GB2290291A - Methanol purification - Google Patents

Methanol purification Download PDF

Info

Publication number
GB2290291A
GB2290291A GB9411311A GB9411311A GB2290291A GB 2290291 A GB2290291 A GB 2290291A GB 9411311 A GB9411311 A GB 9411311A GB 9411311 A GB9411311 A GB 9411311A GB 2290291 A GB2290291 A GB 2290291A
Authority
GB
United Kingdom
Prior art keywords
mixture
methanol
heated
base
purified
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.)
Granted
Application number
GB9411311A
Other versions
GB9411311D0 (en
GB2290291B (en
Inventor
Gerard Kenny
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
G K ANALYTICAL SCIENCES LIMITE
Original Assignee
G K ANALYTICAL SCIENCES LIMITE
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by G K ANALYTICAL SCIENCES LIMITE filed Critical G K ANALYTICAL SCIENCES LIMITE
Priority to GB9411311A priority Critical patent/GB2290291B/en
Priority to BE9400597A priority patent/BE1006528A6/en
Publication of GB9411311D0 publication Critical patent/GB9411311D0/en
Publication of GB2290291A publication Critical patent/GB2290291A/en
Application granted granted Critical
Publication of GB2290291B publication Critical patent/GB2290291B/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/76Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
    • C07C29/80Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/88Separation; Purification; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification of at least one compound

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Feedstock Methanol containing impurities such as Acetone, Methyl Ethyl Ketone, Water, Formic Acid, Formaldehyde, Acetic Acid and Methyl Esters is purified by adding the feedstock together with a reducing agent such as lithium aluminium hydride to the reflux vessel of a batch distillation unit. The mixture is heated for at least half an hour at a temperature of at least 65 DEG C. A strong base such as potassium hydroxide is then added and the mixture is heated to reflux. The optional final stage in the purification process involves adding a weak base such as sodium carbonate and heating the mixture under reflux. A very high level of purity of at least 99.9% is obtained.

Description

"Solvent Purification" The invention relates to solvent purification, in particular to a process for purifying Methanol containing impurities such as Acetone, Methyl Ethyl Ketone, Water, Formic Acid, Formaldehyde, Acetic Acid and Methyl Esters, catalytic amounts of acid and the like.
Methanol is widely used in selective recrystallisation and extractive distillation. Because of its favourable dielectric, solvent and optical properties it is also widely used in analytical chemistry, particularly in high performance liquid chromatography (hplc), organic synthesis, pesticide residue analysis, W and IR spectroscopy, purge and trap analysis, and DNA and peptide synthesis.
As analytical chemistry techniques and analytical machines become ever more sophisticated there is a need to develop processes for producing Methanol to a very high level of purity for use as a standard in such equipment.
This invention is therefore directed towards providing a process for producing Methanol having a very high level of purity in a cost efficient manner.
According to the invention there is provided a purification process for the purification of Methanol containing impurities such as Acetone, Methyl Ethyl Ketone, Water, Formic Acid, Formaldehyde, Acetic Acid and Methyl Esters to produce highly purified Methanol, the process comprising of the steps of : adding a reducing agent to Methanol containing said impurities; adding a strong base to the mixture; distilling the mixture in a distillation column; and recovering purified Methanol from the distillation column.
In one particularly preferred embodiment of the invention the Methanol is further purified by adding an additional base to the mixture prior to distillation. Preferably, the additional base is a weak base such as sodium carbonate.
Preferably the mixture is heated after addition of the reducing agent. Advantageously the mixture is heated to a temperature of at least 650C for a period of one hour.
In a preferred embodiment of the invention, after addition of the base, the mixture is heated to reflux and the mixture is sampled over time to monitor the levels of impurities present.
In one embodiment of the invention the mixture is cooled prior to addition of the base.
Preferably, the reducing agent is lithium aluminium hydride.
The invention also provides purified Methanol whenever purified by the process of the invention.
The invention will be more clearly understood from the following description thereof given by way of example only with reference to the accompanying drawing which is a schematic diagram of a custom designed distillation apparatus used in the process of the invention.
Referring to the drawing, there is illustrated a custom designed distillation apparatus used in the process of the invention comprising a distillation column 1 of packed raschig rings having from 30 to 40 theoretical plates.
Feed material is added into a boiling vessel 2 through an inlet valve 3. The feed material is heated by passing through a reboiler 5 having a steam heated coil 6. Vapour from the distillation column 1 is condensed by passing cooling water through a coil 7 in the condenser 8. Reflux material is returned to the column 1 through a reflux line 9. When the desired purity level has been reached the material is fed through an outlet line 10 to a collection vessel 12. The material may be passed through molecular sieves 11 prior to delivery to the collection vessel 12.
EXAMPLE Feedstock Methanol containing impurities such as Acetone, Methyl Ethyl Ketone, Water, Formic Acid, Formaldehyde, Acetic Acid and Methyl Esters was purified by the following process.
100L of feedstock Methanol is added to the reflux vessel described above and approximately SOg of a reducing agent such as lithium aluminium hydride is added. A small quantity of a strong base such as potassium hydroxide is also added. The strong base acts as an hydrolysing agent.
The mixture is then heated for at least one hour at a temperature of at least 65"C. A weak base such as sodium carbonate is then added to the mixture in an amount of at least 100g (up to 500g) and the mixture is heated to reflux. The levels of impurity present are monitored.
When the levels of impurities have reached desired values the mixture is allowed to cool.
The Methanol purified by this process has a purity of at least 99.9% with a water content of less than 0.1%, an acidity level of less than .001% and a residue level of less than .0001%.
The high grade purified Methanol is used in HPLC analysis and has a wide range of application including applications in organic synthesis and in residue analyses, purge and trap analysis and UV-IR Spectroscopy.
The invention is not limited to the embodiment hereinbefore described which may be varied in detail.

Claims (11)

1. A purification process for the purification of Methanol containing impurities such as Acetone, Methyl Ethyl Ketane, Water, Formic Acid, Formaldehyde, Acetic Acid and Methyl Esters to produce Methanol, the process comprising the steps of : adding a reducing agent to Methanol containing impurities; adding a strong base to the mixture; distilling the mixture in a distillation column; and recovering purified Methanol from the distillation column.
2. A process as claimed in claim 1 wherein the strong base is potassium hydroxide.
3. A process as claimed in claim 1 or 2 wherein the Methanol is further purified by adding an additional base to the mixture prior to distillation.
4. A process as claimed in claim 3 wherein the additional base is a weak base.
5. A process as claimed in claim 4 wherein the additional base is sodium carbonate.
6. A process as claimed in any of claims 1 to 5 wherein the mixture is heated after addition of the reducing agent.
7. A process as claimed in claim 6 wherein the mixture is heated to a temperature of at least 650C for a period of at least one hour.
8. A process as claimed in any of claims 2 to 7 wherein, after addition of the base, the mixture is heated to reflux and the mixture is sampled over time to monitor the levels of impurities present.
9. A process as claimed in any preceding claim wherein the reducing agent is lithium aluminium hydride.
10. A process substantially as hereinbefore described with reference to the Examples.
11. Purified Methanol whenever purified by a process as claimed in any preceding claim.
GB9411311A 1994-06-07 1994-06-07 Methanol purification Expired - Fee Related GB2290291B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
GB9411311A GB2290291B (en) 1994-06-07 1994-06-07 Methanol purification
BE9400597A BE1006528A6 (en) 1994-06-07 1994-06-23 Purification solvent.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9411311A GB2290291B (en) 1994-06-07 1994-06-07 Methanol purification
BE9400597A BE1006528A6 (en) 1994-06-07 1994-06-23 Purification solvent.

Publications (3)

Publication Number Publication Date
GB9411311D0 GB9411311D0 (en) 1994-07-27
GB2290291A true GB2290291A (en) 1995-12-20
GB2290291B GB2290291B (en) 1998-05-13

Family

ID=25662889

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9411311A Expired - Fee Related GB2290291B (en) 1994-06-07 1994-06-07 Methanol purification

Country Status (2)

Country Link
BE (1) BE1006528A6 (en)
GB (1) GB2290291B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2322812A (en) * 1997-03-03 1998-09-09 G K Analytical Sciences Limite Solvent purification
WO2004072007A1 (en) * 2003-02-06 2004-08-26 Honeywell International Inc. Purification of alcohol
CN105541553A (en) * 2016-02-23 2016-05-04 衡阳市凯信化工试剂股份有限公司 Preparation and purification method and device of high performance liquid chromatography (HPLC) solvent

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB344796A (en) * 1929-12-10 1931-03-10 James Ritchie Park Improved method for the purification of synthetic alcohols
GB659727A (en) * 1948-11-19 1951-10-24 Celanese Corp Process for the recovery of methylol, methanol and alkali metal formates
GB1520709A (en) * 1977-05-20 1978-08-09 Inst Neftechimicheskogo Sintez Process for producing c3 - c20 aliphatic alcohols

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB344796A (en) * 1929-12-10 1931-03-10 James Ritchie Park Improved method for the purification of synthetic alcohols
GB659727A (en) * 1948-11-19 1951-10-24 Celanese Corp Process for the recovery of methylol, methanol and alkali metal formates
GB1520709A (en) * 1977-05-20 1978-08-09 Inst Neftechimicheskogo Sintez Process for producing c3 - c20 aliphatic alcohols

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2322812A (en) * 1997-03-03 1998-09-09 G K Analytical Sciences Limite Solvent purification
GB2322812B (en) * 1997-03-03 2001-03-14 G K Analytical Sciences Ltd Solvent purification
WO2004072007A1 (en) * 2003-02-06 2004-08-26 Honeywell International Inc. Purification of alcohol
CN105541553A (en) * 2016-02-23 2016-05-04 衡阳市凯信化工试剂股份有限公司 Preparation and purification method and device of high performance liquid chromatography (HPLC) solvent
CN105541553B (en) * 2016-02-23 2018-09-28 衡阳市凯信化工试剂股份有限公司 A kind of high-efficient liquid phase chromatogram HPLC solvent prepares purification process and device

Also Published As

Publication number Publication date
BE1006528A6 (en) 1994-10-04
GB9411311D0 (en) 1994-07-27
GB2290291B (en) 1998-05-13

Similar Documents

Publication Publication Date Title
US5414154A (en) Phenol with low levels of methylbenzofuran
SU963461A3 (en) Process for isolating acrylic acid
GB2249308A (en) Purification of acetonitrile
GB2290291A (en) Methanol purification
IE74231B1 (en) Solvent purification
US5059288A (en) Recovery of isopropyl acetate and ethanol from an isopropyl acetate, ethanol and water-containing stream
JP2008308500A (en) Production method of high purity butyl acetate
KR980001991A (en) Preparation and fractionation method of dimethyl ether and chloromethane mixtures using methanol as extractant
EP0424436B1 (en) Process for the production of anhydrous oxime from an aqueous solution
US4867849A (en) Purification of alkyl glyoxylate
IES940453A2 (en) Solvent Purification (Methanol)
JP2006514087A (en) Purification of 1,3-propanediol by distillation
JP4259815B2 (en) Method for producing high purity butyl acetate
KR0129753B1 (en) Process for the purification of 2-(4-isobutylpohencyl)-propionic acid
US5705040A (en) Process for preparing a substantially pure aqueous solution of hydrogen peroxide
EP0612714A1 (en) Process and plant for the purification of raw maleic anhydride recovered from gaseous reaction mixtures
US4594462A (en) Preparation of butane-1,4-diol
JPS6013739A (en) Purification of acrylic acid
GB2322812A (en) Solvent purification
JP2002316967A (en) High purity butyl acetate and method for producing the same
CN112430185B (en) Method for distillatively purifying 2, 4-trimethyl-1, 3-pentanediol monoisobutyrate
IE80800B1 (en) Solvent purification
IE903844A1 (en) "Solvent purification"
US5271811A (en) Process for purifying 2-(4-isobutylphenyl)-propionic acid by vacuum distillation
JP2002069477A (en) Method of manufacturing alkyl jasmonate with high epimer concentration

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee

Effective date: 20100607