Background technology
The curing of metal current paint industry or the heat supply of industrial heat exchange type all adopt combustion gas or fuel oil that heater is heated, and the gas that obtains heating is realized heat supply, and its heat production cost height and heat exchanger effectiveness are relatively poor.The heat exchanger that adds commonly used generally heats by the outer Heat Room gas of heat exchanger tube exchange heat pipe that is positioned at Heat Room, realize heat exchange, there are a lot of defectives in this kind heater: at first the length of heat exchanger tube can not be oversize, bend can not be too many, otherwise will influence the velocity of liquid assets of high-temperature gas in it, thereby heat exchange efficiency is reduced; Secondly, the gas contact area in this heat exchanger tube and the Heat Room is less, can't realize high efficient heat exchanging; Moreover when adopting fire coal or coke as heating furnace fuel, a large amount of dusts that high-temperature gas carries can be deposited in the pipeline, influence the channel cross-sectional area in the heat exchanger tube, thereby reduce the circulation of heat exchange efficiency and high-temperature gas.
On April 4th, 2007, the Chinese patent ZL 200620094900.8 of bulletin provided a kind of heating heat exchanger of coalingging that is coated with, and it is made up of housing, coal furnace, heat exchanger tube, guide duct, air exhauster, curing oven, backwind tube and air-introduced machine; Offer the coal stove air inlet on the housing, hot-blast outlet, return air outlet and air-vent, be provided with heat exchanging chamber in the housing, the hot-blast outlet of housing, return air inlet and air-vent communicate with heat exchanging chamber respectively, solidify the road and be provided with door, hot blast import and air inducing outlet, coal furnace and heat exchanger tube are installed in the heat exchanging chamber, the air inlet of coal furnace is communicated with the coal stove air inlet of housing, coal furnace is provided with hot-blast outlet, the air inlet of heat exchanger tube communicates with the hot-blast outlet of coal furnace, the air outlet of heat exchanger tube communicates with the air-vent of housing, air-introduced machine is installed on the air-vent of housing, heat exchanging chamber communicates with the hot-blast outlet of housing, one end of guide duct communicates with the hot-blast outlet of housing, and the other end communicates with the hot blast import of curing oven, and an end of backwind tube communicates with the outlet of the air inducing of curing oven, the other end communicates with the return air inlet of housing, and air exhauster is installed in the hot-blast outlet place of heat exchanging chamber.Though being coated with the heating heat exchanger of coalingging, this can realize with the fire coal being fuel, realize the reduction of heating heat exchange cost to a certain extent, but it exists equally dust to stop up heat exchanging pipe easily, heat exchange efficiency is poor, baroque defective can't realize industrialization promotion and application.Simultaneously exhaust emissions with dust pollution question be well solved.
Summary of the invention
The purpose of this invention is to provide a kind of fire coal or coke of can adopting is fuel, effectively reduce heating heat exchange cost, improve the energy-saving heat exchange compressor of heat exchange efficiency, it is simple in structure, applied widely, can realize long apart from heat exchange, heat exchange efficiency is improved greatly, and can solve the existing heat exchanger that adds and dust takes place easily stop up the defective of pollution emission environment.
For achieving the above object, the technical solution used in the present invention is as follows:
A kind of energy-saving heat exchange compressor, comprise heating cooking stove and the heat exchange compressor that is attached thereto, it is characterized in that being provided with in the described heat exchange compressor air inlet pipe and offgas duct, air inlet pipe one end is connected with heating cooking stove, and the air inlet pipe other end is linked to each other with at least three layers of S shape radiating tube by at least three row S shapes with offgas duct.
Concretely, a side lower part and the opposite side top of described heat exchange compressor are provided with the heated air entry and exit respectively, and the bottom of heat exchange compressor wears air inlet pipe for one jiao, and another angle, the bottom of heat exchange compressor is provided with offgas duct.
Described air inlet pipe enters a section of heat exchange compressor and is inverted U is bent downwardly its end of back ash removing opening is set in heat exchange compressor, is communicated with on the air inlet pipe of ash removing opening upper end S shape radiating tube is set.
Described ash removing opening is the end port of air inlet pipe, and described end port place is provided with the air inlet pipe obturator with the air inlet pipe endcapped.
Described air inlet pipe is located in the Yi Jiaochu of heat exchange compressor bottom, and offgas duct and described air inlet pipe be arranged in parallel, and S shape heat exchanger tube is horizontally fixed between offgas duct and the air inlet pipe.
3-15 that described S shape heat exchanger tube is secured in parallel row, secured in parallel is between offgas duct and air inlet pipe up and down for S shape heat exchanger tube, and the internal diameter of every S shape heat exchanger tube is all less than the internal diameter of described air inlet pipe and offgas duct.
The two ends of described S shape heat exchanger tube are connected with offgas duct and air inlet pipe are vertical.
Described heating cooking stove is positioned at the lower end of heat exchange compressor, and the top of heating cooking stove connects air inlet pipe, and the inner room of described heat exchange compressor is square or cylindrical.
Connect exhaust gas cleaner after one end of described offgas duct passes the heat exchange compressor wall, described exhaust gas cleaner comprises the tail gas clean-up chamber, and offgas duct is positioned on a section of this tail gas clean-up chamber and is distributed with through hole, offers steam vent on the tail gas clean-up locular wall.
One end of described offgas duct connects the discharge that gas in the high pressure smoke suction machine acceleration offgas duct is set after stretching out heat exchange compressor, described tail gas clean-up chamber is two groups, offgas duct enters the back and is passed by the top of tail gas clean-up chamber from the top of a tail gas clean-up chamber, offgas duct penetrates from the top of another tail gas clean-up chamber then, and it is indoor that its end is positioned at this tail gas clean-up.
The mode of this energy-saving heat exchange compressor many S shape heat exchanger tubes in parallel between offgas duct and air inlet pipe, can improve heat exchanger effectiveness significantly, because many S shape pipes are distributed in the heat exchange compressor, occupied heat exchange compressor than large space, gas between each S shape heat exchanger tube is discharged by radiation and conduction pattern heating rapidly, realize high efficient heat exchanging.The number of S shape heat exchanger tube and arrangement mode can be provided with according to the shape and the volume of heat exchange compressor, are advisable with the S shape heat exchanger tube proper space that can distribute.The air inlet pipe that is positioned at heat exchange compressor partly is bend pipe, be preferably inverted-loop tube, air inlet pipe is bent downwardly after can being entered by the bottom vertical of heat exchange compressor, and the air inlet pipe end after its bending is as the connecting portion of S shape heat exchanger tube, and this air inlet pipe end port after the bending simultaneously is as ash removing opening.High-temperature gas upwards enters air inlet pipeline section in the heat exchange compressor by the air inlet pipe at heating top, road, turn to after the bending section of high-temperature gas passes heating tube is descending, level enters S shape heat exchanger tube, the a large amount of dusts that carry in the high-temperature gas can be settled down to the ash removing opening place of this section air inlet pipe bottom owing to the effect of gravity, thus convenient the removing.The internal diameter of S shape heat exchanger tube is less than the internal diameter of air inlet pipe, and high-temperature gas is delivered to offgas duct behind many S shape heat exchange intraductal heat exchanges, is collected by offgas duct and discharges.Adopt the S shape heat exchanger tube of this kind mode can realize longer heat exchange distance, former 3-5 rice can be carried out the thermal energy exchange of 15-25 rice length, the better utilization waste heat.
Offer the heated air entry and exit on the heat exchange compressor wall, heated air enters from the heated air of the bottom of heat exchange compressor one sidewall inlet, is discharged by the heated air outlet on the top of another sidewall.Offgas duct will reclaim through the gas after the heat exchange in each root S shape heat exchanger tube, and dispatch is to exhaust gas cleaner then.Because this moment through the dust in the gas after the heat exchange seldom, therefore can adopt the mode of natural subsidence that tail gas is carried out the subsiding and purifying discharge.Offer through hole with entering on one section indoor offgas duct of tail gas clean-up, make gas diffuse to the tail gas clean-up chamber by through hole, discharged by the exhaust outlet of tail gas clean-up chamber, it is indoor that the dust of the overwhelming majority can be deposited in tail gas clean-up, realizes containing the qualified discharge of flue dust gas.
Because the internal diameter of S shape heat exchanger tube is less than the internal diameter of air inlet pipe, therefore can the high pressure smoke extractor be set on the offgas duct of heat exchange compressor stretching out, make the tail gas pipeline section at this place form negative pressure, quicken gas flow, improve the heat transfer rate.
Beneficial effect of the present invention is, the hot gas source of this energy-saving heat exchange compressor, can be that fuel and various material that can heating are as various timber with fire coal or coke, anthracite, coking coal, can save energy 56%, oil, gas can save energy 38%, as using: culled wood, anthracite is than oil, gas, economy that can 91% is poor, significantly reduce fuel cost, many S shape heat exchanger tubes that are arranged in parallel simultaneously can improve heat exchange efficiency to greatest extent, crooked air inlet pipe that is provided with and ash removing opening can realize entering the ash fall of the high-temperature gas of S shape heat exchanger tube, eliminate the defective because of the heat exchanger tube heat exchange efficiency difference that ash fall caused.This energy-saving heat exchange compressor can be applicable to the heater in fields such as various industrial heat exchange heating plants and application widely.Convertible in hot blast or steam conversion in the described heat exchange compressor, its energy-saving effect all is same.
The specific embodiment
Shown in Fig. 1-4, this energy-saving heat exchange compressor mainly contains heat exchange compressor 2, air inlet pipe 12, offgas duct 5, S shape heat exchanger tube 11 and exhaust gas cleaner and forms, be provided with air inlet pipe 12 and offgas duct 5 in the heat exchange compressor 2, air inlet pipe 12 is connected with heating cooking stove 1, import high-temperature gas, air inlet pipe 12 is communicated with 5 of offgas duct and is provided with plural number row S shape heat exchanger tube 11, and offgas duct derives heat exchange compressor with the gas in the S shape heat exchanger tube.
Heating cooking stove 1 is positioned at the lower end of heat exchange compressor 2, and the top of heating cooking stove connects air inlet pipe 12, and the inner room of heat exchange compressor is square.Air inlet pipe vertically is located in the Yi Jiaochu of heat exchange compressor bottom, offgas duct 5 in the heat exchange compressor be arranged in parallel with described air inlet pipe 12, S shape heat exchanger tube 11 is horizontally fixed between offgas duct and the air inlet pipe, S shape heat exchanger tube is 12 rows of secured in parallel, secured in parallel is between offgas duct and air inlet pipe about the S shape heat exchanger tube, the two ends of S shape heat exchanger tube are connected with offgas duct and air inlet pipe are vertical, and the internal diameter of every S shape heat exchanger tube is all less than the internal diameter of air inlet pipe and offgas duct.Air inlet pipe enters a section of heat exchange compressor and is inverted U is bent downwardly its end of back ash removing opening 13 is set in heat exchange compressor, is communicated with on the air inlet pipe of ash removing opening upper end S shape heat exchanger tube is set.Ash removing opening is the end port of air inlet pipe, and the end port place is provided with the air inlet pipe obturator with the air inlet pipe endcapped.
One end of offgas duct 5 connects the discharge that gas in a high-pressure suction fan 6 acceleration offgas duct is set after stretching out heat exchange compressor, one end of offgas duct connects two exhaust gas cleaners 7 and 8 after passing the heat exchange compressor wall, the exhaust gas cleaner main body is the tail gas clean-up chamber, offgas duct enters the back from the lower sidewall of tail gas clean-up chamber 7 and is passed by the top of tail gas clean-up chamber 8, offgas duct penetrates from the top of another tail gas clean-up chamber then, and it is indoor that its end is positioned at this tail gas clean-up.Offgas duct is positioned on a section of tail gas clean-up chamber and is distributed with through hole 9, offers steam vent 10 on the tail gas clean-up locular wall.
The results showed, this energy-saving heat exchange compressor improves more than 3 times than the heat exchange efficiency of the heating heat exchanger of existing monodromy heat pipe, produce simultaneously under the situation of identical heat, the cost that consumes coal-fired and electric energy is 1/5th of the fuel consumption and the cost of electric energy, though the S shape heat exchanger tube internal diameter of this energy-saving heat exchange compressor is less, but dust deposit is less in it, the ash removing opening periodic cleaning, most dust can be carried out sedimentation in advance, carry amount of dust in the gas of discharging and can meet discharging standards, have good economic and social benefit.