JPH07328433A - Material for absorbing mercury in gas and its production - Google Patents

Material for absorbing mercury in gas and its production

Info

Publication number
JPH07328433A
JPH07328433A JP6155251A JP15525194A JPH07328433A JP H07328433 A JPH07328433 A JP H07328433A JP 6155251 A JP6155251 A JP 6155251A JP 15525194 A JP15525194 A JP 15525194A JP H07328433 A JPH07328433 A JP H07328433A
Authority
JP
Japan
Prior art keywords
added
mercury
gas
pbs
concentrate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP6155251A
Other languages
Japanese (ja)
Other versions
JP3426032B2 (en
Inventor
Toshihiro Nakamichi
俊博 仲道
Jun Ogata
潤 尾形
Kiyomi Yamaguchi
潔実 山口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dowa Holdings Co Ltd
Original Assignee
Dowa Mining Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dowa Mining Co Ltd filed Critical Dowa Mining Co Ltd
Priority to JP15525194A priority Critical patent/JP3426032B2/en
Publication of JPH07328433A publication Critical patent/JPH07328433A/en
Application granted granted Critical
Publication of JP3426032B2 publication Critical patent/JP3426032B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To provide a material for absorbing mercury in gas with absorption efficiency enhanced by using an inexpensive lead concentrate and capable of maintaining the high absorption efficiency for a long period. CONSTITUTION:A lead concentrate is dipped in water and agitated, then sulfuric acid is added to activate the surface, acetic acid is added and agitated, then lead oxide is added, and hydrogen sulfide is blown into the liq. with the temp. adjusted to deposit PbS on the surface of the concentrate. The PbS pulp is adhered to pumice with the grain size controlled to form a mercury absorbent, and a material for absorbing mercuty in gas maitaining high mercury absorption efficiency for a long period as shown in the figure is obtained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ガス中の水銀を除去す
るのに好適な吸収材およびその製造方法に関し、更に詳
しくは安価な鉛精鉱を用いて長期間安定な吸収材を製造
することを目的とする。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorbent material suitable for removing mercury in a gas and a method for producing the same, and more specifically, it produces an absorbent material which is stable for a long period of time using an inexpensive lead concentrate. The purpose is to

【0002】[0002]

【従来の技術】多孔質物質に活性な金属や化合物を付着
させてガス中の重金属、特に水銀を除去する研究は古く
から行われている。
2. Description of the Related Art Studies for removing heavy metals, particularly mercury, in a gas by adhering an active metal or compound to a porous material have been conducted for a long time.

【0003】一例として、特開昭48−13259号公
報(発明の名称:「水銀化合物および元素状水銀を含む
ガスの精製法」)においては、活性成分としてセレン、
硫化セレンまたは他のセレン化合物あるいはこれらの混
合物を含んでなる塊状の精製用物質中に水銀含有ガスを
吹きこんで通過させることを特徴とする気体状の水銀含
有ガスの精製法が開示されている。
As one example, in JP-A-48-13259 (the title of the invention: "Method for purifying gas containing mercury compound and elemental mercury"), selenium as an active ingredient,
Disclosed is a method for purifying a gaseous mercury-containing gas, characterized in that a mercury-containing gas is blown into and passed through a bulk purification substance containing selenium sulfide or another selenium compound or a mixture thereof. .

【0004】また、本出願人も先に特公昭54−847
5号(発明の名称;「酸性排ガス中の水銀の除去法」)
において、気体状またはミスト状の水銀を随伴する酸性
排ガスを非炭素質の無機多孔性物質担体上にZnS、C
dSおよびPbSからなる群より選ばれる少なくとも1
種の金属硫化物を担持させたものからなる吸収材の充て
ん層に導き、これを通過させることを特徴とする酸性排
ガス中の水銀除去法を開示した。
Further, the applicant of the present invention also previously issued Japanese Patent Publication No. 54-847.
No. 5 (Title of invention; "Method of removing mercury in acidic exhaust gas")
In the above, the acidic exhaust gas accompanied by gaseous or mist-like mercury is applied to ZnS, C
At least one selected from the group consisting of dS and PbS
Disclosed is a method for removing mercury in an acidic exhaust gas, which is characterized in that it is led to a packed layer of an absorbent composed of one carrying a metal sulfide of a kind and passed through.

【0005】これらの除去法に使用できる水銀吸収用材
料の一種として、本出願人は特公昭63−2654号公
報(発明の名称:「排ガス中の水銀吸収用材料」)にお
いて、閃亜鉛鉱、方鉛鉱、磁硫鉄鉱または黄銅鉱の少な
くとも一種の鉱酸処理済精鉱に該鉱物の主成分金属の酸
化物と酸を添加し、さらに硫化水素を添加して形成され
た澱物を多孔質担体に担持させてなる排ガス中の水銀吸
収材料を提供して、実操業に少なからず寄与してきた。
As one type of mercury absorbing material that can be used for these removal methods, the applicant of the present invention discloses in Japanese Patent Publication No. Sho 63-2654 (invention name: "mercury absorbing material in exhaust gas"), zinc blende, At least one mineral acid-treated concentrate of galena, pyrrhotite, or chalcopyrite is added with an oxide and an acid of a metal as a main component of the mineral, and hydrogen sulfide is further added to form a precipitate formed into a porous material. By providing a mercury absorbing material in exhaust gas which is supported on a carrier, it has contributed not a little to the actual operation.

【0006】[0006]

【発明が解決しようとする課題】しかしながら上記吸収
剤は、使用当初は高い吸収効率を示すものの、長期間ガ
スを通し続けると吸収効率が比較的短期間に減少するこ
とがその後の試験で判明した。
However, in the subsequent tests, it was found that the above-mentioned absorbent exhibits a high absorption efficiency at the beginning of use, but the absorption efficiency decreases in a relatively short period of time when gas is passed for a long time. .

【0007】上記吸収材は安価な精鉱を用いるものであ
ることから、この素材を活用して更に改良を加え長期的
に安定化された吸収材を開発することが望まれていた。
Since the above-mentioned absorbent material uses inexpensive concentrate, it has been desired to develop an absorbent material that is stabilized for a long period of time by further improving this material.

【0008】[0008]

【課題を解決するための手段】そこで、本発明者等はこ
れらの課題を解決するために鋭意研究した結果、鉛精鉱
を用いて有機酸中でこれら鉛精鉱の表面に化学合成した
PbSを均一に添着させ、得られたPbSパルプを多孔
質物質に担持させることによって、長期的に安定化され
た水銀吸収性材料を安価に製造できることを見い出し
た。
The inventors of the present invention have made extensive studies in order to solve these problems, and as a result, PbS chemically synthesized on the surface of these lead concentrates in an organic acid using lead concentrates. It has been found that a long-term stabilized mercury-absorbing material can be produced at low cost by uniformly impregnating the obtained PbS with the obtained PbS pulp supported on a porous substance.

【0009】すなわち本発明の一つは、鉛精鉱を投入攪
拌した水性液中に鉱酸を添加して精鉱表面を活性化し、
次いで有機酸を添加した後PbOを添加・溶解した液中
に硫化水素を吹き込み鉛精鉱表面にPbSを生成させ、
得られたパルプを多孔質担体に担持してなることを特徴
とするガス中の水銀吸収材料であり、他の発明は、鉛精
鉱を投入攪拌した水性液中に鉱酸を添加して精鉱表面を
活性化する第1工程、上記液中に有機酸を添加して攪拌
後、PbOを添加・溶解し硫化水素を吹き込むことによ
り、鉛精鉱表面にPbSを生成させてPbSパルプを得
る第2工程、上記パルプを多孔質物質に付着させガス吸
収材とする第3工程からなることを特徴とするガス中の
水銀吸収材料の製造方法に関する。
That is, one aspect of the present invention is to add a mineral acid to an aqueous liquid in which lead concentrate is added and stirred to activate the surface of the concentrate.
Next, after adding an organic acid, hydrogen sulfide is blown into the liquid in which PbO is added and dissolved to generate PbS on the surface of the lead concentrate,
Another aspect of the present invention is a mercury absorbing material in a gas, characterized in that the obtained pulp is supported on a porous carrier. First step of activating the ore surface, adding an organic acid to the above liquid and stirring, then adding / dissolving PbO and blowing hydrogen sulfide to produce PbS on the surface of the lead concentrate to obtain PbS pulp. The present invention relates to a method for producing a mercury absorbing material in a gas, which comprises a second step and a third step of adhering the pulp to a porous substance to form a gas absorbing material.

【0010】[0010]

【作用】本発明法において用いるPbSパルプは、安価
な鉛精鉱を出発原料とするが、この精鉱(微粒子)は、
種々の選鉱試薬により鉱物表面が覆われたり酸化したり
しているので、このままでは脱水銀用吸収材として使用
できないため、予め液中で鉱酸処理して選鉱試薬の除去
および酸化被膜の除去を行った鉱酸処理済精鉱を対象と
する。
The PbS pulp used in the method of the present invention uses inexpensive lead concentrate as a starting material, and this concentrate (fine particles) is
Since the mineral surface is covered or oxidized by various beneficiation reagents, it cannot be used as an absorbent for demercury removal as it is. The target is the mineral acid-treated concentrate.

【0011】第1工程において上記鉛精鉱を水性液中に
投入攪拌しながら、鉱酸として硫酸を添加して精鉱表面
を洗浄すると共に活性化し、次いで上澄液を除去して、
新たな水を供給する。
In the first step, while adding and stirring the lead concentrate in an aqueous liquid, sulfuric acid is added as a mineral acid to wash and activate the surface of the concentrate, and then the supernatant liquid is removed.
Supply new water.

【0012】第2工程においては、有機酸として酢酸を
入れて攪拌し、次いで酸化鉛(PbO)を添加し、同様
に攪拌する。これらの液中に、硫化水素をPbO100
gに対して約30ml/minの割合で吹き込み、鉛精鉱粒子
表面にPbSを化学的に合成し均一に添着させた。液中
のPb2+イオンがなくなるまで硫化水素の吹き込みを続
け、反応終了後パルプ水のpHが中性になるまでデカン
テーションにより水洗した後、PbSパルプを反応容器
の系外へ抜き出した。
In the second step, acetic acid is added as an organic acid and the mixture is stirred, then lead oxide (PbO) is added and the mixture is similarly stirred. In these liquids, hydrogen sulfide was added to PbO100.
It was blown at a rate of about 30 ml / min with respect to g, and PbS was chemically synthesized on the surface of the lead concentrate particles and uniformly attached. Hydrogen sulfide was continuously blown in until the Pb 2+ ions in the liquid disappeared, and after the reaction was completed, the pulp water was washed by decantation until the pH became neutral, and then the PbS pulp was taken out of the reaction vessel.

【0013】有機酸の存在下で酸化鉛は徐々に溶解しな
がら硫化水素とゆっくり反応して鉛精鉱粒子表面に化学
合成された均一なPbS層を形成する。他の酸では、P
bSは鉛精鉱粒子表面でも一部合成されるが、そのほと
んどはPbS粒子として生成し、鉛精鉱粒子表面に均一
にPbSを添着することができず、長期に安定して水銀
を吸収する材料にはならない。
In the presence of an organic acid, lead oxide slowly dissolves and slowly reacts with hydrogen sulfide to form a chemically synthesized uniform PbS layer on the surface of lead concentrate particles. For other acids, P
Although bS is partially synthesized on the surface of lead concentrate particles, most of it is produced as PbS particles, and PbS cannot be uniformly impregnated on the surface of lead concentrate particles, and mercury is stably absorbed for a long period of time. Not a material.

【0014】また、有機酸として本実施例では酢酸を用
いたが、これはコスト的に安価な素材であるから好まし
いだけで、蟻酸・シュウ酸・安息香酸等他の有機酸を使
用しても同様な効果が得られる。
In this embodiment, acetic acid was used as the organic acid, but this is preferable because it is a low cost material, and other organic acids such as formic acid, oxalic acid and benzoic acid may be used. Similar effects are obtained.

【0015】第3工程では、上記PbSパルプを多孔質
物質、例えば軽石に付着させる。例えばペレタイザー等
で軽石の表面に軽石1リットルにつき約250gのPb
Sを均一に付着させる。
In the third step, the PbS pulp is attached to a porous material such as pumice stone. For example, about 250g of Pb per liter of pumice on the surface of pumice with a pelletizer.
S is applied uniformly.

【0016】このようにして得られたガス中の水銀吸収
材は、従来例で示した特公昭63−2654号に示す吸
収材に比較すると、初期性能も高くかつ3倍以上初期性
能を持続することが判明し、長期的に安定な水銀吸収材
であることがわかった。
The mercury absorbent in the gas thus obtained has a higher initial performance than the absorbent disclosed in Japanese Patent Publication No. 63-2654, which is shown in the conventional example, and the initial performance is tripled or more. It was found that the mercury absorber is stable for a long period of time.

【0017】[0017]

【実施例1】容量3リットルの容器にA鉱山製の鉛精鉱
を1.5kg入れ水を加えて全体が2リットルになるよう
に調整した。攪拌しながら液温度を約45℃前後にコン
トロールした。次いで、鉱酸として硫酸を少量ずつ合計
10ml添加し、1.5時間攪拌して鉛精鉱表面を活性化
させ、その後約7時間沈降させた。
Example 1 1.5 kg of lead concentrate manufactured by A mine was put in a container having a capacity of 3 liters, and water was added to the container to adjust the total volume to 2 liters. The liquid temperature was controlled to about 45 ° C while stirring. Then, 10 ml of sulfuric acid was added little by little as a mineral acid, and the mixture was stirred for 1.5 hours to activate the surface of the lead concentrate, followed by sedimentation for about 7 hours.

【0018】次いで上澄液を除去した後、再び水を加え
て全体が2リットルになるように調整した(第1工
程)。
Then, after removing the supernatant, water was added again to adjust the total volume to 2 liters (first step).

【0019】上記第1工程のパルプ液中に有機酸として
の酢酸を10ml添加して攪拌後、酸化鉛(PbO)を1
00g添加し、液温度を約45℃前後にコントロールし
た。その液中に、硫化水素(H2 S)をPbO100g
に対して30ml/min の割合で約7時間吹き込み、液中
のPb2+イオンがなくなり反応が終了したことを確認し
た後、硫化水素の吹き込みを停止した。次いでPbSを
沈降させ上澄液を除き、水を加えて攪拌する作業を数度
繰り返し(デカンテーション)、液のpHが6以上の中
性域になるまで水洗した。その後容器底部に沈降したP
bSパルプを別容器に移した(第2工程)。
10 ml of acetic acid as an organic acid was added to the pulp liquid of the first step and stirred, and then lead oxide (PbO) was added to 1 ml.
00 g was added, and the liquid temperature was controlled to about 45 ° C. Hydrogen sulfide (H 2 S) was added to the solution in an amount of 100 g of PbO.
Bubbling was carried out at a rate of 30 ml / min for about 7 hours, and after confirming that the Pb 2+ ions in the liquid had disappeared and the reaction had ended, the blowing of hydrogen sulfide was stopped. Next, PbS was allowed to settle, the supernatant was removed, and the operation of adding water and stirring was repeated several times (decantation), and the solution was washed with water until the pH of the solution became 6 or more in the neutral range. After that, P that settled at the bottom of the container
The bS pulp was transferred to another container (second step).

【0020】次いで該PbSパルプを、5〜15mmに粒
度を調整した軽石1リットルに対して約250gの割合
で、ペレタイザーを用いて付着させ所望のガス中の水銀
吸収材を得た。
Next, the PbS pulp was attached using a pelletizer at a ratio of about 250 g to 1 liter of pumice having a particle size adjusted to 5 to 15 mm to obtain a mercury absorbent in a desired gas.

【0021】上記工程によって得られた吸収材と、比較
用吸収材としての特公昭63−2654号公報記載の硫
化亜鉛精鉱からの殿物を上記と同じ割合で軽石に付着さ
せた吸収材とを用い、各々200mlのカラムに充填し3
リットル/分の割合で水銀を含んだガスを通過させた。
入り口のガス中の水銀濃度を変えることができるように
工夫し、それぞれの入り口・出口のガスを同時に吸引、
液吸収させその吸収液中の水銀を分析することにより、
それぞれの条件での吸収材の水銀吸収性能を調べた。そ
の結果を表1に示した。
The absorbent obtained by the above process, and the absorbent obtained by depositing a substance from the zinc sulfide concentrate described in Japanese Patent Publication No. 63-2654 as a comparative absorbent on pumice in the same proportion as above. Using a column, fill each of the 200 ml columns with 3
A gas containing mercury was passed through at a rate of 1 / min.
It was devised so that the mercury concentration in the gas at the entrance could be changed, and the gas at each entrance and exit was sucked in at the same time.
By absorbing the liquid and analyzing the mercury in the absorbing liquid,
The mercury absorption performance of the absorber under each condition was investigated. The results are shown in Table 1.

【0022】[0022]

【表1】 [Table 1]

【0023】以上のように、初期の水銀吸収性能につい
ては入り口ガス中の水銀濃度が変化しても安定して99
%以上の除去率があることが判明した。
As described above, the initial mercury absorption performance is stable at 99% even if the mercury concentration in the inlet gas changes.
It was found that there was a removal rate of at least%.

【0024】[0024]

【実施例2】実施例1と同様に製造した本発明による吸
収材と比較吸収材の水銀吸収性能の長期安定性を調べ
た。実施例1と同様の通ガス条件にて入り口水銀濃度が
一定になるようにして、カラム内に連続的にガスを通
し、出口ガスの水銀濃度を一定時間毎に吸引・液吸収
し、その吸収液の水銀濃度を分析し除去率を計算した。
その時系列のグラフを図1に示した。
Example 2 The long-term stability of the mercury absorption performance of the absorbent according to the present invention and the comparative absorbent manufactured in the same manner as in Example 1 was examined. Under the same gas passing conditions as in Example 1, the concentration of mercury at the inlet was made constant, gas was continuously passed through the column, and the mercury concentration at the outlet gas was sucked and absorbed at regular intervals, and the absorption was performed. The mercury concentration of the liquid was analyzed and the removal rate was calculated.
The time-series graph is shown in FIG.

【0025】[0025]

【発明の効果】以上詳しく説明したように、本発明の製
造法により得られた吸収材は比較吸収材と比べて初期性
能も高く、かつその高い水銀吸収効率を長期間保持する
ことが判明した。
As described in detail above, it has been found that the absorbent obtained by the production method of the present invention has higher initial performance than the comparative absorbent and retains its high mercury absorption efficiency for a long period of time. .

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の吸収材と比較吸収材とをそれぞれ用い
て水銀吸収効率の持続性について調べた結果を示すグラ
フである。
FIG. 1 is a graph showing the results of examining the durability of mercury absorption efficiency using the absorbent material of the present invention and the comparative absorbent material, respectively.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 鉛精鉱を投入攪拌した水性液中に鉱酸を
添加して精鉱表面を活性化させ、次いで有機酸を添加し
た後PbOを添加・溶解した液中に硫化水素を吹き込み
鉛精鉱粒子の表面にPbSを生成させ、得られたパルプ
を多孔質担体に担持してなることを特徴とするガス中の
水銀吸収材料。
1. A mineral acid is added to an aqueous liquid in which lead concentrate is added and stirred to activate the surface of the concentrate, and then an organic acid is added and then hydrogen sulfide is blown into the liquid in which PbO is added and dissolved. A mercury absorbing material in a gas, characterized in that PbS is produced on the surface of lead concentrate particles, and the obtained pulp is supported on a porous carrier.
【請求項2】 鉛精鉱を投入攪拌した水性液中に鉱酸を
添加して精鉱表面を活性化する第1工程、 上記液中に有機酸を添加して攪拌後、PbOを添加・溶
解し硫化水素を吹き込み、鉛精鉱表面にPbSを生成さ
せてPbSパルプを得る第2工程、 上記PbSパルプを多孔質物質に担持させてガス吸収材
とする第3工程からなることを特徴とするガス中の水銀
吸収材料の製造方法。
2. A first step of activating the surface of a concentrate by adding a mineral acid to an aqueous liquid in which lead concentrate is added and stirred, wherein an organic acid is added to the liquid and stirred, and then PbO is added. It is characterized by comprising a second step of dissolving and blowing hydrogen sulfide to produce PbS on the surface of the lead concentrate to obtain PbS pulp, and a third step of supporting the PbS pulp on a porous material to form a gas absorbent. Method for producing mercury absorbing material in gas.
JP15525194A 1994-06-14 1994-06-14 Method for producing mercury in gas Expired - Fee Related JP3426032B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15525194A JP3426032B2 (en) 1994-06-14 1994-06-14 Method for producing mercury in gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15525194A JP3426032B2 (en) 1994-06-14 1994-06-14 Method for producing mercury in gas

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2003091005A Division JP2003326158A (en) 2003-03-28 2003-03-28 Material for absorbing mercury in gas

Publications (2)

Publication Number Publication Date
JPH07328433A true JPH07328433A (en) 1995-12-19
JP3426032B2 JP3426032B2 (en) 2003-07-14

Family

ID=15601844

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KR100439961B1 (en) * 2000-12-06 2004-07-12 한국원자력연구소 Novel mercury absorbent and the processing method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100439961B1 (en) * 2000-12-06 2004-07-12 한국원자력연구소 Novel mercury absorbent and the processing method thereof

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