The disclosure concerns a process for producing formic acid, having (a) a carbon capture step in which a source of carbon dioxide is contacted with an amine solution in a closed-top scrubber, to obtain an ammonium bicarbonate solution; (b) inducing crystallization in the ammonium bicarbonate solution to obtain a concentrated ammonium bicarbonate solution; (c) subjecting the concentrated ammonium bicarbonate solution to a hydrogenation step to obtain an ammonium formate; and (d) heating the ammonium formate to a temperature in the range of 50-150° C., to obtain a gaseous product containing the amine and a liquid product stream containing formic acid. The source of carbon dioxide has a carbon dioxide content of at least 95 vol % and the amine used in step (a) and reformed in step (d) has a partial vapour pressure above a 40 wt % solution of the amine in water at 20° C. of at least 40 kPa. The disclosure further concerns a system for performing the process.

The presented invention relates to crystalline Forms (I) or (II) or (III) or (IV) of sodium salt of Bempedoic acid, processes for preparation thereof and a composition comprising it.

The presented invention relates to crystalline Forms (I) or (II) or (III) or (IV) of sodium salt of Bempedoic acid, processes for preparation thereof and a composition comprising it.

Disclosed are a method for preparing lithium iron manganese phosphate precursor and a method for preparing lithium iron manganese phosphate. The method for preparing lithium iron manganese phosphate precursor comprises the following steps: (1) preparing liquid material A and liquid material B, wherein the liquid material A is a mixed solution of manganese salt and iron salt, and the liquid material B is oxalic acid or phosphoric acid solution; (2) subjecting liquid material A and liquid material B to a co-precipitation reaction in a rotary packed bed (100) to obtain a first slurry; (3) washing and filtering the first slurry to obtain a filter cake; (4) mixing the filter cake with water, adding a carbon source, and stirring until uniform to obtain a second slurry; (5) homogenizing the second slurry; (6) drying the homogenized second slurry, to obtain the lithium iron manganese phosphate precursor. The particle size of the lithium iron manganese phosphate precursor prepared by the method is finer and more uniform than that of a precursor prepared by a traditional method using a reaction kettle, the preparation speed is increased, and the carbon coating is more uniform. FIG. 1: : lithium iron manganese phosphate precursor FIG. 2: : lithium iron manganese phosphate FIG. 3: (V): Voltage (V) (mAh/g): Specific capacity (mAh/g) : charge curve : discharge curve FIG. 4: (mAh/g): Discharge specific capacity (mAh/g) METHOD FOR PREPARING LITHIUM IRON MANGANESE PHOSPHATE PRECURSOR AND METHOD FOR PREPARING LITHIUM IRON MANGANESE PHOSPHATE