I require the following data $($as provided in the table$)$ regarding carbon dioxide and hydrogen$-$derived products such as methanol, formic

acid, oxalic acid, formaldehyde, dimethyl ether, and urea $(NH3$ and $CO2$ based$).$ The information should encompass inputs, catalysts &

infrastructure, and outputs.

In the outputs section, please ensure to include details about emissions to air, water, and soil. The primary objective behind incorporating

this data is to ensure that the process is optimized for material and energy efficiency. The table below provides a framework for organizing

the necessary information. If you are aware of more efficient production pathways for the mentioned products, kindly include that

information along with appropriate references. CO$2\_$MeOH $(1$ ton$)$ Production CO$2\_$Formic acid $(1$ ton$)$ Production

Inputs Amount Units Inputs Amount Units

CO$21\mathrm{.}46$ t CO$20\mathrm{.}98$ t

H$2($via water electrolysis$)0\mathrm{.}2$ t H$2($via steam reformer$)0\mathrm{.}06$ t

Electricity $0\mathrm{.}25$ MWh Electricity $0\mathrm{.}31$ MWh

Heat $0\mathrm{.}4$ MWh Heat $2\mathrm{.}78$ MWh

Cooling Water $90$ m$^3$ Cooling Water $250$ m$^3$

Catalysts & Infrastructure Methanol $0\mathrm{.}15$ t

CuO $6\mathrm{.}33$E$-02$ kg Amine $0\mathrm{.}12$ t

ZnO $2\mathrm{.}38$E$-02$ kg Catalysts & Infrastructure

Al$2$O$31\mathrm{.}19$E$-02$ kg Ruthenium$-$based catalyst $2\mathrm{.}50$E$-03$ kg

Infrastructure $($P$)2\mathrm{.}35$E$-07-$ Phosphino$-$based catalyst $1\mathrm{.}25$E$-03$ kg

Outputs Amount Units Infrastructure $($P$)5\mathrm{.}00$E$-07-$

Methanol $1$ t

CO$20\mathrm{.}09$ t Outputs Amount Units

H$2$O $0\mathrm{.}58$ t Formic Acid $1$ t

Methanol $($air$)0\mathrm{.}01$ t CO$20\mathrm{.}03$ t

Emissions to water $?$ H$2$O $0\mathrm{.}06$ t

Emissions to soil $?$ Emissions to air $?$

Emissions to water $?$

Emissions to soil $?$