IE42376B1 - Process for producing carbonic acid monoester salts - Google Patents

Process for producing carbonic acid monoester salts

Info

Publication number
IE42376B1
IE42376B1 IE2690/75A IE269075A IE42376B1 IE 42376 B1 IE42376 B1 IE 42376B1 IE 2690/75 A IE2690/75 A IE 2690/75A IE 269075 A IE269075 A IE 269075A IE 42376 B1 IE42376 B1 IE 42376B1
Authority
IE
Ireland
Prior art keywords
process according
carbonic acid
reaction
salt
acid monoester
Prior art date
Application number
IE2690/75A
Other versions
IE42376L (en
Original Assignee
Anic Spa
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Anic Spa filed Critical Anic Spa
Publication of IE42376L publication Critical patent/IE42376L/en
Publication of IE42376B1 publication Critical patent/IE42376B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C68/00Preparation of esters of carbonic or haloformic acids
    • C07C68/04Preparation of esters of carbonic or haloformic acids from carbon dioxide or inorganic carbonates
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F1/00Compounds containing elements of Groups 1 or 11 of the Periodic Table
    • C07F1/005Compounds containing elements of Groups 1 or 11 of the Periodic Table without C-Metal linkages
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F3/00Compounds containing elements of Groups 2 or 12 of the Periodic Table
    • C07F3/003Compounds containing elements of Groups 2 or 12 of the Periodic Table without C-Metal linkages
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Inorganic Fibers (AREA)

Abstract

METHOD FOR THE PREPARATION OF CARBONIC ACID MONOESTER SALTS . A method is disclosed for the preparation of salts of monoesters of the carbonic acid, the improvement consisting in that the alcohols corresponding to the esters are reacted with carbon dioxide and a compound of an alkali metal or an alkaline earth metal. A distinct advantage over the use of the alcoholates is obtained inasmuch as the reaction is less violent, side-reactions are put aside and the costs are lowered.

Description

This invention relates to a process for producing salts of monoesters of carbonic acid.
According to the invention there is provided a process for producing a salt of a carbonic acid monoester having the formula (RO - C - 0) M II where M represents an alkali metal or an 'alkaline earth metal, ji is 1 or 2, and R represents an alkyl radical, a cycloalkyl radical, an aryl radical or an aralkyl radical, which method comprised reacting carbon dioxide, an alcohol of formula ROH and an alkali metal compound or alkaline earth metal compound having an anion selected from C03=, S03=, 0=, B03=, S= and SH-, to form the desired carbonic acid monoester salt.
The radical R may be substituted or unsubstituted, mono- or polyhydroxyl ated, and saturated or unsaturated.
The reaction takes place according to the following equation: „+nC0,+hR0H— (R0C00)nM+HnXnMm-l· where m is 1, 2 or 3. It may be performed simply by causing a stream of COg - 2 42376 to bubble through a solution or a suspension of the selected metal compound in the alcohol which is used, preferably with stirring. It is also possible to carry out the reaction in the presence of a solvent or diluent providing that it is inert to the reactants and products.
The pressure of CO^ may be varied, for example, from 0 to 100 atmospheres gauge.
The temperature of the reaction is preferably maintained between the freezing point and the boiling point temperature of the alcohol, more preferably from 0°C to 60°C.
The salts of carbonic acid monoesters produced by the process of the invention may be isolated 'from the product mixture by, for example filtration, if they are insoluble. Alternatively they may be precipitated from an appropriate solvent, or evaporated off from the product mixture.
The salts produced by the process of the invention may be used instead of the corresponding alcoholates in condensation reactions, for example in the condensation of aldehydes with active-hydrogen-containing molecules, or of esters with ureas. They may also be used as catalysts in the disproportionation reactions of aromatic aldehydes.
By comparison with alcoholates, the salts produced according to the present invention lead, in the above indicated reactions, to a less drastic reaction, which means that side reactions are limited and thus lower costs are incurred.
The following Examples 1 and 2 illustrate the invention; Examples 3 and 4 illustrate the uses to which the products of the process according to the invention may be put. - 3 4 2376 EXAMPLE 1. grants of anhydrous KgCOg were slurried in 100 mis of anhydrous methanol and a stream of COg was bubbled through the slurry with vigorous stirring at 25°C. The amount of COg used was slightly greater than that which was absorbed by the slurry under these conditions.
The reaction was both exothermic and rapid, and was completed within 30 minutes. On completion of the absorption, the residue, that is KHCOg, was collected on a filter and the solution was evaporated in vacuo.
There were obtained 8.5 grams of KOCOOCHgi this product was slightly impure since it contained traces of KHC03< EXAMPLE 2. .6 grams of CaO were slurried in 100 mis of allyl alcohol and stirred at 25°C under a stream of COg. There ensued a reaction which was both exothermic and rapid; this reaction was completed within 35 minutes. The bulky white precipitate which was produced was collected on a filter under a nitrogen atmosphere, washed with ethyl ether and dried in vacuo. There were obtained 20 grams of Ca(OCOOCHgCH=CHg)g.
EXAMPLE 3. grams of NaOCOOCHg (0.1 mol) were dissolved in 100 mis of methanol; grams of diethylmalonate and 6 grams urea were added to the resulting solution. The mixture thus formed was refluxed for about 8 hours, and the reflux product was dried in vacuo to yield about 15 grams of sodium barbiturate. This salt, following hydrolysis with 2 N hydrochloric acid and extraction with ether, gave 12 grams of barbituric acid.
EXAMPLE 4. grams of benzyl cyanide, 11 grams of benzaldehyde and 10 grams of NaOCOOCHg were dissolved in 100 mis of methanol and refluxed for two hours.
The sodium carbonate which formed was filtered from the mixture whilst hot - 4 42376 and the solvent was evaporated in vacuo. There were obtained 22 grams of phenyl cinnamonitrile, having NagCO^ as an impurity. The pure product was obtained by washing with water.

Claims (8)

1. A process for producing a salt of a carbonic acid monoester having the formula (RO - C - 0) n M where M represents an alkali metal or an alkaline earth metal, jn is 1 or 2, and R represents an alkyl radical, a cyeloalkyl radical, an aryl radical or an aralkyl radical, which method comprises reacting carbon dioxide, an alcohol of formula ROH and an alkali metal compound or alkaline earth metal compound having an anion selected from C0 3 =, S0 3 =, 0=, B0 3 =, S= and SH-, to form the desired carbonic acid monoester salt.
2. A process according to Claim 1 wherein the carbon dioxide is at a pressure of from 0 to 100 atmospheres gauge.
3. A process according to Claim 1 or 2 wherein the reaction is carried out at a temperature which is between the freezing point and the boiling point of the alcohol.
4. A process according to Claim 3 wherein the reaction is carried out at a temperature of from 0 to 60°C.
5. A process according to any one of the preceding claims wherein the reaction is carried out in a diluent which is inert to the reactants and products.
6. A process according to any one of the preceding claims which includes the additional step of isolating the desired salt from the product mixture.
7. A process according to Claim T substantially as described in Example 1 or 2. - 5 42376
8. A salt of a carbonic acid mono ester whenever produced by the process according to any one of the preceding claims.
IE2690/75A 1974-12-10 1975-12-10 Process for producing carbonic acid monoester salts IE42376B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT30338/74A IT1026904B (en) 1974-12-10 1974-12-10 PROCEDURE FOR THE PREPARATION OF MONOESTER SALTS OF CARBONIC ACID

Publications (2)

Publication Number Publication Date
IE42376L IE42376L (en) 1976-06-10
IE42376B1 true IE42376B1 (en) 1980-07-30

Family

ID=11229564

Family Applications (1)

Application Number Title Priority Date Filing Date
IE2690/75A IE42376B1 (en) 1974-12-10 1975-12-10 Process for producing carbonic acid monoester salts

Country Status (18)

Country Link
JP (1) JPS593982B2 (en)
AT (1) AT343090B (en)
BE (1) BE836385A (en)
CA (1) CA1058204A (en)
CH (1) CH620193A5 (en)
DE (1) DE2555567C3 (en)
DK (1) DK142749B (en)
ES (1) ES443588A1 (en)
FR (1) FR2294160A1 (en)
GB (1) GB1523477A (en)
IE (1) IE42376B1 (en)
IT (1) IT1026904B (en)
LU (1) LU73950A1 (en)
NL (1) NL175520C (en)
NO (1) NO144703C (en)
SE (1) SE426390B (en)
SU (1) SU656503A3 (en)
ZA (1) ZA757614B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4123446A (en) * 1977-04-11 1978-10-31 Allied Chemical Corporation Synthesis of metal alkyl carbonates
US4217298A (en) * 1977-09-05 1980-08-12 Tokuyama Soda Kabushiki Kaisha Process for preparing organic carbonates
DE2748718A1 (en) * 1977-10-29 1979-05-03 Bayer Ag PROCESS FOR THE PRODUCTION OF DIALKYLCARBONATES
JPH0251684U (en) * 1988-10-03 1990-04-12
FR2669925B1 (en) * 1990-11-30 1993-01-29 Rhone Poulenc Chimie PROCESS FOR THE PREPARATION OF POLYALKOXYLATED AROMATIC COMPOUNDS.

Also Published As

Publication number Publication date
DK142749B (en) 1981-01-12
DE2555567B2 (en) 1978-10-12
IT1026904B (en) 1978-10-20
ES443588A1 (en) 1977-05-01
CA1058204A (en) 1979-07-10
ATA932875A (en) 1977-09-15
CH620193A5 (en) 1980-11-14
DK142749C (en) 1981-08-17
LU73950A1 (en) 1976-07-01
FR2294160B1 (en) 1980-04-25
NL7514361A (en) 1976-06-14
BE836385A (en) 1976-06-08
FR2294160A1 (en) 1976-07-09
AT343090B (en) 1978-05-10
NO754159L (en) 1976-06-11
DE2555567C3 (en) 1979-06-07
JPS5182214A (en) 1976-07-19
IE42376L (en) 1976-06-10
NL175520B (en) 1984-06-18
ZA757614B (en) 1976-11-24
GB1523477A (en) 1978-08-31
JPS593982B2 (en) 1984-01-27
DE2555567A1 (en) 1976-06-16
NL175520C (en) 1984-11-16
NO144703C (en) 1981-10-21
NO144703B (en) 1981-07-13
SU656503A3 (en) 1979-04-05
SE426390B (en) 1983-01-17
SE7513876L (en) 1976-06-11
DK557375A (en) 1976-06-11

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