Amorphous adsorbent, method of obtaining the same and its use in the bleaching of fats and/or oils
View Patent ↗The invention relates to a method for producing an adsorbent, in particular a bleaching earth, wherein a clay material having: a surface area of 180 to 300 m2/g; a total pore volume of 0.5 to 0.7 ml/l; wherein at least 60% of the total pore volume are provided by pores having a pore diameter of at least 140 A, at least 40% of the total pore volume is provided by pores having a pore diameter of less than 250 A and at least 15% of the total pore volume are provided by pores having a pore diameter of 140 to 250 A; and said clay material having an amorphous structure according to XRD data; is activated by an activation procedure. Further, the invention relates to an adsorbent as obtained by the method and a method for purification of oils, fats and biofuels.
1. Method for bleaching fats and/or oils, wherein
a crude oil derived from animal or plant material is provided;
the crude oil is treated with a bleaching material comprising a clay material having:
a surface area of 180 to 300 m 2 /g;
a total pore volume of 0.5 to 0.7 ml/g;
wherein at least 60% of the total pore volume are provided by pores having a pore diameter of at least 140 Å, at least 40% of the total pore volume is provided by pores having a pore diameter of less than 250 Å and at least 15% of the total pore volume are provided by pores having a pore diameter of 140 to 250 Å and less than 20% of the total pore volume is formed by pores having a diameter of >800 Å;
a SiO 2 content of between more than 60 wt. % and less than 75 wt. %;
an aluminum content, calculated as Al 2 O 3 , of between less than 12 wt. % and more than 2 wt. %; and
said clay material having an amorphous structure according to XRD data; and
the bleached oil is separated from the used bleaching material.
2. Method according to claim 1 , wherein the clay material is an acid activated clay material.
3. Method according to claim 2 , wherein the acid is selected from the group of phosphoric acid, sulphuric acid and citric acid.
4. Method according to claim 2 , wherein the clay material is acid-activated by depositing an acid on the clay and the amount of acid deposited on the clay material is selected within a range of 2 to 5 wt.-%, calculated as water-free acid and based on the weight of the dry clay material.
5. Method according to claim 1 , wherein the crude oil is selected from the group of canola oil, soybean oil, rapeseed oil, palm oil, sunflower oil.
6. Method according to claim 1 , wherein the crude oil contains phosphorous in an amount of less than 100 ppm.
7. Method according to claim 1 , wherein the crude oil is transesterified with methanol before treatment with the clay material.
8. Method for producing an adsorbent, in particular a bleaching earth, wherein a clay material having:
a surface area of 180 to 300 m 2 /g;
a total pore volume of 0.5 to 0.7 ml/g;
wherein at least 60% of the total pore volume are provided by pores having a pore diameter of at least 140 Å, at least 40% of the total pore volume is provided by pores having a pore diameter of less than 250 Å and at least 15% of the total pore volume are provided by pores having a pore diameter of 140 to 250 Å and less than 20% of the total pore volume is formed by pores having a diameter of >800 Å;
a SiO 2 content of between more than 60 wt. % and less than 75 wt. %;
an aluminum content, calculated as Al 2 O 3 , of between less than 12 wt. % and more than 2 wt. %; and
said clay material having an amorphous structure according to XRD data;
is activated by an activation procedure, wherein the clay is activated by contacting the clay material with an acid.
9. Method according to claim 8 , wherein at least 20% of the total pore volume of the clay material is provided by pores having a pore diameter of less than 140 Å.
10. Method according to claim 8 , wherein at least 10% of the total pore volume of the clay material is provided by pores having a pore diameter of 75 to 140 Å.
11. Method according to claim 8 , wherein less than 40% of the total pore volume of the clay material is formed by pores having a pore diameter of 250 to 800 Å.
12. Method according to claim 8 , wherein at least 12% of the total pore volume of the clay material is provided by pores having a pore diameter of less than 75 Å.
13. Method according to claim 8 , wherein less than 80% of the total pore volume of the clay material is formed by pores having a pore diameter of more than 140 Å.
14. Method according to claim 8 , wherein less than 60% of the total pore volume is formed by pores having a pore diameter of at least 250 Å.
15. Method according to claim 8 , wherein the clay material contains aluminum, calculated as Al 2 O 3 , in an amount of less than 10 wt.-%.
16. Method according to claim 8 , wherein the acid is deposited on the clay in an amount of 2 to 5 wt.-%, calculated as water-free acid and based on the weight of the dry clay material.
17. Method according to claim 8 , wherein the clay material is leached with the acid.
18. Method according to claim 17 , wherein the amount of acid is selected within a range of 15 to 40 wt.-%, calculated as water-free acid and based on the weight of the dry clay material.
19. Method according to claim 8 , wherein the clay material is separated from the acid after extraction, washed, dried and optionally ground.
20. Method according to claim 8 , wherein the acid is selected from the group of phosphoric acid, sulphuric acid and citric acid.