CN1178768A - Process for preparing high purity nitrogen by deep purification fo coarse nitrogen and technological flow - Google Patents
Process for preparing high purity nitrogen by deep purification fo coarse nitrogen and technological flow Download PDFInfo
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- CN1178768A CN1178768A CN 96119471 CN96119471A CN1178768A CN 1178768 A CN1178768 A CN 1178768A CN 96119471 CN96119471 CN 96119471 CN 96119471 A CN96119471 A CN 96119471A CN 1178768 A CN1178768 A CN 1178768A
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Abstract
According to oxygen content in coarse nitrogen, hydrogen exceeding stoichiometric amount by 200-500 ppm is added. In the first stage purifier, under the action of noble metal Pd and/or Pt deoxidizing catalyst, oxygen content in nitrogen is reduced to below 1 ppm, and in the second stage purifier, under the action of noble metal Pd and MnO catalyst, hydrogen content is reduced to below 1 ppm, so as to obtain high-purity nitrogen with oxygen and hydrogen content below 1 ppm. The said technological process is especially suitable for purification of coarse nitrogen with oxygen content as high as 0.5% or inert gas.
Description
The present invention relates to a kind of method and technical process of producing high purity nitrogen from the thick nitrogen deep purifying that contains hyperoxia amount (～0.5%).Specifically, the thick nitrogen of the first step is excessive hydrogenation earlier, under the effect that contains precious metals pd and/or Pt dehydrogenation catalyst, removes oxygen in the nitrogen, and the nitrogen that contains excessive hydrogen then contains precious metals pd/manganese oxide regulating catalyst through second section, and excessive hydrogen is removed, and obtains O
2, H
2The high purity nitrogen of＜1ppm.
The high pure nitrogen body is widely used in the production process of petrochemical complex, chemical industry, electronic industry, metallurgical industry and building materials industry as the shielding gas in producing.The preparation of high purity nitrogen in the past adopts the empty method of dividing of deep cooling to produce usually, but because the investment of deep cooling air separation plant is huge, and the energy consumption height only is suitable for the production (＞10000M of large-scale high purity nitrogen
3/ hr), the purity nitrogen production of centering, hour scale is non-remunerative economically.
The carbonaceous molecular sieve making nitrogen by pressure swing adsorption is the seventies new developing technology, compares with molten cold nitrogen production by air separation method, and this technology is simple with its equipment, less investment, simple to operate, low power consumption and other advantages, the nitrogen production of centering, hour scale is more reasonable economically, is popular in users.Unique shortcoming of making nitrogen by pressure swing adsorption is that nitrogen gas purity is not too high, generally at 99.5% (0.5%O
2), in most cases, need further to purify, can be used for production process.At present, thick nitrogen deoxidation is mainly catforming, promptly adds excessive 0.2～5.0% hydrogen in smart nitrogen, under the effect of catalyzer such as palladium/aluminum oxide, residual oxygen in the nitrogen is removed.With the purifying method of above-mentioned catalyst removal oxygen, the oxygen level of its finished product gas is 0.2～10ppm, and the hydrogen residual volume surpasses 0.2% in the nitrogen, is high purity nitrogen so be far from being, and can only be used for the industry that thermal treatment etc. needs hydrogen.
Thick nitrogen purifies the general oxide compound absorption process of appraising at the current rate that adopts of the another kind of method that removes oxygen, and carbon burning consumes method.Absorption process reductor commonly used has manganese oxide (MnOx), silver suboxide (Ag
2O), cupric oxide (CiOx) (referring to Wu Yanmin " purification for gas " 23,1983, National Defense Industry Press).5～15 milliliters of the former general every gram reductor deoxidations, because thick nitrogen oxygen level height, so need a large amount of reductors, treating plant is huge, and is more uneconomical economically.Though latter's deoxidation amount is big, belongs to expendable, and 320～900 ℃ of uses, and produce new impurity CO and CO
2Up to now, the purification that contains the thick nitrogen of hyperoxia amount is the difficult problem in the gas sweetening, and Shang Weiyou rational technology is economically solved.
The purpose of this invention is to provide a kind of economy, be suitable for extensive use, is method for gas purification and the technical process that unstripped gas is produced high purity nitrogen with thick nitrogen.
Adopt in the present invention the applicant's early development contain precious metals pd and/or Pt dehydrogenation catalyst (number of patent application 96115578.7) but and not only can inhale hydrogen but also oxygen uptake contain precious metals pd/manganese oxide regulating catalyst, it is high purity nitrogen with thick nitrogen deep purifying that technical process (seeing accompanying drawing 1) divides two sections.In first section cleaner, the thick excessive hydrogenation of nitrogen, under the effect that contains precious metals pd and/or Pt dehydrogenation catalyst, the hydrogen-oxygen catalyzed reaction generates water and removes deoxidation.Remaining hydrogen in the nitrogen after first section purification contains precious metals pd/manganese oxide regulating catalyst reactor adsorbing and removing by second section, obtains H
2, O
2The high pure nitrogen of＜1ppm.Second section cleaner contains precious metals pd/manganese oxide purification reactor by two and forms, switch to use, i.e. and reactor hydrogen in inhaling hydrogen purification nitrogen, another reactor is then logical to contain the thick nitrogen oxidation regeneration of oxygen, hockets operate continuously.If high purity nitrogen requires the control moisture content, then need add conventional 5A molecular sieve purification process in the technical process and be dewatered.The condition of its scavenging process is: first section reactor reaction temperature is normal temperature～200 ℃, air speed 4000～8000hr
-1, oxygen level 0.05～3.0% in the nitrogen, and than excessive 200～500ppm, method of hydrotreating adopts pure hydrogen source or ammonia cracking hydrogen source to the hydrogenation amount by the metering of oxygen level in the thick nitrogen in the thick nitrogen.The dehydrogenation working temperature of two sections cleaners is 100～150 ℃, contains the regeneration of precious metals pd/manganese oxide regulating catalyst and carries out 100～250 ℃ of regeneration temperatures containing under the oxygen-nitrogen atmosphere.Purge gas pressure is 0.1～3MPa.
Below by embodiment invention is described further:
Example 1: the preparation (0.25%Pt+0.25%Pd/TiO that contains precious metals pd and/or Pt dehydrogenation catalyst
2+ Al
2O
3)
Get 100 milliliters of (0.025 gram Pd/ milliliter) aqueous solution+(the 0.025 gram Pt/ milliliter) aqueous solution 100 milliliters+60 ml waters and mix, again with 1000 gram column (TiO
2+ Al
2O
3) carrier pours in the above-mentioned solution, floods 4 hours, 80～120 ℃ of oven dry were got 100 milliliters of reduction of hydrazine hydrate of 50% 12 hours, and deionized water wash is to there not being Cl
-, pH=7 places 80～120 ℃ of baking ovens dry, places in the tube furnace under 500～750 ℃ of nitrogen atmosphere thermal treatment again 1～4 hour, is cooled to the logical nitrogen row hydrogen taking-up of chamber, chamber naturally.
Example 2: the performance of dehydrogenation catalyst
Because oxygen level is widely different in the various thick nitrogen, on φ 25mm continuous flow reaction unit, restrains and contain precious metals pd and/or the Pt dehydrogenation catalyst carries out the quantitative hydrogenation deoxidation evaluation of various oxygen concns with 80.Be equipped with the lecturer in the nitrogen than electrolysis hydrogen, oxygen, air speed 5000hr
-1, temperature of reaction is a normal temperature, follows the tracks of with the Nanjing GH-3 of analytical instrument factory type oxygen analyzer and detects, the results are shown in Table 1 for it.
Table 1 contain precious metals pd and/or the quantitative hydrogenation deoxidation performance of the thick nitrogen of Pt dehydrogenation catalyst oxygen level (ppm) hydrogenation amount (ppm) use temperature (℃) residual hydrogen amount (ppm) 2,000 4,000 25＜0.35000 10,000 25＜0.330000 60,000 25＜0.3
As can be seen from Table 1, during different oxygen, hydrogen, oxygen level are for measuring than under the condition, and this catalyzer also has the very high effect that removes oxygen.Example 3: nitrogen advanced purification process method
Table 2 contains precious metals pd and/or Pt dehydrogenation catalyst industry use properties nitrogen source oxygen level (%) hydrogenation amount (%) residual hydrogen amount (ppm) making nitrogen by pressure swing adsorption 0.5 1.02～1.05＜1
As can be seen from Table 2, contain precious metals pd and/or Pt dehydrogenation catalyst under the big air speed working conditions of industry, effect is still fine.
On said apparatus, nitrogen after the deoxidation carries out hydrogen with the 506HO regulating catalyst and absorbs, the working temperature of dehydrogenation cleaner is 100～150 ℃, pressure 0.6MPa, hydrogen before and after absorbing is followed the tracks of detection with the OHW-01 type and the CD-HY type hydrogen detector of Dalian Inst of Chemicophysics, Chinese Academy of Sciences's system, and the results are shown in Table 3 for it.
Table 3 506HO regulating catalyst dehydrogenation hydrogen richness (ppm) use temperature (℃) the residual hydrogen amount of applying pressure (MPa) (ppm) 200～500 100～150 0.6＜1
As can be seen from Table 3, after the 506HO regulating catalyst was inhaled hydrogen, the hydrogen residual quantity was less than 1ppm, and transformation is adsorbed thick nitrogen after above second cleaner purifies, and hydrogen, oxygen all become high purity nitrogen less than 1ppm.
Below accompanying drawing is described.Accompanying drawing 1 is the high purity nitrogen technical process of the thick nitrogen system of the present invention, among the figure:
The 1:506HO regulating catalyst is regenerated with thick nitrogen variable valve; 2: smart nitrogen variable valve; 3: join the hydrogen variable valve; 4～12:506HO modulation catalyst converter switching valve; 13: high purity nitrogen displacement valve; 14: the regenerant flow meter; 15. smart nitrogen under meter; 16: join the hydrogen under meter; 17: contain precious metals pd and/or Pt dehydrogenation catalyst deoxygenator; 18～19:506HO modulation catalyticreactor; 20:5A molecular sieve dehydration system.
The continuous flow reaction unit is adopted in above-mentioned technical process, catalyzer successive reaction and regeneration, its process stream trend is: the transformation adsorption of nitrogen through valve, under meter to mixing tank; Hydrogen or ammonia cracking hydrogen mix with nitrogen to mixing tank through valve, under meter, and mixed gas enters first class purification device 17, under the effect that contains precious metals pd and/or Pt dehydrogenation catalyst, and the normal temperature deoxidation.Nitrogen after the deoxidation enters one of them 506HO cleaner 18 of second cleaner, under the effect of 506HO regulating catalyst, and the absorbing and removing excessive hydrogen.Nitrogen after the dehydrogenation enters next stage and carries out conventional 5A molecular sieve dehydration, thereby obtains high purity nitrogen.In 506HO cleaner 18 dehydrogenations, to another 506HO cleaner 19,, after having regenerated, replace with high purity nitrogen with the oxygenous oxidation regeneration that carries out of transformation absorption, use in order to switching.
It is 60M that the thick nitrogen of above-mentioned reaction unit carries out tolerance
3/ hr
-1, pressure 0.6MPa contains precious metals pd and/or Pt dehydrogenation catalyst cleaner working temperature and is normal temperature～200 ℃, and the 506HO regulating catalyst inhales hydrogen and regeneration temperature is 100～250 ℃, O in the high purity nitrogen
2, H
2＜1ppm.
Claims (4)
1. one kind is used for the method that thick nitrogen deep purifying is produced high purity nitrogen, be characterized in the excessive hydrogenation of the thick nitrogen of the first step, remove oxygen containing under precious metals pd and/or the effect of Pt dehydrogenation catalyst, nitrogen contains precious metals pd/manganese oxide regulating catalyst through the second stage and removes residual hydrogen in the denitrification then, obtains O
2, H
2The method of the high purity nitrogen of＜1ppm.
2. in accordance with the method for claim 1, it is characterized in that the about 200～500ppm of the excessive hydrogenation of thick nitrogen, by containing precious metals pd and/or Pt dehydrogenation catalyst, oxyhydrogen reaction removes in the denitrification oxygen to 1ppm.
3. in accordance with the method for claim 1, it is characterized in that the nitrogen after the deoxidation, remove residual hydrogen through containing precious metals pd/manganese oxide regulating catalyst, its process is to contain precious metals pd/manganese oxide purification reactor by two to finish, one is used for removing nitrogen hydrogen, another then logical thick nitrogen oxidation regeneration alternately switches and carries out operate continuously.
4. according to claim 1,2,3 described methods is characterized in that containing precious metals pd and/or Pt reductor reaction conditions: normal temperature～200 ℃, air speed 4000～8000h
-1, oxygen level 0.05～3.0% in the nitrogen; Contain precious metals pd/manganese oxide regulating catalyst reaction conditions: 100～150 ℃, purge gas pressure 0.1～3.0MPa; Contain precious metals pd/manganese oxide regulating catalyst regeneration condition: 100～250 ℃, contain under the oxygen-nitrogen atmosphere and carry out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96119471A CN1067653C (en) | 1996-10-09 | 1996-10-09 | Process for preparing high purity nitrogen by deep purification fo coarse nitrogen and technological flow |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96119471A CN1067653C (en) | 1996-10-09 | 1996-10-09 | Process for preparing high purity nitrogen by deep purification fo coarse nitrogen and technological flow |
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| Publication Number | Publication Date |
|---|---|
| CN1178768A true CN1178768A (en) | 1998-04-15 |
| CN1067653C CN1067653C (en) | 2001-06-27 |
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ID=5125724
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96119471A Expired - Fee Related CN1067653C (en) | 1996-10-09 | 1996-10-09 | Process for preparing high purity nitrogen by deep purification fo coarse nitrogen and technological flow |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102515119A (en) * | 2011-12-05 | 2012-06-27 | 西安康本材料有限公司 | Method for regulating hydrogen content in high-pure nitrogen production process |
| CN104030257A (en) * | 2014-06-12 | 2014-09-10 | 鞍钢股份有限公司 | Control method of nitrogen purification system |
| CN104528665A (en) * | 2014-12-22 | 2015-04-22 | 本钢板材股份有限公司 | Method of purifying nitrogen |
| CN110980662A (en) * | 2019-12-28 | 2020-04-10 | 南京宝雅气体有限公司 | Catalytic deoxidation process for producing high-purity nitrogen |
| CN112279222A (en) * | 2020-11-12 | 2021-01-29 | 杭州汉德空分设备有限公司 | Pressure swing adsorption nitrogen making equipment |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN85102710A (en) * | 1985-04-01 | 1986-09-17 | 中国科学院大连化学物理研究所 | Platinum, Pd/TiO 2 deoxygenationcatalyst |
| US4931070A (en) * | 1989-05-12 | 1990-06-05 | Union Carbide Corporation | Process and system for the production of dry, high purity nitrogen |
| US5085674A (en) * | 1990-10-25 | 1992-02-04 | Union Carbide Industrial Gases Technology Corporation | Duplex adsorption process |
-
1996
- 1996-10-09 CN CN96119471A patent/CN1067653C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102515119A (en) * | 2011-12-05 | 2012-06-27 | 西安康本材料有限公司 | Method for regulating hydrogen content in high-pure nitrogen production process |
| CN104030257A (en) * | 2014-06-12 | 2014-09-10 | 鞍钢股份有限公司 | Control method of nitrogen purification system |
| CN104528665A (en) * | 2014-12-22 | 2015-04-22 | 本钢板材股份有限公司 | Method of purifying nitrogen |
| CN110980662A (en) * | 2019-12-28 | 2020-04-10 | 南京宝雅气体有限公司 | Catalytic deoxidation process for producing high-purity nitrogen |
| CN112279222A (en) * | 2020-11-12 | 2021-01-29 | 杭州汉德空分设备有限公司 | Pressure swing adsorption nitrogen making equipment |
| CN112279222B (en) * | 2020-11-12 | 2022-04-26 | 杭州汉德空分设备有限公司 | Pressure swing adsorption nitrogen making equipment |
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| Publication number | Publication date |
|---|---|
| CN1067653C (en) | 2001-06-27 |
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