Transfer line

Patent metadata

Field	Value
Publication number	US-2019015793-A1
Application number	US-201816135084-A
Country	US
Kind code	A1
Filing date	Sep 19, 2018
Priority date	May 2, 2016
Publication date	Jan 17, 2019
Grant date	—

Abstract

A transfer line between the outlet of a steam cracker and the inlet for the quench system has metallic or ceramic inserts having a pore size from about 0.001 to about 0.5 microns inside the line forming a gas tight barrier with the inner surface of the line and having a vent for the resulting gas tight pocket are used to separate H 2 , CH 4 , CO and CO 2 from cracked gases reducing the load on the down-stream separation train of the steam cracker.

First claim

1 - 21 . (canceled)

22 . A method to remove one or more of H 2 , CH 4 , CO, and CO 2 from cracked gases leaving a cracking furnace by passing the gases through a transfer line wherein the transfer line is between an outlet of a steam cracking furnace and an inlet to a quench exchanger and comprises:
i) a continuous passageway of a metal having a melting temperature greater than 1000° C. having a flange at one end of the passageway adapted to cooperate with the outlet from the steam cracking furnace and a flange at the opposite end of the passageway adapted to cooperate with the inlet to the quench exchanger; one or more inserts in said passageway permitting a flow of gases through said passageway, said inserts being permeable to at least one of H 2 , CH 4 , CO, and CO 2 at temperatures from 500° C. to 900° C. and spaced from an interior wall of the passageway and sealed to the interior wall of said passageway to provide one or more gas tight chambers; and one or more ports through the metal to withdraw gases from said one or more gas tight chambers; said inserts being selected from
a) ceramic inserts having a melting point greater than 900° C. and a porosity from 5 to 75% of pores having a size from 0.001 microns to 0.5 microns and fitting within the metal casting and
b) metal inserts having a porosity from 5 to 75% of pores having a size from 0.001 microns to 0.5 microns;
c) or both;
and optionally ii) a membrane permeable to at least one of H 2 , CH 4 , CO, and CO 2 at temperatures from 500° C. to 900° C. on said inserts to permit the passage of at least one of H 2 , CH 4 , CO, and CO 2 there through into the gas tight chamber.

23 . The method according to claim 22 , wherein the insert is a porous ceramic formed from oxides, dioxides, nitrides, carbides and phosphates selected from porous silicon dioxide, fused silicon dioxide, porous aluminum oxide, titanium dioxide, zirconium dioxide, thorium dioxide, lanthanum oxide, magnesium oxide, calcium oxide, barium oxide, tin oxide, cerium dioxide, zinc oxide, boron oxide, boron nitride, boron carbide, boron phosphate, zirconium phosphate, yttrium oxide, aluminum silicate, silicon nitride, silicon carbide and mixtures thereof.

24 . The method according to claim 22 wherein the insert is resistant to coking.

25 . The method according to claim 22 , wherein the insert is in the shape of a cone or an island.

26 . The method according to claim 22 , wherein the insert is a metal alloy comprising one or more of iron, nickel, titanium, chromium, aluminum, chromium, nickel and molybdenum.

27 . The method according to claim 22 , wherein the membrane is present and has a thickness from 0.1 to 10 microns.

28 . The method according to claim 22 , wherein the membrane is present and the membrane comprises one or more metals selected from Pd, Ta, V, Pt, Nb, and Zr.

29 . The method according to claim 28 , wherein the membrane further comprises one or more metal oxide ceramic selected from Al 2 O 3 , BaTiO 3 , SrTiO 3 and ZrO 2 .

30 . The method according to claim 29 , wherein the membrane is a dense metal oxide membrane.

31 . The method according to claim 30 , wherein in the membrane the metal comprises Pd.

32 . The method according to claim 31 , wherein the metal oxide comprises yttria stabilized ZrO 2 .

33 . The method according to claim 31 , wherein the metal oxide comprises calcia stabilized ZrO 2 .

34 . The method according to claim 30 , wherein the membrane is not less than about 95% of theoretical density.

35 . The method according to claim 29 , wherein the membrane is coated on component a).

36 . The method according to claim 35 , wherein component comprises an alumina ceramic.

37 . The method according to claim 29 , wherein the membrane is coated on component b).

38 . The method according to claim 29 , wherein intermediate the ceramic oxide and component b) is a ceramic comprising one or more particles selected from tungsten, alumina oxide, zirconia, titania, silicon carbide, chromium oxide, yttrium oxide, having a particles size from 0.01 to 5 microns.

39 . The method according to claim 22 , wherein the membrane is Si/C/N ceramic formed by:
combining a monomeric and/or oligomeric silazane ceramic precursor with a comonomer comprising one or more of the group consisting of ene (vinyl) functionalized, oligomeric, inorganic or organic silazanes, difunctional thiols, and tetrafunctional thiols; forming the combination as a thin film on a substrate; photopolymerizing the thin film; and pyrolyzing the photopolymerized thin film so as to result in a ceramic membrane that contains substantially no oxide.

40 . The method according to claim 39 , wherein said monomeric and/or oligomeric silazanes contain heteroatoms selected from boron, titanium, aluminum, phosphorus, and combinations thereof.

Assignees

• Nova Chem Int Sa

Inventors

• Benum Leslie Wilfred
• Koselek Michael Edward
• Simanzhenkov Vasily
• Farag Hany Iskandar
• Mah Evan Geevouy
• Kluthe Jeffrey Thomas

Classifications

• C01B3/503

  characterised by membranes · CPC title

• B01J8/009

  Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane · CPC title

• B01D67/0067

  by carbonisation or pyrolysis · CPC title

• B01D71/024

  Oxides · CPC title

• B01D2053/221

  Devices · CPC title