Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
255 words
In a process for producing fuel grade mixtures of methanol and higher alcohols, which process comprises: (a) feeding a gaseous mixture, consisting essentially of carbon monoxide and hydrogen to a synthesis reactor operating at a temperature of from 200° to 500° C. and at a pressure higher than 30 atm to form an intermediate product; and (b) cooling the intermediate product consisting of methanol, higher alcohols, water and unreacted gases, the improvement which comprises: (a 1 ) subjecting the cooled intermediate product to the conversion reaction CO+H.sub.2 O→CO.sub.2 +H.sub.2, operating said conversion process at a temperature of 150° to 250° C. and at the same pressure of the synthesis reactor to form a reaction product consisting essentially of methanol, higher alcohols, unreacted gases, carbon dioxide and traces of water; (b 1 ) cooling the reaction product to form liquid phase consisting essentially of the fuel mixture and a gaseous phase consisting essentially of CO, H 2 and CO 2 ; (c 1 ) separating the gaseous phase and then passing it into an absorption section for the elimination of CO 2 , the gases so purified being in part recycled and in part let off to avoid the accumulation of inert matter; (d 1 ) sending the liquid phase to a stripping section to remove the gases dissolved therein, the let off gases of step (c 1 ) being used as stripping agents; and (e 1 ) sending the liquid phase so purified to the absorption section where it is utilized as an absorbing liquid.
Claim 2
Dependent Claim
255 words
In a process for producing fuel grade mixtures of methanol and higher alcohols, which process comprises: (a) feeding a gaseous mixture, consisting essentially of carbon monoxide and hydrogen to a synthesis reactor operating at a temperature of from 200° to 500° C. and at a pressure higher than 30 atm to form an intermediate product; and (b) cooling the intermediate product consisting of methanol, higher alcohols, water and unreacted gases, the improvement which comprises: (a 1 ) subjecting the cooled intermediate product to the conversion reaction CO+H.sub.2 O→CO.sub.2 +H.sub.2, operating said conversion process at a temperature of 150° to 250° C. and at the same pressure of the synthesis reactor to form a reaction product consisting essentially of methanol, higher alcohols, unreacted gases, carbon dioxide and traces of water; (b 1 ) cooling the reaction product to form liquid phase consisting essentially of the fuel mixture and a gaseous phase consisting essentially of CO, H 2 and CO 2 ; (c 1 ) separating the gaseous phase and then passing it into an absorption section for the elimination of CO 2 , the gases so purified being in part recycled and in part let off to avoid the accumulation of inert matter; (d 1 ) sending the liquid phase to a stripping section to remove the gases dissolved therein, the let off gases of step (c 1 ) being used as stripping agents; and (e 1 ) sending the liquid phase so purified to the absorption section where it is utilized as an absorbing liquid.
Claim 3
Dependent Claim
22 words
A process according to claim 1 wherein the synthesis reactor is operated at a temperature comprised between 300° C. and 500° C.
Claim 4
Dependent Claim
19 words
A process according to claim 11 wherein the synthesis reactor is operated at a pressure higher than 150 ata.
Claim 5
Dependent Claim
16 words
A process according to claim 2 wherein the temperature is between 360° C. and 420° C.
Claim 6
Dependent Claim
14 words
A process according to claim 3 wherein the pressure is higher than 200 ata.
Claim 7
Dependent Claim
22 words
A process according to claim 1 wherein the synthesis reactor is operated at a temperature comprised between 200° C. and 300° C.
Claim 8
Dependent Claim
21 words
A process according to claim 1 wherein the synthesis reactor is operated at a pressure comprised between 30 and 150 ata.
Claim 9
Dependent Claim
16 words
A process according to claim 6 wherein the temperature is between 230° C. and 270° C.
Claim 10
Dependent Claim
15 words
A process according to claim 7 wherein the pressure is between 50 and 100 ata.
Claim 11
Dependent Claim
16 words
A process according to claim 1 wherein the temperature is between 160° C. and 220° C.
Claim 12
Dependent Claim
20 words
A process according to claim 1 wherein the conversion reactor is operated at the same pressure of the synthesis reactor.
Claim 13
Dependent Claim
34 words
A process according to claims 2 or 3 wherein the synthesis reaction takes place in the presence of a catalyst based on zinc and chromium modified with alkali metals and/or with alkaline earth metals.
Claim 14
Dependent Claim
41 words
A process according to claims 6 or 7 wherein the synthesis reaction takes place in the presence of a catalyst based on copper, zinc and with Al and/or Cr and/or V and/or Mn modified with Alkali Metals and/or Alkaline earth metals.
Claim 15
Dependent Claim
23 words
A process according to claims 10 or 12 wherein the conversion reaction takes place in the presence of a catalyst based on copper.
Claim 16
Dependent Claim
34 words
A process according to claim 1 wherein the absorbing liquid is regenerated and freed from the absorbed gases either by bringing it to a lower pressure or by recycling it to the stripping section.
Claim 17
Dependent Claim
25 words
A process according to claim 1 wherein the section of absorption of the CO 2 is operated at the same pressure of the synthesis reactor.