Process for Removing Nitrogen Compounds from a Hydrocarbon Stream
a technology of hydrocarbons and nitrogen compounds, which is applied in the direction of separation processes, organic chemistry, dispersed particle separation, etc., can solve the problems of shortening the effective life of adsorbents, adversely affecting the performance of nitrogen adsorptive materials, shortening the useful life of adsorbents, etc., to minimize the need to regenerate or replace adsorbents, and prolong the life of adsorbents ,
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example 1
[0032]An adsorbent according to the invention was prepared following Example 2 of U.S. Pat. No. 7,115,154. The resulting adsorbent was found to have 0.142 total moles of Na2O per 100 g of adsorbent. The total moles includes the metal component (Madd) added of 0.036 moles of Na2O per 100 g of adsorbent.
example 2
[0033]A commercially available acid treated clay was obtained from Sud-Chemie under the product name TONSIL CO 630 G for use as a comparative adsorbent.
example 3
[0034]A sample of Y-74 zeolite was slurried in a 15 wt % NH4NO3 aqueous solution and the solution temperature was brought up to 75° C. (167° F.). Y-74 zeolite is a stabilized sodium Y zeolite with a bulk Si / Al2 ratio of approximately 5.2, a unit cell size of approximately 24.53, and a sodium content of approximately 2.7 wt % calculated as Na2O on a dry basis. Y-74 zeolite is prepared from a sodium Y zeolite with a bulk Si / Al2 ratio of approximately 4.9, a unit cell size of approximately 24.67, and a sodium content of approximately 9.4 wt % calculated as Na2O on a dry basis that is ammonium exchanged to remove approximately 75% of the Na and then steam de-aluminated at approximately 600° C. (1112° F.) by generally following steps (1) and (2) of the procedure described in col. 4, line 47 to col. 5, line 2 of U.S. Pat. No. 5,324,877. After 1 hour of contact at 75° C. (167° F.), the slurry was filtered and the filter cake was washed with an excessive amount of warm de-ionized water. The...
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