SI9300427A - Process for preparing isocyanates by decomposition of n,n,n'-three substituted ureas - Google Patents
Process for preparing isocyanates by decomposition of n,n,n'-three substituted ureas Download PDFInfo
- Publication number
- SI9300427A SI9300427A SI9300427A SI9300427A SI9300427A SI 9300427 A SI9300427 A SI 9300427A SI 9300427 A SI9300427 A SI 9300427A SI 9300427 A SI9300427 A SI 9300427A SI 9300427 A SI9300427 A SI 9300427A
- Authority
- SI
- Slovenia
- Prior art keywords
- formula
- isocyanate
- boiling point
- reaction conditions
- cyclic
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C263/00—Preparation of derivatives of isocyanic acid
- C07C263/06—Preparation of derivatives of isocyanic acid from or via ureas
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/14—The ring being saturated
Abstract
Description
Chemie Linz Gesellschaft m.b.H.Chemie Linz Gesellschaft m.b.H.
Postopek za pripravo izocianatov z razkrojem Ν,Ν,Ν’-trisubstituiranih sečninA process for the preparation of isocyanates with decomposition of Ν, Ν, Ν′-trisubstituted urea
Izum se nanaša na postopek za pripravo izocianatov z razkrojem Ν,Ν,Ν’-trisubstituiranih sečnin.The invention relates to a process for the preparation of isocyanates with decomposition of Ν, Ν, Ν′-trisubstituted urea.
Izocianati predstavljajo gospodarsko pomembno skupino vmesnih produktov, ki jih uporabimo med drugim v industriji umetnih snovi, pri proizvodnji lakov in pri pripravi sredstev za zaščito rastlin.Isocyanates are an economically important group of intermediates that are used, inter alia, in the plastics industry, in the manufacture of varnishes and in the preparation of plant protection products.
Iz tega razloga so znani tudi številni postopki za pripravo izocianatov, ki pa imajo več hib. Tako izhajajo npr. starejši postopki v glavnem iz fosgena ali iz fosgena nastalih produktov, medtem ko z novejšimi postopki, pri katerih se izognejo uporabi fosgena, dobijo izocianate le v slabih dobitkih.For this reason, a number of processes for the preparation of isocyanates, which have several defects, are also known. Thus, for example, older processes mainly from phosgene or from phosgene-derived products, while newer processes that avoid the use of phosgene yield isocyanates only in poor yields.
Opisani so bili že tudi postopki, ki izhajajo iz substituiranih sečnin, ki jih termično razkrojijo. V FR-PS 1,473,821 razkrojijo trisubstituirane sečnine v estre izocianske kisline in amine pri temperaturi pod 200°C v topilu z dielektrično konstanto pod 40. Izocianate pa dobijo le z dobitkom okoli 60 %. V US-PS 3,936,484 predlagajo postopek za termični razkroj disubstituiranih sečnin, zlasti za pripravo toluilen-2,42 diizocianata. Prednostno nastajajoči amin odstranijo iz reakcijske zmesi s pomočjo toka nosilnega plina, ki mu je lahko dodano dodatno topilo.The processes resulting from the substitution of thermally degraded urea have also been described. In FR-PS 1,473,821 decompose trisubstituted ureas into isocyanic acid esters and amines at a temperature below 200 ° C in a solvent with a dielectric constant below 40. However, isocyanates are only obtained in a yield of about 60%. US-PS 3,936,484 proposes a process for the thermal decomposition of disubstituted ureas, in particular for the preparation of toluene-2,42 diisocyanate. Preferably, the resulting amine is removed from the reaction mixture by a carrier gas stream, to which additional solvent may be added.
Hibe tega postopka pa so, da lahko v glavnem preko vrha odvedejo le nastajajoči amin in dejanski produkt ostane na dnu ter ga je treba nato izolirati in čistiti, in da dosežejo dober dobitek le z dodatkom dodatnega topila.The disadvantages of this process, however, are that they can mainly take the emerging amine through the top and the actual product remains at the bottom and must then be isolated and cleaned, and that they achieve good yield only with the addition of additional solvent.
Sedaj smo lahko nepričakovano našli postopek za pripravo izocianatov, ki izhaja iz določenih Ν,Ν,Ν’-trisubstituiranih sečnin, pri katerem ni treba uporabiti fosgena in pridemo do želenih izocianatov na enostaven način z visokim dobitkom in čistoto.We have now unexpectedly been able to find a process for the preparation of isocyanates derived from certain Ν, Ν, tr′-trisubstituted ureas, which does not require phosgene and yields the desired isocyanates in an easy way with high yield and purity.
Predmet izuma je torej postopek za pripravo izocianatov, označen s tem, da Ν,Ν,Ν’trisubstituirane sečnine s formulo I R2 R1The subject of the invention is therefore a process for the preparation of isocyanates, characterized in that Ν, Ν, Ν'isubstituted urea of the formula I R 2 R 1
R3 R 3
v kateri so Rp R2 in R3 enaki ali različni in pomenijo raven, razvejen ali cikličen, nesubstituiran ali s (C^-CJalkoksi, v danem primeru substituiranim fenilom, halogenom ali z drugimi ostanki, inertnimi ob uporabljenih reakcijskih pogojih, substituiran (C^C^jalkilni ostanek ali R2 in R3 skupaj pomenita heterocikličen nearomatski obroč, ki lahko v danem primeru vsebuje še nadaljnje heteroatome, razkrojimo v razredčilu, inertnem ob reakcijskih pogojih, pri zvišani temperaturi v lahko hlapen izocianat s formulo RjNCO in v težko hlapen sekundarni amin s formulo R2R3NH, katerega vrelišče je nad vreliščem izocianata in nad uporabljeno reakcijsko temperaturo, nakar izocianat s pomočjo toka nosilnega plina odvedemo preko vrha.in which R p R 2 and R 3 are the same or different and represent a level, branched or cyclic, unsubstituted or substituted by (C 1 -C 6 alkoxy, optionally substituted phenyl, halogen or other radicals in use under the reaction conditions used) The C 1 -C 6 alkyl residue or R 2 and R 3 together represent a heterocyclic non-aromatic ring which may optionally contain further heteroatoms, decomposed in a diluent inert under the reaction conditions, at elevated temperature, into a lightly volatile isocyanate of the formula R 1 NCO and into a heavy a volatile secondary amine of the formula R 2 R 3 NH whose boiling point is above the boiling point of the isocyanate and above the reaction temperature used, and then the isocyanate is discharged via the carrier gas stream over the top.
Kot izhodne spojine so primerne načelno vse Ν,Ν,Ν’-trisubstituirane sečnine, ki pri termični obremenitvi razpadejo v lahko hlapen izocianat in v težko hlapen sekundarni amin, katerega vrelišče je nad vreliščem izocianata in nad reacijsko temperaturo. To so spojine s formulo I, v kateri so Rp R2 in R3 enaki ali različni in pomenijo raven, razvejen ali cikličen, nesubstituiran ali s (C^C^alkoksi, v danem primeru substituiranim fenilom, halogenom ali z drugimi ostanki, inertnimi ob uporabljenih reakcijskih pogojih, substituirani (Cj-C24)alkilni ostanek, kot npr. metilni, etilni, n-propilni, i-propilni, n-butilni, sek.butilni, terc.butilni, heksilni, oktilni, decilni, dodecilni, tetradecilni, heksadecilni, oktadecilni, cikloheksilni ali benzilni ostanek.In principle, all Ν, Ν, Ν'-trisubstituted ureas which, under thermal loading, decompose into a readily volatile isocyanate and into a hardly volatile secondary amine whose boiling point is above the isocyanate boiling point and above the reaction temperature are suitable as starting compounds. These are compounds of formula I in which R p R 2 and R 3 are the same or different and represent straight, branched or cyclic, unsubstituted or (C 1 -C 4 alkoxy, optionally substituted phenyl, halogen or other radicals, inert under the reaction conditions used, a substituted (C 1 -C 24 ) alkyl residue, such as methyl, ethyl, n-propyl, i-propyl, n-butyl, sec-butyl, tert-butyl, hexyl, octyl, decyl, dodecyl , tetradecyl, hexadecyl, octadecyl, cyclohexyl or benzyl residues.
(Cj-CJalkoksi ostanki so npr. metoksi, etoksi, propoksi, butoksi in heksoksi. Fenilni ostanek je lahko npr. med drugim substituiran s (Cj-CJalkilom, (C^-CJalkoksi, halogenom, amino ali nitro. R2 in R3 lahko tudi skupaj tvorita heterocikličen nearomatski obroč, ki lahko vsebuje še nadaljnje heteroatome, kot npr. pirolidin, piperidin, piperazin ali morfolin.(C 1 -C 6 alkoxy residues are, for example, methoxy, ethoxy, propoxy, butoxy and hexoxy. The phenyl residue may, for example, be substituted by (C 1 -C 6 alkyl, (C 1 -C 6 alkoxy, halogen, amino or nitro. R 2 and R 3 they may also together form a heterocyclic non-aromatic ring which may contain further heteroatoms such as pyrrolidine, piperidine, piperazine or morpholine.
Prednostne izhodne spojine so spojine s formulo I, v kateri pomenijo R} raven, razvejen ali cikličen (C2-C10)alkilni ostanek ali benzilni ostanek ter R2 in R3 raven, razvejen ali cikličen (C4-C20)alkilni ostanek ali benzilni ostanek.Preferred starting compounds are compounds of formula I, in which R} linear, branched or cyclic (C 2 -C 10) alkyl radical or a benzyl radical and R 2 and R 3 a linear, branched or cyclic (C 4 -C 20) alkyl residue or benzyl residue.
Posebno prednostne Ν,Ν,Ν’-trisubstituirane sečnine so zato med drugim N,Ndioktil-N’-etilsečnina, N,N-dioktil-N’-propilsečnina, N,N-dicikloheksil-N’-propilsečnina, N,N-dioktil-N’-izopropilsečnina, N,N-dibenzil-N’-butilsečnina, N,N-dioktilN’-butilsečnina, N,N-dioktil-N’-benzilsečnina in N,N-dioktil-N’-cikloheksilsečnina.Particularly preferred Ν, Ν, Ν'-trisubstituted ureas are therefore, among others, N, Ndioctyl-N'-ethylurea, N, N-dioctyl-N'-propylurea, N, N-dicyclohexyl-N'-propylurea, N, N- dioctyl-N'-isopropylurea, N, N-dibenzyl-N'-butylurea, N, N-dioctylN'-butylurea, N, N-dioctyl-N'-benzylurea and N, N-dioctyl-N'-cyclohexylurea.
Sečnine lahko pripravimo npr. preko N-alkilirane sečnine, kot je opisano v EP 0 471 983.Urea can be prepared e.g. via N-alkylated urea as described in EP 0 471 983.
Razkroj lahko poteče v razredčilu, inertnem ob reakcijskih pogojih. Kot inertna razredčila pridejo v poštev alifatski ali aromatski ogljikovodiki, kot npr. tetradekan, dodekan, heksadekan, oktadekan, parafin ali njihove zmesi z visokim vreliščem. Kot razredčilo pa lahko uporabimo tudi amin, ki nastane pri razkroju sečnine. Reakcjska temperatura je glede na uporabljeno sečnino približno med 90 do 400°C, prednostno med 150 in 300°C in zlasti prednostno med 210 in 280°. Izocianate izoliramo iz reakcijske zmesi s pomočjo toka inertnega plina, npr. s pomočjo toka dušika ali argona. Nato izocianate bodisi kondenziramo v hladilni pasti ali absorbiramo v topilu. Kot topila za izocianate so primerni alifatski ali aromatski ogljikovodiki, ki so lahko v danem primeru tudi halogenirani, kot npr. kloroform, metilenklorid, trikloretilen, toluol, in etri, kot npr. tetrahidrofuran. Topilo ali njegove dele lahko vnesemo že kot paro s tokom inertnega plina ali v reakcijsko zmes pred začetkom razkroja.Decomposition may occur in a diluent inert under reaction conditions. As inert diluents, aliphatic or aromatic hydrocarbons such as e.g. tetradecane, dodecane, hexadecane, octadecane, paraffin or mixtures thereof with high boiling point. An amine formed from urea degradation may also be used as a diluent. The reaction temperature is about 90 to 400 ° C, preferably between 150 and 300 ° C, and particularly preferably 210 to 280 ° C, depending on the urea used. Isocyanates are isolated from the reaction mixture by an inert gas stream, e.g. by means of a stream of nitrogen or argon. The isocyanates are then either condensed in a cooling trap or absorbed in a solvent. Suitable isocyanate solvents are aliphatic or aromatic hydrocarbons, which may optionally be halogenated, such as e.g. chloroform, methylene chloride, trichlorethylene, toluene, and ethers such as e.g. tetrahydrofuran. The solvent or portions thereof may already be introduced as an inert gas stream or into the reaction mixture prior to the onset of decomposition.
Reakcijo lahko po želji izvedemo tudi ob zmanjšanem ali zvišanem tlaku. Višino tlaka naravnamo pri tem glede na izbrane izhodne produkte in nastajajoče končne produkte na želeno vrednost.The reaction can optionally be carried out under reduced or increased pressure. The pressure level is adjusted according to the selected output products and emerging end products to the desired value.
Reakcijski čas znaša odvisno od reakcjske temperature, od reakcjskega tlaka in izhodnih spojin med 15 in 120 minut. Sekundarni amin, ki ostane pri razkroju na dnu, lahko npr. izoliramo z destilacijo ob zmanjšanem tlaku z dna in uporabimo kot izhodno spojino za različne reakcije. Želene izocianate dobimo z visoko čistoto in z dobitki do 99,9 %.The reaction time varies between 15 and 120 minutes depending on the reaction temperature, the reaction pressure and the starting compounds. The secondary amine remaining in the decomposition at the bottom may e.g. is isolated by distillation under reduced pressure from the bottom and used as a starting compound for various reactions. The desired isocyanates are obtained in high purity and in yields up to 99.9%.
Primer 1Example 1
Etilizocianat g N,N-dioktil-N’-etilsečnine v primerni aparaturi, ki poleg termostatirane reakcijske posode vsebuje napravo za uvajanje in ugodno porazdeljevanje toka inertnega plina v reakcijski zmesi in kolono za olajšanje ločenja produktov (uporabimo npr. zrcalno 30 cm Vigreux-jevo kolono), v 50 g heksadekana in 2,5 g CHC13 segrevamo 30 minut na okoli 250°C.Ethyl isocyanate g N, N-dioctyl-N'-ethylurea in a suitable apparatus, which, in addition to the thermostated reaction vessel, contains a device for introducing and favorable distribution of inert gas flow in the reaction mixture and a column to facilitate the separation of products (eg, use a 30 cm Vigreux mirror column), in 50 g of hexadecane and 2.5 g of CHC1 3 are heated at about 250 ° C for 30 minutes.
Nastajajoči etilizocianat med tem odstranjujemo iz reakcijske zmesi s pomočjo toka dušika (okoli 2 1/h) in kondenziramo v hladilni pasti, hlajeni s tekočim dušikom, kot CHC13 raztopino.The resulting ethylisocyanate is then removed from the reaction mixture by a stream of nitrogen (about 2 l / h) and condensed in a liquid nitrogen-cooled cooling trap as a CHC1 3 solution.
Dobitek: 97 %.Yield: 97%.
Primer 2Example 2
Propilizocianat g N,N-dicikloheksil-N’-propilsečnine segrevamo v aparaturi, opisani v primeru 1, v 50 g heksadekana 40 minut na okoli 250°C ter nastajajoči propilizocianat odstranjujemo s pomočjo toka dušika iz reakcijske zmesi in kondenziramo v hladilni pasti, hlajeni s tekočim dušikom.Propylisocyanate g N, N-dicyclohexyl-N'-propylurea was heated in the apparatus described in Example 1 in 50 g hexadecane for 40 minutes at about 250 ° C, and the resulting propylisocyanate was removed by a stream of nitrogen from the reaction mixture and condensed in a cooling trap, cooled with liquid nitrogen.
Dobitek: 99,9 %.Yield: 99.9%.
Analogno pripravimo naslednje spojine:The following compounds are prepared analogously:
ZaFor
Chemie Linz Gesellschaft m.b.H.Chemie Linz Gesellschaft m.b.H.
Claims (4)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT0163192A AT398762B (en) | 1992-08-13 | 1992-08-13 | METHOD FOR PRODUCING ISOCYANATES BY THE DECOMPOSITION OF N, N, N'-TRISUBSTITUTED UREAS |
Publications (1)
Publication Number | Publication Date |
---|---|
SI9300427A true SI9300427A (en) | 1994-03-31 |
Family
ID=3517594
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SI9300427A SI9300427A (en) | 1992-08-13 | 1993-08-13 | Process for preparing isocyanates by decomposition of n,n,n'-three substituted ureas |
Country Status (20)
Country | Link |
---|---|
EP (1) | EP0583637B1 (en) |
JP (1) | JPH06157449A (en) |
KR (1) | KR940003929A (en) |
CN (1) | CN1085209A (en) |
AT (2) | AT398762B (en) |
AU (1) | AU4427093A (en) |
CA (1) | CA2100718A1 (en) |
CZ (1) | CZ166593A3 (en) |
DE (1) | DE59305711D1 (en) |
DK (1) | DK0583637T3 (en) |
ES (1) | ES2097949T3 (en) |
GR (1) | GR3022795T3 (en) |
HU (1) | HU214218B (en) |
MX (1) | MX9304898A (en) |
NO (1) | NO932691L (en) |
PL (1) | PL300037A1 (en) |
SI (1) | SI9300427A (en) |
SK (1) | SK71693A3 (en) |
TW (1) | TW225517B (en) |
ZA (1) | ZA935235B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2377847A1 (en) * | 2010-04-14 | 2011-10-19 | 3M Innovative Properties Company | Process for producing isocyanates |
JP5165815B2 (en) * | 2011-06-24 | 2013-03-21 | 昭和電工株式会社 | Process for producing ethylenically unsaturated group-containing isocyanate compound |
KR101490202B1 (en) * | 2013-04-10 | 2015-02-05 | 광주과학기술원 | Microporous carbon dioxide adsorbents and method for manufacturing the same |
CN108299294A (en) * | 2017-01-11 | 2018-07-20 | 江苏恒瑞医药股份有限公司 | A kind of pleasure is cut down for the preparation method of Buddhist nun's impurity |
FR3068257B1 (en) * | 2017-06-29 | 2022-01-14 | Commissariat Energie Atomique | CARBAMIDES FOR THE SEPARATION OF URANIUM(VI) AND PLUTONIUM(IV) WITHOUT PLUTONIUM(IV) REDUCTION |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH228816A (en) * | 1940-11-19 | 1943-09-15 | Ig Farbenindustrie Ag | Process for the preparation of i-hexyl isocyanate. |
FR1473821A (en) * | 1963-07-05 | 1967-03-24 | Carbochimique Et Inst Francais | New isocyanic ester manufacturing processes |
US3936484A (en) * | 1974-09-25 | 1976-02-03 | Atlantic Richfield Company | Production of isocyanates from substituted ureas |
US4141913A (en) * | 1978-01-23 | 1979-02-27 | American Carbonyl, Inc. | Method of generating lower alkyl and cycloalkyl isocyanates |
-
1992
- 1992-08-13 AT AT0163192A patent/AT398762B/en not_active IP Right Cessation
-
1993
- 1993-07-08 SK SK716-93A patent/SK71693A3/en unknown
- 1993-07-16 CA CA002100718A patent/CA2100718A1/en not_active Abandoned
- 1993-07-20 ZA ZA935235A patent/ZA935235B/en unknown
- 1993-07-21 DE DE59305711T patent/DE59305711D1/en not_active Expired - Fee Related
- 1993-07-21 ES ES93111624T patent/ES2097949T3/en not_active Expired - Lifetime
- 1993-07-21 EP EP93111624A patent/EP0583637B1/en not_active Expired - Lifetime
- 1993-07-21 DK DK93111624.8T patent/DK0583637T3/en active
- 1993-07-21 AT AT93111624T patent/ATE150010T1/en not_active IP Right Cessation
- 1993-07-23 TW TW082105877A patent/TW225517B/zh active
- 1993-07-26 NO NO932691A patent/NO932691L/en unknown
- 1993-07-28 AU AU44270/93A patent/AU4427093A/en not_active Abandoned
- 1993-08-11 PL PL93300037A patent/PL300037A1/en unknown
- 1993-08-12 JP JP5200824A patent/JPH06157449A/en not_active Withdrawn
- 1993-08-12 MX MX9304898A patent/MX9304898A/en unknown
- 1993-08-12 HU HU9302338A patent/HU214218B/en not_active IP Right Cessation
- 1993-08-12 KR KR1019930015595A patent/KR940003929A/en not_active Application Discontinuation
- 1993-08-12 CN CN93116231A patent/CN1085209A/en active Pending
- 1993-08-13 CZ CZ931665A patent/CZ166593A3/en unknown
- 1993-08-13 SI SI9300427A patent/SI9300427A/en unknown
-
1997
- 1997-03-13 GR GR960403090T patent/GR3022795T3/en unknown
Also Published As
Publication number | Publication date |
---|---|
JPH06157449A (en) | 1994-06-03 |
CA2100718A1 (en) | 1994-02-14 |
CZ166593A3 (en) | 1994-03-16 |
EP0583637A1 (en) | 1994-02-23 |
DK0583637T3 (en) | 1997-04-21 |
CN1085209A (en) | 1994-04-13 |
ATE150010T1 (en) | 1997-03-15 |
ES2097949T3 (en) | 1997-04-16 |
TW225517B (en) | 1994-06-21 |
AU4427093A (en) | 1994-02-17 |
ATA163192A (en) | 1994-06-15 |
DE59305711D1 (en) | 1997-04-17 |
HU9302338D0 (en) | 1993-11-29 |
SK71693A3 (en) | 1994-06-08 |
NO932691D0 (en) | 1993-07-26 |
MX9304898A (en) | 1994-04-29 |
HUT64740A (en) | 1994-02-28 |
EP0583637B1 (en) | 1997-03-12 |
KR940003929A (en) | 1994-03-14 |
ZA935235B (en) | 1994-03-02 |
GR3022795T3 (en) | 1997-06-30 |
PL300037A1 (en) | 1994-04-05 |
NO932691L (en) | 1994-02-14 |
HU214218B (en) | 1998-01-28 |
AT398762B (en) | 1995-01-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0044421B1 (en) | Di- and oligo-1,2,4-triazolidine-3,5 diones and processes for their preparation | |
SI9300427A (en) | Process for preparing isocyanates by decomposition of n,n,n'-three substituted ureas | |
US4003938A (en) | Manufacture of aliphatic isocyanates | |
CZ280732B6 (en) | Process for separating isocyanic acid from a mixture of said acid with ammonia | |
KR100226551B1 (en) | Process for preparing isocyanates | |
EP0410168A2 (en) | Process for the preparation of asymmetrically substituted ureas | |
HU212464B (en) | Process for producing assimetric n,n`-substituated pure phenyl-ureas | |
AT398749B (en) | METHOD FOR PRODUCING ISOCYANIC ACID BY DEGRADING N, N-DISUBSTITUTED UREAS | |
DE4233534A1 (en) | Isocyanate cpds. prodn. from N,N,N'-tri-substd. urea cpds. | |
Xian et al. | A Facile and High-yielding Preparation of 1-Aryl-3, 3-dialkylureas | |
US4864045A (en) | Production of aminoethyl hydrogen sulfate | |
EP0104601A1 (en) | Method for producing tertiary amines from highly hindered aromatic secondary amines and carbonates | |
CZ282512B6 (en) | Process for preparing n-monosubstituted or n,n'-disubstituted urea | |
SI9300429A (en) | Method for producing isocyanic acid by decomposition of n,n-disubstituted ureas | |
CH422824A (en) | Process for preparing 5,5-bis-hydroxymethyl-dioxane-1,3-substituted dicarbamates in position 2 |