Gravity type heat pipe with extended heating surface
Technical Field
The invention belongs to the technical field of heat exchange, and relates to a gravity type heat pipe with an extended heating surface.
Background
In recent years, the national requirements on energy conservation and emission reduction of thermal power plants are increasingly strict, the ultra-low emission of the coal-fired power plants is required to be gradually realized in the action plan for energy conservation and emission reduction and upgrading of coal power (2014-2020) (issue and improvement of energy [2014] 2093), and the average power supply coal consumption after the modification of the existing thermal power generating units is lower than 310g/kWh in 2020, wherein the average power supply coal consumption after the modification of the existing thermal power generating units (except for air cooling units) of 60 ten thousand kilowatts or more is lower than 300 g/kWh. With the proposal of carbon neutralization strategy in 2030 year of carbon peak 2060, the energy-saving and emission-reducing tasks of thermal power plants are more difficult.
The flue gas waste heat loss is the largest loss of a power station boiler, a plurality of flue gas waste heat utilization technologies are developed at present, the flue gas temperature can be reduced to 100-90 ℃, the power generation coal consumption of a unit is saved by 1.5-3.0g/kWh, and the contribution is made to the energy conservation and emission reduction of a thermal power plant. The low-temperature economizer is a main technology for utilizing the waste heat of the flue gas at present and is widely applied in China. However, due to the reasons of high ash content and sulfur content of coal, unstable coal quality, low load, high ammonia escape in flue gas, uneven flow field of flue gas and the like in China, after the low-temperature and low-temperature economizer operates for more than five years, the problems of ash blockage, abrasion, leakage and the like begin to be obvious, the leakage is finally caused by the ash blockage and the abrasion, the ash blockage and the abrasion are aggravated by the leakage, and the vicious circle is caused. After the low-temperature economizer leaks, water vapor enters the dust remover to cause the dust removing device of the dust remover to be blocked; the dust blocking and hardening of the heating surface are caused after leakage, and the cleaning difficulty and the maintenance workload are greatly increased; meanwhile, the smoke temperature at the outlet of the low-temperature economizer is increased, the efficiency of the electrostatic dust collector is reduced, and the risk of standard exceeding of dust at the main discharge port is increased.
The heat pipe heat exchanger can solve the leakage problem, the liquid capacity in each heat pipe is very limited, and the heat pipes are mutually independent, so that the leakage accident can not occur even if the heat exchange pipes are damaged. However, at present, the gravity heat pipe can only be vertically arranged, is suitable for a light pipe, has insufficient heat exchange capacity, cannot meet the requirement of a low-temperature economizer of a large-scale unit, and does not find an expansion heating surface suitable for the gravity heat pipe.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a gravity type heat pipe with an extended heating surface, which can increase the heat exchange area and has excellent heat exchange capacity.
In order to achieve the purpose, the gravity type heat pipe with the expanded heating surface comprises a flue and a heat exchanger body, wherein the heat exchanger body comprises a water chamber and a plurality of heat pipe bodies, the heat pipe bodies are sequentially divided into a heat absorption section, a heat insulation section and a heat release section from bottom to top, the heat absorption section is located in the flue, the heat release section is located in the water chamber, the heat absorption section is connected with the heat release section through the heat insulation section, the heat insulation section is located between the flue and the water chamber, the outer surfaces of the heat absorption section and the heat release section are provided with a plurality of scales, and the outer surface of the heat insulation section is provided with a heat insulation material layer.
The heat pipe bodies are vertically arranged.
The distance between the lower end of the heat absorption section and the bottom of the flue is 200 mm.
The top of the flue is welded with the outer wall of the lower end of the heat insulation section, and the bottom of the water chamber is welded with the outer wall of the upper end of the heat insulation section.
The scales are arranged in sequence or staggered.
The thickness of the scale is 0.3-0.6mm, the included angle between the scale and the axis of the heat pipe body is 30-60 degrees, and all scales are distributed downwards in an inclined mode.
The width of the scale is 2-4mm, and the length is 4-8 mm.
The distance between adjacent scales is 2-6 mm.
The scales are rectangular, triangular or semicircular.
The thickness of the scale is gradually reduced from the root to the end of the scale.
The invention has the following beneficial effects:
when the gravity type heat pipe with the expanded heated surface is in specific operation, the heat absorption section is positioned in the flue, the heat release section is positioned in the water chamber, the heat absorption section is connected with the heat release section through the heat insulation section, the heat insulation section is positioned between the flue and the water chamber, when the gravity type heat pipe works, working media in the heat absorption section absorb heat of flue gas in the flue, then evaporate and move upwards, enter the heat release section to release heat and then condense, and fall into the heat absorption section, the outer surfaces of the heat absorption section and the heat release section are respectively provided with a plurality of scales to increase the heat exchange area and improve the heat exchange efficiency, the outer surface of the heat insulation section is provided with the heat insulation material layer to reduce heat loss and improve the heat exchange efficiency, and the gravity type heat pipe with the expanded heated surface can improve the heat exchange capacity of a heat pipe exchanger, reduce the volume of the heat pipe exchanger, and has higher safety and economical efficiency of equipment.
Drawings
FIG. 1 is a front view of a heat exchanger body according to the present invention;
FIG. 2 is a view A-A of the heat exchanger body of the present invention;
FIG. 3 is a schematic view of a heat exchange tube 3 according to the present invention;
wherein, 1 is a flue, 2 is a water chamber, 3 is a heat exchange tube, 3-1 is a heat absorption section, 3-2 is a heat insulation section, 3-3 is a heat release section, and 3-4 is a scale.
Detailed Description
In order to make the technical solutions of the present invention better understood, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, not all of the embodiments, and are not intended to limit the scope of the present disclosure. Moreover, in the following description, descriptions of well-known structures and techniques are omitted so as to not unnecessarily obscure the concepts of the present disclosure. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
There is shown in the drawings a schematic block diagram of a disclosed embodiment in accordance with the invention. The figures are not drawn to scale, wherein certain details are exaggerated and possibly omitted for clarity of presentation. The shapes of various regions, layers and their relative sizes and positional relationships shown in the drawings are merely exemplary, and deviations may occur in practice due to manufacturing tolerances or technical limitations, and a person skilled in the art may additionally design regions/layers having different shapes, sizes, relative positions, according to actual needs.
Referring to fig. 1, 2 and 3, the gravity type heat pipe with the extended heating surface of the invention comprises a flue 1 and a heat exchanger body, wherein the heat exchanger body comprises a water chamber 2 and a plurality of heat pipe bodies 3, the heat pipe bodies 3 are divided into a heat absorption section 3-1, a heat insulation section 3-2 and a heat release section 3-3, the heat absorption section 3-1 is located in the flue 1, the heat release section 3-3 is located in the water chamber 2, the heat absorption section 3-1 and the heat release section 3-3 are connected through the heat insulation section 3-2, the heat insulation section 3-2 is located between the flue 1 and the water chamber 2, the heat pipe bodies 3 are vertically arranged, the distance between the lower end of the heat absorption section 3-1 and the bottom of the flue 1 is 200mm, and the heat pipe bodies are used as an ash discharge channel for placing accumulated ash.
The top of the flue 1 is welded with the outer wall at the lower end of the heat insulation section 3-2, and the bottom of the water chamber 2 is welded with the outer wall at the upper end of the heat insulation section 3-2.
And a heat insulation material layer is arranged on the outer surface of the heat insulation section 3-2.
The outer surfaces of the heat absorption section 3-1 and the heat release section 3-3 are provided with a plurality of scales 3-4.
The gaps of the scales 3-4 on the heat absorption section 3-1 are the same as or different from the gaps of the scales 3-4 on the heat release section 3-3.
The scales 3-4 are arranged in a row or in a staggered way.
The thickness of the scales 3-4 is 0.3-0.6mm, the included angle between the scales 3-4 and the axis of the heat pipe body 3 is 30-60 degrees, and the scales 3-4 are distributed downwards in an inclined mode. The width of the scales 3-4 is 2-4mm, the length is 4-8mm, and the distance between the adjacent scales 3-4 is 2-6 mm.
The scales 3-4 are rectangular, triangular or semicircular, and the thickness of the scales 3-4 is gradually reduced from the root parts to the end parts of the scales 3-4.
The method for determining the number of the scales 3-4 comprises the following steps: and selecting the number of the scales 3-4 according to thermal calculation, calculating the carrying limit of the heat pipe body, and reducing the number of the scales 3-4 or shortening the length of the heat pipe body 3 and increasing the number of the heat pipe body 3 when the carrying limit of the heat pipe body 3 is exceeded.
The specific working process of the invention is as follows:
the flue gas circulates in the flue 1, the working medium in the heat pipe body 3 absorbs heat in the heat absorption section 3-1 to become gaseous state, the gaseous working medium is heated to the heat release section 3-3 through the heat insulation section 3-2 along the inner wall of the heat pipe body 3, after heat exchange with cold water in the heat release section 3-3, the gaseous working medium is condensed to become liquid state, and then the gaseous working medium flows downwards to the heat absorption section 3-1 along the inner wall of the heat pipe body 3 to form heat absorption and release circulation. The heat exchange area of the heat absorption section 3-1 is increased by 2-3 times through the scales 3-4, and the heat exchange capacity is improved by 2-4 times. The width, the interval and the length of the scales 3-4 are set to be structures which are not easy to accumulate dust, and the scales 3-4 can slightly shake in smoke gas, so that the smoke dust self-cleaning device has a dust self-cleaning function.
Finally, the invention can greatly improve the heat exchange efficiency of the heat pipe body 3, reduce the volume of the heat pipe heat exchanger and improve the safety and the economy of equipment.