Inductive bath plasma cupola background of the invention

Abstract

A method of generating syngas as a primary product from renewable feedstock, fossil fuels, or hazardous waste with the use of a cupola. The cupola operates selectably on inductive heat alone, chemically assisted heat, or plasma assisted heat. Additionally, the operation of the cupola is augmented by the use of direct acting carbon or graphite rods that carry electrical current for additional heat generation into the metal bath that is influenced by the inductive element. The method includes the steps of providing a cupola for containing a metal bath; and operating an inductive element to react with the metal bath. Feedstock in the form of a combination of fossil fuel, a hazardous waste, and a hazardous material is supplied to the cupola. A plasma torch operates on the metal bath selectably directly and indirectly. Steam, air, oxygen enriched air, and oxygen are supplied in selectable combinations.

Claims

1-22. (canceled)

23. A method of producing syngas by converting a feedstock to syngas, the method comprising the steps of: providing a cupola comprising an upper portion, a lower portion, a feedstock inlet, a syngas outlet, a slag drain, and a liquid metal bath, wherein the liquid metal bath fills the lower portion, wherein the upper portion comprises an open area above the liquid metal bath, wherein an inductive element at least partially surrounds the liquid metal bath; depositing a feedstock to the upper portion of the cupola; creating a syngas and a slag product from the feedstock; operating a plasma torch within the upper portion of the cupola, wherein the heat from the metal bath and the plasma torch provide the heat to convert the feedstock to syngas; and removing a slag product from a top portion of the liquid metal bath through a slag drain, wherein the slag drain is remove the slag product to an exterior of the cupola.

24. The method of claim 23, further comprising operating a second plasma torch in an exit section exterior to the cupola to heat the syngas after it exits the cupola.

25. The method of claim 23, wherein the feedstock is a fossil fuel.

26. The method of claim 23, wherein the feedstock is a hazardous waste.

27. The method of claim 23, wherein the feedstock is a combination of any organic compound, fossil fuel, and hazardous material.

28. The method of claim 1, wherein the plasma torch is operated indirectly.

29. The method of claim 23, wherein the plasma torch is operated directly.

30. The method of claim 23, wherein the feedstock is deposited on top of the liquid metal batch after being introduced to the upper portion.

31. The method of claim 23, wherein the step of creating a syngas further comprises injecting steam into the cupola to enhance the creation of syngas.

32. The method of claim 23, wherein the step of creating a syngas further comprises injecting a selectable one of air, oxygen enriched air, and oxygen into the cupola to enhance the creation of syngas.

33. A method of producing syngas by converting a feedstock to syngas, the method comprising the steps of: providing a cupola comprising an upper portion, a lower portion, a feedstock inlet, a syngas outlet, a slag drain, and a liquid metal bath, wherein the liquid metal bath fills the lower portion, wherein the upper portion comprises an open area above the liquid metal bath, wherein an inductive element at least partially surrounds the liquid metal bath; depositing a feedstock to the upper portion of the cupola; creating a syngas and a slag product from the feedstock; operating a first plasma torch within the upper portion of the cupola, wherein the heat from the metal bath and the first plasma torch provide the heat to convert the feedstock to syngas and wherein the first plasma torch is configured to direct energy into the liquid metal bath; and removing a slag product from a top portion of the liquid metal bath through a slag drain, wherein the slag drain is remove the slag product to an exterior of the cupola.

34. The method of claim 33, further comprising operating a second plasma torch in an exit section exterior to the cupola to heat the syngas after it exits the cupola.

35. The method of claim 33, wherein the first plasma torch is configured to operate on the metal bath selectably directly and indirectly.

36. The method of claim 33, wherein the step of creating a syngas further comprises adding chemical heat.

37. The method of claim 33, wherein the step of creating a syngas further comprises injecting steam to enhance the production of syngas.

38. A method of producing syngas by converting a feedstock in a chamber to syngas by the application of heat, the chamber having an inlet for feedstock and an outlet for syngas, the method comprising the steps of: providing said chamber in the form of a cupola containing a bottom portion filled with a liquid metal bath; operating an inductive element to react with a metal or metal alloy in the liquid metal bath to melt the metal or metal alloy, wherein the inductive element at least partially surrounds the liquid metal bath, and wherein the heat from the liquid metal bath provides the heat to convert the feedstock to syngas; supplementing said step of operating an inductive element by the further step of propagating a selectable one of a first plasma torch and electricity into the liquid metal bath to supplement heating of the cupola, wherein the selectable one of the first plasma torch and electricity is configured to direct energy into the liquid metal bath; and removing a slag product from a top portion of the liquid metal bath through a slag drain, wherein the slag drain is remove the slag product to an exterior of the cupola.

39. The method of claim 38, wherein said step of operating a first plasma torch is performed to operate on the liquid metal bath selectably directly and indirectly.

40. The method of claim 38, wherein there is provided the further step of supplementing said step of operating an inductive element by the further step of injecting steam into the cupola to enhance the production of syngas.

41. The method of claim 38, wherein there is provided the further step of supplementing said step of operating an inductive element by the further step of injecting a selectable one of air, oxygen enriched air, and oxygen into the cupola.

42. The method of claim 38, wherein there is provided the further step of supplementing said step of operating an inductive element by the further step of conducting electrical energy via a conductive rod formed of a selectable one of graphite and carbon into the liquid metal bath.

Description

BRIEF DESCRIPTION OF THE DRAWING

[0025] Comprehension of the invention is facilitated by reading the following detailed description, in conjunction with the annexed drawing, in which:

[0026] FIG. 1 is a simplified schematic representation of a cupola arrangement constructed in accordance with the invention;

[0027] FIG. 2 is a simplified schematic representation showing in greater detail a lower portion of the cupola of FIG. 1;

[0028] FIG. 3 is a simplified schematic representation showing an indirect application of a plasma torch on an inductive metal bath and the cupola; and

[0029] FIG. 4 is a simplified schematic representation showing a second indirect application of a plasma torch disposed at an angle relative to the cupola.

DETAILED DESCRIPTION

[0030] FIG. 1 is a simplified schematic representation of a cupola arrangement 100 constructed in accordance with the invention. As shown in this figure, a cupola shell 101 is provided with an inlet 104 for introducing a feedstock (not shown) that in some embodiments of the invention is a renewable feedstock, a fossil fuel, or a hazardous waste (not shown). Any combination of the three forms of feedstock can be used in the practice of the invention. There is additionally provided in an outlet port 106 for enabling removal of the generated syngas (not shown). In contrast to conventional inductive furnaces that facilitate a large outlet for metal or alloy production, there is no other outlet for such product. There is but an additional small drain 110 for eliminating inorganic slag.

[0031] It is a feature of the present invention that primarily organic compounds are processed to produce syngas. The specific illustrative embodiment of the invention described herein is essentially a bucket arrangement wherein an indirect electrical arc services a non-transfer inductive furnace. This is distinguishable from the conventional use of an inductive furnace, which is to make metals and alloys.

[0032] FIG. 1 further shows cupola arrangement 100 to have a direct acting plasma torch 115, which in some embodiments of the invention, as will be described below in relation to FIGS. 3, and 4, is an indirect acting plasma torch, to assist in the cupola heating process. In other embodiments, plasma torch 115 is a carbon or graphite rod that is used to conduct AC or DC electrical energy into a metal bath 120. The return path for the electrical energy has been omitted from this figure for sake of clarity.

[0033] There is provided in this specific illustrative embodiment of the invention a cathode 122 that is coupled electrically to an inductive element 125. Additionally, inductive element 125 has associated therewith an anode 127.

[0034] Air, oxygen enriched air, or oxygen are injected into cupola arrangement 100 via an inlet 130 to assist in the generation of heat using chemical energy and steam that is delivered via an inlet 132. The chemical energy and steam are injected for the further purpose of assisting in the generation of syngas. The process of the present invention can, in some embodiments, be performed in a pyrolysis, or air starved, mode of operation.

[0035] FIG. 2 is a simplified schematic representation showing in greater detail a lower portion of cupola arrangement 100 of FIG. 1. Elements of structure that have previously been discussed are similarly designated. Inductive element 125 reacts on metal bath 120. Metal bath 120 can consist of any metal or alloy such as aluminum for low temperature work or titanium for high temperature work. Metal bath 120 is kept at a constant fill level 134 by operation of slag drain 110 through which a slag product 135 is drained.

[0036] FIG. 3 is a simplified schematic representation showing a cupola arrangement 200, wherein there is illustrated an indirect application of a plasma torch 115 on an inductive metal bath and the cupola for enhancing the heating process. In this specific illustrative embodiment of the invention, plasma torch 115 has a power capacity of 0.2 MW. Elements of structure that have previously been discussed are similarly designated. As shown in this figure, syngas outlet 106 is lengthened in this specific illustrative embodiment of the invention, and is shown to have vertical and horizontal portions, 106a and 106b, respectively. Indirectly acting plasma torch 115 is, in this embodiment, inserted in the end of vertical section 106a. In this specific illustrative embodiment of the invention, syngas outlet 106 is refractory-lined and insulated (not shown).

[0037] In the embodiment of FIG. 3, there is shown an inlet 107 via which is provided municipal solid waste (MSW) (not specifically designated) as a feedstock. Of course, other types of feedstock, as hereinabove noted, can be used in the practice of the invention.

[0038] The product syngas in this embodiment is forced to exit into vertical section 106a where it communicates with the high temperature plume (not specifically designated) and the radiant heat that is issued by plasma torch 115. The syngas and syngas outlet 106 both are heated by operation of plasma torch 115. In this specific illustrative embodiment of the invention, the heated horizontal portion 106b of syngas outlet 106 is subjected to a heat extraction arrangement that delivers the heat to inlet 107 for the purpose of pre-gasifying the MSW feedstock. The heat extraction arrangement is formed by an impeller 210 that urges a fluid (not shown) along a fluid loop that includes a region 212 where the fluid is heated by communication with heated horizontal portion 106b of syngas outlet 106. The heated fluid then is propagated to a heat exchanger 215 where a portion of the heat therein is transferred to the incoming MSW feedstock that is being delivered at inlet 107.

[0039] There is additionally shown in this figure a steam inlet 132, as hereinabove described. However, the steam is shown in this figure to be supplied by a steam supply 220, and the steam then is conducted to a further heat exchanger 225 where a portion of the heat in the steam is transferred to the incoming MSW feedstock that is being delivered at inlet 107. Heat exchangers 215 and 225 thereby constitute a pre-gassifier for the MSW feedstock, whereby the production of syngas is enhanced.

[0040] FIG. 4 is a simplified schematic representation of a cupola arrangement 250 showing a second indirect application of a plasma torch that is disposed at an angle relative to the cupola. Elements of structure that have previously been discussed are similarly designated. As shown in this figure, the outlet port 106 is fabricated in part at an angle that in some embodiments is greater than 90° to induce tumbling and mixing in the product syngas (not shown). Thus, in addition to vertical and horizontal portions, 106a and 106b, respectively, there is shown in this specific illustrative embodiment of the invention an angular portion 106c. Plasma torch 115 is shown to be inserted in angular portion 106c.

[0041] Although the invention has been described in terms of specific embodiments and applications, persons skilled in the art may, in light of this teaching, generate additional embodiments without exceeding the scope or departing from the spirit of the invention described and claimed herein. Accordingly, it is to be understood that the drawing and description in this disclosure are proffered to facilitate comprehension of the invention, and should not be construed to limit the scope thereof.