CN1030375C - Modified molecular sieve adsorber for sulfur hexafluoride gas purification and its process - Google Patents
Modified molecular sieve adsorber for sulfur hexafluoride gas purification and its process Download PDFInfo
- Publication number
- CN1030375C CN1030375C CN 92112229 CN92112229A CN1030375C CN 1030375 C CN1030375 C CN 1030375C CN 92112229 CN92112229 CN 92112229 CN 92112229 A CN92112229 A CN 92112229A CN 1030375 C CN1030375 C CN 1030375C
- Authority
- CN
- China
- Prior art keywords
- molecular sieve
- absorber
- adsorbent
- type
- ion
- 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 - Lifetime
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The present invention relates to a modified A and X molecular sieve absorber for sulfur hexafluoride gas purification, which is modified by A molecular sieves or X molecular sieves of Ca ion pairs or Mg ion pairs and Li ion pairs or K ion pairs. In the process of preparing the absorber, sodium cellulose or sesbania powder is added as a structural adjusting agent of an adhesive and the absorber. Simultaneously, before calcination, silicate solution is used for immersion. The absorber is used for SF6 electrical equipment. The present invention effectively eliminates various poisonous gases produced in the operation of the equipment and in SF6 gases, prolongs the service life of the equipment, and avoids toxic hazard to maintainers. In addition, the absorber has the advantages of weak adsorption capability for the SF6 gases, strong adsorption capability for the poisonous gases and water, high speed, high anti-pressure strength, good abrasive resistance performance and long-term use.
Description
The present invention relates to a kind of adsorbent and preparation method thereof, specifically a kind ofly be used to remove SF
6In the electric equipment, SF
6By the hypertoxic low-fluorine sulfide impurities that produces after arcing or the spark discharge, the adsorbent of acidic materials and moisture content etc. and its preparation method.This adsorbent also is applicable to any system with above-mentioned gas, as industrial production SF
6Gas cleaning etc.
The sulfur hexafluoride electric equipment be a kind of have nontoxic, insulating capacity is strong, arc extinguishing waits the electric equipment of excellent performance rapidly.Yet SF
6The impurity of in manufacture process, leaving over and under the high temperature action of electric arc, the micro-low-fluorine sulfide impurities that decomposes by electrolysis and ionization, all belong to hypertoxic gas, the infringement human lung, the serious harm operator ' s health, and when minor amount of water existed, these low-fluorine sulfides decomposed generation HF, SO gradually
2And H
2SO
3Deng strong corrosive material, not only harmful, and the heavy corrosion electric equipment, influence the electric equipment performance.All adopt both at home and abroad at present and in electric equipment, place adsorbent to remove the method for objectionable impurities gas.Normally used adsorbent has activated alumina and synthetic zeolite class.So far, relevant reported in literature biases toward the low-fluorine sulfide toxicity test more and measures SF both at home and abroad
6Impurity content standard, and to adsorbent preparation, adsorption capability of different absorbate and to remove the research reports such as effect of above-mentioned impurity less.As at Elekfrotech, oh2 1979 68(4), 216-20 has reported when the power circuit switch disconnects, and uses Al
2O
3Absorption SF
6The toxicity low-fluorine sulfide that decompose to generate is at Enorgetlle 1976(11), 13-14(Rnss) reported with Polysorob and adsorbed SF
6The low-fluorine sulfide that decomposes.Inventor of the present invention once proposed to utilize the 5A of modification and LiX mixed molecules sieve adsorbant (CN85102711) to remove SF
6In the electric equipment after arcing and spark discharge, SF
6The hypertoxic low-fluorine sulfide gas that decomposition and ionization produce.The objective of the invention is on the basis of CN85102711 technology, provide a kind of and be adapted at a large amount of SF
6Gas exists down, more can remove SOF effectively
2, SO
2, HF and S
2F
10The adsorbent of molecular sieve of toxic gases such as O.This adsorbent also can be used for industrial production SF simultaneously
6Low-fluorine sulfide in the gas, impurity such as sour gas and moisture content.
Technology provided by the present invention once proposed to carry out on (CN85102711) technical foundation improved present inventors.Because at SF
6Gas behind electric arc and electrion, divide vent one's spleen in key component be SOF
2, SO
2And HF
6Exist.For adapting at a large amount of SF
6Gas exists down, removes above-mentioned molecular size, the impurity that character is different, this adsorbent is to mix with the A of different pore sizes and X molecular sieve, in conjunction with using different ions (Ca, Mg, K, Li etc.) effect of modification, thus adsorbent is had concurrently select shape absorption and to big molecule such as S
2F
10The energy of adsorption of O.Adsorbent specifically provided by the present invention is that the A that mixes with certain proportion and X type molecular sieve are as Main Ingredients and Appearance, utilize Ca or Mg and Li or K ion to carry out A or X molecular sieve that modification must contain Ca or the Mg of Li or K, add the mixed molecules sieve adsorbant that binding agent clay and sodium cellulosate or sesbania powder obtain as the pore structure mediator agent of binding agent and adsorbent, it forms percentage by weight: mixed molecular sieve: 70~85%, the modification ion, Ca or Mg and K or Li ion: 0.2~1.5%; All the other are clay.And in the mixed molecular sieve ratio of A type molecular sieve and X type molecular sieve be 1: 1~3(Wt).In above-mentioned adsorbent, its preferable molecular sieve modified process is to adopt Ca, K ion and A type, and Mg, Li ion and X type molecular sieve, the A type molecular sieve that promptly obtains containing K, Ca ion with contain Li, the X type molecular sieve of Mg ion mixes by a certain percentage and is made into mixed molecular sieve.The various physical properties of the adsorbent that is provided are: surface area 380~480m
2/ g, adsorpting water quantity are 20~24%(wt), and heap is made a gesture of measuring 0.7~0.75 gram/ml, particle size diameter 2-3mm, intensity>10kg/2.5mm and dry linting not.Be applicable to normal temperature, static state, dynamically absorption.Use this adsorbent can be with SF
6SOF in the gas
2, SO
2, S
2F
10O, SO
2F
2, the content that is removed to that impurity such as acid gas, moisture content are high-speed is<1ppm.
Preparation of adsorbent method provided by the present invention adopts following step:
1, gets 4A or NaX molecular sieve, in the soluble-salt solution that contains Ca or Mg and Li or K ion (chloride or nitrate), carry out ion-exchange respectively, make the Ca that contains Li or K or A type or the X type modified molecular screen of Mg.The ion-exchange ion exchange technique of molecular sieve is routinely carried out one or many under 80~95 ℃, after the ion-exchange, after filtration, be washed till no Cl or NO with deionized water
- 3Ion.
2, above-mentioned A type that contains Ca or Mg and Li or K or the X type molecular sieve that obtains mixed in 1: 1~3 ratios, add again by the clay of adsorbent weight 10~25% and in 0.2~1.5% ratio adding sodium cellulosate or the sesbania powder of molecular sieve and clay gross weight, mix moulding, drying.Drying can be carried out through air dry or oven dry in 20-150 ℃.
3, above-mentioned material after drying carries out drying through the process with 2 again with the silicate solutions dipping that contains 10-25%.
4, soak the dried material of silicate,, technology of the present invention is done explanation in further detail below by example after 400-650 ℃ of roasting more than 1 hour, can obtain adsorbent of the present invention.
Example 1: adsorbent preparation
(1) 10 gram LiNO
3, 0.5 the gram Mg(NO
3)
2Be dissolved in the 500ml deionized water, treat dissolving fully after, add 100 gram NaX type molecular sieves, under 80-95 ℃ of condition, stir exchange 3 hours, cross Shanghai, be washed till no NO with deionized water
- 3Till, Shanghai is also following dry 3 hours at 130 ℃.
(2) 20 gram CaCl
2, 2 gram KCl, soluble in water, add 100 gram 4A molecular sieves, in 80-95 ℃ of exchange 3 hours, cross Shanghai under stirring, be washed till no Cl
-Till.Sample was in 130 ℃ of dryings 3 hours.
(3) get the sample that 60 gram (1) kind methods make, get the sample that 40 gram (2) kind methods make, add 20 gram clays and 0.2 gram sesbania powder or sodium cellulosate mixing aftershaping, use 15-25%(Wt after drying or the roasting) silicate handle, 130 ℃ dry down in 550 ℃ of roastings 3 hours, makes finished product.
(4) get (1) 40 gram and (2) 60 grams, add 25 gram clays, add 0.2 gram sesbania powder mixed-forming, dry back made finished product in 3 hours in 550 ℃ of roastings.
Example 2: the performance test 1 of adsorbent,
(1) use-case 1(3) gained adsorbent 2 grams charge into 2.3 liters SF are housed
6Decomposition gas 5Kg/cm
2The absorption narrow-necked earthen jar in, carry out static state absorption, through the interval of certain hour, measure after absorption residual low-fluorine sulfide impurities content in the gas.
(2) for having adsorbed a period of time SF afterwards
6Divide (the SO that vents one's spleen
2, SOF
2, S
2H
10The O residual content adopts chromatography to detect.Mainly adopt its acid number of measurement for various sulfur-bearing components, the method for hydrolyzable fluoride, the result who measures the acid number gained is an aggregate data, SF
6Divide all kinds of catabolite major parts in venting one's spleen to be absorbed by alkali lye.Can comprehensively weigh adsorbent to various SF with this value
6The adsorption effect of catabolite, thereby the performance of mensuration adsorbent.
(3) SF
6Impurity content is SO among the raw material
22500PPm; SOF
2Be 140PPm; S
2F
10O is 270ppm; Acid number is that 887ppm(is in HF); The hydrolyzable fluoride is 438ppm.SO
2F
21080ppm。
Result of experiment is listed in table 1 and table 2.Table 1 is the adsorption capacity of adsorbent to acidic materials, finds out that with data in the table this adsorbent is very fast to the adsorption rate of acidic materials, only 887PPm can be reduced to<5PPm with 48 hours.The hydrolyzable fluoride is reduced to<2PPm by 438PPm.It is very short that adsorbate reaches equilibration time.
Table 1 adsorption experiment result
Absorption back residual impurity content PPm(V)
The adsorption time acid number is (with HF hydrolyzable fluoride
(hour) meter PPm) (SOF
2, HF, SF
4) ppm
0 887 438
6 26 7
12 9 2
24 6 2
Table 2 adsorption experiment result 2
Adsorption time (hour) absorption back residual impurity content PPm(V)
SO
2SOF
2S
2F
10O
0 2500 140 270
6 388 1 152
14 88 1 128
30 28 1 100
48 4 1 7
Claims (3)
1, a kind of sulfur hexafluoride gas purification adsorbent of molecular sieve, it is characterized in that molecular sieve is to contain the Ca of Li or K or A type and two kinds of molecular sieves mixing of the X type molecular sieve composition of Ma, the percentage by weight of its composition is: molecular sieve: 70~85%, Ca or Mg and Li or K ion are 0.2~1.5%, and all the other are clay; A type in its molecular sieve: the weight ratio of X type is 1: 1~3.
2,, it is characterized in that molecular sieve adopts the CaA type molecular sieve that contains K to mix by a certain percentage with the MgX type molecular sieve that contains Li according to the described adsorbent of claim 1.
3, a kind of being used for by the described preparation of adsorbent method of claim 1, it comprise adopt ion exchange technique with modification ion-exchange to molecular sieve, the adding additives moulding, the drying and roasting process is characterized in that:
(1) cellulose or the sesbania powder of adding mixed material total amount 0.2~1.5% before moulding;
(2) material floods with the silicate solutions that contains 10~25%, and then carries out drying and roasting behind shaping and drying.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 92112229 CN1030375C (en) | 1992-12-19 | 1992-12-19 | Modified molecular sieve adsorber for sulfur hexafluoride gas purification and its process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 92112229 CN1030375C (en) | 1992-12-19 | 1992-12-19 | Modified molecular sieve adsorber for sulfur hexafluoride gas purification and its process |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1088481A CN1088481A (en) | 1994-06-29 |
CN1030375C true CN1030375C (en) | 1995-11-29 |
Family
ID=4945839
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 92112229 Expired - Lifetime CN1030375C (en) | 1992-12-19 | 1992-12-19 | Modified molecular sieve adsorber for sulfur hexafluoride gas purification and its process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1030375C (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3356965B2 (en) * | 1997-06-20 | 2002-12-16 | 株式会社日立製作所 | SF6 gas recovery / purification processing apparatus and method |
CN100448525C (en) * | 2005-12-14 | 2009-01-07 | 李宏愿 | Molecular-sieve removing adsorbent of low-fluorine sulfide impurities and its production |
CN101820734A (en) * | 2010-04-01 | 2010-09-01 | 深圳市华测检测技术股份有限公司 | Equipment anticorrosion device in protective box and anticorrosion method |
CN103120928B (en) * | 2011-11-18 | 2014-06-25 | 国家电网公司 | Method for producing adsorbing agent for adsorbing subfluoride in sulfur hexafluoride |
CN102502692B (en) * | 2011-11-21 | 2013-09-25 | 烟台大学 | High-intensity molecular sieve and preparation method thereof |
CN102923673B (en) * | 2012-11-21 | 2014-10-01 | 四川众力氟业有限责任公司 | Purification technology for sulfur hexafluoride |
CN105642225B (en) * | 2014-11-10 | 2018-07-10 | 中国石油天然气股份有限公司 | Preparation method of adsorbent for deacidification of unsaturated acid ester |
CN112371080B (en) * | 2020-10-26 | 2023-03-28 | 松山湖材料实验室 | Mesoporous adsorption material and preparation method and application thereof |
CN112774654A (en) * | 2020-12-31 | 2021-05-11 | 杭州谱育科技发展有限公司 | Preparation method of adsorbent for selectively adsorbing sulfur dioxide |
-
1992
- 1992-12-19 CN CN 92112229 patent/CN1030375C/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
CN1088481A (en) | 1994-06-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1154536C (en) | Zeolite adsorbents, method for obtaining them and their use for removing carbonates from gas stream | |
CN1030375C (en) | Modified molecular sieve adsorber for sulfur hexafluoride gas purification and its process | |
Hutson et al. | Mixed cation zeolites: LixAgy‐X as a superior adsorbent for air separation | |
CA2085180C (en) | Nitrogen adsorption with a ca and/or sr exchanged lithium x-zeolite | |
CN1272074C (en) | Super fine active compound adsorptive indoor air purifying agent | |
Padilla-Ortega et al. | Adsorption of heavy metal ions from aqueous solution onto sepiolite | |
CN1292722A (en) | Decarbonating gas streams using zeolite adsorbents | |
CN107876005B (en) | Adsorbent for removing chlorinated pollutants and preparation method and application thereof | |
JP2002154821A (en) | Apparatus and method for purifying gas | |
JP3066430B2 (en) | Method for producing zeolite X-shaped compact | |
Hutson et al. | Structural effects on adsorption of atmospheric gases in mixed Li, Ag–X‐zeolite | |
CN1597736A (en) | Purification method of polyphenyl thioether | |
CN100448525C (en) | Molecular-sieve removing adsorbent of low-fluorine sulfide impurities and its production | |
US6780806B1 (en) | Lithium-based zeolites containing silver and copper and use thereof for selective absorption | |
CN113083259B (en) | Method for deeply purifying fluorine ions in water by utilizing strong-base resin-based neodymium-loaded nano composite material | |
US3242641A (en) | Purification of polymerizable olefin hydrocarbons | |
Shin et al. | Preparation of zeolitic adsorbents from waste coal fly ash | |
Astuti et al. | The adsorption of lead from aqueous solutions using coal fly ash: effect of crystallinity | |
CN107344062A (en) | A kind of desulfurizing agent, its preparation method and application | |
CN85102711A (en) | Severe toxicity molecular-sieve removing adsorbent of low-fluorine sulfide impurities and preparation thereof | |
CN113083223A (en) | Adsorption dehydrating agent for electronic grade gas and preparation method thereof | |
WO2000040332A1 (en) | Lithium-based zeolites containing silver and copper and use thereof for selective adsorption | |
CN113278204A (en) | VOC adsorption filler, preparation method thereof and polyolefin composite material | |
CN113117639A (en) | Modified molecular sieve adsorbent and preparation method and application thereof | |
CN1115296C (en) | Method of eliminating organic amine from molecular sieve or its composition |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C15 | Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993) | ||
OR01 | Other related matters | ||
C17 | Cessation of patent right | ||
CX01 | Expiry of patent term |
Expiration termination date: 20121219 Granted publication date: 19951129 |