazan\u0131r. Bu, ayn\u0131 zamanda MPA emici tabakas\u0131na sunulan giri\u015f kirletici y\u00fck\u00fcn\u00fc azalt\u0131r (hizmet \u00f6mr\u00fcn\u00fc uzat\u0131r) ve de\u011ferli asidi at\u0131k olarak i\u015fleme tabi tutmak yerine proseste yeniden kullan\u0131m i\u00e7in yakalar. \u0130ki a\u015famal\u0131 yakla\u015f\u0131m \u2013 so\u011fuk yo\u011fu\u015fma geri kazan\u0131m\u0131 + MPA ar\u0131tma \u2013 bak\u0131r eritme asit buhar\u0131 ak\u0131\u015flar\u0131 i\u00e7in en uygun konfig\u00fcrasyondur.<\/li>\n
    • \u2713<\/span>
      \nKompakt 3,6\u00d73,6\u00d713,2 m boyutlar\u0131yla, k\u0131s\u0131tl\u0131 elektroliz salonu alanlar\u0131na kurulabilir:<\/strong> Bak\u0131r elektroliz tesisleri, h\u00fccre s\u0131ralar\u0131, do\u011frultucu \u00fcniteler ve asit y\u00f6netim altyap\u0131s\u0131 aras\u0131nda s\u0131n\u0131rl\u0131 serbest zemin alan\u0131 bulunan, karakteristik olarak yo\u011fun ekipman yerle\u015fimlerine sahiptir. BLCNXB-2W'nin 13 m\u00b2'lik minimum yerle\u015fim alan\u0131, geleneksel alkali y\u0131kama y\u00fckseltmelerinde gerekli olan daha b\u00fcy\u00fck y\u0131kay\u0131c\u0131 tank\u0131, pompa ve reaktif depolama altyap\u0131s\u0131 i\u00e7in kullan\u0131lamayacak alanlara kurulmas\u0131n\u0131 m\u00fcmk\u00fcn k\u0131lar.<\/li>\n
    • \u2713<\/span>
      \nYunnan Ekolojik K\u0131rm\u0131z\u0131 \u00c7izgisinin Uygulanmas\u0131 Kapsam\u0131nda Proaktif Konumland\u0131rma:<\/strong> Yunnan'\u0131n \"\u00dc\u00e7 Hat ve Bir Liste\" \u00e7er\u00e7evesi, bak\u0131r eritme tesisleri i\u00e7in \u00e7ok y\u0131ll\u0131k bir d\u00fczenleyici s\u0131k\u0131la\u015ft\u0131rma s\u00fcreci olu\u015fturuyor. Mevcut emisyon s\u0131n\u0131rlar\u0131n\u0131 zaten a\u015fan MPA teknolojisinin kurulumuyla, tesis, gelecekteki standart revizyonlar\u0131na yan\u0131t olarak daha fazla sermaye yat\u0131r\u0131m\u0131 gerektirme olas\u0131l\u0131\u011f\u0131n\u0131 azaltan bir uyumluluk tamponu olu\u015fturmu\u015ftur. Mod\u00fcler tasar\u0131m ayr\u0131ca, gelecekteki d\u00fczenlemeler gerektirirse ek kapasite eklenmesine de olanak tan\u0131r.<\/li>\n<\/ul>\n

      Teknoloji Kar\u015f\u0131la\u015ft\u0131rmas\u0131: Bak\u0131r Eritme Asit Sisi \u0130\u00e7in MPA ve Geleneksel Alternatifler<\/h3>\n
      \n\n\n\n\n\n\n\n\n\n\n\n
      Kriter<\/th>\nManyetik Duman Azaltma<\/th>\nAlkali (NaOH) ile Temizleme<\/th>\nGGH + Seyreltme<\/th>\n<\/tr>\n<\/thead>\n
      Beyaz t\u00fcy\u00fcn ortadan kald\u0131r\u0131lmas\u0131<\/td>\nTamamlanm\u0131\u015f (g\u00f6r\u00fcnmez)<\/td>\nHay\u0131r (pus devam ediyor)<\/td>\nK\u0131smi<\/td>\n<\/tr>\n
      Alkali reaktifi gereklidir.<\/td>\nHi\u00e7biri<\/td>\nEvet (devam eden NaOH maliyeti)<\/td>\nHi\u00e7biri<\/td>\n<\/tr>\n
      A\u011f\u0131r metaller i\u00e7eren ikincil at\u0131k su<\/td>\nHi\u00e7biri<\/td>\nY\u00fcksek hacimli (s\u00fclfat + Cu, As)<\/td>\nHi\u00e7biri<\/td>\n<\/tr>\n
      S\u00fclf\u00fcrik asit buhar\u0131 giderme verimlili\u011fi<\/td>\n\u226597%<\/td>\n\u224885\u201390%<\/td>\nYok (kald\u0131rma yok)<\/td>\n<\/tr>\n
      \u00c7al\u0131\u015fma g\u00fcc\u00fc (kW)<\/td>\n15 kW<\/td>\n40\u201380 kW (pompalar + fanlar)<\/td>\n60\u2013120 kW<\/td>\n<\/tr>\n
      Ekipman ayak izi<\/td>\n13 m\u00b2 (3,6\u00d73,6 m)<\/td>\nB\u00fcy\u00fck (kap + pompa + depo)<\/td>\nOrta<\/td>\n<\/tr>\n
      Asit geri kazan\u0131m potansiyeli<\/td>\nEvet (yukar\u0131 ak\u0131\u015f so\u011fuk kondenser)<\/td>\nHay\u0131r (at\u0131k olarak n\u00f6tralize edildi)<\/td>\nK\u0131smi<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n<\/div>\n<\/section>\n
      \n

      <\/p>\n

      \n

      06 \u2014 Operasyonel Sonu\u00e7lar<\/p>\n

      \u0130lk Seferde Devreye Alma Ba\u015far\u0131s\u0131 ve Do\u011frulanm\u0131\u015f Sistem Performans\u0131<\/h2>\n

      Manyetik duman azaltma \u00fcnitesi ilk \u00e7al\u0131\u015ft\u0131rmada tam ba\u015far\u0131 elde etti. T\u00fcm i\u015fletme verileri ve duman giderme performans\u0131, ilk \u00e7al\u0131\u015ft\u0131rmadan itibaren tasar\u0131m hedeflerini kar\u015f\u0131lad\u0131. Baca egzozu, t\u00fcm normal \u00e7al\u0131\u015fma ko\u015fullar\u0131nda ger\u00e7ekten g\u00f6r\u00fcnmez hale geldi ve daha \u00f6nce t\u00fcm atmosferik ko\u015fullar alt\u0131nda bak\u0131r eritme tesisinin \u00fczerinde g\u00f6r\u00fclebilen asit sisi beyaz duman\u0131n\u0131n tamamen ortadan kalkt\u0131\u011f\u0131n\u0131 do\u011frulad\u0131.<\/p>\n

      \n
      \n
      \u226410<\/div>\n
      mg\/Nm\u00b3<\/div>\n
      \u00c7\u0131k\u0131\u015f Kar\u0131\u015f\u0131k Kirletici Yo\u011funlu\u011fu<\/div>\n<\/div>\n
      \n
      15 kW<\/div>\n
      \u00c7al\u0131\u015ft\u0131rma G\u00fcc\u00fc<\/div>\n
      Tam Sistem Y\u00fck\u00fc<\/div>\n<\/div>\n
      \n
      4.32<\/div>\n
      10.000 RMB\/y\u0131l<\/div>\n
      Y\u0131ll\u0131k Elektrik Maliyeti<\/div>\n<\/div>\n
      \n
      300<\/div>\n
      g\u00fcn\/y\u0131l<\/div>\n
      Y\u0131ll\u0131k \u00c7al\u0131\u015fma G\u00fcnleri<\/div>\n<\/div>\n<\/div>\n

      \"Bak\u0131r<\/p>\n<\/section>\n

      \n

      <\/p>\n

      \n

      07 \u2014 Uygulama Uyar\u0131lar\u0131<\/p>\n

      Bak\u0131r Eritme \u0130\u015fleminde Elektroliz Y\u00f6ntemiyle Asit Buhar\u0131 Uygulamalar\u0131 \u0130\u00e7in Kritik M\u00fchendislik Hususlar\u0131<\/h2>\n
        \n
      • \u26a0\ufe0f<\/span>
        \nUzun boru hatlar\u0131na sahip \u00e7ok say\u0131da asit buhar\u0131 reaksiyon kab\u0131, boru hatt\u0131 tasar\u0131m\u0131ndan \u00f6nce gaz ak\u0131\u015f alan\u0131 sim\u00fclasyonu gerektirir:<\/strong> Bak\u0131r \u00fcretim tesislerindeki s\u00fclf\u00fcrik asit elektroliz ve buharla\u015ft\u0131rma sistemi, genellikle geni\u015f bir alana yay\u0131lm\u0131\u015f \u00e7ok say\u0131da reaksiyon kab\u0131, buharla\u015ft\u0131rma tank\u0131 ve toplama noktas\u0131na sahiptir. Toplama noktalar\u0131 ile MPA \u00fcnitesi aras\u0131ndaki uzun boru hatlar\u0131, asimetrik ak\u0131\u015f da\u011f\u0131l\u0131m\u0131na neden olur: ind\u00fcklemeli \u00e7eki\u015f fan\u0131na daha yak\u0131n olan kaplar orant\u0131s\u0131z derecede y\u00fcksek hava ak\u0131\u015f\u0131 al\u0131rken, uzaktaki kaplar yetersiz ekstraksiyon al\u0131r. Bu durum, kanal boyutland\u0131rmas\u0131 tamamlanmadan \u00f6nce CFD gaz ak\u0131\u015f alan\u0131 modellemesi ile te\u015fhis edilmeli ve d\u00fczeltilmelidir; ayr\u0131ca dengelemeyi sa\u011flamak i\u00e7in her bir bran\u015f hatt\u0131na manuel damperler tak\u0131lmal\u0131d\u0131r. Bu ad\u0131m\u0131 atlayan tesisler, devreye alma i\u015fleminden sonra reaksiyon kaplar\u0131n\u0131n -501'inin yetersiz topland\u0131\u011f\u0131n\u0131 ve \u00e7al\u0131\u015fma ortam\u0131na asit buhar\u0131 yaymaya devam etti\u011fini s\u0131kl\u0131kla tespit eder.<\/li>\n
      • \u26a0\ufe0f<\/span>
        \nGeleneksel alkali ar\u0131tma y\u00f6ntemi, bak\u0131r, arsenik ve a\u011f\u0131r metaller i\u00e7eren ve basit\u00e7e de\u015farj edilemeyen s\u00fclfatl\u0131 at\u0131k su \u00fcretir:<\/strong> Gelecekteki bir y\u00fckseltme veya acil durum plan\u0131, MPA \u00fcnitesinin \u00f6n\u00fcne veya arkas\u0131na alkali y\u0131kama a\u015famas\u0131 eklemeyi i\u00e7eriyorsa, ortaya \u00e7\u0131kan at\u0131k su sadece sodyum s\u00fclfat veya kalsiyum s\u00fclfat de\u011fil, ayn\u0131 zamanda elektroliz elektrolitinden kaynaklanan bak\u0131r, arsenik ve kadmiyum da i\u00e7erir. Bu durum, at\u0131k suyu standart end\u00fcstriyel at\u0131k su yerine potansiyel olarak tehlikeli at\u0131k olarak s\u0131n\u0131fland\u0131r\u0131r ve \u00f6zel ar\u0131tma veya prosese geri d\u00f6nd\u00fcrme gerektirir. \u0130\u015fte tam olarak bu nedenle bu uygulama i\u00e7in kuru MPA yakla\u015f\u0131m\u0131 se\u00e7ilmi\u015ftir ve reaktif i\u00e7ermeyen tasar\u0131m felsefesinden herhangi bir sapma, tam bir tehlikeli at\u0131k s\u0131n\u0131fland\u0131rma incelemesine tabi tutulmal\u0131d\u0131r.<\/li>\n
      • \u26a0\ufe0f<\/span>
        \nMPA emici \u00fcnitesinden \u00e7\u0131kan s\u00fclf\u00fcrik asit kondensat\u0131, proses kontroll\u00fc bir asit ak\u0131\u015f\u0131 olarak y\u00f6netilmelidir:<\/strong> BLCNXB-2W emici tabakas\u0131 taraf\u0131ndan yakalanan yo\u011fu\u015fma suyu, seyreltik s\u00fclf\u00fcrik asit i\u00e7erir. \u0130la\u00e7 veya eritme uygulamalar\u0131ndan elde edilen yo\u011fu\u015fma suyundan farkl\u0131 olarak, bu yo\u011fu\u015fma suyu, elektroliz banyosu i\u00e7in geri d\u00f6n\u00fc\u015f asidi olarak do\u011frudan proses yeniden kullan\u0131m de\u011ferine sahip olabilir. Yo\u011fu\u015fma suyunun bertaraf yolunu kesinle\u015ftirmeden \u00f6nce, pH, bak\u0131r i\u00e7eri\u011fi, arsenik i\u00e7eri\u011fi ve elektrolizle ilgili di\u011fer parametrelerin laboratuvar analizini yap\u0131n. Kalite uygunsa, yo\u011fu\u015fma suyunu at\u0131k olarak i\u015flemek yerine do\u011frudan asit y\u00f6netim sistemine geri y\u00f6nlendirin.<\/li>\n
      • \u26a0\ufe0f<\/span>
        \nMPA giri\u015f y\u00fcklemesinin kesinle\u015ftirilmesinden \u00f6nce so\u011fuk yo\u011fu\u015fma kulesinin performans\u0131n\u0131n do\u011frulanmas\u0131 gerekmektedir:<\/strong> So\u011fuk yo\u011fu\u015fma kulesi, gaz MPA \u00fcnitesine girmeden \u00f6nce asit sisinin \u00f6nemli bir k\u0131sm\u0131n\u0131 s\u0131v\u0131 yo\u011fu\u015fma suyu olarak uzakla\u015ft\u0131r\u0131r. MPA giri\u015f spesifikasyonu (50 mg\/Nm\u00b3 kar\u0131\u015f\u0131k kirletici y\u00fck\u00fc), ham evaporat\u00f6r buhar bile\u015fimine de\u011fil, so\u011fuk yo\u011fu\u015fma kulesi sonras\u0131 gaz bile\u015fimine dayanmaktad\u0131r. So\u011fuk yo\u011fu\u015fma kulesi yetersiz so\u011futma suyu ak\u0131\u015f\u0131, yo\u011fu\u015fma suyu y\u00fczeylerinin kirlenmesi veya y\u00fcksek ortam s\u0131cakl\u0131\u011f\u0131 nedeniyle yetersiz performans g\u00f6sterirse, ger\u00e7ek MPA giri\u015f y\u00fck\u00fc tasar\u0131m spesifikasyonunu a\u015facakt\u0131r. So\u011fuk yo\u011fu\u015fma kulesi \u00e7\u0131k\u0131\u015f konsantrasyonunu ayr\u0131 olarak izleyin ve MPA tasar\u0131m\u0131n\u0131n, beklenen maksimum yo\u011fu\u015fma kulesi sonras\u0131 y\u00fck\u00fcn \u00fczerinde 20% konsantrasyon marj\u0131na sahip oldu\u011fundan emin olun.<\/li>\n
      • \u26a0\ufe0f<\/span>
        \nElektrolizle asit \u00fcretimi oran\u0131ndaki de\u011fi\u015fim, buharla\u015fma gaz\u0131 hacmini ve asit buhar\u0131 konsantrasyonunu do\u011frudan etkiler:<\/strong> Elektrolizle bak\u0131r \u00fcretimi yapan tesislerin \u00fcretim kapasitesi, elektrik tarifesi ekonomisi, katot talebi ve h\u00fccre hatlar\u0131n\u0131n planl\u0131 bak\u0131m\u0131yla de\u011fi\u015fkenlik g\u00f6sterir. Bu \u00fcretim varyasyonlar\u0131, elektrolit hacminde, buharla\u015fma oran\u0131nda ve dolay\u0131s\u0131yla MPA sistemine giren gaz hacmi ve asit buhar\u0131 konsantrasyonunda kar\u015f\u0131l\u0131k gelen de\u011fi\u015fikliklere neden olur. BLEMG-1KA kontrol sistemi manyetik alan yo\u011funlu\u011funu otomatik olarak ayarlar, ancak devreye alma s\u0131ras\u0131nda kurulan manuel damper dengesi belirli bir \u00fcretim \u00e7al\u0131\u015fma noktas\u0131 i\u00e7in kalibre edilmi\u015ftir. \u00dcretim h\u0131z\u0131 kal\u0131c\u0131 olarak de\u011fi\u015firse (\u00f6rne\u011fin, kapasite geni\u015flemesi veya daralmas\u0131), damper dengesi yeniden kalibre edilmelidir.<\/li>\n
      • \u26a0\ufe0f<\/span>
        \nT\u00fcm havaland\u0131rma kanallar\u0131, fan g\u00f6vdeleri, damperler ve ba\u011flant\u0131 flan\u015flar\u0131, s\u00fcrekli s\u00fclf\u00fcrik asit buhar\u0131 uygulamas\u0131 i\u00e7in belirtilmelidir:<\/strong> Standart karbon \u00e7eli\u011fi veya hatta 304 paslanmaz \u00e7elik, bak\u0131r elektroliz gaz\u0131n\u0131n karakteristik konsantrasyonlar\u0131nda s\u00fclf\u00fcrik asit buhar\u0131yla s\u00fcrekli temas halinde h\u0131zla korozyona u\u011frar. T\u00fcm kanal sistemleri, fan g\u00f6vdeleri ve genle\u015fme derzleri i\u00e7in FRP (fiber takviyeli plastik) veya aside dayan\u0131kl\u0131 kau\u00e7uk kapl\u0131 \u00e7elik kullan\u0131n. T\u00fcm flan\u015fl\u0131 ba\u011flant\u0131larda aside dayan\u0131kl\u0131 conta malzemeleri (PTFE veya e\u015fde\u011feri) kullan\u0131lmal\u0131d\u0131r. Toplama ba\u015fl\u0131klar\u0131ndan MPA \u00fcnitesine kadar olan kanal hatt\u0131 boyunca korozyona dayan\u0131kl\u0131 malzemelerin belirtilmemesi, bu uygulamada sistemin erken ar\u0131zalanmas\u0131n\u0131n en yayg\u0131n nedenidir.<\/li>\n<\/ul>\n<\/section>\n
        \n

        <\/p>\n

        \n

        08 \u2014 M\u00fchendislikten \u00c7\u0131kar\u0131mlar<\/p>\n

        Bu Bak\u0131r Eritme Elektroliz Projesinden \u00c7\u0131kar\u0131labilecek D\u00f6rt Uygulanabilir Ders<\/h2>\n
          \n
        • 1<\/span>
          \n\u0130kincil at\u0131k su \u00fcretmeme \u015fart\u0131, bak\u0131r eritme uygulamalar\u0131nda teknoloji se\u00e7iminde belirleyici bir fakt\u00f6rd\u00fcr.<\/strong> \u0130\u015flem ak\u0131\u015f\u0131nda a\u011f\u0131r metaller (bak\u0131r, arsenik, kadmiyum) bulundu\u011funda ve d\u00fczenleyici ve at\u0131k y\u00f6netimi ortam\u0131 s\u0131k\u0131 oldu\u011funda \u2014 Yunnan'\u0131n ekolojik koruma \u00e7er\u00e7evesinde oldu\u011fu gibi \u2014 ar\u0131tma i\u015fleminde s\u0131v\u0131 reaktifin varl\u0131\u011f\u0131 veya yoklu\u011fu, genellikle ar\u0131tma verimlili\u011fi veya sermaye maliyeti de\u011fil, teknoloji se\u00e7iminde belirleyici kriter olur. Alkali reaktif ilavesi gerektiren ve a\u011f\u0131r metal bula\u015fm\u0131\u015f at\u0131k su \u00fcreten herhangi bir teknoloji, bu ba\u011flamda orant\u0131s\u0131z bir uyumluluk y\u00fck\u00fcyle kar\u015f\u0131 kar\u015f\u0131ya kal\u0131r. MPA kuru prosesi bu sorunun tamam\u0131n\u0131 ortadan kald\u0131r\u0131r.<\/li>\n
        • 2<\/span>
          \nMPA'n\u0131n \u00f6ncesinde uygulanan so\u011fuk yo\u011funla\u015ft\u0131rma \u00f6n ar\u0131tma i\u015flemi, y\u00fcksek konsantrasyonlu asit sisi ak\u0131\u015flar\u0131 i\u00e7in en uygun iki a\u015famal\u0131 konfig\u00fcrasyondur.<\/strong> Bu projede kullan\u0131lan so\u011fuk yo\u011fu\u015fma kulesi iki i\u015flevi birden yerine getiriyor: hem proses yeniden kullan\u0131m\u0131 i\u00e7in s\u0131v\u0131 asidi geri kazan\u0131yor (bak\u0131r elektrolizinde de\u011ferlidir) hem de MPA emici tabakas\u0131ndaki giri\u015f y\u00fck\u00fcn\u00fc azaltarak emici tabakan\u0131n kullan\u0131m \u00f6mr\u00fcn\u00fc uzat\u0131yor. Ham gaz asit buhar\u0131 konsantrasyonunun 50 mg\/Nm\u00b3'\u00fc \u00f6nemli \u00f6l\u00e7\u00fcde a\u015ft\u0131\u011f\u0131 herhangi bir uygulamada, MPA \u00fcnitesinden \u00f6nce so\u011fuk yo\u011fu\u015fma veya k\u0131smi \u00f6n y\u0131kama a\u015famas\u0131 eklemek tercih edilen konfig\u00fcrasyondur ve yo\u011fu\u015fma suyu geri kazan\u0131m yolu, teknoloji se\u00e7iminin ekonomik analizine dahil edilmelidir.<\/li>\n
        • 3<\/span>
          \n\u00c7ok hazneli asit buhar\u0131 toplama sistemleri i\u00e7in gaz ak\u0131\u015f alan\u0131 modellemesi zorunludur, iste\u011fe ba\u011fl\u0131 de\u011fildir.<\/strong> Bu proje i\u00e7in haz\u0131rlanan m\u00fchendislik deneyimi \u00f6zetinde, asit buhar\u0131 boru hatt\u0131 g\u00fczergah\u0131n\u0131n karma\u015f\u0131kl\u0131\u011f\u0131, gaz ak\u0131\u015f\u0131 sim\u00fclasyonu ve manuel damper dengelemesi gerektiren \u00f6nemli bir m\u00fchendislik zorlu\u011fu olarak a\u00e7\u0131k\u00e7a belirtilmi\u015ftir. Ortak bir toplama ba\u015fl\u0131\u011f\u0131na ba\u011fl\u0131 d\u00f6rt veya daha fazla reaksiyon kab\u0131 veya buharla\u015ft\u0131rma tank\u0131 bulunan herhangi bir bak\u0131r eritme tesisinde, kanal a\u011f\u0131ndaki gaz ak\u0131\u015f alan\u0131n\u0131n CFD modellemesi, iste\u011fe ba\u011fl\u0131 bir ekleme de\u011fil, detayl\u0131 tasar\u0131m a\u015famas\u0131nda s\u00f6zle\u015fme gere\u011fi teslim edilmesi gereken bir unsur olmal\u0131d\u0131r. Modellemenin maliyeti, ak\u0131\u015f dengesizli\u011fini d\u00fczeltmek i\u00e7in devreye alma sonras\u0131 yap\u0131lacak onar\u0131mlar\u0131n maliyetine k\u0131yasla \u00f6nemsizdir.<\/li>\n
        • 4<\/span>
          \nY\u0131ll\u0131k 43.200 RMB'lik elektrik maliyeti, 20.000 Nm\u00b3\/h asit buhar\u0131 uyumlulu\u011fu i\u00e7in alt\u0131n standart\u0131 temsil etmektedir.<\/strong> BLCNXB-2W'nin 15 kW \u00e7al\u0131\u015fma g\u00fcc\u00fc ve \u226597% ar\u0131tma verimlili\u011fiyle saatte 20.000 Nm\u00b3'l\u00fck debi sunmas\u0131, bak\u0131r eritme sekt\u00f6r\u00fcnde maliyet etkin uyumluluk i\u00e7in bir \u00f6l\u00e7\u00fct olu\u015fturmaktad\u0131r. Tesis y\u00f6netimine yat\u0131r\u0131m gerek\u00e7esini sunarken, y\u0131ll\u0131k 43.200 RMB'lik elektrik i\u015fletme giderini, geleneksel alkali y\u0131kama alternatifinin birle\u015fik reaktif, at\u0131k su ar\u0131tma ve enerji maliyetiyle kar\u015f\u0131la\u015ft\u0131r\u0131n; aradaki fark genellikle y\u0131ll\u0131k MPA elektrik maliyetinin 5-8 kat\u0131d\u0131r ve bu da sermaye yat\u0131r\u0131m\u0131 i\u00e7in g\u00fc\u00e7l\u00fc bir geri \u00f6deme arg\u00fcman\u0131 olu\u015fturmaktad\u0131r.<\/li>\n<\/ul>\n<\/section>\n
          \n

          <\/p>\n

          \n

          09 \u2014 S\u0131k\u00e7a Sorulan Sorular<\/p>\n

          Bak\u0131r Eritme Asit Sisinin Manyetik Y\u00f6ntemle Giderilmesi: On Soruya Cevap<\/h2>\n

          Elektrolitik bak\u0131r ve bak\u0131r eritme tesislerindeki \u00e7evre uyumluluk m\u00fchendisleri, tesis y\u00f6neticileri ve \u0130SG ekiplerinden MPA teknolojisini de\u011ferlendirirken gelen sorular.<\/p>\n

          \nS1. Bu bak\u0131r eritme asit sisi uygulamas\u0131 i\u00e7in geleneksel alkali y\u0131kama y\u00f6ntemi neden reddedildi ve MPA tercih edildi?<\/summary>\n
          Alkali y\u0131kama y\u00f6nteminin reddedilmesine ve MPA'n\u0131n se\u00e7ilmesine yol a\u00e7an \u00fc\u00e7 fakt\u00f6r \u015funlard\u0131r: (1) S\u00fclf\u00fcrik asit sisinin NaOH veya Ca(OH)\u2082 ile n\u00f6tralizasyonu sonucu olu\u015fan at\u0131k su, elektroliz elektrolitinden kaynaklanan \u00e7\u00f6z\u00fcnm\u00fc\u015f bak\u0131r, arsenik ve kadmiyum i\u00e7erir; bu da onu potansiyel olarak tehlikeli at\u0131k olarak s\u0131n\u0131fland\u0131r\u0131r ve y\u0131kama tasarruflar\u0131ndan \u00e7ok daha maliyetli bir ikincil ar\u0131tma veya bertaraf y\u00fck\u00fcml\u00fcl\u00fc\u011f\u00fc yarat\u0131r; (2) Alkali y\u0131kama, g\u00f6r\u00fcn\u00fcr beyaz duman\u0131 ortadan kald\u0131rmaz - duman\u0131 olu\u015fturan doymu\u015f su buhar\u0131 ve mikron alt\u0131 aerosol fraksiyonu y\u0131kay\u0131c\u0131 dolgusundan ge\u00e7er; ve (3) MPA, s\u0131f\u0131r reaktif giri\u015fi, s\u0131f\u0131r at\u0131k su \u00e7\u0131k\u0131\u015f\u0131 ve \u226597% ar\u0131tma verimlili\u011fine sahip kuru bir i\u015flemdir ve alkali y\u0131kaman\u0131n kar\u015f\u0131layamad\u0131\u011f\u0131 \u00fc\u00e7 gereksinimi de kar\u015f\u0131lar.<\/div>\n<\/details>\n
          \nS2. MPA sistemi, s\u00fclf\u00fcrik asit end\u00fcstrisi emisyonlar\u0131 i\u00e7in GB 26132\u22122010 standard\u0131na uygun mu?<\/summary>\n
          Evet. Kombine ar\u0131tma sistemi \u2013 so\u011fuk yo\u011fu\u015fma kulesi ve ard\u0131ndan MPA ar\u0131tma \u2013 GB 26132\u22122010'da belirtilen t\u00fcm ge\u00e7erli parametrelere uygunluk sa\u011flamaktad\u0131r: NOx \u226450 mg\/Nm\u00b3, SO\u2082 \u226430 mg\/Nm\u00b3 ve partik\u00fcl madde \u226410 mg\/Nm\u00b3, ayr\u0131ca g\u00f6r\u00fcn\u00fcr beyaz duman olmamas\u0131 ve anormal koku olmamas\u0131 \u015fart\u0131 da kar\u015f\u0131lanmaktad\u0131r. \u0130lk devreye alma i\u015flemi, t\u00fcm parametrelerin ayn\u0131 anda yasal s\u0131n\u0131rlar\u0131n alt\u0131nda oldu\u011funu ve baca egzozunun ilk \u00e7al\u0131\u015ft\u0131rmadan itibaren tamamen g\u00f6r\u00fcnmez oldu\u011funu do\u011frulam\u0131\u015ft\u0131r.<\/div>\n<\/details>\n
          \nS3. BLCNXB-2W cihaz\u0131n\u0131n saatte 20.000 Nm\u00b3 bak\u0131r elektroliz asit buhar\u0131n\u0131 i\u015fleme kapasitesinin y\u0131ll\u0131k i\u015fletme maliyeti nedir?<\/summary>\n
          BLCNXB-2W sistemi 15 kW g\u00fc\u00e7le \u00e7al\u0131\u015fmaktad\u0131r. Y\u0131lda 300 g\u00fcn, 0,4 RMB\/kWh fiyatla \u00e7al\u0131\u015ft\u0131r\u0131ld\u0131\u011f\u0131nda, y\u0131ll\u0131k elektrik maliyeti yakla\u015f\u0131k 43.200 RMB'dir. Reaktif maliyeti yoktur. Toplam y\u0131ll\u0131k i\u015fletme gideri, bu kapasitedeki ticari asit buhar\u0131 giderme sistemleri aras\u0131nda en d\u00fc\u015f\u00fckler aras\u0131ndad\u0131r. Kar\u015f\u0131la\u015ft\u0131rma olarak, e\u015fde\u011fer kapasiteli bir NaOH ar\u0131tma sistemi tipik olarak \u015fu maliyetleri i\u00e7erir: NaOH reaktif maliyeti 120.000\u2013200.000 RMB\/y\u0131l; at\u0131k su ar\u0131tma maliyeti 80.000\u2013150.000 RMB\/y\u0131l; pompalar ve fanlar i\u00e7in ek elektrik 60.000\u2013100.000 RMB\/y\u0131l \u2014 sermaye amortisman farklar\u0131 dikkate al\u0131nmadan \u00f6nce toplam y\u0131ll\u0131k i\u015fletme gideri MPA'n\u0131n 5-10 kat\u0131d\u0131r.<\/div>\n<\/details>\n
          \nSoru 4. MPA emici tabakas\u0131 taraf\u0131ndan tutulan s\u00fclf\u00fcrik asit kondensat\u0131 ne olur?<\/summary>\n
          MPA emici tabakas\u0131 taraf\u0131ndan tutulan yo\u011fu\u015fma suyu, seyreltik s\u00fclf\u00fcrik asit ve potansiyel olarak eser miktarda bak\u0131r, arsenik ve di\u011fer elektroliz prosesi kirleticileri i\u00e7erir. Devreye al\u0131nmadan \u00f6nce, yo\u011fu\u015fma suyunun pH'\u0131n\u0131, bak\u0131r i\u00e7eri\u011fini, arsenik i\u00e7eri\u011fini ve di\u011fer ilgili parametrelerini belirlemek i\u00e7in laboratuvar analizi yap\u0131lmal\u0131d\u0131r. Kalite, elektroliz banyosu veya asit y\u00f6netim sistemi \u00f6zellikleriyle uyumluysa, yo\u011fu\u015fma suyu do\u011frudan asit geri kazan\u0131m\u0131 olarak prosese geri d\u00f6nd\u00fcr\u00fclebilir. Kalite yeniden kullan\u0131m kriterlerini kar\u015f\u0131lam\u0131yorsa, yo\u011fu\u015fma suyu tesisin mevcut asit at\u0131k y\u00f6netim altyap\u0131s\u0131 arac\u0131l\u0131\u011f\u0131yla kontroll\u00fc bir asit ak\u0131\u015f\u0131 olarak y\u00f6netilir; genel at\u0131k su olarak de\u015farj edilmez.<\/div>\n<\/details>\n
          \nS5. Ortak toplama ba\u015fl\u0131\u011f\u0131na ba\u011flanan \u00e7oklu reaksiyon kab\u0131 havaland\u0131rma hatlar\u0131 boyunca gaz ak\u0131\u015f\u0131 nas\u0131l dengelenir?<\/summary>\n
          \u00c7oklu tankl\u0131 toplama sistemlerinde gaz ak\u0131\u015f dengesi iki tamamlay\u0131c\u0131 \u00f6nlemle sa\u011flan\u0131r: (1) Beklenen ak\u0131\u015f da\u011f\u0131l\u0131m\u0131 dengesizli\u011fini belirlemek ve bunu en aza indirgemek i\u00e7in kanal boyutland\u0131rmas\u0131na bilgi sa\u011flamak amac\u0131yla, detayl\u0131 tasar\u0131m a\u015famas\u0131nda tamamlanan t\u00fcm kanal a\u011f\u0131n\u0131n CFD gaz ak\u0131\u015f alan\u0131 modellemesi; ve (2) reaksiyon tank\u0131 havaland\u0131rma ba\u011flant\u0131s\u0131 ile ortak toplama ba\u015fl\u0131\u011f\u0131 aras\u0131ndaki her bir bran\u015f hatt\u0131na manuel kelebek damperlerin tak\u0131lmas\u0131. Sistem kurulduktan sonra, t\u00fcm tanklar her bir bran\u015fta pitot t\u00fcp\u00fc traversi ile \u00f6l\u00e7\u00fclen hedef hava ak\u0131\u015f\u0131n\u0131 alana kadar damperler devreye alma s\u0131ras\u0131nda kademeli olarak ayarlan\u0131r. Ayarland\u0131ktan sonra, damper pozisyonlar\u0131 kilitlenir ve ileride referans olmas\u0131 i\u00e7in devreye alma dok\u00fcman\u0131na kaydedilir.<\/div>\n<\/details>\n
          \nS6. S\u00fclf\u00fcrik asit buhar\u0131 servisinde kullan\u0131lan havaland\u0131rma kanallar\u0131 ve toplama ba\u015fl\u0131klar\u0131 i\u00e7in hangi malzeme \u00f6zellikleri gereklidir?<\/summary>\n
          Reaksiyon kab\u0131 havaland\u0131rma ba\u011flant\u0131lar\u0131ndan MPA \u00fcnitesine kadar t\u00fcm kanallar, fan g\u00f6vdeleri, damperler, genle\u015fme derzleri ve flan\u015fl\u0131 ba\u011flant\u0131lar, s\u00fcrekli s\u00fclf\u00fcrik asit buhar\u0131 servisi i\u00e7in belirtilmelidir. Kabul edilebilir malzemeler aras\u0131nda kanallar ve kap ba\u011flant\u0131lar\u0131 i\u00e7in FRP (cam elyaf takviyeli plastik), daha b\u00fcy\u00fck ana hatlar ve ge\u00e7i\u015fler i\u00e7in kau\u00e7uk kapl\u0131 karbon \u00e7elik, daha k\u00fc\u00e7\u00fck bran\u015fman hatlar\u0131 i\u00e7in aside dayan\u0131kl\u0131 PVC veya CPVC ve t\u00fcm flan\u015fl\u0131 ba\u011flant\u0131larda PTFE contalar bulunur. Standart karbon \u00e7elik bu serviste haftalar i\u00e7inde korozyona u\u011frar; 304 paslanmaz \u00e7elik ise aylar i\u00e7inde bozulur. Kar\u015f\u0131la\u015f\u0131lan belirli asit konsantrasyonu ve s\u0131cakl\u0131k aral\u0131\u011f\u0131 i\u00e7in uygunlu\u011fu teyit eden yaz\u0131l\u0131 bir korozyon m\u00fchendisli\u011fi incelemesi olmadan maliyeti d\u00fc\u015f\u00fcrmek i\u00e7in malzeme ikamelerini kabul etmeyin.<\/div>\n<\/details>\n
          \nS7. Elektroliz \u00fcretim h\u0131z\u0131 \u00f6nemli \u00f6l\u00e7\u00fcde artarsa \u200b\u200bveya azal\u0131rsa MPA performans\u0131 nas\u0131l de\u011fi\u015fir?<\/summary>\n
          BLEMG-1KA kontrol sistemi, baca gaz\u0131 parametrelerini s\u00fcrekli olarak \u00e7evrimi\u00e7i olarak izler ve manyetik alan yo\u011funlu\u011funu ger\u00e7ek zamanl\u0131 olarak ayarlayarak, 10%\u2013110% gaz hacmi \u00e7al\u0131\u015fma aral\u0131\u011f\u0131nda \u226597% ar\u0131tma verimlili\u011fini korur. Sistemi bu aral\u0131\u011f\u0131n d\u0131\u015f\u0131na \u00e7\u0131karan kal\u0131c\u0131 \u00fcretim h\u0131z\u0131 de\u011fi\u015fiklikleri (geni\u015fleme veya daralma) i\u00e7in, damper denge kalibrasyonu yeniden g\u00f6zden ge\u00e7irilmeli ve tasar\u0131m giri\u015f y\u00fcklemesi yeni \u00fcretim verimine g\u00f6re yeniden do\u011frulanmal\u0131d\u0131r. \u00d6nemli bir kapasite geni\u015fletme planlan\u0131yorsa, mevcut BLCNXB-2W \u00fcnitesinin yeni \u00fcretim h\u0131z\u0131 i\u00e7in yeterli kapasiteye sahip olup olmad\u0131\u011f\u0131 veya ek bir mod\u00fcle ihtiya\u00e7 duyulup duyulmad\u0131\u011f\u0131 m\u00fchendislik ekibiyle teyit edilmelidir.<\/div>\n<\/details>\n
          \nS8. Kurulum ne kadar s\u00fcrer ve bak\u0131r elektroliz tesisinin kapat\u0131lmas\u0131 gerekir mi?<\/summary>\n
          BLCNXB-2W \u00f6l\u00e7e\u011fi i\u00e7in, saha mobilizasyonundan devreye alma haz\u0131rl\u0131\u011f\u0131na kadar kurulum genellikle 3-5 hafta s\u00fcrer. Kanal \u00f6n imalat\u0131n\u0131n, mod\u00fcl montaj\u0131n\u0131n ve elektrik tesisat\u0131n\u0131n b\u00fcy\u00fck k\u0131sm\u0131, saha in\u015faat haz\u0131rl\u0131\u011f\u0131yla paralel olarak ilerler. Reaksiyon kab\u0131 havaland\u0131rma ba\u011flant\u0131s\u0131n\u0131n yap\u0131lmas\u0131 (ba\u011flant\u0131 s\u0131ras\u0131nda her bir kaptan gaz ak\u0131\u015f\u0131n\u0131n k\u0131sa s\u00fcreli\u011fine durdurulmas\u0131n\u0131 gerektirir), e\u015f zamanl\u0131 \u00fcretim etkisini en aza indirmek i\u00e7in kap toplama noktalar\u0131 aras\u0131nda a\u015famal\u0131 olarak ger\u00e7ekle\u015ftirilebilir. Planl\u0131 bak\u0131m pencereleri s\u0131ras\u0131nda bireysel kap ba\u011flant\u0131lar\u0131 yap\u0131l\u0131rken, ind\u00fcklemeli \u00e7eki\u015f fan\u0131 montaj\u0131 ve MPA \u00fcnitesi yap\u0131sal montaj\u0131 da devam edebilir.<\/div>\n<\/details>\n
          \nS9. Yunnan'daki bir bak\u0131r elektroliz tesisinde MPA \u00e7\u0131k\u0131\u015f\u0131nda hangi CEMS izleme sistemleri gereklidir?<\/summary>\n
          GB 26132\u22122010 ve Yunnan \u00dc\u00e7 Hat ve Bir Liste \u00e7er\u00e7evesi uyar\u0131nca, MPA \u00fcnitesi \u00e7\u0131k\u0131\u015f\u0131 (baca de\u015farj noktas\u0131) i\u00e7in partik\u00fcl madde, SO\u2082, NOx, oksijen konsantrasyonu, s\u0131cakl\u0131k, ak\u0131\u015f h\u0131z\u0131 ve nem i\u00e7eri\u011fi i\u00e7in CEMS kanallar\u0131 gereklidir. Baz\u0131 Yunnan ekolojik \u00e7evre b\u00fcrosu denetim ekipleri, genel partik\u00fcl CEMS kanal\u0131na ek olarak, \u00f6zellikle s\u00fclf\u00fcrik asit buhar\u0131 i\u00e7in periyodik manuel \u00f6rnekleme (izokinetik \u00f6rnekleme ve gravimetrik analiz ile \u00f6l\u00e7\u00fcl\u00fcr) de talep etmektedir. CEMS ekipman\u0131 sat\u0131n almadan \u00f6nce, yetkili makamla \u00f6zel izleme gereksinimlerini teyit ederek, izleme sisteminin kabul denetimi s\u0131ras\u0131nda kontrol edilecek t\u00fcm parametreleri kapsad\u0131\u011f\u0131ndan emin olunmal\u0131d\u0131r.<\/div>\n<\/details>\n
          \nS10. Bak\u0131r eritme veya demir d\u0131\u015f\u0131 metaller i\u00e7in asit buhar\u0131 MPA referans tesislerine ili\u015fkin yerinde inceleme ziyaretleri i\u00e7in ba\u015fka \u00f6rnekler mevcut mu?<\/summary>\n
          Evet. Manyetik Duman Azaltma teknolojisi, bu vaka \u00e7al\u0131\u015fmas\u0131nda belgelenen Yunnan elektroliz tesisinin \u00f6tesinde, asit sisi ar\u0131tma gereksinimleri olan \u00e7ok say\u0131da bak\u0131r eritme, elektroliz ve demir d\u0131\u015f\u0131 metal i\u015fleme tesisinde kullan\u0131lm\u0131\u015ft\u0131r. Nitelikli potansiyel m\u00fc\u015fteriler i\u00e7in, do\u011frulanm\u0131\u015f i\u015fletme izleme kay\u0131tlar\u0131na ve kabul muayene belgelerine eri\u015fim de dahil olmak \u00fczere referans saha ziyaretleri d\u00fczenlenebilir. Referans belgeleri talep etmek veya benzer bir bak\u0131r eritme veya demir d\u0131\u015f\u0131 metal asit sisi azaltma tesisine ziyaret ayarlamak i\u00e7in l\u00fctfen a\u015fa\u011f\u0131daki ileti\u015fim ba\u011flant\u0131s\u0131n\u0131 kullan\u0131n.<\/div>\n<\/details>\n<\/section>\n
          \n

          <\/p>\n

          \n

          Alkali reaktif kullanmadan asit buhar\u0131n\u0131n beyaz duman\u0131n\u0131 ortadan kald\u0131rmaya haz\u0131r m\u0131s\u0131n\u0131z?<\/p>\n

          End\u00fcstriyel Emisyon Kontrol \u00c7\u00f6z\u00fcmlerinin T\u00fcm Yelpazesini Ke\u015ffedin<\/h2>\n

          Bak\u0131r eritme i\u015flemlerinde kullan\u0131lan asit buhar\u0131n\u0131n kuru i\u015flemle manyetik olarak giderilmesinden Y\u00fcksek konsantrasyonlu VOC giderimi i\u00e7in rejeneratif termal oksidasyon sistemleri<\/a>M\u00fchendislik ekibimiz, en zorlu demir d\u0131\u015f\u0131 metal emisyon kontrol gereksinimleri i\u00e7in s\u0131f\u0131r ikincil at\u0131k \u00e7\u00f6z\u00fcmleri sunmaktad\u0131r.<\/p>\n

          Teknik Dan\u0131\u015fmanl\u0131k Talep Edin \u2192<\/a>
          \n          T\u00fcm Emisyon Kontrol Teknolojilerini Ke\u015ffedin<\/a><\/div>\n<\/section>\n

          <\/p>\n