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綜合工藝集成技術在污水處理中的應用

更(geng)新時間:2009-09-16 09:51 來源:水利工程網 作者(zhe): 劭英琦 閱讀:1432 網友評論0

1、概述

由于污(wu)(wu)(wu)水中的(de)污(wu)(wu)(wu)染(ran)物(wu)(wu)成(cheng)份復雜、性(xing)質(zhi)(zhi)(zhi)各異,要想達(da)到理(li)想的(de)處(chu)(chu)理(li)效果,必(bi)須(xu)采(cai)(cai)用(yong)相(xiang)應(ying)的(de)處(chu)(chu)理(li)工(gong)(gong)藝。如:處(chu)(chu)理(li)懸(xuan)浮物(wu)(wu)、膠狀體(ti)、油(you)脂類物(wu)(wu)質(zhi)(zhi)(zhi)一般(ban)采(cai)(cai)用(yong)混凝、氣浮工(gong)(gong)藝;溶解性(xing)有機質(zhi)(zhi)(zhi)一般(ban)采(cai)(cai)用(yong)生物(wu)(wu)化(hua)(hua)學分解工(gong)(gong)藝;沉降性(xing)固(gu)體(ti)顆(ke)粒一般(ban)采(cai)(cai)用(yong)過濾、沉淀等(deng)物(wu)(wu)理(li)分離的(de)方法(fa)……,傳統方法(fa)是把(ba)各種工(gong)(gong)藝設(she)備或設(she)施相(xiang)加,形成(cheng)串(chuan)連或并聯,污(wu)(wu)(wu)水逐一經過各種不(bu)同(tong)(tong)設(she)備或設(she)施,按固(gu)定的(de)路線、程序進行處(chu)(chu)理(li),這樣(yang)必(bi)然(ran)導(dao)致污(wu)(wu)(wu)水處(chu)(chu)理(li)工(gong)(gong)藝復雜、設(she)備或設(she)施占地面積(ji)大、投資多、運行費用(yong)高(gao)、操作管理(li)難等(deng)問題(ti)。由宜(yi)興市(shi)綠(lv)神環保(bao)有限公(gong)司開發的(de)PS型生物(wu)(wu)流化(hua)(hua)床污(wu)(wu)(wu)水處(chu)(chu)理(li)設(she)備采(cai)(cai)用(yong)氣浮、生物(wu)(wu)流化(hua)(hua)、氧化(hua)(hua)反應(ying)、A/OWH工(gong)(gong)藝及過濾等(deng)多種工(gong)(gong)藝技術綜(zong)合(he)(he)集成(cheng),能(neng)根(gen)據污(wu)(wu)(wu)水中不(bu)同(tong)(tong)性(xing)質(zhi)(zhi)(zhi)、不(bu)同(tong)(tong)成(cheng)份、不(bu)同(tong)(tong)狀態的(de)污(wu)(wu)(wu)染(ran)物(wu)(wu),分別在同(tong)(tong)一設(she)備、同(tong)(tong)一過程中采(cai)(cai)用(yong)不(bu)同(tong)(tong)的(de)處(chu)(chu)理(li)手段進行綜(zong)合(he)(he)處(chu)(chu)理(li),各類有機污(wu)(wu)(wu)水經其處(chu)(chu)理(li)后完全(quan)能(neng)達(da)標排放,部份可(ke)以直接回用(yong)。

2、綜合工藝集成技術

2.1、霧(wu)化充氧技術與(yu)浮(fu)選法

污(wu)水(shui)(shui)經閉路循(xun)環高(gao)速噴(pen)射入特殊湍流(liu)裝置形成(cheng)霧化,增大與(yu)空氣(qi)的(de)接(jie)觸(chu)界面,在一(yi)定壓(ya)力下溶(rong)(rong)合成(cheng)溶(rong)(rong)氣(qi)水(shui)(shui),氣(qi)水(shui)(shui)溶(rong)(rong)解度達(da)到一(yi)定比例時,溶(rong)(rong)解氧(yang)(yang)濃度保持在12mg/l左右,部份污(wu)染(ran)物(wu)在高(gao)濃度溶(rong)(rong)解氧(yang)(yang)的(de)情況下發生化學反應,被直(zhi)接(jie)氧(yang)(yang)化分(fen)解。溶(rong)(rong)氣(qi)水(shui)(shui)通過釋(shi)放器將壓(ya)力迅速恢(hui)復到常壓(ya),釋(shi)放出的(de)大量微(wei)(wei)氣(qi)泡(pao)(pao)吸咐凝聚于(yu)污(wu)水(shui)(shui)中(zhong)懸浮(fu)(fu)雜質上,造成(cheng)雜質整體比重小于(yu)污(wu)水(shui)(shui)的(de)狀態,依靠(kao)微(wei)(wei)氣(qi)泡(pao)(pao)的(de)浮(fu)(fu)力,使(shi)其上浮(fu)(fu)至水(shui)(shui)面,從而達(da)到固(gu)液分(fen)離的(de)目(mu)的(de)。

2.2、生物流化床原理(li)

生(sheng)(sheng)物(wu)流(liu)(liu)化(hua)(hua)床內裝有(you)特種懸浮(fu)狀可流(liu)(liu)化(hua)(hua)性(xing)生(sheng)(sheng)物(wu)載體(ti),載體(ti)利用流(liu)(liu)體(ti)動力學原理使(shi)其懸浮(fu)流(liu)(liu)化(hua)(hua),溶(rong)氣水(shui)(shui)釋放的微(wei)氣泡吸(xi)附在載體(ti)上,向好氧微(wei)生(sheng)(sheng)物(wu)提(ti)供(gong)充足的溶(rong)解氧。在特定(ding)條件下,污(wu)水(shui)(shui)作為(wei)微(wei)生(sheng)(sheng)物(wu)培(pei)養基,培(pei)養出微(wei)生(sheng)(sheng)物(wu)菌群,形成以最適宜增殖的微(wei)生(sheng)(sheng)物(wu)為(wei)中(zhong)心,與多(duo)種多(duo)樣生(sheng)(sheng)物(wu)相(xiang)結(jie)合的一個生(sheng)(sheng)態系,并吸(xi)附凝聚大(da)量(liang)的微(wei)生(sheng)(sheng)物(wu)菌膠體(ti),固定(ding)在懸浮(fu)載體(ti)上,溶(rong)解性(xing)有(you)機(ji)質在好氧微(wei)生(sheng)(sheng)物(wu)作用下,促進有(you)機(ji)質的生(sheng)(sheng)化(hua)(hua)分(fen)解進程,使(shi)有(you)機(ji)質轉化(hua)(hua)成無機(ji)質。

2.3、A/OWH工藝與除磷脫(tuo)氮

因為(wei)好氧(yang)(yang)(yang)(yang)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)無(wu)法(fa)(fa)徹底去除污(wu)(wu)水(shui)中的(de)(de)(de)(de)(de)磷和氮,在(zai)(zai)設計污(wu)(wu)水(shui)處理(li)方案時(shi)(shi),一(yi)定要分別選用(yong)(yong)厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)與好氧(yang)(yang)(yang)(yang)工藝(yi)(A/O或(huo)A2/O)相(xiang)搭(da)配,并(bing)要求一(yi)定的(de)(de)(de)(de)(de)回流比(bi),這樣必然導致水(shui)力停留時(shi)(shi)間(jian)長,而(er)且難以控制厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)和好氧(yang)(yang)(yang)(yang)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)之間(jian)的(de)(de)(de)(de)(de)動(dong)(dong)態(tai)平衡,無(wu)法(fa)(fa)消除磷的(de)(de)(de)(de)(de)釋放與吸(xi)(xi)收(shou)之間(jian)的(de)(de)(de)(de)(de)時(shi)(shi)間(jian)差。A/OWH工藝(yi)是指在(zai)(zai)同一(yi)裝置內(nei)混合存(cun)在(zai)(zai)兩種相(xiang)同密度、其(qi)(qi)它物(wu)(wu)(wu)理(li)特性(xing)不同的(de)(de)(de)(de)(de)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)載體(ti)(ti),使(shi)其(qi)(qi)分別適合厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)微(wei)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)和好氧(yang)(yang)(yang)(yang)微(wei)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)的(de)(de)(de)(de)(de)生(sheng)(sheng)(sheng)(sheng)長條件,由(you)于A/O混合,厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)與好氧(yang)(yang)(yang)(yang)同步進行。厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)載體(ti)(ti)具(ju)有極(ji)大的(de)(de)(de)(de)(de)比(bi)表(biao)面積,工作時(shi)(shi)載體(ti)(ti)表(biao)面首先凝聚著(zhu)好氧(yang)(yang)(yang)(yang)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu),并(bing)由(you)里向(xiang)(xiang)外逐(zhu)漸堵塞(sai)載體(ti)(ti)空(kong)間(jian),形成(cheng)一(yi)個(ge)碩大的(de)(de)(de)(de)(de)封閉式的(de)(de)(de)(de)(de)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)團,這時(shi)(shi)外部(bu)(bu)溶(rong)解氧(yang)(yang)(yang)(yang)無(wu)法(fa)(fa)滲透進去,造成(cheng)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)團內(nei)部(bu)(bu)厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)環境(jing),在(zai)(zai)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)團中心好氧(yang)(yang)(yang)(yang)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)逐(zhu)步被(bei)厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)所(suo)替代,厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)活性(xing)不斷增(zeng)強,同樣,厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)菌從(cong)里向(xiang)(xiang)外逐(zhu)漸分解掉生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)團內(nei)部(bu)(bu)被(bei)包裹(guo)的(de)(de)(de)(de)(de)有機(ji)質(zhi)(zhi),直(zhi)到(dao)整個(ge)菌膠體(ti)(ti)從(cong)載體(ti)(ti)上脫落。然后,隨著(zhu)載體(ti)(ti)的(de)(de)(de)(de)(de)懸浮運動(dong)(dong)及流體(ti)(ti)的(de)(de)(de)(de)(de)推(tui)動(dong)(dong)力,包裹(guo)在(zai)(zai)里面的(de)(de)(de)(de)(de)水(shui)質(zhi)(zhi)與外部(bu)(bu)的(de)(de)(de)(de)(de)水(shui)質(zhi)(zhi)自(zi)動(dong)(dong)交(jiao)換,重復A/O交(jiao)替過(guo)程。A/OWH工藝(yi)就是利用(yong)(yong)除磷菌在(zai)(zai)厭(yan)(yan)(yan)(yan)(yan)(yan)(yan)氧(yang)(yang)(yang)(yang)條件下釋放磷,在(zai)(zai)好氧(yang)(yang)(yang)(yang)條件下吸(xi)(xi)收(shou)磷的(de)(de)(de)(de)(de)多次(ci)交(jiao)替過(guo)程,從(cong)而(er)達到(dao)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)除磷的(de)(de)(de)(de)(de)目的(de)(de)(de)(de)(de)。同樣氨氮在(zai)(zai)有氧(yang)(yang)(yang)(yang)存(cun)在(zai)(zai)的(de)(de)(de)(de)(de)環境(jing)下,通過(guo)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)硝化過(guo)程將污(wu)(wu)水(shui)中的(de)(de)(de)(de)(de)有機(ji)氮和氨氮氧(yang)(yang)(yang)(yang)化為(wei)硝態(tai)氮,在(zai)(zai)缺氧(yang)(yang)(yang)(yang)環境(jing)下通過(guo)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)的(de)(de)(de)(de)(de)硝化過(guo)程將硝態(tai)氮還(huan)原(yuan)為(wei)氮氣從(cong)水(shui)中逸(yi)出,部(bu)(bu)份(fen)氨氮被(bei)微(wei)生(sheng)(sheng)(sheng)(sheng)物(wu)(wu)(wu)新陳代謝所(suo)利用(yong)(yong)而(er)變(bian)成(cheng)細胞組成(cheng)部(bu)(bu)份(fen),并(bing)逐(zhu)漸老化轉變(bian)成(cheng)剩(sheng)余污(wu)(wu)泥從(cong)系統中排出。

2.4、重力過濾法

污水(shui)經(jing)生化(hua)和物(wu)化(hua)的共同作用,溶解性(xing)有機物(wu)和比重較(jiao)輕(qing)的懸(xuan)浮(fu)物(wu)得(de)(de)到徹底去除,部份比重較(jiao)大、難分解的固體(ti)物(wu)仍存(cun)在水(shui)中(zhong),PS型生物(wu)流(liu)(liu)化(hua)床污水(shui)處理設備利用流(liu)(liu)化(hua)區出水(shui)的重力流(liu)(liu)過(guo)(guo)濾(lv)(lv)(lv)(lv),過(guo)(guo)濾(lv)(lv)(lv)(lv)時以石英砂(或纖維球(qiu)、活(huo)性(xing)炭、過(guo)(guo)濾(lv)(lv)(lv)(lv)膜等)截留(liu)水(shui)中(zhong)固體(ti)雜質或菌膠體(ti),反洗時水(shui)流(liu)(liu)逆(ni)向通過(guo)(guo)濾(lv)(lv)(lv)(lv)料(liao)(liao)層,使濾(lv)(lv)(lv)(lv)料(liao)(liao)層膨脹(zhang)懸(xuan)浮(fu),借水(shui)流(liu)(liu)剪(jian)切和顆粒(li)濾(lv)(lv)(lv)(lv)料(liao)(liao)間(jian)的碰撞摩擦力清洗濾(lv)(lv)(lv)(lv)料(liao)(liao)層,過(guo)(guo)濾(lv)(lv)(lv)(lv)和反洗兩(liang)個過(guo)(guo)程(cheng)交替(ti)進行,從(cong)而(er)使水(shui)最終獲得(de)(de)澄清。

3、兼具好氧與厭氧的懸浮填料(AOF復合填料)

A/OWH工藝關鍵是使用兼具(ju)好(hao)氧(yang)(yang)與(yu)厭(yan)(yan)氧(yang)(yang)的(de)懸(xuan)浮復(fu)合填料(liao)(liao),該(gai)種復(fu)合填料(liao)(liao)其外殼象多面空(kong)心球體(ti),內(nei)(nei)部空(kong)間設置有(you)呈(cheng)(cheng)放(fang)射狀纖(xian)維體(ti),復(fu)合后(hou)的(de)平均(jun)比重為1.03-1.05g/cm3,使用過程中(zhong),比重能隨(sui)著污水(shui)密度的(de)變化(hua)而變化(hua),該(gai)填料(liao)(liao)同時(shi)生(sheng)(sheng)長(chang)著好(hao)氧(yang)(yang)微生(sheng)(sheng)物(wu)(wu)和厭(yan)(yan)氧(yang)(yang)微生(sheng)(sheng)物(wu)(wu),形(xing)似一(yi)個巨大的(de)生(sheng)(sheng)物(wu)(wu)團,既可以進(jin)行有(you)機物(wu)(wu)的(de)好(hao)氧(yang)(yang)分解、氧(yang)(yang)化(hua)物(wu)(wu)的(de)硝(xiao)(xiao)化(hua)、磷的(de)吸收,又可以進(jin)行厭(yan)(yan)氧(yang)(yang)水(shui)解、酸化(hua)、反硝(xiao)(xiao)化(hua)以及(ji)磷的(de)釋放(fang)等一(yi)系列過程,從而使硝(xiao)(xiao)化(hua)、反硝(xiao)(xiao)化(hua)、磷的(de)吸收和釋放(fang)之間保持動(dong)態平衡,消除(chu)兩者(zhe)之間的(de)時(shi)間差(cha),由(you)于填料(liao)(liao)呈(cheng)(cheng)微觀狀態獨立(li)懸(xuan)浮在污水(shui)中(zhong),形(xing)成無(wu)數個微型多相(xiang)生(sheng)(sheng)物(wu)(wu)反應器,在運行過程中(zhong),好(hao)氧(yang)(yang)與(yu)厭(yan)(yan)氧(yang)(yang)交替進(jin)行、往復(fu)循(xun)環,并在氣水(shui)流的(de)帶動(dong)下,慢(man)慢(man)旋轉調整狀態,內(nei)(nei)外水(shui)體(ti)互相(xiang)交換,生(sheng)(sheng)物(wu)(wu)污泥自動(dong)脫落,該(gai)填料(liao)(liao)充(chong)填率為80%,在單位體(ti)積內(nei)(nei)具(ju)有(you)很高(gao)的(de)生(sheng)(sheng)物(wu)(wu)量,生(sheng)(sheng)物(wu)(wu)高(gao)度濃縮,耐(nai)沖擊負荷及(ji)降階有(you)機物(wu)(wu)能力極強。

4、城鎮污水處理廠設備化與建設投資分析

采用(yong)綜(zong)(zong)合(he)工(gong)藝集成(cheng)(cheng)技(ji)(ji)術使(shi)污水(shui)(shui)(shui)處(chu)(chu)理(li)(li)(li)的(de)(de)工(gong)藝流程簡單(dan)(dan)化(hua)(hua),處(chu)(chu)理(li)(li)(li)效(xiao)率成(cheng)(cheng)倍提高(gao),處(chu)(chu)理(li)(li)(li)時間大(da)(da)大(da)(da)減(jian)小(xiao)(xiao)(設(she)備(bei)內停留時間僅為(wei)0.75-1小(xiao)(xiao)時),大(da)(da)大(da)(da)節省投(tou)資(zi)(zi)費用(yong)及占(zhan)地(di)(di)(di)面積,從而使(shi)小(xiao)(xiao)城(cheng)鎮(zhen)的(de)(de)污水(shui)(shui)(shui)處(chu)(chu)理(li)(li)(li)廠(chang)設(she)備(bei)化(hua)(hua)建設(she)成(cheng)(cheng)為(wei)現實。據(ju)清華大(da)(da)學環境(jing)工(gong)程系對我國89個城(cheng)市二級污水(shui)(shui)(shui)處(chu)(chu)理(li)(li)(li)廠(chang)的(de)(de)單(dan)(dan)方投(tou)資(zi)(zi)、規(gui)模占(zhan)地(di)(di)(di)和(he)對污水(shui)(shui)(shui)處(chu)(chu)理(li)(li)(li)工(gong)藝等方面進行了定(ding)量考察和(he)多層次(ci)的(de)(de)比(bi)較(jiao)與分(fen)析,分(fen)析顯示:61座(zuo)小(xiao)(xiao)型污水(shui)(shui)(shui)處(chu)(chu)理(li)(li)(li)廠(chang)總處(chu)(chu)理(li)(li)(li)能(neng)力194.05×104m3/d,單(dan)(dan)方投(tou)資(zi)(zi)(當年(nian)價)為(wei)1445.43元(yuan)/m3·d,規(gui)模占(zhan)地(di)(di)(di)2.04hm2/104m3·d,當然污水(shui)(shui)(shui)處(chu)(chu)理(li)(li)(li)工(gong)藝及處(chu)(chu)理(li)(li)(li)效(xiao)果的(de)(de)不(bu)(bu)同有密切的(de)(de)關(guan)(guan)系,就單(dan)(dan)方投(tou)資(zi)(zi)而言,活(huo)(huo)性(xing)(xing)污泥法和(he)活(huo)(huo)性(xing)(xing)污泥+A/O法較(jiao)小(xiao)(xiao),不(bu)(bu)足(zu)1000元(yuan)/m3·d,而A/O、A2/O以(yi)及SBR法由于(yu)處(chu)(chu)理(li)(li)(li)效(xiao)果較(jiao)好(hao),單(dan)(dan)方投(tou)資(zi)(zi)相應也比(bi)較(jiao)高(gao),接(jie)近(jin)甚(shen)至超過2000元(yuan)/m3·d,。如果使(shi)用(yong)綜(zong)(zong)合(he)工(gong)藝集成(cheng)(cheng)技(ji)(ji)術設(she)備(bei)化(hua)(hua),每處(chu)(chu)理(li)(li)(li)2×104m3/d污水(shui)(shui)(shui),單(dan)(dan)方投(tou)資(zi)(zi)為(wei)950元(yuan)/m3·d,僅為(wei)非設(she)備(bei)化(hua)(hua)的(de)(de)65%,規(gui)模占(zhan)地(di)(di)(di)為(wei)0.35hm2/104m3·d,僅為(wei)非設(she)備(bei)化(hua)(hua)的(de)(de)17.5%,而且處(chu)(chu)理(li)(li)(li)效(xiao)果可直接(jie)達到生活(huo)(huo)雜用(yong)水(shui)(shui)(shui)水(shui)(shui)(shui)質標(biao)準。工(gong)程實例(li)有關(guan)(guan)指標(biao)見表1。

由此(ci)可見,采(cai)用綜合工(gong)(gong)藝(yi)集成技術設備化建(jian)設小城鎮污(wu)水(shui)處理廠(chang),不僅單方投(tou)資下降約(yue)30%,規(gui)模占地僅為傳(chuan)統工(gong)(gong)藝(yi)的(de)五分之一,而且出(chu)水(shui)完全能夠直(zhi)接達到cj25.1-89《生活雜用水(shui)水(shui)質標(biao)準》,直(zhi)接節省了(le)深度處理、中水(shui)回(hui)用的(de)投(tou)資,若是(shi)點源污(wu)水(shui)處理后可以(yi)就地回(hui)用,又節省了(le)中水(shui)回(hui)用的(de)管路(lu)投(tou)資,對我國污(wu)水(shui)資源化再利用,特別(bie)是(shi)西(xi)北、華北缺水(shui)地區具有顯著的(de)環境效(xiao)益和經濟效(xiao)益,其社會意義十分深遠。

5、結論

綜合(he)工(gong)藝集(ji)成(cheng)技術在(zai)污水(shui)處(chu)(chu)理(li)(li)中的(de)應用(yong)(yong),由于其(qi)技術集(ji)中,功能(neng)完善(shan),適(shi)用(yong)(yong)范(fan)圍廣,處(chu)(chu)理(li)(li)效率(lv)(lv)高(gao),大部份工(gong)業有(you)機廢水(shui)經處(chu)(chu)理(li)(li)后能(neng)夠達到國家排放標準(zhun);生活類污水(shui)能(neng)夠直接達到生活雜用(yong)(yong)水(shui)水(shui)質標準(zhun)。該方法(fa)不僅適(shi)用(yong)(yong)于點源污水(shui)和小城鎮污水(shui)的(de)設備化處(chu)(chu)理(li)(li),也適(shi)合(he)大中型城市污水(shui)處(chu)(chu)理(li)(li)廠的(de)工(gong)藝改進(jin),該方法(fa)不但在(zai)處(chu)(chu)理(li)(li)效率(lv)(lv)上比傳(chuan)統工(gong)藝有(you)大的(de)提(ti)高(gao),而且(qie)在(zai)單方投資(zi)、規模占地、資(zi)源化利用(yong)(yong)、運行管理(li)(li)方面有(you)很(hen)大的(de)潛(qian)在(zai)價(jia)值。

參考文獻:
[1] 王維斌,吳凡松.小型污水處理廠的設計.中國給水排水,2002,18(3)57-60.
[2] 白曉慧.利用好氧顆粒污泥實現同步硝化反硝化.中國給水排水,2002,18(2)26-28.
[3] 趙文玉,劉康懷等.南寧味精廠廢水處理工程設計與運行.給水排水,2002,28(1)51-53.
[4] 夏平安,崔樹榮等.高氨氮高含硫廢水處理新工藝的研究.給水排水,2002,28(3)43-45.
[5] 褚俊英,陳吉寧等.我國城市污水廠投資效率的定量分析.中國給水排水,2002,18(3)27-29.
[6] 李軍,王寶貞,聶梅生.序批式生物膜法除磷機理研究.中國給水排水,2002,18(1)1-4.
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