CN106090928A - Ion energy house refuse incineration process device and incineration process method - Google Patents
Ion energy house refuse incineration process device and incineration process method Download PDFInfo
- Publication number
- CN106090928A CN106090928A CN201610629462.9A CN201610629462A CN106090928A CN 106090928 A CN106090928 A CN 106090928A CN 201610629462 A CN201610629462 A CN 201610629462A CN 106090928 A CN106090928 A CN 106090928A
- Authority
- CN
- China
- Prior art keywords
- washing
- washing tank
- gas
- air
- incinerator
- 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
- 238000000034 method Methods 0.000 title claims abstract description 98
- 230000008569 process Effects 0.000 title claims abstract description 76
- 238000005406 washing Methods 0.000 claims abstract description 101
- 150000002500 ions Chemical class 0.000 claims abstract description 70
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 31
- 239000007921 spray Substances 0.000 claims abstract description 30
- 238000001179 sorption measurement Methods 0.000 claims abstract description 23
- 238000012544 monitoring process Methods 0.000 claims abstract description 22
- 230000009931 harmful effect Effects 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 11
- 239000003463 adsorbent Substances 0.000 claims abstract description 8
- 230000009471 action Effects 0.000 claims abstract description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract 2
- 239000003546 flue gas Substances 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims description 60
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 36
- 230000000694 effects Effects 0.000 claims description 31
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 28
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 claims description 22
- 239000002956 ash Substances 0.000 claims description 20
- 239000000463 material Substances 0.000 claims description 16
- 239000000126 substance Substances 0.000 claims description 13
- 235000002918 Fraxinus excelsior Nutrition 0.000 claims description 9
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 9
- 239000000523 sample Substances 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims description 6
- 239000000243 solution Substances 0.000 claims description 6
- 239000004642 Polyimide Substances 0.000 claims description 5
- 229920001721 polyimide Polymers 0.000 claims description 5
- 229920000049 Carbon (fiber) Polymers 0.000 claims description 4
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 4
- 238000005276 aerator Methods 0.000 claims description 4
- 239000004917 carbon fiber Substances 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 150000004816 dichlorobenzenes Chemical class 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 4
- 239000011259 mixed solution Substances 0.000 claims description 4
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 4
- 150000002910 rare earth metals Chemical class 0.000 claims description 4
- 229910000938 samarium–cobalt magnet Inorganic materials 0.000 claims description 4
- 229920006395 saturated elastomer Polymers 0.000 claims description 4
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 4
- 235000011152 sodium sulphate Nutrition 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 3
- 229910000828 alnico Inorganic materials 0.000 claims description 3
- 238000005842 biochemical reaction Methods 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 239000010882 bottom ash Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000005034 decoration Methods 0.000 claims description 3
- 239000012467 final product Substances 0.000 claims description 3
- 230000004907 flux Effects 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 230000007935 neutral effect Effects 0.000 claims description 3
- 239000002904 solvent Substances 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 238000009834 vaporization Methods 0.000 claims description 3
- 230000008016 vaporization Effects 0.000 claims description 3
- 235000013311 vegetables Nutrition 0.000 claims description 3
- WJEIYVAPNMUNIU-UHFFFAOYSA-N [Na].OC(O)=O Chemical compound [Na].OC(O)=O WJEIYVAPNMUNIU-UHFFFAOYSA-N 0.000 claims 1
- 239000003034 coal gas Substances 0.000 claims 1
- 230000005389 magnetism Effects 0.000 claims 1
- 238000006386 neutralization reaction Methods 0.000 claims 1
- 230000001954 sterilising effect Effects 0.000 description 28
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 21
- 239000002699 waste material Substances 0.000 description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 description 9
- 241000700605 Viruses Species 0.000 description 8
- 230000000844 anti-bacterial effect Effects 0.000 description 8
- 229910001220 stainless steel Inorganic materials 0.000 description 8
- 239000010935 stainless steel Substances 0.000 description 8
- 102000004190 Enzymes Human genes 0.000 description 7
- 108090000790 Enzymes Proteins 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 7
- 238000002955 isolation Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 7
- 238000004659 sterilization and disinfection Methods 0.000 description 7
- 239000002912 waste gas Substances 0.000 description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 6
- 230000001580 bacterial effect Effects 0.000 description 5
- -1 hydroxyl free radical Chemical class 0.000 description 5
- 238000009413 insulation Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- 230000002159 abnormal effect Effects 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 239000000796 flavoring agent Substances 0.000 description 4
- 235000019634 flavors Nutrition 0.000 description 4
- 230000001699 photocatalysis Effects 0.000 description 4
- 208000035473 Communicable disease Diseases 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000011449 brick Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 201000010099 disease Diseases 0.000 description 3
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 3
- 208000015181 infectious disease Diseases 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 239000012774 insulation material Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 230000002940 repellent Effects 0.000 description 3
- 239000005871 repellent Substances 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 244000052616 bacterial pathogen Species 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 230000000740 bleeding effect Effects 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000007146 photocatalysis Methods 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- 230000029058 respiratory gaseous exchange Effects 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- WURBVZBTWMNKQT-UHFFFAOYSA-N 1-(4-chlorophenoxy)-3,3-dimethyl-1-(1,2,4-triazol-1-yl)butan-2-one Chemical compound C1=NC=NN1C(C(=O)C(C)(C)C)OC1=CC=C(Cl)C=C1 WURBVZBTWMNKQT-UHFFFAOYSA-N 0.000 description 1
- 229940126655 NDI-034858 Drugs 0.000 description 1
- 241000290929 Nimbus Species 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- 230000037237 body shape Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000002354 daily effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000005560 droplet transmission Effects 0.000 description 1
- 238000005183 dynamical system Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 210000003953 foreskin Anatomy 0.000 description 1
- 230000002070 germicidal effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 150000002466 imines Chemical class 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000001968 nicotinic acid Nutrition 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000005180 public health Effects 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000000241 respiratory effect Effects 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/006—General arrangement of incineration plant, e.g. flow sheets
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
- F23G5/0276—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/085—High-temperature heating means, e.g. plasma, for partly melting the waste
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/304—Burning pyrosolids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2204/00—Supplementary heating arrangements
- F23G2204/20—Supplementary heating arrangements using electric energy
- F23G2204/201—Plasma
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Plasma & Fusion (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Ion energy house refuse incineration process device and incineration process method, it is characterized in that, by incinerator, first washing tank, second washing tank, 3rd washing tank, adsorption tanks are sequentially connected with composition, wherein: supporting with incinerator has an air inlet device, one preheating device, one device for monitoring temperature and an automatic spray heat sink, there are magnetic field generator and small-power plasma torch generator, cumulonimbus layer is formed in stove when rubbish burns in incinerator, and under the action of a magnetic force, due to cumulonimbus layer and the continuously existence of magnetic field force, lightning is caused continuously to produce；In the region of lightning generation, the most continuously causing superhigh temperature to make rubbish quickly burn, harmful components are separated after adsorbent by discharge flue gas through three grades of washings.
Description
[technical field]
The invention belongs to environmental protection sciemtifec and technical sphere, relate to a kind of energy-saving, miniaturization, innoxious ion energy house refuse and burn
Change processing means and incineration process method.
[background technology]
Along with the continuous propelling of country's urbanization strategy, urban population is continuously increased, and Urban Scale constantly expands, therewith
Derivative problem the most constantly occurs, the daily social life highly impacting the people having.Wherein, town dweller is raw
Live the process problem of rubbish, it is simply that troubling a, stubborn problem.
At present, the processing method of town dweller's house refuse mainly has two kinds: one is landfill；One is to burn.
The method of landfill, simple and easy to do, cost is the lowest, is people's methods of being happy to most use, but the method for landfill is only fitted
For underpopulated rural area and outlying district, because quantity of refuse is few, can degrade in time after landfill.But the city in population concentration
Area, town is the most not all right, and owing to Urban Areas is populous, quantity of refuse is big, is piled into mountain, it is impossible to degrade in time, forms fermentation anti-
Should, produce various harmful gas and harmful liquid, enter aerial, contaminated air, permeate the ground, polluted underground water, formed ring
The heavy damage in border, the social life of the harm people.To this end, western developed country has been forbidden processing raw by the method for landfill
Rubbish alive.
The method burned, divides again two kinds: one is fuel oil and gas furnace burning；One is high power plasma incinerator
Superhigh temperature is incinerated, and generates electricity to make up energy consumption simultaneously.
Fuel oil and gas furnace burn, and advantage is that equipment is simple, easily realizes；Shortcoming is that furnace temperature is the highest, garbage disposal is clean,
Not thorough, association flue dust and harmful gas composition are many；And when after the flue dust and the entrance in the air of harmful gas composition of association, to periphery
The pollution that air ambient causes is more serious.
High power plasma incinerator superhigh temperature is incinerated, and garbage disposal is clean, thorough, and environmentally safe, is current
The life refuse processing method that western developed country is commonly used, is also the developing direction of future life technology of garbage disposal.I
State area with good conditionsi, has used the method to carry out domestic rubbish disposal the most.But, high power plasma incinerator, equipment
Complexity, gigantic project, huge investment, although garbage treatment quantity is big, but financial resources burden is the heaviest, and only large-scale central city can be born
Afford to carry on a shoulder pole, the most only large-scale central city just has the house refuse of flood tide for its process；Therefore, rubbish owning amount thin with financial resources
Relatively small general Small Urban is for no reason at all；Even if its effort is built up thoroughly, also tend to enough house refuses for it
Operate and make the idleness of equipment, waste；Cause promoting limited.
[summary of the invention]
The purpose of the present invention, be to develop high power plasma incinerator process house refuse totally, advantage thoroughly,
High power plasma incinerator is overcome to promote limited weakness, it is provided that a kind of energy-saving, miniaturization, innoxious ion
Can house refuse incineration process device.
Second object of the present invention, is to provide a kind of harmless house refuse incineration process method, and the method processes raw
Rubbish alive, clean, thorough, surrounding enviroment are not produced any pollution.
The present invention is realized energy-conservation and equipment miniaturization by following methods:
Cause a kind of magnetic field environment similar with magnetic field of the earth and cumulonimbus layer, in incinerator in cumulonimbus layer just
Anion under the action of a magnetic force, is assembled respectively, is formed negative ions group, again due to the effect of affinity, and negative ions group
The most mutually draw close again, collide and form lightning；The heat that this lightning produces, can reach the height of 28000～30000 DEG C in local
Temperature, make house refuse in local incinerate in moment, it is to avoid generally material smoulder process and due to burning
Process and produce various adverse chemicals reaction.Owing to magnetic field and cumulonimbus layer continuously exist, cause lightning the most not
Occur disconnectedly, thus realize the successive incineration of house refuse.And owing to the lightning during this is in cumulonimbus layer
Negative ions produces under magnetic field force effect, it is not necessary to external power, eliminates this main power consumption of burning process,
Save the energy to limits.
But, due to the restriction of current scientific and technological level, artificial magnetic field limited strength, the dynamics of formed artificial lightning
Also it is difficult to reach desirable level；To this end, set up small-power plasma torch generator again, make up with plasma torch
The deficiency of artificial lightning dynamics, so that people are able to according to actual needs, indiscriminately ad. as one wishes designs the use scale of incinerator.
Due to the fact that at incineration course without large-scale external power, greatly simplifie the safety management bar of equipment
Part, eliminates huge auxiliary equipment, and the miniaturization for present device creates necessary premise.
Ion energy house refuse incineration process device, it is characterised in that: by incinerator, the first washing tank, the second washing tank,
3rd washing tank, adsorption tanks are sequentially connected with composition；Wherein:
What A was supporting with incinerator has an air inlet device, preheating device, a device for monitoring temperature and
Individual automatic spray heat sink；The top of incinerator is dome, and dome, to being externally connected with air feeder, inwardly connects and has gas ash
Filter mantle；Upper cover inner top surface has the shower nozzle of automatic spray heat sink；Upper cover tilts two sides and is provided with garbage feeding door；Burning
Change and be provided with in furnace sidewall
Magnetic field generator,
Small-power plasma torch generator,
The nozzle of air inlet device,
The nozzle of preheating device,
The probe of device for monitoring temperature,
It is provided with ashpit on incinerator side wall lower ends middle part, base；
B, the first washing tank, the second washing tank and the 3rd washing tank all use totally-enclosed vertical receiver；First washing tank
Chemical washing tank, built with can the chemical substance of biochemical reaction anti-with dioxin and other oxious components, as sodium hydroxide,
The saturated alkaline mixed solution such as sodium carbonate, sodium sulfate；Second washing tank is physics washing tank, built with can dissolve dioxin and
The solvent borne material of oxious component, such as dichloro-benzenes, vegetable fatty class solution；3rd washing tank is to neutralize washing tank, built with
Can be miscible with acid-base class material and be allowed to the neutral flux separated with gas, such as H2O solution；
C, adsorption tanks use totally-enclosed vertical type cylinder material-storage jar, and the adsorbent in adsorption tanks is activated carbon or polyimides
Fiber or carbon fiber matter adsorbing material；Adsorption tanks top arranges strong drawing machine and exhaust chimney.Its effect is by washing
After gas in also the dioxin of the denier of remaining and other oxious component may carry out again the removing of the degree of depth, it is ensured that institute
Cleaning completely of discharge gas.
Described ion energy house refuse incineration process device, it is characterised in that:
Magnetic field generator: use high temperature resistant strong permanent magnets rare earth samarium cobalt magnet to make, also can be made by alnico magnet,
The structure of permanent magnet can be spherical or cylindrical shape or rectangular-shaped；Magnetic field generator is placed in the four of incinerator medial wall
Angle or other positions of sidewall.Magnetic field generator produced stove internal magnetic field intensity is 3～30 teslas；Magnetic field generator is high temperature resistant
More than 400 DEG C.
Small-power plasma torch generator: arrange 1～6；Every power is 10～30kW；Adjacent magnetic field generator it
Under, it is placed in corner or other positions of sidewall of incinerator medial wall.
Described ion energy house refuse incineration process device, it is characterised in that:
Air inlet device: include aerator, flow control valve, nozzle, be sequentially connected with by pipeline；Each nozzle is placed in
Corner, base or sidewall in incinerator；Blower power is: 1～3kW.Pipeline can use stainless steel tube or copper pipe or its
Its metallic conduit；
Preheating device: include gas tank, flow control valve, nozzle, be sequentially connected with by pipeline；Each nozzle is placed in sidewall
Middle and lower part；Pipeline can use stainless steel tube or copper pipe or other metallic conduit；
Automatic spray heat sink: include water pump, flow control valve, shower nozzle, be sequentially connected with by pipeline；Each shower nozzle is arranged
Edge in upper cover inner top surface surrounding；The motor switch of water pump is by the micro processor of data wire with device for monitoring temperature
Couple；Water pump is directly connected with water source；Automatic spray heat sink links with device for monitoring temperature, and working procedure is by micro computer controlled
System；Pump power is: 1～3kW.
Device for monitoring temperature: include micro processor, display and probe, connected respectively by data wire；Each probe
It is placed in the middle and upper part of sidewall.
Sidewall: include heat-insulation layer；Heat-insulation layer uses light heat insulation material；Base lays water repellent refractory brick.Base and sidewall
Joint arranges pressure angle transition block.
Described ion energy house refuse incineration process device, it is characterised in that: the first air feeder, the second air feeder, the 3rd
Air feeder, the 4th air feeder are air press, and power is 1～7kW；First air feeder, the second air feeder, the 3rd air feeder
The first shower nozzle, the second shower nozzle, the 3rd spray is connected the most respectively after connecting the first check-valves, the second check-valves, the 3rd check-valves respectively
Head；4th air feeder is directly connected into adsorption tanks；Air-introduced machine uses strength air exhauster, and power is 1～7kW.By outwards bleeding, make
Adsorption tanks afterbody forms negative pressure, with strengthen scrubbed after gas flow forces between adsorbent.
Described ion energy house refuse incineration process device, it is characterised in that: the first washing tank, the second washing can be chosen
One in tank, the 3rd washing tank is used alone, in order to dioxin in gas and oxious component few in the case of, by real
Border needs, and only carries out one-level washing: or chemical washing or physics washing or neutralize washing.
Described ion energy house refuse incineration process device, it is characterised in that: each washing tank is corresponding arranges waste water and waste liquid
Reservoir, centralized collection waste water and waste liquid, in order to focus on, utilize.Waste water and waste liquid reservoir uses concrete for making.
The method that described ion energy house refuse incineration process device carries out incineration process to house refuse, its feature exists
In: sequentially carry out according to the following step:
The first step: refuse collection；Its quantity of refuse need to guarantee that incinerator can run more than twenty four hours continuously.
Second step: garbage sorting；The single-row utilization of thing that will be available, as metal top pop tank, vial, litter decoration, cardboard,
Woodenware etc., can recycle, and do not make incineration process.
3rd step: lay fire-lighter in stove；Start air inlet device.
4th step: igniting, starts preheating device.
5th step: insert rubbish.
6th step: open plasma generator, strengthens ion concentration and temperature in stove.
7th step: when device for monitoring temperature monitoring position, middle and upper part, stove medial wall temperature reaches 100 DEG C, start automatic spray
Heat sink spray cooling, it is necessary to being to be sprayed by water with bulk form, spray 3 minutes, are spaced 7 minutes, then spray 3 points every time
Clock, successively, and controls in-furnace temperature at 60～70 DEG C, if in-furnace temperature is more than 70 DEG C, then extends spray time to 7
Minute, other are constant.In the process, form cumulonimbus layer in stove, and under the action of a magnetic force, positive and negative in cumulonimbus layer
Ion is assembled respectively, is formed negative ions group, again due to the effect of affinity, negative ions group is multiple the most mutually to be drawn close, collide and
Form lightning；Due to cumulonimbus layer and the continuously existence of magnetic field force, lightning is caused continuously to produce；Produce at lightning
The region of life, the most continuously causes superhigh temperature；Meanwhile, under the effect further of plasma torch, this superhigh temperature region
Interior house refuse is the most continuously incinerated, and generates H2、CO、CO2In the solid ashes such as gas and C；H2Fire again with CO
Burn and generate H2O and CO2, H2O vaporization and CO2Overflowing together, the volume of the solid ashes such as remaining C has greatly reduced, the most former rubbish
The 3～5% of rubbish volume, slump is deposited on bottom incinerator.Owing to the zone of action of artificial lightning and plasma torch is at center
Position, although heat is very big, and temperature is the highest, but when passing to surrounding, temperature significantly reduces, adds temperature lowering water and cumulonimbus layer
Effect, make the temperature of furnace wall and upper cover can control in prescribed limit,
8th step: when ashes reach certain thickness, such as, more than 30cm, get final product ash discharge, but need to keep bottom ash thickness 10-
20cm.Ash discharge simultaneously, adds rubbish, rubbish height in holding furnace.
9th step: in produced gas, except H2O and CO2In addition, some undesirable constituentss are also had, such as dioxin etc.；To this end,
By air feeder, check-valves, nozzle, gas is forcibly fed into washing tank and washs；Washing process divides three grades, being respectively as follows:
Learn washing, physics washing, neutralize washing；The effect of chemical washing is to eliminate the great majority in gas by the way of chemical reaction
Dioxin and other oxious component；The effect of physics washing is by the way of dissolving, remaining dioxin and oxious component
Separate from gas；The effect neutralizing washing is that the soda acid composition in gas is separated, and makes gas clean completely.
Tenth step: through the gas of washing, enters adsorption tanks, more fine through activated carbon or polyimide fiber or other carbon
The absorption of dimension matter adsorbing material, being harmful to into other by the dioxin of denier that may be the most remaining in the gas after washing
Part, carry out again the removing of the degree of depth, it is ensured that cleaning completely of discharged gas；Emit through air-introduced machine after and.
The operation principle of ion energy house refuse incineration process device of the present invention
Lightning and the superhigh temperature caused, derive from a kind of marvellous and powerful natural agent, and this power is exactly the magnetic of the earth
Field force.Marine aqueous water, under the photothermy of the sun, vaporizes and enters in air, when water loading of the air reaches
During saturation, i.e. form cumulonimbus layer.In cumulonimbus layer, negative ions gathering respectively under the effect of magnetic field of the earth power,
Formation negative ions group, again due to the effect of affinity, negative ions group is multiple the most mutually to be drawn close, collide and form lightning；Adjoint
Lightning and around local cause the superhigh temperature of about 28000～30000 DEG C.
The principle of the ion energy house refuse incineration process device of the present invention, it is simply that: in the local of a constant volume, cause
One magnetic field similar to magnetic field of the earth power and cumulonimbus layer, form artificial lightning, and come with artificial lightning institute liberated heat
Incinerate house refuse, thus save the energy to greatest extent.But due to the restriction of current scientific and technological level, artificial magnetic field strong
Spending limited, the dynamics of formed artificial lightning is also difficult to reach desirable level；To this end, set up small-power plasma again
Torch generator, makes up the deficiency of artificial lightning dynamics with plasma flare, so that people are able to according to actual needs, follow one's inclinations
Design the use scale of incinerator with being intended to
Advantages of the present invention
1, comply with the trend of mankind's environmental protection development in science and technology, use for reference the marvellous principle of the Nature mystery mighty force, use bionics
Means in environmental protection cause, creatively invented ion energy house refuse incineration process device, it is achieved that Small Urban resident
The harmless treatment of house refuse, saves the energy combustion gas of preciousness, electric power to greatest extent, without any noxious emission,
To environment without any harmful effect, there are the most real economic results in society.
2, achieve the miniaturization of town dweller's house refuse incineration process installations and facilities, invest little, floor space is little, work
Make that efficiency is high, operation cost is low, be easy to popularize.
3, simple in construction, easy and simple to handle, room temperature, normal pressure, safe and reliable, zero defects hidden danger.
4, adaptability is good, low to environmental requirement, and either cities and towns, industrial and mineral, school, military camp, island etc. have personnel to live
Region, all can install and use.
It is an object of the invention to overcome disadvantages mentioned above, it is provided that a kind of negative pressure air purifying sterilizing apparatus.
It is a further object of the present invention to provide one negative pressure air purifying sterilizing apparatus and propagate disease to by air, breathing etc.
The method that sick infectious disease operation room, Supply House decontamination area and isolation ward carries out disinfection.
The present invention uses in Negative Pressure Isolation Ward, and first, the clean air after sterilization is discharged into outdoor by the present invention, keeps away
Exempt from virus and antibacterial overseas publicity.It is indoor that next present invention can make fresh air pass through fresh air pipeline entrance, and the 3rd, negative pressure is isolated
Ward is to control respiratory infectious disease and cut off air, droplet transmission approach effectively medical treatment isolation facility, and the present invention can make to bear
Pressure isolation ward room air pressure less than outdoor and forms suction gradient in ward, control room internal contamination air shadow to external world
Ring.
Negative pressure air purifying sterilizing apparatus, has structure division and circuit control part, it is characterized in that, structure division is: at case
Internal be sequentially arranged with from the bottom up intermediate effcient filter, activated charcoal strainer, except Formaldehyde decomposition drainage screen, the efficient mistake of enzyme and sterilizing
Filter, ballast, uviol lamp, circulating fan；Top outlet inlet at casing connects T-shaped threeway, has air channel to open in T-shaped threeway
Close；The side of the T-shaped threeway that exhaust piping one end is arranged on casing, the other end of exhaust piping connects through the hole on exterior wall
At outdoor exhaust outlet assembly；Fresh air pipeline one end is arranged on the opposite side of T-shaped threeway, and the fresh air pipeline other end connects air-out
Mouthful；
Circuit control part is: have new wind air channel on & off switch, the on & off switch connecting T-shaped threeway of new wind air channel on power board
Built-in air channel switch, power board has exhaust piping on & off switch, the wind that exhaust piping on & off switch connecting T-shaped threeway is built-in
Road switchs；Power supply connects ballast, and ballast connects uviol lamp, and power supply connects circulating fan.
Described negative pressure air purifying sterilizing apparatus, is characterized in that: negative pressure air purifying sterilizing apparatus is to embed ceiling type side
Formula is arranged between ceiling and furred ceiling, by drawing quick-fried expansion tube to be fixed on the ceiling of reinforcement, is determined by screw mandrel
Suitable ceiling height, assembles the most supporting nut, flat spring washer circle fastens.
Described negative pressure air purifying sterilizing apparatus, is characterized in that: uviol lamp uses ultraviolet C wave band 253.7nmD type ultraviolet
Spool.
Described negative pressure air purifying sterilizing apparatus is to by the pathophorous infectious disease operation such as air, breathing room, supply
The method that room decontamination area and isolation ward carry out disinfection, is characterized in that: arbitrarily carry out the following step
A. the step of the first function:
A1. if indoor need waste air, using control panel to automatically turn on waste gas on & off switch, this sterilizing machine closes automatically
Close new wind air channel；ON cycle blower fan simultaneously；
A2. indoor air, dust, abnormal flavour and the antibacterial that is attached on dust carried disease germs is with negative pressure ventilation air-flow, through thick
Medium effeciency filter, activated charcoal strainer, except Formaldehyde decomposition drainage screen, the high efficiency particulate air filter of enzyme and sterilizing；Wherein intermediate effcient filter
Leach dust particle more than 0.5 μm in air；Activated charcoal strainer can adsorb the abnormal flavour in air, waste gas, removal effectively
Pollutant in air, purify for rear class and create conditions；Except Formaldehyde decomposition drainage screen decomposing formaldehyde gas, the efficient mistake of enzyme and sterilizing
Filter is efficient nano photo-catalytic filtering screen, the permanently effective generation photocatalysis of energy, produces the hydroxyl free radical of strong oxidizing property,
Can effectively decompose harmful gas in air, kill antibacterial, suppression virus activity, and be broken down into harmless material；
A3. along with the air draft of circulating fan, the uviol lamp region of high-level radiation in waste gas entrance machine；Purple in the machine
Under outer light irradiation, there is strong light-catalyzed reaction, can effectively kill by the bacterial virus in machine, decompose having in air
Evil gas, such as formaldehyde, benzene, ammonia etc., and can discharge negative oxygen ion, can be greatly improved the efficiency of air sterilizing apparatus；In air
After antibacterial is killed, the exhaust piping through casing top is discharged to outdoor；
B. the step of the second function: under the effect of this sterilizing machine, outside the air discharge chamber after sterilizing, makes room
Interior air keeps negative pressure forever, effectively prevents the bacterial virus in hospital ward to spread away；
C. the step of the 3rd function: if during the indoor new wind of needs, uses control panel to automatically turn on air channel switch, closes
Waste gas air channel, closes uviol lamp, circulating fan；Strong compensation fresh air, new wind through exhaust outlet assembly, exhaust piping, from
Switched by the built-in air channel of T-shaped threeway, the new wind of inspiration, by fresh air pipeline and air outlet to the indoor fresh sky of strong compensation
Gas.
Principle is as follows: see the step of Fig. 1 the first function: if indoor need waste air, uses control panel automatically to open
Opening waste gas on & off switch, this sterilizing machine is automatically switched off new wind air channel.The air, dust, the abnormal flavour that carry disease germs in indoor and be attached on dust
Antibacterial with negative pressure ventilation air-flow, through intermediate effcient filter, activated charcoal strainer, except Formaldehyde decomposition drainage screen, enzyme and sterilizing
High efficiency particulate air filter leaches in air dust particle more than 0.5 μm, along with the air draft of circulating fan, high-level radiation in entrance machine
Uviol lamp region；After antibacterial in air is killed, the exhaust piping through casing top is discharged to outdoor.Waste gas is disappeared
The discharge of poison, deodorizing sterilizing.By filter, activated charcoal strainer, except Formaldehyde decomposition drainage screen, the high efficiency particulate air filter of enzyme and sterilizing, purple
Outer lamp, circulating fan, T-shaped threeway, exhaust piping, exhaust outlet assembly complete.
The step of the second function: under the effect of this sterilizing machine, outside the air discharge chamber after sterilizing, makes indoor
Air keeps negative pressure forever, effectively prevents the bacterial virus in hospital ward to spread away；
The step of the 3rd function: if during the indoor new wind of needs, uses control panel to automatically turn on new wind air channel, closes useless
Gas air channel.Fresh air pipeline is arranged on the opposite side of the T-shaped threeway of casing, and the air channel built-in by T-shaped threeway switchs, new wind strength
Compensating fresh air, new wind has exported through exhaust outlet assembly, exhaust piping, T-shaped threeway, fresh air pipeline, new wind.
Properties of product and main feature:
1, negative pressure air purifying sterilizing apparatus, is according to WS/T311-2009 " hospital's isolation technology specification ", WS/T367-
2012 " medical institutions' disinfection technology standards ", WS/T368-2012 " hospital air purification management regulation ", GB 9706.1-
2007 " medical electrical equipment part 1s: safety general require ", GB 13554-2008 " high efficiency particle air filter ",
Pertinent regulations in GB19258-2012 " ultraviolet germicidal lamp ", Ministry of Public Health " disinfection technology standard " (version in 2002), and combination should
The disinfection of indoor air product that the feature of product determines.Present patent application is that the Negative Pressure Isolation Ward air cleaning of novel concept disappears
Poison air exhausting device, under the effect of this sterilizing machine, makes room air forever keep negative pressure, and the air after sterilizing is discharged
Outdoor, effectively prevents the bacterial virus in hospital ward to spread away.
2, casing air inlet fill intermediate effcient filter, activated charcoal strainer, except Formaldehyde decomposition drainage screen, enzyme and sterilizing
High efficiency particulate air filter, use unique multistage filtering, its structure is designed as modular combination, and sanitation and hygiene are very convenient, can have
Effect ground adsorbs the pollutant in the abnormal flavour in air, waste gas, removal air, purifies for rear class and creates conditions；Apply high-tech
Nano photo-catalytic semiconductor technology, the high efficiency particulate air filter being provided with enzyme and sterilizing at casing internal is efficient nano photocatalyst filter
Net, the permanently effective generation photocatalysis of energy, produce the hydroxyl free radical of strong oxidizing property, can effectively decompose harmful gas in air
Body, kill antibacterial, suppression virus activity, and be broken down into harmless material, under ultra violet lamp in the machine, occur strong
Strong light-catalyzed reaction, can effectively kill by the bacterial virus in machine, decomposes the harmful gas in air, as formaldehyde, benzene,
Ammonia etc., and negative oxygen ion can be discharged, the efficiency of air sterilizing apparatus can be greatly improved.Ultraviolet radiation sterilizes.Application ultraviolet C
Wave band 253.7nmD type ultraviolet tube, makes the antibacterial in air be killed further；During ballast work, produce high frequency voltage,
High intensity ultraviolet pipe produces ultraviolet sterilization.
[accompanying drawing explanation]
Fig. 1: ion energy house refuse incineration process process chart.
Fig. 2: ion energy house refuse incineration process apparatus structure schematic diagram.
Fig. 3: the incinerator structure schematic diagram of ion energy house refuse incineration process device.
The incinerator A-A direction view of Fig. 4: Fig. 3 intermediate ion energy house refuse incineration process device.
The incinerator B-B direction view of Fig. 5: Fig. 3 intermediate ion energy house refuse incineration process device.
[detailed description of the invention]
See Fig. 2, described ion energy house refuse incineration process device, by incinerator 1, air feeder 2, check-valves 3, ball valve 4,
Shower nozzle the 5, first washing tank the 6, second air feeder the 7, second check-valves the 8, second ball valve the 9, second shower nozzle the 10, second washing tank 11,
3rd air feeder 12, the 3rd check-valves 13, the 3rd ball valve 14, the 3rd shower nozzle 15, the 3rd washing tank 16, the 4th air feeder 17,
Four ball valves 18, adsorption tanks 19, strong drawing machine 20, exhaust chimney 21 and connection pipeline composition.
See Fig. 3, the incinerator 1 of ion energy house refuse incineration process device, including: dome 22, upper cover 23, garbage feeding
Door 24, sidewall 25, magnetic field generator 26, small-power plasma torch generator 27, air inlet device 28, ashpit 29, the end
Seat 30, preheating device 31, device for monitoring temperature 32, automatic spray heat sink 33, gas ash filter mantle 34.
Ion energy house refuse incineration process device, it is characterised in that: washed by incinerator the 1, first washing tank 6, second
Tank the 11, the 3rd washing tank 16, adsorption tanks 19 are sequentially connected with composition；Wherein:
What A was supporting with incinerator 1 has an air inlet device 31, device for monitoring temperature of 28, preheating device
32 and an automatic spray heat sink 33；The top of incinerator 1 is dome 22, and dome 22 is to being externally connected with air feeder 2, inwardly
Connect and have gas ash filter mantle 34；Upper cover 23 inner top surface has the shower nozzle of automatic spray heat sink 33；Upper cover 23 tilts both sides
Face is provided with garbage feeding door 24；Incinerator 1 sidewall 25 is provided with
Magnetic field generator 26,
Small-power plasma torch generator 27,
The nozzle of air inlet device 28,
The nozzle of preheating device 31,
The probe of device for monitoring temperature 32,
It is provided with ashpit 29 on middle part, incinerator sidewall 25 lower end, base 30；
B, first washing tank the 6, second washing tank 11 and the 3rd washing tank 16 all use totally-enclosed vertical receiver；First washes
Washing tank 6 is chemical washing tank, built with can the chemical substance of biochemical reaction anti-with dioxin and other oxious components, such as hydrogen-oxygen
Change the saturated alkaline mixed solution such as sodium, sodium carbonate, sodium sulfate；Second washing tank 11 is physics washing tank, built with dissolving
The solvent borne material of dioxin and oxious component, such as dichloro-benzenes, vegetable fatty class solution；3rd washing tank 16 is to neutralize washing
Tank, built with can be miscible with acid-base class material and be allowed to the neutral flux separated with gas, such as H2O solution；
C, adsorption tanks 19 use totally-enclosed vertical type cylinder material-storage jar, and the adsorbent in adsorption tanks 19 is activated carbon or polyamides
Imine fiber or carbon fiber matter adsorbing material；Adsorption tanks 19 top arranges strong drawing machine 20 and exhaust chimney 21.Its effect is
Carrying out again the degree of depth by dioxin and other oxious component of denier that may be the most remaining in the gas after washing
Remove, it is ensured that cleaning completely of discharged gas.
Described ion energy house refuse incineration process device, it is characterised in that:
Magnetic field generator 26: use high temperature resistant strong permanent magnets rare earth samarium cobalt magnet make, also can be iron by aluminium-nickel-cobalt magnetic
Making, the structure of permanent magnet can be spherical or cylindrical shape or rectangular-shaped；Magnetic field generator 26 is placed in inside incinerator
The corner of wall or other positions of sidewall.Magnetic field generator 26 produced stove internal magnetic field intensity is 3～30 teslas；Magnetic field occurs
Device 26 is high temperature resistant more than 400 DEG C.
Small-power plasma torch generator 27: arrange 1～6；Every power is 10～30kw；Adjacent magnetic field generator
Under 26, it is placed in corner or other positions of sidewall of incinerator medial wall.
Described ion energy house refuse incineration process device, it is characterised in that:
Air inlet device 28: include aerator, flow control valve, nozzle, be sequentially connected with by pipeline；Each nozzle disposes
Corner, base or sidewall in incinerator；Blower power is: 1～3kw.Pipeline can use stainless steel tube or copper pipe or
Other metallic conduit；
Preheating device 31: include gas tank, flow control valve, nozzle, be sequentially connected with by pipeline；Each nozzle is placed in side
The middle and lower part of wall 25；Pipeline can use stainless steel tube or copper pipe or other metallic conduit；
Automatic spray heat sink 33: include water pump, flow control valve, shower nozzle, be sequentially connected with by pipeline；Each shower nozzle sets
It is placed in the edge of upper cover inner top surface surrounding；The motor switch of water pump is processed by the micro computer of data wire with device for monitoring temperature
Device couples；Water pump is directly connected with water source；Automatic spray heat sink 33 links with device for monitoring temperature 32, and working procedure is by micro-
Computer controls；Pump power is: 1～3kW.
Device for monitoring temperature 32: include micro processor, display and probe, connected respectively by data wire；Each spy
Head is placed in the middle and upper part of sidewall 25.
Sidewall 25: include heat-insulation layer；Heat-insulation layer uses light heat insulation material；Base 30 lays water repellent refractory brick.Base with
Sidewall joint arranges pressure angle transition block.
Described ion energy house refuse incineration process device, it is characterised in that: first air feeder the 2, second air feeder 7,
Three air feeder the 12, the 4th air feeders 17 are air press, and power is 1～7kW；First air feeder the 2, second air feeder 7,
Three air feeders 12 connect the most respectively after connecting first check-valves the 3, second check-valves the 8, the 3rd check-valves 13 respectively the first shower nozzle 5,
Second shower nozzle the 10, the 3rd shower nozzle 15；4th air feeder 17 is directly connected into adsorption tanks 19；Air-introduced machine 20 uses strength air exhauster, merit
Rate is 1～7kW.By outwards bleeding, make adsorption tanks afterbody formed negative pressure, with strengthen scrubbed after gas between adsorbent
Flow forces.
Described ion energy house refuse incineration process device, it is characterised in that: the first washing tank 6 can be chosen, second wash
One washed in tank the 11, the 3rd washing tank 16 is used alone, in order to dioxin in gas and the few situation of oxious component
Under, according to actual needs, only carry out one-level washing: or chemical washing or physics washing or neutralize washing.
Described ion energy house refuse incineration process device, it is characterised in that: each washing tank is corresponding arranges waste water and waste liquid
Reservoir, centralized collection waste water and waste liquid, in order to focus on, utilize.Waste water and waste liquid reservoir uses concrete for making.
The method that described ion energy house refuse incineration process device carries out incineration process to house refuse, its feature exists
In: sequentially carry out according to the following step:
The first step: refuse collection；Its quantity of refuse need to guarantee that incinerator can run more than twenty four hours continuously.
Second step: garbage sorting；The single-row utilization of thing that will be available, as metal top pop tank, vial, litter decoration, cardboard,
Woodenware etc., can recycle, and do not make incineration process.
3rd step: lay fire-lighter in stove；Start air inlet device 28.
4th step: igniting, starts preheating device 31.
5th step: insert rubbish.
6th step: open plasma generator, strengthens ion concentration and temperature in stove.
7th step: device for monitoring temperature 32 monitors position, middle and upper part, stove medial wall 25 temperature when reaching 100 DEG C, starts automatically
Spraying ventilating device 33 spray cooling, it is necessary to being to be sprayed by water with bulk form, spray 3 minutes, are spaced 7 minutes, then spray every time
Drench 3 minutes, successively, and in-furnace temperature is controlled at 60～70 DEG C, if in-furnace temperature is more than 70 DEG C, then when extending spray
Between to 7 minutes, other are constant.In the process, formation cumulonimbus layer in stove, and under the action of a magnetic force, in cumulonimbus layer
Negative ions assemble respectively, form negative ions group, again due to the effect of affinity, negative ions group is multiple the most mutually to be drawn close,
Collide and form lightning；Due to cumulonimbus layer and the continuously existence of magnetic field force, lightning is caused continuously to produce；?
The region of lightning generation, the most continuously causes superhigh temperature；Meanwhile, under the effect further of plasma torch, this superelevation
House refuse in temperature area is the most continuously incinerated, and generates H2、CO、CO2In the solid ashes such as gas and C；H2With
CO burns and generates H2O and CO2, H2O vaporization and CO2Overflowing together, the volume of the solid ashes such as remaining C has greatly reduced, only
Having the 3～5% of former garbage bulk, slump is deposited on bottom incinerator.Due to artificial lightning and the zone of action of plasma torch
In centre, although heat is very big, and temperature is the highest, but when passing to surrounding, temperature significantly reduces, add temperature lowering water and amass
The effect of nimbus layer, makes the temperature of furnace wall and upper cover can control in prescribed limit,
8th step: when ashes reach certain thickness, such as, more than 30cm, get final product ash discharge, but need to keep bottom ash thickness 10-
20cm.Ash discharge simultaneously, adds rubbish, rubbish height in holding furnace.
9th step: in produced gas, except H2O and CO2In addition, some undesirable constituentss are also had, such as dioxin etc.；To this end,
By air feeder, check-valves, nozzle, gas is forcibly fed into washing tank and washs；Washing process divides three grades, being respectively as follows:
Learn washing, physics washing, neutralize washing；The effect of chemical washing is to eliminate the great majority in gas by the way of chemical reaction
Dioxin and other oxious component；The effect of physics washing is by the way of dissolving, remaining dioxin and oxious component
Separate from gas；The effect neutralizing washing is that the soda acid composition in gas is separated, and makes gas clean completely.
Tenth step: through the gas of washing, enters adsorption tanks, more fine through activated carbon or polyimide fiber or other carbon
The absorption of dimension matter adsorbing material, being harmful to into other by the dioxin of denier that may be the most remaining in the gas after washing
Part, carry out again the removing of the degree of depth, it is ensured that cleaning completely of discharged gas；Emit through air-introduced machine after and.
Wherein:
The incinerator 1 of described ion energy house refuse incineration process device: length × width × height size press 2400mm ×
1800mm × 2300mm makes.
The incinerator gases ash filter mantle 34 of described ion energy house refuse incineration process device: filter screen density presses 30 mesh
Make, be installed on dome lower port.
The incinerator sidewall 25 of described ion energy house refuse incineration process device: heat-insulation layer material uses asbestos.
The incinerator base 30 of described ion energy house refuse incineration process device: insulation material uses water repellent refractory brick.
The incinerator magnetic field generator 26 of described ion energy house refuse incineration process device: use high temperature resistant powerful permanent
Body rare earth samarium cobalt magnet is made by flat bar body shape, and magnetic field intensity is 20 teslas, high temperature resistant more than 400 DEG C, is installed on incinerator
The stage casing, corner of this body sidewall 25.
The incinerator small-power plasma torch generator 27 of described ion energy house refuse incineration process device: arrange 4
?；Every power is 20kw；Under adjacent magnetic field generator 26, it is placed in the corner of incinerator medial wall.
The incinerator ashpit 29 of described ion energy house refuse incineration process device: a size of H300 × L400 or H300
×L500.It is placed in the centre position on each side wall lower ends, base.
The incinerator air inlet device 28 of described ion energy house refuse incineration process device: the corner of sidewall is respectively arranged
Air inlet spray head one, is installed under small-power plasma torch generator, and bottom surface arranges air inlet five；Unified by aerator
Air inlet, each air inlet regulates air inflow respectively；Pipeline uses stainless steel tube；Blower power is: 1.5kW.
The big sidewall of incinerator preheating device 31: two of described ion energy house refuse incineration process device respectively arranges gas injection
Four, mouth, is placed in the middle and lower part of sidewall；Unification is supplied by gas tank, and each nozzle regulates firepower respectively；Pipeline uses rustless steel
Pipe.
The incinerator device for monitoring temperature of described ion energy house refuse incineration process device: two big sidewalls respectively arrange probe
3, it is placed in the middle and lower part of sidewall；Data wire uses high temperature resistant foreskin line.
The incinerator automatic spray heat sink 33 of described ion energy house refuse incineration process device: nozzle 24 is set
Individual, it is installed on the edge of upper cover inner top surface surrounding；The electric switch of automatic spray heat sink is supervised with temperature by data wire
The micro processor of control device couples, and accepts its work order；Automatic water jetting, injection flow rate and interval time are processed by micro computer
Device controls；Being supplied water by water pump is unified, each nozzle regulates injection flow rate respectively；Pipeline uses stainless steel tube；Pump power is: 1.5kW.
First air feeder the 2, second air feeder the 7, the 3rd air feeder 12 of described ion energy house refuse incineration process device,
4th air feeder 17: all use air press；Power is: 1kW.
The air-introduced machine 20 of described ion energy house refuse incineration process device: using strength air exhauster, power is: 2kW.
First washing tank the 6, second washing tank the 11, the 3rd washing tank of described ion energy house refuse incineration process device
16: all use totally-enclosed vertical receiver, stainless steel, diameter ￠ 700 × H1700；The first built-in hydroxide of washing tank 6
The saturated alkaline mixed solution such as sodium, sodium carbonate, sodium sulfate；The second built-in dichloro-benzenes of washing tank 11；3rd washing tank 16 is built-in
H2O。
The adsorption tanks 19 of described ion energy house refuse incineration process device: use totally-enclosed vertical type cylinder basin, stainless
Steel matter, diameter ￠ 1100 × H1700.Adsorbent in adsorption tanks, uses activated carbon adsorbent.
The waste liquid waste water reservoir of described ion energy house refuse incineration process device: using concrete for making, capacity is
30m3。
All standard system parts, such as: water pump, air exhauster, air press, flow control valve, stop valve and other control
Valve, connection pipeline and electronic element etc., directly chosen by market or standard component producer, perform by national standard；Remaining is non-
Standard system part, then pressed design drawing by device fabrication producer and make.
The startup of dynamical system, stopping, the micro computer by temperature monitoring system automatically controls.
After various parts is complete, by Fig. 2,3 orders, installation specification and this specification requirement, in place, debugging is being installed just
Often, after the assay was approved, operation is entered by preceding method.
Ion energy house refuse incineration process device of the present invention and incineration process method, every every day can innoxious place
The house refuse that reason 2～30,000 town dweller produced in one day；Emission is water vapour and the carbon dioxide of cleaning；To ring
Border is pollution-free, the miniaturization of ion energy house refuse incineration process device the most of the present invention and power save mode, has the most existing
Real economic results in society.
Claims (6)
1. ion energy house refuse incineration process device, it is characterised in that by incinerator, the first washing tank, the second washing tank,
Three washing tanks, adsorption tanks are sequentially connected with composition, wherein:
What A was supporting with incinerator has an air inlet device, a preheating device, a device for monitoring temperature and one certainly
Dynamic spraying ventilating device, the top of incinerator is dome, and dome, to being externally connected with air feeder, inwardly connects and has gas ash to filter
Cover, upper cover inner top surface has the shower nozzle of automatic spray heat sink, and upper cover tilts two sides and is provided with garbage feeding door, at incinerator
It is provided with on sidewall
Magnetic field generator,
Small-power plasma torch generator,
The nozzle of air inlet device,
The nozzle of preheating device,
The probe of device for monitoring temperature,
It is provided with ashpit on middle part, each lower end of incinerator sidewall, base；
B, the first washing tank, the second washing tank and the 3rd washing tank all use totally-enclosed vertical receiver, the first being of washing tank
Learn washing tank, built with can the chemical substance of biochemical reaction anti-with dioxin and other oxious components, such as sodium hydroxide, carbonic acid
Sodium, the saturated alkaline mixed solution of sodium sulfate, the second washing tank is physics washing tank, built with dissolving dioxin and be harmful to
The solvent borne material of composition, such as dichloro-benzenes, vegetable fatty class solution, the 3rd washing tank is to neutralize washing tank, built with can
Miscible with acid-base class material and be allowed to the neutral flux separated with gas, such as H2O solution；
C, adsorption tanks use totally-enclosed vertical type cylinder material-storage jar, the adsorbent in adsorption tanks be activated carbon or polyimide fiber,
Or carbon fiber matter adsorbing material, adsorption tanks top arranges strong drawing machine and exhaust chimney.
Ion energy house refuse incineration process device the most according to claim 1, it is characterised in that:
Magnetic field generator uses high temperature resistant strong permanent magnets rare earth samarium cobalt magnet to make, also can be made by alnico magnet；Permanent magnetism
The structure of body can be spherical or cylindrical shape or rectangular-shaped；
Small-power plasma torch generator, arranges 1～6, the adjacent lower section being placed in magnetic field generator.
Ion energy house refuse incineration process device the most according to claim 2, it is characterised in that:
Air inlet device, including aerator, flow control valve, nozzle, is sequentially connected with by pipeline；Preheating device, including coal
Gas tank, flow control valve, nozzle, be sequentially connected with by pipeline；Automatic spray heat sink, including water pump, flow control valve, spray
Head, is sequentially connected with by pipeline；Device for monitoring temperature, including micro processor, display and probe, by data wire respectively
Connect.
Ion energy house refuse incineration process device the most according to claim 3, it is characterised in that:
First air feeder, the second air feeder, the 3rd air feeder, the 4th air feeder are air press, and air-introduced machine is taken out for strength
Mechanism of qi.
5. according to ion energy house refuse incineration process device described in claim 1 or 2 or 3 or 4, it is characterised in that:
One can chosen in the first washing tank, the second washing tank, the 3rd washing tank is used alone, in order to two in flue gas
Dislike English and oxious component few in the case of, according to actual needs, only carry out one-level washing: or chemical washing or physics washes
Wash or neutralize washing.
Ion energy house refuse incineration process device the most according to claim 1 carries out the side of incineration process to house refuse
Method, it is characterised in that: sequentially carry out according to the following step:
The first step: refuse collection, quantity of refuse need to guarantee that incinerator can run more than twenty four hours continuously；
Second step: garbage sorting, the single-row utilization of thing that will may utilize, such as metal top pop tank, vial, litter decoration, cardboard, woodenware
Deng, can recycle, not make incineration process；
3rd step: lay fire-lighter in stove, start air inlet device；
4th step: igniting, starts preheating device；
5th step: insert rubbish；
6th step: open plasma generator, strengthens ion concentration and temperature in stove；
7th step: when device for monitoring temperature (33) monitoring stove medial wall (25) position, middle and upper part temperature reaches 100 DEG C, start automatically
Spraying ventilating device (34) spray cooling, it is necessary to being to be sprayed by water with bulk form, spray 3 minutes, are spaced 7 minutes every time, then
Spray 3 minutes, successively, and in-furnace temperature is controlled at 60～70 DEG C, if in-furnace temperature is more than 70 DEG C, then extend spray
Time, other were constant to 7 minutes, in the process, and formation cumulonimbus layer in stove, and under the action of a magnetic force, cumulonimbus layer
In negative ions assemble respectively, form negative ions group, again due to the effect of affinity, negative ions group is multiple the most mutually leans on
Hold together, collide and form lightning, due to cumulonimbus layer and the continuously existence of magnetic field force, cause the successive real estate of lightning
Raw, in the region of lightning generation, the most continuously cause superhigh temperature, meanwhile, under the effect further of plasma torch, should
House refuse in superhigh temperature region is the most continuously incinerated, and generates H2、CO、CO2In the solid ashes such as gas and C,
H2Burn generation H with CO again2O and CO2, H2O vaporization and CO2Overflowing together, the volume of the solid ashes such as remaining C the most greatly subtracts
Little, the 3～5% of the most former garbage bulk, slump is deposited on bottom incinerator, due to artificial lightning and the effect of plasma torch
Region is in centre, although heat is very big, and temperature is the highest, but when passing to surrounding, temperature significantly reduces, adds temperature lowering water
With the effect of cumulonimbus layer, make the temperature of furnace wall and upper cover can control in prescribed limit.
8th step: when ashes reach certain thickness, such as, more than 30cm, get final product ash discharge, but need to keep bottom ash thickness 10-
20cm.Ash discharge simultaneously, adds rubbish, rubbish height in holding furnace；
9th step: in produced gas, except H2O and CO2In addition, also have some undesirable constituentss, such as dioxin, to this end, by giving
Mechanism of qi, check-valves, nozzle, be forcibly fed into washing tank by gas and wash, and washing process divides three grades, be respectively as follows: chemical washing,
Physics washing, neutralization washing；The effect of chemical washing is to eliminate the most of dioxin in gas by the way of chemical reaction
And other oxious component, the effect of physics washing is by the way of dissolving, remaining dioxin and oxious component from gas
In separate, neutralize washing effect be that the soda acid composition in gas is separated, make gas clean completely；
Tenth step: through the gas of washing, enters adsorption tanks, then through activated carbon or polyimide fiber or other carbon fiber matter
The absorption of adsorbing material, dioxin and other oxious component of the denier by remaining may be gone back in the gas after washing,
Carry out again the removing of the degree of depth, it is ensured that cleaning completely of discharged gas, and after emit through air-introduced machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610629462.9A CN106090928B (en) | 2016-08-03 | 2016-08-03 | Ion energy house refuse incineration process device and incineration process method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610629462.9A CN106090928B (en) | 2016-08-03 | 2016-08-03 | Ion energy house refuse incineration process device and incineration process method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106090928A true CN106090928A (en) | 2016-11-09 |
| CN106090928B CN106090928B (en) | 2019-02-05 |
Family
ID=57453854
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610629462.9A Active CN106090928B (en) | 2016-08-03 | 2016-08-03 | Ion energy house refuse incineration process device and incineration process method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106090928B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109442431A (en) * | 2018-12-06 | 2019-03-08 | 航天环境工程有限公司 | A kind of power regulating system of the DC plasma torch using constant current source power supply and application |
| CN109839010A (en) * | 2019-03-26 | 2019-06-04 | 宁夏三元中泰冶金有限公司 | A kind of large-scale mineral heating furnace flue residual heat reutilizing system removing dioxin |
| CN109847556A (en) * | 2019-04-04 | 2019-06-07 | 哈尔滨工大环能科技有限公司 | A kind of rubbish mineralising processing equipment |
| CN113231428A (en) * | 2021-04-16 | 2021-08-10 | 光大环境修复(江苏)有限公司 | Gas distribution station, system and adjusting method for ecological restoration of household garbage landfill |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3113190B2 (en) * | 1995-10-26 | 2000-11-27 | 義次 桜井 | Waste oil incinerator using incinerator |
| CN1432119A (en) * | 2001-04-02 | 2003-07-23 | 菊地政市 | Small ion-decomposing melting furnace |
| CN202898333U (en) * | 2012-10-18 | 2013-04-24 | 东南大学 | Negative ion oxygen-free straw burning device |
| CN104482539A (en) * | 2014-12-12 | 2015-04-01 | 台州伟博环保设备科技有限公司 | Plasma cracking device |
| CN206055631U (en) * | 2016-08-03 | 2017-03-29 | 辜美全 | Ion energy house refuse incineration process device |
-
2016
- 2016-08-03 CN CN201610629462.9A patent/CN106090928B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3113190B2 (en) * | 1995-10-26 | 2000-11-27 | 義次 桜井 | Waste oil incinerator using incinerator |
| CN1432119A (en) * | 2001-04-02 | 2003-07-23 | 菊地政市 | Small ion-decomposing melting furnace |
| CN202898333U (en) * | 2012-10-18 | 2013-04-24 | 东南大学 | Negative ion oxygen-free straw burning device |
| CN104482539A (en) * | 2014-12-12 | 2015-04-01 | 台州伟博环保设备科技有限公司 | Plasma cracking device |
| CN206055631U (en) * | 2016-08-03 | 2017-03-29 | 辜美全 | Ion energy house refuse incineration process device |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109442431A (en) * | 2018-12-06 | 2019-03-08 | 航天环境工程有限公司 | A kind of power regulating system of the DC plasma torch using constant current source power supply and application |
| CN109839010A (en) * | 2019-03-26 | 2019-06-04 | 宁夏三元中泰冶金有限公司 | A kind of large-scale mineral heating furnace flue residual heat reutilizing system removing dioxin |
| CN109839010B (en) * | 2019-03-26 | 2024-03-12 | 宁夏三元中泰冶金有限公司 | Large submerged arc furnace flue gas waste heat recycling system for removing dioxin |
| CN109847556A (en) * | 2019-04-04 | 2019-06-07 | 哈尔滨工大环能科技有限公司 | A kind of rubbish mineralising processing equipment |
| CN109847556B (en) * | 2019-04-04 | 2024-05-21 | 哈尔滨工大环能科技有限公司 | Garbage mineralization treatment equipment |
| CN113231428A (en) * | 2021-04-16 | 2021-08-10 | 光大环境修复(江苏)有限公司 | Gas distribution station, system and adjusting method for ecological restoration of household garbage landfill |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106090928B (en) | 2019-02-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106090928A (en) | Ion energy house refuse incineration process device and incineration process method | |
| US20220016305A1 (en) | Indoor and outdoor nano air purifier and system comprising said purifier | |
| CN206055631U (en) | Ion energy house refuse incineration process device | |
| CN106734103B (en) | Magnetization decomposition device and method for household garbage treatment | |
| CN205109350U (en) | Energy -concerving and environment -protective type domestic sewage septic tank gas conditioning equipment | |
| CN206244566U (en) | A kind of night soil-treatment lavatory | |
| CN211952789U (en) | Distributed medical waste incineration treatment system | |
| CN109364593A (en) | A kind of paint-spraying baking booth waste gas processing method and device | |
| CN201421147Y (en) | Disinfection and purification device | |
| CN111998346A (en) | Garbage disposal equipment | |
| CN201289090Y (en) | Flyash combustible recycling and dioxin pollution removing device | |
| CN204026685U (en) | One way of life high temperature garbage anaerobism pyrolysis system | |
| CN111495130A (en) | Ion deodorizing device for high-humidity waste gas | |
| CN207422231U (en) | A kind of waste incinerator with Novel filter device | |
| CN109931617A (en) | A kind of innoxious incineration treatment of garbage technique | |
| CN204799006U (en) | Device is recycled in disinfection based on exhaust gases filter | |
| CN205782951U (en) | A kind of environment protection garbage incineration device | |
| CN212680578U (en) | Peculiar smell deodorization clarifier is used in workshop | |
| CN101224463A (en) | Processing device of waste battery and poisonous condensate | |
| CN101496995B (en) | Malodorous gas processing system and processing method thereof | |
| CN103994457A (en) | Flue gas cleaning device with flue gas quencher | |
| CN108817039B (en) | Deodorant room in msw pond of msw incineration power plant | |
| CN203469781U (en) | UV light oxygen deodorizer | |
| CN208493814U (en) | A kind of dioxin removing means of applications catalyst | |
| CN202938394U (en) | Pipeline-insertion type photochemical cooking fume odor remover |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210826 Address after: 610000 No. 13-1-5, unit 1, building 1, No. 199, middle section of Tianfu Avenue, Chengdu hi tech Zone, Chengdu pilot Free Trade Zone, Sichuan Province Patentee after: RUINENG ELECTRIC POWER Co.,Ltd. Address before: 518000 dormitory 506 of shangmeilin Zhongkang company, Futian District, Shenzhen City, Guangdong Province Patentee before: Gu Mei Quan |
|
| TR01 | Transfer of patent right |