The invention relates to a method for the hydroformnylation of triglycerides by homogeneous catalysis in the presence of at least one substituted cyclodextrin, said method comprising a step a) of combining, under agitation, at least one catalyst, waiter, at least one unsaturated triglyceride and said substituted cyclodextrin, in the presence of gaseous hydrogen and carbon monoxide, said step being carried out in reactive conditions allowing the formation of an emulsion during the agitation and a decanting of the products once the agitation has stopped.

An integrated energy system comprising a power plant including at least one nuclear reactor and an electrical power generation system, the at least one nuclear reactor being configured to generate steam, and a supercritical water oxidation system operably coupled to the power plant. The supercritical water oxidation system including a desalination plant configured to produce first water and brine, a chlor-alkali membrane process configured to receive the brine and produce at least a Sodium Hydroxide solution, a reactor configured to receive the first water, the steam, and the Sodium Hydroxide solution to produce a waste solution and a solid waste, and a separator configured to receive the waste solution and produce Carbon Dioxide and second water.

An integrated energy system comprising a power plant including at least one nuclear reactor and an electrical power generation system, the at least one nuclear reactor being configured to generate steam, and a supercritical water oxidation system operably coupled to the power plant. The supercritical water oxidation system including a desalination plant configured to produce first water and brine, a chlor-alkali membrane process configured to receive the brine and produce at least a Sodium Hydroxide solution, a reactor configured to receive the first water, the steam, and the Sodium Hydroxide solution to produce a waste solution and a solid waste, and a separator configured to receive the waste solution and produce Carbon Dioxide and second water.

An acetic acid plant and associated process is provided, in which a biogas stream is fed to a reformer section, in which a first synthesis gas stream is provided. An acetic acid synthesis section is arranged to receive a synthesis gas stream from the reformer section and provide a raw acetic acid product stream.

An acetic acid plant and associated process is provided, in which a biogas stream is fed to a reformer section, in which a first synthesis gas stream is provided. An acetic acid synthesis section is arranged to receive a synthesis gas stream from the reformer section and provide a raw acetic acid product stream.