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Publication numberUS2907176 A
Publication typeGrant
Publication dateOct 6, 1959
Filing dateMar 12, 1956
Priority dateMar 12, 1956
Publication numberUS 2907176 A, US 2907176A, US-A-2907176, US2907176 A, US2907176A
InventorsKenneth Tsunoda, Kurt Kuhlmann
Original AssigneeAmerican Messer Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Apparatus for vaporizing normally gaseous material from liquefied form
US 2907176 A
Abstract  available in
Images(4)
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Claims  available in
Description  (OCR text may contain errors)

Oct. 6, 1959 K, TSUNODA EIAL 2,907,176

APPARATUS FOR VAPORIZING NORMALLY GASEOUS MATERIAL FROM LIQUEFIED FORM Filed March l2, 1956 4 Sheets-Sheet 1 Oct. 6, 1959 K. TsuNoDA ETAL 2,907,176

APPARATUS FOR vAPoRIzING NORMALLY GAsEous MATERIAL FROM LIQUEFIED FORM Filed March l2, 1956 4 Sheets-Sheet 2 7a 1 -EL 69 di m3 db 52 Oct. 6, 1959 K TSUNODA EIAL 2,907,176

APPARATUS FOR VAPORIZING NORMALLY GASEOUS MATERIAL FROM LIQUEFIED FORM Filed March 12, 1956 4 Sheets-Sheet 5 T UZI:

TLC'E- ATTO NEY Oct. 6, 1959 K, TSUNODA EVAL 2,907,176

APPARATUS FOR VAPORIZING NORMALLY GASEOUS MATERIAL FROM LIQUEFIED FORM Filed March l2. 1956 4 Sheets-Sheet 4 ATTORNEY i United States Patent O APPARATUS FOR VAPORIZING NORMALLY GAS- EOUS MATERIAL FROM LIQUEFIED FORM Kenneth Tsunoda, New York, and Kurt Kuhlmann, Flushing, N.Y., assignors to American Messer Corporation, New York, N.Y., a corporation of New York Application March 12, 1956, Serial No. 571,039 4 Claims. (Cl. 62-50) This invention relates to the vaporization of fluids which `are stored in liquid form and are adapted to be utilized in gaseous form, and in certain of its more specific aspects relates to improved heat vaporization means for converting flowing liquids into the gaseous phase.

Apparatus embodying the invention is particularly well suited to supply gaseous oxygen, nitrogen, argon, or the like, as needed from a storage tank of liquefied gas, since many of the uses of such fluid are of such nature as to be subject to sudden, widely varying, and discontinuous demands which are reflected on the ow requirements, and the present apparatus embodies a variety of features contributing to efective and rapid responsiveness to such demands.

Among the features of the invention in Various of its aspects are the provision of various automatic and semiautomatic controls, the provision of a pressurization loop to compensate for undue pressure-reduction in the storage tank, the provision of means to compensate for excessive pressure in the storage tank, and the provision of an improved type of vaporization means.

In the provision of vaporization means for a normallygaseous fluid in a liquid state, an important consideration is that the fluid passing thru the heater should always be subjected to the desired heating effect, and should be warmed or vaporized as required, in spite of sudden flow volume surges and the always-prevalent time delays of manual or automatic heater controls. Obviously, since controls and heat sources require a finite time to take effect, an instantaneously-acting heat storage must provide the initial input of heat into the fluid which passes thru the system. In accordance with the invention, this heat storage is established by means of a mass of metal from which heat can be drawn during that period which is necessary for the heater power source and its controls to take effect, satisfying the heat input for the system. The fluid to be heated, the source of heat, the heat-storing metal mass and the thermal control devices are brought into mutual thermal contact in such a manner that their interaction results in the desired effect.

The invention accordingly comprises apparatus embodying features of construction, combinations and arrangement of parts, and the relation of elements which will be exemplified in the apparatus hereinafter described, the scope of the application of which will be indicated in the claims.

For a fuller understanding of the nature and objects of the invention, reference should be had to the following detailed description taken in connection with the accompanying drawings, in which:

Figure l is a diagrammatic view illustrating one form of apparatus embodying the invention;

Fig. 2 is a perspective View of one form of vaporizer embodying the invention with a section thereof cut away to reveal the interior;

Fig. 3 is a similar View of a modified form of vaporizer;

Fig. 4 is a side view of another form of vaporizer;

Fig. 5 is a top View of the vaporizer of Fig. 4;

Fig. 6 is a diagrammatic side View showing a modified vaporizer arrangement;

Fig. 7 is a top view thereof on an enlarged scale; and

Fig. 8 is a similar view showing another form of vaporizer arrangement.

In the embodiment of the invention exemplified in Fig. 1, liquid oxygen, stored in an insulated spherical storage tank 15, is drawn from the bottom of the tank thru a flow-line conduit 16, past a shut-off valve 13 to heater vaporizer means 26 which may be one of the forms hereinafter described and in which the liquid oxygen is transformed into the gaseous phase. The gaseous oxygen is carried from the vaporizer by a ow line conduit 22, past a thermometer 23 and a shut-off valve 24 to a connection 25 for attachment to conduit means to one or more positions in which the oxygen gas is to be utilized.

In order to assure against an uneven pressure-drop in the tank due to extra heavy demands or other causes, there is provided, in accordance with the invention, a pressuriZing-loop conduit 26-26a, running from the bottom of the tank 15 to trap ...7 having a drain 28, to a heater yvaporizer means, which may be part of the heater vaporizer means 2@ as hereinafter exemplified, but which, as shown in Fig. 1, is an independent heater vaporizer means 29, and back to the upper portion of the tank 15. A shut-off Valve 30, and an adjustable but automaticallyoperating pressure-controlled valve 32 are provided in the portion of the conduit 26 beyond the vaporizer 29. The valve 32 will be set for operation at a pressure lower than that normally desired in tank 15. Thus, any drop in pressure in the tank 15 will cause the valve 32 to open permitting immediate flow thru conduit 26-26a, vaporization by vaporizer 29 and restoration of the pressure in the top of tank 15. Safety escape means are provided at 34, 35, and 35.

In order to assure against excessive pressure in tank 15, there is provided in accordance with the invention a pressure-controlled connection 26a-33 between the upper portion of the tank 15 and a point 39 in the conduit 16 beyond the valve 18, and a valve in the tank set at a pressure somewhat above that normally desired in tank 15. This connection, as exemplified, comprises the later portion 26a of conduit 26 and a bridging conduit 38, extending therefrom to conduit 16. An adjustable but automatically-operating pressurecontrolled valve 4f? is disposed in the conduit 38.

Further in accordance with the invention, there is provided in the conduit 22 an adjustable pressure-controlled valve 42 whereby the pressure at 25 may be kept as low as possible consistent with the users requirements in order to have the greatest possible leeway for taking up vaporization losses. There is also provided a temperature-controlled valve 44 to protect the users piping system from temperatures below an admissible minimum. The valve 44 is controlled by the temperature at an earlier point 4S of the conduit 22 (near the vaporizer 20), as indicated by the dotted line 46. Safety escape means are provided at 50, 52, and 54. A single vent 55 may be provided for several escape means, as 35, 36, 50, 52, and 54.

The vaporizer 29 is in the form of a finned tube 56, which is heated, for instance, by electrical heating element 57, and about which an expanded portion 58 of the conduit 26 runs.

Various forms of construction which may be utilized at 20 or otherwise utilized in accordance with the invention are illustrated in Figs. 2-7.

The embodiment shown in Fig. 2 is in the form of a vaporizer for liquid oxygen, i.e., a heating device which converts a flow of oxygen, which is in its liquid phase and therefore at very low temperatures (depending on pressure, approximately 200 F. to -300 E), into a ow of gaseous oxygen at ambient temperature. The

3 flow volume may vary at any time, and instantaneously within the entire range from Zero capacity to full capacity. A fundamenta-l requirement of such a device is that at no time should the temperature of the euent gas fall below a specified temperature.

A metal block 61 which may, for example, be about a foot in diameter and threefeet long, vis provided. As exemplified, it` isformed of high-conductivity bronze. Other metals having a high thermal conductivity, e.g., copper, copper alloys, or aluminum, may be used. The block 61 is provided on its cylindrical surface with a helical groove 62 of semi-circular cross section. A tube 63, which may connect the conduits 16 and 22 in Fig. 1, is wound around the block 61, the tube 63 resting with a close t in the groove 62 whereby the tube 63 and metal block 61 are in good thermal contact with each other.

` A number of bores 64 are provided within the block 1 and lthese bores accommodate cylindrical heating elements 65. l

O ne bore 66 is located near the grooved, cylindrical surface of the block, within which a thermostatic sensing element 67 is located at a position about midway of the length of the bore.

The inside surface of the tubing coil 63 provides the heat-exchange larea which is needed to transfer heat radially and 4axially from the heater into the fluid which is to be warmed. Lower tubing end 68 is connected with a source of liquid oxygen (e.g., conduit 16) and upper tubing end 69 leads into a reception means (e.g., conduit 22).

The heating elements 65 are connected with a source of electrical power -by electrical connectors 70 by closing a switch 71 under control of the temperature-control primary element 67.

Any type of thermo-sensing element may be installed.

as vapor tension bulbs, gas pressure bulbs, resistance thermometers, thermocouples etc., their choice being dictated mainly by the instruments with which they are to work in conjunction, but their and their instruments speed of response being a factor which iniluences the quantity of metal to be provided in the heat-storing metal blocks.

The embodiment described above relates to the warming to ambient temperature of a gas which enters at very low temperatures. The heat storage is maintained at ambient temperature which is adequate, since ambient temperature can be considered being high, relative to the temperature of liquid oxygen.

However, these operating conditions can be fully extrapolated, in principle, to a heating process which takes place at a higher temperature level, where the gas or liquid to be heated meters at near or above ambient temperature. ln that case, while the unit is dormant but ready for operation, the metal block should be maintained above ambient temperature. This condition will be automatically maintained by appropriate setting of the temperature-control primary elements which then will occasionally switch on the heating elements in order to maintain an elevated block temperature against the leak of heat into the surroundings.

In operation, assuming that the vaporizer is initially dormant, i.e., that no oxygen vapor is drawn via upper tubing end 69 and therefore no liquid oxygen enters the lower tubing end 68, and the metal block 61 and the thermostat sensing element 67 are both at ambient temperature, while the temperature-control primary element is set to keep the heating elements disconnected from the electric power circuit: oxygen vapor is now drawn from the upper tube end 69, which will at the same moment cause liquid oxygen to enter the heater tube 63 via the lower tubing end 68. Heat exchange will take place, with heat transfer from the metal block into the cold oxygen, with the result that the oxygen becomes warmed and vaporized and will exit from upper tube end 69 at a temperature only slightly below ambient. The heat which is absorbed by the fluid is drawn from the heat capacity represented in the metal mass and this heat is available readily'f and `without delay since tube walls 63 and thestorage mass 61 are of metal, which is characterized by a very large thermal conductivity coefficient. Heat-conduction in the metal block is both radial and axial.

Obviously the metal block 61 will cool down as heat is drawn from it, this cooling process beginning in the lower part where the cold gas enters and progressing upwards as the heat exchange proceeds into regions where the block 61 is still relatively warm and provides high temperature ldifferentials against the cold fluid in tube 63. Throughout this progressive cooling process the upper part of the metal block 61 will remain at or near ambient temperature and the gas will exist at almost constant temperature from upper tube end 69. At -a certain moment the cooling process will reach the metal mass in the vicinity of the thermostat sensing element 67 and cool said element to a temperature at which it is set to actuate the switching mechanism which connects the heating elcments to electric power. This heater control circuit will require a finite time until it achieves a state in which full power is fed from the electric heating'elements into the block 61. During the delay action period, the parts of the metal block which are still Warm will continue to carry the heating duty of the system. Before the heat storage in block 61 is exhausted, i.e., before the uppermost section of the block drops -appreciably in temperature, the electric heating system should come in to take over further heating duty.

On the other hand, when the ow of fluid thru the heater is stopped, or is decreased to a point Where the heat output is not absorbed in full, the average metal block temperature will rise with the result that the thermostatic sensing element will attain a temperature a which it will trigger the electric control mechanism to disconnect power from the heating elements.

Obviously, the quantity of metal mass which has to be provided in this arrangement is a function of the maximum heater capacity, the speed of response of the electric heater circuit and its thermostatc controls. Furthermore, the heat storage in the mass provides a thermal flywheel effect which will have a direct effect on the switching frequency of the electric circuit, with the result that the lange metal mass will reduce the frequency of switching and'there'ny lengthen the service life of electrical components.

Smoother control and fewer and lower electric power surges can be -achieved by connecting the multitude of heating elements in two or more groups, controlled by as many temperature-control primary elements as there are groups of heaters. The advantage is that when only partial capacity of the heater is used not all of the electrical heater elements need to be actuated, which results in fewer switching cycles and switching of lower electric power. In a design of splitting the to-tal heating capacities into two or more separate circuits, it appears advantageous to install these heating elements which cut in iirst in the lower, colder section of the metal block while the heaters, which cut in only when full capacity is approached, should be installed in the upper part of block. Such arrangement offers uniform heat transfer at high ilow capacity, but avoids overheating of the upper parts of the metal block, when operating at low capacity.

In Fig. 3 there is shown such an arrangement, a block 61a having a spiral groove 62a similar to the groove 62, and a tube 63a similar to the tube 63 and similarly arranged and connected. Heating elements 65a under control of temperature-control primary element y67a are provided in the upper part of the block, and heating elements 65b under control of temperature-control primary element 67b are provided in the lower part of the block. The temperature-control piimaryeletnet 67a is responsive to a lower temperature than the temperature-control primary element 67b.

A preferred form of vaporizer for use at 20 in Fig. 1 is shown in Figs. 4 and 5. A cylindrical high-heat-conductivity bronze block `611C is provided on its cylindrical periphery with a spiral groove 62C in which there is tightly fitted -a copper tube 63C, the inlet portion of which forms part of the ilow line 16 the major portion of which is in the form of a coil 88 and the outlet portion of which forms the initial part of the llow line 22. Two sets of heating elements are provided. One, which is composed of heating elements 65, is located somewhat nearer the periphery than the other, which is composed of heating elements 65. A temperature-control primary element 67' responsive when the temperature actuates the heating elements 65', and a temperature-control primary element '67 responsive when the temperature of the block falls below a relatively lower temperature actuates the heating elements 65". Electrical connections 80 and 81, the latter controlled by -a switch 82 under control of elements l67', lead respectively toI connector rings 87 and I84 which are connected to the heating elements 65' and electrical connections 80 and 82, the latter controlled by a switch 85 under control of element 67, lead respectively to electrical connection rings `83 and 86 which are connected to the heating elements 65.

In Figs. 6 and 7 there is shown -a form of construction utilizing two blocks in series, each having a pair of tubes therein. One tube 63d leads from a source of liquid oxygen (e.g., conduit 16) and is suitably brought into elective heat-transfer relationship with spiral groove in the upper portion of a metal block 61d as by being coiled spirally upwardly around the major portion of the periphery of a block 61d, which, as shown, is cylindrical in shape like the block 61, but which, like the block 61, may be any suitable shape. Thence the tube 63d leads to a spiral groove in the upper portion of a similar block `61e and winds upwardly around the block in the groove, and leads thence to a reception means (e,g., conduit 22).

In the bottom portions of blocks 61d and 61e, there are provided spiral grooves in which are wound portions of a tube 92 leading from another source of normally gaseous material in the liquid phase (eg, the earlier portion of conduit 26) to a reception means for the material in the gaseous phase (e.g., a later portion of conduit 26).

The blocks 61d and 61e are provided, respectively, with heating elements 65d and 65e, thermostatic elements 67d and 67e, and electrical connections 93 and 94.

In Fig. 8 there is shown an arrangement of a plurality of vaporizer units in parallel as substituted for vaporizer arrangement 20 of. Fig. 1. There are provided, in the present instance, three blocks 611, I61g, and 61h, all identical except that no temperature-control primary elements are provided in the block 61] and 61h. A tube 63f leads from conduit 16 and is coiled about block 61f and thence leads to conduit 22. A tube 63g leads from conduit 16 and is coiled about block 61g and thence leads to conduit 22, a tube 63h leads from conduit 16 and is coiled about block `61h and thence leads to conduit 22. A set of heating elements 65j are provided in block 61f, a similar set of heating elements 65g in block 61g, and a similar set of heating elements 65h in the block 61h. A temperature-control primary element 67g in block 61g controls a switch 100 in a circuit 101 extending to heating element y65h and having branch circuits 102 and 103 leading to heating elements 65f and 65g, respectively.

Since certain changes may be made in the above apparatus and diierent embodiments of the invention could be made without departing from the scope thereof, it is intended that all matter contained in the above description or shown in the accompanying drawings shall be interpreted as illustrative and not in a limiting sense.

We claim:

1. Apparatus for vaporizing from liquid form a material used in gaseous form, comprising a container for the material in liquid form, a valve-controlled iiow line from a lower point therein, product heater vaporizer means in said tlow line, a control valve in said flow line beyond said heater vaporizer means and actuated in response to the pressure in said tlow line beyond the valve to maintain a substantially constant pressure in the line beyond thevalve, and means to increase the pressure in said container When the pressure therein falls below a given point and comprising a conduit leading from a lower point in said container and back to an upper point in said container, auxiliary heater vaporizer means for vaporizing material in said conduit, and a pressure-controlled valve in the portion of said conduit leading back to said container from said auxiliary heater vaporizer means, the last-mentioned valve being arranged to be closed when there is excess pressure in said container.

2. Apparatus as set forth in claim l wherein at least the first-mentioned heater vaporizer means comprises a heat-conductive metallic block having a plurality of temperature-controlled heating elements distributed at points intermediate the center thereof and the periphery thereof to provide heat-storage capacity interiorly and exteriorly of said heating elements and between said heating elements, and a tube connecting said flow lines and in heatconductive relationship with the block exteriorly of said heating elements.

3. Apparatus for vaporizing from liquid form a material used in gaseous form, comprising a container for the material in liquid form, a valve-controlled ilow line from a lower point therein to a point of delivery of the material in gaseous form, a conduit leading from a lower point in said container and back to said container, and a heat-conductive block having temperature-actuated heating means therein, a portion of said flow line being in heat-conductive relationship with said block so that the block serves as a heater vaporizer means for the material owing in the flow line, and a portion of said conduit being also in heat-conductive relationship with said block so that the block also serves as a heater vaporizer means for the material flowing in said conduit.

4. Apparatus for supplying in gaseous form normally gaseous material stored in liquid form, comprising a container for material in liquid form, heater-vaporizer means, delivery means extending from said heater-vaporizer means, a Valve in said delivery means, a flow line leading from a lower point in said container to said heater-vaporizer means, conducting means at said heater-vaporizer means extending from said flow line to said delivery means and having an upward component so that vapor formed therein will rise therein to be carried ott by 4said delivery means, a conduit leading from an upper point in said container to said flow line, said ow line having a portion which extends above said upper point, and pressureresponsive means for permitting iiow thru said conduit while said ilow line remains open to permit gas in said upper portion of the container to escape to reduce excess pressure in said container in preference to the escape of gravity-retarded liquid when the mst-mentioned valve is opened at a time when excess pressure exists in said container.

References Cited in the le of this patent UNITED STATES PATENTS 1,162,537 Yager Nov. 30, 1915 1,838,680 Hudson Dec. 29, 1931 2,247,816 Mclllrath July 1, 1941 2,343,727 Zenner Mar. 7, 1944 2,348,546 Kercher May 9, 1944 2,464,835 Thayer et al. Mar. 22, 1949 2,515,835 Preston Iuly 18, 1950 2,576,984 Wildhack Dec. 4, 1951 2,576,985 Wildhack Dec. 4, 1951 2,673,919 Arvins et al Mar. 30, 1954 2,673,920 Donovan et al Mar. 30, 1954 2,747,374 Thompson May 29, 1956

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1162537 *Feb 2, 1915Nov 30, 1915John Joseph YagerCompressed-gas heater.
US1838680 *Jul 25, 1927Dec 29, 1931Burdick CorpHeating element
US2247816 *Jun 20, 1940Jul 1, 1941Mcilrath Roy EHeating unit
US2343727 *Apr 26, 1941Mar 7, 1944Linde Air Prod CoVaporizing device
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3229472 *May 15, 1964Jan 18, 1966Union Carbide CorpMethod and apparatus for pumping and vaporizing liquefied gas
US3446029 *Jun 28, 1967May 27, 1969Exxon Research Engineering CoMethod for heating low temperature fluids
US3727651 *Mar 17, 1971Apr 17, 1973Biever RPortable high volume gas supply system
US4255646 *Mar 3, 1978Mar 10, 1981Sam Dick Industries, Inc.Electric liquefied petroleum gas vaporizer
US4438729 *Mar 31, 1980Mar 27, 1984Halliburton CompanyFlameless nitrogen skid unit
US4458633 *May 18, 1981Jul 10, 1984Halliburton CompanyFlameless nitrogen skid unit
US5551242 *Mar 14, 1984Sep 3, 1996Halliburton CompanyFlameless nitrogen skid unit
US6311738Jun 21, 2000Nov 6, 2001Technical Gas ProductsMedical liquid oxygen storage, dispensing, and billing system and method
US6488056Aug 15, 2001Dec 3, 2002Technical Gas ProductsMedical liquid oxygen storage, dispensing, and billing system and method
WO1979000702A1 *Mar 2, 1979Sep 20, 1979Dick Ind Inc SamElectric liquefied petroleum gas vaporizer
Classifications
U.S. Classification62/50.2, 392/397
International ClassificationF17C9/02, F25J3/00, F17C9/00
Cooperative ClassificationF17C9/02
European ClassificationF17C9/02