The disclosure relates to a method for operating an internal combustion engine of a watercraft, in particular on inland waters, in which (i) in an electrolysis unit for the production of hydrogen, water is split into hydrogen and oxygen, (ii) a carbon dioxide sorption unit extracts carbon dioxide from the ambient air, (iii) the hydrogen and the carbon dioxide are fed to a methanol synthesis unit for the production of methanol, and are synthesized therein to methanol, (iv) a photovoltaic unit absorbs solar energy and converts it into electrical energy. The electrolysis unit, the carbon dioxide sorption unit and the methanol synthesis unit are powered by the electrical energy generated in the photovoltaic unit. The methanol produced is transported by means of a distributor system to at least one tank of the watercraft, and is fed from the tank as required to the internal combustion engine, and therein is combusted to generate mechanical energy.

A method for treating powdered activated carbon (PAC) and/or coal combustion residues (CCRs) by heating at least one of a spent PAC and/or a CCR to separate at least one heavy metal from the at least one of the spent PAC and/or the CCR to create a clean stream and a heavy metal stream, combining the heavy metal stream with a water soluble alkaline-earth metal sulfide to create a combined stream, and removing at least a portion of the at least one heavy metal from the combined stream. The heating may further include heating the at least one of the spent PAC and/or the CCR in an inert atmosphere. Further, the combining may include combining the heavy metal stream with the water soluble alkaline-earth metal sulfide and a catalyst and/or a surfactant or hyperdispersant.

A combustion apparatus of this invention comprises: a heat-resistant container having an opening in its upper part; and a pot with a fire-extinguishing lid, provided with a fire-extinguishing lid which can open and close the opening in the upper part of the heat-resistance container, closes the opening with the fire-extinguishing lid by hand, vibration, or impact, and receives a fuel dropped from the heat-resistant container.

Embodiments of the invention include a filtration system with a separation system including a primary process vessel with a main body enclosing an internal volume, and a removable end cap coupled to one of the ends of the main body. The primary process vessel includes fluid apertures enabling a fluid stream to enter or exit the inner volume. The separation system includes a filter support positioned in the inner volume, and a filter assembly coupled to the filter support. In some embodiments, the filtration system further includes a support frame, and the separation system is mounted on the support frame. In some embodiments, the separation system is fluidly coupled to another separation system. In some embodiments, the filter assembly includes a coalescing filter. In some further embodiments, the filter assembly includes a filter configured and arranged to filter hydrocarbons.

A membrane permeation system and process accommodates varying acid gas inlet concentrations over time while utilizing only the initially installed equipment and still maintaining the non-permeate gas specification. The system and process provide flexibility to operate efficiently over a wide range of inlet CO.sub.2 concentrations by adjustments to primary permeate, secondary permeate, and recycle gas operations. The glassy polymer membrane devices used in the system and process are selected so removal duty efficiency increases as acid gas concentration increase. Designing the system and process to handle about a 15% increase in acid gas concentrations over initial conditions effectively treats acid gas concentrations well above that 15% increase, thereby eliminating the need for additional equipment or for additional downstream amines and physical solvents.