CN105085179A - Purification method of methanol for liquid chromatography-mass spectrometer - Google Patents

Purification method of methanol for liquid chromatography-mass spectrometer Download PDF

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CN105085179A
CN105085179A CN201410209273.7A CN201410209273A CN105085179A CN 105085179 A CN105085179 A CN 105085179A CN 201410209273 A CN201410209273 A CN 201410209273A CN 105085179 A CN105085179 A CN 105085179A
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methyl alcohol
mass spectrometer
purification
liquid chromatograph
methanol
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CN105085179B (en
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范文林
张群星
张怡
魏丽
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Shanghai Xingke High Purity Solvent Co Ltd
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Shanghai Xingke High Purity Solvent Co Ltd
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Abstract

The invention discloses a purification method of methanol for a liquid chromatography-mass spectrometer. The method is characterized in that impurities in a raw material methanol are removed through processes such as modified active carbon adsorption and the like so as to obtain methanol for a liquid chromatography-mass spectrometer. By the purification method of methanol for a liquid chromatography-mass spectrometer, methanol with purity being greater than or equal to 99.99 wt% can be obtained. The method meets high-purity requirement of a liquid chromatography-mass spectrometer. Therefore, methanol obtained after purification can be applied in the field of liquid chromatography-mass spectrometers, and the application range of methanol is broadened.

Description

The method of purification of liquid chromatograph-mass spectrometer methyl alcohol
Technical field
The present invention relates to solvent purification field, particularly a kind of method of purification of liquid chromatograph-mass spectrometer methyl alcohol.
Background technology
The separating power of chromatogram combines with mass spectrographic qualitative function by the on-line coupling of chromatography-mass spectroscopy, realizes complex mixture quantitative and qualitative analysis more accurately.And also simplify the pretreatment process of sample, make sample analysis easier.Chromatograph-mass spectrometer coupling comprises gas chromatography-mass spectrography and liquid chromatography mass coupling, and LC-MS and gas chromatography mass spectrometry complement one another, and analyzes compound of different nature.
Liquid chromatography mass combined instrument (liquidChromatographMassSpectrometer), being called for short LC-MS, is the high end instrument in Analysis of Organic Substances market.Organic components in organism testing sample can effectively be separated by liquid chromatography (LC), and mass spectrum (MS) to the organism separated analysis one by one, can obtain organic matter molecular mass, the information such as structure and concentration.LC-MS is Analysis of Organic Substances laboratory, medicine, food test room, the requisite analysis tools of department such as production process control, quality inspection.Need to use moving phase in LC organic components to be separated, conventional moving phase is the mixture of methyl alcohol, methyl alcohol, water and their different ratioss.As the solvent of moving phase, purity is higher, in sample, separating organic matters effect is better, and the phenomenon that the measured object ionization that the existence because of impurity can be avoided as much as possible to cause of the high solvent of purity is insufficient, particularly metal ion, with measured object complexing in mass spectroscopy, production Interference Peaks in mass spectrum, thus cause causing erroneous judgement to the isoparametric mensuration of molecular weight, greatly reduce the precision of liquid chromatograph-mass spectrometer measuring result.
Methyl alcohol, as a kind of solvent of excellent property, can dissolve multiple organic and inorganic and gaseous matter, but its purification is very difficult.Industrial synthesizing methanol almost all adopts the method for carbon monoxide pressurized catalysis hydrogenation, technological process comprises the operations such as gas making, cleaning up, methanol-fueled CLC and crude carbinol rectifying, containing the many organic impuritys produced in the course of processing in product, as various hydro carbons, heterocyclic arene etc., their boiling range is close with methyl alcohol, even if use very outstanding rectifying device, obtains highly purified solvent gradient methyl alcohol after also impurity can not being removed
Summary of the invention
The object of the invention is to overcome deficiency of the prior art, a kind of method of purification improving the liquid chromatograph-mass spectrometer methyl alcohol of methanol purity is provided.
For realizing above object, the present invention is achieved through the following technical solutions:
The method of purification of liquid chromatograph-mass spectrometer methyl alcohol, is characterized in that, comprises the steps:
A. material benzenemethanol is got, add potassium permanganate or superoxide wherein and stir, distill out methyl alcohol, the impurity containing double bond in removal material benzenemethanol is as impurity such as ethene, vinyl cyanide, prussic acid, propenal, methacrylonitrile, vinylcarbinol, oxazole, ethanamides.Wherein, superoxide includes but not limited to hydrogen peroxide.
B. add alkalimetal oxide (including but not limited to sodium oxide), alkali metal hydroxide (including but not limited to sodium hydroxide) or carbonate (including but not limited to sodium carbonate, sodium bicarbonate, salt of wormwood, saleratus) in the methyl alcohol distilled out in step a, pH value is adjusted in the scope of 7 ~ 8; Jolting, makes the acidic impurities in alkalimetal oxide, alkali metal hydroxide or carbonate and material benzenemethanol fully react, production precipitation of salts thing; After stratification, discard water layer, and the organic layer being dissolved with methyl alcohol is filtered, retain filtrate;
C. the sorbent material post above-mentioned filtrate passing into being equipped with modified activated carbon carries out adsorption treatment, for removing the organic compound of carbon-carbon double bonds in the material of the high degree of polarization formed in oxidising process and material benzenemethanol, as alkene, and heteroaromatic hydrocarbon etc.
D. by the methyl alcohol of step b gained with 0.5 ~ 30 column volume/hour flow velocity pass into that particle diameter is housed is that the sorbent material post of the ion exchange resin of 0.01 ~ 0.2cm carries out ion exchange treatment, remove the impurity such as aldehydes, metal ion, namely obtain the liquid chromatograph-mass spectrometer methyl alcohol of purity >=99.99% (wt).
Preferably, in described step a, while adding potassium permanganate or superoxide, add highly basic and basic oxide, as sodium hydroxide and calcium oxide, slow down the oxidisability of potassium permanganate, the acidic substance that neutralization oxidation simultaneously produces, adjust ph is in 8 ~ 14 scopes.
Preferably, in described step a, before adding potassium permanganate or superoxide, porous mass is added as zeolite, molecular sieve, activated carbon etc. in material benzenemethanol, stir 1 ~ 2 hour, make material benzenemethanol be attached to activated carbon surface, increase the contact area of potassium permanganate or superoxide and material benzenemethanol, improve oxidation efficiency.Oxygenant consumption can be reduced simultaneously, reduce methanol loss, improve methanol yield.
Preferably, also comprise step a ˊ, by adding reductive agent in the methyl alcohol to step a gained and stirring, distill out methyl alcohol; Described reductive agent is ferrous sulfate, sodium pyrosulfate, sodium bisulfite, Sodium phosphate dibasic, iron protoxide or sodium bicarbonate.Remove the excess oxide produced in oxidising process.
Preferably, in described step c, modified activated carbon is the activated carbon of surface attachment ethylenediamine tetraacetic acid (EDTA), aluminum oxide, aluminium hydroxide, nitric acid, trolamine or hypochlorite.The mass concentration of ethylenediamine tetraacetic acid (EDTA), aluminium hydroxide, nitric acid, trolamine or hypochlorite solutions is 5 ~ 30%; The particle diameter of activated carbon is 20 ~ 100 orders.
Preferably, in described step c, before filtrate passing into is equipped with the sorbent material post of modified activated carbon, first passes into and the sorbent material post that particle diameter is 20 ~ 100 orders, model is the molecular sieve of 3A or 4A is housed, remove moisture.
Preferably, methyl alcohol with 0.5 ~ 30 column volume/hour speed flow through the sorbent material post that molecular sieve is housed.
Preferably, in described steps d, the surface attachment of ion exchange resin has alcohol compound or acetonitrile; Described alcohols includes but not limited to methyl alcohol.
Preferably, also comprise step e, the methyl alcohol of adsorption treatment gained is carried out rectifying; Rectifying still Heating temperature is 68 ~ 75 DEG C, methanol liquid temperature 65 ~ 70 DEG C in still, distill out liquid temp and be 64 ~ 66 DEG C, control reflux ratio 8: 1 ~ 15:1.
The method of purification of liquid chromatograph-mass spectrometer methyl alcohol provided by the invention, after potassium permanganate oxidation, the methyl alcohol that ion-exchange obtains purity >=99.99% (wt) is carried out through modified active carbon adsorption and ion exchange resin, meet the high purity requirement of liquid chromatograph-mass spectrometer, the methyl alcohol that purification is obtained is applied to liquid chromatograph-mass spectrometer field, expands range of application.Method of purification provided by the invention, the production having filled up domestic high purity methanol is blank, reduces cost needed for import, alleviates the degree pind down by foreign technology simultaneously.Method of purification provided by the invention also has that energy consumption is low, production process is easy, stable, be applicable to the advantages such as suitability for industrialized production.
Embodiment
Below in conjunction with embodiment, the present invention is described in detail:
Embodiment 1
The method of purification of LC-MS analysis methyl alcohol, is characterized in that, comprises the steps:
A. get material benzenemethanol, add potassium permanganate wherein and carry out oxide treatment, the impurity of removal containing double bond is as impurity such as ethene, vinyl cyanide, prussic acid, propenal, methacrylonitrile, vinylcarbinol, oxazole, ethanamides.While adding potassium permanganate, add sodium hydroxide and calcium oxide, slow down the oxidisability of potassium permanganate, the acidic substance that neutralization oxidation simultaneously produces, adjust ph is 8.After oxide treatment, distill out methyl alcohol rapidly.
A ˊ. by adding reductive agent iron protoxide in the methyl alcohol to step a gained and stirring, distill out methyl alcohol.
B. in the methyl alcohol distilled out, add sodium carbonate by the pH regulator to 7 of solution, and jolting makes the acidic impurities in sodium carbonate and material benzenemethanol fully react, generate precipitation of salts thing; Stratification, discards water layer and precipitation, filters organic layer, retains filtrate.
C. by above-mentioned filtrate with 0.5 column volume/hour speed pass into the sorbent material post that particle diameter is 50 object 3A molecular sieves be housed, remove the moisture in organic layer further; After absorption, methyl alcohol water content control is ≤0.03%; Utilize molecular sieve to remove moisture after extraction in methyl alcohol in this step, as moisture content > 0.03% need change molecular sieve after proceed molecular sieve adsorption process again;
And then, by above-mentioned effluent liquid with 24 column volumes/hour speed pass into and surface attachment is housed has the sorbent material post of the modified activated carbon of edta solution to carry out adsorption treatment, for removing the unsaturated organic compound of oxide-based, arene, polar compound class and carbon-carbon double bonds as impurity such as heterocyclic arenes.Wherein, the particle diameter of activated carbon is 20 orders, and the mass concentration of edta solution is 5%.
D. by the methyl alcohol of step c gained with 0.5 column volume/hour speed pass into the sorbent material post that surface attachment has the ion exchange resin of methyl alcohol be housed, remove the impurity such as aldehydes, metal ion.Avoid metal ion in mass spectroscopy with measured object complexing and production Interference Peaks, improve the precision of liquid chromatograph-mass spectrometer measuring result.The particle diameter of ion exchange resin is 0.2cm.
E. the methyl alcohol of step c gained is carried out rectifying, namely obtain the liquid chromatograph-mass spectrometer methyl alcohol of purity >=99.99% (wt).
Rectifying can adopt known manner to carry out.A kind of optimal way of the present invention is, rectifying still Heating temperature is 68 DEG C, methanol liquid temperature is 66 DEG C, goes out liquid temp and be 65 DEG C, control reflux ratio 15: 1 in still.Rectifying fluid detects qualified rear bottling, and inflated with nitrogen is preserved.
Embodiment 2
The method of purification of LC-MS analysis methyl alcohol, is characterized in that, comprises the steps:
A. get material benzenemethanol, add potassium permanganate wherein and carry out oxide treatment, the impurity of removal containing double bond is as impurity such as ethene, vinyl cyanide, prussic acid, propenal, methacrylonitrile, vinylcarbinol, oxazole, ethanamides.While adding potassium permanganate, add sodium hydroxide and calcium oxide, slow down the oxidisability of potassium permanganate, the acidic substance that neutralization oxidation simultaneously produces, adjust ph is 14.After oxide treatment, distill out methyl alcohol rapidly.
A ˊ. by adding reductive agent sodium pyrosulfate in the methyl alcohol to step a gained and stirring, distill out methyl alcohol.
B. in the above-mentioned methyl alcohol distilled out, add potassium hydroxide by the pH regulator to 8 of solution, and jolting makes the acidic impurities in potassium hydroxide and material benzenemethanol fully react, generate precipitation of salts thing; Stratification, discards water layer and precipitation, filters organic layer, retains filtrate.
C. by filtrate with 30 column volumes/hour speed pass into the sorbent material post that particle diameter is 20 object 3A molecular sieves be housed, remove the moisture in organic layer further; After absorption, methyl alcohol water content control is ≤0.03%; Utilize molecular sieve to remove moisture after extraction in methyl alcohol in this step, as moisture content > 0.03% need change molecular sieve after proceed molecular sieve adsorption process again;
And then, by above-mentioned effluent liquid with 0.5 column volume/hour speed pass into and surface attachment is housed has the sorbent material post of the modified activated carbon of hypochlorite solutions to carry out adsorption treatment, for removing the unsaturated organic compound of oxide-based, arene, polar compound class and carbon-carbon double bonds as impurity such as heterocyclic arenes.Wherein, the particle diameter of activated carbon is 100 orders, and the mass concentration of hypochlorite solutions is 30%.
D. by the methyl alcohol of step c gained with 30 column volumes/hour speed pass into the sorbent material post that surface attachment has the ion exchange resin of methyl alcohol be housed, remove the impurity such as aldehydes, metal ion.Avoid metal ion in mass spectroscopy with measured object complexing and production Interference Peaks, improve the precision of liquid chromatograph-mass spectrometer measuring result.The particle diameter of ion exchange resin is 0.17cm.
E. the methyl alcohol of steps d gained is carried out rectifying, namely obtain the liquid chromatograph-mass spectrometer methyl alcohol of purity >=99.99% (wt).
Rectifying can adopt known manner to carry out.A kind of optimal way of the present invention is, rectifying still Heating temperature is 75 DEG C, methanol liquid temperature is 70 DEG C, goes out liquid temp and be 64.5 DEG C, control reflux ratio 8: 1 in still.Rectifying fluid detects qualified rear bottling, and inflated with nitrogen is preserved.
Embodiment 3
The method of purification of LC-MS analysis methyl alcohol, is characterized in that, comprises the steps:
A. get material benzenemethanol, add potassium permanganate wherein and carry out oxide treatment, the impurity of removal containing double bond is as impurity such as ethene, vinyl cyanide, prussic acid, propenal, methacrylonitrile, vinylcarbinol, oxazole, ethanamides.While adding potassium permanganate, add sodium hydroxide and calcium oxide, slow down the oxidisability of potassium permanganate, the acidic substance that neutralization oxidation simultaneously produces, adjust ph is 10.After oxide treatment, distill out methyl alcohol rapidly.
A ˊ. by adding reductive agent Sodium phosphate dibasic in the methyl alcohol to step a gained and stirring, distill out methyl alcohol.
B. in the above-mentioned methyl alcohol distilled out, add sodium oxide by the pH regulator to 7.5 of solution, and jolting makes the acidic impurities in sodium oxide and material benzenemethanol fully react, generate precipitation of salts thing; Stratification, discards water layer and precipitation, filters organic layer, retains filtrate.
C. by above-mentioned filtrate with 15 column volumes/hour speed pass into the sorbent material post that particle diameter is 100 order molecular sieves be housed, remove the moisture in organic layer further; After absorption, methyl alcohol water content control is ≤0.03%; Utilize molecular sieve to remove moisture after extraction in methyl alcohol in this step, as moisture content > 0.03% need change molecular sieve after proceed molecular sieve adsorption process again;
And then, by above-mentioned effluent liquid with 30 column volumes/hour speed pass into the sorbent material post that aluminum oxide is housed, the sorbent material post that silica gel is housed and surface attachment be housed and have the sorbent material post of the modified activated carbon of salpeter solution to carry out adsorption treatment, for removing the unsaturated organic compound of oxide-based, arene, polar compound class and carbon-carbon double bonds as impurity such as heterocyclic arenes.Wherein, the particle diameter of activated carbon is 55 orders, and the mass concentration of salpeter solution is 19%.
D. by the methyl alcohol of step c gained with 21 column volumes/hour speed pass into the sorbent material post that surface attachment has the ion exchange resin of acetonitrile be housed, remove the impurity such as aldehydes, metal ion.Avoid metal ion in mass spectroscopy with measured object complexing and production Interference Peaks, improve the precision of liquid chromatograph-mass spectrometer measuring result.The particle diameter of ion exchange resin is 0.01cm.
E. the methyl alcohol of steps d gained is carried out rectifying, namely obtain the liquid chromatograph-mass spectrometer methyl alcohol of purity >=99.99% (wt).
Rectifying can adopt known manner to carry out.A kind of optimal way of the present invention is, rectifying still Heating temperature is 70 DEG C, methanol liquid temperature is 65 DEG C, goes out liquid temp and be 64 DEG C, control reflux ratio 10: 1 in still.Rectifying fluid detects qualified rear bottling, and inflated with nitrogen is preserved.
Embodiment 4
The method of purification of LC-MS analysis methyl alcohol, is characterized in that, comprises the steps:
A. get material benzenemethanol, add potassium permanganate wherein and carry out oxide treatment, the impurity of removal containing double bond is as impurity such as ethene, vinyl cyanide, prussic acid, propenal, methacrylonitrile, vinylcarbinol, oxazole, ethanamides.While adding potassium permanganate, add potassium hydroxide and calcium oxide, slow down the oxidisability of potassium permanganate, the acidic substance that neutralization oxidation simultaneously produces, adjust ph is 9.After oxide treatment, distill out methyl alcohol rapidly.
A ˊ. by adding reductive agent ferrous sulfate in the methyl alcohol to step a gained and stirring, distill out methyl alcohol.
B. in the above-mentioned methyl alcohol distilled out, add potassium hydroxide by the pH regulator to 8 of solution, and jolting makes the acidic impurities in potassium hydroxide and material benzenemethanol fully react, generate precipitation of salts thing; Stratification, discards water layer and precipitation, filters organic layer, retains filtrate.
C. by above-mentioned filtrate with 24 column volumes/hour speed pass into the sorbent material post that particle diameter is 65 molecules of interest sieves be housed, remove further the moisture in organic layer; After absorption, methyl alcohol water content control is ≤0.03%; Utilize molecular sieve to remove moisture after extraction in methyl alcohol in this step, as moisture content > 0.03% need change molecular sieve after proceed molecular sieve adsorption process again;
And then, by above-mentioned effluent liquid with 12 column volumes/hour speed pass into and surface attachment is housed has the sorbent material post of the modified activated carbon of triethanolamine solution to carry out adsorption treatment, for removing the unsaturated organic compound of oxide-based, arene, polar compound class and carbon-carbon double bonds as impurity such as heterocyclic arenes.Wherein, the particle diameter of activated carbon is 76 orders, and the mass concentration of triethanolamine solution is 27%.
D. by the methyl alcohol of step c gained with 14 column volumes/hour speed pass into the sorbent material post that surface attachment has the ion exchange resin of methyl alcohol be housed, remove the impurity such as aldehydes, metal ion.Avoid metal ion in mass spectroscopy with measured object complexing and production Interference Peaks, improve the precision of liquid chromatograph-mass spectrometer measuring result.The particle diameter of ion exchange resin is 0.09cm.
E. the methyl alcohol of steps d gained is carried out rectifying, namely obtain the liquid chromatograph-mass spectrometer methyl alcohol of purity >=99.99% (wt).
Rectifying can adopt known manner to carry out.A kind of optimal way of the present invention is, rectifying still Heating temperature is 72 DEG C, methanol liquid temperature is 68 DEG C, goes out liquid temp and be 66 DEG C, control reflux ratio 12: 1 in still.Rectifying fluid detects qualified rear bottling, and inflated with nitrogen is preserved.
Embodiment 5
The method of purification of LC-MS analysis methyl alcohol, is characterized in that, comprises the steps:
A. get material benzenemethanol, add potassium permanganate wherein and carry out oxide treatment, the impurity of removal containing double bond is as impurity such as ethene, vinyl cyanide, prussic acid, propenal, methacrylonitrile, vinylcarbinol, oxazole, ethanamides.While adding hydrogen peroxide, add potassium hydroxide and calcium oxide, slow down the oxidisability of potassium permanganate, the acidic substance that neutralization oxidation simultaneously produces, adjust ph is 8.5.After oxide treatment, distill out methyl alcohol rapidly.
A ˊ. by adding reductive agent sodium bisulfite in the methyl alcohol to step a gained and stirring, distill out methyl alcohol.
B. in the above-mentioned methyl alcohol distilled out, add potassium hydroxide by the pH regulator to 7.4 of solution, and jolting makes the acidic impurities in potassium hydroxide and material benzenemethanol fully react, generate precipitation of salts thing; Stratification, discards water layer and precipitation, filters organic layer, retains filtrate.
C. by above-mentioned filtrate with 23 column volumes/hour speed pass into the sorbent material post that particle diameter is 60 molecules of interest sieves be housed, remove further the moisture in organic layer; After absorption, methyl alcohol water content control is ≤0.03%; Utilize molecular sieve to remove moisture after extraction in methyl alcohol in this step, as moisture content > 0.03% need change molecular sieve after proceed molecular sieve adsorption process again;
And then, by above-mentioned effluent liquid with 9 column volumes/hour speed pass into and surface attachment is housed has the sorbent material post of the modified activated carbon of aluminum hydroxide solution to carry out adsorption treatment, for removing the unsaturated organic compound of oxide-based, arene, polar compound class and carbon-carbon double bonds as impurity such as heterocyclic arenes.Wherein, the particle diameter of activated carbon is 57 orders, and the mass concentration of aluminum hydroxide solution is 8%.
D. by the methyl alcohol of step c gained with 3 column volumes/hour speed pass into the sorbent material post that surface attachment has the ion exchange resin of acetonitrile be housed, remove the impurity such as aldehydes, metal ion.Avoid metal ion in mass spectroscopy with measured object complexing and production Interference Peaks, improve the precision of liquid chromatograph-mass spectrometer measuring result.The particle diameter of ion exchange resin is 0.11cm.
E. the methyl alcohol of steps d gained is carried out rectifying, inflated with nitrogen is preserved, and namely obtains the liquid chromatograph-mass spectrometer methyl alcohol of purity >=99.99% (wt).
Rectifying can adopt known manner to carry out.A kind of optimal way of the present invention is, rectifying still Heating temperature is 74 DEG C, methanol liquid temperature is 69 DEG C, goes out liquid temp and be 64.5 DEG C, control reflux ratio 9: 1 in still.Rectifying fluid detects qualified rear bottling, and inflated with nitrogen is preserved.
Embodiment 1 ~ 5 purify after LC-MS analysis methyl alcohol technical indicator as shown in Table 1:
Table one
As shown in Table 1, by the liquid chromatograph-mass spectrometer methyl alcohol that method of purification provided by the invention is obtained, purity is increased to 99.99% further by 99.5%, and residue on evaporation, water content, metal (K, Na) content reduce all greatly.Yield is not less than 88%, and the yield of more traditional method of purification 80% improves greatly.To wavelength be the incident light of 195nm, 200nm, 210nm and 230nm transmittance comparatively raw material also greatly improve, improve the optical property of liquid chromatograph-mass spectrometer methyl alcohol.
Embodiment in the present invention, only for the present invention will be described, does not form the restriction to right, other equivalent in fact substituting, all in scope that those skilled in that art can expect.

Claims (8)

1. the method for purification of liquid chromatograph-mass spectrometer methyl alcohol, is characterized in that, comprises the steps:
A. get material benzenemethanol, add potassium permanganate or superoxide wherein and after stirring, distill out methyl alcohol;
B. add alkalimetal oxide, alkali metal hydroxide or carbonate in the methyl alcohol distilled out in step a, after jolting, stratification, discard water layer, filter organic layer, retain filtrate;
C. the sorbent material post above-mentioned filtrate passing into being equipped with modified activated carbon carries out adsorption treatment;
D. the methyl alcohol of step c gained is passed into the sorbent material post that ion exchange resin is housed and carry out ion exchange treatment, obtain the liquid chromatograph-mass spectrometer methyl alcohol of purity >=99.99% (wt).
2. the method for purification of liquid chromatograph-mass spectrometer methyl alcohol according to claim 1, is characterized in that, in described step a, while adding potassium permanganate or superoxide, adds highly basic and basic oxide.
3. the method for purification of liquid chromatograph-mass spectrometer methyl alcohol according to claim 1, is characterized in that, in described step a, before adding potassium permanganate or superoxide, in material benzenemethanol, adds porous mass, stirs 1 ~ 2 hour.
4. the method for purification of liquid chromatograph-mass spectrometer methyl alcohol according to claim 1, is characterized in that, also comprises step a ˊ, will add reductive agent and after stirring, distill out methyl alcohol in the methyl alcohol to step a gained; Described reductive agent is iron protoxide, sodium bicarbonate, ferrous sulfate, sodium pyrosulfate, sodium bisulfite or Sodium phosphate dibasic.
5. the method for purification of liquid chromatograph-mass spectrometer methyl alcohol according to claim 1, it is characterized in that, in described step c, modified activated carbon is the activated carbon of surface attachment ethylenediamine tetraacetic acid (EDTA), aluminum oxide, nitric acid, trolamine, aluminium hydroxide or hypochlorite.
6. the method for purification of liquid chromatograph-mass spectrometer methyl alcohol according to claim 1, is characterized in that, in described step c, before filtrate passing into is equipped with the sorbent material post of modified activated carbon, first passes into the sorbent material post that molecular sieve is housed.
7. the method for purification of liquid chromatograph-mass spectrometer methyl alcohol according to claim 1, is characterized in that, in described steps d, the surface attachment of ion exchange resin has acetonitrile or alcohol compound.
8. the method for purification of the liquid chromatograph-mass spectrometer methyl alcohol according to above-mentioned any one claim, is characterized in that, also comprise step e, and the methyl alcohol of adsorption treatment gained is carried out rectifying.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112321393A (en) * 2020-11-04 2021-02-05 北京化学试剂研究所有限责任公司 Method for purifying chromatographically pure methanol

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB958828A (en) * 1961-09-08 1964-05-27 Chemical Construction Corp Purification of synthetic methanol
US20030094417A1 (en) * 2001-10-31 2003-05-22 Snoble Karel A.J. Purification of organic solvents
CN1844070A (en) * 2006-04-24 2006-10-11 广东西陇化工有限公司 Method for preparing ultra high-purity alcohol compound

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB958828A (en) * 1961-09-08 1964-05-27 Chemical Construction Corp Purification of synthetic methanol
US20030094417A1 (en) * 2001-10-31 2003-05-22 Snoble Karel A.J. Purification of organic solvents
CN1844070A (en) * 2006-04-24 2006-10-11 广东西陇化工有限公司 Method for preparing ultra high-purity alcohol compound

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
张志刚等: "我国工业甲醇提纯精制高纯甲醇的可行性", 《精细石油化工进展》 *
张志刚等: "用工业甲醇脱水纯化制取高纯甲醇", 《化学试剂》 *
韩银群等: "精甲醇中酸值的控制", 《中氮肥》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112321393A (en) * 2020-11-04 2021-02-05 北京化学试剂研究所有限责任公司 Method for purifying chromatographically pure methanol
CN112321393B (en) * 2020-11-04 2022-08-05 北京化学试剂研究所有限责任公司 Method for purifying chromatographically pure methanol

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