US2075678A - Transferring combustible liquefied gases - Google Patents

Transferring combustible liquefied gases Download PDF

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US2075678A
US2075678A US5311235A US2075678A US 2075678 A US2075678 A US 2075678A US 5311235 A US5311235 A US 5311235A US 2075678 A US2075678 A US 2075678A
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container
auxiliary
gas
liquefied
containers
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Langen Walter Von
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NAAMLOOZE VENNOOTSCHOP MACHINE
NAAMLOOZE VENNOOTSCHOP MACHINERIEEN-EN APPARATENFABRIEKEN MEAF
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NAAMLOOZE VENNOOTSCHOP MACHINE
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/02Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C7/00Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02Discharging liquefied gases
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/6416With heating or cooling of the system
    • Y10T137/6552With diversion of part of fluid to heat or cool the device or its contents

Definitions

  • This invention relates :to a method of and apparatus for transferring liquefied combustible gases, particularly those having a low pressure at working temperatures, such for example as propane and butane.
  • Liquefied gases such as propane and butane
  • propane and butane are employed for a great variety of technical purposes and require frequent transferring, as, for instance, from a transporting to a stock vessel.
  • the liquefied gas is transferred from a transportation drum to a buoy or the like, using an intermediate container.
  • the liquefied gas is first passed from the transporta- 'tiondrum to be emptied into the intermediate container by means of a vacuum pump, the pipe line to the buoy or ultimate receptacle being kept closed.
  • a sufdcient quantity of liquefied gas has been accumulated in the intermediate receptacle, communication between the latter and the transportation drum is cut off and that between the intermediate container and the buoy or the like opened, and the pump is used to force the liquefied gas. from the intermediate container into the buoy or the like.
  • the object of this prior method and of the apparatus for carrying it into eifect is to enable the liquefied gas to be transferred without the necessity of vaporizing more than a small part of the transferred liquefied gas, and in fact this process provides for the recondensation of the comparatively small proportion of vapour drawn off by the vacuum pump during the operation.
  • the prior method has the advantage that it can be used where only one filling orifice is available in the buoy or like receptacle to be supplied.
  • two intermediate and interconnected containers are provided between the supply vessel and the contain- ,er, such as a buoy, to be filled, and, one of said intermediate containers is adapted to pass liquid to the container to be filled while the other intermediate container is being filled from the supply vessel, and vice versa, the two operations being effected by means of the same pump.
  • a vacuum pump is used to effect the transfer and evolves a certain quantity of vapor on the suction side of the pump. This results in heat being taken up from the surroundings. At the same time heat is liberated on the discharge side of the pump because of the recondensation of vaporized gas, and a further feature of the present 1 invention resides in the provision of heat-exchange or heat-equalizing means between the suction and discharge sides of the pump.
  • Such means may assume theform of a water tank in which the intermediate containers are immersed.
  • the invention is illustrated by way of example in the accompanying drawing which shows an apparatus for transferring the contents of a transporting vessel to another container, for example a buoy adapted to be lighted with propane gas.
  • the receiving container may be filled in a continuous manner by the apparatus illustrated, even although it is provided with one filling orifice only.
  • i designates a pump capable of compressing and forwarding gas.
  • 3 represents a transporting vessel fitted with a stop valve 2 and containing liquefied gas to be transferred to the container 4, which is provided with astop valve 5.
  • 6 and I are two additional containers disposed in a water tank 8.
  • the containers 3, 4, 6, and I are interconnected by the conduits 9, and the conduits l0 connect the containers 6, .I with the pump I.
  • the conduits 9 and I0 are fitted with the valves ll, I2, I3, l4, l5, l6, l1, l8, divided'into two' groups, viz. H to M and i5 to i8.”
  • the valves of each of these groups may be opened or closed together. Valves H and [5 are connected to the inlet of pump l 45 and valves l2 and I6 to the outlet thereof.
  • the apparatus shown in the drawing functions in the following manner:
  • the container 1 is filled with or contains a substantial amount ofa liquefied gas to be transferred to the container or buoy. 4, as in the particular instance illustrated in the drawing.
  • Valves H to l4 are opened and valves IE to l8 closed.
  • Thepump l. is actuated and the valve 2 of the vessel 3 opened. 55
  • a certain amount of residual gas or vapor is present in the container 6 from the previous working phase and this, together with a certain amount of vapor which is evolved by the suction effect 5 of the pump on the contents of container 6, is
  • valves I I to I4 are now closed and I5 to IE opened, and the pump I operated. Gas or vapor is now withdrawn from the container I in the same way that it was withdrawn from 6 in the previous case, and the liquefied gas accumulated in container 6 flows out into 4 while container 1 is being refilled with liquefied gas from the vessel 3 by suction.
  • the situation illustrated in the drawing has again been reached .-and the apparatus is ready for a fresh working cycle.
  • the operation outlined above may be repeated as often as is necessary to transfer the requisite amount of liquefied gas, e. g. propane, from the 40 transporting vessel 3 to the container or buoy 4.
  • liquefied gas e. g. propane
  • the capacity of containers 6 and I is preferably calibrated so that the amount of liquefied gas transferred to the container 4 may be readily determined.
  • vapor e. g. gaseous propane
  • the vapor is recondensed in the other container (for example, 'l) and liberates the latent heat of evaporation. If the two containers are disposed in a common water tank 8, the necessary heat exchange from container '2 to container 6, or vice versa, can readily be effected.
  • the method of transferring liquefied combustible gases, such as propane, between a supply vessel and a container to be filled with the use of first and second auxiliary containers which comprises exerting a suction on the first auxiliary container and thereby passing the gas in substantially liquefied condition from said supply vessel to said first auxiliary container while simultaneously exerting a pressure on said second auxiliary container to pass gas in substantially liquefied condition from said second auxiliary container to the container to be filled, and then exerting a pressure on said first auxiliary container and thereby passing said gas still in substantially liquefied condition from the first auxiliary container to the container to be filled, while simultaneously exerting a suction on the second auxiliary containerand thereby drawing gas in substantially liquefied condition into said second auxiliary chamber from the supply vessel.
  • liquefied combustible gases such as propane
  • the method of transferring liquefied combustible gases between a supply vessel and a container to be filled with the use of two auxiliary containers which comprises exerting a suction on the first auxiliary container to withdraw gas in gaseous state therefrom and thereby to draw gas in substantially liquefied condition from said supply vessel to the first auxiliary container, passing said withdrawn gas from said first auxiliary container to the second auxiliary container, thereby exerting pressure on said second auxiliary container and forcing liquefied gas from the second auxiliary container into the container to be filled and then exerting suction on said second container'to withdraw gas in gaseous state there from and thereby to draw gas in substantially liquefied condition from the supply vessel into the second container, passing said withdrawn gas from said second auxiliary container into the first auxiliary container, thereby exerting a pressure in said first auxiliary container to force gas in substantially liquefied condition from the first auxiliary container to the container to be filled, the alternate charging and discharging of said auxiliary containers being carried out continuously.
  • Apparatus for transferring combustible liquefied gases, such as propane, between a' supply vessel and a container to be filled comprising first and second auxiliary containers, conduit means connecting the upper pontions of said auxiliary g containers, a gas pump in said connecting conduit means, means to reverse the flow created by said pump in said conduit means, further conduits connecting each of said auxiliary containers to the supply .vessel and to the container to be 30 filled, and a cut-01f valve in each of said last conduits.
  • Apparatus for transferring combustible liquefied gases, such as propane, between a supply vessel and a container to be filled comprising 35 first and second auxiliary containers, a, conduit leading from the upper end of each of said auxiliary containers, a forked conduit having arms interconnecting said first conduits at their ends remote from the auxiliary containers, a secondary 9 conduit connection interconnecting points in the arms of said forked conduits, a gas pump in said secondary connection, a second conduit leading from the lower end of each of said auxiliary containers, a second forked conduit having arms I interconnecting said second conduits at their ends remote from the auxiliary containers, a discharge conduit leading from one of the arms of said second forked conduit to the container to be filled, and a feed conduit between the, other arm of said second forked conduit and the supply vessel, and valve means in each of the arms of I said first and second forked conduits.
  • combustible liquefied gases such as propane
  • Apparatus for transferring combustible liquefied gases, such as propane, between a supply vessel and a container to be filled comprising first and second auxiliary containers, conduit means connecting the upper portions of said auxiliary containers, a gas pump in said connecting conduit means, means to reverse the flow created by said pump in said conduit means, further conduits connecting each of said auxiliary containers to the supply vessel and to the container to be filled, and
  • valve means in said last conduits adapted to provide communication between said supply vessel and one of said'auxiliary containers only while providing communication betwe'en the container to be filled and the other auxiliary container only.
  • Apparatus for transferring combustible liquefied gases, such as propane, between a supply vessel and a container to be filled comprising first and second auxiliary containers, conduit means connecting the upper portions of said auxiliary containers, a gas pump in said connecting conduit means, means to reverse the flow created by said pump in said conduit means, further conduits connecting each of saidauxiliary containers to the supply vessel and to the container to be filled, and means for cooling the contents of said auxiliary containers.
  • cooling meabs is a water tank in which the auxiliary containers are placed.

Description

Patented Mar. 30, 1937 UNITED STATES PATENT orrlce TRANSFEERING COMBUSTIBLE LIQUEFIED GASES Utrecht, Germany Application December 5, 1935, Serial No. 53,112 In Germany September 26, 1935 Claims.
This invention relates :to a method of and apparatus for transferring liquefied combustible gases, particularly those having a low pressure at working temperatures, such for example as propane and butane.
Liquefied gases, such as propane and butane, are employed for a great variety of technical purposes and require frequent transferring, as, for instance, from a transporting to a stock vessel.
10 A method of and apparatus for transferring liquefied gases have already been proposed,
wherein the liquefied gas is transferred from a transportation drum to a buoy or the like, using an intermediate container. In this instance the liquefied gas is first passed from the transporta- 'tiondrum to be emptied into the intermediate container by means of a vacuum pump, the pipe line to the buoy or ultimate receptacle being kept closed. When a sufdcient quantity of liquefied gas has been accumulated in the intermediate receptacle, communication between the latter and the transportation drum is cut off and that between the intermediate container and the buoy or the like opened, and the pump is used to force the liquefied gas. from the intermediate container into the buoy or the like.
The object of this prior method and of the apparatus for carrying it into eifect is to enable the liquefied gas to be transferred without the necessity of vaporizing more than a small part of the transferred liquefied gas, and in fact this process provides for the recondensation of the comparatively small proportion of vapour drawn off by the vacuum pump during the operation.
Moreover the prior method has the advantage that it can be used where only one filling orifice is available in the buoy or like receptacle to be supplied.
It is an object of-the present invention to achieve all the advantages presented by this proposal, and at the same time to provide a method of transferring liquefied combustible gases, which is continuous and in which there is no interruption of the flow of liquefied gas to thebuoy or like ultimate receptacle, while an intermediate 1 container is being filled.
It is a further object of the invention to avoid the use of a'liquid pump for the transfer operation, so as to eliminate risk of interruption of the fiow of liquefied gas on the suction side of the pump due to rapid evaporation of the liquefied gas on account of the vacuum produced.
According to the present invention two intermediate and interconnected containers are provided between the supply vessel and the contain- ,er, such as a buoy, to be filled, and, one of said intermediate containers is adapted to pass liquid to the container to be filled while the other intermediate container is being filled from the supply vessel, and vice versa, the two operations being effected by means of the same pump.
- A vacuum pump is used to effect the transfer and evolves a certain quantity of vapor on the suction side of the pump. This results in heat being taken up from the surroundings. At the same time heat is liberated on the discharge side of the pump because of the recondensation of vaporized gas, and a further feature of the present 1 invention resides in the provision of heat-exchange or heat-equalizing means between the suction and discharge sides of the pump. Ad-
vantageously such means may assume theform of a water tank in which the intermediate containers are immersed. The invention is illustrated by way of example in the accompanying drawing which shows an apparatus for transferring the contents of a transporting vessel to another container, for example a buoy adapted to be lighted with propane gas. The receiving container may be filled in a continuous manner by the apparatus illustrated, even although it is provided with one filling orifice only.
- Referring to the drawing, i designates a pump capable of compressing and forwarding gas. 3 represents a transporting vessel fitted with a stop valve 2 and containing liquefied gas to be transferred to the container 4, which is provided with astop valve 5. 6 and I are two additional containers disposed in a water tank 8. The containers 3, 4, 6, and I are interconnected by the conduits 9, and the conduits l0 connect the containers 6, .I with the pump I. The conduits 9 and I0 are fitted with the valves ll, I2, I3, l4, l5, l6, l1, l8, divided'into two' groups, viz. H to M and i5 to i8." The valves of each of these groups may be opened or closed together. Valves H and [5 are connected to the inlet of pump l 45 and valves l2 and I6 to the outlet thereof.
The apparatus shown in the drawing functions in the following manner:
It will be first assumed thatthe container 1 is filled with or contains a substantial amount ofa liquefied gas to be transferred to the container or buoy. 4, as in the particular instance illustrated in the drawing. Valves H to l4 are opened and valves IE to l8 closed. Thepump l. is actuated and the valve 2 of the vessel 3 opened. 55
A certain amount of residual gas or vapor is present in the container 6 from the previous working phase and this, together with a certain amount of vapor which is evolved by the suction effect 5 of the pump on the contents of container 6, is
drawn out of the container 6 by the pump and forced into the container 1. Pressure is thereby gradually built up in the latter until it is in excess of that obtaining in the container or buoy 4, 10 whereupon liquefied gas flows from the container I through the open valve I4 into the container 4. Simultaneously with this building up of pres sure in I however, the withdrawal of the gas or vapor from container 6 by the pump has the efiect of reducing the pressure in this container, so that eventually liquefied gas flows from the vessel 3, through valves Zand I3 into the container 6 as a result of the difference of pressure between container 6 and vessel 3. The operation of pump I is preferably discontinued when container 1 is empty or practically empty of liquefied gas, in which event it will be found that container 6 is full or nearly full of fresh liquid from 3.
The valves I I to I4 are now closed and I5 to IE opened, and the pump I operated. Gas or vapor is now withdrawn from the container I in the same way that it was withdrawn from 6 in the previous case, and the liquefied gas accumulated in container 6 flows out into 4 while container 1 is being refilled with liquefied gas from the vessel 3 by suction. When all or most of the liquid has been discharged from 6 into the container or buoy 4 and the container 1 correspondingly filled, the situation illustrated in the drawing has again been reached .-and the apparatus is ready for a fresh working cycle.
The operation outlined above may be repeated as often as is necessary to transfer the requisite amount of liquefied gas, e. g. propane, from the 40 transporting vessel 3 to the container or buoy 4.
The capacity of containers 6 and I is preferably calibrated so that the amount of liquefied gas transferred to the container 4 may be readily determined.
When liquefied gas is drawn ofi (for example into container 6), vapor, e. g. gaseous propane, is evolved and heat accordingly taken up from the surroundings. On the other hand, the vapor is recondensed in the other container (for example, 'l) and liberates the latent heat of evaporation. If the two containers are disposed in a common water tank 8, the necessary heat exchange from container '2 to container 6, or vice versa, can readily be effected.
I claim:
1. The method of transferring liquefied combustible gases, such as propane, between a supply vessel and a container to be filled with the use of first and second auxiliary containers, which comprises exerting a suction on the first auxiliary container and thereby passing the gas in substantially liquefied condition from said supply vessel to said first auxiliary container while simultaneously exerting a pressure on said second auxiliary container to pass gas in substantially liquefied condition from said second auxiliary container to the container to be filled, and then exerting a pressure on said first auxiliary container and thereby passing said gas still in substantially liquefied condition from the first auxiliary container to the container to be filled, while simultaneously exerting a suction on the second auxiliary containerand thereby drawing gas in substantially liquefied condition into said second auxiliary chamber from the supply vessel.
2. The method of transferring liquefied combustible gases between a supply vessel and a container to be filled with the use of two auxiliary containers, which comprises exerting a suction on the first auxiliary container to withdraw gas in gaseous state therefrom and thereby to draw gas in substantially liquefied condition from said supply vessel to the first auxiliary container, passing said withdrawn gas from said first auxiliary container to the second auxiliary container, thereby exerting pressure on said second auxiliary container and forcing liquefied gas from the second auxiliary container into the container to be filled and then exerting suction on said second container'to withdraw gas in gaseous state there from and thereby to draw gas in substantially liquefied condition from the supply vessel into the second container, passing said withdrawn gas from said second auxiliary container into the first auxiliary container, thereby exerting a pressure in said first auxiliary container to force gas in substantially liquefied condition from the first auxiliary container to the container to be filled, the alternate charging and discharging of said auxiliary containers being carried out continuously.
3. The method of transferring liquefied combustible gases between a supply vessel and a container to be filled with the use of two auxiliary containers, which comprises exerting a suction 0n the first auxiliary container to withdraw gas in gaseous state therefrom and thereby to draw gas in substantially liquefied condition from said supply vessel to the first auxiliary container, passing said withdrawn gas from said first auxiliary container to the second auxiliarycontainer, thereby exerting pressure on said second auxiliary container and forcing liquefied gas from the second auxiliary container into the container to be filled together with gas in substantially liquefied condition drawn from said first into said second auxiliary container under the suction efiect of the gas in the gaseous state passing from the first to the second auxiliary chamber, and then exerting suction on said second container to withdraw gas in gaseous state therefrom and thereby to draw gas in substantially liquefied condition from the supply vessel into the second container, passing said withdrawn gas from said second auxiliary container into the first auxiliary container, thereby exerting a pressure in said first auxiliary container to force gas in substantially liquefied condition from the first auxiliary container to the container to be filled, the alternate charging and discharging of said auxiliary containers being carried out. continuously.
4. The method of transferring liquefied combustible gases between a supply vessel and a container to be filled with the use of two auxiliary containers, which comprises exerting a suction on the first auxiliary container to withdraw gas in gaseous state therefrom and thereby to draw gas in substantially liquefied condition from said supply vessel to the first auxiliary container, passing said withdrawn gas from said first auxiliary container to the second auxiliary container into the container to be filled, and then exerting suction on said second container to withdraw gas in gaseous state therefrom and thereby to draw gas in substantially liquefied condition from the supply vessel into the second container, passing said withdrawn gas from said second auxiliary container into the first auxiliary container, thereby exerting a pressure in said first auxiliary container to force gas in substantially liquefied condition from the first auxiliary container to the container to be filled, the alternate charging and discharging of said auxiliary containers being by said pump in said conduit means, and further conduits connecting eachof said auxiliary containers to the supply vessel and to the container to be filled.
20 6. Apparatus for transferring combustible liquefied gases, such as propane, between a' supply vessel and a container to be filled, comprising first and second auxiliary containers, conduit means connecting the upper pontions of said auxiliary g containers, a gas pump in said connecting conduit means, means to reverse the flow created by said pump in said conduit means, further conduits connecting each of said auxiliary containers to the supply .vessel and to the container to be 30 filled, and a cut-01f valve in each of said last conduits.
'7. Apparatus for transferring combustible liquefied gases, such as propane, between a supply vessel and a container to be filled, comprising 35 first and second auxiliary containers, a, conduit leading from the upper end of each of said auxiliary containers, a forked conduit having arms interconnecting said first conduits at their ends remote from the auxiliary containers, a secondary 9 conduit connection interconnecting points in the arms of said forked conduits, a gas pump in said secondary connection, a second conduit leading from the lower end of each of said auxiliary containers, a second forked conduit having arms I interconnecting said second conduits at their ends remote from the auxiliary containers, a discharge conduit leading from one of the arms of said second forked conduit to the container to be filled, and a feed conduit between the, other arm of said second forked conduit and the supply vessel, and valve means in each of the arms of I said first and second forked conduits.
8. Apparatus for transferring combustible liquefied gases, such as propane, between a supply vessel and a container to be filled, comprising first and second auxiliary containers, conduit means connecting the upper portions of said auxiliary containers, a gas pump in said connecting conduit means, means to reverse the flow created by said pump in said conduit means, further conduits connecting each of said auxiliary containers to the supply vessel and to the container to be filled, and
valve means in said last conduits adapted to provide communication between said supply vessel and one of said'auxiliary containers only while providing communication betwe'en the container to be filled and the other auxiliary container only.
9. Apparatus for transferring combustible liquefied gases, such as propane, between a supply vessel and a container to be filled, comprising first and second auxiliary containers, conduit means connecting the upper portions of said auxiliary containers, a gas pump in said connecting conduit means, means to reverse the flow created by said pump in said conduit means, further conduits connecting each of saidauxiliary containers to the supply vessel and to the container to be filled, and means for cooling the contents of said auxiliary containers.
10. Apparatus according to claim 9- wherein the cooling meabs is a water tank in which the auxiliary containers are placed. I
WALTER you mean.
US5311235 1935-09-26 1935-12-05 Transferring combustible liquefied gases Expired - Lifetime US2075678A (en)

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DEN38657D DE641997C (en) 1933-03-29 1935-09-26 Process for transferring liquefied, flammable gases

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2469434A (en) * 1943-02-01 1949-05-10 Linde Air Prod Co Apparatus and method for filling gas storage cylinders
US2536299A (en) * 1945-04-23 1951-01-02 Jessie F Smith Pressure filling system
US2788637A (en) * 1952-12-04 1957-04-16 Phillips Petroleum Co Underground storage systems and improved method of operating
US3155049A (en) * 1961-10-16 1964-11-03 Union Tank Car Co Duplex liquid handling apparatus having improved electrode-type control system
US3353711A (en) * 1964-01-31 1967-11-21 Cie Generale D Automatisme Soc Device for the mixing of liquids
US3864062A (en) * 1972-04-18 1975-02-04 Erap System for storing a flowable mass
US3864060A (en) * 1973-02-21 1975-02-04 Nasa Automatic liquid inventory collecting and dispensing unit
US10940402B2 (en) * 2016-09-30 2021-03-09 Cytiva Sweden Ab Method and system for transferring separation resin
US11291929B2 (en) 2017-01-31 2022-04-05 Cytiva Sweden Ab Method and system for transferring separation resin

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE550940A (en) * 1955-09-16
DE19839233A1 (en) * 1998-08-28 2000-03-02 Linde Ag Installation for compression of fluidized gas involves compressor with cylinder and piston, storage tank for fluidized gas and evaporator, piston moving in cylinder at speed between 1 and 250 mm/s.

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2469434A (en) * 1943-02-01 1949-05-10 Linde Air Prod Co Apparatus and method for filling gas storage cylinders
US2536299A (en) * 1945-04-23 1951-01-02 Jessie F Smith Pressure filling system
US2788637A (en) * 1952-12-04 1957-04-16 Phillips Petroleum Co Underground storage systems and improved method of operating
US3155049A (en) * 1961-10-16 1964-11-03 Union Tank Car Co Duplex liquid handling apparatus having improved electrode-type control system
US3353711A (en) * 1964-01-31 1967-11-21 Cie Generale D Automatisme Soc Device for the mixing of liquids
DE1288328B (en) * 1964-01-31 1969-01-30 Cie Generale D Automatisme Oct Device for the continuous proportional addition of small amounts of a liquid aggressive additive to a main amount of liquid
US3864062A (en) * 1972-04-18 1975-02-04 Erap System for storing a flowable mass
US3864060A (en) * 1973-02-21 1975-02-04 Nasa Automatic liquid inventory collecting and dispensing unit
US10940402B2 (en) * 2016-09-30 2021-03-09 Cytiva Sweden Ab Method and system for transferring separation resin
US11291929B2 (en) 2017-01-31 2022-04-05 Cytiva Sweden Ab Method and system for transferring separation resin

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DE629833C (en) 1936-05-14
DE641997C (en) 1937-02-19
NL44193C (en) 1938-10-15
FR769392A (en) 1934-08-23
GB446242A (en) 1936-04-27
FR46730E (en) 1936-08-10

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