[go: up one dir, main page]

JPS634847A - Adsorbent for ammonia - Google Patents

Adsorbent for ammonia

Info

Publication number
JPS634847A
JPS634847A JP61147809A JP14780986A JPS634847A JP S634847 A JPS634847 A JP S634847A JP 61147809 A JP61147809 A JP 61147809A JP 14780986 A JP14780986 A JP 14780986A JP S634847 A JPS634847 A JP S634847A
Authority
JP
Japan
Prior art keywords
ammonia
carboxyl group
copper salt
adsorbent
polymer
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
Application number
JP61147809A
Other languages
Japanese (ja)
Inventor
Tomosaku Imoto
井本 友三久
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.)
Nok Corp
Original Assignee
Nok 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 Nok Corp filed Critical Nok Corp
Priority to JP61147809A priority Critical patent/JPS634847A/en
Publication of JPS634847A publication Critical patent/JPS634847A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To obtain the titled powdery adsorbent capable of being repeatedly used by using the copper salt-chelate compd. of a polymer contg. carboxyl group as a component. CONSTITUTION:A polymer contg. carboxyl group is dispersed and dissolved in a copper salt aq. soln. having about 0.01-0.1 molar concn. 0.1N aq. ammonia is added thereto and pH is regulated to 10 and the mixture is allowed to gel and the copper salt-chelate compd. of the polymer contg. carboxyl group is formed. Then after filtering this chelate compd. and sufficiently washing it by hydrochloric acid having 4.5pH, it is dried to obtain a powdery adsorbent for ammonia. In this case, copper salt is used in about 0.1-1mol ratio for carboxyl group incorporated in the polymer. Further polyacrylic acid is preferable as the polymer contg. carboxyl group. In the obtained adsorbent, 3mol of ammonia can be adsorbed for one equivalent of carboxyl group and also adsorbed ammonia can be easily separated i.e. by hydrochloric acid or the like not less than 4.5pH, therefore this adsorbent can be repeatedly used for adsorption.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、アンモニア吸着材に関する。更に詳しくは、
カルボキシル基含有重合体系のアンモニア吸着材に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an ammonia adsorbent. For more details,
This invention relates to an ammonia adsorbent based on a carboxyl group-containing polymer.

〔従来の技術〕[Conventional technology]

アンモニアを除去するための最も一般的な方法は、それ
を水に吸収させてアンモニア水とする方法あるいは酸水
溶液に吸収させてアンモニア塩とする方法などであり、
この他に硫酸第1鉄水溶液と反応させ硫酸アンモニウム
とする方法なども知られている。しかしながら、これら
の方法は、いずれも不可逆性であって、−旦飽和状態に
達するとそれ以上はアンモニアが吸収されなくなる。
The most common methods for removing ammonia include absorbing it in water to form aqueous ammonia or absorbing it in an aqueous acid solution to form ammonia salt.
In addition, a method of reacting with an aqueous ferrous sulfate solution to form ammonium sulfate is also known. However, all of these methods are irreversible; once saturation is reached, no more ammonia is absorbed.

また、固体状のものとしてはポリカルボン酸タイプのも
のが考えられるが、この場合にもそこに含有されるカル
ボキシルjjJ1当量に対し1モルのアンモニアが吸収
されるだけであるので、吸着能力は小さいといえる。
In addition, polycarboxylic acid type substances can be considered as solid substances, but in this case as well, only 1 mole of ammonia is absorbed per 1 equivalent of carboxyl jjJ contained therein, so the adsorption capacity is small. It can be said.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

そこで、本発明者らは、アンモニアの吸着能力の大きい
ものを求めて検討するに際し、銅塩キレート化合物が銅
塩1モルに対し最大6モルのアンモニアが配位し得るこ
とに着目し、銅塩キレート化合物をカルボキシル基含有
重合体に形成させることにより、かかる課題の解決を図
った。
Therefore, when searching for and investigating a compound with a large ammonia adsorption capacity, the present inventors focused on the fact that a copper salt chelate compound can coordinate up to 6 moles of ammonia per 1 mole of copper salt. The inventors attempted to solve this problem by forming a chelate compound into a carboxyl group-containing polymer.

〔問題点を解決するための手段〕[Means for solving problems]

従って1本発明はアンモニア吸着材に係り、このアンモ
ニア吸着材は、カルボキシル基含有重合体の銅塩キレー
ト化物よりなる。
Accordingly, the present invention relates to an ammonia adsorbent, which is made of a copper salt chelate of a carboxyl group-containing polymer.

銅塩キレート化物を形成させるカルボキシル基含有重合
体としては、カルボキシル基含量の最も多いポリアクリ
ル酸が好んで用いられ、この他エチレンーアクリル酸共
重合体、エチレン−メタアクリル酸共重合体なども用い
られる。
As the carboxyl group-containing polymer that forms the copper salt chelate, polyacrylic acid, which has the highest carboxyl group content, is preferably used, and ethylene-acrylic acid copolymers, ethylene-methacrylic acid copolymers, etc. used.

キレート化物を形成させる銅塩としては、例えば硝酸銅
、塩化銅、過塩素酸銅などの第1銅塩が用いられる。こ
れらの銅塩は、重合体中のカルボキシル基に対して約0
.1〜1のモル比で一般に用いられる。
As the copper salt for forming the chelate, for example, cuprous salts such as copper nitrate, copper chloride, and copper perchlorate are used. These copper salts have approximately 0
.. Generally used in a molar ratio of 1-1.

キレート化反応物は、約0.01〜0.1モル濃度の銅
塩水溶液中にカルボキシル基含有重合体を分散、溶解さ
せ、これに0.INアンモニア水を添加し、pHを10
.0に調整してゲル化させることにより取得される。ゲ
ル化物として得られたカルボキシル基含有重合体の銅塩
キレート化物は、日別後p)14.5の塩酸で十分に洗
浄し、乾燥させる。。
The chelation reaction product is prepared by dispersing and dissolving a carboxyl group-containing polymer in an aqueous copper salt solution having a concentration of about 0.01 to 0.1 molar, and dissolving the carboxyl group-containing polymer therein. Add IN ammonia water and adjust pH to 10
.. It is obtained by adjusting it to 0 and gelling it. The copper salt chelate of the carboxyl group-containing polymer obtained as a gel is thoroughly washed with hydrochloric acid (p) 14.5 after being separated for a day and dried. .

〔発明の効果〕 本発明に係るアンモニア吸着材は、カルボキシル基含有
重合体を銅塩キレート化することにより、カルボキシル
基1当量に対して3モルのアンモニアを吸着させること
ができ、しかも吸着させたアンモニアは例えばpH4,
5以上の塩酸などで容易に脱離させることができるので
、それをアンモニア吸着用にくり返して使用することが
できるという効果を奏する。具体的には、粉末状のこの
アンモニア吸着材を、悪臭空気中などのアンモニア成分
の優先的な吸着、除去に使用することができる。
[Effects of the Invention] The ammonia adsorbent according to the present invention can adsorb 3 moles of ammonia per equivalent of carboxyl group by chelating a carboxyl group-containing polymer with a copper salt. For example, ammonia has a pH of 4,
Since it can be easily desorbed using 5 or more hydrochloric acid, it can be used repeatedly for ammonia adsorption. Specifically, this powdered ammonia adsorbent can be used to preferentially adsorb and remove ammonia components from foul-smelling air.

〔実施例〕〔Example〕

次に、実施例について本発明を説明する。 Next, the present invention will be explained with reference to examples.

実施例 ポリアクリル酸ナトリウム(東亜合成化学製品)5g(
カルボキシル基として0.07モル)を、0.02モル
濃度のCu(NO,)2−311.o I Q中に分散
、溶解させ、次いで0.INアンモニア水でpHをl0
10に調整してゲルを生成させた。このゲルをロ別後、
P旧、5の塩酸で十分洗浄し、乾燥させると、青色のポ
リアクリル酸の銅塩キレート化物が得られた。
Example Sodium polyacrylate (Toagosei Chemicals) 5g (
0.07 mol as carboxyl group) and 0.02 mol of Cu(NO,)2-311. o Dispersed and dissolved in IQ, then 0. Adjust the pH to 10 with IN ammonia water.
10 to produce a gel. After separating this gel,
After thorough washing with hydrochloric acid and drying, a blue copper salt chelate of polyacrylic acid was obtained.

得られたポリアクリル酸の銅塩キレート化物3gを0.
1%アンモニア蒸気にさらしてアンモニアを飽和吸着さ
せたものを、容jlQのテトラパックに入れ、そこにア
ンモニア500ppmを送り込んだ、 20分間経過後
のテトラパック中のアンモニア濃度を検知管により測定
したが、濃度に変化は見られなかった。
3 g of the obtained copper salt chelate of polyacrylic acid was added to 0.
The ammonia was saturated and adsorbed by exposure to 1% ammonia vapor, and then placed in a Tetra Pak with a volume of JlQ, and 500 ppm of ammonia was introduced into it.After 20 minutes had elapsed, the ammonia concentration in the Tetra Pak was measured using a detection tube. , no change in concentration was observed.

このようにしてアンモニアを飽和状態迄吸着させたポリ
アクリル酸硝酸銅キレート化物を、pH4゜5の塩酸で
洗浄することによりアンモニアを脱離させたものを乾燥
した後、上記と同様にしてテトラパック中で500pp
mのアンモニアと接触させると、20分間経過後のテト
ラパック中のアンモニア濃度は1100ppに低下して
いた。
The polyacrylic acid copper nitrate chelate with ammonia adsorbed to a saturated state in this way was washed with hydrochloric acid of pH 4.5 to remove ammonia, and after drying, Tetra Pak was prepared in the same manner as above. 500pp inside
When the Tetra Pak was brought into contact with ammonia of m, the ammonia concentration in the Tetra Pak decreased to 1100 pp after 20 minutes.

比較例 実施例で用いられたポリアクリル酸ナトリウム5gを、
P旧、0の塩酸水溶液100a+ Q中に加え、生成し
たゲルを0別、乾燥した。
Comparative Example 5 g of sodium polyacrylate used in the example,
P was added to 100a+Q of an aqueous solution of hydrochloric acid, and the resulting gel was separated and dried.

このゲル化物3gを容量IQのテトラパックに入れ、そ
こに500ppmのアンモニアを送り込み、20分間経
過後のアンモニア濃度を測定すると、その値は300p
pmであった。
Put 3g of this gelled product into a Tetra Pak with a capacity of IQ, feed 500ppm of ammonia into it, and measure the ammonia concentration after 20 minutes.The value is 300ppm.
It was pm.

Claims (1)

【特許請求の範囲】 1、カルボキシル基含有重合体の銅塩キレート化物より
なるアンモニア吸着材。 2、カルボキシル基含有重合体がポリアクリル酸である
特許請求の範囲第1項記載のアンモニア吸着材。
[Scope of Claims] 1. An ammonia adsorbent comprising a copper salt chelate of a carboxyl group-containing polymer. 2. The ammonia adsorbent according to claim 1, wherein the carboxyl group-containing polymer is polyacrylic acid.
JP61147809A 1986-06-24 1986-06-24 Adsorbent for ammonia Pending JPS634847A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61147809A JPS634847A (en) 1986-06-24 1986-06-24 Adsorbent for ammonia

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61147809A JPS634847A (en) 1986-06-24 1986-06-24 Adsorbent for ammonia

Publications (1)

Publication Number Publication Date
JPS634847A true JPS634847A (en) 1988-01-09

Family

ID=15438703

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61147809A Pending JPS634847A (en) 1986-06-24 1986-06-24 Adsorbent for ammonia

Country Status (1)

Country Link
JP (1) JPS634847A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63200837A (en) * 1987-02-17 1988-08-19 Mishima Seishi Kk Deodorant and sheet-shaped deodorizing material
WO2000040324A1 (en) * 1998-12-31 2000-07-13 Kemira Agro Oy Process for separation of ammonia gas and a solid adsorbent composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63200837A (en) * 1987-02-17 1988-08-19 Mishima Seishi Kk Deodorant and sheet-shaped deodorizing material
WO2000040324A1 (en) * 1998-12-31 2000-07-13 Kemira Agro Oy Process for separation of ammonia gas and a solid adsorbent composition

Similar Documents

Publication Publication Date Title
Becker et al. Adsorption of nickel (II), zinc (II) and cadmium (II) by new chitosan derivatives
CA1060591A (en) Method for removing phosphates from aqueous solutions
Roozemond et al. Preferred uptake of Cu (II) and Cd (II) by novel pyrazole-functionalized chelating polymers
JPS634847A (en) Adsorbent for ammonia
JPS631098B2 (en)
US2906762A (en) Polyhydroxyethyl polyamine compound
CN103342722B (en) Preparation method of alkaline bismuth gallate
WO2024037662A1 (en) Preparation method for and use of bismuth ion filter membrane
Massaoud et al. Separation of Ga (III) from Cu (II), Ni (II) and Zn (II) in aqueous solution using synthetic polymeric resins
Murray III et al. The halogen-metal interconversion reaction and its application to the synthesis of nicotinic acid labeled with isotopic carbon
JP3663437B2 (en) Heavy metal ion adsorbent and method for producing the same
JP2005213477A (en) Chelate resin and method for producing the same
JPS63224735A (en) Adsorbent for recovering gallium
US3901677A (en) Method for improving soil
US3043867A (en) Method for the purification of aminocarboxylic acids
JPS62292165A (en) Deodorant
GB2527128A (en) Method for reducing arsenic concentration in aqueous solutions
JPH01203040A (en) Adsorbent and manufacture thereof
JP2560067B2 (en) Deodorant
RU2230034C2 (en) Method of recovering ruthenium-106 from transplutonium element production raffinates
TWI704109B (en) Method of recovering gold using thiourea graphene
SU1002389A1 (en) Method for recovering germanium from solutions by sorption
JPH10305224A (en) Cadmium adsorbent
JP2641239B2 (en) Silver adsorbent and method of using the same
JP3412003B2 (en) Novel lithium adsorbent and method for producing the same