JPS5879591A - Method of preparing sulfide in aqueous system - Google Patents

Method of preparing sulfide in aqueous system

Info

Publication number
JPS5879591A
JPS5879591A JP57174087A JP17408782A JPS5879591A JP S5879591 A JPS5879591 A JP S5879591A JP 57174087 A JP57174087 A JP 57174087A JP 17408782 A JP17408782 A JP 17408782A JP S5879591 A JPS5879591 A JP S5879591A
Authority
JP
Japan
Prior art keywords
compound
hydrogen peroxide
rate
sodium
molded form
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
JP57174087A
Other languages
Japanese (ja)
Other versions
JPS603871B2 (en
Inventor
ウイリアム・エイチ・キベル・ジユニア
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.)
FMC Corp
Original Assignee
FMC Corp
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 FMC Corp filed Critical FMC Corp
Publication of JPS5879591A publication Critical patent/JPS5879591A/en
Publication of JPS603871B2 publication Critical patent/JPS603871B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/722Oxidation by peroxides

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Paper (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は所定の溶解速度をもつコンパクトな形態の過酸
素を用いる水溶液中の硫化物および他の還元剤調節の簡
便法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a convenient method for controlling sulfides and other reducing agents in aqueous solutions using a compact form of peroxygen with a defined dissolution rate.

過酸化水素は水溶液中の硫化水素調節に有用であると知
られている。p)(7又はそれ以下で使えば過酸化水素
は硫化水素を硫酸塩よりも元素いおうに経済的に酸化す
る。汚水中の硫化物を元素いお5に酸化して過酸化水素
からの臭気を軽減するこの過酸化水素の用途は米国特許
第470翫098号および3,550,067号に発表
されている。しかし極少量の排水又は一時的廃水のいづ
れかにおける硫化物を処理する液温量系の経費は甚しく
かかる。また不溶性元素いおうを含む排水廃棄は好まし
くないので処理排水を廃棄する前溶液からいおうをr過
又は凝集沈澱させる必要が  ゛ある。
Hydrogen peroxide is known to be useful for controlling hydrogen sulfide in aqueous solutions. p) (When used at 7 or less, hydrogen peroxide oxidizes hydrogen sulfide to elemental sulfur more economically than sulfate. It oxidizes sulfide in wastewater to elemental sulfur and eliminates odors from hydrogen peroxide. Applications of this hydrogen peroxide to reduce sulfides have been published in U.S. Pat. Nos. 470-098 and 3,550,067. The cost of the system is considerable.Also, since it is undesirable to dispose of wastewater containing insoluble elemental sulfur, it is necessary to filter or coagulate the sulfur from the solution before disposing of the treated wastewater.

過酸化水素は酸化剤および還元剤としてよく知られてい
る。それはアルカリ性溶液中では酸化剤として最も有効
に作用する。故に溶液中の化学的酸素賛求量を減少する
に過酸化水素又は過酸化水素の付加化合物を使う場合p
Hを7以上に上げるとよい。過酸化水素によって硫化物
を完全に硫酸塩に酸化する場合は溶液pHを少なくも8
とする必要がある。多くの排水はpH7又はそれ以下で
あるので、pHを適当範囲に連続上昇しかつ溶液中に過
酸化水素を保つには追加設備や薬品が必要でこの処理経
費は増加する。
Hydrogen peroxide is well known as an oxidizing and reducing agent. It acts most effectively as an oxidizing agent in alkaline solutions. Therefore, when using hydrogen peroxide or an adduct compound of hydrogen peroxide to reduce the chemical oxygen demand in solution, p
It is better to raise H to 7 or higher. If the sulfide is completely oxidized to sulfate by hydrogen peroxide, the solution pH should be at least 8.
It is necessary to do so. Since many wastewaters have a pH of 7 or less, additional equipment and chemicals are required to continuously raise the pH to a reasonable range and keep the hydrogen peroxide in solution, increasing the cost of this process.

過酸化炭酸ナトリウム又は過はう酸ナトリウムの様な固
体アルカリ性過酸化水素付加化合物を添加すれば溶液の
pH@節と硫化物を硫酸塩に酸化する水素過酸素とを同
時に与える。しかし系に粉末又は結晶を供給することは
困難である。%に小規模の場合はむつかしい。更にこの
化合物によってできた有効アルカリ性度と活性酸素は溶
液のpH調節と硫化物の硫酸塩への酸化の双方に対し最
適割合にはならないだろう。
Addition of a solid alkaline hydrogen peroxide addition compound, such as sodium peroxide carbonate or sodium perphosphate, simultaneously provides pH adjustment of the solution and hydrogen peroxygen that oxidizes sulfides to sulfates. However, it is difficult to feed the system with powder or crystals. It is difficult when the scale is small. Furthermore, the available alkalinity and active oxygen produced by this compound will not be in optimal proportions for both solution pH adjustment and oxidation of sulfide to sulfate.

本発明は固体過酸累を、必要ならば添加剤と共K、適当
な溶解速度をもつ固体型に圧縮することによって上記の
欠点を解決する。この様に固体形態を溶解すれば同時K
pHを調節しかつ一定時間にわた9酸化剤を生ずる予め
測定された薬品となる。
The present invention overcomes the above-mentioned drawbacks by compressing the solid peracid concentrate, optionally with additives, into a solid form with suitable dissolution rates. If a solid form is dissolved in this way, the simultaneous K
It becomes a pre-measured chemical that adjusts the pH and produces oxidizer 9 over a period of time.

本発明において過酸化炭酸ナトリウム又は過は511ナ
トリウムの様な過酸化水素の固体付加化合物は時間基準
で溶液に必要アルカリ性度と活性酸素を与える形態に物
理的に圧縮される。これは溶液中の硫化物を硫酸塩に絶
えず酸化する薬品を供給する秤量設備使用の必要はない
。過酸化炭酸ナトリウム又は過はう酸ナトリウムのいづ
れも単独で又は添加剤と共に溶解速度を調節しかつ望む
薬品均衡を与える様に圧縮成型できる。
In the present invention, a solid addition compound of hydrogen peroxide, such as sodium carbonate peroxide or sodium peroxide, is physically compressed into a form that provides the necessary alkalinity and active oxygen to the solution on a time basis. This eliminates the need for the use of weighing equipment to supply chemicals that constantly oxidize the sulfide in solution to sulfate. Either sodium peroxide carbonate or sodium perphosphate can be compression molded alone or with additives to control the rate of dissolution and provide the desired chemical balance.

圧縮成型品の大きさと形は更に溶解速度を調節するため
変更できる。錠剤は小規模試験に特に便利である。しか
しより均一な溶解速度のためには同心孔をもつ円筒形が
溶解する際全表面形が一定のままでいるので使用できる
。この用途のため“錠剤゛とは便利な形態も包含する*
味である。
The size and shape of the compression molded article can be varied to further control the rate of dissolution. Tablets are particularly convenient for small-scale trials. However, for a more uniform rate of dissolution, a cylindrical shape with concentric holes can be used since the overall surface shape remains constant during dissolution. For this purpose, the term “tablet” also includes any convenient form*
It's the taste.

製錠又は成型は添加剤又は賦形剤を使用してもしなくて
も普通の方法と設備で行なわれる。しかし調合の安全性
と適合性が検討されることが重要である。添加剤は貯蔵
又は性能に関して多様の効果を与える。例えば非常に遅
溶性添加剤は錠剤製品の溶解速度減少のため使用できる
。また不活性添加剤は活性酸素部分の僅少量が必要な場
合それを稀釈するに使用できる。アルカリ性添加剤は特
に酸性排水のpHを上昇するに使用でき、また着色剤又
は香料は美的又は個人的理由から加えられる。貯蔵安定
性又はプレスからのより容易な廃棄のための他の添加剤
使用はこの技術分野の知Rある者には明らかであろう。
Tablet making or molding is carried out using conventional methods and equipment, with or without the use of additives or excipients. However, it is important that the safety and suitability of the formulation be considered. Additives provide a variety of effects on storage or performance. For example, very slowly dissolving additives can be used to reduce the rate of dissolution of tablet products. Inert additives can also be used to dilute active oxygen moieties when small amounts are required. Alkaline additives may be used to raise the pH of particularly acidic wastewater, and colorants or fragrances may be added for aesthetic or personal reasons. The use of other additives for storage stability or easier disposal from the press will be apparent to those skilled in the art.

実用のため添加剤は安価であり酸化されないものである
必要がある。過酸化炭酸ナトIJウムの溶解速度を減少
するに使われる代表的2添加剤の効果データは実施例に
示されている。
For practical use, additives need to be inexpensive and non-oxidizable. Efficacy data for two representative additives used to reduce the dissolution rate of sodium peroxide carbonate is shown in the Examples.

直径約29 w、厚さ15mの錠剤1個を大気温の水9
5〇−入れた1tビーカーの水面すぐ下につけた網籠中
において溶解速度を測定した。渦流をおこす速度より僅
かおそい速度で撹拌棒をビーカー底で回転した。溶解時
間な観察記録した。過酸化水素濃度は硫酸第2セレン滴
定によって測定した。
One tablet with a diameter of approximately 29 W and a thickness of 15 m is poured into 9 liters of water at ambient temperature.
The dissolution rate was measured in a mesh basket placed just below the water surface of a 1 t beaker containing 50 liters of water. A stir bar was rotated at the bottom of the beaker at a speed slightly slower than that to create the vortex. The dissolution time was observed and recorded. Hydrogen peroxide concentration was measured by selenium sulfate titration.

与えられた排水の硫化物濃度と流量はpH調節用アルカ
リと共に活性酸素の放出される速度および錠剤交換の間
の望まれる操作時間と匹適する必要がある。
The sulfide concentration and flow rate of a given wastewater must be commensurate with the rate at which active oxygen is released along with the pH-adjusting alkali and the desired operating time between tablet changes.

過酸化炭酸ナトリウム錠剤を排水に入れる機械的装置は
多数ある。重力−流動系の非常に簡単な1方法は錠剤を
満たした金網筒の一部を液流に浸漬するのである。フォ
ースメインズの様な圧力系においては錠剤補給は弁付バ
イパスを付けて行なわせる。バイパスを使うことによっ
てまた錠剤補給中も処理は中断しない。操作中錠剤露出
と錠剤周囲の排水流速の組合せによって薬品供給は調節
できる。
There are many mechanical devices that introduce sodium peroxide and carbonate tablets into wastewater. One very simple method of gravity-flow system is to immerse a portion of a wire mesh cylinder filled with tablets in a liquid stream. In pressure systems such as Force Mains, tablet feeding is performed using a bypass with a valve. By using bypass, the process is also not interrupted during tablet replenishment. During operation, drug delivery can be controlled by a combination of tablet exposure and drainage flow rate around the tablet.

操作初期において望む硫化物調節をする助変数を調整し
使用錠剤大きさに基いて装入物のライフサイクルが決定
される。望むサイクルの長短によって装入錠剤大きさは
必要な丈は増減される。
The life cycle of the charge is determined based on the tablet size used by adjusting parameters to provide the desired sulfide control early in the operation. Depending on the length of the desired cycle, the required length of the loaded tablet can be increased or decreased.

実施例1 直径29闘のダイを使って圧縮圧力95MPaで過酸化
炭酸ナトリウム錠剤を生成した。錠剤は過酸化炭酸ナト
リウムのみ15F又はそれと10%115%又は20チ
のカルボキシメチルセルロース又はメチルセルロースを
含んでいた。錠剤の溶解時間(単位、分)は大体次式:
%式%(48 (但しAは調合中のカルボキシメチルセルロース又はメ
チルセルロースいづれかのパーセントである)で表わさ
れることがわかった。
Example 1 Sodium peroxide carbonate tablets were produced using a 29 mm diameter die at a compression pressure of 95 MPa. The tablets contained sodium peroxide carbonate only 15F or it with 10% 115% or 20% carboxymethylcellulose or methylcellulose. The dissolution time of a tablet (in minutes) is approximately calculated by the following formula:
It was found that it is expressed in the % formula % (48 (where A is the percentage of either carboxymethyl cellulose or methyl cellulose in the formulation).

実施例2 過はう酸ナトリウム4水化物を単独で、またカルボキシ
メチルセルロース(CMC)、メチルセルロース(MC
)、炭酸ナトリウム(ソーダ灰)、および塩化ナトリウ
ムと調合して製錠した。錠剤強度はCMC又はMCの5
−20%添加で改良されまたソーダ灰又は塩化ナトリウ
ムの添加で減少するとわかった。CMC又はMCの増加
とともに溶解速度は減少した。CMCを10重量−以上
添加した場合溶解は極めておそい。MCはCMC同様よ
い結合剤であるが、溶解の稍速し錠剤ができる。
Example 2 Sodium perphosphate tetrahydrate alone, carboxymethylcellulose (CMC), methylcellulose (MC
), sodium carbonate (soda ash), and sodium chloride to make tablets. Tablet strength is CMC or MC 5
It was found that the addition of -20% improved this and the addition of soda ash or sodium chloride reduced it. The dissolution rate decreased with increasing CMC or MC. When 10 weight or more of CMC is added, dissolution is extremely slow. MC is a good binder like CMC, but dissolves more quickly and forms tablets.

線通はう酸ナトリウムはその濃度を[101%から4.
0−に増すにつれ水道水pHを&7から1α2に上昇し
た。
The concentration of sodium borate in the wire ranges from 101% to 4.
As the pH of the tap water increased to 0-, the pH of the tap water increased from &7 to 1α2.

101%からn、slで最も変動が大きかった。同様の
濃度において粗汚水のpHは&3から11.1に増加し
た。
The largest variation was from 101% to n and sl. At similar concentrations, the pH of crude sewage increased from &3 to 11.1.

過はう酸塩錠剤は水道水中の7−8 ppm硫化物溶液
と反応し15分以内で硫化物を硫酸塩に酸化した。この
時間は初め約7 ppmの硫化物を含む汚水試料におい
て認められた。
The perborate tablets reacted with a 7-8 ppm sulfide solution in tap water and oxidized the sulfide to sulfate within 15 minutes. This time was initially observed in wastewater samples containing about 7 ppm sulfide.

表  1 。Table 1.

0           3      !11’0 
            40     4815  
         65     7020     
     135    140辛 カルボキシメチル
セルロース(CMC)又はメチルセルロース(MC)と
混合した15F炭酸ナトリウム錠剤。
0 3! 11'0
40 4815
65 7020
135 140 Spicy 15F sodium carbonate tablets mixed with carboxymethylcellulose (CMC) or methylcellulose (MC).

Claims (1)

【特許請求の範囲】 1、時間を基準として溶液にアルカリ物質と過酸化水素
の双方を加えて溶液をアルカリ性過酸化水素で連続酸化
し水性硫化物イオンを硫酸塩に転化する方法において、
固体アルカリ性過酸化水素付加化合物を成型形態に圧縮
することにより上記化合物の溶解速度を変更してアルカ
リ物質の添加速度と過酸化水素の添加速度を調整するこ
とを特徴とする改良法。 Z 過酸化水素付加化合物が過酸化炭酸ナトリウム又は
過はう酸ナトリウム4水化物より成る群から選ばれた化
合物である%杵請求の範囲第1項に記載の方法。 五 改良法が更に上記成型形態中に速度変更用化合物を
含む特許請求の範囲第1項又は2項に記載の方法。 4、上記成型形態が速度変更用化合物として25−迄の
カルボキシメチルセルロースを含む特許請求の範囲第3
項に記載の方法。 5 上記成型形態が速度変更用化合物として25−迄の
メチルセルロースを含む特許請求の範囲第5項に記載の
方法。 直 上記成型形態が速度変更用化合物として25%まで
の炭酸す) IJウムを含む特許請求の範囲第3項に記
載の方法。 2 上記成型形態が速度変更用化合物として25%まで
の塩化ナトリウムを含む特許請求の範囲第3項に記載の
方法。 a 時間を基準として溶液にアルカリ物質と過酸化水素
双方を加え溶液をアルカリ性過酸化水素で連続酸化して
水性硫化物イオンを硫酸塩に転化する方法において、(
a)過酸化炭酸ナトリウムおよび過はう酸ナトリウム4
水化物より成る群から選ばれた化合物、(b)追加塩基
および(c)速度変更用化合物の混合物を成型形態に圧
縮して上記混合物の溶解速度を変更することによりアル
カリ物質と過酸化水素双方の添加速度およびアルカリ対
過酸化水素比率を調整することを特徴とする改良法。 2 塩基(b)が25チ迄の炭酸ナトリウムよ抄成る特
許請求の範囲第8項に記載の方法。 1α速度変更化合物(C)がカルボキシメチルセルロー
スとメチルセルロースより成る群から選ばれた化合物で
ある特許請求の範囲第8項および9項に記載の方法。
[Claims] 1. A method in which both an alkaline substance and hydrogen peroxide are added to a solution on a time basis and the solution is continuously oxidized with alkaline hydrogen peroxide to convert aqueous sulfide ions to sulfate,
An improved method characterized in that the solid alkaline hydrogen peroxide addition compound is compressed into a molded form to alter the rate of dissolution of said compound to adjust the rate of addition of the alkaline material and the rate of addition of hydrogen peroxide. 2. The method according to claim 1, wherein the hydrogen peroxide addition compound is a compound selected from the group consisting of sodium peroxide carbonate or sodium perphosphate tetrahydrate. 5. The method according to claim 1 or 2, wherein the improved method further comprises a speed-altering compound in the molded form. 4. Claim 3, wherein the molded form contains up to 25-carboxymethyl cellulose as a speed-changing compound.
The method described in section. 5. A method according to claim 5, wherein the molded form contains up to 25-methylcellulose as the rate-altering compound. 4. The method of claim 3, wherein the molded form contains up to 25% IJ carbonate as a speed modifying compound. 2. A method according to claim 3, wherein the molded form contains up to 25% sodium chloride as a speed modifying compound. a. In a method in which both an alkaline substance and hydrogen peroxide are added to a solution on a time basis and the solution is continuously oxidized with alkaline hydrogen peroxide to convert aqueous sulfide ions to sulfate, (
a) Sodium peroxide carbonate and sodium perphosphate 4
a compound selected from the group consisting of hydrates, (b) an additional base, and (c) a rate-modifying compound, by compressing the mixture into a molded form to modify the rate of dissolution of said mixture. An improved method characterized by adjusting the addition rate and the alkali to hydrogen peroxide ratio. 2. The method of claim 8, wherein base (b) comprises up to 25% sodium carbonate. 10. The method of claims 8 and 9, wherein the 1α rate-altering compound (C) is a compound selected from the group consisting of carboxymethylcellulose and methylcellulose.
JP57174087A 1981-10-05 1982-10-05 Method for adjusting sulfide in aqueous systems Expired JPS603871B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US308625 1981-10-05
US06/308,625 UST102905I4 (en) 1981-10-05 1981-10-05 Control of sulfides in aqueous systems

Publications (2)

Publication Number Publication Date
JPS5879591A true JPS5879591A (en) 1983-05-13
JPS603871B2 JPS603871B2 (en) 1985-01-31

Family

ID=23194725

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57174087A Expired JPS603871B2 (en) 1981-10-05 1982-10-05 Method for adjusting sulfide in aqueous systems

Country Status (3)

Country Link
US (1) UST102905I4 (en)
JP (1) JPS603871B2 (en)
ES (1) ES8308804A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015120128A (en) * 2013-12-25 2015-07-02 株式会社Tio技研 Waste water purification material

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4110055A1 (en) * 1991-03-27 1992-10-01 Degussa METHOD FOR DETOXIFYING CYANIDIC AQUEOUS SOLUTIONS
US7291276B1 (en) * 2004-06-21 2007-11-06 Winston Company, Inc. Controlled production and release of oxygen activated biocide into holding tanks for RV's, boats and the like

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015120128A (en) * 2013-12-25 2015-07-02 株式会社Tio技研 Waste water purification material

Also Published As

Publication number Publication date
ES516182A0 (en) 1983-10-01
JPS603871B2 (en) 1985-01-31
UST102905I4 (en) 1983-04-05
ES8308804A1 (en) 1983-10-01

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