US3577880A - Means for varying the physical conditions of a gas - Google Patents

Means for varying the physical conditions of a gas Download PDF

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Publication number
US3577880A
US3577880A US793673*A US3577880DA US3577880A US 3577880 A US3577880 A US 3577880A US 3577880D A US3577880D A US 3577880DA US 3577880 A US3577880 A US 3577880A
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United States
Prior art keywords
compartment
gas
liquid
expansion
compression
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Expired - Lifetime
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US793673*A
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English (en)
Inventor
George W D Leslie
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Anglo American Corp of South Africa Ltd
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Anglo American Corp of South Africa Ltd
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
    • B01D5/0012—Vertical tubes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/28—Evaporating with vapour compression
    • B01D1/2887—The compressor is integrated in the evaporation apparatus
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/06—Flash distillation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0033—Other features
    • B01D5/0039—Recuperation of heat, e.g. use of heat pump(s), compression
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/043—Details
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination

Definitions

  • This invention relates to a method and apparatus for varying the physical condition or state of a gas.
  • the basic physical conditions envisaged are temperature, and moisture content of the gas.
  • a method of changing the condition of a gas by means of a'compression compartment and an expansion compartment having a valve controlled inlet and a valve controlled outlet, and each compartment embodying a liquid piston comprising operating said pistons to reciprocate in unison but in opposite directions to draw gas into the one compartment at one pressure, thereafter to change the gas pressure in the same compartment and convey it at said changed pressure to the other compartment and then to restore the gas to approximately its original pressure in the latter compartment and discharge it therefrom, said gas being subjected to a heat exchange operation during its passage from the inlet of the one compartment to the outlet of the other compartment.
  • apparatus for changing the condition of a gas comprising a compression and expansion compartment interconnected at the lower ends thereof, liquid in said compartments forming a liquid piston in each, an inlet and an outlet valve connected to each compartment, a connection between the outlet valve of the one compartment and the inlet valve of the other? compartment, means for oscillating the liquid in said compartments, and an additional liquid level responsive outlet valve communicating with each compartment.
  • FIG. 1 shows the apparatus with various possible attachments
  • FIG. 2 shows the apparatus in the basic form used to carry out gas heating and dehumidification
  • FIG. 3 shows the apparatus in the basic form used to carry out gas cooling
  • FIG. 4 shows a modification in the shape of the basic apparatus.
  • the apparatus may comprise a U-tube partly filled with liquid 1.
  • Barrier floats 2, 3, are supported on the liquid, one in each of the an'ns 4,5, each of which forms a separate compartment.
  • the arms 4,5 are connected to a high pressure vessel 6 via valves 7,8, and to a low pressure vessel 9 by valves 10,11.
  • the liquid is caused to oscillate in the tube by means hereinafter described, and the valves are operated generally in accordance with the pressure conditions prevailing in the apparatus.
  • air may be drawn in through connection 12 and vessel 6 and into leg 4 which forms the expansion chamber of the apparatus.
  • the air may then be expanded in leg 4, discharged at low pressure into leg via vessel 9 and compressed to approximately its original pressure in leg 5, which forms the compression chamber of the apparatus.
  • the air at approximately its original pressure may then be discharged from leg 5 back into vessel 6.
  • the gas may be drawn into leg 5 via connection 13 and vessel 9, compressed in leg 5, discharged at highpressure into leg 4 via vessel 6, expanded in leg 4 and recirculated to vessel 9 at approximately its original pressure.
  • Inlet valve 11 and outlet valve 8 are of a simple clack valve type operated by a pressure difi'erential on opposite sides thereof, these valves being lightly spring loaded to close.
  • Valve 7 cannot be operated by an ordinary pressure differential since it is basically required to limit the amount of gas drawn into leg 4 and close before the bottom limit of the downward movement of float 3 so as to ensure expansion of gas in leg 4.
  • valve 7 Since the air drawn into leg 4 will always be at high pressure relative to that in vessel 9 it has been found convenient to make the operation of valve 7 dependent on the pressure in leg 5 into which vessel 9 discharges.
  • valve 7 is fitted with an air cylinder 14 connected to leg 4 and acting to open valve 7 against the loading of a spring 15 when the pressure in leg 4 is below a predetermined value.
  • the air cylinder 14 can no longer hold valve 7 open against its spring loading and it will accordingly close.
  • Valve 10 opens due to the pressure differential when the pressure in leg 4 is less than that in vessel 9 and is positively closed near the top of the stroke of float 3. This may be done in any convenient manner such as the incorporation of a magnet 16 in float 3 which actuates a short term delay switch 17 connected to operate the valve closing solenoid 18.
  • valves 7 and 8 open upwardly they cannot remain closed against the pressure of the compressed gas and accordingly two additional upwardly closing valves 19 and 20 are used. These are made liquid level responsive for example by the use of magnets 21, short term delay switches 22 and solenoids 23 operating in a manner similar to that described in relation to valve 10.
  • the apparatus may be used in conjunction with a heat exchange operation for heating or cooling air or other gas.
  • FIG. 2 illustrating a method of carrying out a heating process, and in which the single intermediate low pressure chamber 9 is used.
  • the air is drawn via valve 7 into leg 4 in a moist or humid condition but before the liquid in leg 4 has reached the bottom of its travel valve 7 is closed. Since at this stage of the cycle valve 10 is also closed the air expands in leg 4 resulting in condensation of part of the liquid in leg 4, the latent heat of condensation being transferred to the gas so that the enthalpy or total heat content of the gas itself is increased as opposed to the enthalpy of the gas vapor system.
  • the low pressure gas is now transferred to vessel 9 at subatmospheric temperature and pressure via valve 10 where if desired it may be subjected to a heat exchange operation using a heat exchanger 24.
  • a heat exchanger 24 During the upward movement of the liquid in leg 4 there is a corresponding downward movement of the liquid in leg 5, which, via open valve 11, is utilized to draw into leg 5, at subatmospheric temperature and pressure, air which had been transferred to vessel 9 in a previous cycle.
  • valves 8 and 11 are closed and the low temperature low pressure air compressed to atmospheric pressure and discharged for use through valve 8. It will be seen that since the enthalpy of the gas discharged has been increased by the latent heat of condensation of its original liquid content, even without the use of a heat exchanger 24 it may be discharged dryer and at appreciably higher temperature than the air drawn into leg 4.
  • the apparatus may be used as an evaporator, for example for desalination of brine and in general for any like operation in which it is desired to separate a liquid component of a mixture, solution or suspension.
  • Various cycles may be used based on compression of a gas to heat it, spraying liquid containing other components into the hot compressed gas during compression, to vaporise part of the liquid content, and subsequent sufficient expansion of the hot moist compressed gas to effect condensation of the liquid content.
  • leg 5 air may be compressed in leg 5 with brine injected through spray 26 into leg 5 during compression.
  • the moist compressed air may then be transferred via vessel 6 to leg 4 where it is expanded and the water condensed.
  • the liquid 1 forming the liquid piston will normally be brine so that admixture of the concentrated brine with it in leg 5 will not matter provided the volume of the liquid piston is maintained constant. Since increase in volume of the liquid piston will result in increase in maximum pressure in leg 5, surplus liquid may be automatically discharged through a suitable relief valve 27, which may be used in all applications of the invention in which the volume of the liquid piston lends to build up.
  • the water condensed in leg 4 must necessarily be kept separated from the liquid piston and separately drawn off.
  • the float 3 cannot usefully be used solely as a barrier to separate the liquid 1 from the liquid condensed in leg 4 since the necessary frictional engagement of float 3 with leg 4 would materially reduce the efficiency of the apparatus. For this reason other suitable means such as, for example, the collapsible skirt 28 connecting float 3 to leg 4 may be used, the condensed liquid being drawn off through flexible tube 29.
  • low pressure chamber 9 shown in FIG. 1 may be in the form of a receptacle for the crops and also housing high pressure chamber 6, which latter is made in the form of a heat exchanger.
  • Warm moist air is drawn into leg 5, compressed therein and transferred in a hot compressed condition to chamber 6 whence it is withdrawn via leg 4 and expanded with loss of moisture to approximately atmospheric pressure and lower temperature, since chamber 6 is in the form of a heat exchanger. It is then, in a saturated condition at this stage, circulated at approximately atmospheric pressure in a progressive sequence around chamber 6 and throughthe crops in chamber 9 and back to leg 5 or discharged to atmosphere. Since there is progressive exchange of heat from chamber 6 to the low temperature air it is heated and so is able progressively to absorb moisture from the crops.
  • Movement of the liquid 1 forming pistons in legs 4 and 5 is basically effected by the pressure difference in legs 4 and 5. While the liquid pistons have very low frictional losses energy must be supplied to the system to compensate for the total energy losses. This may be done by the use of the vacuum pump 30 shown in FIG. 2 or the compressor 31 shown in FIG. 3. In the crop drying application referred to above, steam injected into the chamber 6 near valve 8 may be used to introduce energy into the system. The energy may also be introduced by bodily movement of the U-tube using a crank 32 to effect a sideways rocking movement as shown in FIG. 2, or crank 33 to effect a vertical reciprocatory movement as shown in FIG. 3, in both cases the crank movements being in registration with the movements of the liquid 1. The input energy can also be applied by other means.
  • the apparatus may be in the form of units connected in series or parallel. Units may also be interconnected, for example by compressing in leg 5 of one apparatus and expanding in a leg 4 of another apparatus.
  • a method of changing the condition of a gas by means of a compression compartment and an expansion compartment each having a valve controlled inlet and a valve controlled outlet, and each compartment embodying in a liquid piston comprising operating said pistons to reciprocate in unison but in opposite directions to draw gas into the one compartment at one pressure, thereafter to change the gas pressure in the same compartment and convey it at said changed pressure to the other compartment, and then to restore the gas to approximately its original pressure in the latter compartment and discharge it therefrom, said gas being subjected to a heat exchange operation during its passage from the inlet of the one compartment to the outlet of the other compartment.
  • a method as claimed in claim 1 in which the gas is introduced into the compression compartment in a moist condition, and then in sequence compressed in the compression compartment, cooled sufficiently during the heat exchange operation to effect condensation of part of the liquid content thereof, further cooled by expansion in the expansion compartment, and utilized after expansion in conjunction with the heat exchanger to effect a drying operation by absorption in said gas of further liquid.
  • a method as claimed in claim 1 in which the gas is introduced into the compression compartment in a warm moist condition, compressed in the compression compartment while being subjected to the action of water sprays during such compression, and thereafter in sequence cooled sufficiently during the heat exchange operation to effect condensation of part of the liquid content thereof, further cooled by expansion in the expansion compartment, and utilized after expansion in conjunction with the heat exchanger to efiect a drying operation by absorption in said gas of further liquid.
  • a method as claimed in claim 1 in which gas is compressed in the compression compartment, liquid containing other components is sprayed into the gas during said compression to effect evaporation of part of said liquid, and the gas and vapor are then transferred to the expansion compartment to effect condensation of the vapor.
  • a method as claimed in claim 1 in which the gas is drawn into the first at atmospheric temperature and pressure, expanded in this compartment and subjected to a heat transfer process while in the expanded condition to increase the enthalpy of said gas, the gas then being transferred while in the expanded condition to the second compartment, compressed in the second compartment to super atmospheric temperature and thereafter discharged at said super atmospheric temperature.
  • Apparatus for changing the condition of a gas comprising a compression compartment, an expansion compartment, means interconnecting the lower ends of said compression and expansion compartments,'liquid in said compartments and in said means interconnecting the lower ends thereof and forming a liquid piston in each compartment, means establishing fluid communication between said compartments, an inlet valve and an outlet valve in each compartment for interrupting fluid communication therebetween, a liquid level responsive valve in each compartment and adapted to close when the liquid in said compartment reaches a predetermined level, means for oscillating the liquid in said compartments, and means for controlling operation of said valves in conjunction with oscillation of said liquid to effect compression of gas in one compartment, transfer of the gas between saidcompartments, and expansion of the gas in the other compartment.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Drying Of Gases (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Drying Of Solid Materials (AREA)
US793673*A 1968-02-02 1969-01-24 Means for varying the physical conditions of a gas Expired - Lifetime US3577880A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
ZA686058 1968-02-02

Publications (1)

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US3577880A true US3577880A (en) 1971-05-11

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US (1) US3577880A (fr)
AT (1) AT319904B (fr)
BE (1) BE727730A (fr)
DE (1) DE1905191A1 (fr)
FR (1) FR2001243A1 (fr)
GB (1) GB1199554A (fr)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4403478A (en) * 1982-03-26 1983-09-13 The United States Of America As Represented By The Secretary Of The Navy Expander stroke delay mechanism for split stirling cryogenic cooler
US4418547A (en) * 1980-12-08 1983-12-06 The Saint E. Company, Inc. Thermally powered heat transfer systems
US4450690A (en) * 1983-01-10 1984-05-29 Clark Jr Robert W Thermally powered, gravitationally assisted heat transfer systems
WO1984003139A1 (fr) * 1983-02-14 1984-08-16 Gen Pneumatics Corp Appareil de refroidissement cryogenique a cycle ferme
US4566291A (en) * 1983-02-14 1986-01-28 General Pneumatics Corporation Closed cycle cryogenic cooling apparatus
WO2010130356A1 (fr) * 2009-05-12 2010-11-18 Linde Aktiengesellschaft Compresseur comprenant un faux piston

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR3107127B1 (fr) 2020-02-07 2023-03-24 Commissariat Energie Atomique Procédé et dispositif de conception d’un circuit mémoire calculatoire
FR3113332B1 (fr) 2020-08-04 2022-08-26 Commissariat Energie Atomique Module mémoire reconfigurable adapté à mettre en oeuvre des opérations de calcul

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1152394A (en) * 1912-01-31 1915-09-07 Humphrey Gas Pump Company Utilizing heat energy.
US1254693A (en) * 1917-06-19 1918-01-29 Humphrey Gas Pump Company Method of compressing an elastic fluid.
US1257607A (en) * 1908-07-17 1918-02-26 Humphrey Gas Pump Company Method of compressing air or gases.
US1258407A (en) * 1916-09-16 1918-03-05 Stirling B Hill Air-compressor.
US1469729A (en) * 1923-10-02 myers

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1469729A (en) * 1923-10-02 myers
US1257607A (en) * 1908-07-17 1918-02-26 Humphrey Gas Pump Company Method of compressing air or gases.
US1152394A (en) * 1912-01-31 1915-09-07 Humphrey Gas Pump Company Utilizing heat energy.
US1258407A (en) * 1916-09-16 1918-03-05 Stirling B Hill Air-compressor.
US1254693A (en) * 1917-06-19 1918-01-29 Humphrey Gas Pump Company Method of compressing an elastic fluid.

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4418547A (en) * 1980-12-08 1983-12-06 The Saint E. Company, Inc. Thermally powered heat transfer systems
US4403478A (en) * 1982-03-26 1983-09-13 The United States Of America As Represented By The Secretary Of The Navy Expander stroke delay mechanism for split stirling cryogenic cooler
US4450690A (en) * 1983-01-10 1984-05-29 Clark Jr Robert W Thermally powered, gravitationally assisted heat transfer systems
WO1984003139A1 (fr) * 1983-02-14 1984-08-16 Gen Pneumatics Corp Appareil de refroidissement cryogenique a cycle ferme
US4566291A (en) * 1983-02-14 1986-01-28 General Pneumatics Corporation Closed cycle cryogenic cooling apparatus
WO2010130356A1 (fr) * 2009-05-12 2010-11-18 Linde Aktiengesellschaft Compresseur comprenant un faux piston

Also Published As

Publication number Publication date
AT319904B (de) 1975-01-10
FR2001243A1 (fr) 1969-09-26
DE1905191A1 (de) 1969-08-28
GB1199554A (en) 1970-07-22
BE727730A (fr) 1969-07-01

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