{"id":2370,"date":"2024-09-13T07:05:27","date_gmt":"2024-09-13T07:05:27","guid":{"rendered":"https:\/\/www.winsonda.com\/?p=2370"},"modified":"2024-09-13T07:08:09","modified_gmt":"2024-09-13T07:08:09","slug":"advanced-wastewater-solutions","status":"publish","type":"post","link":"https:\/\/www.winsonda.com\/tr\/advanced-wastewater-solutions\/","title":{"rendered":"Geli\u015fmi\u015f At\u0131ksu \u00c7\u00f6z\u00fcmleri: K\u00f6m\u00fcr Kimyasal Tesislerinde 15 Ton Kar\u0131\u015f\u0131k Tuz Ana S\u0131v\u0131s\u0131"},"content":{"rendered":"

K\u00f6m\u00fcr kaynaklar\u0131 ile su kaynaklar\u0131n\u0131n g\u00fcn\u00fcm\u00fczdeki e\u015fitsiz da\u011f\u0131l\u0131m\u0131 ve k\u00f6m\u00fcr kimya end\u00fcstrisinin y\u00fcksek su t\u00fcketimi nedeniyle, modern k\u00f6m\u00fcr kimya end\u00fcstrisinin geli\u015fimi end\u00fcstriyel su al\u0131m\u0131 ve su kullan\u0131m\u0131 sorununu \u00e7\u00f6zmelidir. Modern k\u00f6m\u00fcr kimyasal at\u0131k su s\u0131f\u0131r emisyona yak\u0131n teknolojisi, ekolojik \u00e7evre ile enerji talebi aras\u0131ndaki \u00e7eli\u015fkiyi koordine etmenin ve k\u00f6m\u00fcr ile su kaynaklar\u0131 aras\u0131ndaki \u00e7eli\u015fkiyi \u00e7\u00f6zmenin anahtar\u0131d\u0131r. Daha sonra, g\u00fcnde 15 ton kar\u0131\u015f\u0131k tuz ana lik\u00f6r\u00fc i\u015fleyen b\u00fcy\u00fck bir k\u00f6m\u00fcr kimyasal i\u015fletmesi \u00f6rne\u011fi \u00fczerinden, k\u00f6m\u00fcr kimyasal at\u0131k suyunun s\u0131f\u0131r emisyonunun tipik proses yolunu ve at\u0131k suyun "s\u0131f\u0131r emisyonuna" ula\u015fmaya yard\u0131mc\u0131 olan temel prosesi tan\u0131taca\u011f\u0131z.<\/p>\n

B\u00fcy\u00fck k\u00f6m\u00fcr kimyasal i\u015fletmelerinden \u00e7\u0131kan at\u0131k sular\u0131n detaylar\u0131<\/h2>\n

M\u00fc\u015fteri, \u015fu anda d\u00fcnyan\u0131n in\u015fa halindeki en b\u00fcy\u00fck k\u00f6m\u00fcr kimya projesi olan devlete ait s\u00fcper b\u00fcy\u00fck bir enerji ve kimya i\u015fletmesidir. K\u00f6m\u00fcrden g\u00fcbreye, k\u00f6m\u00fcr kokla\u015ft\u0131rma, k\u00f6m\u00fcr tuzu, k\u00f6m\u00fcr bazl\u0131 metanol derin i\u015fleme ve k\u00f6m\u00fcrden ya\u011fa olmak \u00fczere olu\u015fturulan be\u015f b\u00fcy\u00fck end\u00fcstriyel y\u00f6n, \u00fclkemin k\u00f6m\u00fcr kalitesinin ve kalitesinin verimli bir \u015fekilde d\u00f6n\u00fc\u015ft\u00fcr\u00fclmesinin ve k\u00f6m\u00fcr kaynaklar\u0131n\u0131n yak\u0131ttan hammaddeye d\u00f6n\u00fc\u015ft\u00fcr\u00fclmesinin te\u015fvik edilmesinin \u00f6nc\u00fcleridir. Projenin ilk a\u015famas\u0131n\u0131n 1,8 milyon ton\/y\u0131l etilen glikol projesi, yeni k\u00f6m\u00fcr kimya end\u00fcstrisinin tipik bir temsilcisidir.<\/p>\n

K\u00f6m\u00fcr kimyasal tuz i\u00e7eren at\u0131k sular \u00e7o\u011funlukla \u00fcretim ve canl\u0131 ham su, ham k\u00f6m\u00fcr, \u00fcretim s\u00fcreci \u00fcretilen su ve su ar\u0131tma s\u00fcrecinden gelir. \u00dcretim s\u00fcrecinde \u00e7o\u011funlukla gaz y\u0131kama at\u0131k suyu, dola\u015f\u0131m suyu sistemi drenaj\u0131, tuzdan ar\u0131nd\u0131r\u0131lm\u0131\u015f su sistemi drenaj\u0131, yeniden kullan\u0131m sistemi konsantre suyu vb. \u00fcretim s\u00fcrecinde gelir ve bazen karma\u015f\u0131k bile\u015fim, y\u00fcksek tuz i\u00e7eri\u011fi ve y\u00fcksek organik i\u00e7erik ile karakterize edilen biyokimyasal ar\u0131tmadan sonraki at\u0131\u011f\u0131 da i\u00e7erir. K\u00f6m\u00fcr kimya end\u00fcstrisinin y\u00fcksek tuzlu at\u0131k suyu etkili bir \u015fekilde ar\u0131t\u0131lmazsa ciddi kirlili\u011fe neden olur ve \u00e7evreye ve \u00fcretime zarar verir.<\/p>\n

At\u0131k su bertaraf\u0131 i\u00e7in s\u0131f\u0131r de\u015farj rotas\u0131 ve son saf olmayan tuz ana lik\u00f6r\u00fc bertaraf\u0131ndaki sorunlar<\/h2>\n

K\u00f6m\u00fcr kimyasal \u00fcretiminde tuzlu at\u0131k su genellikle "\u00f6n ar\u0131tma + membran ar\u0131tma + buharla\u015ft\u0131rma kristalizasyonu" kombine bir ar\u0131tma s\u00fcrecini benimser. \u00d6n ar\u0131tma genellikle flotasyon, koag\u00fclasyon, filtrasyon ve di\u011fer ad\u0131mlar\u0131 i\u00e7erir. \u00d6n ar\u0131tmadan sonra at\u0131k su membran konsantrasyon sistemine girer. \u015eu anda, ar\u0131tma i\u00e7in \u00e7o\u011funlukla \u00e7ift membran y\u00f6ntemi (ultrafiltrasyon + ters ozmoz) kullan\u0131l\u0131r. Bu i\u015flemde elde edilen tatl\u0131 su, dola\u015f\u0131ml\u0131 so\u011futma suyu sistemi i\u00e7in ek su veya i\u015fletme \u00fcretimi i\u00e7in geri d\u00f6n\u00fc\u015ft\u00fcr\u00fclm\u00fc\u015f su olarak kullan\u0131labilirken, ar\u0131tma hacminin yakla\u015f\u0131k 35%'sini olu\u015fturan yo\u011funla\u015ft\u0131r\u0131lm\u0131\u015f tuzlu su, yo\u011funla\u015ft\u0131r\u0131lm\u0131\u015f tuzlu su ikincil konsantrasyon \u00fcnitesine girer. \u0130kincil konsantrasyondan sonra, tuzlu at\u0131k su hacminin yakla\u015f\u0131k 5%'sini olu\u015fturan y\u00fcksek konsantrasyonlu tuzlu su \u00fcretilir, tuzluluk oran\u0131 5% ila 8% veya daha y\u00fcksek olur ve sonraki buharla\u015ft\u0131rma kristalizasyonu i\u015flemi daha da yo\u011funla\u015ft\u0131r\u0131l\u0131r ve kat\u0131la\u015ft\u0131r\u0131l\u0131r. buharla\u015fma kristalle\u015fme s\u00fcreci<\/a><\/strong> At\u0131ksu i\u00e7erisindeki tuzun kristaller halinde \u00e7\u00f6keltilmesi i\u00e7in termal konsantrasyon kullan\u0131l\u0131r ve ana \u00e7\u00f6zelti biyokimyasal sisteme g\u00f6nderilir veya kurutularak ar\u0131t\u0131l\u0131r.<\/p>\n

K\u00f6m\u00fcr kimyasal at\u0131k suyunun s\u0131f\u0131r de\u015farj s\u00fcrecinde, en yayg\u0131n kullan\u0131lan ana lik\u00f6r kurutma i\u015flemi esas olarak tambur kurutma i\u015flemidir ve az miktarda p\u00fcsk\u00fcrtmeli kurutma i\u015flemi kullan\u0131l\u0131r. M\u00fc\u015fterinin yerinde tasar\u0131m\u0131 20 ton\/g\u00fcn kapasiteli bir tambur kurutma sistemi kullan\u0131yor ve i\u015fletim sorunlar\u0131 \u00e7ok a\u00e7\u0131k. 1. \u0130\u015fleme verimlili\u011fi d\u00fc\u015f\u00fckt\u00fcr ve kullan\u0131ma al\u0131nd\u0131\u011f\u0131ndan beri tasarlanan \u00e7al\u0131\u015fma durumuna ula\u015fmam\u0131\u015ft\u0131r. Ger\u00e7ek i\u015fleme hacmi tasarlanan hacmin yakla\u015f\u0131k 30%'sidir ve ana lik\u00f6r kurutulamaz; 2. Ana lik\u00f6r\u00fcn \u00e7\u0131k\u0131\u015f\u0131 yoktur, bu da buharla\u015ft\u0131r\u0131c\u0131ya geri sirk\u00fclasyon hacminin artmas\u0131na neden olur, \u00f6n u\u00e7 buharla\u015ft\u0131r\u0131c\u0131n\u0131n normal \u00e7al\u0131\u015fmas\u0131n\u0131 etkiler ve tuz ay\u0131rma kalitesini etkiler ve s\u0131f\u0131r emisyonun ekonomik faydalar\u0131n\u0131 etkiler; 3. Tambur kurutma sisteminin s\u0131k s\u0131k temizlenmesi gerekir ve kaz\u0131y\u0131c\u0131 mesafesinin ayarlanmas\u0131 ve kaz\u0131y\u0131c\u0131n\u0131n d\u00fczenli olarak de\u011fi\u015ftirilmesi gerekir, bu da y\u00fcksek bak\u0131m maliyetlerine sahiptir; bo\u015faltma hunisi genellikle k\u00f6pr\u00fclenir ve ar\u0131za oran\u0131 y\u00fcksektir; 4. Enerji t\u00fcketimi y\u00fcksektir. M\u00fc\u015fteri, y\u00fcksek otomasyona, y\u00fcksek i\u015fleme verimlili\u011fine ve iyi bertaraf etkisine sahip yeni bir ana lik\u00f6r kurutma cihaz\u0131 bulmay\u0131 umuyor.<\/p>\n

Kar\u0131\u015f\u0131k tuz ana lik\u00f6r\u00fc i\u00e7in y\u00fcksek verimli \u00e7\u00f6z\u00fcm \u2014 Winsonda d\u00fc\u015f\u00fck s\u0131cakl\u0131kl\u0131 buharla\u015ft\u0131rma kurutma cihaz\u0131<\/h2>\n

Winsonda, erken a\u015famada derinlemesine ileti\u015fim ve sistematik k\u00fc\u00e7\u00fck \u00f6l\u00e7ekli ve pilot testlerin ard\u0131ndan orijinal tambur kurutma s\u00fcrecini y\u00fckseltti ve de\u011fi\u015ftirdi ve 15 ton\/g\u00fcn d\u00fc\u015f\u00fck s\u0131cakl\u0131kta buharla\u015ft\u0131rma kurutma \u00e7\u00f6z\u00fcm\u00fc tasarlad\u0131 ve sa\u011flad\u0131. Winsonda'n\u0131n mod\u00fcler k\u0131zak montajl\u0131 tasar\u0131m\u0131, m\u00fc\u015fterinin k\u00fc\u00e7\u00fck yerindeki ger\u00e7ek sorun noktas\u0131na da uyuyor.<\/p>\n

1. At\u0131ksu toplama ve \u00f6n ar\u0131tma (flotasyon, koag\u00fclasyon ve filtrasyon vb.)<\/p>\n

2. Membran konsantrasyon teknolojisi ar\u0131tma (iz organik madde, mikrobiyal ila\u00e7 kal\u0131nt\u0131lar\u0131n\u0131n giderilmesi)<\/p>\n

3. MVR\/\u00e7ok etkili buharla\u015ft\u0131rma i\u015flemi (konsantrasyon)<\/p>\n

4. Winsonda d\u00fc\u015f\u00fck s\u0131cakl\u0131kta buharla\u015ft\u0131rma i\u015flemi (ana lik\u00f6r kurutma) \u2013 En zor ba\u011flant\u0131 tamamen s\u0131f\u0131r at\u0131k su de\u015farj\u0131 olabilir<\/p>\n

(K\u00f6m\u00fcr kimyasal at\u0131k suyunun s\u0131f\u0131r de\u015farj\u0131 i\u00e7in tipik proses rotas\u0131)<\/p>\n

\"Winsonda'n\u0131n<\/p>\n

(Winsonda'n\u0131n m\u00fc\u015fterinin tesisindeki ilk d\u00fc\u015f\u00fck s\u0131cakl\u0131k buharla\u015ft\u0131r\u0131c\u0131s\u0131n\u0131n resmi)<\/p>\n

\"Winsonda<\/p>\n

(Winsonda d\u00fc\u015f\u00fck s\u0131cakl\u0131kta buharla\u015ft\u0131rma kurutma prosesi c\u00fcruf diyagram\u0131)<\/p>\n

Winsonda d\u00fc\u015f\u00fck s\u0131cakl\u0131k buharla\u015ft\u0131rma kurutma \u00fcnitesi Aral\u0131k 2023'te devreye al\u0131nd\u0131 ve kullan\u0131m s\u00fcreci ve ar\u0131tma etkisi m\u00fc\u015fteriler taraf\u0131ndan do\u011fruland\u0131 ve tan\u0131nd\u0131. Ar\u0131tma kapasitesi tasar\u0131m gereksinimlerini istikrarl\u0131 bir \u015fekilde kar\u015f\u0131layabilir; at\u0131k su kalitesi iyidir, COD\u2264100mg\/L, TDS\u2264100mg\/L, m\u00fc\u015fterinin yeniden kullan\u0131m gereksinimlerini kar\u015f\u0131lar; gelen suyun kalitesine ba\u011fl\u0131 olarak c\u00fcrufun nem i\u00e7eri\u011fi yakla\u015f\u0131k 10%'de stabildir.<\/p>\n

De\u011ferli ana lik\u00f6r d\u00fc\u015f\u00fck s\u0131cakl\u0131kta buharla\u015ft\u0131rma ve kurutma teknolojisinin m\u00fc\u015fterilere sa\u011flad\u0131\u011f\u0131 faydalar<\/h2>\n

Winsonda ana lik\u00f6r kurutma teknolojisi, m\u00fc\u015fterilerin at\u0131k su ar\u0131t\u0131m\u0131ndaki sorunlar\u0131n\u0131 ger\u00e7ek anlamda \u00e7\u00f6zmelerine yard\u0131mc\u0131 olmakla kalm\u0131yor, ayn\u0131 zamanda maliyet azalt\u0131m\u0131 ve verimlilik art\u0131\u015f\u0131 da sa\u011fl\u0131yor.<\/p>\n

De\u011fer 1: M\u00fc\u015fteriler i\u00e7in y\u00fcksek tuzlu at\u0131ksuyun s\u0131f\u0131r de\u015farj\u0131n\u0131n son kilometresini a\u00e7\u0131yor ve ana lik\u00f6r\u00fcn kurutulmas\u0131 sorununu ger\u00e7ek anlamda \u00e7\u00f6z\u00fcyor;<\/p>\n

De\u011fer 2: B\u00fcy\u00fck miktarda ana lik\u00f6r\u00fcn buharla\u015ft\u0131rma sistemine geri d\u00f6nmesini \u00f6nler, \u00f6n u\u00e7 buharla\u015ft\u0131rma sisteminin \u00e7al\u0131\u015fmas\u0131na m\u00fcdahaleyi azalt\u0131r ve tuz ay\u0131rma kalitesini art\u0131r\u0131r;<\/p>\n

De\u011fer 3: K\u0131zak \u00fczerine monte edilmi\u015f ekipman, k\u00fc\u00e7\u00fck ayak izi, d\u00f6n\u00fc\u015f\u00fcm sahas\u0131 i\u00e7in b\u00fcy\u00fck \u00f6l\u00e7ekli in\u015faat m\u00fchendisli\u011fi gereksinimlerinin olmamas\u0131 ve k\u0131sa bir d\u00f6n\u00fc\u015f\u00fcm d\u00f6ng\u00fcs\u00fc;<\/p>\n

De\u011fer 4: Orijinal tambur kurutma ile kar\u015f\u0131la\u015ft\u0131r\u0131ld\u0131\u011f\u0131nda, d\u00fc\u015f\u00fck s\u0131cakl\u0131ktaki buharla\u015ft\u0131rma i\u015flemi enerji t\u00fcketimi nispeten d\u00fc\u015f\u00fckt\u00fcr, bu da ana lik\u00f6r kurutman\u0131n i\u015fletme maliyetini azalt\u0131r.<\/p>\n

Winsonda ana lik\u00f6r kurutman\u0131n etkisi, sahibi taraf\u0131ndan oybirli\u011fiyle kabul edilmi\u015ftir. \u00dcretim kapasitesindeki ve at\u0131k su hacmindeki art\u0131\u015fla birlikte m\u00fc\u015fteriler yeni Winsonda ekipman\u0131 sipari\u015f etmi\u015ftir.<\/p>\n