| 摘要 |
<PICT:1003119/C4-C5/1> Carbon monoxide and hydrogen are produced, when waste substance containing inorganic and lignin-derived organic components is treated with steam at several hundred degrees Centigrade in the absence of an oxygen-containing atmosphere. As shown, waste sulphite liquor and steam at a temperature of several hundred degrees Centigrade are introduced into an oxygen free reactor 3, and a gaseous mixture containing H2, an oxide of carbon, and gaseous decomposition products of at least partially pyrolysed and/or carbonized lignin is removed at 7, and may be used directly in fuel cell 11 if desired. Inorganic chemicals, e.g. sulphides and carbonates may be recovered at 111. Alternatively, the sulphite liquor may be introduced with calcium hydroxide into 13 in order to precipitate the lignin-derived components, which are then admitted to oxygen-free reactor 3 and treated as before. In this case the supernatant liquor containing inorganic chemicals and wood sugars is separated at 19 for recovery if desired. Included in the lignin derived organic compounds may be lignin sulphonic acid, lignin sulphonates, alkali lignins, acid lignins and products of the reaction of lignin-containing materials with alkali carbonate and sulphide, e.g. as obtained from the "Kraft" or sulphide process. Included in the gaseous product may be CO and/or CO2, gaseous decomposition products of pyrolysed lignin and gaseous sulphur compounds including H2S. Temperatures which provide partial pyrolysing and carbonizing of the lignin-derived organic components in chamber 3 lie within the range 550-1000 DEG C.
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