Hydrogen Sulfide Production Process and Related Reactor Vessels

Patent metadata

Field	Value
Publication number	US-2018319663-A1
Application number	US-201816029731-A
Country	US
Kind code	A1
Filing date	Jul 9, 2018
Priority date	Dec 10, 2015
Publication date	Nov 8, 2018
Grant date	—

Abstract

The present invention discloses a hydrogen sulfide reactor vessel with an external heating system that is conductively and removably attached to an exterior portion of the reactor vessel. Also disclosed are processes for producing hydrogen sulfide utilizing the reactor vessel.

First claim

1 - 16 . (canceled)

17 . A H 2 S production process comprising:
controlling a reaction chamber containing liquid sulfur at a start-up temperature above the melting point of sulfur with an external heating system comprising a heated reactor conduit conductively and removably attached to an exterior surface of the reaction chamber; (ii) adding liquid sulfur to the reaction chamber to a level sufficient to immerse an internal heating system positioned within the reaction chamber; (iii) engaging the internal heating system to reach and maintain an operating temperature of the liquid sulfur of at least about 300° C.; (iv) adding a hydrogen-containing gas into the liquid sulfur and reacting to produce H 2 S; and (v) optionally, discontinuing the operation of the external heating system.

18 . The process of claim 17 , wherein:
the start-up temperature is at least about 120° C.; the operating temperature is in a range from about 350° C. to about 600° C.; and the hydrogen-containing gas comprises H 2 .

19 . The process of claim 17 , wherein the process comprises discontinuing the operation of the external heating system in step (v).

20 . The process of claim 17 , wherein:
the process does not include a catalyst; and the process does not employ an internal steam coil heating apparatus or a heating jacket or steam jacket on the exterior surface of the reaction chamber.

21 . The process of claim 17 , further comprising a step of purifying the H 2 S by removing at least a portion of CS 2 , and/or at least a portion of H 2 , and/or at least a portion of sulfur vapor, from the H 2 S.

22 . The process of claim 21 , wherein H 2 S is produced at a purity of at least about 95 wt. % H 2 S.

23 . The process of claim 17 , wherein:
the start-up temperature is in a range from about 120° C. to about 200° C.; and the operating temperature is in a range from about 400° C. to about 600° C.

24 . The process of claim 23 , wherein the reacting in step (iv) is conducted at an operating pressure in a range from about 3 to about 15 bars.

25 . The process of claim 17 , wherein the internal heating system is an electric heating system.

26 . The process of claim 17 , further comprising a step of operating a quench column positioned above the internal heating system and below a reactor inlet for adding the liquid sulfur to the reaction chamber; and
controlling a quench column operating temperature of the liquid sulfur in the quench column above the melting point of sulfur with the external heating system, wherein the external heating system further comprises a heated column conduit conductively and removably attached to at least a portion of an exterior surface of the quench column.

27 . The process of claim 26 , wherein the quench column operating temperature is in a range from about 125° C. to about 450° C.

28 . The process of claim 26 , wherein the heated column conduit is present on less than about 20% of the surface area of the exterior surface of the quench column.

29 . The process of claim 26 , wherein the heated column conduit comprises steam circulating through a pipe constructed of a conductive metal material.

30 . The process of claim 26 , wherein a heat transfer material is present between the heated column conduit and the exterior surface of the quench column.

31 . The process of claim 26 , wherein:
the external heating system comprises a cover over the heated column conduit, the cover configured to be removably attached to the exterior surface of the quench column; and the exterior surface of the quench column further comprises an attachment point configured for the removable attachment of the cover.

32 . The process of claim 17 , wherein the heated reactor conduit comprises steam circulating through a pipe constructed of a conductive metal material.

33 . The process of claim 17 , wherein a heat transfer material is present between the heated reactor conduit and the exterior surface of the reaction chamber.

34 . The process of claim 17 , wherein the heated reactor conduit is present on less than about 10% of the surface area of the exterior surface of the reaction chamber.

35 . The process of claim 17 , wherein:
the external heating system comprises a cover over the heated reactor conduit, the cover configured to be removably attached to the exterior surface of the reaction chamber; and the exterior surface of the reaction chamber further comprises an attachment point configured for the removable attachment of the cover.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Hasenberg Daniel M
• Pauwels Alex
• Mertens Ives

Classifications

• B01J4/004

  Sparger-type elements · CPC title

• B01J2219/182

  horizontal · CPC title

• B01J10/005

  carried out at high temperatures in the presence of a molten material · CPC title

• B01J2219/00092

  Tubes · CPC title

• B01J19/24

  Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title