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The invention relates to novel and innovative PCC pigments, able to be used in a paper coating formulations to manufacture coated “multipurpose” papers, in particular for inkjet applications, whose print qualities would be identical or quite similar to high resolution commercial papers, while mainta

The invention relates to novel and innovative PCC pigments, able to be used in a paper coating formulations to manufacture coated “multipurpose” papers, in particular for inkjet applications, whose print qualities would be identical or quite similar to high resolution commercial papers, while maintaining a reduced paper manufacturing and production cost. Said pigments are obtained by a carbonation process using a reduced flow rate of CO2/air, which leads to porous agglomerates of PCC of a very specific structure and unique properties, followed by an upconcentration step leading to substantially the same agglomerates but with a higher, appropriate, solids content.

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1. A precipitated calcium carbonate (PCC) product comprising porous spherical aggregates/agglomerates having a mean aggregate diameter of 1 to 5 μm and a specific surface area of 30-100 m2/g, wherein the porousrical aggregates/agglomerates consist of ultrafine calcium carbonate particles bound toget

1. A precipitated calcium carbonate (PCC) product comprising porous spherical aggregates/agglomerates having a mean aggregate diameter of 1 to 5 μm and a specific surface area of 30-100 m2/g, wherein the porousrical aggregates/agglomerates consist of ultrafine calcium carbonate particles bound together to form the porous spherical aggregates/agglomerates, and wherein the ultrafine calcium carbonate particles have a primary acicular particle size of 20 to 50 nm, and an aspect ratio of between 1:2 and 1:10. 2. The PCC product of claim 1, which is prepared by the process comprising the steps of: a) preparing a calcium hydroxide slurry by mixing quicklime (CaO) with water;b) screening the calcium hydroxide slurry obtained in step a) to obtain a screened slurry;c) adjusting the temperature of the screened slurry to obtain a temperature adjusted slurry;d) contacting the temperature adjusted slurry with a carbon dioxide-containing gas at a carbonation gas flow rate of below 30 liters per minute at standard temperature and pressure per kilogram calcium hydroxide in the presence of sulphuric acid and i) magnesium sulphate and aluminium sulphate, (ii) magnesium sulphate and zinc sulphate, or (iii) magnesium sulphate, aluminium sulphate and zinc sulphate, to obtain aggregates/agglomerates;e) screening the aggregates/agglomerates obtained in step d) to obtain ultrafine PCC aggregates/agglomerates having a mean aggregate diameter of 1 to 5 μm; andf) subjecting the ultrafine PCC aggregates/agglomerates obtained in step e) to dewatering and/or redispersing steps to obtain a PCC product comprising porous spherical aggregates/agglomerates having a mean aggregate diameter of 1 to 5 μm and a specific surface area of 30-100 m2/g, wherein the porous spherical aggregates/agglomerates consist of ultrafine calcium carbonate particles bound together to form the porous spherical aggregates/agglomerates, and wherein the ultrafine calcium carbonate particles have a primary acicular particle size of 20 to 50 nm, and an aspect ratio of between 1:2 and 1:10. 3. The PCC product of claim 1, wherein the aggregates/agglomerates have an average diameter of 2 μm. 4. The PCC product of claim 1, having a fraction of fines below 2 μm of less than 20%. 5. The PCC product of claim 1, having a fraction of fines below 2 μm of less than 15%. 6. The PCC product of claim 1, having a specific surface area of 50 to 80 m2/g. 7. The PCC product of claim 1, having a solids content of 25 to 60%. 8. The PCC product of claim 1, having a solids content of 35 to 50%. 9. The PCC product of claim 1, having a solids content of 39 to 40%. 10. The PCC product of claim 1, comprising a dispersant aid. 11. The PCC product of claim 10, wherein the aggregates/agglomerates are coated with the dispersant aid. 12. The PCC product of claim 10, wherein the dispersant aid is a cationic, anionic or combination dispersant. 13. The PCC product of claim 10, wherein the dispersant aid comprises a sodium salt of polyacrylic acid. 14. The PCC product of claim 1, which comprises 1.5 to 3.5 dry weight percent of polyacrylic acid based on the dry weight percent of PCC. 15. The PCC product of claim 1, which is in the form of a dried pigment. 16. The PCC product of claim 1, which is in the form of a slurry. 17. A coating formulation comprising the PCC product of claim 1. 18. The coating formulation of claim 17, for use in the paper making industry. 19. An inkjet paper comprising the coating formulation of claim 18. 20. The inkjet paper of claim 19, which is a multipurpose inject paper or a specialty, high quality paper. 21. An inkjet paper coated by at least the coating composition of claim 18.