Abstract:
A DECANTING APPARATUS WITH HEAT EXCHANGER AND QUIESCENT CHAMBERS IS DESCRIBED. THE INLET CHAMBER IS CONNECTED VIA A PRODUCT CHAMBER OF A SPIRAL HEAT EXCHANGER TO A DISCHARGE CHAMBER DISPOSED ROUND THE HEAT EXCHANGER, THE SAID PRODUCT CHAMBER BEING NARROW AS COMPARED TO ITS HEIGHT AND BEING ARRANGED IN SEVERAL TURNS ROUND THE INLET CHAMBER.
Abstract:
Process for the separation of acetylene from gases obtained by pyrolysis by absorption by means of a high boiling solvent which absorbs acetylene selectively and by subsequent desorption, in which the portions of the gas components absorbed by the solvent are again expelled in several stages, partly with the use of stripping gases.
Abstract:
IMPROVEMENT IN THE PROCESS FOR ISOLATING CARBON DIOXIDE AND ACETYLENE FROM CRACKED GASES WHICH SUBSTANTIALLY CONTAIN HYDROGEN, CARBON MONOXIDE, METHANE, CARBON DIOXIDE, ETHYLENE AND ACETYLENE, BY MULTISTAGE WASHINGS USING ACETONE AND DIMETHYLFORMAMIDE AS SOLVENTS.
Abstract:
A PROCESS IS DESCRIBED FOR THE ISOLATION OF CARBON DIOXIDE AND ACETYLENE FROM A CRACKED GAS BY MULTISTAGE WASHINGS USING ACETONE AND DIMETHYLFORMAMIDE, WHEREIN THE CRACKED GAS IS FIRST WSASHED WITH ACETON, THEN ACETYLENE, CARBON DIOXIDE AND ETHYLENE ARE EXPELLED FROM THE
ACETONE SOLUTION BY RELEASE FROM PRESSURE AND THE ACETYLENE IS WASHED OUT OF THIS MIXTURE WITH DIMETHYLFORMAMIDE.
Abstract:
The invention relates to a process for selective absorption of chlorine and/or bromine from CO2-containing waste gases. The waste gas must contain at least 1 mol of SO2 per mol of Cl2 and/or per mol of Br2; if necessary, such a quantity of SO2 is added to the waste gas that the said relative quantity is present. For the absorption of the chlorine and/or bromine, the waste gas is mixed with steam and the mixture is then cooled until the steam condenses. An example of suitable apparatus is an upright pipe with an internal cooling coil.
Abstract:
1,256,052. Separating carbon dioxide and acetylene from cracked gas. FARBWERKE HOECHST A.G. 15 Jan., 1970 [16 Jan., 1969], No. 1985/70. Addition to 1,242,634. Heading B1L. The rich dimethylformamide loaded principally with carbon dioxide and acetylene from used in the process of the Parent Specification, predegassed at 1.05-1.3 ats. abs. and 95- 110C.; 60-70% of the still partially charged product is returned directly for reuse, while the remaining 40-30% is completely degassed at 0.25-0.55 ats. abs. and 110-130C. before also being returned to the final wash stage of the process.
Abstract:
of the disclosure: A process for the continuous rectification of a liquid mixture containing alcohols, in particular a fermented mash which has been substantially or completely freed from suspended substances, in an apparatus which is composed of several distillation columns linked with one another on the vapor side and which, in addition to a section used for the concentration of alcohol, can also contain a section used for the production of absolute alcohol, with the repeated utilization of the heat energy supplied on the multi-effect principle, which comprises a) distributing the liquid mixture in parallel to the distillation columns in the section of apparatus used for the concentration of alcohol, and feeding direct steam, having a temperature of 130 to 160.degree.C, to the sump of the column operated at the highest pressure; b) recovering heat energy in the form of direct steam from the top vapor of this column by means of a heat exchanger and feeding this steam, together with flash steam, formed in the sump of the same column, in a flash vessel, to the stripping section of the second column following; c) recovering direct steam in the same manner also from the top vapor of the second column and feeding this steam, together with the flash steam obtained from the sump of this column, to the third column, and, if appropriate also operating further downstream columns in this manner, the contentrated alcohol condensing in the heat exchangers being withdrawn, minus the portion refluxed, and, if appropriate being fed to a section for the production of absolute alcohol, in which d) the residual water still remaining is substantially removed from the concentrated alcohol by azeotropic distillation in one or more columns connected with one another in tandem on the vapor side.
Abstract:
A process for continuous rectification of a liquid mixture containing alcohols, particularly a liquid fermate, employs a plurality of distillation columns to which the liquid mixture is fed in parallel, and which have successively reduced operating pressures and temperatures from an initial one to a final one thereof. The top vapor distillate from the higher-pressure columns supplies driving heat to the sumps of the next successively lower-pressure columns. Direct steam at 130 DEG C. to 160 DEG C. is fed to the sump of the column operated at the highest pressure. Direct steam is generated by indirect heat exchange of water with the top vapor withdrawn from the columns, and the resulting direct steam is fed to the sumps of the next-lower-pressure columns. The apparatus can also include a section for the production of absolute alcohol.