設(shè)備動靜密封點泄漏VOCs排放量參考計算表

1、列1,列2,列3,列4,列5,列6,列7,列8,列9,列10,列11,列12,列13,列14,列15,列16,列17,列18,列19,列20,列21,列22,列23,列24,列25,列26,列27,列28,列29,列30,列31,列32,列33,列34,列35,列36,列37,列38,列39,列40,列41,列42,列43,列44,列45,列46,列47,列48,列49,列50,列51,列52,列53,列54,列55,列56,列57,列58,列59,列60,列61,列62,列63,列64,列65,列66,列67基礎(chǔ)信息,第一次檢測,第二次檢測,第三次檢測,第四次檢測,序號,密封點編號,行業(yè),密

2、封點類型,服務(wù)介質(zhì)類型,介質(zhì)中TOC質(zhì)量分數(shù),介質(zhì)中VOCs質(zhì)量分數(shù),氣體介質(zhì)中甲烷質(zhì)量分數(shù),上一年末次監(jiān)測時間,核算方法,方法等級,第一次檢測時間,第一次檢測濃度（ppmv）,二級零值,二級限值50000,二級關(guān)系值,三級,實測,四級,同類密封點數(shù),排放速率（千克/小時）,第一次運行時間（小時）,第一次排放量（千克/小時）,核算方法,方法等級,第二次檢測時間,第二次檢測濃度（ppmv）,二級零值,二級限值50000,二級關(guān)系值,三級,實測,四級,同類密封點數(shù),排放速率（千克/小時）,第二次運行時間（小時）,第二次排放量（千克/小時）,核算方法,方法等級,第三次檢測時間,第三次檢測濃度（ppm

3、v）,二級零值,二級限值50000,二級關(guān)系值,三級,實測,四級,同類密封點數(shù),排放速率（千克/小時）,第三次運行時間（h）,第三次排放量（千克/小時）,核算方法,方法等級,第四次檢測時間,第四次檢測濃度（ppmv）,二級零值,二級限值50000,二級關(guān)系值,三級,實測,四級,同類密封點數(shù),排放速率（千克/小時）,第四次運行時間（小時）,第四次排放量（千克/小時）,下一年第一次檢測時間,年排放量（千克/年）1,石油煉制,泄壓設(shè)備,所有,2014/11/13 14:22,相關(guān)方程法,二級,2015/3/4 8:15,56,0.000004,0.11,1.46E-04,0.0447,#N/A,1,

4、1.46E-04,2614.15 ,0.38 ,相關(guān)方程法,二級,2015/6/19 10:40,56,0.000004,0.11,1.46E-04,0.0447,#N/A,1,1.46E-04,2232.50,0.33,相關(guān)方程法,二級,2015/9/6 9:15,56,0.000004,0.11,1.46E-04,0.0447,#N/A,1,1.46E-04,1813.97,0.26,相關(guān)方程法,二級,2015/11/17 14:36,56,0.000004,0.11,1.46E-04,0.0447,#N/A,1,1.46E-04,1862.27,0.27,2016/2/8 13:48,1

5、.24E+002,石油煉制,泵,輕液體,2014/11/13 14:22,相關(guān)方程法,二級,2015/3/4 8:15,57,0.000024,0.16,5.92E-04,0.012,0.114,2,1.18E-03,2626.15 ,3.11 ,相關(guān)方程法,二級,2015/6/20 10:40,57,0.000024,0.16,5.92E-04,0.012,0.114,2,1.18E-03,2244.50,2.66,相關(guān)方程法,二級,2015/9/7 9:15,57,0.000024,0.16,5.92E-04,0.012,0.114,2,1.18E-03,1813.97,2.15,相關(guān)方程

6、法,二級,2015/11/18 14:36,57,0.000024,0.16,5.92E-04,0.012,0.114,2,1.18E-03,1862.27,2.21,2016/2/9 13:48,1.01E+013,石油煉制,連接件,所有,2014/11/13 14:22,相關(guān)方程法,二級,2015/3/4 8:15,58,0.0000075,0.03,3.03E-05,0.00006,0.00025,3,9.08E-05,2638.15 ,0.24 ,相關(guān)方程法,二級,2015/6/21 10:40,58,0.0000075,0.03,3.03E-05,0.00006,0.00025,3,

7、9.08E-05,4118.77,0.37,實測法,實測,2015/9/8 9:15,58,0.0000075,0.03,3.03E-05,0.00006,0.00025,3,0.00E+00,0.00,0.00,篩選范圍法,三級,2015/11/19 14:36,58,0.0000075,0.03,3.03E-05,0.00006,0.00025,3,1.80E-04,0.00,0.00,2016/2/10 13:48,6.13E-014,石油煉制,連接件,所有,2014/11/13 14:22,相關(guān)方程法,二級,2015/3/4 8:15,59,0.0000075,0.03,3.06E-0

8、5,0.00006,0.00025,4,1.23E-04,2650.15 ,0.32 ,相關(guān)方程法,二級,2015/6/22 10:40,59,0.0000075,0.03,3.06E-05,0.00006,0.00025,4,1.23E-04,4130.77,0.51,篩選范圍法,三級,2015/9/9 9:15,59,0.0000075,0.03,3.06E-05,0.00006,0.00025,4,2.40E-04,0.00,0.00,篩選范圍法,三級,2015/11/20 14:36,59,0.0000075,0.03,3.06E-05,0.00006,0.00025,4,2.40E-

9、04,0.00,0.00,2016/2/11 13:48,8.31E-015,石油煉制,連接件,所有,2014/11/13 14:22,平均排放系數(shù)法,四級,2015/3/4 8:15,60,0.0000075,0.03,3.10E-05,0.00006,0.00025,5,1.25E-03,2662.15 ,3.33 ,篩選范圍法,三級,2015/6/23 10:40,60,0.0000075,0.03,3.10E-05,0.00006,0.00025,5,3.00E-04,4142.77,1.24,相關(guān)方程法,二級,2015/9/10 9:15,60,0.0000075,0.03,3.10

10、E-05,0.00006,0.00025,5,1.55E-04,0.00,0.00,相關(guān)方程法,二級,2015/11/21 14:36,60,0.0000075,0.03,3.10E-05,0.00006,0.00025,5,1.55E-04,0.00,0.00,2016/2/12 13:48,4.57E+006,石油化工,開口閥或開口管線,所有,2014/11/13 14:22,平均排放系數(shù)法,四級,2015/3/4 8:15,61,0.000002,0.079,3.97E-05,0.0015,0.0017,6,1.02E-02,2674.15 ,27.28 ,平均排放系數(shù)法,四級,2015

11、/6/24 10:40,61,0.000002,0.079,3.97E-05,0.0015,0.0017,6,1.02E-02,2292.50,23.38,相關(guān)方程法,二級,2015/9/11 9:15,61,0.000002,0.079,3.97E-05,0.0015,0.0017,6,2.38E-04,1813.97,0.43,實測法,實測,2015/11/22 14:36,61,0.000002,0.079,3.97E-05,0.0015,0.0017,6,0.00E+00,1862.27,0.00,2016/2/13 13:48,5.11E+017,石油煉制,泄壓設(shè)備,所有,2014/

12、11/13 14:22,篩選范圍法,三級,2015/3/4 8:15,62,0.000004,0.11,1.55E-04,0.0447,#N/A,7,3.13E-01,2686.15 ,840.50 ,篩選范圍法,三級,2015/6/25 10:40,62,0.000004,0.11,1.55E-04,0.0447,#N/A,7,3.13E-01,2304.50,721.08,篩選范圍法,三級,2015/9/12 9:15,62,0.000004,0.11,1.55E-04,0.0447,#N/A,7,3.13E-01,1813.97,567.59,相關(guān)方程法,二級,2015/11/23 14

13、:36,62,0.000004,0.11,1.55E-04,0.0447,#N/A,7,1.08E-03,1862.27,2.02,2016/2/14 13:48,2.13E+038,石油化工,開口閥或開口管線,所有,2014/11/13 14:22,平均排放系數(shù)法,四級,2015/3/4 8:15,63,0.000002,0.079,4.07E-05,0.0015,0.0017,8,1.36E-02,2698.15 ,36.69 ,平均排放系數(shù)法,四級,2015/6/26 10:40,63,0.000002,0.079,4.07E-05,0.0015,0.0017,8,1.36E-02,23

14、16.50,31.50,相關(guān)方程法,二級,2015/9/13 9:15,63,0.000002,0.079,4.07E-05,0.0015,0.0017,8,3.25E-04,1813.97,0.59,平均排放系數(shù)法,四級,2015/11/24 14:36,63,0.000002,0.079,4.07E-05,0.0015,0.0017,8,1.36E-02,1862.27,25.33,2016/2/15 13:48,9.41E+019,石油煉制,攪拌機,所有,2014/11/13 14:22,實測法,實測,2015/3/4 8:15,64,0.000004,0.11,1.58E-04,#N/A,#N/A,9,0.00E+00,2710.15 ,0.00 ,實測法,實測,2015/6/27 10:40,64,0.000004,0.11,1.58E-04,#N/A,#N/A,9,0.00E+00,2328.50,0.00,相關(guān)方程法,二