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4411火力發(fā)電行業(yè)產(chǎn)排污系數(shù)表,,,,,,,,,,注:①煤炭干燥無灰基揮發(fā)分為20<Vdaf(%)≤37;②煤炭干燥無灰基揮發(fā)分為Vdaf(%)>37。③煤炭干燥無灰基揮發(fā)分為Vdaf(%)≤10;④煤炭干燥無灰基揮發(fā)分為10<Vdaf(%)≤20;⑤煤炭干燥無灰基揮發(fā)分為Vdaf(%)>37。⑥工業(yè)廢水若為部分利用,利用率一般介于40~60%,此工況下適用末端處理技術(shù)為“利用+直排”的排污系數(shù)。以下同。
產(chǎn)品名稱,原料名稱,工藝名稱,規(guī)模等級(jí),污染物指標(biāo),單位,產(chǎn)污系數(shù),末端處理技術(shù)名稱,排污系數(shù),,
電能、電能+熱能(單機(jī)容量≥750兆瓦),煤炭,煤粉爐,≥750兆瓦,工業(yè)廢水量,噸/噸-原料,0.392,重復(fù)利用,0,,
,,,,,,,利用+直排,0.196,,
,,,,化學(xué)需氧量,克/噸-原料,17.6,物理+化學(xué)法,0,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"8,271",直排,"8,271",,
,,,,煙塵,千克/噸-原料,9.23Aar+8.76,靜電除塵法+石灰石石膏法,-0.00026Aar2+0.022Aar+0.01,,
,,,,,,,靜電除塵法,(0.00026Aar2+0.022Aar+0.01)×1.001,,
,,,,二氧化硫,千克/噸-原料,17.2Sar+0.04,石灰石石膏法,-0.227Sar+1.789+0.002,,
,,,,,,,直排,17.2Sar+0.04,,
,,,,氮氧化物,千克/噸-原料,6.09①,(低氮燃燒)直排,6.09,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.13,,
,,,,,,4.10②,(低氮燃燒)直排,4.1,,
,,,,,,,(低氮燃燒)煙氣脫硝,1.44,,
,,,,工業(yè)固體廢物(粉煤灰),千克/噸-原料,9.22Aar+8.58,-,-,,
,,,,工業(yè)固體廢物(爐渣),千克/噸-原料,0.71Aar+0.63,-,-,,
,,,,工業(yè)固體廢物(脫硫石膏),千克/噸-原料,0.61Sar2+41.6Sar+0.11,-,-,,
電能、電能+熱能(單機(jī)容量450~749兆瓦),煤炭,煤粉爐,450~749兆瓦,工業(yè)廢水量,噸/噸-原料,0.569,重復(fù)利用,0,,
,,,,化學(xué)需氧量,克/噸-原料,20.5,物理+化學(xué)法,0,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"10,150",直排,"10,150",,
,,,,煙塵,千克/噸-原料,9.2Aar+9.33,靜電除塵法,-0.0005Aar2+0.042Aar+0.041,,
,,,,,,,靜電除塵法+石灰石石膏法,-0.00026Aar2+0.022Aar+0.015,,
,,,,二氧化硫,千克/噸-原料,17.04Sar,直排,17.04Sar,,
,,,,,,17.04Sar,石灰石石膏法,-0.224Sar+1.771Sar,,
,,,,,,17.04Sar,海水脫硫,1.704Sar,,
電能、電能+熱能(單機(jī)容量450~749兆瓦),煤炭,煤粉爐,450~749兆瓦,氮氧化物,千克/噸-原料,13.40③,直排,13.4,,
,,,,,,7.95③,(低氮燃燒)直排,7.95,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.79,,
,,,,,,5.57③,(低氮燃燒+SNCR)直排,5.57,,
,,,,,,11.20④,直排,11.2,,
,,,,,,6.72④,(低氮燃燒)直排,6.72,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.35,,
,,,,,,4.70④,(低氮燃燒+SNCR)直排,4.7,,
,,,,,,10.11①,直排,10.11,,
,,,,,,6.07①,(低氮燃燒)直排,6.07,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.12,,
,,,,,,4.25①,(低氮燃燒+SNCR)直排,4.25,,
,,,,,,6.80⑤,直排,6.8,,
,,,,,,4.08⑤,(低氮燃燒)直排,4.08,,
,,,,,,,(低氮燃燒)煙氣脫硝,1.43,,
,,,,,,2.86⑤,(低氮燃燒+SNCR)直排,2.86,,
電能、電能+熱能(單機(jī)容量450~749兆瓦),煤炭,煤粉爐,450~749兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,9.19Aar+8.95,-,-,,
,,,,工業(yè)固體廢物(爐渣),千克/噸-原料,0.72Aar+0.62,-,-,,
,,,,工業(yè)固體廢物(脫硫石膏),千克/噸-原料,0.61Sar2+41.23Sar,-,-,,
電能、電能+熱能(單機(jī)容量250~449兆瓦),煤炭,煤粉爐或循環(huán)流化床鍋爐,250~449兆瓦,工業(yè)廢水量,噸/噸-原料,0.669,重復(fù)利用,0,,
,,,,,,,循環(huán)利用+直排⑥,0.335,,
,,,,化學(xué)需氧量,克/噸-原料,27.7,物理+化學(xué)法(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)法(循環(huán)利用+直排),6.7,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"9,713",直排,"9,713",,
,,煤粉爐,250~449兆瓦,煙塵,千克/噸-原料,9.21Aar+11.13,靜電除塵法,-0.0005Aar2+0.042Aar+0.057,,
,,,,,,,靜電除塵法+石灰石石膏法,-0.00026Aar2+0.022Aar+0.016,,
,,循環(huán)流化床鍋爐,250~449兆瓦,煙塵,千克/噸-原料,6.31Aar+7.54+61.94Sar,靜電除塵法,-0.0004Aar2+0.035Aar+0.034+0.124Sar,,
,,煤粉爐,250~449兆瓦,二氧化硫,千克/噸-原料,16.98Sar,直排,16.98Sar,,
,,,,,,,,,,,
,,,,,,,石灰石石膏法,-0.223Sar+1.765Sar,,
,,,,,,,海水脫硫法,1.698Sar,,
,,,,,,,,,,,
,,,,,,,煙氣循環(huán)流化床脫硫,1.698Sar,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,250~449兆瓦,二氧化硫,千克/噸-原料,2.55Sar,直排,2.55Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量250~449兆瓦),煤炭,煤粉爐,250~449兆瓦,氮氧化物,千克/噸-原料,13.35③,直排,13.35,,
,,,,,,8.01③,(低氮燃燒)直排,8.01,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.8,,
,,,,,,5.61③,(低氮燃燒+SNCR)直排,5.61,,
,,,,,,11.09④,直排,11.09,,
,,,,,,6.65④,(低氮燃燒)直排,6.65,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.33,,
,,,,,,4.66④,(低氮燃燒+SNCR)直排,4.66,,
,,,,,,9.70①,直排,9.7,,
,,,,,,5.82①,(低氮燃燒)直排,5.82,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.04,,
,,,,,,4.07①,(低氮燃燒+SNCR)直排,4.07,,
,,,,,,6.78⑤,直排,6.78,,
,,,,,,4.07⑤,(低氮燃燒)直排,4.07,,
,,,,,,,(低氮燃燒)煙氣脫硝,1.42,,
,,,,,,2.85⑤,(低氮燃燒+SNCR)直排,2.85,,
電能、電能+熱能(單機(jī)容量250~449兆瓦),煤炭,煤粉爐,250~449兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,9.2Aar+10.76,-,-,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,250~449兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,6.29Aar+7.26+61.82Sar,-,-,,
,,,,,,,,,,,
,,煤粉爐,250~449兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,0.715Aar+0.61,-,-,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,250~449兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,3.43Aar+2.42+32.29Sar,-,-,,
,,,,,,,,,,,
,,煤粉爐,250~449兆瓦,工業(yè)固體廢物(脫硫石膏),千克/噸-原料,0.61Sar2+41.23Sar,-,-,,
電能、電能+熱能(單機(jī)容量150~249兆瓦),煤炭,煤粉爐或循環(huán)流化床鍋爐,150~249兆瓦,工業(yè)廢水量,噸/噸-原料,0.6,重復(fù)利用,0,,
,,,,,,,循環(huán)利用+直排,0.3,,
,,,,化學(xué)需氧量,克/噸-原料,28.7,物理+化學(xué)法(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)法(循環(huán)利用+直排),7.5,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"9,305",直排,"9,305",,
,,煤粉爐,150~249兆瓦,煙塵,千克/噸-原料,9.33Aar+7.77,靜電除塵法,-0.0005Aar2+0.042Aar+0.098,,
,,,,,,,靜電除塵法+石灰石石膏法,-0.00026Aar2+0.0241Aar+0.022,,
,,循環(huán)流化床鍋爐,150~249兆瓦,煙塵,千克/噸-原料,6.24Aar+7.57+61.94Sar,靜電除塵法,0.02Aar+0.016+0.124Sar,,
,,,,,,,,,,,
,,煤粉爐,150~249兆瓦,二氧化硫,千克/噸-原料,16.96Sar,直排,16.96Sar,,
,,,,,,,,,,,
,,,,,,,石灰石石膏法,-0.223Sar2+1.763Sar,,
,,,,,,,海水脫硫法,1.696Sar,,
,,,,,,,,,,,
,,,,,,,煙氣循環(huán)流化床脫硫,4.24Sar,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,150~249兆瓦,二氧化硫,千克/噸-原料,5.09Sar,直排,5.09Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量150~249兆瓦),煤炭,煤粉爐,150~249兆瓦,氮氧化物,千克/噸-原料,12.8③,直排,12.8,,
,,,,,,7.68③,(低氮燃燒)直排,7.68,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.69,,
,,,,,,5.38③,(低氮燃燒+SNCR)直排,5.38,,
,,,,,,11.02④,直排,11.02,,
,,,,,,6.61④,(低氮燃燒)直排,6.61,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.31,,
,,,,,,4.63④,(低氮燃燒+SNCR)直排,4.63,,
,,,,,,9.35①,直排,9.35,,
,,,,,,5.61①,(低氮燃燒)直排,5.61,,
,,,,,,,(低氮燃燒)煙氣脫硝,1.96,,
,,,,,,3.93①,(低氮燃燒+SNCR)直排,3.93,,
,,,,,,6.57⑤,直排,6.57,,
,,,,,,3.94⑤,(低氮燃燒)直排,3.94,,
,,,,,,,(低氮燃燒)煙氣脫硝,1.38,,
,,,,,,2.76⑤,(低氮燃燒+SNCR)直排,2.76,,
電能、電能+熱能(單機(jī)容量150~249兆瓦),煤炭,煤粉爐,150~249兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,9.31Aar+7.31,-,-,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,150~249兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,6.22Aar+7.551+61.75Sar,-,-,,
,,,,,,,,,,,
,,煤粉爐,150~249兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,0.712Aar+0.407,-,-,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,150~249兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,3.21Aar+2.63+32.29Sar,-,-,,
,,,,,,,,,,,
,,煤粉爐,150~249兆瓦,工業(yè)固體廢物(脫硫石膏),千克/噸-原料,0.6Sar2+41.03Sar,-,-,,
電能、電能+熱能(單機(jī)容量75~149兆瓦),煤炭,煤粉爐或循環(huán)流化床鍋爐,75~149兆瓦,工業(yè)廢水量,噸/噸-原料,0.505,重復(fù)利用,0,,
,,,,,,,循環(huán)利用+直排,0.253,,
,,,,化學(xué)需氧量,克/噸-原料,31.5,物理+化學(xué)法(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)法(循環(huán)利用+直排),7.6,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"8,178",直排,"8,178",,
,,煤粉爐,75~149兆瓦,煙塵,千克/噸-原料,9.31Aar+9.18,文丘里水膜除塵法,0.49Aar+0.46,,
,,,,,,,濕式除塵法,1.94Aar+1.84,,
,,,,,,,濕式除塵脫硫一體化,0.68Aar+0.64,,
,,,,,,,靜電除塵法,0.049Aar+0.046,,
,,,,,,,靜電除塵法+石灰石石膏法,0.024Aar+0.023,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,75~149兆瓦,煙塵,千克/噸-原料,6.31Aar+61.94,靜電除塵法,0.048Aar+0.046+0.31Sar,,
,,,,,,7.27Sar,,,,
電能、電能+熱能(單機(jī)容量75~149兆瓦(續(xù))),煤炭,煤粉爐,75~149兆瓦,二氧化硫,千克/噸-原料,16.94Sar,直排,16.94Sar,,
,,,,,,,,,,,
,,,,,,,石灰石石膏法,-0.223Sar2+1.76Sar,,
,,,,,,,文丘里水膜除塵法,14.34Sar,,
,,,,,,,,,,,
,,,,,,,濕式除塵法,16.09Sar,,
,,,,,,,,,,,
,,,,,,,濕式除塵脫硫一體化,5.08Sar,,
,,,,,,,,,,,
,,,,,,,海水脫硫,1.694Sar,,
,,,,,,,,,,,
,,,,,,,煙氣循環(huán)流化床脫硫,4.23Sar,,
,,,,,,,,,,,
,,,,,,,噴霧干燥法(或)簡易石灰石石膏濕法,5.08Sar,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,75~149兆瓦,二氧化硫,千克/噸-原料,5.08Sar,直排,5.08Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量75~149兆瓦(續(xù))),煤炭,煤粉爐,75~149兆瓦,氮氧化物,千克/噸-原料,12.31③,直排,12.31,,
,,,,,,7.49③,(低氮燃燒)直排,7.49,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.63,,
,,,,,,5.24③,(低氮燃燒+SNCR)直排,5.24,,
,,,,,,10.97④,直排,10.97,,
,,,,,,6.58④,(低氮燃燒)直排,6.58,,
,,,,,,,(低氮燃燒)煙氣脫硝,2.3,,
,,,,,,4.61④,(低氮燃燒+SNCR)直排,4.61,,
,,,,,,9.13①,直排,9.13,,
,,,,,,5.48①,(低氮燃燒)直排,5.48,,
,,,,,,,(低氮燃燒)煙氣脫硝,1.92,,
,,,,,,3.84①,(低氮燃燒+SNCR)直排,3.84,,
,,,,,,6.44⑤,直排,6.44,,
,,,,,,3.86⑤,(低氮燃燒)直排,3.86,,
,,,,,,,(低氮燃燒)煙氣脫硝,1.35,,
,,,,,,2.70⑤,(低氮燃燒+SNCR)直排,2.7,,
電能、電能+熱能(單機(jī)容量75~149兆瓦(續(xù))),煤炭,煤粉爐,75~149兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,9.02Aar+8.72,文丘里水膜除塵法,-,,
,,,,,,,,,,,
,,,,,,7.47Aar+7.35,濕式除塵法,,,
,,,,,,8.73Aar+8.54,濕式除塵脫硫一體化,,,
,,,,,,9.26Aar+9.13,靜電除塵法,,,
,,,,,,9.38Aar+9.16,靜電除塵法+石灰石石膏法,,,
,,循環(huán)流化床鍋爐,75~149兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,6.28Aar+7.24+61.69Sar,靜電除塵法,-,,
,,,,,,,,,,,
,,煤粉爐,75~149兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,1.08Aar+1.02,-,-,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,75~149兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,3.28Aar+2.44+32.29Sar,-,-,,
,,,,,,,,,,,
,,煤粉爐,75~149兆瓦,工業(yè)固體廢物(脫硫石膏),千克/噸-原料,0.6Sar2+40.98Sar,-,-,,
電能、電能+熱能(單機(jī)容量35~74兆瓦),煤炭,煤粉爐或循環(huán)流化床鍋爐,35~74兆瓦,工業(yè)廢水量,噸/噸-原料,0.734,重復(fù)利用,0,,
,,,,,,,循環(huán)利用+直排,0.367,,
,,,,化學(xué)需氧量,克/噸-原料,36.7,物理+化學(xué)法(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)法(循環(huán)利用+直排),11.8,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"7,558",直排,"7,558",,
,,煤粉爐,35~74兆瓦,煙塵,千克/噸-原料,9.36Aar+10.44,文丘里水膜除塵法,0.49Aar+0.52,,
,,,,,,,濕式除塵法,1.95Aar+2.09,,
,,,,,,,濕式除塵脫硫一體化,0.68Aar+0.731,,
,,,,,,,靜電除塵法,0.049Aar+0.052,,
,,,,,,,靜電除塵法+石灰石石膏法,0.024Aar+0.026,,
,,,,,,,,,,,
,,,,,,,靜電除塵法+氨法脫硫,0.024Aar+0.026,,
,,,,,,,,,,,
,,,,,,9.36Aar+10.44+61.94Sar,爐內(nèi)噴鈣,0.049Aar+0.052+0.31Sar,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,35~74兆瓦,煙塵,千克/噸-原料,6.24Aar+7.24+61.94Sar,靜電除塵法,0.049Aar+0.052+0.31Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量35~74兆瓦(續(xù))),煤炭,煤粉爐,35~74兆瓦,二氧化硫,千克/噸-原料,16.78Sar,直排,16.78Sar,,
,,,,,,,,,,,
,,,,,,,石灰石石膏法,-0.22Sar2+1.74Sar,,
,,,,,,,氨法脫硫,0.84Sar,,
,,,,,,,,,,,
,,,,,,,文丘里水膜除塵法,14.26Sar,,
,,,,,,,,,,,
,,,,,,,濕式除塵法,15.94Sar,,
,,,,,,,,,,,
,,,,,,,濕式除塵脫硫一體化,5.03Sar,,
,,,,,,,,,,,
,,,,,,,煙氣循環(huán)流化床脫硫,5.03Sar,,
,,,,,,,,,,,
,,,,,,,噴霧干燥法(或)簡易石灰石石膏濕法,5.03Sar,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,35~74兆瓦,二氧化硫,千克/噸-原料,5.87Sar,直排,5.87Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量35~74兆瓦(續(xù))),煤炭,煤粉爐,35~74兆瓦,氮氧化物,千克/噸-原料,11.50③,直排,11.5,,
,,,,,,,氨法脫硫,9.78,,
,,,,,,6.90③,(低氮燃燒)直排,6.9,,
,,,,,,,(低氮燃燒)氨法脫硫,5.86,,
,,,,,,9.86④,直排,9.86,,
,,,,,,,氨法脫硫,8.38,,
,,,,,,5.92④,(低氮燃燒)直排,5.92,,
,,,,,,,(低氮燃燒)氨法脫硫,5.03,,
,,,,,,6.88①,直排,6.88,,
,,,,,,,氨法脫硫,5.85,,
,,,,,,4.13①,(低氮燃燒)直排,4.13,,
,,,,,,,(低氮燃燒)氨法脫硫,3.51,,
,,,,,,5.07⑤,直排,5.07,,
,,,,,,,氨法脫硫,4.31,,
,,,,,,3.04⑤,(低氮燃燒)直排,3.04,,
,,,,,,,(低氮燃燒)氨法脫硫,2.58,,
電能、電能+熱能(單機(jī)容量35~74兆瓦(續(xù))),煤炭,煤粉爐,35~74兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,8.87Aar+9.92,文丘里水膜,-,,
,,,,,,,除塵法,,,
,,,,,,7.41Aar+8.35,濕式除塵法,,,
,,,,,,8.68Aar+9.71,濕式除塵脫硫一體化,,,
,,,,,,9.31Aar+10.39,靜電除塵法,,,
,,,,,,9.31Aar+10.39+61.8Sar,爐內(nèi)噴鈣,,,
,,,,,,,,,,,
,,,,,,9.34Aar+10.42,靜電除塵法+石灰石石膏法,,,
,,,,,,9.37Aar+10.42,靜電除塵法+氨法脫硫,,,
,,循環(huán)流化床鍋爐,35~74兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,6.2Aar+7.2+61.63Sar,-,-,,
,,煤粉爐,35~744兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,1.09Aar+1.16,-,-,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,35~744兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,3.32Aar+2.38+32.29Sar,-,-,,
,,,,,,,,,,,
,,煤粉爐,35~744兆瓦,工業(yè)固體廢物(脫硫石膏),千克/噸-原料,0.6Sar2+40.6Sar,-,-,,
電能、電能+熱能(單機(jī)容量20~34兆瓦),煤炭,煤粉爐或循環(huán)流化床鍋爐,20~34兆瓦,工業(yè)廢水量,噸/噸-原料,0.932,直排,0.932,,
,,,,,,,重復(fù)利用,0,,
,,,,,,,循環(huán)利用+直排,0.466,,
,,,,化學(xué)需氧量,克/噸-原料,37.8,直排,37.8,,
,,,,,,,物理+化學(xué)法(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)法(循環(huán)利用+直排),15.8,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"7,729",直排,"7,729",,
,,煤粉爐,20~34兆瓦,煙塵,千克/噸-原料,9.16Aar+0.45,文丘里水膜除塵法,0.458Aar+0.023,,
,,,,,,,濕式除塵法,1.83Aar+0.09,,
,,,,,,,濕式除塵脫硫一體化,0.642Aar+0.031,,
,,,,,,,靜電除塵法,0.092Aar+0.005,,
,,,,,,,靜電除塵法+氨法脫硫,0.046Aar+0.002,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,20~34兆瓦,煙塵,千克/噸-原料,6.3Aar+7.79+61.94Sar,靜電除塵法,0.049Aar+0.052+0.31Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量20~34兆瓦(續(xù))),煤炭,煤粉爐,20~34兆瓦,二氧化硫,千克/噸,16.64Sar+0.24,直排,16.64Sar+0.24,,
,,,,,,,文丘里水膜除塵法,14.15Sar+0.2,,
,,,,,,,濕式除塵法,15.81Sar+0.23,,
,,,,,,,濕式除塵脫硫一體化,4.99Sar+0.07,,
,,,,,,,煙氣循環(huán)流化床脫硫,4.99Sar+0.07,,
,,,,,,,氨法脫硫,0.83Sar+0.012,,
,,,,,,,噴霧干燥法(或)簡易石灰石石膏濕法,4.99Sar+0.071,,
,,循環(huán)流化床鍋爐,20~34兆瓦,二氧化硫,千克/噸,5.83Sar+0.083,直排,5.83Sar+0.083,,
電能、電能+熱能(單機(jī)容量20~34兆瓦(續(xù))),煤炭,煤粉爐,20~34兆瓦,氮氧化物,千克/噸-原料,10.79③,直排,10.79,,
,,,,,,,氨法脫硫,9.18,,
,,,,,,6.47③,(低氮燃燒)直排,6.47,,
,,,,,,,(低氮燃燒)氨法脫硫,5.5,,
,,,,,,8.97④,直排,8.97,,
,,,,,,,氨法脫硫,7.63,,
,,,,,,5.28④,(低氮燃燒)直排,5.28,,
,,,,,,,(低氮燃燒)氨法脫硫,4.49,,
,,,,,,6.54①,直排,6.54,,
,,,,,,,氨法脫硫,5.55,,
,,,,,,3.92①,(低氮燃燒)直排,3.92,,
,,,,,,,(低氮燃燒)氨法脫硫,3.33,,
,,,,,,5.02⑤,直排,5.02,,
,,,,,,,氨法脫硫,4.27,,
,,,,,,3.01⑤,(低氮燃燒)直排,3.01,,
,,,,,,,(低氮燃燒)氨法脫硫,2.56,,
電能、電能+熱能(單機(jī)容量20~34兆瓦(續(xù))),煤炭,煤粉爐,20~34兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,8.71Aar+0.43,文丘里水膜除塵法,-,,
,,,,,,,,,,,
,,,,,,7.33Aar+0.36,濕式除塵法,,,
,,,,,,,,,,,
,,,,,,8.52Aar+0.42,除塵脫硫一體化,,,
,,,,,,,,,,,
,,,,,,9.07Aar+0.45,靜電除塵法,,,
,,循環(huán)流化床鍋爐,20~34兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,6.23Aar+7.71+61.32Sar,-,-,,
,,煤粉爐,20~34兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,1.02Aar+0.052,-,-,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,20~34兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,3.34Aar+2.68+32.29Sar,-,-,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量9~19兆瓦),煤炭,煤粉爐或循環(huán)流化床鍋爐或?qū)尤紶t,9~19兆瓦,工業(yè)廢水量,噸/噸-原料,1.489,直排,1.489,,
,,,,,,,重復(fù)利用,0,,
,,,,,,,循環(huán)利用+直排,0.745,,
,,,,化學(xué)需氧量,克/噸-原料,74.5,直排,74.5,,
,,,,,,,物理+化學(xué)法(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)法(循環(huán)利用+直排),26.1,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"7,958",直排,"7,958",,
電能、電能+熱能(單機(jī)容量9~19兆瓦(續(xù))),煤炭,煤粉爐,9~19兆瓦,煙塵,千克/噸-原料,9.18Aar+7.56,文丘里水膜除塵法,0.46Aar+0.38,,
,,,,,,,濕式除塵法,1.84Aar+1.51,,
,,,,,,,濕式除塵脫硫一體化,0.64Aar+0.53,,
,,,,,,,多管或旋風(fēng)除塵法,2.29Aar+1.89,,
,,,,,,,靜電除塵法,0.092Aar+0.076,,
,,,,,,,靜電除塵法+氨法脫硫,0.046Aar+0.038,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,9~19兆瓦,煙塵,千克/噸-原料,6.3Aar+8.97+61.94Sar,靜電除塵法,0.063Aar+0.09+0.619Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量9~19兆瓦(續(xù))),煤炭,層燃爐,9~19兆瓦,煙塵,千克/噸-原料,1.6Aar,(煙煤)單筒旋風(fēng)除塵法,0.61Aar,,
,,,,,,,(煙煤)多管旋風(fēng)除塵法,0.4Aar,,
,,,,,,,(煙煤)濕法除塵/濕式除塵脫硫一體化,0.2Aar,,
,,,,,,,(煙煤)管式電除塵法,0.29Aar,,
,,,,,,,(煙煤)臥式電除塵法,0.05Aar,,
,,,,,,,(煙煤)靜電+過濾式/過濾式,0.01Aar,,
,,,,,,1.85Aar,(無煙煤)單筒旋風(fēng)除塵法,0.71Aar,,
,,,,,,,多管旋風(fēng)除塵法,0.46Aar,,
,,,,,,,(無煙煤)濕法除塵/濕式除塵脫硫一體化,0.24Aar,,
,,,,,,,管式電除塵法,0.33Aar,,
,,,,,,,(無煙煤)臥式電除塵法,0.06Aar,,
,,,,,,,(無煙煤)靜電+過濾式/過濾式,0.02Aar,,
,,,,,,1.60Aar,(褐煤)單筒旋風(fēng)除塵法,0.61Aar,,
,,,,,,,(褐煤)多管旋風(fēng)除塵法,0.4Aar,,
,,,,,,,(褐煤)濕法除塵/濕式除塵脫硫一體化,0.2Aar,,
,,,,,,,(褐煤)管式電除塵法,0.29Aar,,
,,,,,,,(褐煤)臥式電除塵法,0.05Aar,,
,,,,,,,(褐煤)靜電+過濾式/過濾式,0.01Aar,,
電能、電能+熱能(單機(jī)容量9~19兆瓦(續(xù))),煤炭,煤粉爐,9~19兆瓦,二氧化硫,千克/噸-原料,16.5Sar,直排,16.5Sar,,
,,,,,,,,,,,
,,,,,,,文丘里水膜除塵法,14.02Sar,,
,,,,,,,,,,,
,,,,,,,濕式除塵法,15.67Sar,,
,,,,,,,,,,,
,,,,,,,濕式除塵脫硫一體化,4.95Sar,,
,,,,,,,,,,,
,,,,,,,氨法脫硫,0.83Sar,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,9~19兆瓦,二氧化硫,千克/噸-原料,5.77Sar,直排,5.77Sar,,
,,,,,,,,,,,
,,層燃爐,9~19兆瓦,二氧化硫,千克/噸-原料,15.95Sar,(無爐內(nèi)脫硫)直排,15.95Sar,,
,,,,,,,,,,,
,,,,,,,(無爐內(nèi)脫硫)濕法除塵法,13.56Sar,,
,,,,,,,,,,,
,,,,,,,(無爐內(nèi)脫硫)濕式除塵脫硫一體化,4.79Sar,,
,,,,,,,,,,,
,,,,,,11.2Sar,(爐內(nèi)脫硫)直排,11.2Sar,,
,,,,,,,,,,,
,,,,,,,(爐內(nèi)脫硫)濕法除塵法,9.52Sar,,
,,,,,,,,,,,
,,,,,,,(爐內(nèi)脫硫)濕式除塵脫硫一體化,3.36Sar,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量9~19兆瓦(續(xù))),煤炭,煤粉爐,9~19兆瓦,氮氧化物,千克/噸-原料,9.70③,直排,9.7,,
,,,,,,,氨法脫硫,8.24,,
,,,,,,5.82③,(低氮燃燒)直排,5.82,,
,,,,,,,(低氮燃燒)氨法脫硫,4.95,,
,,,,,,6.78④,直排,6.78,,
,,,,,,,氨法脫硫,5.77,,
,,,,,,4.07④,(低氮燃燒)直排,4.07,,
,,,,,,,(低氮燃燒)氨法脫硫,3.46,,
,,,,,,5.14①,直排,5.14,,
,,,,,,,氨法脫硫,4.37,,
,,,,,,3.08①,(低氮燃燒)直排,3.08,,
,,,,,,,(低氮燃燒)氨法脫硫,2.62,,
,,,,,,4.93⑤,直排,4.93,,
,,,,,,,氨法脫硫,4.19,,
,,,,,,2.96⑤,(低氮燃燒)直排,2.96,,
,,,,,,,(低氮燃燒)氨法脫硫,2.52,,
,,層燃爐,9~19兆瓦,氮氧化物,千克/噸-原料,5.61③,直排,5.61,,
,,,,,,5④,直排,5,,
,,,,,,4.38①,直排,4.38,,
,,,,,,4.22⑤,直排,4.22,,
電能、電能+熱能(單機(jī)容量9~19兆瓦(續(xù))),煤炭,煤粉爐,9~19兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,8.72Aar+7.18,文丘里水膜除塵法,-,,
,,,,,,,,,,,
,,,,,,7.34Aar+6.05,濕式除塵法,,,
,,,,,,,,,,,
,,,,,,8.53Aar+7.03,除塵脫硫一體化,,,
,,,,,,,,,,,
,,,,,,6.88Aar+5.67,多管或旋風(fēng)除塵法,,,
,,,,,,,,,,,
,,,,,,9.08Aar+7.49,靜電除塵法,,,
,,循環(huán)流化床鍋爐,9~19兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,6.24Aar+8.88+62.32Sar,靜電除塵法,-,,
,,,,,,,,,,,
,,層燃爐,9~19兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,1.67Aar,-,-,,
,,煤粉爐,9~19兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,1.62Aar+1.34,-,-,,
,,層燃爐,9~19兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,8.45Aar,-,-,,
,,循環(huán)流化床鍋爐,9~19兆瓦,工業(yè)固體廢物(爐渣),千克/噸-原料,3.58Aar+3.47+32.29Sar,-,-,,
,,,,,,,,,,,
電能、電能+熱能(單機(jī)容量≤8兆瓦),煤炭,全部類型鍋爐(鍋內(nèi)水處理),≤8兆瓦,工業(yè)廢水量,噸/噸-原料,0.44,(鍋爐排污水)直排,0.44,,
,,,,,,,(鍋爐排污水)重復(fù)利用,0,,
,,,,,,,(鍋爐排污水)循環(huán)利用+直排,0.22,,
,,,,化學(xué)需氧量,克/噸-原料,70,直排,70,,
,,,,,,,物理+化學(xué)(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)(循環(huán)利用+直排),20,,
,,全部類型鍋爐(鍋外水處理),≤8兆瓦,工業(yè)廢水量,噸/噸-原料,0.605,(鍋爐排污水+軟化處理廢水)直排,0.605,,
,,,,,,,(鍋爐排污水+軟化處理廢水)重復(fù)利用,0,,
,,,,,,,(鍋爐排污水+軟化處理廢水)利用+直排,0.302,,
,,,,化學(xué)需氧量,克/噸-原料,90,直排,90,,
,,,,,,,物理+化學(xué)(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)(循環(huán)利用+直排),30,,
,,層燃爐,≤8兆瓦,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"10,290",(煙煤)直排,"10,290",,
,,煤粉爐,≤8兆瓦,,,"9,186",(煙煤)直排,"9,186",,
,,循環(huán)流化床鍋爐,≤8兆瓦,,,"9,415",(煙煤)直排,"9,415",,
,,層燃爐,≤8兆瓦,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"10,197",(無煙煤)直排,"10,197",,
,,循環(huán)流化床鍋爐,≤8兆瓦,,,"11,034",(無煙煤)直排,"11,034",,
,,層燃爐,≤8兆瓦,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"5,915",(褐煤)直排,"5,915",,
,,煤粉爐,≤8兆瓦,,,"5,915",(褐煤)直排,"5,915",,
電能、電能+熱能(單機(jī)容量≤8兆瓦(續(xù))),煤炭,層燃爐,≤8兆瓦,煙塵,千克/噸-原料,1.25Aar,(煙煤)單筒旋風(fēng)除塵法,0.5Aar,,
,,,,,,,(煙煤)多管旋風(fēng)除塵法,0.38Aar,,
,,,,,,,(煙煤)濕法除塵/濕式除塵脫硫一體化,0.16Aar,,
,,,,,,,(煙煤)管式電除塵法,0.23Aar,,
,,,,,,,(煙煤)臥式電除塵法,0.04Aar,,
,,,,,,,(煙煤)靜電+過濾/過濾,0.01Aar,,
,,煤粉爐,≤8兆瓦,,,8.93Aar,(煙煤)機(jī)械+濕法除塵法/濕式除塵脫硫一體化,0.71Aar,,
,,,,,,,(煙煤)臥式電除塵法,0.27Aar,,
,,,,,,,(煙煤)靜電+過濾/過濾,0.09Aar,,
,,循環(huán)流化床鍋爐,≤8兆瓦,,,5.19Aar,(煙煤)機(jī)械+濕法除塵法/濕式除塵脫硫一體化,0.42Aar,,
,,,,,,,(煙煤)臥式電除塵法,0.16Aar,,
,,,,,,,(煙煤)靜電+過濾/過濾,0.05Aar,,
,,層燃爐,≤8兆瓦,煙塵,千克/噸-原料,1.8Aar,(無煙煤)單筒旋風(fēng)除塵法,0.72Aar,,
,,,,,,,(無煙煤)多管旋風(fēng)除塵法,0.54Aar,,
,,,,,,,(無煙煤)濕法除塵/濕式除塵脫硫一體化,0.23Aar,,
,,,,,,,(無煙煤)管式電除塵法,0.32Aar,,
,,,,,,,(無煙煤)臥式電除塵法,0.05Aar,,
,,,,,,,(無煙煤)靜電+過濾/過濾,0.02Aar,,
,,循環(huán)流化床鍋爐,≤8兆瓦,,,4.63Aar,(無煙煤)機(jī)械+濕法除塵法/濕式除塵脫硫一體化,0.37Aar,,
,,,,,,,(無煙煤)臥式電除塵法,0.14Aar,,
,,,,,,,(無煙煤)靜電+過濾/過濾,0.05Aar,,
電能、電能+熱能(單機(jī)容量≤8兆瓦(續(xù))),煤炭,層燃爐,≤8兆瓦,煙塵,千克/噸-原料,1.25Aar,(褐煤)單筒旋風(fēng)除塵法,0.5Aar,,
,,,,,,,(褐煤)多管旋風(fēng)除塵法,0.38Aar,,
,,,,,,,(褐煤)濕法除塵/濕式除塵脫硫一體化,0.16Aar,,
,,,,,,,(褐煤)管式電除塵法,0.23Aar,,
,,,,,,,(褐煤)臥式電除塵法,0.04Aar,,
,,,,,,,(褐煤)靜電+過濾/過濾,0.01Aar,,
,,煤粉爐,≤8兆瓦,煙塵,千克/噸-原料,8.93Aar,(褐煤)機(jī)械+濕法除塵法/濕式除塵脫硫一體化,0.71Aar,,
,,,,,,,(褐煤)臥式電除塵法,0.27Aar,,
,,,,,,,(褐煤)靜電+過濾/過濾,0.09Aar,,
電能、電能+熱能(單機(jī)容量≤8兆瓦(續(xù))),煤炭,層燃爐,≤8兆瓦,二氧化硫,千克/噸-原料,16Sar,(煙煤)直排(無爐內(nèi)脫硫),16Sar,,
,,,,,,,(煙煤)濕法除塵法(無爐內(nèi)脫硫),13.6Sar,,
,,,,,,,(煙煤)濕式除塵脫硫一體化(無爐內(nèi)脫硫),4.8Sar,,
,,,,,,11.2Sar,(煙煤)直排(爐內(nèi)脫硫),11.2Sar,,
,,,,,,,(煙煤)濕式除塵脫硫一體化(爐內(nèi)脫硫),3.36Sar,,
,,固態(tài)排渣煤粉爐,≤8兆瓦,二氧化硫,千克/噸-原料,17Sar,(煙煤)直排,17Sar,,
,,,,,,,(煙煤)濕法除塵法,14.45Sar,,
,,,,,,,(煙煤)濕式除塵脫硫一體化,5.1Sar,,
,,循環(huán)流化床鍋爐,≤8兆瓦,二氧化硫,千克/噸-原料,15Sar,(煙煤)直排(無脫硫劑),15Sar,,
,,,,,,,(煙煤)濕法除塵法(無脫硫劑),12.75Sar,,
,,,,,,,(煙煤)濕式除塵脫硫一體化(無脫硫劑),4.5Sar,,
,,,,,,4.5Sar,(煙煤)直排(添加脫硫劑),4.5Sar,,
,,,,,,,(煙煤)濕式除塵脫硫一體化(添加脫硫劑),1.35Sar,,
電能、電能+熱能(單機(jī)容量≤8兆瓦(續(xù))),煤炭,層燃爐,≤8兆瓦,二氧化硫,千克/噸-原料,16Sar,(無煙煤)直排(無脫硫劑),16Sar,,
,,,,,,,(無煙煤)濕法除塵法(無脫硫劑),13.6Sar,,
,,,,,,,(無煙煤)濕式除塵脫硫一體化(無脫硫劑),4.8Sar,,
,,,,,,11.2Sar,(無煙煤)直排(添加脫硫劑),11.2Sar,,
,,,,,,,(無煙煤)濕式除塵脫硫一體化(添加脫硫劑),3.36Sar,,
,,循環(huán)流化床鍋爐,≤8兆瓦,二氧化硫,千克/噸-原料,15Sar,(無煙煤)直排(無脫硫劑),15Sar,,
,,,,,,,(無煙煤)濕法除塵法(無脫硫劑),12.75Sar,,
,,,,,,,(無煙煤)濕式除塵脫硫一體化(無脫硫劑),4.5Sar,,
,,,,,,4.5Sar,(無煙煤)直排(添加脫硫劑),4.5Sar,,
,,,,,,,(無煙煤)濕式除塵脫硫一體化(添加脫硫劑),1.35Sar,,
,,層燃爐,≤8兆瓦,二氧化硫,千克/噸-原料,15Sar,(褐煤)直排(無脫硫劑),15Sar,,
,,,,,,,(褐煤)濕法除塵法(無脫硫劑),12.75Sar,,
,,,,,,,(褐煤)濕式除塵脫硫一體化(無脫硫劑),4.5Sar,,
,,,,,,10.5Sar,(褐煤)直排(添加脫硫劑),10.5Sar,,
,,,,,,,(褐煤)濕式除塵脫硫一體化(添加脫硫劑),3.15Sar,,
,,煤粉爐,≤8兆瓦,二氧化硫,千克/噸-原料,17Sar,(褐煤)直排(無脫硫劑),17Sar,,
,,,,,,,(褐煤)濕法除塵法(無脫硫劑),14.45Sar,,
,,,,,,,(褐煤)濕式除塵脫硫一體化(無脫硫劑),5.1Sar,,
,,,,,,11.9Sar,(褐煤)直排(添加脫硫劑),11.9Sar,,
,,,,,,,(褐煤)濕式除塵脫硫一體化(添加脫硫劑),3.57Sar,,
電能、電能+熱能(單機(jī)容量≤8兆瓦(續(xù))),煤炭,層燃爐,≤8兆瓦,氮氧化物,千克/噸-原料,4.35,(煙煤)直排,4.35,,
,,煤粉爐,≤8兆瓦,氮氧化物,千克/噸-原料,5.04,,5.04,,
,,循環(huán)流化床鍋爐,≤8兆瓦,氮氧化物,千克/噸-原料,3.63,,3.63,,
,,層燃爐,≤8兆瓦,氮氧化物,千克/噸-原料,5.51,(無煙煤)直排,5.51,,
,,循環(huán)流化床鍋爐,≤8兆瓦,氮氧化物,千克/噸-原料,5.53,,5.53,,
,,層燃爐,≤8兆瓦,氮氧化物,千克/噸-原料,4.71,(褐煤)直排,4.71,,
,,煤粉爐,≤8兆瓦,氮氧化物,千克/噸-原料,4.9,,4.9,,
電能、電能+熱能(單機(jī)容量≤8兆瓦(續(xù))),煤炭,層燃爐,≤8兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,1.01Aar,-,-,,
,,,,,,,,,,,
,,,,工業(yè)固體廢物(爐渣),千克/噸-原料,9.24Aar,,,,
,,,,,,,,,,,
,,煤粉爐,≤8兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,8.51Aar,,,,
,,,,,,,,,,,
,,,,工業(yè)固體廢物(爐渣),千克/噸-原料,1.05Aar,,,,
,,,,,,,,,,,
,,循環(huán)流化床鍋爐,≤8兆瓦,工業(yè)固體廢物(粉煤灰),千克/噸-原料,4.73Aar,,,,
,,,,,,,,,,,
,,,,工業(yè)固體廢物(爐渣),千克/噸-原料,5.25Aar,,,,
,,,,,,,,,,,
電能、電能+熱能(煤矸石),煤矸石,循環(huán)流化床鍋爐,所有規(guī)模,工業(yè)廢水量,噸/噸-原料,0.618,直排,0.618,,
,,,,,,,重復(fù)利用,0,,
,,,,,,,循環(huán)利用+直排,0.309,,
,,,,化學(xué)需氧量,克/噸-原料,65.5,直排,65.5,,
,,,,,,,物理+化學(xué)(重復(fù)利用),0,,
,,,,,,,物理+化學(xué)(循環(huán)利用+直排),16.4,,
,,,,工業(yè)廢氣量,標(biāo)立方米/噸-原料,"4,806",直排,"4,806",,
,,,,煙塵,千克/噸-原料,238.6+61.94Sar,(爐內(nèi)脫硫)文丘里水膜除塵法,11.93+3.1Sar,,
,,,,,,,(爐內(nèi)脫硫)濕式除塵法,47.72+12.39Sar,,
,,,,,,,(爐內(nèi)脫硫)多管或旋風(fēng)除塵法,59.65+15.49Sar,,
,,,,,,,(爐內(nèi)脫硫)靜電除塵法,1.67+0.43Sar,,
,,,,二氧化硫,千克/噸-原料,2.84,(爐內(nèi)脫硫)直排,2.84,,
,,,,煙塵,千克/噸-原料,238.6,(無爐內(nèi)脫硫)文丘里水膜除塵法,11.93,,
,,,,,,,(無爐內(nèi)脫硫)濕式除塵法,47.72,,
,,,,,,,(無爐內(nèi)脫硫)多管或旋風(fēng)除塵法,59.65,,
,,,,,,,(無爐內(nèi)脫硫)靜電除塵法,1.67,,
,,,,二氧化硫,千克/噸-原料,9.47,(無爐內(nèi)脫硫)直排,9.47,,
電能、電能+熱能(煤矸石(續(xù))),煤矸石,循環(huán)流化床鍋爐,所有規(guī)模,氮氧化物,千克/噸-原料,0.95,直排,0.95,,
,,,,工業(yè)固體廢物(粉煤灰),千克/噸-原料,226.7+58.8Sar,文丘里水膜除塵法,-,,
,,,,,,190.9+49.5Sar,濕式除塵法,-,,
,,,,,,179+46.4Sar,多管或旋風(fēng)除塵法,-,,
,,,,,,236.9+61.5Sar,靜電除塵法,-,,
,,,,工業(yè)固體廢物(爐渣),千克/噸-原料,180.3,-,-,,
電能、電能+熱能(垃圾),垃圾,焚燒爐,所有規(guī)模,工業(yè)廢水量,噸/噸-原料,0.146,直
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