KR20000031296A - Method of preparing nitrogen by pressure swing absorption and device therefor - Google Patents

Method of preparing nitrogen by pressure swing absorption and device therefor Download PDF

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KR20000031296A
KR20000031296A KR1019980047267A KR19980047267A KR20000031296A KR 20000031296 A KR20000031296 A KR 20000031296A KR 1019980047267 A KR1019980047267 A KR 1019980047267A KR 19980047267 A KR19980047267 A KR 19980047267A KR 20000031296 A KR20000031296 A KR 20000031296A
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nitrogen
adsorption
pressure
product
automatic valve
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KR1019980047267A
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Korean (ko)
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KR100275858B1 (en
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박두선
민경현
이선우
최태환
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김영대
대성산소 주식회사
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/047Pressure swing adsorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0454Controlling adsorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2256/00Main component in the product gas stream after treatment
    • B01D2256/10Nitrogen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/10Single element gases other than halogens
    • B01D2257/104Oxygen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/80Water

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

PURPOSE: A method of preparing nitrogen by pressure-change absorption and a device therefor are provided which separates gaseous nitrogen from air and produces the nitrogen by employing pressure swing absorption method. CONSTITUTION: The method comprises steps of: (i) absorption process; (ii) atmospheric desorption process(I); (iii) washing desorption process; (iv) uniform-pressure process; (v) condensing-pressure process; and (vi) atmospheric desorption process(II). In the absorption process, raw material air is compressed at an air compressor(1) and then gone through a filter(2), and it is moisture-eliminated and cooled down at an air drier(3) and then introduced to an absorption tower(20), where oxygen, carbon dioxide and moisture is absorbed, and non-absorbed product nitrogen component is stored at a product tank. In the atmospheric desorption process(I), the absorbed oxygen, carbon dioxide and moisture are emitted through a muffler(4) by opening an automatic valve(17). In the washing desorption process, product nitrogen component is stored at the product tank through the absorption process by continuously opening automatic valves(6 and 10) at the absorption tower(20), while an absorption tower(21) opens a hand valve(28) and an automatic valve(18) at the product storing tank and washes inside of the top with washing gas. In the uniform-pressure process, the pressure of the absorption tower(20) and the absorption tower(21) become same by closing the automatic valves(6), (17), (18) and (10) and opening a uniform automatic valve(9). In the condensing-pressure process, the nitrogen gas in the product tank compresses inside of the absorption tower by closing the automatic valve(9) and opening the automatic valve(18), so the oxygen on top of the absorption tower is moved downward. In the atmospheric desorption process(II), the absorbed oxygen, carbon dioxide and moisture are emitted through the muffler(4) by opening the automatic valve(17).

Description

압력변동흡착식 질소 제조방법 및 장치Pressure swing adsorption nitrogen production method and device

본 발명은 압력변동흡착법에 의해 공기로부터 기체질소를 분리, 생산하는 압력변동흡착식 질소 제조방법 및 장치에 관한 것이다.The present invention relates to a pressure swing adsorption nitrogen production method and apparatus for separating and producing gaseous nitrogen from the air by pressure swing adsorption.

종래의 압력변동흡착법(PSA: Pressure Swing Adsorption)에 의해 질소를 제조하는 방법은 공기중의 수분을 제거하기 위해 흡착탑의 하부에 활성알루미나를, 상부에는 탄소분자체(CMS: Carbon Molecular Sieve) 흡착제를 충진한 2 기의 흡착탑을 이용하여 공기중의 산소, 탄산가스, 수분을 선택적으로 흡착 제거하여 질소를 회수하고 대기압까지 감압하여 흡착제의 탈착재생을 행하는 것을 연속적으로 반복하는 질소 제조방법 및 장치의 개발이 오래 전부터 급속히 보급되어 왔다.In the conventional method of preparing nitrogen by pressure swing adsorption (PSA), the activated alumina is filled at the bottom of the adsorption tower and the carbon molecular sieve (CMS) is adsorbed at the top to remove moisture from the air. Development of a nitrogen production method and apparatus for continuously repeating the adsorption and desorption of adsorbents by selectively adsorbing and removing oxygen, carbon dioxide, and water in the air using two adsorption towers, recovering nitrogen and reducing the pressure to atmospheric pressure It has been rapidly spreading for a long time.

특히 일본 특허공보 평5-32087 호에서는 흡착공정에서 분리된 제품질소의 일부를 오리피스를 통하여 상압탈착 공정인 탑내로 보내어 세정가스로 사용되는데, 상압탈착시에 세정가스 유량이 사용되므로 제품 회수율 저하를 초래할 수 도 있고, 또한 균압공정에서 공급하는 측의 흡착탑 하부의 산소성분이 공급받는 측의 흡착탑 하부로 공급하는 측의 흡착탑 상부의 질소성분이 공급받는 측의 흡착탑 상부로 이동되므로 탑내부 가스의 흐름이 바뀌게 되어 질소농도 구배의 불안정은 제품순도를 일정하게 유지하기 곤란할 뿐만 아니라, 제품회수율이 떨어지는 결과를 초래한다.In particular, Japanese Patent Publication No. H5-32087 sends part of the product nitrogen separated in the adsorption process into the tower, which is an atmospheric pressure desorption process, through an orifice, and is used as a cleaning gas. Also, in the pressure equalization process, the oxygen content in the lower part of the adsorption tower on the supply side is transferred to the upper part of the adsorption tower on the side of the adsorption tower on the side of the absorption tower. This change causes the instability of the nitrogen concentration gradient to be difficult to keep the product purity constant, resulting in a drop in product recovery.

또한 한국 특허공고 제 95-703396 호에서는 흡착공정에서 분리되어 밸런스 탱크에 저장된 제품질소를 체크밸브를 통하여 탈착공정인 탑내로 보내어 세정가스로 사용되는데, 이것도 탈착 초기에 세정가스 유량이 사용되므로 제품회수율 저하를 초래한다. 그리고 균압공정에서도 공급하는 측의 흡착탑과 공급받는 측의 흡착탑이 균압과 동시에 대기방출 되므로 질소회수율이 떨어지게 되는 문제점이 있다.In addition, in Korean Patent Publication No. 95-703396, product nitrogen, which is separated in the adsorption process and stored in the balance tank, is sent to the tower, which is a desorption process, through a check valve, which is used as a cleaning gas. Causes deterioration. And even in the equalization process, the adsorption tower on the supply side and the adsorption tower on the receiving side are released to the atmosphere at the same time as the equalization pressure, there is a problem that the nitrogen recovery rate is lowered.

본 발명의 목적은 상기와 같은 문제점을 해결하기 위하여 흡착탑의 하부에는 활성알루미나를, 상부에는 산소를 선택적으로 흡착하는 탄소분자체를 충진한 2 기의 흡착탑을 이용하여 공기중의 질소를 농축 회수하고, 흡착공정에서 흡착탑에 충진되어 있는 탄소분자체는 산소를 선택적으로 흡착하고 배기되는 농축질소를 제품탱크에 포집하여 제품으로 회수하며, 산소로 포화된 흡착탑은 먼저 대기압으로 상압탈착한 다음에 제품질소로 세정하여 재생하고 흡착공정 후 상부의 잔류 질소성분은 탈착공정이 끝난 탑과 연결하여 잔류 질소성분을 회수하여 제품의 순도 및 회수율의 향상을 도모하는 압력변동흡착식 질소 제조방법 및 장치를 제공하고자 하는 것이다.An object of the present invention is to recover the concentration of nitrogen in the air by using a two-stage adsorption tower filled with carbon alumina to selectively adsorb the active alumina, the upper portion of the adsorption column to solve the above problems, In the adsorption process, the carbon molecular sieve filled in the adsorption column selectively adsorbs oxygen and collects the concentrated nitrogen exhausted in the product tank and recovers it to the product tank. After the regeneration and adsorption process, the residual nitrogen component in the upper part is connected to the tower where the desorption process is completed to recover the residual nitrogen component to provide a pressure change adsorption nitrogen production method and apparatus to improve the purity and recovery rate of the product.

본 발명의 압력변동흡착식 질소 제조방법은 상압탈착시에 흡착탑에 제품질소가스를 도입하지 않는 상압탈착 공정과 균압공정이 끝난 탑에 제품질소를 축압시키는 축압공정 및 압력을 공급하는 측과 압력을 받는 측의 흡착탑 상부로 연결하는 균압공정을 가진다.The pressure swing adsorption nitrogen production method of the present invention is subjected to a pressure storing process and a pressure supplying side and a pressure supplying side to pressurize a product nitrogen to a tower which has been subjected to an atmospheric pressure desorption process and a pressure equalizing process, which does not introduce product nitrogen gas into an adsorption tower during atmospheric pressure desorption. It has a pressure equalization process connecting to the upper side of the adsorption tower.

본 발명의 압력변동흡착식 질소 제조장치는 공기중의 수분을 제거하기 위하여 흡착탑의 하부에는 활성알루미나를, 상부에는 산소를 선택적으로 흡착하는 탄소분자체를 충진한 2 기의 흡착탑을 이용하여 공기중의 질소를 농축 회수한다.The apparatus for producing pressure swing adsorption nitrogen according to the present invention uses nitrogen in the air by using two adsorption towers filled with activated alumina in the lower part of the adsorption column and carbon molecules for selectively adsorbing oxygen in the upper part to remove moisture in the air. Concentrate and recover.

도1은 본 발명의 질소 제조방법 및 장치를 도시하는 공정흐름도1 is a process flow diagram showing a nitrogen production method and apparatus of the present invention.

<도면의 부호에 대한 설명><Description of Symbols in Drawings>

1: 공기압축기 2: 필터1: air compressor 2: filter

3: 공기드라이어 4: 소음기3: air dryer 4: silencer

5: 제품탱크 6,16: 공기공급 자동밸브5: Product tank 6,16: Automatic air supply valve

7,17: 배기가스 자동밸브 8,18: 세정가스공급 자동밸브7,17: Automatic exhaust gas valve 8,18: Automatic cleaning gas supply valve

9: 균압 자동밸브 10,19: 생산토출 자동밸브9: Equal pressure automatic valve 10,19: Production discharge automatic valve

20,21: 흡착탑 28: 세정가스공급 수동밸브20, 21: adsorption column 28: cleaning gas supply manual valve

본 발명을 첨부된 도면을 참조하여 상세히 설명한다.The present invention will be described in detail with reference to the accompanying drawings.

도1은 본 발명의 질소 제조방법 및 장치를 도시하는 공정흐름도 이다.1 is a process flow diagram showing a nitrogen production method and apparatus of the present invention.

본 발명의 장치는 원료공기를 공급하는 공기압축기(1), 공급된 공기중의 불순물을 제거하는 필터(2), 공기를 제습 및 냉각시키는 냉동식 공기드라이어(3), 제품세정가스를 대기방출시키는 소음기(4), 제품탱크(5), 흡착탑(20)및(21)에 원료공기를 공급하는 공기공급 자동밸브(6)및(16)와 흡착탑으로부터 배기가스를 배기하는 배기가스 자동밸브(7)및(17), 제품탱크로부터 흡착탑으로 세정가스를 보내는 세정가스공급 자동밸브(8)및(18)과 수동밸브(28), 균압자동밸브(9)및 제품질소 생산토출 자동밸브(10)및(19)로 구성된다.The apparatus of the present invention provides an air compressor (1) for supplying raw air, a filter (2) for removing impurities in the supplied air, a refrigeration air dryer (3) for dehumidifying and cooling the air, and product cleaning gas. Air supply automatic valves 6 and 16 for supplying raw air to the silencer 4, product tank 5, adsorption tower 20 and 21, and an exhaust gas automatic valve for exhausting exhaust gas from the adsorption tower ( 7) and (17), automatic cleaning gas supply valves (8) and (18), manual valves (28), pressure equalizing automatic valves (9) and product nitrogen production discharge automatic valves (10), which send cleaning gas from the product tank to the adsorption tower. And (19).

본 발명의 질소 제조방법은 다음과 같은 공정으로 이루어 진다.Nitrogen production method of the present invention consists of the following steps.

본 발명의 질소 제조방법은 흡착공정, 상압탈착공정, 세정탈착공정, 균압공정, 축압공정 및 상압탈착공정으로 이루어 진다.Nitrogen production method of the present invention consists of an adsorption process, atmospheric desorption process, cleaning desorption process, pressure equalization process, pressure storage process and atmospheric pressure desorption process.

흡착공정은 공기압축기(1)에서 소정압력으로 압축된 원료공기가 필터(2)를 거쳐서 공기 드라이어(3)에서 제습, 냉각되어 자동밸브(6)를 거쳐서 흡착탑(20)으로 도입되어 산소, 탄산가스, 수분은 흡착하고 흡착되지 않는 제품질소성분은 자동밸브(10)를 거쳐서 제품탱크에 저장되어 이루어 진다.In the adsorption process, raw air compressed at a predetermined pressure in the air compressor (1) is dehumidified and cooled in the air dryer (3) via the filter (2), and introduced into the adsorption tower (20) via the automatic valve (6) to provide oxygen and carbonic acid. Gas and moisture are adsorbed, but the product nitrogen component is not adsorbed is made to be stored in the product tank via an automatic valve (10).

상압탈착공정은 흡착탑(21) 탑내에 흡착된 산소, 탄산가스, 수분 등을 자동밸브(17)를 열어서 소음기(4)를 통하여 대기 방출하여 이루어 진다.The atmospheric desorption process is performed by releasing oxygen, carbon dioxide, moisture, etc. adsorbed in the adsorption tower 21 to the atmosphere through the silencer 4 by opening the automatic valve 17.

세정탈착공정은 흡착탑(20)의 자동밸브(6)및(10)를 계속하여 열어서 흡착공정을 하여 제품질소 성분을 제품저장 탱크에 저장하고, 반면에 흡착탑(21)은 제품저장 탱크의 수동밸브(28)와 자동밸브(18)를 열어서 제품세정 가스로 탑내를 세정하고 자동밸브(17)와 소음기(4)를 통하여 대기방출 하여 이루어 진다.The cleaning desorption process continuously opens the automatic valves 6 and 10 of the adsorption tower 20 to perform the adsorption process to store the product nitrogen components in the product storage tank, while the adsorption tower 21 is a manual valve of the product storage tank. (28) and the automatic valve 18 are opened to clean the inside of the tower with the product cleaning gas, and the air is discharged through the automatic valve 17 and the silencer (4).

균압공정은 자동밸브(6),(17),(18)및(10)를 닫고 균압 자동밸브(9)를 열어서 흡착공정이 끝난 흡착탑(20)의 압력이 상압탈착 공정과 세정탈착 공정이 끝난 흡착탑(21)으로 압력 이동하며, 이 때 흡착탑(20)의 상부에 잔류하고 있는 질소성분을 흡착탑(21)에서 회수하고 압력균등화 하여 이루어 진다.The pressure equalizing step is to close the automatic valves (6), (17), (18) and (10), and open the equalizing pressure automatic valve (9) so that the pressure of the adsorption step 20, where the adsorption step is completed, is the normal pressure desorption step and the cleaning desorption step. The pressure is moved to the adsorption tower 21, and at this time, the nitrogen component remaining in the upper part of the adsorption tower 20 is recovered from the adsorption tower 21 and pressure equalization is performed.

축압공정은 자동밸브(9)를 닫고 자동밸브(18)를 열어서 제품탱크의 질소가스를 흡착탑(21)의 탑내를 축압시키므로 탑 내의 흡착공정에 들어가기 전에 흡착탑의 상부의 산소성분을 가능한 하부쪽으로 이동시켜 이루어 지며, 제품의 순도 및 제품회수율 향상을 도모할 수 있다.In the pressure storing process, the automatic valve 9 is closed and the automatic valve 18 is opened to accumulate nitrogen gas in the product tank in the column of the adsorption tower 21. Therefore, the oxygen component of the upper part of the adsorption tower is moved as low as possible before entering the adsorption process in the tower. It can be made by improving the purity and product recovery rate of the product.

상압탈착공정은 흡착탑(20) 탑내에 흡착된 산소, 탄산가스, 수분 등을 자동밸브(7)를 열어서 소음기(4)를 통해서 대기 방출하여 이루어 진다.The atmospheric desorption process is performed by releasing oxygen, carbon dioxide, moisture, etc. adsorbed in the adsorption tower 20 to the atmosphere through the silencer 4 by opening the automatic valve 7.

본 발명의 질소 제조방법은 상기와 같은 공정으로 흡착탑(20)및(21)을 번갈아서 흡착, 탈착, 균압, 축압을 반복하여 실시하여 제품질소를 연속적으로 제조할 수 있다.In the nitrogen production method of the present invention, product nitrogen can be continuously produced by repeatedly performing adsorption, desorption, equalization, and accumulating by alternating adsorption towers 20 and 21 in the same process as described above.

본 발명의 질소 제조방법은 흡착공정에서 흡착탑에 충진되어 있는 탄소분자체는 산소를 선택적으로 흡착하고 배기되는 농축질소를 제품탱크에 포집하여 제품으로 회수하고, 산소로 포화된 흡착탑은 먼저 대기압으로 상압탈착한 다음에 제품질소로 세정하여 재생한다.In the nitrogen production method of the present invention, the carbon molecular sieve filled in the adsorption tower in the adsorption process selectively absorbs oxygen and collects the concentrated nitrogen exhausted in the product tank and recovers the product, and the adsorption tower saturated with oxygen is first subjected to atmospheric pressure desorption to atmospheric pressure. Then, it is washed with product nitrogen and regenerated.

또한, 흡착공정 후 상부의 잔류 질소성분은 탈착공정이 끝난 탑과 연결하여 잔류 질소성분을 회수하여 제품위 순도 및 회수율의 향상을 도모한다.In addition, the residual nitrogen component of the upper part after the adsorption process is connected to the tower after the desorption process to recover the residual nitrogen component to improve the purity and recovery rate of the product.

실시예Example

도1에 도시된 본 발명의 질소 제조장치를 사용하여 공기로부터 질소의 제조를 본 발명의 질소 제조방법에 따라 실시하였다.Production of nitrogen from air using the nitrogen production apparatus of the present invention shown in Figure 1 was carried out according to the nitrogen production method of the present invention.

공기중의 수분을 제거하기 위해 에어 드라이어 및 흡착탑의 하부에는 활성알루미나를, 상부에는 탄소분자체로 충진하였으며, 흡착탑(20)및(21)의 내경을 84.9 mm, 높이 2,600 mm 를 사용하였다.In order to remove moisture in the air, the bottom of the air dryer and the adsorption tower was filled with activated alumina, and the upper part was filled with carbon molecular sieve. The inner diameters of the adsorption towers 20 and 21 were 84.9 mm and the height 2,600 mm.

한 탑 당 흡착제 충진량은 알루미나 1.7 kg, 탄소분자체 8.7 kg 이었다.The adsorbent filling amount per tower was 1.7 kg of alumina and 8.7 kg of carbon molecular sieve.

상기의 실험장치를 사용하여 원료공기의 압력을 6 내지 7 kg/cm2G, 유량을 66.0 ℓ/min 사용하고, 운전반싸이클 시간은 120 초로써 실시한 결과 99.9 % 의 제품질소를 17.5 ℓ/min 생산하고 회수율 34 % 을 얻었다.Using the above experimental device, the raw material air pressure was 6 to 7 kg / cm 2 G, the flow rate was 66.0 ℓ / min, and the operating cycle time was 120 seconds. It produced and obtained 34% recovery.

상기 조건과 같은 조건으로 제품질소순도 99.9 % 를 유지하고 제품질소량 13.0 ℓ/min 을 생산하는데 회수율 25.5 % 을 얻었다.Under the same conditions as above, the product nitrogen purity was maintained at 99.9%, and the yield was 25.5% to produce 13.0 L / min of product nitrogen.

비교예Comparative example

실시예와 같은 동일한 설비를 이용하여 상압탈착 공정에서 제품질소 가스로 탑 내를 세정하고, 축압공정을 생략하여 실시예와 같은 공정에서 공기로부터 질소를 분리했다. 그 결과 제품질소순도 99.9 % 일 때 제품질소 회수율 32 % 을 얻었고, 제품질소순도 99.99 % 일 때 제품질소 회수율 23 % 을 얻었다.The same equipment as in Example was used to clean the inside of the column with product nitrogen gas in the atmospheric desorption process, and the pressure storing step was omitted to separate nitrogen from the air in the same process as in Example. As a result, the product nitrogen recovery was 32% when the product nitrogen purity was 99.9%, and the product nitrogen recovery was 23% when the product nitrogen purity was 99.99%.

본 발명의 질소 제조방법 및 장치에서는 상압탈착 공정인 탑과 제품질소 탱크사이에 자동밸브를 설치하여 상압탈착시에 제품질소 세정가스가 대기로 방출되지 않으므로 제품회수율 향상은 물론 최적치의 세정가스를 도입하므로써 제품질소 순도를 일정하게 유지할 수 있다.In the nitrogen production method and apparatus of the present invention, an automatic valve is installed between the tower and the product nitrogen tank, which is an atmospheric pressure desorption process, so that the product nitrogen cleaning gas is not discharged to the atmosphere during atmospheric pressure desorption, thereby improving the product recovery rate and introducing an optimal cleaning gas. In this way, the product nitrogen purity can be kept constant.

그리고 균입공정에서 공급하는 측의 흡착탑 상부와 공급받는 측의 흡착탑 상부를 연결하여 공급하는 측 흡착탑 상부의 질소성분이 공급받는 측의 흡착탑 상부로 이동되므로 탑 내부 가스의 흐름이 바뀌지 않고, 또한 흡착탑 상부를 제품질소로 축압하므로 제품질소와 탑 내에 잔류하는 산소성분과의 물질이동을 최대로 용이하게 하여 흡착공정에 들어가기 전에 흡착탑 상부의 산소성분을 가능한 하부쪽으로 이동시키므로 제품의 순도 및 제품회수율 향상을 도모할 수 있다.In addition, since the nitrogen component of the upper part of the adsorption tower connected to the upper part of the adsorption tower of the supply side and the upper side of the adsorption tower of the supply side is moved to the upper part of the adsorption tower of the receiving side, the flow of gas inside the tower does not change, and the upper part of the adsorption tower By accumulating the product with nitrogen, it facilitates the material movement between the product nitrogen and the oxygen component remaining in the tower to the maximum, and moves the oxygen component of the upper part of the adsorption column to the lower part as possible before entering the adsorption process, thereby improving the purity and product recovery rate of the product. can do.

Claims (2)

흡착공정, 상압탈착공정, 세정탈착공정, 균압공정, 축압공정 및 상압탈착공정으로 이루어 지며, 상기 흡착공정은 공기압축기(1)에서 소정압력으로 압축된 원료공기가 필터(2)를 거쳐서 공기 드라이어(3)에서 제습, 냉각되어 자동밸브(6)를 거쳐서 흡착탑(20)으로 도입되어 산소, 탄산가스, 수분은 흡착하고 흡착되지 않는 제품질소성분은 자동밸브(10)를 거쳐서 제품탱크(5)에 저장되며, 상기 상압탈착공정은 흡착탑(21) 탑내에 흡착된 산소, 탄산가스, 수분 등을 자동밸브(17)를 열어서 소음기(4)를 통하여 대기 방출하여 이루어 지고, 상기 세정탈착공정은 흡착탑(20)의 자동밸브(6)및(10)를 계속하여 열어서 흡착공정을 하여 제품질소 성분을 제품탱크에 저장하고, 반면에 흡착탑(21)은 제품탱크의 수동밸브(28)와 자동밸브(18)를 열어서 제품세정 가스로 탑내를 세정하고 자동밸브(17)와 소음기(4)를 통하여 대기방출 하여 이루어 지며, 상기 균압공정은 자동밸브(6),(17),(18)및(10)를 닫고 균압 자동밸브(9)를 열어서 흡착공정이 끝난 흡착탑(20)의 압력이 상압탈착 공정과 세정탈착 공정이 끝난 흡착탑(21)으로 압력 이동하며, 이 때 흡착탑(20)의 상부에 잔류하고 있는 질소성분을 흡착탑(21)에서 회수하고 압력균등화 하고, 상기 축압공정은 자동밸브(9)를 닫고 자동밸브(18)를 열어서 제품탱크의 질소가스를 흡착탑(21)의 탑내를 축압시키므로 탑 내의 흡착공정에 들어가기 전에 흡착탑의 상부의 산소성분을 가능한 하부쪽으로 이동시켜 이루어 지며, 상기 상압탈착공정은 흡착탑(20) 탑내에 흡착된 산소, 탄산가스, 수분 등을 자동밸브(7)를 열어서 소음기(4)를 통해서 대기 방출하여 이루어 지는 압력변동흡착식 질소 제조방법.It consists of adsorption process, atmospheric desorption process, cleaning desorption process, pressure equalizing process, accumulating process and atmospheric pressure desorption process, wherein the adsorption process is carried out through the filter (2) where the raw air compressed at a predetermined pressure in the air compressor (1) is passed through the filter (2). The product nitrogen (3) is dehumidified and cooled and introduced into the adsorption tower (20) through the automatic valve (6) to adsorb oxygen, carbon dioxide, and water, and the non-adsorbed product nitrogen components through the automatic valve (10). The atmospheric pressure desorption process is performed by releasing oxygen, carbon dioxide, and moisture adsorbed in the adsorption tower 21 into the air through the silencer 4 by opening the automatic valve 17. The cleaning desorption process is performed by the adsorption tower. The automatic valves (6) and (10) of (20) are continuously opened to perform the adsorption process to store the product nitrogen components in the product tank, while the adsorption tower 21 is a manual valve 28 and an automatic valve (in the product tank). 18) Open and wash the inside of the tower with product cleaning gas. The air is discharged through the automatic valve 17 and the silencer 4, and the equalizing process is performed by closing the automatic valves 6, 17, 18 and 10, and opening the equalizing automatic valve 9. The pressure of the adsorption tower 20 after the adsorption process is moved to the adsorption tower 21 where the atmospheric pressure desorption process and the cleaning desorption process are completed. At this time, the nitrogen component remaining in the upper portion of the adsorption tower 20 is recovered from the adsorption tower 21. The pressure accumulating process closes the automatic valve 9 and opens the automatic valve 18 to accumulate the nitrogen gas in the product tank in the column of the adsorption tower 21 so that the oxygen in the upper part of the adsorption tower before entering the adsorption process in the tower. It is made by moving the components to the lower side as possible, the atmospheric pressure desorption process is the pressure that is released through the silencer (4) by opening the automatic valve (7) of oxygen, carbon dioxide, water, etc. adsorbed in the adsorption tower (20) tower Variable adsorption nitrogen production method. 제1항에 있어서,The method of claim 1, 상기와 같은 공정으로 흡착탑(20)및(21)을 번갈아서 흡착, 탈착, 균압, 축압을 반복하여 실시하여 제품질소를 연속적으로 제조하는 질소 제조방법.Nitrogen production method for continuously producing the product nitrogen by repeatedly performing the adsorption, desorption, equalization, accumulator alternately adsorption tower (20) and (21) in the same process as described above.
KR1019980047267A 1998-11-05 1998-11-05 Pressure and apparatus for nitrogen production by pressure swing adsorption KR100275858B1 (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100824025B1 (en) * 2007-11-14 2008-04-21 주식회사 예성이엔지 Nitrogen generator
KR101354905B1 (en) * 2012-03-21 2014-01-24 한국에너지기술연구원 Continuous oxygen separation method and apparatus using oxygen selective sorbent
KR101498269B1 (en) * 2014-08-18 2015-03-05 주식회사 코더엔지니어링 Nitrogen generator
KR20200018042A (en) * 2018-08-10 2020-02-19 주식회사 젠스엔지니어링 Method of Removing Argon and Concentrating Nitrogen by Adsorbing and Separating Nitrogen from Gas Mixture of Argon and Nitrogen or Air
CN112723324A (en) * 2021-01-26 2021-04-30 东南大学 Method and device for producing oxygen by air separation based on pressure swing adsorption nitrogen production and chemical chain

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100824025B1 (en) * 2007-11-14 2008-04-21 주식회사 예성이엔지 Nitrogen generator
KR101354905B1 (en) * 2012-03-21 2014-01-24 한국에너지기술연구원 Continuous oxygen separation method and apparatus using oxygen selective sorbent
US9149758B2 (en) 2012-03-21 2015-10-06 Korea Institute Of Energy Research Continuous oxygen production method and continuous oxygen adsorption and desorption device using oxygen adsorbing agent
KR101498269B1 (en) * 2014-08-18 2015-03-05 주식회사 코더엔지니어링 Nitrogen generator
KR20200018042A (en) * 2018-08-10 2020-02-19 주식회사 젠스엔지니어링 Method of Removing Argon and Concentrating Nitrogen by Adsorbing and Separating Nitrogen from Gas Mixture of Argon and Nitrogen or Air
CN112723324A (en) * 2021-01-26 2021-04-30 东南大学 Method and device for producing oxygen by air separation based on pressure swing adsorption nitrogen production and chemical chain

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