Method and apparatus for feeding municipal solid waste to a plasma gasifier reactor

Patent metadata

Field	Value
Publication number	US-9656863-B2
Application number	US-201213721846-A
Country	US
Kind code	B2
Filing date	Dec 20, 2012
Priority date	Dec 20, 2012
Publication date	May 23, 2017
Grant date	May 23, 2017

Abstract

A method and apparatus are described for supplying municipal solid waste (MSW), and/or other types of solid waste comprising both organic waste material and inorganic waste material, into a plasma gasifier reactor (PGR) in which the solid waste is to be processed.

First claim

The invention claimed is:

1. A method of processing solid waste comprising both organic and inorganic waste material, the method comprising the steps of:
(i) compacting the solid waste to form a compacted solid waste;
(ii) adding a carbon bed source material and a sludge material to the compacted solid waste to form a combined feed comprising the compacted solid waste, carbon bed source material, and the sludge material;
(iii) compacting the combined feed using a compression screw feeder to create a compressed combined feed;
(iv) introducing the compressed combined feed into a plasma gasifier reactor, the plasma gasifier reactor comprising:
a reactor vessel having an interior volume in which conversion of solid waste to syngas and molten slag can take place;
a solid waste inlet port via which the combined feed is charged into the vessel; a carbon bed, located inside the reactor vessel below the solid waste port, on which newly charged solid waste and carbon bed source material rests, through which molten slag can flow, and which is replenished by the carbon bed source material;
one or more plasma torches;
a slag outlet port at the bottom of the vessel; and
a syngas outlet port at the top of the vessel;

(v) supplying thermal energy from the one or more plasma torches to the carbon bed and solid waste so as to generate a syngas from the carbon bed and the organic waste material and a molten slag from the inorganic waste material;
(vi) withdrawing molten slag from the slag outlet port;
(vii) withdrawing syngas from the syngas outlet port; and
(viii) contacting the syngas stream with water to remove particulates from the syngas stream and form a sludge material comprising water and removed particulates.

2. The method of claim 1 , wherein the interior volume of the reactor vessel comprises a gasification zone in which gasification of organic waste material takes place, and wherein the method further comprises introducing a gaseous feed comprising molecular oxygen into the gasification zone, the mass ratio of water to molecular oxygen entering the gasification zone of the plasma gasifier reactor being controlled so as to be from 0.5 to 2.0.

3. The method of claim 2 , wherein the mass ratio of water to molecular oxygen entering the gasification zone of the plasma gasifier reactor is controlled so as to be from 0.8 to 1.8.

4. The method of claim 2 , wherein the mass ratio of carbon to molecular oxygen entering the gasification zone of the plasma gasifier reactor is controlled so as to be from 0.85 to 1.4.

5. The method of claim 2 , wherein the mass ratio of carbon to molecular oxygen entering the gasification zone of the plasma gasifier reactor is controlled so as to be from 1.0 to 1.4.

6. The method of claim 1 , wherein the interior volume of the reactor vessel comprises a gasification zone in which gasification of organic waste material takes place, and a gas retention zone above the gasification zone, and wherein the solid waste inlet port is located in the gasification zone of the vessel such that the combined feed is charged directly into the gasification zone.

7. A method of processing solid waste comprising both organic and inorganic waste material, the method comprising the steps of:
(a) providing a solid waste feed at a solid waste flow rate, the solid waste feed having a solid waste moisture content;
(b) compacting the solid waste feed to form a compacted solid waste;
(c) adding to the compacted solid waste a carbon bed source material at a carbon bed mass flow rate and a sludge material at a sludge mass flow rate to produce a combined feed having a combined feed moisture content, wherein the combined feed moisture content is greater than the solid waste moisture content;
(d) feeding the combined feed into a compactor at a combined feed mass flow rate to form a compacted combined feed;
(e) feeding the compacted combined feed into a plasma gasifier reactor, thereby generating a syngas stream and a slag stream;
(f) feeding a gaseous feed comprising molecular oxygen into the plasma gasifier reactor at a gaseous feed flow rate;
(g) contacting the syngas stream with water to separate the syngas stream into a sludge material and a particulate-depleted syngas stream, the sludge material comprising water and particulates removed from the syngas stream, the sludge material having a sludge moisture content, the sludge moisture content being greater than the combined feed moisture content;
(h) monitoring a ratio of water to molecular oxygen in the plasma gasification reactor; and
(i) adjusting at least one selected from the group of: the solid waste mass flow rate, the sludge material mass flow rate, the combined feed mass flow rate, and the gaseous feed flow rate, in order to maintain the ratio of water to oxygen in the plasma gasification reactor within a desired range.

8. The method of claim 7 , wherein step (h) comprises:
(h) adjusting at least one selected from the group of: the solid waste mass flow rate, the sludge material mass flow rate, the combined feed mass flow rate, and the gaseous feed flow rate, in order to maintain the ratio of water to oxygen in the plasma gasification reactor between 0.5 and 2.0.

9. The method of claim 7 , wherein step (h) comprises:
(h) adjusting at least one selected from the group of: the solid waste mass flow rate, the sludge material mass flow rate, the combined feed mass flow rate, and the gaseous feed flow rate, in order to maintain the ratio of water to oxygen in the plasma gasification reactor between 0.8 and 1.8.

10. The method of claim 7 further comprising:
(i) monitoring a ratio of carbon to molecular oxygen in the plasma gasification reactor;
(j) adjusting at least one selected from the group of: the solid waste mass flow rate, the sludge material mass flow rate, the combined feed mass flow rate, and the gaseous feed flow rate, in order to maintain the ratio of carbon to oxygen in the plasma gasification reactor between 0.85 and 1.4.

11. The method of claim 10 , wherein step (j) comprises:
(j) adjusting at least one selected from the group of: the solid waste mass flow rate, the sludge material mass flow rate, the combined feed mass flow rate, and the gaseous feed flow rate, in order to maintain the ratio of carbon to oxygen in the plasma gasification reactor between 1.0 and 1.4.

Assignees

• Air Prod & Chem

Inventors

• Anderson Alan Donald
• Petrocelli Francis Peter
• Winger Frank Stephen

Classifications

• F23G2201/301

  Treating pyrogases · CPC title

• C10J2300/0959

  Oxygen · CPC title

• C10J2300/0946

  Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale · CPC title

• C10J2300/0973

  Water · CPC title

• C10J3/30

  Fuel charging devices · CPC title