A water processing system (10) comprises a reactor (12) configured to receive a feed water input (FW). The reactor (12) is configured to convert the feed water input (FW) into a steam output (S) for use in a downstream operation. The processing system (10) is configured to utilise the thermal and/or mechanical energy of the feed water input (FW) to partially power the conversion of the feed water input (FW) to the steam output (S). The system (10) further comprises a heat generator arrangement operatively associated with the reactor (12), the heat generator arrangement supplying the remaining thermal energy required to convert the feed water input (FW) into the steam output (S).

A water processing system (10) comprises a reactor (12) configured to receive a feed water input (FW). The reactor (12) is configured to convert the feed water input (FW) into a steam output (S) for use in a downstream operation. The processing system (10) is configured to utilise the thermal and/or mechanical energy of the feed water input (FW) to partially power the conversion of the feed water input (FW) to the steam output (S). The system (10) further comprises a heat generator arrangement operatively associated with the reactor (12), the heat generator arrangement supplying the remaining thermal energy required to convert the feed water input (FW) into the steam output (S).

The present invention relates to an independent power generating method using water pressure and vapor, and a generating device thereof, which: sequentially circulate water by using a head drop of water and high-pressure vapor so as to continuously generate power, and generate power with a natural head drop caused by the gravity of water and, simultaneously, produce power with vapor; and naturally increase, condense, and reuse the vapor so as to hardly waste water resources such that power can be efficiently generated by efficiently rotating water wheels connected to an electric generator.

The present invention relates to an independent power generating method using water pressure and vapor, and a generating device thereof, which: sequentially circulate water by using a head drop of water and high-pressure vapor so as to continuously generate power, and generate power with a natural head drop caused by the gravity of water and, simultaneously, produce power with vapor; and naturally increase, condense, and reuse the vapor so as to hardly waste water resources such that power can be efficiently generated by efficiently rotating water wheels connected to an electric generator.

A steam vaporizer assembly includes an internal steam generator having a vessel configured to hold water, a vaporizer unit having a heating element configured to heat the water to generate saturated steam; and a controller configured to: cause the heating element to heat the water to a stand-by temperature; and while maintaining a water level of the water in the vessel between two control points: maintain the water in the vessel at the stand-by temperature until steam generation is required, and when steam generation is required, heating the water in the vessel from the stand-by temperature to a temperature at or above a vaporization temperature of the water using a heating element, to generate the steam.

A steam vaporizer assembly includes an internal steam generator having a vessel configured to hold water, a vaporizer unit having a heating element configured to heat the water to generate saturated steam; and a controller configured to: cause the heating element to heat the water to a stand-by temperature; and while maintaining a water level of the water in the vessel between two control points: maintain the water in the vessel at the stand-by temperature until steam generation is required, and when steam generation is required, heating the water in the vessel from the stand-by temperature to a temperature at or above a vaporization temperature of the water using a heating element, to generate the steam.

A low-carbon energy utilization system for steam and power cogeneration of oil field is provided, which includes a first water pump device, a second water pump device, electric heating devices, a liquid mixer, a fossil-fuel steam injection boiler, a steam mixer, a super-heater, and a new energy generation station. The electric heating devices are connected to the first water pump device. The liquid mixer is connected to the second water pump device and the electric heating devices. The fossil-fuel steam injection boiler is connected to the liquid mixer. The steam mixer is connected to the electric heating devices and the fossil-fuel steam injection boiler. The super-heater is connected to the steam mixer. The new energy generation station is used for supplying power to the electric heating devices.

A low-carbon energy utilization system for steam and power cogeneration of oil field is provided, which includes a first water pump device, a second water pump device, electric heating devices, a liquid mixer, a fossil-fuel steam injection boiler, a steam mixer, a super-heater, and a new energy generation station. The electric heating devices are connected to the first water pump device. The liquid mixer is connected to the second water pump device and the electric heating devices. The fossil-fuel steam injection boiler is connected to the liquid mixer. The steam mixer is connected to the electric heating devices and the fossil-fuel steam injection boiler. The super-heater is connected to the steam mixer. The new energy generation station is used for supplying power to the electric heating devices.

A steam supply system includes a steam generator disposed to produce wet steam for introduction into a steam separator. The steam separator includes a saturated condensate outlet. A superheater receives dry saturated steam from the steam separator and produces superheated steam. An evaporator with an evaporator vessel having a saturated condensate inlet, a soluble solids slurry outlet and a dry steam outlet is in fluid communication with the saturated condensate outlet of the steam separator. Disposed within the evaporator vessel is a superheated steam heat exchanger having a superheated steam outlet and a superheated steam inlet which superheated steam inlet is in fluid communication with the superheater to receive superheated steam. The dry steam outlet of the evaporator is in fluid communication with a steam mixing vessel where the dry steam is mixed with superheated steam from the superheated steam outlet of the heat exchanger.

A steam supply system includes a steam generator disposed to produce wet steam for introduction into a steam separator. The steam separator includes a saturated condensate outlet. A superheater receives dry saturated steam from the steam separator and produces superheated steam. An evaporator with an evaporator vessel having a saturated condensate inlet, a soluble solids slurry outlet and a dry steam outlet is in fluid communication with the saturated condensate outlet of the steam separator. Disposed within the evaporator vessel is a superheated steam heat exchanger having a superheated steam outlet and a superheated steam inlet which superheated steam inlet is in fluid communication with the superheater to receive superheated steam. The dry steam outlet of the evaporator is in fluid communication with a steam mixing vessel where the dry steam is mixed with superheated steam from the superheated steam outlet of the heat exchanger.