FIELD: fat and oil industry. SUBSTANCE: method involves the successive two-stage separation of catalyst. At the first stage the separation of catalyst particles is carried out at 140-200 C at magnetic field 0.7-1.3 Tl, and at the second stage at 80-130 C by either filtration or magnetic separation method in the field with 1.4-2.0 Tl. EFFECT: improved method of nickel removal. 1 tbl
| Title | Year | Author | Number |
|---|---|---|---|
| METHOD OF FAT HYDROGENIZATION | 1988 |
|
SU1587913A1 |
| METHOD FOR SEPARATION OF DISPERSE NICKEL CATALYST OF HYDROGENATED FATS | 1993 |
|
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| METHOD OF PRODUCING HYDROGENATED FATS AND FATTY ACIDS ON STATIONARY CATALYST | 1992 |
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| ROTARY ELECTROMAGNETIC SEPARATOR FOR CLEARING TECHNOLOGIC LIQUIDS FROM FINELY DIVIDED FERROMAGNETIC PARTICLES | 1992 |
|
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| ROTOR ELECTROMAGNETIC SEPARATOR FOR CLEANING OF PROCESS LIQUIDS | 1992 |
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| ROTARY ELECTROMAGNET SEPARATOR FOR CLEANING TECHNOLOGICAL LIQUIDS OF LOW MAGNETIC FINELY DIVIDED PARTICLES | 1992 |
|
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| METHOD OF PRODUCING CATALYST FOR HYDROGENATION OF FATS | 0 |
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SU1595555A1 |
| PROCESS FOR PRODUCING EDIBLE DEODORIZED HYDROGENATED FAT | 0 |
|
SU1830077A3 |
