CN202164110U - Saline water pyrolyzer and energy-saving and emission-reducing boiler with same - Google Patents
Saline water pyrolyzer and energy-saving and emission-reducing boiler with same Download PDFInfo
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- CN202164110U CN202164110U CN201120233695XU CN201120233695U CN202164110U CN 202164110 U CN202164110 U CN 202164110U CN 201120233695X U CN201120233695X U CN 201120233695XU CN 201120233695 U CN201120233695 U CN 201120233695U CN 202164110 U CN202164110 U CN 202164110U
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- Prior art keywords
- boiler
- pyrolyzer
- emission
- saving
- energy
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- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 title abstract 4
- 239000011780 sodium chloride Substances 0.000 title abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title abstract 4
- 239000000463 material Substances 0.000 claims abstract description 21
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000001301 oxygen Substances 0.000 claims abstract description 13
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 13
- 238000002485 combustion reaction Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 20
- 239000012530 fluid Substances 0.000 claims description 16
- 239000012266 salt solution Substances 0.000 claims description 15
- 238000005336 cracking Methods 0.000 claims description 13
- 238000013461 design Methods 0.000 claims description 5
- 210000000038 chest Anatomy 0.000 claims description 3
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 3
- 150000002910 rare earth metals Chemical class 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 2
- 239000007769 metal material Substances 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 239000003245 coal Substances 0.000 abstract description 9
- 239000000446 fuel Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 abstract 3
- 239000007788 liquid Substances 0.000 abstract 3
- 238000006243 chemical reaction Methods 0.000 abstract 2
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 239000000919 ceramic Substances 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910018487 Ni—Cr Inorganic materials 0.000 description 1
- VNNRSPGTAMTISX-UHFFFAOYSA-N chromium nickel Chemical compound [Cr].[Ni] VNNRSPGTAMTISX-UHFFFAOYSA-N 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000013536 elastomeric material Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001360 synchronised 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Meat, Egg Or Seafood Products (AREA)
Abstract
The utility model discloses a saline water pyrolyzer and an energy-saving and emission-reducing boiler with the same. In the utility model, an oxidation body and an oxygen injecting head are arranged in a reaction tank of the saline water pyrolyzer; the reaction tank is provided with a material injecting pipe, a material injecting hopper and a liquid filtering conduit; a magnetizing device is arranged on an outer wall of the liquid filtering conduit; the tail end of the liquid filtering conduit is connected with a high-temperature pyrolyzer; a pyrolyzing steam pipe is arranged in the high-temperature pyrolyzer; the lower segment of the pyrolyzing steam pipe downwards protrudes out of a bottom wall of the high-temperature pyrolyzer; an air supply device is arranged below the high-temperature pyrolyzer; and the lower end of the pyrolyzing steam pipe is communicated with an air inlet pipe of the air supply device. When the saline water pyrolyzer disclosed by the utility model is adopted, coal combusting environment in the boiler is obviously improved; as fuel and gaseous combustion improver are supplied synchronously, coal can be combusted completely; and a multi-level and multilateral combustion-supporting means is realized through a plurality of links so that utilization rate of fuel is greatly increased, and the obvious effects of saving energy and reducing emission are achieved.
Description
Technical field
The utility model relates to a kind of salt solution cracker, and the utility model also relates to a kind of energy-saving and emission-reduction boiler that has this salt solution cracker.
Background technology
Be accompanied by the depleted day by day of the global energy, the price of crude oil and bunker coal is all rising violently for successive years fast, and these all are that modernized sustainable development of economy has caused huge obstruction.In order to alleviate this pressure, all among carrying out on a grand and spectacular scale, before mankind's energy substitution article that successfully exploitation does not make new advances, saving coal is the most important thing in our present each item work in countries in the world at present global energy-saving and emission-reduction campaign.The boiler that domestic production at present, life are used mostly is main fuel with coal, and all will consume a large amount of feed coals every day.According to incompletely statistics; The existing coal firing boiler great majority of China all do not reach best burning state; The equipment of many backwardnesss is also constantly received the yellow-card warning of environmental administration, this sight be we human existence present situation and our national conditions institute are flagrant fully now.These precious energy fullests of research and inquirement, the most effectively to utilize method be our the current top priority that will accomplish, and it is in short supply that this not only helps alleviating coal, but also help the improvement of human ecological environment.Therefore we must go into overdrive, and improve the rate of combustion of boiler by fair means or foul, make the national economy of China can stablize, advance constantly.
Summary of the invention
The goal of the invention of the utility model is to provide a kind of salt solution cracker, and this equipment can provide economic hydrogen and oxygen for boiler fully burns.The another one goal of the invention of the utility model also is to provide a kind of energy-saving and emission-reduction boiler that has this salt solution cracker.
The salt solution cracker of the utility model comprises the retort of a sealing, oxysome is housed in it and annotates the oxygen head, annotates the oxygen head and is connected with the outer notes oxygen pump of tank body through pipeline; Side bottom in retort is equipped with filling tube, and filling tube is bent upwards with the material feeding bucket and is connected, and outside tank body, also is provided with observation tube; The fluid catheter of crossing of non-metallic material also is housed in the bottom of retort, on the outer wall of crossing fluid catheter, the magnetizing assembly of being processed by some group rare-earth permanent magnets is housed, the end of crossing fluid catheter is connected with the Pintsch process device; The Pintsch process device is a cylindricality seal case, and the cracking vapour pipe of upright setting is housed in the casing, and the hypomere of cracking vapour pipe stretches out downwards from the diapire of Pintsch process device; Below the Pintsch process device, be provided with the air supply device of being made up of blast pipe and pneumatic pump, the lower end of cracking vapour pipe communicates with blast pipe.
Above-mentioned design can be installed in the casing, on the outer wall of casing, facility switching is housed.
The structure that has the energy-saving and emission-reduction boiler of above-mentioned salt solution cracker is: above-mentioned Pintsch process device is installed on the thorax wall of fire grate top in the boiler furnace, and the outer wall that the rear of mistake fluid catheter passes boiler is connected with the Pintsch process device; The pneumatic pump of air supply device was installed in the below of fluid catheter, and blast pipe passes the below of the outer wall entering fire grate of boiler, and the cracking vapour pipe passes fire grate and is connected with blast pipe.
On the inwall of burner hearth, can also be provided with the far-infrared ray material liner, this far-infrared ray material liner is mixed and made into by far infrared ceramic powder and clay, and its thickness the best is 15-20cm.
Above burner hearth internal combustion district, also be provided with one deck far-infrared ray material net.
The salt solution cracker of the utility model has obviously improved the burning situation of coal in the boiler, through the synchronous supply of fuel and ignition dope gas, makes coal can access the most fully, burn completely.Because the employed salt solution of this equipment or seawater are a kind of inexhaustible cheap natural resource, thereby it is low to have a cost, the characteristic that efficient is high.Because fuel and ignition dope gas are that this not only makes the structure of equipment simpler by means of the environment generation of natural magnetic field and boiler itself in this equipment, compactness, and also the cost of making is able to reduce widely.In the design's energy-saving and emission-reduction boiler,, can make the temperature in the burner hearth more even, eliminate aflame dead angle owing to be provided with the far-infrared ray material liner.The infrared material net of burner hearth top can make some also burnt completely by the dust of carried away by air movement, short grained fuel.The utility model has constituted multi-level, multi-faceted combustion-supporting means from several links, has improved the utilization ratio of fuel widely, has received very considerable energy saving emission reduction effect.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is specified.
Fig. 1 is the structural representation of the utility model.
Fig. 2 is the structural representation of embodiment 2.
Label among the figure:
1, retort 2, oxysome 3, notes oxygen head 4, notes oxygen pump 5, filling tube
6, material feeding bucket 7, observation tube 8, mistake fluid catheter 9, magnetizing assembly 10, Pintsch process device
11, cracking vapour pipe 12, blast pipe 13, pneumatic pump 14, facility switching 15, casing
16, fire grate 17, far-infrared ray material liner 18, far-infrared ray material net.
Embodiment
Example 1
As shown in Figure 1, the design's salt solution cracker comprises retort 1, and this retort 1 is a closed container, oxysome 2 is housed in it and annotates oxygen head 3, annotates oxygen head 3 and is connected with the outer notes oxygen pump 4 of tank body through pipeline.Described oxysome 2 is learned material for oxygenerating, is prior art.
Side bottom in retort 1 is equipped with filling tube 5, and filling tube 5 is bent upwards with material feeding bucket 6 and is connected, and outside tank body, also is provided with observation tube 7.Observation tube 7 is located between filling tube 5 and the material feeding bucket 6.In the bottom of retort 1 fluid catheter of processing with elastomeric material 8 excessively is housed also, with the magnetizing assembly of being processed by some group rare-earth permanent magnets 9, the end of crossing fluid catheter 8 is connected with Pintsch process device 10 on the outer wall of crossing fluid catheter 8.Pintsch process device 10 is a cylindricality seal case, and the cracking vapour pipe 11 of upright setting is housed in the casing, and the hypomere of cracking vapour pipe 11 stretches out downwards from the diapire of Pintsch process device 10.Below Pintsch process device 10, be provided with the air supply device of being made up of blast pipe 12 and pneumatic pump 13, the lower end of cracking vapour pipe 11 communicates with the blast pipe of this air supply device 12.Above-mentioned design and installation is equipped with facility switching 14 on casing 15 outer walls in a casing 15.
Example 2
As shown in Figure 1, this example is for having the energy-saving and emission-reduction boiler of this salt solution cracker, and the Pintsch process device 10 in the example 1 is installed on the thorax wall of fire grate 16 tops in the boiler furnace, and the outer wall that the rear of mistake fluid catheter 8 passes boiler is connected with Pintsch process device 10.The pneumatic pump 13 of air supply device was installed in the below of fluid catheter 8, and blast pipe 12 passes the below of the outer wall entering fire grate 16 of boiler, and cracking vapour pipe 11 passes fire grate 16 and is connected with blast pipe 12.
On the inwall of burner hearth, also be provided with far-infrared ray material liner 17.This far-infrared ray material liner 17 is mixed and made into by far infrared ceramic powder and clay, and its thickness is 20cm.
Above burner hearth internal combustion district, also be provided with one deck far-infrared ray material net 18, the staple of its employed far-infrared ray material is a nickel chromium triangle.See Fig. 2.
Claims (5)
1. salt solution cracker, it is characterized in that: this salt solution cracker comprises the retort (1) of a sealing, oxysome (2) is housed in it and annotates oxygen head (3), annotates oxygen heads (3) and is connected with tank body notes oxygen pump (4) outward through pipeline; Side bottom in retort (1) is equipped with filling tube (5), and filling tube (5) is bent upwards with material feeding bucket (6) and is connected, and outside tank body, also is provided with observation tube (7); The fluid catheter (8) excessively of non-metallic material also is housed in the bottom of retort (1), on the outer wall of crossing fluid catheter (8), the magnetizing assembly of being processed by some group rare-earth permanent magnets (9) is housed, the end of crossing fluid catheter (8) is connected with Pintsch process device (10); Pintsch process device (10) is a cylindricality seal case, and the cracking vapour pipe (11) of upright setting is housed in the casing, and the hypomere of cracking vapour pipe (11) stretches out downwards from the diapire of Pintsch process device (10); Be provided with the air supply device of being made up of blast pipe (12) and pneumatic pump (13) in the below of Pintsch process device (10), the lower end of cracking vapour pipe (11) communicates with blast pipe (12).
2. salt solution cracker according to claim 1 is characterized in that: above-mentioned design and installation is equipped with facility switching (14) on the outer wall of casing (15) in a casing (15).
3. one kind has the energy-saving and emission-reduction boiler of salt solution cracker according to claim 1; It is characterized in that: described Pintsch process device (10) is installed on the thorax wall of fire grate (16) top in the boiler furnace, and the outer wall that the rear of mistake fluid catheter (8) passes boiler is connected with Pintsch process device (10); The pneumatic pump of air supply device (13) was installed in the below of fluid catheter (8), and blast pipe (12) passes the below of the outer wall entering fire grate (16) of boiler, and cracking vapour pipe (11) passes fire grate (16) and is connected with blast pipe (12).
4. energy-saving and emission-reduction boiler according to claim 3 is characterized in that: on the inwall of burner hearth, also be provided with far-infrared ray material liner (17).
5. according to claim 3 or 4 described energy-saving and emission-reduction boilers, it is characterized in that: above burner hearth internal combustion district, also be provided with one deck far-infrared ray material net (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120233695XU CN202164110U (en) | 2011-07-05 | 2011-07-05 | Saline water pyrolyzer and energy-saving and emission-reducing boiler with same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120233695XU CN202164110U (en) | 2011-07-05 | 2011-07-05 | Saline water pyrolyzer and energy-saving and emission-reducing boiler with same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202164110U true CN202164110U (en) | 2012-03-14 |
Family
ID=45799952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120233695XU Expired - Fee Related CN202164110U (en) | 2011-07-05 | 2011-07-05 | Saline water pyrolyzer and energy-saving and emission-reducing boiler with same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202164110U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102620283A (en) * | 2012-03-26 | 2012-08-01 | 北京中煤神州节能环保技术开发有限公司 | Energy saving system and method for clean burning of layer burning boiler |
| CN104807001A (en) * | 2015-05-13 | 2015-07-29 | 张宝生 | Hydrolysis combustion device for improving thermal efficiency inside boiler |
-
2011
- 2011-07-05 CN CN201120233695XU patent/CN202164110U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102620283A (en) * | 2012-03-26 | 2012-08-01 | 北京中煤神州节能环保技术开发有限公司 | Energy saving system and method for clean burning of layer burning boiler |
| CN102620283B (en) * | 2012-03-26 | 2014-11-19 | 北京中煤神州节能环保技术开发有限公司 | Energy saving system and method for clean burning of layer burning boiler |
| CN104807001A (en) * | 2015-05-13 | 2015-07-29 | 张宝生 | Hydrolysis combustion device for improving thermal efficiency inside boiler |
| CN104807001B (en) * | 2015-05-13 | 2017-07-28 | 中海国利环保科技有限公司 | Water decomposition burner for improving boiler internal thermal effect |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHUHAI LVFENGZHOU TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: GU QINGQUAN Effective date: 20140702 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20140702 Address after: 519000, No. 1, Da Ha Road, Tang Wan Town, Guangdong, Zhuhai, -4-A102 Patentee after: Zhuhai green continent Technology Co., Ltd. Address before: 1303 room 78, building 1, 519000 Zhuhai Avenue, Xiangzhou District, Guangdong, Zhuhai Patentee before: Gu Qingquan |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120314 Termination date: 20150705 |
|
| EXPY | Termination of patent right or utility model |