EP0860183B1 - Noxious component removal process and system - Google Patents
Noxious component removal process and system Download PDFInfo
- Publication number
- EP0860183B1 EP0860183B1 EP98102829A EP98102829A EP0860183B1 EP 0860183 B1 EP0860183 B1 EP 0860183B1 EP 98102829 A EP98102829 A EP 98102829A EP 98102829 A EP98102829 A EP 98102829A EP 0860183 B1 EP0860183 B1 EP 0860183B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- chlorine
- treatable material
- removal agent
- sulfur
- 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.)
- Expired - Lifetime
Links
Images
Classifications
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
- A62D3/30—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents
- A62D3/34—Dehalogenation using reactive chemical agents able to degrade
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
- A62D3/40—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by heating to effect chemical change, e.g. pyrolysis
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- 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
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/20—Organic substances
- A62D2101/22—Organic substances containing halogen
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/40—Inorganic substances
- A62D2101/47—Inorganic substances containing oxygen, sulfur, selenium or tellurium, i.e. chalcogen
Definitions
- chlorine-containing compound and chlorine component in the treatable material can be converted into sodium or potassium chloride and water, and therefore hydrogen chloride forming part of a source of dioxin cannot be formed thereby realizing the unexpected results of making both emitted gas and residue harmless.
- the thermal treatment or heating of the mixture in the thermal treatment furnace 2 is accomplished within temperature and time ranges to cover the temperature and time of generation of HCl gas and SOx gas from the treatable material, the temperature (for example, 600 °C) and time (for example, 1 hour) having been determined under a previous investigation.
- These temperature and time are in relation to a condition (such as the size and the heating coil) of the thermal treatment furnace, the treatment amount of the treatable material, the treatment time of the thermal treatment of the treatable material, the treatment temperature of the thermal treatment of the treatable material. Therefore, the above temperature and time are required to be previously determined under a sufficient investigation and to accumulate the data to be taken for the temperature and time.
- the chlorine removal agent sodium hydrogen carbonate
- the chlorine removal agent was in the form of powder having an average particle size of 100 ⁇ m, in all Examples
- the thus sealed tank was stepwise heated with a heating coil, in which heating was made at eight temperature steps of 250 °C, 300 °C, 350 °C, 400 °C, 450 °C, 500 °C, 550 °C, 600 °C.
- the temperature at each of the eight steps was kept for 5 minutes, in which a concentration of HCl gas and a concentration of SO 2 in the tank was measured at each temperature rising time (at which the temperature was rising from one temperature step to the next temperature step) and at each temperature keeping time (at which the temperature at each temperature step was keeping).
- the temperature rising time is indicated as "Rising time” while the temperature keeping time is indicated as "Keeping time” in Tables 1 and 2.
- the temperature for heating the mixture of the treatable material and the chlorine removal agent may be selected according to form of facilities for accomplish the thermal treatment, time of the thermal treatment, amount of the treatable material and the like.
- sodium hydrogen carbonate (NaHCO 3 ), sodium carbonate (Na 2 CO 3 ), sodium sesqui carbonate (Na 2 CO 3 • NaHCO 3 • 2H 2 O), natural soda (containing Na 2 CO 3 • NaHCO 3 • 2H 2 O), sodium hydroxide (NaOH), potassium hydroxide (KOH), potassium carbonate (K 2 CO 3 ), and potassium hydrogen carbonate (KHCO 3 ) can react with noxious HCl thereby to convert HCl into harmless chloride (NaCl and KCl) according to reaction formulae discussed before. It will be understood that sodium potassium carbonate and sodium carbonate hydrate can also react with noxious HCl similarly to the above.
- chlorine-containing compound and chlorine component in the treatable material can be converted into sodium chloride (NaCl), potassium chloride (KCl), water (H 2 O) and carbon dioxide gas (CO 2 ), and therefore hydrogen chloride forming part of a source of dioxin cannot be formed thereby realizing the unexpected result of making both emitted gas and residue harmless.
- NaOH or KOH smoothly reacts with SO2 thereby to newly form harmless sulfite (Na 2 SO 3 , K 2 SO 3 ).
- sulfur-containing compound and sulfur component in the treatable material can be converted into sodium sulfite (Na 2 SO 3 ) in powder form, and potassium sulfite (K 2 SO 3 ) in powder form, water (H 2 O) and carbon dioxide gas (CO 2 ), and therefore SOx gas can be prevented from generation thus realizing the unexpected result of making both emitted gas and residue harmless.
- noxious hydrogen chloride and/or sulfur oxide are converted into harmless chloride (NaCl, KCl) and/or sulfite (Na 2 SO 3 , K 2 SO 3 ), thereby making it possible to remove noxious components (hydrogen chloride and/or sulfur oxide) from the decomposition gas generated from the treatable material upon heating.
- the decomposition gas or emitted gas from the furnace can be effectively made harmless.
- the chloride and/or sulfite form part of the residue and can be effectively removed under a rinsing or dissolving treatment with water or the like.
- the residual materials can be separated into respective materials which are different in characteristics by any separating means.
- the separated respective materials are dried and massed to be usable as fuel or the like.
- liquid (such as water) used for the above rinsing treatment hardly contains no noxious substances and therefore can be discharged as it is to a river and the sea.
Landscapes
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Business, Economics & Management (AREA)
- Emergency Management (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Treating Waste Gases (AREA)
- Processing Of Solid Wastes (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Fire-Extinguishing Compositions (AREA)
- Hardware Redundancy (AREA)
- Removal Of Specific Substances (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Applications Claiming Priority (21)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9038737A JPH10235311A (ja) | 1997-02-24 | 1997-02-24 | 塩化ビニル系物質の脱塩素処理方法 |
JP9038726A JPH10235147A (ja) | 1997-02-24 | 1997-02-24 | 脱塩素処理方法 |
JP3873797 | 1997-02-24 | ||
JP9038728A JPH10235148A (ja) | 1997-02-24 | 1997-02-24 | 脱塩素処理方法 |
JP3872897 | 1997-02-24 | ||
JP3872697 | 1997-02-24 | ||
JP38728/97 | 1997-02-24 | ||
JP9038729A JPH10235149A (ja) | 1997-02-24 | 1997-02-24 | 塩化ビニル系物質の脱塩素処理方法 |
JP38726/97 | 1997-02-24 | ||
JP38729/97 | 1997-02-24 | ||
JP3872997 | 1997-02-24 | ||
JP38737/97 | 1997-02-24 | ||
JP160914/97 | 1997-06-18 | ||
JP160911/97 | 1997-06-18 | ||
JP16091197 | 1997-06-18 | ||
JP9160911A JPH119938A (ja) | 1997-06-18 | 1997-06-18 | 脱塩素処理方法 |
JP9160914A JPH119939A (ja) | 1997-06-18 | 1997-06-18 | 塩化ビニル系物質の脱塩素処理方法 |
JP16091497 | 1997-06-18 | ||
JP265993/97 | 1997-09-30 | ||
JP9265993A JPH11101417A (ja) | 1997-09-30 | 1997-09-30 | 有害ガスの発生防止方法 |
JP26599397 | 1997-09-30 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0860183A2 EP0860183A2 (en) | 1998-08-26 |
EP0860183A3 EP0860183A3 (en) | 1999-01-20 |
EP0860183B1 true EP0860183B1 (en) | 2002-11-13 |
Family
ID=27564474
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP98102829A Expired - Lifetime EP0860183B1 (en) | 1997-02-24 | 1998-02-18 | Noxious component removal process and system |
Country Status (10)
Country | Link |
---|---|
EP (1) | EP0860183B1 (ko) |
KR (1) | KR100341551B1 (ko) |
CN (1) | CN1095687C (ko) |
AT (1) | ATE227598T1 (ko) |
AU (1) | AU714634B2 (ko) |
DE (1) | DE69809310T2 (ko) |
DK (1) | DK0860183T3 (ko) |
ES (1) | ES2186931T3 (ko) |
MY (1) | MY121329A (ko) |
NO (1) | NO316905B1 (ko) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101597387B (zh) * | 2009-05-22 | 2011-12-07 | 上海岚淼水处理科技有限公司 | 用于工业水处理的多糖纳米除氯剂的制备方法 |
US9440218B2 (en) * | 2013-06-13 | 2016-09-13 | Clariant Corporation | Methods and active materials for reducing halide concentration in gas streams |
CN104971609B (zh) * | 2015-07-22 | 2017-04-05 | 南京格洛特环境工程股份有限公司 | 一种氟化氢废气治理及资源化利用的方法及设备 |
CN108339365B (zh) * | 2017-01-24 | 2020-09-25 | 内蒙古大学 | 一种用于控制化工工业废气排放的装置及方法 |
CN109001007A (zh) * | 2018-08-22 | 2018-12-14 | 汉能新材料科技有限公司 | 一种物料的处理方法 |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4938936A (en) * | 1988-09-01 | 1990-07-03 | Mobil Oil Corporation | Hydrogen fluoride vapor containment and neutralization |
DE3839799A1 (de) * | 1988-11-25 | 1990-07-05 | Rwe Entsorgung Ag | Verfahren zur aufarbeitung kontaminierter oele |
US5064526A (en) * | 1990-04-27 | 1991-11-12 | The United States Of America As Represented By The Administrator Of The Environmental Protection Agency | Method for the base-catalyzed decomposition of halogenated and non-halogenated organic compounds in a contaminated medium |
US5039350A (en) * | 1990-04-27 | 1991-08-13 | The United States Of America As Represented By The Administrator Of The Environmental Protection Agency | Method for the decomposition of halogenated organic compounds in a contaminated medium |
JPH06179877A (ja) * | 1991-12-20 | 1994-06-28 | Toshiba Corp | 廃プラスチックの熱分解方法及び装置 |
JP3213134B2 (ja) * | 1993-09-13 | 2001-10-02 | 株式会社東芝 | 加熱油化方法及びその装置 |
JP3288164B2 (ja) * | 1993-12-28 | 2002-06-04 | 株式会社東芝 | 廃プラスチックの熱分解装置 |
CA2159521C (en) * | 1994-10-07 | 1999-11-09 | Shigeo Iiyama | Method for desulfurizing exhaust gas |
NO308831B1 (no) * | 1995-03-22 | 2000-11-06 | Nkt Res Ct As | FremgangsmÕte for behandling av halogenholdig avfallsmateriale |
-
1998
- 1998-02-18 DE DE69809310T patent/DE69809310T2/de not_active Expired - Fee Related
- 1998-02-18 EP EP98102829A patent/EP0860183B1/en not_active Expired - Lifetime
- 1998-02-18 AT AT98102829T patent/ATE227598T1/de not_active IP Right Cessation
- 1998-02-18 ES ES98102829T patent/ES2186931T3/es not_active Expired - Lifetime
- 1998-02-18 DK DK98102829T patent/DK0860183T3/da active
- 1998-02-23 KR KR1019980005575A patent/KR100341551B1/ko not_active IP Right Cessation
- 1998-02-23 NO NO19980758A patent/NO316905B1/no unknown
- 1998-02-23 CN CN98107704A patent/CN1095687C/zh not_active Expired - Fee Related
- 1998-02-23 MY MYPI98000755A patent/MY121329A/en unknown
- 1998-02-24 AU AU56329/98A patent/AU714634B2/en not_active Ceased
Also Published As
Publication number | Publication date |
---|---|
ES2186931T3 (es) | 2003-05-16 |
CN1095687C (zh) | 2002-12-11 |
AU5632998A (en) | 1998-08-27 |
EP0860183A3 (en) | 1999-01-20 |
NO980758D0 (no) | 1998-02-23 |
CN1197685A (zh) | 1998-11-04 |
NO980758L (no) | 1998-08-25 |
ATE227598T1 (de) | 2002-11-15 |
KR100341551B1 (ko) | 2002-08-22 |
AU714634B2 (en) | 2000-01-06 |
KR19980071609A (ko) | 1998-10-26 |
DK0860183T3 (da) | 2003-03-10 |
MY121329A (en) | 2006-01-28 |
DE69809310T2 (de) | 2003-03-20 |
NO316905B1 (no) | 2004-06-21 |
DE69809310D1 (de) | 2002-12-19 |
EP0860183A2 (en) | 1998-08-26 |
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