Apparatus for the production of water absorbing polymers
US-9238215-B2 · Jan 19, 2016 · US
US2016161184A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016161184-A1 |
| Application number | US-201615047074-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 18, 2016 |
| Priority date | Sep 25, 2013 |
| Publication date | Jun 9, 2016 |
| Grant date | — |
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When a kneaded mixture produced by adding a hinder-containing additive and water to carbon powder and kneading the mixture is formed into a rod-shaped carbon heat source (HS) and the carbon. heat source (HS) is subsequently dried to manufacture a finished product, a drying method according to the present invention includes generating a dry atmosphere in which an evaporation rate (Vo) at which the water evaporates through an outer surface of the carbon heat source (HS) is made approximately equal to a speed (Vs) at which the water in the carbon heat source (HS) moves toward the outer surface while a weight absolute humidity (AH) is lowered in a stepwise manner, and drying the carbon heat source (HS) in the dry atmosphere.
Opening claim text (preview).
1 . A carbon heat source drying method in which a kneaded mixture produced by adding a binder-containing additive and water to carbon powder and kneading the mixture is formed into a rod-shaped carbon heat source and the carbon heat source is subsequently dried to manufacture a finished product, characterized in that the method comprises: generating a dry atmosphere in which an evaporation rate at which the water evaporates through an outer surface of the carbon heat source is made approximately equal to a speed at which the water in the carbon heat source moves from a center thereof toward the outer surface while a weight absolute humidity is lowered in a stepwise manner; and drying the carbon heat source in the dry atmosphere. 2 . The carbon heat source drying method according to claim 1 , characterized in that the drying of the carbon heat source is carried out in a plurality of drying stages in accordance with a changing degree of dryness of the carbon heat source, and between adjacent drying stages, at least one of a dry bulb temperature and a relative humidity of the dry atmosphere is changed. 3 . The carbon heat source drying method according to claim 2 , characterized in that the dry bulb temperature and the relative humidity of the dry atmosphere in each of the drying stages are so determined. as to maintain a transverse cross-sectional shape of the carbon heat source irrespective of the changing degree of dryness of the carbon heat source. 4 . The carbon heat source drying method according to claim 2 , characterized in that the dry bulb temperature in a first drying stage of the drying stages is set at a value greater than or equal to the dry bulb temperatures in the subsequent drying stages. 5 . The carbon heat source drying method according to claim 4 , characterized in that the weight absolute humidity in each of the drying stages corresponds to at least 40% of the water content in the carbon heat source in the corresponding drying stage to which the carbon heat source has transitioned. 6 . The carbon heat source drying method according to claim 3 , characterized in that the dry bulb temperature in a first drying stage of the drying stages is set to be higher than or equal to the dry bulb temperatures in the subsequent drying stages. 7 . The carbon heat source drying method according to claim 6 , characterized in that the weight absolute humidity in each of the drying stages corresponds to at least 40% of the water content in the carbon heat source in the corresponding drying stage to which the carbon heat source has transitioned.
Humidity · CPC title
Temperature; Pressure · CPC title
Controlling the drying process in dependence on liquid content of solid materials or objects · CPC title
comprising as heat source a carbon fuel or an oxidized or thermally degraded carbonaceous fuel, e.g. carbohydrates, cellulosic material · CPC title
Mechanical Engineering · mapped topic
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