JP2002180146A - Method for recovering mercury from waste fluorescent lamp - Google Patents
Method for recovering mercury from waste fluorescent lampInfo
- Publication number
- JP2002180146A JP2002180146A JP2000404107A JP2000404107A JP2002180146A JP 2002180146 A JP2002180146 A JP 2002180146A JP 2000404107 A JP2000404107 A JP 2000404107A JP 2000404107 A JP2000404107 A JP 2000404107A JP 2002180146 A JP2002180146 A JP 2002180146A
- Authority
- JP
- Japan
- Prior art keywords
- mercury
- waste fluorescent
- fluorescent lamp
- silver
- gold
- 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
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 title claims abstract description 110
- 229910052753 mercury Inorganic materials 0.000 title claims abstract description 104
- 239000002699 waste material Substances 0.000 title claims abstract description 29
- 238000000034 method Methods 0.000 title claims description 24
- 229910052709 silver Inorganic materials 0.000 claims abstract description 19
- 239000004332 silver Substances 0.000 claims abstract description 19
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims abstract description 17
- 229910052737 gold Inorganic materials 0.000 claims abstract description 17
- 239000010931 gold Substances 0.000 claims abstract description 17
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 15
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 15
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052802 copper Inorganic materials 0.000 claims abstract description 13
- 239000010949 copper Substances 0.000 claims abstract description 13
- 239000007864 aqueous solution Substances 0.000 claims abstract description 12
- 239000000126 substance Substances 0.000 claims description 10
- 239000000843 powder Substances 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 5
- 239000011521 glass Substances 0.000 claims description 3
- 238000001179 sorption measurement Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 6
- 229910052751 metal Inorganic materials 0.000 abstract description 4
- 239000002184 metal Substances 0.000 abstract description 4
- 238000001035 drying Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 28
- 229910000497 Amalgam Inorganic materials 0.000 description 9
- 229910000474 mercury oxide Inorganic materials 0.000 description 7
- UKWHYYKOEPRTIC-UHFFFAOYSA-N mercury(ii) oxide Chemical compound [Hg]=O UKWHYYKOEPRTIC-UHFFFAOYSA-N 0.000 description 7
- 238000000926 separation method Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229940008718 metallic mercury Drugs 0.000 description 6
- 238000012856 packing Methods 0.000 description 6
- 239000000835 fiber Substances 0.000 description 4
- 238000011049 filling Methods 0.000 description 4
- 239000012494 Quartz wool Substances 0.000 description 3
- 229920001429 chelating resin Polymers 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012784 inorganic fiber Substances 0.000 description 2
- 150000003568 thioethers Chemical class 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- -1 aluminum Chemical compound 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/82—Recycling of waste of electrical or electronic equipment [WEEE]
Landscapes
- Treating Waste Gases (AREA)
- Processing Of Solid Wastes (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、廃蛍光ランプの
水銀を金属水銀として回収する廃蛍光ランプの水銀回収
方法である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering mercury of a waste fluorescent lamp for recovering mercury of a waste fluorescent lamp as metallic mercury.
【0002】[0002]
【従来の技術】従来より、使用済みの廃蛍光ランプの水
銀処理には次のような方法が行われている。 1)活性炭やキレート樹脂でガス状の水銀を処理する。 2)水の中での廃蛍光ランプの破砕やガラスの水洗。 3)硫化物や各種の薬品の使用 4)金属による水銀のアマルガム処理は石英ウールなど
の繊維に金、銀を担持する方法や銅のワイヤーネットに
銀をコーテイングする方法や金属をメッキしたプラスチ
ックによる方法などがある。2. Description of the Related Art Conventionally, the following method has been used for mercury treatment of used waste fluorescent lamps. 1) Treat gaseous mercury with activated carbon or chelating resin. 2) Crushing of waste fluorescent lamps in water and washing of glass with water. 3) Use of sulfides and various chemicals 4) Amalgam treatment of mercury with metal is carried out by carrying gold and silver on fibers such as quartz wool, by coating silver on copper wire nets, or by metal-plated plastic. There are methods.
【0003】1)の活性炭やキレート樹脂でガス状の水
銀を処理する方法は水銀を吸着した活性炭やキレート樹
脂の再生が出来ない。2)水の中での廃蛍光ランプの破
砕やガラスの水洗は微細な蛍光体が水銀と共に水中にま
ざり、濾過、乾燥に多大の費用がかかる。3)硫化物や
各種の薬品の使用も水銀を金属にするためのコストが高
くなる。4)金属による水銀のアマルガム処理は廃蛍光
ランプのように大量の水銀が排出される場合、直接使用
することは好ましくない。In the method of (1) for treating gaseous mercury with activated carbon or chelating resin, the activated carbon or chelating resin adsorbing mercury cannot be regenerated. 2) Disruption of the waste fluorescent lamp in water and washing of the glass with water involve fine phosphors in the water together with mercury, so that filtration and drying are very expensive. 3) The use of sulfides and various chemicals also increases the cost of converting mercury into metal. 4) The amalgam treatment of mercury with a metal is not preferable to be used directly when a large amount of mercury is discharged like a waste fluorescent lamp.
【0004】[0004]
【発明が解決しようとする課題】前記問題を解決するた
めに、本発明では廃蛍光ランプをリサイクルする時、水
銀を金属水銀として安く、かつ簡単なプロセスで回収さ
れる水銀回収方法を提供する。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a mercury recovery method in which mercury is recovered as metallic mercury at a low cost and in a simple process when a waste fluorescent lamp is recycled.
【0005】[0005]
【課題を解決するための手段】蛍光ランプの水銀は点灯
中にランプの構成材料と化学的に反応して、酸化水銀、
アマルガムなどの化合物になる。金属水銀は260℃以
下、酸化水銀は350℃以下、アマルガムは350℃以
上でそれぞれ熱分解し水銀を放出する。The mercury of the fluorescent lamp chemically reacts with the constituent materials of the lamp during operation to produce mercury oxide,
It becomes a compound such as amalgam. Metallic mercury is thermally decomposed at 260 ° C. or less, mercury oxide at 350 ° C. or less, and amalgam at 350 ° C. or more to release mercury.
【0006】従って、水銀が酸化水銀、アマルガム以外
に変化しない水溶液に水銀を含む気体を通し、大部分の
水銀、酸化水銀、アマルガムを水溶液中で回収し、取り
きれなかった水銀、酸化水銀、アマルガムは金、銀、
銅、アルミ等の水銀と反応あるいは吸着する物質の充填
層を通過させて、水銀を回収する。Therefore, mercury-containing gas is passed through an aqueous solution in which mercury does not change except for mercury oxide and amalgam, and most of mercury, mercury oxide and amalgam are recovered in the aqueous solution. Is gold, silver,
Mercury is recovered by passing through a packed layer of a substance that reacts or adsorbs with mercury such as copper and aluminum.
【0007】水銀と反応あるいは吸着した金、銀、銅、
アルミ等は蛍光粉他水銀を回収する必要のある物と同じ
ように真空加熱装置と凝縮器等公知の方法で水銀を分離
し、真空ポンプの排気体は水溶液の中を通過させ、続い
て金、銀、銅、アルミ等の水銀と反応あるいは吸着する
物質の充填層を通過させ、水銀を吸着、反応し水銀を回
収する。この方法により、廃蛍光ランプの水銀はすべて
金属水銀として回収される。[0007] Gold, silver, copper, which has reacted or adsorbed with mercury,
Aluminum is separated from mercury by a well-known method such as a vacuum heating device and condenser in the same way as fluorescent powder and other materials that need to recover mercury, and the exhaust of a vacuum pump is passed through an aqueous solution, followed by gold. It passes through a packed layer of a substance that reacts or adsorbs with mercury such as silver, copper, and aluminum, and adsorbs and reacts with mercury to recover mercury. By this method, all mercury in the waste fluorescent lamp is recovered as metallic mercury.
【0008】[0008]
【発明の実施の形態】廃蛍光ランプを乾式で処理する場
合、蛍光粉の回収方法で2種類に分けることが出来る。 1)電極部を水素バーナーや機械的に切断し、蛍光粉を
空気で吹き飛ばしたり、吸引で回収する方法。 2)特開2000−202319及び特開平11−30
0332で処理し、気体の流れを少なくし、蛍光粉を篩
で回収する方法。この両者の違いは水銀を含む気体の量
が大きく違うことである。DESCRIPTION OF THE PREFERRED EMBODIMENTS When a waste fluorescent lamp is treated in a dry manner, it can be divided into two types according to the method of recovering the fluorescent powder. 1) A method in which the electrode portion is cut with a hydrogen burner or mechanically, and the fluorescent powder is blown off with air or collected by suction. 2) JP-A-2000-202319 and JP-A-11-30
0332, a method of reducing the flow of gas and collecting fluorescent powder through a sieve. The difference between the two is that the amount of gas containing mercury is greatly different.
【0009】1)の場合は水銀を含む気体の量が多いこ
とから水銀を回収する水溶液との接触は湿式集塵機の特
開平9−49627煙の煤塵・有毒ガス除去装置やベン
チュリスクラバーやジェットスクラバー等のスクラバー
方式、株式会社ミューカンパニーリミテドの高性能湿式
廃ガス洗浄塔ミキシングスクラバー方式ミュースクラバ
ー塔などの使用が必要になる。In the case of 1), since the amount of gas containing mercury is large, contact with an aqueous solution for recovering mercury is carried out using a wet dust collector disclosed in Japanese Unexamined Patent Publication No. 9-49627, a device for removing soot and toxic gas, a venturi scrubber, a jet scrubber, and the like. It is necessary to use a scrubber system, such as a high-performance wet waste gas washing tower mixing scrubber system mu scrubber tower of Mu Company Limited.
【0010】2)の場合は水銀を含む気体の量が少ない
ことから特開平10−165716流動濾過器と散気板
を併用して水銀を回収する方法などの水溶液を固定する
方法で充分である。In the case of 2), since the amount of gas containing mercury is small, a method of fixing an aqueous solution such as a method of recovering mercury using a combined use of a fluidized filter and a diffuser plate as disclosed in JP-A-10-165716 is sufficient. .
【0011】図1に2)の場合の廃蛍光ランプ処理工場
の工程図を示す。全体を透明な板1で囲み、廃蛍光ラン
プの投入口のみ開いている。粉砕機の下他数カ所から投
入口より水銀を含む気体が吹き出さない程度に吸引す
る。蛍光ランプの内部が減圧されていることから吸引量
はわずかである。FIG. 1 shows a process chart of a waste fluorescent lamp processing plant in the case of 2). The whole is surrounded by a transparent plate 1 and only the inlet of the waste fluorescent lamp is open. The gas containing mercury is sucked from several other places under the pulverizer so that gas containing mercury does not blow out. Since the inside of the fluorescent lamp is depressurized, the suction amount is small.
【0012】図2に水銀回収装置の1例を示す。この水
銀回収装置にはこの他に、各種の湿式集塵装置が使用可
能である。FIG. 2 shows an example of a mercury recovery apparatus. Various other wet dust collectors can be used for the mercury recovery device.
【0013】図3に大部分の水銀を除去した気体が整流
板で流れを均一にし、水銀を除去する装置を示す。排気
体は廃蛍光ランプの投入口へ導かれる。FIG. 3 shows an apparatus for removing the mercury in which the gas from which most of the mercury has been removed is made uniform by the current plate. The exhaust body is led to the inlet of the waste fluorescent lamp.
【0014】図2の水銀回収装置について説明する。ハ
ウジングは密閉容器の上部ハウジング6と、その底部に
連結した下部ハウジング7との2分割構造からなる。上
部ハウジング6の下端部外縁に雄ねじ8が形成され、下
部ハウジング7の上部に上部ハウジング6の雄ねじ8が
螺合する雌ねじ9が設けられ、上部ハウジング6の雄ね
じ8を下部ハウジング7の雌ねじ9に螺合することによ
り、両ハウジング6,7は一体化されている。上部ハウ
ジング6の底部と下部ハウジング7の頂部間に下に凸な
円錐形状の第1分離部2が挟持された構造に形成されて
いる。第1分離部2の下面は排気体が吹き付けられて水
銀を分離する分離面10はその下端部から上端部まで連
続する縦スリットより成る透孔11が周方向に配設され
てなる構造である。また第1分離部の分離面は前記スリ
ット孔構造のものではなく、網等の多孔部材で形成して
も良い。尚、第1分離面2は前記円錐形状に限定されな
い。この分離面の上部13に散気板を設置する。水銀は
下部14に貯まり、15より排出される。The mercury recovery apparatus shown in FIG. 2 will be described. The housing has a two-part structure consisting of an upper housing 6 of a closed container and a lower housing 7 connected to the bottom. A male screw 8 is formed on the outer edge of the lower end of the upper housing 6, and a female screw 9 for screwing the male screw 8 of the upper housing 6 is provided above the lower housing 7. The two housings 6 and 7 are integrated by screwing. The first separating portion 2 having a conical shape that is convex downward is sandwiched between the bottom of the upper housing 6 and the top of the lower housing 7. The lower surface of the first separation unit 2 has a structure in which a separation surface 10 from which an exhaust body is blown to separate mercury is provided with a through hole 11 formed of a vertical slit continuous from the lower end to the upper end in the circumferential direction. . In addition, the separation surface of the first separation portion may be formed of a porous member such as a net instead of having the slit hole structure. Note that the first separation surface 2 is not limited to the conical shape. A diffuser plate is provided on the upper part 13 of the separation surface. Mercury accumulates in the lower part 14 and is discharged from 15.
【0015】そして、上部ハウジング6内には無機繊維
で球状にした球状物12が多数封入されている。無機繊
維はセラミックファイバーやガラス繊維でも良いし、
金、銀をコーテイングした石英ウールや金、銀、アルミ
などの繊維でも良い。この球状物は流動する状態で使用
する。上部ハウジング6の上部16には水滴分離部が設
けられている。In the upper housing 6, a large number of spherical materials 12 made of inorganic fibers are sealed. The inorganic fiber may be ceramic fiber or glass fiber,
Quartz wool coated with gold or silver or fibers of gold, silver, aluminum or the like may be used. The sphere is used in a flowing state. The upper part 16 of the upper housing 6 is provided with a water drop separating part.
【0016】3より水銀を含んだ気体が投入され、大部
分の水銀を除去除去された気体は5より排出される。A gas containing mercury is introduced from 3, and a gas from which most of the mercury has been removed is removed from 5.
【0017】また、図示していないが、3の水銀を含ん
だ気体の投入口から水銀を含んだ気体を吹き込むような
吹き込み機を接続するか、また、5の排出口から水銀を
含んだ気体を吸引するような吸引機を接続する。Although not shown, a blower that blows in a gas containing mercury from the inlet of the gas containing mercury is connected, or a gas containing mercury is discharged from the outlet of the gas. Connect a suction machine that sucks in.
【0018】図3は特開平9−276634を応用す
る。図2で大部分の水銀を除去した気体は図3の装置で
排気体の流れを均一にし、球体の充填物により、残りの
水銀を除去する。球体の充填物には金、銀をコーテイン
グした石英ウールや金、銀、アルミなどの繊維を使用す
る。FIG. 3 is based on Japanese Patent Application Laid-Open No. 9-276634. The gas from which most of the mercury has been removed in FIG. 2 makes the flow of the exhaust body uniform in the apparatus of FIG. 3, and the remaining mercury is removed by filling the sphere. For the filling of the sphere, use is made of quartz wool coated with gold or silver or fibers of gold, silver, aluminum or the like.
【0019】21は水銀を含む気体の投入口である。2
2は23の球体の充填物を保持するメッシュ板または多
孔板である。24は23の球体の充填物を通過して、水
銀が除去された気体の排出口である。25は投入口21
から水銀を含む気体が均一かつ平行に球体の充填物に向
かって上昇するように23の球体の充填物の下方に配置
した整流板であり、26は球体の充填物を通過した水銀
を含まない気体が平行に流れるように23の球体の充填
物の上方に配設した整流板である。27は投入口21に
設けられた整流板、28は排出口24に設けられた整流
板である。Reference numeral 21 denotes an inlet for a gas containing mercury. 2
Reference numeral 2 denotes a mesh plate or a perforated plate holding a packing of 23 spheres. Reference numeral 24 denotes a gas outlet from which the mercury has been removed through the filling of the 23 spheres. 25 is the inlet 21
A current plate disposed below the 23 spherical packing so that the gas containing mercury rises uniformly and parallel to the spherical packing, and 26 does not contain mercury passing through the spherical packing. A current plate disposed above the 23 spherical packing so that gas flows in parallel. Reference numeral 27 denotes a rectifying plate provided at the inlet 21, and reference numeral 28 denotes a rectifying plate provided at the outlet 24.
【0020】また、図示していないが、21の水銀を含
んだ気体の投入口から水銀を含んだ気体を吹き込むよう
な吹き込み機を接続するか、また、24の排出口から気
体を吸引するような吸引機を接続することもある。何れ
の手段においても気体が低速で流れるように吸引力また
は吹き込み力が調整されている。Although not shown, a blower for blowing a gas containing mercury from an inlet for mercury-containing gas 21 is connected, or a gas is sucked from an outlet 24. In some cases, a simple suction device may be connected. In any of the means, the suction force or the blowing force is adjusted so that the gas flows at a low speed.
【0021】廃蛍光ランプの処理が終わった時あるいは
機械の整備の時は、廃蛍光ランプの投入口を閉じ、図3
の排気体の排出口24から空気を廃蛍光ランプ処理工場
へ送り、循環しながら装置の中の水銀を回収する。When the processing of the waste fluorescent lamp is completed or when the machine is maintained, the inlet of the waste fluorescent lamp is closed, and FIG.
Air is sent from a discharge port 24 of the exhaust body to a waste fluorescent lamp processing plant, and mercury in the apparatus is recovered while circulating.
【0022】水銀と反応あるいは吸着した金、銀、銅、
アルミ等は蛍光粉他水銀を回収する必要のある物と同じ
ように真空加熱装置と凝縮器等公知の方法で水銀を分離
し、真空ポンプの排気体は水溶液の中を通過させ、続い
て金、銀、銅、アルミ等の水銀と反応あるいは吸着する
物質の中を排気体の流れを均一にし、充填層を通過さ
せ、水銀を吸着、反応し水銀を回収する。この方法によ
り、廃蛍光ランプの水銀はすべて金属水銀として回収さ
れる。Gold, silver, copper, which has reacted or adsorbed with mercury,
Aluminum is separated from mercury by a known method such as a vacuum heating device and condenser in the same manner as fluorescent powder and other materials that need to recover mercury. The flow of the exhaust body is made uniform in a substance that reacts or adsorbs with mercury, such as silver, copper, and aluminum, and is passed through a packed bed to adsorb and react with mercury to recover mercury. By this method, all mercury in the waste fluorescent lamp is recovered as metallic mercury.
【0023】以上本発明はこのような実施形態に何ら限
定されるものではなく、本発明の要旨を逸脱しない範囲
において種々なる態様で実施することが出来る。The present invention is not limited to such an embodiment at all, and can be implemented in various modes without departing from the gist of the present invention.
【0024】[0024]
【発明の効果】以上のように本発明では廃蛍光ランプの
破砕処理で生ずる水銀を含む気体を水銀が酸化水銀、ア
マルガム以外に変化しない水溶液に通し、大部分の水
銀、酸化水銀、アマルガムを水溶液中で回収し、取りき
れなかった水銀、酸化水銀、アマルガムは金、銀、銅、
アルミ等の水銀と反応あるいは吸着する物質の充填層を
排気体の流れを均一にし通過させて、水銀を回収する。
蛍光粉や水銀を吸着、反応した金、銀、銅、アルミ等は
真空加熱装置と凝縮器等で水銀を回収する。これによ
り、水銀はすべて金属水銀として回収される。As described above, in the present invention, most of mercury, mercury oxide, and amalgam are passed through an aqueous solution in which mercury is generated by the crushing treatment of a waste fluorescent lamp and the mercury is not changed except for mercury oxide and amalgam. Mercury, mercury oxide, and amalgam that were collected and removed in gold, silver, copper,
The flow of the exhaust body is made uniform through a packed layer of a substance that reacts with or adsorbs mercury such as aluminum, and the mercury is recovered.
Gold, silver, copper, aluminum, etc., which have absorbed and reacted with fluorescent powder and mercury, recover the mercury with a vacuum heater and condenser. As a result, all mercury is recovered as metallic mercury.
【図1】廃蛍光ランプの処理工程図の1例FIG. 1 is an example of a processing diagram of a waste fluorescent lamp.
【図2】廃蛍光ランプの破砕処理で生ずる水銀を含む気
体を水溶液中で水銀回収する方法の1例FIG. 2 shows an example of a method for recovering mercury-containing gas generated by crushing of a waste fluorescent lamp in an aqueous solution.
【図3】大部分の水銀を除去した気体が整流板で流れを
均一にし、水銀を除去する装置の1例FIG. 3 shows an example of an apparatus for removing mercury by making the flow of most of the mercury-removed gas uniform with a flow straightening plate.
1廃蛍光ランプの処理工場を囲む透明な板 2第1分離部 3水銀を含む気体の入口 4水溶液の投入口 5排出口 6上部ハウジング 7下部ハウジング 8雄ねじ 9雌ねじ 10分離面 11透孔 12球状物 13散気板 14水銀貯留部 15水銀排出口 16水滴分離部 21水銀を含む気体の投入口 22球体の充填物を保持するメッシュ板または多孔板 23球体の充填物 24水銀が除去された気体の排出口 25、26,27,28整流板 1 Transparent plate surrounding the waste fluorescent lamp processing plant 2 First separating part 3 Gas inlet containing mercury 4 Inlet of aqueous solution 5 Outlet 6 Upper housing 7 Lower housing 8 Male screw 9 Female screw 10 Separation surface 11 Through hole 12 spherical Object 13 diffuser plate 14 mercury storage unit 15 mercury outlet 16 water drop separator 21 inlet for gas containing mercury 22 mesh plate or perforated plate holding packing of sphere 23 filling of sphere 24 gas from which mercury is removed Outlet 25, 26, 27, 28 Rectifier plate
フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C22B 9/02 B09B 3/00 Z H01J 9/50 303A 5/00 ZABZ Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) C22B 9/02 B09B 3/00 Z H01J 9/50 303A 5/00 ZABZ
Claims (5)
ンプの破砕、粉砕、選別を行い、発生した水銀ガスを含
む気体は吸引で水溶液の中を通過させ、続いて金、銀、
銅、アルミ等の水銀と反応あるいは吸着する物質の充填
層を通過させ、水銀を吸着、反応させる廃蛍光ランプの
水銀回収方法。In a closed box, waste fluorescent lamps are crushed, crushed and sorted in a dry manner, and the generated gas containing mercury gas is passed through an aqueous solution by suction, followed by gold, silver,
A mercury recovery method for waste fluorescent lamps that adsorbs and reacts with mercury by passing it through a packed layer of substances that react or adsorb with mercury such as copper and aluminum.
と反応、吸着する物質を混入したことを特徴とする請求
項1の水銀を吸着、反応させる廃蛍光ランプの水銀回収
方法。2. A method for recovering mercury from a waste fluorescent lamp for adsorbing and reacting with mercury according to claim 1, wherein a substance which reacts with and adsorbs mercury such as gold, silver, copper and aluminum is mixed in the aqueous solution. .
を特徴とする請求項1の水銀を吸着させる廃蛍光ランプ
の水銀回収方法。3. The method for recovering mercury of a waste fluorescent lamp for adsorbing mercury according to claim 1, wherein a fluorescent powder having a small amount of exhaust is separated by a sieve.
は吸着する物質の充填層で水銀を回収する工程におい
て、整流板で水銀を含む気体の流れを均一にすることを
特徴とする請求項1の水銀を吸着させる廃蛍光ランプの
水銀回収方法。4. A process for recovering mercury in a packed bed of a substance which reacts with or adsorbs mercury such as gold, silver, copper, aluminum or the like, wherein a flow of a gas containing mercury is made uniform by a current plate. The method for collecting mercury of a waste fluorescent lamp for adsorbing mercury according to claim 1.
用した金、銀、銅、アルミ等の水銀を真空加熱、凝縮器
で回収する時、真空ポンプの排気体は水溶液の中を通過
させ、続いて金、銀、銅、アルミ等の水銀と反応あるい
は吸着する物質の充填層を通過させ、水銀を吸着、反応
する廃蛍光ランプの水銀回収方法。5. When the mercury such as gold, silver, copper, and aluminum used for the adsorption of the mercury, the glass, the electrode, and the mercury is vacuum-heated and collected by the condenser, the exhaust of the vacuum pump is carried out in the aqueous solution. A method of collecting mercury from a waste fluorescent lamp that adsorbs and reacts with mercury by passing through a packed layer of a substance that reacts or adsorbs with mercury such as gold, silver, copper, and aluminum.
Priority Applications (1)
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JP2000404107A JP2002180146A (en) | 2000-12-13 | 2000-12-13 | Method for recovering mercury from waste fluorescent lamp |
Applications Claiming Priority (1)
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JP2000404107A JP2002180146A (en) | 2000-12-13 | 2000-12-13 | Method for recovering mercury from waste fluorescent lamp |
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Cited By (7)
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WO2005005025A1 (en) * | 2003-07-10 | 2005-01-20 | Taiheiyo Cement Corporation | Device and method for processing combustion exhaust gas |
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US8282263B2 (en) | 2005-10-31 | 2012-10-09 | Taiheiyo Cement Corporation | Apparatus and method for adding wet ash to cement |
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2000
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2005005025A1 (en) * | 2003-07-10 | 2005-01-20 | Taiheiyo Cement Corporation | Device and method for processing combustion exhaust gas |
JPWO2005005025A1 (en) * | 2003-07-10 | 2007-09-20 | 太平洋セメント株式会社 | Combustion exhaust gas treatment device and treatment method |
US7799297B2 (en) | 2003-07-10 | 2010-09-21 | Taiheiyo Cement Corporation | Device and method for processing combustion exhaust gas |
JP4615443B2 (en) * | 2003-07-10 | 2011-01-19 | 太平洋セメント株式会社 | Combustion exhaust gas treatment apparatus and treatment method |
US7947229B2 (en) | 2005-08-26 | 2011-05-24 | Taiheiyo Cement Corporation | Apparatus and method for dissolution reaction |
US8282263B2 (en) | 2005-10-31 | 2012-10-09 | Taiheiyo Cement Corporation | Apparatus and method for adding wet ash to cement |
US8893892B2 (en) | 2005-12-07 | 2014-11-25 | Taiheiyo Cement Corporation | Apparatus and method for removing unburned carbon from fly ash |
US8607469B2 (en) | 2006-06-28 | 2013-12-17 | Taiheiyo Cement Corporation | Cement burning apparatus and method of drying high-water-content organic waste |
US7837963B2 (en) | 2006-10-24 | 2010-11-23 | Taiheiyo Cement Corporation | Method for removing lead from cement burning furnace |
US8439202B2 (en) | 2006-12-05 | 2013-05-14 | Taiheiyo Cement Corporation | Coal ash treatment method and apparatus |
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