CN103759239A - Detachable steam generator - Google Patents
Detachable steam generator Download PDFInfo
- Publication number
- CN103759239A CN103759239A CN201410041064.6A CN201410041064A CN103759239A CN 103759239 A CN103759239 A CN 103759239A CN 201410041064 A CN201410041064 A CN 201410041064A CN 103759239 A CN103759239 A CN 103759239A
- Authority
- CN
- China
- Prior art keywords
- flue gas
- communicated
- pipe
- directly
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 131
- 239000003546 flue gas Substances 0.000 claims description 131
- 238000013021 overheating Methods 0.000 claims description 11
- 239000000779 smoke Substances 0.000 abstract description 12
- 238000012423 maintenance Methods 0.000 abstract description 11
- 238000004140 cleaning Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 description 14
- 238000010438 heat treatment Methods 0.000 description 11
- 238000001816 cooling Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 8
- 239000002918 waste heat Substances 0.000 description 8
- 239000003517 fume Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 229920006395 saturated elastomer Polymers 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- 239000011229 interlayer Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 239000003129 oil well Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 239000002817 coal dust Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000010079 rubber tapping Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a detachable steam generator. The detachable steam generator comprises a tank body, directly-heated type heat exchangers, a smoke diverter, a smoke collector, a water inlet preheating device, a smoke exhaust pipe and superheated steam exhaust ports, wherein the superheated steam exhaust ports are arranged on the sides, located at the smoke diverter, of the directly-heated type heat exchangers respectively. The smoke diverter is formed by a first empty tank body, first air inlet connectors and second air inlet connectors. The smoke collector is formed by a second empty tank body, first air exhaust connectors and second air exhaust connectors communicated with second smoke exhaust ports. The first air exhaust connectors are detachably connected with first smoke exhaust ports. The second air exhaust connectors are detachably connected with the second smoke exhaust ports. The detachable steam generator has the advantages that internal devices can be replaced, daily maintenance and cleaning are facilitated, the heat exchange efficiency is high, and the detachable steam generator is durable in structure and safe in use and saves cost.
Description
Technical field
The invention belongs to boiler plant field, particularly a kind of detachable steam generator.
Background technology
At present, using waste heat from tail gas discharge recycling present situation, the equipment such as the burning of industrial and mining enterprises and oven dry produce a large amount of using waste heat from tail gas and are wasted.Flue gas waste heat recovery approach adopts two kinds of methods conventionally: a kind of is pre-heated work pieces; Two kinds to be that preheated air carries out combustion-supporting.Smoke pre-heating workpiece need utilize the heat transmission equipment of larger volume to carry out heat exchange, is often subject to the restriction of Active workings.Adopting the equipment of said method is mainly that boiler carries out waste heat recovery.What is boiler? other heat energy is transformed into other working medium heat energy, and the equipment of the working medium of production regulation parameter and quality is called boiler.Boiler structure and operation principle pot: refer to the water-steam system of boiler, by equipment such as drum, down-comer, header, water-cooling wall, superheater and economizers, formed.(1) task of boiler is to make water heat absorption, is finally varied to the steam of certain parameter.Its process is: feedwater is squeezed into economizer heat absorption gradually later by feed pump, and temperature is elevated to the boiling point of drum operating pressure, becomes saturation water; Saturation water continues heat absorption in evaporation equipment (stove), flashes to saturated vapor temperature-resistant in the situation that; Saturated vapor is introduced superheater from drum and is superheated to gradually set point of temperature later, becomes qualified superheated steam, then arrives steam turbine acting.Drum: drum is commonly called as drum.What the drum of steam boiler was in-built is hot water and steam.Drum has certain water capacity, and with down-comer, water-cooling wall is connected, and forms natural water circulation system, and meanwhile, drum is accepted again the feedwater of economizer, to superheater, carries saturated vapor; Drum is heating, the decomposition point of evaporation, overheated three processes.Down-comer: effect is that the water in drum is continuously sent into lower collecting box, supplies with water-cooling wall, makes heating surface have enough quantity of circulating water, to guarantee reliable operation.In order to guarantee the reliability of water circulation, down-comer is all arranged in outside stove after drum is drawn.Header: claim again header.Be generally that diameter is larger, the pipe of closed at both ends, is used for connecting pipe.Play a part to collect, mix and distribute carbonated drink to guarantee that each heating surface supplies water reliably or collects water or the steam water interface of each heating surface.(be positioned at the lower collecting box of fire grate both sides, claim again anti-scorch header) water-cooling wall lower collecting box is all equipped with periodic blowdown conventionally.Water-cooling wall: water-cooling wall is arranged in combustion chamber surrounding or part is arranged in the middle of combustion chamber.It is comprised of many tedges, take and accepts radiant heat transfer as main heating surface.Effect: the thermal-flame and the radiant heat transfer of flue gas to water-cooling wall that rely on burner hearth, make water (unsaturated water or saturation water) heating evaporation become saturated vapor, because furnace wall inner surface is hidden by water screen tube, so temperature of furnace wall greatly reduces, make that furnace wall is unlikely to be burned.And can prevent again the erosion to furnace wall of slagging scorification and slag; Cylinder has been changed the structure of furnace wall, alleviates furnace wall weight.The form of water-cooling wall: 1. light pipe type 2. membrane type superheaters: be the auxiliary heating surface of steam boiler, its effect is in the situation that pressure is constant, draws saturated vapor from drum, then through heating, make saturated vapor become the superheated steam of uniform temperature.Economizer: be arranged in boiler back end ductwork, utilize the equipment of the waste-heat boiler feedwater of flue gas, its effect is exactly to improve feed temperature, reduces exhaust gas temperature, reduces heat loss due to exhaust gas, improves the thermal efficiency of boiler.Desuperheating device: guarantee steam temperature within the limits prescribed.Steam temperature regulates: 1, steam tempering (employing attemperator) 2, fume side adjusting (adopting swing type burner) stove stove are exactly the combustion system of boiler, burner hearth, flue, burner and air preheater etc., consist of.Operation principle: pressure fan is sent into air to absorb the heat of flue gas in air preheater and send hot-flow flue to, is then divided into two strands: one is given pulverized coal preparation system and carries coal dust as a wind and send into coal powder injection device, and another strand is directly sent to coal powder injection device as Secondary Air.Coal dust and primary and secondary air spray into burner hearth header burning heat release through burner, and heat is passed to the radiation heating-surfaces such as water-cooling wall of burner hearth surrounding with radiation mode, the high-temperature flue gas that burning produces along flue stream through superheater, the equipment such as economizer and air preheater, heat is mainly passed to them with convection type, in diabatic process, flue-gas temperature constantly reduces, and finally by induced-draught fan, sends into chimney and enters atmosphere.Burner hearth: burner hearth is surrounded by a furnace wall, the principal space conducting heat well for fuel combustion, its surrounding is covered with water-cooling wall.Burner hearth bottom is ash discharge cinder notch, and the furnace bottom of dry bottom furnace is furnace hopper crooked by front and back water screen tube and inclination that form, and the furnace bottom of slag tapping boiler is the molten slag bath of level.Upper furnace is to be hung with pendant superheater, and the passage of burner hearth back upper place smoke gas flow flake hearth-tapping is furnace outlet.Air preheater: be to utilize the heat of boiler exhaust gas to add the heat-exchange apparatus of hot-air.It is to be contained in the vertical gas pass of boiler tail.Because technological difficulties are exactly that its volume is too large with conventional boiler recovery waste heat, usually, because there being enough positions to install, be limited to the defect of special equipment supervision, and waste heat exhaust emissions point is many, input cost weight, period of investment return limit for length, poor practicability.How to realize a kind ofly reduce costs, volume is little, is not subject to enclose in pot standard the restriction of interior supervision, and facilitates installation and maintenance, the steam generator that can produce high-quality steam becomes the larger market demand.In addition, boiler belongs to pressure vessel, and the volume of inner employing water is generally more than 30 liters.
For example, the diesel engine that oil exploitation oil well is used is discharged flue gas up to more than 300 degree, possesses very high recycling and is worth.But because discharged diesel oil flue gas is messy; And be subject to condition restriction water quality to be difficult to reach the requirement that boiler is used; In addition, because the power variation of diesel-driven generator is frequent, the variations in temperature that tail gas is discharged is large, and conventional waste heat boiler is difficult to adapt to service condition.
Summary of the invention
In view of the above problems, the object of the present invention is to provide a kind of replaceable internal unit, facilitate regular maintenance and cleaning, heat exchange efficiency high, and structure durable and saving cost, safe detachable steam generator also used.
For achieving the above object, a kind of detachable steam generator provided by the invention, wherein, casing, the directly-heated type heat exchanger being provided with in casing, on directly-heated type heat exchanger one end, be provided with the flue gas shunting device being communicated with directly-heated type heat exchanger, on the directly-heated type heat exchanger other end, be provided with the flue gas collector being communicated with directly-heated type heat exchanger, the flue gas exhaust pipe that is provided with the inlet preheating device being communicated with flue gas collector and is provided with on inlet preheating device on flue gas collector, and the superheated steam exhaust outlet that is provided with of the directly-heated type heat exchanger that is positioned at flue gas shunting device one side.On directly-heated type heat exchanger one end, be provided with the first flue gas inlet port being communicated with flue gas shunting device, in directly-heated type heat exchanger one side, be provided with the second flue gas inlet port being communicated with flue gas shunting device.On the directly-heated type heat exchanger other end, be provided with the first flue gas discharge opening being communicated with flue gas collector, in directly-heated type heat exchanger one side, be provided with the second flue gas discharge opening being communicated with flue gas collector.Flue gas shunting device by the first empty van body being communicated with directly-heated type heat exchanger one end, on the first empty van body, be provided with the first intake interface being communicated with the first flue gas inlet port respectively and form the second intake interface being communicated with the second flue gas inlet port.On the first empty van body, be provided with high-temperature flue gas entry.The first intake interface is removable connection with being connected of the first flue gas inlet port, and the second intake interface is removable connection with being connected of the second flue gas inlet port.The first intake interface on the first empty van body and the second intake interface can guarantee that high-temperature flue gas is supplied to directly-heated type heat exchanger from different azimuth, improve heat exchange efficiency.
Flue gas collector by the second empty van body being communicated with the directly-heated type heat exchanger other end, on the second empty van body, be provided with the first exhaust port being communicated with the first flue gas discharge opening respectively and become with the second exhaust interface group being communicated with the second flue gas discharge opening.The first exhaust port on the second empty van body and the second exhaust port can guarantee that high-temperature flue gas, from the different azimuth discharge of directly-heated type heat exchanger, improves the speed of heat exchange.The first exhaust port is removable connection with being connected of the first flue gas discharge opening, and the second exhaust port is removable connection with being connected of the second flue gas discharge opening.Because directly-heated type heat exchanger is respectively removable connection with the flue gas shunting device at two ends with flue gas collector, when if desired carrying out regular maintenance and cleaning, easy disassembly; Meanwhile, regular maintenance only need be carried out the replacing of internal part, has guaranteed integrally-built durability.In addition, effective water capacity of directly-heated type heat exchanger inside is less than 30 liters, improves the generation speed from water to steam.Above-mentioned direct-heating heat exchanger can adapt to the fume emission environment under the mal-conditions such as oil well, and can, by removable replacing, realized reduction regular maintenance and cleaned cost, and steam produce object efficiently.
In some embodiments, directly-heated type heat exchanger is to be obliquely installed in case, and the angle that directly-heated type heat exchanger tilts is 15 °-22 °.Wherein, the angle of inclination of 20 ° is best, has guaranteed that the directly-heated type heat exchanger integral body in heeling condition obtains sufficient heat exchange, has improved efficiency and the steam generation speed of heat exchange.
In some embodiments, described directly-heated type heat exchanger comprise shell main body, in shell main body, be provided with first tubulation of many, the first tube sheet being respectively equipped with on the first tubulation two ends, respectively through the second tubulation of many first tubulations and the second tube sheet being respectively equipped with on the two ends of the second tubulation.The space forming between the outer wall of the inwall of the first tubulation and the second tubulation is shell side, the second tubulation that runs through the first tubulation extends to respectively the second tube sheet to two ends, shell body interior between the second tube sheet on second tubulation one end and the first flue gas inlet port is provided with inlet chamber, the second tube sheet on the second tubulation other end and the shell body interior between the first flue gas discharge opening are provided with discharge chamber, the first tube sheet is parallel with the second tube sheet, delivery port on coil pipe is communicated with the cavity between first row tube sheet in directly-heated type heat exchanger in flue gas collector one end and the second tube sheet.Due to the structure of above-mentioned the first tubulation and the second tubulation employing pipe-in-pipe, guaranteed that the water in the first tubulation obtains comprehensively fully contact heat-exchanging, improve further the efficiency of heat exchange.
In some embodiments, in the first empty van body, be provided with overheating steam heater.Overheating steam heater comprises many first longitudinal pipes side by side, on first longitudinal pipe one end, be provided with the first transverse pipe of being communicated with the first longitudinal pipe, on the first longitudinal pipe other end, be provided with the second transverse pipe, one end of being communicated with the first transverse pipe is communicated with the second transverse pipe and in the first longitudinal pipe one side, is provided with side by side second longitudinal pipe of many, at the second longitudinal pipe other end, is provided with the 3rd transverse pipe being communicated with the second longitudinal pipe, and in the first transverse pipe, is provided with the air inlet of input superheated steam and in the 3rd transverse pipe, is provided with the exhaust outlet of output superheated steam.In the second transverse pipe, be provided with blow-off pipe.On air inlet, be provided with bend pipe, on exhaust outlet, be provided with the straight tube that crosses and be communicated with bend pipe, on the bend pipe crossing between connectivity part of the turning of bend pipe and bend pipe and straight tube, be provided with the first valve that opens and closes bend pipe, on the bend pipe that bend pipe and straight tube cross between connectivity part and the first valve, be provided with the second valve that opens and closes bend pipe.Owing to being provided with overheating steam heater in the first empty van body, utilize the open to shut to regulate of the first valve or the second valve, and the high-temperature flue gas in the first empty van body, whether the superheated steam of discharging from directly-heated type heat exchanger is carried out to post bake; In addition, effect during blow-off pipe closed condition be guaranteed steam after heat exchange the first longitudinal pipe with in the second longitudinal pipe, can fully contact with high-temperature flue gas comprehensively.The structure of this and existing coil pipe compares, and the vapor (steam) temperature of discharging through overheating steam heater is higher, possesses high efficiency.Effect for blow-off pipe open mode is thoroughly to discharge the dirt forming in the first longitudinal pipe and the second longitudinal pipe, cleans more thorough.And the effect of the first valve and the second valve is whether steam to be carried out to the adjusting of post bake as required, has strengthened the flexibility of use procedure.
In some embodiments, the tube connector that on the bend pipe between the first valve and the second valve, setting and bend pipe and superheated steam exhaust outlet are interconnected.Its structure can change arbitrarily.
In some embodiments, on tube connector, be provided with safety valve.Because the effect of safety valve is that the whole equipment of protection prevents in the course of the work that pressure is excessive and causes danger, further improved the security of work.
In some embodiments, inlet preheating device forms by being provided with the body being communicated with the second empty van body and being provided with coil pipe on the second empty van body in body.On body, be provided with the water inlet and the delivery port that are communicated with coil pipe.Because first the water entering before directly-heated type exchanged heat device carry out heat exchange in advance through coil pipe and the flue gas being discharged in body from directly-heated type exchanged heat device, further improve the utilization ratio of steam generation speed and flue gas, and reduced fume emission to extraneous temperature.Can utilize in addition the coil pipe of different sizes to adjust fume emission to extraneous temperature.For example, coil pipe is large, and the flue-gas temperature of discharge will be low, otherwise.Realized the phenomenon of avoiding producing dew point corrosion according to different smoke properties.
In some embodiments, flue gas shunting device one side is provided with the water level mark rod of water capacity accumulated amount in prompting shell main body.The effect of this water level mark rod is more accurately to point out the duty of directly-heated type heat exchanger, and when water level is too high or too high, the inductor being connected with water level mark rod can start alarm signal.
In some embodiments, casing is comprised of incubator body and the thermal insulating door thermally insulated door that is provided with on incubator body.Owing to there being interlayer in the middle of casing, and insulation material is mounted in interlayer, the heat loss while having avoided water to carry out heat exchange.
In some embodiments, thermal insulating door thermally insulated door is arranged at respectively on the casing of directly-heated type heat exchanger both sides.During use, if during a plurality of directly-heated type heat exchanger, can from both sides by directly-heated type heat exchanger, pull down or load onto very easily.Further improved the efficiency of regular maintenance.
The invention has the beneficial effects as follows replaceable internal unit, facilitate regular maintenance and cleaning, heat exchange efficiency high, and structure durable and saving cost, safety also used.
Accompanying drawing explanation
Fig. 1 is the structural representation of the embodiment of the present invention;
Fig. 2 is internal structure schematic diagram embodiment illustrated in fig. 1;
Fig. 3 is the structural representation of flue gas shunting device and directly-heated type heat exchanger in the embodiment of the present invention;
Fig. 4 is the structural representation of overheating steam heater in the embodiment of the present invention;
Fig. 5 is the structural representation of directly-heated type heat exchanger in the embodiment of the present invention;
Fig. 6 is the structural representation that in the embodiment of the present invention, directly-heated type heat exchanger is inner and amplify part;
Fig. 7 is the blast structural representation of flue gas collector in the embodiment of the present invention, inlet preheating device and flue gas exhaust pipe;
Fig. 8 is the overall structure schematic diagram of flue gas collector in the embodiment of the present invention, inlet preheating device and flue gas exhaust pipe;
Fig. 9 is the blast structural representation of thermal insulating door thermally insulated door in the embodiment of the present invention.
The specific embodiment
Below in conjunction with accompanying drawing, invention is described in further detail.
Embodiment mono-
As shown in Fig. 1-9, a kind of detachable steam generator, casing 1, the directly-heated type heat exchanger 2 being provided with in casing 1, on directly-heated type heat exchanger 2 one end, be provided with the flue gas shunting device 3 being communicated with directly-heated type heat exchanger 2, on directly-heated type heat exchanger 2 other ends, be provided with the flue gas collector 4 being communicated with directly-heated type heat exchanger 2, on flue gas collector 4, be provided with the inlet preheating device 5 being communicated with flue gas collector 4 and the flue gas exhaust pipe 6 being provided with on inlet preheating device 5, and the superheated steam exhaust outlet 7 that is provided with of the directly-heated type heat exchanger 2 that is positioned at flue gas shunting device 3 one sides.On directly-heated type heat exchanger 2 one end, be provided with the first flue gas inlet port 21 being communicated with flue gas shunting device 3, in directly-heated type heat exchanger 2 one sides, be provided with the second flue gas inlet port 22 being communicated with flue gas shunting device 3.On directly-heated type heat exchanger 2 other ends, be provided with the first flue gas discharge opening 23 being communicated with flue gas collector 4, in directly-heated type heat exchanger 2 one sides, be provided with the second flue gas discharge opening 24 being communicated with flue gas collector 4.Flue gas shunting device 3 by the first empty van body 31 being communicated with directly-heated type heat exchanger 2 one end, on the first empty van body 31, be provided with the first intake interface 32 being communicated with the first flue gas inlet port 21 respectively and form the second intake interface 33 being communicated with the second flue gas inlet port 22.On the first empty van body 31, be provided with high-temperature flue gas entry 10.The first intake interface 32 is removable connection with being connected of the first flue gas inlet port 21, and the second intake interface 33 is removable connection with being connected of the second flue gas inlet port 22.The first intake interface 32 on the first empty van body 31 and the second intake interface 33 can guarantee that high-temperature flue gas is supplied to directly-heated type heat exchanger 2 from different azimuth.The first above-mentioned empty van body 31 can be designed to L shaped empty van body.
Flue gas collector 4 by the second empty van body 41 being communicated with directly-heated type heat exchanger 2 other ends, on the second empty van body 41, be provided with the first exhaust port 42 being communicated with the first flue gas discharge opening 23 respectively and form the second exhaust port 43 being communicated with the second flue gas discharge opening 24.The first exhaust port 42 on the second empty van body 41 and the second exhaust port 43 can guarantee that high-temperature flue gas, from the different azimuth discharge of directly-heated type heat exchanger 2, improves the speed of heat exchange.The first exhaust port 42 is removable connection with being connected of the first flue gas discharge opening 23, and the second exhaust port 43 is removable connection with being connected of the second flue gas discharge opening 24.Because directly-heated type heat exchanger 2 is respectively removable connection with the flue gas shunting device 3 at two ends with flue gas collector 4, when if desired carrying out regular maintenance and cleaning, easy disassembly; Meanwhile, regular maintenance only need be carried out the replacing of internal part, has guaranteed integrally-built durability.In addition, effective water capacity of directly-heated type heat exchanger 2 inside is less than 30 liters, improves the generation speed from water to steam.Above-mentioned direct-heating heat exchanger can adapt to the fume emission environment under the mal-conditions such as oil well, and can be by removable replacing.The second above-mentioned empty van body 41 can be designed to 7 font empty van bodies.This connected mode of the first above-mentioned intake interface 32 and the first flue gas inlet port 21, the second intake interface 33 and the second flue gas inlet port 22, the first exhaust port 42 and the first flue gas discharge opening 23, the second exhaust port 43 and the second flue gas discharge opening 24 is to adopt first socket, the mode being locked with metallic aluminium sheet afterwards.Directly-heated type heat exchanger 2 comprises shell main body 211, is provided with first tubulation 221 of many in shell main body 211, the first tube sheet 231 being respectively equipped with on the first tubulation 221 two ends, respectively through the second tubulation 241 of many first tubulations 221 and the second tube sheet 251 being respectively equipped with on the two ends of the second tubulation 241.The space forming between the outer wall of the inwall of the first tubulation 221 and the second tubulation 241 is shell side 261, the second tubulation 241 that runs through the first tubulation 221 extends to respectively the second tube sheet 251 to two ends, the second tube sheet 251 on second tubulation 241 one end and shell main body 211 inside between the first flue gas inlet port 21 are provided with inlet chamber 27, the second tube sheet 251 on second tubulation 241 other ends and shell main body 211 inside between the first flue gas discharge opening 23 are provided with discharge chamber 28, the first tube sheet 231 is parallel with the second tube sheet 251, delivery port 54 on coil pipe 52 is communicated with the cavity 29 between the first tubulation 221 plates in directly-heated type heat exchanger 2 in flue gas collector 4 one end and the second tube sheet 251.Due to the structure of above-mentioned the first tubulation 221 and the second tubulation 241 employing pipe-in-pipe, guaranteed that the water in the first tubulation 221 obtains comprehensively fully contact heat-exchanging.
The tube connector 9 being interconnected with bend pipe 88 and superheated steam exhaust outlet 7 is set on the bend pipe 88 between the first valve 810 and the second valve 811.Casing 1 is comprised of incubator body and the thermal insulating door thermally insulated door 11 that is provided with on incubator body.Owing to having interlayer in the middle of casing 1, and insulation material is mounted in interlayer, the heat loss while having avoided water to carry out heat exchange.Thermal insulating door thermally insulated door 11 is arranged at respectively on the casing 1 of directly-heated type heat exchanger 2 both sides.During use, if during a plurality of directly-heated type heat exchanger 2, can from both sides by directly-heated type heat exchanger 2, pull down or load onto very easily.
Embodiment bis-
As shown in Fig. 1,2,3,5, in the situation that not changing above-described embodiment one, directly-heated type heat exchanger 2 is to be obliquely installed in case, and the angle that directly-heated type heat exchanger 2 tilts is 15 °-22 °.Preferably, the angle of inclination of 20 ° is best.
Embodiment tri-
As shown in Figure 4, in the situation that not changing above-described embodiment one, in the first empty van body 31, be provided with overheating steam heater 8.Overheating steam heater 8 comprises many first longitudinal pipes 81 side by side, on first longitudinal pipe 81 one end, be provided with the first transverse pipe 82 being communicated with the first longitudinal pipe 81, on first longitudinal pipe 81 other ends, be provided with the second transverse pipe 83 being communicated with the first transverse pipe 82, one end is communicated with the second transverse pipe 83 and in the first longitudinal pipe 81 1 sides, is provided with side by side second longitudinal pipe 84 of many, at second longitudinal pipe 84 other ends, be provided with the 3rd transverse pipe 85 being communicated with the second longitudinal pipe 84, and in the first transverse pipe 82, be provided with the air inlet 86 of input superheated steam and in the 3rd transverse pipe 85, be provided with the exhaust outlet 87 of exporting superheated steam.In the second transverse pipe 83, be provided with blow-off pipe.On air inlet 86, be provided with bend pipe 88, on exhaust outlet 87, be provided with the straight tube 89 that crosses and be communicated with bend pipe 88, on the bend pipe 88 crossing between connectivity part of the turning of bend pipe 88 and bend pipe 88 and straight tube 89, be provided with the first valve 810 that opens and closes bend pipe 88, on the bend pipe 88 that bend pipe 88 and straight tube 89 cross between connectivity part and the first valve 810, be provided with the second valve 811 that opens and closes bend pipe 88.In the first empty van body 31, be provided with overheating steam heater 8, utilize the open to shut to regulate of the first valve 810 or the second valve 811, and the high-temperature flue gas in the first empty van body 31, whether the superheated steam of discharging from directly-heated type heat exchanger 2 is carried out to post bake.Effect during blow-off pipe closed condition is to have guaranteed that the steam after heat exchange can fully contact with high-temperature flue gas with in the second longitudinal pipe 84 at the first longitudinal pipe 81 comprehensively.The structure of this and existing coil pipe 52 compares, and the vapor (steam) temperature of discharging through overheating steam heater 8 is higher, possesses high efficiency.Effect for blow-off pipe open mode is the dirt that can thoroughly discharge the first longitudinal pipe 81 and the second longitudinal pipe 84 interior formation, cleans more thorough.
Embodiment tetra-
As shown in Figure 2, in the situation that not changing above-described embodiment one, on tube connector 9, be provided with safety valve 91.Quantity for safety valve 91 is generally 2, and effect is when detachable steam generator is normal, if stopping up appears in any one pipeline, one of them safety valve 91 just can carry out pressure release automatically, avoids causing danger; Another one safety valve 91 rises and prevents that pipeline from occurring that secondary stops up, and plays prevention effect.
Embodiment five
As shown in Figure 7,8, in the situation that not changing above-described embodiment one, inlet preheating device 5 forms by being provided with the body 51 being communicated with the second empty van body 41 and being provided with coil pipe 52 on the second empty van body 41 in body 51.On body 51, be provided with the water inlet 53 and the delivery port 54 that are communicated with coil pipe 52.Because first the water entering before directly-heated type exchanged heat device carry out heat exchange in advance through coil pipe 52 and the flue gas being discharged in body 51 from directly-heated type exchanged heat device, further improve the utilization ratio of steam generation speed and flue gas, and reduced fume emission to extraneous temperature.Can utilize in addition the coil pipe 52 of different sizes to adjust fume emission to extraneous temperature.For example, coil pipe 52 is large, and the flue-gas temperature of discharge will be low.
Embodiment six,
As shown in Figure 2, in the situation that not changing above-described embodiment one, flue gas shunting device 3 one sides are provided with the water level mark rod 12 of prompting shell main body 211 interior water capacity accumulated amounts.The effect of this water level mark rod 12 is more accurately to point out the duty of directly-heated type heat exchanger 2, and when water level is too high or too high, the inductor being connected with water level mark rod can start alarm signal.Wherein water level mark rod has three prompting positions, is respectively high water level, ordinary water level and low water level, between the corresponding shell main body 211 interior water levels of these three water levels and superheated steam exhaust outlet 7, forms certain space.Dischargeable capacity at directly-heated type heat exchanger 2 interior water is less than 30 liters.
Embodiment seven
As shown in Fig. 1,2,3,5, in the situation that not changing above-described embodiment one to four, at the interior increase by 1 of casing 1 or 2 directly-heated type heat exchangers 2.
Below in conjunction with embodiment mono-to five explanation operation principle:
After the water inlet 53 of water from inlet preheating device 5 enters, the coil pipe 52 of flowing through flows out from delivery port 54, be diverted to afterwards the first tubulation 221 in 2 or 3 directly-heated type heat exchangers 2, until the water in the first tubulation 221 is filled to the ordinary water level of water level mark rod.
High-temperature flue gas pours into the high-temperature flue gas entry 10 on the first empty van body 31 from casing 1, pours into the second tubulation 241 and pours into shell main body 211 inside from the second flue gas inlet port 22 respectively from the first flue gas inlet port 21.Water in the first tubulation 221 and the flue gas of high temperature enter after heat exchange, produce superheated steam and discharge from superheated steam exhaust outlet 7, the tube connector 9 of flowing through.
If do not need, steam is not carried out to second heat exchange, close the first valve 810, open the second valve 811, directly from bend pipe 88 other ends, discharge.If desired steam is carried out to second heat exchange, open the first valve 810, open the second valve 811, steam is diverted to each the first longitudinal pipe 81 after entering the first transverse pipe 82, then discharges the second transverse pipe 83 from first longitudinal pipe 81 other ends; Be diverted to afterwards each the second longitudinal pipe 84, then be discharged to the 3rd transverse pipe 85 from second longitudinal pipe 84 other ends, then from exhaust outlet 87 exhaust steams, finally directly from bend pipe 88 other ends, discharge.If desired clean each body 51, first that each pipe of water input is inner, from blow-off pipe, discharge afterwards.
After 2 heat exchanges of directly-heated type heat exchanger, high-temperature flue gas enters in the second empty van body 41 from the first flue gas discharge opening 23 and the second flue gas discharge opening 24 respectively, enters afterwards in the body 51 on inlet preheating device 5, and the water of the coil pipe 52 of flowing through is entered to preheat.Finally directly from flue gas exhaust pipe 6, discharge.
If desired change or clean directly-heated type heat exchanger 2, can directly open the thermal insulating door thermally insulated door 11 of both sides, pulling down directly-heated type heat exchanger 2 and just can carry out regular maintenance or cleaning.
Above-described is only some embodiments of the present invention.For the person of ordinary skill of the art, without departing from the concept of the premise of the invention, can also make some distortion and improvement, these all belong to the protection domain of invention.
Claims (10)
1. a detachable steam generator, it is characterized in that, the directly-heated type heat exchanger that comprise casing, is provided with in casing, on directly-heated type heat exchanger one end, be provided with the flue gas shunting device that is communicated with directly-heated type heat exchanger, on the directly-heated type heat exchanger other end, be provided with the flue gas collector being communicated with directly-heated type heat exchanger, the flue gas exhaust pipe that is provided with the inlet preheating device being communicated with flue gas collector and is provided with on flue gas collector on inlet preheating device, and be positioned at the superheated steam exhaust outlet that the directly-heated type heat exchanger of flue gas shunting device one side is provided with;
On described directly-heated type heat exchanger one end, be provided with the first flue gas inlet port being communicated with flue gas shunting device; In described directly-heated type heat exchanger one side, be provided with the second flue gas inlet port being communicated with flue gas shunting device;
On the described directly-heated type heat exchanger other end, be provided with the first flue gas discharge opening being communicated with flue gas collector; In described directly-heated type heat exchanger one side, be provided with the second flue gas discharge opening being communicated with flue gas collector;
Described flue gas shunting device by the first empty van body being communicated with directly-heated type heat exchanger one end, on the first empty van body, be provided with the first intake interface being communicated with the first flue gas inlet port respectively and form the second intake interface being communicated with the second flue gas inlet port; On the first described empty van body, be provided with high-temperature flue gas entry;
The first described intake interface is removable connection with being connected of the first flue gas inlet port;
The second described intake interface is removable connection with being connected of the second flue gas inlet port;
Described flue gas collector by the second empty van body being communicated with the directly-heated type heat exchanger other end, on the second empty van body, be provided with the first exhaust port being communicated with the first flue gas discharge opening respectively and become with the second exhaust interface group being communicated with the second flue gas discharge opening;
The first described exhaust port is removable connection with being connected of the first flue gas discharge opening;
The second described exhaust port is removable connection with being connected of the second flue gas discharge opening.
2. a kind of detachable steam generator according to claim 1, is characterized in that,
Described directly-heated type heat exchanger is to be obliquely installed in case;
The angle that described directly-heated type heat exchanger tilts is 150-220.
3. a kind of detachable steam generator according to claim 1, it is characterized in that, described directly-heated type heat exchanger comprises shell main body, is provided with first tubulation of many in shell main body, the first tube sheet being respectively equipped with on the first tubulation two ends, respectively through the second tubulation of many first tubulations and the second tube sheet being respectively equipped with on the two ends of the second tubulation;
The space forming between the outer wall of the inwall of described the first tubulation and the second tubulation is shell side;
Described the second tubulation that runs through the first tubulation extends to respectively the second tube sheet to two ends;
The second tube sheet on second described tubulation one end and the shell body interior between the first flue gas inlet port are provided with inlet chamber;
The second tube sheet on the second described tubulation other end and the shell body interior between the first flue gas discharge opening are provided with discharge chamber;
The first described tube sheet is parallel with the second tube sheet;
Delivery port on described coil pipe is communicated with the cavity between first row tube sheet in directly-heated type heat exchanger in flue gas collector one end and the second tube sheet.
4. a kind of detachable steam generator according to claim 1, is characterized in that, in the first described empty van body, is provided with overheating steam heater;
Described overheating steam heater comprises many first longitudinal pipes side by side, on first longitudinal pipe one end, be provided with the first transverse pipe being communicated with the first longitudinal pipe, on the first longitudinal pipe other end, be provided with the second transverse pipe being communicated with the first transverse pipe, one end is communicated with the second transverse pipe and is provided with side by side second longitudinal pipe of many in the first longitudinal pipe one side, at the second longitudinal pipe other end, be provided with the 3rd transverse pipe being communicated with the second longitudinal pipe, and in the first transverse pipe, be provided with the air inlet of input superheated steam and in the 3rd transverse pipe, be provided with the exhaust outlet of exporting superheated steam,
In the second described transverse pipe, be provided with blow-off pipe;
On described air inlet, be provided with bend pipe;
On described exhaust outlet, be provided with the straight tube that crosses and be communicated with bend pipe;
On the bend pipe crossing between connectivity part of the turning of described bend pipe and bend pipe and straight tube, be provided with the first valve that opens and closes bend pipe;
On the bend pipe that described bend pipe and straight tube cross between connectivity part and the first valve, be provided with the second valve that opens and closes bend pipe.
5. a kind of detachable steam generator according to claim 4, is characterized in that, the tube connector that on the first described valve and the bend pipe between the second valve, setting and bend pipe and superheated steam exhaust outlet are interconnected.
6. a kind of detachable steam generator according to claim 5, is characterized in that, on described tube connector, is provided with safety valve.
7. a kind of detachable steam generator according to claim 1, is characterized in that, described inlet preheating device forms by being provided with the body being communicated with the second empty van body and being provided with coil pipe on the second empty van body in body; On described body, be provided with the water inlet and the delivery port that are communicated with coil pipe.
8. according to a kind of detachable steam generator described in claim 1 or 2 or 3 or 4 or 5 or 6 or 7, it is characterized in that, described flue gas shunting device one side is provided with the water level mark rod of water capacity accumulated amount height in prompting shell main body.
9. a kind of detachable steam generator according to claim 8, is characterized in that, described casing is comprised of incubator body and the thermal insulating door thermally insulated door that is provided with on incubator body.
10. a kind of detachable steam generator according to claim 9, is characterized in that, described thermal insulating door thermally insulated door is arranged at respectively on the casing of directly-heated type heat exchanger both sides.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410041064.6A CN103759239B (en) | 2014-01-27 | 2014-01-27 | Detachable steam generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410041064.6A CN103759239B (en) | 2014-01-27 | 2014-01-27 | Detachable steam generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103759239A true CN103759239A (en) | 2014-04-30 |
| CN103759239B CN103759239B (en) | 2015-04-29 |
Family
ID=50526522
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410041064.6A Active CN103759239B (en) | 2014-01-27 | 2014-01-27 | Detachable steam generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103759239B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109520314A (en) * | 2018-11-14 | 2019-03-26 | 山东泰山生力源玻璃有限公司 | A kind of residual neat recovering system of glass furnace |
| CN112030476A (en) * | 2020-09-02 | 2020-12-04 | 安徽苏立科技股份有限公司 | Steam generator applied to washing machine |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2141551Y (en) * | 1992-12-10 | 1993-09-01 | 胡庆彦 | High-effect energy-saving steam-water and water-water two-stage heat exchanger |
| CN201093900Y (en) * | 2007-06-19 | 2008-07-30 | 北京建筑工程学院 | Compact type two return-stroke flue tube flue gas condensing energy conservation equipment |
| US20110303164A1 (en) * | 2010-06-14 | 2011-12-15 | Gas Technology Institute | Integrated contact condensing water heater |
| CN202297123U (en) * | 2011-10-13 | 2012-07-04 | 上海奥格利环保工程有限公司 | SO3 flue evaporator for sulfuric acid system |
| CN202494365U (en) * | 2012-03-19 | 2012-10-17 | 黄华杰 | Composite directly-heated type heat exchanger |
| CN203731362U (en) * | 2014-01-27 | 2014-07-23 | 黄华杰 | Detachable vapor generator |
-
2014
- 2014-01-27 CN CN201410041064.6A patent/CN103759239B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2141551Y (en) * | 1992-12-10 | 1993-09-01 | 胡庆彦 | High-effect energy-saving steam-water and water-water two-stage heat exchanger |
| CN201093900Y (en) * | 2007-06-19 | 2008-07-30 | 北京建筑工程学院 | Compact type two return-stroke flue tube flue gas condensing energy conservation equipment |
| US20110303164A1 (en) * | 2010-06-14 | 2011-12-15 | Gas Technology Institute | Integrated contact condensing water heater |
| CN202297123U (en) * | 2011-10-13 | 2012-07-04 | 上海奥格利环保工程有限公司 | SO3 flue evaporator for sulfuric acid system |
| CN202494365U (en) * | 2012-03-19 | 2012-10-17 | 黄华杰 | Composite directly-heated type heat exchanger |
| CN203731362U (en) * | 2014-01-27 | 2014-07-23 | 黄华杰 | Detachable vapor generator |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109520314A (en) * | 2018-11-14 | 2019-03-26 | 山东泰山生力源玻璃有限公司 | A kind of residual neat recovering system of glass furnace |
| CN112030476A (en) * | 2020-09-02 | 2020-12-04 | 安徽苏立科技股份有限公司 | Steam generator applied to washing machine |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103759239B (en) | 2015-04-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105953231B (en) | A kind of high parameter garbage burning boiler with reheating | |
| CN106439855B (en) | A kind of steam air pre-heating system of garbage burning boiler | |
| CN205090598U (en) | Coal -fired powder boiler of vertical extreme misery tubular construction | |
| WO2021258647A1 (en) | Natural circulation box structure for ferrosilicon waste heat boiler | |
| CN108775573A (en) | A kind of novel electricity generation boiler of burning away the refuse | |
| CN203464262U (en) | Circulating fluidized bed boiler for combusting palm dreg | |
| CN104180359B (en) | Large-tonnage subcritical pressure boiler steam generator | |
| CN103759239B (en) | Detachable steam generator | |
| CN107477564A (en) | A kind of biomass recirculating fluidized bed boiler flue gas waste heat recovery system and method | |
| CN203731362U (en) | Detachable vapor generator | |
| CN209978041U (en) | High-temperature high-pressure waste incineration boiler | |
| CN106524104A (en) | Furnace hearth split large-tonnage fixed type superheated steam generator | |
| CN204301027U (en) | Verticle coal-burning stem boiler | |
| CN105318307B (en) | A kind of double-barrel transverse formula expansion chamber sprays denitration corner tube boiler | |
| CN110118356A (en) | A kind of high parameter fire grate garbage burning boiler | |
| CN203203010U (en) | Boiler for yellow phosphorus tail gas combustion | |
| CN206001919U (en) | Ultra-low NOx emission environmental protection and energy saving tubular heater | |
| CN205825033U (en) | High parameter garbage burning boiler with reheating | |
| CN105318309B (en) | A kind of pair of drum sprays denitration sedimentation separation corner tube boiler | |
| CN112097287B (en) | Boiler energy-saving and flue gas whitening system, process and application | |
| CN209763080U (en) | High-temperature high-pressure waste incineration pi-type boiler | |
| CN204006633U (en) | A kind of modular convection heating surface fire tube boiler | |
| CN106195968A (en) | Flue gas processing device and rotary hearth furnace high-temperature high dust smoke processing system | |
| CN209386313U (en) | Segmented water- to-water heat exchanger | |
| CN208670988U (en) | A kind of novel electricity generation boiler of burning away the refuse |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: GUANGDONG SHUNDE HYNOV ENERGY SCIENCE AND TECHNOLO Free format text: FORMER OWNER: HUANG HUAJIE Effective date: 20150429 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 528099 FOSHAN, GUANGDONG PROVINCE TO: 528311 FOSHAN, GUANGDONG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20150429 Address after: Beijiao town Shunde District Guangdong city Foshan province 528311 Shun Jiang Chen Dajiao neighborhood Industrial Zone 6 South Road No. four building Patentee after: Guangdong Shunde HYNOV Heat Technology Co., Ltd. Address before: 528099 Guangdong Province Nanhai District of Foshan city Guicheng Street South Road No. 39 Jiangnan in Jinyuan 2 Room 303 Patentee before: Huang Huajie |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 528311 no.3-5, Huanzhen East Road, Shunjiang neighborhood committee, Beijiao Town, Shunde District, Foshan City, Guangdong Province Patentee after: Guangdong Huan Neng Technology Co., Ltd. Address before: Beijiao town Shunde District Guangdong city Foshan province 528311 Shun Jiang Chen Dajiao neighborhood Industrial Zone 6 South Road No. four building Patentee before: Guangdong Shunde HYNOV Heat Technology Co., Ltd. |