JPS5869710A - Absorbing liquid for carbon monoxide - Google Patents

Absorbing liquid for carbon monoxide

Info

Publication number
JPS5869710A
JPS5869710A JP56167898A JP16789881A JPS5869710A JP S5869710 A JPS5869710 A JP S5869710A JP 56167898 A JP56167898 A JP 56167898A JP 16789881 A JP16789881 A JP 16789881A JP S5869710 A JPS5869710 A JP S5869710A
Authority
JP
Japan
Prior art keywords
liquid
absorbing liquid
hmpa
water
chloride
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
JP56167898A
Other languages
Japanese (ja)
Other versions
JPH0135771B2 (en
Inventor
Takanori Kuwabara
桑原 隆範
Taiji Kamiguchi
上口 泰司
Kazue Tsuda
津田 和枝
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP56167898A priority Critical patent/JPS5869710A/en
Publication of JPS5869710A publication Critical patent/JPS5869710A/en
Publication of JPH0135771B2 publication Critical patent/JPH0135771B2/ja
Granted 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

  • Gas Separation By Absorption (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To improve the water-resistance and heat stability of CO absorbing liquid composed of cuprous chloride dissolved in hexamethyl phosphoryl triamide, by adding proper amounts of hydrochloric acid and lanthanum chloride to the liquid. CONSTITUTION:A CO-absorbing liquid obtained by dissolving cuprous chloride (CuCl) in hexamethyl phosphoryl triamide (HMPA) is incorporated with the lowest possible amounts of hydrochloric acid (HCl) and lanthanum chloride (LaCl3) to maintain th CO absorption capacity. A stable absorbing liquid having high water resistance can be obtained by this process. When the liquid is used in the CO-separation and CO-concentration processes, the pretreatment such as the removal of water from the exhaust gas becomes unnecessary.

Description

【発明の詳細な説明】 本発明は一酸化炭素の吸収液に係り、特にプロセス排ガ
スから一酸化炭素(以下、COと記すことがある)を分
離、濃縮して回収するためのCOの吸収液に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a carbon monoxide absorption liquid, and in particular to a CO absorption liquid for separating, concentrating and recovering carbon monoxide (hereinafter sometimes referred to as CO) from process exhaust gas. It is related to.

化学工業、製鉄工業等において、合成用原料ガスの製造
またはエネルギー回収といった考えのもとに、例えばプ
ロセス排ガスからCOを分離、濃縮して回収することが
大きな技術的線層になっている。
In the chemical industry, iron and steel industry, etc., separation, concentration, and recovery of CO from process exhaust gas, for example, has become a major technological focus, based on the idea of producing raw material gas for synthesis or recovering energy.

従来、COを含有するガス源からCOな分離、娘縮する
方法には、第1銅塩の溶液等の吸収液を使用する吸収液
法、およびこれとは原理的に異なる深冷分離法が知られ
ている。後者の深冷分離法は、複雑な冷却、熱回収シス
テムからなり、操作温度が低温であるため、装置材料と
して高価なものを使用する必要があり、また低、温を得
るために動力消費量が大きくなるという欠点がある。
Conventionally, methods for separating and condensing CO from a gas source containing CO include the absorption liquid method, which uses an absorption liquid such as a solution of cuprous salt, and the cryogenic separation method, which is fundamentally different from this method. Are known. The latter cryogenic separation method consists of a complex cooling and heat recovery system, and because the operating temperature is low, it is necessary to use expensive equipment materials, and it also requires high power consumption to obtain low temperature. The disadvantage is that it becomes large.

一方、吸収液法に使用されるCO吸収液としては、アン
モニア性第1銅塩水溶液または塩酸性第1銅塩水溶液が
用いられてきたが、いずれも水溶液単位体積あたりのC
O吸収量が小さいという問題があった。これに対し発明
者らはCO吸収量の痛い、塩化第1銅(CμC1)をヘ
キサメチルホスホルトリアミド(HMPA、別名トリス
(ジメチルアi〕)ホスフィンオキシト)K溶解せしめ
た吸収液を開発したが(特願昭55−21708号)、
この吸収液は単位体積当りのCO吸収量が水溶液係のも
のに較ぺて非常に高く、実際のプロセス適用上、数々の
利点があるが、この吸収液が水分を含むガスと接触し、
さらにCOを脱離するために加熱すると、次式に示すよ
うに溶解した塩化第1銅(Cμcg>が一部加水分解し
て酸化第1銅(CtLzQ)を生成し、吸収液のCO吸
収量が低下するという問題を生じた。
On the other hand, as the CO absorption liquid used in the absorption liquid method, an ammoniacal cuprous salt aqueous solution or a hydrochloric acidic cuprous salt aqueous solution has been used;
There was a problem that the amount of O absorbed was small. In response to this, the inventors developed an absorption liquid in which cuprous chloride (CμC1) was dissolved in hexamethylphosphortriamide (HMPA, also known as tris(dimethylai)phosphine oxide) K, which had a poor CO absorption capacity. (Patent Application No. 55-21708),
This absorption liquid has a very high CO absorption amount per unit volume compared to aqueous solutions, and has many advantages in actual process application.
When further heated to desorb CO, the dissolved cuprous chloride (Cμcg> is partially hydrolyzed to produce cuprous oxide (CtLzQ) as shown in the following formula, and the amount of CO absorbed by the absorbent increases. This resulted in a problem of a decrease in

CLLCl−HMPA + HxO→CLL幻↓+1−
LCI −HMPA本発明の目的は、CO吸収性能が高
く、かつ排ガス中の水分の影響を受けKくいCO吸収液
を提供することKある。
CLLCl-HMPA + HxO→CLL illusion ↓+1-
LCI-HMPA An object of the present invention is to provide a CO absorption liquid that has high CO absorption performance and is not affected by moisture in exhaust gas.

本発明の吸収液は、塩化第1銅(CμCI)をヘキサメ
チルホスホルトリアミド(HMPA)に溶解したCO吸
収液(以下、CuC4/ HMPA液と称する)に、塩
酸(HCI )および塩化ランタン(LaC4m)を、
実用的なCO吸収量を保持する最少限度の量で添加する
ことにより、耐水性および熱安定性の高い吸収液とした
ものである。
The absorption liquid of the present invention is a CO absorption liquid in which cuprous chloride (CμCI) is dissolved in hexamethylphosphortriamide (HMPA) (hereinafter referred to as CuC4/HMPA liquid), hydrochloric acid (HCI) and lanthanum chloride (LaC4mPA). )of,
By adding it in the minimum amount that maintains a practical amount of CO absorption, an absorbent liquid with high water resistance and thermal stability can be obtained.

本発明において、上記HCjの添加量は0.1〜0.2
凰01/lSLαCj3の絵加量は0.O1〜0.1講
o1/jが好ましい。
In the present invention, the amount of HCj added is 0.1 to 0.2
The amount of painting for 凰01/lSLαCj3 is 0. O1 to 0.1 degrees o1/j is preferred.

以下、本発明を比較例および実施例によりさらに評細に
説明する。
Hereinafter, the present invention will be explained in more detail with reference to comparative examples and examples.

比較例 空気中の酸素の影響を受けないようK、栓付き試験管(
容量10m)内にC@LC1/ HMPA (2mat
/l)液に水を5s含有させたものを封入し、90℃に
保持した恒温槽に入れて加熱した。その結果、加熱に従
い、謄色の沈澱物が生成した。これは、前記したように
CμCI・HMPA錯体の一部が加水分解し、酸化第1
銅(CMIO)を生成したためである。CbxOが生成
すると吸収液のCO吸収量が低下するので、水を含むガ
ス源からのCO分離濃縮用の吸収液として不適当なこと
がある。
Comparative Example A test tube with a stopper (K) so as not to be affected by oxygen in the air.
C@LC1/HMPA (2mat
/l) solution containing water for 5 seconds was sealed and heated in a constant temperature bath kept at 90°C. As a result, as the mixture was heated, a dark-colored precipitate was formed. As mentioned above, part of the CμCI/HMPA complex is hydrolyzed, resulting in oxidized first
This is because copper (CMIO) was produced. When CbxO is generated, the amount of CO absorbed by the absorbent decreases, so that it may be unsuitable as an absorbent for separating and concentrating CO from a gas source containing water.

実施例 ガス中の水分に対して影響されない吸収液、すなわちC
Oの吸収量を低下させない耐水性のある吸収液を得るた
めに、 CμC4/HMPA系液に1種々の酸液または
金属塩死物を添加し、上記比較例と同様に試験管を用い
てその効果を検討した。その結果、種々の添加剤の中で
最も液の安定性に対して効果のあったものは、塩化水素
(HCI )および塩化ランタン(LaC1m )であ
った。
Example Absorbing liquid that is not affected by moisture in the gas, that is, C
In order to obtain a water-resistant absorbent solution that does not reduce the amount of O absorbed, various acid solutions or dead metal salts were added to the CμC4/HMPA-based solution, and the mixture was added to the CμC4/HMPA solution using a test tube in the same manner as in the comparative example above. We examined the effects. As a result, among the various additives, the ones that were most effective on liquid stability were hydrogen chloride (HCI) and lanthanum chloride (LaC1m).

第1図は、MCIおよびLaCl3の添加量をそれぞれ
変え、90℃で4時間加熱した後の結果を示したもので
ある。図中、○印は沈殿が生成した場合、X印は沈殿が
生成した場合を示す。図から、HCIをO,Lm01/
I以上、LaCl3を0.01鷺61/1以上、添加す
れば、沈殿が生成しないことがわかる。
FIG. 1 shows the results after heating at 90° C. for 4 hours while varying the amounts of MCI and LaCl3 added. In the figure, the ○ mark indicates that a precipitate was formed, and the X mark indicates a case that a precipitate was formed. From the figure, HCI is O, Lm01/
It can be seen that if LaCl3 is added in an amount of 0.01 61/1 or more, no precipitate is formed.

次に第2図は、第1図の吸収液をさらに90℃で長時間
加熱(20時間)した場合の結果を示したものである。
Next, FIG. 2 shows the results when the absorption liquid shown in FIG. 1 was further heated at 90° C. for a long time (20 hours).

長時間加熱することにより、4時間で安定であったもの
が沈殿を生成する傾向にある。この条件においても沈殿
しないのは、HCjO,1mol / lでLaC45
0,05罵01 / 1以上の添加量のときである。 
HCjは0.2*0171より以上添加すると、COの
吸収量は大幅な低下を招く。またLaC15の添加量は
、多いほど望ましいことが予測されるが、薬品自体が高
価なため、0゜05〜0,1++aO4/ lが最適際
加量と考えられる ここでLaC15は通常、市販され
ているLaCj s・7H20が使用されるが、これは
CμCtの溶媒であるHMPAK溶解しないので、あら
かじめLaC1鴫・7H20を水に溶解してHMPAK
溶解させる必要がある。第1表は、実際のCO吸収プロ
セスで適用する上で最も望ましい液組成の一例を示した
ものである。
By heating for a long time, what was stable for 4 hours tends to form a precipitate. Even under these conditions, LaC45 does not precipitate at 1 mol/l of HCjO.
This is when the amount added is 0.05 to 01/1 or more.
When HCj is added in an amount of more than 0.2*0171, the amount of CO absorbed is significantly reduced. It is predicted that the larger the amount of LaC15 added, the more desirable it is, but since the chemical itself is expensive, 0.05 to 0.1++ aO4/l is considered to be the optimum amount. Here, LaC15 is usually commercially available. LaCj s・7H20 is used, but since it does not dissolve HMPAK, which is the solvent for CμCt, LaCj s・7H20 is dissolved in water in advance and HMPAK is used.
Needs to be dissolved. Table 1 shows an example of the most desirable liquid composition for application in an actual CO absorption process.

吸収・脱離実験塔において、CO含有ガスの連続吸収実
験を行った結果、吸収液は100時間以上、沈殿を生成
することなく、安定であった、以上、本発明によれば、
CbCl / HMP A系のCO吸収液にHcjおよ
びLaC1mを含有させることにより、耐水性の良い安
定な吸収液を得ることができる。この吸収液をCO分離
・濃縮プロセスに用いた場合には、前処理装置として排
ガス中の水分を除去する撃賛がなく、装置的にも、また
運転コストの面でも有利となる。
As a result of continuous absorption experiments of CO-containing gas in an absorption/desorption experimental tower, the absorption liquid was stable for more than 100 hours without forming a precipitate.According to the present invention, as described above, according to the present invention,
By incorporating Hcj and LaC1m into the CbCl/HMP A-based CO absorption liquid, a stable absorption liquid with good water resistance can be obtained. When this absorption liquid is used in a CO separation/concentration process, there is no need for a pretreatment device to remove moisture from the exhaust gas, which is advantageous in terms of equipment and operating costs.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図および第2図は、それぞれCμCI /HMPA
C2v*01/II)の吸収液に水を5−含ませ、これ
にLaC15およびHCjを種々のlll&で添加した
場合の沈殿生成の有無を示した説明図である。 代坤人 弁理士  川 北 武 長 第1図 第2図 HCJl濃戻(moVL)
Figures 1 and 2 are CμCI/HMPA, respectively.
FIG. 2 is an explanatory diagram showing the presence or absence of precipitation when an absorption liquid of C2v*01/II) is impregnated with water and LaC15 and HCj are added thereto in various amounts. Daikonto Patent Attorney Takenaga Kawakita Figure 1 Figure 2 HCJl Noboru (moVL)

Claims (1)

【特許請求の範囲】[Claims] (1)塩化第1銅(CucJ)、ヘキサメチルホスホル
トリアミド(HMPA)、塩化ランタン(LaC1s 
)、塩化水素(HCI ) 、および水を含むことを%
像とする一酸化炭素の吸収液。
(1) Cuprous chloride (CucJ), hexamethylphosphortriamide (HMPA), lanthanum chloride (LaC1s)
), hydrogen chloride (HCI), and water.
Carbon monoxide absorption liquid for imaging.
JP56167898A 1981-10-22 1981-10-22 Absorbing liquid for carbon monoxide Granted JPS5869710A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56167898A JPS5869710A (en) 1981-10-22 1981-10-22 Absorbing liquid for carbon monoxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56167898A JPS5869710A (en) 1981-10-22 1981-10-22 Absorbing liquid for carbon monoxide

Publications (2)

Publication Number Publication Date
JPS5869710A true JPS5869710A (en) 1983-04-26
JPH0135771B2 JPH0135771B2 (en) 1989-07-27

Family

ID=15858096

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56167898A Granted JPS5869710A (en) 1981-10-22 1981-10-22 Absorbing liquid for carbon monoxide

Country Status (1)

Country Link
JP (1) JPS5869710A (en)

Also Published As

Publication number Publication date
JPH0135771B2 (en) 1989-07-27

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