Gasification reactor with superheater and superheated steam line

Patent metadata

Field	Value
Publication number	US-9523052-B2
Application number	US-201214345667-A
Country	US
Kind code	B2
Filing date	Sep 19, 2012
Priority date	Sep 20, 2011
Publication date	Dec 20, 2016
Grant date	Dec 20, 2016

Abstract

A process and a reactor for the of a carbonaceous feed. The reactor has a reactor chamber; steam generating heat exchange units; at least one steam drum; and recirculation lines for circulating water and steam between one or more of the heat exchange units and the steam drum. The steam drum further includes a steam feed line for transporting steam via a heat exchange unit and a superheated steam line to a superheated steam header. The superheated steam line is split into a return line leading to a heat exchange line through the steam drum, and a header feed line.

First claim

That which is claimed is:

1. A gasification reactor comprising:
a reactor chamber;
a cooling channel connected to a syngas outlet of the reactor chamber, the cooling channel comprising a series of steam generating heat exchange units, at least one of the heat exchange units being a superheater;
at least one steam drum;
recirculation lines for circulating water and steam between one or more of the heat exchange units and the steam drum,
a superheated steam header,
a steam feed line configured to transport steam from the steam drum to the superheater,
a superheated steam line configured to transport superheated steam from the superheater to the superheated steam header,
the superheated steam line being split into a return line leading to a heat exchange line through the steam drum, and a header feed line leading to the superheated steam header,
a first valve configured to selectively open or close the return line,
a second valve configured to selectively open or close the header feed line, and
a secondary superheated steam feed line connected to an outlet of the heat exchange line through the steam drum and leading to the superheated steam header, the secondary superheated steam feed line being connected to the header feed line between the second valve and the superheated steam header.

2. A gasification reactor according to claim 1 , the superheated steam feed line upstream of the return line being provided with one or more temperature sensors and
the reactor comprising one or more valve control units configured to open or close the return line and the header feed line respectively responsive to the measured temperature.

3. A gasification reactor according to claim 1 , the heat exchange line through the steam drum being connected to a line to a cross flow heat exchanger configured to pre-heat oxygen,
the cross flow heat exchanger being connected to an oxygen feed line configured to feed the pre-heated oxygen to one or more burners in the reactor chamber.

4. A gasification reactor according to claim 3 , comprising a return line configured to return condensed steam from the cross flow heat exchanger to the steam drum via a pressurizer.

5. A gasification reactor according to claim 1 , the heat exchange unit between the steam drum and the super heated steam header being a waste heat recovery unit downstream of the reactor chamber.

6. A gasification reactor according to claim 5 , the waste heat recovery unit being the first in a series of downstream waste heat recovery units.

7. A gasification reactor according to claim 1 , at least one of the heat exchange units comprising a water cooled membrane wall built of parallel cooling lines interconnected to form a gastight wall.

8. Process of reducing the temperature of a flow of superheated steam to a super heated steam header in a gasification reactor according to claim 1 , wherein saturated steam from a steam drum is fed into a superheater and subsequently via a feed line to the superheated steam header, wherein superheated steam of a temperature exceeding an upper limit is detoured to a heat exchange line through the steam drum to create additional steam in the steam drum.

9. A process according to claim 8 wherein steam after passing the heat exchange line through the steam drum is subsequently fed into the superheated steam header.

10. A process according to claim 8 wherein steam after passing the heat exchange line through the steam drum is subsequently passed through a cross flow heater crossing a counterflow of oxygen and wherein the oxygen is subsequently fed to one or more burners in the reactor chamber.

11. A process according to claim 10 wherein steam after passing the cross flow heat exchanger is subsequently fed back into the steam drum via a pressurizer.

Assignees

• Shell Oil Co

Inventors

• Kar Ibrahim
• Schmitz-Goeb Manfred

Classifications

• F22G5/16

  by indirectly cooling or heating the superheated steam in auxiliary enclosed heat-exchanger · CPC title

• F01K13/02 Primary

  Controlling, e.g. stopping or starting · CPC title

• Y02P20/129

  Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title

• C10J3/723

  Controlling or regulating the gasification process · CPC title

• C10J2300/1687

  with steam generation · CPC title