Calculate Embedded Emissions for Unwrought Aluminium (HS7601)

Enter your input

Payable emissions (tCO₂e/t)

Total CBAM Cost (€)

Notes:
There may be a difference when calculating the price with respect to import volume, carbon price, and benchmark emissions, as the embedded formula may result in minor variations due to decimal rounding. Therefore, the actual value may vary.

CBAM is applicable to trade volumes starting from 50 metric tonnes. For trade volumes below 50 metric tonnes, CBAM does not apply.

Usage Procedure – How to use the CBAM Calculator Sheet

Enter or update values only in the INPUT
PARAMETERS section (Highlighted in blue) , including
the carbon price, benchmark emissions, CBAM
chargeable percentage (as per the phase-in year),
and imported quantity.

The system will automatically calculate the payable
emissions and the total CBAM cost (€) based on the
inputs provided.

Notes:
• Change any input value to automatically update CBAM cost.
• Formula used: Carbon price × payable emissions × quantity.
• Model aligned with CBAM supplier-side illustrative methodology.

19 NOVEMBER 2025 PRESS RELEASE

Improvement of the effectiveness of making alumina by the Updated ILTD Process: alumina refineries in India as examples (Part 2)

5MINS READ

The updated ILTD (UILTD) process and the Sustainable Development Goals (SDGs). The 17 SDGs were adopted at the UN Sustainable Development Summit in New York in September 2015. “United Nations, 2015” Since that time numerous conferences, and publications were organised and prepared most of them connected with the 2030 Agenda for Sustainable Development. The UILTD Process comprises significant improvements in processing efficiencies and cost reductions, with the major focus on sustainability and alignment 6 SDGs. This paper presents significant potential, especially within materials science, industrial ecology and environmental engineering.

The updated ILTD (UILTD) process and the Sustainable Development Goals (SDGs)

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The amount and composition of the bauxite feedstocks, the bauxite residues, the same for the dicalcium-silicate (C₂S, belite) by-products were calculated and presented for Conventional Low Temperature Digestion (CLTD) and compared with the Updated ILTD Process. The calculation results are shown in Table 3 to 5 for the NALCO Damanjodi, Hindalco Utkal and Vedanta Lanjigarh alumina refineries, respectively.

table 3