Liquefaction of chlorine by multi-stage compression and cooling

Claim 2

In a method of liquefying chlorine out of a chlorine rich feed gas mixture containing chlorine gas and non-condensable gases, which method comprises: A. feeding the gas mixture to compressor means and compressing the gas within the compressor means; B. feeding the compressed gas mixture to condenser means and recovering liquid chlorine and a second gas mixture, reduced in chlorine content, from the condenser; C. feeding the liquefied chloride from the condenser means to a heat exchanger means as a refrigerant while feeding the second gas mixture to the heat exchanger means in indirect thermal contact with the liquefied chlorine; D. recovering liquefied chlorine condensed out of said second gas mixture; and E. passing chlorine refrigerant vaporized in the heat exchanger means back to said compressor means; the improvement comprising: A. compressing the feed gas mixture in compressor means containing a plurality of individual compressors in series, thereby increasing the feed gas pressure from the first compressor through at least a subsequent compressor to a last compressor in the compressor means; B. feeding the liquefied chlorine sequentially through a heat exchanger means containing a plurality of individual heat exchangers in series, from a high pressure end from an outlet of the condenser means through a heat exchanger to a low pressure while feeding the second gas mixture through the heat exchanger means, thereby vaporizing the liquid chlorine refrigerant in the individual heat exchangers at decreasing pressures along the series of individual heat exchangers in the direction of flow, condensing chlorine out of second gas mixture; C. recovering the chlorine condensed out of the second gas mixture; and D. passing substantially all of the chlorine refrigerant vaporized in a first individual heat exchanger to a first individual compressor having a suction pressure which is, relative to all of the individual heat exchangers of said heat exchanger means, most nearly equal to but lower than the pressure of said individual heat exchanger,; and E. repeating steps (C) through (D) for all of said individual heat exchangers in said heat exchanger means while recovering the chlorine condensed out of the second gas mixture in the said heat exchangers.

Claim 3

The method of claim 1 wherein the first gas mixture contains more than about 0.8 percent noncondensables and at least about 97 percent of the chlorine in said first gas mixture is recovered as a liquid substantially free of noncondensables.

Claim 4

The method of claim 1 wherein the pressure of the refrigerant in an individual heat exchanger exceeds the pressure of the inlet to the individual compressor to which it is fed.

Claim 5

The method of claim 1 wherein the temperature difference between the chlorine refrigerant and the second gas mixture is from about 1.0° to about 5.0° Centigrade.

Claim 6

The method of claim 1 comprising withdrawing a portion of liquid chlorine from a tank, passing said liquid chlorine to said condenser as a refrigerant, vaporizing said liquid chlorine, and recovering a chlorine gas reduced in noncondensable content.

Claim 7

In a method of liquefying a high boiling component out of a gas mixture containing the high boiling component and non-condensable gases, which method comprises: A. feeding the gas mixture fo compressor means and compressing the gas within the compressor means; B. feeding the compressed gas mixture to condenser means and recovering the liquefied high boiling gas and a second gas mixture, reduced in high boiling component content, from the condenser; C. feeding the liquefied high boiling component from the condenser means to a heat exchanger means as a refrigerant, while feeding the second gas mixture to the heat exchanger means in indirect thermal contact with the liquefied high boiling component; D. recovering liquefied high boiling component condensed out of said second gas mixture; and E. passing high boiling component refrigerant vaporized in the heat exchanger means back to said compressor means; the improvement comprising: A. compressing the feed gas mixture in compressor means containing a plurality of individual compressors in series, thereby increasing the feed gas pressure from the first compressor through at least a subsequent compressor to a last compressor in the compressor means; B. feeding the liquefied high boiling component through a heat exchanger means containing a plurality of individual heat exchangers in series, from a high pressure end from an outlet of the condenser means through the heat exchanger to a lower pressure while feeding the second gas mixture through the heat exchanger means, thereby vaporizing the liquid high boiling component as a refrigerant in the individual heat exchangers at decreasing pressures along the series of individual heat exchangers in the direction of flow, condensing high boiling component out of the second gas mixture; C. recovering the high boiling component condensed out of the second gas mixture; D. passing substantially all of the high boiling refrigerant vaporized as a refrigerant in a first individual heat exchanger to a first individual compressor having a suction pressure which is, relative to all of the individual heat exchangers of said heat exchanger means, most nearly equal to but lower than the pressure of said individual heat exchanger; E. removing the condensate of the second gas mixture from the individual heat exchangers; and F. repeating steps (C) through (E) for all of said individual heat exchangers in said heat exchanger means.

Claim 8

In a method of liquefying a high boiling component out of a gas mixture containing the high boiling component and non-condensable gases, which method comprises: A. feeding the gas mixture fo compressor means and compressing the gas within the compressor means; B. feeding the compressed gas mixture to condenser means and recovering the liquefied high boiling gas and a second gas mixture, reduced in high boiling component content, from the condenser; C. feeding the liquefied high boiling component from the condenser means to a heat exchanger means as a refrigerant, while feeding the second gas mixture to the heat exchanger means in indirect thermal contact with the liquefied high boiling component; D. recovering liquefied high boiling component condensed out of said second gas mixture; and E. passing high boiling component refrigerant vaporized in the heat exchanger means back to said compressor means; the improvement comprising: A. compressing the feed gas mixture in compressor means containing a plurality of individual compressors in series, thereby increasing the feed gas pressure from the first compressor through at least a subsequent compressor to a last compressor in the compressor means; B. feeding the liquefied high boiling component through a heat exchanger means containing a plurality of individual heat exchangers in series, from a high pressure end from an outlet of the condenser means through the heat exchanger to a lower pressure while feeding the second gas mixture through the heat exchanger means, thereby vaporizing the liquid high boiling component as a refrigerant in the individual heat exchangers at decreasing pressures along the series of individual heat exchangers in the direction of flow, condensing high boiling component out of the second gas mixture; C. recovering the high boiling component condensed out of the second gas mixture; D. passing substantially all of the high boiling refrigerant vaporized as a refrigerant in a first individual heat exchanger to a first individual compressor having a suction pressure which is, relative to all of the individual heat exchangers of said heat exchanger means, most nearly equal to but lower than the pressure of said individual heat exchanger; E. removing the condensate of the second gas mixture from the individual heat exchangers; and F. repeating steps (C) through (E) for all of said individual heat exchangers in said heat exchanger means.

Claim 9

The method of claim 6 wherein said high boiling component is selected from the group consisting of SO 2 , NH 3 , CO 2 , and Cl 2 .

Claim 10

In a method of liquefying chlorine out of a chlorine rich feed gas mixture containing chlorine gas and non-condensable gases, which method comprises: A. feeding the gas mixture to compressor means and compressing the gas within the compressor means; B. feeding the compressed gas mixture to condenser means and recovering liquid chlorine and a second gas mixture, reduced in chlorine content, from the condenser; C. feeding the liquefied chloride from the condenser means to a heat exchanger means as a refrigerant, while feeding the second gas mixture to the heat exchanger means in indirect thermal contact with the liquefied chlorine; D. recovering liquefied chlorine condensed out of said second gas mixture; and E. passing chlorine refrigerant vaporized in the heat exchanger means back to said compressor means; the improvement comprising: A. compressing the feed gas mixture in compressor means containing a plurality of individual compressors in series, thereby increasing the feed gas pressure from the first compressor through at least a subsequent compressor to a last compressor in the compressor means; B. feeding the liquefied chlorine to a heat exchanger means containing a plurality of individual heat exchangers in series, from a high pressure end from an outlet of the condenser means through a heat exchanger to a lower pressure while feeding the second gas mixture through the heat exchanger means, thereby vaporizing the liquid chlorine refrigerant in the individual heat exchangers at decreasing pressures along the series of individual heat exchangers in the direction of flow condensing chlorine out of the second gas mixture; C. recovering liquefied chlorine condensed out of said second gas mixture; D. passing substatially all of the chlorine refrigerant vaporized in an individual heat exchanger to a first individual compressor having a suction pressure which is, relative to all of the individual heat exchangers of said heat exchanger means, most nearly equal to but lower than the pressure of said individual heat exchanger; E. removing the condensate of the second gas mixture from the individual heat exchangers; and F. repeating steps (C) through (E) for all of said individual heat exchangers in said heat exchanger means.

Claim 11

In a method of liquefying chlorine out of a chlorine rich feed gas mixture containing chlorine gas and non-condensable gases, which method comprises: A. feeding the gas mixture to compressor means and compressing the gas within the compressor means; B. feeding the compressed gas mixture to condenser means and recovering liquid chlorine and a second gas mixture, reduced in chlorine content, from the condenser; C. feeding the liquefied chloride from the condenser means to a heat exchanger means as a refrigerant, while feeding the second gas mixture to the heat exchanger means in indirect thermal contact with the liquefied chlorine; D. recovering liquefied chlorine condensed out of said second gas mixture; and E. passing chlorine refrigerant vaporized in the heat exchanger means back to said compressor means; the improvement comprising: A. compressing the feed gas mixture in compressor means containing a plurality of individual compressors in series, thereby increasing the feed gas pressure from the first compressor through at least a subsequent compressor to a last compressor in the compressor means; B. feeding the liquefied chlorine to a heat exchanger means containing a plurality of individual heat exchangers in series, from a high pressure end from an outlet of the condenser means through a heat exchanger to a lower pressure while feeding the second gas mixture through the heat exchanger means, thereby vaporizing the liquid chlorine refrigerant in the individual heat exchangers at decreasing pressures along the series of individual heat exchangers in the direction of flow condensing chlorine out of the second gas mixture; C. recovering liquefied chlorine condensed out of said second gas mixture; D. passing substatially all of the chlorine refrigerant vaporized in an individual heat exchanger to a first individual compressor having a suction pressure which is, relative to all of the individual heat exchangers of said heat exchanger means, most nearly equal to but lower than the pressure of said individual heat exchanger; E. removing the condensate of the second gas mixture from the individual heat exchangers; and F. repeating steps (C) through (E) for all of said individual heat exchangers in said heat exchanger means.