Use of semipermeable membranes in cracking coils

Patent metadata

Field	Value
Publication number	US-2019241815-A1
Application number	US-201716340403-A
Country	US
Kind code	A1
Filing date	Oct 19, 2017
Priority date	Oct 25, 2016
Publication date	Aug 8, 2019
Grant date	—

Abstract

A pass or tube or a section thereof or “U” bend in a coil in a paraffin cracker having section having a pore size in the metal substrate from about 0.001 to 0.5 microns over coated with a dense metal membrane permits the permeation of one or more of H2, CH4, CO and CO2 from cracked gases moving the reaction equilibrium to the production of ethylene and reduces the load on the down-stream separation train of the steam cracker.

First claim

1 . A furnace coil for a steam cracker comprising one or more sections consisting of:
i) a continuous metal passageway permitting the flow of cracked gasses there through having a melting temperature greater than 1000° C. adapted to co-operate with passes in the coil;
said metal having one or more areas comprising:
a) a porosity so that from 5 to 75% of the pores having a size from 0.001 to 0.05 microns; or
b) ceramic inserts in or over coating on said metal having a melting point greater than 900° C. and a porosity so that from 5 to 75% of pores having a size from 0.001 microns to 0.5 microns;

said areas being over coated with a dense gas-selective membrane having a thickness from 0.1 to 10 microns permitting the diffusion of at least one of H 2 , CH 4 , CO and CO 2 at temperatures from 500° C. to 900° C. out of said passageway.

2 . The furnace coil according to claim 1 , wherein the metal or ceramic inserts or overcoating have a porosity so that from 10 to 50% of the pores have a size from 0.001 to 0.05 microns.

3 . The furnace coil according to claim 2 , wherein the ceramic is formed from oxides, dioxides, nitrides, carbides and phosphates selected from the group consisting of 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.

4 . The furnace coil according to claim 3 , wherein said section the dense gas-selective membrane comprises one or more of iron, nickel, titanium, chromium, aluminum, and molybdenum.

5 . The furnace coil according to claim 4 , wherein the dense gas-selective membrane further comprises one or more metals selected from the group consisting of Pd, Ta, V, Pt, Nb and Zr.

6 . The furnace coil according to claim 5 , wherein the dense gas-selective membrane further comprises one or more metal oxide ceramic selected from the group consisting of Al 2 O 3 , BaTiO 3 , SrTiO 3 and ZrO 2 .

7 . The furnace coil according to claim 6 , wherein the dense gas-selective membrane is a dense metal oxide membrane.

8 . The furnace coil according to claim 7 , wherein in the dense gas-selective membrane comprises Pd.

9 . The furnace coil according to claim 7 , wherein the dense gas-selective membrane comprises yttria stabilized ZrO 2 .

10 . The furnace coil according to claim 7 , wherein the dense gas-selective membrane comprises calcia stabilized ZrO 2 .

11 . The furnace coil according to claim 7 , wherein the dense gas-selective membrane is not less than about 95% of theoretical density.

12 . The furnace coil according to claim 2 , wherein the ceramic is a 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.

13 . The furnace coil according to claim 12 , wherein said monomeric and/or oligomeric silazanes contain heteroatoms selected from the group consisting of boron, titanium, aluminum, phosphorus, and combinations thereof.

14 . The furnace coil according to claim 1 , wherein the continuous metal passage way is a tubular passage way forming part of the coil.

15 . The furnace coil according to claim 1 , wherein the continuous metal passage way is a 90° bend or a 180° bend forming part of the coil.

16 . A method to remove one or more of H 2 , CH 4 , CO and CO 2 from cracked gasses in a furnace coil by incorporating one or more sections according to claim 1 .

17 . A cracking furnace comprising one or more coils according to claim 1 .

18 . A method for cracking a paraffin by passing it through a furnace coil according to claim 1 , at a temperature from 850° C. to 950° C.

19 . The method according to claim 18 , wherein said paraffin is a C 2-4 paraffin.

20 . The method according to claim 19 , wherein the paraffin is ethane.

Assignees

• Nova Chem Int Sa

Inventors

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

Classifications

• B01J6/008

  Pyrolysis reactions (of hydrocarbons C10G9/00) · CPC title

• C01B2203/0216

  containing a non-catalytic steam reforming step · CPC title

• B01D69/02

  characterised by their properties · CPC title

• C01B2203/041

  In-situ membrane purification during hydrogen production · CPC title

• F16L9/02

  of metal (F16L9/16 - F16L9/22 take precedence) · CPC title