US786061A - Process of regulating air and steam supplied to gas-producers. - Google Patents

Process of regulating air and steam supplied to gas-producers. Download PDF

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US786061A
US786061A US21288704A US1904212887A US786061A US 786061 A US786061 A US 786061A US 21288704 A US21288704 A US 21288704A US 1904212887 A US1904212887 A US 1904212887A US 786061 A US786061 A US 786061A
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air
gas
water
producers
vane
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Harry F Smith
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension

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  • This invention has relation to the art or process of providing and regulating the air supplied to the producer of suction gas-producers, so that the said air shall bear a constant percentage of moisture regardless of the actual quantity of air supplied or the rapidity with which this quantity may change to suit varying loads on the engine.
  • equations of the form herein used are universally accepted by engineers and physicists in dealing with the quantities involved.
  • the formulas used are matters of no concern in this case excepting with respect to the form of the equations and not with the actual values of any of the constants mentioned, and even then only in the fact that the two equations have the same form, regardless of what that form may be.
  • Figure 1 is a substantially vertical central sectional view of the entire -apparatus or so much thereof as is necessary to give an understanding of the invention.
  • Fig. 2 is a transverse vertical central sectional view of the apparatus designed to regulate the supply of air and water to the heating' means to furnish the required air and steam to the producer.
  • Fig. 3 is a sectional detail view, hereinafter referred to.
  • D is a cylindrical vessel supported by the shaft L on suitable bearings, preferably knife-edge,so as to rotate freely about its center through an arc of twenty or thirty degrees.
  • This vessel is provided with a slot in its circumference to admit the stationary water-pipe P.
  • O is antechnisch whose size can be controlled by a valve N.
  • W is a weight so placed on the circumference of the cylindcr as to be directly under the supporting'- shaft when the orifice O lies in the plane of water-level-vl.
  • Vanes H H are arranged to act as dashpots to steady the movement of the whole.
  • a Vane A is carried upon the extremity of a curved arm, so as to move freely and occupy a central position in the curved air-pipe T. As it has already been noted, this vane A and air-pipe T have been taken as one of the important means for carrying this invention into effect.
  • This cylinder D is supported by and carried within a semicylindrical housing' E, which is divided into two parts, one of which receives the drip from the overfiow K and discharges it through the opening' Cr into a waste-pipe (not shown) and another above and to the right, which receives the water discharged from the orifice O and conducts it through the opening into the air-pipe T.
  • C is a chamber through which pass the hot gases as the exhaust from the gas-engine, and which contains the hollow disks B, or it may be other extended heating-surfaces which contain and convey the air and water admitted into the air-pipe T.
  • the operation of theapparatus in carrying' out the process is as follows:
  • the valve M is opened and water is admitted to the interior of the cylinderD until it is filled to the height of the overfiow K, at which point the Water-level is maintained, thesurplus passing out of the overfiow to waste.
  • I/Vhen air is passed or is caused to pass through the apparatus, the vane Ais acted upon by the aircurrent passing through the pipe T.
  • Numerous experiments have demonstrated the action of air-currents on a vane so exposed to be of the following nature: LetP equal pressure exerted on the vane; V equal velocity of aircurrent; C equal a numerical constant; then P equals CVZ.
  • I claim- 1 The art ofsupplying steam and heated air to suction gas-producers, which consists in causing the air and water to be heated to pass through an air-tube, interposing a vane in said tube to be acted upon and moved by the air as well as to control the water-supply by its movements, and heating the air and converting the water into steam and supplying the steam and air to the producer, as set forth.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Description

PATENTBB MAR. 28, 1905.
H. E. SMITH. PROCESS OP REGULATING AIR AND STEAM SUPPLIED TO GAS PRODUCERS.
APPLICATION FILED JUNE 16.1904.
2 SHEETS-SHEET l.
WATER INLET L E V E L R E T m EXHAUST FROM As EN@ NE AmoaP'HsRE AIR AND ST6/u1 To PRoDureR NO- 786,061. PATPNTDD MAR.28. 1905.
H. P. SMITH. PROCESS 0F REGULATING AIR AND STEAM SUPPLIED To GAS PRODUCERS.v
APPLICATION FILED JUNE 16, 1904.
2 SHEETS-SHEET 2.
OVER now UNITED STATES Patented March 28, 1905.
HARRY F. SMITH, OF LEXINGTON, OHIO.
PROCESS 0F REGULATING AIR AND STEAM SUPPLIED TO GAS-PRODUCERS.
SPECIFICATION forming part of' Letters Patent No. 786,061, dated March 28, 1905.
Application filed June 16, 1904. Serial NO- 212,887.
To all whom, it may concern,.-
Beit known that I, HARRY F. SMITH, a citizen of the United States, residing at Lexington, in the county of Richland and State of Ohio, have invented new and useful Improvements in the Art or Process of Providing and Regulating the Air Supplied to the Producers of Suction Gas-Producers, of which the following is a specification.
This invention has relation to the art or process of providing and regulating the air supplied to the producer of suction gas-producers, so that the said air shall bear a constant percentage of moisture regardless of the actual quantity of air supplied or the rapidity with which this quantity may change to suit varying loads on the engine.
In the description of my improved method or process it becomes necessary to deal with the means employed or with some form of means in order that the method may be understood.
Inasmuch as by my invention I provide an improved process whereby the amount of steam or moisture in the air supplied to the producer is made or regulated to agree to all intents and purposes with the amount required whether the exact requirement at particular times varies or not, it is seen that I must deal to some degree with the machine itself or employ some parts ofthe machine as a tangible vehicle, whereby my improved art can be made effective.
' In another application for a patent of even date herewith I have shown, described, and claimed an apparatus for supplying steam and heated air to suction gas-producers, and I have chosen said machine to illustrate and describe my presentimprovements in the art, and, furthermore, in order to make my present improvements effective, and as it is ever tangible, I have also chosen to employ the functions of the air-tube and vane shown and described in said other application as the tangible things dealt with, and hence they are fully referred to without in their embodiment as mechanical features of the machine becoming any part of this invention. So, also, with other parts and features of this machine, while it may be deemed advisable to show and describe the process it is not in its constructive vnature made a part of this invention. Again, it is to be noted that equations of the form herein used are universally accepted by engineers and physicists in dealing with the quantities involved. The formulas used, it will be noted, are matters of no concern in this case excepting with respect to the form of the equations and not with the actual values of any of the constants mentioned, and even then only in the fact that the two equations have the same form, regardless of what that form may be.
Before proceeding to describe the mode of operation of this invention it may be well in order to give a clear understanding of the same to explain that in suction or aspirating gas-producers which are used for power-gas generation no storage of gas is attempted, the gas as made passing directly from the producer to the engine.
Since mixtures of producer-gas and air mixtures are explosive only over a very narrow range of possibilities, it is readily seen that even a very slight variation in the quality of gas furnished to the engine will cause a serious loss in the power of explosion and will frequently require a readjustment of air to gas. It therefore becomes apparent that great uniformity in the quality of gas to its requirements is necessary; but uniform gas cannot be made unless there is a uniform percentage of steam incorporated with the airblast to the furnace.
To maintain a uniform percentage of steam at varying loads on the engine, it is necessary that the supply of water from which the steam is generated should not only be proportioned to the load on the engine, but should vary quite as rapidly as the load changesthat is to say, the variation in the requirement should as quickly have a variation in effects to answer the requirement.
By long, careful, and intelligent experiments I have produced an important improvement in the art, as will appear from a description of the construction and operation of the apparatus or device shown in the accompanying drawings, forming' a part of this specification, which apparatus, based on the said experiments, does the work for which it is designed in a highly satisfactory manner and preserves the proper proportion of air to steam so nearly constant that no disturbance is observable in the operation of the producer.
In the said drawings, Figure 1 is a substantially vertical central sectional view of the entire -apparatus or so much thereof as is necessary to give an understanding of the invention. Fig. 2 is a transverse vertical central sectional view of the apparatus designed to regulate the supply of air and water to the heating' means to furnish the required air and steam to the producer. Fig. 3 is a sectional detail view, hereinafter referred to.
In the drawings, D is a cylindrical vessel supported by the shaft L on suitable bearings, preferably knife-edge,so as to rotate freely about its center through an arc of twenty or thirty degrees. This vessel is provided with a slot in its circumference to admit the stationary water-pipe P. An annular overffowoutlet, arranged as an annular opening K, surrounds the central supporting-shaft in such a manner that its lower edge shall be tangent to the same horizontal plane in whatever position the cylinder may be rotated about its supporting-shaft. O is an orice whose size can be controlled by a valve N. W is a weight so placed on the circumference of the cylindcr as to be directly under the supporting'- shaft when the orifice O lies in the plane of water-level-vl. c., the horizontal plane tangent to the lower edge of the overflow-orifice K. Vanes H H are arranged to act as dashpots to steady the movement of the whole. A Vane A is carried upon the extremity of a curved arm, so as to move freely and occupy a central position in the curved air-pipe T. As it has already been noted, this vane A and air-pipe T have been taken as one of the important means for carrying this invention into effect. This cylinder D is supported by and carried within a semicylindrical housing' E, which is divided into two parts, one of which receives the drip from the overfiow K and discharges it through the opening' Cr into a waste-pipe (not shown) and another above and to the right, which receives the water discharged from the orifice O and conducts it through the opening into the air-pipe T.
C is a chamber through which pass the hot gases as the exhaust from the gas-engine, and which contains the hollow disks B, or it may be other extended heating-surfaces which contain and convey the air and water admitted into the air-pipe T.
The operation of theapparatus in carrying' out the process is as follows: The valve M is opened and water is admitted to the interior of the cylinderD until it is filled to the height of the overfiow K, at which point the Water-level is maintained, thesurplus passing out of the overfiow to waste. I/Vhen air is passed or is caused to pass through the apparatus, the vane Ais acted upon by the aircurrent passing through the pipe T. Numerous experiments have demonstrated the action of air-currents on a vane so exposed to be of the following nature: LetP equal pressure exerted on the vane; V equal velocity of aircurrent; C equal a numerical constant; then P equals CVZ. Consequently since for small pressures and velocities quantity equals area fvV, quantity of air equals CK/P; but, similarly, considering the fiow of water through an orifice, quantity of water equals C"-/ H1 where H is the head of water above the orifice. Comparing these equations, (and perhaps we should before have noted that C C,ll C'" are differentnumerical constants.) we observe that if we made P equal C" H, then Q air equals CHH Q water, ("Qair and Q water meaning quantity of air and quantity of water) that is, if the head of water over an orifice is kept proportional to the pressure on the vane A then the flow of water through the orifice will always be proportional to the flow of air through the pipe T; but the pressure on the vane A is determined bythe resistance it offers to displacement c., by the resistance offered by the cylinder D to axial rotationsince if no resistance were offered to such movement the Vane would move with equal velocity with the air-current and no pressure would be exerted upon it. In this construction, however, the weight WV tends continuously to return the vane A to its original position, and hence determines the pressure on the vane A; but for any given displacement like that shown in the dotted lines the turning' moment exerted by W equals I/V/r where fr equals perpendicular distance from center of gravity of W to the vertical line through the center of rotation. This turning moment is balanced by that exerted by the vane A-viz. Pv"-where fr is the distance from the center of rotation to the center of pressure on A. Consequently fr equals Pfr', and since W and r are constants fr equals constant xP; but from the construction it is obvious that h the head of water over the orifice C---is proportional to fr. Consequently for this construction P equals constant XH, and for any rrate of flow of air such a displacement of the vane and attached cylinder will occur as to cause a proportional ffow of water from the orifice O. The actual quantity of waterdischarged per cubic foot of air can be regulated by the valve N. Since the water discharged at the orifice O is at once conveyed to the hot surfaces B and there entirely converted into steam, the percentage of moisture carried by the air to the producer willv be constant and remain constant regardless of the quantity of the air passing.
The exact arrangement need not of course be that shown. For instance, the gases discharged from the producer could be used instead of the exhaust. The water from the orifice O could be vaporized in a separate IOO chamber and afterward mixed with the air. However, the arrangement shown is desirable, since by the use of the exhaust considerable heat is returned to the producer that would be otherwise wasted. Y
It might be well to observe that in case it should be found that an exact proportion is not maintained, or if for any reason other than a direct proportion of water to air should be desired, suitable correction can be made or such other proportion secured by suitably Varying the area ofthe tube T at the several sections successively occupied by the vane A.
In view of the fact that I have already constructed and operated a machine of the type described and claimed in this case, and in View of the further fact that it is understood that I am not limited in the manufacture of my machine to the detailed dimensions stated, and that further disclosures in this regard are not essential in order to enable those skilled in the art to make and use the machine, but that it might be helpful to them in making a machine to avoid tedious experiments, it may be further stated that in the machine in use at present by me the dimensions are as follows: diameter of Vessel D, live and onehalf inches; diameter of orifice O, nine onehundredths of an inch; weight of weights WV, fourteen hundred and fifty grains; diameter of pipe T, two and eleven-sixteenths inches; diameter of vane A, two inches.
I claim- 1. The art ofsupplying steam and heated air to suction gas-producers, which consists in causing the air and water to be heated to pass through an air-tube, interposing a vane in said tube to be acted upon and moved by the air as well as to control the water-supply by its movements, and heating the air and converting the water into steam and supplying the steam and air to the producer, as set forth.
2. The art of supplying air to be heated and water to be converted into steam to be supplied to suction gas-producers, which consists in causing the air to pass through an airtube, interposing a vane in said tube to be acted upon and moved by the air as well as to control the water-supply by its movements, as set forth.
3. In the art of supplying steam and heated Y scribing witnesses.
HARRY F. SMITH. Witnesses:
A. B. BEvERsTocK, H. B. SowERs.
US21288704A 1904-06-16 1904-06-16 Process of regulating air and steam supplied to gas-producers. Expired - Lifetime US786061A (en)

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