US2489887A - Rotary pump - Google Patents

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US2489887A
US2489887A US682827A US68282746A US2489887A US 2489887 A US2489887 A US 2489887A US 682827 A US682827 A US 682827A US 68282746 A US68282746 A US 68282746A US 2489887 A US2489887 A US 2489887A
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gas
impellers
casing
pump
outlet
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Carl R Houghton
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ROOTS CONNERSVILLE BLOWER CORP
ROOTS-CONNERSVILLE BLOWER Corp
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ROOTS CONNERSVILLE BLOWER CORP
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C29/00Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
    • F04C29/04Heating; Cooling; Heat insulation
    • F04C29/042Heating; Cooling; Heat insulation by injecting a fluid

Description

Filed July 11, 1946 2 Sheets-Sheet l FI I- I N V E TOR.
1) [d n/ml -A TTORNE Y3 Patented Nov. 29, 1949 ROTARY PUMP Carl R. Houghton, Connersville, Ind., assignor to Roots-Connersville Blower Corporation, Connersville, Ind.-, a corporation of Indiana Appllcatlon July 11, 1946, Serial No. 682,827
18 Claims.
This invention relates to apparatus for the compression of air or other gas, and more particularly to rotary positive displacement pumps or boosters for handling hot gases.
It is an object of this invention to provide rotary positive displacement pumps or boosters equipped with impellers having small operating clearances in which the proper operating clearances are maintained when handling hot gases, such that the pumps can successfully and emciently handle hot gases.
Another object of this invention is to cool the impellers by introducing gas of a lower temperature into the gas being displaced by the pumps in order to maintain such proper operating clearances.
Another object of this invention is the provision of ports for introducing cooling gas in direct contact with the impellers, which ports are so located that the rotating impellers will act as valves to admit the cooling gas at the proper time for eiTective cooling without loss of emciency of the pumps.
It is a still further object of this invention to utilize gas being handled to control the temperature of impellers and casings in such a manner that circulation of gas for temperature control is obtained without the use of additional outside energy.
Other objects and advantages of the invention will be apparent from the following description, the accompanying drawings, and the appended claims.
Rotary positive displacement pumps or boost ers usually comprise two multilobed impellers rotating within a surrounding casing. The two impellers are mounted on parellel shafts which are geared together'so that the impellers rotate in opposite directions. The contour and finish of the impellers and the accuracy of cut of the gears is such that 'a small, substantially gas-tight operating clearance of a few thousands of an inch or less is maintained between the impellers as they rotate. The surrounding casing has semicylindrical sides conforming to the paths de-- scribed by the ends of the impeller lobes and is otherwise so shaped that a small, substantially gas-tight operating clearance of a few thousands of an inch or less is provided between the sides and the ends of the casing and the rotating impellers.
As the impellers revolve gas flows through a gas inlet into pockets formed by adjacent lobes of each impeller and the surrounding casing, is trapped in the pockets, is carried to a gas outlet,
and is forced positively into a discharge pipe. During each complete revolution of the impellers this action is repeated a number of times equal to the total number of impeller lobes. At high impeller speeds this results in a practically constant flow of gas without surging.
In many cases it is edsirable to use gas pumps of the rotary positive displacement type for high pressures, with corresponding high heat due to the heat of compression. Highly heated gas is also encountered at lower ratios of compression when initially hot gas must be handled, the problem frequently arising of handling gases initially at 400 F. up to F. When handling hot gases with compressors of the reciprocating type it is customary to water-jacket the cylinder to avoid overheating, and to provide the piston with snap rings which expand or contract as necessary to make close contact with the cylinder. Temperature differences between the cylinder and piston, resulting in unequal expansions, are not such a serious problem with that type of construction because of the tolerances permitted by the use of snap rings. 1
With rotary displacement pumps of the type described no satisfactory way to provide snap rings or the equivalent has been devised. Such rotary positive displacement pumps must be designed for operation with very small operating clearances between coacting impellers, and between impellers and the surrounding casing in order to provide substantially gas-tight seals against slip of gas through the pump wtih resultant loss of efliciency. change as a result of the impellers reaching an appreciably higher temperature than the surrounding casing, the impellers may strike each other or the casing and failure or serious damage to the pump may result. Therefore, waterjacketing of the casing of such rotary pumps without cooling the impellers is a distinct hazard. Nevertheless such rotary pumps have many advantages. For example, the absence of sliding or wearing contacts within the casing makes it unnecessary to have lubricants in contact with the gas being handled, and there are no valves, springs, or similar small parts to fail or require adjustment or replacement. The gas is delivered without surging and is uncontaminated by lubricants or other pump liquids.
In accordance with this invention provision is made for introducing gas of a lower temperature into the casing in direct contact with the impellers in order to prevent overheating of the impellers and to maintain a substantially uniform If these clearances temperature. Preferably this cooling gas is obtained by withdrawing gas from the high pressure outlet side of the pump, passing it through a gas cooler, and then introducing the cooled gas into the gas being displaced from the low pressure inlet side of the pump to the outlet side. It has been found that, when the cooling gas is introduced at the proper place in the pump in proper relation with the rotation of the impellers, the difference in pressures between the gas being displaced within the pump and the gas at the outlet side of the pump will produce the desired flow of gas without material loss of emciency of the pump, and without the necessity of using any substantial additional power. Provision is also made for using the motion of the impellers to control the flow of cooling gas so that it is introduced at the proper times in proper coordination with the pump operation and with a, minimum of auxiliary mechanism.
Since the casing surrounding the pump impellers would normally be cooled b the surrounding atmosphere as well as by the cooling gas introduced, it would, tend to reach a temperature sufliciently below that of the impellers where the discharged gas was in a highly heated condition to cause the diificulties with loss of clearances as discussed above. Therefore provision is preferably made for circulating gas around the casing at suflicient temperature to maintain the casing at a temperature comparable with that of the impellers such that the small operating clearances are maintained sufficiently unchanged, or the temperatures of the casing and the impellers are correlated in such a way that this eifect is obtained. Preferably turbulence in the outlet gas resulting from the pumping action of the impellers is used to cause circulation of outlet gas around the casing within a suitable casing jacket. Except in unusual cases this will maintain the casing at the proper temperature, and more positive means of heating will not be necessary.
Reference is made to the drawings which illustrate preferred embodiments of the invention, and in which like parts are designated by the same numerals.
Fig. 1 is a side elevation, partially in section, of a rotary displacement pump for compressing hot gases constructed in accordance with the present invention, the section being taken on the line l-l of Fig. 3;
Fig. 2 is a top view, partially in section, of a part of Fig. 1, showing how the impeller shafts are ared together;
Fig. 3 is a vertical sectional view on. the line 33 of Fig. 1;
Fig. 4 is another vertical sectional view of the casing shown in Fig. 3, with the section taken on line 44 of Fig. 1;
Figs. 5 and 6 are vertical sectional views of the impellers and impeller casing of a modified pump construction Fig. 7 is an end view of the pump shown in Figs. 5 and 6 drawn to a different scale; and
Figs. 8 and 9 are vertical sectional views of the impellers and impeller casing of a pump having two-lobed impellers instead of the three-lobed impellers previously shown, illustrating application of the invention to this type of pump.
The rotary pump shown in Figs. 1 to 4 is of symmetrical construction about a plane passed midway between the two impeller shafts l0 and H, perpendicular to a plane passed through the axes of the two shafts. The construction shown in Fig. 1, in which only shaft It can be seen, ap-
piles as well to the opposite side of the pump, with the exception that shaft I0 is driven by suitable means, such as an electric motor l2, whereas shaft H is driven by shaft l0. Shafts l0 and II are supported by bearings 13 and are geared together by gears, such as the herringbone gears indicated at I4, so that they turn in opposite directions at the same speed of rotation. Mounted on shafts I0 and H are two coacting three-lobed impellers I5 and I6. These impellers are of suitable contour, such as involute or cycloldal design. and interfit with each other in such manner that a very small and substantially gas-tight operating clearance is maintained between them in all positions of rotation. Surroundin the impeller is a casing i1, provided with semicylindrical sides It which conform to the paths described by the ends of the impeller lobes, in which the impellers rotate with a very small operating clearance so that a substantially gas-tight fit is provided. The casing is provided with packing glands is and 20 to form a gas-tight fit around the shafts ill and l i. As the impellers rotate, a part of the gas in gas inlet opening 2| is trapped in gas pockets such as 22 and 23, formed by two adjacent impeller lobes and the surrounding case, and is carried around by the rotation of the impellers and forced into the high pressure gas outlet opening 26. Compression of the gas carried forward occurs as it is forced into space 24.
Ports 25 and 26 are provided in the semicylindrical sides I8 0f the casing for introducing gas of a higher pressure and lower temperature into the gas pockets between impeller lobes in direct contact with the impellers. Each port is located approximately 120 degrees of an impeller revolution from the edge of the gas inlet opening 2! so that it is opened to a gas pocket immediately after the pocket is closed off from the gas inlet. In Fig. 3 impeller I5 is shown just as it is closing gas pocket 22 off from the gas inlet 2i and opening it to port 25. Impeller I6 is shown at a later point in its revolution after the gas pocket 23 has been opened to port 2 6.
The cooling gas to be introduced into the gas pockets may be from any source which is at a higher pressure than the gas in the pocket and is at a sufliciently low temperature to have the required cooling effect on the impellers. It will usually be of the same composition as the gas entering through gas inlet 2|, but in some circumstances need not be. Preferably it is gas withdrawn from the outlet side of the pump, since this gas is already at a higher pressure than the gas in the gas pockets. As shown in Fig. 3 gas may be withdrawn from the outlet gas manifold '21 through pipes 28 and 29, passed through gas coolers, indicated diagrammatically at 30 and 3|, to reduce its temperature the required amount,
50 and introduced into the gas pockets through ports 25 and 2B. The gas coolers 30 and 3| may be of suitable design, such as the shell and tube type in which cooling fluid such as water is circulated through a bank of pipes and the gas to be cooled is passed around the outside of the pipes, and should be of adequate capacity to give the desired cooling eifect.
The gas in the gas pockets is initially at substantially the pressure of the inlet gas. Introduction of gas from the outlet side of the pump will raise the pressure in the gas pockets somewhat but the withdrawal of gas from the discharge manifold 21 is in relatively small quantity compared with the total discharge of the pump and does not materially reduce the output pressure. Since the impellerrotate at high speed and one pocket is being discharged into the gas outlet while another pocket is receiving gas through its gas port from the outlet gas, any pulsation of pressure in the outlet gas is negligible. There need be no overall loss of pump efliciency so long as the ports are located as described so that gas from the gas outlet cannot escape back into the gas inlet.
Also shown in Figs. 1, 3, and 4 is a jacket 32 surrounding the casing II. This may extend around both sides and the remainder of the casing as shown, or may extend around the semicylindrical sides l8 only, depending upon the temperature conditions which are encountered. The jacket provides a space within which a heating fluid may .be circulated around the casing to heat the casing to a temperature which is of the same order as, and preferably slightly higher than, the temperature of the impellers. In this way undesirable cooling, or irregular temperature conditions of the casing, are prevented and the temperatures of the casing and of the impellers may thus be controlled so that the casing may always be heated sufilciently relative to the impellers to insure maintenance of the desired operating clearances and prevent undue expansion of impellers relative to each other and relative to the casing. While it is preferable that the casing be maintained at a higher temperature. than the impellers, it is not desirable to have a large differential in temperature as the clearances would then become excessive. In some cases it may be suflicient to rely entirely on the jacket to maintain said casing at a temperature correlated to that of the impellers such that the required small operating clearances are maintained, and not provide for introducing cooling gas into the gas pockets.
The fluid circulated through the jacket may be any inert gas or liquid of suitable temperature. Preferably, however, the outlet gas from the pump is used to keep the casing at the required temperature. This may be done readily by providing openings 33 from the top of the jacket space into'the gas outlet space 24 immediately above the impellers. At this .point sufficient turbulence is created by the impellers to cause the gas to circulate through the jacket. In most. cases no other openings need be provided into or out of the jacket space. However, in some cases .it may be found desirable to connect the bottom of the jacket space to a subsequent part of the high pressure gas manifold by means of pipes, in order to obtain an increased circulation of gas. The temperature of the casing is preferably maintained at about the same tempera-, ture as the impellers so the same amount of expansion will take place in both.
Referring to Figs. 5, 6, and 7, a modification is shown in which cooling gas is admitted into the gas pockets through ports in the ends of the casing instead of through the semicylindrical sides as previously shown. Gas is withdrawn from the gas outlet side of the pump through pipe 40, passes through gas cooler 41, and the cooled gas passes through pipe 42 and into the gals pockets through ports 43 and 44. Cooling fluid, such as water, is circulated through the cooler in the usual manner through pipes 45 and 48. When the impellers are in the position pocket, with resultant cooling of the impeller l5. When the impellers have rotated a part of a revolution to the position shown in Fig. 6, port 44 is commencing to close and port 43 is commencing to open. Momentarily, gas pockets 41 and 48 are connected through pipe 42. Since gas pocket 48 has assumed a pressure approaching that of gas outlet 24, whereas gas pocket 41 contains gas at the lower'pressure of gas inlet 2|, gas will pass from gas pocket 48 to gas pocket 41 without passing through the cooler 4!. However, this condition is of such short duration that it does not seriously interfere with the desired flow of cooling gas to the impellers. Therefore, it is practicable to use a single gas cooler,
whereas the use of a single cooler in the ar-' rangement shown in Fig. 3' would be less desirable because, when the ports are located in the semicylindrical sides of the casing, the ports are simultaneously open for an appreciable time. Another advantage to locating the ports in the ends of the casing is that the cooling gas is admitted in a more favorableposition for cooling the impellers with less cooling of the casing sides.
However, it may sometimes be desirable to use both the above modification and the previously described arrangement shown in Fig. 3 on the same pump, in order to admit cooling gas to the impeller at several points and obtain greater cooling effect.
Figs. 8 and 9 show how the invention may be adapted to a rotary displacement pump having two-lobed impellers. With the usual design of impellers and easing shown it will be necessary to locate the ports 50, 5| for admitting cooling gas quite near to the high pressure outlet side of the pump 24, in order to avoid flow of high pressure gas backward through the pump and into the'lower pressure space 2|. Nevertheless there is'ashort interval of time during which a port will be open into a gas pocket before the gas pocket is open directly to the high pressure gas space 24, as will be apparent by comparing Figs. 8 and 9, which show successive impeller positions. It would appear that the moment an impeller rotates to the position on the right of Fig. 9 there would be an instantaneous rush of gas from the space 24 into the advancing impeller pocket, but oscillograph readings show that there is a time lag and this would appear to provide for more effective functioning of ports 50, 5| than is indicated by Figs. 8 and 9. The interval of time will be suflicient to start a rush of cooling gas into'a gas pocket and materially assist in prevent overheating of the impellers.
If this usual design of two-lobed impeller pump is modified, as by providing for the cylindrical sides of the casing to follow the path of the ends of the impellers for a greater distance, it is possible to increase the interval of time between opening of the gas pocket to the cooling gas and opening of the gas pocket to the gas space 24. The ports for cooling gas can also be arranged in the ends of the casing, as illustrated inFigs. 5, 6, and 7, but with two-lobed impellers the ports will usually have to be located close to the gas space 24 for the reasons discussed above.
While the forms of apparatus described and illustrated constitute preferred embodiments of the invention,'it is to be understood that the invention is not limited to these precise forms of apparatus, and changes may be made therein without departing from the scope of the invention as defined in the appended claims.
What is claimed is:
l. A gas pump of the rotary displacement type for handling hot gases comprising a casing having a gas inlet and a gas outlet, a plurality of multilobed rotary interfitting impellers rotatably mounted in said casing with a small operating clearance between said impellers providing-a substantially gas-tight seal and adapted to displace gas from said gas inlet to said gas outlet when rotated, and means for introducing cooling gas into said casing in direct contact with said impellers to prevent overheating of said impellers and to maintain said small operating clearance therebetween.
2. A gas pump of the rotary displacement type for handling hot gases comprising a casing having a gas inlet and a gas outlet, a plurality of multilobed rotary interfitting impellers rotatably mounted in said casing with a small operating clearance providing a substantially gas-tight seal and adapted to displace gas from said gas inlet to said gas outlet when rotated, means for introducing cooling gas into said casing in direct contact with said impellers to prevent overheating of said impellers, and means for circulating higher temperature gas around said casing to maintain said casing at a temperature comparable with that of said impellers such that said small operating clearance is maintained.
3. A gas pump of the rotary displacement type for handling hot gases comprising a casing having a gas inlet and a gas outlet, a pair of multilobed rotary interfitting impellers rotatably mounted in said casing with a small operating clearance between said impellers providing a substantially gas-tight seal and adapted to displace gas from said gas inlet to said gas outlet when rotated, a gas cooler, and means for passing gas from said gas outlet through said gas cooler and into said casing in direct contact with said im pellers to prevent overheating of said impellers and to maintain said small operating clearance therebetween.
4. A gas pump of the rotary displacement type for handling hot gases comprising a jacketed casing having a gas inlet and a gas outlet, a plurality of multilobed rotary interfitting impellers rotatably mounted in said casing with a small operating clearance between said casing and said impellers providing a substantially gas-tight seal and adapted to displace gas from said gas inlet to said gas outlet when rotated, and means for circulating heated gas from said gas outlet through said jacket to maintain said casing at an increased temperature comparable with that of said impeller means such that said small operating clearance is maintained.
5. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to provide a small and substantially gastight operating clearance between said impellers in all positions, a casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and displace the trapped gas into said gas outlet as said impellers rotate, and means for introducing cooling gas into said gas pockets to prevent overheating of said impellers and to maintain said small operating clearance between said impellers.
6. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to provide a small and substantially gastight operating clearance between said impellers in all positions, a casing provided with a gas inlet and a gas outlet and having substantially semicylindircal sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and displace the trapped gas into said gas outlet as said impellers rotate, a source of gas of lower temperature and higher pressure than the gas at said gas inlet, said casing having ports for introducing said lower temperature gas into said gas pockets to prevent overheating of said impellers and to maintain said small operating clearance between said impellers, and means for conducting said lower tempcrature gas from said source to said ports.
'7. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to provide a small and substantially gastight operating clearance between said impellers in all positions, a casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and displace the trapped gas into said gas outlet as said impellers rotate, a source of gas of lower temperature and higher pressure than the gas at said gas inlet, the semicylindrical sides of said casing having ports for introducing said lower temperature gas into said gas pockets to prevent overheating of said impellers and to maintain said small operating clearance between said impellers, and means for conducting said lower temperature gas from said source to said ports.
8. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to provide a small and substantially gastight operating clearance between said impellers in all positions, a casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and displace the trapped gas into said gas outlet as said impellers rotate, a source of gas of lower temperature and higher pressure than the gas at said gas inlet, said casing having ports located adjacent to said semicylindrical sides for introducing said lower temperature gas into said gas pockets to prevent overheating of said impellers and to maintain said small operating clearance between said impellers, and means for conducting said lower temperature gas from said source to said ports.
9. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to provide a small and substantially gastight operating clearance between said impellers in all positions, a casing provided with a gas inand the surrounding casing adapted to trap gas A at said gas inlet and displace the trapped gas into said gas outlet as said impellers rotate, said casing having ports for introducing gas into said gas pockets, a gas cooler, means for conducting gas from said gas outlet to said gas cooler to cool said gas, and means for conducting said cooled gas from said gas cooler to said ports and into said gas pockets to prevent overheating of said impellers and to maintain said small operating clearance between said impellers.
10. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to provide a small and substantially gastight operating clearance between said impellers in all positions, a casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotatin impellers surrounding said impellers with a, small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and displace the trapped gas into said gas outlet as said impellers rotate, said casing having ports adjacent said semicylindrical'sides of said casing of such size and so located that said ports are closed during the rotation of said impellers except during the time when said gas pockets are closed off from said gas inlet and from said gas outlet, said ports being open to substantially only one gas pocket at a time, a gas cooler, means for conducting gas from said gas outlet to said gas cooler to cool said gas, and means for conducting said cooled gas from said gas cooler to said ports and into said gas pockets to prevent overheating of said impellers and to maintain said small operating clearance between said impeller.
11. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to provide a small and substantially gastight operating clearance between said impellers in all positions, a casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and displace the trapped gas into said gas outlet as said impellers rotate, means for introducing cooling gas into said trapped gas to prevent overheating of said impellers, and means for circulating heating gas around said casing to maintain said casing at a temperature relative to said impellers which will maintain said small clearances.
12. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers l l0 coacting to maintain a small and substantially gas-tight operating clearance between said impellers in all positions, a jacketed casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and to displace said trapped gas from said gas inlet to said gas outlet as said impellers rotate, a gas cooler, means for conducting gas from said gas outlet to said gas cooler to cool said gas, means for conducting said cooled gas from said gas cooler through said casing and into said gas pockets to prevent overheating or said impellers, and means for circulating gas from said gas outlet around said casing within said casing jacket to maintain said casing at a, temperature comparable with that of said impellers such that said small operating clearances are maintained.
13. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to maintain a small and substantially gas-tight operating clearance between said impellers in all positions, a jacketed casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described 'by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and to displace said trapped gas from said gas inlet to said gas outlet as said impellers rotate, a gas cooler, means for conducting gas from said gas outlet to said gas cooler to cool said gas, means for conducting said cooled gas from said gas cooler through said casing and into said gas pockets to prevent overheating of said im ellers, said casing jacket having openings into said gas outlet providing for circulation of gas from said gas outlet around said casing within said jacket to maintain said casing at a temperature comparable with that of said impellers such that said small operating clearances are maintained.
14. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to maintain a small and substantially gas-tight operating clearance between said impellers in all positions, a jacketed casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conform ng to the paths described by the ends of the lobes of said rotating impellers surrounding sa d impellers with asmall and substantiallv gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and to displace said trapped gas from said gas inlet to said gas outlet as said im ellers rotate, and means for circulating gas around said casing within said casing jacket to maintain said casing at a temperature correlated to that of said impellers such that said small operating clearance between said impellers and said cas ng is maintained.
gas-tight operating clearance between said impellers in all positions, a jacketed casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and to displace said trapped gas from said gas inlet to said gas outlet as said impellers rotate, and means for circulating gas from said gas outlet around said casing within said casing jacket to maintain said casing at a temperature correlated to that of said impellers such that said small operating clearance between said impellers and said casing is maintained.
16. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to maintain a small and substantially gas-tight operating clearance between said impellers in all positions, a jacketed casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and to displace said trapped gas from said gas inlet to said gas outlet as said impellers rotate, said casing jacket having openings into said gas outlet providing for circulation of gas from said gas outlet around said casing within said jacket to maintain said casing at a temperature correlated to that of said impellers such that said small operating clearance between said impellers and said casing is maintained.
17. A gas pump of the rotary displacement type for handling hot gases comprising a pair of oppositely rotating multilobed interfitting impellers coacting to maintain a small and substantially gas-tight operating clearance between said impellers in all positions, a jacketed casing provided with a gas inlet and a gas outlet and having substantially semicylindrical sides conforming to the paths described by the ends of the lobes of said rotating impellers surrounding said impellers with a small and substantially gas-tight operating clearance, gas pockets defined by adjacent lobes of said impellers and the surrounding casing adapted to trap gas at said gas inlet and to displace said trapped gas from said gas inlet to said gas outlet as said impellers rotate, said casing jacket having openings into said gas outlet so located that turbulence created by the rotation of said impellers causes circulation of gas from said gas outlet around said casing within said jacket and maintains said casing at a temperature comparable to that of said impellers such that said small operating clearance between said impellers and said casing is maintained.
18. A gas pump of the rotary displacement type comprising a casing having a gas inlet and a gas outlet, a plurality of multilobed interfitting rotary impellers rotatably mounted in said casing with a small operating clearance providing a substantially gas-tight seal adapted to displace gas from said gas inlet to said gas outlet when rotated with resulting increase in the temperature of the gas, means for introducing a cooling fluid into said casing in direct contact with said impellers to lower the temperature thereof, and means for applying heat to said casing to raise the temperature thereof toward that of said impeller means to provide for maintaining said small operating clearance.
CARL R. HOUGHTON.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,058,646 Tomlinson Apr. 8, 1913 1,475,683 Carrey Nov. 27, 1923 1,558,639 Schmied Oct. 27, 1925 1,893,171 Kagi 'Jan. 3, 1933 FOREIGN PATENTS Number Country Date 313,815 Italy Jan. 9, 1934 664,937 Germany Sept. 13, 1938
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Cited By (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2697402A (en) * 1950-09-15 1954-12-21 Arthur E Lindquist Impeller construction for rotary pressure pumps
US2906448A (en) * 1954-10-28 1959-09-29 W C Heraus G M B H Roots type vacuum pumps
US3059835A (en) * 1960-01-12 1962-10-23 Gen Motors Corp Rotary blower
US3121529A (en) * 1962-05-02 1964-02-18 Polysius Gmbh Blower
US3180569A (en) * 1962-05-21 1965-04-27 Gast Mfg Corp Cooled rotary pump
US3430848A (en) * 1966-02-23 1969-03-04 Plessey Co Ltd Rotary-displacement compressors
US3531227A (en) * 1968-07-05 1970-09-29 Cornell Aeronautical Labor Inc Gear compressors and expanders
US4215977A (en) * 1977-11-14 1980-08-05 Calspan Corporation Pulse-free blower
JPS59115489A (en) * 1982-12-23 1984-07-03 Unozawagumi Tekkosho:Kk Counter-flow cooling system multistage root type vacuum pump
JPS62157289A (en) * 1985-12-29 1987-07-13 Anretsuto:Kk Roots blower for high vacuum
JPS63154884A (en) * 1986-12-18 1988-06-28 Unozawagumi Tekkosho:Kk Inner branch flow/counter flow cooling type multi-stage roots vacuum pump
DE3726683A1 (en) * 1987-08-11 1989-02-23 Rietschle Masch App Roots vacuum pump
WO1989004924A1 (en) * 1987-11-16 1989-06-01 Weinbrecht John F High ratio recirculating gas compressor
JPH01113183U (en) * 1988-05-25 1989-07-31
US4995796A (en) * 1988-09-05 1991-02-26 Unozawa - Gumi Iron Works, Ltd. Multi-section roots vacuum pump of reverse flow cooling type
US5090879A (en) * 1989-06-20 1992-02-25 Weinbrecht John F Recirculating rotary gas compressor
EP0506189A1 (en) * 1991-03-28 1992-09-30 Grasso's Koninklijke Machinefabrieken N.V. Rotary compressor
US5173041A (en) * 1990-09-21 1992-12-22 Ebara Corporation Multistage vacuum pump with interstage solid material collector and cooling coils
US5273412A (en) * 1991-03-28 1993-12-28 Grasso's Koninklijke Machinefabrieken N.V. Lubricated rotary compressor having a cooling medium inlet to the delivery port
EP0447716B1 (en) * 1990-03-22 1995-08-02 The Nash Engineering Company Two-stage pumping system
US5702240A (en) * 1995-05-05 1997-12-30 Tuthill Corporation Rotary positive displacement blower having a diverging outlet part
WO1998027341A1 (en) * 1996-12-16 1998-06-25 Zhangqiu Blower Factory, Shandong New structure of roots blower or roots vacuum pump with a multi-lobes impeller and a reverse flow unit
US6176693B1 (en) * 1997-03-17 2001-01-23 Finder Pompe S.P.A. Volumetric blower with covers having a duct for connection to the delivery manifold
US6203297B1 (en) * 1999-09-29 2001-03-20 Dresser Equipment Group, Inc. Fluid flow device with improved cooling system and method for cooling a vacuum pump
US6312240B1 (en) * 1999-05-28 2001-11-06 John F. Weinbrecht Reflux gas compressor
CN1094174C (en) * 1997-11-20 2002-11-13 山东省章丘鼓风机厂 Multi-blade type impeller Roots blower (pump) structure with counter-flow device
US20040228752A1 (en) * 2002-08-28 2004-11-18 Dieter Peters External gear pump with pressure fluid pre-loading
US7226280B1 (en) * 2006-06-01 2007-06-05 Anlet Co., Ltd. Roots vacuum pump
US20070274842A1 (en) * 2006-05-26 2007-11-29 Clifford Howard Campen Subsea multiphase pumping systems
US20080181803A1 (en) * 2007-01-26 2008-07-31 Weinbrecht John F Reflux gas compressor
US20090004039A1 (en) * 2005-12-27 2009-01-01 Tetsushi Ohtsuka Single Stage Root Type-Vacuum Pump and Vacuum Fluid Transport System Employing the Single Stage Root Type-Vacuum Pump
US20110300014A1 (en) * 2010-06-08 2011-12-08 Paul Xiubao Huang Rotary lobe blower (pump) or vacuum pump with a shunt pulsation trap
US20120020824A1 (en) * 2010-07-20 2012-01-26 Paul Xiubao Huang Roots supercharger with a shunt pulsation trap
US20120171069A1 (en) * 2011-01-05 2012-07-05 Paul Xiubao Huang Screw compressor with a shunt pulsation trap
CN102878084A (en) * 2012-08-04 2013-01-16 百事德机械(江苏)有限公司 Counter flow cooling structure of single-stage negative-pressure roots blower
US9140261B2 (en) 2011-03-14 2015-09-22 Hi-Bar Blowers, Inc. Shunt pulsation trap for cyclic positive displacement (PD) compressors
US9243557B2 (en) 2011-09-17 2016-01-26 Paul Xiubao Huang Shunt pulsation trap for positive displacement (PD) internal combustion engines (ICE)
US9551342B2 (en) 2014-05-23 2017-01-24 Paul Xiubao Huang Scroll compressor with a shunt pulsation trap
US9683521B2 (en) 2013-10-31 2017-06-20 Eaton Corporation Thermal abatement systems
US9732754B2 (en) 2011-06-07 2017-08-15 Hi-Bar Blowers, Inc. Shunt pulsation trap for positive-displacement machinery
US20170241327A1 (en) * 2014-04-30 2017-08-24 Edward Charles Mendler, III Supercharger Cooling Means
US9758320B2 (en) 2012-03-21 2017-09-12 Maricap Oy Method and apparatus for treating the outlet air of a pneumatic waste conveying system
USD816717S1 (en) 2014-08-18 2018-05-01 Eaton Corporation Supercharger housing
US20180135631A1 (en) * 2015-09-15 2018-05-17 Gree Electric Appliances, Inc. Of Zhuhai Screw Compressor and a Compressor Body Thereof
US20220145885A1 (en) * 2020-11-12 2022-05-12 Ingersoll-Rand Industrial U.S., Inc. Positive displacement roots blower noise suppression

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1058646A (en) * 1907-01-12 1913-04-08 Allis Chalmers Condenser air-pump.
US1475683A (en) * 1919-08-02 1923-11-27 Carrey Rotory Engine Company Rotary air compressor
US1558639A (en) * 1923-07-27 1925-10-27 Schmied Walther Rotary machine
US1893171A (en) * 1930-11-17 1933-01-03 Sulzer Ag Rotary compressor
DE664937C (en) * 1935-03-09 1938-09-13 Becker Otto Rotary piston compressor with air-cooled housing

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1058646A (en) * 1907-01-12 1913-04-08 Allis Chalmers Condenser air-pump.
US1475683A (en) * 1919-08-02 1923-11-27 Carrey Rotory Engine Company Rotary air compressor
US1558639A (en) * 1923-07-27 1925-10-27 Schmied Walther Rotary machine
US1893171A (en) * 1930-11-17 1933-01-03 Sulzer Ag Rotary compressor
DE664937C (en) * 1935-03-09 1938-09-13 Becker Otto Rotary piston compressor with air-cooled housing

Cited By (55)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2697402A (en) * 1950-09-15 1954-12-21 Arthur E Lindquist Impeller construction for rotary pressure pumps
US2906448A (en) * 1954-10-28 1959-09-29 W C Heraus G M B H Roots type vacuum pumps
US3059835A (en) * 1960-01-12 1962-10-23 Gen Motors Corp Rotary blower
US3121529A (en) * 1962-05-02 1964-02-18 Polysius Gmbh Blower
US3180569A (en) * 1962-05-21 1965-04-27 Gast Mfg Corp Cooled rotary pump
US3430848A (en) * 1966-02-23 1969-03-04 Plessey Co Ltd Rotary-displacement compressors
US3531227A (en) * 1968-07-05 1970-09-29 Cornell Aeronautical Labor Inc Gear compressors and expanders
US4215977A (en) * 1977-11-14 1980-08-05 Calspan Corporation Pulse-free blower
JPS59115489A (en) * 1982-12-23 1984-07-03 Unozawagumi Tekkosho:Kk Counter-flow cooling system multistage root type vacuum pump
JPS62157289A (en) * 1985-12-29 1987-07-13 Anretsuto:Kk Roots blower for high vacuum
JPS63154884A (en) * 1986-12-18 1988-06-28 Unozawagumi Tekkosho:Kk Inner branch flow/counter flow cooling type multi-stage roots vacuum pump
JPH0733834B2 (en) 1986-12-18 1995-04-12 株式会社宇野澤組鐵工所 Inner partial-flow reverse-flow cooling multistage three-leaf vacuum pump in which the outer peripheral temperature of the housing with built-in rotor is stabilized
DE3726683A1 (en) * 1987-08-11 1989-02-23 Rietschle Masch App Roots vacuum pump
WO1989004924A1 (en) * 1987-11-16 1989-06-01 Weinbrecht John F High ratio recirculating gas compressor
US4859158A (en) * 1987-11-16 1989-08-22 Weinbrecht John F High ratio recirculating gas compressor
JPH01113183U (en) * 1988-05-25 1989-07-31
US4995796A (en) * 1988-09-05 1991-02-26 Unozawa - Gumi Iron Works, Ltd. Multi-section roots vacuum pump of reverse flow cooling type
US5090879A (en) * 1989-06-20 1992-02-25 Weinbrecht John F Recirculating rotary gas compressor
EP0447716B1 (en) * 1990-03-22 1995-08-02 The Nash Engineering Company Two-stage pumping system
US5173041A (en) * 1990-09-21 1992-12-22 Ebara Corporation Multistage vacuum pump with interstage solid material collector and cooling coils
EP0506189A1 (en) * 1991-03-28 1992-09-30 Grasso's Koninklijke Machinefabrieken N.V. Rotary compressor
US5273412A (en) * 1991-03-28 1993-12-28 Grasso's Koninklijke Machinefabrieken N.V. Lubricated rotary compressor having a cooling medium inlet to the delivery port
US5702240A (en) * 1995-05-05 1997-12-30 Tuthill Corporation Rotary positive displacement blower having a diverging outlet part
WO1998027341A1 (en) * 1996-12-16 1998-06-25 Zhangqiu Blower Factory, Shandong New structure of roots blower or roots vacuum pump with a multi-lobes impeller and a reverse flow unit
US6176693B1 (en) * 1997-03-17 2001-01-23 Finder Pompe S.P.A. Volumetric blower with covers having a duct for connection to the delivery manifold
CN1094174C (en) * 1997-11-20 2002-11-13 山东省章丘鼓风机厂 Multi-blade type impeller Roots blower (pump) structure with counter-flow device
US6312240B1 (en) * 1999-05-28 2001-11-06 John F. Weinbrecht Reflux gas compressor
US6203297B1 (en) * 1999-09-29 2001-03-20 Dresser Equipment Group, Inc. Fluid flow device with improved cooling system and method for cooling a vacuum pump
US20040228752A1 (en) * 2002-08-28 2004-11-18 Dieter Peters External gear pump with pressure fluid pre-loading
US6935851B2 (en) * 2002-08-28 2005-08-30 SCHWäBISCHE HüTTENWERKE GMBH External gear pump with pressure fluid pre-loading
US7950911B2 (en) * 2005-12-27 2011-05-31 Sekisui Chemical Co., Ltd. Single stage root type-vacuum pump and vacuum fluid transport system employing the single stage root type-vacuum pump
US20090004039A1 (en) * 2005-12-27 2009-01-01 Tetsushi Ohtsuka Single Stage Root Type-Vacuum Pump and Vacuum Fluid Transport System Employing the Single Stage Root Type-Vacuum Pump
US7569097B2 (en) 2006-05-26 2009-08-04 Curtiss-Wright Electro-Mechanical Corporation Subsea multiphase pumping systems
US20070274842A1 (en) * 2006-05-26 2007-11-29 Clifford Howard Campen Subsea multiphase pumping systems
US7226280B1 (en) * 2006-06-01 2007-06-05 Anlet Co., Ltd. Roots vacuum pump
US20080181803A1 (en) * 2007-01-26 2008-07-31 Weinbrecht John F Reflux gas compressor
US20110300014A1 (en) * 2010-06-08 2011-12-08 Paul Xiubao Huang Rotary lobe blower (pump) or vacuum pump with a shunt pulsation trap
US9140260B2 (en) * 2010-06-08 2015-09-22 Hi-Bar Blowers, Inc. Rotary lobe blower (pump) or vacuum pump with a shunt pulsation trap
US20120020824A1 (en) * 2010-07-20 2012-01-26 Paul Xiubao Huang Roots supercharger with a shunt pulsation trap
US20120171069A1 (en) * 2011-01-05 2012-07-05 Paul Xiubao Huang Screw compressor with a shunt pulsation trap
US9151292B2 (en) * 2011-01-05 2015-10-06 Hi-Bar Blowers, Inc. Screw compressor with a shunt pulsation trap
US9140261B2 (en) 2011-03-14 2015-09-22 Hi-Bar Blowers, Inc. Shunt pulsation trap for cyclic positive displacement (PD) compressors
US9732754B2 (en) 2011-06-07 2017-08-15 Hi-Bar Blowers, Inc. Shunt pulsation trap for positive-displacement machinery
US9243557B2 (en) 2011-09-17 2016-01-26 Paul Xiubao Huang Shunt pulsation trap for positive displacement (PD) internal combustion engines (ICE)
US9758320B2 (en) 2012-03-21 2017-09-12 Maricap Oy Method and apparatus for treating the outlet air of a pneumatic waste conveying system
CN102878084A (en) * 2012-08-04 2013-01-16 百事德机械(江苏)有限公司 Counter flow cooling structure of single-stage negative-pressure roots blower
US9683521B2 (en) 2013-10-31 2017-06-20 Eaton Corporation Thermal abatement systems
US11085403B2 (en) 2013-10-31 2021-08-10 Eaton Intelligent Power Limited Thermal abatement systems
US20170241327A1 (en) * 2014-04-30 2017-08-24 Edward Charles Mendler, III Supercharger Cooling Means
US10316737B2 (en) * 2014-04-30 2019-06-11 Edward Charles Mendler, III Supercharger cooling means
US9551342B2 (en) 2014-05-23 2017-01-24 Paul Xiubao Huang Scroll compressor with a shunt pulsation trap
USD816717S1 (en) 2014-08-18 2018-05-01 Eaton Corporation Supercharger housing
US20180135631A1 (en) * 2015-09-15 2018-05-17 Gree Electric Appliances, Inc. Of Zhuhai Screw Compressor and a Compressor Body Thereof
US10487834B2 (en) * 2015-09-15 2019-11-26 Gree Electric Appliances, Inc. Of Zhuhai Screw compressor and a compressor body thereof
US20220145885A1 (en) * 2020-11-12 2022-05-12 Ingersoll-Rand Industrial U.S., Inc. Positive displacement roots blower noise suppression

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