Methods of and apparatus for storing and delivering a fluid

• US 4,583,372 A
• Filed: 01/30/1985
• Issued: 04/22/1986
• Est. Priority Date: 01/30/1985
• Status: Expired due to Term

• Current Assignee: AT&T Technologies Inc (Nokia Corporation)
• Original Assignee: AT&T Technologies Inc (Nokia Corporation)
• Inventors: Koze, Jeffrey T., Egan, James J., Kumagai, Henry Y.
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US06/696,279
• Time in Patent Office: 447 Days
• Field of Search: 62/52, 62/53, 62/55
• US Class Current: 62/50.1
• CPC Class Codes: C23C 16/4485 by evaporation without using carrier gas in contact with the source material C23C16/4486 takes precedence
• CPC Class Codes: F17C 2201/0109 with exteriorly curved end-piece
• CPC Class Codes: F17C 2201/0119 with flat end-piece
• CPC Class Codes: F17C 2201/032 with substantially vertical main axis
• CPC Class Codes: F17C 2201/054 medium (>1 m3)
• CPC Class Codes: F17C 2201/056 Small (<1 m3)
• CPC Class Codes: F17C 2205/0134 characterised by the presence of fluid connection between vessels
• CPC Class Codes: F17C 2205/0146 with details of the manifold
• CPC Class Codes: F17C 2205/0176 with ventilation
• CPC Class Codes: F17C 2205/0332 Safety valves or pressure relief valves
• CPC Class Codes: F17C 2205/0338 Pressure regulators
• CPC Class Codes: F17C 2221/011 Oxygen
• CPC Class Codes: F17C 2221/017 Helium
• CPC Class Codes: F17C 2223/0123 gaseous, e.g. CNG, GNC
• CPC Class Codes: F17C 2223/0153 Liquefied gas, e.g. LPG, GPL
• CPC Class Codes: F17C 2223/047 with a dip tube
• CPC Class Codes: F17C 2225/0123 gaseous, e.g. CNG, GNC
• CPC Class Codes: F17C 2225/043 in the gas
• CPC Class Codes: F17C 2227/0107 by pressurising the ullage
• CPC Class Codes: F17C 2227/0192 by using a working fluid
• CPC Class Codes: F17C 2227/0393 : using a vaporiser
• CPC Class Codes: F17C 2250/043 : Pressure
• CPC Class Codes: F17C 2260/042 : Reducing risk of explosion
• CPC Class Codes: F17C 2270/0518 : Semiconductors
• CPC Class Codes: F17C 7/02 : Discharging liquefied gases

Abstract

A fluid (12), such as dichlorosilane, is stored in a pressure vessel (17) located at a site remote from a processing facility within the confines of a building (14). At such remote site the pressure vessel (17) is subject to climatic temperature variations over a range at the lower temperatures of which a vapor pressure of the fluid may be insufficient to generate a pressure within the pressure vessel to drive the fluid through a duct (36) toward the processing facility. A supply of an inert gas (34) is applied at a first predetermined pressure to the pressure vessel (17) to urge the fluid under such predetermined pressure through the duct (36) toward an evaporator vessel (38) located at the processing facility. The evaporator vessel (38) is maintained at a first predetermined elevated temperature at which the fluid at such first predetermined pressure is in a gaseous state. Any of the fluid urged toward and entering the evaporator vessel (38) is evaporated, such that a supply of the fluid in its gaseous state at the first predetermined pressure is maintained within the evaporator vessel (38). Fluid is drawn from the evaporator vessel and its pressure is reduced, advantageously by a heated regulator (43), to a second predetermined and stable pressure at which the fluid remains a gas at temperatures existing at the processing facility within the building (14). The amount of the fluid within the confines of the building (14) is by the described method and apparatus kept near a practical minimum.

Claims

1. A method of storing and delivering a fluid, comprising:

storing the fluid in its liquid state in a pressure vessel located at a site remote from a processing facility;

delivering the fluid in its liquid state under a first predetermined pressure to an evaporator vessel located at the processing facility;

maintaining the evaporator vessel substantially at a first predetermined temperature above an ambient temperature range, such that the fluid at such first predetermined temperature and first predetermined pressure is substantially always in a gaseous state, thereby evaporating the fluid entering the evaporator vessel and maintaining in the evaporator vessel a supply of the fluid in its gaseous state at such first predetermined pressure;

drawing fluid from the supply of fluid in the evaporator vessel for use within the processing facility;

reducing the pressure of such drawn off fluid to a second predetermined pressure of such magnitude at which the fluid retains its gaseous state at a temperature in a range expected to be maintained within the processing facility; and

delivering the fluid at substantially such second predetermined pressure to a usage destination within the processing facility.

2. A method of storing and delivering a fluid according to claim 1, wherein delivering the fluid in its liquid state under a first predetermined pressure to an evaporator vessel comprises:

applying a nonreactive gas at said first predetermined pressure to the pressure vessel; and

urging the fluid under the combined pressure of the applied nonreactive gas and vapor pressure of the fluid through a duct coupled to the evaporator vessel located at the processing facility.

3. A method of storing and delivering a fluid according to claim 2, wherein storing the fluid in its liquid state in a pressure vessel located at a site remote from a processing facility comprises storing the fluid at a site which is subject to climatically determined temperature variations, and wherein applying a nonreactive gas at said first predetermined pressure to the pressure vessel comprises observing a currently existing climatically determined environmental temperature, comparing such observed currently existing temperature with an expected range of temperatures, and adjusting a pressure at which the nonreactive gas is applied to a value which is less than the first predetermined pressure if the observed currently existing temperature is less than a mean of an expected range of temperatures to maintain a pressure applied to the pressure vessel in an acceptable range about such preselected first pressure.

4. A method of storing and delivering a fluid according to claim 2, wherein the fluid is dichlorosilane, and the step of applying a nonreactive gas at said first predetermined pressure to the pressure vessel comprises applying a nonreactive gas at a pressure which combines with a partial gas pressure of the dichlorosilane, thereby maintaining a total gas pressure in the pressure vessel in a desired range about a preselected median pressure value.

5. A method of storing and delivering a fluid according to claim 4,

wherein the step of applying the nonreactive gas comprises applying the nonreactive gas at a pressure which combines with the partial gas pressure to maintain a total gas pressure of substantially 40 PSIG in the pressure vessel:

and wherein maintaining the evaporator vessel at a first predetermined temperature comprises maintaining the evaporator vessel at a temperature of substantially 160 degrees Fahrenheit.

6. A method of storing and delivering a fluid according to claim 4, wherein the nonreactive gas is applied at a pressure which maintains the total gas pressure in the pressure vessel between 15 and 65 PSIG as a desired range about a preselected pressure value of 40 PSIG, and wherein the evaporator vessel is maintained at a temperature of substantially 160 degrees Fahrenheit.

7. A method of storing and delivering a fluid according to claim 4, wherein reducing the pressure of the drawn off fluid to a second predetermined pressure comprises drawing said fluid through a pressure regulator to reduce the pressure from such first predetermined pressure to such second predetermined pressure, and maintaining said pressure regulator at an elevated temperature with respect to its ambient.

8. A method of storing and delivering a fluid according to claim 2, wherein reducing the pressure of the drawn off fluid to a second predetermined pressure comprises reducing the pressure of the drawn off fluid in a pressure regulator to the second predetermined pressure, and maintaining the temperature of the pressure regulator at a temperature above an ambient temperature range.

9. A method of storing and delivering a fluid according to claim 8, wherein storing the fluid in its liquid state in a pressure vessel located at a site remote from a processing facility comprises storing the fluid at a site which is subject to climatically determined temperature variations, and wherein applying a nonreactive gas at said first predetermined pressure to the pressure vessel comprises observing a current climatically determined environmental temperature, comparing such observed current temperature with an expected range of environmental temperatures, and, if the observed current temperature is less than a mean temperature of the expected range of environmental temperatures, applying the nonreactive gas at a first predetermined pressure proportionally less than a desired mean value of an expected pressure variation of a total gas pressure in the pressure vessel due to variations in the environmental temperatures.

10. A method of storing and delivering a fluid according to claim 9, wherein the fluid is dichlorosilane and applying a nonreactive gas at said first predetermined pressure to the pressure vessel comprises applying a nonreactive gas at a pressure which combines with a partial gas pressure of the dichlorosilane, thereby maintaining a total gas pressure in the pressure vessel in a desired range about the desired mean value of the expected pressure variation.

11. A method of storing and delivering a fluid according to claim 10, wherein the nonreactive gas is helium stored at an initial first helium gas pressure higher than the first predetermined pressure, and the pressure of the helium is reduced to such first predetermined pressure before being applied to said pressure vessel.

12. Apparatus for storing and delivering a fluid, comprising:

a pressure vessel for storing the fluid under pressure in its liquid state, said pressure vessel being located remote from a processing facility;

an evaporator vessel located at the processing facility;

a fluid duct coupled between the pressure vessel and the evaporator vessel;

means coupled to the pressure vessel for raising the pressure of the fluid in the pressure vessel to a first predetermined pressure to urge the fluid through the duct from the pressure vessel toward the evaporator vessel; and

means for maintaining the fluid in the evaporator vessel substantially at a first predetermined temperature at which the fluid while remaining at such first predetermined pressure is substantially always in a gaseous state.

13. Apparatus for storing and delivering a fluid according to claim 12, wherein the evaporator vessel is located adjacent to a boundary wall of and within the confines of the processing facility.

14. Apparatus for storing and delivering a fluid according to claim 12, wherein the evaporator vessel is located adjacent to a boundary wall of and within the confines of the processing facility, the apparatus further comprising:

a duct coupled between the evaporator vessel and an apparatus using the fluid;

means, coupled into said duct between the evaporator vessel and said apparatus using the fluid, for reducing the pressure of the fluid flowing through said duct between the evaporator vessel and the fluid using apparatus from said first predetermined pressure to a second predetermined pressure at which the fluid retains its gaseous state at a temperature in a range of temperatures expected to be maintained within said processing facility; and

means for maintaining the pressure reducing means at a temperature above the expected range of ambient temperatures within said processing facility.

15. Apparatus for storing and delivering a fluid according to claim 14, wherein the fluid which is to be stored and delivered is dichlorosilane and the means coupled to the pressure vessel for raising the dichlorosilane stored in the pressure vessel to a first predetermined pressure comprises:

means for storing a nonreactive gas under pressure greater than the first predetermined pressure;

means for reducing the pressure of the nonreactive gas to such first predetermined pressure; and

means for applying the nonreactive gas at such first predetermined pressure to the pressure vessel to raise the pressure of the dichlorosilane to such first predetermined pressure.

16. Apparatus for storing and delivering a fluid according to claim 15, wherein the site at which the pressure vessel is located is subject to climatic temperature variations, such temperature variations being impressed on the dichlorosilane stored in the pressure vessel to affect a partial gas pressure component of the dichlorosilane of a total pressure value of the first predetermined pressure in the pressure vessel, such means for reducing the pressure of the nonreactive gas to such first predetermined pressure including means for adjusting the value of the pressure of the nonreactive gas to be applied to the pressure vessel to allow such gas to be applied to a first predetermined pressure lower than a desired mean value of an acceptable range of pressures expected in the pressure vessel as a result of such climatic temperature variations.

17. Apparatus for storing and delivering a fluid according to claim 16, wherein the first predetermined pressure is in a range between 15 PSIG and 65 PSIG and the means for maintaining the dichlorosilane in the evaporator vessel is capable of maintaining the first predetermined temperature substantially at a nominal temperature of 160 degrees Fahrenheit.

18. Apparatus for storing and delivering a fluid according to claim 17, wherein the means for reducing the pressure of the dichlorosilane from such first predetermined pressure to such second predetermined pressure is an adjustable regulator capable of maintaining the second predetermined pressure of the dichlorosilane at 9 PSIG as the first predetermined pressure ranges between 15 and 65 PSIG.