JPS62237984A - Waste materials treatment for asbestos-containing substance - Google Patents
Waste materials treatment for asbestos-containing substanceInfo
- Publication number
- JPS62237984A JPS62237984A JP61080894A JP8089486A JPS62237984A JP S62237984 A JPS62237984 A JP S62237984A JP 61080894 A JP61080894 A JP 61080894A JP 8089486 A JP8089486 A JP 8089486A JP S62237984 A JPS62237984 A JP S62237984A
- Authority
- JP
- Japan
- Prior art keywords
- asbestos
- waste
- melting
- disposing
- insulation material
- 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.)
- Pending
Links
- 239000010425 asbestos Substances 0.000 title claims abstract description 107
- 229910052895 riebeckite Inorganic materials 0.000 title claims abstract description 107
- 239000002699 waste material Substances 0.000 title claims abstract description 45
- 239000000126 substance Substances 0.000 title claims abstract description 5
- 238000002844 melting Methods 0.000 claims abstract description 53
- 230000008018 melting Effects 0.000 claims abstract description 53
- 239000000463 material Substances 0.000 claims abstract description 35
- 239000000654 additive Substances 0.000 claims abstract description 11
- 239000000835 fiber Substances 0.000 claims abstract description 9
- 239000000203 mixture Substances 0.000 claims abstract description 7
- 239000013078 crystal Substances 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 25
- 239000012774 insulation material Substances 0.000 claims description 15
- -1 boric acid compound Chemical class 0.000 claims description 11
- 229910001868 water Inorganic materials 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- AYJRCSIUFZENHW-UHFFFAOYSA-L barium carbonate Chemical compound [Ba+2].[O-]C([O-])=O AYJRCSIUFZENHW-UHFFFAOYSA-L 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 claims description 4
- 239000000378 calcium silicate Substances 0.000 claims description 4
- 229910052918 calcium silicate Inorganic materials 0.000 claims description 4
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 4
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- 239000004327 boric acid Substances 0.000 claims description 3
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 claims description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims description 3
- 239000007800 oxidant agent Substances 0.000 claims description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Substances OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 3
- 239000005909 Kieselgur Substances 0.000 claims description 2
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 claims description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 239000004568 cement Substances 0.000 claims description 2
- 239000011248 coating agent Substances 0.000 claims description 2
- 238000000576 coating method Methods 0.000 claims description 2
- 239000006063 cullet Substances 0.000 claims description 2
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 claims description 2
- 239000001095 magnesium carbonate Substances 0.000 claims description 2
- 229910000021 magnesium carbonate Inorganic materials 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims description 2
- 239000010451 perlite Substances 0.000 claims description 2
- 235000019362 perlite Nutrition 0.000 claims description 2
- 239000004323 potassium nitrate Substances 0.000 claims description 2
- 235000010333 potassium nitrate Nutrition 0.000 claims description 2
- 239000004317 sodium nitrate Substances 0.000 claims description 2
- 235000010344 sodium nitrate Nutrition 0.000 claims description 2
- 239000004753 textile Substances 0.000 claims description 2
- 239000010455 vermiculite Substances 0.000 claims description 2
- 229910052902 vermiculite Inorganic materials 0.000 claims description 2
- 235000019354 vermiculite Nutrition 0.000 claims description 2
- QHGNHLZPVBIIPX-UHFFFAOYSA-N tin(ii) oxide Chemical compound [Sn]=O QHGNHLZPVBIIPX-UHFFFAOYSA-N 0.000 claims 2
- TXUICONDJPYNPY-UHFFFAOYSA-N (1,10,13-trimethyl-3-oxo-4,5,6,7,8,9,11,12,14,15,16,17-dodecahydrocyclopenta[a]phenanthren-17-yl) heptanoate Chemical compound C1CC2CC(=O)C=C(C)C2(C)C2C1C1CCC(OC(=O)CCCCCC)C1(C)CC2 TXUICONDJPYNPY-UHFFFAOYSA-N 0.000 claims 1
- 229910021626 Tin(II) chloride Inorganic materials 0.000 claims 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims 1
- 239000010439 graphite Substances 0.000 claims 1
- 229910002804 graphite Inorganic materials 0.000 claims 1
- 238000003672 processing method Methods 0.000 claims 1
- 239000001119 stannous chloride Substances 0.000 claims 1
- 235000011150 stannous chloride Nutrition 0.000 claims 1
- 229910052725 zinc Inorganic materials 0.000 claims 1
- 239000011701 zinc Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 abstract description 16
- 238000003860 storage Methods 0.000 abstract description 9
- 230000000996 additive effect Effects 0.000 abstract description 5
- 238000001816 cooling Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract description 2
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical class OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 4
- 229910003480 inorganic solid Inorganic materials 0.000 description 4
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 4
- 239000004111 Potassium silicate Substances 0.000 description 3
- 239000004115 Sodium Silicate Substances 0.000 description 3
- NNHHDJVEYQHLHG-UHFFFAOYSA-N potassium silicate Chemical compound [K+].[K+].[O-][Si]([O-])=O NNHHDJVEYQHLHG-UHFFFAOYSA-N 0.000 description 3
- 229910052913 potassium silicate Inorganic materials 0.000 description 3
- 235000019353 potassium silicate Nutrition 0.000 description 3
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 3
- 229910052911 sodium silicate Inorganic materials 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- 229910021538 borax Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 239000004328 sodium tetraborate Substances 0.000 description 2
- 235000010339 sodium tetraborate Nutrition 0.000 description 2
- 229910021532 Calcite Inorganic materials 0.000 description 1
- 235000016936 Dendrocalamus strictus Nutrition 0.000 description 1
- 241001590997 Moolgarda engeli Species 0.000 description 1
- 229910021260 NaFe Inorganic materials 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 description 1
- 239000005388 borosilicate glass Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 1
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 1
- VDQVEACBQKUUSU-UHFFFAOYSA-M disodium;sulfanide Chemical compound [Na+].[Na+].[SH-] VDQVEACBQKUUSU-UHFFFAOYSA-M 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910052635 ferrosilite Inorganic materials 0.000 description 1
- 239000002783 friction material Substances 0.000 description 1
- 239000005350 fused silica glass Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052892 hornblende Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- VLCLHFYFMCKBRP-UHFFFAOYSA-N tricalcium;diborate Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]B([O-])[O-].[O-]B([O-])[O-] VLCLHFYFMCKBRP-UHFFFAOYSA-N 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000004017 vitrification Methods 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、石綿繊維その他の石綿を含有する物品の廃棄
処理を行う方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for disposing of asbestos fibers and other articles containing asbestos.
石綿は、熱や摩擦に強く、断熱性にも優れた性質を有し
ているために建築材料、摩擦材料、シール材料、断熱材
料等に極めて大量のものが使用されていた。Asbestos is resistant to heat and friction, and has excellent heat insulating properties, so extremely large amounts of asbestos have been used in building materials, friction materials, sealing materials, heat insulating materials, and the like.
しかしながら、これらに使用される石綿に、発ガン物質
の疑いがあるとの疑問が出されるにいたって、これら石
綿製品の国内に於ける取扱いも法令で規制されるように
なってきつつある。〔例えば昭和47年9月30日労働
省令第39号並びに昭和50年9月30日(改正)第2
6号による特定化学物質等障害予防規則(特化則)によ
る規制〕
また、これらの規制は、日本国内に止まらず、米国にあ
っては日本よりも更に古くから規制が提案され、最近に
至っては、昭和61年1月に米国環境保護局(E P
A)が「石綿の使用を年々縮小し、10年後に全面使用
を禁止する」旨の厳しい規制方針を提案している。However, as questions have been raised that the asbestos used in these products is suspected of being a carcinogen, the handling of these asbestos products in Japan is also becoming regulated by law. [For example, Ministry of Labor Ordinance No. 39 of September 30, 1971 and Ministry of Labor Ordinance No. 2 of September 30, 1975 (revised)
Regulations based on the Ordinance on Prevention of Hazards from Specified Chemical Substances, etc. (Specialized Regulations) under No. 6] In addition, these regulations are not limited to Japan; in the United States, regulations have been proposed for a longer time than in Japan, and have recently been implemented. was approved by the U.S. Environmental Protection Agency (EP) in January 1986.
A) proposes a strict regulatory policy that ``reduces the use of asbestos year by year and completely bans its use in 10 years.''
このような情勢に対応して、石綿に代替できるガラス繊
維が開発され、その結果石綿を使用した製品の種類及び
数量も飛躍的に少なくなってきつつある。In response to this situation, glass fibers that can replace asbestos have been developed, and as a result, the types and quantities of products that use asbestos are decreasing dramatically.
しかしながら、上記のような石綿に関する厳しい規制が
打ち出され、実施されるに至ってもそれは将来に向かっ
ての安全を保証するだけであり、過去において多量に使
用をされてきた石綿製品を廃棄する場合の安全について
は何も保証をされていない。However, even if strict regulations regarding asbestos such as those mentioned above are established and implemented, they will only guarantee future safety, and will not be effective when disposing of asbestos products that have been used in large quantities in the past. There are no guarantees regarding safety.
過去において、石綿を使用することによって産出されて
いる製品の量(建築製品、プラント等に使用をされてい
るものを含む)は膨大なものである、このような、ビル
やプラント装置を解体撤去する場合には必然的に極めて
大量の石綿を含有する廃棄物が発生することとなり、前
記した危険の指摘は一層切実なものとなってくる。In the past, the amount of products produced using asbestos (including those used in building products, plants, etc.) was enormous. In this case, waste containing extremely large amounts of asbestos will inevitably be generated, making the above-mentioned danger all the more urgent.
上記したような発ガンの危険を考えればこれらの廃棄処
理には相当の注意と手段が必要となりそうであるが、現
在のところ廃棄に際しても特別の防護策を採ることなく
石綿製品を他の建築部材とともに機械等で壊しているの
が実情である。Considering the risk of cancer mentioned above, it is likely that considerable care and measures will be required to dispose of these products, but at present, asbestos products cannot be used in other buildings without taking special protective measures when disposing of them. The reality is that the parts are destroyed together with machines.
現在の法令による規制の流れを勘案すれば、これら石綿
製品を廃棄する場合の処理方法も当然問題となることが
予想されるが、現在のところわが国において、ビルの解
体やプラント装置の解体工事を行うに際して、石綿製品
の廃棄のための取扱いを対象とした法律や規制は存在せ
ず、わずかに一部の地方自治体が、石綿を混入した材料
を使用している建築物を解体する場合に、作業者に「防
塵マスクの着用」を義務付け、作業現場において石綿繊
維の飛散を防止するために「石綿材料への撒水」と「建
物の内側にビニール幕を設置」することを義務付けてい
る程度である。Considering the flow of regulations under current laws and regulations, it is expected that the disposal methods for disposing of these asbestos products will naturally become a problem, but at present in Japan, there are no plans to dismantle buildings or dismantle plant equipment. However, there are no laws or regulations that cover the handling of asbestos products for disposal, and only some local governments do so when demolishing buildings that use asbestos-containing materials. It only requires workers to "wear dust masks" and to "sprinkle water on asbestos materials" and "install vinyl curtains inside buildings" to prevent asbestos fibers from scattering at work sites. be.
本発明は、これらの事情に鑑みそれに対応しようとする
ものであり、その目的とするところは、石綿繊維を含有
した廃棄物を高温溶融し、ガラス化または石綿以外の結
晶構造を有する物質に変換し安定で無害な無機固体にす
ることを特徴とする石綿含有物の廃棄処理方法を提供し
ようとするものである。The present invention is intended to address these circumstances, and its purpose is to melt waste containing asbestos fibers at high temperature and convert it into vitrification or into a substance with a crystal structure other than asbestos. The present invention aims to provide a method for disposing of asbestos-containing materials, which is characterized by converting them into stable and harmless inorganic solids.
また、本発明の他の目的は、石綿を含有する廃棄物の体
積を小さくし、廃棄処理のための処分を容易にすること
ができる新しい廃棄処理方法を提供せんとするものであ
る。Another object of the present invention is to provide a new waste treatment method that can reduce the volume of asbestos-containing waste and facilitate its disposal.
更にまた、本発明の他の目的は、廃棄処理をしようとす
る石綿含有物の石綿含有量の範囲が高しヘルのものから
低レベルのものまでのすべてのものに適用をすることが
でき、しかも処理をしようとする材料が無機質のものの
場合でも、或いはを機質のものの場合でも適当な溶融助
剤と添加剤を用いることによって極めて容易に廃棄処理
を行うことのできる石綿含有物の廃棄処理方法を提供せ
んとするものである。Furthermore, another object of the present invention is that it can be applied to all asbestos-containing materials to be disposed of, ranging from high to low-level asbestos content, Moreover, even if the material to be treated is inorganic or organic, it can be disposed of very easily by using appropriate melting aids and additives. The purpose is to provide a method.
また更に、本発明の他の目的は、高温溶融で得られた無
機固体物が、土木、建築のための資材としての用途を有
することができるようにして、資源の有効利用を図れる
ようにした石綿含有物の廃棄処理方法を提供しようとす
るものである。Still another object of the present invention is to enable inorganic solids obtained by high-temperature melting to be used as materials for civil engineering and construction, thereby making it possible to utilize resources effectively. The present invention aims to provide a method for disposing of asbestos-containing materials.
本発明は、石綿を含有する廃棄物に、溶融助剤を混合し
たのちこれを溶融窯に投入し、該溶融窯中において高温
加熱を行うことによって、廃棄物を溶融しながらその全
景を溶融固化することをその要点とするものである。The present invention involves mixing asbestos-containing waste with a melting aid, then putting it into a melting kiln, and heating the waste at a high temperature in the melting kiln to melt and solidify the waste in its entirety. The main point is to do so.
本発明は、処理をしようとする石綿を含有する廃棄物に
、溶融助剤を混合し、それを溶融窯に投入して高温加熱
を行うことによって、溶融しながら、廃棄物の全量を溶
融同化することを特徴とする石綿含有物の廃棄処理方法
である。In the present invention, a melting aid is mixed with waste containing asbestos to be treated, and the mixture is put into a melting furnace and heated at high temperature, thereby melting and assimilating the entire amount of waste while melting. This is a method for disposing of asbestos-containing materials.
なお、本発明でいう「石綿」は、その種類を問わないも
のであり、一般に「石綿」として認識される
■温石綿 84M g 3S t 209■青石綿
NaFe (Sins)z・FeSiO3■角閃石綿
Ca (Mg、 F e) 3 (S i 03
) a■直直方石綿(F e、 Mg) S i 03
をいう。In addition, "asbestos" as used in the present invention is not limited to its type, and generally includes warm asbestos 84M g 3S t 209 blue asbestos.
NaFe (Sins)z・FeSiO3 ■ Hornblende Ca (Mg, Fe) 3 (S i 03
) a■ Orthogonal asbestos (F e, Mg) S i 03
means.
また、本発明にいう、石綿含有廃棄物とは、石綿保温材
、珪藻土保温材、塩基性炭酸マグネシウム保温材、パー
ライト保温材、バーミキュライト保温材等の成形保温材
、並びにこれらの粉体、或いは水練保温材、更には他の
粉体と混合した保温外装塗材、又は石綿繊維、石綿糸、
石綿紐、石綿ロープ、石綿チューブ、石綿リボン、石綿
布及びこれらの紡織品並びに加工品、ガスケット、パッ
キング、ブレーキライニング、クラッチフェーシング、
石綿紙、石綿板、及び石綿セメント製品、並びに石綿珪
酸カルシウム板、吹付石綿、石綿タイルなどをいう。In addition, the asbestos-containing waste referred to in the present invention refers to molded insulation materials such as asbestos insulation materials, diatomaceous earth insulation materials, basic magnesium carbonate insulation materials, perlite insulation materials, and vermiculite insulation materials, as well as powdered or water-mixed materials thereof. Heat insulation materials, heat insulation exterior coating materials mixed with other powders, asbestos fibers, asbestos threads,
Asbestos string, asbestos rope, asbestos tube, asbestos ribbon, asbestos cloth, textile products and processed products thereof, gaskets, packing, brake linings, clutch facings,
Refers to asbestos paper, asbestos board, asbestos cement products, asbestos calcium silicate board, sprayed asbestos, asbestos tile, etc.
また、本発明に用いる溶融助剤とは、硼酸化合物、燐化
合物、珪酸化合物、炭酸化合物及びアルカリ土類金属水
酸化物若しくは本発明の実施過程で発生した溶融固化物
のカレットをいう。Further, the melting aid used in the present invention refers to a boric acid compound, a phosphorus compound, a silicate compound, a carbonate compound, an alkaline earth metal hydroxide, or a cullet of a melt-solidified product generated in the process of carrying out the present invention.
硼酸化合物としては
BzOi(無水硼酸)
H3BO3(、硼酸)
Na2B40?・10H20(硼砂)
Na2B40? ・5HzO(脱水硼砂)Ca B4O
7’ 6 H2O(硼酸カルシウム)N a ZCa
2 (B4O7) 3 ’ 18H20(ポロナイトカ
ルサイト)
燐酸化合物としては
P2O,(五酸化e4)
Hs p o a (燐酸)
NaHPOn’ 12H20(第二燐酸ナトリウム)C
a3 (PO4)! (第三燐酸カルシウム)珪酸化合
物としては
1Oz
Na2S t2o5(珪酸ナトリウム)N a 2S
i O3(珪酸ナトリウム)Na4S i O4(珪酸
ナトリウム)K2Si40.(珪酸カリ)
KzSizOs(珪酸カリ)
K2S > 03 (珪酸カリ)
炭酸化合物としては
Na2COa (炭酸ナトリウム)
KgCO3(炭酸カリウム)
Li2CO1+(炭酸リチウム)
などがそれぞれ挙げられる。Examples of boric acid compounds include BzOi (boric anhydride), H3BO3 (boric acid), and Na2B40?・10H20 (borax) Na2B40?・5HzO (dehydrated borax) Ca B4O
7' 6 H2O (calcium borate) Na ZCa
2 (B4O7) 3' 18H20 (polonite calcite) Phosphoric acid compounds include P2O, (e4 pentoxide) Hs po a (phosphoric acid) NaHPOn' 12H20 (secondary sodium phosphate) C
a3 (PO4)! (Third calcium phosphate) As a silicate compound, 1Oz Na2S t2o5 (sodium silicate) Na 2S
i O3 (sodium silicate) Na4S i O4 (sodium silicate) K2Si40. (Potassium silicate) KzSizOs (Potassium silicate) K2S > 03 (Potassium silicate) Examples of the carbonate compound include Na2COa (sodium carbonate), KgCO3 (potassium carbonate), Li2CO1+ (lithium carbonate), and the like.
また、減容の効果を一層高めるためには溶融助剤ととも
に溶融促進剤、酸化剤、還元剤などの溶融助長剤等を添
加することが望ましい。Further, in order to further enhance the volume reduction effect, it is desirable to add a melting aid such as a melting promoter, an oxidizing agent, a reducing agent, etc. together with the melting aid.
前記した溶融助長剤としては、 溶融促進剤として BaCC1+(炭酸バリウム) 13asO4(硫酸バリウム) 酸化剤として NaN0i(硝酸ナトリウム) KNOs(硝酸カリウム) 還元剤として C(炭素) SnO(酸化第一錫) SnC#z・2H20(塩化第一錫) をそれぞれ挙げることができる。As the above-mentioned melting promoter, As a melt accelerator BaCC1+ (barium carbonate) 13asO4 (barium sulfate) as an oxidizing agent NaN0i (sodium nitrate) KNOs (potassium nitrate) as a reducing agent C (carbon) SnO (stannic oxide) SnC#z・2H20 (Stannic chloride) can be mentioned respectively.
硼酸化合物をはじめとする、前記した「溶融助剤」は石
綿含有廃棄物の溶融時における融点降下の働きを有して
いるのに対して、炭酸バリウム等の「溶融促進剤」は溶
融時間の短縮を図るのに有効なものである。The above-mentioned "melting aids" such as boric acid compounds have the function of lowering the melting point when asbestos-containing waste is melted, whereas "melting accelerators" such as barium carbonate reduce the melting time. This is effective for shortening the time.
以下に本発明の具体的な実施例を、廃棄処理装置のチャ
ート図面を参照して説明する。Hereinafter, specific embodiments of the present invention will be described with reference to charts of a waste treatment apparatus.
溶融化を行おうとする石綿含有廃棄物1は、計量器2a
により計量を行った後、ホッパー3から粉砕194 a
に投入されて適度の粒度に粉砕されたのちミキサー5に
案内される。The asbestos-containing waste 1 to be melted is measured using a measuring device 2a.
After weighing, the pulverizer 194 a
After being pulverized to an appropriate particle size, it is guided to a mixer 5.
なお、溶融化を行おうとする石綿含有廃棄物が解体時に
撒水下で得られたものである場合は、水分を含有した廃
棄物を専門に計量する計量器2bにより計量を行ったの
ち湿式粉砕機4bに投入されたのちミキサー5に案内さ
れるものである。In addition, if the asbestos-containing waste to be melted was obtained under water sprinkling during demolition, it should be weighed using a weighing device 2b that is specialized for weighing waste containing water, and then transferred to a wet crusher. 4b and then guided to the mixer 5.
6a、6bは溶融助剤の貯蔵ビン、7a、7bは添加剤
の貯蔵ビンであり、溶融化を行おうとする廃棄物の材質
に応じて、これらの中からその種類及び量を適宜選択計
量したのち、前記ミキサー5中の石綿含有廃棄物1に添
加し、湿式混合を行う。6a and 6b are storage bottles for melting aids, 7a and 7b are storage bottles for additives, and the type and amount of these were selected and weighed as appropriate depending on the material of the waste to be melted. Thereafter, it is added to the asbestos-containing waste 1 in the mixer 5 and wet-mixed.
ミキサー5によって溶融助剤及び必要に応じて添加剤を
混合された石綿含有廃棄物1は、コンベアー8aによっ
て溶融窯9に移送投入される。The asbestos-containing waste 1 mixed with a melting aid and optionally additives by the mixer 5 is transferred to a melting furnace 9 by a conveyor 8a.
なお、前記コンベアー8aにはヒーター等の加熱乾燥装
置8bを設けることによって石綿含有廃棄物1の水分の
除去を図るようにすることが望ましい。Note that it is desirable to remove moisture from the asbestos-containing waste 1 by providing a heating drying device 8b such as a heater on the conveyor 8a.
また、加熱乾燥装置8bに用いるヒーターとしては、抵
抗加熱、マイクロ波加熱、電熱線加熱、遠赤外線加熱等
を用いることが考えられるが、その他に溶融窯9からの
排気ガスと接触させて乾燥を図ることもできる。Further, as the heater used in the heating drying device 8b, resistance heating, microwave heating, heating wire heating, far infrared heating, etc. may be used; You can also try it out.
前記、加熱乾燥装置8b部分を移送された粉砕後の石綿
含有廃棄物1は、その移送中に大部分の水分が取り除か
れるが若干の水分が残ることは否定できない、但し、こ
れらの残余水分は溶融窯9の投入口9bから落下する間
に、高温ガスと輻射熱によってほぼ完全な乾燥状態とす
ることができる。Although most of the water content of the pulverized asbestos-containing waste 1 transferred to the heating drying device 8b is removed during the transfer process, it cannot be denied that some water remains. While falling from the input port 9b of the melting furnace 9, it can be brought into an almost completely dry state by high-temperature gas and radiant heat.
粉砕された石綿含有廃棄物1の溶融窯9に対する投入は
処理作業の予定に合わせて連続的に若しくは間欠的に行
われる。The pulverized asbestos-containing waste 1 is charged into the melting furnace 9 continuously or intermittently according to the treatment schedule.
溶融窯9内に投入された石綿含有廃棄物1はそれだけを
単独で溶融する場合よりも溶融助剤を投入して溶融を行
う場合の方が融点を低くすることができる。The melting point of the asbestos-containing waste 1 placed in the melting furnace 9 can be lowered when a melting aid is added to the asbestos-containing waste 1 than when it is melted alone.
前記した溶融窯9の加熱方法としてはアークによる加熱
、抵抗加熱、廃棄物自体に通電しそこで発生するジュー
ル熱を利用して行う加熱、高周波加熱、或いはこれらの
併用が可能であるが、作業の煩雑さを避けられるという
点から見れば電気加熱が最も良い方法と言えるであろう
。The melting furnace 9 can be heated by arc heating, resistance heating, heating using the Joule heat generated by passing electricity through the waste itself, high frequency heating, or a combination of these methods, but depending on the work. From the point of view of avoiding complications, electric heating can be said to be the best method.
溶融窯9中では溶融時に、石綿含有廃棄物、溶融助剤、
添加剤中の分解物H20:O□:CO□等が発生し、こ
れらの分解物の一部が溶融前の乾燥物の粉とともに溶融
窯9の投入口9bから排出されることがある、この排出
されたガスや粉は、コンベアー8aによって移送されて
くる水分を含んだ廃棄物と熱交換されて、廃棄物の温度
上昇と乾燥に寄与し、且つ、排出されたきた粉体の一部
はここで捕集される。During melting in the melting kiln 9, asbestos-containing waste, melting aid,
Decomposed products such as H20:O□:CO□ are generated in the additive, and a part of these decomposed products may be discharged from the inlet 9b of the melting furnace 9 together with the powder of the dried material before melting. The discharged gas and powder exchange heat with the moisture-containing waste transported by the conveyor 8a, contributing to the temperature rise and drying of the waste, and a part of the discharged powder is It is collected here.
なお、ここに排出されたガス等の気体はダクト8Cを通
って集塵機10に吸引されるようにしている。Note that the gas discharged here is sucked into the dust collector 10 through the duct 8C.
溶融窯9は、各種の材料を溶融させることから通常のガ
ラス窯と異なり、耐熱性よりもむしろ耐食性が要求され
る、従って電鋳耐火物や硼珪酸ガラス溶融に強い溶融石
英ブロックを使うことが必要である。The melting kiln 9 is different from a normal glass kiln because it melts various materials, and requires corrosion resistance rather than heat resistance. Therefore, it is recommended to use fused quartz blocks that are resistant to electrocast refractories and borosilicate glass melting. is necessary.
溶融窯9中で溶融された石綿含有廃棄物1ば、下端部に
設けた排出ノズルから成形型11に注入された後冷却機
構12によって徐冷固化させる。The asbestos-containing waste 1 melted in the melting kiln 9 is injected into the mold 11 from a discharge nozzle provided at the lower end, and then slowly cooled and solidified by the cooling mechanism 12.
固化後の成形物は成形型11から脱型し、タンクまたは
ドラム罐などの廃棄物貯蔵容器中に収納して所定の貯蔵
場所に保管する。The molded product after solidification is removed from the mold 11, stored in a waste storage container such as a tank or drum, and stored at a predetermined storage location.
実施例1
石綿布(クリソクイル石綿) 100部最高使用温
度 480℃溶融温度
1.520°C硼 砂
30部上記の配合とした混合物を1.10
0℃で加熱を行って固化物を得た。得られた固化物は5
0ccのガラス固化体であり、その減容比は1/2とい
う小さいものとすることが出来た。また、水に対する溶
出率は10−hg/C−・dayというものであった。Example 1 Asbestos cloth (chrysoquil asbestos) 100 parts Maximum usage temperature 480°C Melting temperature
1.520°C sand
30 parts 1.10 parts of the above mixture
A solidified product was obtained by heating at 0°C. The solidified product obtained is 5
The volume of the vitrified material was 0 cc, and the volume reduction ratio was as small as 1/2. Further, the dissolution rate with respect to water was 10-hg/C-day.
実施例2
珪酸カルシウム保温材 100部最高使用温
度 650°C1へ
溶融温度 1.550℃かさ比重
0.2硼 砂
25部炭酸ナトリウム
10部上記の配合とした混合物を
1.000”Cで加熱を行って固化物を得た。得られた
固化物は50ccのガラス固化体であり、その減容比は
1/10という極めて小さいものとすることができた。Example 2 Calcium silicate heat insulating material 100 parts Maximum operating temperature: 650°C Melting temperature: 1.550°C Bulk specific gravity: 0.2 Boron Sand
25 parts sodium carbonate
10 parts The mixture having the above composition was heated at 1.000"C to obtain a solidified product. The obtained solidified product was a vitrified product of 50 cc, and the volume reduction ratio was extremely small at 1/10. I was able to make it happen.
また、水に対する溶出率は10−6g/cJ−d a
yというものであった。In addition, the dissolution rate for water is 10-6 g/cJ-da
It was called y.
上記の方法による本発明の効果を述べれば以下の通りで
ある。The effects of the present invention obtained by the above method are as follows.
(1)建造物等の廃棄処分によって産出された石綿含有
物は、加熱溶融によってガラス化、若しくは石綿以外の
結晶構造を有する物質に変換させた安定で無害な無機固
体に変換することができるので石綿繊維を他に飛散させ
ることによる害の発生を簡単に防止することができる。(1) Asbestos-containing materials produced through the disposal of buildings, etc. can be vitrified by heating and melting, or converted into stable and harmless inorganic solids that have a crystal structure other than asbestos. It is possible to easily prevent harm caused by scattering asbestos fibers to other places.
(2)処理された廃棄物の体積は、処理前のものに
G
比較して1/2乃至l/10という極めて優れた比率に
減容固化できるので、処理後の物の廃棄貯蔵場所も狭い
場所で済ますことができる。(2) The volume of treated waste is the same as that before treatment.
Since the volume can be reduced and solidified to an extremely superior ratio of 1/2 to 1/10 compared to G, the waste and storage area for the processed material can be stored in a small space.
(3)廃棄処理される石綿含有物は、それ自体では全く
転用性のない物であるが、廃棄処理に伴う爾後成形によ
って無機固体物を土木・建築資材等に再利用をすること
が可能となり、これによって公害の防止と資源の再利用
という優れた副次的効果を奏することができる。(3) Asbestos-containing materials that are disposed of are completely irreversible by themselves, but by forming them after disposal, the inorganic solids can be reused as civil engineering and construction materials, etc. This can have excellent side effects of preventing pollution and reusing resources.
(4)廃棄処理(減容固化)前の石綿含有物の形状は極
めて不定型なものであるが、減容固化を行う際に特定の
形状に成形することができるので、廃棄処理によって得
られたものは、爾後の用途に適合するような形に自由に
成形をすることができるという優れた効果を有している
。(4) Although the shape of asbestos-containing materials before disposal (volume reduction and solidification) is extremely amorphous, it is possible to form them into a specific shape during volume reduction and solidification. This has the excellent effect that it can be freely molded into a shape that is suitable for later use.
(5)廃棄処理をしようとする石綿含有物の、石綿含有
量の範囲は、高レベルのものから低レベルのものまです
べての範囲のものに適用することができる。(5) The range of asbestos content of asbestos-containing materials to be disposed of can be applied to all ranges from high to low levels.
(6)廃棄処理をしようとする材質が無機質のもの O
でも、有機質のものでもよく、更に溶融温度の高低も溶
融助剤及び必要に応じて添加する添加剤を使用すること
によって自由に処理をすることができる。(6) The material to be disposed of may be inorganic or organic, and the melting temperature can be adjusted freely by using melting aids and additives added as necessary. can do.
図は、本発明の実施をするための装置を示す概略的チャ
ート図である。
1・・・石綿含有廃棄物、2a、2b・・・計量器、3
・・・ホッパー、4a・・・粉砕機、4b・・・湿式粉
砕機、5・・・ミキサー、5a、5b・・・溶融助剤の
貯蔵ビン、7a、7b・・・添加材の貯蔵ビン、8a・
・・コンベアー、8b・・・乾燥装置、9・・・溶融窯
、9b・・・投入口特許出願人 明星工業株式会社
手 続 ネ甫 正 書(方式)
昭和61年 6月 25日
特許庁長官 宇 賀 道 部 殿
昭和61年特許願第80894号
2、発明の名称
石綿含有物の廃棄処理方法
3、補正をする者
事件との関係 特許出願人
住所 大阪市西区京町堀1丁目8番5号名称 明星工業
株式会社
代表者 富 木 信 太 部
4、代理人
住所 東京都千代田区神田司町2丁目7番4号6、補正
の対象 願書添付の明細書及び図面7、補正の内容
別紙訂正書のとおり
訂 正 書
願書添付明細書中下記の部分を以下のとおり訂正します
。
(1)明細書第18頁第5行以下の図面の簡単な説明を
「4、図面の簡単な説明
第1図は本発明の実施をするための装置を示す概略的チ
ャート図である。」
と訂正する。
(2)願書添付図面に別紙の通り図番を記入致しまず。The figure is a schematic chart diagram illustrating an apparatus for carrying out the invention. 1... Asbestos-containing waste, 2a, 2b... Measuring instrument, 3
...Hopper, 4a...Crusher, 4b...Wet grinder, 5...Mixer, 5a, 5b...Storage bottle for melting aid, 7a, 7b...Storage bottle for additive material , 8a・
...Conveyor, 8b...Drying device, 9...Melting kiln, 9b...Input port Patent applicant Meisei Kogyo Co., Ltd. Procedures Neho Authorized Letter (Method) June 25, 1986 Commissioner of the Patent Office Michibu Uga, Patent Application No. 80894, filed in 1986, 2, Name of the invention: Method for disposing of asbestos-containing materials 3, Relationship with the case of the person making the amendment Patent applicant address: 1-8-5 Kyomachibori, Nishi-ku, Osaka Name: Myojo Kogyo Co., Ltd. Representative: Shinta Tomiki Department 4, Agent address: 2-7-4-6, Kanda Tsukasa-cho, Chiyoda-ku, Tokyo Subject of amendment: Specification and drawings 7 attached to the application, Attached statement of correction regarding the content of the amendment Correction as follows: The following part of the attached details of the application is corrected as follows. (1) Brief description of the drawings starting from line 5 on page 18 of the specification: ``4. Brief description of the drawings Figure 1 is a schematic chart showing an apparatus for carrying out the present invention.'' I am corrected. (2) Please write the drawing number on the drawing attached to the application as shown in the attached sheet.
Claims (9)
に応じて溶融促進剤などの添加剤を添加したのち、溶融
窯中において高温加熱を施して、石綿繊維をガラス化し
、又は、石綿以外の結晶構造を有する物質に変換するこ
とを特徴とする石綿含有物の廃棄処理方法。(1) Mix a melting aid with waste containing asbestos, add additives such as a melting accelerator as necessary, and then heat the asbestos fibers at high temperature in a melting kiln to vitrify the asbestos fibers, or , a method for disposing of asbestos-containing materials, characterized by converting them into substances having a crystal structure other than asbestos.
温材、塩基性炭酸マグネシウム保温材、珪酸カルシウム
保温材、パーライト保温材、バーミキュライト保温材等
の成形保温材或いはこれらの粉体若しくは水練保温材、
或いはその他の粉体を混合した保温外装塗材である特許
請求の範囲第1項記載の石綿含有物の廃棄処理方法。(2) The waste containing asbestos is a molded insulation material such as asbestos insulation material, diatomaceous earth insulation material, basic magnesium carbonate insulation material, calcium silicate insulation material, perlite insulation material, vermiculite insulation material, or powder or water paste of these materials. insulation material,
The method for disposing of asbestos-containing materials according to claim 1, which is a heat-insulating exterior coating material mixed with other powders.
綿紐、石綿ロープ、石綿チューブ、石綿リボン、石綿布
及びこれらの紡織品、或いは、これらの加工品の一つ、
若しくはこれらの混合物である特許請求の範囲第1項記
載の石綿含有物の廃棄処理方法。(3) The waste containing asbestos is asbestos fiber, asbestos thread, asbestos string, asbestos rope, asbestos tube, asbestos ribbon, asbestos cloth, textile products thereof, or one of these processed products,
or a mixture thereof. The method for disposing of asbestos-containing materials according to claim 1.
グ、ブレーキライニング、クラッチフェーシングである
特許請求の範囲第1項記載の石綿含有物の廃棄処理方法
。(4) The method for disposing of asbestos-containing materials according to claim 1, wherein the asbestos-containing waste is a gasket, packing, brake lining, or clutch facing.
特許請求の範囲第1項記載の石綿含有物の廃棄処理方法
。(5) The method for disposing of asbestos-containing material according to claim 1, wherein the asbestos-containing waste is asbestos paper or asbestos board.
綿珪酸カルシウム板或いは石綿タイルである特許請求の
範囲第1項記載の石綿含有物の廃棄処理方法。(6) The method for disposing of asbestos-containing materials according to claim 1, wherein the asbestos-containing waste is an asbestos-cement product, an asbestos-calcium silicate board, or an asbestos tile.
求の範囲第1項記載の石綿含有物の廃棄処理方法。(7) The method for disposing of asbestos-containing material according to claim 1, wherein the asbestos-containing waste is sprayed asbestos.
、珪酸化合物、炭酸化合物及びアルカリ土類金属水酸化
物若しくは、本発明方法の実施過程で発生した溶融固化
物のカレットの何れか一つ若しくはこれらの組み合わせ
である特許請求の範囲第1項記載の石綿含有物の廃棄処
理方法。(8) The melting aid to be added is either a boric acid compound, a phosphoric acid compound, a silicate compound, a carbonic acid compound, an alkaline earth metal hydroxide, or a cullet of the melt-solidified product generated in the process of carrying out the method of the present invention. 2. The method for disposing of asbestos-containing materials according to claim 1, which is a combination of these.
ウム、硫酸バリウム等の溶融促進剤、硝酸ナトリウム、
硝酸カリウム等の酸化剤、炭素、酸化第一錫、塩化第一
錫、黒鉛、亜鉛等の還元剤の何れか一つ若しくはこれら
の組み合わせである特許請求の範囲第1項記載の石綿含
有物の廃棄処理方法。(9) Additives to be added together with the melting aid include melting promoters such as barium carbonate and barium sulfate, sodium nitrate,
Disposal of asbestos-containing material as set forth in claim 1, which is any one or a combination of oxidizing agents such as potassium nitrate, reducing agents such as carbon, stannous oxide, stannous chloride, graphite, zinc, etc. Processing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61080894A JPS62237984A (en) | 1986-04-08 | 1986-04-08 | Waste materials treatment for asbestos-containing substance |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61080894A JPS62237984A (en) | 1986-04-08 | 1986-04-08 | Waste materials treatment for asbestos-containing substance |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62237984A true JPS62237984A (en) | 1987-10-17 |
Family
ID=13731068
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61080894A Pending JPS62237984A (en) | 1986-04-08 | 1986-04-08 | Waste materials treatment for asbestos-containing substance |
Country Status (1)
Country | Link |
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JP (1) | JPS62237984A (en) |
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01171685A (en) * | 1987-12-25 | 1989-07-06 | Mitsui Eng & Shipbuild Co Ltd | Treatment of waste containing asbestos |
JPH02251289A (en) * | 1988-11-29 | 1990-10-09 | Hitachi Zosen Eng Kk | Method for melting treatment of asbestos waste material |
JPH02303585A (en) * | 1989-05-17 | 1990-12-17 | Kubota Corp | Method for melting asbestos |
JPH0330885A (en) * | 1989-06-27 | 1991-02-08 | Osaka Gas Co Ltd | Melt-treatment of asbestos |
JPH0360789A (en) * | 1989-07-28 | 1991-03-15 | Osaka Gas Co Ltd | Melting treatment of asbestos |
FR2668726A1 (en) * | 1990-11-02 | 1992-05-07 | Commissariat Energie Atomique | Method for destroying asbestos fibres by melting, and implementation device |
JPH04180879A (en) * | 1990-11-15 | 1992-06-29 | Tokyo Electric Power Co Inc:The | Treatment of asbestos waste and calcium silicate waste material |
CH680198A5 (en) * | 1990-07-06 | 1992-07-15 | Sulzer Ag | |
EP0568367A2 (en) * | 1992-05-01 | 1993-11-03 | The Dow Chemical Company | Process for treating wastes of asbestos |
JP2003055072A (en) * | 2001-08-10 | 2003-02-26 | Ig Tech Res Inc | Recycled fertilizer and soil conditioner |
WO2007005855A1 (en) * | 2005-06-30 | 2007-01-11 | Ari Technologies, Inc. | System and method for accelerating the conversion of asbestos in the process of mineralogical conversion |
JP2007301419A (en) * | 2006-01-27 | 2007-11-22 | A & A Material Corp | Treatment method for inorganic based waste material |
WO2008041416A1 (en) * | 2006-09-29 | 2008-04-10 | K.K.M-Tec | Method of treating asbestos |
JP2008105020A (en) * | 2006-09-28 | 2008-05-08 | Mitsubishi Materials Corp | Treatment method of asbestos-containing material and fluoride sludge and cement manufacturing method |
WO2008111512A1 (en) * | 2007-03-12 | 2008-09-18 | Street Design Corp. | Method of asbestos detoxification |
JP2008264652A (en) * | 2007-04-18 | 2008-11-06 | Hiroshi Nanba | Asbestos treatment method and continual injection ball mill |
JP2008272537A (en) * | 2006-07-24 | 2008-11-13 | Hirase Ryuichi | Detoxifying apparatus of waste asbestos material |
JP2009514673A (en) * | 2005-11-03 | 2009-04-09 | アトン−エイチティー エス.エー. | Method and apparatus for conversion of materials containing asbestos |
WO2009147834A1 (en) * | 2008-06-06 | 2009-12-10 | 株式会社トクヤマシルテック | Method of detoxifying asbestos-containing solid waste |
US7658703B2 (en) | 2006-09-29 | 2010-02-09 | Nichias Corporation | Method of preventing exposure of asbestos-containing material, method of treating asbestos-containing waste material, method of melt treating asbestos-containing waste material, asbestos-containing waste material treated article, and asbestos-containing melt treated article |
JPWO2008072467A1 (en) * | 2006-12-15 | 2010-03-25 | 独立行政法人産業技術総合研究所 | Method for melting asbestos and apparatus therefor |
JP2011016051A (en) * | 2009-07-07 | 2011-01-27 | Fuji Denki Thermosystems Kk | Waste asbestos detoxification apparatus |
US7939705B2 (en) | 2005-06-30 | 2011-05-10 | Ari Technologies, Inc. | System and method for treating asbestos |
JP5194297B2 (en) * | 2005-09-20 | 2013-05-08 | 大学共同利用機関法人自然科学研究機構 | Asbestos modification method |
KR101709612B1 (en) * | 2016-06-02 | 2017-03-24 | 주식회사 한공 | Lithium Silicate Glass-Ceramics Type Dust Suppressant to Prevent Flying-Asbestos |
CN111361083A (en) * | 2020-03-25 | 2020-07-03 | 杭州蒙图机械设计有限公司 | Injection molding process for automobile parts |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5268081A (en) * | 1975-12-04 | 1977-06-06 | Kureha Chem Ind Co Ltd | Method of recovering asbestos-contg. waste material |
JPS5711277A (en) * | 1980-05-27 | 1982-01-20 | Nat De Raminante Soc | Production of modified asbestos fiber |
JPS5723900A (en) * | 1980-07-19 | 1982-02-08 | Doryokuro Kakunenryo | Method of melting waste |
-
1986
- 1986-04-08 JP JP61080894A patent/JPS62237984A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5268081A (en) * | 1975-12-04 | 1977-06-06 | Kureha Chem Ind Co Ltd | Method of recovering asbestos-contg. waste material |
JPS5711277A (en) * | 1980-05-27 | 1982-01-20 | Nat De Raminante Soc | Production of modified asbestos fiber |
JPS5723900A (en) * | 1980-07-19 | 1982-02-08 | Doryokuro Kakunenryo | Method of melting waste |
Cited By (41)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01171685A (en) * | 1987-12-25 | 1989-07-06 | Mitsui Eng & Shipbuild Co Ltd | Treatment of waste containing asbestos |
JPH0436753B2 (en) * | 1987-12-25 | 1992-06-17 | Mitsui Shipbuilding Eng | |
JPH02251289A (en) * | 1988-11-29 | 1990-10-09 | Hitachi Zosen Eng Kk | Method for melting treatment of asbestos waste material |
JPH02303585A (en) * | 1989-05-17 | 1990-12-17 | Kubota Corp | Method for melting asbestos |
JPH0330885A (en) * | 1989-06-27 | 1991-02-08 | Osaka Gas Co Ltd | Melt-treatment of asbestos |
JPH0360789A (en) * | 1989-07-28 | 1991-03-15 | Osaka Gas Co Ltd | Melting treatment of asbestos |
CH680198A5 (en) * | 1990-07-06 | 1992-07-15 | Sulzer Ag | |
FR2668726A1 (en) * | 1990-11-02 | 1992-05-07 | Commissariat Energie Atomique | Method for destroying asbestos fibres by melting, and implementation device |
JPH04180879A (en) * | 1990-11-15 | 1992-06-29 | Tokyo Electric Power Co Inc:The | Treatment of asbestos waste and calcium silicate waste material |
EP0568367A3 (en) * | 1992-05-01 | 1994-12-28 | Dow Chemical Co | Process for treating wastes of asbestos. |
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JP2003055072A (en) * | 2001-08-10 | 2003-02-26 | Ig Tech Res Inc | Recycled fertilizer and soil conditioner |
WO2007005855A1 (en) * | 2005-06-30 | 2007-01-11 | Ari Technologies, Inc. | System and method for accelerating the conversion of asbestos in the process of mineralogical conversion |
US9314825B2 (en) | 2005-06-30 | 2016-04-19 | Ari Global Technologies Limited | System and method for treating asbestos |
US8093443B2 (en) | 2005-06-30 | 2012-01-10 | Ari Technologies, Inc. | System and method for accelerating the conversion of asbestos in the process of mineralogical conversion |
JP4808252B2 (en) * | 2005-06-30 | 2011-11-02 | エーアールアイ テクノロジーズ,インコーポレーテッド | System and method for accelerating the conversion of asbestos in a mineralogical conversion process |
AU2006265089B2 (en) * | 2005-06-30 | 2011-05-26 | Ari Technologies, Inc. | System and method for accelerating the conversion of asbestos in the process of mineralogical conversion |
US7939705B2 (en) | 2005-06-30 | 2011-05-10 | Ari Technologies, Inc. | System and method for treating asbestos |
JP2008544851A (en) * | 2005-06-30 | 2008-12-11 | エーアールアイ テクノロジーズ,インコーポレーテッド | System and method for accelerating the conversion of asbestos in a mineralogical conversion process |
JP5194297B2 (en) * | 2005-09-20 | 2013-05-08 | 大学共同利用機関法人自然科学研究機構 | Asbestos modification method |
JP2009514673A (en) * | 2005-11-03 | 2009-04-09 | アトン−エイチティー エス.エー. | Method and apparatus for conversion of materials containing asbestos |
JP4663794B2 (en) * | 2005-11-03 | 2011-04-06 | アトン−エイチティー エス.エー. | Method and apparatus for conversion of materials containing asbestos |
JP2007301419A (en) * | 2006-01-27 | 2007-11-22 | A & A Material Corp | Treatment method for inorganic based waste material |
JP2008272537A (en) * | 2006-07-24 | 2008-11-13 | Hirase Ryuichi | Detoxifying apparatus of waste asbestos material |
JP2008105020A (en) * | 2006-09-28 | 2008-05-08 | Mitsubishi Materials Corp | Treatment method of asbestos-containing material and fluoride sludge and cement manufacturing method |
KR101085087B1 (en) * | 2006-09-29 | 2011-11-18 | 가부시키가이샤 엠-테크 | Method of treating asbestos |
US7658703B2 (en) | 2006-09-29 | 2010-02-09 | Nichias Corporation | Method of preventing exposure of asbestos-containing material, method of treating asbestos-containing waste material, method of melt treating asbestos-containing waste material, asbestos-containing waste material treated article, and asbestos-containing melt treated article |
WO2008041416A1 (en) * | 2006-09-29 | 2008-04-10 | K.K.M-Tec | Method of treating asbestos |
JPWO2008072467A1 (en) * | 2006-12-15 | 2010-03-25 | 独立行政法人産業技術総合研究所 | Method for melting asbestos and apparatus therefor |
WO2008111512A1 (en) * | 2007-03-12 | 2008-09-18 | Street Design Corp. | Method of asbestos detoxification |
US8835707B2 (en) | 2007-03-12 | 2014-09-16 | Street Design Corp. | Method of asbestos detoxification |
JP2008264652A (en) * | 2007-04-18 | 2008-11-06 | Hiroshi Nanba | Asbestos treatment method and continual injection ball mill |
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CN102015135A (en) * | 2008-06-06 | 2011-04-13 | 德山硅技术株式会社 | Method of detoxifying asbestos-containing solid waste |
JP2009291730A (en) * | 2008-06-06 | 2009-12-17 | Tokuyama Siltech:Kk | Method for detoxifying solid waste containing asbestos |
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JP2012504492A (en) * | 2008-10-01 | 2012-02-23 | エーアールアイ テクノロジーズ,インコーポレーテッド | System and method for treating asbestos |
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JP2011016051A (en) * | 2009-07-07 | 2011-01-27 | Fuji Denki Thermosystems Kk | Waste asbestos detoxification apparatus |
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