JP2616900B2 - How to make the temperature distribution of the adsorbent uniform - Google Patents

How to make the temperature distribution of the adsorbent uniform

Info

Publication number
JP2616900B2
JP2616900B2 JP8146568A JP14656896A JP2616900B2 JP 2616900 B2 JP2616900 B2 JP 2616900B2 JP 8146568 A JP8146568 A JP 8146568A JP 14656896 A JP14656896 A JP 14656896A JP 2616900 B2 JP2616900 B2 JP 2616900B2
Authority
JP
Japan
Prior art keywords
adsorbent
gas
adsorption
temperature distribution
adsorption tank
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.)
Expired - Fee Related
Application number
JP8146568A
Other languages
Japanese (ja)
Other versions
JPH09850A (en
Inventor
一生 春名
岩光 塩沢
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.)
Sumitomo Seika Chemicals Co Ltd
Original Assignee
Sumitomo Seika Chemicals 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 Sumitomo Seika Chemicals Co Ltd filed Critical Sumitomo Seika Chemicals Co Ltd
Priority to JP8146568A priority Critical patent/JP2616900B2/en
Publication of JPH09850A publication Critical patent/JPH09850A/en
Application granted granted Critical
Publication of JP2616900B2 publication Critical patent/JP2616900B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、プレッシャースイ
ング用吸着槽内の吸着剤温度分布を均一化する方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for uniformizing the temperature distribution of an adsorbent in a pressure swing adsorption tank.

【0002】[0002]

【従来の技術】従来、ゼオライトモレキュラーシーブを
吸着剤とし、プレッシャースイング法により空気を加圧
導入して窒素ガスを吸着分離し酸素ガスを濃縮回収する
場合、窒素ガスがゼオライトモレキュラーシーブ細孔内
へ優先的に吸着して吸着ガス1Nl当たり約0.2kc
alの熱量を発生し温度が上昇しながら分離したガス
が、吸着槽出口側へ移動し、発生熱はガスにより顕熱と
して吸着槽外へ持ち出される。一方、吸着時の圧力より
減圧して窒素を脱着し再生する場合は吸着時と可逆的に
吸熱し断熱冷却現象により温度が降下し吸着槽入口側に
近い吸着剤程冷却される。この温度が低くなり過ぎる
と、ガス中の吸着力の強い水分やCO2 が吸着剤との吸
着力をさらに増加し、その為に却って脱着しにくくな
り、吸着層に蓄積し、その結果窒素と酸素の分離効率が
低下するものと推定される。
2. Description of the Related Art Conventionally, when a zeolite molecular sieve is used as an adsorbent and air is introduced under pressure by a pressure swing method to adsorb and separate nitrogen gas and concentrate and recover oxygen gas, nitrogen gas is introduced into pores of the zeolite molecular sieve. Approximately 0.2kc per 1Nl of adsorbed gas with preferential adsorption
The separated gas while generating the heat of al and increasing in temperature moves to the adsorption tank outlet side, and the generated heat is taken out of the adsorption tank as sensible heat by the gas. On the other hand, when nitrogen is desorbed and regenerated at a pressure lower than the pressure at the time of adsorption, heat is reversibly absorbed at the time of adsorption, the temperature drops due to the adiabatic cooling phenomenon, and the adsorbent closer to the adsorption tank inlet side is cooled. If this temperature is too low, the strongly adsorbing water or CO 2 in the gas will further increase the adsorbing power with the adsorbent, which makes it more difficult to desorb and accumulates in the adsorbent layer, resulting in the accumulation of nitrogen and It is estimated that the oxygen separation efficiency decreases.

【0003】[0003]

【発明が解決しようとする課題】上記の吸着、脱着現象
を重ねていくと図1に示すような温度分布に収瞼するよ
うになり充填高さによる吸着剤の温度勾配が著しくな
る。これを改善し吸着剤温度分布を均一化する為に本発
明者らは出口ガスと吸着剤を熱交換すべく、吸着槽出口
配管を吸着剤の中を貫通して配設することを発明した。
また、プレッシャースイング法では配管内をガスが瞬時
に流れる時があり、その時高温を発し外部に対して騒音
となる。本発明者らは前記の如く出口ガス通路を吸着剤
充填層の中を貫通させると、この騒音防止にも効果があ
ることを見出した。
When the above-mentioned adsorption and desorption phenomena are repeated, the temperature distribution as shown in FIG. 1 becomes visible, and the temperature gradient of the adsorbent due to the filling height becomes remarkable. In order to improve this and to make the temperature distribution of the adsorbent uniform, the present inventors have invented to arrange the outlet pipe of the adsorption tank through the adsorbent in order to exchange heat between the outlet gas and the adsorbent. .
Further, in the pressure swing method, gas may flow instantaneously in the pipe, and at that time, a high temperature is generated, which causes noise to the outside. The present inventors have found that if the outlet gas passage penetrates through the adsorbent-filled layer as described above, it is also effective in preventing this noise.

【0004】本発明は、吸着槽にゼオライトモレキュラ
ーシーブ又はカーボンモレキュラーシーブ等を充填して
プレッシャースイング法により混合ガスを吸着分離する
際、温度が入口ガスより上昇した吸着槽出口ガスにて、
温度が入口ガスより降下した吸着槽入口部吸着剤を加温
し、脱着再生時に必要な熱エネルギーを供給することに
より、脱着再生能力を増大させると共に、ガスが高速度
で出口配管内を流動する際に発生する騒音を低減するこ
との出来る吸着層を用いて吸着剤温度分布を均一化する
方法を提供する事を目的とする。特に酸素と窒素を主成
分とする混合ガスの場合、前記温度差が大きくなるので
一層有利に本発明が利用できる。
According to the present invention, when the adsorption tank is filled with zeolite molecular sieve or carbon molecular sieve and the mixed gas is adsorbed and separated by the pressure swing method, the temperature of the adsorbent tank outlet gas is higher than the inlet gas.
By heating the adsorbent at the inlet of the adsorption tank whose temperature has dropped below the inlet gas and supplying the necessary thermal energy during desorption regeneration, the desorption regeneration capacity is increased and the gas flows in the outlet pipe at a high speed. It is an object of the present invention to provide a method for making the temperature distribution of an adsorbent uniform by using an adsorbent layer capable of reducing noise generated at the time. In particular, in the case of a mixed gas containing oxygen and nitrogen as main components, the temperature difference becomes large, so that the present invention can be used more advantageously.

【0005】[0005]

【課題を解決するための手段】即ち、本発明の要旨は、
プレッシャースイング法により混合ガスを吸着分離する
に際し、吸着熱を顕熱として保持する吸着槽出口ガスに
より吸着時に吸着剤を加温しながら排出するように、吸
着剤充填層内を貫通するように配設された複数本の貫通
管内に吸着槽出口ガスを通過させることを特徴とする吸
着剤温度分布の均一化方法、に関する。
That is, the gist of the present invention is as follows.
When the mixed gas is adsorbed and separated by the pressure swing method, it is arranged so as to penetrate through the adsorbent packed layer so that the adsorbent is heated and discharged at the time of adsorption by the adsorption tank outlet gas that holds the heat of adsorption as sensible heat. The present invention relates to a method for making an adsorbent temperature distribution uniform, wherein an outlet gas of an adsorption tank is passed through a plurality of provided through-tubes.

【0006】[0006]

【発明の実施の形態】本発明の吸着槽は、吸着槽出口ノ
ズルと出口ガス通路を一体とし、吸着剤充填層内を少な
くとも1本以上、好ましくは複数本の貫通管で貫通させ
る構造とすることによって、吸着槽出口ガスが顕熱とし
て持ち出す熱量を吸着槽出口ガスが貫通管を通過する時
に熱交換により回収し、吸着剤を加温する効果を持たせ
ることができる。その結果、図1に示すように吸着剤温
度分布が均一化され吸着分離効率の低下が防止できる。
BEST MODE FOR CARRYING OUT THE INVENTION The adsorption tank of the present invention has a structure in which an adsorption tank outlet nozzle and an outlet gas passage are integrated, and the inside of the adsorbent packed layer is penetrated by at least one, preferably a plurality of through tubes. Thereby, the heat quantity brought out by the gas at the outlet of the adsorption tank as sensible heat can be recovered by heat exchange when the gas at the outlet of the adsorption tank passes through the through-tube, and the adsorbent can be heated. As a result, as shown in FIG. 1, the temperature distribution of the adsorbent is made uniform, and a decrease in the adsorption separation efficiency can be prevented.

【0007】[0007]

【実施例】以下、実施例により本発明をさらに詳しく説
明するが、本発明はこれらの実施例によりなんら限定さ
れるものではない。 実施例1 具体的な構造として円筒竪型の場合は図2または図3の
ように出口ガス通路が貫通管として吸着剤で包まれるよ
うに吸着槽内部に組み込まれる為、配管内より発せられ
るガス流れ音が吸着剤に吸収され防音対策が不要とな
る。特に図3の如く貫通管の本数を多く設定する程、こ
の熱回収効果は大きくなる。従って、本発明において好
適な態様としては、複数本の貫通管を備えた吸着槽が挙
げられ、かかる吸着槽を用いた場合、吸着剤温度分布の
均一化が効率よく達成される。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the present invention. Example 1 In a case of a cylindrical vertical type as a specific structure, as shown in FIG. 2 or FIG. 3, since an outlet gas passage is incorporated in an adsorption tank so as to be wrapped with an adsorbent as a penetrating pipe, gas emitted from the pipe is used. The flow noise is absorbed by the adsorbent, and no soundproofing measures are required. In particular, as the number of through tubes is increased as shown in FIG. 3, the heat recovery effect becomes greater. Therefore, a preferred embodiment of the present invention includes an adsorption tank having a plurality of through-tubes. When such an adsorption tank is used, uniformization of the adsorbent temperature distribution can be efficiently achieved.

【0008】[0008]

【発明の効果】吸着剤の下部層が吸着剤の内部を貫通す
る配管内を通過するガスによって加温されることによ
り、脱着再生時に必要な熱エネルギーが熱交換により供
給され、槽内吸着剤の温度分布が均一化され脱着再生能
力が増大する。また配管を吸着剤充填層内部に貫通させ
ることにより吸着剤が吸音材となり、防音対策が不要と
なる。一方装置が大型化すると温度の不均一化傾向が増
大するので本発明がさらに有効に活用できる。
The lower layer of the adsorbent is heated by the gas passing through the pipe penetrating through the interior of the adsorbent, so that heat energy required for desorption regeneration is supplied by heat exchange, and the adsorbent in the tank is supplied. Is uniformed, and the desorption / regeneration capability is increased. In addition, since the pipe penetrates through the adsorbent-filled layer, the adsorbent becomes a sound absorbing material, so that soundproofing measures are not required. On the other hand, as the size of the apparatus increases, the tendency of the temperature to become non-uniform increases, so that the present invention can be used more effectively.

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

【図1】図1は、吸着槽における充填高さと吸着剤温度
分布を示す曲線であり改善前(従来装置)と改善後(本
発明装置)の差を示している。
FIG. 1 is a curve showing a filling height and an adsorbent temperature distribution in an adsorption tank, showing a difference between before improvement (conventional device) and after improvement (device of the present invention).

【図2】図2は貫通管1本を備え、吸着剤充填層内に貫
通せしめた状態を示す略図である。
FIG. 2 is a schematic diagram showing a state in which one penetrating tube is provided and penetrated into an adsorbent packed layer.

【図3】図3は貫通管5本を備え、吸着剤充填層内に貫
通せしめた状態を示す略図である。
FIG. 3 is a schematic view showing a state in which five penetrating pipes are provided and penetrated into an adsorbent packed layer.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 プレッシャースイング法により混合ガス
を吸着分離するに際し、吸着熱を顕熱として保持する吸
着槽出口ガスにより吸着時に吸着剤を加温しながら排出
するように、吸着剤充填層内を貫通するように配設され
た複数本の貫通管内に吸着槽出口ガスを通過させること
を特徴とする吸着剤温度分布の均一化方法。
1. When adsorbing and separating a mixed gas by a pressure swing method, the adsorbent packed layer is heated and discharged at the time of adsorption by an adsorbing tank outlet gas which holds adsorption heat as sensible heat. A method for making the temperature distribution of an adsorbent uniform, wherein an outlet gas of an adsorption tank is passed through a plurality of through-tubes arranged so as to penetrate the adsorbent.
JP8146568A 1996-05-15 1996-05-15 How to make the temperature distribution of the adsorbent uniform Expired - Fee Related JP2616900B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8146568A JP2616900B2 (en) 1996-05-15 1996-05-15 How to make the temperature distribution of the adsorbent uniform

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8146568A JP2616900B2 (en) 1996-05-15 1996-05-15 How to make the temperature distribution of the adsorbent uniform

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP60106736A Division JPH0620504B2 (en) 1985-05-17 1985-05-17 Adhesive tank for press swing

Publications (2)

Publication Number Publication Date
JPH09850A JPH09850A (en) 1997-01-07
JP2616900B2 true JP2616900B2 (en) 1997-06-04

Family

ID=15410630

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8146568A Expired - Fee Related JP2616900B2 (en) 1996-05-15 1996-05-15 How to make the temperature distribution of the adsorbent uniform

Country Status (1)

Country Link
JP (1) JP2616900B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002345964A (en) * 2001-05-28 2002-12-03 Teijin Ltd Medical pressure variable oxygen condensing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002345964A (en) * 2001-05-28 2002-12-03 Teijin Ltd Medical pressure variable oxygen condensing device

Also Published As

Publication number Publication date
JPH09850A (en) 1997-01-07

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