Patent classifications
F22B15/00
RADIANT TO CONVECTION TRANSITION FOR FIRED EQUIPMENT
Modern steam generators typically include a radiant section and a convection section. Due to differing performance requirements of the radiant and convection sections, the radiant section often has a round cross-section, while the convection section often has a rectangular cross-section. Previous designs utilized a target wall to affect the transition. An angled transition section is disclosed herein that substantially eliminates the target wall and/or the reverse target and provides a corresponding improvement in steam generator efficiency.
Condensing heat exchanger system
An integrated reaction condensing heat exchanger system (IRCHX) may be installed in a fossil power plant flue gas treatment system. More particularly, the IRCHX system may be used for recovering water from combustion flue gas by phase change to reduce fresh water consumption in fossil power plants including coal-, oil- and gas-fired plants. To recover water from flue gas, the IRCHX system may be installed in a current flue gas treatment system in a new or existing power plant, which allows power plants to save fresh water consumption up to 20%. Additionally, it benefits: 1) low temperature heat recovery after economizer, 2) lower exhaust temperature of flue gas at stack, 3) lower moisture contents in exhaust flue gas at stack, and 4) reduced acid emission in flue gas at stack.
Combination heat exchanger and burner
It is common in heating systems, such as in a hot water heater for there to be a combustor with the exhaust gases from the combustor provided to a heat exchanger to heat up the water. Disclosed herein is an integrated heat exchanger and burner assembly in which the combustion occurs proximate the surface of the heat exchanger. Such a system may include at least one tube that is coiled into a number of turns, that is a tube coil with the at least one tube having an inlet and an outlet and the distance between adjacent turns is less than a predetermined distance, i.e. a the quench distance.
Water heater
A water heater includes a burner of a premixed type, a heat exchanger, and a fan suctioning combustion gas and exhausting combustion gas to the outside. The burner includes a burner case partitioned into a combustion chamber and a gas introduction chamber by a partition plate and a plurality of combustion tubes arranged in the combustion chamber. An air supply opening for supplying air into the gas introduction chamber is provided in the burner case. The partition plate has a plurality of opening portions communicating with the inside of the combustion tubes and a plurality of through holes communicating with the outside of the combustion tubes within the combustion chamber. The air supply opening is constructed to have an opening area smaller than the total sum of the total of opening areas of the plurality of opening portions and the total of opening areas of the plurality of through holes.
Water heater
A water heater includes a burner of a premixed type, a heat exchanger, and a fan suctioning combustion gas and exhausting combustion gas to the outside. The burner includes a burner case partitioned into a combustion chamber and a gas introduction chamber by a partition plate and a plurality of combustion tubes arranged in the combustion chamber. An air supply opening for supplying air into the gas introduction chamber is provided in the burner case. The partition plate has a plurality of opening portions communicating with the inside of the combustion tubes and a plurality of through holes communicating with the outside of the combustion tubes within the combustion chamber. The air supply opening is constructed to have an opening area smaller than the total sum of the total of opening areas of the plurality of opening portions and the total of opening areas of the plurality of through holes.
Radiant to convection transition for fired equipment
Modern steam generators typically include a radiant section and a convection section. Due to differing performance requirements of the radiant and convection sections, the radiant section often has a round cross-section, while the convection section often has a rectangular cross-section. Previous designs utilized a target wall to effect the transition. An angled transition section is disclosed herein that substantially eliminates the target wall and/or the reverse target and provides a corresponding improvement in steam generator efficiency.
Radiant to convection transition for fired equipment
Modern steam generators typically include a radiant section and a convection section. Due to differing performance requirements of the radiant and convection sections, the radiant section often has a round cross-section, while the convection section often has a rectangular cross-section. Previous designs utilized a target wall to effect the transition. An angled transition section is disclosed herein that substantially eliminates the target wall and/or the reverse target and provides a corresponding improvement in steam generator efficiency.
Heat exchanger with pipe bundle
A heat exchanger including a pipe bundle to guide a fluid between first and second pipe connectors, the pipes being distributed in layers of pipes, wherein pipes of each of the layers of pipes each includes. A length of a flow path section is at least 1.7 times greater than lengths of two other flow path sections, wherein a first bend of the two bends is provided between the longer flow path section and a first of the shorter flow path section, and wherein a second of the two said bends is provided between the first, shorter flow path section and the other shorter flow path section, and wherein each of the layers of pipes includes two pipe subgroups. The bend between the two shorter flow path sections of the respective pipes in one of the pipe subgroups in the pipe layer is arranged substantially opposite to bends extending between the two shorter flow path sections of pipes in the other pipe subgroup of the same pipe layer.
Heat exchanger with pipe bundle
A heat exchanger including a pipe bundle to guide a fluid between first and second pipe connectors, the pipes being distributed in layers of pipes, wherein pipes of each of the layers of pipes each includes. A length of a flow path section is at least 1.7 times greater than lengths of two other flow path sections, wherein a first bend of the two bends is provided between the longer flow path section and a first of the shorter flow path section, and wherein a second of the two said bends is provided between the first, shorter flow path section and the other shorter flow path section, and wherein each of the layers of pipes includes two pipe subgroups. The bend between the two shorter flow path sections of the respective pipes in one of the pipe subgroups in the pipe layer is arranged substantially opposite to bends extending between the two shorter flow path sections of pipes in the other pipe subgroup of the same pipe layer.
Forced circulation steam generator
An oil recovery process entails recovering an oil-water mixture from an oil bearing formation and separating the oil-water mixture to produce an oil product and produced water. The produced water includes suspended and dissolved solids and is subjected to treatment which removes suspended and dissolved solids therefrom. The treated water is then directed to a forced circulation steam generator that includes a furnace having a burner, water cooled walls and an evaporator unit. The treated water is pumped through the water cooled walls and the evaporator unit. The water passing through the water cooled walls and evaporator unit are heated to produce approximately 10% to approximately 30% quality steam in both the water cooled walls and the evaporator unit. The steam is collected and separated from a water-steam mixture to produce high quality steam, on the order of 95% or greater quality steam. This steam constitutes injection steam which is injected into an injection well to facilitate the recovery of the oil-water mixture.