JPS61219853A - Method for automatically measuring concentration of ammonia - Google Patents

Method for automatically measuring concentration of ammonia

Info

Publication number
JPS61219853A
JPS61219853A JP6239785A JP6239785A JPS61219853A JP S61219853 A JPS61219853 A JP S61219853A JP 6239785 A JP6239785 A JP 6239785A JP 6239785 A JP6239785 A JP 6239785A JP S61219853 A JPS61219853 A JP S61219853A
Authority
JP
Japan
Prior art keywords
ammonia
refractometer
pressure
cooler
temp
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
JP6239785A
Other languages
Japanese (ja)
Inventor
Masaru Nakamura
勝 中村
Taichi Iio
太一 飯尾
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.)
Sumikin Coke Co Ltd
Original Assignee
Sumikin Coke 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 Sumikin Coke Co Ltd filed Critical Sumikin Coke Co Ltd
Priority to JP6239785A priority Critical patent/JPS61219853A/en
Publication of JPS61219853A publication Critical patent/JPS61219853A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To continuously and automatically measure the concn. of ammonia, by providing an analytical specimen line, which consists of a pressure reducing valve, a cooler and a refractometer, so as to branch the same from an ammonia supply system and converting high temp. and high pressure aqueous ammonia to low temp. and low pressure aqueous ammonia. CONSTITUTION:In ammonia recovery equipment, an ammonia analytical specimen sampling line is branched on the way of the piping for connecting an ammonical liquor tank 9 and a rectifying column 10. That is, a pressure reducing valve 1, a blocking valve 2, a cooler 3 and a refractometer 4 are connected to a branch pipe 2 in series and the exit side of the refractometer 4 is connected to a conductor 6 and a recorder 5 for recording a measured value is connected to the refractometer 4. The high temp. and high pressure aqueous ammonia flowed in the branch pipe 12 is reduced in pressure by the pressure reducing valve 1 and further cooled to low temp. by the cooler 3 to be passed through the refractometer 4. Noticing that the change in a refractive index per 1 deg.C is 0.00173 in a liquid temp. range of 16.9-38.3 deg.C, a conversion mechanism is provided from the relational formula of ammonia concn. and a refractive index to measure the concn.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、コークス炉ガス中のアンモニアを液体アン
モニアとして回収する液安設備等におけるアンモニア水
中のアンモニア濃度を自動測定する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for automatically measuring the ammonia concentration in aqueous ammonia in a liquid bathing facility or the like that recovers ammonia in coke oven gas as liquid ammonia.

従来の技術 特有の刺激臭で知られるアンモニアは、窒息性の有毒気
体であり、空気中に5 ppm混入していても感知でき
、悪臭防止法では、5 ppm以下と規制されている。
Ammonia, known for its pungent odor unique to conventional technology, is a suffocating and toxic gas that can be detected even at 5 ppm in the air, and is regulated at 5 ppm or less under the Offensive Odor Prevention Act.

コークス炉ガス中のアンモニアを液体アンモニアとして
回収する方法の1つとして、米国のUSスチール社が開
発したホーサムプロセス(PHO3AHPROCESS
)があり、我国においても広く使用されている。
The PHO3AHPROCESS was developed by US Steel as a method for recovering ammonia in coke oven gas as liquid ammonia.
) and is widely used in our country.

この方法は、コークス炉ガス中のアンモニアを燐酸アン
モニウム吸収液(以下吸収液という)に吸収せしめたの
ち、該吸収液を熱交換器を経てコンダクタ−に導入し、
溶解しているH2S、CO2等の酸性ガスの除去を行っ
たのち、ストリッパーに導入してダイレクトスチームに
よりアンモニアをアンモニア水として分離し、該アンモ
ニア水を精留塔に導入してスチーム加熱によりアンモニ
アを精密している。この精留塔の運転は、供給されるア
ンモニア水中のアンモニア濃度によって加熱スチーム量
をコントロールするため、供給するアンモニア水中のア
ンモニア濃度を測定する必要がある。
In this method, ammonia in coke oven gas is absorbed into an ammonium phosphate absorption liquid (hereinafter referred to as absorption liquid), and then the absorption liquid is introduced into a conductor through a heat exchanger.
After removing dissolved acidic gases such as H2S and CO2, the ammonia is introduced into a stripper and separated as aqueous ammonia using direct steam.The aqueous ammonia is introduced into a rectification column and heated with steam to remove ammonia. It's precise. In operation of this rectification column, the amount of heated steam is controlled by the ammonia concentration in the supplied ammonia water, so it is necessary to measure the ammonia concentration in the supplied ammonia water.

従来、精留塔へ送入するアンモニア水中のアンモニア濃
度の測定は、作業員が防毒マスクを装着して送入系から
アンモニア水をサンプリングするのであるが、精留塔や
その供給系等は、13〜17−着程度の高圧で運転され
ているため、冷却してアンモニア水としてサンプリング
時、アンモニアが大気中に発散するばかりでなく、サン
プリングしたアンモニア水に硫酸を添加してアンモニア
濃度滴定時もアンモニアが発散し、アンモニア特有の刺
激臭で作業環境を悪化するばかりでなく、手作業のため
測定頻度が制限されていた。
Conventionally, to measure the ammonia concentration in ammonia water fed to a rectification tower, a worker wears a gas mask and samples the ammonia water from the feed system. Because it is operated at high pressures such as 13 to 17, it not only releases ammonia into the atmosphere when it is cooled and sampled as ammonia water, but also when titrating ammonia concentration by adding sulfuric acid to the sampled ammonia water. Not only did ammonia emit and the pungent odor characteristic of ammonia worsen the working environment, but the measurement frequency was limited because it was done manually.

又、アンモニア水溶液のアンモモニア濃度と屈折率の関
係は知られているが、精留塔へ供給するアンモニア水中
には、アンモニアばかりでなく、微量のH2S、CO2
等の不純物が含有され屈折率が変化し、しかも精留塔へ
の供給は、高圧で運転されているため、プロセス屈折計
を設置することは不可能であった。
Furthermore, although the relationship between the ammonia concentration and the refractive index of an ammonia aqueous solution is known, the ammonia water supplied to the rectification column contains not only ammonia but also trace amounts of H2S and CO2.
It was impossible to install a process refractometer because the refractive index changes due to impurities such as, and the supply to the rectification column is operated at high pressure.

発明が解決しようとする問題点 上記精留塔へ供給するアンモニア水は、高温で、かつ高
圧のため、そのままではアンモニア水として試料を採取
することはできない。
Problems to be Solved by the Invention Since the ammonia water supplied to the rectification column is at high temperature and high pressure, it is impossible to collect a sample as ammonia water as it is.

この発明は、上記精留塔へ送入する高圧アンモニア水中
のアンモニア濃度をアンモニアを発散せしめることなく
、自動的に連続測定する方法を提供し、分析試料採取時
及び分析時における作業環境を改善するものである。
The present invention provides a method for automatically and continuously measuring the ammonia concentration in high-pressure ammonia water fed to the rectification column without causing ammonia to emit, thereby improving the working environment during analysis sample collection and analysis. It is something.

問題点を解決するための手段 ]−ウス炉ガス中のアンモニアを燐酸アンモニウム吸収
液に吸収せしめたのち、ストリッパーに富アンモニア吸
収液を導入してアンモニアを離脱せしめ、得られたアン
モニア水を精留塔で分留して液体アンモニアとして回収
するに際し、精留塔への供給系に分析試料採取ラインを
設け、減圧弁、冷却器を介して屈折計に接続し、減圧、
冷却して得たアンモニア水中のアンモニア濃度を連続自
動測定することを特徴とするアンモニア濃度自動測定方
法である。
Measures to solve the problem] - After the ammonia in the gas furnace gas is absorbed into the ammonium phosphate absorption liquid, the ammonia-rich absorption liquid is introduced into the stripper to remove the ammonia, and the obtained ammonia water is rectified. When recovering liquid ammonia through fractional distillation in the column, an analysis sample collection line is installed in the supply system to the rectification column, and connected to a refractometer via a pressure reducing valve and a cooler.
This is an automatic ammonia concentration measuring method characterized by automatically and continuously measuring the ammonia concentration in cooled ammonia water.

作用 この発明においては、アンモニアの供給系から分岐して
減圧弁、冷却器、及び屈折計からなる分析試料ラインを
設け、高温高圧のアンモニア水を減圧、冷却して低温低
圧のアンモニア水とすることによって、該アンモニア水
をプロセス屈折計に導入し、アンモニア濃度を連続的に
自動測定するのである。
Function: In this invention, an analysis sample line consisting of a pressure reducing valve, a cooler, and a refractometer is branched from the ammonia supply system, and high-temperature, high-pressure ammonia water is depressurized and cooled to become low-temperature, low-pressure ammonia water. The ammonia water is introduced into a process refractometer and the ammonia concentration is continuously and automatically measured.

又、屈折計からのアンモニア水は、導管によって低圧部
、例えばストリッパーへ入る前の富アンモニア吸収液か
ら)12 S 、 CO2等の酸性ガスを除去するコン
ダクタ−等に導入することによって、サンプリング時や
アンモニア濃度の測定時の発散を完全に防止するするこ
とができる。
In addition, the ammonia water from the refractometer can be introduced through a conduit into a low-pressure section, such as a conductor that removes acidic gases such as 12S and CO2 from the ammonia-rich absorption liquid before entering the stripper, during sampling or the like. Emissions during measurement of ammonia concentration can be completely prevented.

実施例 この発明の詳細を、その一実施例を示す図面に基いて説
明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The details of this invention will be explained based on the drawings showing one embodiment thereof.

第1図はコークス炉ガスのアンモニア回収設備の一例を
示したもので、(7)は吸収塔、(6)はコンダクタ−
1(8)はストリッパー、(9)は安水タンク、(10
)は精留塔、(11)は液安タンクであり、吸収塔〔7
)の下部よりコークス炉ガスを送入し、塔内に噴射され
ている吸収液と向流接触せしめ、アンモニアを除去した
コークス炉ガスは上部より次工程へ送出する。
Figure 1 shows an example of ammonia recovery equipment from coke oven gas, where (7) is an absorption tower and (6) is a conductor.
1 (8) is a stripper, (9) is a cheap water tank, (10
) is a rectification tower, (11) is a liquid ammonium tank, and an absorption tower [7
) The coke oven gas is introduced from the lower part of the tower, brought into countercurrent contact with the absorption liquid injected into the tower, and the coke oven gas from which ammonia has been removed is sent to the next process from the upper part.

一方、アンモニアを吸収した富アンモニア吸収液の一部
は熱交換器を経てコンダクタ−(6)に送入され、溶解
しているH2S5C02等の酸性ガスの除去が行なわれ
る。酸性ガスを除去した富アンモニア吸収液は熱交換器
を経てストッパー(8)に送入される。このストリッパ
ー(8)の底部にはスチームが吹き込まれ、富アンモニ
ア吸収液からアンモニアの大部分を離脱せしめる。
On the other hand, a portion of the ammonia-rich absorption liquid that has absorbed ammonia is sent to the conductor (6) via a heat exchanger, where dissolved acidic gases such as H2S5C02 are removed. The ammonia-rich absorption liquid from which acidic gas has been removed is sent to the stopper (8) via a heat exchanger. Steam is blown into the bottom of this stripper (8) to remove most of the ammonia from the ammonia-rich absorption liquid.

上記によりアンモニアを!!脱した貧アンモニア吸収液
はストリッパー(8)の底から後出され、熱交換器及び
冷却器を経て冷却されたのち再び吸収塔(7)に循環す
る。
Ammonia from the above! ! The removed ammonia-poor absorption liquid is discharged from the bottom of the stripper (8), cooled through a heat exchanger and a cooler, and then circulated back to the absorption tower (7).

そして、離脱したアンモニアペーパーはストリッパー(
8)の上部より、熱交換器及び冷却器で凝縮されてアン
モニア水となり安水タンク(9)に一時貯留後、ざらに
精留塔(10)へ送入される。精留塔内では底部から送
入されたスチームにより加熱蒸溜され、塔頂から純粋の
アンモニアベーパーとして流出し液安タンク(11)に
貯留される。
Then, the separated ammonia paper is removed by a stripper (
8), it is condensed in a heat exchanger and a cooler to become ammonia water, temporarily stored in an ammonium water tank (9), and then roughly sent to a rectification column (10). Inside the rectification column, steam is introduced from the bottom to heat and distill the ammonia vapor, which flows out from the top of the column as pure ammonia vapor and is stored in the ammonium tank (11).

この発明は上記アンモニア回収設備において、安水タン
ク(9)と精留塔(10)を接続する配管途中よりアン
モニア分析試料採取ラインを分岐せしめるのである。す
なわち、分岐管(12)に減圧弁(1)、遮断弁(2)
、冷却器(3)及び屈折計(4)を直列に接続し、屈折
計(4)の出側をコンダクタ−(6)に接続する。又、
屈折計(4)には測定値を記録するための記録計(5)
を接続する。なお、遮断弁(2)は異常圧力変動が生じ
たとき、アンモニア水の流入を停止するためのものであ
る。
In the ammonia recovery equipment described above, the present invention branches an ammonia analysis sample collection line from the middle of the piping connecting the ammonium water tank (9) and the rectification column (10). That is, the branch pipe (12) has a pressure reducing valve (1) and a cutoff valve (2).
, a cooler (3) and a refractometer (4) are connected in series, and the outlet of the refractometer (4) is connected to a conductor (6). or,
The refractometer (4) has a recorder (5) for recording the measured values.
Connect. Note that the shutoff valve (2) is for stopping the inflow of ammonia water when abnormal pressure fluctuation occurs.

したがって、分岐管(12)に流入した高温高圧(12
0〜150℃、13〜17−4)のアンモニア水は、ま
ず減圧弁(1)により低圧(3h4)に減圧され、さら
に冷却器(3)により低温(20〜40℃)に冷却され
、屈折計(4)を通過する。この屈折計(4)は市販の
ものが使用されるが、この発明は液温16.9℃〜38
.3℃の間において1℃当りの屈折率変化は0、000
173であることに着目し、アンモニア濃度と屈折率の
関係式より変換機構を設けて濃度を測定する。
Therefore, the high temperature and high pressure (12) flowing into the branch pipe (12)
Ammonia water at a temperature of 0 to 150°C, 13 to 17-4) is first reduced to a low pressure (3h4) by a pressure reducing valve (1), then cooled to a low temperature (20 to 40°C) by a cooler (3), and then refracted. Pass through total (4). This refractometer (4) is a commercially available one, but the present invention is capable of
.. The refractive index change per 1°C between 3°C is 0,000
173, a conversion mechanism is provided and the concentration is measured from the relational expression between the ammonia concentration and the refractive index.

今、アンモニア9.27/Nm’を含有するコークス炉
ガス140.0008m’/Hのアンモニア回収設備に
おいて、安水タンク(9)から送り出された温度140
℃、圧力16kiJのアンモニア水を分岐して温度30
°C1圧力3に14の低温低圧アンモニア水に変で屈折
計で濃度を測定した。すなわち、日に6回30分間隔で
1時間の測定を2日にわたり行った。その結果を平均値
で第1表に示した。なお、比較のため手分析で行う従来
法によるものも行った。この結果より、この発明法と従
来法との値の差は微差の範囲にあり、実操業において十
分信頼できることがわかる。
Now, in an ammonia recovery facility where coke oven gas 140.0008 m'/H containing ammonia 9.27/Nm' is sent out from the ammonium water tank (9), the temperature is 140
℃, ammonia water with a pressure of 16 kiJ is branched and the temperature is 30
The concentration was measured using a refractometer at low temperature and low pressure ammonia water at 3°C and 14°C. That is, measurements were taken for 1 hour at 30-minute intervals six times a day over two days. The results are shown in Table 1 as average values. For comparison, a conventional method of manual analysis was also conducted. From this result, it can be seen that the difference in value between this invention method and the conventional method is within the range of a slight difference, and is sufficiently reliable in actual operation.

(以下余白) 発明の効果 この発明は、上記のごとく、コークス炉ガスからのアン
モニア回収設備において、分離されたアンモニア液の濃
度を、サンプリングすることなく連続的に自動測定でき
るため、アンモニア刺激臭が発散せず、作業環境を悪化
することがない。又、連続自動測定により精留塔の管理
が容易となる。
(Blank below) Effects of the Invention As described above, the present invention can continuously and automatically measure the concentration of separated ammonia solution without sampling in equipment for recovering ammonia from coke oven gas, thereby eliminating the irritating odor of ammonia. It does not emit light and does not deteriorate the working environment. Moreover, continuous automatic measurement makes it easier to manage the rectification column.

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

第1図はこの発明を実施するためのアンモニア濃度連続
自動測定装置を有するコークス炉ガスからアンモニアを
回収する設備のフローシニトである。 1・・・減圧弁、2・・・遮断弁、3・・・冷却器、4
・・・屈折計、5・・・記録計、6・・・コンダクタ−
17・・・吸収塔、8・・・ストリッパー、9安水タン
ク、1G・・・精留塔、11・・・液安タンク、12・
・・分岐管。
FIG. 1 shows a Flowcinit system for recovering ammonia from coke oven gas, which is equipped with a continuous automatic ammonia concentration measuring device for carrying out the present invention. 1... Pressure reducing valve, 2... Shutoff valve, 3... Cooler, 4
...Refractometer, 5...Recorder, 6...Conductor
17... Absorption tower, 8... Stripper, 9 Ammonium water tank, 1G... Rectification tower, 11... Ammonium tank, 12.
... Branch pipe.

Claims (1)

【特許請求の範囲】[Claims] コークス炉ガス中のアンモニアを燐酸アンモニウム吸収
液に吸収せしめたのち、ストリッパーに富アンモニア吸
収液を導入してアンモニアを離脱せしめ、得られたアン
モニア水を精留塔で分留して液体アンモニアとして回収
するに際し、精留塔への供給系から分析試料採取ライン
を分岐し、減圧弁、冷却器を介して屈折計に接続し、減
圧、冷却して得たアンモニア水中のアンモニア濃度を連
続自動測定することを特徴とするアンモニア濃度自動測
定方法。
After the ammonia in the coke oven gas is absorbed into the ammonium phosphate absorption liquid, the ammonia-rich absorption liquid is introduced into the stripper to remove the ammonia, and the resulting ammonia water is fractionated in a rectification column and recovered as liquid ammonia. When doing this, an analytical sample collection line is branched from the supply system to the rectification column, connected to a refractometer via a pressure reducing valve and a cooler, and the ammonia concentration in the ammonia water obtained by reducing the pressure and cooling is continuously and automatically measured. An automatic ammonia concentration measuring method characterized by:
JP6239785A 1985-03-26 1985-03-26 Method for automatically measuring concentration of ammonia Pending JPS61219853A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6239785A JPS61219853A (en) 1985-03-26 1985-03-26 Method for automatically measuring concentration of ammonia

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6239785A JPS61219853A (en) 1985-03-26 1985-03-26 Method for automatically measuring concentration of ammonia

Publications (1)

Publication Number Publication Date
JPS61219853A true JPS61219853A (en) 1986-09-30

Family

ID=13198960

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6239785A Pending JPS61219853A (en) 1985-03-26 1985-03-26 Method for automatically measuring concentration of ammonia

Country Status (1)

Country Link
JP (1) JPS61219853A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102331480A (en) * 2011-05-31 2012-01-25 黑龙江建龙钢铁有限公司 Method for measuring coke oven gas by multiterm series absorption
CN105784638A (en) * 2016-01-07 2016-07-20 云南云天化股份有限公司 Vinyl acetate rectified product purity online detection device, control device and detection method
JP2018054535A (en) * 2016-09-30 2018-04-05 住鉱テクノリサーチ株式会社 Method of analyzing solution

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102331480A (en) * 2011-05-31 2012-01-25 黑龙江建龙钢铁有限公司 Method for measuring coke oven gas by multiterm series absorption
CN105784638A (en) * 2016-01-07 2016-07-20 云南云天化股份有限公司 Vinyl acetate rectified product purity online detection device, control device and detection method
JP2018054535A (en) * 2016-09-30 2018-04-05 住鉱テクノリサーチ株式会社 Method of analyzing solution

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