초록 ▼

A gas-to-liquid (GTL) process and system for converting a natural gas) into liquid hydrocarbons (e.g. diesel, naphtha, distillates, etc.) wherein the equipment subsystems from existing gas-to-methanol plants are re-utilized in the (GTL) process. The syngas generator from the methanol plant is used

A gas-to-liquid (GTL) process and system for converting a natural gas) into liquid hydrocarbons (e.g. diesel, naphtha, distillates, etc.) wherein the equipment subsystems from existing gas-to-methanol plants are re-utilized in the (GTL) process. The syngas generator from the methanol plant is used to generate syngas in the present process. The syngas is then adjusted to remove CO2 and H2 before the syngas is passed through a Fischer-Tropsch (FT) reactor to convert the syngas to liquid hydrocarbons. The FT reactor is comprised of the same equipment that was use previously to convert syngas into methanol except for the respective catalysts. The liquid hydrocarbons are then upgraded and separated into individual hydrocarbon products.

대표청구항 ▼

What is claimed is: 1. A method for modifying a natural gas-to-methanol conversion system having a syngas synthesis subsystem and a product synthesis subsystem to a natural gas-to-liquid hydrocarbon products system, said method comprising: installing a syngas adjusting subsystem to receive syngas f

What is claimed is: 1. A method for modifying a natural gas-to-methanol conversion system having a syngas synthesis subsystem and a product synthesis subsystem to a natural gas-to-liquid hydrocarbon products system, said method comprising: installing a syngas adjusting subsystem to receive syngas from said syngas synthesis subsystem and remove carbon dioxide and hydrogen from said syngas to produce an adjusted syngas; and changing the catalyst in said product synthesis subsystem from a catalyst which converts syngas to methanol to a catalyst which converts said adjusted syngas to said liquid hydrocarbon products. 2. The method of claim 1 including: installing a line for flowing carbon dioxide from said syngas adjusting subsystem to said syngas synthesis subsystem for mixing with said natural gas. 3. The method of claim 2 including: a product upgrading subsystem adapted to receive said liquid hydrocarbon products from said product synthesis subsystem. 4. The method of claim 3 including: returning at least a portion of said removed hydrogen to said syngas synthesis subsystem for use as fuel and to said product upgrading subsystem for use in upgrading said liquid hydrocarbons. 5. A method for converting an original natural gas-to-methanol system having a syngas synthesis subsystem and a product synthesis subsystem into a natural gas-to-liquid hydrocarbon products system, said method comprising: adapting said syngas synthesis subsystem of said original natural gas-to-methanol to be connected to an inlet stream of natural gas from a local source for converting said natural gas into syngas; installing a syngas adjusting subsystem between the original said syngas subsystem and the original said product synthesis subsystem, said syngas adjusting subsystem being adapted to receive syngas from said syngas synthesis subsystem and remove at least a portion of the carbon dioxide and at least a portion of the hydrogen from said syngas as said syngas passes therethrough whereby the hydrogen to carbon dioxide in said syngas is adjusted to a ratio of about 2 as the adjusted syngas exits said syngas adjusting subsystem; and changing the catalyst in the Fischer-Tropsch reactor in the original said product synthesis subsystem from a catalyst which converts syngas to methanol to a catalyst which converts said adjusted syngas to said liquid hydrocarbon products. 6. The method of claim 5 wherein said Fischer-Tropsch reactor is comprised of a pressure vessel having a plurality of tubes therein which are filled with said catalyst for converting the adjusted syngas to said liquid hydrocarbons. 7. The method of claim 5 including: installing a product upgrading subsystem in said natural gas-to-liquid hydrocarbon products system adapted to receive the liquid hydrocarbons from said reactor in said product synthesis subsystem and separate said liquid hydrocarbons products into the desired individual products. 8. The method of claim 7 wherein one of said desired individual products is diesel. 9. The method of claim 7 including: providing means within said original product synthesis subsystem for recycling a portion of said liquid hydrocarbon products to said Fischer-Tropsch reactor before said liquid hydrocarbons enter said product upgrading subsystem to control the temperature in said reactor. 10. The method of claim 8 including: providing means for recycling carbon dioxide separated from said syngas in said syngas adjusting subsystem to said inlet natural gas stream before said inlet stream enters said syngas synthesis subsystem. 11. The method of claim 9 including: providing means for returning at least a portion of said removed hydrogen to said syngas synthesis subsystem for use as fuel therein. 12. The method of claim 8 including: providing means for returning at least a portion of said removed hydrogen to said product upgrading subsystem for use in upgrading said liquid hydrocarbons. 13. The method of claim 7 wherein said product upgrading subsystem includes: a fractionating column adapted to receive said liquid hydrocarbon products from said Fischer-Trospch reactor for separating said liquid hydrocarbon products into individual liquid hydrocarbon products.