TWI789600B - Method for enhancing stabilization and detoxification of thermal treatment facilities collected powder - Google Patents
Method for enhancing stabilization and detoxification of thermal treatment facilities collected powder Download PDFInfo
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- 239000000843 powder Substances 0.000 title claims abstract description 47
- 238000000034 method Methods 0.000 title claims abstract description 22
- 230000006641 stabilisation Effects 0.000 title claims abstract description 19
- 238000011105 stabilization Methods 0.000 title claims abstract description 19
- 238000001784 detoxification Methods 0.000 title abstract description 4
- 238000007669 thermal treatment Methods 0.000 title abstract 2
- 230000002708 enhancing effect Effects 0.000 title 1
- 238000011282 treatment Methods 0.000 claims abstract description 17
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 15
- 239000002002 slurry Substances 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 150000002013 dioxins Chemical class 0.000 claims abstract description 10
- 125000005575 polycyclic aromatic hydrocarbon group Chemical group 0.000 claims abstract description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000010828 elution Methods 0.000 claims abstract description 6
- 239000000126 substance Substances 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 15
- 239000000428 dust Substances 0.000 claims description 14
- 238000002156 mixing Methods 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 4
- 239000003381 stabilizer Substances 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- 230000001737 promoting effect Effects 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 229910052717 sulfur Inorganic materials 0.000 claims description 2
- 239000011593 sulfur Substances 0.000 claims description 2
- 229910019142 PO4 Inorganic materials 0.000 claims 1
- 238000004091 panning Methods 0.000 claims 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims 1
- 239000010452 phosphate Substances 0.000 claims 1
- 239000002253 acid Substances 0.000 abstract description 4
- 239000000383 hazardous chemical Substances 0.000 abstract description 3
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 abstract description 2
- 238000001514 detection method Methods 0.000 abstract 2
- 238000003915 air pollution Methods 0.000 abstract 1
- 231100001261 hazardous Toxicity 0.000 abstract 1
- 239000002440 industrial waste Substances 0.000 abstract 1
- 239000002956 ash Substances 0.000 description 4
- 239000010881 fly ash Substances 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 235000019739 Dicalciumphosphate Nutrition 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000010882 bottom ash Substances 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 239000010883 coal ash Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- NEFBYIFKOOEVPA-UHFFFAOYSA-K dicalcium phosphate Chemical compound [Ca+2].[Ca+2].[O-]P([O-])([O-])=O NEFBYIFKOOEVPA-UHFFFAOYSA-K 0.000 description 1
- 229940038472 dicalcium phosphate Drugs 0.000 description 1
- 229910000390 dicalcium phosphate Inorganic materials 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000003895 groundwater pollution Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
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Abstract
Description
本發明係與熱處理設施產生含有害重金屬及/或有害有機污染物之集塵粉體之穩定化及無害化技術領域有關,尤其本方法為較便捷且有效之促進集塵粉體之穩定化與無害化方法,藉由逐步處理與判斷步驟,將集塵粉體有害物質去除或降低至再利用標準,而利於後續成為再利用原料。 The present invention is related to the technical field of stabilization and detoxification of dust-collecting powder containing harmful heavy metals and/or harmful organic pollutants produced by heat treatment facilities. The harmless method, through the step-by-step processing and judgment steps, removes or reduces the harmful substances in the dust collection powder to the reuse standard, which is conducive to subsequent reuse of raw materials.
熱處理設施(如金屬冶煉/熔煉廠、粉末冶金廠、垃圾焚化廠、醫療廢棄物焚化爐、有害廢氣燃燒爐等)之空污防制設備(APCDs)中,其集塵設備(如旋風集塵器、靜電集塵器、洗滌塔、袋式集塵器等)所收集之粉體,常含重金屬、戴奧辛(DXN)、多環芳香烴(PAHs)等有害物質,經檢測後常為有害事業廢棄物且無法再利用。由於此類集塵粉體性質仍有所差異,如有的以無機之重金屬為主、有的以有機之戴奧辛為主、有的以有機之多環芳香烴為主、或有的兼而有前述 有害物質,故不易有一較簡便之穩定化及無害化方法。因此,目前市面上處理此類有害集塵粉體之作法多以水泥固化為主,其後再將固化物進行掩埋處置。惟固化不僅增加粉體廢棄物體積,且固化物長期置於掩埋場,降雨時可能溶出有害物質,造成土壤、地表水、或地下水之污染。 Dust collection equipment (such as cyclone dust collection dust collector, electrostatic precipitator, washing tower, bag filter, etc.) often contain harmful substances such as heavy metals, dioxins (DXN), polycyclic aromatic hydrocarbons (PAHs), and are often harmful substances after testing waste and cannot be reused. Due to the differences in the properties of such dust-collecting powders, for example, some are mainly composed of inorganic heavy metals, some are mainly composed of organic dioxins, some are mainly composed of organic polycyclic aromatic hydrocarbons, or some are composed of both. aforementioned Hazardous substances, so it is not easy to have a simpler method of stabilization and harmlessness. Therefore, most of the methods currently on the market to deal with such harmful dust-collecting powders are solidified with cement, and then the solidified matter is buried for disposal. However, solidification not only increases the volume of powder waste, but also the solidified material is placed in a landfill for a long time, and harmful substances may be dissolved out during rainfall, causing soil, surface water, or groundwater pollution.
習知相關高溫處理後粉體或物質之處理技術,如下列中華民國發明或新型專利案或公開案: Known technologies for processing powders or substances after high-temperature treatment, such as the following ROC invention or new patents or publications:
發明第301697號「灰燼之穩定與再利用」;發明第468021號「灰熔融方法及灰熔融爐」;發明第502099號「再加工垃圾熱處理之爐渣及/或灰燼之方法」;第I278442號「除去底灰所含氯化物之方法及裝置」;第I314543號「煤灰製成吸附材料之方法」;第I328095號「焚化爐飛灰再利用處理方法」;第I325795號「使用磷酸二鈣二水合物粉末穩定於焚化爐底渣重金屬及氣味控制之方法」;第I310699號「分解戴奧辛之方法與裝置」;第I288028號「焚化底渣水洗程序」;第I257330號「焚化飛灰之處理方法及裝置」;第I231234號「焚化爐排放戴奧辛類化合物之處理劑及程序」;發明公開第523550號「以電弧爐將垃圾焚化飛灰回收再利用之鍊鋼方法」;第M369800號「飛灰螯合劑混合添加設備」等專利案及公開案。 Invention No. 301697 "stabilization and reuse of ashes"; Invention No. 468021 "ash melting method and ash melting furnace"; Method and device for removing chloride contained in bottom ash"; No. I314543 "Method for making coal ash into adsorption material"; No. I328095 "Method for reusing incinerator fly ash"; No. I325795 "Using dicalcium phosphate Method for Stabilizing Hydrate Powder in Incinerator Bottom Slag of Heavy Metals and Odor Control"; No. I310699 "Method and Device for Decomposing Dioxin"; No. I288028 "Washing Procedure of Incineration Bottom Slag"; No. I257330 "Treatment Method of Incineration Fly Ash and device"; No. I231234 "Treatment agent and procedure for dioxin compounds discharged from incinerators"; Invention Publication No. 523550 "A chain steel method for recycling waste incineration fly ash by electric arc furnace"; No. M369800 "Fly ash Chelating agent mixing and adding equipment" and other patents and publications.
進一步說明前揭與本發明案不同之處。由前述相關之處理方法可知,多數技術係採水洗、氣化、曝氣、高 溫熔融等方式,其機制藉水洗或高溫將含重金屬固相有害物質分解或轉化為液相或氣相、或藉高溫使無機物熔融進而包覆灰渣,使之不易溶出。 The differences between the preceding disclosure and the present invention are further described. It can be seen from the above-mentioned related processing methods that most of the technologies are water washing, gasification, aeration, high Its mechanism is to decompose or convert solid-phase harmful substances containing heavy metals into liquid or gas phases by washing or high temperature, or to melt inorganic substances by high temperature and then coat ash to make it difficult to dissolve.
本案之主要處理技術係先利用水將集塵粉體進行洗脫分離,即將集塵粉體有害重金屬由粉體移出成廢液(廢液另需處理),並進行加酸(或再加穩定劑)之穩定化處理。其後,進行粉體檢測,若符合再利用之原料標準,即可進行再利用。反之,進行高溫之熱處理,藉高溫破壞分解有機物之機制,移出或降低戴奧辛、多環芳香烴等有害物質,達到符合再利用之原料標準。 The main treatment technology in this case is to first use water to elute and separate the dust collection powder, that is, to remove the harmful heavy metals from the dust collection powder into a waste liquid (the waste liquid needs to be treated separately), and add acid (or re-stabilize agent) stabilization treatment. Afterwards, the powder is inspected, and if it meets the raw material standards for reuse, it can be reused. On the contrary, high-temperature heat treatment can remove or reduce harmful substances such as dioxins and polycyclic aromatic hydrocarbons through the mechanism of high-temperature destruction and decomposition of organic matter, so as to meet the raw material standards for reuse.
本發明主要目的係提供促進熱處理設施集塵粉體之穩定化與無害化方法,俾達到「穩定化」、「無害化」及「資材化」之再利用目的。緣是,為達到前述目的,本發明之穩定化及無害化包含下列步驟: The main purpose of the present invention is to provide a method for promoting the stabilization and harmlessness of dust collection powder in heat treatment facilities, so as to achieve the reuse purposes of "stabilization", "harmlessness" and "materialization". The reason is that, in order to achieve the aforementioned purpose, the stabilization and harmlessness of the present invention include the following steps:
將集塵粉體與水在特定比例下進行投料,即先將水倒入預拌槽,並調控馬達以帶動水產生漩渦及擾動,再將集塵粉體投入預拌槽進行充分之拌合。 Feed the dust-collecting powder and water in a specific ratio, that is, pour the water into the pre-mixing tank first, and adjust the motor to drive the water to generate vortex and disturbance, and then put the dust-collecting powder into the pre-mixing tank for sufficient mixing .
將前述預拌槽內之漿體(slurry)輸送至淘洗槽中,進行一或二步驟之洗脫處理,包括以可控制轉速之攪拌器進行漿體之淘洗,及以離心式(或壓濾式)進行漿體之固液分離。 The slurry (slurry) in the aforementioned premixing tank is transported to the elutriation tank for one or two steps of elution treatment, including elutriation of the slurry with a stirrer that can control the rotation speed, and centrifugal (or Press filter) for solid-liquid separation of slurry.
前述一或二步驟之洗淘過程中,加入高濃度酸液(如硫酸、或鹽酸等),控制漿體pH值,以利粉體原所含重金屬形成重金屬沉澱物,而達穩定化。更有甚者,亦可再加入無機類之重金屬穩定劑,以加強穩定化成效。 In the washing process of the above-mentioned one or two steps, high-concentration acid solution (such as sulfuric acid or hydrochloric acid, etc.) is added to control the pH value of the slurry, so as to facilitate the formation of heavy metal precipitates from the heavy metals contained in the original powder and achieve stabilization. What's more, inorganic heavy metal stabilizers can also be added to enhance the stabilization effect.
進行固液分離後粉體之物化性質檢測,若已達再利用標準,即成為無害化且可再利用粉體。 After the solid-liquid separation, the physical and chemical properties of the powder are tested. If it meets the reuse standard, it becomes a harmless and reusable powder.
反之,則進行高溫之熱處理,以去除戴奧辛、多環芳香烴等有機類有害物質。 On the contrary, high-temperature heat treatment is carried out to remove organic harmful substances such as dioxins and polycyclic aromatic hydrocarbons.
進行熱處理後粉體之物化性質檢測,若已達再利用標準,即成為無害化且可再利用粉體;反之,則返回穩定化處理程序。 After the heat treatment, the physical and chemical properties of the powder are tested. If the reuse standard is met, it becomes a harmless and reusable powder; otherwise, it returns to the stabilization treatment procedure.
本發明方法適合性質仍有所差異之熱處理設施之集塵粉體,且以粉體再利用為主要目的;另本發明作法具有逐步性,符合再利用標準後,即成為無害化之再利用粉體,達到簡化處理步驟及節能減碳之目的。 The method of the present invention is suitable for the dust collection powder of heat treatment facilities with different properties, and the main purpose is to reuse the powder; in addition, the method of the present invention is step-by-step, and after meeting the reuse standard, it becomes a harmless recycled powder body, to achieve the purpose of simplifying the processing steps and saving energy and reducing carbon.
100:焚化粉體 100: incineration powder
110:預攪拌混合 110: pre-stirred mix
120:一或二步驟洗脫處理 120: One or two step elution treatment
130:穩定化處理 130: Stabilization treatment
140:無害化再利用粉體 140: Harmless reuse powder
150:熱處理 150: heat treatment
圖1係本發明一較佳實施例之流程圖。 Fig. 1 is a flow chart of a preferred embodiment of the present invention.
請參閱圖一所示,本發明較佳實施例包含下列步驟: Referring to Figure 1, a preferred embodiment of the present invention includes the following steps:
100為備妥欲處理之熱處理設施之集塵粉體。 100 is the dust collection powder ready for the heat treatment facility to be treated.
於110預拌槽注入特定水量(液固比介於1.5-6.0),開啟馬達將預拌槽內水體形成擾動渦流,並逐步倒入集塵粉體,進行預攪拌混合。 Inject a specific amount of water (liquid-solid ratio between 1.5-6.0) into the 110 pre-mixing tank, turn on the motor to form a turbulent vortex in the water body in the pre-mixing tank, and gradually pour in the dust collection powder for pre-mixing and mixing.
將前述預拌槽內之漿體(slurry)輸送至淘洗槽中,進行120一或二步驟之洗脫處理,包括以可控制轉速(轉速介於100-600rpm)之攪拌器進行漿體之淘洗,及以離心式(或壓濾式)進行漿體之固液分離。 The slurry (slurry) in the aforementioned premixing tank is transported to the elutriation tank, and the elution treatment of 120 or two steps is carried out, including the stirring of the slurry with a controllable rotation speed (the rotation speed is between 100-600rpm). Elutriation, and the solid-liquid separation of the slurry by centrifugal (or press filter).
前述一或二步驟之洗淘過程中,加入高濃度酸液(如硫酸、或鹽酸等),控制漿體pH值(介於9.0-12.0),以利粉體原所含重金屬形成重金屬沉澱物,進行130穩定化處理。 In the washing process of the above-mentioned one or two steps, add high-concentration acid solution (such as sulfuric acid, or hydrochloric acid, etc.) to control the pH value of the slurry (between 9.0-12.0), so as to facilitate the formation of heavy metal precipitates from the heavy metals contained in the original powder , performing 130 stabilization treatments.
更有甚者,可再加入無機類之重金屬穩定劑,如硫基、磷酸基之穩定劑等,以加強穩定化成效。 What's more, inorganic heavy metal stabilizers, such as sulfur-based and phosphoric acid-based stabilizers, can be added to enhance the stabilization effect.
進行固液分離後粉體之物化性質檢測,若已符合再利用標準,即成為140無害化再利用粉體。 After the solid-liquid separation, the physical and chemical properties of the powder are tested. If it meets the reuse standard, it becomes 140 harmless reuse powder.
反之,則進行高溫之150熱處理,溫度控制介於800-950℃,以去除戴奧辛、多環芳香烴等有機類有害物質。
On the contrary,
進行熱處理後粉體之物化性質檢測,若已符合再利用標準,即成為140無害化再利用粉體;反之,則返回130穩定化處理。 After the heat treatment, the physical and chemical properties of the powder are tested. If it meets the reuse standard, it becomes 140 harmless reuse powder; otherwise, it returns to 130 stabilization treatment.
100:集塵粉體 100: Dust collection powder
110:預攪拌混合 110: pre-stirred mix
120:一或二步驟洗脫處理 120: One or two step elution treatment
130:穩定化處理 130: Stabilization treatment
140:無害化再利用粉體 140: Harmless reuse powder
150:熱處理 150: heat treatment
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| TW201013123A (en) * | 2008-09-16 | 2010-04-01 | Kun-Sen Chang | Detoxification method for heavy metal-containing incineration fly ash |
| TW201212974A (en) * | 2010-09-24 | 2012-04-01 | Univ Nat United | Method for quickly removing hazardous matters from MSWI fly ash |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| TW201013123A (en) * | 2008-09-16 | 2010-04-01 | Kun-Sen Chang | Detoxification method for heavy metal-containing incineration fly ash |
| TW201212974A (en) * | 2010-09-24 | 2012-04-01 | Univ Nat United | Method for quickly removing hazardous matters from MSWI fly ash |
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