US3109292A - System for handling refrigerant upon shut-down - Google Patents

System for handling refrigerant upon shut-down Download PDF

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US3109292A
US3109292A US88098A US8809861A US3109292A US 3109292 A US3109292 A US 3109292A US 88098 A US88098 A US 88098A US 8809861 A US8809861 A US 8809861A US 3109292 A US3109292 A US 3109292A
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conduit
gas
flow
fluid
temperature
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Walter O Schellenberg
John H Engel
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Phillips Petroleum Co
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Phillips Petroleum Co
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02—Discharging liquefied gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B45/00—Arrangements for charging or discharging refrigerant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022—Hydrocarbons, e.g. natural gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0248—Stopping of the process, e.g. defrosting or deriming, maintenance; Back-up mode or systems
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0249—Controlling refrigerant inventory, i.e. composition or quantity
    • F25J1/025—Details related to the refrigerant production or treatment, e.g. make-up supply from feed gas itself
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2345/00—Details for charging or discharging refrigerants; Service stations therefor
    • F25B2345/002—Collecting refrigerant from a cycle

Definitions

  • This invention relates to process and apparatus for handling refrigerant upon shut-down of a refrigeration system.
  • this invention relates to a process for disposal of quantities of cold liquid from a refrigeration system which comprises admixing this cold liquid with a heated gas before disposing of it.
  • this invention relates to a refrigerant liquid removal apparatus which comprises a refrigeration system, a fluid heating means, a fluid mixing means, first conduit means operatively connected between a source of gas and said fluid heating means, second conduit means operatively connected between said fluid heating means and said fluid mixing means, third conduit means operatively connected between said refrigeration system and said fluid mixing means, and fourth conduit means operatively connected between said fluid mixing means and a point of fluid utility.
  • this invention relates to a control system for controlling the process and apparatus.
  • a process for disposal of quantities of cold liquid from a refrigeration system which comprises admixing this cold liquid with a heated gas before disposing of it.
  • a process for rapid removal of cold liquid from a refrigeration system which comprises heating a gas stream in a heat exchanger, admixing into the resulting heated gas stream the cold liquid, passing this resulting mixture to a separation zone, separating out and removing any condensed water from the stream, and re- -United States Patent 3,l9,292 Patented Nov. 5, 1963 ice movingthe remainder of the resulting mixture from the separation zone for further utility.
  • a refrigerant liquid removal apparatus which comprises a refrigeration system, fluid heating means, fluid mixing means, first conduit means operatively connected between a source of gas in said fluid heating means, second conduit means opcratively connected between said fluid heating means and said fluid mixing means, third conduit means operatively connected between said refrigeration system and said fluid mixing means and fourth conduit means operatively connected between said fluid mixing means and a point of fluid utility.
  • an automatic control system for the process and apparatus.
  • a fuel or residue gas or other plant gas is passed by Way of conduits 1 and 2 through heater 3.
  • the resulting heated gas can be mixed with gas resulting from regeneration of a desiccant by way of conduit 22.
  • the gas mixture is then passed by way of conduit 4 through conduit 5 and its associated hand indicating controller and/or by Way of conduit 6 and its associated cooler 7 to conduit 8 'Which can contain therein check valve 9.
  • the gas is then passed through mixer ill by way of conduit 11 to a separator 12. Any liquid contained in this gas stream, such as condensed Water, is removed by Way of conduit 13 and its associated liquid level controller 14.
  • the dry gas is taken from an upper part of the separator by way of conduit 15 for further utility in the plant, such as e.g. a flare, as desired.
  • conduit 15 for further utility in the plant, such as e.g. a flare, as desired.
  • a refrigeration system There is depicted at 2.3 a refrigeration system.
  • Cold liquid from this refrigeuation unit- is passed by way of conduit 24, at such times as may be desired or necessary, to mixer Ill.
  • Valve 25 in conduit 24 can be manually operated or can be operated in response to some signal of plant shut-down.
  • the cold liquid in line 24 is mixed with a warm gas in his 0 at mixer fill.
  • the resulting gas mixture in conduit ll can then be separated as previously recited.
  • a portion of the gas in conduit 1 can by-pass heater 3 and separator 12 by way of conduit 16 and its associated control valve 17.
  • This valve is operated in response to differential pressure obtained between lines 1 and 115.
  • Other portions of the residue gas can be passed by way of lines l3 and 1% and their associated hand indicator controllers to conduit 2rd, Where they can be used to reactivate and regenerate the previously-mentioned desiccant.
  • conduit 2rd There can also be associated with conduit 2% a flow indicator.
  • Fuel gas is indicated as being supplied by way of conduit 21 to heater 3, the fuel gas being burned therein to provide heat for the gas in conduit 2.
  • This fuel gas conduit 2i can be provided with a flow recorder, as shown. a
  • Flow of heated gas in conduit 2 can be controlled by control valve 26, which is actuated in response to a-flow indicator controller in conduit 2.
  • the temperature obtained in separator 12 can conveniently be used to control one of two variables in the process.
  • a temperature recorder-controller 29 which can, by a proper manipulation of valves 36) and 31, be utilized to control either flow of cold liquid from the refrigeration unit by way of conduit 24 by manipulation of valve 28 or flow of heated gas to the separation zone by manipulation of valve 27 associated with the by-pass around valve 26.
  • controller 29 senses a temperature prevailing in separator 12 which can be either a gas or a liquid temperature, and transmits a correcting signal to the proper control valve.
  • a temperature control system for heater 3 which will now be described.
  • conduit 21 supplying fuel gas to the heater 3 a valve 32 associated with pressure controller 33, which senses pressure in conduit 21.
  • the index point of this pressure controller can be reset in response to signals from temperature recorder-controller 34 sensing temperature in conduit 2.
  • a control system which auto matically operates to remove quantifies of cold liquid from a refrigeration system at the time of shut-down or when otherwise desirable.
  • the flow of fuel gas to heater 3 is controlled primarily by pressure in the fuel gas line by valve 32 and controller 33.
  • the desired pressure can be reset in response to a temperature signal from controller 34 which senses temperature in the heater efiiuent. If the temperature of the heater goes above a predetermined point, as sensed by alarm 36, this alarm actuates valve 35 such that control valve 32 is closed.
  • the temperature controller 29 can be used to control either valve 28 or valve 27 as desired, suitable manipulation of valves 31? and 31 accomplishing this result. Controller 29 can either decrease the flow of cold liquid by manipulation of valve 28 or increase the flow of warm gas by manipulation of valve 27 as temperature in an upper portion of the separator zone decreases.
  • Instruments such as level controller 14, pressure controller 33, temperature controller 34, the various hand indicator controllers, flow recorders, flow indicators, temperature alarm, and differential pressure controller, are instruments commercially available. These can be, for example, Model 40 Foxboro units as described in Foxboro Bulletin 5A10'A of November 1955.
  • the heater inlet conduit 2 is operated at about 118 p.s.i.g. and 50 R, the heater efliuent is operated at about 112 p.s.i.g. and 606 F., and the separator vessel is operated at about llll F. and 97 p.s.i.g.
  • the fuel gas in line 21 is natural gas.
  • the residue gas introduced by way of line 1 is a plant residue gas comprising essentially methane, and the regenerator outlet gas in line 22 is a wet residue gas stream resulting from regeneration of dryers by passing residue gas therethrough.
  • the refrigerant in line 24 comprises a mixture of ethylene and propylene.
  • a process for rapid removal of cold liquid froma refrigeration system comprising removing said cold liquid from said system, heating a gas stream in a heat exchange zone, admixing into the resulting heated gas stream the thus-renroved cold liquid refrigerant, passing the resulting mixture to a separation zone, separating out and removing any condensed liquid therefrom, removing the remainder of said resulting mixture from said separation zone, passing said remainder to further utility, and controlling the rate of admixing in response to a temperature prevailing in said separation zone.
  • Refrigerant liquid removal apparatus comprising a 4 refirigeration system, fluid heating means, first conduit means operatively connected between a source of gas and sm'd fluid heating means, fluid mixing means, second conduit means operatively connected between said fluid heating means and said fluid mixing means, third conduit means operatively connected between said refrigeration system and said fluid mixing means, and fourth conduit means operatively connected between said fluid mixing means and a point of fluid utility, said point of fluid utility comprising vapor-liquid separating means having fifth con duit means operatively connected to a lower portion thereof for liquid removal and sixth conduit means operatively connected between an upper portion of said separating means and a. point of vapor utility.
  • Apparatus of claim 2 further provided with means sensing temperature in an upper portion of said separating means and adapted to control the flow of fluid in said third conduit means.
  • Apparatus of claim 10 further provided with flow sensing means in said first conduit means and adapted to control the flow of fluid in said second conduit means.
  • Apparatus of claim 2 further provided with seventh conduit means operatively connected between said source of gas and said point of vapor utility, said seventh conduit means being provided with flow control means therein adapted to control the flow therethrough in response to the pressure differential obtained between said source of gas and said point of vapor utility.
  • Apparatus of claim 2 further provided with a heating fluid source, eighth conduit means nected between said heating fluid source and said fluid heating means, flow control means in said eighth conduit means normally responsive to signal generating means sensing pressure in said eighth conduit means, said signal generating means being further responsive to temperature of fluid in said second conduit means, and means sensing temperature in said fluid heating means, said means sensing temperature being adapted to disengage said signal generating means from said flow control means in said eighth conduit means upon the temperature in said fluid heating means exceeding a predetermined value.
  • Apparatus of claim 2 further provided with ninth conduit means operatively connected between said fluid heating means and said fluid mixing means, means in said second conduit means adapted to control flow therein in response to flow in said first conduit means, and means in said ninth conduit means adapted to control flow therein in response to temperature in an upper portion of said separating means.
  • a process for treating cold liquid comprising ethyl ene and propylene which comprises heating a residue gas stream in a heat exchange Zone, admixing into the resulting heated residue gas stream said cold liquid, passing the resulting mixture to a separation zone wherein condensed liquids are removed, removing the remainder of said resulting mixture from said separation zone, passing said remainder to a point of utility, controlling the rate of flow of said resulting heated residue gas stream in response to temperature prevailing in an upper portion of said separation zone, controlling the rate of flow of said resulting heated residue gas stream in response to the rate ⁇ of flow of said residue gas stream, controlling the rate of flow of heating fluid to said heat exchange zone in response to the pressure thereof and further in response to the temperature in said heat exchange zone and the temperature of said resulting heated residue gas, passing a portion of said residue gas stream directly into admixture wtih said remainder, and controlling the rate of said last-recited passing in response to the pressure difierential prevailing between said residue gas stream and said remainder.

Description

3,199,292 SYSTEM FQR HANDLTNG REFRlG-ERANT WGN SHUT-DQWN Walter G. Sch llenberg and .lohn ll. Engel, gweeny, Tern,
assignors to Phillips Petroleum Company, a corporation of Delaware Filed Feb. 9, 1951, Ser. No. 88,698 15 Qlaims. (62. 62-52) This invention relates to process and apparatus for handling refrigerant upon shut-down of a refrigeration system. In one of its aspects, this invention relates to a process for disposal of quantities of cold liquid from a refrigeration system which comprises admixing this cold liquid with a heated gas before disposing of it. In another aspect, this invention relates to a refrigerant liquid removal apparatus which comprises a refrigeration system, a fluid heating means, a fluid mixing means, first conduit means operatively connected between a source of gas and said fluid heating means, second conduit means operatively connected between said fluid heating means and said fluid mixing means, third conduit means operatively connected between said refrigeration system and said fluid mixing means, and fourth conduit means operatively connected between said fluid mixing means and a point of fluid utility. In yet another aspect, this invention relates to a control system for controlling the process and apparatus.
In plants utilizing low-boiling compounds, such as methane, ethane and ethylene, in the liquid phase, there can be considerable difficulty in emptying vessels, lines and other eqm'pment. Plants equipped with small steamheated finned exchangers to vaporize the low-boiling liquids are generally unsuccessful in rapidly vaporizing large quantities of liquid. The large temperature difference between condensing steam and the boiling hydrocarbon probably tends to retard heat transfer because of vapor bianketin-g. Release of the materials to conventional flare or fuel gas systems presents the hazard of thermal shock to lines or formation of a liquid phase in normally gaseous fuels. The result of this practice is fractured relief lines and overheated furnace tubes. An expensive alternative is construction of large alloy pipe relief lines and specially designed flares. Most plants utilizing the above refrigerants have small, fired heaters for regenerating desiccant beds. The heaters are generally idle during plant shutdown and at some times during normal operation.
It is an object of this invention to provide process and apparatus for handling large quantities of cold liquid refrigerant. it is another object of this invention to provide process and apparatus for rapid disposal of large quantities of cold liquid refrigerant occasioned by shutdown of related processes. it is still another object of this invention to provide automatic controls for a process and apparatus useful in rapid disposal of large quantities of cold liquid refrigerant.
Other aspects, objects, advantages and features of this invention will become apparent from the following detailed description wmch is taken in conjunction with the accompanying drawing and appended claims.
According to this invention, there is provided a process for disposal of quantities of cold liquid from a refrigeration system which comprises admixing this cold liquid with a heated gas before disposing of it. There is further provided a process for rapid removal of cold liquid from a refrigeration system which comprises heating a gas stream in a heat exchanger, admixing into the resulting heated gas stream the cold liquid, passing this resulting mixture to a separation zone, separating out and removing any condensed water from the stream, and re- -United States Patent 3,l9,292 Patented Nov. 5, 1963 ice movingthe remainder of the resulting mixture from the separation zone for further utility. There is further provided a refrigerant liquid removal apparatus which comprises a refrigeration system, fluid heating means, fluid mixing means, first conduit means operatively connected between a source of gas in said fluid heating means, second conduit means opcratively connected between said fluid heating means and said fluid mixing means, third conduit means operatively connected between said refrigeration system and said fluid mixing means and fourth conduit means operatively connected between said fluid mixing means and a point of fluid utility. There is further provided an automatic control system for the process and apparatus.
The invention will now be described in connection with the accompanying drawing. A fuel or residue gas or other plant gas is passed by Way of conduits 1 and 2 through heater 3. The resulting heated gas can be mixed with gas resulting from regeneration of a desiccant by way of conduit 22. The gas mixture is then passed by way of conduit 4 through conduit 5 and its associated hand indicating controller and/or by Way of conduit 6 and its associated cooler 7 to conduit 8 'Which can contain therein check valve 9. The gas is then passed through mixer ill by way of conduit 11 to a separator 12. Any liquid contained in this gas stream, such as condensed Water, is removed by Way of conduit 13 and its associated liquid level controller 14. The dry gas is taken from an upper part of the separator by way of conduit 15 for further utility in the plant, such as e.g. a flare, as desired. There is depicted at 2.3 a refrigeration system. Cold liquid from this refrigeuation unit-is passed by way of conduit 24, at such times as may be desired or necessary, to mixer Ill. Valve 25 in conduit 24 can be manually operated or can be operated in response to some signal of plant shut-down. Thus, it is seen that the cold liquid in line 24 is mixed with a warm gas in his 0 at mixer fill. The resulting gas mixture in conduit ll can then be separated as previously recited. A portion of the gas in conduit 1 can by-pass heater 3 and separator 12 by way of conduit 16 and its associated control valve 17. This valve is operated in response to differential pressure obtained between lines 1 and 115. Other portions of the residue gas can be passed by way of lines l3 and 1% and their associated hand indicator controllers to conduit 2rd, Where they can be used to reactivate and regenerate the previously-mentioned desiccant. There can also be associated with conduit 2% a flow indicator. Fuel gas is indicated as being supplied by way of conduit 21 to heater 3, the fuel gas being burned therein to provide heat for the gas in conduit 2. This fuel gas conduit 2i can be provided with a flow recorder, as shown. a
in many instances, it is desired to provide automatic control for the above-described system. Flow of heated gas in conduit 2 can be controlled by control valve 26, which is actuated in response to a-flow indicator controller in conduit 2. The temperature obtained in separator 12 can conveniently be used to control one of two variables in the process. For this purpose, there is provided a temperature recorder-controller 29 which can, by a proper manipulation of valves 36) and 31, be utilized to control either flow of cold liquid from the refrigeration unit by way of conduit 24 by manipulation of valve 28 or flow of heated gas to the separation zone by manipulation of valve 27 associated with the by-pass around valve 26. As is understoodin the art, controller 29 senses a temperature prevailing in separator 12 which can be either a gas or a liquid temperature, and transmits a correcting signal to the proper control valve. There is further provided a temperature control system for heater 3, which will now be described. There is provided in conduit 21 supplying fuel gas to the heater 3 a valve 32 associated with pressure controller 33, which senses pressure in conduit 21. The index point of this pressure controller can be reset in response to signals from temperature recorder-controller 34 sensing temperature in conduit 2. Further, there is interposed in the signal line connecting pressure recorder-controller 33 and valve 32 a cut-off valve 35. This valve is actuated in response to signals from temperature alarm 35, which senses temperature in an upper portion of heater 3.
Thus, it is seen that there is provided in one preferred embodiment of the invention a control system which auto matically operates to remove quantifies of cold liquid from a refrigeration system at the time of shut-down or when otherwise desirable. The flow of fuel gas to heater 3 is controlled primarily by pressure in the fuel gas line by valve 32 and controller 33. The desired pressure can be reset in response to a temperature signal from controller 34 which senses temperature in the heater efiiuent. If the temperature of the heater goes above a predetermined point, as sensed by alarm 36, this alarm actuates valve 35 such that control valve 32 is closed.
As stated previously, the temperature controller 29 can be used to control either valve 28 or valve 27 as desired, suitable manipulation of valves 31? and 31 accomplishing this result. Controller 29 can either decrease the flow of cold liquid by manipulation of valve 28 or increase the flow of warm gas by manipulation of valve 27 as temperature in an upper portion of the separator zone decreases.
Instruments, such as level controller 14, pressure controller 33, temperature controller 34, the various hand indicator controllers, flow recorders, flow indicators, temperature alarm, and differential pressure controller, are instruments commercially available. These can be, for example, Model 40 Foxboro units as described in Foxboro Bulletin 5A10'A of November 1955.
As a. specific example, the heater inlet conduit 2 is operated at about 118 p.s.i.g. and 50 R, the heater efliuent is operated at about 112 p.s.i.g. and 606 F., and the separator vessel is operated at about llll F. and 97 p.s.i.g. The fuel gas in line 21 is natural gas. The residue gas introduced by way of line 1 (is a plant residue gas comprising essentially methane, and the regenerator outlet gas in line 22 is a wet residue gas stream resulting from regeneration of dryers by passing residue gas therethrough. The refrigerant in line 24 comprises a mixture of ethylene and propylene.
It is thus seen that there has been provided a method and apparatus for automatically handling quantities of cold liquid rei rigerant.
The normal boiling points of various liquid refrigerants are as follows: methane, 16l.5 (3.; ethylene, -103.9 C.; ethane, 88.3 C.; and propylene, -47.0 C.
Reasonable variation and modification are possible within the scope of the foregoing disclosure, drawing and the appended claims to the invention, the essence of which is that there are provided a process and apparatus for re moval of quantities of cold liquid from a refrigeration system which comprises admixing this cold liquid with a heated gas before disposal thereof.
We claim:
21. A process for rapid removal of cold liquid froma refrigeration system comprising removing said cold liquid from said system, heating a gas stream in a heat exchange zone, admixing into the resulting heated gas stream the thus-renroved cold liquid refrigerant, passing the resulting mixture to a separation zone, separating out and removing any condensed liquid therefrom, removing the remainder of said resulting mixture from said separation zone, passing said remainder to further utility, and controlling the rate of admixing in response to a temperature prevailing in said separation zone. i
2. Refrigerant liquid removal apparatus comprising a 4 refirigeration system, fluid heating means, first conduit means operatively connected between a source of gas and sm'd fluid heating means, fluid mixing means, second conduit means operatively connected between said fluid heating means and said fluid mixing means, third conduit means operatively connected between said refrigeration system and said fluid mixing means, and fourth conduit means operatively connected between said fluid mixing means and a point of fluid utility, said point of fluid utility comprising vapor-liquid separating means having fifth con duit means operatively connected to a lower portion thereof for liquid removal and sixth conduit means operatively connected between an upper portion of said separating means and a. point of vapor utility.
3. The process of claim '1 wherein the rate of flow of said resulting heated gas stream is controlled in response to the rate of flow of said gas stream.
4. The process of claim 3 wherein the rate of flow of heating fluid to said heat exchange zone is controlled in response to the pressure of said fluid.
5. The process of claim 4 wherein said rate of flow of heating fluid is further controlled in response to the temerature in said heat exchange zone.
6. The process of claim 5 wherein said rate of flow of heating fluid is further controlled in response to the temperature of said resulting heated gas stream.
7. The process of claim 1 wherein a portion of said gas stream is passed directly into admixture with said remainder.
8. The process of claim 7 wherein the rate of flow of said portion is controlled in response to the pressure differential prevailing between said gas stream and said remainder.
9. The process of claim 1 wherein the rate or flow of said resulting heated gas stream is controlled in response to both the temperature prevailing in an upper portion of said separation zone and the rate of flow of said gas" stream, a second portion of said gas stream being withdrawn for further use. 1
10. Apparatus of claim 2 further provided with means sensing temperature in an upper portion of said separating means and adapted to control the flow of fluid in said third conduit means.
11. Apparatus of claim 10 further provided with flow sensing means in said first conduit means and adapted to control the flow of fluid in said second conduit means.
12. Apparatus of claim 2 further provided with seventh conduit means operatively connected between said source of gas and said point of vapor utility, said seventh conduit means being provided with flow control means therein adapted to control the flow therethrough in response to the pressure differential obtained between said source of gas and said point of vapor utility.
13. Apparatus of claim 2 further provided with a heating fluid source, eighth conduit means nected between said heating fluid source and said fluid heating means, flow control means in said eighth conduit means normally responsive to signal generating means sensing pressure in said eighth conduit means, said signal generating means being further responsive to temperature of fluid in said second conduit means, and means sensing temperature in said fluid heating means, said means sensing temperature being adapted to disengage said signal generating means from said flow control means in said eighth conduit means upon the temperature in said fluid heating means exceeding a predetermined value.
operatively con- 14. Apparatus of claim 2 further provided with ninth conduit means operatively connected between said fluid heating means and said fluid mixing means, means in said second conduit means adapted to control flow therein in response to flow in said first conduit means, and means in said ninth conduit means adapted to control flow therein in response to temperature in an upper portion of said separating means.
15. A process for treating cold liquid comprising ethyl ene and propylene which comprises heating a residue gas stream in a heat exchange Zone, admixing into the resulting heated residue gas stream said cold liquid, passing the resulting mixture to a separation zone wherein condensed liquids are removed, removing the remainder of said resulting mixture from said separation zone, passing said remainder to a point of utility, controlling the rate of flow of said resulting heated residue gas stream in response to temperature prevailing in an upper portion of said separation zone, controlling the rate of flow of said resulting heated residue gas stream in response to the rate \of flow of said residue gas stream, controlling the rate of flow of heating fluid to said heat exchange zone in response to the pressure thereof and further in response to the temperature in said heat exchange zone and the temperature of said resulting heated residue gas, passing a portion of said residue gas stream directly into admixture wtih said remainder, and controlling the rate of said last-recited passing in response to the pressure difierential prevailing between said residue gas stream and said remainder.
References Cited in the file of this patent UNITED STATES PATENTS 485,877 Noteman Nov. 8, 1892 1,864,250 Lucas June 21, 1932 2,089,760 Paris Aug. 10, 1937 2,230,500 Harlow Feb. 11, 1941 2,242,108 Bullowa et al. May 13, 1941 2,246,875 Carney June 24, 1941 2,522,026 Evans Sept. 12, 1950 2,878,165 Oottle Mar. 17, 1959 2,960,839 Hoag Nov. 22, 1960

Claims (1)

1. A PROCESS FOR RAPID REMOVAL OF COLD LIQUID FROM A REFRIGERATION SYSTEM COMPRISING REMOVING SAID COLD LIQUID FROM SAID SYSTEM, HEATING A GAS STREAM IN A HEAT EXCHANGE ZONE, ADMIXING INTO THE RESULTING HEATED GAS STREAM THE THUS-REMOVED COLD LIQUID REFRIGERANT, PASSING THE RESULTING MIXTURE TO A SEPARATION ZONE, SEPARATING OUT AND REMOVING ANY CONDENSED LIQUID THEREFROM, REMOVING THE REMAINDER OF SAID RESULTING MIXTURE FROM SAID SEPARATION ZONE, PASSING SAID REMAINDER TO FURTHER UTILITY, AND CONTROLLING THE RATE OF ADMIXING IN RESPONSE TO A TEMPERATURE PREVAILING IN SAID SEPARATION ZONE.
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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US485877A (en) * 1892-11-08 Apparatus for making gas
US1864250A (en) * 1931-02-06 1932-06-21 Reese H Lucas Method of and means for disposing of dangerous fluids
US2089760A (en) * 1934-10-25 1937-08-10 Jr Auguste J Paris Method of treating hydrocarbon oils
US2231500A (en) * 1939-06-26 1941-02-11 Phillips Petroleum Co Transportation of oil and gas vapors in a pipe line
US2242108A (en) * 1939-05-23 1941-05-13 Jesse G M Bullowa Oxygen vaporizer
US2246875A (en) * 1939-04-03 1941-06-24 Phillips Petroleum Co Method and apparatus for loading receptacles with volatile liquids
US2522026A (en) * 1945-12-26 1950-09-12 Phillips Petroleum Co Apparatus for vaporizing liquefied gas
US2878165A (en) * 1953-11-16 1959-03-17 Phillips Petroleum Co Ammonia storage and recovery system
US2960839A (en) * 1959-09-14 1960-11-22 Phillips Petroleum Co Transforming liquid to a gas or vapor

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US485877A (en) * 1892-11-08 Apparatus for making gas
US1864250A (en) * 1931-02-06 1932-06-21 Reese H Lucas Method of and means for disposing of dangerous fluids
US2089760A (en) * 1934-10-25 1937-08-10 Jr Auguste J Paris Method of treating hydrocarbon oils
US2246875A (en) * 1939-04-03 1941-06-24 Phillips Petroleum Co Method and apparatus for loading receptacles with volatile liquids
US2242108A (en) * 1939-05-23 1941-05-13 Jesse G M Bullowa Oxygen vaporizer
US2231500A (en) * 1939-06-26 1941-02-11 Phillips Petroleum Co Transportation of oil and gas vapors in a pipe line
US2522026A (en) * 1945-12-26 1950-09-12 Phillips Petroleum Co Apparatus for vaporizing liquefied gas
US2878165A (en) * 1953-11-16 1959-03-17 Phillips Petroleum Co Ammonia storage and recovery system
US2960839A (en) * 1959-09-14 1960-11-22 Phillips Petroleum Co Transforming liquid to a gas or vapor

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