PL80B1 - The method of obtaining catalysts for the hydrogenation of unsaturated organic compounds. - Google Patents
The method of obtaining catalysts for the hydrogenation of unsaturated organic compounds. Download PDFInfo
- Publication number
- PL80B1 PL80B1 PL80A PL8019A PL80B1 PL 80 B1 PL80 B1 PL 80B1 PL 80 A PL80 A PL 80A PL 8019 A PL8019 A PL 8019A PL 80 B1 PL80 B1 PL 80B1
- Authority
- PL
- Poland
- Prior art keywords
- nickel
- organic compounds
- catalysts
- unsaturated organic
- hydrogenation
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims description 12
- 238000000034 method Methods 0.000 title claims description 8
- 150000002894 organic compounds Chemical class 0.000 title claims 2
- 238000005984 hydrogenation reaction Methods 0.000 title 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 15
- 229910052759 nickel Inorganic materials 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 4
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 claims description 4
- 229910001385 heavy metal Inorganic materials 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 150000002815 nickel Chemical class 0.000 claims description 4
- 229910001388 sodium aluminate Inorganic materials 0.000 claims description 4
- 239000004927 clay Substances 0.000 claims description 3
- -1 nickel aluminate Chemical class 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 150000004645 aluminates Chemical class 0.000 claims description 2
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 claims description 2
- 230000036571 hydration Effects 0.000 claims 1
- 238000006703 hydration reaction Methods 0.000 claims 1
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 claims 1
- 239000002244 precipitate Substances 0.000 claims 1
- 239000012266 salt solution Substances 0.000 claims 1
- 229920006395 saturated elastomer Polymers 0.000 claims 1
- 238000010791 quenching Methods 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Description
W latach ostatnich stosowanie katali¬ zatorów metalowych do hartowania kwa¬ sów tluszczowych i ich estrów przybralo znaczne rozmiary, przyczem katalizator}', przewaznie niklowe, byly preparowane w najrozmaitszy sposób. Zadaniem wiel¬ kiej wagi jest wytworzenie katalizatora w mozliwie najprostszej formie, a przy- tem o mozliwie najwyzszej sprawnosci.Próby wykazaly, ze gliniany ciezkich metalów, zwlaszcza niklu, daja kataliza¬ tory o wydatnem dzialaniu. Bardzo spraw¬ nie dzialajacy katalizator otrzymuje sie w nastepujacy prosty sposób.Z roztworów soli ciezkich metali, zwlaszcza soli niklowych, naprzyklad siar¬ czanu niklu straca sie przy miernej tem¬ peraturze rozpuszczalnemi glinianami, na¬ przyklad glinianem sodowym glinian niklowy, osad przemywa, suszy i traktuje wodorem przy 300—400°C.Niniejszy sposób otrzymywania kata¬ lizatora ma nastepujace zalety: wymaga stosunkowo drobnych ilosci niklu, prze¬ mywanie osadu latwo daje sie uskutecz¬ nic, nikiel rozdzielony jest w kataliza¬ torze na nadzwyczajnie drobne czasteczki, wreszcie, dzieki temu rozdrobnieniu, kata¬ lizator w czasie procesu hartowania ole¬ jów i tluszczów nie opada na dno, lecz pozostaje w zawieszeniu, wskutek czego dzialanie reakcyjne pomiedzy olejami, katalizatorem i wodorem jest bardzo ulatwione.Mozna takze obojetne ciala, jak na¬ przyklad krzemionke, przepoic roztworem soli niklowych, glinian niklu osadzic na powierzchni ciala obojetnego zapomocaa': glinianu sodowego i dalej stosowac jak wyzej. PL PLIn recent years, the use of metal catalysts for quenching fatty acids and their esters has become very large, and the catalysts, mostly nickel-based, have been prepared in a variety of ways. The task of great importance is to make the catalyst as simple as possible and at the same time as efficient as possible. Trials have shown that clay from heavy metals, especially nickel, produces catalysts with high performance. A very efficient catalyst can be obtained in the following simple way: From solutions of heavy metal salts, especially nickel salts, for example nickel sulphate, at moderate temperatures, are lost by soluble aluminates, for example sodium aluminate, nickel aluminate, sludge washed, dried and treated with hydrogen at 300-400 ° C. The present method of obtaining the catalyst has the following advantages: it requires relatively small amounts of nickel, washing the sludge is easily effective, the nickel is separated in the catalyst into extremely fine particles, and finally Due to this fragmentation, the catalyst does not sink to the bottom during the quenching process of oils and fats, but remains in suspension, as a result of which the reaction between oils, catalyst and hydrogen is greatly facilitated. Inert bodies, such as for example silica, permeate with a solution of nickel salts, deposit nickel aluminate on the surface of the inert body with a sodium aluminate and continue as above. PL PL
Claims (4)
Publications (1)
| Publication Number | Publication Date |
|---|---|
| PL80B1 true PL80B1 (en) | 1924-05-26 |
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