Table 1 Stream properties after dust is filtered in a running waste incinerator plant in Japan with waste throughput of 30 t day−1

From: Steam recovery from flue gas by organosilica membranes for simultaneous harvesting of water and energy

Measurement month

Flow rate [m3(STP) h−1]

Temperature [°C]

Composition

H2O [%]

N2a [%]

O2 [%]

CO2 [%]

HCl [ppm]

NOx [ppm]

SOx [ppm]

CO [ppm]

Ash dust [g m−3 (STP)]

Feb. 2019

14,700

170

39.6

40.6

9.0

10.8

25

130

1

8

<0.001

Feb. 2019

13,100

169

38.1

42.0

11.4

8.5

14

130

<1

6

<0.001

Jan. 2021

11,900

166

39.0

41.5

11.5

8.0

30

100

11

4

<0.001

Average

13,200

168

38.9

41.4

10.6

9.1

23

120

4

6

<0.001

  1. aCalculated via 100% minus the compositions of other products. The measurements of flow rate and temperature followed JIS Z 8808, and those of the compositions of H2O, O2, CO2, HCl, NOx, SOx, CO, and ash dust followed JIS Z 8808, JIS K 0301, JIS K 0301, JIS K 0107, JIS K 0104, JIS K 0103, JIS K 0098, and JIS Z 8808, respectively53,54,55,56,57,58. The amount of ash dust was less than the detection limit.
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