WO2004043898A1 - A process for the mononitration of alkanediols - Google Patents
A process for the mononitration of alkanediols Download PDFInfo
- Publication number
- WO2004043898A1 WO2004043898A1 PCT/EP2003/012376 EP0312376W WO2004043898A1 WO 2004043898 A1 WO2004043898 A1 WO 2004043898A1 EP 0312376 W EP0312376 W EP 0312376W WO 2004043898 A1 WO2004043898 A1 WO 2004043898A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- nitric acid
- formula
- stabilised
- mononitrate
- compound
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 24
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 39
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 35
- 150000001875 compounds Chemical class 0.000 claims abstract description 29
- 238000006396 nitration reaction Methods 0.000 claims abstract description 10
- 238000002360 preparation method Methods 0.000 claims abstract description 8
- 125000002947 alkylene group Chemical group 0.000 claims abstract description 5
- 229910004679 ONO2 Inorganic materials 0.000 claims abstract description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 36
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims description 20
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 11
- FBOGSWRRYABFKU-UHFFFAOYSA-N 4-hydroxybutyl nitrate Chemical compound OCCCCO[N+]([O-])=O FBOGSWRRYABFKU-UHFFFAOYSA-N 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 10
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 8
- 239000004202 carbamide Substances 0.000 claims description 8
- 239000002904 solvent Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000003960 organic solvent Substances 0.000 claims description 4
- SEADOCMODJSLKS-UHFFFAOYSA-N 1-hydroxyethyl nitrate Chemical compound CC(O)O[N+]([O-])=O SEADOCMODJSLKS-UHFFFAOYSA-N 0.000 claims description 3
- PTMLFFXFTRSBJW-UHFFFAOYSA-N 3-hydroxypropyl nitrate Chemical compound OCCCO[N+]([O-])=O PTMLFFXFTRSBJW-UHFFFAOYSA-N 0.000 claims description 3
- DVOSRLSVEOCANS-UHFFFAOYSA-N 5-hydroxypentyl nitrate Chemical compound OCCCCCO[N+]([O-])=O DVOSRLSVEOCANS-UHFFFAOYSA-N 0.000 claims description 3
- RWHOTTRMDQXOPY-UHFFFAOYSA-N 6-hydroxyhexyl nitrate Chemical compound OCCCCCCO[N+]([O-])=O RWHOTTRMDQXOPY-UHFFFAOYSA-N 0.000 claims description 3
- 238000010790 dilution Methods 0.000 claims description 2
- 239000012895 dilution Substances 0.000 claims description 2
- 229930195733 hydrocarbon Natural products 0.000 claims description 2
- LNOPIUAQISRISI-UHFFFAOYSA-N n'-hydroxy-2-propan-2-ylsulfonylethanimidamide Chemical compound CC(C)S(=O)(=O)CC(N)=NO LNOPIUAQISRISI-UHFFFAOYSA-N 0.000 claims description 2
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- CDQSJQSWAWPGKG-UHFFFAOYSA-N butane-1,1-diol Chemical compound CCCC(O)O CDQSJQSWAWPGKG-UHFFFAOYSA-N 0.000 claims 1
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 21
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 239000000243 solution Substances 0.000 description 8
- 239000003795 chemical substances by application Substances 0.000 description 7
- 229940021182 non-steroidal anti-inflammatory drug Drugs 0.000 description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000041 non-steroidal anti-inflammatory agent Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- QELUAJBXJAWSRC-UHFFFAOYSA-N 4-nitrooxybutyl nitrate Chemical compound [O-][N+](=O)OCCCCO[N+]([O-])=O QELUAJBXJAWSRC-UHFFFAOYSA-N 0.000 description 3
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000012074 organic phase Substances 0.000 description 3
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000012045 crude solution Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- -1 diol compounds Chemical class 0.000 description 2
- 150000002009 diols Chemical class 0.000 description 2
- 231100001261 hazardous Toxicity 0.000 description 2
- 230000000802 nitrating effect Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000004448 titration Methods 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 1
- 206010059024 Gastrointestinal toxicity Diseases 0.000 description 1
- CMWTZPSULFXXJA-UHFFFAOYSA-N Naproxen Natural products C1=C(C(C)C(O)=O)C=CC2=CC(OC)=CC=C21 CMWTZPSULFXXJA-UHFFFAOYSA-N 0.000 description 1
- SNIOPGDIGTZGOP-UHFFFAOYSA-N Nitroglycerin Chemical compound [O-][N+](=O)OCC(O[N+]([O-])=O)CO[N+]([O-])=O SNIOPGDIGTZGOP-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000003110 anti-inflammatory effect Effects 0.000 description 1
- 230000001754 anti-pyretic effect Effects 0.000 description 1
- 239000002221 antipyretic Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 229950005499 carbon tetrachloride Drugs 0.000 description 1
- 229960001701 chloroform Drugs 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 229960001259 diclofenac Drugs 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 231100000414 gastrointestinal toxicity Toxicity 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 229960003711 glyceryl trinitrate Drugs 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 229960001680 ibuprofen Drugs 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 229960000991 ketoprofen Drugs 0.000 description 1
- 229960002009 naproxen Drugs 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000000144 pharmacologic effect Effects 0.000 description 1
- 229910001961 silver nitrate Inorganic materials 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
- 238000011179 visual inspection Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/20—Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
- C01B21/38—Nitric acid
- C01B21/46—Purification; Separation ; Stabilisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C201/00—Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
- C07C201/02—Preparation of esters of nitric acid
Definitions
- the present invention provides an efficient process for the mononitration of alkanediols, which is easily controllable and safe to operators.
- the invention provides a process for industrial scale production of compounds of formula wherein A is a straight or branched C 2 -C 6 alkylene chain.
- NO-NSAIDs NO-releasing non steroidal anti inflammatory drugs
- NO-NSAIDs are NO-acetylsalicylic acid, NO-diclofenac, NO- naproxen, NO-ketoprofen and NO-ibuprofen.
- NO-NSAIDs have antipyretic and anti-inflammatory activity, but show reduced gastrointestinal toxicity and are endowed with further useful pharmacological properties.
- WO 98/25918 and WO 01/10814 in particular disclose the use of compounds of formula (I) in the preparation of NO-NSAIDs.
- alkanediols of formula (I) The mononitration of alkanediols of formula (I) with the above methods is very poorly selective and troublesome on an industrial scale. In particular, dangerous decompositions easily occur, since a strong oxidizing agent (nitric acid) is contacted with extremely unstable substrates, in particular with alkanediols wherein A is a C 2 -C alkylene chain.
- a strong oxidizing agent nitric acid
- Object of the present invention is therefore a process for the preparation of a compound of formula:
- Preferred compounds of formula (I) obtainable with the process of the invention are ethanediol-mononitrate; 1,3-propanediol-mononitrate; 1,4- butanediol-mononitrate; 1,5-pentanediol-mononitrate or 1,6-hexanediol- mononitrate, more preferably 1,4-butanediol-mononitrate.
- the term "stabilised nitric acid” means a specific preparation of nitric acid, which is a further object of the invention. This preparation consists of nitric acid diluted in water to a concentration of about 83 - 85%, preferably about 84.5 - 84.8% w/w, and is substantially free from nitrous acid and nitrogen oxides.
- the expression “substantially free from nitrous acid and nitrogen oxides” means that the concentration of nitrous acid and nitrogen oxides is typically lower than 10 p.p.m., preferably lower than 5 p.p.m.
- Stabilization of nitric acid can be achieved by a process which comprises dilution of fuming nitric acid with water and treatment of the diluted nitric acid with an agent able to remove nitrous acid and nitrogen oxides (hereinafter referred to as "(the) agent/s"). It will be appreciated that the same result can also be obtained by adding an aqueous solution of the agent to fuming nitric acid.
- agents are urea and sulfamic acid, preferably urea.
- the contact time of the agents with nitric acid and their amount should be sufficient to make the nitric acid substantially free from the nitrous acid and nitrogen oxides, but should not salify an excessive amount of nitric acid, as this would lower the titre and the nitrating power.
- the absence of nitrogen oxides and nitrous acid in the "stabilised" nitric acid can be evaluated, for example, by visual inspection (colour), as well as by permanganate titration.
- Stabilised nitric acid is prepared by adding 83 - 85% w/w nitric acid (which usually contains from about 0.06 to about 0.12% of nitrous acid and nitrogen oxides) with an amount of agent ranging from about 0.3 to about 1% w/w. To completely remove nitrous acid and nitrogen oxides the time contact with nitric acid ranges from about 80 minutes to about 130 minutes.
- the amount typically ranges from about 0.6 to about 1% w/w, preferably from about 0.7 to about 1% w/w and the time contact is preferably from about 95 to about 120 minutes.
- the "stabilised” nitric acid according to the invention must be used within about three hours from stabilization, as relevant amounts of nitrous acid and nitrogen oxides are released again over time.
- chlorinated solvent a water-immiscible chlorinated organic solvent
- chlorinated solvents are mono-, di-, tri- and tetra-chloro C*-C 4 alkyl hydrocarbons, preferably dichloromethane, trichloromethane, tetrachloromethane, trichloroethane and tetrachloroethane, in particular dichloromethane.
- the reaction is preferably carried out by contacting a solution of the compound of formula (II) in a chlorinated solvent, with "stabilised” nitric acid dispersed in the same solvent.
- the solution of the compound of formula (II) should be as homogeneous as possible.
- a homogeneous solution of 1 ,4-butanediol in dichloromethane can be obtained at concentrations ranging from about 60 to about 75%, preferably from about 65 to about 70% w/w.
- the weight ratio of "stabilised” nitric acid to compounds of formula (II) ranges from about 10 : 1 to about 15 : 1, depending on the characteristics of the compound of formula (II).
- the weight ratio of "stabilised" nitric acid to 1,4-butanediol preferably ranges from about 1 1 : 1 to about 14.5 : 1.
- the concentration of 1,4-butanediol in the nitration mixture ranges from about 2.1 to about 2.8% w/w, preferably from about 2.3 to about 2.6% w/w.
- the mononitration of compounds of formula (II) is carried out at a reaction temperature lower than room temperature, preferably equal to or lower than 0°C, more preferably at 0°C, for reaction times ranging from about 10 to about 30 minutes, preferably from about 15 to about 20 minutes.
- the progress of the reaction can be monitored with conventional analytical methods and the optimal reaction time can thus be determined.
- the reaction is typically quenched with cold water (precooled to a temperature lower than about 6°C, preferably lower than about 3°C).
- the process of the invention allows to obtain the compounds of formula (I) in advantageous yields from the industrial standpoint and is definitely less hazardous than nitration with concentrated nitric acid, and optionally sulfuric acid, in the presence of urea.
- the mononitration of 1,4-butanediol according to the invention affords 1 ,4-butanediol mononitrate with molar yield ranging from about 30% to about 40%, with a selectivity, expressed as percentage ratio 1,4-butanediol mononitrate/( 1,4-butanediol mononitrate + 1,4-butanediol dinitrate) equal to about 70-75%).
- the nitration mixture which is a further object of the invention, is a crude mixture dispersed in the organic chlorinated solvent comprising the compound of formula (I), in amount of about 2% w/w, the corresponding dinitrate by-product, the unreacted compound of formula (II) and unreacted nitric acid, and other by-products deriving from dehydration and/or oxidation.
- the nitration mixture is first partially neutralized with a concentrated sodium hydroxide solution. Most of the unreacted compound of formula (II) is extracted in the resulting aqueous sodium nitrate solution. The organic phase is then concentrated by evaporation of the solvent and neutralized with a diluted sodium carbonate or sodium hydroxide solution.
- the mixture in said chlorinated organic solvent generally contains a compound of formula (I) in amount approx. ranging from 11% to 15% w/w, the corresponding dinitrated by-product in amount approx. ranging from 3 to 4, 5% w/w; and the corresponding diol of formula (II) in amount approx. ranging from 0.2 to 0.8% w/w [compared with the compound of formula (I)].
- Mixtures with total nitroesters concentrations higher than 15% w/w have explosive characteristics and are potentially hazardous to operators.
- the compounds of formula (I) can be separated from the corresponding dinitrated by-products and from traces of the corresponding diols of formula (II) according to known methods. The following examples further illustrate the invention.
- a stainless steel reactor equipped with condenser and stirrer, is loaded with 90 kg of diluted nitric acid (84.7%) having a nitrous acid content of about 0,09%) and 675 g of urea beads is added under stirring. After about 90 minutes, removal of nitrous acid and nitrogen oxides is controlled by colour inspection and permanganate titration. If necessary, further urea is added in small portions.
- a stainless steel reactor is loaded in succession with 931 g of dichloromethane and 385 g of "stabilised" nitric acid.
- the dispersion is cooled to about 0°C under stirring, thereafter 50 g of 1 ,4-butanediol in dichloromethane (70/30) is added in a single portion.
- the reaction mixture is kept under stirring at a temperature ranging from about -2°C to 2°C.
- the kinetics of the nitration is monitored by taking samples of the mixture during the reaction. After 20 minutes the reaction is quickly quenched by pouring it into a water/ice mixture (385 g), then neutralized with 433 g of 40% NaOH, keeping the temperature below 15°C.
- the organic phase (980 g), which contains 1,4-butanediol-mononitrate (19.2 g), 1,4-butanediol-dinitrate (6.4 g) and 1,4-butanediol (0.1 g), is separated and concentrated to 15%.
- the molar yield of 1,4-butanediol-mononitrate in the crude solution amounts to 36.6%.
- the solution is then subjected to the subsequent purification.
- the following compounds can also be obtained through the same procedure: ethanediol-mononitrate, 1 ,3-propanediol-mononitrate, 1 ,5-pentanediol- mononitrate and 1,6-hexanediol-mononitrate.
- the reactor is loaded with 21.78 kg of dichloromethane and 9 kg of "stabilised" nitric acid.
- the mixture is cooled to -5-0°C, then 1.26 kg of a mixture of 1,4-butanediol (0.819 kg) in dichloromethane (0.441 kg) is added under vigorous stirring in a single portion.
- the reaction is rapidly quenched in water (9 kg), precooled at 2°C.
- the solution is then neutralized with 40% sodium hydroxide (9 kg).
- the organic phase (23 kg), which contains 1,4-butanediol-mononitrate (0.46 kg), 1,4-butanediol-dinitrate (0.155 kg) and 1 ,4-butanediol (0.002 kg), is separated and concentrated to 15%.
- the molar yield of 1 ,4-butanediol- mononitrate in the crude solution amounts to 37.4%.
- the solution is then subjected to the subsequent purification.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Light Receiving Elements (AREA)
- Saccharide Compounds (AREA)
Abstract
Description
Claims
Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK03772310T DK1560804T3 (en) | 2002-11-14 | 2003-11-06 | Process for mononitration of alkanediols |
JP2004550944A JP2006506418A (en) | 2002-11-14 | 2003-11-06 | Mononitration of alkanediol |
AT03772310T ATE430121T1 (en) | 2002-11-14 | 2003-11-06 | METHOD FOR MONONITRATION OF ALKANDIOLS |
EP03772310A EP1560804B1 (en) | 2002-11-14 | 2003-11-06 | A process for the mononitration of alkanediols |
DE60327457T DE60327457D1 (en) | 2002-11-14 | 2003-11-06 | METHOD FOR MONONITRATING ALKANDIOLS |
AU2003279363A AU2003279363A1 (en) | 2002-11-14 | 2003-11-06 | A process for the mononitration of alkanediols |
US10/534,868 US7335789B2 (en) | 2002-11-14 | 2003-11-06 | Process for the mononitration of alkanediols |
HR20050413A HRP20050413A2 (en) | 2002-11-14 | 2005-05-10 | A process for the mononitration of alkanediols |
IL168541A IL168541A (en) | 2002-11-14 | 2005-05-11 | Process for the mononitration of alkanediols |
NO20052328A NO20052328L (en) | 2002-11-14 | 2005-05-12 | Process for the mononitration of alkanediols |
US12/036,555 US7851649B2 (en) | 2002-11-14 | 2008-02-25 | Process for the mononitration of alkanediols |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITMI2002A002410 | 2002-11-14 | ||
IT002410A ITMI20022410A1 (en) | 2002-11-14 | 2002-11-14 | PROCEDURE FOR THE NITRATION OF ALCANDIOLI. |
Related Child Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10534868 A-371-Of-International | 2003-11-06 | ||
US12/036,555 Continuation US7851649B2 (en) | 2002-11-14 | 2008-02-25 | Process for the mononitration of alkanediols |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2004043898A1 true WO2004043898A1 (en) | 2004-05-27 |
Family
ID=32310162
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2003/012376 WO2004043898A1 (en) | 2002-11-14 | 2003-11-06 | A process for the mononitration of alkanediols |
Country Status (15)
Country | Link |
---|---|
US (2) | US7335789B2 (en) |
EP (1) | EP1560804B1 (en) |
JP (1) | JP2006506418A (en) |
AT (1) | ATE430121T1 (en) |
AU (1) | AU2003279363A1 (en) |
DE (1) | DE60327457D1 (en) |
DK (1) | DK1560804T3 (en) |
ES (1) | ES2322897T3 (en) |
HR (1) | HRP20050413A2 (en) |
IL (1) | IL168541A (en) |
IT (1) | ITMI20022410A1 (en) |
NO (1) | NO20052328L (en) |
PL (1) | PL377000A1 (en) |
PT (1) | PT1560804E (en) |
WO (1) | WO2004043898A1 (en) |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006182671A (en) * | 2004-12-27 | 2006-07-13 | Tokuyama Corp | Method for producing nitric acid ester |
JP2008521770A (en) * | 2004-11-25 | 2008-06-26 | ニコックス エス エイ | Method for producing halogenoalkyl nitrate |
WO2009000723A1 (en) | 2007-06-28 | 2008-12-31 | Nicox S.A. | Process for preparing 1,4-butandiol mononitrate |
WO2009080755A1 (en) | 2007-12-20 | 2009-07-02 | Dsm Fine Chemicals Austria Nfg Gmbh & Co Kg | Formation of nitrate esters in microreactors and millireactors using a continuous product extraction in a turbulent flow regime |
WO2019145346A1 (en) | 2018-01-24 | 2019-08-01 | Dsm Ip Assets B.V. | Novel use |
WO2019145345A1 (en) | 2018-01-24 | 2019-08-01 | Dsm Ip Assets B.V. | Novel use |
CN110467920A (en) * | 2019-08-16 | 2019-11-19 | 紫光宏茂微电子(上海)有限公司 | A kind of separation of 3D Stacked Die Packaging component chip corrosive agent and separation method |
WO2020053194A1 (en) | 2018-09-14 | 2020-03-19 | Dsm Ip Assets B.V. | Process for the manufacture of omega nitrooxy-1-alkanols |
WO2020053193A1 (en) | 2018-09-14 | 2020-03-19 | Dsm Ip Assets B.V. | Process for the manufacture of omega nitrooxy-1-alkanols |
WO2020212348A1 (en) | 2019-04-16 | 2020-10-22 | Dsm Ip Assets B.V. | Early life nutrition |
WO2022218963A1 (en) | 2021-04-15 | 2022-10-20 | Dsm Ip Assets B.V. | Novel use |
WO2022218780A1 (en) | 2021-04-13 | 2022-10-20 | Dsm Ip Assets B.V. | Method for monitoring the use of a methane inhibitor |
WO2022218965A1 (en) | 2021-04-15 | 2022-10-20 | Dsm Ip Assets B.V. | Use of gossypol and propandiol mononitrate for reducing the formation of methane emanating from the digestive activites of ruminants |
WO2022218967A1 (en) | 2021-04-15 | 2022-10-20 | Dsm Ip Assets B.V. | Use of gossypol and a methane inhibitor for reducing the formation of methane emanating from the digestive activities of ruminants |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004007706A1 (en) * | 2004-02-16 | 2005-08-25 | Dynamit Nobel Gmbh Explosivstoff- Und Systemtechnik | Liquid nitrate esters production by esterifying alcohols with nitrating acid is effected in a microreactor to give improved safety |
EP2048129A1 (en) * | 2007-10-12 | 2009-04-15 | Lonza Ag | Method for the preparation of organic nitrates |
CN107986250B (en) * | 2017-10-31 | 2020-08-04 | 湖北东方化工有限公司 | Concentration device for treating low-concentration dilute nitric acid by nitrotoluene waste sulfuric acid |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1040139A (en) * | 1962-06-07 | 1966-08-24 | Nitrochemie Gmbh | A method of partially nitrating polyhydric alcohols |
DE2039609A1 (en) * | 1970-06-30 | 1972-02-17 | Council Scient Ind Res | Nitration of glycol ethers - to give alkyl nitrate esters for improving cetane ratings of diesel fuels |
US5162568A (en) * | 1983-11-21 | 1992-11-10 | E. I. Du Pont De Nemours And Company | Nitration of alkanols |
EP1038862A2 (en) * | 1999-03-26 | 2000-09-27 | Dinamite Dipharma S.p.A. | Process for the preparation of nitric monoesters of dihydroxyalkyl, dihydroxycycloalkyl and dihydroxy(poly)cycloalkyl compounds |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1596622A (en) * | 1921-02-18 | 1926-08-17 | Silica Gel Corp | Stabilizer for nitrated organic compounds |
US2294849A (en) * | 1938-08-20 | 1942-09-01 | Sharples Chemicals Inc | Manufacture of nitric acid esters |
US2760845A (en) * | 1953-05-04 | 1956-08-28 | North American Aviation Inc | Stabilized fuming nitric acid |
US2981617A (en) * | 1957-06-25 | 1961-04-25 | Karl F Hager | Inhibited fuming nitric acids |
US3019081A (en) * | 1959-07-17 | 1962-01-30 | Phillips Petroleum Co | Stabilized nitric acid |
US3113836A (en) * | 1959-08-12 | 1963-12-10 | Phillips Petroleum Co | Stabilized nitric acid |
US3063945A (en) * | 1959-08-12 | 1962-11-13 | Phillips Petroleum Co | Stabilized nitric acid |
US5741432A (en) * | 1995-01-17 | 1998-04-21 | The Dexter Corporation | Stabilized nitric acid compositions |
DE19515970A1 (en) * | 1995-05-02 | 1996-11-07 | Bayer Ag | Acetylsalicylsäurenitrate |
-
2002
- 2002-11-14 IT IT002410A patent/ITMI20022410A1/en unknown
-
2003
- 2003-11-06 DE DE60327457T patent/DE60327457D1/en not_active Expired - Lifetime
- 2003-11-06 ES ES03772310T patent/ES2322897T3/en not_active Expired - Lifetime
- 2003-11-06 DK DK03772310T patent/DK1560804T3/en active
- 2003-11-06 JP JP2004550944A patent/JP2006506418A/en not_active Ceased
- 2003-11-06 US US10/534,868 patent/US7335789B2/en not_active Expired - Fee Related
- 2003-11-06 AT AT03772310T patent/ATE430121T1/en active
- 2003-11-06 EP EP03772310A patent/EP1560804B1/en not_active Expired - Lifetime
- 2003-11-06 PT PT03772310T patent/PT1560804E/en unknown
- 2003-11-06 PL PL377000A patent/PL377000A1/en not_active Application Discontinuation
- 2003-11-06 AU AU2003279363A patent/AU2003279363A1/en not_active Abandoned
- 2003-11-06 WO PCT/EP2003/012376 patent/WO2004043898A1/en active Application Filing
-
2005
- 2005-05-10 HR HR20050413A patent/HRP20050413A2/en not_active Application Discontinuation
- 2005-05-11 IL IL168541A patent/IL168541A/en not_active IP Right Cessation
- 2005-05-12 NO NO20052328A patent/NO20052328L/en not_active Application Discontinuation
-
2008
- 2008-02-25 US US12/036,555 patent/US7851649B2/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1040139A (en) * | 1962-06-07 | 1966-08-24 | Nitrochemie Gmbh | A method of partially nitrating polyhydric alcohols |
DE2039609A1 (en) * | 1970-06-30 | 1972-02-17 | Council Scient Ind Res | Nitration of glycol ethers - to give alkyl nitrate esters for improving cetane ratings of diesel fuels |
US5162568A (en) * | 1983-11-21 | 1992-11-10 | E. I. Du Pont De Nemours And Company | Nitration of alkanols |
EP1038862A2 (en) * | 1999-03-26 | 2000-09-27 | Dinamite Dipharma S.p.A. | Process for the preparation of nitric monoesters of dihydroxyalkyl, dihydroxycycloalkyl and dihydroxy(poly)cycloalkyl compounds |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008521770A (en) * | 2004-11-25 | 2008-06-26 | ニコックス エス エイ | Method for producing halogenoalkyl nitrate |
JP4587374B2 (en) * | 2004-12-27 | 2010-11-24 | 株式会社トクヤマ | Method for producing nitrate ester |
JP2006182671A (en) * | 2004-12-27 | 2006-07-13 | Tokuyama Corp | Method for producing nitric acid ester |
WO2009000723A1 (en) | 2007-06-28 | 2008-12-31 | Nicox S.A. | Process for preparing 1,4-butandiol mononitrate |
CN101903328B (en) * | 2007-12-20 | 2013-05-15 | Dsm精细化学奥地利Nfg两合公司 | Formation of nitrate esters in microreactors and millireactors using a continuous product extraction in a turbulent flow regime |
CN101903328A (en) * | 2007-12-20 | 2010-12-01 | Dsm精细化学奥地利Nfg两合公司 | Utilize the continuous product extraction under the turbulent model in microreactor and milli reactor, to form nitric ether |
US8536366B2 (en) | 2007-12-20 | 2013-09-17 | Dsm Fine Chemicals Austria Nfg Gmbh & Co Kg | Formation of nitrate esters in microreactors and millireactors using a continuous product extraction in a turbulent flow regime |
WO2009080755A1 (en) | 2007-12-20 | 2009-07-02 | Dsm Fine Chemicals Austria Nfg Gmbh & Co Kg | Formation of nitrate esters in microreactors and millireactors using a continuous product extraction in a turbulent flow regime |
US11712424B2 (en) | 2018-01-24 | 2023-08-01 | Dsm Ip Assets B.V. | Non-therapeutic methods for alleviating or reducing stress symptoms of ruminants |
WO2019145346A1 (en) | 2018-01-24 | 2019-08-01 | Dsm Ip Assets B.V. | Novel use |
WO2019145345A1 (en) | 2018-01-24 | 2019-08-01 | Dsm Ip Assets B.V. | Novel use |
WO2020053194A1 (en) | 2018-09-14 | 2020-03-19 | Dsm Ip Assets B.V. | Process for the manufacture of omega nitrooxy-1-alkanols |
WO2020053193A1 (en) | 2018-09-14 | 2020-03-19 | Dsm Ip Assets B.V. | Process for the manufacture of omega nitrooxy-1-alkanols |
CN112702923A (en) * | 2018-09-14 | 2021-04-23 | 帝斯曼知识产权资产管理有限公司 | Method for preparing omega-nitrooxy-1-alkanol |
WO2020212348A1 (en) | 2019-04-16 | 2020-10-22 | Dsm Ip Assets B.V. | Early life nutrition |
CN110467920A (en) * | 2019-08-16 | 2019-11-19 | 紫光宏茂微电子(上海)有限公司 | A kind of separation of 3D Stacked Die Packaging component chip corrosive agent and separation method |
WO2022218780A1 (en) | 2021-04-13 | 2022-10-20 | Dsm Ip Assets B.V. | Method for monitoring the use of a methane inhibitor |
WO2022218965A1 (en) | 2021-04-15 | 2022-10-20 | Dsm Ip Assets B.V. | Use of gossypol and propandiol mononitrate for reducing the formation of methane emanating from the digestive activites of ruminants |
WO2022218967A1 (en) | 2021-04-15 | 2022-10-20 | Dsm Ip Assets B.V. | Use of gossypol and a methane inhibitor for reducing the formation of methane emanating from the digestive activities of ruminants |
WO2022218966A1 (en) | 2021-04-15 | 2022-10-20 | Dsm Ip Assets B.V. | Use of propandiol mononitrate and limonene for reducing the formation of methane emanating and for improving the digestibility |
WO2022218963A1 (en) | 2021-04-15 | 2022-10-20 | Dsm Ip Assets B.V. | Novel use |
Also Published As
Publication number | Publication date |
---|---|
ES2322897T3 (en) | 2009-07-01 |
HRP20050413A2 (en) | 2005-06-30 |
DK1560804T3 (en) | 2009-07-20 |
AU2003279363A1 (en) | 2004-06-03 |
DE60327457D1 (en) | 2009-06-10 |
US7851649B2 (en) | 2010-12-14 |
ITMI20022410A1 (en) | 2004-05-15 |
IL168541A (en) | 2010-04-15 |
NO20052328D0 (en) | 2005-05-12 |
EP1560804B1 (en) | 2009-04-29 |
US7335789B2 (en) | 2008-02-26 |
PT1560804E (en) | 2009-06-02 |
EP1560804A1 (en) | 2005-08-10 |
NO20052328L (en) | 2005-05-12 |
JP2006506418A (en) | 2006-02-23 |
US20060128983A1 (en) | 2006-06-15 |
ATE430121T1 (en) | 2009-05-15 |
PL377000A1 (en) | 2006-01-23 |
US20080146830A1 (en) | 2008-06-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7851649B2 (en) | Process for the mononitration of alkanediols | |
ES2552760T3 (en) | Method for the production of dinitrotoluene | |
Castellan et al. | Nitric acid reaction of cyclohexanol to adipic acid | |
US20150166461A1 (en) | Process for the preparation of nitrated aromatics and mixtures thereof | |
US4918250A (en) | Process for the production of dinitrotoluene using an inorganic salt as a phase separation agent | |
US7947855B2 (en) | Process for the purification of 1,4-butanediol mononitrate | |
EP3849340B1 (en) | Process for the manufacture of omega nitrooxy-1-alkanols | |
US5089652A (en) | Nitrate ester preparation | |
US5354924A (en) | Process for the production of dinitrotoluene | |
JP3179930B2 (en) | Method for producing aromatic nitro compound | |
US5576463A (en) | Process for the preparation of 2-nitrobenzaldehydes | |
US4788346A (en) | Process for the preparation of para-nitrophenol | |
EP0169441B1 (en) | Production of dinitrotoluene | |
CN114364655A (en) | Preparation method of nitric acid alpha-methyl- [4- (nitro) -2- (trifluoromethyl) ] -benzyl ester | |
GB2318116A (en) | Nitration of Diphenoxy compounds | |
KR0164447B1 (en) | Process for nitration of aromatic compound | |
JPH03291241A (en) | Production of 2,6-dichloro-substituted phenol | |
WO1998008786A1 (en) | Nitration system, and method for nitration of aromatic compounds | |
CA2138391A1 (en) | Process for the production of dinitrotoluene | |
IL47244A (en) | Process for the mononitration of ortho-xylene | |
PL154456B1 (en) | Method for manufacturing chlornitrobenzene |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): BW GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: P20050413A Country of ref document: HR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 168541 Country of ref document: IL |
|
WWE | Wipo information: entry into national phase |
Ref document number: 377000 Country of ref document: PL Ref document number: 2004550944 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2003772310 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 2003772310 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: 2006128983 Country of ref document: US Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 10534868 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 10534868 Country of ref document: US |