CN203794616U - Remote explosion-proofing type gasifying hydrogen generating device capable of recycling carbon dioxide - Google Patents

Remote explosion-proofing type gasifying hydrogen generating device capable of recycling carbon dioxide Download PDF

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CN203794616U
CN203794616U CN201420050220.0U CN201420050220U CN203794616U CN 203794616 U CN203794616 U CN 203794616U CN 201420050220 U CN201420050220 U CN 201420050220U CN 203794616 U CN203794616 U CN 203794616U
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communicated
tank
steam
plasmatorchs
reaction chamber
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程礼华
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/133Renewable energy sources, e.g. sunlight

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The utility model relates to the field of hydrogen generation, and in particular relates to a remote explosion-proofing type gasifying hydrogen generating device capable of recycling carbon dioxide. The device comprises a CO2 tank, a multi-plasma torch generator, an intelligent coal conveyor, a solar steam generator, a steam tank, a reaction chamber, a steam generator unit, a purifier, a separator, a solar electrolyzing device, an H2 tank, an O2 tank, an online detector, and a master remote explosion-proofing control system; the CO2 tank and the steam generator unit are communicated with the multi-plasma torque generator; the intelligent coal conveyor, the steam tank and the multi-plasma torque generator are communicated with the reaction chamber. The remote explosion-proofing type gasifying hydrogen generating device capable of recycling carbon dioxide has the beneficial effects that 1, the structure is simple and variable; 2, any pollution discharge is not caused, and CO2 can be recycled; 2, the waste can be effectively utilized, and the hydrogen generating, oxygen producing and byproduct integrated chain is created; 4, the solar energy is effectively utilized, which lowers down the energy consumption compared with the traditional device; and 5, the master remote explosion-proofing system performs strict monitoring for the whole production process, so as to ensure the safety in a production line.

Description

Long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen
Technical field
The utility model relates to hydrogen preparation field, relates in particular to long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen.
Background technology
Coal, as the daily energy, has multiple use, and Ye Shi China distributes the most extensively, has abundant a kind of fossil oil.In for some time in the past, China is using coal as the main energy, and estimates within the time of growing future, thisly can not change taking coal as main energy structure.But in burning use procedure, easily there are various pollutions, ecotope is damaged, especially CO 2as the principal element of Greenhouse effect, how by its elimination or conversion, namely finding a kind of new coal utilization mode is the important subject of existing field of energy utilization.
Except this energy obtain manner that directly coal burnt, also having one is exactly indirect utilization.Hydrogen Energy, as a kind of novel, clean secondary energy, has very high fuel value and pollution-free.Hydrogen production process is mainly fossil oil hydrogen manufacturing and water electrolysis hydrogen producing at present, consider the restriction of product source, production capacity, cost and prior art, water electrolysis hydrogen producing can consume a large amount of electric energy, the total conversion efficiency of energy is generally lower than 20%, cost is comparatively expensive, so fossil oil hydrogen manufacturing, namely hydrogen production from coal gasification is main research direction.
Fossil oil hydrogen manufacturing is taking coal, oil, Sweet natural gas as raw material, utilizes carbon and the burning of airborne oxygen, passes into high temperature coal organic partial oxidation reaction occurs, then by techniques such as purification, separation, hydrogen is separated.Current conventional hydrogen production from coal gasification is sent into Reaktionsofen (vapourizing furnace) using water vapour+air+oxygen as vaporized chemical, make water vapour and coal generation gas making reaction generate synthetic gas, and by outside heat supply or air and the heat supply of coal generation oxidizing reaction.But this mode has increased the raw material consumption of coal, increased the waste gas waste materials such as carbonic acid gas simultaneously, affect the purity of synthesizer and environment has been caused to pollution.
Utility model content
The utility model is to overcome above-mentioned weak point, and object is to provide that a kind of equipment is simple, efficiency of conversion is high, pollution-free and realize the long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen of suitability for industrialized production.
The utility model is to achieve the above object by the following technical programs:
Long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, comprising: CO 2tank, many plasmatorchs producer, intelligence deliver coal device, solar steam generator, vapor can, reaction chamber, steam-electric power unit, cleaner, separator, sun power electrolysis device, H 2tank, O 2tank, at thread detector, long-range explosion-proof turn-key system; Described CO 2tank, steam-electric power unit are communicated with many plasmatorchs producer, solar steam generator is communicated with vapor can, deliver coal device, vapor can of intelligence is communicated with reaction chamber by unique pipeline with many plasmatorchs producer, reaction chamber bottom is provided with the cinder notch that produces coal, reaction chamber upper end is provided with outlet and is communicated with steam-electric power unit, steam-electric power unit, cleaner, separator, H 2tank is communicated with successively, and steam-electric power unit is communicated with vapor can, sun power electrolysis device, and cleaner is communicated with purifying processor, separator and CO 2tank is communicated with, sun power electrolysis device and H 2tank, O 2tank is communicated with; Described in thread detector is arranged on pipeline and reaction chamber, long-range explosion-proof each device of turn-key system on-line monitoring.
As preferably, long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen also includes steam coal slurry shotcrete machine; Solar steam generator is communicated with vapor can, and deliver coal device, vapor can of intelligence is communicated with steam coal slurry shotcrete machine, and many plasmatorchs producer is communicated with reaction chamber by unique pipeline with steam coal slurry shotcrete machine.
As preferably, long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, comprising: CO 2tank, many plasmatorchs producer, intelligence deliver coal device, solar steam generator, vapor can, reaction chamber, steam-electric power unit, cleaner, separator, sun power electrolysis device, H 2tank, O 2tank, at thread detector, long-range explosion-proof turn-key system; Described CO 2tank, steam-electric power unit are communicated with many plasmatorchs producer, solar steam generator is communicated with vapor can, described vapor can is communicated with the bottom of reaction chamber, many plasmatorchs producer and the intelligence device of delivering coal is communicated with reaction chamber by unique pipeline, reaction chamber bottom is provided with the cinder notch that produces coal, reaction chamber upper end is provided with outlet and is communicated with steam-electric power unit, steam-electric power unit, cleaner, separator, H 2tank is communicated with successively, and steam-electric power unit is communicated with vapor can, sun power electrolysis device, and cleaner is communicated with purifying processor, separator and CO 2tank is communicated with, sun power electrolysis device and H 2tank, O 2tank is communicated with; Described in thread detector is arranged on pipeline and reaction chamber, long-range explosion-proof each device of turn-key system on-line monitoring.
As preferably, long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, comprising: CO 2tank, many plasmatorchs producer, intelligence deliver coal device, solar steam generator, vapor can, reaction chamber, steam-electric power unit, cleaner, separator, sun power electrolysis device, H 2tank, O 2tank, at thread detector, long-range explosion-proof turn-key system; Described CO 2tank, steam-electric power unit, vapor can are communicated with many plasmatorchs producer, solar steam generator is communicated with vapor can, many plasmatorchs producer and the intelligence device of delivering coal is communicated with reaction chamber by unique pipeline, reaction chamber bottom is provided with the cinder notch that produces coal, reaction chamber upper end is provided with outlet and is communicated with steam-electric power unit, steam-electric power unit, cleaner, separator, H 2tank is communicated with successively, and steam-electric power unit is communicated with vapor can, sun power electrolysis device, and cleaner is communicated with purifying processor, separator and CO 2tank is communicated with, sun power electrolysis device and H 2tank, O 2tank is communicated with; Described in thread detector is arranged on pipeline and reaction chamber, long-range explosion-proof each device of turn-key system on-line monitoring.
As preferably, described steam-electric power unit is made up of gas heat energy steam interchanger and multiscrew expansion power generation machine; Described gas heat energy steam interchanger is communicated with reaction chamber, vapor can, cleaner, multiscrew expansion power generation machine, and multiscrew expansion power generation machine is communicated with many plasmatorchs producer, sun power electrolysis device.
As preferably, many plasmatorchs producer is made up of several plasmatorchs, and each plasmatorch power is 50KW-3MW.
As preferably, the rounded or rectangle of the plasmatorch of many plasmatorchs producer is arranged.
As preferably, sun power electrolysis device comprises: catalytic electrolysis plate, anode, negative electrode, adjustable resistance, electrolyzer; The two ends of described electrolyzer are provided with anode, negative electrode, are provided with catalytic electrolysis plate in electrolyzer, between anode and negative electrode, are connected to adjustable resistance, anodic gas outlet and the O of electrolyzer 2tank is communicated with, cathode gas outlet and the H of electrolyzer 2tank is communicated with.
As preferably, many plasmatorchs producer is made up of 6 plasmatorchs.
The beneficial effects of the utility model are: 1, the utility model is simple in structure, changeable, can transform according to practical situation, are applicable to the hydrogen manufacturing environment of multiple scale; 2, zero disposal of pollutants, CO 2effectively seizure, recycle; 3, dirt, sulphur, nitre, the comprehensive utilization of coal tar wet goods, increase added value, reduces hydrogen manufacturing cost, builds hydrogen manufacturing, produces oxygen, the integrated chain of byproduct; 4, the utility model device is introduced solar steam generator, sun power electrolysis device, effectively utilizes these novel pollution-free energy source of sun power, and prior device reduces energy consumption relatively; 5, master control island is long-range explosion-proof, and on-line monitoring temperature, pressure, gaseous constituent are strictly monitored production whole process, ensures the safety of production line and eliminates production hidden danger, finds in advance dangerous situation, warning, and emergent solution is quick-fried.
Brief description of the drawings
Fig. 1 is the structural representation of the long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen of embodiment 1;
Fig. 2 is the structural representation of the long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen of embodiment 2;
Fig. 3 is the structural representation of the long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen of embodiment 3;
Fig. 4 is the structural representation of the long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen of embodiment 4;
Fig. 5 is the structural representation of many plasmatorchs producer of circular configuration;
Fig. 6 is the structural representation of many plasmatorchs producer of rectangle structure;
Fig. 7 is the structural representation of steam-electric power unit;
Fig. 8 is the structural representation of sun power electrolysis device.
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, long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, comprising: standby power supply 1, CO 2tank 14, many plasmatorchs producer 2, intelligence deliver coal device 3, solar steam generator 18, vapor can 4, reaction chamber 7, steam-electric power unit 10, cleaner 11, separator 13, sun power electrolysis device 16, H 2tank 15, O 2tank 17, in thread detector I 61, in thread detector II 62, at thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92, long-range explosion-proof turn-key system 19; Described standby power supply 1, CO 2tank 14, steam-electric power unit 10 are communicated with many plasmatorchs producer 2, solar steam generator 18 is communicated with vapor can 4, deliver coal device 3, vapor can 4 of intelligence is communicated with reaction chamber 7 by unique pipeline with many plasmatorchs producer 2, reaction chamber 7 bottoms are provided with the cinder notch 8 that produces coal, reaction chamber 7 upper ends are provided with outlet and are communicated with steam-electric power unit 10, steam-electric power unit 10, cleaner 11, separator 13, H 2tank 15 is communicated with successively, and steam-electric power unit 10 is communicated with vapor can 4, sun power electrolysis device 16, and cleaner 11 is communicated with purifying processor 12, separator 13 and CO 2tank 14 is communicated with, sun power electrolysis device 16 and H 2tank 15, O 2tank 17 is communicated with; Described in thread detector I 61, be arranged on pipeline in thread detector II 62, be arranged in reaction chamber 7 in thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92 is arranged on H 2in tank 15, long-range explosion-proof each device of turn-key system 19 on-line monitorings.
Implementation step:
The first step, open long-range explosion-proof turn-key system 19, standby power supply 11 switches successively; Open in thread detector I 61, in thread detector II 62, at thread detector III 63 power switches online detected temperatures, pressure, gaseous constituent; Open long-range explosion-proof apparatus I 91, long-range explosion-proof apparatus II 92 power switches, carry out online long-range anti-explosion alarming with in time emergent separate quick-fried;
Second step, open solar steam generator 18 valves, enter in pipeline after water vapor is sent into vapor can 4; The intelligence device 3 of delivering coal delivers into coal in pipeline;
Preferably vapor temperature is 150-450 DEG C;
Preferably pulverized coal particle fineness is 200-300 orders;
The 3rd step, open CO for subsequent use 2tank 20 valves, by CO 2send into water vapor that many plasmatorchs producer 2 and vapor can 4 carry and the intelligence coal that device 3 carries of delivering coal and carry out rapid reaction in pipeline and reaction chamber 7;
Preferred many plasmatorchs producer 2 temperature outs are 1000-1500 DEG C;
Temperature of reaction in preferred reaction chamber 7 is 150-850 DEG C;
The 4th step, send steam-electric power unit 10 by the reactant gases of reaction chamber 7 interior generations, the steam of formation send vapor can 4, and electricity is for many plasmatorchs producer 2 and sun power electrolysis device 16;
Steam-electric power unit 10 major function principles, are to utilize the reactant gases temperature of reaction chamber 7 interior generations to produce steam, and a heat energy part are converted into electric energy;
Preferably the generator in steam-electric power unit 10 is multiscrew expansion power generation machine;
The gas temperature preferably exporting after steam-electric power unit 10 is lower than 150 DEG C;
The 5th step, the gas after steam-electric power unit 10 is lowered the temperature is sent into cleaner 11 carries out dedusting, desulphurization and denitration and a small amount of coal tar wet goods carries out purifying treatment.Dirt, desulphurization and denitration, coal tar wet goods purifying processor 12 are fully utilized;
The gas temperature that preferably cleaner 11 exports is lower than 50 DEG C;
The 6th step, send separator 13 to separate purified gas, pass through H 2the H of molecular sieve 2send H 2tank 15, CO 2send CO 2tank 14, for recycling;
Electric power after the 7th step, steam-electric power unit 10 supply many plasmatorchs producer 2 unnecessary, send sun power electrolysis device 16 to carry out water electrolysis hydrogen production, H 2send H 2tank 15, O 2send O 2tank 17.
Many plasmatorchs producer 2 is made up of several plasmatorchs, plasmatorch number is 2-80, the power of single plasmatorch is 50KW-3MW, can be applicable to the hydrogen manufacturing scale of large and small factory, the arrangement mode of plasmatorch be circle as shown in Figure 5, also can arrange as shown in Figure 6 by rectangle.
It is the structural representation of steam-electric power unit 10 referring to Fig. 7, steam-electric power unit 10 is made up of gas heat energy steam interchanger and multiscrew expansion power generation machine, described gas heat energy steam interchanger is communicated with reaction chamber 7, vapor can 4, cleaner 11, multiscrew expansion power generation machine, and multiscrew expansion power generation machine is communicated with many plasmatorchs producer 2, sun power electrolysis device 16.
Implementation step:
The first step, the reactant gases of reaction chamber 7 is sent into gas heat energy steam interchanger 22 produce steam, a part of steam send vapor can 4, and a part of steam send multiscrew expansion power generation machine 23 to generate electricity, for many plasmatorchs producer 2 and 16 electricity consumptions of sun power electrolysis device; The vapor temperature that preferred gas heat energy steam interchanger 22 produces is 150-300 DEG C; Preferably multiscrew expansion power generation machine is 2-50 screw expansion devices;
Second step, send cleaner 11 to purify the gas after gas heat energy steam interchanger 22 is lowered the temperature.
Be the structural representation of sun power electrolysis device 16 referring to Fig. 8, sun power electrolysis device 16 is made up of catalytic electrolysis plate 25, anode 26, negative electrode 27, adjustable resistance 28, electrolyzer 29; The two ends of described electrolyzer 29 are provided with anode 26, negative electrode 27, in electrolyzer 29, be provided with catalytic electrolysis plate 25, between anode 26 and negative electrode 27, be connected to adjustable resistance 28, the anodic gas outlet of electrolyzer 29 is communicated with O2 tank 17, and the cathode gas outlet of electrolyzer 29 is communicated with H2 tank 15.The sun 24 is just according to electrolyzer 29.
Implementation step:
The first step, will send in electrolyzer 29 by the clear water of membrane separation;
Preferably in electrolytic aqueous solution, add tensio-active agent yellow humic acid: concentration 0.05-0.1%;
Preferably in electrolytic aqueous solution, adding photocatalyst is titanium rare-earth compound;
Preferred catalytic electrolytic zinc-coated steel sheet 25 is Ni or Ni alloy, Ni+Zn alloy;
Second step, open standby power supply 11 or steam-electric power unit 10 power switches, carry out electrolytic reaction; The O that reaction generates 2send O 2tank 17, H 2send H 2tank 15, preferably 60-120 DEG C of electrolysis temperatures.
Embodiment 2: as shown in Figure 2, long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, comprising: standby power supply 1, CO 2tank 14, many plasmatorchs producer 2, intelligence deliver coal device 3, solar steam generator 18, vapor can 4, steam coal slurry shotcrete machine 5, reaction chamber 7, steam-electric power unit 10, cleaner 11, separator 13, sun power electrolysis device 16, H 2tank 15, O 2tank 17, in thread detector I 61, in thread detector II 62, at thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92, long-range explosion-proof turn-key system 19; Described standby power supply 1, CO 2tank 14, steam-electric power unit 10 are communicated with many plasmatorchs producer 2, solar steam generator 18 is communicated with vapor can 4, deliver coal device 3, vapor can 4 of intelligence is communicated with steam coal slurry shotcrete machine 5, many plasmatorchs producer 2 is communicated with reaction chamber 7 by unique pipeline with steam coal slurry shotcrete machine 5, reaction chamber 7 bottoms are provided with the cinder notch 8 that produces coal, reaction chamber 7 upper ends are provided with outlet and are communicated with steam-electric power unit 10, steam-electric power unit 10, cleaner 11, separator 13, H 2tank 15 is communicated with successively, and steam-electric power unit 10 is communicated with vapor can 4, sun power electrolysis device 16, and cleaner 11 is communicated with purifying processor 12, separator 13 and CO 2tank 14 is communicated with, sun power electrolysis device 16 and H 2tank 15, O 2tank 17 is communicated with; Described in thread detector I 61, be arranged on pipeline in thread detector II 62, be arranged in reaction chamber 7 in thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92 is arranged on H 2in tank 15, long-range explosion-proof each device of turn-key system 19 on-line monitorings.CO for subsequent use 2tank 20 and CO 2tank 14 is the same can store CO 2.
Implementation step:
The first step, open long-range explosion-proof turn-key system 19, standby power supply 11 switches successively; Open in thread detector I 61, in thread detector II 62, at thread detector III 63 power switches online detected temperatures, pressure, gaseous constituent; Open long-range explosion-proof apparatus I 91, long-range explosion-proof apparatus II 92 power switches, carry out online long-range anti-explosion alarming with in time emergent separate quick-fried;
Second step, open solar steam generator 18 valves, water vapor is sent into after vapor can 4, then sent into steam coal slurry shotcrete machine 5, the coal of sending here with the device 3 of delivering coal from intelligence carries out coal slurry processing;
Preferably vapor temperature is 150-450 DEG C;
Preferably pulverized coal particle fineness is 200-300 orders;
The 3rd step, open CO for subsequent use 2tank 20 valves, by CO 2send into many plasmatorchs producer 2 and in pipeline and reaction chamber 7, carry out rapid reaction with the coal slurry that steam coal slurry shotcrete machine 5 gushes out;
Preferred many plasmatorchs producer 2 temperature outs are 1000-1500 DEG C;
Temperature of reaction in preferred reaction chamber 7 is 150-850 DEG C;
The 4th step, send steam-electric power unit 10 by the reactant gases of reaction chamber 7 interior generations, the steam of formation send vapor can 4, and electricity is for many plasmatorchs producer 2 and sun power electrolysis device 16;
Steam-electric power unit 10 major function principles, are to utilize the reactant gases temperature of reaction chamber 7 interior generations to produce steam, and a heat energy part are converted into electric energy;
Preferably the generator in steam-electric power unit 10 is multiscrew expansion power generation machine;
The gas temperature preferably exporting after steam-electric power unit 10 is lower than 150 DEG C;
The 5th step, the gas after steam-electric power unit 10 is lowered the temperature is sent into cleaner 11 carries out dedusting, desulphurization and denitration and a small amount of coal tar wet goods carries out purifying treatment.Dirt, desulphurization and denitration, coal tar wet goods purifying processor 12 are fully utilized;
The gas temperature that preferably cleaner 11 exports is lower than 50 DEG C;
The 6th step, send separator 13 to separate purified gas, pass through H 2the H of molecular sieve 2send H 2tank 15, CO 2send CO 2tank 14, for recycling;
Electric power after the 7th step, steam-electric power unit 10 supply many plasmatorchs producer 2 unnecessary, send sun power electrolysis device 16 to carry out water electrolysis hydrogen production, H 2send H 2tank 15, O 2send O 2tank 17.
The present embodiment is sent into water vapor and coal in steam coal slurry shotcrete machine 5 and is carried out coal slurry processing, and major function effect is that coal dust is softened to processing by steam.
Embodiment 3: as shown in Figure 3, long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, comprising: standby power supply 1, CO 2tank 14, many plasmatorchs producer 2, intelligence deliver coal device 3, solar steam generator 18, vapor can 4, reaction chamber 7, steam-electric power unit 10, cleaner 11, separator 13, sun power electrolysis device 16, H 2tank 15, O 2tank 17, in thread detector I 61, in thread detector II 62, at thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92, long-range explosion-proof turn-key system 19; Described standby power supply 1, CO 2tank 14, steam-electric power unit 10 are communicated with many plasmatorchs producer 2, solar steam generator 18 is communicated with vapor can 4, described vapor can 4 is communicated with the bottom of reaction chamber 7, many plasmatorchs producer 2 and the intelligence device 3 of delivering coal is communicated with reaction chamber 7 by unique pipeline, reaction chamber 7 bottoms are provided with the cinder notch 8 that produces coal, reaction chamber 7 upper ends are provided with outlet and are communicated with steam-electric power unit 10, steam-electric power unit 10, cleaner 11, separator 13, H 2tank 15 is communicated with successively, and steam-electric power unit 10 is communicated with vapor can 4, sun power electrolysis device 16, and cleaner 11 is communicated with purifying processor 12, separator 13 and CO 2tank 14 is communicated with, sun power electrolysis device 16 and H 2tank 15, O 2tank 17 is communicated with; Describedly be arranged on pipeline in thread detector I 61, in thread detector II 62 is arranged on the passage that vapor can 4 is communicated with reaction chamber 7, be arranged in reaction chamber 7 in thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92 is arranged on H 2in tank 15, long-range explosion-proof each device of turn-key system 19 on-line monitorings.
Implementation step:
The first step, open long-range explosion-proof turn-key system 19, standby power supply 11 switches successively; Open in thread detector I 61, in thread detector II 62, at thread detector III 63 power switches online detected temperatures, pressure, gaseous constituent; Open long-range explosion-proof apparatus I 91, long-range explosion-proof apparatus II 92 power switches, carry out online long-range anti-explosion alarming with in time emergent separate quick-fried;
Second step, open solar steam generator 18 valves, from reaction chamber 7 bottoms, water vapor is exported after water vapor is sent into vapor can 4; The intelligence device 3 of delivering coal delivers into coal in pipeline;
Preferably vapor temperature is 150-450 DEG C;
Preferably pulverized coal particle fineness is 200-300 orders;
The 3rd step, open CO for subsequent use 2tank 20 valves, by CO 2send into the water vapor that many plasmatorchs producer 2 and vapor can 4 carry, the water vapor that vapor can 4 is carried carries out rapid reaction in reaction chamber 7;
Preferred many plasmatorchs producer 2 temperature outs are 1000-1500 DEG C;
Temperature of reaction in preferred reaction chamber 7 is 150-850 DEG C;
The 4th step, send steam-electric power unit 10 by the reactant gases of reaction chamber 7 interior generations, the steam of formation send vapor can 4, and electricity is for many plasmatorchs producer 2 and sun power electrolysis device 16;
Steam-electric power unit 10 major function principles, are to utilize the reactant gases temperature of reaction chamber 7 interior generations to produce steam, and a heat energy part are converted into electric energy;
Preferably the generator in steam-electric power unit 10 is multiscrew expansion power generation machine;
The gas temperature preferably exporting after steam-electric power unit 10 is lower than 150 DEG C;
The 5th step, the gas after steam-electric power unit 10 is lowered the temperature is sent into cleaner 11 carries out dedusting, desulphurization and denitration and a small amount of coal tar wet goods carries out purifying treatment.Dirt, desulphurization and denitration, coal tar wet goods purifying processor 12 are fully utilized;
The gas temperature that preferably cleaner 11 exports is lower than 50 DEG C;
The 6th step, send separator 13 to separate purified gas, pass through H 2the H of molecular sieve 2send H 2tank 15, CO 2send CO 2tank 14, for recycling;
Electric power after the 7th step, steam-electric power unit 10 supply many plasmatorchs producer 2 unnecessary, send sun power electrolysis device 16 to carry out water electrolysis hydrogen production, H 2send H 2tank 15, O 2send O 2tank 17.
Embodiment 4: as shown in Figure 4, long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, comprising: standby power supply 1, CO 2tank 14, many plasmatorchs producer 2, intelligence deliver coal device 3, solar steam generator 18, vapor can 4, reaction chamber 7, steam-electric power unit 10, cleaner 11, separator 13, sun power electrolysis device 16, H 2tank 15, O 2tank 17, in thread detector I 61, at thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92, long-range explosion-proof turn-key system 19; Described standby power supply 1, CO 2tank 14, steam-electric power unit 10, vapor can 4 are communicated with many plasmatorchs producer 2, solar steam generator 18 is communicated with vapor can 4, many plasmatorchs producer 2 and the intelligence device 3 of delivering coal is communicated with reaction chamber 7 by unique pipeline, reaction chamber 7 bottoms are provided with the cinder notch 8 that produces coal, reaction chamber 7 upper ends are provided with outlet and are communicated with steam-electric power unit 10, steam-electric power unit 10, cleaner 11, separator 13, H 2tank 15 is communicated with successively, and steam-electric power unit 10 is communicated with vapor can 4, sun power electrolysis device 16, and cleaner 11 is communicated with purifying processor 12, separator 13 and CO 2tank 14 is communicated with, sun power electrolysis device 16 and H 2tank 15, O 2tank 17 is communicated with; Describedly be arranged on pipeline in thread detector I 61, be arranged in reaction chamber 7 in thread detector III 63, long-range antiriot device I 91, long-range antiriot device II 92 is arranged on H 2in tank 15, long-range explosion-proof each device of turn-key system 19 on-line monitorings.
Implementation step:
The first step, open long-range explosion-proof turn-key system 19, standby power supply 11 switches successively; Open in thread detector I 61, at thread detector III 63 power switches online detected temperatures, pressure, gaseous constituent; Open long-range explosion-proof apparatus I 91, long-range explosion-proof apparatus II 92 power switches, carry out online long-range anti-explosion alarming with in time emergent separate quick-fried;
Second step, by vapor can 4 and CO 2the water vapor of tank 14 and CO 2mix to send in many plasmatorchs producer 2 and react under isoionic state; Preferably vapor temperature is 150-450 DEG C;
The 3rd step, by the mixed gas exporting through many plasmatorchs producer 2, comprise H 2o, CO 2, H 2cO 3, HCOOH and coal divide and in reaction chamber 7, carry out rapid reaction;
Preferably pulverized coal particle fineness is 200-300 orders;
Preferred many plasmatorchs producer 2 temperature outs are 1000-1500 DEG C;
Temperature of reaction in preferred reaction chamber 7 is 150-850 DEG C;
The 4th step, send steam-electric power unit 10 by the reactant gases of reaction chamber 7 interior generations, the steam of formation send vapor can 4, and electricity is for many plasmatorchs producer 2 and sun power electrolysis device 16;
Steam-electric power unit 10 major function principles, are to utilize the reactant gases temperature of reaction chamber 7 interior generations to produce steam, and a heat energy part are converted into electric energy;
Preferably the generator in steam-electric power unit 10 is multiscrew expansion power generation machine;
The gas temperature preferably exporting after steam-electric power unit 10 is lower than 150 DEG C;
The 5th step, the gas after steam-electric power unit 10 is lowered the temperature is sent into cleaner 11 carries out dedusting, desulphurization and denitration and a small amount of coal tar wet goods carries out purifying treatment.Dirt, desulphurization and denitration, coal tar wet goods purifying processor 12 are fully utilized;
The gas temperature that preferably cleaner 11 exports is lower than 50 DEG C;
The 6th step, send separator 13 to separate purified gas, pass through H 2the H of molecular sieve 2send H 2tank 15, CO 2send CO 2tank 14, for recycling;
Electric power after the 7th step, steam-electric power unit 10 supply many plasmatorchs producer 2 unnecessary, send sun power electrolysis device 16 to carry out water electrolysis hydrogen production, H 2send H 2tank 15, O 2send O 2tank 17.
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 specification sheets and accompanying drawing contain yet, must belong to protection domain of the present utility model.

Claims (9)

1. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen, is characterized in that comprising: CO 2tank (14), many plasmatorchs producer (2), intelligence deliver coal device (3), solar steam generator (18), vapor can (4), reaction chamber (7), steam-electric power unit (7), cleaner (11), separator (13), sun power electrolysis device (16), H 2tank (15), O 2tank (17), at thread detector, long-range explosion-proof turn-key system (19); Described CO 2tank (14), steam-electric power unit (7) are communicated with many plasmatorchs producer (2), solar steam generator (18) is communicated with vapor can (4), deliver coal device (3), vapor can (4) of intelligence is communicated with reaction chamber (7) by unique pipeline with many plasmatorchs producer (2), reaction chamber (7) bottom is provided with the cinder notch that produces coal (8), reaction chamber (7) upper end is provided with outlet and is communicated with steam-electric power unit (7), steam-electric power unit (7), cleaner (11), separator (13), H 2tank (15) is communicated with successively, and steam-electric power unit (7) is communicated with vapor can (4), sun power electrolysis device (16), and cleaner (11) is communicated with purifying processor, separator (13) and CO 2tank (14) is communicated with, sun power electrolysis device (16) and H 2tank (15), O 2tank (17) is communicated with; Described in thread detector is arranged on pipeline and reaction chamber (7), each device of long-range explosion-proof turn-key system (19) on-line monitoring.
2. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 1, is characterized in that, also includes steam coal slurry shotcrete machine (5); Solar steam generator (18) is communicated with vapor can (4), deliver coal device (3), vapor can (4) of intelligence is communicated with steam coal slurry shotcrete machine (5), and many plasmatorchs producer (2) is communicated with reaction chamber (7) by unique pipeline with steam coal slurry shotcrete machine (5).
3. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 1, it is characterized in that, described vapor can (4) is communicated with the bottom of reaction chamber (7), and many plasmatorchs producer (2) and the intelligence device (3) of delivering coal is communicated with reaction chamber (7) by unique pipeline.
4. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 1, is characterized in that described CO 2tank (14), steam-electric power unit (7), vapor can (4) are communicated with many plasmatorchs producer (2), solar steam generator (18) is communicated with vapor can (4), and many plasmatorchs producer (2) and the intelligence device (3) of delivering coal is communicated with reaction chamber (7) by unique pipeline.
5. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 2, is characterized in that, described steam-electric power unit (7) is made up of gas heat energy steam interchanger (22) and multiscrew expansion power generation machine (23); Described gas heat energy steam interchanger (22) is communicated with reaction chamber (7), vapor can (4), cleaner (11), multiscrew expansion power generation machine (23), and multiscrew expansion power generation machine (23) is communicated with many plasmatorchs producer (2), sun power electrolysis device (16).
6. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 1, is characterized in that sun power electrolysis device (16) comprising: catalytic electrolysis plate (25), anode (26), negative electrode (27), adjustable resistance (28), electrolyzer (29); The two ends of described electrolyzer (29) are provided with anode (26), negative electrode (27), are provided with catalytic electrolysis plate (25) in electrolyzer (29), between anode (26) and negative electrode (27), are connected to adjustable resistance (28), anodic gas outlet and the O of electrolyzer (29) 2tank (17) is communicated with, cathode gas outlet and the H of electrolyzer (29) 2tank (15) is communicated with.
7. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 6, is characterized in that many plasmatorchs producer (2) is made up of several plasmatorchs (21), and each plasmatorch (21) power is 50KW-3MW.
8. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 7, is characterized in that the rounded or rectangle of the plasmatorch (21) of many plasmatorchs producer (2) arranges.
9. long-range explosion-proof coalification carbon dioxide recycling device for producing hydrogen according to claim 8, is characterized in that many plasmatorchs producer (2) is made up of 6 plasmatorchs (21).
CN201420050220.0U 2014-01-26 2014-01-26 Remote explosion-proofing type gasifying hydrogen generating device capable of recycling carbon dioxide Withdrawn - After Issue CN203794616U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103787274A (en) * 2014-01-26 2014-05-14 程礼华 Remote explosion-proof hydrogen production device for recycling coalified carbon dioxide and technology thereof
CN104531214A (en) * 2014-12-10 2015-04-22 程礼华 Integrated carbon-oxygen-hydrogen circulating device and process thereof for producing solar energy, coal, power, aluminum, fertilizers, carbon, oil and paper

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103787274A (en) * 2014-01-26 2014-05-14 程礼华 Remote explosion-proof hydrogen production device for recycling coalified carbon dioxide and technology thereof
CN103787274B (en) * 2014-01-26 2015-06-10 程礼华 Remote explosion-proof hydrogen production device for recycling coalified carbon dioxide and technology thereof
CN104531214A (en) * 2014-12-10 2015-04-22 程礼华 Integrated carbon-oxygen-hydrogen circulating device and process thereof for producing solar energy, coal, power, aluminum, fertilizers, carbon, oil and paper
CN104531214B (en) * 2014-12-10 2016-10-19 程礼华 The solar energy coal electrit fertilizer carbon oil paper hydrocarbon Oxygen cycle device of integration and technique thereof

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