Assertion: ethane | /r/CapableOf | recover a desorption effluent stream
Facets:
value: by contacting the adsorbent bed
type: MANNER
value: from the adsorbent bed
type: LOCATION
Source sentences:
text: Provided is a process for separating ethane and optionally C 3+ paraffins from a mixture comprising methane, ethane and optionally C 3+ paraffins, the process comprising: i) passing the mixture through an adsorbent bed comprising an ETS-10 type material at a pressure at of at least 200 psia wherein ethane and, if present, C 3+ paraffins are selectively adsorbed relative to methane, to give an adsorption effluent stream; ii) recovering a desorption effluent stream from the adsorbent bed by contacting the adsorbent bed with water; wherein the adsorption effluent stream is enriched in methane relative to the mixture and the desorption effluent stream is enriched in ethane and optionally C 3+ paraffins relative to the mixture.
text: Provided is a process for separating ethane and optionally C 3+ paraffins from a mixture comprising methane, ethane and optionally C 3+ paraffins, the process comprising: i) passing the mixture through an adsorbent bed comprising an ETS-10 type material at a pressure at of at least 200 psia wherein ethane and, if present, C 3+ paraffins are selectively adsorbed relative to methane, to give an adsorption effluent stream; ii) recovering a desorption effluent stream from the adsorbent bed by contacting the adsorbent bed with water; wherein the adsorption effluent stream is enriched in methane relative to the mixture and the desorption effluent stream is enriched in ethane and optionally C 3+ paraffins relative to the mixture.
text: Provided is a process for separating ethane and optionally C 3+ paraffins from a mixture comprising methane, ethane and optionally C 3+ paraffins, the process comprising: i) passing the mixture through an adsorbent bed comprising an ETS-10 type material at a pressure at of at least 200 psia wherein ethane and, if present, C 3+ paraffins are selectively adsorbed relative to methane, to give an adsorption effluent stream; ii) recovering a desorption effluent stream from the adsorbent bed by contacting the adsorbent bed with water; wherein the adsorption effluent stream is enriched in methane relative to the mixture and the desorption effluent stream is enriched in ethane and optionally C 3+ paraffins relative to the mixture.