AU599729B2 - Preparation of phosphorus-containing intermediates for herbicides - Google Patents

Preparation of phosphorus-containing intermediates for herbicides Download PDF

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Publication number
AU599729B2
AU599729B2 AU82618/87A AU8261887A AU599729B2 AU 599729 B2 AU599729 B2 AU 599729B2 AU 82618/87 A AU82618/87 A AU 82618/87A AU 8261887 A AU8261887 A AU 8261887A AU 599729 B2 AU599729 B2 AU 599729B2
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Australia
Prior art keywords
process according
compound
formula
reaction
optionally substituted
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AU82618/87A
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AU8261887A (en
Inventor
Jean-Pierre Corbet
Michel Mulhauser
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Bayer CropScience SA
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Rhone Poulenc Agrochimie SA
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/38Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
    • C07F9/44Amides thereof
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • C07F9/38Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
    • C07F9/40Esters thereof
    • C07F9/4003Esters thereof the acid moiety containing a substituent or a structure which is considered as characteristic
    • C07F9/4006Esters of acyclic acids which can have further substituents on alkyl

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Fertilizers (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Cephalosporin Compounds (AREA)

Abstract

Preparation of intermediates for herbicides of formula: <IMAGE> by reaction of products of formula: <IMAGE> with products of formula: <IMAGE> in which R, R<1>, R<2>, R<3> and R<4> are organic radicals or H in some cases and X is halogen. The molar ratio II/III is greater than 1.5.

Description

lie 599729 PH 4286 COMMONWEALTH OF AUSTRALIA PATENTS ACT 1952-1973 COMPLETE SPECIFICATION
(ORIGINAL)
FOR OFFICE USE: ,9 'e d> O0 Class Application Number: Lodged: Complete Specification Lodged: Accepted: Published: Priority.
Related Art: Its f rrs t-I .j i" i. o i i Int Class 9 0 Name of Applicant: Address of Applicant: Actual Inventor(s) Address for Service: RHONE-POULENC AGROCHIMIE 14-20 Rue 'Pierre Baizet, Lyon 69009, France.
Jean.,-Pierre CORBET and Michel MULHAUSER Davies Collison, Patent Attorneys, 1 Little Collins Street, Melbourne, Victoria 3000, Australia Complete Specification for the .nvention entitled: "PREPARATION OF PL2JSPHORUS-CONTAINING INTERMEDIATES FOR HERBICID ES" The following statement is a full description of this invention, including the best method of performing it known to us:- I 'I -2- This invention relates to a process for the preparation of compounds which are useful as intermediates for herbicides.
The present invention relates to a process for the preparation of a compound of formula: 2 4 OR R I I (1) 0 F CH2 N CH 2 CO N S0 2
R
0 0 o oo0 10 wherein o0,
R
1 represents an optionally substituted o -D oo hydrocarbon radical, preferably alkyl, aryl or cycloalkyl, o 00 each of which may be substituted; suitable substituents 0o include halogen atoms and phenyl, cyano, alkyl, alkoxy and o0oo 15 alkylcarboxylate groups in which the alkyl groups preferably 0 00 contain from 1 to 4 carbon atoms; R' generally contains from 00 0 0 0 6 0 o0 1 to 18 carbon atoms, preferably from 1 to 7 carbon atoms, 0 o 0 and more particularly from 3 to 7 carbon atoms when R is a cycloalkyl group; preferably R 1 represents an alkyl group 0 o 00 20 containing from 1 to 4 carbon atoms, optionally substituted by halogen, especially chlorine or fluorine, e.g. CF 3 R represents a hydrogen atom or has one of the meanings given for R and is preferably an alkyl group containing from 1 to 4 carbon atoms,
R
2 and R 3 are such that OR 2 and OR 3 in which R 2 and R' may together form a single optionally substituted 1, 1 -3divalent radical, are hydrolysable groups; R 2 and R 3 preferably represent an optionally substituted alkyl, aryl or arylalkyl radical (suitable substituents are those mentioned for R 1 or R and R 3 may together form a single optionally substituted divalent radical preferably containing from 2 to 6 carbon atoms, e.g. an optionally o subsituted alkylene radical an ethylene or propylene 0 o. 2 3 a radical); R and R generally each contain from 1 to 12 o o 0 .o carbon atoms and preferably from 1 to 8 carbon atoms; and 00 0 S10 R represents a radical of formula Ar(R 5
(R
6
)C-
0 0 0 0 0 So in which Ar is an optionally substituted aromatic group, preferably phenyl, a an and R 6 each represent a hydrogen 0 0 a at atom or an (aromatic) radical Ar or an alkyl group o0° preferably containiing not more than 6 carbon atoms 0; 0 4 15 (preferably R represents benzyl), a e ooa by reacting a compound of formula: OR 2
OR
wherein R2, R3 and R4 are as hereinbefore defined with a compound of formula: ni t 0 z(II) 0 P Cl 2
I
OR
3 wherein R R and R are as hereinbefore defined with a compound of formula: X" C2 Co a SO 2 h i
(III)
wherein -4- X represents a halogen atom, e.g. chlorine, bromine or iodine, preferably chlorine, and R and RIare as hereinbef-ore defined.
Suitable substituents for the group Ar include alkyl and alkoxy groups, preferably containing from I to 4 o 0S carbon atoms, nitro radicals and halogen atoms.
Such a reaction is known from European Patent Application No. 0,189,725. The compou~nds of formula are intermediates for herbicides.
The present invention seeks to' provide an improved process for the preparation of the compounds of formula for a more satisfactory implementation on an industrial scale. The present invention also seeks to provide a simplified preparation process.
is It has been fuund that the molar ratio of the compound. of formula II to the compound of formula III is important in the reaction: in particular the use of a molar ratio greater than 1.5 4llows the presence of add~itional acceptor for acid to be avoide,:. This leads to two important advantages: firstly, it enables any stage for the removal of the said acceptor for acid to be omitted and secondly, it enables the yield to be increased.
Another important consequence of this total or near total absence of additional acceptor for acid is that it enables a recycling process to be carried out, further improving sigrificantly the ,-,ield and the implementation or) an industrial scale.
I r The present invention accordingly provides a process for the preparation of a compound of formula (I) wherein the various symbols are as hereinbefore defined by the reaction of a compound of formula (II) wherein the various symbols are as hereinbefore defined with a compound of formula (III) as hereinbefore defined, the molar ratio of c the compound of formula (II) to the compound of formula (III) being greater than The reaction according to the invention may be carried out in the absence, or more preferably in the presence, of a solvent. In fact, the presence of the solvent enables the temperature to be controlled more satisfactorily. The reaction is preferably carried out in an inert organic solvent at an elevated temperature.
Suitable solvents include nitriles (especially acetonitrile), ketones (especially acetone, cyclohexanone, methyl ethyl ketone and methyl isobutyl ketone), halogenated or non-halogenated hydrocarbons (especially benzene, toluene, xylenes and chlorobenzene), esters such as alkyl alkanoates (especially ethyl acetate), and aprotic polar solvents such as dimethylformamide and N-methylpyrrolidone.
The reaction temperature is generally from 30 to 150°C and preferably from 40 to 120 0
C.
The reaction product of formula may be isolated by any means known per se.
Some compounds of formula (II) are known 7 iinilir ill.^ l ^l j ^l^ -6- (Tetrahedron Letters no. 46, p. 4645, 1973). They can be prepared conveniently by reacting tris(aralkyl)hexahydrotriazines with diorganophosphites.
The compounds of formula (III) are also known.
The molar ratio of compound (II) to compound S' (III) is preferably greater than 1.8 and advantageously from S1.9 to 4.
According to a preferred feature, the process of the invention is carried out in the total or near total absence of additional acid acceptor. Near total absence means that the reaction medium may contain traces of acceptor for various reasons.
According to a further feature of the process according to the invention, the process is carried out continuously by recycling the compound of formula (II).
S.
C This recycling is accomplished at the end of the S' reaction, by extraction of unreacted compound of formula (II) into an acidic aqueous medium and then, after neutralization, transferring the compound of formula (II) into an organic phase for reaction with further compounid of formula (III).
The process is more particularly suitable for compounds in which R and R 1 are alkyl groups containing from 1 to 4 carbon atoms, preferably methyl, and/or in which R 2 and R 3 are alkyl, phenyl or benzyl groups.
The following Examples illustrate the invention.
F a u ra~ -7- Example 1 A mixture of diisopropyl N-benzylaminomethanephosphonate 285; 11.43 g; 4 x 10 2 moles) and "2 N-methyl-N-methysulphonylchloroacetamide (3.71 g; 2 x 10 2 moles) is heated for 2 h at 80°C. The reaction mixture is diluted to 50 cc with toluene and treated with water and oo°0a with hydrochloric acid. The aqueous phase and the toluene o 0:0 phase are separated. The toluene phase is concentrated and 0,C0 it is observed, by chromatography, that 8.025 g of the product is obtained, which corresponds to a yield of 92.4% relative to the N-methyl-N-methylsulphonylchloroacetamide employed.
The aqueous phase containing diisopropyl N-benzyl-aminomethanephosphonate hydrochloride is poured S 15 into toluene (20 rc), the mixture is neutralized with a stoichiometric quantity of aqut.uus 2 N sodium hydroxide.
e The aqueous phase and the toluene phase are separated. The S* toluene phase contains diisopropyl N-benzylamino- -2 methanephosphonate (1.82 x 10 2 moles) in the form of the base which can be recycled, after the distillation of toluene if j required.
SExample 2 The same trial carried out at 70 0 C leads to a yield, as determined by chromatography, of 72.5% relative to the N-methyl-N-meth, vsulphonylchloroacetamide employed.
Example 3 The same trial carried out at 90°C leads to a -8yield, as determined by, chromatography, of 86.7% relative to the N-me thyl-N-me thyl sulphor' Ichloroace tami le employed.
Comartive Example Diisopropyl N-benzylaminomethanephosphonate (5.71 2 x 10 -2 mole) and N-methyl-N-methylsulphonylchloroacetamide (3.71 g; 2 x 10 2 mole) are heated for 2 h at 0:0::80 0 C. A solution of triethyl:imine (2.8 cc; 2 x 102 molle) in toluene (15 cc) is poured gradually.. in the course of h, into the reaction mixture which is maintained at 80 0
C.
It The mixture is th'en cooled to 20 0 C, poured into water cc) at ambient temperature and the aqueous phase and the toluene phase are a;eparated. The toluene phase is conc:,,entrated under vacuum. It is observed, by chromatography, that 6.6 9 of the expected product was 1obtained, which corresponds to a yield of 75.8% relative to V. a the 2 reagents charged.
*~1Example4 l,3,5-trilbenzylhexahydrotriazine (59.5 0.166 mole) diisopropyl plbosphite (83 g; 0.5 mole) and toluene (100 g) are heated for 41 h 30 min at 120 0 C. The mixture is cooled to 20 0 C. An analysis by chromatography shows that the reaction yield of diisopropyl N-benzylaminomethanephosphoria Ie is quantitative. N-methyl-N-methylsuolphony'1chloroacetamide (37.1 g; 0.2 mole) is added. The reaction mixture is heated to 80 0Cfor 2 hours and then cooled to ambirnt temperature. It is then poured into water I i ~il -9- (150 g) and aqueous 37% HC1 (12 cc) is added in order to adjust the pH to 1. The phases are decanted and separated.
The organic phase has a weight of 173 g. The aqueous phase (265 g) is neutralized to pH 6 with aqueous 30% sodium hydroxide (30 cc) after adding toluene (100 The phases are decanted and separated. The second organic phase has a o oo weight of 195 g.
S The first organic phase (173 g) contains f 0 44.6% of the product expected, which amounts to 0.18 mole.
10 The second organic phase (195 g) contains 42% of diisopropyl St N-benzylaminomethanephosphonate which amounts to 0.287 mole.
S1st recycling T> e 2nd organic phase (195 g) is azeotropically dried (67 g of toluene and water are removed) and a solution (120 g) containing diisopropyl N-benzylaminomeqthanephosphonate (0.25 mole) and N-methyl-N-methylsulphonylchloroacetamide (37.1 g; 0.2 mole) in toluene is added and the mixture is heated for 2 h at 80 C. The reaction mass is treated exactly as before.
2nd recycling A 2nd recycling of diisopropyl N-benzylaminomethanephosphonate was carrried out exactly as above.
All the results are given in the table below: A diisopropyl N-benzylaminomethanephosphonate B N-methyl-N-methylsulphonylchloroacetamide ar t L m C condensation product expected R-ai materials jA recycled Yield of em ployed A 0.5 mole 89% B 0. 2 mole 1st recycling A 0. 25 mole 0.28 mole 100% B 0. 2 mole 2nd recycling A 0.25 mole 0.18 mole 100% B 0.2 mole O 0 0 a 00
C
6 9 t C
CO
00 0 000 0 40 0 C 'C 00 0 0 00 O 0 400000 C 0
CC
CC

Claims (9)

1. A process for the preparation of a c mpound of the formula: OR 2 a I (I) o P C N Cu 2 co so 2 1 O I 0 wherein 0 1 R represents an optionally substituted *081@ O t €oo°hydrocarbon rarcical; @o'I o a R represents a hydrogen atom 6r an optionally substituted hydrocarbon radical; n *e R 2 and R) are such that OR 2 and OR, in which R2 and R 3 may together form a single optionally substituted divalent radical, are hydrolysable groups; and 4 5 R represents a radical of formula Ar(R )C- in which Ar is an optionally substituted aromatic group, and R 5 and R 6 are a hydrogen atom or a radical Ar or an alkyl group,, which process comprises the reaction of A compound of the formula: OR 2 0 ;e .CH^ 2 -H R 1R QR 3 I 0 and R" may together form a single optionally substituted divatent radical, are hydrolysable groups; and /2 4 wi whe.ein R 2 R' and R 4 are as hereinbefore defined th a compound of formula: X C CO 02 a (XI) 0 9
9. 0 9 0 o a. 4 0 *400 *9 0 .4 *9 9. 4 9 09 wherein X represents a halogen atom and R and R2 are as hereinbefore defined, the molar ratio of compound (II) to compound (11) being greater than 1.5; and wherein said reaction temperature is from 30 0 C to 150 0 C. 2. A process according to claim 1 in which R' represents a hydrocarbon radical optionally substituted by halogen, phenyl, cyano, alkyl,, alkoxy or alkylcarboxylate. 3. A process according to claim 2 in which the hydrocarbon ralical represented by R' is alkyl, aryl or cycloalkyl. A process according to claim 1, 2 or 3 in which the hydrocarbon radical represented by R 1 contains from 1 to 7 carbon atoms or from-. 3 to 7 carbon atoms when R' repres.ents a cycloalkyl group, A pxaaess according to any one of the preceding claims in which R' represents an alkyl group containing from 1 to 4 carbon atoms optionally substituted by halogen. 6. A process according to any one of the preceding claims in which R represents an alkyl group containing from 1 to 4 carbon atoms. 7. A process according to any one of the preceding claims in which R 2 and R 3 represent an alkyl, aryl or 9 9 9 9 o o~ 9 CO -13- arylalkyl radical optionally substitute by halogen, phenyl, cyano, alkyl, alkoxy or alkylcarboxylate, or R 2 and R 3 together represent a single optionally substituted divalent radical containing from 2 to 6 carbon atoms. 8. A process according to any one of the preceding claims wherein R and R 1 each represent an alkyl group containing from I to 4 carbon atoms. 9. A process according to any one of the preceding claims wherein R and R 1 each represent methyl. A process according to any one of the preceding claims wherein R 2 and R 3 each represent an alkyl, phenyl or benzyl group.
11. A process according to any one of the preceding claims wherein R 4 represents benzyl. I 12. A process according to any one of the preceding claims wherein X represents chlorine.
13. A process according to any one of the preceding claims, wherein the molar ratio of compound (II) to compound (III) is greater than 1.8. 4. A process according to any one of claims I to 12 wherein the molar ratio of compound (II) to compound (III) is from 1.9 to 4. A process according to any one of the preceding claimus wherein the reaction is carried out in the total or near total absence of additional acid acceptor. -14-
16. A process according to any one of the preceding claims wherein the reaction is carried out from 30° to 150 C.
17. A process according to any one of claims 1 to wherein the reaction is carried out from 40° to 120 0 C.
18. A process according to any one of the preceding 0"oo" claims wherein the reaction is carried out in the presence aovent of a solvent. 9 co 0 0 t o0 0 19. A process according to claim 18, wherein the 0 t solvent is a nitrile, a ketone, an ester, a halogenated or non-halogenated hydrocarbon, or an aprotic polar solvent. o 20. A process according to any one of the preceding claims, wherein unreacted compound of formula (II) is recycled. S21. A process according to claim 20, wherein the recycling is accomplished, at the end of the reaction, by extractiQn of unreacted compound of formula (II) into an acidic aqueous medium, separation and then, after neutralization, transferring the compound of formula (II) into an organic phase for reaction with further compound of formula (III).
22. A process according to claim 1 substantially as hereinbefore described in any one of Examples 1 to 4.
23. A compound of formula as defined in claim 1 when prepared by a process claimed in any one of claims 1 to 22. to or indicated~ in the specification and-/-(i5r- claims of this application, individual]L~y-oif"collectively, and any and all Dated this 16th day of December 1987 t, RHONE-POULENC AGROCHIMIE By its Patent Attorneys DAVIES COLLISON
AU82618/87A 1986-12-18 1987-12-16 Preparation of phosphorus-containing intermediates for herbicides Ceased AU599729B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8618308A FR2608609B1 (en) 1986-12-18 1986-12-18 PREPARATION OF PHOSPHORUS INTERMEDIATES FOR HERBICIDE USE
FR8618308 1986-12-18

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AU8261887A AU8261887A (en) 1988-06-23
AU599729B2 true AU599729B2 (en) 1990-07-26

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EP (1) EP0275804B1 (en)
JP (1) JPS63165391A (en)
KR (1) KR880007408A (en)
CN (1) CN87105951A (en)
AT (1) ATE67998T1 (en)
AU (1) AU599729B2 (en)
BR (1) BR8706887A (en)
CA (1) CA1297493C (en)
DD (1) DD264921A5 (en)
DE (1) DE3773482D1 (en)
DK (1) DK665087A (en)
ES (1) ES2025201B3 (en)
FR (1) FR2608609B1 (en)
GR (1) GR3003011T3 (en)
HU (1) HU202881B (en)
IL (1) IL84482A (en)
PT (1) PT86395B (en)
ZA (1) ZA879478B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU6723887A (en) * 1985-12-04 1987-06-30 Rhone-Poulenc Agrochimie Process for the preparation of n-sulfonyl n-(phosphonomethylglycyl) amines usable as weed-killers
AU573410B2 (en) * 1984-12-26 1988-06-09 Rhone-Poulenc Agrochimie N-sulphonyl-(n-(phoponomethyl)glycyl)amine derivatives
AU577916B2 (en) * 1985-01-14 1988-10-06 Rhone-Poulenc Agrochimie N-(phosphonomethylglycyl) sulphonylamine type herbicides

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU573410B2 (en) * 1984-12-26 1988-06-09 Rhone-Poulenc Agrochimie N-sulphonyl-(n-(phoponomethyl)glycyl)amine derivatives
AU577916B2 (en) * 1985-01-14 1988-10-06 Rhone-Poulenc Agrochimie N-(phosphonomethylglycyl) sulphonylamine type herbicides
AU6723887A (en) * 1985-12-04 1987-06-30 Rhone-Poulenc Agrochimie Process for the preparation of n-sulfonyl n-(phosphonomethylglycyl) amines usable as weed-killers

Also Published As

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HU202881B (en) 1991-04-29
EP0275804B1 (en) 1991-10-02
CA1297493C (en) 1992-03-17
PT86395A (en) 1988-01-01
JPS63165391A (en) 1988-07-08
ATE67998T1 (en) 1991-10-15
EP0275804A1 (en) 1988-07-27
PT86395B (en) 1990-11-20
IL84482A (en) 1992-11-15
ES2025201B3 (en) 1992-03-16
BR8706887A (en) 1988-07-26
KR880007408A (en) 1988-08-27
DE3773482D1 (en) 1991-11-07
IL84482A0 (en) 1988-04-29
AU8261887A (en) 1988-06-23
DD264921A5 (en) 1989-02-15
FR2608609A1 (en) 1988-06-24
DK665087D0 (en) 1987-12-17
GR3003011T3 (en) 1993-02-17
DK665087A (en) 1988-06-19
FR2608609B1 (en) 1989-06-02
CN87105951A (en) 1988-06-29
ZA879478B (en) 1988-06-14
HUT48634A (en) 1989-06-28

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