TWI459998B - Diagnostic method of gas separation system - Google Patents

Diagnostic method of gas separation system Download PDF

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TWI459998B
TWI459998B TW101133015A TW101133015A TWI459998B TW I459998 B TWI459998 B TW I459998B TW 101133015 A TW101133015 A TW 101133015A TW 101133015 A TW101133015 A TW 101133015A TW I459998 B TWI459998 B TW I459998B
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distillation column
low pressure
pressure distillation
temperature
argon
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TW201410307A (en
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China Steel Corp
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氣體分離系統的診斷方法Diagnostic method for gas separation system

本發明是有關於一種診斷方法,特別是指一種氣體分離系統的診斷方法。The present invention relates to a diagnostic method, and more particularly to a diagnostic method for a gas separation system.

蒸餾塔的操作原理是利用混合物中,各組成物質沸點之差異,以及在汽/液相中分配率的不同,以進行物質純化的分離技術。而低溫蒸餾氣體分離系統,是工業上用以生產大量高純度的氮、氧及氫氣的主要方法。The operation principle of the distillation column is to utilize a separation technique in which the difference in boiling points of the constituent materials in the mixture and the distribution ratio in the vapor/liquid phase are different for the purification of the substance. The cryogenic distillation gas separation system is the main method used in the industry to produce a large amount of high-purity nitrogen, oxygen and hydrogen.

參閱圖1,現有低溫蒸餾氣體分離系統1包括一加壓蒸餾塔11、一第一熱交換器12、一第二熱交換器13、一低壓蒸餾塔14、一第一粗氬蒸餾塔15、一具有一第一冷凝器17的第二粗氬蒸餾塔16,一具有一第二冷凝器19的精氬蒸餾塔18。Referring to Fig. 1, a conventional cryogenic distillation gas separation system 1 includes a pressurized distillation column 11, a first heat exchanger 12, a second heat exchanger 13, a low pressure distillation column 14, and a first crude argon distillation column 15, A second crude argon distillation column 16 having a first condenser 17, and a fine argon distillation column 18 having a second condenser 19.

該加壓蒸餾塔11能使被冷卻到設定溫度的壓縮空氣100,形成流向該第一熱交換器12的高壓蒸氣111,與流向該第二熱交換器13之富含氧的液態空氣112。The pressurized distillation column 11 enables compressed air 100 cooled to a set temperature to form high pressure steam 111 flowing to the first heat exchanger 12 and oxygen-enriched liquid air 112 flowing to the second heat exchanger 13.

富含氧的液態空氣112是經該第二熱交換器13,形成流向該精氬蒸餾塔18的次待處理液131,以及分別流向該第一冷凝器17與該第二冷凝器19的待冷凝氣132。The oxygen-enriched liquid air 112 passes through the second heat exchanger 13 to form a secondary liquid to be treated 131 flowing to the fine argon distillation column 18, and flows to the first condenser 17 and the second condenser 19, respectively. Condensate 132.

高壓蒸氣111經該第一熱交換器12形成氮氣121,與流向該低壓蒸餾塔14的待處理液122,該待處理液122經該低壓蒸餾塔14形成氧氣141、流向該第一粗氬蒸餾塔15之富含氬的氬餾分142,以及回流至該第一熱交換器12的 第一回流氣體143。The high pressure steam 111 forms a nitrogen gas 121 through the first heat exchanger 12, and a liquid to be treated 122 flowing to the low pressure distillation column 14, the liquid to be treated 122 forms oxygen gas 141 through the low pressure distillation column 14, and flows to the first crude argon distillation. An argon-rich argon fraction 142 of column 15 and refluxed to the first heat exchanger 12 The first reflux gas 143.

氬餾分142經該第一粗氬蒸餾塔15與該第二粗氬蒸餾塔16形成流向該精氬蒸餾塔18的粗氬161。粗氬161與待處理液131經該精氬蒸餾塔18,形成氬氣181,與回流至該第二熱交換器13的第二回流氣體182。The argon fraction 142 forms a crude argon 161 flowing to the refined argon distillation column 18 via the first crude argon distillation column 15 and the second crude argon distillation column 16. The crude argon 161 and the liquid to be treated 131 pass through the purified argon distillation column 18 to form argon gas 181 and a second reflux gas 182 which is refluxed to the second heat exchanger 13.

但是,由於氬餾分142中所含之氮氣的沸點較低,並無法被第一冷凝器17所冷凝,因此,只要氬餾分142中所含之氮氣濃度超過1000ppm,即會使氮氣持續聚集於該第二粗氬蒸餾塔16的頂端,使得該第二粗氬蒸餾塔16之塔頂的壓力過高而造成上升氣流不足,不但分離效率差,甚至導致粗氬塔氮塞(nitrogen blocking),使該第二粗氬蒸餾塔16無法操作。However, since the nitrogen contained in the argon fraction 142 has a low boiling point and cannot be condensed by the first condenser 17, as long as the concentration of nitrogen contained in the argon fraction 142 exceeds 1000 ppm, nitrogen is continuously accumulated in the argon fraction 142. The top end of the second crude argon distillation column 16 is such that the pressure at the top of the second crude argon distillation column 16 is too high to cause insufficient rising gas flow, which not only causes poor separation efficiency, but also causes nitrogen blocking of the crude argon column. This second crude argon distillation column 16 is inoperable.

由上述可知,若為了避免發生粗氬塔氮塞,則必需嚴格控制氬餾分142中所含之氮氣的濃度,但是,目前對於氬餾分142中氮氣組成的分析技術尚未成熟,造成氬餾分142中氮氣濃度的分析結果變異大,難以有效應用。From the above, it is understood that the concentration of nitrogen contained in the argon fraction 142 must be strictly controlled in order to avoid the occurrence of a nitrogen argon plug in the crude argon column. However, the analysis technique for the nitrogen composition in the argon fraction 142 is not yet mature, resulting in the argon fraction 142. The analysis results of the nitrogen concentration are highly variable and difficult to apply effectively.

一般而言,低壓蒸餾塔14中組成的分佈與溫度分佈呈一對應關係,因此,現有多以低壓蒸餾塔14的溫度,反推低壓蒸餾塔14中氮氣組成以避免發生粗氬塔氮塞。但是,操作過程中,溫度隨操作條件變化不一,僅考慮低壓蒸餾塔14的溫度,並不足以完全反應低壓蒸餾塔14中的氮氣濃度,往往都是等到低壓蒸餾塔14的溫度低於設定值才會進行處理,但是此時粗氬塔氮塞已經發生。In general, the distribution of the composition in the low-pressure distillation column 14 has a correspondence with the temperature distribution. Therefore, the temperature of the low-pressure distillation column 14 is often reversed, and the nitrogen composition in the low-pressure distillation column 14 is reversed to avoid the occurrence of a nitrogen argon plug in the crude argon column. However, during operation, the temperature varies depending on the operating conditions, and only the temperature of the low pressure distillation column 14 is considered, and it is not sufficient to completely react the nitrogen concentration in the low pressure distillation column 14, and it is often waited until the temperature of the low pressure distillation column 14 is lower than the set. The value will be processed, but at this point the crude argon column nitrogen plug has occurred.

因此,本發明之目的,即在提供一種有效避免粗氬塔氮塞之氣體分離系統的診斷方法。Accordingly, it is an object of the present invention to provide a diagnostic method for a gas separation system that effectively avoids nitrogen plugging of a crude argon column.

於是,本發明氣體分離系統的診斷方法,適用於一氣體分離系統,該氣體分離系統包括一用以分離氧氣的低壓蒸餾塔,及一與該低壓蒸餾塔連通的第一粗氬蒸餾塔。Thus, the diagnostic method of the gas separation system of the present invention is applicable to a gas separation system comprising a low pressure distillation column for separating oxygen and a first crude argon distillation column in communication with the low pressure distillation column.

該診斷方法包含下列步驟:(A)擷取該低壓蒸餾塔內的溫度,(B)計算該低壓蒸餾塔的溫度變化速率,及(C)若該低壓蒸餾塔中的溫度持續降低,且該低壓蒸餾塔的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔的溫度。The diagnostic method comprises the steps of: (A) drawing the temperature in the low pressure distillation column, (B) calculating a temperature change rate of the low pressure distillation column, and (C) if the temperature in the low pressure distillation column is continuously lowered, and When the temperature change rate of the low pressure distillation column is greater than 0.01 ° C / min, the temperature of the low pressure distillation column is raised.

本發明的有益效果在於:利用該低壓蒸餾塔的溫度變化速率,反推低壓蒸餾塔中的氮氣濃度,且當該低壓蒸餾塔中的溫度持續降低,而該低壓蒸餾塔的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔的溫度,進而控制該低壓蒸餾塔之氬餾分中的氮氣濃度,避免發生粗氬塔氮塞。The beneficial effects of the present invention are: using the temperature change rate of the low pressure distillation column, pushing back the nitrogen concentration in the low pressure distillation column, and when the temperature in the low pressure distillation column is continuously decreased, and the temperature change rate of the low pressure distillation column is greater than 0.01 °C/min, the temperature of the low pressure distillation column is raised, and then the nitrogen concentration in the argon fraction of the low pressure distillation column is controlled to avoid the occurrence of a nitrogen argon plug in the crude argon column.

有關本發明之前述及其他技術內容、特點與功效,在以下配合參考圖式之一個較佳實施例的詳細說明中,將可清楚的呈現。The above and other technical contents, features and advantages of the present invention will be apparent from the following detailed description of the preferred embodiments.

參閱圖2、3,本發明氣體分離系統的診斷方法的較佳實施例,適用於如圖3所示的氣體分離系統3,該氣體分離系統3包括一加壓蒸餾塔31、一第一熱交換器32、一第二熱交換器33、一低壓蒸餾塔34、一第一粗氬蒸餾塔35、一具有一第一冷凝器361的第二粗氬蒸餾塔36,及一具有一第二冷凝器371的精氬蒸餾塔37。由於該氣體分離系統3 與圖1的現有技術相同,因此,在此不予多加贅述。Referring to Figures 2 and 3, a preferred embodiment of the diagnostic method of the gas separation system of the present invention is applicable to a gas separation system 3 as shown in Figure 3, the gas separation system 3 comprising a pressurized distillation column 31, a first heat An exchanger 32, a second heat exchanger 33, a low pressure distillation column 34, a first crude argon distillation column 35, a second crude argon distillation column 36 having a first condenser 361, and a second An argon distillation column 37 of condenser 371. Due to the gas separation system 3 It is the same as the prior art of FIG. 1, and therefore, no further details are provided herein.

該診斷方法,首先如步驟21所示,將一溫度感測器200設置於該低壓蒸餾塔34上,且每間隔一固定時間擷取一次該低壓蒸餾塔34內的溫度。In the diagnostic method, first, as shown in step 21, a temperature sensor 200 is disposed on the low pressure distillation column 34, and the temperature in the low pressure distillation column 34 is taken once every fixed time interval.

參閱圖4,並回顧圖3,該低壓蒸餾塔34具有相反的一塔頂341與一塔底342,及一介於該塔頂341與該塔底342間且與該第一粗氬蒸餾塔35相連接以抽出氬餾分340的氬餾分抽出口343,而該溫度感測器200與該氬餾分抽出口343間的距離,小於該溫度感測器200與該塔頂341間的距離。Referring to FIG. 4, and referring back to FIG. 3, the low pressure distillation column 34 has an opposite tower top 341 and a bottom 342, and a tower between the top 341 and the bottom 342 and the first crude argon distillation column 35. The argon fraction withdrawal port 343 is connected to extract the argon fraction 340, and the distance between the temperature sensor 200 and the argon fraction extraction port 343 is smaller than the distance between the temperature sensor 200 and the column top 341.

在此要特別說明的是,在正常操作條件下,該低壓蒸餾塔34愈接近塔底342的氮氣濃度就愈低,愈接近塔頂341的氮氣濃度愈高,但是,相對地愈接近塔底342的氬氣濃度愈高,因此,氬餾分抽出口343大多介於中間處。而將該溫度感測器200設置在鄰近該氬餾分抽出口343,雖然不是直接量測氬餾分340的溫度,但是仍可充分反應氬餾分340的溫度變化情形。實際使用時,該氬餾分抽出口343約是位於業界通稱該低壓蒸餾塔34之第38板的位置,而該溫度感測器200則是安裝在自第38板向上3~4個板數的位置。It should be particularly noted that under normal operating conditions, the lower the nitrogen concentration of the low pressure distillation column 34 near the bottom 342, the higher the nitrogen concentration near the top 341, but relatively closer to the bottom of the column. The higher the argon concentration of 342, the more the argon fraction extraction port 343 is interposed. While the temperature sensor 200 is disposed adjacent to the argon fraction extraction port 343, although the temperature of the argon fraction 340 is not directly measured, the temperature change of the argon fraction 340 can be sufficiently reacted. In actual use, the argon fraction extraction port 343 is located at the 38th plate of the low-pressure distillation column 34 in the industry, and the temperature sensor 200 is installed at a plate number of 3 to 4 plates from the 38th plate. position.

參閱圖2、3,接下來,如步驟22所示,計算該低壓蒸餾塔34的溫度變化速率。每間隔一固定時間擷取一次該低壓蒸餾塔34內的溫度有利於溫度變化速率的計算,且能正確掌握該低壓蒸餾塔34內的溫度變化情形。Referring to Figures 2 and 3, next, as shown in step 22, the rate of temperature change of the low pressure distillation column 34 is calculated. The temperature in the low pressure distillation column 34 is taken once every fixed time interval to facilitate the calculation of the temperature change rate, and the temperature change in the low pressure distillation column 34 can be correctly grasped.

最後,如步驟23所示,若該低壓蒸餾塔34中的溫度持續降低,且該低壓蒸餾塔34的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔34的溫度,使該低壓蒸餾塔34的溫度維持在-185℃~-187℃之間。Finally, as shown in step 23, if the temperature in the low pressure distillation column 34 continues to decrease and the temperature change rate of the low pressure distillation column 34 is greater than 0.01 ° C / min, the temperature of the low pressure distillation column 34 is raised to make the low pressure distillation The temperature of column 34 is maintained between -185 ° C and -187 ° C.

經理論與現場驗證可知,當氬餾分340中的氮氣濃度上升時,雖不會立即發生粗氬塔氮塞,但是大多都會伴隨著不利的結果,例如:產能或品質下降。According to theoretical and on-site verification, when the concentration of nitrogen in the argon fraction 340 rises, the nitrogen argon plug of the crude argon column does not immediately occur, but most of them are accompanied by unfavorable results, such as a decrease in productivity or quality.

但是,只要氬餾分340的溫度一低於氮氣濃度為1000ppm之氬餾分340的液化溫度,則一定會引發粗氬塔氮塞,所以,若該低壓蒸餾塔34中的溫度持續降低,且該低壓蒸餾塔34的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔34的溫度,以控制該低壓蒸餾塔34之氬餾分340中的氮氣濃度。以溫度變化速率大於0.01℃/min作為提升該低壓蒸餾塔34的溫度的分界,才能有充分的反應時間以提升該低壓蒸餾塔34的溫度,使該低壓蒸餾塔34的溫度維持高於氮氣濃度為1000ppm之氬餾分340的液化溫度,以避免發生粗氬塔氮塞,且溫度變化速率小於0.01℃/min也能維持產能或品質的穩定。However, as long as the temperature of the argon fraction 340 is lower than the liquefaction temperature of the argon fraction 340 having a nitrogen concentration of 1000 ppm, the nitrogen argon plug of the crude argon column is surely caused, so if the temperature in the low pressure distillation column 34 continues to decrease, and the low pressure The temperature change rate of the distillation column 34 is greater than 0.01 ° C / min, and the temperature of the low pressure distillation column 34 is raised to control the nitrogen concentration in the argon fraction 340 of the low pressure distillation column 34. At a temperature change rate of more than 0.01 ° C / min as a boundary for raising the temperature of the low pressure distillation column 34, sufficient reaction time can be obtained to raise the temperature of the low pressure distillation column 34 so that the temperature of the low pressure distillation column 34 is maintained higher than the nitrogen concentration. It is the liquefaction temperature of 1000 ppm of argon fraction 340 to avoid the occurrence of crude argon nitrogen plug, and the temperature change rate is less than 0.01 ° C / min to maintain the stability of production capacity or quality.

綜上所述,本發明氣體分離系統的診斷方法是利用該低壓蒸餾塔34的溫度變化速率,反推低壓蒸餾塔34中的氮氣濃度,已準確研判是否會發生粗氬塔氮塞,且當該低壓蒸餾塔34中的溫度持續降低,而該低壓蒸餾塔34的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔34的溫度,進而控制該低壓蒸餾塔34之氬餾分340中的氮氣濃度 ,避免發生粗氬塔氮塞,故確實能達成本發明之目的。In summary, the diagnostic method of the gas separation system of the present invention utilizes the temperature change rate of the low pressure distillation column 34 to reverse the nitrogen concentration in the low pressure distillation column 34, and has accurately determined whether a coarse argon column nitrogen plug will occur, and when The temperature in the low pressure distillation column 34 is continuously lowered, and the temperature change rate of the low pressure distillation column 34 is greater than 0.01 ° C / min, thereby raising the temperature of the low pressure distillation column 34, thereby controlling the argon fraction 340 of the low pressure distillation column 34. Nitrogen concentration In order to avoid the occurrence of a nitrogen argon plug in the crude argon column, the object of the present invention can be achieved.

惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,即大凡依本發明申請專利範圍及發明說明內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。The above is only the preferred embodiment of the present invention, and the scope of the invention is not limited thereto, that is, the simple equivalent changes and modifications made by the scope of the invention and the description of the invention are All remain within the scope of the invention patent.

21‧‧‧擷取該低壓蒸餾塔內的溫度21‧‧‧Draw the temperature in the low pressure distillation column

22‧‧‧計算該低壓蒸餾塔的溫度變化速率22‧‧‧ Calculate the rate of temperature change of the low pressure distillation column

23‧‧‧若該低壓蒸餾塔中的溫度持續降低,且該低壓蒸餾塔的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔的溫度23‧‧‧If the temperature in the low-pressure distillation column continues to decrease, and the temperature change rate of the low-pressure distillation column is greater than 0.01 ° C / min, the temperature of the low-pressure distillation column is raised

200‧‧‧溫度感測器200‧‧‧temperature sensor

3‧‧‧氣體分離系統3‧‧‧Gas Separation System

31‧‧‧加壓蒸餾塔31‧‧‧Pressure distillation tower

32‧‧‧第一熱交換器32‧‧‧First heat exchanger

33‧‧‧第二熱交換器33‧‧‧second heat exchanger

34‧‧‧低壓蒸餾塔34‧‧‧Low Pressure Distillation Tower

340‧‧‧抽出氬餾分340‧‧‧Extracted argon fraction

341‧‧‧塔頂341‧‧‧Tower

342‧‧‧塔底342‧‧‧Totto

343‧‧‧氬餾分抽出口343‧‧‧ argon fraction extraction

35‧‧‧第一粗氬蒸餾塔35‧‧‧First Crude Argon Distillation Tower

36‧‧‧第二粗氬蒸餾塔36‧‧‧Second crude argon distillation tower

361‧‧‧第一冷凝器361‧‧‧First condenser

37‧‧‧精氬蒸餾塔37‧‧‧ Fine Argon Distillation Tower

371‧‧‧第二冷凝器371‧‧‧second condenser

圖1是一示意圖,說明一現有的低溫蒸餾氣體分離系統;圖2是一流程圖,說明本發明氣體分離系統的診斷方法的較佳實施例;圖3是一示意圖,說明該診斷方法的較佳實施利所應用的氣體分離系統;及圖4是一示意圖,說明該溫度感測器的安裝位置。1 is a schematic view showing a conventional cryogenic distillation gas separation system; FIG. 2 is a flow chart showing a preferred embodiment of the diagnostic method of the gas separation system of the present invention; and FIG. 3 is a schematic view showing the comparison of the diagnostic method A gas separation system applied by a good implementation; and FIG. 4 is a schematic diagram showing the installation position of the temperature sensor.

21‧‧‧擷取一低壓蒸餾塔內的溫度21‧‧‧ Capture the temperature in a low pressure distillation column

22‧‧‧計算該低壓蒸餾塔的溫度變化速率22‧‧‧ Calculate the rate of temperature change of the low pressure distillation column

23‧‧‧若該低壓蒸餾塔中的溫度持續降低,且該低壓蒸餾塔的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔的溫度23‧‧‧If the temperature in the low-pressure distillation column continues to decrease, and the temperature change rate of the low-pressure distillation column is greater than 0.01 ° C / min, the temperature of the low-pressure distillation column is raised

Claims (3)

一種診斷方法,適用於一氣體分離系統,該氣體分離系統包括一低壓蒸餾塔,及一第一粗氬蒸餾塔,該診斷方法包含:(A)擷取該低壓蒸餾塔內的溫度;(B)計算該低壓蒸餾塔的溫度變化速率;及(C)若該低壓蒸餾塔中的溫度持續降低,且該低壓蒸餾塔的溫度變化速率大於0.01℃/min,則提升該低壓蒸餾塔的溫度。 A diagnostic method for a gas separation system comprising a low pressure distillation column and a first crude argon distillation column, the diagnostic method comprising: (A) drawing the temperature in the low pressure distillation column; Calculating a rate of temperature change of the low pressure distillation column; and (C) increasing the temperature of the low pressure distillation column if the temperature in the low pressure distillation column is continuously lowered and the rate of temperature change of the low pressure distillation column is greater than 0.01 ° C / min. 根據申請專利範圍第1項所述的診斷方法,其中,該步驟(A)是每間隔一固定時間擷取一次該低壓蒸餾塔內的溫度。 The diagnostic method according to claim 1, wherein the step (A) is that the temperature in the low-pressure distillation column is taken once every fixed time interval. 根據申請專利範圍第1項所述的診斷方法,其中,該低壓蒸餾塔具有相反的一塔頂與一塔底,及一介於該塔頂與該塔底間且與該第一粗氬蒸餾塔相連接的氬餾分抽出口,該步驟(A)是將一溫度感測器設置於該氬餾分抽出口與該塔頂間以擷取該低壓蒸餾塔內的溫度,且該溫度感測器與該氬餾分抽出口間的距離,小於該溫度感測器與該塔頂間的距離。 The diagnostic method according to claim 1, wherein the low pressure distillation column has an opposite top and a bottom, and a bottom between the top and the bottom and the first crude argon distillation tower a connected argon fraction withdrawal port, the step (A) is a temperature sensor is disposed between the argon fraction withdrawal port and the top of the column to extract the temperature in the low pressure distillation column, and the temperature sensor is The distance between the argon fraction withdrawal ports is less than the distance between the temperature sensor and the top of the tower.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0195065B1 (en) * 1984-09-26 1989-11-08 ERICKSON, Donald Charles Nitrogen production by low energy distillation
JP2000337766A (en) * 1999-05-21 2000-12-08 Boc Group Inc:The Method of and tower for distillation

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0195065B1 (en) * 1984-09-26 1989-11-08 ERICKSON, Donald Charles Nitrogen production by low energy distillation
JP2000337766A (en) * 1999-05-21 2000-12-08 Boc Group Inc:The Method of and tower for distillation

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