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Publication numberUS2966040 A
Publication typeGrant
Publication dateDec 27, 1960
Filing dateJun 24, 1958
Priority dateJun 24, 1958
Publication numberUS 2966040 A, US 2966040A, US-A-2966040, US2966040 A, US2966040A
InventorsHenry James J
Original AssigneeConch Int Methane Ltd
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Tank for the storage and transportation of a low boiling liquid
US 2966040 A
Abstract  available in
Previous page
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Claims  available in
Description  (OCR text may contain errors)


l 1 r 1 I I I I 1 INVENTOR. James J Henry 14220 rngys into service.

United States PatentO TANK FOR STORAGE AND TRANSPORTA- TION OF A LOW BOILING LIQUID James 'J. Henry, New York, N.Y., assignor, by mesne assignments, to Conch International Methane Limited, Nassau, Bahamas, a corporation of the Bahamas Filed June 24, 1958, Ser. No. 744,141

4 Claims. (CI. 62-54) This invention relates to the storage and transportation of a hquefied gas or other liquid that needs to be maintamed at extremely low temperatures, and it relates more particularly to the filling of a large tank with such cold boiling liquefied gas for storage or transportation.

Description of the invention will be made with reference to the storage and transportation of a liquefied natural gas. It will be understood, however, that the concepts of this invention can be employed also for the storage or transportation of other low boiling liquefied gases or other liquids that need to be maintained at low temperature, such as helium, nitrogen, air and the like gases capable of liquefaction.

For the storage or transportation of natural gas or other l1quefied gases, it is most economical and practical to house the liquid in storage tanks of large capacity. From a practical standpoint, such containers of large capacity should be designed for operation at low pres sure, otherwise the walls of the container would have to be fabricated of such thickness as markedly to increase the cost of the tank and to provide an excessive amount of dead weight.

liquefied natural gas is composed chiefly of methane which boils at 258 F. at atmospheric pressure. It usually contains small amounts of higher boiling hydrocarbons which will raise the boiling point slightly. Thus, it can be considered that, at atmospheric pressure, the liquefied natural gas will have a boiling point of about 240 to 258 F depending upon the amount and type of heavier hydrocarbons in the gas. Liquefied oxygen,

nitrogen, air, helium, and the like will have still lower boiling points at atmospheric pressure.

In the storage or ship transportation of liquefied natural gas from a source of plentiful supply to an area where a deficiency exists, use is made of large containers which are insulated to minimize heat loss, so that very little of the liquefied cargo will be vaporized by the heat which naturally enters the tank by reason of the wide temperature differential between the ambient atmosphere and the temperature of the cargo. Insulated tanks of thousands of barrels capacity have been constructed in which the heat loss has resulted in the separation of less than one-half of one percent of the liquid per day. The vapors released can easily be handled either for use to power the ship, or for re-liquefaction and returned to the storage tank in ship transportation or for an end use as a raw material, refrigerant and fuel in land storage.

One of the major problems that arises is in the filling of the tank with the liquefied gas when the tank, or portions thereof, is at an elevated temperature by comparison with boiling-point temperature of the liquid cargo.

-The elevated temperature condition may result from the return of the tank while empty, or with a cargo other than a cold liquefied gas, or when the tank is first put Whatever the reason, it has been found that unless the tank is cooled down to about the temperature of the cargo, such vigorous boiling takes place as the liquid cargo is introduced into the warmer areas ice of the tank as to cause excessive and vigorous boiling, which releases forces sometimes incapable of being properly harnessed, and releases vapors in an amount incapable of being properly handled.

The combination of excessive vaporization coupled with violent agitation appears also to develop a frothing condition which often results in overflow of the liquefied gas. Forces developed by the tremendous amount of vapor suddenly released can also cause destruction of the tank and elements associated therewith. These conditions are undesirable with any liquid, let alone a liquid as combustible as natural-gas liquids.

Thus it is an object of this invention to produce a fluid-handling system for safely and efiiciently filling large storage tanks with a low-boiling liquefied gas, and it is a related object to provide a tank for the storage and transportation of liquefied gas characterized by means for cooling down the tank to a desired low temperature level sufficient to enable the liquefied gas to be poured into the tank at a high rate for filling without uncontrolled or excessive vaporization, and without the development of pressures and forces, frothing or agitation which leads to spilling over of the liquids or deterioration of the tank.

These and other objects and advantages of this invention will hereinafter appear and for purposes of illustration, but not of limitation, an embodiment of the invention is shown in the accompanying drawings, in which- Figure 1 is a diagrammatic view of an arrangement of parts which may be employed in the practice of this invention;

Figure 2 is a sectional elevational view ofa tank embodying the features of this invention and representing the conditions existing during the cool-down stage; and

rate, preferably as a spray onto the inner side walls of the tank.

Introduction until the liquid is able to wet the walls of the tank is indicative of the reduction of the walls of the tank to a temperature at which the liquid can be introduced at a rapid rate for filling without excessive boiling. This is further indicated by a differential in the amount of liquid introduced by comparison with the amount of vapors coming off during the cool-down step, or a reduction in the vapor pressure when the liquid is sprayed into the tank at a constant rate. Instead of using reduction in the amount of vapor given off as an end point to the spraying of the material onto the walls of the tank, use can be made of thermocouples or other recording means for following the temperature change in wall portions of the tank to indicate the reduction of temperature in the tank to a level where the tank can be safely filled at a high rate without boiling or without vaporization in amounts incapable of being handled or controlled.

Referring now to the drawings, 10 indicates a tank preferably formed of a metal which is capable of retaining its ductility at the temperatures of the liquefied gas. Ordinary mild steel is impractical for this purpose since it loses its ductility at temperatures below F. and is therefore subject to deterioration and cracking at the low temperatures to which it would be exposed when filled with the liquefied gas. It is preferred to make use of such metals as aluminum, alloys of aluminum,

copper, or austenitic steels, such as 18-8 stainless steel, which metals are capable of retaining their strength at the extreme low temperatures of use.

The tank is insulated with a thick layer 12 of a material having low heat conductivity to minimize heat loss into the tank. For this purpose, use can be made of a structurally strong insulation, such as panels of balsa wood, quippo wood, or the like highly porous woody materials, or panels of foamed glass or plastics built up on the outer walls of the tank 10. When use is made of an outer shell 14 in spaced relation with the inner tank 10, the space between the tank and the shell can be either evacuated or else filled with insulating material of the type described, or a packed insulation, such as glass wool, ground cork, exfoliated vermiculite, Santocel, and the like, preferably with separators to divide the space into a sufficient number of compartments to minimize settling of the insulation in response to repeated expansions and contractions of the tank occasioned by the wide temperature changes which take place in use. When use is made of an outer shell or tank 14 with an insulated space in between, the outer tank can be formed of mild steel or any other suitable metal or structural material, because it will be protected by the insulation layer 12 from the low temperatures of the liquid content material.

The tank is completely sealed but various openings are provided in the walls, and preferably in the top wall, for gaining access into the tank for various purposes which will hereinafter be described. The top wall 16 is provided with a manhole 18 dimensioned to be sufliciently large to enable a person to gain access to the interior of the tank for purposes of inspection, repair, or replacement of parts. A cover 20 is provided for the manhole with means to secure the cover in sealing relation over the manhole when the latter is not in use.

A down pipe 22 of large diameter extends downwardly through the top wall to a level adjacent the bottom of the tank for use in filling the tank with liquid. Discharge is eflected by a similar pipe having a pump on the upper end thereof. Instead, the filling pipe may extend through the side wall or the bottom wall of the tank into the bottom portion thereof. The feed and discharge pipe 22 is connected by the trunk line 24 to the filling and discharging header 26 which extends from the tank to a source of supply or a source of storage or use of the liquefied gas. The header 26 may be used for the transmission of liquid into and from a number of tanks of the type described.

A plurality of spray heads 28 are arranged within the tank with the heads preferably positioned to direct the spray 30 of liquid onto the adjacent wall portions of the tank. The spray heads 28 (also shown in the form of openings 280 in the pipes) can be arranged at about the same level in the upper portion of the tank with preferably uniform lateral spacing therebetween substantially completely to cover the inner surface of the tank with the spray issuing from the heads. Instead of arranging the spray heads or openings at the same level, they can be arranged at different levels as illustrated by the group 28a in Figure 2, and some of the spray heads or spray openings can be positioned to direct the spray onto the walls of the tank, while others can be positioned to direct the spray into the interior of the tank for optimum coverage during cool-down. It is desirable to provide for a substantially uniform and complete coverage of the walls of the tank to minimize the existence of wide temperature differentials during cool-down.

The spray heads are connected to a header 32 extending about the interior of the tank, and the header is connected by line 34 to a spray line 36 which branches off of the trunk line 24. The branch line 36 is of considerably smaller capacity than the main header 26 or the trunk line 24, since the liquefied gas is adapted to be fed to the spray heads at a rate which is much lower than the rate of filling through the trunk line 24. The branch line 36 is provided with a valve 38 to control the flow of fluids, and the trunk line 24 is also provided with a fluid-control valve 40 at a point preferably beyond the branch line 36. In the illustrated modification, a branch line of about 2 inches outside diameter could be used in combination with a trunk line of about 6 inches in diameter whereby an amount of liquid could be carried in the branch line to the spray heads to cool down the tank without generation of so much vapor as would exceed the amount that could be handled or vented, or would cause build-up of excessive pressures within the tank to cause destruction or deterioration thereof.

The tank is provided with an outlet 42 in the top wall for the removal of vapors 44 generated from the liquid 46 introduced into the tank. The vapor outlet communicates with a vapor header 48 through a connecting vapor branch line 50. The header 48 can connect with the shore if the tank is on ship or it can connect either with a transmission pipe for use as refrigerant, fuel, raw material or the like, or it can connect with a reliquefaction unit for reconversion of the vapor into a liquefied state for possible return with the feed to the tank. The trunk line 50 is usually provided with means to record the amount of vapor being generated, as illustrated by the calibrated orifice 52 connected to a flow transmitter 54 and recorder 56. A shutoff valve 58 is also provided in the trunk line either before or after the recorder.

To avoid the build-up of excessive vapor pressure within the tank, an additional venting means is adapted to be provided in the form of a vapor outlet 60 which communicates with a line 62 that divides into a pair of trunk lines 64 and 66 of smaller dimension to communicate the relief vent 60 with a relief header 68. Since the relief lines are adapted to come into operation only when an emergency exists which will cause the sudden development of vapors in the tank, it is desirable to construct the relief lines for handling a large vapor load. Thus, the trunk lines 64 and 66 and the relief header 68 are usually of greater capacity than the vapor lines 50 and 48 that are used to remove the vapor formed in the course of normal operation of the tank.

The trunk lines 64 and 66 are each provided with a pressure valve 70 set to open at predetermined maximum pressures, such as 2 pounds per square inch. The relief valves can also be set to open when vacuum conditions develop in the tank, as in response to the drop in pressure when the liquid cargo isbeing removed at a too rapid rate. Opening of the valves, such for example as at a setting of /2 pound vacuum, will enable air or vapor, or preferably an inert gas, to flow into the tank to relieve the vacuum and thereby minimize the possibility of collapse of the tank. It is desirable to subdivide the trunk lines of the relief into two sub-lines, as illustrated, and to provide separate pressure control valves for each so that better and more certain control can be achieved.

Other elements for operation of the tank are provided but these need not be described herein in detail since they do not enter into the concepts forming the subject matter of this invention. The following dimensional characteristics of the various units are given by way of illustration in a commercial operation for the shipment of liquefied natural gas in large volumes in insulated tanks from a source of plentiful supply to an area where a deficiency exists. It will be understood that the dimensional characteristics of the units can be changed, depending upon the capacity of the tanks, the capicity of the equipment associated with the storage tanks, the material which is being transported or stored as cargo, and the location of the tanks.

For a ships tank having a capacity of better than 50,000 barrels, and calculated to filled at a rate of about 10,000 barrels per hour per tank, and to have a normal vaporization of about 25-50 percent of the liquid per day, which is equivalent to about 100,000 to 200,000 cubic feet of vapor flow per hour, the following specifications will be sufficient:

Inches Inches Header 26 12 Trunk line 50 6 Trunk line 24 6 Relief pipe 62 Branch line 36 2 Trunk line 64 8 Header 48 10 Relief header 68 16 In operation, when starting to fill a tank which is at an elevated temperature, because of non-use for the storage of the liquefied gas immediately prior to filling, the valve 40 in the trunk line 24 will be closed and the valve 38 of the spray line 36 is opened. The valve 38 is adjusted to permit flow of cargo to the spray heads in an amount which, when instantaneously converted to vapor, can be easily handled by the vapor lines 50 and 48. Exposure of the liquid to temperatures above its boiling point (-258 F. for methane at atmospheric pressure) causes the liquid immediately to vaporize with a resulting reduction in temperature. Thus, the liquid is sprayed into the tank at a slow rate until the tank has been cooled down in temperature to a level at which immediate vaporization of the liquid does not take place. When this occurs, the liquid will be able to stay on the walls of the tank to wet the walls, and the amount of vapor issuing from the tank to the vapor connections will diminish. This decrease in the amount of vapor generation will be evident from the readings on the flow meter so that it can be determined either visually by the wet walls or by the rate of vapor flow as to when the tank is in a cooled down condition to enable the liquid cargo to be introduced at a rapid rate for filling without turbulence and without generation of excessive amounts of vapor. When this condition is reached, the valve 40 is openend. The valve 38 may be closed or it may be allowed to remain open to feed liquid into the tank through the trunk line 24 and the branch line 36. When filled, all of the feed valves 40 and 38 are closed and the valve 58 in the vapor line is left open to permit the removal of vapors which are normally generated from the natural heat gain which takes place through the insulated walls of the tank.

It will be understood that the concepts described may be embodied in a shore installation or in a ship installation of large tanks for the storage and transportation of a low-boiling liquefied gas. It will be further understood that the dimensional characteristics described for the respective elements may be varied, depending upon the number of tanks employed, their capacity, and others of the variable conditions previously described.

It will be understood that changes may be made in the details of construction, arrangement and operation without departing from the spirit of the invention, especially as defined in the following claims.

6 I claim: 1. A storage tank for containing a large volume of a low-boiling liquified gas comprising A. an insulated housing of large capacity, and means for filling the housing with a low boiling liquefied natural gas composed mostly of methanol consisting of B. (1) a filling tube of large dimension extending into the housing,

(2) a header for the transmission for the liquefied gas, and

(3) a trunk line connecting the header with the filling tube,

C. (l) a spray tube extending into the housing,

(2) a spray means arranged in spaced-apart relation in the container and in communication with the spray tube,

(3) a branch line communicating the spray line with the trunk line,

. (1) a vapor outlet in the upper portion of the housing in communication with the vapor space above the liquid level in the housing,

(2) a vapor header for the transmission of vapor released from the housing, and

(3) a vapor line communicating the vapor outlet with the vapor header.

2. A storage tank as claimed in claim 1 which includes a flow valve in the branch line for controlling the flow of liquefied gas to the spray means to an amount which, when immediately converted to vapor, can be handled by the vapor lines.

3. A storage tank as claimed in claim 1 which includes a means for measuring the flow of vapors from the vapor outlet.

4. A storage tank for containing a large volume of a low boiling liquefied gas as claimed in claim 1 which includes References Cited in the file of this patent UNITED STATES PATENTS Jackson Aug. 30, 1949 Thompson May 1, 1951 UNITED STATES PATENT OFFICE ERTIFECATION OF CORRECTIN Patent Nos 2366 040 December 27 i960 James J, Henry It is hereby certified that error appears in the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.

Column 6 line 6 for "methanol" read methane m,

Signed and sealed this 23rd day of May 1961a (SEAL) Attest:

ERNEST W. SWIDER DAVID L. LADD Attesting Officer Commissioner of Patents

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2480472 *Sep 20, 1944Aug 30, 1949Pittsburgh Des Moines CompanyMethod and means of precooling insulated tanks for storing cold liquids
US2550886 *Feb 12, 1947May 1, 1951Union Carbide & Carbon CorpSystem for conserving liquefied gases
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3123982 *Nov 8, 1960Mar 10, 1964 Cryogenic gas sampler
US3298186 *Apr 21, 1965Jan 17, 1967Richfield Oil CorpAtmospheric lpg storage tank and process
US3717006 *May 27, 1971Feb 20, 1973Parker Hannifin CorpTransit handling system for volatile fluids
US5921421 *Apr 26, 1995Jul 13, 1999Fuquan; LiangBladder-type multipurpose vessel
US6367265 *Jun 2, 2000Apr 9, 2002Kabushiki Kaisha Kobe Seiko Sho.Vaporizer for a low temperature liquid
US7806166 *Dec 15, 2005Oct 5, 2010Parker-Hannifin CorporationInsulated spray cooling system for extreme environments
DE1277885B *Apr 12, 1965Sep 19, 1968TechnigazWaermeisolierter Behaelter fuer tiefsiedene verfluessigte Gase
U.S. Classification62/47.1, 114/74.00A, 141/4, 220/560.12, 62/52.1
International ClassificationF17C6/00
Cooperative ClassificationF17C6/00
European ClassificationF17C6/00