Method and system for preparing a lean methane-containing gas stream

1. A method of preparing a lean methane-containing gas stream, comprising:

feeding a hydrocarbon feed stream into a separator, said hydrocarbon feed stream containing at least methane, ethane, propane, butane and pentane;

withdrawing from the separator a vaporous methane enriched overhead stream containing at least a majority of the methane from the hydrocarbon feed stream;

withdrawing from the separator a liquid bottom stream;

passing the liquid bottom stream to a stabilizer column;

withdrawing from the stabilizer column a stabilized condensate stream enriched in pentane,

withdrawing from the stabilizer column a stabilizer overhead stream enriched in ethane, propane and butane;

splitting the overhead stream according to a split ratio into a main stream portion and a slip stream portion,

passing the slip stream portion to a fractionation unit comprising one or more fractionation columns to obtain an ethane enriched stream and a bottom stream enriched in propane and butane,

forming the lean methane-containing gas stream by combining the

the vaporous methane enriched overhead stream obtained from the separator, and

the main stream portion of the stabilizer overhead stream obtained from the stabilizer column.

2. The method according to claim 1 , wherein the method further comprises

feeding the lean methane-containing gas stream to a liquefaction system to obtain a liquefied lean methane-containing stream.

3. The method according to claim 1 , wherein the separator is one of a scrub column and an extraction column.

4. The method according to claim 1 , wherein the fractionation unit comprises a first fractionation column and a second fractionation column, wherein passing the slip stream portion to the fractionation unit comprises:

feeding the slip stream portion to the first fractionation column,

obtaining the ethane enriched stream as top stream from the first fractionation column and obtaining the bottom stream enriched in propane and butane from the first fractionation column,

passing the bottom stream enriched in propane and butane to the second fractionation column,

obtaining a propane enriched stream as top stream from the second fractionation column and obtaining a butane enriched stream as bottom stream from the second fractionation column.

5. The method according to claim 1 , wherein the method further comprises

passing the ethane enriched stream to an ethane storage or adding the ethane enriched stream to the lean methane-containing gas stream,

passing the propane enriched stream to a propane storage or adding the propane enriched stream to the lean methane-containing gas stream,

passing the butane enriched stream to a butane storage or adding the butane enriched stream to the lean methane-containing gas stream.

6. The method according to claim 1 , wherein the method comprises

collecting in a re-injection vessel:

the vaporous methane enriched overhead stream obtained from the separator,

the main stream portion of the stabilizer overhead stream obtained from the stabilizer column,

the butane enriched stream obtained from the fractionation unit,

optionally the top stream enriched in ethane and

optionally the top stream enriched in propane;

obtaining a re-injection stream from the re-injection vessel and

combining the re-injection stream with the vaporous methane enriched overhead stream obtained from the separator to form the lean methane-containing gas stream.

7. The method according to claim 1 , wherein the split ratio is defined as the flow rate of the split stream portion divided by the flow rate of the stabilizer overhead stream and wherein the method comprises

actively controlling the split ratio.

8. The method according to claim 1 , wherein the split ratio is actively controlled to vary in the range 0-0.25.

9. The method according to claim 1 , wherein feeding the hydrocarbon feed stream into the separator comprises

providing the hydrocarbon feed stream,

cooling the hydrocarbon feed stream by passing the hydrocarbon feed stream over an expansion-cooling device, such as a valve or an expander, to obtain a cooled hydrocarbon feed stream and

further cooling the cooled hydrocarbon feed stream by heat exchanging against the vaporous methane enriched overhead stream, obtaining a further cooled hydrocarbon feed stream and a warmed vaporous methane enriched overhead stream,

feeding the further cooled hydrocarbon feed stream into the separator,

compressing the warmed vaporous methane enriched overhead stream obtaining a pressurized warmed vaporous methane enriched overhead stream and

passing the warmed vaporous methane enriched overhead stream to be comprised in the lean methane-containing gas stream.

10. The method according to claim 1 , wherein prior to feeding the hydrocarbon feed stream into the separator, the method comprises:

receiving a raw hydrocarbon feed stream and passing the raw hydrocarbon feed stream through one or more of the following units to obtain the hydrocarbon feed stream:

condensate removal unit arranged to remove condensable such as water and added corrosion inhibitors,

acid gas removal unit arranged to lower amount of acid components, such as CO 2 and H 2 S,

dehydration unit arranged to lower the water content,

mercury removal unit arranged to lower a mercury content.

11. The method according to claim 1 , wherein the pressure level in the stabilizer column is below 17 bara.

12. The method according to claim 1 , wherein the method further comprises:

adding the butane enriched stream obtained from the fractionation unit to the methane enriched liquefaction feed stream or

passing the butane enriched stream to a butane storage.

13. A system for preparing a lean methane-containing gas stream comprising:

a separator arranged to receive a hydrocarbon feed stream containing at least methane, ethane, propane, butane and pentane;

the separator comprising an overhead outlet arranged to discharge a vaporous methane enriched overhead stream containing at least a majority of the methane from the hydrocarbon feed stream;

the separator comprising a bottom outlet arranged to discharge a liquid bottom stream;

a stabilizer column being in fluid communication with the bottom outlet of the separator to receive the liquid bottom stream,

the stabilizer column comprising a bottom outlet arranged to discharge a stabilized condensate stream enriched in pentane,

the stabilizer column comprising an overhead outlet arranged to discharge a stabilizer overhead stream enriched in ethane, propane and butane;

a splitter arranged to receive the stabilizer overhead stream and split the stabilizer overhead stream into a main stream portion and a slip stream portion,

a fractionation unit being in fluid communication with the splitter to receive the slip stream portion, the fractionation unit comprising one or more fractionation columns arranged to obtain an ethane enriched stream;

a lean methane-containing gas stream conduit arranged to receive

the vaporous methane enriched overhead stream obtained from the separator, and

the main stream portion of the stabilizer overhead stream obtained from the stabilizer column.

14. The method according to claim 1 , wherein the split ratio is actively controlled to vary in the range 0-0.10.