HYDROCARBON FLUID PROCESSING PLANT DESIGN

• US 20070208432A1
• Filed: 05/31/2005
• Published: 09/06/2007
• Est. Priority Date: 06/18/2004
• Status: Abandoned Application

• Current Assignee: Daniel Hawrysz
• Original Assignee: Daniel Hawrysz
• Inventors: Hawrysz, Daniel
• Application Number:
  US11/579,193
• Publication Number:
  US 20070208432A1
• Time in Patent Office: Days
• US Class Current: 700/1
• CPC Class Codes: C10L 3/10 Working-up natural gas or synthetic natural gas
• CPC Class Codes: C10L 3/102 of acid contaminants
• CPC Class Codes: F25J 1/0022 Hydrocarbons, e.g. natural gas
• CPC Class Codes: F25J 1/0259 Modularity and arrangement of parts of the liquefaction unit and in particular of the cold box, e.g. pre-fabrication, assembling and erection, dimensions, horizontal layout "plot"
• CPC Class Codes: F25J 2240/70 Steam turbine, e.g. used in a Rankine cycle
• CPC Class Codes: F25J 2290/10 Mathematical formulae, modeling, plot or curves; Design methods
• CPC Class Codes: G05B 17/02 electric
• CPC Class Codes: H01M 8/04089 of gaseous reactants
• CPC Class Codes: H01M 8/04305 Modeling, demonstration models of fuel cells, e.g. for training purposes
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

The current invention is related to methods of designing hydrocarbon fluid processing plants and methods of producing hydrocarbon fluids using hydrocarbon fluid processing plants. More particularly, some embodiments of the invention are related to methods of designing natural gas liquefaction plants and methods of producing LNG using natural gas liquefaction plants. One embodiment of the invention includes a method of designing a hydrocarbon fluid processing plant, including: A) providing a process unit configuration for one or more processing units included in a hydrocarbon fluid processing plant; B) determining a cost to capacity relationship for a plurality of equipment types included in the one or more processing units; C) running a process simulation model to obtain a process simulation for the process unit configuration, the process simulation including the estimated capacity of the plurality of equipment types; D) determining a cost measure for the process simulation, the cost measure including an equipment cost measure determined using said estimated capacity of the plurality of equipment types and the cost to capacity relationships; E) altering a process variable in the process simulation model; and F) repeating steps C through E a plurality of times.

Claims

1. A method of designing a hydrocarbon fluid processing plant, comprising:

A) providing a process unit configuration for one or more processing units included in a hydrocarbon fluid processing plant;

B) determining a cost to capacity relationship for a plurality of equipment types included in said one or more processing units;

C) running a process simulation model to obtain a process simulation for said process unit configuration, said process simulation including the estimated capacity of said plurality of equipment types;

D) determining a cost measure for said process simulation, said cost measure including an equipment cost measure determined using said estimated capacity of said plurality of equipment types and said cost to capacity relationships;

E) altering a process variable in said process simulation model; and

F) repeating steps C through E a plurality of times.

2. A method according to claim 1, wherein said altering a process variable step E) includes altering multiple variables iteratively.

3. A method according to claim 2, wherein said altering a process variable step E) includes altering respective variables a plurality of times iteratively.

4. A method according to claim 3, wherein said hydrocarbon fluid processing plant is an LNG liquefaction plant.

5. A method according to claim 4, wherein said plurality of equipment types includes higher cost equipment types.

6. A method according to claim 5, wherein said higher cost equipment types is selected from refrigerant compressors, cryogenic heat exchangers, motors, turbine drivers, steam boilers, electrical generation and distribution equipment and combinations thereof.

7. A method according to claim 5, wherein said plurality of equipment types includes less than all the equipment types includes in said one or more processing units.

8. A method according to claim 5, wherein:

said running a process simulation model step C further includes said process simulation including a utility usage estimate; and

said determining a cost measure step D, further includes determining a utilities cost measure.

9. A method according to claim 8, wherein:

said running a process simulation model step C further includes said process simulation including a product quantity estimate; and

said determining a cost measure step D, further includes determining a product value cost measure.

10. A method according to claim 9, wherein said utilities cost measure, said product value cost measure and said equipment cost measure are all determined on a capital cost basis.

11. A method according to claim 10, wherein said cost measure is at least partially determined by summing said equipment cost measure, said utilities cost measure and said product value cost measure.

12. A method according to claim 11, further comprising:

G) determining for one or more of the process variables altered in step E, the value for said process variable that optimizes said cost measure.

13. A method according to claim 12, further comprising:

H) producing a process design for said one or more processing units based upon the value for said process variable that optimizes said cost measure.

14. A method according to claim 13, further comprising:

I) constructing a hydrocarbon fluid processing plant using said process design.

15. A method according to claim 14, further comprising:

J) producing a hydrocarbon fluid product from said hydrocarbon fluid processing plant.

16. A method according to claim 15, further comprising:

K) loading said hydrocarbon fluid product onto a transportation vessel.

17. A method of producing a hydrocarbon fluid product, said hydrocarbon fluid product produced from a hydrocarbon fluid processing plant, said hydrocarbon fluid processing plant designed at least partially using the following steps:

a) providing a process unit configuration for one or more processing units included in said hydrocarbon fluid processing plant;

b) determining a cost to capacity relationship for a plurality of equipment types included in said one or more processing units;

c) running a process simulation model to obtain a process simulation for said process unit configuration, said process simulation including the estimated capacity of said plurality of equipment types;

d) determining a cost measure for said process simulation, said cost measure including an equipment cost measure determined using said estimated capacity of said plurality of equipment types and said cost to capacity relationships;

e) altering a process variable in said process simulation model; and

f) repeating steps c through e a plurality of times, said method comprising producing said hydrocarbon fluid product from said hydrocarbon fluid processing plant.

18. A method according to claim 17, wherein said hydrocarbon fluid product is LNG.

19. A method according to claim 18, further comprising loading said LNG unto a transportation vessel.

20. A tangible media including a set of instructions readable by a computer, said set of instructions comprising:

A) a process configuration module suitable for inputting a process unit configuration for one or more processing units included in a hydrocarbon fluid processing plant;

B) a register module suitable for storing cost to capacity relationships for a plurality of equipment types included in said one or more processing units;

C) a process simulation model suitable for obtaining a process simulation for a process unit configuration, said process simulation suitable for estimating the capacity of said plurality of equipment types;

D) a cost calculation module suitable for determining a cost measure for said process simulation, said cost measure including an equipment cost measure determined using said estimated capacity of said plurality of equipment types and said cost to capacity relationships;

E) a process variable interfacing module suitable for allowing alteration of a process variable of said process simulation model;

F) a repetition module suitable for repeating modules C through E a plurality of times; and

G) an output module suitable for producing a data display.