CN115738161A - Method for degrading toxic and harmful substances in fire residues - Google Patents
Method for degrading toxic and harmful substances in fire residues Download PDFInfo
- Publication number
- CN115738161A CN115738161A CN202211419744.8A CN202211419744A CN115738161A CN 115738161 A CN115738161 A CN 115738161A CN 202211419744 A CN202211419744 A CN 202211419744A CN 115738161 A CN115738161 A CN 115738161A
- Authority
- CN
- China
- Prior art keywords
- solid waste
- fire
- harmful substances
- toxic
- sodium
- 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
- 239000000126 substance Substances 0.000 title claims abstract description 60
- 231100000331 toxic Toxicity 0.000 title claims abstract description 36
- 230000002588 toxic effect Effects 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 33
- 230000000593 degrading effect Effects 0.000 title claims abstract description 16
- 239000002910 solid waste Substances 0.000 claims abstract description 106
- 230000015556 catabolic process Effects 0.000 claims abstract description 35
- 238000006731 degradation reaction Methods 0.000 claims abstract description 35
- 229920002521 macromolecule Polymers 0.000 claims abstract description 10
- 239000003440 toxic substance Substances 0.000 claims abstract description 8
- 231100000614 poison Toxicity 0.000 claims abstract description 6
- 239000003463 adsorbent Substances 0.000 claims description 33
- 239000002265 redox agent Substances 0.000 claims description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 26
- 239000000463 material Substances 0.000 claims description 26
- 239000007789 gas Substances 0.000 claims description 19
- 239000003795 chemical substances by application Substances 0.000 claims description 17
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 238000002309 gasification Methods 0.000 claims description 15
- 238000000197 pyrolysis Methods 0.000 claims description 15
- 239000000440 bentonite Substances 0.000 claims description 13
- 229910000278 bentonite Inorganic materials 0.000 claims description 13
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims description 13
- 239000002351 wastewater Substances 0.000 claims description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 10
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 10
- 239000008394 flocculating agent Substances 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 230000018044 dehydration Effects 0.000 claims description 8
- 238000006297 dehydration reaction Methods 0.000 claims description 8
- -1 precipitants Substances 0.000 claims description 8
- 230000003472 neutralizing effect Effects 0.000 claims description 7
- 238000006479 redox reaction Methods 0.000 claims description 7
- 150000003384 small molecules Chemical class 0.000 claims description 6
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims description 5
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 5
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 5
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 claims description 5
- 239000005708 Sodium hypochlorite Substances 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 5
- 229910021536 Zeolite Inorganic materials 0.000 claims description 5
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 5
- 239000000920 calcium hydroxide Substances 0.000 claims description 5
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 5
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 5
- 239000000292 calcium oxide Substances 0.000 claims description 5
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 5
- 239000004927 clay Substances 0.000 claims description 5
- 229910052570 clay Inorganic materials 0.000 claims description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 5
- 239000011790 ferrous sulphate Substances 0.000 claims description 5
- 235000003891 ferrous sulphate Nutrition 0.000 claims description 5
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 5
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 5
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 5
- 229910017604 nitric acid Inorganic materials 0.000 claims description 5
- 229920002401 polyacrylamide Polymers 0.000 claims description 5
- 239000012286 potassium permanganate Substances 0.000 claims description 5
- 239000000741 silica gel Substances 0.000 claims description 5
- 229910002027 silica gel Inorganic materials 0.000 claims description 5
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 5
- HRZFUMHJMZEROT-UHFFFAOYSA-L sodium disulfite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])(=O)=O HRZFUMHJMZEROT-UHFFFAOYSA-L 0.000 claims description 5
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 claims description 5
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 5
- 235000010262 sodium metabisulphite Nutrition 0.000 claims description 5
- 229910052979 sodium sulfide Inorganic materials 0.000 claims description 5
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 5
- 239000010457 zeolite Substances 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 4
- 230000001376 precipitating effect Effects 0.000 claims description 3
- 206010021143 Hypoxia Diseases 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 230000033116 oxidation-reduction process Effects 0.000 claims description 2
- 230000007096 poisonous effect Effects 0.000 claims description 2
- 239000002699 waste material Substances 0.000 claims description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims 2
- 239000000383 hazardous chemical Substances 0.000 claims 1
- 230000001146 hypoxic effect Effects 0.000 claims 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 32
- 238000011282 treatment Methods 0.000 abstract description 20
- 238000003911 water pollution Methods 0.000 abstract description 19
- 239000002480 mineral oil Substances 0.000 abstract description 4
- 235000010446 mineral oil Nutrition 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 description 32
- 238000001179 sorption measurement Methods 0.000 description 16
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 12
- 239000003814 drug Substances 0.000 description 9
- 239000003344 environmental pollutant Substances 0.000 description 8
- 231100000719 pollutant Toxicity 0.000 description 8
- 239000011269 tar Substances 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000006386 neutralization reaction Methods 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 239000008213 purified water Substances 0.000 description 4
- 238000005345 coagulation Methods 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- 238000009270 solid waste treatment Methods 0.000 description 3
- 231100000167 toxic agent Toxicity 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 235000019645 odor Nutrition 0.000 description 2
- 230000035943 smell Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 150000002605 large molecules Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000013585 weight reducing agent Substances 0.000 description 1
Images
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
本发明涉及有毒有害物质降解技术领域,且公开了一种火灾残留物有毒有害物质降解方法,包括以下步骤:S1:有毒物质收集,对变电站发生火灾后所产生的固体废物进行收集,并将收集好的固体废物放入固体废物一体化处理器中,等待统一处理,同时对被矿物油所污染的水进行收集,放入水污染一体化处理器中。本发明不仅能够使降解完成的固体废物中的大分子发生断裂,产生小分子气体、焦油和残渣,实现固体废物的无害化、减量化和资源化,从而对固体废物进行再循环利用,回收能源和资源,节省了能源,而且能够实现水体和大气可以进行二次使用,改善了环境减小了污染,还能够快速有效的对固体废物进行降解,提高了对固体废物的降解效率。
The invention relates to the technical field of degradation of toxic and harmful substances, and discloses a method for degrading toxic and harmful substances in fire residues, which includes the following steps: S1: collecting toxic substances, collecting solid waste generated after a fire in a substation, and collecting Good solid waste is put into the integrated solid waste processor, waiting for unified treatment, and at the same time, the water polluted by mineral oil is collected and put into the integrated water pollution processor. The invention can not only break the macromolecules in the degraded solid waste, produce small molecular gas, tar and residue, realize the harmlessness, reduction and resource utilization of solid waste, and thus recycle the solid waste, Recycling energy and resources saves energy, and enables water and air to be reused, improves the environment and reduces pollution, and can quickly and effectively degrade solid waste, improving the degradation efficiency of solid waste.
Description
技术领域technical field
本发明涉及有毒有害物质降解技术领域,具体为一种火灾残留物有毒有害物质降解方法。The invention relates to the technical field of degradation of toxic and harmful substances, in particular to a method for degrading toxic and harmful substances of fire residues.
背景技术Background technique
变电站是把一些设备组装起来,用以切断或接通、改变或者调整电压,在电力系统中,变电站是输电和配电的集结点,变电站主要分为:升压变电站,主网变电站,二次变电站,配电站,由于变电站属于高压场所,在变电站内一不小心便会引发火灾,火焰燃烧变电站后,会产生大量的有毒有害物质。A substation is an assembly of some equipment to cut off or connect, change or adjust the voltage. In the power system, the substation is the assembly point of power transmission and distribution. The substation is mainly divided into: step-up substation, main network substation, secondary Substations, distribution substations, because the substation is a high-voltage place, if you are not careful in the substation, it will cause a fire. After the flame burns the substation, a large amount of toxic and harmful substances will be produced.
在变电站发生火灾后,如果不及时对有毒有害物质进行降解,则会对环境造成非常大的影响,但是现有的降解方法降解不全面,无法对变电站火灾后所留下的有毒有害物质进行全方位的降解,所以提出一种火灾残留物有毒有害物质降解方法。After a substation fire, if the toxic and harmful substances are not degraded in time, it will have a very large impact on the environment, but the existing degradation methods are not comprehensive, and cannot fully degrade the toxic and harmful substances left after the substation fire. Therefore, a method for the degradation of toxic and harmful substances in fire residues is proposed.
发明内容Contents of the invention
(一)解决的技术问题(1) Solved technical problems
针对现有技术的不足,本发明提供了一种火灾残留物有毒有害物质降解方法,主要为解决现有的现有的降解方法降解不全面,无法对变电站火灾后所留下的有毒有害物质进行全方位的降解的问题。Aiming at the deficiencies of the prior art, the present invention provides a method for degrading toxic and harmful substances in fire residues, mainly to solve the problem that the existing existing degradation methods are not fully degraded, and the toxic and harmful substances left after substation fires cannot be degraded. A full range of degradation problems.
(二)技术方案(2) Technical solution
为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:
1.一种火灾残留物有毒有害物质降解方法,其特征在于,其方法包括以下步骤:1. A fire residue poisonous and harmful substance degradation method is characterized in that, its method comprises the following steps:
S1:获取发生火灾后所产生的固体废物;S1: Obtain solid waste generated after a fire;
S2:对所述固体废物进行脱水和破碎处理,获取固定废物中脱离的废水;S2: Dehydrating and crushing the solid waste to obtain waste water separated from the fixed waste;
S3:利用氧化还原剂对固体废物中的有毒有害物质进行氧化还原反应,降解所述固体废物;S3: using a redox agent to carry out redox reactions on toxic and harmful substances in the solid waste to degrade the solid waste;
S4:利用中和剂对被降解后的固体废物进行pH值中和,以及使用热解气化炉对固体废物进行热解气化;S4: Use a neutralizer to neutralize the pH value of the degraded solid waste, and use a pyrolysis gasifier to pyrolyze and gasify the solid waste;
S5:利用氧化还原剂对废水中的有毒有害物质进行氧化还原反应,随后依次加入吸附剂、沉淀剂和絮凝剂之后,对废水进行过滤;S5: Use oxidation-reduction agents to perform oxidation-reduction reactions on toxic and harmful substances in wastewater, and then add adsorbents, precipitants and flocculants in sequence to filter wastewater;
S6:利用中和剂对过滤后的废水进行pH中和;S6: Using a neutralizer to neutralize the pH of the filtered wastewater;
S7:在火灾发生处上空分别喷洒氧化还原剂、吸附剂、沉淀剂、絮凝剂和中和剂,直到火灾发生处的大气环境恢复正常标准;S7: Spray redox agents, adsorbents, precipitants, flocculants and neutralizers over the fire site until the atmospheric environment returns to normal standards;
S8:对火灾发生处进行清理。S8: Clean up the place where the fire occurred.
进一步地,所述步骤S2中脱水的时间为20-30min,破碎的时间为10-15min,破碎的转率为500-800r/min。Further, in the step S2, the dehydration time is 20-30 minutes, the crushing time is 10-15 minutes, and the crushing rotation rate is 500-800 r/min.
进一步地,所述S5中吸附剂的制作材料包括下述中的至少一种:活性炭、硅胶、矾土、白土、膨润土和沸石。Further, the material for making the adsorbent in S5 includes at least one of the following: activated carbon, silica gel, alumina, clay, bentonite and zeolite.
进一步地,所述中和剂的制作材料包括下述中的至少一种:硫酸、盐酸、硝酸、碳酸钠、碳酸氢钠、氢氧化钙、氢氧化钠和氧化钙。Further, the manufacturing material of the neutralizer includes at least one of the following: sulfuric acid, hydrochloric acid, nitric acid, sodium carbonate, sodium bicarbonate, calcium hydroxide, sodium hydroxide and calcium oxide.
进一步地,所述氧化还原剂的制作材料均包括下述中的至少一种:双氧水、高锰酸钾、次氯酸钠、焦亚硫酸钠、亚硫酸氢钠、硫酸亚铁。Further, the materials for making the redox agent include at least one of the following: hydrogen peroxide, potassium permanganate, sodium hypochlorite, sodium pyrosulfite, sodium bisulfite, and ferrous sulfate.
进一步地,所述絮凝剂的制作材料包括下述中的至少一种:聚丙烯酰胺、三氯化铁、聚合氯化铝、聚合硫酸铁。Further, the material for making the flocculant includes at least one of the following: polyacrylamide, ferric chloride, polyaluminum chloride, and polyferric sulfate.
进一步地,所述沉淀剂的制作材料包括下述中的至少一种:硫化钠,所述S4中固化剂的制作材料包括乙二胺、苯酚、甲醛和曼其尼。Further, the preparation material of the precipitant includes at least one of the following: sodium sulfide, and the preparation material of the curing agent in S4 includes ethylenediamine, phenol, formaldehyde and mancini.
进一步地,所述步骤S4中热解气化是指在无氧或缺氧的条件下,固体废物中有机组分的大分子发生断裂,产生小分子气体、焦油和残渣的过程。Further, the pyrolysis and gasification in the step S4 refers to a process in which the macromolecules of the organic components in the solid waste are broken to produce small molecule gas, tar and residue under the condition of no oxygen or oxygen deficiency.
(三)有益效果(3) Beneficial effects
与现有技术相比,本发明提供了一种火灾残留物有毒有害物质降解方法,具备以下有益效果:Compared with the prior art, the present invention provides a method for degrading toxic and harmful substances in fire residues, which has the following beneficial effects:
1、本发明通过对降解完成的固体废物进行热解气化处理,使降解完成的固体废物中的大分子发生断裂,产生小分子气体、焦油和残渣,实现固体废物的无害化、减量化和资源化,从而对固体废物进行再循环利用,回收能源和资源,节省了能源。1. The present invention performs pyrolysis and gasification treatment on the degraded solid waste to break the macromolecules in the degraded solid waste to produce small molecular gas, tar and residue, so as to realize the harmlessness and weight reduction of solid waste It can recycle solid waste, recycle energy and resources, and save energy.
2、本发明通过对液体和大气进行吸附、氧化还原、沉淀、凝固和中和一系列处理,能够完全的降解水体和大气中的污染物,同时还中和了水体和大气中的PH值,使水体和大气能够正常的使用,让水体和大气可以进行二次使用,改善了环境减小了污染。2. The present invention can completely degrade the pollutants in the water body and the atmosphere by performing a series of treatments of adsorption, redox, precipitation, solidification and neutralization on the liquid and the atmosphere, and at the same time neutralize the pH value in the water body and the atmosphere, The water body and the atmosphere can be used normally, and the water body and the atmosphere can be used for secondary use, which improves the environment and reduces pollution.
3、本发明通过使用活性炭和膨润土制作吸附剂,活性炭能够快速的对水体和大气中的污染物和异味进行吸附,同时膨润土对各种气体、液体、有机物质有一定的吸附能力,最大吸附量可达5倍于自身的重量,在两者的配合下,使吸附剂能够快速的对净化过后的水体和大气中的物质进行吸附,提高了吸附剂的吸附效果。3. The present invention uses activated carbon and bentonite to make adsorbents. Activated carbon can quickly adsorb pollutants and odors in water and the atmosphere. At the same time, bentonite has a certain adsorption capacity for various gases, liquids, and organic substances. The maximum adsorption capacity is It can be up to 5 times its own weight. With the cooperation of the two, the adsorbent can quickly adsorb the purified water and the substances in the atmosphere, and the adsorption effect of the adsorbent is improved.
4、本发明通过对固体废物进行收集、脱水和破碎的一系列处理,方便对固体废物进行统一的处理,而且能够更好对固体废物进行氧化还原和中和处理,能够快速有效的对固体废物进行降解,提高了对固体废物的降解效率。4. The present invention facilitates the uniform treatment of solid waste through a series of treatments of collecting, dehydrating and crushing solid waste, and can better redox and neutralize solid waste, and can quickly and effectively treat solid waste Degradation is carried out, and the degradation efficiency of solid waste is improved.
附图说明Description of drawings
图1为本发明提出的一种火灾残留物有毒有害物质降解方法的流程结构示意图。FIG. 1 is a schematic flow chart of a method for degrading toxic and harmful substances in fire residues proposed by the present invention.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
实施例1Example 1
参照图1,一种火灾残留物有毒有害物质降解方法,包括以下步骤:Referring to Fig. 1, a method for degrading toxic and harmful substances of fire residues comprises the following steps:
S1:有毒物质收集,对变电站发生火灾后所产生的固体废物进行收集,并将收集好的固体废物放入固体废物一体化处理器中,等待统一处理,同时对被矿物油所污染的水进行收集,放入水污染一体化处理器中;S1: Toxic substance collection, collect the solid waste generated after the fire in the substation, and put the collected solid waste into the solid waste integrated processor, waiting for unified treatment, and at the same time carry out the water polluted by mineral oil Collect and put into the integrated water pollution processor;
S2:固体废物处理,使用固体废物一体化处理器中的脱水机构和破碎机构对收集好的固体废物进行脱水和破碎处理,并将从固体废物上脱离的废水输送进水污染一体化处理器中,本发明通过对固体废物进行收集、脱水和破碎的一系列处理,方便对固体废物进行统一的处理,而且能够更好对固体废物进行氧化还原和中和处理,能够快速有效的对固体废物进行降解,提高了对固体废物的降解效率;S2: Solid waste treatment, use the dehydration mechanism and crushing mechanism in the solid waste integrated processor to dehydrate and crush the collected solid waste, and transport the wastewater separated from the solid waste into the water pollution integrated processor , the present invention facilitates the uniform treatment of solid waste through a series of treatments of collecting, dehydrating and crushing solid waste, and can better redox and neutralize solid waste, and can quickly and effectively treat solid waste Degradation, improving the degradation efficiency of solid waste;
S3:备药,使用溶药装置将吸附剂、中和剂、絮凝剂、氧化还原剂和沉淀剂依次进行溶解,将上述溶解好的药物装好以待备用;S3: Prepare the medicine, use the medicine dissolving device to dissolve the adsorbent, neutralizing agent, flocculant, redox agent and precipitant in sequence, and pack the above dissolved medicine for standby;
S4:固体废物降解,将溶解好的氧化还原剂加入到加药器中,使用加药器均匀的向固体废物一体化处理器中加入氧化还原剂,对固体废物中的有毒有害物质进行氧化还原反应,使固体废物开始降解,然后使用加药器均匀的向固体废物一体化处理器中加入溶解好的中和剂,对被降解后的固体废物进行PH值中和,最后使用热解气化炉对固体废物进行热解气化,使固体废物进二次利用,本发明通过对降解完成的固体废物进行热解气化处理,使降解完成的固体废物中的大分子发生断裂,产生小分子气体、焦油和残渣,实现固体废物的无害化、减量化和资源化,从而对固体废物进行再循环利用,回收能源和资源,节省了能源;S4: Degradation of solid waste, adding the dissolved redox agent to the dosing device, using the dosing device to evenly add the redox agent to the solid waste integrated processor, and redox the toxic and harmful substances in the solid waste React to make the solid waste start to degrade, then use the doser to evenly add the dissolved neutralizer to the solid waste integrated processor, neutralize the pH value of the degraded solid waste, and finally use pyrolysis gasification The furnace performs pyrolysis and gasification on the solid waste, so that the solid waste can be used for secondary use. The present invention performs pyrolysis and gasification treatment on the degraded solid waste, so that the macromolecules in the degraded solid waste are broken to produce small molecules Gas, tar and residue, realize the harmlessness, reduction and recycling of solid waste, so as to recycle solid waste, recover energy and resources, and save energy;
S5:液体降解,使用加药器向水污染一体化处理器中均匀的加入氧化还原剂,对液体中的有毒有害物质进行氧化还原反应,然后使用加药器向水污染一体化处理器中均匀的加入吸附剂,液体降解后所产生的物质进行吸附,随后使用加药器均匀的向水污染一体化处理器中加入沉淀剂,使液体中吸附后物质进行快速沉淀,然后使用加药器均匀的向水污染一体化处理器中加入絮凝剂,对沉淀的物质进行凝聚,然后对液体进行过滤,将凝聚的物体过滤出来,并对其进行分解,最后使用加药器均匀的向水污染一体化处理器中加入中和剂,对液体的PH值进行中和,让液体能够二次使用;S5: Liquid degradation, use a dosing device to evenly add redox agents to the integrated water pollution processor, perform oxidation-reduction reactions on toxic and harmful substances in the liquid, and then use a dosing device to uniformly add redox agents to the integrated water pollution processor The adsorbent is added, and the substances produced after the liquid degradation are adsorbed, and then the precipitant is evenly added to the integrated water pollution processor using the dosing device, so that the adsorbed substances in the liquid are rapidly precipitated, and then the dosing device is used to evenly Add flocculants to the water pollution integrated processor to condense the precipitated substances, then filter the liquid, filter out the condensed objects, and decompose them, and finally use the dosing device to uniformly pour the water into the whole Neutralizing agent is added to the chemical processor to neutralize the pH value of the liquid so that the liquid can be used again;
S6:气体降解,通知所有工作人员待在建筑内不要出来,然后将S4中溶解后吸附剂、中和剂、絮凝剂、氧化还原剂、沉淀剂分别加入到五个不同喷洒器中,然后使用直升机携带喷洒器在变电站上空依次进行喷洒氧化还原剂、吸附剂、沉淀剂、絮凝剂和中和剂,对变电站上空的大气进行降解和中和,从而使变电站周围的大气环境恢复正常标准,本发明通过对液体和大气进行吸附、氧化还原、沉淀、凝固和中和一系列处理,能够完全的降解水体和大气中的污染物,同时还中和了水体和大气中的PH值,使水体和大气能够正常的使用,让水体和大气可以进行二次使用,改善了环境减小了污染;S6: Gas degradation, inform all staff to stay in the building and not come out, then add the dissolved adsorbent, neutralizer, flocculant, redox agent, and precipitant in S4 to five different sprayers, and then use Helicopters carry sprinklers to spray redox agents, adsorbents, precipitants, flocculants and neutralizers in sequence over the substation to degrade and neutralize the atmosphere above the substation, thereby restoring the atmospheric environment around the substation to normal standards. The invention can completely degrade the pollutants in the water body and the atmosphere through a series of treatments of adsorption, redox, precipitation, coagulation and neutralization on the liquid and the atmosphere, and at the same time neutralize the pH value of the water body and the atmosphere, making the water body and the atmosphere The atmosphere can be used normally, so that the water body and the atmosphere can be used twice, which improves the environment and reduces pollution;
S7:结束收尾,对变电站内的固体废物、液体和气体中所含有的有毒有害物质进行降解完成后,对变电站所有的地面和建筑进行统一的打扫,将有毒物质降解后的遗留物质进行收集并清理。S7: At the end of the finishing touch, after the degradation of the toxic and harmful substances contained in the solid waste, liquid and gas in the substation is completed, all the ground and buildings of the substation are cleaned uniformly, and the residual substances after the degradation of toxic substances are collected and collected. clean up.
本发明的,S2中脱水的时间为20min,S3中破碎的时间为10min,破碎的转率为500r/min,S3中吸附剂的制作材料包括:活性炭、硅胶、矾土、白土、膨润土和沸石,本发明通过使用活性炭和膨润土制作吸附剂,活性炭能够快速的对水体和大气中的污染物和异味进行吸附,同时膨润土对各种气体、液体、有机物质有一定的吸附能力,最大吸附量可达5倍于自身的重量,在两者的配合下,使吸附剂能够快速的对净化过后的水体和大气中的物质进行吸附,提高了吸附剂的吸附效果,S3中和剂的制作材料包括硫酸、盐酸、硝酸、碳酸钠、碳酸氢钠、氢氧化钙、氢氧化钠和氧化钙。In the present invention, the time of dehydration in S2 is 20min, the time of crushing in S3 is 10min, and the turning rate of crushing is 500r/min, and the making materials of adsorbent in S3 include: activated carbon, silica gel, alumina, white clay, bentonite and zeolite , the present invention makes adsorbent by using activated carbon and bentonite, activated carbon can quickly adsorb pollutants and peculiar smells in water and air, while bentonite has certain adsorption capacity for various gases, liquids and organic substances, and the maximum adsorption capacity can be It is up to 5 times its own weight. With the cooperation of the two, the adsorbent can quickly adsorb the purified water and the substances in the atmosphere, which improves the adsorption effect of the adsorbent. The production materials of S3 neutralizer include Sulfuric Acid, Hydrochloric Acid, Nitric Acid, Sodium Carbonate, Sodium Bicarbonate, Calcium Hydroxide, Sodium Hydroxide, and Calcium Oxide.
本发明中,需要特别说明的,S3中氧化还原剂的制作材料包括双氧水、高锰酸钾、次氯酸钠、焦亚硫酸钠、亚硫酸氢钠、硫酸亚铁,S3中絮凝剂的制作材料包括聚丙烯酰胺、三氯化铁、聚合氯化铝、聚合硫酸铁,S3中沉淀剂的制作材料包括硫化钠,S4中固化剂的制作材料包括乙二胺、苯酚、甲醛和曼其尼,S5中热解气化是指在无氧或缺氧的条件下,固体废物中有机组分的大分子发生断裂,产生小分子气体、焦油和残渣的过程。In the present invention, it needs to be specially explained that the production materials of the redox agent in S3 include hydrogen peroxide, potassium permanganate, sodium hypochlorite, sodium pyrosulfite, sodium bisulfite, and ferrous sulfate, and the production materials of the flocculant in S3 include polyacrylamide , ferric chloride, polyaluminum chloride, polyferric sulfate, the precipitating agent in S3 includes sodium sulfide, the curing agent in S4 includes ethylenediamine, phenol, formaldehyde and mancini, and pyrolyzes in S5 Gasification refers to the process in which the macromolecules of organic components in solid waste are broken to produce small molecular gases, tar and residues under the condition of anaerobic or anoxic.
实施例2Example 2
参照图1,一种火灾残留物有毒有害物质降解方法,包括以下步骤:Referring to Fig. 1, a method for degrading toxic and harmful substances of fire residues comprises the following steps:
S1:有毒物质收集,对变电站发生火灾后所产生的固体废物进行收集,并将收集好的固体废物放入固体废物一体化处理器中,等待统一处理,同时对被矿物油所污染的水进行收集,放入水污染一体化处理器中;S1: Toxic substance collection, collect the solid waste generated after the fire in the substation, and put the collected solid waste into the solid waste integrated processor, waiting for unified treatment, and at the same time carry out the water polluted by mineral oil Collect and put into the integrated water pollution processor;
S2:固体废物处理,使用固体废物一体化处理器中的脱水机构和破碎机构对收集好的固体废物进行脱水和破碎处理,并将从固体废物上脱离的废水输送进水污染一体化处理器中,本发明通过对固体废物进行收集、脱水和破碎的一系列处理,方便对固体废物进行统一的处理,而且能够更好对固体废物进行氧化还原和中和处理,能够快速有效的对固体废物进行降解,提高了对固体废物的降解效率;S2: Solid waste treatment, use the dehydration mechanism and crushing mechanism in the solid waste integrated processor to dehydrate and crush the collected solid waste, and transport the wastewater separated from the solid waste into the water pollution integrated processor , the present invention facilitates the uniform treatment of solid waste through a series of treatments of collecting, dehydrating and crushing solid waste, and can better redox and neutralize solid waste, and can quickly and effectively treat solid waste Degradation, improving the degradation efficiency of solid waste;
S3:备药,使用溶药装置将吸附剂、中和剂、絮凝剂、氧化还原剂和沉淀剂依次进行溶解,将上述溶解好的药物装好以待备用;S3: Prepare the medicine, use the medicine dissolving device to dissolve the adsorbent, neutralizing agent, flocculant, redox agent and precipitant in sequence, and pack the above dissolved medicine for standby;
S4:固体废物降解,将溶解好的氧化还原剂加入到加药器中,使用加药器均匀的向固体废物一体化处理器中加入氧化还原剂,对固体废物中的有毒有害物质进行氧化还原反应,使固体废物开始降解,然后使用加药器均匀的向固体废物一体化处理器中加入溶解好的中和剂,对被降解后的固体废物进行PH值中和,最后使用热解气化炉对固体废物进行热解气化,使固体废物进二次利用,本发明通过对降解完成的固体废物进行热解气化处理,使降解完成的固体废物中的大分子发生断裂,产生小分子气体、焦油和残渣,实现固体废物的无害化、减量化和资源化,从而对固体废物进行再循环利用,回收能源和资源,节省了能源;S4: Degradation of solid waste, adding the dissolved redox agent to the dosing device, using the dosing device to evenly add the redox agent to the solid waste integrated processor, and redox the toxic and harmful substances in the solid waste React to make the solid waste start to degrade, then use the doser to evenly add the dissolved neutralizer to the solid waste integrated processor, neutralize the pH value of the degraded solid waste, and finally use pyrolysis gasification The furnace performs pyrolysis and gasification on the solid waste, so that the solid waste can be used for secondary use. The present invention performs pyrolysis and gasification treatment on the degraded solid waste, so that the macromolecules in the degraded solid waste are broken to produce small molecules Gas, tar and residue, realize the harmlessness, reduction and recycling of solid waste, so as to recycle solid waste, recover energy and resources, and save energy;
S5:液体降解,使用加药器向水污染一体化处理器中均匀的加入氧化还原剂,对液体中的有毒有害物质进行氧化还原反应,然后使用加药器向水污染一体化处理器中均匀的加入吸附剂,液体降解后所产生的物质进行吸附,随后使用加药器均匀的向水污染一体化处理器中加入沉淀剂,使液体中吸附后物质进行快速沉淀,然后使用加药器均匀的向水污染一体化处理器中加入絮凝剂,对沉淀的物质进行凝聚,然后对液体进行过滤,将凝聚的物体过滤出来,并对其进行分解,最后使用加药器均匀的向水污染一体化处理器中加入中和剂,对液体的PH值进行中和,让液体能够二次使用;S5: Liquid degradation, use a dosing device to evenly add redox agents to the integrated water pollution processor, perform oxidation-reduction reactions on toxic and harmful substances in the liquid, and then use a dosing device to uniformly add redox agents to the integrated water pollution processor The adsorbent is added, and the substances produced after the liquid degradation are adsorbed, and then the precipitant is evenly added to the integrated water pollution processor using the dosing device, so that the adsorbed substances in the liquid are rapidly precipitated, and then the dosing device is used to evenly Add flocculants to the water pollution integrated processor to condense the precipitated substances, then filter the liquid, filter out the condensed objects, and decompose them, and finally use the dosing device to uniformly pour the water into the whole Neutralizing agent is added to the chemical processor to neutralize the pH value of the liquid so that the liquid can be used again;
S6:气体降解,通知所有工作人员待在建筑内不要出来,然后将S4中溶解后吸附剂、中和剂、絮凝剂、氧化还原剂、沉淀剂分别加入到五个不同喷洒器中,然后使用直升机携带喷洒器在变电站上空依次进行喷洒氧化还原剂、吸附剂、沉淀剂、絮凝剂和中和剂,对变电站上空的大气进行降解和中和,从而使变电站周围的大气环境恢复正常标准,本发明通过对液体和大气进行吸附、氧化还原、沉淀、凝固和中和一系列处理,能够完全的降解水体和大气中的污染物,同时还中和了水体和大气中的PH值,使水体和大气能够正常的使用,让水体和大气可以进行二次使用,改善了环境减小了污染;S6: Gas degradation, inform all staff to stay in the building and not come out, then add the dissolved adsorbent, neutralizer, flocculant, redox agent, and precipitant in S4 to five different sprayers, and then use Helicopters carry sprinklers to spray redox agents, adsorbents, precipitants, flocculants and neutralizers in sequence over the substation to degrade and neutralize the atmosphere above the substation, thereby restoring the atmospheric environment around the substation to normal standards. The invention can completely degrade the pollutants in the water body and the atmosphere through a series of treatments of adsorption, redox, precipitation, coagulation and neutralization on the liquid and the atmosphere, and at the same time neutralize the pH value of the water body and the atmosphere, making the water body and the atmosphere The atmosphere can be used normally, so that the water body and the atmosphere can be used twice, which improves the environment and reduces pollution;
S7:结束收尾,对变电站内的固体废物、液体和气体中所含有的有毒有害物质进行降解完成后,对变电站所有的地面和建筑进行统一的打扫,将有毒物质降解后的遗留物质进行收集并清理。S7: At the end of the finishing touch, after the degradation of the toxic and harmful substances contained in the solid waste, liquid and gas in the substation is completed, all the ground and buildings of the substation are cleaned uniformly, and the residual substances after the degradation of toxic substances are collected and collected. clean up.
本发明的,S2中脱水的时间为25min,S3中破碎的时间为12min,破碎的转率为650r/min,S3中吸附剂的制作材料包括:活性炭、硅胶、矾土、白土、膨润土和沸石,本发明通过使用活性炭和膨润土制作吸附剂,活性炭能够快速的对水体和大气中的污染物和异味进行吸附,同时膨润土对各种气体、液体、有机物质有一定的吸附能力,最大吸附量可达5倍于自身的重量,在两者的配合下,使吸附剂能够快速的对净化过后的水体和大气中的物质进行吸附,提高了吸附剂的吸附效果,S3中和剂的制作材料包括硫酸、盐酸、硝酸、碳酸钠、碳酸氢钠、氢氧化钙、氢氧化钠和氧化钙。In the present invention, the time of dehydration in S2 is 25min, the time of crushing in S3 is 12min, and the turning rate of crushing is 650r/min, and the making material of adsorbent in S3 includes: activated carbon, silica gel, alumina, white clay, bentonite and zeolite , the present invention makes adsorbent by using activated carbon and bentonite, activated carbon can quickly adsorb pollutants and peculiar smells in water and air, while bentonite has certain adsorption capacity for various gases, liquids and organic substances, and the maximum adsorption capacity can be It is up to 5 times its own weight. With the cooperation of the two, the adsorbent can quickly adsorb the purified water and the substances in the atmosphere, which improves the adsorption effect of the adsorbent. The production materials of S3 neutralizer include Sulfuric Acid, Hydrochloric Acid, Nitric Acid, Sodium Carbonate, Sodium Bicarbonate, Calcium Hydroxide, Sodium Hydroxide, and Calcium Oxide.
本发明中,需要特别说明的,S3中氧化还原剂的制作材料包括双氧水、高锰酸钾、次氯酸钠、焦亚硫酸钠、亚硫酸氢钠、硫酸亚铁,S3中絮凝剂的制作材料包括聚丙烯酰胺、三氯化铁、聚合氯化铝、聚合硫酸铁,S3中沉淀剂的制作材料包括硫化钠,S4中固化剂的制作材料包括乙二胺、苯酚、甲醛和曼其尼,S5中热解气化是指在无氧或缺氧的条件下,固体废物中有机组分的大分子发生断裂,产生小分子气体、焦油和残渣的过程。In the present invention, it needs to be specially explained that the production materials of the redox agent in S3 include hydrogen peroxide, potassium permanganate, sodium hypochlorite, sodium pyrosulfite, sodium bisulfite, and ferrous sulfate, and the production materials of the flocculant in S3 include polyacrylamide , ferric chloride, polyaluminum chloride, polyferric sulfate, the precipitating agent in S3 includes sodium sulfide, the curing agent in S4 includes ethylenediamine, phenol, formaldehyde and mancini, and pyrolyzes in S5 Gasification refers to the process in which the macromolecules of organic components in solid waste are broken to produce small molecular gases, tar and residues under the condition of anaerobic or anoxic.
实施例3Example 3
参照图1,一种火灾残留物有毒有害物质降解方法,包括以下步骤:Referring to Fig. 1, a method for degrading toxic and harmful substances of fire residues comprises the following steps:
S1:有毒物质收集,对变电站发生火灾后所产生的固体废物进行收集,并将收集好的固体废物放入固体废物一体化处理器中,等待统一处理,同时对被矿物油所污染的水进行收集,放入水污染一体化处理器中;S1: Toxic substance collection, collect the solid waste generated after the fire in the substation, and put the collected solid waste into the solid waste integrated processor, waiting for unified treatment, and at the same time carry out the water polluted by mineral oil Collect and put into the integrated water pollution processor;
S2:固体废物处理,使用固体废物一体化处理器中的脱水机构和破碎机构对收集好的固体废物进行脱水和破碎处理,并将从固体废物上脱离的废水输送进水污染一体化处理器中,本发明通过对固体废物进行收集、脱水和破碎的一系列处理,方便对固体废物进行统一的处理,而且能够更好对固体废物进行氧化还原和中和处理,能够快速有效的对固体废物进行降解,提高了对固体废物的降解效率;S2: Solid waste treatment, use the dehydration mechanism and crushing mechanism in the solid waste integrated processor to dehydrate and crush the collected solid waste, and transport the wastewater separated from the solid waste into the water pollution integrated processor , the present invention facilitates the uniform treatment of solid waste through a series of treatments of collecting, dehydrating and crushing solid waste, and can better redox and neutralize solid waste, and can quickly and effectively treat solid waste Degradation, improving the degradation efficiency of solid waste;
S3:备药,使用溶药装置将吸附剂、中和剂、絮凝剂、氧化还原剂和沉淀剂依次进行溶解,将上述溶解好的药物装好以待备用;S3: Prepare the medicine, use the medicine dissolving device to dissolve the adsorbent, neutralizing agent, flocculant, redox agent and precipitant in sequence, and pack the above dissolved medicine for standby;
S4:固体废物降解,将溶解好的氧化还原剂加入到加药器中,使用加药器均匀的向固体废物一体化处理器中加入氧化还原剂,对固体废物中的有毒有害物质进行氧化还原反应,使固体废物开始降解,然后使用加药器均匀的向固体废物一体化处理器中加入溶解好的中和剂,对被降解后的固体废物进行PH值中和,最后使用热解气化炉对固体废物进行热解气化,使固体废物进二次利用,本发明通过对降解完成的固体废物进行热解气化处理,使降解完成的固体废物中的大分子发生断裂,产生小分子气体、焦油和残渣,实现固体废物的无害化、减量化和资源化,从而对固体废物进行再循环利用,回收能源和资源,节省了能源;S4: Degradation of solid waste, adding the dissolved redox agent to the dosing device, using the dosing device to evenly add the redox agent to the solid waste integrated processor, and redox the toxic and harmful substances in the solid waste React to make the solid waste start to degrade, then use the doser to evenly add the dissolved neutralizer to the solid waste integrated processor, neutralize the pH value of the degraded solid waste, and finally use pyrolysis gasification The furnace performs pyrolysis and gasification on the solid waste, so that the solid waste can be used for secondary use. The present invention performs pyrolysis and gasification treatment on the degraded solid waste, so that the macromolecules in the degraded solid waste are broken to produce small molecules Gas, tar and residue, realize the harmlessness, reduction and recycling of solid waste, so as to recycle solid waste, recover energy and resources, and save energy;
S5:液体降解,使用加药器向水污染一体化处理器中均匀的加入氧化还原剂,对液体中的有毒有害物质进行氧化还原反应,然后使用加药器向水污染一体化处理器中均匀的加入吸附剂,液体降解后所产生的物质进行吸附,随后使用加药器均匀的向水污染一体化处理器中加入沉淀剂,使液体中吸附后物质进行快速沉淀,然后使用加药器均匀的向水污染一体化处理器中加入絮凝剂,对沉淀的物质进行凝聚,然后对液体进行过滤,将凝聚的物体过滤出来,并对其进行分解,最后使用加药器均匀的向水污染一体化处理器中加入中和剂,对液体的PH值进行中和,让液体能够二次使用;S5: Liquid degradation, use a dosing device to evenly add redox agents to the integrated water pollution processor, perform oxidation-reduction reactions on toxic and harmful substances in the liquid, and then use a dosing device to uniformly add redox agents to the integrated water pollution processor The adsorbent is added, and the substances produced after the liquid degradation are adsorbed, and then the precipitant is evenly added to the integrated water pollution processor using the dosing device, so that the adsorbed substances in the liquid are rapidly precipitated, and then the dosing device is used to evenly Add flocculants to the water pollution integrated processor to condense the precipitated substances, then filter the liquid, filter out the condensed objects, and decompose them, and finally use the dosing device to uniformly pour the water into the whole Neutralizing agent is added to the chemical processor to neutralize the pH value of the liquid so that the liquid can be used again;
S6:气体降解,通知所有工作人员待在建筑内不要出来,然后将S4中溶解后吸附剂、中和剂、絮凝剂、氧化还原剂、沉淀剂分别加入到五个不同喷洒器中,然后使用直升机携带喷洒器在变电站上空依次进行喷洒氧化还原剂、吸附剂、沉淀剂、絮凝剂和中和剂,对变电站上空的大气进行降解和中和,从而使变电站周围的大气环境恢复正常标准,本发明通过对液体和大气进行吸附、氧化还原、沉淀、凝固和中和一系列处理,能够完全的降解水体和大气中的污染物,同时还中和了水体和大气中的PH值,使水体和大气能够正常的使用,让水体和大气可以进行二次使用,改善了环境减小了污染;S6: Gas degradation, inform all staff to stay in the building and not come out, then add the dissolved adsorbent, neutralizer, flocculant, redox agent, and precipitant in S4 to five different sprayers, and then use Helicopters carry sprinklers to spray redox agents, adsorbents, precipitants, flocculants and neutralizers in sequence over the substation to degrade and neutralize the atmosphere above the substation, thereby restoring the atmospheric environment around the substation to normal standards. The invention can completely degrade the pollutants in the water body and the atmosphere through a series of treatments of adsorption, redox, precipitation, coagulation and neutralization on the liquid and the atmosphere, and at the same time neutralize the pH value of the water body and the atmosphere, making the water body and the atmosphere The atmosphere can be used normally, so that the water body and the atmosphere can be used twice, which improves the environment and reduces pollution;
S7:结束收尾,对变电站内的固体废物、液体和气体中所含有的有毒有害物质进行降解完成后,对变电站所有的地面和建筑进行统一的打扫,将有毒物质降解后的遗留物质进行收集并清理。S7: At the end of the finishing touch, after the degradation of the toxic and harmful substances contained in the solid waste, liquid and gas in the substation is completed, all the ground and buildings of the substation are cleaned uniformly, and the residual substances after the degradation of toxic substances are collected and collected. clean up.
高锰酸钾、次氯酸钠、焦亚硫酸钠、亚硫酸氢钠、硫酸亚铁,S3中絮本发明的,S2中脱水的时间为30min,S3中破碎的时间为15min,破碎的转率为800r/min,S3中吸附剂的制作材料包括:活性炭、硅胶、矾土、白土、膨润土和沸石,本发明通过使用活性炭和膨润土制作吸附剂,活性炭能够快速的对水体和大气中的污染物和异味进行吸附,同时膨润土对各种气体、液体、有机物质有一定的吸附能力,最大吸附量可达5倍于自身的重量,在两者的配合下,使吸附剂能够快速的对净化过后的水体和大气中的物质进行吸附,提高了吸附剂的吸附效果,S3中和剂的制作材料包括硫酸、盐酸、硝酸、碳酸钠、碳酸氢钠、氢氧化钙、氢氧化钠和氧化钙。Potassium permanganate, sodium hypochlorite, sodium pyrosulfite, sodium bisulfite, ferrous sulfate, the flocculation of the present invention in S3, the dehydration time in S2 is 30min, the crushing time in S3 is 15min, and the crushing conversion rate is 800r/min , The materials for making the adsorbent in S3 include: activated carbon, silica gel, bauxite, clay, bentonite and zeolite. The present invention uses activated carbon and bentonite to make the adsorbent, and the activated carbon can quickly adsorb pollutants and odors in water and the atmosphere At the same time, bentonite has a certain adsorption capacity for various gases, liquids, and organic substances, and the maximum adsorption capacity can reach 5 times its own weight. With the cooperation of the two, the adsorbent can quickly detoxify the purified water and atmosphere. The substances in the neutralizer are adsorbed, which improves the adsorption effect of the adsorbent. The materials of the S3 neutralizer include sulfuric acid, hydrochloric acid, nitric acid, sodium carbonate, sodium bicarbonate, calcium hydroxide, sodium hydroxide and calcium oxide.
本发明中,需要特别说明的,S3中氧化还原剂的制作材料包括双氧水、凝剂的制作材料包括聚丙烯酰胺、三氯化铁、聚合氯化铝、聚合硫酸铁,S3中沉淀剂的制作材料包括硫化钠,S4中固化剂的制作材料包括乙二胺、苯酚、甲醛和曼其尼,S5中热解气化是指在无氧或缺氧的条件下,固体废物中有机组分的大分子发生断裂,产生小分子气体、焦油和残渣的过程。In the present invention, it needs to be specified that the production materials of the redox agent in S3 include hydrogen peroxide, and the production materials of the coagulant include polyacrylamide, ferric chloride, polyaluminum chloride, polyferric sulfate, and the preparation of the precipitant in S3 The materials include sodium sulfide. The materials for the curing agent in S4 include ethylenediamine, phenol, formaldehyde and mancini. The pyrolysis and gasification in S5 refers to the decomposition of organic components in solid waste under the condition of anaerobic or anoxic. The process in which large molecules break down to produce small molecule gases, tars, and residues.
在该文中的描述中,需要说明的是,诸如第一和第二等之类的关系术语仅仅用来将一个实体或者操作与另一个实体或操作区分开来,而不一定要求或者暗示这些实体或操作之间存在任何这种实际的关系或者顺序。而且,术语“包括”、“包含”或者其任何其他变体意在涵盖非排他性的包含,从而使得包括一系列要素的过程、方法、物品或者设备不仅包括那些要素,而且还包括没有明确列出的其他要素,或者是还包括为这种过程、方法、物品或者设备所固有的要素。In the description in this article, it should be noted that relational terms such as first and second etc. are only used to distinguish one entity or operation from another entity or operation and do not necessarily require or imply that these entities or operations, any such actual relationship or order exists. Furthermore, the term "comprises", "comprises" or any other variation thereof is intended to cover a non-exclusive inclusion such that a process, method, article, or apparatus comprising a set of elements includes not only those elements, but also includes elements not expressly listed. other elements of or also include elements inherent in such a process, method, article, or device.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211419744.8A CN115738161B (en) | 2022-11-14 | 2022-11-14 | A method for degrading toxic and harmful substances in fire residues |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202211419744.8A CN115738161B (en) | 2022-11-14 | 2022-11-14 | A method for degrading toxic and harmful substances in fire residues |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115738161A true CN115738161A (en) | 2023-03-07 |
CN115738161B CN115738161B (en) | 2024-06-18 |
Family
ID=85371261
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202211419744.8A Active CN115738161B (en) | 2022-11-14 | 2022-11-14 | A method for degrading toxic and harmful substances in fire residues |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115738161B (en) |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1243558A1 (en) * | 2001-03-20 | 2002-09-25 | SILICA VERFAHRENSTECHNIK GmbH | Process for removing halogenated pollutants from industrial wastewater |
CN110627325A (en) * | 2019-10-16 | 2019-12-31 | 新疆水处理工程技术研究中心有限公司 | Process method for treating food wastewater |
CN110759610A (en) * | 2019-12-24 | 2020-02-07 | 山东万圣博化工有限公司 | Adhesive industrial wastewater treatment method |
CN110937730A (en) * | 2019-05-08 | 2020-03-31 | 安阳师范学院 | Method for recovering organic nutrients and water in organic synthetic industrial waste |
CN111195647A (en) * | 2020-03-11 | 2020-05-26 | 贵州美瑞特环保科技有限公司 | Flash evaporation treatment system and method for recycling multi-element mercury-containing dangerous solid waste resources |
CN112077125A (en) * | 2020-09-15 | 2020-12-15 | 四川同益环境科技有限责任公司 | Energy treatment method for household garbage |
CN112209528A (en) * | 2020-10-20 | 2021-01-12 | 广东佳德环保科技有限公司 | Method for synergistic treatment of desulfurization wastewater and fly ash |
KR102207832B1 (en) * | 2020-03-10 | 2021-02-10 | (주)상길테크 | Organic Waste and Waste Liquid Homogenization Advanced Pretreatment Apparatus and Method |
CN113275370A (en) * | 2021-05-19 | 2021-08-20 | 国网福建省电力有限公司 | Transformer substation's electrical equipment conflagration soil pollutant processing apparatus |
-
2022
- 2022-11-14 CN CN202211419744.8A patent/CN115738161B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1243558A1 (en) * | 2001-03-20 | 2002-09-25 | SILICA VERFAHRENSTECHNIK GmbH | Process for removing halogenated pollutants from industrial wastewater |
CN110937730A (en) * | 2019-05-08 | 2020-03-31 | 安阳师范学院 | Method for recovering organic nutrients and water in organic synthetic industrial waste |
CN110627325A (en) * | 2019-10-16 | 2019-12-31 | 新疆水处理工程技术研究中心有限公司 | Process method for treating food wastewater |
CN110759610A (en) * | 2019-12-24 | 2020-02-07 | 山东万圣博化工有限公司 | Adhesive industrial wastewater treatment method |
KR102207832B1 (en) * | 2020-03-10 | 2021-02-10 | (주)상길테크 | Organic Waste and Waste Liquid Homogenization Advanced Pretreatment Apparatus and Method |
CN111195647A (en) * | 2020-03-11 | 2020-05-26 | 贵州美瑞特环保科技有限公司 | Flash evaporation treatment system and method for recycling multi-element mercury-containing dangerous solid waste resources |
CN112077125A (en) * | 2020-09-15 | 2020-12-15 | 四川同益环境科技有限责任公司 | Energy treatment method for household garbage |
CN112209528A (en) * | 2020-10-20 | 2021-01-12 | 广东佳德环保科技有限公司 | Method for synergistic treatment of desulfurization wastewater and fly ash |
CN113275370A (en) * | 2021-05-19 | 2021-08-20 | 国网福建省电力有限公司 | Transformer substation's electrical equipment conflagration soil pollutant processing apparatus |
Non-Patent Citations (1)
Title |
---|
韩宝平: "《固体废物处理与利用》", 中国矿业大学出版社, pages: 164 - 165 * |
Also Published As
Publication number | Publication date |
---|---|
CN115738161B (en) | 2024-06-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS6247572B2 (en) | ||
CN112807874A (en) | Resource utilization system and method for hazardous waste incineration fly ash and deacidification washing water | |
CN111569625A (en) | System and method for in-situ removing and purifying peculiar smell in pesticide polluted site | |
CN107159684B (en) | Domestic waste incineration fly ash and waste SCR catalyst co-treatment method | |
CN1850371A (en) | Micro-wave heating desorption/alkyl catalytic decomposition treatment method for polychlorinated biphenyl in soil | |
CN111266394A (en) | A kind of efficient dechlorination agent and dechlorination method and device for waste incineration fly ash | |
CN102921278A (en) | Method for collaboratively controlling multi-pollutants produced from waste incineration smokes | |
CN102068890A (en) | Method and device for treating complex industrial organic waste gas | |
CN101732822A (en) | Method for treating waste or soil polluted by heavy metal or dioxin | |
CN111195647B (en) | A flash treatment system and method for recycling multi-component mercury-containing hazardous solid waste resources | |
CN103949153A (en) | Method and device for purifying flue gas by utilizing photochemical Fenton reaction | |
CN111847480A (en) | A kind of purification treatment and resource recycling method of industrial sodium chloride waste salt | |
CN105233641A (en) | Deep purifying method and device for dioxin and mercury which are generated in waste incineration | |
CN104984743A (en) | Preparation method of waste-derived adsorbent for removing mercury, and product thereof | |
WO2021203708A1 (en) | Landfill leachate stench purification device and process thereof | |
CN111744922A (en) | Fly ash treatment process in waste incineration process | |
CN111450660A (en) | Landfill leachate odor purification device and process thereof | |
CN205717254U (en) | The high-efficiency environment friendly exhaust gas processing device that a kind of chemical plant is special | |
CN115738161A (en) | Method for degrading toxic and harmful substances in fire residues | |
CN205517195U (en) | Be used for garbage incinerator smoke and dust purifier | |
CN211938390U (en) | Flash distillation processing system that many units contain dangerous solid waste resource recovery of mercury | |
CN111847483A (en) | A kind of comprehensive treatment and reuse method of industrial inorganic waste salt containing organic pollutants | |
CN206152606U (en) | Rubbish stench integrated processing system | |
CN214108258U (en) | A processing system for thermally desorbed waste incineration fly ash | |
CN212731610U (en) | Landfill leachate odor purification device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |