US487639A - Process of elevating liquids - Google Patents
Process of elevating liquids Download PDFInfo
- Publication number
- US487639A US487639A US487639DA US487639A US 487639 A US487639 A US 487639A US 487639D A US487639D A US 487639DA US 487639 A US487639 A US 487639A
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- United States
- Prior art keywords
- pipe
- water
- air
- layers
- liquid
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- 239000007788 liquid Substances 0.000 title description 52
- 238000000034 method Methods 0.000 title description 28
- 230000003028 elevating Effects 0.000 title description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 100
- 239000010410 layer Substances 0.000 description 64
- 239000012530 fluid Substances 0.000 description 14
- 238000005086 pumping Methods 0.000 description 6
- 230000003292 diminished Effects 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- SXYIRMFQILZOAM-HVNFFKDJSA-N (3R,5aS,6R,8aS,9R,10S,12R,12aR)-10-methoxy-3,6,9-trimethyldecahydro-3,12-epoxypyrano[4,3-j][1,2]benzodioxepines Chemical compound C1C[C@H]2[C@H](C)CC[C@H]3[C@@H](C)[C@@H](OC)O[C@H]4[C@]32OO[C@@]1(C)O4 SXYIRMFQILZOAM-HVNFFKDJSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 230000000630 rising Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002356 single layer Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
- F04F1/00—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped
- F04F1/18—Pumps using positively or negatively pressurised fluid medium acting directly on the liquid to be pumped the fluid medium being mixed with, or generated from the liquid to be pumped
Definitions
- Tus Noam Perses oo. Pumau'mo., wAsmnamn D. c.
- the invention relates to the art of elevating water by compressed air; and it consists in improved processes and apparatus where'- by the compressed air is delivered in/fbulk int-o the lower end of the Water-eduction pipe and the water and air are caused/to ascend through said pipe in distinct alternate layers of definite dimensions.
- the object of the invention is to successfully and practically effect theelevation of the water to a much greater height than has heretofore been deemed economic with compressed air and to avoid the results due to an intimate commingling of the air and water, as well as to dispense with all valves, annular spaces, and solid pistons.
- the air is not directed into the water in the form of iine jets or bubbles, which would very readily commingle intimately with the water, but is delivered in mass, and the water and air ascend in welldened alternate layers through the ed uctionpipe.
- the drawings represent the apparatus in a state of action pumping water, the shaded sections within the eduction-pipe W representing waterlayers and the intervening blank spaces air layers.
- the pressure per square inch of column 1 is seen to be 1.74 pounds; that of 2, consisting of two columns or layers 1 and 2, each 4.02 feet long, to be 3.49 pounds, and that of 10, consistingof nine columns or layers of water 1 to 9, inclusive, each 4.02 feet long, and one of 3.80-viz., layer 10-feet in length to be 17.35 pounds, and the aggregate length of the layers of water is 39.98 feet in a total length of ninety-one feet of pipe.
- the length of pipe below the surface of the water in the well is 55.5 feet, and that the diierence between this and the aggregate length of the water layers (39.98) is 15.52 feet-that is, on equal area-s the pressure outside of the pipe is greater than the pressure on the inside by the weight due this difference of level, which is 47.65 pounds for the end of the discharge-pipe. It is this difference of 15.52 feet, acting as a head, that supplies the water-pipe, puts the contents ot' the pipe in motion, and overcomes the resistance in the pipe.
- the water layers are equal each to each, and the pressure upon any layer of air is due to the number of water layers above it.
- the enlargement at the lower end of the eduction-pipe I have found to be of advantage, not only as compensating for the space taken up by the air-pipe, but, where the mouth of the latter is well below the upper end of the enlargement, as facilitating the formation ot' bubbles sufficiently large to make the desired4 pipe-fitting piston-like layers, rapidly and continuously following each other at very short intervals in the flow up the eductionpipe.
- the fluid pressure is preferably diminished, as indicated hereinbefore. In practice I so reduce the pressure to a point below the weight of the column of liquid which, standing in the eduction-pipe above the point of entrance of the gaseous fluid, has been removed, as stated.
- the process which consists in submerging a portion of an open-ended eduction-pipe in a body ot' the liquid to be raised and continuously introducing into the liquid within the lower part of the pipe a series of bubbles of compressed gaseous iuid containing enough of the fluid to expand immediately across the pipe and iill the same from side to side, forming pipe-fitting piston-like layers at or just above the point of their entrance into the pipe, whereby the column of liquid rising in the pipe after the forcing out of the liquid first standing in the latter is subdivided by the gaseous fluid into small portions before it reaches the level of the liquid outside of the pipe, and a continuouslyupward-flowing series of well-defined alternate layers of gaseous duid and short layers of liquid is formed and forced up the pipe, substantially as and for the purpose specied.
- the process whlch consists in submerging a portion of an openended pipe in a body of the liquid to be raised, removing the upper portion of the column of liquid within the pipe and injecting into the latter at a point well below the level of the liquid in which the pipe is submerged gaseous duid in quantity sufficient to form bubbles, which will expand immediately across the pipe and iill the same from side to side and under pressure less than the weight of a column of liquid in the pipe extending from the point of entrance of the gaseous fluid to the level of the body of liquid surrounding the pipe, so that a continuous upward-moving series of alternate well-defined gaseous iiuid and liquid layers will be formed in and forced up the pipe, substantially as and for the purpose described.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Jet Pumps And Other Pumps (AREA)
Description
(No Model.)
J.G.VP0HLE.
PROCESS 0F ELEVATING LIQUIDS.
No.- 487,639. Patented Dec. 6, 1892.
G d, 9. W
Tus Noam: Perses oo. Pumau'mo., wAsmnamn D. c.
UNITED STATESl PATENT OFFICE.
JULIUS G. POHL, OF JERSEY CITY, NEIV JERSEY.
PROCESS 0F ELEVATING LIQUIDS.
SPECIFICATION forming part of Letters Patent No. 487,639, dated December 6, 1892.
Application filed October 24, 1891. Serial No. l09,701. (No model.)
Too/ZZ whom it may concern.-
Be it known that I, JULIUS G. POHL, a citizen of the United States,and a resident of Jersey City, in the county of Hudson and State of New Jersey,have invented a certain new and useful Process of Elevating Liquids, of which the following is a specification.
The invention relates to the art of elevating water by compressed air; and it consists in improved processes and apparatus where'- by the compressed air is delivered in/fbulk int-o the lower end of the Water-eduction pipe and the water and air are caused/to ascend through said pipe in distinct alternate layers of definite dimensions.
The object of the invention is to successfully and practically effect theelevation of the water to a much greater height than has heretofore been deemed economic with compressed air and to avoid the results due to an intimate commingling of the air and water, as well as to dispense with all valves, annular spaces, and solid pistons. In accordance with my invention the air is not directed into the water in the form of iine jets or bubbles, which would very readily commingle intimately with the water, but is delivered in mass, and the water and air ascend in welldened alternate layers through the ed uctionpipe.
'In the art of raising water by means of ej ectors it is essential to use a continuous and rapid current of steam or air, which by its velocity and momentum forms, primarily, a vacuum into which the water flows by suction. From thence it is secondarily drawn along by the induced velocity current of the steam or air thus used. In my process, which I term the air-lift process or method, it is not necessary to create a vacuum at all, nor is it necessary to use a velocity current for the purpose of raising water, for its action depends, primarily, upon the gravity force of the liquid into which an eduction-pipe is submerged, and, secondarily, it depends upon the elastic energy stored in compressed air when used in the manner to be described. I have discovered that when air of suitable pressure is allowed to enter in a constant stream and in suitable quantity into an eduction-pipe at or near its lower end when it is submerged in water, while its upper end rises above the water about the same distance that its lower end is submerged, the compressed air thus introd uced will at first expel the standing water from the pipe in an unbroken column free from air, and subsequently, bythe continued intlowing of the compressed air under a pressure just suflicient to overcome the resistance of the water outside of the eduction-pipe, it will arrange itself in alternate layers with "the water, while the latter flows into the lower end of the eduction-pipe by force of gravity until it is discharged at the upper or exitend of the pipe. This alternate interposition of determinate quantities of air between the also determinate quantities of water elongates the entire column of arand water, thus facilitating, without materially adding to the weight of the column, the discharge of the Water at a higher level than would be the case were these air sections or layers absent. I have also discovered that under the abovementioned conditions the compressed air will not escape through the water overlying it, and also that the water overlying the compressed air Will not fall back through the underlying air while both are in upward motion, but lind that the elasticity stored in the compressed-air layer, pressing alike in all directions, forms a temporary water-tight airpiston, which lifts the water above it to its final discharge without appreciable loss by leakage or so-called slippage, while this compressed-air piston after having expended its elastic energy in work of lifting water is dispelled with only a practically-unimportant loss of power. To elucidate this process of pumping more clearly, I will refer to the accompanying drawings, in Which-- Figure l illustrates a central vertical section of an apparatus embodying the invention; and Fig. 2, a like section, on an enlarged scale, of the lower ends of the air and discharge pipes, and in which- A B designate an Artesian well or its equivalent; S, the surface of the water-level; NV, an eduction-pipe submerged therein (being represented as three inches in diameter to correspond with the lengths and weights of the water and air layers) and having at its lower end the enlarged extension C, and @indicates the air conveying pipe, coming from any source of compressed air and terminating IOO wwith an upturned exit end within the enlargethe exit end of air-pipe a, and said end of said pipe a passes through the vertical side of the enlargement C, as shown, and derives support therefrom.
The drawings represent the apparatus in a state of action pumping water, the shaded sections within the eduction-pipe W representing waterlayers and the intervening blank spaces air layers.
At and before the beginning of pumping the level of the water is the same outside and inside of the discharge-pipe W-incidentally, also, in the air-pipe. Hence the vertical pressures per square inch are equal at the submerged end of the discharge-pipe. When, therefore, compressed air is admitted into the air-pipe a, it must tirst expel the incidental standing water before air can enter the eduction-pipe W. XVheu this has been accomplished, the air-pressure is maintained until the water within the @duction-pipe has been forced out, which it will be inone unbroken column, free from air-bubbles. When this has occurred, the pressure" of the air is lowered or its bulk diminished and adjusted to a pressure j ust sufficient to overcome the external water-pressure. Itis thus adjusted for the performance of regular and uniform work, which will ensue with the infiowing air and water, which adj ust themselves automatically in alternate layers or sections of definite lengths and weights. It will be seen in the drawings that the lengths of the water-columns (shaded) and air (blank spaces) 1 and l are entered at the right of the dischargepipe W'; also, that under the pressure of two layers of water 1 and 2 the length of the air column 2 is 6.71 feet long, and so on. The lengths of aggregate water columns and the air columns which they respectively compress are also entered on the right of the waterpipe. On the left of the water-pipe are entered the pressures per square inch of these water columns or layers. Thus the pressure per square inch of column 1 is seen to be 1.74 pounds; that of 2, consisting of two columns or layers 1 and 2, each 4.02 feet long, to be 3.49 pounds, and that of 10, consistingof nine columns or layers of water 1 to 9, inclusive, each 4.02 feet long, and one of 3.80-viz., layer 10-feet in length to be 17.35 pounds, and the aggregate length of the layers of water is 39.98 feet in a total length of ninety-one feet of pipe. It will be noted that the length of pipe below the surface of the water in the well is 55.5 feet, and that the diierence between this and the aggregate length of the water layers (39.98) is 15.52 feet-that is, on equal area-s the pressure outside of the pipe is greater than the pressure on the inside by the weight due this difference of level, which is 47.65 pounds for the end of the discharge-pipe. It is this difference of 15.52 feet, acting as a head, that supplies the water-pipe, puts the contents ot' the pipe in motion, and overcomes the resistance in the pipe. In general the water layers are equal each to each, and the pressure upon any layer of air is due to the number of water layers above it. Thus the pressure upon the bottom layer of air 10 in the drawings is due to all the layers of water in the pipe, (17.35 pounds,) and the pressure upon the uppermost layer of air 1 is due to the single layer of water I at the moment of its discharges beginning-viz., 1.74 pounds per square inch. As this discharge progresses this is lessened, until at the completion of 'the discharge of the water layer the air layer is of the same tension as the normal atmosphere.
The quantitative relations of the air to water are determinable, but vary with the relations of submergence to lift, diameter of pipe, temperature, and atmospheric pressure, and
range from 1.5 to more volumes of normal air,
compressed to an adequate pressure, for each volume of water raised by this process. The best efficiency is attained when the submersion is three-fifths of the total length of the eduction-pipe. Whatever the submergence or lift .may be, in order to secure the desired continuous upward flow of the contents of the ed notion-pipe without stoppage or downward dropping of the same it is necessary that the air as introduced into the pipe should be in quantity suicient to form, immediately upon its issue from the air-pipe bubbles which will expand across to fill the eduction-pipe from side to side and make distinct piston-like layers, entirely separating the portions of the water column between which they enter said pipe. Where the bubbles are smaller than this, they will pass up through the water, and, while necessarily elongating the water column, will not exert the positive elevating power that my pipe-filling air layers, entirely dividingthelayers of water from eachother, do.
The enlargement at the lower end of the eduction-pipe I have found to be of advantage, not only as compensating for the space taken up by the air-pipe, but, where the mouth of the latter is well below the upper end of the enlargement, as facilitating the formation ot' bubbles sufficiently large to make the desired4 pipe-fitting piston-like layers, rapidly and continuously following each other at very short intervals in the flow up the eductionpipe. When the bodyof water first standing in the eduction-pipe has been forced up out of the latter by the compressed gaseous fluid used, the fluid pressure is preferably diminished, as indicated hereinbefore. In practice I so reduce the pressure to a point below the weight of the column of liquid which, standing in the eduction-pipe above the point of entrance of the gaseous fluid, has been removed, as stated.
It is evident that the process above described is applicable to all other liquids besides Water-such as petroleum-oil, saline solutions, brewers and tanners liquors, sewage, dre-and therefore I do not limit the invention to the elevating of water. Neither do I confine the invention to compressed air alone for the purpose of raising liquids by this process, but claim any aeriform body, such as natural gas and steam when used in oily liquids.
What 1 claim as my invention, and desire to secure by Letters Patent, is-
1. As an improvement in the art of elevating liquid, the process which consists in submerging a portion of an open-ended eduction-pipe in a body ot' the liquid to be raised and continuously introducing into the liquid within the lower part of the pipe a series of bubbles of compressed gaseous iuid containing enough of the fluid to expand immediately across the pipe and iill the same from side to side, forming pipe-fitting piston-like layers at or just above the point of their entrance into the pipe, whereby the column of liquid rising in the pipe after the forcing out of the liquid first standing in the latter is subdivided by the gaseous fluid into small portions before it reaches the level of the liquid outside of the pipe, and a continuouslyupward-flowing series of well-defined alternate layers of gaseous duid and short layers of liquid is formed and forced up the pipe, substantially as and for the purpose specied.
2. As an improvement in the art of elevating liquid, the process which consists in submerging in the body of the liquid to be raised a portion of an open-ended eduction-pipe having an enlarged chamber on its lower end and continuously injecting into such enlargement well below its upper end gaseous fluid under pressure to form bubbles in the pipe above the enlargement large enough to extend across from side to side of the pipe proper and form pipe-fitting piston-like layers therein interposed between and entirely separating Well-dened layers of liquid in the pipe, substantially as and for the purpose described.
3. As an improvement in the art of elevating Water or other liquid, the process whlch consists in submerging a portion of an openended pipe in a body of the liquid to be raised, removing the upper portion of the column of liquid within the pipe and injecting into the latter at a point well below the level of the liquid in which the pipe is submerged gaseous duid in quantity sufficient to form bubbles, which will expand immediately across the pipe and iill the same from side to side and under pressure less than the weight of a column of liquid in the pipe extending from the point of entrance of the gaseous fluid to the level of the body of liquid surrounding the pipe, so that a continuous upward-moving series of alternate well-defined gaseous iiuid and liquid layers will be formed in and forced up the pipe, substantially as and for the purpose described.
Signed at New York, in the county of New York and State of New York, this 23d day of October, A. D. 1891.
J ULIUS G. POHLE.
Witnesses:
CHAS. C. GILL, ED. D. MILLER.
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US487639A true US487639A (en) | 1892-12-06 |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2571932A (en) * | 1946-03-16 | 1951-10-16 | Olsson Bengt | Apparatus for pumping viscou materials |
US3047004A (en) * | 1958-12-01 | 1962-07-31 | Vance C Sterrett | Proportioner and mixer, and tumbling differential for controlling the action thereof |
US4135364A (en) * | 1977-12-12 | 1979-01-23 | Busick Eugene D | Air lift pump energy conversion apparatus |
US5080560A (en) * | 1990-02-20 | 1992-01-14 | Leroy Jack W | Dryrite borehole dewatering system |
CN104937282A (en) * | 2013-01-18 | 2015-09-23 | 株式会社村田制作所 | Liquid lifting device and liquid lifting method |
US20150322970A1 (en) * | 2013-01-18 | 2015-11-12 | Murata Manufacturing Co., Ltd. | Pressurized liquid lifting device and liquid lifting method |
-
0
- US US487639D patent/US487639A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2571932A (en) * | 1946-03-16 | 1951-10-16 | Olsson Bengt | Apparatus for pumping viscou materials |
US3047004A (en) * | 1958-12-01 | 1962-07-31 | Vance C Sterrett | Proportioner and mixer, and tumbling differential for controlling the action thereof |
US4135364A (en) * | 1977-12-12 | 1979-01-23 | Busick Eugene D | Air lift pump energy conversion apparatus |
US5080560A (en) * | 1990-02-20 | 1992-01-14 | Leroy Jack W | Dryrite borehole dewatering system |
CN104937282A (en) * | 2013-01-18 | 2015-09-23 | 株式会社村田制作所 | Liquid lifting device and liquid lifting method |
US20150322970A1 (en) * | 2013-01-18 | 2015-11-12 | Murata Manufacturing Co., Ltd. | Pressurized liquid lifting device and liquid lifting method |
US20150322969A1 (en) * | 2013-01-18 | 2015-11-12 | Murata Manufacturing Co., Ltd. | Liquid lifting device and liquid lifting method |
US9316235B2 (en) * | 2013-01-18 | 2016-04-19 | Murata Manufacturing Co., Ltd. | Pressurized liquid lifting device and liquid lifting method |
US9512857B2 (en) * | 2013-01-18 | 2016-12-06 | Murata Manufacturing Co., Ltd. | Liquid lifting device and liquid lifting method |
CN104937282B (en) * | 2013-01-18 | 2017-10-24 | 株式会社村田制作所 | Pumping device and liquid pumping method |
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