US2014291578A1PendingUtilityA1

Process to prepare adsorbents from organic fertilizer and their applications for removal of acidic gases from wet air streams

Assignee: UNIV CITY NEW YORK RES FOUNDPriority: Nov 29, 2000Filed: Mar 31, 2014Published: Oct 2, 2014
Est. expiryNov 29, 2020(expired)· nominal 20-yr term from priority
B01J 20/22B01J 20/2808B01D 2253/102B01J 20/30B01J 20/28069B01D 2253/10B01D 2257/304B01D 53/1456Y10T428/2982B01D 53/8612B01D 2257/408B01J 2220/4887B01D 2257/404B01J 20/28061B01J 20/08B01J 20/20B01J 20/0237B01J 2220/42B01J 20/3078B01J 20/0229B01J 20/28057B01D 2257/302B01J 20/103B01J 20/24B01J 20/0244B01J 20/041B01J 20/28071B01D 53/02
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Claims

Abstract

The invention is directed to an adsorbent comprising: a) 20-30% porous carbon with incorporated organic nitrogen species; and b) 70-80% inorganic matter. The invention is directed to a method of making an adsorbent which comprises: a) thermally drying dewatered sewage sludge to form granulated organic fertilizer; and b) pyrolyzing said the organic fertilizer at temperatures between 600 and 1000° C. The invention is additionally directed to the process of removing acidic gases from wet air streams comprising putting an adsorbent in contact with the wet air stream and allowing the adsorbent to adsorb the acidic gases.

Claims

exact text as granted — not AI-modified
1 - 28 . (canceled) 
     
     
         29 . An adsorbent derived from dewatered sewage sludge, comprising:
 20-30% porous non-activated carbon; and   70-80% inorganic matter,   wherein the adsorbent has a basic pH, and   wherein the adsorbent maintains a basic pH after hydrogen sulfide adsorption to a breakthrough capacity.   
     
     
         30 . The adsorbent as defined in  claim 29 , wherein said carbon is present as an organic nitrogen species. 
     
     
         31 . The adsorbent as defined in  claim 30 , wherein said the nitrogen species comprise amine or pyridine groups. 
     
     
         32 . The adsorbent as defined in  claim 29 , wherein the pH of the adsorbent is greater than 10. 
     
     
         33 . The adsorbent as defined in  claim 29 , wherein the adsorbent reacts with hydrogen sulfide to produce elemental sulfur and salt forms thereof. 
     
     
         34 . An adsorbent as defined in  claim 29 , wherein said adsorbent has a surface area of 100-500 m 2 /g. 
     
     
         35 . An adsorbent as defined in  claim 34 , wherein said adsorbent has a surface area of 100-200 m 2 /g.

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