Calorimetry system

• US 4,809,190 A
• Filed: 04/08/1987
• Issued: 02/28/1989
• Est. Priority Date: 04/08/1987
• Status: Expired due to Term

• Current Assignee: Stock Equipment Co. Inc. (Schenck Process Holding GmbH)
• Original Assignee: General Signal Corporation (SPX Corporation)
• Inventors: Ross, Steven L., Nowshiravani, Shahriar, Lutz, Gilbert F., Homer, John C.
• Primary Examiner(s): Lall, Parshotam S.
• Assistant Examiner(s): Ramirez, Ellis B.
• Application Number:
  US07/036,048
• Time in Patent Office: 692 Days
• Field of Search: 364/500, 364/510, 364/550, 364/551, 364/172, 364/557, 374/36, 374/37, 374/43, 374/29, 374/8, 374/40, 374/41, 374/54, 110/185, 110/342
• US Class Current: 700/285
• CPC Class Codes: G01N 25/28 the rise in temperature of the gases resulting from combustion being measured directly
• CPC Class Codes: G01N 33/0091 Powders
• CPC Class Codes: G01N 33/222 Solid fuels, e.g. coal

Abstract

A calorimetry systems for the continuous measurement of the heating value of coal, which provides heating value data used to control coal-fired furnaces. The system has apparatus for pulverizing the coal, a gravimetric feeder for providing pulverized coal at a measured mass feed rate, an initiating self-sustained combustion of the coal therein without the need for further supporting fuel gases. Instrumentation measures the flow rates of the cooling air, primary and secondary combustion air as well as the mass flow rates of the coal into the combustor. A computer is provided which is responsive to the measuring instruments (thermocouples and pressure gauges) for controlling the feeding of the coal and fuel gases during initiation of combustion and for computing the heating value of the coal. The computer has a memory with storage for specific heat values of the constituents of the products of combustion of various ranks of coal (bituminous, subbituminous, lignite, etc.) and the average mass fraction of each constituent in the coal by rank so that the heating value thereof can be determined with accuracy.

Claims

1. A calorimetry system for measuring the heating value of a fuel comprising combustion means into which said fuel and oxidizing gas are fed for converting said fuel into combustion gas, means for mixing said combustion gas with a mixing gas to provide a combined gas, means for measuring the temperature of said mixing gas, and said combined gas at the inlet and outlet of said mixing means, respectively, said oxidizing and said mixing gas being parts of a total gas means for measuring the mass feed rate of said fuel fed into said combustion means, means for measuring the mass flow rate of said total gas, computer means for computing the heat flow Q_c of said combustion gas in accordance with the equation ##EQU3## where m₁ is the mass feed rate of the fuel, m₂ is the mass feed rate of the total gas, T₁ is the temperature of said mixing gas at said inlet, and T₂ is the temperature of said combined gas at said outlet, and C_pf is the specific heat of said combined gas represented by a polynomial whose coefficients are the weighted sum of coefficients of similar polynomials that represent the specific heat of constituents of the combined gas over the temperature range T₂ -T₁, and said computer means also having means for computing the heating value of said fuel as the ratio of Q_c to m₁.

2. The system according to claim 1 wherein said computer means has means providing storage for the data representing heat capacity of each constituent of said combustion gas over a temperature range including T₂ -T₁ for a plurality of different types of fuel.

3. The system according to claim 2 wherein said fuel is coal and said other gas and said oxidizing gas is air, and said computer storage means stores the polynomial coefficients for CO₂, H₂ O, SO₂, N₂, O₂ and ash for a plurality of different ranks of coal which constitute said types.

4. A calorimeter system for the direct and continuous measurement of heating value of fuel which comprises combustion means into which said fuel and an oxidizing gas is fed for converting said fuel into a combustion gas, means for mixing said combustion gas with another gas to form a combined gas, said combustion means comprising a combustion chamber having an outlet for said combustion gas, an inlet for said fuel, and an inlet for said oxidizing gas, a cell of porous insulating material disposed around said chamber for absorbing radiant heat loss from said chamber, and means for communication of said oxidizing gas through said cell with said oxidizing gas inlet of said chamber for convecting said radiant heat back to said chamber, said mixing means comprising a channel having an inlet end in communication with said combustion gas outlet, an outlet end for said combined gas and an inlet for said other gas also at said inlet end, means for absorbing heat from said channel disposed around said channel, said channel heat absorbing means defining a passage for said other gas therethrough for converting the heat absorbed by said channel heat absorbing means back to said mixing means, and means responsive at least to the temperature of said other gas supplied to said mixing means inlet, the temperature of said combined gas at said mixing means outlet and the mass feed rate of said fuel into said chamber for computing the heating value of said fuel.

5. The system according to claim 4 wherein said combustion chamber and said cell are disposed in a housing, the inside of which with the outside of said cell defines a space, and a pipe communicating said oxidizing gas under pressure into said space.

6. The system according to claim 5 wherein said combustion chamber has an upper end with a plurality of openings spaced from each other along an annular path, an annular manifold disposed at said upper end and having a plurality of openings in communication with said annular openings to provide said inlet for said fuel, said fuel being solid fossil fuel, and means for feeding said fuel in particulate form into said manifold and said chamber under pressure.

7. The system according to claim 6 wherein said outlet from said chamber is a pipe defining a chimney extending from said upper end of said chamber, said manifold being disposed around said chimney pipe.

8. The system according to claim 6 wherein said chamber is a cylinder with a conical bottom, a plurality of holes below the midplane of said cylinder for said entry of pressurized oxidizing gas.

9. The system according to claim 8 further comprising an inlet for a gas for preheating said chamber and initiating combustion of said solid fuel therein, and an igniter for said preheating and combustion initiating gas disposed in said chamber.

10. The system according to claim 4 wherein said mixing means comprises a second housing disposed upon a first housing containing said combustion chamber, a pipe in said housing, said pipe defining a chimney providing said channel and extending upward1y, the lower end of said pipe defining said inlet end and having an opening at the bottom of said lower end for said combustion gas and an opening about the side thereof at said lower end for said other gas, an annular member spaced between the inside of said housing and the outside of said pipe defining a labyrinth path around said pipe, said path defining said passage and having said opening about said side of said pipe at said lower end as the outlet thereof and an opening through said housing at the opposite end of said path as the inlet for said other gas.

11. The system according to claim 10 further comprising baffle means in said channel pipe including a plurality of members spaced between the opposite ends thereof.

12. The system according to claim 11 wherein said baffle means members comprise a series of rings having openings therein spaced from each other axially along said channel pipe, and a series of discs spaced from each other axially along said pipe, the diameter of said discs being greater than the openings in said rings and less than the diameter of said channel pipe, and said rings and discs being disposed alternately axially along said pipe.

13. The system according to claim 12 further comprising a thermocouple for measuring the temperature of the combined gas exiting said channel pipe, said thermocouple being disposed between the ring and disc closest to the outlet end of said pipe.

14. The system according to claim 10 wherein a pipe defining a chimney extends from said combustion chamber into the lower end of said channel pipe, and a plurality of openings along the side of said channel pipe at the lower end thereof and provided, baffles extending inwardly of said openings into said pipe, each of said openings being disposed along the lower end of said pipe, a first side extending upwardly from said base to a height not exceeding the extension of said chimney pipe into said channel pipe, and another side extending between the end of said first side and the end of said base.

15. A calorimeter system for the direct and continuous measurement of the heating value of coal which comprises means for converting said coal into a combustion gas, means for mixing said gas with air to provide a combined gas, means to measure mass rate of total air flow, means for measuring at least the increase in temperature between the temperature of said mixing air and the temperature of said combined gas and the mass feed rate of said coal into said converting means for deriving said heating value, means for converting said coal into particulate form, gravimetric feeding means for feeding said coal at a constant mass rate and providing an output to said measuring means representing said mass feed rate of said coal, and means operated by pressurized air for transferring said coal from said feeding means to said converting means.

16. The system according to claim 15 wherein said converting means comprises a combustion chamber, means for initiation of the self-sustained combustion of said coal in said chamber, including means for preheating said chamber, and means controlling said feeding means for controlling the rate of delivery of said coal until said self-sustained combustion takes place.

17. The system according to claim 16 wherein said preheating means comprises a source of fuel gas, connected to said chamber, means for igniting said gas, and means for decreasing the flow of said gas while increasing the feed rate of said coal.

18. The system according to claim 15 wherein said gravimetric feeding means comprises a belt, a hopper disposed over said belt, means for controlling the flow of particulate coal into and out of said hopper, means for driving said belt and controlling the speed thereof, and means for measuring the weight of coal on said belt.

19. The system according to claim 18 wherein said hopper has a negative draft.

20. The system according to claim 18 wherein said hopper flow controlling means comprises means for sensing the level of coal in said hopper, and a dam at the exit end of said hopper moveable into and out of said exit end.

21. The system according to claim 20 further comprising pulverizer means for delivering said pulverized coal to said hopper, and means operative at a plurality of feed speeds for feeding said coal into said pulverizer.

22. The system according to claim 15 wherein said transferring means comprises a Venturi eductor having a hopper for receiving said coal from said gravimetric feeder.

23. The system according to claim 15 wherein said measuring means further comprises means for measuring the mass rate of total air flow which contributes to said combined gas including to said combustion gas.