Method for selective hydrogenation using a catalyst containing copper and at least one metal selected from between nickel or cobalt
US-9783745-B2 · Oct 10, 2017 · US
US10501694B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10501694-B2 |
| Application number | US-201715852337-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 22, 2017 |
| Priority date | Dec 22, 2016 |
| Publication date | Dec 10, 2019 |
| Grant date | Dec 10, 2019 |
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Selective hydrogenation of polyunsaturated compounds containing at least 2 carbon atoms per molecule contained in a hydrocarbon feed with a final boiling point of 300° C. or less, in the presence of a catalyst having a support formed from alumina and an active phase constituted by nickel, said catalyst being prepared by: i) bringing said support into contact with at least one solution containing at least one precursor of nickel; ii) bringing said support into contact with at least one solution containing at least one organic compound comprising at least one amine function with the empirical formula C x N y H z in which x is in the range 1 to 20, y=1−x and z=2−2x+2, or an amide function, or an amino acid, iii) drying said impregnated support at a temperature of less than 250° C.; steps i) and ii) being carried out separately, in any order, or simultaneously.
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The invention claimed is: 1. A process comprising selective hydrogenation of polyunsaturated compounds containing at least 2 carbon atoms per molecule, contained in a hydrocarbon feed that is a C2 cut from steam cracking, a C2-C3 cut from steam cracking, a C3 cut from steam cracking, a C4 cut from steam cracking, a C5 cut from steam cracking or gasolines from steam cracking, with a final boiling point of 300° C. or less, said process being carried out at a temperature in the range 0° C. to 300° C., at a pressure in the range 0.1 to 10 MPa, in liquid phase at a molar ratio of hydrogen/(polyunsaturated compounds to be hydrogenated) in the range 0.1 to 10 and at an hourly space velocity in the range 0.1 to 200 h −1 , or in gas phase at a molar ratio of hydrogen/(polyunsaturated compounds to be hydrogenated) in the range 0.5 to 1000 and at an hourly space velocity in the range 100 to 40000 h −1 , in the presence of a catalyst comprising a support formed from alumina and an active phase constituted by nickel, said catalyst being prepared by a process comprising at least: i) bringing said support into contact with at least one solution containing at least one precursor of nickel; ii) bringing said support into contact with at least one solution containing at least one organic compound having 1 to 20 carbon atoms and at least one amine function with the empirical formula C x N y H z in which 1≤x≤20, 1≤y≤x, 2≤z≤2x+2, or at least one amide function, or at least one amino acid, to produce an impregnated support, iii) drying said impregnated support at a temperature of less than 250° C. so as to obtain a dried catalyst comprising nickel in the form of nanoparticles measured, in oxide form, of 1.5 to 10.0 nm; i) and ii) being carried out separately, in any order, or simultaneously. 2. The process as claimed in claim 1 , further comprising at iv) at least one calcination of said dried catalyst obtained in iii) at a temperature in the range 250° C. to 1000° C. 3. The process as claimed in claim 1 , wherein i) and ii) are carried out simultaneously. 4. The process as claimed in claim 1 , wherein i) is carried out before ii). 5. The process as claimed in claim 1 , wherein ii) is carried out before i). 6. The process as claimed in claim 1 , wherein i) and/or ii) is (are) carried out by dry impregnation. 7. The process as claimed in claim 1 , wherein the catalyst has a nickel content is in the range 1% to 35% by weight with respect to the total catalyst weight. 8. The process as claimed in claim 1 , wherein the at least one organic compound is an amino acid. 9. The process as claimed in claim 1 , wherein the at least one organic compound comprises at least one amide function that is an acyclic amide function or a cyclic amide function. 10. The process as claimed in claim 1 , wherein the at least one organic compound comprises at least one amide function and at least one other function which differs from the at least one amide function, that is a carboxylic acid function or an alcohol function. 11. The process as claimed in claim 9 , wherein the at least one organic compound furthermore comprises a supplemental nitrogen heteroatom and is urea, N-methylurea, N,N′-dimethylurea, 1,1-dimethylurea or tetramethylurea, in any one of their isomeric forms. 12. The process as claimed in claim 1 , wherein the feed is a C2 cut from steam cracking or a C2-C3 cut from steam cracking, and in which process in a gas phase the molar ratio of (hydrogen)/(polyunsaturated compounds to be hydrogenated) is in the range 0.5 to 1000, the temperature is in the range 0° C. to 300° C., the hourly space velocity (HSV) is in the range 100 to 40000 h −1 , and the pressure is in the range 0.1 to 6.0 MPa. 13. The process as claimed in claim 1 , wherein the feed is gasolines from steam cracking and in which process in a liquid phase the molar ratio of (hydrogen)/(polyunsaturated compounds to be hydrogenated) is in the range 0.5 to 10, the temperature is in the range 0° C. to 200° C., the hourly space velocity (HSV) is in the range 0.5 to 100 h −1 , and the pressure is in the range 0.3 to 8.0 MPa. 14. The process as claimed in claim 1 , wherein the polyunsaturated compounds containing at least 2 carbon atoms per molecule are diolefins, acetylenes and/or alkenylaromatics. 15. The process as claimed in claim 1 , carried out in gas phase. 16. The process as claimed in claim 1 , carried out in liquid phase.
containing nickel or cobalt metal, or compounds thereof · CPC title
containing carboxylic acids or their salts {(B01J31/0277 - B01J31/0298 take precedence; multi-metal carboxylate complexes like Pd (II) acetate, i.e. Pd3 (OAc) 6 or Cr(II)acetate, i.e. Cr2(OAc)4 B01J31/2226)} · CPC title
Alumina · CPC title
Nickel · CPC title
Imides, amides or imidates (R-C=NR(OR)) · CPC title
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