CN203478306U - Power plant carbon and oxygen recycling device - Google Patents
Power plant carbon and oxygen recycling device Download PDFInfo
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- CN203478306U CN203478306U CN201320546359.XU CN201320546359U CN203478306U CN 203478306 U CN203478306 U CN 203478306U CN 201320546359 U CN201320546359 U CN 201320546359U CN 203478306 U CN203478306 U CN 203478306U
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/32—Direct CO2 mitigation
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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
- Y02P20/00—Technologies relating to chemical industry
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Abstract
The utility model relates to the field of energy saving and environmental protection and recycling of CO2 and O2, particularly to a power plant carbon and oxygen recycling device. The power plant carbon and oxygen recycling device comprises a coal feeder (17), a CO2 refluxing device (6), a plasma torch catalyst (1), an energy-saving boiler (2), a heat exchanger (3), a CO2 collecting separator (12), a deaerator (14), a remote anti-explosion master control detecting system (18) and a chimney (13). The power plant carbon and oxygen recycling device has the advantages of achieving low-cost pure oxygen combustion, achieving CO2 reflux catalyzing and deaeration recycling, reducing equipment investment and the volume of the boiler and equipment used in procedures such as dedusting, denitration and desulfuration by 70-80%, saving coal consumption by 45-70% and improving the heat energy net conversion rate to be more than doubled.
Description
Technical field
The utility model relates to energy-conserving and environment-protective field, relates to recycling of CO2 and O2, relates in particular to power plant's carbon oxygen cycle use device.
Background technology
Power plant's generating produces greenhouse effects arch-criminal CO2, is unfavorable for existing environmental requirement, and existing traditional power plant technology, except IGCC generating, also exists following defect simultaneously:
1, air burning, the clean low conversion rate of heat energy, key reaction formula is: C+O2+N2---CO2+N2;
The 1 ton of mark coal that burns needs approximately 2.7 tons of O2, and brings approximately 10 tons of N2 into, in burning and exhausting flue gas, and N2 content 78-85%, CO2 content is 8-15% only.In flue gas, N2 content is high, and the one, cause the immediate cause of the clean low conversion rate of heat energy, the 2nd, cause the conveyance system volumes of equipment such as boiler and dedusting, denitration, desulfurization, chimney large, waste power plant's cost of investment and operating cost.
2, the CO2 wasting of resources, contaminated environment: because CO2 content is too low in flue gas, strengthen CO2 trapping cost, cause power plant's CO2 resource generally to waste.
3, thermal loss is large, the clean low conversion rate of heat energy: the heat energy of 500-1000 ℃ in traditional power-plant flue gas, and almost in dedusting, denitration, sweetening process, all consumed and fallen by smoke stack emission, be to cause the clean low conversion rate of power plant's heat energy in 40% one of the main reasons.
Therefore in energy-saving and emission-reduction, improve the main development direction that the clean conversion ratio of heat energy is existing power plant.
Utility model content
The utility model is to overcome above-mentioned weak point, and object is to provide power plant's carbon oxygen cycle use device, solves the problems such as existing power plant heat energy low conversion rate, CO2 and the O2 wasting of resources, contaminated environment, realizes power plant's carbon oxygen cycle utilization, improves heat energy conversion ratio.
The utility model is to achieve the above object by the following technical programs: power plant's carbon oxygen cycle use device, comprising: the device of delivering coal, CO2 return channel, plasmatorch catalyst converter, power economized boiler, heat exchanger, CO2 trapping separator, degasifier, long-range explosion-proof master control detection system, chimney; Described plasmatorch catalyst converter one end connects deliver coal device, CO2 return channel, the other end is communicated with the gas approach of power economized boiler bottom, power economized boiler top is provided with outlet, the outlet on top is communicated with CO2 return channel, power economized boiler bottom is also provided with exhanst gas outlet, and the exhanst gas outlet of bottom is connected with the gas approach flue of heat exchanger; The exhanst gas outlet flue of described heat exchanger is connected with CO2 trapping separator, and CO2 trapping separator is connected with the oxygen feeder of heat exchanger by degasifier, air blast, and degasifier is connected with carbon recover, and CO2 trapping separator is also connected with chimney; Described long-range explosion-proof master control detection system is connected with each device and detects in real time.
As preferably, power plant's carbon oxygen cycle use device also includes system for desulfuration and denitration, and described system for desulfuration and denitration comprises desulfurizer, denitrification apparatus; Desulfurizer is communicated between the exhanst gas outlet flue and CO2 trapping separator of heat exchanger, and described denitrification apparatus is arranged between the outlet and CO2 return channel on power economized boiler top; Described desulfurizer comprises: deduster, air-introduced machine, desulfurization slag liquid, desulfurizing tower, heat exchanger, the exhanst gas outlet flue of described heat exchanger is connected with CO2 trapping separator by deduster, air-introduced machine, desulfurization slag liquid, desulfurizing tower, heat exchanger successively.
As preferably, power plant's carbon oxygen cycle use device also includes steam case, clarifier, sulfur-based compound fertilizer production line, and described steam case is communicated with power economized boiler and booster fan, and booster fan is communicated with CO2 return channel and plasmatorch catalyst converter; Described clarifier is communicated with exhanst gas outlet flue and the CO2 trapping separator of heat exchanger, and described clarifier is also connected with sulfur-based compound fertilizer production line.
As preferably, described plasmatorch catalyst converter comprises: hollow cathode base, concavo-convex negative electrode, an anode, two anodes, long pressurization cylinder, negative electrode cooling circulating water, anode cooling circulating water, long pressurization cylinder cooling circulating water, carrier wind, electrode catalyst core, insulator, dc source, high-voltage pulse power source, high-voltage pulse device; Described carrier wind comprises: first via carrier wind, the second road carrier wind, Third Road carrier wind, tetra-road carrier wind, five road carrier winds; Described hollow cathode base, concavo-convex negative electrode, an anode, two anodes, long pressurization cylinder are arranged in order and are symmetrical, the negative electrode of described dc source is connected with the hollow cathode base of a side, concavo-convex negative electrode, an anode of the anode of dc source and homonymy, two anodic bondings; The negative electrode of described high-voltage pulse power source is connected with the hollow cathode base of opposite side, concavo-convex negative electrode, an anode of the anode of high-voltage dc pulse power and homonymy, two anodic bondings; Cellular electrode catalyst core is inserted in plasmatorch catalyst converter central authorities, and one end is connected with high-voltage pulse device by insulator; Negative electrode cooling circulating water flow through the hollow cathode base of the left and right sides, concavo-convex negative electrode, anode cooling circulating water flow through an anode, two anodes of the left and right sides, the translateral long pressurization cylinder of long pressurization cylinder cooling circulating water stream.
As preferably, described power economized boiler comprises: send oxygen device, ,Shang booster zone, ,Zhong Ciran district, lower primary zone; ,Shang booster zone, ,Zhong Ciran district, described lower primary zone is located in the combustion chamber of power economized boiler from the bottom up successively, send oxygen device to be located at power economized boiler bottom and is connected with the oxygen exhaust of heat exchanger.
As preferably, described degasifier comprises: O2 air accumulator, high frequency waveforms device, high frequency pulse power supply, degasifier shell, insulator, electrode cores, explosion-proof sensor, infrared sensing viewer; Described degasifier shell bottom is connected with carbon recover, degasifier shell bottom is connected with CO2 trapping separator, degasifier shell top is connected with O2 air accumulator, degasifier shell top is provided with insulator, insulator is provided with electrode cores, one end that insulator is positioned at degasifier shell outside is connected with high frequency waveforms device, and high frequency pulse power supply is connected with high frequency waveforms device; Described explosion-proof sensor, infrared sensing viewer are located at respectively the top and bottom of degasifier, detect deoxidation process.
The beneficial effects of the utility model are: the one, and low-cost pure oxygen burning, the 2nd, CO2 backflow catalysis and deoxidation recycle, the 3rd, reduce equipment investment, reduce the link volume of equipment 70-80% such as boiler and dedusting, denitration, desulfurization, the 4th, the 45-70% that is sparing in the use of coal, the 5th, the clean conversion ratio of heat energy improves more than 1 times.
Accompanying drawing explanation
Fig. 1 is the structural representation of power plant's carbon oxygen cycle use device of embodiment 1;
Fig. 2 is the structural representation of power plant's carbon oxygen cycle use device of embodiment 2;
Fig. 3 is the structural representation of plasmatorch catalyst converter;
Fig. 4 is the structural representation of power economized boiler;
Fig. 5 is the structural representation of degasifier.
The specific embodiment
Below in conjunction with specific embodiment, the utility model is described further, but protection domain of the present utility model is not limited in this:
Embodiment 1: as shown in Figure 1, power plant's carbon oxygen cycle use device is comprised of the device 17 of delivering coal, CO2 return channel 6, plasmatorch catalyst converter 1, power economized boiler 2, denitrator 5, heat exchanger 3, deduster 7, booster fan 16, air-introduced machine 8, desulfurization slag liquid 10, desulfurizing tower 11, heat exchanger 9, CO2 trapping separator 12, degasifier 14, air blast 4, carbon recover 15, long-range explosion-proof master control detection system 18, chimney 13; Described plasmatorch catalyst converter 1 one end connects deliver coal device 17, CO2 return channel 6, the other end is communicated with the gas approach of power economized boiler 2 bottoms, power economized boiler 2 tops are provided with outlet, the outlet on top is communicated with CO2 return channel 6, power economized boiler 2 bottoms are also provided with exhanst gas outlet, and the exhanst gas outlet of bottom is connected with the gas approach flue of heat exchanger 3; The exhanst gas outlet flue of described heat exchanger 3 is connected with CO2 trapping separator 12, CO2 trapping separator 12 is connected with the oxygen feeder of heat exchanger 3 by degasifier 14, air blast 4, degasifier 14 is connected with carbon recover 15, and CO2 trapping separator 12 is also connected with chimney 13; Described long-range explosion-proof master control detection system 18 is connected with each device and detects in real time; Described denitrator 5 is arranged between the outlet and CO2 return channel 6 on power economized boiler 2 tops; The exhanst gas outlet flue of described heat exchanger 3 is connected with CO2 trapping separator 12 by deduster 7, air-introduced machine 8, desulfurization slag liquid 10, desulfurizing tower 11, heat exchanger 9 successively.
Concrete operations comprise:
The first step: open long-range explosion-proof master control monitoring system 18 switches.And by operational procedure, open each system switching successively;
Second step: start CO2 return channel 6 use CO2 the coal dust of delivering coal in device 17 is sent into 1 catalysis of plasmatorch catalyst converter, complete CO2+C(coal)---CO reaction, CO is sent into power economized boiler 2 with fully burning with O2;
The 3rd step: the rear 600-800 ℃ of flue gas CO2 part of power economized boiler 2 burning returned to CO2 return channel 6 and recycled; A part send CO2 trapping separator 12 separation after dedusting, denitration, desulfurization, and N2 send chimney 13 discharges, and CO2 send degasifier 14 deoxidations, and O2 more than 80 ℃, send power economized boiler 2 burnings through heat exchanger 3 heating.Carbon send carbon recover 15 to reclaim, and does carbon black and sells, or recycle for the device 17 of delivering coal.
As shown in Figure 3, plasmatorch catalyst converter 1 comprises: hollow cathode base 22, concavo-convex negative electrode 23, an anode 24, two anodes 25, long pressurization cylinder 26, negative electrode cooling circulating water 27, anode cooling circulating water 28, long pressurization cylinder cooling circulating water 29, carrier wind, electrode catalyst core 35, insulator 36, dc source 37, high-voltage pulse power source 38, high-voltage pulse device 39; Described carrier wind comprises: first via carrier wind 30, the second road carrier wind 31, Third Road carrier wind 32, tetra-road carrier wind 33, five road carrier winds 34; Described hollow cathode base 22, concavo-convex negative electrode 23, an anode 24, two anodes 25, long pressurization cylinder 26 is arranged in order and symmetrical, the negative electrode of described dc source 37 is connected with hollow cathode base 22, the concavo-convex negative electrode 23 of a side, and the anode of dc source 37 is connected with an anode 24, two anodes 25 of homonymy; The negative electrode of described high-voltage pulse power source 38 is connected with hollow cathode base 22, the concavo-convex negative electrode 23 of opposite side, and the anode of high-voltage dc pulse power 38 is connected with an anode 24, two anodes 25 of homonymy; Cellular electrode catalyst core 35 is inserted in plasmatorch catalyst converter central authorities, and one end is connected with high-voltage pulse device 39 by insulator 36; Negative electrode cooling circulating water 27 flow through hollow cathode base 22, the concavo-convex negative electrode 23 of the left and right sides, anode cooling circulating water 28 flow through an anode 24, two anodes 25 of the left and right sides, the translateral long pressurization cylinder 26 of long pressurization cylinder cooling circulating water 29 stream; Long pressurization cylinder 26 is communicated with the gas approach of 40 lower ends, energy saving pot furnace wall.
Wherein, carrier wind blast is preferred: first via carrier wind 30 >=1KPa, second road carrier wind 31 >=5KPa, Third Road carrier wind 32 >=10KPa ， tetra-road carrier wind 33 >=15KPa ， five road carrier wind 34 >=20KPa.
Take the multiple collocation of the multichannel carrier wind mode of delivering coal, preferably first via carrier wind 30, the second road carrier wind 31, Third Road carrier wind 32 are the CO2 powder of delivering coal; Carrier wind 33, five road carrier winds 34 in Si road are the water vapour powder of delivering coal.
During concrete operations:
The first step: the switch of opening negative electrode cooling circulating water 27, anode cooling circulating water 28;
Second step: open dc source 37, high-voltage pulse power source 38, high-voltage pulse device 39 switches;
The 3rd step, open first via carrier wind 30, the second road carrier wind 31, Third Road carrier wind 32, tetra-road carrier wind 33, five road carrier wind 34 switches;
As shown in Figure 4, power economized boiler 2 comprises: send oxygen device 42,43 44,Shang booster zone, ,Zhong Ciran district 45, lower primary zone; 43 44,Shang booster zone, ,Zhong Ciran district 45, described lower primary zone are located in the combustion chamber (41) of power economized boiler 2 from the bottom up successively, send oxygen device 42 to be located at power economized boiler 2 bottoms and are connected with the oxygen exhaust of heat exchanger 3.
Multilayer combustion district is arranged with and is beneficial to abundant burning, and significantly improves the clean conversion ratio of heat energy.
During concrete operations:
The first step: open and send oxygen device 42 switches to send O2 in power economized boiler 2, oxygen deliverng pipe road junction is 1 layer or multilayer, and every layer one or more send O2 entrance.
Second step: open successively 43 44,Shang booster zone, ,Zhong Ciran district 45, lower primary zone, plasmatorch catalyst converter 1 power switch, by CO+C(coal)+H2O(water vapour) gas of catalytic reaction is sent in power economized boiler 2 and is burnt with the O2 that send oxygen device 42 to send here.
As shown in Figure 5, degasifier 14 comprises: O2 air accumulator 46, high frequency waveforms device 47, high frequency pulse power supply 48, degasifier shell 49, insulator 50, electrode cores 51, explosion-proof sensor 52, infrared sensing viewer 53; Described degasifier shell 49 bottoms are connected with carbon recover 15, degasifier shell 49 bottoms are connected with CO2 trapping separator 12, degasifier shell 49 tops are connected with O2 air accumulator 46, degasifier shell 49 tops are provided with insulator 50, insulator 50 is provided with electrode cores 51, one end that insulator 50 stretches out degasifier shell outside is connected with high frequency waveforms device 47, and high frequency pulse power supply 48 is connected with high frequency waveforms device 47; Described explosion-proof sensor 52, infrared sensing viewer 53 are located at respectively the top and bottom of degasifier 14, detect deoxidation process.
During concrete operations:
The first step: open successively high frequency pulse power supply 48 and CO2 trapping separator 12 switches, and explosion-proof sensor 52 and infrared sensing viewer 53 switches;
Second step: CO2 becomes C and O2 through electrode cores 51 catalytic decomposition, and C send carbon recover 15, and O2 send O2 air accumulator 46, for power economized boiler 2 burnings.
Embodiment 2: as shown in Figure 2, power plant's carbon oxygen cycle use device is comprised of the device 17 of delivering coal, CO2 return channel 6, plasmatorch catalyst converter 1, power economized boiler 2, heat exchanger 3, booster fan 16, CO2 trapping separator 12, degasifier 14, air blast 4, carbon recover 15, long-range explosion-proof master control detection system 18, steam case 19, clarifier 20, sulfur-based compound fertilizer production line 21; Described plasmatorch catalyst converter 1 one end connects the device 17 of delivering coal, the other end is communicated with the gas approach of power economized boiler 2 bottoms, power economized boiler 2 tops are provided with outlet, the outlet on top is communicated with CO2 return channel 6, power economized boiler 2 bottoms are provided with exhanst gas outlet, and the exhanst gas outlet of bottom is connected with the gas approach flue of heat exchanger 3; Described steam case 19 is communicated with power economized boiler 2 and booster fan 16, and booster fan 16 is communicated with CO2 return channel 6 and plasmatorch catalyst converter 1; Described clarifier 20 is communicated with exhanst gas outlet flue and the CO2 trapping separator 12 of heat exchanger 3, and described clarifier 20 is also connected with sulfur-based compound fertilizer production line 21; CO2 trapping separator 12 is connected with the oxygen feeder of heat exchanger 3 by degasifier 14, air blast 4, and degasifier 14 is connected with carbon recover 15.
The device of the present embodiment is sent the coal dust of the device 17 of delivering coal into plasmatorch catalyst converter after steam case 19 (1 is carried out catalyzed conversion by the water vapour of power economized boiler 2 is sent together with CO2.Key reaction formula is:
CO2+C(coal)---2CO (1)
C(coal)+H2O---CO+H2 (2)
CO+H2O——CO2+H2 （3）
Complete after above-mentioned reaction, send clarifier 20 to carry out dedusting, denitration, desulfurization integrated purified treatment flue gas, dirt nitre sulfur material send sulfur-based compound fertilizer production line 21 to produce fertilizer, and CO2 send CO2 trapping separator 12 to recycle.
This device has been realized recycling and recycling of carbon resource, oxygen resource, dirt sulphur nitre material, reduces the discharge of the pollutants such as flue gas in the time of energy-conserving and environment-protective, has reduced the generation of nitrogen oxide.
Described in above, be specific embodiment of the utility model and the know-why used; if the change of doing according to conception of the present utility model; when its function producing does not exceed spiritual that description and accompanying drawing contain yet, must belong to protection domain of the present utility model.
Claims (6)
1. power plant's carbon oxygen cycle use device, is characterized in that comprising: the device of delivering coal (17), CO2 return channel (6), plasmatorch catalyst converter (1), power economized boiler (2), heat exchanger (3), CO2 trapping separator (12), degasifier (14), long-range explosion-proof master control detection system (18), chimney (13); Described plasmatorch catalyst converter (1) one end connects deliver coal device (17), CO2 return channel (6), the other end is communicated with the gas approach of power economized boiler (2) bottom, power economized boiler (2) top is provided with outlet, the outlet on top is communicated with CO2 return channel (6), power economized boiler (2) bottom is also provided with exhanst gas outlet, and the exhanst gas outlet of bottom is connected with the gas approach flue of heat exchanger (3); The exhanst gas outlet flue of described heat exchanger (3) is connected with CO2 trapping separator (12), CO2 trapping separator (12) is connected with the oxygen feeder of heat exchanger (3) by degasifier (14), air blast (4), degasifier (14) is connected with carbon recover (15), and CO2 trapping separator (12) is also connected with chimney (13); Described long-range explosion-proof master control detection system (18) is connected with each device and detects in real time.
2. power plant according to claim 1 carbon oxygen cycle use device, is characterized in that, also include system for desulfuration and denitration, described system for desulfuration and denitration comprises desulfurizer, denitrification apparatus; Desulfurizer is communicated between the exhanst gas outlet flue and CO2 trapping separator (12) of heat exchanger (3), and described denitrification apparatus is arranged between the outlet and CO2 return channel (6) on power economized boiler (2) top; Described desulfurizer comprises: deduster (7), air-introduced machine (8), desulfurization slag liquid (10), desulfurizing tower (11), heat exchanger (9), the exhanst gas outlet flue of described heat exchanger (3) is connected with CO2 trapping separator (12) by deduster (7), air-introduced machine (8), desulfurization slag liquid (10), desulfurizing tower (11), heat exchanger (9) successively.
3. power plant according to claim 1 carbon oxygen cycle use device, it is characterized in that, also include steam case (19), clarifier (20), sulfur-based compound fertilizer production line (21), described steam case (19) is communicated with power economized boiler (2) and booster fan (16), and booster fan (16) is communicated with CO2 return channel (6) and plasmatorch catalyst converter (1); Described clarifier (20) is communicated with exhanst gas outlet flue and the CO2 trapping separator (12) of heat exchanger (3), and described clarifier (20) is also connected with sulfur-based compound fertilizer production line (21).
4. power plant according to claim 2 carbon oxygen cycle use device, it is characterized in that, described plasmatorch catalyst converter (1) comprising: hollow cathode base (22), concavo-convex negative electrode (23), an anode (24), two anodes (25), long pressurization cylinder (26), negative electrode cooling circulating water (27), anode cooling circulating water (28), long pressurization cylinder cooling circulating water (29), carrier wind, electrode catalyst core (35), insulator (36), dc source (37), high-voltage pulse power source (38), high-voltage pulse device (39); Described carrier wind comprises: first via carrier wind (30), the second road carrier wind (31), Third Road carrier wind (32), tetra-road carrier wind (33), five road carrier winds (34); Described hollow cathode base (22), concavo-convex negative electrode (23), an anode (24), two anodes (25), long pressurization cylinder (26) are arranged in order and are symmetrical, the negative electrode of described dc source (37) is connected with the hollow cathode base (22) of a side, concavo-convex negative electrode (23), and the anode of dc source (37) is connected with an anode (24), two anodes (25) of homonymy; The negative electrode of described high-voltage pulse power source (38) is connected with the hollow cathode base (22) of opposite side, concavo-convex negative electrode (23), and the anode of high-voltage dc pulse power (38) is connected with an anode (24), two anodes (25) of homonymy; Cellular electrode catalyst core (35) is inserted in plasmatorch catalyst converter (1) central authorities, and one end is connected with high-voltage pulse device (39) by insulator (36); Negative electrode cooling circulating water (27) flow through the hollow cathode base (22) of the left and right sides, concavo-convex negative electrode (23), anode cooling circulating water (28) flow through an anode (24), two anodes (25) of the left and right sides, long pressurization cylinder cooling circulating water (29) flows translateral long pressurization cylinder (26).
5. power plant according to claim 4 carbon oxygen cycle use device, is characterized in that, described power economized boiler (2) comprising: send oxygen device (42), ,Zhong Ciran district, lower primary zone (43) (44), upper booster zone (45); ,Zhong Ciran district, described lower primary zone (43) (44), upper booster zone (45) are located in the combustion chamber of power economized boiler from the bottom up successively, send oxygen device (42) to be located at power economized boiler (2) bottom and are connected with the oxygen exhaust of heat exchanger (3).
6. power plant according to claim 5 carbon oxygen cycle use device, it is characterized in that, described degasifier (14) comprising: O2 air accumulator (46), high frequency waveforms device (47), high frequency pulse power supply (48), degasifier shell (49), insulator (50), electrode cores (51), explosion-proof sensor (52), infrared sensing viewer (53); Described degasifier shell (49) bottom is connected with carbon recover (15), degasifier shell (49) bottom is connected with CO2 trapping separator (12), degasifier shell (49) top is connected with O2 air accumulator (46), degasifier shell (49) top is provided with insulator (50), insulator (50) is provided with electrode cores (51), insulator (50) stretches out the outside one end of degasifier shell (49) and is connected with high frequency waveforms device (47), and high frequency pulse power supply (47) is connected with high frequency waveforms device (48); Described explosion-proof sensor (52), infrared sensing viewer (53) are located at respectively the top and bottom of degasifier (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320546359.XU CN203478306U (en) | 2013-09-03 | 2013-09-03 | Power plant carbon and oxygen recycling device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320546359.XU CN203478306U (en) | 2013-09-03 | 2013-09-03 | Power plant carbon and oxygen recycling device |
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| CN203478306U true CN203478306U (en) | 2014-03-12 |
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| CN201320546359.XU Withdrawn - After Issue CN203478306U (en) | 2013-09-03 | 2013-09-03 | Power plant carbon and oxygen recycling device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103453542A (en) * | 2013-09-03 | 2013-12-18 | 程礼华 | Power plant carbon and oxygen circulation utilization device and process of device |
| CN104406161A (en) * | 2014-11-17 | 2015-03-11 | 北京联优创展科技有限公司 | Coal-fired boiler flue gas backflow and supplement burning device |
| CN110498394A (en) * | 2019-05-30 | 2019-11-26 | 赫普能源环境科技有限公司 | A kind of thermal power plant's coke hydrogen generating system and method |
-
2013
- 2013-09-03 CN CN201320546359.XU patent/CN203478306U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103453542A (en) * | 2013-09-03 | 2013-12-18 | 程礼华 | Power plant carbon and oxygen circulation utilization device and process of device |
| CN103453542B (en) * | 2013-09-03 | 2015-07-15 | 程礼华 | Power plant carbon and oxygen circulation utilization device and process of device |
| CN104406161A (en) * | 2014-11-17 | 2015-03-11 | 北京联优创展科技有限公司 | Coal-fired boiler flue gas backflow and supplement burning device |
| CN110498394A (en) * | 2019-05-30 | 2019-11-26 | 赫普能源环境科技有限公司 | A kind of thermal power plant's coke hydrogen generating system and method |
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