Distillation of methane from a methane-containing crude gas

Claim 2

In a separation in a rectification column of methane and optionally lower-boiling components from a methane-containing crude gas, which gas contains additionally higher-boiling hydrocarbons, hydrogen sulfide, carbon dioxide, or mixtures thereof, wherein an auxiliary cycle containing a fluid medium is employed for the production of cooling to produce reflux liquid at the head of the rectifying column, the improvement wherein liquid in the rectifying column located in the region of plates numbers 0.4 x-0.6 x, wherein x is the number of theoretical plates in the column, is vaporized in indirect heat exchange with condensing auxiliary cycle medium, without said condensing auxiliary cycle medium reboiling the bottoms, and reboiling the bottoms with feed to the rectification column without indirect heat exchange in said region of plates.

Claim 3

The process of claim 1, wherein an open auxiliary cycle is utilized wherein gaseous product methane is expanded and combined with the auxiliary cycle medium which has been expanded after passage through the liquid vaporization operation; the mixture of the two sources of methane being used as heat exchange medium to produce the reflux liquid at the column head, and subsequently being divided into two flows, one forming the product gas and the other subsequently being compressed and used as a heat exchange medium to vaporize the reflux liquid.

Claim 4

The process of claim 1, wherein a closed auxiliary cycle is utilized wherein a mixture of ethane, ethylene or higher-boiling hydrocarbons circulates as the auxiliary cycle medium.

Claim 5

The process of claim 1, wherein the temperature of the reflux liquid in the region of the column in which it is vaporized by the condensing auxiliary cycle medium is 175°-205° K. and the temperature of the condensing auxiliary cycle medium used to effect the vaporization is 180°-275° K.

Claim 6

The process of claim 1, wherein the liquid which is vaporized in heat exchange with condensing auxiliary cycle medium is located at about the middle of the column.

Claim 7

In the separation in a rectification column of methane and optionally lower-boiling components from a methane-containing crude gas, which gas contains additionally higher-boiling hydrocarbons, hydrogen sulfide, carbon dioxide, or mixtures thereof, wherein an auxiliary cycle containing a fluid medium is employed for the production of cooling to produce reflux liquid at the head of the rectifying column located in the region of plates numbers 0.4 x-0.6 x, wherein x is the number of theoretical plates in the column, is vaporized in indirect heat exchange with condensing auxiliary cycle medium, wherein an open auxiliary cycle is utilized wherein gaseous product methane is expanded and combined with the auxiliary cycle medium which has been expanded after passage through the liquid vaporization operation; the mixture of the two sources of methane being used as heat exchange medium to produce the reflux liquid at the column head, and subsequently being divided into two flows, one forming the product gas and the other subsequently being compressed and used as a heat exchange medium to vaporize the reflux liquid.

Claim 8

In the separation in a rectification column of methane and optionally lower-boiling components from a methane-containing crude gas, which gas contains additionally higher-boiling hydrocarbons, hydrogen sulfide, carbon dioxide, or mixtures thereof, wherein an auxiliary cycle containing a fluid medium is employed for the production of cooling to produce reflux liquid at the head of the rectifying column located in the region of plates numbers 0.4 x-0.6 x, wherein x is the number of theoretical plates in the column, is vaporized in indirect heat exchange with condensing auxiliary cycle medium, wherein an open auxiliary cycle is utilized wherein gaseous product methane is expanded and combined with the auxiliary cycle medium which has been expanded after passage through the liquid vaporization operation; the mixture of the two sources of methane being used as heat exchange medium to produce the reflux liquid at the column head, and subsequently being divided into two flows, one forming the product gas and the other subsequently being compressed and used as a heat exchange medium to vaporize the reflux liquid.