Process for preparing ethene

Claim 2

Process for preparing ethene by dehydrating ethyl alcohol in the presence of catalyst, characterized in that ethyl alcohol is heated by indirect heat exchange, up to a temperature in the range from 180°-600° C., introducing thus heated ethyl alcohol into one or more adiabatic reactors containing in its interior a catalyst fixed bed, said adiabatic reactor being maintained in a pressure range between 0.2 and 20 kg/cm 2 absolute, and said fixed catalyst bed being maintained at a temperature comprised within the range from 600° C. on the top to 180° C. in the bottom, by means of a sensible heat carrying stream heated up to a temperature up to 800° C., the weight ratio between the sensible heat carrying fluid stream and the stream of ethyl alcohol varies within a 0.2:1 to 20:1 range, and the ratio between the amounts of ethyl alcohol and the catalyst is comprised within a range from 10 to 0.01 g/h of ethyl alcohol per gram of catalyst; removing the effluent from said adiabatic reactor and sending the same to the purification step.

Claim 3

Process for preparing ethene in accordance to claim 1, characterized in that the heat required for the dehydrating reactions is supplied to the process by means of a sensible heat carrying fluid introduced in the adiabatic reactor simultaneously with the feed.

Claim 4

Process for preparing ethene in accordance to claim 2, characterized in that the sensible heat carryng fluid is selected from at least one of the following: part of the adiabatic effluent used as recycle stream, steam provided by an external source, and heated inert gas provided by an external source.

Claim 5

Process for preparing ethene in accordance to claim 1, characterized in that ethyl alcohol is heated by indirect heat exchange up to a temperature in the range from 180° to 600° C., thus introducing the heated ethyl alcohol into one or more adiabatic reactors containing in its interior a fixed catalyst bed, said adiabatic reactor being maintained within a pressure range between 0.2 an 20 kg/cm 2 absolute, and said fixed catalyst bed being maintained within a temperature range from 600° C. on top to 180° C. in the bottom by means of sensible heat carrying fluid previously heated to a temperature up to 800° C. said heated fluid being selected from an inert gas, steam or a combination of inert gas and steam, the weight ratio between the sensible heat carrying fluid stream and the ethyl alcohol stream varies within the range from 0.2:1 to 20:1 and the ratio between the amounts of ethyl alcohol and the catalyst is comprised within a range from 10 to 0.01 g/h of ethyl alcohol per gram of catalyst; removing the effluent from said adiabatic reactor and sending it to purification stage.

Claim 6

Process for preparing ethene, in accordance to claim 1, characterized in that the ethyl alcohol is heated through indirect heat exchange within the temperature range from 180° to 600° C., introducing the thus heated ethyl alcohol into one or more adiabatic reactors containing internally a catalyst fixed bed, said adiabatic reactor being maintained within absolute pressure range between 0.2 and 20 kg/cm 2 and said catalyst fixed bed being maintained at a temperature comprised within the range from 600° C. on the top to 180° C. in the bottom through a recycle stream as a sensible heat carrying fluid, separating the effluent from said adiabatic reactor into two streams one of them after exchanging heat with ethyl alcohol being introduced into the adiabatic reactor and going through a compressor being reheated to a temperature up to 800° C. and introduced into the adiabatic reactor as said recycled stream and the other portion of the effluent being sent after having exchanged heat with ethyl alcohol which will be introduced into the adiabatic reactor, to the ethene purification stage, the weight ratio between the sensible heat carrying fluid and the ethyl alcohol stream varying within the range from 0.2:1 to 20:1 and the ratio between the amounts of ethyl alcohol and catalyst being comprised within a range between 10 g and 0.01 g/h of ethyl alcohol per gram of catalyst.

Claim 7

Process for preparing ethene, in accordance to claims 1 or 4 or 5, characterized in that the catalyst which comprises the fixed bed inside said adiabatic reactors is selected from silica, alumina, silica-alumina, refractory metal oxides, zeolites, phosphoric acid supported on carbon, calcium phosphates and calcium molybdates.

Claim 8

Process for preparing ethene, in accordance to claims 1 or 4 or 5, characterized in that the catalyst comprising said fixed bed inside said adiabatic reactors is selected from the group consisting of silica-alumina and alumina.

Claim 9

Process for preparing ethene, in accordance to claims 1 or 4 or 5, characterized in that the reaction is carried out in a single adiabatic reactor.

Claim 10

Process for preparing ethene, in accordance to claims 1 or 4 or 5 characterized in that the reaction is carried out in adiabatic reactors arranged in parallel.

Claim 11

Process for preparing ethene, in accordance to claims 1 or 4 or 5, characterized in that the reaction is carried out in adiabatic reactors forming assemblies of parallel series.

Claim 12

Process for preparing ethene, in accordance to claims 1, 4 or 5, wherein said ethyl alcohol is heated by said indirect heat exchange to a temperature within the range 300°-500° C.

Claim 13

In a process for preparing ethene by the dehydration of ethanol, the improvement which comprises providing the required heat for the reaction directly to the reaction by means of simultaneously introducing the ethanol feed and a heat-carrying fluid into at least one adiabatic reactor containing a fixed bed catalyst.

Claim 14

In a process for preparing ethene by the dehydration of ethanol, the improvement which comprises providing the required heat for the reaction directly to the reaction by means of simultaneously introducing the ethanol feed and a heat-carrying fluid into at least one adiabatic reactor containing a fixed bed catalyst.