US285822A - Eenst kobtbtg - Google Patents

Eenst kobtbtg Download PDF

Info

Publication number
US285822A
US285822A US285822DA US285822A US 285822 A US285822 A US 285822A US 285822D A US285822D A US 285822DA US 285822 A US285822 A US 285822A
Authority
US
United States
Prior art keywords
tube
water
steam
nozzle
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
Publication date
Application granted granted Critical
Publication of US285822A publication Critical patent/US285822A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31242Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the central area of the venturi, creating an aspiration in the circumferential part of the conduit

Definitions

  • This invention has special reference to that class of condensers wherein a jet of fluid delivered from one nozzle is caused to pass through one or'more succeeding nozzles and combined with a second fluid entering spaces through or between the successive nozzles, the combined fluids finally escaping through a discharge-tube, which is enlarged toward the delivery end to permit the expansion of the fluid and a consequent decrease of pressure.
  • a centrally located nozzle through which the water-jet is delivered; a mixing or combining tube which has a bore or passage of substantially cylindrical form, with numerous small slits or openings entering the same from the exterior with a forward inclination; a delivery tube or nozzle communicating with the mixing-tube and enlarging toward the delivery end, and an encircling body or its equivalent, through which the steam or other vapor may be permitted to surround the mixing tube and pass inward through its openings.
  • the action of the apparatus is based upon the same general principles which are involved in the ordinary steam-jet apparatus, which is familiar in a great variety of forms to all persons skilled in the art.
  • My present apparatus differs, however, from those hitherto produced in the essential particular that the mixing-tube has its bore or central passage of uniform or substantially uniform diameter from end to end that it presents an approximately continuous surface on the interior, and that it contains a large number of small inlet-openings, whereby it is caused, when usedin comsults than can be obtained by jet apparatus of the ordinary kind when worked under low pressures.
  • Figure 1 represents a longitudinal central section of my condenser in its most simple form.
  • Fig. 2 is a similar view of the same provided with a regulating or controlling sleeve and with means for imparting a spiral motion to
  • Fig. 3 isa cross-sectlon the infiowing water. 011 the line 00 a: of Fig. 2.
  • A represents a centrally located tapering nozzle, through which the water or other liquid employed for the purpose of condensation is delivered.
  • This tube B is made, as shown, of uniform diameter interthe combination of a series of tapered nozzles inserted one within another with spaces between them.
  • D represents a body or chamber, provided with an inlet-neck on one side, and surrounding the delivery end of the water-nozzle A and the mixing-tube B at a suitable distance from the latter, in order to leave an annular space, so that the steam may completely encircle the mixing-tube.
  • the water or other liquid enters the nozzle A, and is delivered thence through the mixing-tube, past the inlets and the thin metallic edges, through the delivery-tube O.
  • the liquid In passing the inlets b the liquid is subjected to the action of numer- -ous small jets of steam entering under pressure through the inlets, the steam thus entering being delivered in a forward direction and acting to urge the liquid column forward in a Very efficient manner.
  • the large number of inlets and the corresponding number of inflowing jets secure a thorough admixture of the steam with the inflowing liquid.
  • spiral device E any other equivalent form of device which will have the effect of breaking up or atomizing the liquid column to permit the fluid to permeate the same may be employed.
  • a sliding sleeve, F may be mounted upon the throat or mixing tube, as in Fig. 2. When this slide is moved forward, all the inlets are uncovered and are operative but by moving the sleeve backward any required number of the openings may be closed and rendered inoperative. Any suitable means to be operated from the exterior may be employed for adj ustingthe sleeve; but I prefer, as shown in Figs.
  • the regulating-sleeve F is more desirable in an apparatus where the elastic force of steam, air, or gas is to be employed as the actuating force.
  • the apparatus herein represented may be variously employed as an exhauster for moving steam, air, or gas as a means of condensing steam or other vapors for the purpose of setting air in motion, and also that it may be employed with equal efficiency where the elastic force of steam, air, or gas is utilized to create or augment the speed of a water-jet, as in ordinary jet injectors or elevators.
  • the water be not delivered to the apparatus under pressure, but require to be elevated or drawn thereto, provision must be made to first bring the water to the apparatus and induce a current therein.
  • This may be done in any suitable manneras for example, by a second nozzle passing through the waternozzle and enteringthe combining-tube, the second nozzle being supplied with water, steam, or other fluid under pressure; or it may be done by means of a suction apparatus placed in the discharge-pipe, or by an apparatus connected with the water-supply, by means of which water under pressure may be supplied and a current established.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nozzles (AREA)

Description

(Model.)
B. KORTING.
I JET CONDENSER.
Patented Oct. 2, 1883.
' practically available for the purpose of pro-' NITED STATES PATENT OFFICE.
ERNST KRTING, OF HANOVER, BRUNSWICK, GERMANY.
JET-CONDENSER;
SPECIFICATION forming part of Letters Patent No. 285,822, dated October 2, 1883, 1
Application filed October 11,1as2. (Model) To all whom it may concern:
Be it known that I, ERNST KoRrING, ofHanover, Brunswick, Germany, have invented certain new and useful Improvements in J et-Condensers, of which the following is a specification.
This invention has special reference to that class of condensers wherein a jet of fluid delivered from one nozzle is caused to pass through one or'more succeeding nozzles and combined with a second fluid entering spaces through or between the successive nozzles, the combined fluids finally escaping through a discharge-tube, which is enlarged toward the delivery end to permit the expansion of the fluid and a consequent decrease of pressure.
It is the special aim of the invention to effeet a more thorough and economical combination of the'two fluids-such as steam and waterand to render steam at low pressures pelling or assisting to propel water or other condensingfiuid.
To this end it consists, essentially, in an apparatus embracing in combination the follow ing elements: a centrally located nozzle, through which the water-jet is delivered; a mixing or combining tube which has a bore or passage of substantially cylindrical form, with numerous small slits or openings entering the same from the exterior with a forward inclination; a delivery tube or nozzle communicating with the mixing-tube and enlarging toward the delivery end, and an encircling body or its equivalent, through which the steam or other vapor may be permitted to surround the mixing tube and pass inward through its openings.
The action of the apparatus is based upon the same general principles which are involved in the ordinary steam-jet apparatus, which is familiar in a great variety of forms to all persons skilled in the art. My present apparatus differs, however, from those hitherto produced in the essential particular that the mixing-tube has its bore or central passage of uniform or substantially uniform diameter from end to end that it presents an approximately continuous surface on the interior, and that it contains a large number of small inlet-openings, whereby it is caused, when usedin comsults than can be obtained by jet apparatus of the ordinary kind when worked under low pressures.
I am aware that a jet apparatus has been constructed with a series of nozzles arranged to discharge one into another, the nozzles being made of tapering form on the interior, and being arranged in such manner as to leave annular inlets between them. I am also aware that an air-pump condenser has been proposed, with a cylindrical water-passage provided with numerous oblique inlets and with a surrounding steam-jacket, the combination being one, however, in which'the movement of the water was secured by the positive action of a pump and in which the action was not secured by or dependent upon the action of the steam upon the water-jet. To a structure such as mentioned I lay no claim, my invention being restricted to an apparatus in which the perforated mix-' ing-tube, of uniform diameter, is combined with a supply-nozzle and with an expanded discharge-tube.
Referring to the accompanying drawings, Figure 1 represents a longitudinal central section of my condenser in its most simple form. Fig. 2 is a similar view of the same provided with a regulating or controlling sleeve and with means for imparting a spiral motion to Fig. 3 isa cross-sectlon the infiowing water. 011 the line 00 a: of Fig. 2.
Referringto the drawings, A represents a centrally located tapering nozzle, through which the water or other liquid employed for the purpose of condensation is delivered.
B represents the mixing or combining tube,
arranged opposite the inner end of the water nozzle and in line therewith. This tube B is made, as shown, of uniform diameter interthe combination of a series of tapered nozzles inserted one within another with spaces between them.
represents the discharge-tube joined to the end of the mixing-tube B, but enlarged thence toward the delivery end in a form and manner common in other classes of jet apparatus. W
D represents a body or chamber, provided with an inlet-neck on one side, and surrounding the delivery end of the water-nozzle A and the mixing-tube B at a suitable distance from the latter, in order to leave an annular space, so that the steam may completely encircle the mixing-tube.
In the operation of the apparatus, the water or other liquid enters the nozzle A, and is delivered thence through the mixing-tube, past the inlets and the thin metallic edges, through the delivery-tube O. In passing the inlets b the liquid is subjected to the action of numer- -ous small jets of steam entering under pressure through the inlets, the steam thus entering being delivered in a forward direction and acting to urge the liquid column forward in a Very efficient manner. The large number of inlets and the corresponding number of inflowing jets secure a thorough admixture of the steam with the inflowing liquid.
In practice it is found that, by means of the large number of openings and the consequent distribution of the elastic force of the steam or' other fluid over the surface of the liquid, greatly improved results are secured as compared with the ordinary form of apparatus, in which a like distribution of the pressure is not secured. The distribution of the fluidpressure over the surface of the liquid is advantageous both in securing a more perfect admixture, and consequently a more economical condensation, and also in that the pressure is more effectively applied to drive the fluid column forward.
For the purpose of shattering or atomizing the liquid as it enters the apparatus, in order that the steam may combine more intimately and quickly therewith, I introduce into the water-nozzle A a spiral blade, E. The inflowing water, encountering this blade, is caused to pursue a spiral or gyratory motion, the effect of which is to break up or shatter the inflowing column, thereby permitting the steam to pass more readily between its drops or atoms, and thus permeate the entire body of liquid.
While it is preferred to employ the spiral device E, any other equivalent form of device which will have the effect of breaking up or atomizing the liquid column to permit the fluid to permeate the same may be employed.
As a means for opening and closing a greater or less number of the inlets I), as circumstances may require, a sliding sleeve, F, may be mounted upon the throat or mixing tube, as in Fig. 2. When this slide is moved forward, all the inlets are uncovered and are operative but by moving the sleeve backward any required number of the openings may be closed and rendered inoperative. Any suitable means to be operated from the exterior may be employed for adj ustingthe sleeve; but I prefer, as shown in Figs. 2 and 8, to provide an external handwheel having a spindle extended inward through the side of the body, and provided at the inner end with a disk bearing a crankpin, 0, which enters atransverse groove in the sleeve, so that by turning the hand-wheel the crank-pin is caused to move the sleeve forward and backward. The regulating-sleeve F, is more desirable in an apparatus where the elastic force of steam, air, or gas is to be employed as the actuating force.
It will be readily perceived by one skilled in the art that the apparatus herein represented may be variously employed as an exhauster for moving steam, air, or gas as a means of condensing steam or other vapors for the purpose of setting air in motion, and also that it may be employed with equal efficiency where the elastic force of steam, air, or gas is utilized to create or augment the speed of a water-jet, as in ordinary jet injectors or elevators.
lVhere the water-discharge is required to overcome a counter-pressure from the commencement-as for example, when the apparatus is used as a boiler-feederit willbe provided with the well-known overflow between the combining-tube and the discharge-tube, or with a starting-valve in the pressure or discharge pipe. These devices being wellunderstood by those skilled in the art, and being represented in various forms in numerous patents hitherto granted to me, it is deemed unnecessary to illustrate them herein.
If the water be not delivered to the apparatus under pressure, but require to be elevated or drawn thereto, provision must be made to first bring the water to the apparatus and induce a current therein. This may be done in any suitable manneras for example, by a second nozzle passing through the waternozzle and enteringthe combining-tube, the second nozzle being supplied with water, steam, or other fluid under pressure; or it may be done by means of a suction apparatus placed in the discharge-pipe, or by an apparatus connected with the water-supply, by means of which water under pressure may be supplied and a current established. These means, however, for establishing a primary supply of water constitute no part of this invention.
The present invention is restricted to those matters and things which are hereinafter claimed, and as to all matters which may be described or shown, but which are not claimed,
the right is reserved to make the same the subject of a separate application.
Having thus described myinvention, what I claim is 1. In a jet-condenser, the combination of a liquid-supply nozzle, a combining-tube of uniform or substantially uniform diameter from end to end, with numerous inlets having an inclination in the direction of the discharge, a delivery-tube enlarged or expanded in the direction of the discharge, and means for supplying steam or other fluid through the eXterior of the combining-tube.
' 2. In a jet apparatus, the combination, with an expanded delivery-tube, of a mixing-tube provided with numerous inletsinclined inaforward direction, a water-nozz1e, means for supplying vapor to the exterior of the mixingtube, and a spiral blade or agitator located in the water-nozzle, substantially as described, to shatter 0r atomize the inflowing liquid.
3. In a jet apparatus, the combination of the central water-nozzle, A, the expanded delivery mouth or tube 0, the body D, and the combinin g throat or passage, of substantially uniform diameter from end to end, with numerous restricted inlets having a forward direction or inclination.
- ERNST KORTING.
Witnesses:
WILLIAMs 0. Fox, J 011s. KRAOKE.
US285822D Eenst kobtbtg Expired - Lifetime US285822A (en)

Publications (1)

Publication Number Publication Date
US285822A true US285822A (en) 1883-10-02

Family

ID=2355021

Family Applications (1)

Application Number Title Priority Date Filing Date
US285822D Expired - Lifetime US285822A (en) Eenst kobtbtg

Country Status (1)

Country Link
US (1) US285822A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3219483A (en) * 1961-08-19 1965-11-23 Escher Wyss Gmbh Apparatus for continuous gelatinization of starch
US6637731B2 (en) * 2001-05-03 2003-10-28 Tomco2 Equipment Company Diffuser for use in a carbonic acid control system
US20050275119A1 (en) * 2004-05-21 2005-12-15 Karsten Glomset Oxygenating nozzle
US10279323B2 (en) * 2015-04-10 2019-05-07 Infuze, L.L.C. Shuttling Venturi

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3219483A (en) * 1961-08-19 1965-11-23 Escher Wyss Gmbh Apparatus for continuous gelatinization of starch
US6637731B2 (en) * 2001-05-03 2003-10-28 Tomco2 Equipment Company Diffuser for use in a carbonic acid control system
US20050275119A1 (en) * 2004-05-21 2005-12-15 Karsten Glomset Oxygenating nozzle
US7533874B2 (en) * 2004-05-21 2009-05-19 Aga Ab Oxygenating nozzle
US10279323B2 (en) * 2015-04-10 2019-05-07 Infuze, L.L.C. Shuttling Venturi

Similar Documents

Publication Publication Date Title
US20050061378A1 (en) Multi-stage eductor apparatus
US285822A (en) Eenst kobtbtg
US6534023B1 (en) Fluid dynamic ozone generating assembly
US640463A (en) Hydraulic elevator.
US2642813A (en) Aspirator
US1031289A (en) Jet-jump.
US2107340A (en) Washer
EP0645541A1 (en) Self-priming centrifugal pump
US1267897A (en) Air-pump.
RU2142072C1 (en) Liquid-and-gas ejector
RU2142070C1 (en) Liquid and-gas ejector
US393488A (en) Ejector-condenser
US372070A (en) Apparatus for producing a vacuum
RU2072454C1 (en) Liquid-gas ejector
US554073A (en) Momentum-engine
US330157A (en) Steam-jet condenser
JP6593610B2 (en) Air-mixing nozzle
US117504A (en) Improvement in hydraulic motors
US649282A (en) Ejector-pump.
US134900A (en) Improvement in steam-condensers
US573611A (en) Ejector for mining and dredging
US166657A (en) Improvement in apparatus for drawing or raising water
US165843A (en) Improvement in injectors
RU2228463C2 (en) Jet apparatus
US817620A (en) Injector.