Chloride → Bisulfite

HRID 1381845

反応式

HRID 1381845 の反応式
[OH-].[Ca+2].[OH-].[Mg:4].[Cl-].[S:6]([O-])([O-:9])(=[O:8])=[O:7].[OH-].[Mg+2].[OH-].S(=O)=O>>[S:6]([O-:9])([O-:8])=[O:7].[Mg+2:4].[S:6](=[O:7])([OH:9])[O-:8]

参加物

8

実験手順

The present invention provides for substantially complete removal of sulfur dioxide (SO2) from SO2 -containing effluent gases, particularly from SO2 -containing flue gas streams of fossil fuel power plants. An absorbent is formed by combining seawater and hydrated lime usually at a pH in the range from 8.0 to 10.0, producing magnesium hydroxide by the reaction of the hydrated lime with soluble magnesium which is naturally present in the seawater as chloride and sulfate. The absorbent is then added to a recirculating absorbent stream, typically at a more acid pH, usually below about 6.0, and the absorbent stream is contacted with the flue gas in a suitable contact vessel. In the contact vessel, the magnesium hydroxide reacts with the SO2 in the flue gas to form magnesium sulfite and bisulfite. The magnesium sulfite and bisulfite, in turn, are oxidized, to soluble magnesium sulfate, typically by air sparging in the contact vessel or a separate tank. Magnesium sulfate reacts with the added hydrated lime to regenerate magnesium hydroxide and produce gypsum. These reaction products are recirculated as a slurry in the scrubber for the removal of SO2 and sulfurous acid without the requirement of separating magnesium hydroxide from the rest of the slurry stream. The gypsum is non-toxic and may safely be returned to the marine environment in soluble form at very low concentrations.

後処理

  1. additionThe absorbent is then added to a recirculating absorbent stream, typically at a more acid pH, usually below about 6.0
  2. customthe absorbent stream is contacted with the flue gas in a suitable contact vessel

出典と根拠

ORDレコード
ord-1f649c1fa88b4901b8c0e46a5ba07fc5
出典データセット
uspto-grants-1989_02
特許番号
US04804523

関連ノート

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