US904276A - Thermo-compressor. - Google Patents

Thermo-compressor. Download PDF

Info

Publication number
US904276A
US904276A US43912108A US1908439121A US904276A US 904276 A US904276 A US 904276A US 43912108 A US43912108 A US 43912108A US 1908439121 A US1908439121 A US 1908439121A US 904276 A US904276 A US 904276A
Authority
US
United States
Prior art keywords
steam
bars
nozzle
driving
jet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US43912108A
Inventor
Charles Prache
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LA D'EXPLOITATION DE PROCEDES EVAPORATOIRES (SYSTEME PRACHE ET BONILLON) Ste
PROCEDES EVAPORATOIRES SYSTEME PRACHE ET BONILLON SOC D EXPL DE
Original Assignee
PROCEDES EVAPORATOIRES SYSTEME PRACHE ET BONILLON SOC D EXPL DE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by PROCEDES EVAPORATOIRES SYSTEME PRACHE ET BONILLON SOC D EXPL DE filed Critical PROCEDES EVAPORATOIRES SYSTEME PRACHE ET BONILLON SOC D EXPL DE
Priority to US43912108A priority Critical patent/US904276A/en
Application granted granted Critical
Publication of US904276A publication Critical patent/US904276A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04FPUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
    • F04F5/00Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow
    • F04F5/14Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow the inducing fluid being elastic fluid
    • F04F5/16Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow the inducing fluid being elastic fluid displacing elastic fluids
    • F04F5/20Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow the inducing fluid being elastic fluid displacing elastic fluids for evacuating
    • F04F5/22Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow the inducing fluid being elastic fluid displacing elastic fluids for evacuating of multi-stage type

Definitions

  • FIG. 1 is a longitudinal section of the apparatus
  • Fig. 2 a. cross-section on line LAB of Fig. 1,'Figs. 3 and. 4 are sections 4on an enlarged scale. l
  • the nozzle 1 receives the driving steam which, on expanding, has to draw in through the ports and mix with and carry 4the steam arriving through the branch.
  • the diffuser 3 is the exact continualion of the diver-ging portion ot' thenozzlc.
  • the driving nozzle consists of a. divergent conduit .d and a convergent conduit c terminating at' the top in a reservoir r into which the steam is admittedthrough the branch 5, after having passed through a metal netting filter 6.
  • the said filter' the cross-sectional area of the passage of which is at least equal t the cross-section of the branch 5, is intended to keep back the solid particles that may be carried by the steam and that would be larger than the reduced section 4 of the Aexpansion nozzle.
  • tliesteam reservoir r can he given any other shape or connected in any Vother way to the convergent portion, the said shape and method of connection being immat'erial for the working of the apparatus.
  • the reduced portion of the' nozzle has the shape of a rectamglf ⁇ the small side ot' which must lnot exceed 2 ruin.
  • the driving jet escaping from the divergent conduit continues itspath between two series of symmetrical bars 7 arranged in ⁇ such manner that the discharge edges 8 are situated in two lanes forming with eachl other an angle/equa' to that of the divergent conduit Aof the nozzle which is thus extended in an exact manner.
  • the bars 7 are arranged at certain inter-- valsfromeach otherand form conduits or ports 9 through which enters the st eaiu l drawn in.
  • the shape of the bars is such. that the said conduits or ports formed by them,A converge towards the axis of the driving jet.
  • each bar-must be parallel to the axis A-B of the apparatus, so that the y*faces 10 of two symmetrically opposite' bars ⁇ should form :r conduit of a constant. crosss'ectionjn order that the average speed ofthe mixture should be the same at the 1nlet and at the outlet of the conduit inques-l tion.. Otherwise the average speed of the vmixture entering the speed conduit would change with the cross-section of the c onduit itself, and if the Said conduit were a diverg- It is the connection of'the said two gratos by means of triangles 1 3 that, forms an'inclosure surrounding the driving-Jet and connozzle.
  • the grates are isolated from the nozzle by screws ll and tappets l2 so as to revent the bars, owing to the 'high heat con uctivity of the metal, from() assuming the temperature of the driving steam which is necessarily higher than that of the drivenv steam, which would have the disadvantage of transform- .ing the bars into desiccators which would keep then back at their passage 'the light solid matter that maybe carried by the driven steam. This deposit would acculnu late on the bars'and finally clog up the ports.
  • the screws 11 enable the said inclosure to '-tinuin'g the divergent part of the driving be given the exact position which it has to occupy relatively to the said divergent part.
  • the working of the apparatus is as follows:
  • the length of the divergent part is such that the steam arriving at. its end is expanded to a pressure slightly lower than the pressure in the chamber 2 which receivesthe steam to be drawn in or carried through the" branch a.
  • the "driving steam having the maximum speed that itf Acould have begins to draw through the ports the-steam to be driven and becomes mixed with it.
  • the mixture thus obtained meets continually increasing cross-sections and ture is converted into a greater l) ril Leitel s PatentI No. 904,276.
  • Y ressure energy than that in the chamberl 2.
  • the number of suction ports and the final cross-'section of the diffuser depend of course on' the quantity of steam that it is desired to draw in by means of a given Weight oi" the driving steam and on the degree to which the pressure of the final mixture of the driving and driven steam has to .be raised.
  • a casing having an inlet-opening atthe upper part, a nozzle extending into the casing laterally .froxn'one side thereof, a series of bars below the nozzle to lead the steam downwardly through the casing in adivergent jet and between which the steam. in the casing enters, and a dili' user at the lower part of the casing into which the jet is discharged.
  • thermdconipressor In a thermdconipressor, the combination of a nozzle, and a series of flat bars arranged faee' to face and forming a diverging conduit for the steam jet.
  • thermo-wlmipresser the combination of a nozzle, and opposing series of fiat bars between wh ichv the steam-enters, the discharge edges of said'bars being located in' diverging planes.
  • thermo-compressor opposing sets of bars arranged in pairs and having-'their discharge edges located in diverging planes, the bars of each set being so formed and located at their adjacent edges as tocreate ports which converge toward the center-of thejet issuing between said sets of bars.
  • the working of the apparatus is as follows:
  • the length of the divergent part is such that the steam arriving at. its end is expanded to a pressure slightly lower than the pressure in the chamber 2 which receivesthe steam to be drawn in or carried through the" branch a.
  • the "driving steam having the maximum speed that itf Acould have begins to draw through the ports the-steam to be driven and becomes mixed with it.
  • the mixture thus obtained meets continually increasing cross-sections and ture is converted into a greater l) ril Leitel s PatentI No. 904,276.
  • Y ressure energy than that in the chamberl 2.
  • the number of suction ports and the final cross-'section of the diffuser depend of course on' the quantity of steam that it is desired to draw in by means of a given Weight oi" the driving steam and on the degree to which the pressure of the final mixture of the driving and driven steam has to .be raised.
  • a casing having an inlet-opening atthe upper part, a nozzle extending into the casing laterally .froxn'one side thereof, a series of bars below the nozzle to lead the steam downwardly through the casing in adivergent jet and between which the steam. in the casing enters, and a dili' user at the lower part of the casing into which the jet is discharged.
  • thermdconipressor In a thermdconipressor, the combination of a nozzle, and a series of flat bars arranged faee' to face and forming a diverging conduit for the steam jet.
  • thermo-wlmipresser the combination of a nozzle, and opposing series of fiat bars between wh ichv the steam-enters, the discharge edges of said'bars being located in' diverging planes.
  • thermo-compressor opposing sets of bars arranged in pairs and having-'their discharge edges located in diverging planes, the bars of each set being so formed and located at their adjacent edges as tocreate ports which converge toward the center-of thejet issuing between said sets of bars.

Description

lTHERMO COMPRESSOR# APPLIUATION rILBD JUNI: is, 196s.'
. Patented NOV. 17, 1908.
2 unna-SHEET z.
"WITNESES I INV' .mi
f ATTURNQYS' i having'for its object to utilize directly the f',. speed of steam, generated by the expansion UNITED s'rATEsrATENT oFFioE.
(.tlA RLES IFBAOHE, O1" PA RIS, FRANCE, A'SSIGNOR TO LA SOCIT DEXPLOITATION DE PRO- CDS VAPORATOIRES (SYSTEME PRAUHE ET BONILTON), OF PARIS, FRANCE.
THERMO-comrnnss'on.
Specification of Letters Patent.
' ,Patented Nov. 17, 1908.
Application med :une 18,'1903. serial No. 439,121.
which thermo-compresser is fully set forth iu. the following specification.
This mventlon relates to an apparatus of the said steam from a high to a low pressure, tor drawing-1n other steam at the bottom pressure, mixing it and then compress' ing it together with the first'steam to a pressure between the highest and the lowest pressures of the driving steam.
Anapparatus according to this invention is illustrated by way of example in Figures '1-4 ol. the accompanying drawing.
`Fig. 1 is a longitudinal section of the apparatus, Fig. 2 a. cross-section on line LAB of Fig. 1,'Figs. 3 and. 4 are sections 4on an enlarged scale. l
ln Figs. l and Q, the nozzle 1 receives the driving steam which, on expanding, has to draw in through the ports and mix with and carry 4the steam arriving through the branch. a of the casing 2 surrounding the nozzle. The diffuser 3 is the exact continualion of the diver-ging portion ot' thenozzlc.
'In the said diffuser the speed energy of the mixture of the driving steam and' the driven steam, is converted into pressure energy.
The driving nozzle consists of a. divergent conduit .d and a convergent conduit c terminating at' the top in a reservoir r into which the steam is admittedthrough the branch 5, after having passed through a metal netting filter 6. The said filter', the cross-sectional area of the passage of which is at least equal t the cross-section of the branch 5, is intended to keep back the solid particles that may be carried by the steam and that would be larger than the reduced section 4 of the Aexpansion nozzle.
Obviously tliesteam reservoir r can he given any other shape or connected in any Vother way to the convergent portion, the said shape and method of connection being immat'erial for the working of the apparatus. lThe reduced portion of the' nozzle has the shape of a rectamglf` the small side ot' which must lnot exceed 2 ruin.
.As Wlll be seen7 the convergent-divergent condult and the reservoir of the nozzle are constituted by two -symmetrical half-nozzles connected together in a plane A-B simply by placing together their mach-ined faces.
The driving jet escaping from the divergent conduit continues itspath between two series of symmetrical bars 7 arranged in `such manner that the discharge edges 8 are situated in two lanes forming with eachl other an angle/equa' to that of the divergent conduit Aof the nozzle which is thus extended in an exact manner.- w
The bars 7 are arranged at certain inter-- valsfromeach otherand form conduits or ports 9 through which enters the st eaiu l drawn in.
The shape of the bars is such. that the said conduits or ports formed by them,A converge towards the axis of the driving jet.
The face l0 of each bar-must be parallel to the axis A-B of the apparatus, so that the y*faces 10 of two symmetrically opposite' bars `should form :r conduit of a constant. crosss'ectionjn order that the average speed ofthe mixture should be the same at the 1nlet and at the outlet of the conduit inques-l tion.. Otherwise the average speed of the vmixture entering the speed conduit would change with the cross-section of the c onduit itself, and if the Said conduit were a diverg- It is the connection of'the said two gratos by means of triangles 1 3 that, forms an'inclosure surrounding the driving-Jet and connozzle. Y
The grates are isolated from the nozzle by screws ll and tappets l2 so as to revent the bars, owing to the 'high heat con uctivity of the metal, from() assuming the temperature of the driving steam which is necessarily higher than that of the drivenv steam, which would have the disadvantage of transform- .ing the bars into desiccators which would keep then back at their passage 'the light solid matter that maybe carried by the driven steam. This deposit would acculnu late on the bars'and finally clog up the ports. rThe screws 11 enable the said inclosure to '-tinuin'g the divergent part of the driving be given the exact position which it has to occupy relatively to the said divergent part.
The working of the apparatus is as follows: The driving steam admitted at l, escapes into the reservoir and expands in the convergent divergent nozzle, the reduced crosssection of which is 'at 4. The length of the divergent part is such that the steam arriving at. its end is expanded to a pressure slightly lower than the pressure in the chamber 2 which receivesthe steam to be drawn in or carried through the" branch a. As soon as it leaves the divergent part, the "driving steam having the maximum speed that itf Acould have, begins to draw through the ports the-steam to be driven and becomes mixed with it. The mixture thus obtained meets continually increasing cross-sections and ture is converted into a greater l) ril Leitel s PatentI No. 904,276.
finally escapes through the diffuser at the moment when the lspeed energy of the mix.-`
Y ressure energy than that in the chamberl 2. The number of suction ports and the final cross-'section of the diffuser depend of course on' the quantity of steam that it is desired to draw in by means of a given Weight oi" the driving steam and on the degree to which the pressure of the final mixture of the driving and driven steam has to .be raised.
The above described arrangement renders it possible: l. To utilize the speed energy given by the expansion ot the steam, from the moment when it has expanded to the low'- est pressure, that is to say, from Vthe moment when the speed of the steam is a'maximum. "l, To l'n'ing the maximum oi `the molecules of the said steam into direct contact-With the steam to be driven by giving the jet the shape which results in a minimum lloss of energy by friction. To adopt an absolutely symmetrical shape of the jet of driving steam, Which enables the steam to be driven., to be brought into Contact with the said jet through convergent conduits of rectangular cross-section in which each of the molecules driven is submitted to the same laws. 4. To keep the speed'of the mixture of the driving and driven steam constant between each two suction ports.
In the description of the apparatus, the
the Patent Oice.
rrectia luid adopted was steam, and the driven fluid also steam. 'But the apparatus can be used for the expansion of `any gas or vapor, and
tion of a casing having an inlet-opening atthe upper part, a nozzle extending into the casing laterally .froxn'one side thereof, a series of bars below the nozzle to lead the steam downwardly through the casing in adivergent jet and between which the steam. in the casing enters, and a dili' user at the lower part of the casing into which the jet is discharged.
2. In a thermdconipressor, the combination of a nozzle, and a series of flat bars arranged faee' to face and forming a diverging conduit for the steam jet.
3. ln a. thermo-wlmipresser, the combination of a nozzle, and opposing series of fiat bars between wh ichv the steam-enters, the discharge edges of said'bars being located in' diverging planes.
' 4:. In a thernio-compressor, opposing series of fiat bars betwc'n which the steam enters having their discharge edges arranged in diverging planes, the. inner opposing faces of said bars being parallel to each other.
-5. Inv a thermo-compressor, opposing sets of bars arranged in pairs and having-'their discharge edges located in diverging planes, the bars of each set being so formed and located at their adjacent edges as tocreate ports which converge toward the center-of thejet issuing between said sets of bars.
` (i. In a therm(rcoiiipiessoi', the combina` tion of a nozzle, opposing sets of bars forming a divergent path for the steam, and means by which said bars are positioned With respect to the nozzle though kept isolated therefrom.
In testimony whereof I have signed this specification in the'presence of two subscribing Witnesses. i
CHARLES' PRACHE.
Witnesses: i
EMILE LEDRET,
H. C. Coxn.
It is hereby 'certiied that in LettersPatent No. 904,276, granted November 17, 1908, upon the application of Charles Prache, of Paris, ifrance, for an improvement in Thernio'Compressorgf an error appears in the printed specification reeuiring correction, as follows: In the assignment at the headof the specification the wordv Bouillon should read Bouillon; and that the said Letters'Patent should be read.
with this correction therein that the same may conform -to the record o`f the .case in signed am; sealed this 15th day of June, A. D.,1909. i
. C. C. BILLINGS,
Acting Cmmnssfour of [5a/'ents'.
be given the exact position which it has to occupy relatively to the said divergent part.
The working of the apparatus is as follows: The driving steam admitted at l, escapes into the reservoir and expands in the convergent divergent nozzle, the reduced crosssection of which is 'at 4. The length of the divergent part is such that the steam arriving at. its end is expanded to a pressure slightly lower than the pressure in the chamber 2 which receivesthe steam to be drawn in or carried through the" branch a. As soon as it leaves the divergent part, the "driving steam having the maximum speed that itf Acould have, begins to draw through the ports the-steam to be driven and becomes mixed with it. The mixture thus obtained meets continually increasing cross-sections and ture is converted into a greater l) ril Leitel s PatentI No. 904,276.
finally escapes through the diffuser at the moment when the lspeed energy of the mix.-`
Y ressure energy than that in the chamberl 2. The number of suction ports and the final cross-'section of the diffuser depend of course on' the quantity of steam that it is desired to draw in by means of a given Weight oi" the driving steam and on the degree to which the pressure of the final mixture of the driving and driven steam has to .be raised.
The above described arrangement renders it possible: l. To utilize the speed energy given by the expansion ot the steam, from the moment when it has expanded to the low'- est pressure, that is to say, from Vthe moment when the speed of the steam is a'maximum. "l, To l'n'ing the maximum oi `the molecules of the said steam into direct contact-With the steam to be driven by giving the jet the shape which results in a minimum lloss of energy by friction. To adopt an absolutely symmetrical shape of the jet of driving steam, Which enables the steam to be driven., to be brought into Contact with the said jet through convergent conduits of rectangular cross-section in which each of the molecules driven is submitted to the same laws. 4. To keep the speed'of the mixture of the driving and driven steam constant between each two suction ports.
In the description of the apparatus, the
the Patent Oice.
[SEAL] rrectia luid adopted was steam, and the driven fluid also steam. 'But the apparatus can be used for the expansion of `any gas or vapor, and
tion of a casing having an inlet-opening atthe upper part, a nozzle extending into the casing laterally .froxn'one side thereof, a series of bars below the nozzle to lead the steam downwardly through the casing in adivergent jet and between which the steam. in the casing enters, and a dili' user at the lower part of the casing into which the jet is discharged.
2. In a thermdconipressor, the combination of a nozzle, and a series of flat bars arranged faee' to face and forming a diverging conduit for the steam jet.
3. ln a. thermo-wlmipresser, the combination of a nozzle, and opposing series of fiat bars between wh ichv the steam-enters, the discharge edges of said'bars being located in' diverging planes.
' 4:. In a thernio-compressor, opposing series of fiat bars betwc'n which the steam enters having their discharge edges arranged in diverging planes, the. inner opposing faces of said bars being parallel to each other.
-5. Inv a thermo-compressor, opposing sets of bars arranged in pairs and having-'their discharge edges located in diverging planes, the bars of each set being so formed and located at their adjacent edges as tocreate ports which converge toward the center-of thejet issuing between said sets of bars.
` (i. In a therm(rcoiiipiessoi', the combina` tion of a nozzle, opposing sets of bars forming a divergent path for the steam, and means by which said bars are positioned With respect to the nozzle though kept isolated therefrom.
In testimony whereof I have signed this specification in the'presence of two subscribing Witnesses. i
CHARLES' PRACHE.
Witnesses: i
EMILE LEDRET,
H. C. Coxn.
It is hereby 'certiied that in LettersPatent No. 904,276, granted November 17, 1908, upon the application of Charles Prache, of Paris, ifrance, for an improvement in Thernio'Compressorgf an error appears in the printed specification reeuiring correction, as follows: In the assignment at the headof the specification the wordv Bouillon should read Bouillon; and that the said Letters'Patent should be read.
with this correction therein that the same may conform -to the record o`f the .case in signed am; sealed this 15th day of June, A. D.,1909. i
. C. C. BILLINGS,
Acting Cmmnssfour of [5a/'ents'.
It is lwreby ccrtilied that in Lettere Patent No. 904,27i` ,g111ntcd November i7, 1908, upon the application of Charles Prache, of Paris, Ifraucv, lo." :in improvement in "hanno-Compressors, an error appears in the printcd specification requiring correction, as follows: In thc assignment at the head of tlmA npccilcation the word Bouillon should read Bouillon,- aud that the said Leuvrslatvnt, bhoulcl he read with this. correction therein that the same may conform to the record of tho .case in the Patent Oice. i
Signed and sealed this 15th day of June, A. D.. 1909.
C. BILLINGS,
Ac/[uvl/ (21mmmoncr uf 'almts.
US43912108A 1908-06-18 1908-06-18 Thermo-compressor. Expired - Lifetime US904276A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US43912108A US904276A (en) 1908-06-18 1908-06-18 Thermo-compressor.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US43912108A US904276A (en) 1908-06-18 1908-06-18 Thermo-compressor.

Publications (1)

Publication Number Publication Date
US904276A true US904276A (en) 1908-11-17

Family

ID=2972711

Family Applications (1)

Application Number Title Priority Date Filing Date
US43912108A Expired - Lifetime US904276A (en) 1908-06-18 1908-06-18 Thermo-compressor.

Country Status (1)

Country Link
US (1) US904276A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3371618A (en) * 1966-02-18 1968-03-05 Chambers John Pump
US4051671A (en) * 1974-10-31 1977-10-04 Brewer John A Jet engine with compressor driven by a ram air turbine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3371618A (en) * 1966-02-18 1968-03-05 Chambers John Pump
US4051671A (en) * 1974-10-31 1977-10-04 Brewer John A Jet engine with compressor driven by a ram air turbine

Similar Documents

Publication Publication Date Title
US2386298A (en) Diffusion pump
Sun Experimental investigation of the performance characteristics of a steam jet refrigeration system
US1137767A (en) Ejector.
US904276A (en) Thermo-compressor.
Kastner et al. An investigation of the performance and design of the air ejector employing low-pressure air as the driving fluid
US1449504A (en) Method of and apparatus for compressing elastic fluids
US1267897A (en) Air-pump.
US20020119051A1 (en) High efficiency steam ejector for desalination applications
Gurulingam et al. Performance improvement of forced draught jet ejector using constant rate momentum change method
Harris et al. Characteristics of the steam-jet vacuum pump
US220006A (en) Improvement in air and gas injectors
US6416042B1 (en) Gas-liquid ejector
US1203841A (en) Centrifugal air-pump.
US2447636A (en) Pump
US1344967A (en) Method of and apparatus for compressing fluid
US2905374A (en) Diffusion ejector pump
US1732930A (en) Ejector and method of operating the same
USRE16156E (en) A cobpoba
US1499350A (en) Elastic-fluid ejector
US282074A (en) Paul h
US1580177A (en) Method of and apparatus for compressing fluid
US1499349A (en) Ejector with cooled walls
CA2277196A1 (en) Operation process of a pumping-ejection apparatus and related apparatus
US826355A (en) Steam pumping device.
US1143348A (en) Method of and apparatus for utilizing the energy of steam.