CN201724384U - Energy-saving environment-friendly high temperature jet type hot blast stove - Google Patents
Energy-saving environment-friendly high temperature jet type hot blast stove Download PDFInfo
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- CN201724384U CN201724384U CN2009202025027U CN200920202502U CN201724384U CN 201724384 U CN201724384 U CN 201724384U CN 2009202025027 U CN2009202025027 U CN 2009202025027U CN 200920202502 U CN200920202502 U CN 200920202502U CN 201724384 U CN201724384 U CN 201724384U
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- 239000002918 waste heat Substances 0.000 claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000004062 sedimentation Methods 0.000 claims abstract description 11
- 239000000779 smoke Substances 0.000 claims description 46
- 238000002485 combustion reaction Methods 0.000 claims description 6
- 235000019504 cigarettes Nutrition 0.000 claims 4
- 238000011084 recovery Methods 0.000 abstract description 25
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 11
- 239000003546 flue gas Substances 0.000 abstract description 11
- 239000002245 particle Substances 0.000 abstract description 4
- 238000009776 industrial production Methods 0.000 abstract description 3
- 241001122767 Theaceae Species 0.000 abstract description 2
- 239000003814 drug Substances 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 230000006698 induction Effects 0.000 description 9
- 239000000428 dust Substances 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 239000011449 brick Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 101100484380 Fowlpox virus (strain NVSL) FPV061 gene Proteins 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- 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
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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Abstract
一种节能环保高温喷流式热风炉,涉及与工业生产线配套使用的茶叶、医药、化工、食品等的加热生产设备。热风炉由炉体连接余热回收器,余热回收器连接沉降水浴除尘池构成;炉体的出烟口连接送烟管,送烟管与余热回收器的下烟道连接,余热回收器的出烟管与烟囱连接,烟囱与沉降水浴除尘池连接。本实用新型可将日常排出的400℃左右的烟气降至100℃-130℃左右,减少了热污染,提高了热效率。炉体的炉芯设有喷流环,使空气得以加速热交换,如对流和传导的。沉降水浴除尘池配有颗料沉降室,可将40μ以上颗料经三次沉降后排出烟道,再经水浴室沉淀处理排放。
An energy-saving and environment-friendly high-temperature jet-flow hot blast furnace relates to heating production equipment for tea, medicine, chemical industry, food, etc. used in conjunction with industrial production lines. The hot blast stove is composed of a furnace body connected to a waste heat recovery device, and the waste heat recovery device is connected to a sedimentation water bath dedusting pool; The pipe is connected with the chimney, and the chimney is connected with the sedimentation water bath dedusting tank. The utility model can reduce the flue gas discharged daily at about 400°C to about 100°C-130°C, thereby reducing thermal pollution and improving thermal efficiency. The furnace core of the furnace body is provided with a jet flow ring, so that the air can accelerate heat exchange, such as convection and conduction. The settling water bath dedusting tank is equipped with a particle settling chamber, which can discharge the particles above 40μ out of the flue after three times of settling, and then discharge through the water bath settling treatment.
Description
技术领域technical field
本实用新型的节能环保高温喷流式热风炉涉及与工业生产线配套使用的茶叶、医药、化工、食品等的加热生产设备,输出温度可达280-380℃。 The energy-saving and environment-friendly high-temperature jet flow hot air stove of the utility model relates to heating production equipment for tea, medicine, chemical industry, food, etc. used in conjunction with industrial production lines, and the output temperature can reach 280-380°C. the
背景技术Background technique
热风炉在市场上使用较广泛,但是要解决高温输出,满足工业生产需要,仍是个大家探究的疑难问题,如FP14高温炉,其热转换不够合理,烟气带走的余热在300-400℃左右,其浪费了资源,散失了大量的可利用热源,对环保造成了热污染,不值得提倡。 Hot blast stoves are widely used in the market, but it is still a difficult problem for everyone to solve high-temperature output and meet the needs of industrial production. For example, the heat conversion of FP14 high-temperature stove is not reasonable enough, and the waste heat taken away by the flue gas is at 300-400°C Left and right, it wastes resources, loses a lot of available heat sources, and causes thermal pollution to environmental protection, which is not worth promoting. the
发明内容Contents of the invention
本实用新型而提供一种节能环保的高温喷流式热风炉。 The utility model provides an energy-saving and environment-friendly high-temperature jet-flow hot blast stove. the
本实用新型是通过如下技术方案来实现的:它包括:余热回收器,送烟管、出烟管、烟囱撑、烟囱、沉降水浴除尘池、引烟电机、引烟风机、炉体、调风管、引风机、引风管、炉体进风管、热风管组成,其中所述炉体由炉门、底盘、壳体、炉芯、喷流环、助燃风口、风道、烟道、膨胀圈、炉体进风口、出烟口、热风出口、炉桥、耐火砖、底座等组成;所述余热回收器由下烟道、上烟道、下风道、上风道、风道回流仓、烟道回流仓等组成。 The utility model is realized through the following technical scheme: it includes: a waste heat recovery device, a smoke delivery pipe, a smoke outlet pipe, a chimney support, a chimney, a settling water bath dust removal pool, a smoke induction motor, a smoke induction fan, a furnace body, and an air conditioning Pipe, induced fan, induced air pipe, furnace body air inlet pipe, hot air pipe, wherein the furnace body is composed of furnace door, chassis, shell, furnace core, jet ring, combustion air outlet, air duct, flue, Expansion ring, furnace body air inlet, smoke outlet, hot air outlet, furnace bridge, refractory bricks, base, etc.; the waste heat recovery device consists of lower flue, upper flue, lower air duct, upper air duct, air duct return chamber, Flue return chamber and other components. the
所述热风炉由炉体连接余热回收器,余热回收器连接沉降水浴除尘池构成;炉体的出烟口连接送烟管,送烟管与余热回收器的下烟道连接,余热回收器的出烟管与烟囱连接,烟囱与沉降水浴除尘池连接; The hot blast stove is composed of a furnace body connected to a waste heat recovery device, and the waste heat recovery device is connected to a sedimentation water bath dust removal pool; the smoke outlet of the furnace body is connected to a smoke delivery pipe, and the smoke delivery pipe is connected to the lower flue of the waste heat recovery device. The outlet pipe is connected to the chimney, and the chimney is connected to the sedimentation water bath dust removal tank;
所述的炉体由炉门、底盘、壳体、炉芯,风道、烟道构成,炉桥设在炉芯内,喷流环设在炉芯的外面,在喷流环与风道之间设有烟道;底盘上设有烟环与热风环;所述烟环与出烟口相连接,所述热风环与热风出口相连接;出烟口与送烟管相连接;热风出口与热风管相连接;壳体设在最外层;炉桥的前后成180度设有炉门和热风出口,出烟口设在热风出口之下;炉体进风口设在炉体底座的一侧; The furnace body is composed of a furnace door, a chassis, a shell, a furnace core, an air duct, and a flue. There is a flue between them; a smoke ring and a hot air ring are arranged on the chassis; the smoke ring is connected to the smoke outlet, and the hot air ring is connected to the hot air outlet; the smoke outlet is connected to the smoke delivery pipe; the hot air outlet is connected to the The hot air pipes are connected; the shell is set on the outermost layer; the front and back of the furnace bridge are 180 degrees with a furnace door and a hot air outlet, and the smoke outlet is set under the hot air outlet; side;
炉芯与烟道相连接处设有膨胀圈; There is an expansion ring at the connection between the furnace core and the flue;
所述余热回收器设有上下两层,在上下层交汇处设有烟气回流仓和空气回流仓。 The waste heat recovery device is provided with upper and lower floors, and a flue gas return chamber and an air return chamber are arranged at the junction of the upper and lower floors. the
本实用新型炉芯顶部设有四个膨胀圈来解决炉芯因热膨胀对其配合尺寸制约的补偿。余热回收器,采用列管式余热传导的方式进行余热回收的。余热回收器包括下烟道和上烟道,烟气从下烟道经烟道回流仓进入上烟道;冷风由下风道经风道回流仓进入上风道进行热交换的。余热回收器可将日常排出的400℃左右的烟气降至100℃-130℃左右,减少了热污染,搞高了热效率。炉体的炉芯设有喷流环,使空气得以加速热交换,如对流和传导的。喷流环设有无数多个小孔方便进行热交换,在喷流环下部设有对称的缺口以方便热空气汇聚。采用高温处喷流换热,低温处对流换热,使设计更合理,热效率更高。沉降水浴除尘池配有颗料沉降室,可将40μ以上颗料经三次沉降后排出烟道,再经水浴室沉淀处理排放。 The top of the furnace core of the utility model is provided with four expansion rings to solve the compensation for the restriction of the furnace core due to thermal expansion to its matching size. The waste heat recovery device adopts the tube-type waste heat conduction method for waste heat recovery. The waste heat recovery device includes a lower flue and an upper flue. The flue gas enters the upper flue from the lower flue through the flue return bin; the cold air enters the upper flue from the lower flue through the air return bin for heat exchange. The waste heat recovery device can reduce the flue gas discharged daily at about 400°C to about 100°C-130°C, reducing thermal pollution and improving thermal efficiency. The furnace core of the furnace body is provided with a jet flow ring, so that the air can accelerate heat exchange, such as convection and conduction. The jet ring is provided with countless small holes to facilitate heat exchange, and symmetrical gaps are provided at the lower part of the jet ring to facilitate hot air convergence. Jet flow heat exchange at high temperature and convection heat exchange at low temperature make the design more reasonable and the thermal efficiency higher. The settling water bath dedusting tank is equipped with a particle settling chamber, which can discharge the particles above 40μ out of the flue after three times of settling, and then discharge through the water bath settling treatment. the
附图说明Description of drawings
图1是本实用新型的主视图; Fig. 1 is the front view of the utility model;
图2是本实用新型的俯视图; Fig. 2 is the top view of the utility model;
图3是本实用新型的后视图; Fig. 3 is the back view of the utility model;
图4是本实用新型炉体主剖视图; Fig. 4 is the main sectional view of the furnace body of the present utility model;
图5是本实用新型炉体的A-A剖视图; Fig. 5 is the A-A sectional view of body of heater of the present utility model;
图6是本实用新型炉体的B-B剖视图; Fig. 6 is the B-B sectional view of body of heater of the present utility model;
图7是本实用新型炉体的C-C剖视图; Fig. 7 is the C-C sectional view of body of heater of the present utility model;
图8是本实用新型喷流环的展开零件图; Fig. 8 is the unfolded part diagram of the utility model spray ring;
图9是本实用新型余热回收器主剖视图; Fig. 9 is the main sectional view of the utility model waste heat recovery device;
图10是本实用新型余热回收器D-D剖视图; Figure 10 is a D-D cross-sectional view of the waste heat recovery device of the present utility model;
图11是本实用新型沉降水浴除尘池主剖视图。 Fig. 11 is a main sectional view of the sedimentation water bath dedusting tank of the present invention. the
具体实施方式Detailed ways
下面通过实施例,并结合附图,对本实用新型的技术方案作进一步具体的说明。 The technical solutions of the present utility model will be further specifically described below through the embodiments and in conjunction with the accompanying drawings. the
实施例1:如图1,图2,图3,图4,图6,图9,图10,图11所示,本实用新型主要包括余热回收器1,送烟管2、出烟管3、烟囱撑4、烟囱5、沉降水浴除尘池6、引烟电机7、引烟风机8、炉体9、调风管10、引风机11、引风管12、炉体进风管13、热风管14。所述炉体主要包括炉门901、底盘902、壳体903、炉芯904、喷流环905、助燃风口906、风道907、烟道908、膨胀圈909、炉体进风口910、出烟口911、炉桥912、耐火砖913、底座914、热风出口915等;所述余热回收器1主要包括烟道101包括下烟道1011和上烟道1012、风道102包括下风道1021和上风道1022、风道回流仓103、烟道回流仓104;所述底盘902包括烟环9021和热风环9023。 Embodiment 1: As shown in Figure 1, Figure 2, Figure 3, Figure 4, Figure 6, Figure 9, Figure 10, and Figure 11, the utility model mainly includes a waste
所述炉体9的出烟口911与送烟管2相连,炉体9的炉体进风口910与进风口13相连。所述送烟管2与余热回收器1的下烟道1011相接,余热回收器1的上烟道1012与出烟管3相连接。所述引烟电机7与引烟风机8相连接。所述引烟风机电与出烟管3相连接。所述出烟管3与烟囱5经烟囱撑4相连接。所述烟囱5与沉降除尘池相接。所述调风管10与余热回收器1的下风道1021相连接。所述余热回收器1的上风道1021经引风机11与炉体进风管13相连接。所述热风管14与炉体9热风出风口915相连接。所述余热回收器1风上下两层,下层分别进冷空气和烟气,在所述烟气和空气上下层交汇处设有烟气回流仓104和空气回流仓103。所述炉体9是这样组成的,所述炉桥912设在炉芯904内,所述炉芯主要由耐火砖913等耐高温材料制成。所述喷流环905设在炉芯904的外面,所述烟道908设在喷流环905与风道907之间。所述膨胀圈909设在炉芯904上与烟道908相连接处,烟直至底盘902汇集上。所述底盘902上设有烟环9021与热风环9023。所述烟环9021与出烟口911相连接,所述热风环9022与热风出口915相连接。所述出烟口911与送烟管2相连接直至余热回收器1进行热交换。所述热风出口915与热风管14相连接提供给所需要热风的对象。在所述壳体903设在最外层,隔绝了外界空气与炉内空气的热交换。在所述炉桥912的前后成180度设有炉门901和热风出口915,出烟口设在热风出口之下。所述炉体进风口设在炉体底座914的一侧。 The
在本实用新型使用的时候,煤由炉门901进入,燃烧在炉桥912上,烧热了炉芯904,启动引风机11和引烟风机8,在大气压的作用下空气进入了调风管10,由调风管10进入余热回收器1的下风道1021经风道回流仓103进入上风道1022,由上风道1022经引风机11从炉体进风口910底部进入风道907,空气在风道内主要进行着与烟道908的热传导交换,当空气进入炉芯顶部904与和膨胀圈909时,空气从喷流环905向下行走,边喷射在炉芯904与烟道908之间主要进行着热对流交换,最后空气底达炉盘902处汇集由热风管14排出热风。助然空气从炉体底部透过炉桥912进入炉芯904,参和炉内烟气一道由膨胀圈909抽出经烟道908释放热量流至底盘902的烟环9021,经送烟管2送至余热回收器1的下烟道101,穿过下烟道101汇集在烟道回流仓104内,再经上烟道送至出烟管3,经引烟风机8抽出至烟囱5,经过烟囱5的烟气由沉降水浴除尘池6处理进行两次沉降除渣之后排放入大气。 When the utility model is in use, coal enters through the
本实用新型的节能环保高温喷流式热风炉可提供280℃-390℃食品加工所需要的温度,烟气经余热回收后所排放的烟气温度在90℃-110℃之间。 The energy-saving and environment-friendly high-temperature jet-flow hot blast stove of the utility model can provide the temperature required for food processing at 280°C-390°C, and the temperature of the flue gas discharged after the waste heat recovery is between 90°C-110°C. the
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104194397A (en) * | 2014-09-05 | 2014-12-10 | 山西青山化工有限公司 | Reaction device and process for reducing loss of cyanuric chloride in synthesis of fluorescent brightener |
| CN105509312A (en) * | 2016-01-20 | 2016-04-20 | 霍山县叶王农机制造有限公司 | Jet boiler |
| CN107202423A (en) * | 2017-07-11 | 2017-09-26 | 叶培科 | A kind of heat-exchange system based on hot-blast stove |
| CN108036651A (en) * | 2017-10-10 | 2018-05-15 | 东旭科技集团有限公司 | Glass furnace fume export structure |
| CN111765633A (en) * | 2020-06-18 | 2020-10-13 | 富阳三凌机械制造有限公司 | Biomass particle hot blast stove |
-
2009
- 2009-12-17 CN CN2009202025027U patent/CN201724384U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104194397A (en) * | 2014-09-05 | 2014-12-10 | 山西青山化工有限公司 | Reaction device and process for reducing loss of cyanuric chloride in synthesis of fluorescent brightener |
| CN104194397B (en) * | 2014-09-05 | 2016-02-17 | 山西青山化工有限公司 | Reaction device and process for reducing the loss of cyanuric chloride in the synthesis of fluorescent whitening agents |
| CN105509312A (en) * | 2016-01-20 | 2016-04-20 | 霍山县叶王农机制造有限公司 | Jet boiler |
| CN107202423A (en) * | 2017-07-11 | 2017-09-26 | 叶培科 | A kind of heat-exchange system based on hot-blast stove |
| CN107202423B (en) * | 2017-07-11 | 2022-05-31 | 肇庆市元科机械科技有限公司 | Heat exchange system based on hot blast stove |
| CN108036651A (en) * | 2017-10-10 | 2018-05-15 | 东旭科技集团有限公司 | Glass furnace fume export structure |
| CN108036651B (en) * | 2017-10-10 | 2019-06-07 | 东旭科技集团有限公司 | Glass furnace fume export structure |
| CN111765633A (en) * | 2020-06-18 | 2020-10-13 | 富阳三凌机械制造有限公司 | Biomass particle hot blast stove |
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