A vaporization pipe for a kerosene lamp has an oil tube, a thermally conductive tube, and a first passage. The oil tube is made of steel and has a vaporization jet on a top of the oil tube. The thermally conductive tube is mounted in the oil tube and forms a first channel. The first passage is disposed between the oil tube and the thermally conductive tube. The steel oil tube can prevent the vaporization pipe from being softened and bent during the preheating of vaporization pipe or burning of the kerosene, and thus a useful lifetime of the vaporization pipe is prolonged. The thermally conductive tube is made of high-thermal-conductivity material for keeping the vaporization pipe with adequate thermal conductivity and improving a burning rate of kerosene. The first passage allows the kerosene to flow upward, preventing the kerosene from being vaporized incompletely because the kerosene is over pressurized.

A vaporization pipe for a kerosene lamp has an oil tube, a thermally conductive tube, and a first passage. The oil tube is made of steel and has a vaporization jet on a top of the oil tube. The thermally conductive tube is mounted in the oil tube and forms a first channel. The first passage is disposed between the oil tube and the thermally conductive tube. The steel oil tube can prevent the vaporization pipe from being softened and bent during the preheating of vaporization pipe or burning of the kerosene, and thus a useful lifetime of the vaporization pipe is prolonged. The thermally conductive tube is made of high-thermal-conductivity material for keeping the vaporization pipe with adequate thermal conductivity and improving a burning rate of kerosene. The first passage allows the kerosene to flow upward, preventing the kerosene from being vaporized incompletely because the kerosene is over pressurized.

A chemical plant may include one or more fired heaters for heating of process streams. A fired heater may include a direct-fired heat exchanger that uses the hot gases of combustion to raise the temperature of a process fluid feed flowing through tubes positioned within the heater. Fired heaters may deliver feed at a predetermined temperature to the next stage of the reaction process or perform reactions such as thermal cracking. Systems and methods are disclosed to optimize the performance of fired heaters or reduce energy consumption of fired heaters.

The present invention provides a deep fat fryer providing an oil vat for holding hot oil. The hot oil of the vat is heated by a heat exchanger system that includes a pair of heat tubes. Heat transfer along a length of the heat tubes is facilitated by a heat conductive baffle substantially filling the interior of the heat tubes in volume and length. Heated air and gas are forced through the dense and elongated baffle to facilitate heat transfer to the walls of the heat tubes.

A burner system includes a plurality of burners, each having a nozzle positioned to emit a stream of fuel into a combustion volume, and a perforated flame holder, including a plurality of apertures extending between first and second faces thereof, and positioned to receive a stream of fuel from the respective nozzle. In operation, the flame holders are configured to hold a flame substantially within the plurality of apertures.

The invention relates to a heat exchanger (1) comprising a shell (2) containing a heat exchange device (3) and delimiting a combustion chamber (30), said shell (2) being provided with an access opening and with a door (5) provided on its inner face with a burner (4).

It is remarkable in that said door (5) is mounted pivotally around a pivot (6) attached to the end of a slide (7), in that said shell (2) is provided on its exterior surface with axial guide means (8) of said slide (7) along a displacement axis X2-X2 which extends parallel to the longitudinal axis X-X of said shell (2), in that the pivot (6) extends along an axis Z-Z perpendicular to said displacement axis X2-X2, the travel of said slide (7) being greater than the length of the burner (4).

Provided is an oil diffusion pump equipped with an oil vapor generator capable of eliminating the problems occurring when a heater wire is used as a heating source for an operating oil. The present invention is a vacuum pump for which an oil vapor generator (70) is arranged within a casing (51) and this oil vapor generator is operated to vaporize an operating oil (8), thereby producing oil vapor and this oil vapor is sprayed from a jet (53, 53a) to exhaust intake air. The oil vapor generator (70) is equipped with: a container (71, 72) in the interior of which oil is stored, with the lower end of the tubular member (71), which comprises a material to be heated, being closed; and induction coil (75) wrapped around the atmosphere-side perimeter of the tubular member (71) (in particular, the case inner wall (71b)) with an insulating material (73) therebetween; and a power supply means that applies a low-frequency alternating current of several tens of Hz to several hundreds of Hz to the induction coil (75). The configuration is such that the tubular member (71) itself is heated when the power supply means is operated and the low-frequency alternating current is applied to the induction coil (75), thereby vaporizing the oil within the container.

A reactor system includes a pressure vessel having a vessel wall, a feed port at a superior end of the pressure vessel, a permeable liner disposed within the pressure vessel and at least one hydrothermal jet mounted to the pressure vessel. The feed port is configured for feeding a liquid target reactant stream into the pressure vessel. The permeable liner separates the pressure vessel into an internal reaction zone and an outer annular chamber. The hydrothermal jet is mounted external to the reaction zone and is configured to add heated mixture of carrier and oxidizer to the internal reaction zone. A dividing wall portions the outer annular chamber into a cooling zone and an exhaust zone through which by-products of the reaction exit from the reaction zone.