EP0057928B1 - Atmospheric vaporizer - Google Patents
Atmospheric vaporizer Download PDFInfo
- Publication number
- EP0057928B1 EP0057928B1 EP19820100879 EP82100879A EP0057928B1 EP 0057928 B1 EP0057928 B1 EP 0057928B1 EP 19820100879 EP19820100879 EP 19820100879 EP 82100879 A EP82100879 A EP 82100879A EP 0057928 B1 EP0057928 B1 EP 0057928B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- passes
- fins
- pass
- length
- tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/14—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
-
- 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
- F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
- F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
-
- 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0138—Shape tubular
-
- 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
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
-
- 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
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0388—Localisation of heat exchange separate
- F17C2227/0393—Localisation of heat exchange separate using a vaporiser
-
- 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
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/0636—Flow or movement of content
Definitions
- the fin thickness is from 0.16 to 0.32 cm; a convenient thickness is 0.25 cm.
- the number of fins can range from 3 to 8 fins per pass.
- Figure 1 illustrates a four-fin arrangement. The fins are spaced substantially equidistant around the center tube.
- the fins 22 are arranged around the center tube 21 at about 90° from each other.
- the fins 32 are arranged around the center tube 31 at about 45° from each other.
- the fins 42 are arranged around the center tube 41 at about 120° from each other.
Abstract
Description
- This invention relates to an atmospheric vaporizer suitable for vaporizing cryogenic liquids on a substantially continuous basis at greatly improved operating efficiency.
- Atmospheric gases such as oxygen, nitrogen and argon find wide use in a variety of applications. These gases are typically produced by means of air separation plants. Users of large quantities of such gases may have air separation units at the site of gas usage, while users of small quantities of such gases generally find it convenient to purchase their requirements in cylinders. Users of intermediate or moderate amounts of such gases generally do not have sufficient usage to justify an on-site air separation plant, but generally their requirements are large enough to make purchasing of gas in cylinders uneconomical. Typically, moderate users of gases will find it convenient to maintain on-site cryogenic liquid storage tanks and vaporize the liquid as requirements dictate. The gas is then piped to the use locations. The usage requirements may be intermittent or continuous.
- An atmospheric vaporizer is a device which vaporizes cryogenic liquids by employing heat absorbed from the ambient air. Atmospheric vaporizers have been employed by users of intermediate quantities of gases as means of vaporizing the stored cryogenic liquid when the user's gas requirements are intermittent, but generally not when the user's gas requirements are continuous. The reason why atmospheric vaporizers are not generally used for continuous service is because ice and frost build up on the outside surfaces of the atmospheric vaporizer, rendering the unit inefficient after a sustained period of use.
- Typically (FR-A-1 239 402 and US-A-2322341), an atmospheric vaporizer is comprised of one or more passes vertically positioned and piped together. The passes are comprised of a center tube through which the liquid passes, and the tube generally has one or more fins attached to it to increase the heat transfer area. The passes e.g. may be spaced about 23.5 cm, centerline to centerline, from each other. The cryogenic liquid enters at the bottom of one pass, passes up through it and then through a connection to the top of another pass through which it descends. This flow pattern is repeated through other passes as conditions such as usage and ambient temperature dictate. As the cryogenic liquid passes through the atmospheric vaporizer, the liquid is vaporized and the gas then further heated by heat transferred from the ambient air to the fluid through the vaporizer. The gas exits the atmospheric vaporizer at the required flow rate and exit temperature.
- Furthermore JP-Y-73 032 064 discloses an apparatus for continuously vaporizing a cryogenic liquid by employing heat absorbed from the ambient air comprising at least three vertically positioned passes which are piped together, each pass being comprised of a center tube provided with 8 fins substantially equally spaced around said tube, each fin having a radial length of about 1.5 times the outside diameter of said tube and extending longitudinally along substantially the entire length of said tube, wherein the ratio of the distance between adjacent fin tips to radial fin length is about 1.2.
- As the fluid passes through the vaporizer and as heat is exchanged from the ambient air, the moisture in the air condenses and freezes on the surfaces of the vaporizer. This frost and ice continues to build up during operation of the vaporizer resulting in decreasing efficiency until a steady state condition is attained. As the efficiency of the atmospheric vaporizer decreases, either the exit flow rate or the exit temperature or both must be decreased. Depending on the relative importance of these parameters, one or both of them are decreased until the steady state condition is achieved. Typically, this steady state condition is achieved at about 20 percent of the capacity of the vaporizer without the frost buildup.
- When the user's requirements are intermittent, the frost buildup is generally not a problem because whatever frost buildup does occur during operation melts off or can be easily removed while the unit is not in operation. Under these conditions, the vaporizer is operating efficiently, and the above-mentioned low efficiency steady state is generally not encountered.
- However, when the atmospheric vaporizer is operating in the continuous mode, the frost and ice do not get a chance to melt, and the vaporizer is soon operating inefficiently. For this reason, atmospheric vaporizers are generally not preferred for continuous vaporization of stored cryogenic liquids. Instead, a vaporizer is employed which utilizes a source of heat other than or in addition to ambient heat. This source of heat or energy is normally obtained from steam or electricity. Due to the escalating cost of energy, it is desirable to reduce or eliminate the need for a supplementary heat source of the vaporizer. It would be desirable to vaporize stored cryogenic liquid continuously without encountering the heretofore unavoidable drastic decrease in operating efficiency characteristic of atmospheric vaporizers of the prior art.
- Accordingly, it is an object of this invention to provide an improved atmospheric vaporizer for cryogenic liquids that is suitable for continuous operation while substantially avoiding the drastic reduction in operating efficiency characteristic of prior art atmospheric vaporizers.
- The above and other objects which will be apparent to those skilled in the art are achieved by the present invention which comprises an apparatus for continuously vaporizing a cryogenic liquid by employing heat absorbed from the ambient air, said apparatus comprising at least three substantially vertically positioned passes which are piped together, each pass being comprised of a center tube provided with a plurality of fins substantially equally spaced around said tube, each fin having a radial length of at least 1.5 times the outside diameter of said tube and extending longitudinally along substantially the entire length of said tube, wherein the ratio of the distance between the tips of the most adjacent fins of adajcent passes to radial fin length is above 1, said apparatus being characterized in that each center tube has an outside diameter of from 1.27 to 3.81 cm and is provided with 3 to 8 fins, each fin has a radial length of from 1.5 to 7 times the outside diameter of said tube, each pass has a length of from 1.52 to 6.08 m and a vertical distance from the ground or other support platform to the bottom edge of the fins from 0.3 to 1.2 m, and the ratio of the distance between the tips of the most adjacent fins of adjacent passes to radial fin length is from 1.5 to 5.
- Accordingly, the vaporizer of the present invention employs relatively wide spaces between each vertical pass. The wide spaces would be thought, under conventional thinking, to hinder efficient heat transfer. However, the combination of the wide space with the above defined fin length, tube diameter, tube length and vertical distance from the ground or other support platform to the bottom edge of the fins (shortly called ground clearance) serve not only to compensate for the expected loss of heat transfer efficiency, but surprisingly work together to actually provide improved overall heat transfer over the conventional design.
- Preferred embodiments of the invention are described in detail below with reference to the drawings in which
- Figure 1 illustrates a typical atmospheric vaporizer pass;
- Figure 2, Figure 3, and Figure 4 are each a plan view of a vaporizer pass, wherein Figure 2 illustrates a pass having four fins, Figure 3 illustrates a pass having eight fins, and Figure 4 illustrates a pass having three fins;
- Figure 5, Figure 6, and Figure 7 are each a plan view of a vaporizer pass array, wherein Figure 5 illustrates a square array of four-finned passes,
- Figure 6 illustrates a triangular array of four-finned passes, and Figure 7 illustrates a square array of three-finned passes;
- Figure 8 illustrates one embodiment of the atmospheric vaporizer of this invention; and
- Figure 9 is a graphical representation of steady state flow rate versus spacing ratio.
- The atmospheric vaporizer of this invention is comprised of three of more finned passes piped together and arranged in an array having defined spacing in between individual passes.
- Figure 1 illustrates a
typical pass 10 comprising a center tube 11 andfins 12. The center tube has an outside diameter of from 1.27 to 3.81 cm, preferably about 2.54 cm, and is of sufficient thickness to contain the fluid at the requisite supply pressure. The cryogenic fluid passes through the center tube as it passes through the vaporizer. Thefins 12 extend from the tube in radial fashion and extend longitudinally along the tube for substantially the entire length of the tube. The fins normally have a radial length of from 1.5 to 7 times the diameter of the tube, preferably about 3.5 times the diameter of the tube. The fin thickness is not critical, and is generally sufficient to obtain adequate mechanical strength to permit support of the unit in an upright position with suitable brackets and leg supports. Generally, the fin thickness is from 0.16 to 0.32 cm; a convenient thickness is 0.25 cm. The number of fins can range from 3 to 8 fins per pass. Figure 1 illustrates a four-fin arrangement. The fins are spaced substantially equidistant around the center tube. Thus, for the four-finned tube 20 shown in Figure 2 thefins 22 are arranged around thecenter tube 21 at about 90° from each other. For the eight-finned tube 30 shown in Figure 3, thefins 32 are arranged around the center tube 31 at about 45° from each other. And for the three-finned tube 40 shown in Figure 4, thefins 42 are arranged around thecenter tube 41 at about 120° from each other. - Each pass has a length of from 1.52 to 6.08 m, preferably from 2.44 to 4.88 m, most preferably about 3.66 m. The fins extend along the length of the center tube substantially from end to end; however, there is a small length at both the top and bottom of the tube where the fins do not extend so as to permit connecting of the passes together. The passes are connected together in any suitable manner; a convenient method of connecting is by use of U-bend joints.
- The passes may be constructed from any material having good heat transfer characteristics. Aluminum is the preferred material. When high pressure is required, the center tube may be fabricated from stainless steel or monel and fitted with the aluminum fins.
- The passes are usually set on the ground, positioned vertically and held in place by suitable leg supports. Normally, the passes have a ground clearance of from about 0.3 to 1.2 m, preferably from about 0.46 to 0.92 m. By ground clearance it is meant the vertical distance from the ground, or other platform such as a concrete pad, to the bottom edge of the radial fins. The higher ground clearances would be better suited for climates having significant accumulations of snow so that the vaporizer can clear the level of snow.
- The passes may be piped in series or in a combination of series and parallel configurations. The top of one pass is piped to the top of an adjacent pass, and the bottom of a pass is piped to the bottom of an adjacent pass. Thus, cryogenic fluid enters one pass at the bottom, travels up the pass and over through the connection to an adjacent pass, down that pass and over through the connection to another pass, and so on until it exits as a gas at the temperature appropriate for the end use. The number of passes the fluid flows through, and the path of the fluid, i.e. series or combination series and parallel, will depend on various factors, such as end use temperature and flow rate requirements, ambient temperature, heat transfer characteristics, pressure drop factors and other considerations which are known to those skilled in the art.
- The passes of the atmospheric vaporizer of this invention are spaced apart from one another such that the ratio of the distance between fin tips to the fin length, herein also called the spacing ratio, is from 1.5 to 5. For example, one embodiment of the atmospheric vaporizer of this invention employs 2.54 cm diameter passes spaced 33.66 cm apart centerline to centerline or (31.12 cm) apart edge to edge with fins having a radial length of 8.89 cm. In this case, the distance between fin tips or the gap between fins is the distance between passes minus the fin radial length on each pass, or 31.12 cm-2(8.89 cm)=13.34 cm and the spacing ratio is 13.34 cm/8.89 cm=1.5. This spacing ratio is calculated with reference to the two closest fins on adjacent passes.
- As previously mentioned, the spacing ratio may be from 1.5 to 5; preferably the spacing ratio is from 2 to 4 and most preferably it is about 3. There is a sharp increase in the operating efficiency of the atmospheric vaporizer at the lower end of the defined spacing ratio range. The efficiency gradually increases and then evens out as the upper limit of the range is approached and attained. This phenomenon is shown more clearly in Figure 9 and in the Examples.
- Heretofore, it was felt that atmospheric vaporizers would operate at better efficiency, i.e., better heat transfer could be attained, when the passes were closer together. This invention comprises the discovery that moving the individual passes further apart than heretofore thought prudent will result, surprisingly, in an increase in efficiency when the spacing ratio is increased to 1.5, and that the efficiency continues to increase until the spacing ratio is increased to 5.
- The passes of the atmospheric vaporizer of this invention are arranged in a square, rectangular or triangular array. Figure 5 illustrates an
array 50 of four-finned passes. Here one square array is demarcated byindividual passes array 60 of four-finned passes. Here one triangular array is demarcated byindividual passes individual passes array 70 of three-finned passes. Here one square array is demarcated byindividual passes - Figure 5 may be used to illustrate some typical modes of operating for the atmospheric vaporizer of this invention. For example, a cryogenic liquid may enter the bottom of
pass 51, travel up through it and over to pass 52, down this pass and so on down the line until it is discharged as a gas frompass 55. This illustrates operation in series. Similarly, the fluid may enter pass 53 andexit pass 56, or enterpass 58 andexit pass 57. Alternatively, the inlet fluid could be combined so that the inlets ofpass pass - Figure 8 illustrates a typical atmospheric vaporizer of this invention. The front supports are shown in broken view in order to more clearly show the inlet and outlet connections. As shown in Figure 8, liquid cryogen enters the vaporizer through
inlet 81, travels uppass 82 and across pipingconnection 83 to pass 84, downpass 84 and across pipingconnection 85 to pass 86, uppass 86 and across pipingconnection 87 to pass 88, and downpass 88 and outoutlet 89 in the form of a gas. - The passes which comprise the atmospheric vaporizer of this invention may be deployed in any suitable spatial configuration consistent with the spacing ratio defined previously. It is expected that the array of three or more passes will define an enclosed air space between them, i.e. that the passes will not all be in a straight line. Preferred arrays are rectangular or square arrays as shown in Figures 5 and 7 and triangular arrays as shown in Figure 6.
- The atmospheric vaporizer of this invention may also be provided with one or more control devices. One such device is to control the flow rate of the fluid. By regulating the flow of fluid, one can compensate for changes in ambient air temperature and/or system heat transfer efficiency in order to keep the exit gas temperature constant. Such an arrangement is most useful when the particular usage to which the gas is put requires a specific gas temperature or temperature range.
- This invention, by employing the critical pass spacing ratio and the other defined features provides an atmospheric vaporizer which is capable of vaporizing cryogenic liquids on a continuous basis at an efficiency considerably higher than is achievable by the use of atmospheric vaporizers of the prior art.
- The following examples serve to further illustrate preferred embodiments of the atmospheric vaporizer of this invention, and the greatly improved results attainable by its use over those obtained with conventional atmospheric vaporizers. The examples are intended to illustrate the invention, and are not intended to limit the scope of the invention.
- An atmospheric vaporizer having four passes in a square array was employed to vaporize liquid oxygen and was evaluated to determine its flow capacity at steady state. The evaluation was conducted in a climate control house so that ambient temperature and humidity were relatively constant throughout the evaluation. The vaporizer passes were 2.29 m in height, each had a ground clearance of 0.46 m each had a center tube diameter of 2.54 cm and each was provided with eight fins. Each fin had a radial length of 8.89 cm and a thickness of 0.25 cm. The pass spacing, centerline to centerline, was 33.66 cm between adjacent passes and the spacing gap, i.e. the space from fin tip to fin tip was 13.34 cm. Thus, the spacing ratio was 13.34 cm/8.89 cm=1.5.
- The ambient temperature was kept at about 1.7°C throughout the evaluation and the relative humidity was kept about 100 percent. The gas exit temperature was maintained relatively constant throughout the evaluation at about -15°C by periodically adjusting the flow through the vaporizer. As the ice and frost blanket continued to increase, the flow was adjusted downward to maintain the gas exit temperature essentially constant. After about six days of operation the vaporizer operating conditions reached steady state and the flow rate was measured. The results appear in Table 1 under Example 1.
-
- As shown in Table 1 there is a sharp increase in steady state flow rate when the atmospheric vaporizer of this invention is employed over that obtained in the comparative example wherein the atmospheric vaporizer of this invention was not employed. This increase in steady state flow rate is indicative of the increase in operating efficiency.
- Comparison of Example 1 with Example 4 demonstrates that the increase in pass spacing ratio from 0.4 to 1.5 results in an increase in steady state flow capacity of 57 percent. Comparison of Example 2 with Example 4 demonstrates that the increase in pass spacing ratio from 0.4 to 2.9 results in an increase in steady state flow capacity of 90 percent. Comparison of Example 3 with Comparative Example 4 demonstrates that even though the fin number per pass was reduced from 8 to 4 resulting in a decrease in the heat transfer area of about 50 percent, an increase in pass spacing ratio from 0.4 to 2.9 results in an increase in steady state flow capacity of 43 percent.
- The results of these examples are shown graphically in Figure 9; curve E represents the results employing the vaporizer provided with 8 was increased to 45.7 cm giving a spacing gap of 25.4 cm and a spacing ratio of 2.9. The vaporizer was evaluated for steady state flow rate and the results are shown in Table 1 under Example 2.
- The above-described procedure was repeated a third time. The pass spacing again was 45.7 cm. However, in this example the number of fins used on each pass was four instead of eight. The vaporizer was evaluated for steady state flow rate. The results are reported in Table 1 under Example 3.
- For comparative purposes the above-described procedure was repeated, but without employing the atmospheric vaporizer of this invention. The vaporizer employed herein was identical to the eight-fin vaporizer described above except that the pass spacing was only 23.5 cm. The spacing gap was only 3.2 cm and the spacing ratio was only 0.4. This vaporizer was also evaluated for steady state flow rate and the results are also reported in Table 1 under Example 4. fins per pass and curve F represents the results employing the vaporizer provided with 4 fins per pass.
Claims (13)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT82100879T ATE12424T1 (en) | 1981-02-10 | 1982-02-08 | AMBIENT AIR EVAPORATOR. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US23311181A | 1981-02-10 | 1981-02-10 | |
US233111 | 1999-01-19 |
Publications (4)
Publication Number | Publication Date |
---|---|
EP0057928A2 EP0057928A2 (en) | 1982-08-18 |
EP0057928A3 EP0057928A3 (en) | 1982-09-01 |
EP0057928B1 true EP0057928B1 (en) | 1985-03-27 |
EP0057928B2 EP0057928B2 (en) | 1991-12-11 |
Family
ID=22875928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19820100879 Expired - Lifetime EP0057928B2 (en) | 1981-02-10 | 1982-02-08 | Atmospheric vaporizer |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0057928B2 (en) |
JP (2) | JPS57146999A (en) |
AT (1) | ATE12424T1 (en) |
BR (1) | BR8200676A (en) |
CA (1) | CA1160946A (en) |
DE (1) | DE3262739D1 (en) |
MX (1) | MX157500A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0635799U (en) * | 1992-10-12 | 1994-05-13 | 昭和アルミニウム株式会社 | Multi-tube evaporator |
US8403902B2 (en) * | 2010-05-18 | 2013-03-26 | Kci Licensing, Inc. | Reduced-pressure medical systems and methods employing a moisture processing device |
CN110631392A (en) * | 2019-10-08 | 2019-12-31 | 唐伟明 | Novel air-temperature vaporizer |
CN112161194B (en) * | 2020-09-07 | 2022-01-28 | 哈尔滨工业大学 | Novel high-efficient empty warm formula vaporizer |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2322341A (en) * | 1940-01-27 | 1943-06-22 | Morris F Booth | Heat exchange unit |
FR1239402A (en) * | 1959-07-11 | 1960-08-26 | Thermiques Fives Penhoet Soc E | Bundle of tubes with rectilinear external fins, finned tube for its constitution and exchanger elements thus obtained |
JPS5129546U (en) * | 1974-08-26 | 1976-03-03 |
-
1982
- 1982-01-29 CA CA000395206A patent/CA1160946A/en not_active Expired
- 1982-02-08 EP EP19820100879 patent/EP0057928B2/en not_active Expired - Lifetime
- 1982-02-08 DE DE8282100879T patent/DE3262739D1/en not_active Expired
- 1982-02-08 AT AT82100879T patent/ATE12424T1/en not_active IP Right Cessation
- 1982-02-08 BR BR8200676A patent/BR8200676A/en not_active IP Right Cessation
- 1982-02-09 MX MX19130382A patent/MX157500A/en unknown
- 1982-02-09 JP JP1829982A patent/JPS57146999A/en active Pending
-
1987
- 1987-10-28 JP JP16376287U patent/JPS63166800U/ja active Pending
Also Published As
Publication number | Publication date |
---|---|
MX157500A (en) | 1988-11-28 |
DE3262739D1 (en) | 1985-05-02 |
BR8200676A (en) | 1982-12-14 |
ATE12424T1 (en) | 1985-04-15 |
JPS63166800U (en) | 1988-10-31 |
EP0057928B2 (en) | 1991-12-11 |
EP0057928A2 (en) | 1982-08-18 |
EP0057928A3 (en) | 1982-09-01 |
CA1160946A (en) | 1984-01-24 |
JPS57146999A (en) | 1982-09-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4399660A (en) | Atmospheric vaporizer | |
US5251452A (en) | Ambient air vaporizer and heater for cryogenic fluids | |
US5390500A (en) | Cryogenic fluid vaporizer system and process | |
CA2124361C (en) | Combination direct and indirect closed circuit evaporative heat exchanger | |
KR100196791B1 (en) | Combination direct and indirect closed circuit evaporative heat exchanger | |
US3994999A (en) | Combination wet-dry cooling tower | |
US4584843A (en) | Method and apparatus of storing ice slurry and its use for cooling purposes | |
US3997635A (en) | Method and device for evaporative cooling | |
US3290025A (en) | Trough system for evaporative heat exchangers | |
US3282797A (en) | Thin film liquid evaporator formed of a thin corrugated sheet-like member | |
JPH0531042B2 (en) | ||
US20100101240A1 (en) | Configurations and Methods for Ambient Air Vaporizers | |
US3435623A (en) | Cryogenic vaporizer | |
JP5221136B2 (en) | Heating tower apparatus with direction adjuster | |
EP0057928B1 (en) | Atmospheric vaporizer | |
US4594855A (en) | Process and apparatus for ventilation with heat exchange | |
RU2077010C1 (en) | Heat exchanger with jet escape of liquid and plant for separation of air by distillation | |
US5351504A (en) | Heat pump for heating or refrigerating buildings and delivering in combination hot water for sanitary fixtures | |
ES2663084T5 (en) | Cryogenic air separation | |
US3165455A (en) | Distilling arrangement | |
USRE33026E (en) | Process and device for vaporizing a liquid by heat exchange with a second fluid and their application in an air distillation installation | |
JPH0648146B2 (en) | Double pipe type open rack type vaporizer | |
Lüchow et al. | Investigation of a spray cooling system in a plastic-film greenhouse | |
GB1587364A (en) | Vapourisation | |
US11774189B2 (en) | Heat exchanger, hardway fin arrangement for a heat exchanger, and methods relating to same |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB LU NL SE |
|
AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB LU NL SE |
|
17P | Request for examination filed |
Effective date: 19830228 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB LI LU NL SE |
|
REF | Corresponds to: |
Ref document number: 12424 Country of ref document: AT Date of ref document: 19850415 Kind code of ref document: T |
|
REF | Corresponds to: |
Ref document number: 3262739 Country of ref document: DE Date of ref document: 19850502 |
|
ET | Fr: translation filed | ||
PLBI | Opposition filed |
Free format text: ORIGINAL CODE: 0009260 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 19860122 Year of fee payment: 5 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19860228 |
|
26 | Opposition filed |
Opponent name: LINDE AKTIENGESELLSCHAFT, WIESBADEN Effective date: 19851220 |
|
NLR1 | Nl: opposition has been filed with the epo |
Opponent name: LINDE AKTIENGESELLSCHAFT |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19870112 Year of fee payment: 6 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Effective date: 19890208 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Effective date: 19890228 Ref country code: CH Effective date: 19890228 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PUAH | Patent maintained in amended form |
Free format text: ORIGINAL CODE: 0009272 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: PATENT MAINTAINED AS AMENDED |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19911204 Year of fee payment: 11 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19911209 Year of fee payment: 11 Ref country code: SE Payment date: 19911209 Year of fee payment: 11 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19911210 Year of fee payment: 11 |
|
27A | Patent maintained in amended form |
Effective date: 19911211 |
|
AK | Designated contracting states |
Kind code of ref document: B2 Designated state(s): AT BE CH DE FR GB LI LU NL SE |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19920127 Year of fee payment: 11 |
|
NLR2 | Nl: decision of opposition | ||
ET3 | Fr: translation filed ** decision concerning opposition | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19920229 Year of fee payment: 11 |
|
NLR3 | Nl: receipt of modified translations in the netherlands language after an opposition procedure | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Effective date: 19930208 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19930209 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Effective date: 19930228 |
|
BERE | Be: lapsed |
Owner name: UNION CARBIDE CORP. Effective date: 19930228 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19930901 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19930208 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Effective date: 19931029 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Effective date: 19931103 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
EUG | Se: european patent has lapsed |
Ref document number: 82100879.4 Effective date: 19930912 |
|
APAH | Appeal reference modified |
Free format text: ORIGINAL CODE: EPIDOSCREFNO |