CN102558209A - Bis(pinacolato)diboron production process - Google Patents

Bis(pinacolato)diboron production process Download PDF

Info

Publication number
CN102558209A
CN102558209A CN2012100072034A CN201210007203A CN102558209A CN 102558209 A CN102558209 A CN 102558209A CN 2012100072034 A CN2012100072034 A CN 2012100072034A CN 201210007203 A CN201210007203 A CN 201210007203A CN 102558209 A CN102558209 A CN 102558209A
Authority
CN
China
Prior art keywords
hole bottle
reaction
parts
under
mass parts
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
CN2012100072034A
Other languages
Chinese (zh)
Other versions
CN102558209B (en
Inventor
薛嵩
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.)
Haimen Ruiyi Pharmaceutical Technology Co Ltd
Original Assignee
Haimen Ruiyi Pharmaceutical Technology Co Ltd
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 Haimen Ruiyi Pharmaceutical Technology Co Ltd filed Critical Haimen Ruiyi Pharmaceutical Technology Co Ltd
Priority to CN201210007203.4A priority Critical patent/CN102558209B/en
Publication of CN102558209A publication Critical patent/CN102558209A/en
Application granted granted Critical
Publication of CN102558209B publication Critical patent/CN102558209B/en
Active 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 bis(pinacolato)diboron production process which is characterized in that boron trichloride is used as a raw material and is aminated with dimethylamine gas in an n-hexane system, the desalinated reaction solution and boron tribromide react at the room temperature, the prepared intermediate and magnesium are coupled in toluene, 1, 2-dichloroethane solution of pinacol is dropped into the desalinated reaction solution, and the target product is prepared via transesterification. The invention has the advantages that: n-hexane is used as a reaction solvent for the first two steps, the conversion rate of reaction is increased, and the ultra low temperature can be avoided; the safety of the process is improved due to use of magnesium; and the yield of the product is increased in transesterification through controlling the reaction temperature.

Description

Join boric acid pinacol ester production technique
Technical field
The present invention relates to join the production technique of boric acid pinacol ester.
Background technology
Joining boric acid pinacol ester, is a kind of medicine intermediate, its English another name: bis (pinacolato) diboron; Molecular formula is C12H24B2O4, and the production technique security of existing boric acid pinacol ester is not high, and reaction conversion ratio is low; Product yield is low, causes the wasting of resources.Therefore, should provide a kind of new technical scheme to address the above problem.
Summary of the invention
The objective of the invention is:, the production technique of the couplet boric acid pinacol ester that a kind of process safety is high, reaction conversion ratio is high, product yield is high is provided to above-mentioned deficiency.
For realizing above-mentioned purpose, the technical scheme that the present invention adopts is:
Join boric acid pinacol ester production technique, comprise the steps:
(1) will be equipped with earlier that to add 1900-2100 parts by volume mass concentrations in the four-hole bottle of mechanical stirring, TM, device for absorbing tail gas and prolong be 97-99% normal hexane; And stir, feed the boron trichloride gas of 180-210 mass parts, under 10-15 ℃, condition of normal pressure; Feed the n n dimetylaniline gas of 470-490 mass parts; Carry out amination reaction, suction filtration is removed the salt of separating out then, and filtrating joins in the four-hole bottle again;
(2) in above-mentioned filtrating, drip the boron tribromide of 210-230 mass parts in the time at 55-65min; Under the normal temperature and pressure, reaction 4.5-5.5h is after reaction is accomplished; On four-hole bottle, load onto rectifying volumn; At 68-70 ℃, distillation earlier obtains normal hexane under the condition of normal pressure, reduces pressure-0.09-0.1MPa again, is cooled to 60-65 ℃ and distills out midbody;
(3) get a four-hole bottle again; In four-hole bottle, add 2900-3100 parts by volume mass concentrations and be 97-99% toluene, the MAGNESIUM METAL 99 of 29-32 mass parts is divided put in the four-hole bottle for 3 times then, be warming up to 110-112 ℃ of backflows under the normal pressure; The midbody that obtains at last in the step (2) is added drop-wise in 30-60min in the four-hole bottle of this step; GC detects, and reduces temperature to 100-110 ℃, after the raw material complete reaction; Suction filtration desalination under protection of nitrogen gas, filtrating joins in this four-hole bottle again;
(4) with 290-310 mass parts tetramethyl ethylene ketone solution be dissolved in 480-520 parts by volume mass concentrations be 97-99% 1, in the 2-ethylene dichloride, in 50-65min, be added drop-wise to then in the employed four-hole bottle of step (3); Stir, normal pressure is warming up to 80-90 ℃ of backflows and carries out transesterification reaction, and the n n dimetylaniline gas of generation absorbs with 18-22% hydrochloric acid; GC monitoring raw material reaction is complete; Suction filtration obtains product, reclaims toluene and 1, the 2-ethylene dichloride after the filtrating rectifying.
Four above-mentioned steps, its reaction equation is following successively:
Figure 418423DEST_PATH_IMAGE001
Figure 397880DEST_PATH_IMAGE002
Figure 2012100072034100002DEST_PATH_IMAGE003
Figure 239934DEST_PATH_IMAGE004
Advantage of the present invention is: select for use normal hexane as preceding two step reaction solvents, improved reaction conversion ratio, avoided utmost point coldcondition simultaneously; In the linked reaction of step (3), use MAGNESIUM METAL 99, the security that has improved technology.
Embodiment
Embodiment 1
Join boric acid pinacol ester production technique, comprise the steps:
(1) will be equipped with earlier that to add 1900 parts by volume mass concentrations in the four-hole bottle of mechanical stirring, TM, device for absorbing tail gas and prolong be 97% normal hexane; And stir, feed the boron trichloride gas of 180 mass parts, under 10 ℃, condition of normal pressure; Feed the n n dimetylaniline gas of 470 mass parts; Carry out amination reaction, suction filtration is removed the salt of separating out then, and filtrating joins in the four-hole bottle again;
(2) in 55min, in above-mentioned filtrating, drip the boron tribromide of 210 mass parts, under the normal temperature and pressure, reaction 4.5h; Reaction is loaded onto rectifying volumn, at 68 ℃ after accomplishing on four-hole bottle; Distillation earlier obtains normal hexane under the condition of normal pressure, reduces pressure-0.09MPa, is cooled to 60 ℃ again and distill out midbody;
(3) get a four-hole bottle again, adding 2900 parts by volume mass concentrations are 97% toluene in four-hole bottle, 29 parts of MAGNESIUM METAL 99s are divided put in the four-hole bottle for 3 times then; Be warming up to 110 ℃ of backflows under the normal pressure, the midbody that obtains at last in the step (2) is added drop-wise in 30min in the four-hole bottle of this step, GC detects; Reduce temperature to 100 ℃; After the raw material complete reaction, suction filtration desalination under protection of nitrogen gas, filtrating joins in this four-hole bottle again;
(4) with 290 mass parts tetramethyl ethylene ketone solution be dissolved in 480 parts by volume mass concentrations be 97% 1, in the 2-ethylene dichloride, in 50min, be added drop-wise to then in the employed four-hole bottle of step (3); Stir, normal pressure is warming up to 80 ℃ of backflows and carries out transesterification reaction, and the n n dimetylaniline gas of generation absorbs with 18% hydrochloric acid; GC monitoring raw material reaction is complete; Suction filtration obtains product, reclaims toluene and 1, the 2-ethylene dichloride after the filtrating rectifying.
Embodiment 2
Join boric acid pinacol ester production technique, comprise the steps:
(1) will be equipped with earlier that to add 2000 parts by volume mass concentrations in the four-hole bottle of mechanical stirring, TM, device for absorbing tail gas and prolong be 98% normal hexane; And stir, feed the boron trichloride gas of 200 mass parts, under 12 ℃, condition of normal pressure; Feed the n n dimetylaniline gas of 480 mass parts; Carry out amination reaction, suction filtration is removed the salt of separating out then, and filtrating joins in the four-hole bottle again;
(2) in above-mentioned filtrating, drip the boron tribromide of 220 mass parts in the time at 60min; Under the normal temperature and pressure, reaction 5h is after reaction is accomplished; On four-hole bottle, load onto rectifying volumn; At 69 ℃, distillation earlier obtains normal hexane under the condition of normal pressure, reduces pressure-0.095MPa, is cooled to 62 ℃ again and distill out midbody;
(3) get a four-hole bottle again, in four-hole bottle, add 3000 parts by volume mass concentrations and be 98% toluene, the MAGNESIUM METAL 99 of 30 mass parts is divided put in the four-hole bottle for 3 times then; Be warming up to 111 ℃ of backflows under the normal pressure, the midbody that obtains at last in the step (2) is added drop-wise in 45min in the four-hole bottle of this step, GC detects; Reduce temperature to 105 ℃; After the raw material complete reaction, suction filtration desalination under protection of nitrogen gas, filtrating joins in this four-hole bottle again;
(4) with 300 mass parts tetramethyl ethylene ketone solution be dissolved in 500 parts by volume mass concentrations be 98% 1, in the 2-ethylene dichloride, in 55min, be added drop-wise to then in the employed four-hole bottle of step (3); Stir, normal pressure is warming up to 85 ℃ of backflows and carries out transesterification reaction, and the n n dimetylaniline gas of generation absorbs with 20% hydrochloric acid; GC monitoring raw material reaction is complete; Suction filtration obtains product, reclaims toluene and 1, the 2-ethylene dichloride after the filtrating rectifying.
Embodiment 3
Join boric acid pinacol ester production technique, comprise the steps:
(1) will be equipped with earlier that to add 2100 parts by volume mass concentrations in the four-hole bottle of mechanical stirring, TM, device for absorbing tail gas and prolong be 99% normal hexane; And stir, feed the boron trichloride gas of 210 mass parts, under 15 ℃, condition of normal pressure; Feed the n n dimetylaniline gas of 490 mass parts; Carry out amination reaction, suction filtration is removed the salt of separating out then, and filtrating joins in the four-hole bottle again;
(2) in 65min, in above-mentioned filtrating, drip the boron tribromide of 230 mass parts, under the normal temperature and pressure, reaction 5.5h; Reaction is loaded onto rectifying volumn, at 70 ℃ after accomplishing on four-hole bottle; Distillation earlier obtains normal hexane under the condition of normal pressure, reduces pressure-0.1MPa, is cooled to 65 ℃ again and distill out midbody;
(3) get a four-hole bottle again, in four-hole bottle, add 3100 parts by volume mass concentrations and be 99% toluene, the MAGNESIUM METAL 99 of 32 mass parts is divided put in the four-hole bottle for 3 times then; Be warming up to 112 ℃ of backflows under the normal pressure, the midbody that obtains at last in the step (2) is added drop-wise in 60min in the four-hole bottle of this step, GC detects; Reduce temperature to 110 ℃; After the raw material complete reaction, suction filtration desalination under protection of nitrogen gas, filtrating joins in this four-hole bottle again;
(4) with 310 mass parts tetramethyl ethylene ketone solution be dissolved in 520 parts by volume mass concentrations be 99% 1, in the 2-ethylene dichloride, in 65min, be added drop-wise to then in the employed four-hole bottle of step 3; Stir, normal pressure is warming up to 90 ℃ of backflows and carries out transesterification reaction, and the n n dimetylaniline gas of generation absorbs with 22% hydrochloric acid; GC monitoring raw material reaction is complete; Suction filtration obtains product, reclaims toluene and 1, the 2-ethylene dichloride after the filtrating rectifying.

Claims (1)

1. join boric acid pinacol ester production technique, it is characterized in that, comprise the steps:
(1) will be equipped with earlier that to add 1900-2100 parts by volume mass concentrations in the four-hole bottle of mechanical stirring, TM, device for absorbing tail gas and prolong be 97-99% normal hexane; And stir, feed the boron trichloride gas of 180-210 mass parts, under 10-15 ℃, condition of normal pressure; Feed the n n dimetylaniline gas of 470-490 mass parts; Carry out amination reaction, suction filtration is removed the salt of separating out then, and filtrating joins in the four-hole bottle again;
(2) in above-mentioned filtrating, drip the boron tribromide of 210-230 mass parts in the time at 55-65min; Under the normal temperature and pressure, reaction 4.5-5.5h is after reaction is accomplished; On four-hole bottle, load onto rectifying volumn; At 68-70 ℃, distillation earlier obtains normal hexane under the condition of normal pressure, reduces pressure-0.09-0.1MPa again, is cooled to 60-65 ℃ and distills out midbody;
(3) get a four-hole bottle again; In four-hole bottle, add 2900-3100 parts by volume mass concentrations and be 97-99% toluene, the MAGNESIUM METAL 99 of 29-32 mass parts is divided put in the four-hole bottle for 3 times then, be warming up to 110-112 ℃ of backflows under the normal pressure; The midbody that obtains at last in the step (2) is added drop-wise in 30-60min in the four-hole bottle of this step; GC detects, and reduces temperature to 100-110 ℃, after the raw material complete reaction; Suction filtration desalination under protection of nitrogen gas, filtrating joins in this four-hole bottle again;
(4) with 290-310 mass parts tetramethyl ethylene ketone solution be dissolved in 480-520 parts by volume mass concentrations be 97-99% 1, in the 2-ethylene dichloride, in 50-65min, be added drop-wise to then in the employed four-hole bottle of step (3); Stir, normal pressure is warming up to 80-90 ℃ of backflows and carries out transesterification reaction, and the n n dimetylaniline gas of generation absorbs with 18-22% hydrochloric acid; GC monitoring raw material reaction is complete; Suction filtration obtains product, reclaims toluene and 1, the 2-ethylene dichloride after the filtrating rectifying.
CN201210007203.4A 2012-01-11 2012-01-11 Bis(pinacolato)diboron production process Active CN102558209B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210007203.4A CN102558209B (en) 2012-01-11 2012-01-11 Bis(pinacolato)diboron production process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210007203.4A CN102558209B (en) 2012-01-11 2012-01-11 Bis(pinacolato)diboron production process

Publications (2)

Publication Number Publication Date
CN102558209A true CN102558209A (en) 2012-07-11
CN102558209B CN102558209B (en) 2014-10-15

Family

ID=46404953

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210007203.4A Active CN102558209B (en) 2012-01-11 2012-01-11 Bis(pinacolato)diboron production process

Country Status (1)

Country Link
CN (1) CN102558209B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104478917A (en) * 2014-12-31 2015-04-01 大连联化化学有限公司 Synthesis method for 1-substitution-1H-pyrazol-4-boric acid pinacol ester
CN105524099A (en) * 2016-01-12 2016-04-27 沧州普瑞东方科技有限公司 Bis(borate) preparation technology
CN111978343A (en) * 2020-09-14 2020-11-24 上海思阔化学科技有限公司 Preparation method of bis-pinacol borate
CN115219635A (en) * 2022-09-20 2022-10-21 广东国标医药科技有限公司 Detection method of pinacol diboron based on gas chromatography
CN116655674A (en) * 2023-01-16 2023-08-29 中国科学院兰州化学物理研究所 Method for synthesizing high-abundance boron 10 isotope biboronate

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002057280A2 (en) * 2001-01-18 2002-07-25 Equistar Chemicals, Lp Method for preparation of boratabenzene derivatives
WO2004076467A1 (en) * 2003-02-28 2004-09-10 Boron Molecular Pty Ltd Preparation of diboronic esters

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002057280A2 (en) * 2001-01-18 2002-07-25 Equistar Chemicals, Lp Method for preparation of boratabenzene derivatives
WO2004076467A1 (en) * 2003-02-28 2004-09-10 Boron Molecular Pty Ltd Preparation of diboronic esters

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
FIONAJ.LAWLOR ET AL.: ""Bis-Catecholate,Bis-Dithiocatecholate,and Tetraalkoxy Diborane(4) Compounds:Aspects of Synthesis and Electronic Structure"", 《INORG.CHEM.》 *
XINYU LIU: ""Bis(pinacolato)diboron"", 《SYNLETT》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104478917A (en) * 2014-12-31 2015-04-01 大连联化化学有限公司 Synthesis method for 1-substitution-1H-pyrazol-4-boric acid pinacol ester
CN105524099A (en) * 2016-01-12 2016-04-27 沧州普瑞东方科技有限公司 Bis(borate) preparation technology
CN111978343A (en) * 2020-09-14 2020-11-24 上海思阔化学科技有限公司 Preparation method of bis-pinacol borate
CN115219635A (en) * 2022-09-20 2022-10-21 广东国标医药科技有限公司 Detection method of pinacol diboron based on gas chromatography
CN115219635B (en) * 2022-09-20 2023-02-17 广东国标医药科技有限公司 Detection method of pinacol diboron based on gas chromatography
CN116655674A (en) * 2023-01-16 2023-08-29 中国科学院兰州化学物理研究所 Method for synthesizing high-abundance boron 10 isotope biboronate
CN116655674B (en) * 2023-01-16 2024-04-16 中国科学院兰州化学物理研究所 Method for synthesizing high-abundance boron 10 isotope biboronate

Also Published As

Publication number Publication date
CN102558209B (en) 2014-10-15

Similar Documents

Publication Publication Date Title
CN102558209A (en) Bis(pinacolato)diboron production process
CN111041203B (en) Mixed extracting agent for nickel-lithium separation and separation method
CN104447299A (en) M-phthaloyl chloride production process and production device thereof
CN102731699B (en) Preparation method of ultra high molecular weight anionic polyacrylamide
CN104387234A (en) Method for synthesizing 3-methyl-3-butene-1-ol
CN103755520B (en) Method for producing substituted benzyl alcohol, substituted benzaldehyde and substituted benzyl acid through oxidizing substituted methylbenzene with air based on gas-liquid-solid heterogeneous reaction separation synchronization reactor
CN104086363A (en) Energy-saving process for recycling n-butyl acetate and butyl alcohol from waste acid water
CN102382221B (en) Phellandrene resin production process
CN103772214A (en) Methods for preparing ethambutol and ethambutol hydrochloride
CN103772327B (en) A kind of extracting process of epoxy chloropropane
CN109134258B (en) Product separation process for preparing methyl glycolate by dimethyl oxalate hydrogenation
CN102031201B (en) Molecular distillation and purification method for conjugated linolenic acid
CN102992959A (en) Method for preparing aluminium isopropoxide by using high water content isopropanol
KR20150025397A (en) Method for preparing 5-hydroxymethyl-2-furfural using metal triflate catalysts under biomass-derived ethylene glycol based solvent condition
CN104004006A (en) Synthetic method of 3,6-dihydro-2H-pyran-4-boronic acid pinacol ester
CN105585451B (en) A kind of method that cyclopentene direct hydration prepares cyclopentanol
CN1733729A (en) 2,6-dimethylpyridine preparation method
MX2013006954A (en) Process for preparing divinylarene oxides.
CN104230972B (en) A kind of method to methyl phenyl ethers anisole-boron trifluoride complex purified treatment
CN102336737B (en) Method for catalytically reducing alkyl-substituted benzocrown ether with Pichler ruthenium
CN102675120A (en) Preparation method of 3, 4-dichloronitrobenzene by solid acid catalyst
CN102659507A (en) Perfluoro alkyl alkane preparation method
CN102212011B (en) Method for preventing nitration product rectifying tower from exploding
CN105418537A (en) Synthetic method of 2-methoxy phenothiazine
CN105435650A (en) Preparation method of polyvinylidene fluoride separation membrane

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