NO158433B - AXIAL PUMP PUMP DRIVE MECHANISM. - Google Patents
AXIAL PUMP PUMP DRIVE MECHANISM. Download PDFInfo
- Publication number
- NO158433B NO158433B NO821441A NO821441A NO158433B NO 158433 B NO158433 B NO 158433B NO 821441 A NO821441 A NO 821441A NO 821441 A NO821441 A NO 821441A NO 158433 B NO158433 B NO 158433B
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- Norway
- Prior art keywords
- drive member
- reaction
- axis
- barrel
- acid
- Prior art date
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- 239000002253 acid Substances 0.000 claims description 23
- 239000003054 catalyst Substances 0.000 claims description 18
- MBYBMQAKTSFTJP-UHFFFAOYSA-N 2-(cyanomethoxy)acetic acid Chemical class OC(=O)COCC#N MBYBMQAKTSFTJP-UHFFFAOYSA-N 0.000 claims description 17
- 150000007513 acids Chemical class 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 11
- JLPJFSCQKHRSQR-UHFFFAOYSA-N oxolan-3-one Chemical class O=C1CCOC1 JLPJFSCQKHRSQR-UHFFFAOYSA-N 0.000 claims description 9
- 239000012429 reaction media Substances 0.000 claims description 9
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 8
- 230000032050 esterification Effects 0.000 claims description 8
- 238000005886 esterification reaction Methods 0.000 claims description 8
- 125000002560 nitrile group Chemical group 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000003385 ring cleavage reaction Methods 0.000 claims description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 239000003960 organic solvent Substances 0.000 claims description 4
- 238000005809 transesterification reaction Methods 0.000 claims description 4
- 238000005661 deetherification reaction Methods 0.000 claims description 3
- 230000007062 hydrolysis Effects 0.000 claims description 3
- 238000006460 hydrolysis reaction Methods 0.000 claims description 3
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 38
- 238000006243 chemical reaction Methods 0.000 description 34
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 21
- 239000000047 product Substances 0.000 description 19
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 13
- 238000006146 oximation reaction Methods 0.000 description 13
- 235000011121 sodium hydroxide Nutrition 0.000 description 13
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 12
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- 238000001953 recrystallisation Methods 0.000 description 7
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 6
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 6
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 6
- 230000008707 rearrangement Effects 0.000 description 6
- 238000007127 saponification reaction Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- HWFLEGUPVIFSJN-UHFFFAOYSA-N 2,2,5,5-tetramethyloxolan-3-one Chemical compound CC1(C)CC(=O)C(C)(C)O1 HWFLEGUPVIFSJN-UHFFFAOYSA-N 0.000 description 5
- 229910021529 ammonia Inorganic materials 0.000 description 5
- 150000002148 esters Chemical class 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- 125000001142 dicarboxylic acid group Chemical group 0.000 description 4
- 230000035484 reaction time Effects 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- QEVGZEDELICMKH-UHFFFAOYSA-N Diglycolic acid Chemical compound OC(=O)COCC(O)=O QEVGZEDELICMKH-UHFFFAOYSA-N 0.000 description 3
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N acetic acid Substances CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 3
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 150000002576 ketones Chemical class 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- MXAJVDHGJCYEKL-UHFFFAOYSA-N morpholine-3,5-dione Chemical compound O=C1COCC(=O)N1 MXAJVDHGJCYEKL-UHFFFAOYSA-N 0.000 description 3
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 3
- 150000002923 oximes Chemical class 0.000 description 3
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- HORQAOAYAYGIBM-UHFFFAOYSA-N 2,4-dinitrophenylhydrazine Chemical compound NNC1=CC=C([N+]([O-])=O)C=C1[N+]([O-])=O HORQAOAYAYGIBM-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001447 alkali salts Chemical class 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- 150000003949 imides Chemical class 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- -1 oxime salt Chemical class 0.000 description 2
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- FYSNRJHAOHDILO-UHFFFAOYSA-N thionyl chloride Chemical compound ClS(Cl)=O FYSNRJHAOHDILO-UHFFFAOYSA-N 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- MCSXGCZMEPXKIW-UHFFFAOYSA-N 3-hydroxy-4-[(4-methyl-2-nitrophenyl)diazenyl]-N-(3-nitrophenyl)naphthalene-2-carboxamide Chemical compound Cc1ccc(N=Nc2c(O)c(cc3ccccc23)C(=O)Nc2cccc(c2)[N+]([O-])=O)c(c1)[N+]([O-])=O MCSXGCZMEPXKIW-UHFFFAOYSA-N 0.000 description 1
- 229910015900 BF3 Inorganic materials 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 229910006124 SOCl2 Inorganic materials 0.000 description 1
- 229910003074 TiCl4 Inorganic materials 0.000 description 1
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 229960003116 amyl nitrite Drugs 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 239000011260 aqueous acid Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- VEFXTGTZJOWDOF-UHFFFAOYSA-N benzene;hydrate Chemical compound O.C1=CC=CC=C1 VEFXTGTZJOWDOF-UHFFFAOYSA-N 0.000 description 1
- IYMAUEAFOBSGCY-UHFFFAOYSA-N benzene;sulfurochloridic acid Chemical compound OS(Cl)(=O)=O.C1=CC=CC=C1 IYMAUEAFOBSGCY-UHFFFAOYSA-N 0.000 description 1
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- VAYGXNSJCAHWJZ-UHFFFAOYSA-N dimethyl sulfate Chemical compound COS(=O)(=O)OC VAYGXNSJCAHWJZ-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012259 ether extract Substances 0.000 description 1
- 125000004494 ethyl ester group Chemical group 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 150000002430 hydrocarbons Chemical group 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 239000011499 joint compound Substances 0.000 description 1
- 125000000468 ketone group Chemical group 0.000 description 1
- 150000007517 lewis acids Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- CSDTZUBPSYWZDX-UHFFFAOYSA-N n-pentyl nitrite Chemical compound CCCCCON=O CSDTZUBPSYWZDX-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002927 oxygen compounds Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M potassium chloride Inorganic materials [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- QDRKDTQENPPHOJ-UHFFFAOYSA-N sodium ethoxide Chemical compound [Na+].CC[O-] QDRKDTQENPPHOJ-UHFFFAOYSA-N 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 239000000375 suspending agent Substances 0.000 description 1
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 description 1
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 description 1
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B1/00—Multi-cylinder machines or pumps characterised by number or arrangement of cylinders
- F04B1/12—Multi-cylinder machines or pumps characterised by number or arrangement of cylinders having cylinder axes coaxial with, or parallel or inclined to, main shaft axis
- F04B1/14—Multi-cylinder machines or pumps characterised by number or arrangement of cylinders having cylinder axes coaxial with, or parallel or inclined to, main shaft axis having stationary cylinders
- F04B1/141—Details or component parts
- F04B1/146—Swash plates; Actuating elements
- F04B1/148—Bearings therefor
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Reciprocating Pumps (AREA)
- Centrifugal Separators (AREA)
- Massaging Devices (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Medicines Containing Plant Substances (AREA)
- Vending Machines For Individual Products (AREA)
- Details And Applications Of Rotary Liquid Pumps (AREA)
- Manufacturing Of Micro-Capsules (AREA)
- Details Of Reciprocating Pumps (AREA)
- Supplying Of Containers To The Packaging Station (AREA)
- Fertilizing (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
Abstract
Description
Fremgangsmåte for fremstilling av a,a'-tetra-alkylsubstituerte (cyanometoksy)-eddik8yrer og derivater herav. Process for the production of α,α'-tetra-alkyl-substituted (cyanomethoxy)-acetic acids and derivatives thereof.
Oppfinnelsen angår fremstilling av «.«'-tetraalkylsubstituerte (cyanometoksy)-eddiksyrer og derivater herav, f. eks. de tilsvarende diglykolimider og diglykolsyrer. a,a'-tetraalkylsubstituerte (cyanometoksy )-eddiksyrer og de tilsvarende diglykolsyrer (oksy-2,2'-dieddiksyrer) danner vanskelig forsåpbare estere, og hit-til bare vanskelig tilgjengelige komponenter for polyestere og polyamider. De «.«'-tetraalkylsubstituerte diglykolimider er viktige komponenter for formaldehyd-harpikser. a-oksykarboksylsyrene og estre herav som kan fremstilles fra de a, a-tetraalkylsubstituerte (cyanometoksy )-eddiksyrer, resp. fra deres derivater, ut-gjør endelig verdifulle råstoffer for fremstilling av metakrylsyre, dens høyere homologer og dens estre. The invention relates to the production of «.«'-tetraalkyl-substituted (cyanomethoxy)-acetic acids and derivatives thereof, e.g. the corresponding diglycolimides and diglycolic acids. α,α'-tetraalkyl-substituted (cyanomethoxy)-acetic acids and the corresponding diglycolic acids (oxy-2,2'-diacetic acids) form difficult-to-saponify esters, and until now only difficult-to-access components for polyesters and polyamides. The «.«'-tetraalkyl substituted diglycolimides are important components for formaldehyde resins. The α-oxycarboxylic acids and esters thereof which can be prepared from the α,α-tetraalkyl-substituted (cyanomethoxy)-acetic acids, resp. from their derivatives, finally constitute valuable raw materials for the production of methacrylic acid, its higher homologues and its esters.
Oppfinnelsen angår en fremgangsmåte for fremstilling av «.«'-tetraalkylsubstituerte (cyanometoksy )-eddiksyrer med den generelle formel: The invention relates to a process for the production of «.«'-tetraalkyl-substituted (cyanomethoxy)-acetic acids with the general formula:
hvor R1; R2, R3, R4 betyr metyl- eller etyl-ester, og deres derivater, som ved eterspaltning eller hydrolyse kan spaltes til a-oksykarboksylsyrer. Det karakteristiske ved fremgangsmåten er at 4-oksimino-2,2,5,5-tetraalkylsubstituerte 3-oksotetrahydrofuraner med den generelle formel: where R1; R 2 , R 3 , R 4 mean methyl or ethyl ester, and their derivatives, which can be split into α-oxycarboxylic acids by ether cleavage or hydrolysis. The characteristic feature of the method is that 4-oximino-2,2,5,5-tetraalkyl-substituted 3-oxotetrahydrofurans with the general formula:
behandles ved temperaturer på 40—200°C med vann, alkohol eller et overfor karboksyl- og/eller karboksylsyrenitrilgrup-per inert organisk oppløsningsmiddel med kokepunkt over 75°C under ringspaltning mellom C(3) og C(4), og de dannede «.«'-tetrasubstituerte jScyanometoksy )-eddiksyrer overføres eventuelt til de tilsvarende diglykolimider eller diglykolsyrer ved viderebehandling med foran nevnte reaksjonsmedium, eventuelt i nærvær av forestrings- eller omestringskatalysatorer eller i nærvær av anhydriddannende forbindelser. treated at temperatures of 40-200°C with water, alcohol or an organic solvent inert to carboxyl and/or carboxylic acid nitrile groups with a boiling point above 75°C during ring cleavage between C(3) and C(4), and the formed " .«'-tetrasubstituted jScyanomethoxy)-acetic acids are optionally transferred to the corresponding diglycolimides or diglycolic acids by further treatment with the aforementioned reaction medium, optionally in the presence of esterification or transesterification catalysts or in the presence of anhydride-forming compounds.
4-oksimino-2,2,5,5-tetraalkylsubstituerte 3-oksotetrahydrofuraner oppstår ved 4-oximino-2,2,5,5-tetraalkyl-substituted 3-oxotetrahydrofurans occur by
omsetning av «,a'-tetraalkylsubstituerte 3-oksotetrahydrofuraner med salpeter-syrling, resp. dens derivater. reaction of «,α'-tetraalkyl-substituted 3-oxotetrahydrofurans with nitric acid, resp. its derivatives.
Som midler som virker oppløsende på oksimeringsproduktet, som har en; ringspaltingsevne, og som er inerte overfor de dannete karboksyl- og/eller nitril-grupper, bør nevnes organiske oppløs-ningsmidler med et kokepunkt på over 75°C, så som aromatiske eller alifatiske hydrokarboner, f. eks. benzen, toluen, xylen, gasolin, høyere ketoner, f. eks. metyl-etylketon, karboksylsyreamider, f. eks. dimetylformamid, «,«'-sekundær dikar-boksylsyreamidisopropyleter, eller pyridin og homologer. As agents that act solubilizing on the oxidation product, which has a; ring cleavage ability, and which are inert towards the formed carboxyl and/or nitrile groups, mention should be made of organic solvents with a boiling point above 75°C, such as aromatic or aliphatic hydrocarbons, e.g. benzene, toluene, xylene, gasoline, higher ketones, e.g. methyl ethyl ketone, carboxylic acid amides, e.g. dimethylformamide, ","-secondary dicarboxylic acid amide isopropyl ether, or pyridine and homologues.
Stoffer som virker oppløsende på oksimeringsproduktet, og som har en ringspaltingsevne og som kan reagere med de dannede karboksyl- og/eller nitrilgrupper, er først og fremst stoffer som under for-såpning eller forestring kan reagere med karboksyl- og/eller karboksylsyrenitril-gruppene, så som vann og enverdige eller flerverdige alkoholer med mettet eller umettet hydrokarbonrest som kan være alifatisk eller aromatisk. Substances which have a dissolving effect on the oxidation product, and which have a ring-cleaving ability and which can react with the formed carboxyl and/or nitrile groups, are primarily substances which during saponification or esterification can react with the carboxyl and/or carboxylic acid nitrile groups, such as water and monohydric or polyhydric alcohols with a saturated or unsaturated hydrocarbon residue which may be aliphatic or aromatic.
Hensiktsmessig akselereres reaksjonen. Dette kan skje ved at det opphetes til temperaturer på 40—200°C, eller ved at det brukes forsåpnings-, forestrings-eller omestrings-katalysatorer eller anhydriddannende forbindelser. Selvsagt kan begge metoder kombineres. Appropriately, the reaction is accelerated. This can be done by heating to temperatures of 40-200°C, or by using saponification, esterification or transesterification catalysts or anhydride-forming compounds. Of course, both methods can be combined.
Som forsåpnings-, forestrings- eller omestrings-katalysatorer kan man bruke stoffer som virker basisk, nøytralt eller surt, så som alkali- eller jordalkalihyd-roksyder, -oksyder, -alkoholater, alkyles-tere av 'titansyre, uorganiske, Lewis- og organiske syrer, f. eks. mineralsyrer i liten mengde, så som H2SO., (anvendelse av H2SP4 av høyere konsentrasjon er nært mere beskrevet i norsk patent nr. 113 333, H3P04, HC1, deres tilsvarende virkende organiske forbindelser, f. eks. paratolu-en-sulfonsyre, sulfonerte ioneutvekslings-harpikser, surt reagerende forbindelser, som FeCl3, TiCl4, SnCl4, BF3, ZnCl2, A1C13. Som anhydriddannende forbindelser kan man bruke syreanhydrider eller syreklo-rider i nærvær av HCl-bindende forbin^ deiser, f. eks. pyridin. As saponification, esterification or transesterification catalysts, one can use substances that act basic, neutral or acidic, such as alkali or alkaline earth hydroxides, -oxides, -alcoholates, alkylesters of 'titanic acid, inorganic, Lewis and organic acids, e.g. mineral acids in small quantities, such as H2SO., (the use of H2SP4 of higher concentration is more closely described in Norwegian patent no. 113 333, H3P04, HC1, their correspondingly active organic compounds, e.g. paratoluene-sulfonic acid, sulfonated ion-exchange resins, acid-reactive compounds, such as FeCl3, TiCl4, SnCl4, BF3, ZnCl2, A1C13.As anhydride-forming compounds, acid anhydrides or acid chlorides can be used in the presence of HCl-binding compounds, e.g. pyridine.
Når man anvender surt virkende for-estringskatalysatorer, bør man bruke dem bare dersom reaksjonsmediet er varinfritt, dvs. at man bør bruke disse surt virkende katalysatorer bare når re-aksjonsmédiet er et organisk oppløs-ningsmiddel som er inert overfor karboksyl og/eller nitril-grupper, eller en alkohol, men ikke vann. Dersom man bruker vandige syrer, skjer ingen ringspait-ning mellom C,,- og C4-karbonet, men det oppstår «^'-diketotetrahydrofuraner. When you use acid-acting esterification catalysts, you should only use them if the reaction medium is alcohol-free, i.e. you should use these acid-acting catalysts only when the reaction medium is an organic solvent that is inert to carboxyl and/or nitrile groups, or an alcohol, but not water. If aqueous acids are used, no ring splitting occurs between the C1 and C4 carbons, but "^'-diketotetrahydrofurans are formed.
Arten og mengden av de anvendte katalysatorer er avhengig'av om den a, a-tetrasubstituerte (cyanometoksy )-eddiksyre skal isoleres eller om den skal over-føres til sine derivater som f.eks.diglykolimid eller diglykolsyre, ved reaksjon av karboksyl- og/eller nitrilgruppen i selve reaksjonsmediet. Dersom (cyanometoksy )-eddiksyren skal isoleres, arbeides hensiktsmessig således at oksimeringsproduktet av de tilsvarende 2,2,5,5rtetraalkylsubstituerte 3-oksotetrahydrofuraner fordeles i et inert oppløsningsmiddel, f. eks. toluen, eller i overfor karboksyl-og/eller nitrilgrupper reaksjonsdyktige oppløsningsmidler, f. eks. alkohol, vann og at det som katalysator brukes alkalihydroksyd. Hensiktsmessig brukes pr. mol oksim 1 mol alkalihydroksyd. Ved si-den av at det virker som katalysator tje-ner alkalihydroksydet samtidig som sta-biliseringsmiddel for den a,a'-tetrasubstituerte (cyanometoksy ).eddiksy-re som kan isoleres som alkalisaltet. Her bør man merke seg at saitet etter avsluttet ringspaltning bør isoleres snarest. Lar man saltet forbli i reaksjonsmediet etter at saltet er dannet, danner det seg en tilsvarende diglykolsyre ved hydrolyse av nitrilgruppen. Tidspunktet for den av-sluttede ringspaltning kan konstateres ved at ammoniakken" begynner å utvik-les. Når man som oppløsningsmiddel bruker vann, kan man konstatere slutten av reaksjonen ved at fargen skifter fra dyp rød til gul, The nature and quantity of the catalysts used depends on whether the α,α-tetrasubstituted (cyanomethoxy)-acetic acid is to be isolated or whether it is to be transferred to its derivatives such as diglycolimide or diglycolic acid, by reaction of carboxylic and /or the nitrile group in the reaction medium itself. If the (cyanomethoxy)-acetic acid is to be isolated, it is expedient to work so that the oxidation product of the corresponding 2,2,5,5-tetraalkyl-substituted 3-oxotetrahydrofurans is distributed in an inert solvent, e.g. toluene, or in solvents reactive towards carboxyl and/or nitrile groups, e.g. alcohol, water and that alkali hydroxide is used as a catalyst. Appropriately used per mol oxime 1 mol alkali hydroxide. In addition to acting as a catalyst, the alkali hydroxide also serves as a stabilizer for the α,α'-tetrasubstituted (cyanomethoxy)acetic acid which can be isolated as the alkali salt. Here it should be noted that the site should be isolated as soon as possible after ring splitting has been completed. If the salt is allowed to remain in the reaction medium after the salt has been formed, a corresponding diglycolic acid is formed by hydrolysis of the nitrile group. The time for the completed ring cleavage can be ascertained by the fact that ammonia begins to evolve. When water is used as solvent, the end of the reaction can be ascertained by the color changing from deep red to yellow,
Når man ikke bruker, eller bare bruker en liten mengde av. katalysatoren, om-leires den «.«'-tetrasubstituerte (eyano-metoksyX-eddiksyré til sitt diglykolimid: When one does not use, or only uses a small amount of. catalyst, the «.«'-tetrasubstituted (eyano-methoxyX-acetic acid is converted to its diglycolimide:
Her er det å nevne at oppløsningsmidlet som er i stand til å spalte ringen, kan vir-ke reaksjpnsstyrende. Hvis man f, eks. til ringspaltning bruker eii alkohol, med den generelle formel ROH (R = alkyl), kan denne alkohol med karboksylgruppen i (.cyanometoksy )-eddiksyren danne den tilsvarende ester, som derpå under pm-<1 >dannelsen leder til et N-substituert d> glykoiimid med formelen: Tilsvarende kan det ved å anvende anhydrid-dannende tilsetning, oppnås N-substituerte digiykoUmider med den generelle formel;'' < It should be mentioned here that the solvent, which is capable of cleaving the ring, can act as a reaction regulator. If one f, e.g. for ring cleavage an alcohol is used, with the general formula ROH (R = alkyl), this alcohol with the carboxyl group in (.cyanomethoxy)-acetic acid can form the corresponding ester, which then during the pm-<1 >formation leads to an N-substituted d > glycoimide with the formula: Similarly, by using an anhydride-forming addition, N-substituted diglycomides with the general formula can be obtained;'' <
p,ersprn det brukes større mengder ay katalysatoren (f. eks. KOH), eller hvis man lar den dannede (cyanometoksy )--eddiksyre forbli i reaksjonsmediet uten å isolere den eller hvis tidligere isolert (cyanometoksy )-eddiksyre føres inn i reaksjonsmediet, gjennomgår nitrilgruppen f<p>rsåpning og det dannes den tilsvarende diglykolsyre, resp. dens salter. if larger quantities of the catalyst (e.g. KOH) are used, or if the formed (cyanomethoxy)-acetic acid is allowed to remain in the reaction medium without isolating it or if previously isolated (cyanomethoxy)-acetic acid is introduced into the reaction medium, undergoes initial opening of the nitrile group and the corresponding diglycolic acid is formed, resp. its salts.
Hva angår bruken av varme som re-aksjonsakselererende middel, kan det generelt sies at det i fravær av katalysar torer- allerede er tilstrekkelig å bruke temperaturer på 9.0°C for å oppnå, til-fredsstillende . omsetningshastigheter. Dersom man bruker- katalysatorer, oppr nåes disse' hastigheter allerede ved temperaturer' på ca. 50°C. Regarding the use of heat as a reaction-accelerating agent, it can generally be said that in the absence of catalysts it is already sufficient to use temperatures of 9.0°C to achieve satisfactory results. turnover rates. If you use catalysts, these speeds are already reached at temperatures of approx. 50°C.
Fremstillingen av a-oksimeringspro,-dukter ay 2v2i5,,5-tetrÆalkylsubsti;tuerte 3,-qksptetrahydrpfuraner kan skje på kjent måte, ved addisjon ay 2- mol; keton til- 1 mpL acetylen, omdannelse av den dannede tetraalkylsubsMuerte heksindiol i nærvær av oppløselige kvikksøly.( li.)katalysatorer til vannuoppløselig 2,2,5,5-tetraal-kylsubstituert 3-oksotetrahydrofuran, og endelig ved den a-oksimering med salpe-tersyrling, dens estere, klorid eller anhyd-rider. The production of a-oximation products ay 2v2i5,,5-tetraAlalkylsubstituted 3,-qksptetrahydrfurans can take place in a known manner, by addition ay 2- mol; ketone to 1 mpL of acetylene, conversion of the formed tetraalkylsubsMuated hexinediol in the presence of soluble mercury oil (li.) catalysts to water-insoluble 2,2,5,5-tetraalkyl-substituted 3-oxotetrahydrofuran, and finally by the α-oximation with salp -tertacid, its esters, chloride or anhydrides.
Fremstillingen av a-oksimeringsproduktet og den videre omsetning i henhold til oppfinnelsen kan også skje i selve re-aksjonsbeholderen (sammenlign eksempel). The production of the a-oximation product and the further reaction according to the invention can also take place in the reaction vessel itself (compare example).
Forløpet av prosessen i samsvar med formelen minner om den kjente «Beckmanske <p>mleiring» som fører fra keto-oksimer til substituerte primære karboksylsyreamider. Ved den praktiske gjen-nomføring av den «Beckmanske omleiring» <p>g av fremgangsmåten ifølge oppfinnelsen møter man imidlertid vesentli-ge forskjeller ved de to reaksjoner. Ifølge moderne og anerkjente betraktninger The course of the process in accordance with the formula is reminiscent of the well-known "Beckman reaction" which leads from keto-oximes to substituted primary carboxylic acid amides. However, in the practical implementation of the "Beckman rearrangement" <p>g of the method according to the invention, one encounters significant differences in the two reactions. According to modern and recognized considerations
trenges for å utløse den «Beckmanske omleiring» sterkt sure resp. syredannende stoffer, så som H2SO„ S03, P905, SOCl2, is needed to trigger the "Beckmanian rearrangement" strongly acidic resp. acid-forming substances, such as H2SO„ S03, P905, SOCl2,
PCI,. PCI, .
Under innvirkning av disse syrer dannes fra oksimene kationer og etter av-spaltning av vann fullføres den «Beckmanske omleiring». Ved den nye fremgangsmåte kan derimot ikke bare bruken av syrer sløyfes, men man har også opp-nådd med sterke alkalier i overskudd en vesentlig reaksjonsakselerering og høye utbytter av de ønskede reaksjonsproduk-ter. Under the influence of these acids, cations are formed from the oximes and, after splitting off water, the "Beckman rearrangement" is completed. With the new method, on the other hand, not only can the use of acids be dispensed with, but a significant reaction acceleration and high yields of the desired reaction products have also been achieved with strong alkalis in excess.
Den nye fremgangsmåte er begrenset til de som gule krystaller erholdte oksi-meringsprodukter av 2,2,5,5-tetraalkylsubstituerte 3-oksotetrahydrofuraner som utgangsforbindelser. Hvis man underkas-ter de analogt a-oksimerte tri-, di-, mono-alkylsubstituerte eller i det hele tatt ikke substituerte 3-oksotetrahydrofuraner for betingelser ved hvilke den nye fremgangsmåte uten vanskeligheter skrider frem, får man ikke, eller med ikke merkbare utbytter, de tilsvarende (cyanometoksy )-eddiksyrer og deres derivater. Ved den nye fremgangsmåte må. det derfor antas at de spesielle steriske betingelser ved a-oksotetrahydrofuraner er kjemisk sett en vesentlig forutsetning og at. de begunsti-ger omleiringen fra de. fullstendig substituerte 5-leddete oksygenforbindelser i de åpenbart mer avspente, resp. 6-leddete forbindelser. Også. her ligger en vesentlig forskjell med den kjente «Beckmanske omleiring» ved hvilken det skjer teknisk en omleiring av det 6-le.ddete cykloheksan-monooksim til det 7-leddete caprolaktam. The new method is limited to the oxidation products of 2,2,5,5-tetraalkyl-substituted 3-oxotetrahydrofurans obtained as yellow crystals as starting compounds. If one subjects the analogous α-oximerized tri-, di-, mono-alkyl-substituted or not at all substituted 3-oxotetrahydrofurans to conditions under which the new method proceeds without difficulty, one does not obtain, or with not noticeable yields , the corresponding (cyanomethoxy)-acetic acids and their derivatives. In the new procedure must. it is therefore assumed that the special steric conditions of α-oxotetrahydrofurans are chemically an essential prerequisite and that. they favor the relocation from them. fully substituted 5-membered oxygen compounds in the obviously more relaxed, resp. 6-joint compounds. Also. here lies a significant difference with the well-known "Beckman rearrangement", in which a rearrangement of the 6-membered cyclohexane monooxime to the 7-membered caprolactam takes place technically.
De ifølge fremgangsmåten fremstilte (cyanometoksy )-eddiksyrer, resp. deres derivater kan ved eterspaltning med kon-sentrerte syrer overføres til tilsvarende substituerte «-oksykarboksylsyrer. The (cyanomethoxy)-acetic acids produced according to the method, resp. their derivatives can, by ether cleavage with concentrated acids, be transferred to correspondingly substituted '-oxycarboxylic acids.
Eksempel 1. Example 1.
0,3 mol 4-isonitroso-2,2,5,5-tetrametyl-3-oksotetrahydrofuran overføres til det tilsvarende kaliumsalt av oksimet med en ekvimolar mengde av 25% KOH ved lav temperatur. Den kraftige røde, vandige oppløsning av oksimsaltet opphetes til kokepunktet under tilbakeløp. Etter 10— 15 minutter kan man konstatere en fullstendig omleiring ved en skarp farge-skiftning av reaksjonsoppløsningen fra rødt til svakt gult. Det kjøles med én gang. Deretter rystes reaksjonsoppløsnin-gen med eter for å fjerne forurensninge-ne, og til det vandige skikt tilsettes langsomt under kjøling en ekvimolar mengde saltsyre. For å isolere karboksylsyren rystes en gang til med eter, og det tørke-te eteruttrekk fordampes ved lav temperatur under et svakt vakuum. Det erholdes umiddelbart 41,5 g av a,a'-tetrametyl- (cyanometoksy) -eddiksyre, hvilket 0.3 mol of 4-isonitroso-2,2,5,5-tetramethyl-3-oxotetrahydrofuran is transferred to the corresponding potassium salt of the oxime with an equimolar amount of 25% KOH at low temperature. The strong red, aqueous solution of the oxime salt is heated to the boiling point under reflux. After 10-15 minutes, a complete rearrangement can be observed by a sharp color change of the reaction solution from red to faint yellow. It cools right away. The reaction solution is then shaken with ether to remove the impurities, and an equimolar amount of hydrochloric acid is slowly added to the aqueous layer while cooling. To isolate the carboxylic acid, shake once more with ether, and the dried ether extract is evaporated at low temperature under a weak vacuum. 41.5 g of α,α'-tetramethyl-(cyanomethoxy)-acetic acid are immediately obtained, which
svarer til et utbytte på 81% av det teoretiske. Dette råprodukt smelter ved 69— 71°C og oppfyller, hva angår renheten, de fleste krav (syretall funnet: 327, syretall beregnet: 328). Ved omkrystallisering opptrer gjennom dannelse av biproduk-ter vesentlig tap (opp til 60%). Fra gasolin erholdes en syre med følgende egenskaper : corresponds to a yield of 81% of the theoretical. This crude product melts at 69-71°C and meets, in terms of purity, most requirements (acid number found: 327, acid number calculated: 328). During recrystallization, significant losses (up to 60%) occur through the formation of by-products. An acid with the following properties is obtained from gasoline:
Syretall funnet: 330, beregnet: 328 Acid number found: 330, calculated: 328
N funnet: 8,25%, beregnet: 8,18% Smp. 72,5°C for de farveløse krystaller. N found: 8.25%, calculated: 8.18% Smp. 72.5°C for the colorless crystals.
Ved å omsette kaliumsaltet av den ovenfor nevnte (cyanometoksy )-eddiksy-re med et overskudd av dimetylsulfat i benzen-vannoppslemming ved koketempe-' råtur erholdes «,a'-tetrametyl-( cyanometoksy )-eddiksyremetylester. Denne forbindelse har følgende egenskaper: Forsåpningstall funnet: 575 Forsåpningstall beregnet: 605 Brytningsindeks ved 20°C: 1,4262 By reacting the potassium salt of the above-mentioned (cyanomethoxy)-acetic acid with an excess of dimethyl sulfate in a benzene-water slurry at boiling temperature, α'-tetramethyl-(cyanomethoxy)-acetic acid methyl ester is obtained. This compound has the following properties: Saponification number found: 575 Saponification number calculated: 605 Refractive index at 20°C: 1.4262
Kokepunkt av den vannklare fargeløse væske ved 0,3—0,4 mm Hg: 38—40°C. Boiling point of the water-clear colorless liquid at 0.3-0.4 mm Hg: 38-40°C.
Eksempel 2. Example 2.
For å fremstille utgangsmaterialet 4-isonitroso-2,2,5,5-tetrametyl-3-oksotetrahydrofuran (a-oksimeringsproduktet av 2,2,5,5-tetrametyl-3-oksotetrahydrofura-net) oksimeres under omrøring 0,2 mol av 2,2,5,5-tetrametyl-3<:>oksotetrahydrofuran med 0,22 mol av amylnitrit ved 40— 50°C og i nærvær av 7,5 ml konsentrert saltsyre. Allerede under rø ringen erholdes over 65% av den teoretiske mengde av a-oksimeringsproduktet. Produktet kan omkrystalliseres fra dimetyleter (smp.: 127°C, Funnet: 8,07% N, Beregnet: 8,18% N). To prepare the starting material 4-isonitroso-2,2,5,5-tetramethyl-3-oxotetrahydrofuran (the α-oximation product of 2,2,5,5-tetramethyl-3-oxotetrahydrofuran), 0.2 mol of 2,2,5,5-tetramethyl-3<:>oxotetrahydrofuran with 0.22 mol of amyl nitrite at 40-50°C and in the presence of 7.5 ml of concentrated hydrochloric acid. Already during the stirring, more than 65% of the theoretical quantity of the α-oximation product is obtained. The product can be recrystallized from dimethyl ether (m.p.: 127°C, Found: 8.07% N, Calculated: 8.18% N).
Ved tilsetning av 1 mol av en van-dig 30%'s natronlut til reaksjonsblandin-geh skjer en ringspaltning. (Cyanometoksy )-eddiksyren kan isoleres som i eksempel 1 i form av sitt alkalisalt. Hvis denne (cyanometoksy )-eddiksyre ikke isoleres, men forblir videre i reaksjonsmediet, opptrer en sterk ammoniakkut-vikling. Ved hjelp av vanndamp og under oppvarmning fjernes gjennom en nedad-skrånende kjøler den frigjorte ammoniakk og amylalkoholen som stammer fra oksimeringen. Reaksjonsproduktet far-ges rød-brunt når alkali tilsettes, og det blir lysere under omsetningen. Reaksjonen er avsluttet så snart destillatet er fritt for ammoniakk. For å overføre i fri syre innstilles litt etter litt pH-verdien med konsentrert saltsyre ved ca. 90°C til omtrent 2, eller det nøytraliseres med tilsammen 1 mol HC1. Fra den svakgult fargete reaksjonsoppløsning utkrystalliserer hurtig 2,2'-tetrametyl-diglykolsyren som fargeløst produkt i en mengde på ca. 80% av den teoretiske. Det suges av ved 60°C. Syren kan befries for innesluttet al-kaliklorid ved omkrystallisering fra vann eller benzen, eller bare ved vasking med vann. Dens smeltepunkt ligger ved 158°C (syretall beregnet: 590, funnet: 580, C beregnet: 50,5%, funnet 50,5%. H beregnet: 7,4%, funnet 7,4%, N beregnet: 0,0 %, funnet 0,3%). When 1 mol of an aqueous 30% sodium hydroxide solution is added to the reaction mixture, ring cleavage occurs. The (cyanomethoxy)-acetic acid can be isolated as in example 1 in the form of its alkali salt. If this (cyanomethoxy)-acetic acid is not isolated, but remains in the reaction medium, a strong ammonia evolution occurs. With the help of water vapor and during heating, the released ammonia and the amyl alcohol originating from the oxidation are removed through a downward-sloping cooler. The reaction product is colored red-brown when alkali is added, and it becomes lighter during the reaction. The reaction is finished as soon as the distillate is free of ammonia. To transfer in free acid, adjust the pH value little by little with concentrated hydrochloric acid at approx. 90°C to approximately 2, or it is neutralized with a total of 1 mol of HC1. From the slightly yellow colored reaction solution, the 2,2'-tetramethyl-diglycolic acid quickly crystallizes as a colorless product in an amount of approx. 80% of the theoretical. It is sucked off at 60°C. The acid can be freed from trapped alkali-potassium chloride by recrystallization from water or benzene, or simply by washing with water. Its melting point is at 158°C (acid number calculated: 590, found: 580, C calculated: 50.5%, found 50.5%. H calculated: 7.4%, found 7.4%, N calculated: 0, 0%, found 0.3%).
Dersom man i stedenfor • natronlut bruker en tilsvarende mengde av kalilut med en konsentrasjon på ca..40%, øker utbyttet til ca, 90% av det teoretiske. If, instead of • caustic soda, a corresponding amount of caustic soda with a concentration of approx. 40% is used, the yield increases to approx. 90% of the theoretical amount.
På analog måte og med minst like store utbytter erholdes ved bruken av høyere substituerte a-oksimeringsproduk-ter de tilsvarende diglykolsyrer, f. eks. fra a-oksimeringsproduktet av 2,5-dime-tyl:2,5-dietyl-3-oksotetrahydrofurah erholdes den tilsvarende 2,5-dimetyl-2,5-dietyl-diglykolsyre. Den smelter ved 151°C. In an analogous manner and with at least equal yields, the corresponding diglycolic acids are obtained by the use of higher substituted α-oximation products, e.g. from the α-oximation product of 2,5-dimethyl:2,5-diethyl-3-oxotetrahydrofurah the corresponding 2,5-dimethyl-2,5-diethyl-diglycolic acid is obtained. It melts at 151°C.
Hvis omsetningen med alkalilut gjen-nomføres på analog måte med ved omkrystallisering rensete a-oksimeringspro-dukter, erholdes etter nøytralisering med saltsyre de ventede diglykolsyrer med like høye utbytter. If the reaction with alkaline lye is carried out in an analogous manner with α-oximation products purified by recrystallization, the expected diglycolic acids are obtained after neutralization with hydrochloric acid with equally high yields.
Eksempel 3. Example 3.
Ved oppvarmning av 0,0585 mol av et 98,8%'s a-oksimeringsprodukt av 2,2,-5,5-tetrametyl-3-oksotetrahydrofuran i 40 g toluen som suspenderingsmiddel, og 0,2 g NaOH som katalysator, til kokepunktet avsluttes reaksjonen etter 2 timer, hvilket man kan konstatere ved den negative påvisning av karbonylgrupper med 2,4-dinitrofenylhydrazin. Fra det i vakuum inndampete residuum utkrystalliseres umiddelbart 48% av den teoretiske mengde av 2,2,5,5-tetrametyl-diglykolimid. Ytterligere 37 % erholdes ved omkrystallisering av residuet fra 1 % saltsyre, hvilket gir et totalt utbytte på 85 %. Når reaksjonen utføres på analog måte i fravær av NaOH, varer omsetningen 9 timer, og de isolerte utbytter er omtrent 30 % lavere. Hvis toluen .erstattes med den lavere kokende benzen, øker reaksjonstiden i nærvær av NaOH. ikke vesentlig, men i fravær av NaOHrøker den til ca. 12 timer. I høyere kokende xylen er reaksjonen avsluttet i nærvær av NaOH etter 1,5 .timer, og i nærvær- av n-butyltitanat allerede etter 45 minutter. Ved 150°C i kokende dimetylformamid skjer en fullstendig omsetning i fravær av reaksjoiisakselére-rende tilsetninger i løpet av 3,5 timer. Når temperaturen øker ytterligere, kan reaksjonstidene forkortes enda mer også i fravær av katalysatorer. By heating 0.0585 mol of a 98.8% a-oximation product of 2,2,-5,5-tetramethyl-3-oxotetrahydrofuran in 40 g of toluene as suspending agent, and 0.2 g of NaOH as catalyst, to boiling point, the reaction ends after 2 hours, which can be ascertained by the negative detection of carbonyl groups with 2,4-dinitrophenylhydrazine. 48% of the theoretical amount of 2,2,5,5-tetramethyl-diglycolimide immediately crystallizes from the vacuum evaporated residue. A further 37% is obtained by recrystallization of the residue from 1% hydrochloric acid, which gives a total yield of 85%. When the reaction is carried out analogously in the absence of NaOH, the reaction lasts 9 hours and the isolated yields are approximately 30% lower. If toluene is replaced by the lower boiling benzene, the reaction time increases in the presence of NaOH. not significantly, but in the absence of NaOH it smokes to approx. 12 hours. In higher-boiling xylene, the reaction is finished in the presence of NaOH after 1.5 hours, and in the presence of n-butyl titanate already after 45 minutes. At 150°C in boiling dimethylformamide, a complete reaction takes place in the absence of reaction-accelerating additives within 3.5 hours. When the temperature increases further, the reaction times can be shortened even more even in the absence of catalysts.
Eksempel 4. Example 4.
En blanding bestående av 0,2 mol a-oksimeringsprodukt av 2,2,5,5-tetrametyl-3-oksotetrahydrofuran, 5 vektprosent beregnet på dette produkt av n-butylorto-titanat som forestringskatalysator, og 0,22 mol av n-butanol, oppslemmes i benzen-overskudd og opphetes til koking under tilbakeløp på en 10 cm lang fyll-le-gemkolonne med kolonnehode. Det ut-skilte forestringsvann fjernes som destil-lat. Som øvre skikt erholdes ca. 1,5 ml vann (= 41,7% av det teoretiske). A mixture consisting of 0.2 mol of α-oximation product of 2,2,5,5-tetramethyl-3-oxotetrahydrofuran, 5% by weight calculated on this product of n-butyl ortho-titanate as esterification catalyst, and 0.22 mol of n-butanol , is slurried in excess benzene and heated to boiling under reflux on a 10 cm long packed column with a column head. The separated esterification water is removed as distillate. As an upper layer, approx. 1.5 ml of water (= 41.7% of the theoretical).
Oppløsningsmidlet (benzen) og n-bu-tanoloverskuddet fjernes ved destillasjon. Det oppstår et med krystaller blandet oljeaktig residuum. Med petroleter opp-løses den krystallinske andel og utkrystalliseres påny. Etter omkrystallisering fra benzen erholdes 7,8 g 2,2,5,5-tetrametyl-diglykolimid, tilsvarende et utbytte på 23 % av det teoretiske. Stoffet smelter ved 137°C, og det ble funnet 7,95 % og beregnet 8,18 %. The solvent (benzene) and the n-butanol excess are removed by distillation. An oily residue mixed with crystals is formed. With petroleum ether, the crystalline portion is dissolved and crystallized again. After recrystallization from benzene, 7.8 g of 2,2,5,5-tetramethyl-diglycolimide are obtained, corresponding to a yield of 23% of the theoretical. The substance melts at 137°C, and it was found 7.95% and calculated 8.18%.
Destillasjon av residuet fører til iso- Distillation of the residue leads to iso-
leringen av 21,9 g 2,2,5,5-tetrametyl-digly-kol-N-n-butylsubstituert imid. /Kp ved 0,3 mm Hg = 77°C, C beregnet 63,4.%, C funnet 63,3 %, H beregnet 9,3 %, H funnet: 9,3 %, Nberegnet: 6,17 %, Nfunnet: 6,0 %/. Utbyttet av- 21,9- g svarer til 48 % av det teoretiske. Således utgjør det isolerte samlede utbytte 23,0 % + 48 % = 71 % av det teoretiske. Infrarøde spektra-av de to. isolerte stoffer svarer til de an-tatte formler. Begge to lar seg. overføre med moderat konsentrert saltsyre (konsentrasjon 10—25 % ) i overskudd, til a-oksyisosmørsyre. the formation of 21.9 g of 2,2,5,5-tetramethyl-digly-chol-N-n-butyl substituted imide. /Kp at 0.3 mm Hg = 77°C, C calculated 63.4%, C found 63.3%, H calculated 9.3%, H found: 9.3%, Ncalculated: 6.17%, Nfound: 6.0%/. The yield of 21.9 g corresponds to 48% of the theoretical. Thus, the isolated total yield amounts to 23.0% + 48% = 71% of the theoretical. Infrared spectra-of the two. isolated substances correspond to the assumed formulas. Both agree. transfer with moderately concentrated hydrochloric acid (concentration 10-25%) in excess, to a-oxyisobutyric acid.
Ved å bruke et større overskudd av n-butanol økes, som ventet, utbyttet av dekarboksylsy reimideter. Using a larger excess of n-butanol increases, as expected, the yield of decarboxyl reimides.
Istedenfor n-butyltitanat kan> man også bruke små mengder av NaOH som katalysator. Herved.økes utbyttet av ikke substituert diglykolimid på bekostning av den substituerte forbindelse, og samtidig forlenges reaksjonstiden fra 1 time til 2 timer. Instead of n-butyl titanate, small amounts of NaOH can also be used as a catalyst. This increases the yield of unsubstituted diglycolimide at the expense of the substituted compound, and at the same time the reaction time is extended from 1 hour to 2 hours.
Eksempel 5. Example 5.
0,176- mol- av a-oksimeringsproduktet av 2,2,5,5-tetrametyl-3-oksotetrahydrofuran oppløses i 120-g. et<y>lalkohol, det tilsettes 0,5 g NaOH og. det opphetes under til-bakeløp. Det uttaes av, og til prøver, og', reaksjonsforløpet kontrolleres ved hjelp av typiske reagenser på frie ketogrupper (f. eks. 2,4-dinitrolfenylhydrazin). Etter ca. 3 timer er reaksjonen avsluttet. Små<" bireaksjoner (forsåpninger) viser seg ved ammoniakkavspaltning. 0.176 mol of the a-oximation product of 2,2,5,5-tetramethyl-3-oxotetrahydrofuran is dissolved in 120 g. et<y>lalcohol, 0.5 g NaOH is added and. it heats up during backflow. It is extracted from, and into samples, and', the course of the reaction is controlled using typical reagents on free keto groups (e.g. 2,4-dinitrophenylhydrazine). After approx. After 3 hours, the reaction is complete. Small <" side reactions (saponifications) appear during ammonia decomposition.
Ved å arbeide, som.angitt i eksempel 2, isoleres: ca. 60 % av det teoretiske av 2,2,5,5- tetrametyldiglykolimid ( «^'-sekundær dikarboksylsyreamid-diisopro-pyleter). By working as indicated in example 2, isolate: approx. 60% of the theoretical of 2,2,5,5- tetramethyldiglycolimide («^'-secondary dicarboxylic acid amide diisopropyl ether).
ca. 35 % av det teoretiske av 2,2;5,5-tetrametyl-diglykol-N-etyl-imid ( a,- a - sekundær dikarboksylsyreamid-N-etyldiisopropyleter). about. 35% of the theoretical of 2,2;5,5-tetramethyl-diglycol-N-ethyl-imide ( a,- a - secondary dicarboxylic acid amide-N-ethyl diisopropyl ether).
tilsammen ca. 95 % samlet utbytte. in total approx. 95% overall yield.
De infrarøde spektra av reaksjons-produktene svarer til de teoretiske. The infrared spectra of the reaction products correspond to the theoretical ones.
Innvirkningen av en reaksjonsaksele-rator kan konstateres ved å sammenlig-ne reaksjonstidene for parallellforsøk. Ved å sløyfe NaOH er omsetningen ennå ikke avsluttet etter 8 timer, men hvis man anvender natriumetylat i stedenfor NaOH, er reaksjonen avsluttet allerede etter 30 minutter. The impact of a reaction accelerator can be ascertained by comparing the reaction times for parallel experiments. By omitting NaOH, the reaction is not yet finished after 8 hours, but if sodium ethylate is used instead of NaOH, the reaction is already finished after 30 minutes.
Eksempel 6. Example 6.
En oppløsning av 0,2 mol (= 34,2 g) A solution of 0.2 mol (= 34.2 g)
av a-oksimeringsproduktet av 2,2,5,5-tetrametyl-3-oksotetrahydrofuran i 100 g of the a-oximation product of 2,2,5,5-tetramethyl-3-oxotetrahydrofuran in 100 g
pyridin opphetes under omrøring til 80°C, pyridine is heated with stirring to 80°C,
og det tilsettes dråpevis 0,22 mol benzen-sulfoklorid. Det skjer en eksotermisk reaksjon. Reaksjonstemperaturen holdes and 0.22 mol of benzene sulphochloride is added dropwise. An exothermic reaction occurs. The reaction temperature is maintained
ved 80°C ved hjelp av svak kjøling. Kjøl-ingen avbrytes når den dråpevise tilsetning er avsluttet. Man lar reaksjonen full-føre seg. Fra reaksjonsoppløsningen erholdes umiddelbart 26 g ( = 80,5 % av det at 80°C using slight cooling. The cooling process is interrupted when the dropwise addition is finished. The reaction is allowed to complete. 26 g ( = 80.5% of it) are immediately obtained from the reaction solution
teoretiske) av et ved 156°C smeltende N-substituert diglykolimid méd formel (V) theoretical) of an N-substituted diglycolimide with formula (V) melting at 156°C
som kan renses ved omkrystallisering fra which can be purified by recrystallization from
aceton. (N funnet: 8,68%, N beregnet: 8,63%.) acetone. (N found: 8.68%, N calculated: 8.63%).
Eksempel 7. Example 7.
I en skål gnis sammen intimt 0,1 mol In a bowl, intimately rub together 0.1 mol
(= 17,1 g) av a,a'-sekundær dikarboksyl-syreimiddiisopropyleter (som et middel (= 17.1 g) of a,a'-secondary dicarboxylic acid imide diisopropyl ether (as an agent
med ringspaltningsevne) og 0,1 mol av a-oksimeringsproduktet av 2,2,5,5-tetrametyl-3-oksotetrahydrofuran, og blandingen with ring cleavage ability) and 0.1 mol of the α-oximation product of 2,2,5,5-tetramethyl-3-oxotetrahydrofuran, and the mixture
opphetes langsomt i en rørekolbe under is heated slowly in a stirrer underneath
tilbakeløp. Ved 80°C begynner blandingen backflow. At 80°C, mixing begins
å smelte, og ved 90°C begynner en eksotermisk reaksjon, hvorved reaksjons-blandingen oppvarmes av seg selv til to melt, and at 90°C an exothermic reaction begins, whereby the reaction mixture is heated by itself to
150°C. Etter noen få minutter er reaksjonen avsluttet, og det erholdes en meget 150°C. After a few minutes, the reaction is complete, and a very
viskøs masse som utkrystalliserer langsomt. Omsetningen er fullstendig, og de viscous mass that crystallizes slowly. The turnover is complete, and they
vanlige reaksjoner for å påvise ketoner common reactions to detect ketones
forløper negativt. Ved omkrystallisering proceeds negatively. Upon recrystallization
fra benzen erholdes 25 g av 2,2,5,5<:>tetrametyl-diglykolimid med et smp. på 135— from benzene, 25 g of 2,2,5,5<:>tetramethyl-diglycolimide with a m.p. at 135—
137°C. 137°C.
Claims (1)
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FR8110602A FR2506857A1 (en) | 1981-05-27 | 1981-05-27 | BARREL MECHANISM |
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NO821441L NO821441L (en) | 1982-11-29 |
NO158433B true NO158433B (en) | 1988-05-30 |
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JP (1) | JPS57200678A (en) |
AT (1) | ATE9175T1 (en) |
CA (1) | CA1203711A (en) |
DE (1) | DE3260625D1 (en) |
DK (1) | DK151491C (en) |
ES (1) | ES8304271A1 (en) |
FR (1) | FR2506857A1 (en) |
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FR2548284B1 (en) * | 1983-07-01 | 1987-10-23 | Creusot Loire | OBLIQUE PLATE MECHANISM FOR THE CONTROL OF A PUMP |
US9545643B2 (en) | 2008-10-22 | 2017-01-17 | Graco Minnesota Inc. | Portable airless sprayer |
JP5739340B2 (en) | 2008-10-22 | 2015-06-24 | グラコ ミネソタ インコーポレーテッド | Portable airless sprayer |
US9016599B2 (en) | 2009-05-07 | 2015-04-28 | Graco Minnesota Inc. | Wobble assembly for fluid pumping mechanism |
US11986850B2 (en) | 2018-04-10 | 2024-05-21 | Graco Minnesota Inc. | Handheld airless sprayer for paints and other coatings |
CN115739435A (en) | 2019-05-31 | 2023-03-07 | 固瑞克明尼苏达有限公司 | Hand-held fluid sprayer |
US10968903B1 (en) | 2020-06-04 | 2021-04-06 | Graco Minnesota Inc. | Handheld sanitary fluid sprayer having resilient polymer pump cylinder |
US10926275B1 (en) | 2020-06-25 | 2021-02-23 | Graco Minnesota Inc. | Electrostatic handheld sprayer |
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JPS5212693Y2 (en) * | 1971-08-03 | 1977-03-22 | ||
FR2204230A5 (en) * | 1972-10-20 | 1974-05-17 | Dowell Schlumberger | |
FR2211090A5 (en) * | 1972-12-14 | 1974-07-12 | Creusot Loire | |
US3862587A (en) * | 1973-09-24 | 1975-01-28 | Parker Hannifin Corp | Hydraulic motor |
-
1981
- 1981-05-27 FR FR8110602A patent/FR2506857A1/en active Granted
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1982
- 1982-04-26 CA CA000401694A patent/CA1203711A/en not_active Expired
- 1982-04-30 NO NO821441A patent/NO158433C/en unknown
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- 1982-05-25 DK DK235782A patent/DK151491C/en active
- 1982-05-26 EP EP82400975A patent/EP0069605B1/en not_active Expired
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NO158433C (en) | 1988-09-07 |
JPH0125896B2 (en) | 1989-05-19 |
DE3260625D1 (en) | 1984-10-04 |
CA1203711A (en) | 1986-04-29 |
JPS57200678A (en) | 1982-12-08 |
DK235782A (en) | 1982-11-28 |
FR2506857A1 (en) | 1982-12-03 |
NO821441L (en) | 1982-11-29 |
ES511958A0 (en) | 1983-02-16 |
FR2506857B1 (en) | 1985-05-24 |
EP0069605B1 (en) | 1984-08-29 |
DK151491C (en) | 1988-08-08 |
SU1259966A3 (en) | 1986-09-23 |
EP0069605A1 (en) | 1983-01-12 |
ES8304271A1 (en) | 1983-02-16 |
DK151491B (en) | 1987-12-07 |
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