Supersonic treatment of vapor streams for separation and drying of hydrocarbon gases

Patent metadata

Field	Value
Publication number	US-11266924-B2
Application number	US-202016872410-A
Country	US
Kind code	B2
Filing date	May 12, 2020
Priority date	Dec 22, 2015
Publication date	Mar 8, 2022
Grant date	Mar 8, 2022

Abstract

Selective recovery of C2 to C4 hydrocarbons is achieved through the use of a converging-diverging nozzle, or de Laval nozzle. The vapor stream comprising C2 to C4 hydrocarbons is fed into an inlet of a de Laval nozzle having a throat. The vapor stream may have an initial temperature of between 0° C. and 100° C., and an initial pressure of between 200 psig and 500 psig. In the de Laval nozzle, the vapor stream expands after passing through the throat of the de Laval nozzle, producing a vapor stream having re-duced temperature and pressure. Then, C2 to C4 hydrocarbons condense from the reduced-temperature vapor stream as liquid droplets, which may be recovered. Fractionation of C2 to C4 hydrocarbons by means of a de Laval nozzle is possible; the technique allows select-ive recovery of propane from a mixture of propane and ethane.

First claim

What is claimed is:

1. A method of drying a vapor stream comprising C1 to C4 hydrocarbon gases, or a mixture thereof;
said method comprising;
passing said vapor stream comprising said C1 to C4 hydrocarbon gases into an inlet of a de Laval nozzle having a throat, said vapor stream having an initial temperature of between 25° C. and 90° C. and an initial pressure of between 150 psig and 1000 psig, wherein the vapor stream contains 500 to 10,000 ppm H 2 O by volume;
expanding the vapor stream after the vapor stream passes through the throat of the de Laval nozzle, producing a reduced-temperature vapor stream; condensing said H 2 O from the reduced-temperature vapor stream to produce a dried stream;
recovering the condensed H 2 O from said vapor stream; and
wherein the dried stream comprises said C1 to C4 hydrocarbon gases and from 0 ppm to 150 ppm water,
wherein the vapor stream comprises, based on the weight of the C1 to C4 hydrocarbon gases, from 0% to 10% methane.

2. The method of claim 1 , wherein said vapor stream has an initial temperature of between 25° C. and 40° C.

3. The method of claim 1 , wherein the C1 to C4 hydrocarbon gases are selected from the group consisting of ethane, ethene, propane, propene, n-butane, isobutane, 1-butene, 2-butene, isobutylene, butadiene, and mixtures thereof.

4. The method of claim 1 , wherein the C1 to C4 hydrocarbon gases are C3 gases selected from the group consisting of propane, propene, and mixtures thereof.

5. The method of claim 1 , wherein the C1 to C4 hydrocarbon gases are C2 gases selected from the group consisting of ethane, ethene, acetylene, and mixtures thereof.

6. The method of claim 1 , wherein the C1 to C4 hydrocarbon gases comprise from 80 to 100% by mass of a mixture of C2 and C3 gases.

7. The method of claim 1 , wherein the C1 to C4 hydrocarbon gases comprise from 80 to 100% by mass of a mixture of C2 and C3 gases, in a C2 to C3 ratio of between 1:9 and 9:1.

8. The method of claim 1 , further comprising a step of inducing swirling flow in said vapor stream prior to said recovering;
wherein said swirling flow drives said condensed H 2 O toward the wall of said de Laval nozzle or the wall of a pipe connected to an exit of said de Laval nozzle by centrifugal force.

9. The method of claim 1 , wherein the vapor stream comprises condensable C2 to C4 hydrocarbon gases.

10. A method of recovering C2 to C4 hydrocarbon gases from a vapor stream comprising C2 to C4 hydrocarbon gases;
said method comprising:
drying said vapor stream comprising C2 to C4 hydrocarbon gases by the method of claim 1 to produce said dried stream;
passing said dried stream into an inlet of a de Laval nozzle having a throat, said dried stream having an initial temperature of between 0° C. and 100° C. and an initial pressure of between 200 psig and 500 psig;
expanding the dried stream after the vapor stream passes through the throat of the de Laval nozzle, producing a second reduced-temperature stream; condensing C2 to C4 hydrocarbons from the second reduced-temperature stream as a liquid; and
recovering the condensed liquid C2 to C4 hydrocarbons from said reduced-temperature stream,
wherein the vapor stream comprises, based on the weight of the C2 to C4 hydrocarbon gases, from 0% to 10% methane.

11. A method of recovering hydrocarbon gases in a vapor stream comprising C2 to C4 hydrocarbon gases, wherein the vapor stream is a waste gas stream from a chemical reactor,
said method comprising:
drying said vapor stream comprising C2 to C4 hydrocarbon gases by the method of claim 1 to produce said dried stream:
passing said dried stream into an inlet of a de Laval nozzle having a throat, said dried stream having an initial temperature of between 0° C. and 100° C. and an initial pressure of between 200 psig and 500 psig;
expanding the dried stream after the vapor stream passes through the throat of the de Laval nozzle, producing a second reduced-temperature stream; condensing C2 to C4 hydrocarbons from the second reduced-temperature stream as a liquid; and at least one of
recycling at least a portion of the condensed C2 to C4 hydrocarbons to said chemical reactor; or
transferring at least a portion of he condensed C2 to C4 hydrocarbons to a recovery unit,
wherein the vapor stream comprises, based on the weight of the C2 to C4 hydrocarbon gases, from 0% to 10% methane.

12. The method of claim 11 , wherein the chemical reactor is a hydroformylation reactor.

13. The method of claim 11 , wherein the chemical reactor is a gas phase polymerization reactor.

14. The method of claim 11 , wherein the recovery unit is a propane/propene separator, de-methanizer, or de-propanizer.

15. A method of reducing the moisture content of a vapor stream with a defined relative humidity, said vapor stream comprising C1 to C4 hydrocarbon gases and H 2 O,
said method comprising:
passing said vapor stream at subsonic velocity into an inlet of a de Laval nozzle assembly, said vapor stream having an initial temperature of between 25° C. and 90° C. and an initial pressure of between 150 psig and 1000 psig;
producing at least one reduced-temperature vapor stream in the de Laval nozzle assembly;
condensing said H 2 O from said at east one reduced-temperature vapor stream to produce a dried stream; and
recovering the condensed H 2 O;
wherein said relative humidity of the vapor stream prior to entering the de Laval nozzle is between about 2% and about 100%; and
wherein the dried stream comprises said C1 to C4 hydrocarbon gases and from 0 ppm to 150 ppm water,
wherein the vapor stream comprises, based on the weight of he C1 to C4 hydrocarbon gases, from 0% to 10% methane.

16. The method of claim 15 , wherein the de Laval nozzle assembly comprises at least two de Laval nozzles connected in series;
wherein said producing at least one reduced-temperature vapor stream comprises:
accelerating said vapor stream to supersonic velocity in a first de Laval nozzle to produce a first reduced- temperature vapor stream;
passing the vapor stream from an outlet of said first de Laval nozzle to an inlet of a second de Laval nozzle; and
accelerating said vapor stream to supersonic velocity in the second de Laval nozzle to produce a second reduced-temperature vapor stream.

17. The method of claim 16 , wherein said recovering the condensed H 2 O comprises recovering the condensed H 2 O from said first reduced-temperature vapor stream and from said second reduced-temperature vapor stream.

18. The method of claim 15 , wherein the de Laval nozzle assembly comprises at least two de Laval nozzles connected in parallel.

19. The method of claim 16 , wherein the de Laval nozzle assembly comprises:
a) a low-temperature condenser which condenses a portion of said H 2 O from said vapor stream at subsonic velocity; connected in series with
b) a de Laval nozzle which accelerates said vapor stream to supersonic velocity to produce said
c) reduced-temperature vapor stream.

Assignees

• Eastman Chem Co
• Univ North Carolina State

Inventors

• Shaikh Ashfaq Shahanawaz
• Puckette Thomas Allen
• Owens Scott
• Maaz Syed
• Edwards Jack R

Classifications

• B01D3/06 Primary

  Flash distillation · CPC title

• B01D3/16

  Fractionating columns in which vapour bubbles through liquid (packing elements B01J19/30, B01J19/32) · CPC title

• B01D53/24

  by centrifugal force (centrifuges B04B; cyclones B04C) · CPC title

• C10G50/00

  Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation · CPC title

• B01D53/265

  by refrigeration (condensation) · CPC title