CN100556887C - 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa - Google Patents

2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa Download PDF

Info

Publication number
CN100556887C
CN100556887C CN 200510023334 CN200510023334A CN100556887C CN 100556887 C CN100556887 C CN 100556887C CN 200510023334 CN200510023334 CN 200510023334 CN 200510023334 A CN200510023334 A CN 200510023334A CN 100556887 C CN100556887 C CN 100556887C
Authority
CN
China
Prior art keywords
solvent
high boiling
purification
hfc
phenoxy
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 - Fee Related
Application number
CN 200510023334
Other languages
Chinese (zh)
Other versions
CN1803759A (en
Inventor
施沁清
黄莹
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.)
Shanghai Huayi Group Corp
Original Assignee
Shanghai Huayi Group Corp
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 Shanghai Huayi Group Corp filed Critical Shanghai Huayi Group Corp
Priority to CN 200510023334 priority Critical patent/CN100556887C/en
Publication of CN1803759A publication Critical patent/CN1803759A/en
Application granted granted Critical
Publication of CN100556887C publication Critical patent/CN100556887C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a kind of 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa.The present invention is dissolved in reaction solvent N with Meta-dinitrobenzene, hexafluoro bisphenol-a, in the dinethylformamide, the reaction solution that obtains with the salt of wormwood condensation after filtration, underpressure distillation, wet distillation, add high boiling solvent, molecular distillation, target product is collected in the distillate extraction from distillate.With method of purification of the present invention obtain 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, 3-HFC-236fa, purity reach more than 98%, productive rate is greater than 80%.The generation that method of purification cost of the present invention is low, avoided a large amount of waste water has reduced pollution, can reclaim the use reaction solvent, and resulting constant product quality is suitable for suitability for industrialized production.

Description

2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa
Technical field
The present invention relates to 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa.
Background technology
2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the 3-HFC-236fa is a kind of important industrial chemicals, especially can be used as the monomer of preparation polyimide, and application promise in clinical practice is arranged.Its structural formula is:
Figure C20051002333400031
European patent EP 0192480 is a raw material with Meta-dinitrobenzene, hexafluoro bisphenol-a, at reaction solvent N, carries out condensation with salt of wormwood in the dinethylformamide (DMF), reaction solution pours a large amount of water, isolates to contain 2 two [4-(3-nitro-phenoxy) phenyl]-1 of 2-, 1,1,3,3, the tarry crude product of 3-HFC-236fa is dissolved in the benzene, washing, method with silica gel column chromatography is purified, and obtains the purpose product.
In above-mentioned preparation method, adopt the method purification operations difficulty of silica gel column chromatography big, the cost height has a large amount of waste water to produce in the reaction process, difficult solvent recovery, industrial prospect is undesirable.
Summary of the invention
The object of the present invention is to provide a kind of 2, two [4-(3-nitro-phenoxy) phenyl]-1,1 of 2-, 1,3,3, the method of purification of 3-HFC-236fa, available technology adopting silica gel column chromatography purification operations is loaded down with trivial details, cost is high to overcome, produce a large amount of waste water, the deficiency of difficult solvent recovery.
Method of purification of the present invention may further comprise the steps:
Meta-dinitrobenzene, hexafluoro bisphenol-a are dissolved in reaction solvent N, in the dinethylformamide (DMF), carry out condensation with salt of wormwood, with resulting reacting liquid filtering, vacuum distillation recovered solvent, wet distillation is removed low molecular weight impurities and remaining Meta-dinitrobenzene and N, dinethylformamide adds high boiling solvent, at 150~165 ℃, 0.01 target product is collected in molecular distillation under the condition of~0.2Pa from distillate.According to the present invention, adopt extraction agent from distillate, to collect target product, said extraction agent is C 1~C 3No water unit alcohol in a kind of, preferred dehydrated alcohol, the consumption of extraction agent is a hexafluoro bisphenol-a: extraction agent=1.0: 2.0~5.0, weightmeasurement ratio;
Said high boiling solvent is C 15~C 30Alkane solvent, preferred C 20~C 25Alkane solvent, the consumption of high boiling solvent is a hexafluoro bisphenol-a: high boiling solvent=1.0: 0.2~2.0, weightmeasurement ratio.
With method of purification of the present invention obtain 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, 3-HFC-236fa, purity reach more than 98%, productive rate is 81%.
Reaction solution used in the present invention can prepare with reference to the method for EP0192480.
Beneficial effect
The present invention has the generation that constant product quality, cost are low, avoided a large amount of waste water compared with prior art, has reduced pollution, and reaction solvent can reclaim use, is suitable for the advantage of suitability for industrialized production.
Embodiment
The invention will be further described below by embodiment, but embodiment does not limit protection scope of the present invention.
Embodiment 1
In the reactor that reflux condensing tube, agitator, thermometer are housed, add Meta-dinitrobenzene 24g (0.14mol) respectively, hexafluoro bisphenol-a 20g (0.059mol), N, dinethylformamide (DMF) 100ml stirs adding salt of wormwood 19.4g (0.14mol) down, be heated to backflow gradually, reacted 7 hours, the reaction solution cooling is filtered, the filtrate decompression distillation is steamed and is removed DMF solvent (recovery set is used).Steam surplus liquid wet distillation, steam and remove low-molecular-weight fraction, cooling adds C 20~C 25Alkane solvent 10ml, 160 ± 2 ℃ of controlled temperature, pressure 0.1Pa carries out molecular distillation, adds dehydrated alcohol 50ml in the cut of collection and extracts, and stirs 10min, leaves standstill the back and divides oil-yielding stratum, the C that obtains 20~C 25Alkane solvent recovery set usefulness desolventizes ethanol with alcohol layer underpressure distillation steaming, obtains light yellow oily 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, 3-HFC-236fa product 27.6g, productive rate 81%, purity 98.6% (HPLC).
Comparative example 1
The reaction solution that obtains with example 1 same procedure filters, and the filtrate decompression distillation adds C after the wet distillation 20~C 25Alkane solvent 20ml, 190 ± 2 ℃ of controlled temperature, pressure 0.1~0.2Pa carries out molecular distillation, has decomposing phenomenon to produce in the fraction collection process, extracts adding dehydrated alcohol 50ml in the cut of collecting, and stirs, leaves standstill the back and divide oil-yielding stratum, the C that obtains 20~C 25Alkane solvent recovery set usefulness desolventizes ethanol with alcohol layer underpressure distillation steaming, obtains light yellow oily 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, 3-HFC-236fa product 23.1g, productive rate 68%, purity 98.2% (HPLC).
As can be seen, too high from comparative example 1 when the temperature of molecular distillation, can cause in the fraction collection process and to produce decomposing phenomenon and then reduction productive rate because of temperature is high.
Comparative example 2
The reaction solution that obtains with example 1 same procedure filters, and underpressure distillation is after the wet distillation, 160 ± 2 ℃ of controlled temperature, pressure 0.1Pa carries out molecular distillation, obtains light yellow oily 2, two [4-(3-nitro-phenoxy) phenyl]-1 of 2-, 1,1,3,3,3-HFC-236fa product 25.6g, productive rate 75%, purity 98.1% (HPLC).
As can be seen, the use of high boiling solvent if the cancellation high boiling solvent can cause productive rate to descend, therefore must be used high boiling solvent for guaranteeing that good productive rate is very important from comparative example 2.

Claims (5)

1. one kind 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa is characterized in that comprising the steps:
Meta-dinitrobenzene, hexafluoro bisphenol-a are dissolved in reaction solvent N, in the dinethylformamide, carry out condensation with salt of wormwood, with resulting reacting liquid filtering, vacuum distillation recovered solvent, wet distillation is removed low molecular weight impurities and remaining Meta-dinitrobenzene and N, and dinethylformamide adds high boiling solvent, at 150-165 ℃, 0.01-0.2Pa condition under molecular distillation, adopt extraction agent from distillate, to collect target product, described high boiling solvent is C 15~C 30Alkane solvent; Said extraction agent is C 1~C 3No water unit alcohol in a kind of.
2. method according to claim 1 is characterized in that high boiling solvent is C 20~C 25Alkane solvent.
3. method according to claim 1 is characterized in that extraction agent is a dehydrated alcohol.
4. method according to claim 1, the consumption that it is characterized in that high boiling solvent is a hexafluoro bisphenol-a: high boiling solvent=1.0: 0.2~2.0, weightmeasurement ratio.
5. method according to claim 1, the consumption that it is characterized in that extraction agent is a hexafluoro bisphenol-a: extraction agent=1.0: 2.0~5.0, weightmeasurement ratio.
CN 200510023334 2005-01-14 2005-01-14 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa Expired - Fee Related CN100556887C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200510023334 CN100556887C (en) 2005-01-14 2005-01-14 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200510023334 CN100556887C (en) 2005-01-14 2005-01-14 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa

Publications (2)

Publication Number Publication Date
CN1803759A CN1803759A (en) 2006-07-19
CN100556887C true CN100556887C (en) 2009-11-04

Family

ID=36865935

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200510023334 Expired - Fee Related CN100556887C (en) 2005-01-14 2005-01-14 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa

Country Status (1)

Country Link
CN (1) CN100556887C (en)

Also Published As

Publication number Publication date
CN1803759A (en) 2006-07-19

Similar Documents

Publication Publication Date Title
CN1032132C (en) Process for preparation of arude terphthalic acid suitable for reduction to prepane purified terephthalic acid
RU2594159C2 (en) Method of separating ethylene glycol and 1,2-butanediol
WO2007089527A2 (en) Method of forming a dianhydrosugar alcohol
WO2008025852A1 (en) Recovery of bis(diarylphenol) ligands during the production of isopulegol
CN105152980A (en) Chiral preparation method for N-t-butyloxycarboryl-(4S)-(p-phenyl phenyl methyl)-4-amino-(2R)-methylbutyric acid
CN102020554A (en) Synthesis method of 2-[4-(hydroxyphenoxy)] propionic acid
CN100556887C (en) 2, two [4-(3-nitro-phenoxy) phenyl]-1,1,1,3,3 of 2-, the method for purification of 3-HFC-236fa
CN111018819A (en) Preparation method of luteolin
CN101508678B (en) Process for preparing 2-methyl-4-amino-5-acetyl aminomethyl pyrimidine
CN107715909B (en) Pentaerythritol-supported proline catalyst and preparation method and application thereof
CN106966980A (en) The preparation method of high-purity Eptazocine intermediate
WO2013153957A1 (en) Method for producing hydrogenated biphenol
CN100340535C (en) Solanesol purifying method
CN101906058A (en) Method for preparing dithiocyano-methane
CN112047815A (en) Preparation method of cannabidiol compound
CN101811934A (en) Preparation method of mannitol
CN102584765B (en) Synthetic method of liquid phase combination of hydroxyisoflavone compound
CN112409182A (en) Synthesis, purification and separation method of menthyl lactate
JP3981550B2 (en) Method for producing acrylic ester
CN112125793B (en) 2, 4-Di-n-octoxybenzophenone and synthetic method and application thereof
CN111732540B (en) Preparation method of roximelic
CN111718266A (en) Purification method and application of p-nitroaniline
CN115282627B (en) Purification device and purification method of 1, 5-pentanediamine carbamate
CN114149403B (en) Mixed crystal form glycolide and preparation method and application thereof
JP7066849B2 (en) Production method and system of alkylene oxide

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
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20091104

Termination date: 20120114