Process for manufacturing a composite sorbent material for chromatographical separation of biopolymers

Abstract

The present invention relates to a sorbent material for separation and purification of biopolymers, particularly nucleic acids, having a solid support substantially modified with a copolymer coating comprising aromatic monomers and crosslinking compounds and unsaturated esters or ethers preferably attached to the support via a vinylchlorsilane. The use of these materials for separation of nucleic acids, particularly a one-step isolation of DNA from lysates of different biological sources, is an object of the invention as well as a chromatographic column or cartridge at least partially filled with the sorbent material of the invention, a membrane-like device comprising the sorbent material of the invention, and a kit comprising the sorbent material of the invention in bulk or packed in chromatographic devices as well as other devices necessary for performing sample preparations.

1 - 22 . (canceled) 
     
     
         23 . A process for the purification and/or isolation of nucleic acids wherein the process comprises
 lysing cells yielding a sample containing nucleic acids and proteins,   contacting the sample with a sorbent material binding the proteins, and   collecting the eluate containing the nucleic acids   where the sorbent material comprises a porous inorganic material comprising silica which is at least partially covered by a polymer coating having the general formula   
       
         
           
           
               
               
           
         
         wherein the mass ratio of copolymer components [A], [B], and [M] complies with the formula 1:0.03-0.3:0-0.2 and
 [A] is derived from a monomer with general formula 
 
       
       
         
           
           
               
               
           
         
       
       R═H; 2, 3, 4 —OH; —COCH; —NO 2 ; —Cl; —Br; —F; —OAlk; —OAc;
   —NH 2 ; —NHAc; —N(Alk) 2 ; -Alk (C 1 -C 16 )   [B] is derived from a monomer of general formula   
 
       
         
           
           
               
               
           
         
         
           R═H; 2, 3, —OH; —COOH; —NO 2 ; —Cl; —Br, —F; —OAlk; —OAc; —NH 2 ; —NHAc; —N(Alk) 2 ; -Alk (C 1 -C 15 ); and 
         
         [M] is derived from a monomer of general formula 
       
       
         
           
           
               
               
           
         
       
       R═H; Ar; Alk (C 1 -C 12 )
   R 1 ═H; Ar; Alk (C 1 -C 12 ); —(—CH 2 —) n —OH n=2-18   or a monomer of general formula   
 
       
         
           
           
               
               
           
         
       
       n=1-18
   R═H; Ar; Alk, (C 1 -C 12 )   R 1 ═H; Ar; Alk.(C 1 -C 12 ); CH 2  m OH m=2 -18   
 
     
     
         24 . The process of  claim 23  wherein the support is a porous inorganic material comprising inorganic metal oxide. 
     
     
         25 . The process of  claim 24  wherein the porous inorganic metal oxides show a bidisperse distribution of pore sizes. 
     
     
         26 . The process of  claim 23  wherein the support has an average pore size of 2-200 nm. 
     
     
         27 . The process of  claim 23  wherein the polymer coating has a thickness of about 10 to 250 Angstrom. 
     
     
         28 . The process of  claim 24  wherein the inorganic metal oxide is selected from the group consisting of oxides of aluminum, titanium, zirconium, silicon oxides, iron oxides, controlled pore glass (CPG), diatomaceous earth and combinations thereof. 
     
     
         29 . The process of  claim 25  wherein the porous inorganic metal oxide shows a bidisperse distribution with mean pore diameters in the range of 20-100 nm for the larger pore size. 
     
     
         30 . The process of  claim 29  wherein the porous inorganic metal oxide has a mean pore diameter in the range of 2-15 nm for the smaller pore size. 
     
     
         31 . The process of  claim 29  wherein the ratio of the mean diameter of the large pore size distribution and the lower pore size distribution is in the range of 2-15. 
     
     
         32 . The process of  claim 26 , wherein the support has an average pore size of 2-100 nm. 
     
     
         33 . The process of  claim 26  wherein the support has a specific surface area of 20-300 m 2 /g. 
     
     
         34 . The process of  claim 33  wherein the support has a specific surface area of 20-100 m 2 /g. 
     
     
         35 . The process of  claim 27  wherein the polymer coating has a thickness of 10 to 100 Angstrom. 
     
     
         36 . The process of  claim 27  wherein the polymer coating has micropores of less than 50 Angstrom accessible to water, salts, and low molecular weight substances. 
     
     
         37 . The process of  claim 27  wherein the polymer coating is non-adsorptive towards nucleic acids and adsorptive towards proteins. 
     
     
         39 . The process of  claim 23  comprising component [M]. 
     
     
         40 . The process of claim  38 , wherein [M] is selected from the group consisting of hydroxyethyl methacrylate, methacrylic acid and allyl alcohol. 
     
     
         41 . The process of  claim 23 , wherein x and y are independent of each other, x and y are an integer of 1-100 and z is an integer of 0-100.