Soot water cleaning by means of continuous pressure filtration

Patent metadata

Field	Value
Publication number	US-9827516-B2
Application number	US-201113989190-A
Country	US
Kind code	B2
Filing date	Nov 16, 2011
Priority date	Dec 9, 2010
Publication date	Nov 28, 2017
Grant date	Nov 28, 2017

Abstract

A pressure filtration system for cleaning residual quenching water of a gasifying device that gasifies carbon-containing fuels under elevated pressure is provided. The soot water from the quencher is passed to a filter system, which has pressure filter chambers operating alternately in filtering mode under gasifying pressure or in cleaning mode. The filtrate from these chambers is passed to a quenching water reservoir, from which the quencher is fed with quenching water. Only small temperature and pressure losses with respect to the residual quenching water leaving, and only a small additional amount of energy has to be expended to overcome the remaining pressure difference to bring the filtrate that is to be returned back to the gasifying pressure. The residual quenching water is cleaned substantially under gasifying pressure in a pressure filter, avoids flash evaporation of the residual quenching water into the vacuum area, with vapour cooling and a subsequent increase in pressure and reheating.

First claim

The invention claimed is:

1. A pressure filtration system for continuous cleaning of residual quench water from a gasifying device that gasifies carbon-containing fuels under gasification pressure, comprising:
a parallel filter wherein the filter has a plurality of pressure filter chambers operated alternately or in parallel in filtering mode or in cleaning mode under gasification pressure;
a quencher in fluid communication with the filter;
a quench water in fluid communication with the quencher wherein the filter is in fluid communication with the quench water reservoir; and
a pressure reducer in fluid communication with the plurality of pressure filter chambers via reducing valves,
wherein soot water from the quencher is fed to the filter with no substantial reduction in pressure or flash evaporation to ambient pressure,
wherein filtrate from the plurality of pressure filter chambers is fed to the quench water reservoir and the quencher is fed with quench water from the quench water reservoir, and
wherein a concentrated filter cake is expelled from the filter chamber during filter cleaning into the pressure reducer as a slurry by means of the reducing valves,
wherein the gasification pressure is in a range from 2 MPa to 5 MPa.

2. The pressure filtration system as claimed in claim 1 ,
wherein a throughput rate of the filter is a function of a fill level in the quencher.

3. The pressure filtration system as claimed in claim 1 ,
wherein the soot water is fed to the filter directly from the quencher or via an intermediate container connected in between.

4. The pressure filtration system as claimed in claim 1 , further comprising a fill-level regulator,
wherein a time interval for the filtration performed in the individual pressure filter chambers is set as a function of the respective flow rate determined by the fill-level regulator.

5. The pressure filtration system as claimed in claim 1 , further comprising a slurry cooler,
wherein the slurry is cooled in the slurry cooler prior to reduction to temperatures of 40-90° C.

6. The pressure filtration system as claimed in claim 1 , further comprising a booser pump group,
wherein the soot water is fed to the filter during a startup process via the booster pump group at low gasification pressure.

7. The pressure filtration system as claimed in claim 1 , further comprising a plurality of shutdown coolers,
wherein the cleaned/filtered soot water is cooled during a shutdown process by means of the plurality of shutdown coolers with an accompanying reduction in pressure.

8. The pressure filtration system as claimed in claim 1 , further comprising a wastewater receptacle,
wherein slag water from a slag sluice system is cleaned in a filter unit at pressures of around 0.3 to 0.4 MPa (3-4 bar) and fed directly to the wastewater receptacle.

9. The pressure filtration system as claimed in claim 8 , further comprising a sludge storage tank and a dewatering stage,
wherein an underflow from the filter unit is fed to the sludge storage tank and to the dewatering stage.

10. A method to clean residual quench water by continuous pressure filtration, comprising:
feeding soot water from a quencher to a parallel filter with no substantial reduction in pressure or flash evaporation to ambient pressure wherein the parallel filter has a plurality of filter chambers operated alternately or in parallel in filtering mode or in cleaning mode under gasification pressure; and
expelling a concentrated filter cake from each filter chamber of the plurality of filter chambers during filter cleaning into a pressure reducer as a slurry by means of reducing valves,
wherein gasification pressure lies in a range of 2 MPa to 5 Mpa,
wherein the quencher is in fluid communication with the filter, and
wherein the pressure reducer is in fluid communication with the plurality of pressure filter chambers via the reducing valves.

Assignees

• Fischer Norbert
• Hannemann Frank
• Mehlhose Friedemann
• Putz Mirko
• Taffelt Peter
• Siemens Ag

Inventors

• Fischer Norbert
• Hannemann Frank
• Mehlhose Friedemann
• Putz Mirko
• Taffelt Peter

Classifications

• C10J3/84

  with means for removing dust or tar from the gas · CPC title

• B01D29/52 Primary

  in parallel connection · CPC title

• C10J3/485 Primary

  Entrained flow gasifiers · CPC title

• C10J3/78

  High-pressure apparatus · CPC title

• C10J2300/169

  with water treatments · CPC title