Method of removing entrained sulfuric acid from alkylate

Abstract

An improvement in the alkylation of olefins with isoalkanes in the presence of sulfuric acid wherein the sulfuric acid is removed from the product by a mechanical coalescer means prior to fractionation. No water wash or caustic treatment is required. Any sulfonates or sulfonic esters are removed by hydrodesulfurization or decomposition catalyst in a separate reactor or in either the deisobutanizer (DIB) or debutanizer (DB) column.

1 - 10 . (canceled)  
     
     
         11 . The alkylation product having a water content of less than 100 ppm produced by the process comprising passing the alkylation product through a deentrainment device containing coalescer material to remove the sulfuric acid therefrom and recovering an effluent comprising alkylation product.  
     
     
         12 . The alkylation product having a water content of less than 100 ppm produced by the process according to claim  8  comprising the steps of: 
 (a) passing said effluent through a deentrainment device containing coalescer material wherein any entrained sulfuric acid is removed from the effluent:    (b) passing the effluent from said deentrainment device to a deisobutanizer (DIB) column containing a hydrodesulfurization catalyst within the stripping section thereof:    (c) concurrently within said deisobutanizer (DIB) column 
 (i) contacting said sulfonates and sulfonic esters with said hydrodesulfurization catalyst to convert at least a of portion of said sulfonates and said sulfonic esters to hydrogen sulfide,  
 (ii) separating isobutane and hydrogen sulfide from said effluent as overheads by fractional distillation: and  
 (iii) removing alkylate product and normal butane from said deisobutanizer (DIB) column as bottoms:  
   (d) recycling the isobutane and hydrogen sulfide to the alkylation process: and    (e) separating the normal butane from the alkylate product.    
     
     
         13 . An alkylate product produced in an acid alkylation process having a water content of less than 100 ppm.  
     
     
         14 . The process according to  claim 11  wherein the effluent from the deentrainment device is contacted with a hydrodesulfurization catalyst to convert any sulfonates and sulfonic esters contained therein to hydrogen sulfide which is removed from the alkylation product.  
     
     
         15 . The process according to  claim 11  wherein the effluent from the deentrainment device is contacted with a decomposition catalyst to convert any sulfonates and sulfonic esters contained therein to their constituent components.  
     
     
         16 . The process according to  claim 14  wherein said hydrodesulfurization catalyst is contained within the stripping section of a deisobutanizer (DIB) column which separates isobutane from the alkylation product.  
     
     
         17 . The process according to  claim 14  wherein said hydrodesulfurization catalyst is contained within the stripping section of a debutanizer column which separates normal butane from alkylation product.  
     
     
         18 . The process according to  claim 15  wherein said decomposition catalyst is contained within the stripping section of a deisobutanizer (DIB) column which separates isobutane from the alkylation product.  
     
     
         19 . The process according to  claim 15  wherein said decomposition catalyst is contained within the stripping section of a debutanizer (DB) column which separates normal butane from the alkylation product.  
     
     
         20 . The process according to  claim 11  wherein the normal butane is separated from the alkylate in a separate debutanizer tower.  
     
     
         21 . The process according to  claim 11  wherein the normal butane is separated from the alkylate as a side draw in the deisobutanizer (DIB) column.