TEST OF A "STOCKPORT" GAS-ENGINE WITH |
DOWSON PRESSURE GAS PLANT |
Made by R. Mathot at the Works of the "Union Electrique" |
Cie, Brussels, June 27, 1901 |
Piston Diameter: 151⁄2". Piston stroke, 22". |
Normal number of revolutions, 210. |
| 1. | Calorific value of the coal | 12750 B.T.U. |
| 2. | Nature and origin of fuel: Anthracite coal of Charleroi (Belgium). |
| 3. | Cost of fuel per ton at the mine | $5.50 |
| 4. | Cost of fuel per ton at the plant | $6.39 |
| 5. | Fuel consumption per hour in the generator | 46.3 lbs. |
| 6. | Fuel consumption per hour in the boiler | 7 lbs. |
| 7. | Proportion of ash in the coal | 6 per cent. |
| 8. | Weight of steam at 66 lbs. generated per hour | 42.7 lbs. |
| 9. | Average brake horse-power | 53 B.H.P. |
| 10. | Fuel consumption for gas per B.H.P. per hour |
0.875 lbs. |
| 11. | Fuel consumption for steam per B.H.P. per hour | 0.133 lbs. |
| 12. | Total fuel consumption | 1.008 lbs. |
| 13. | Steam consumption at 66 lbs. pressure | 0.81 lbs. |
| 14. | Gas pressure at the engine | 13⁄8 inches |
| 15. | Weight of water per B.H.P. per hour for
cooling the cylinder entering at 68° F. and leaving at 105° F. |
51.5 lbs. |
|
|
| 16. | Corresponding heat absorbed in cooling | 1970 B.T.U. |
| 17. | Average initial explosive pressure on piston | 324 lbs. |
| 18. | Average pressure on piston per square inch | 72 lbs. |
| 19. | Average indicated horse-power with 85 per cent. misses |
92.5 I.H.P. |
| 20. | Corresponding mechanical efficiency | 84 per cent. |
| 21. | Corresponding electric load | 31.950 K.W. |
| 22. | Cost of B.H.P. per hour in anthracite | $0.0029 |
| 23. | Cost of kilowatt per hour in anthracite | $0.0048 |
| 24. | Electric power generated per B.H.P. | 602.8 W. |
| 25. | Thermal efficiency at 53 B.H.P. with 85 per cent. explosions |
18.5 per cent. |
|
TEST OF A 20 H.P. WINTERTHUR ENGINE |
With Winterthur Suction-Producer made by R. Mathot |
at Winterthur, June 4 and 5, 1902 |
DATA OF TESTS WITH ILLUMINATING GAS AND WITH FUEL GAS |
Dimensions of Winterthur Engine—Piston diameter: 103⁄8". Stroke:
167⁄8". Compression: 177 pounds per square inch. Regulation:
hit and miss. Ignition: electro-magnetic. Fly-wheel: normal,
with external bearing. Lubrication of piston: with oil-pump.
Of main bearings, with rings (as in dynamos). |
FULL LOAD WITH STREET-GAS |
| 1. | Number of revolutions per minute | 200 |
| 2. | Corresponding number of explosions | 96 per cent. |
| 3. | Net load on brake | 120 lbs. |
| 4. | Corresponding effective power | 22 B.H.P. |
| 5. | Mean initial explosive pressure on piston per square inch |
455 lbs. |
| 6. | Average pressure on piston per square inch | 78 lbs. |
| 7. | Gas consumption per B.H.P. at 24° C. and 721 mm. mean pressure |
15.5 cubic feet |
| 8. | Gas consumption per B.H.P. reduced to 0° C. and 760 mm. mean pressure | 13.5 cubic feet |
|
|
HALF LOAD WITH STREET-GAS |
| 9. | Number of revolutions per minute | 204 |
| 10. | Corresponding number of explosions | 60 per cent. |
| 11. | Net load on brake | 60 lbs. |
| 12. | Corresponding effective power | 11.6 B.H.P. |
| 13. | Gas consumption per B.H.P. per hour at 24° C. |
| and 721 mm. mean pressure. | 21 cubic feet |
| 14. | Gas consumption per B.H.P. per hour at 0° C.
and 760 mm. mean pressure. | 18.3 cubic feet |
|
RUNNING WITH NO LOAD WITH STREET-GAS |
| 15. | Number of revolutions per minute | 206 |
| 16. | Corresponding number of explosions | 22 per cent. |
| 17. | Total gas consumption per hour at 24° C.
and 721 mm. mean pressure. | 106 cubic feet |
| 18. | Maximum calorific power of gas per cubic foot | 598 B.T.U. |
| 19. | Thermal efficiency with 96 per cent. explosions | 31 per cent. |
| 20. | Mechanical efficiency with 96 per cent. explosions |
82 per cent. |
| 21. | Temperature of water at the jacket-inlet | 75 degs. F. |
| 22. | Temperature of water at the jacket-outlet | 130 degs. F. |
| 23. | Compression per square inch on piston surface | 178 lbs. |
| 24. | Pressure after expansion | 37 lbs. |
|
TEST OF WINTERTHUR PLANT WITH PRODUCER-GAS |
| 1. | Nature of fuel. Belgian anthracite, "Bonne Esperance et Batterie"; size, |
3⁄4 inch. |
| 2. | Chemical composition: Carbon, 86.5 per cent.;
hydrogen, 3.5 per cent.; oxygen and nitrogen, 4.65 per cent.; ash, 5.35 per cent. |
|
|
| 3. | Calorific value per pound of coal | 14200 B.T.U. |
| 4. | Net calorific value per pound of fuel | 15050 B.T.U. |
| 5. | Price of anthracite delivered at the plant | $3.50 per ton |
| 6. | Number of revolutions of engine per minute | 200 |
| 7. | Corresponding number of explosions | 91 per cent. |
| 8. | Load on brake | 106 lbs. |
| 9. | Corresponding effective horse-power | 20.2 B.H.P. |
| 10. | Fuel consumption at the generator per hour | 16.4 lbs. |
| 11. | Fuel consumed per B.H.P. per hour | 0.81 lbs. |
| 12. | Proportion of ash resulting from the tests | 6 per cent. |
| 13. | Mean initial explosive pressure per square inch |
419.5 lbs. |
| 14. | Average pressure on piston per square inch | 72.5 lbs. |
| 15. | Indicated horse-power with 91 per cent. explosions |
25.4 I.H.P. |
| 16. | Mechanical efficiency | 79 per cent. |
| 17. | Thermal efficiency at the producer | 22 per cent. |
| 18. | Water consumption per hour in the scrubber | 66 gals. |
| 19. | Cost per B.H.P. per hour in anthracite | 62 gals. |
|
TEST OF A 60 B.H.P. GAS-ENGINE, TYPE G 9, WITH
A SUCTION-GAS PLANT OF THE GASMOTOREN
FABRIK DEUTZ |
(Made at Cologne, March 15, 1904, by R. Mathot.) |
DATA OF THE TESTS |
Diameter of Piston = 16.5". Piston Stroke = 18.9" |
FULL LOAD |
| 1. | Average number of revolutions per minute | 188.66 |
| 2. | Corresponding effective work | 65.11 B.H.P. |
| 3. | Average compression per square inch | 176 lbs. |
| 4. | Average initial explosive pressure per square inch |
397 lbs. |
| 5. | Average final expansion pressure | 25 lbs. |
| 6. | Vacuum at suction | 4.4 lbs. |
| 7. | Average pressure on piston | 81 lbs. |
| 8. | Corresponding indicated horse-power | 77 I.H.P. |
|
|
|
FUEL |
| 9. | Nature of fuel: Anthracite coal 0.4" to 0.8" |
| 10. | Origin: Coalpit of Zeihe, Morsbach at Aix-la-Chapelle. |
| 11. | Chemical composition of coal: |
| Carbon | 83.22% |
| Hydrogen | 3.31% |
| Nitrogen and Oxygen | 3.01% |
| Sulphur | 0.44% |
| Ash | 7.33% |
| Water | 2.69% |
| 12. | Calorific value. | 13650 B.T.U. |
|
GAS |
| 13. | Chemical composition of gas: |
| Carbonic acid | 6.60% |
| Oxygen | 0.30% |
| Hydrogen | 18.90% |
| Methane | 0.57% |
| Carbon monoxide | 24.30% |
| Nitrogen | 49.33% |
| 14. | Calorific value of gas, combination water, at 59° F. constant
volume reduced to 32° F. and atmospheric pressure | 140 B.T.U. |
|
TEMPERATURES |
Engine |
| 15. | Cooling water at the inlet of the cylinder-head |
55.4 deg. F. |
| Temperature at the outlet | 109.5 deg. F. |
| 16. | Temperature at outlet of cylinder | 127.5 deg. F. |
|
Gas-Generator |
| 17. | Temperature of water in the vaporizer | 158.3 deg. F. |
|
EFFICIENCIES AND CONSUMPTION |
| 18. | Mechanical efficiency | 84.6% |
| 19. | Gross consumption of coal per B.H.P. per hour | 0.86 lbs |
| 20. | Thermal efficiency in proportion to the effective work
and the gross consumption of coal in the gas-generator | 24.3% |
|
|
HALF LOAD |
WORK |
| 1. | Average number of revolutions per minute | 195.5 |
| 2. | Corresponding effective work | 33.85 B.H.P. |
| 3. | Corresponding average compression | 125 lbs. |
| 4. | Average initial explosive pressure | 258 lbs. |
| 5. | Average final expansion | 18 lbs. |
| 6. | Vacuum at suction | 6.8 lbs. |
| 7. | Average mean pressure on piston | 46.2 lbs. |
| 8. | Corresponding indicated power | 45. I.H.P. |
| 9. | Speed variation between full and half load | 3.5% |
|
CONSUMPTION |
| 10. | Gross consumption of coal per B.H.P. per hour | 1.155 lbs. |
|
RUNNING WITH NO LOAD |
| 1. | Average number of revolutions per minute | 199 |
| 2. | Minimum corresponding compression | 95.55 lbs. |
| 3. | Average initial explosive pressure | 220 lbs. |
| 4. | Average final expansion | 0 lbs. |
| 5. | Vacuum at suction | 8.8 lbs. |
| 6. | Average pressure on piston | 11.2 lbs. |
| 7. | Corresponding indicated horse-power. | 11 I.H.P. |
| 8. | Speed variation between full load and no load | 5.2% |
|
TEST OF A GAS PLANT OF A FOUR-CYCLE DOUBLE-ACTING
ENGINE OF 200 H.P. AND A SUCTION-PRODUCER
IN THE WORKS OF THE GASMOTOREN
FABRIK DEUTZ, COLOGNE |
March 14 and 15, 1904, by Messrs. A. Witz, R. Mathot, and de
Herbais |
DATA OF THE TESTS |
Piston Diameter: 211⁄4". Stroke: 279⁄16". Diameter of Piston-Rods:
front, 43⁄4"; rear, 45⁄16" |
|
ENGINE |
Full Load Tests |
| 1. | Average number of revolutions per minute | 151.29 and 150.20 |
| 2. | Corresponding effective load | 214.22 B.H.P.
and 222.83 B.H.P. |
| 3. | Duration of the tests | 3 hours and 10 hours |
| 4. | Average temperature of water after cooling the piston |
117.5 deg. F. |
| 5. | Average temperature of water after cooling the cylinder and valve-seats |
135 deg. F. |
| 6. | Water consumption per hour for cooling the piston | 39 gal. |
|
PRODUCER |
| 7. | Nature and Origin of Fuel: Anthracite coal
"Bonne-Esperance et Batterie" Herstal, Belgium. |
| 8. | Calorific value of fuel | 14650 B.T.U. |
| 9. | Consumption of fuel per hour (plus 53 lbs.
on the night of the 14th for keeping the generator fired during 14 hours, the
engine being stopped) | 199 lbs.-160 lbs. |
| 10. | Water consumption per hour in the vaporiser | 14.2 gals. |
| 11. | Water consumption per hour in the scrubbers | 318 gals. |
| 12. | Average temperature of gas at the outlet of the generator |
558 deg. F. |
| 13. | Average temperature of gas at the outlet of the scrubbers |
62.5 deg. F. |
|
EFFICIENCIES |
| 14. | Gross consumption of coal per B.H.P. per hour | 0.927 lbs.-0.720 lbs. |
| 15. | Consumption of coal per B.H.P. after deduction of the water |
0.907 lbs.-0.705 lbs. |
|
| 16. | Thermal efficiency relating to the
effective H.P. and to the dry coal consumed in the generator | 19%-24.4% |
| 17. | Water consumption per B.H.P. hour: |
| For the cylinder, stuffing-boxes and valve-seat jackets |
4.65 gals. |
| For the piston and piston-rods | 1.75 gals. |
| For the vaporizer | 0.0655 gals. |
| For washing the gas in the scrubbers | 1.42 gals. |
| 18. | Water converted in steam per lb. consumed in the generator |
0.193 gals. |