CN104003601A - Process and device for generating power by using solar multidimensional electrode and microwave catalysis sludge - Google Patents
Process and device for generating power by using solar multidimensional electrode and microwave catalysis sludge Download PDFInfo
- Publication number
- CN104003601A CN104003601A CN201410232328.6A CN201410232328A CN104003601A CN 104003601 A CN104003601 A CN 104003601A CN 201410232328 A CN201410232328 A CN 201410232328A CN 104003601 A CN104003601 A CN 104003601A
- Authority
- CN
- China
- Prior art keywords
- island
- sludge
- power
- steam
- microwave
- 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
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
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
-
- 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
- Y02E20/12—Heat utilisation in combustion or incineration of waste
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Abstract
The invention relates to the field of sludge treatment and in particular relates to a process and device for generating power by using solar multidimensional electrode and microwave catalysis sludge. The process comprises the steps of generating power by using solar multidimensional electrode sludge and generating power by using microwave carbon cycle catalytic sludge. The device comprises a power island, a multidimensional electrode electrochemical island, a rotation drum drying island, a microwave carbon cycle catalytic island, a power generating island, a steam island, a carbon black island and a remote explosion-proof general monitoring island. The process and the device has the advantages that the continuous daily treatment amount of sludge is 100-3000ton, the large-scale treatment of sludge is realized, and the existing sludge treatment requirement is met; the sludge treatment is short in time and low in energy consumption; since solar energy, air energy and steam energy are used for generating power, the electric supply consumption is reduced and the energy consumption can be effectively reduced by 70%; the sludge dehydration rate is more than 90%, so that the energy loss due to the high content of water in the sludge is reduced; the sludge is cracked in situ for power generation and co-generation of high value-added carbon black products.
Description
Technical field
The present invention relates to field of sludge treatment, relate in particular to sun power multidimension electrode and microwave catalysis sludge power generation technique and device thereof.
Background technology
Along with further developing of China's urbanization, sewage work needs municipal sludge to be processed to get more and more.The end of the year in 2010, national town sewage treatment capacity reaches 343 billion cubic meters, and dewatered sludge generation approaches 2,200 ten thousand tons, and nearly 80% mud is not dealt carefully with.At present, China's mud main methods, the one, landfill, the 2nd, burning electricity generation, the 3rd, for brickmaking.But landfill need to take a large amount of soils, easily cause secondary pollution; Burning electricity generation because of water content too high, deficiency in economic performance; Brickmaking meeting produces a large amount of odor pollution surrounding enviroment.Therefore these existing treatment processs better lignin-sludge all.
At present, comparatively advanced sludge disposal technology, is to adopt electrochemistry sludge dewatering both at home and abroad.Although it is a variety of that existing domestic and international electrochemistry method for sludge treatment has,, the sludge treatment overwhelming majority is undesirable, the major defect that it is common: the one, processing mode mostly is intermittent type and processes, and is difficult to a large amount of mass-producings of continuity and processes.The 2nd, the electrochemical treatment time is long, needs 5-50 minutes kinds, causes energy consumption cost large.The 3rd, how costs and poor dehydration results, can only dewater below 70%.
Summary of the invention
The present invention overcomes above-mentioned weak point, and object is to provide a kind of mass-producing processing, processing cost is low, treatment effect is good sun power multidimension electrode and microwave catalysis sludge power generation technique and device thereof.
The present invention achieves the above object by the following technical programs: sun power multidimension electrode and microwave catalysis sludge power generation technique, comprising: sun power multidimension electrode sludge power generation and microwave carbon cycle catalysis sludge power generation;
Sun power multidimension electrode sludge power generation comprises the following steps:
(1) mud send drum dried island after sending multidimension electrode electrochemistry island electrochemical dehydration, and under vapor action, mud carries out secondary quick dewatering drying;
(2) dry mud send generating island burning electricity generation, burns and produces steam cycle utilization, and vapor portion send drum dried island, and another part send Power island for the work of multidimension electrode electrochemistry island;
(3) generating island is burned and is produced collecting carbonic anhydride recycle or send carbon black island to produce carbon black; Long-range explosion-proof each island running condition of total monitoring island on-line monitoring;
Microwave carbon cycle catalysis sludge power generation comprises the following steps:
(1) mud and carbonic acid gas send microwave carbon cycle catalysis island to produce inflammable gas and liquid fuel;
(2) inflammable gas and liquid fuel send generating island burning electricity generation, burn and produce steam cycle utilization, and steam send Power island for the work of microwave carbon cycle catalysis island;
(3) generating island is burned and is produced collecting carbonic anhydride recycle or send carbon black island to produce carbon black; Long-range explosion-proof each island running condition of total monitoring island on-line monitoring.
As preferably, described Power island power supply comprises a kind of how several in solar electrical energy generation power supply, air energy power-generating power supply, steam-electric power power supply, mains-supplied.
As preferably, described steam island output steam comprise steam that solar steam machine produces, the steam that air energy steamer produces, the steam of generating island output.
As preferably, the sludge moisture content after the electrochemical dehydration of described multidimension electrode electrochemistry island is 45-60%.
As preferably, described sludge moisture content after the secondary quick dewatering drying of drum dried island is 1-10%.
Sun power multidimension electrode and microwave catalysis sludge power generation device, comprising: Power island, multidimension electrode electrochemistry island, drum dried island, microwave carbon cycle catalysis island, generating island, steam island, carbon black island, long-range explosion-proof total monitoring island; Described Power island is connected with multidimension electrode electrochemistry island, microwave carbon cycle catalysis island, multidimension electrode electrochemistry island is connected with drum dried island, drum dried island, microwave carbon cycle catalysis island and generating island are connected, generating island is connected with carbon black island, steam island, and steam island is connected with Power island, drum dried island; The running condition on each island of on-line monitoring, long-range explosion-proof total monitoring island.
Beneficial effect of the present invention is: the one, and 100-3000 tons of running days lignin-sludges, realize extensive lignin-sludge, meet existing sludge treatment demand; The 2nd, the sludge treatment time is short, and power consumption is few, utilizes solar electrical energy generation, air energy power-generating and steam-electric power power supply, saves city's electric consumption, effectively reduces energy consumption 70%; The 3rd, dewatering rate reaches more than 90%, reduces and because sludge moisture content is high, causes energy waste; The 4th, mud is cracking generating and coproduction high added value carbon black product on the spot.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is the structural representation of sun power multidimension electrode sludge power generation device;
Fig. 3 is the structural representation of multidimension electrode treater;
Fig. 4 is the structural representation of second electrode water strainer;
Fig. 5 is the structural representation of steam dram treater;
Fig. 6 is the structural representation of microwave carbon cycle catalysis device of sludge;
In figure: 1, device of solar generating; 2, air source generating device; 3, steam electric power generator; 4, civil power; 5, solar steam machine; 6, air energy steamer; 7, storage mud pretreatment system; 8, multidimension electrode treater; 9, steam dram treater; 10, foul smell negative-pressure conveying system; 11, sludge incineration generating and purification system; 12, collecting carbonic anhydride production of carbon black by system; 13, oxygen canister; 14, grey slag bath; 15, hydrogen gas tank; 16, super-high pressure pulse desulfurization separator; 17, sulphur pond; 18, water vapor tank; 19, long-range explosion-proof turn-key system; 20, anode; 21, negative electrode; 22, longitudinal aeration pulse catalysis utmost point; 23, solarization air cap; 24, the horizontal aeration pulse catalysis utmost point; 25, aerator; 26, thermopnore rotating band; 27, thermopnore runner; 28, remote monitoring sensor; 29, voltage stabilized source; 30, the pulse power; 311, isolator I; 312, isolator II; 32, second electrode water strainer; 33, water tank; 34, remote-control system; 35, primary dewatering mud travelling belt; 361, driving wheel I; 362, driving wheel II; 37, follow-up pulley; 38, filter screen conductive glass steel plate with holes; 39, battery lead plate; 40, filter cloth-net-type travelling belt; 41, microwave transformer; 42, magnetron; 43, carbon dioxide tank; 44, carbonic acid gas sprocket hole pipe; 45, carbonic acid gas production well; 46, thermopnore transmission belt; 47, mud and liquid-fuel tank; 48, inflammable gas tank; 49, microwave carbon cycle catalysis sludge sump; 50, long-range anti-explosion surveillance sensor; 51, catalyst tank; 52, long-range explosion-proof monitoring system; 53, electric motor; 54, drum rotating axle; 551, support I; 552, support II; 56 steam dram are processed chamber.
Embodiment
Below in conjunction with specific embodiment, the present invention is described further, but protection scope of the present invention is not limited in this:
Embodiment 1: as shown in Figure 1, sun power multidimension electrode and microwave catalysis sludge power generation device, is characterized in that comprising: Power island, multidimension electrode electrochemistry island, drum dried island, microwave carbon cycle catalysis island, generating island, steam island, carbon black island, long-range explosion-proof total monitoring island; Described Power island is connected with multidimension electrode electrochemistry island, microwave carbon cycle catalysis island, multidimension electrode electrochemistry island is connected with drum dried island, drum dried island, microwave carbon cycle catalysis island and generating island are connected, generating island is connected with carbon black island, steam island, and steam island is connected with Power island, drum dried island; The running condition on each island of on-line monitoring, long-range explosion-proof total monitoring island.
Sun power multidimension electrode and the microwave catalysis sludge power generation technique of utilizing said apparatus, comprising: sun power multidimension electrode sludge power generation and microwave carbon cycle catalysis sludge power generation;
As shown in Figure 2, sun power multidimension electrode sludge power generation device comprises: device of solar generating 1, air source generating device 2, steam electric power generator 3, civil power 4, solar steam machine 5, air energy steamer 6, storage mud pretreatment system 7, multidimension electrode treater 8, steam dram treater 9, foul smell negative-pressure conveying system 10, sludge incineration generating and purification system 11, collecting carbonic anhydride production of carbon black by system 12, oxygen canister 13, grey slag bath 14, hydrogen gas tank 15, super-high pressure pulse desulfurization separator 16, sulphur pond 17, water vapor tank 18, long-range explosion-proof turn-key system 19.Device of solar generating 1, air source generating device 2, steam electric power generator 3, civil power 4 and multidimension electrode treater 8, sludge incineration generating are connected with purification system 11, long-range explosion-proof turn-key system 19; Storage mud pretreatment system 7 is connected with multidimension electrode treater 8, foul smell negative-pressure conveying system 10, multidimension electrode treater 8 is connected with steam dram treater 9, foul smell negative-pressure conveying system 10, and foul smell negative-pressure conveying system 10 is connected with purification system 11 with sludge incineration generating; The steam that solar steam machine 5, air energy steamer 6 produce send steam dram treater 9, steam electric power generator 3; Steam dram treater 9 is connected with purification system 11, super-high pressure pulse desulfurization separator 16 with sludge incineration generating, and super-high pressure pulse desulfurization separator 16 is connected with sulphur pond 17, hydrogen gas tank 15, water vapor tank 18; Sludge incineration generating is connected with water vapor tank 18, grey slag bath 14, collecting carbonic anhydride production of carbon black by system 12 with purification system 11, collecting carbonic anhydride production of carbon black by system 12 is connected with oxygen canister 13, and oxygen canister 13 is connected with purification system 11, multidimension electrode treater 8 with sludge incineration generating; The water vapor of water vapor tank 18 send steam dram treater 9, steam electric power generator 3.
Implementation step:
The first step, open long-range explosion-proof turn-key system 19 power switches and open device of solar generating 1 or air source generating device 2, steam electric power generator 3, civil power 4 Switching powers, for multidimension electrode treater 8, carry out electrochemistry sludge dewatering;
Second step, will send after multidimension electrode treater 8 electrochemical dehydrations through the mud of storage mud pretreatment system 7, and send steam dram treater 9 further dry fast dewatering, send sludge incineration generating and purification system 11 burning electricity generations and gas cleaning processing; The foul smell that storage mud pretreatment system 7, multidimension electrode treater 8 produce, sends into sludge incineration generating and purification system 11 burning electricity generations by foul smell negative-pressure conveying system 10, makes not externally discharge of foul smell;
Wherein, storage mud pretreatment system 7 pretreated sludge moisture contents are 75-98.5%; Sludge moisture content after multidimension electrode treater 8 is processed is 45-60%; The dried sludge moisture content of steam dram treater 9 is below 10%;
The 3rd step, solar steam machine 5 or air energy steamer 6 switched and send steam dram treater 9, mud is carried out to drying treatment;
Wherein, the vapor temperature of solar steam machine 5, air energy steamer 6 is 150-500 ℃, and vapor pressure is 10-100KPa;
The 4th step, a large amount of sulfide hydrogens and other organic gas that steam dram treater 9 is produced, send super-high pressure pulse desulfurization separator 16 to process, and the hydrogen producing send hydrogen gas tank 15, for sludge incineration generating and purification system 11 recycle burnings; The sulphur producing, send sulphur pond 17 recyclings;
The voltage of super-high pressure pulse desulfurization separator 16 is 100-1000KV;
Carbonic acid gas in the 5th step, sludge incineration generating and purification system 11 flue gases, trapping production of carbon black by through collecting carbonic anhydride production of carbon black by system 12, separated oxygen send oxygen canister 13, an oxygen is for sludge incineration generating and purification system 11 recycle burnings, and a part send multidimension electrode treater 8 for aeration oxidized sludge.Sludge incineration generating and purification system 11 lime-ash send grey slag bath 14, send landfill yard, or other recyclings;
Sludge incineration temperature is 900-1200 ℃.
Collecting carbonic anhydride production of carbon black by system 12 completes main reaction:
CO
2——C+O
2；
The 6th step, the water vapor that sludge incineration generating and purification system 11 produced, send respectively steam electric power generator 3 generating and 9 recycles of steam dram treater.
As shown in Figure 3, multidimension electrode treater 8 comprises: anode 20, negative electrode 21, longitudinal aeration pulse catalysis utmost point 22, solarization air cap 23, the horizontal aeration pulse catalysis utmost point 24, aerator 25, thermopnore rotating band 26, thermopnore runner 27, remote monitoring sensor 28, voltage stabilized source 29, the pulse power 30, isolator I 311, isolator II 312, second electrode water strainer 32, water tank 33, remote-control system 34.Described device of solar generating 1, air source generating device 2, steam electric power generator 3, civil power 4 is connected with voltage stabilized source 29, the anodal jointed anode 20 of voltage stabilized source 29, negative pole connects negative electrode 21, the import of multidimension electrode treater shell is connected with storage mud pretreatment system 7, aerator 25 is connected with isolator II 312, isolator II 312 is connected with the horizontal aeration pulse catalysis utmost point 24, laterally the aeration pulse catalysis utmost point 24 is provided with longitudinal aeration pulse catalysis utmost point 22, longitudinal aeration pulse catalysis utmost point 22, laterally the aeration pulse catalysis utmost point 24 is provided with solarization air cap 23, laterally the aeration pulse catalysis utmost point 24 the other ends are connected with isolator I 311, isolator I 311 is connected with the pulse power 30, multidimension electrode treater 8 bottoms are provided with thermopnore rotating band 26, and thermopnore rotating band 26 drives thermopnore runner 27 to rotate, and thermopnore rotating band 26 is connected with second electrode water strainer 32, and second electrode water strainer 32 is connected with water tank 33, steam dram treater 9, multidimension electrode treater shell top is provided with outlet and is connected with foul smell negative-pressure conveying system 10, remote monitoring sensor 28 is arranged in multidimension electrode treater shell.
Implementation step:
The first step, open remote-control system 34 power switches and thermopnore rotating band 26 power switches, the pulse power 30 switches respectively;
Second step, open storage mud pretreatment system 7 valves, mud is sent in the next aeration multidimension electrode treater and dewatered;
The 3rd step, by solar steam machine 5 or air energy steamer 6, the steam of water vapor tank 18 and the oxygen of oxygen canister 13, under the temperature condition of 60-150 ℃, mix in aerator 25 is sent into the horizontal aeration pulse catalysis utmost point 24 and longitudinal aeration pulse catalysis utmost point 22, steam and oxygen are discharged from solarization air cap 23, and mud is carried out to oxidation and aeration;
The 4th step, open voltage stabilized source 29 switches, mud, at anode 20, negative electrode 21 and the horizontal aeration and catalyzing utmost point 24 and longitudinally under the multidimension electrode electrochemical action of the aeration and catalyzing utmost point 22, carries out fast dewatering;
Wherein, the voltage of voltage stabilized source 29 is 20-50V; The mud thickness that mud multidimension electrode is processed is 2-20cm, and the treatment time is 30 seconds-2 minutes; The material of anode 20, negative electrode 21 is made by electroconductive frp or electrically conductive graphite or conduction active-carbon; Laterally the aeration pulse catalysis utmost point 24 and longitudinal aeration pulse catalysis utmost point 22 can be made by pore shape conductive aluminum titanium alloy, electroconductive frp, electrically conductive graphite, conduction active-carbon, as catalysis electrode, promote mud fast dewatering; Anode 20, negative electrode 21 form multidimension electrode by multipair anode, negative electrode and a plurality of longitudinal aeration pulse catalysis utmost point 22 respectively, are conducive to a large amount of mud fast dewaterings; Spacing between anode 20, negative electrode 21, longitudinal aeration pulse catalysis utmost point 22 is 3-10cm; The pulsed voltage of the pulse power 30 is 10-600KV, and pulse width is between Millisecond and nanosecond;
The 5th step, thermopnore rotating band 26 switches, by process the mud of dehydration through multidimension electrode, send steam dram treater 9 further drying and dehydrating through water strainer 32, and the water filtering down from second electrode water strainer 32 send water tank 33 to carry out sewage disposal qualified discharge; The solid content of processing the mud of dehydration through multidimension electrode is greater than 45%.
The 6th step, open remote monitoring sensor 28 switches, the temperature of on-line monitoring multidimension electrode sludge treatment device.
As shown in Figure 4, second electrode water strainer 32 is comprised of primary dewatering mud travelling belt 35, driving wheel I 361, driving wheel II 362, follow-up pulley 37, filter screen conductive glass steel plate 38 with holes, battery lead plate 39, filter cloth-net-type travelling belt 40; 35, driving wheel I 361, driving wheel II 362, follow-up pulley 37, filter cloth-net-type travelling belt 40 form a belt drive system, filter screen conductive glass steel plate 38 with holes presses close to be fixed on filter cloth-net-type travelling belt 40 belows between driving wheel I 361 and follow-up pulley 37, filter cloth-net-type travelling belt 40 tops of filter screen conductive glass steel plate with holes 38 correspondences arrange battery lead plate 39, angle between battery lead plate 39 and filter screen conductive glass steel plate 38 with holes is 15-45 °, and angle of the present invention is set to 30 °.
Because filter cloth-net-type travelling belt 40 has certain toughness, therefore the mud that primary dewatering mud travelling belt 35 transmits, enter filter cloth-net-type travelling belt 40, can make to filter cloth-net-type travelling belt 40 deforms, make the mud between filter screen conductive glass steel plate 38 with holes and battery lead plate 39 depart from filter cloth-net-type travelling belt 40, thereby cause, mud and battery lead plate are anodal to depart from, and causes osmosis phenomenon to stop.Therefore below filter cloth-net-type travelling belt 40, a filter screen conductive glass steel plate 38 with holes is set.
Due to after mud dewaters under electric field action, sludge volume reduces, and in order not make mud and battery lead plate depart from, constantly keeps the state that contact with pole plate, specially filter screen conductive glass steel plate 38 with holes is to 15-45 with battery lead plate 39 settings spends angles.After switching on power, between filter screen conductive glass steel plate 38 with holes and battery lead plate 39, form the electric field region of different field intensity.Along with the carrying out of sludge dewatering, on the one hand, mud remains and contacts with pole plate; Strength of electric field increases gradually on the other hand, increases the dehydrating amount of mud.
Transmission along with filter cloth-net-type travelling belt 40, utilize the gap between filter screen conductive glass steel plate 38 with holes and filter cloth-net-type travelling belt 40 to reduce, mud has been increased to pressure to dewater, further reinforcement sludge dehydrating amount, this is also that filter screen conductive glass steel plate 38 with holes arranges with battery lead plate 39 Another reason that is angle.
Implementation step:
Driving wheel I 361, driving wheel II 362 provide motivating force by filter cloth-net-type travelling belt 40, follow-up pulley 37 for whole electrode water strainer 32; The filter screen conductive glass steel plate 38 with holes negative pole that switches on power, is fixed on and is close to filter cloth-net-type travelling belt 40 belows; Battery lead plate 39 positive pole that switches on power.During energising, between filter screen conductive glass steel plate 38 with holes and battery lead plate 39, form an electric field, when mud enters between filter screen conductive glass steel plate 38 with holes and battery lead plate 39, under electric field action, carry out second dehydration.Because mud is when carrying out electroosmotic dewatering, moisture removes from mud inside, and sludge volume is reduced.
As shown in Figure 5, steam dram treater 9 comprises: electric motor 53, drum rotating axle 54, support I 551, support II 552, steam dram are processed chamber 56.Shown in be provided with steam dram in steam dram treater shell and process chamber 56, drum rotating axle 54 is arranged on steam dram and processes chamber 56, electric motor 53 drives 54 rotations of drum rotating axles, steam dram treater shell is supported by support I 551, support II 552; The steam of solar steam machine 5, air energy steamer 6, water vapor tank 18 send steam dram to process chamber 56, and the mud of multidimension electrode treater 8 outputs send steam dram to process chamber 56, carries out the quick flash-evaporation dehydration of mud and process in steam dram processing chamber 56; Sludge-drying send sludge incineration generating and purification system 11, and the gas that steam dram is processed in chamber 56 send super-high pressure pulse desulfurization separator 16; Steam dram is processed in chamber 56 and is provided with long-range anti-explosion surveillance sensor 50.
Implementation step:
The first step, open long-range explosion-proof monitoring system power supply 52 and electric motor 53 power switches.
Second step, open solar steam 6 or air energy steam 6, water vapor tank 18 switch valve switches, steam is sent into steam dram and process in chamber 56, multidimension electrode treater 8 is sent to the mud coming, carry out quick flash-evaporation dehydration;
The 3rd step, the mud that steam dram is processed to chamber 56 inner dryings send sludge incineration generating and purification system 11 burning electricity generations and gas cleaning to process; The gas that steam dram is processed in chamber 56 send 16 desulfurization of super-high pressure pulse desulfurization separator to process;
The 4th step, open long-range anti-explosion surveillance sensor 50 power switches, on-line monitoring steam dram is processed the temperature in chamber 56;
The temperature that wherein steam dram is processed in chamber 56 is 120-150 ℃; The water content of the mud of steam dram processing chamber 56 dehydrations is lower than 10%.
As shown in Figure 6, microwave carbon cycle catalysis device of sludge, comprising: microwave transformer 41, magnetron 42, carbon dioxide tank 43, carbonic acid gas sprocket hole pipe 44, carbonic acid gas production well 45, thermopnore transmission belt 46, mud and liquid-fuel tank 47, inflammable gas tank 48, microwave carbon cycle catalysis sludge sump 49, long-range anti-explosion surveillance sensor 50, catalyst tank 51, long-range explosion-proof monitoring system 52; Catalyst tank 51, storage mud pretreatment system 7 are connected with microwave carbon cycle catalysis sludge sump 49, and microwave carbon cycle catalysis sludge sump 49 pneumatic outlets are connected with inflammable gas tank 48; Microwave transformer 41 is connected with magnetron 42; Carbon dioxide tank 43 is connected with carbonic acid gas sprocket hole pipe 44, and carbonic acid gas sprocket hole pipe 44 is provided with carbonic acid gas production well 45; Thermopnore transmission belt 46 is connected with liquid-fuel tank 47 with mud, mud is connected with purification system 11 with liquid-fuel tank 47, inflammable gas tank 48 and sludge incineration generating, and sludge incineration generating is connected with carbon dioxide tank 41 through collecting carbonic anhydride production of carbon black by system 12 with purification system 11 output carbonic acid gas; By microwave carbon cycle catalysis sludge sump 49, magnetron 42 and carbonic acid gas, there is hot electro-chemical reaction successively in mud, produce inflammable gas, liquid fuel and mud, inflammable gas send inflammable gas tank 48, and liquid fuel and mud send mud and liquid-fuel tank 47 by thermopnore transmission belt 46.
Implementation step
The first step, open long-range explosion-proof monitoring system 51 power switches.
Second step, open storage mud pretreatment system 7 valves and catalyst tank 51 valves, mud and catalyzer are sent in microwave carbon cycle catalysis sludge sump 49.
Wherein, catalyzer is composite alumina silicon-calcium-magnesium ferripotassium sodium powder, or compound rare-earth titanium zinc-aluminium silicon-calcium-magnesium ferripotassium sodium powder.
The 3rd step, open microwave transformer 41 power switches, microwave carbon cycle catalysis sludge sump 49 interior mud are carried out to microwave dehydration.
The microwave frequency of microwave transformer 41 is 2450-50000MHZ, and power is 0.5-600KW, and the voltage that microwave transformer 41 power supplys provide to magnetron 42 is 4-100KV high pressure.
The 4th step, open carbon dioxide tank 43 valves, carbonic acid gas is sent in carbonic acid gas sprocket hole pipe 44, carbonic acid gas is defeated from carbonic acid gas production well 45 out, enters microwave carbon cycle catalysis sludge sump 49 and the hot electro-chemical reaction of sludge creation, produces inflammable gas (CH
4, H
2, CO) and liquid fuel (methyl alcohol, acetylene).Inflammable gas send inflammable gas tank 48 for sludge incineration generating and purification system 11 combustion power generations, and liquid fuel and the complete mud of part unreacted send mud and liquid-fuel tank 47, for sludge incineration generating and purification system 11 combustion power generations.
Complete main reaction
CO
2+ C (organic in mud)---CO
CO
2+ H
2o---inflammable gas (CH
4, H
2, CO)+liquid fuel (methyl alcohol, acetylene)
The 5th step, the flue gas that sludge incineration generating and purification system 11 combustion power generations are produced carry out separated.A carbonic acid gas part of separating send collecting carbonic anhydride production of carbon black by system 12 production of carbon black by, and a part of carbonic acid gas send carbon dioxide tank 43 recycles.
The 6th step, open long-range anti-explosion surveillance sensor 50 power switches, on-line monitoring temperature, pressure, gaseous constituent.
The temperature of microwave carbonic acid gas circulation catalysis mud is 75-85 ℃.
Described in above, be specific embodiments of the invention and the know-why used, if the change of doing according to conception of the present invention, when its function producing does not exceed spiritual that specification sheets and accompanying drawing contain yet, must belong to protection scope of the present invention.
Claims (6)
1. sun power multidimension electrode and microwave catalysis sludge power generation technique, is characterized in that comprising: sun power multidimension electrode sludge power generation and microwave carbon cycle catalysis sludge power generation;
Sun power multidimension electrode sludge power generation comprises the following steps:
(1) mud send drum dried island after sending multidimension electrode electrochemistry island electrochemical dehydration, and under vapor action, mud carries out secondary quick dewatering drying;
(2) dry mud send generating island burning electricity generation, burns and produces steam cycle utilization, and vapor portion send drum dried island, and another part send Power island for the work of multidimension electrode electrochemistry island;
(3) generating island is burned and is produced collecting carbonic anhydride recycle or send carbon black island to produce carbon black; Long-range explosion-proof each island running condition of total monitoring island on-line monitoring;
Microwave carbon cycle catalysis sludge power generation comprises the following steps:
(1) mud and carbonic acid gas send microwave carbon cycle catalysis island to produce inflammable gas and liquid fuel;
(2) inflammable gas and liquid fuel send generating island burning electricity generation, burn and produce steam cycle utilization, and steam send Power island for the work of microwave carbon cycle catalysis island;
(3) generating island is burned and is produced collecting carbonic anhydride recycle or send carbon black island to produce carbon black; Long-range explosion-proof each island running condition of total monitoring island on-line monitoring.
2. sun power multidimension electrode according to claim 1 and microwave catalysis sludge power generation technique, is characterized in that, described Power island power supply comprises one or more in solar electrical energy generation power supply, air energy power-generating power supply, steam-electric power power supply, mains-supplied.
3. sun power multidimension electrode according to claim 1 and microwave catalysis sludge power generation technique, is characterized in that, described steam island output steam comprises steam, the steam of air energy steamer generation, the steam of generating island output that solar steam machine produces.
4. sun power multidimension electrode according to claim 1 and microwave catalysis sludge power generation technique, is characterized in that, the sludge moisture content after the electrochemical dehydration of described multidimension electrode electrochemistry island is 45-60%.
5. sun power multidimension electrode according to claim 1 and microwave catalysis sludge power generation technique, is characterized in that, described sludge moisture content after the secondary quick dewatering drying of drum dried island is 1-10%.
6. sun power multidimension electrode and microwave catalysis sludge power generation device, is characterized in that comprising: Power island, multidimension electrode electrochemistry island, drum dried island, microwave carbon cycle catalysis island, generating island, steam island, carbon black island, long-range explosion-proof total monitoring island; Described Power island is connected with multidimension electrode telephony island, microwave carbon cycle catalysis island, multidimension electrode electrochemistry island is connected with drum dried island, drum dried island, microwave carbon cycle catalysis island and generating island are connected, generating island is connected with carbon black island, steam island, and steam island is connected with Power island, drum dried island; The running condition on each island of on-line monitoring, long-range explosion-proof total monitoring island.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410232328.6A CN104003601B (en) | 2014-05-28 | 2014-05-28 | Sun power multidimension electrode and microwave catalysis sludge power generation technique and device thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410232328.6A CN104003601B (en) | 2014-05-28 | 2014-05-28 | Sun power multidimension electrode and microwave catalysis sludge power generation technique and device thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104003601A true CN104003601A (en) | 2014-08-27 |
| CN104003601B CN104003601B (en) | 2015-12-09 |
Family
ID=51364546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410232328.6A Active CN104003601B (en) | 2014-05-28 | 2014-05-28 | Sun power multidimension electrode and microwave catalysis sludge power generation technique and device thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104003601B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105576295A (en) * | 2016-02-02 | 2016-05-11 | 程礼华 | Solar integrated preparation device and process for graphene lithium and aluminum magnesium alloy battery |
| CN106090926A (en) * | 2016-06-24 | 2016-11-09 | 湖北合加环境设备有限公司 | A kind of electro-osmosis sludge high-drying dehydration and burning combined treatment sludge method |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1057998A (en) * | 1996-08-20 | 1998-03-03 | Nkk Corp | Treatment of sludge and system therefor |
| JP2002192196A (en) * | 2000-12-28 | 2002-07-10 | Tokyo Gas Co Ltd | Method and apparatus for treating sludge |
| JP2003042429A (en) * | 2001-07-27 | 2003-02-13 | Mitsubishi Heavy Ind Ltd | Ash melting furnace equipment for gasifying/melting plasma, and method for its control |
| CN101463261A (en) * | 2009-01-09 | 2009-06-24 | 北京博奇电力科技有限公司 | Integrated system and method for producing oil from sludge and refuse incineration |
| JP2010005491A (en) * | 2008-06-24 | 2010-01-14 | Tokyo Metropolis | Electrolytic phosphorus recovery device and sewage treatment system using it |
| CN201678575U (en) * | 2010-03-30 | 2010-12-22 | 浙江大学 | Sludge drying and incineration and power generation integrated device |
| CN202881065U (en) * | 2012-10-18 | 2013-04-17 | 武汉托普森能源有限公司 | Solar sludge drying and burning power generation energy-saving device |
| CN203360247U (en) * | 2013-06-24 | 2013-12-25 | 四川海普流体技术有限公司 | Comprehensive sludge treatment integrated equipment |
| CN203890209U (en) * | 2014-05-28 | 2014-10-22 | 程礼华 | Solar multidimensional electrode and microwave catalysis sludge power generation device |
-
2014
- 2014-05-28 CN CN201410232328.6A patent/CN104003601B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1057998A (en) * | 1996-08-20 | 1998-03-03 | Nkk Corp | Treatment of sludge and system therefor |
| JP2002192196A (en) * | 2000-12-28 | 2002-07-10 | Tokyo Gas Co Ltd | Method and apparatus for treating sludge |
| JP2003042429A (en) * | 2001-07-27 | 2003-02-13 | Mitsubishi Heavy Ind Ltd | Ash melting furnace equipment for gasifying/melting plasma, and method for its control |
| JP2010005491A (en) * | 2008-06-24 | 2010-01-14 | Tokyo Metropolis | Electrolytic phosphorus recovery device and sewage treatment system using it |
| CN101463261A (en) * | 2009-01-09 | 2009-06-24 | 北京博奇电力科技有限公司 | Integrated system and method for producing oil from sludge and refuse incineration |
| CN201678575U (en) * | 2010-03-30 | 2010-12-22 | 浙江大学 | Sludge drying and incineration and power generation integrated device |
| CN202881065U (en) * | 2012-10-18 | 2013-04-17 | 武汉托普森能源有限公司 | Solar sludge drying and burning power generation energy-saving device |
| CN203360247U (en) * | 2013-06-24 | 2013-12-25 | 四川海普流体技术有限公司 | Comprehensive sludge treatment integrated equipment |
| CN203890209U (en) * | 2014-05-28 | 2014-10-22 | 程礼华 | Solar multidimensional electrode and microwave catalysis sludge power generation device |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105576295A (en) * | 2016-02-02 | 2016-05-11 | 程礼华 | Solar integrated preparation device and process for graphene lithium and aluminum magnesium alloy battery |
| CN105576295B (en) * | 2016-02-02 | 2017-11-17 | 程礼华 | Graphene lithium and almag battery solar integration preparation facilities and technique |
| CN106090926A (en) * | 2016-06-24 | 2016-11-09 | 湖北合加环境设备有限公司 | A kind of electro-osmosis sludge high-drying dehydration and burning combined treatment sludge method |
| CN106090926B (en) * | 2016-06-24 | 2018-06-19 | 湖北合加环境设备有限公司 | A kind of electro-osmosis sludge high-drying dehydration is with burning combined treatment sludge method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104003601B (en) | 2015-12-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2016127594A1 (en) | Sludge treatment method using solar pyrolysis carbonization technology | |
| CN202558749U (en) | Improved device for sludge pyrolysis treatment | |
| CN103094597A (en) | Microbial fuel cell with function of efficiently and synchronously removing nitrogen and carbon | |
| CN104926066A (en) | Method for simultaneously realizing heavy metal harmless treatment and deep dehydration for dehydrated sludge | |
| CN203890209U (en) | Solar multidimensional electrode and microwave catalysis sludge power generation device | |
| CN104003601B (en) | Sun power multidimension electrode and microwave catalysis sludge power generation technique and device thereof | |
| CN106277664A (en) | A kind of sludge semi-dry processes technique | |
| CN105776430B (en) | Electrocatalysis oxidation apparatus and method for sewage treatment | |
| CN114574329A (en) | Biogas carbon reduction coupling biogas slurry pollution reduction device and method based on biogas circulating fermentation | |
| CN107964552B (en) | Method for improving methane synthesis efficiency by coupling anaerobic digestion with MFC | |
| CN101591132A (en) | A kind of method for dehydrating municipal sludge | |
| CN103482830A (en) | Device for concentrating and digesting sludge and generating power synchronously | |
| CN106676572B (en) | The extracting method and device of black liquid rugose wood element based on woodceramics electrode | |
| CN203119032U (en) | Microorganism fuel battery capable of efficiently achieving synchronous denitrification and carbon removal | |
| CN206814610U (en) | A kind of sludge dehydration device | |
| CN203741202U (en) | Anode for electro-osmotic sludge dewatering equipment and equipment | |
| CN111087053A (en) | Preparation method and application of sludge-based gas diffusion particle electrode | |
| CN105836842B (en) | Intermittent photocatalysis collection of energy reactor and the method for handling waste water using it | |
| CN113175766B (en) | Double-helix finned tube type adsorption bed for adsorption refrigeration system and application | |
| CN211004703U (en) | Advanced treatment device for solar electrocatalytic oxidation sewage | |
| CN103395941B (en) | Lignite upgrading condensate recycling system | |
| CN105176800A (en) | Biomass power generating equipment | |
| CN102688878B (en) | Municipal solid waste biomass environment-friendly renewable energy drying system | |
| CN215947192U (en) | Household garbage pyrolysis resource utilization system | |
| CN108033663A (en) | A kind of method and apparatus of multianode sludge electric dehydration |
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 | ||
| CP02 | Change in the address of a patent holder |
Address after: Shogun East Gulou District of Nanjing city of Jiangsu Province, No. 199 210000 Patentee after: Cheng Lihua Address before: 11, 1102, new building, Xicheng, 98, Gu Dun Road, 310010, Zhejiang, Hangzhou Patentee before: Cheng Lihua |
|
| CP02 | Change in the address of a patent holder | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20211018 Granted publication date: 20151209 |
|
| PP01 | Preservation of patent right |