Method for preparing a nano-calcium carbonate slurry from waste gypsum as calcium source, the product and use thereof
The present invention discloses a process for producing a nano calcium carbonate slurry from a feedstock of waste gypsum, wherein: an aqueous gypsum slurry of the feedstock is mixed with ammonia water by stirring; with CO 2 injected in the slurry is under continuous stirring until the calcium sulfate in the waste gypsum is completely carbonated into nano calcium carbonate; after filtration, the filter cake is dispersed in water to obtain the nano calcium carbonate slurry. This process is easy to operate and to obtain a low-cost and a lower decomposition temperature of calcium carbonate. The present invention also discloses a nano calcium carbonate slurry and its application in preparation of a CaO-based carbon dioxide adsorbent and complex catalyst used for a reactive sorption enhanced reforming process for hydrogen production from methane. The CaO-based carbon dioxide adsorbent prepared shows good cycle stability and fast sorption rate, and complex catalyst used for reactive sorption enhanced methane steam reforming can obtain the hydrogen with purity of more than 90%.
1. A method for preparation of a CaO-based CO 2 adsorbent from a nano calcium carbonate slurry comprising the steps of: adding a dispersing agent and a binder to the nano calcium carbonate slurry, stirring until uniform, drying, molding, calcination to obtain the CaO-based CO 2 adsorbent, wherein the nano calcium carbonate slurry is produced from the following steps: (a) an aqueous gypsum slurry of waste gypsum is mixed with ammonia water by stirring; (b) with CO 2 being injected in the slurry, the slurry is under continuous stirring until the calcium sulfate in the waste gypsum is completely formed nano calcium carbonate; (c) after filtration, a filter cake is dispersed into water to obtain a slurry of nano calcium carbonate.
2. The process according to claim 1 , wherein the waste gypsum is phosphogypsum, desulfurization gypsum or fluorgypsum.
3. The process according to claim 1 , wherein the mass ratio of waste gypsum to water in aqueous gypsum slurry is 1:1-10; the molar ratio of ammonia to calcium sulfate in waste gypsum is 1-5:1; the mass ratio of filter cake to water in nano calcium carbonate slurry is 1:1-10.
4. The method according to claim 1 , wherein: the binder is alumina sol or silica sol; the mass ratio of Al 2 O 3 in alumina sol to CaCO 3 in nano calcium carbonate slurry is 0-0.7:1; the mass ratio of SiO 2 in silica sol to CaCO 3 in nano calcium carbonate slurry is 0-0.7:1; the mass ratio of dispersing agent to nano calcium carbonate slurry is 0.002-0.005:1, the dispersing agent is polyethyleneglycol stearate or polyethylene glycol or sodium dodecylbenzenesulfonate.
5. The method according to claim 1 , wherein: the condition of drying is under the temperature range of 80-150° C. for 1-15 hours; the condition of calcination is under the temperature range of 750-950° C. for 1-12 hours; the molding is extruded molding or spray granulation molding.