CN201310875Y - Fuel gas superheated steam generator with dust blowing and removing system - Google Patents
Fuel gas superheated steam generator with dust blowing and removing system Download PDFInfo
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- CN201310875Y CN201310875Y CNU200820123027XU CN200820123027U CN201310875Y CN 201310875 Y CN201310875 Y CN 201310875Y CN U200820123027X U CNU200820123027X U CN U200820123027XU CN 200820123027 U CN200820123027 U CN 200820123027U CN 201310875 Y CN201310875 Y CN 201310875Y
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Abstract
The utility model relates to a fuel gas superheated steam generator with a dust blowing and removing system, which is applied to preparing high-pressure overheated steam. The inner side of a thermal insulating layer is provided with a stainless protecting layer, a furnace body is symmetrically fixed with a front dust blowing tube and a rear dust blowing tube, the bottom of the furnace body is provided with a dust removing hole, a radiation tube in the furnace body adopts a structure with an inner coil and an outer coil, the distance between the inner coil and the outer coil is 100-500 mm, the inner coil is a superheater, and the outer coil is an evaporator. The two coils are respectively provided with an inlet and an outlet and are symmetrically fixed at the front end of the furnace body. The utility model can periodically and effectively blow and remove dust in a three-pass smoke flue and a second-pass smoke flue of a boiler, ensure that the flues are in a cleaner state for a long time, lower the flowed friction loss of smoke, reduce the fan output, ensure better thermal exchange environment, improve the thermal exchange efficiency, reduce the maintenance cost of the boiler and increases the effective rate of utilization of energy.
Description
Technical field
The utility model relates to the boiler for preparing high pressure superheated steam, and particularly the high pressure superheated steam boiler flue has soot cleaning system.Can be applied to steam-electric power, oven dry, heat supply, and technical field such as oil field steam-assisted recovery.
Background technology
At present, the preparation high pressure superheated steam generally is to adopt the secondary steam heating means are obtained.As Chinese patent application number is 03226903 and 02145063 etc.Existing superheated vapour heating-furnace generally lays particular emphasis on the utilization of heat energy, improves the thermal efficiency, the energy savings aspect.For superheater inwall salt scale coagulation problem, fail to be well solved.When the superheater salt scale coagulation is serious, can cause boiler overheating pipe explosion accident.In addition, the fuel-firing gas-firing superheated vapour heating-furnace, after the long-time running, dust deposit in flue is serious, and is difficult to remove, and influences heating furnace operation heat exchange efficiency, improves exhaust gas temperature, causes heat greatly to lose, and environment is caused seriously influence.Dust deposit in flue, the flue gas circulation area reduces, the increase of the spontaneous draught capacity of flue gas is much smaller than the increase of dust stratification resistance, smooth and easy in order to guarantee to discharge fume, must strengthen power of fan, increase power consumption, thereby additionally increase operation and maintenance cost, improve the back current cost, and do not meet that country repeats injunctions, the policy of energy-saving and emission-reduction.The utility model is primarily aimed at these situations, in the past on the basis of superheated vapour heating-furnace, based on theory, base oneself upon reality, the response policy has designed the brand-new practical ash blowing and cleaning system of a cover, can very solve a series of problems that dust stratification brings effectively and fundamentally.
Summary of the invention
The purpose of this utility model provides a kind of fuel gas superheated vapour generator with ash blowing and cleaning system, can guarantee the smooth and easy circulation and the high efficient heat exchanging of heating furnace air and gas system.The fuel gas superheated vapour generator design of this band ash blowing and cleaning system has ash blowing and cleaning system; comprehensively in conjunction with existing boiler technology; take into full account various physical conditions; merged multinomial new technology well; in body of heater thermal insulation layer inboard the stainless steel protection inner core is set, in case damage thermal insulation layer during ash blowing and cleaning.
The utility model is that the technical scheme that its technical problem of solution is taked is: the fuel gas superheated vapour generator of band ash blowing and cleaning system is mainly by burner; body of heater; chimney and safety valve are formed; refractory insulating layer is arranged in the body of heater; there is stainless protection layer the thermal insulation layer inboard; it is characterized in that: the front end of body of heater is symmetrically fixed with preceding blowing pipe; the rear end of body of heater is fixed with the back blowing pipe; bottom of furnace body has cleaning door; radiant tube in the body of heater is inside and outside two-layer coil arrangement; distance between outer coil pipe and the inner coil pipe is between 100~500 millimeters; inner coil pipe is a superheater, and outer coil pipe is an evaporimeter.Two-layer coil pipe has import and outlet and symmetry to be fixed on the rear end of body of heater respectively.
Be connected high pressure blower with the back on the blowing pipe at preceding blowing pipe, the time opening gate, pressure-air is by preceding blowing pipe and back blowing pipe, and externally the cigarette ash on coil pipe and the inner coil pipe outer wall is cleared up.The ash blowing and cleaning system structure has tangible novelty and very strong practicality, blows ash mouthful symmetric design in the body of heater front and back end, and cleaning door designs at bottom of furnace body.According to boiler operation situation, can regularly purge deashing to flue system handles, guarantee that two, three backhaul flue streams are clear and coherent smooth, reduce flue circulation drag losses, reduce blower fan and exert oneself, clear disk tube wall face cigarette ash accumulation horizon, reduce the heat convection thermal resistance, reach the effect of enhanced heat exchange, thereby improve heat transfer efficiency, reduce exhaust gas temperature, improve rate of energy.Adopt the ash blowing and cleaning system innovative technology, must consider the protection of thermal insulation layer, therefore, this superheated vapour heating-furnace is provided with the stainless steel inner core in the thermal insulation layer inboard, prevents to blow ash and damages thermal insulation layer.
In order to regulate temperature in the body of heater, prevention is too high near the inner coil pipe temperature of burner, and there is the compound heat-insulation layer inboard near inner coil pipe, and the thickness of compound heat-insulation layer is 10~30 millimeters, and length is 500~1200 millimeters.
The beneficial effects of the utility model are: the fuel gas superheated vapour generator of the utility model band ash blowing and cleaning system, can regularly purge deashing to boiler two, three backhaul flue gas flow channels effectively, guarantee that flue is in cleaner state for a long time, reduce the flow of flue gas drag losses, reduce blower fan and exert oneself, guarantee good heat exchange environment, improve heat exchange efficiency, reduce the boiler attendance expense, improved effective utilization rate of energy.Popularization of the present utility model saves a large amount of energy will for country, brings harmonious looks for society and environment.
Description of drawings
Fig. 1 is the fuel gas superheated vapour generator architecture generalized section of the utility model band ash blowing and cleaning system.Represent its inner coil pipe 6, outer coil pipe 7, stainless steel inner core 5, fore blow ash mouth 2, after-blow ash mouth 9, the shape of cleaning door 10 and the position in body of heater, and represent the position relation between each structure member.
Fig. 2 is accompanying drawing 1 left view, shape and the position of fore blow ash mouth 2 on body of heater 11 of expression body of heater 11 front ends.
Fig. 3 is accompanying drawing 1 right view, the outer coil pipe import 12 and the outer coil pipe outlet 13 of after-blow ash mouth 9, inner coil pipe import 15 and the inner coil pipe outlet 14 and the outer coil pipe 7 of expression body of heater rear end.
Among the figure, 1. burner, 2. fore blow ash mouthful, 3. compound heat-insulation layer, 4. thermal insulation layer, 5. stainless protection layer; 6. inner coil pipe, 7. outer coil pipe, 8. chimney, 9. after-blow ash mouthful, 10. cleaning door; 11. body of heater, 12. outer coil pipe imports, 13. outer coil pipe outlets, the outlet of 14. inner coil pipes, 15. inner coil pipe imports.
The specific embodiment
Embodiment: with reference to figure 1.The fuel gas superheated vapour generator of the utility model band ash blowing and cleaning system mainly is made up of burner 1, body of heater 11, chimney 8 and safety valve etc.Burner 1 adopts dual fuel burner, promptly not only can fuel oil but also burner that can combustion gas, be installed in the leading section of body of heater 11.Body of heater 11 adopts cylindrical horizontal, and body of heater 11 diameters are 2500 millimeters, and length is 6000 millimeters.Body of heater 11 inwalls have refractory insulating layer 4, and there is stainless steel inner core 5 thermal insulation layer 4 inboards.
In the body of heater 11 radiant tube is arranged, radiant tube is that inner coil pipe 6 and outer coil pipe 7 are two-layer.Distance between inner coil pipe 6 and the outer coil pipe 7 is 200 millimeters.It is that 85 millimeters seamless steel pipe welding is made that inner coil pipe 6 and outer coil pipe 7 all adopt diameter, and diameter was 1400 millimeters after inner coil pipe 6 dishes were good, and outer coil pipe 7 coils into 1700 millimeters of diameters.Inner coil pipe 6 is a superheater, and outer coil pipe 7 is an evaporimeter.A cleaning door 10 is arranged at body of heater 11 bottoms.
Consult Fig. 2.Body of heater 11 leading sections 4 fore blows ash mouthfuls 2 that on concentric circles, is symmetrically distributed.
Consult Fig. 3.Body of heater 11 rearward end are provided with the outer coil pipe import 12 and the outer coil pipe outlet 13 of outer coil pipe 7, the inner coil pipe import 15 of inner coil pipe 6 and inner coil pipe 14, and 4 after-blow ash mouths 9 are symmetrically distributed on concentric circles.
Consult Fig. 1.Inboard near inner coil pipe 6 is fixed with compound heat-insulation layer 3, and the thickness of compound heat-insulation layer 3 is 20 millimeters, and length is 1000 millimeters.Prevention is too high near inner coil pipe 6 temperature of burner.
Outer coil pipe exports the steam inlet that 13 pipelines connect high-pressure stream-water separator, and inner coil pipe 6 inlet line connect the venthole of high-pressure stream-water separator.The steam that evaporimeter (outer coil pipe) produces will contain the graininess ingress filter of impurity through high-pressure stream-water separator in the steam, the gas that enters superheater (inner coil pipe) is pure vapour, and is free from foreign meter.Inner coil pipe 6 inwalls can not produce scale formation.
Claims (2)
1; a kind of fuel gas superheated vapour generator with ash blowing and cleaning system; mainly by burner (1); body of heater (11); chimney (8) and safety valve are formed; refractory insulating layer (4) is arranged in the body of heater (11); it is characterized in that: there is stainless protection layer (5) thermal insulation layer (4) inboard; the front end of body of heater (11) is symmetrically fixed with preceding blowing pipe (2); the rear end of body of heater (11) is fixed with back blowing pipe (9); cleaning door (10) is arranged at body of heater (11) bottom; radiant tube in the body of heater (11) is inside and outside two-layer coil arrangement; distance between outer coil pipe (7) and the inner coil pipe (6) is between 100~500 millimeters; inner coil pipe (6) is a superheater; outer coil pipe (7) is an evaporimeter, and two-layer coil pipe has import and outlet and symmetry to be fixed on the rear end of body of heater (11) respectively.
2, the fuel gas superheated vapour generator of band ash blowing and cleaning system according to claim 1, it is characterized in that: in inboard near inner coil pipe (6), compound heat-insulation layer (3) is arranged, and the thickness of compound heat-insulation layer (3) is 10~30 millimeters, and length is 500~1200 millimeters.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CNU200820123027XU CN201310875Y (en) | 2008-10-15 | 2008-10-15 | Fuel gas superheated steam generator with dust blowing and removing system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU200820123027XU CN201310875Y (en) | 2008-10-15 | 2008-10-15 | Fuel gas superheated steam generator with dust blowing and removing system |
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CN201310875Y true CN201310875Y (en) | 2009-09-16 |
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CNU200820123027XU Expired - Lifetime CN201310875Y (en) | 2008-10-15 | 2008-10-15 | Fuel gas superheated steam generator with dust blowing and removing system |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107054386A (en) * | 2017-04-06 | 2017-08-18 | 浙江水利水电学院 | Steam-powered tourist train drive system |
CN107089237A (en) * | 2017-04-06 | 2017-08-25 | 浙江水利水电学院 | Oil-engine driven tourist train drive system |
CN107388270A (en) * | 2017-08-09 | 2017-11-24 | 胜利油田华滨实业有限公司石油机械滨州分公司 | Wet steam generator convection section automatic ash blowing system |
CN107975789A (en) * | 2017-12-28 | 2018-05-01 | 无锡博勒能源科技有限公司 | A kind of DC low-voltage superhigh temperature steam superheating device and control method |
CN111076200A (en) * | 2019-11-25 | 2020-04-28 | 内蒙古大唐国际托克托发电有限责任公司 | Boiler hearth soot blowing device and soot blowing method thereof |
-
2008
- 2008-10-15 CN CNU200820123027XU patent/CN201310875Y/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107054386A (en) * | 2017-04-06 | 2017-08-18 | 浙江水利水电学院 | Steam-powered tourist train drive system |
CN107089237A (en) * | 2017-04-06 | 2017-08-25 | 浙江水利水电学院 | Oil-engine driven tourist train drive system |
CN107054386B (en) * | 2017-04-06 | 2020-02-21 | 浙江水利水电学院 | Steam-driven sightseeing train driving system |
CN107089237B (en) * | 2017-04-06 | 2020-02-28 | 浙江水利水电学院 | Sightseeing train driving system driven by internal combustion engine |
CN107388270A (en) * | 2017-08-09 | 2017-11-24 | 胜利油田华滨实业有限公司石油机械滨州分公司 | Wet steam generator convection section automatic ash blowing system |
CN107975789A (en) * | 2017-12-28 | 2018-05-01 | 无锡博勒能源科技有限公司 | A kind of DC low-voltage superhigh temperature steam superheating device and control method |
CN111076200A (en) * | 2019-11-25 | 2020-04-28 | 内蒙古大唐国际托克托发电有限责任公司 | Boiler hearth soot blowing device and soot blowing method thereof |
CN111076200B (en) * | 2019-11-25 | 2024-03-19 | 内蒙古大唐国际托克托发电有限责任公司 | Soot blower of boiler hearth and soot blowing method thereof |
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GR01 | Patent grant | ||
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CX01 | Expiry of patent term |
Granted publication date: 20090916 |