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Publication numberUS2751031 A
Publication typeGrant
Publication dateJun 19, 1956
Filing dateMay 21, 1953
Priority dateMay 21, 1953
Publication numberUS 2751031 A, US 2751031A, US-A-2751031, US2751031 A, US2751031A
InventorsJames A Smith, Cornelius J Lyons
Original AssigneeClark & Vicario Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Conditioning paper-making stock
US 2751031 A
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Description  (OCR text may contain errors)

June 19, 1956 SMITH ETAL 2,751,031

CONDITIONING PAPER-MAKING STOCK Filed May 21, 1953 3 Sheets-Sheet 1 @mmz-m p INV'ENTORSI James A, Smith Cornelius J. Lyons BY MM YMLM ATTORNEY June 19, 1956 J, sMlTH ETAL 2,751,031

CONDITIONING PAPER-MAKING STOCK Filed May 21, 1953 3.Sheets- Sheet 2 INVENTORSI Fig. 2. James A Smith Cornelius J. Lyons m MMAW ATTORNEY June 19, 1956 J. A. SMITH ETAL 2,751,031

CONDITIONING PAPER-MAKING STOCK Filed May 21, 1953 5 Sheets-Sheet 3 JNVENTOR James A. Smi1h Cornelius J. Lyons BY (LJM Mam ATTORNEY CONDITIONING PAPER-MAKING STOCK James A. Smith, Greenburgh, N. Y., and Cornelius J.

Lyons, Nor-walk, Cnn., assignors, by mesne assignments, to Clark & Vicario Corporation, Bronxville, N. Y., a corporation of New York Application May 21, 1953, erial No. 356,382

2 Claims. (Cl. 183-25) This invention relates to devices for de-aerating dilute suspensions such as paper-making stock and other papermaking constituents. More particularly it relates to improvements in the kind of de-aerator illustrated in the patent to Clark and Vicario, No. 2,614,656, granted October 21, 1952. In that patent, the dilute paper stock to be de-aerated before it goes to a paper-making machine is atomizingly sprayed into a stock-deaerating receiver tank maintained under the effect of high vacuum, and in the receiver, the sprayed atomized dilute stock, during its de-aeration by the vacuum, falls to be collected in a pool of de-aerated stock whose liquid-level is maintained constant. De-aerated stock is then conducted to the paper-making machine under air-excluding conditions. The effect of vacuum is applied to the receiver by means of piping leading to a vacuum-producer, such as a pump. The pump, in applying suction through the piping to the receiver, sucks a certain amount of moist vapor, if not actual Water, and this has to be returned to atmospheric pressure through a condenser tank with which is connected a barometric drop-leg. Such a leg, as is known, is of the order of 34 feet long so this takes up a lot of head-room in the paper-mill. So it is among the objects of this invention to eliminate from the arrangement of said patent the need for a barometric drop-leg, with its high head-room requirement; and to eliminate the requirement of cooling water in the condenser.

These objects were attained by the use of dilute papermaking stock, or white Water, as the cooling medium or coolant, which was collected in the bottom of the con- I denser as a pool thereof, and then conducted back to the receiver tank, to be injected therein in the form of an atomized spray. This recycling arrangement gave rise to a new problem, namely, of generating enough pressure on the condensate with its suspended paper-making fibers to force it through an atomizing spray nozzle in the receiver. Normally, it would be expected that a pump would be necessary, so it became another object of this invention to devise ways and means other than a pump to accomplish this pressure build-up. This recycling arrangement then gave rise to another object of this invention, namely, to eliminate the vacuum pumping station altogether. Both of these objects are realized by a single means that accomplishes these dual results. The single means comprise a steam jet ejector placed ahead of the condenser in the vapor-sucking pipeline leading from the receiver, as a substitute for at least one stage of a vacuum pump station. The object to eliminate vacuum pumps altogether was realized by the use of a sequence of steam jet ejectors with a condenser following each ejector. With such a sequence of ejectors, the condensate from the last one, having been brought up substantially to atmospheric pressure, does not need to be returned to the receiver but can be emitted to the atmosphere Without a barometric drop-leg.

Then, in those installations where one or more steam ejectors are used, operating on high pressure steam, it is an important object of this invention to recover a signifinited States Patent 9 Patented June 19, 1956 cant quantity of British thermal units (B. t. u.) of heat from that steam, which otherwise would be lost in going down the barometric drop-leg with the high pressure steam condensate. This is important especially in northern paper-mills where steam is relatively expensive. It is also quite important in southern mills Where, although steam is not as expensive, large quantities are consumed in heating the dilute paper-making stock to high temperatures. In the southern mills making kraft paper, temperatures run around 135 F. in the headbox, while in northern mills, the temperature runs around F. in making newsprint. The higher temperatures in the southern mills tend to better drainage of the water from the fibre on the Fourdrinier wire, which is what these mills require in order to operate at very high speeds to produce very high tonnages. This object of heat-recovery from the high pressure steam used by the vacuum-producing ejector station is realized by recycling to the stock-treating receiver in atomized spray form, the condensate from the condenser which comprises fibre-bearing stock, condensed vapor, and condensed steam. The super-pressure created in the condenser by the steam from the ejector provides the necessary force to spray the condensate from a maintained pool thereof back into the receiver for retreatment therein for de-aeration.

The foregoing objects are realizable by using ways and means comprising apparatus that can be made to function by maintaining the de-aerating effect of vacuum in an enclosed de-aerating chamber by a vacuum-producer, atomizingly spraying the suspension into the chamber, maintaining constant the liquid-level of a pool of such sprayed suspension that has thus become de-aerated, con ducting such de-aerated suspension to discharge, sucking vapor from the chamber to the vacuum-producer meanwhile condensing condensables of such vapor and col1ecting a pool thereof shielded from the atmosphere, and conducting condensate from that pool back to the chamber by spraying it into the chamber. Other steps comprise effecting the condensing in the presence of atomizingly sprayed dilute suspension such as goes to the chamber. Also, the vapor from the chamber can be impelled to the place of its condensing by a steam-ejector. Further, the vacuum-producer, instead of involving a vacuum-pump, can be a sequence of steam-ejectors each followed by a condenser with a vapor from a preceding condensing step being. acted on by a subsequent ejector, and the condensate from the final condensing step emitted to the atmosphere.

The invention has been illustrated in the accompanying drawings which show two embodiments of the invention, for illustrative but not limiting purposes. In the drawings, Figure 1 is an isometric view, with parts broken away of the entire system in its usual environment. Fig. 2 is a vertical sectional view through a portion of the stock receiver tank, the vacuum-header, the stock-feeder header, the condenser, its coolant supply, and the steam ejector. Fig. 3 is a plan view, wth parts in section of the parts shown in Fig. 2. Fig. 4 is a vertical sectional view taken through the stock receiver, with details of the atomizing spray nozzles. And Fig. 5 is a somewhat diagrammatic view of a modification.

In the drawings, the enclosed chamber wherein the stock or dilute suspension to be de-aerated is a stockdeaerating receiver or tank 11 on which the tie-aerating effect of vacuum is maintained through pipes 12 leading to a vacuum-header 13 connected by a pipe 14 to a condenser 15 whose top has a pipe 16 leading to a vacuumproducer or vacuum pump 17, from which vapor is exhausted through pipe 18 and water through pipe 19. Stock to be de-aerated is pumped by centrifugal or fan pump 21 through feed pipe 22 in which is an automatic control valve 23. Pipe 22 leads to a stock-feed header 24 with which is connected a plurality of feed pipes 25, each leading and discharging into a double atomizing spray nozzle 26 within the tank 11. In the tank between each lateral pair of nozzles is an impingement plate 27 against which the inwardly directed sprays 28 impinge. The outwardlydirected sprays 29 impinge against the inner wall of the tank. The sprays atomize the stock that is in dilute suspension into a mist or fog that assumes a somewhat spiralized path toward its impingement. This mist or fog of stock which has thus been de-aerated by the vacuum within the tank, falls toward the bottom of the tank where it is collected in a pond or pool 30 thereof, whose liquidlevel 31 is controlled to be constant, at about the midheight of the tank. De-aerated stock from this pool 30 is drawn off from the bottom thereof through stock drawoil" pipe 32 by pump 33 through stock delivery pipe 34 to the head-box 36 of the paper-making machine of which 37 represents the wire, and 38 the wire-pit.

To the pipe 14 in the suction line from the vacuum header i3. is a steam jet ejector 40 fed from a high-pressure steamline 4i coming from any suitable source, that injects steam into the venturi section 42 of the vacuum pipe l ft that terminates in a downwardly-directed open elbow in the condenser 15. The condenser has a sight glass at 44 through which can be seen the liquidlevel of the maintained pool 45 of condensate reaching to an elevation above the tank 11. Condensate fiows from the pool thereof through pipe 46 from its bottom, valved at 47, to the tank 11, wherein it is connected with two dual atomizing spray nozzles 4-8. The coolant for the condenser 15 is provided through coolant pipe 59, valved at 51, leading through branch pipe 52 connected with the stock feed pipe 22 ahead of its automatic valve 23, or from other sources such as branch pipe 53 valved at 54. The upper end of the coolant pipe 59 is branched again at 55 and 56, both of which are valved, and each terminates in the condenser 15, in an atomizing spray nozzle 57 and 53, respectively, similar in construction and function to spray nozzles 26 and 48, for forming into a mist or fog the stock suspension used as a coolant for the condenser.

Fig. 5 shows a modification that difiFers from the arrang ment of the other figures, and particularly Fig. 2, by the absence of vacuum-pumps and by the use of an additional set or sets of steam ejector and condenser. So in this figure, the reference numerals up to 58 indicate the same elements as in the earlier figures. The added structure, or second stage condensing, is illustrated by using in the top pipe 16 from condenser 15, a second steamejector 61, fed with high-pressure steam through pipe 64 from steam supply pipe ill, or other suitable source. This second or secondary steam ejector is in a venturi section 62 of pipe -53 leading from condenser top pipe 16 to a second condenser 6d and terminating therein with an elbow as. In that condenser is one or more atomizing spray nozzles 66 for spraying into the secondary condenser white-water,

or stock from the receiver 11, conveyed to the nozzle through pipe 67. Condensate from a pool 59 thereof in this condenser can be carried to discharge through pipe 63 valved at 72 leading to a splash box as in the wire pit 33. This pipe 68 is not a barometric drop-leg. Valve '72 can be used to control the height of the liquid-level of the pool 59 in condenser 64.

Referring back to Fig. 1, 76 indicates an automatic controller of the liquid-level of the de-aerated stock pool in the stock receiver 11, by making the incoming feed equal to the withdrawn de-aerated stock, while 71 indicates an indicator panel for showing what is happening in the various stations, and, if desired, containing any necessary or desired controls.

In operation, dilute paper-making stock is pumped by pump 21 through stock feed pipe 22 in quantity regulated by valve 23, to stock header 24 and feed pipes 25 to be atomizingly sprayed through spray nozzles 26 to be impinged against either impingement plate 27, or the side walls of the stock receiver tank 11, to become atomized as to simulate a mist or fog. Meanwhile, the effect of vacuum is produced within the receiver 11 by a primary vacuum-producing high-pressure steam ejector 4t) supplied with steam through pipe 41, with the vacuum operating through vacuum header 13 and branch pipes 12 on the receiver. Secondary vacuumproducing means is the pump 17 sticking through pipe 16 from condenser 15 into which the steam ejector discharges. The vacuum effective within the receiver 11 de-aerates the atomized stock sprayed thereinto, and the de-aerated stock falls to collect in a pool 3% whose liquid-level 31 is maintained constant. Deacrated stock from the pool is conducted under air-excluding conditions through stock drawotl pipe 32 by pump 33 and conducted to the head-box 36 of a paper-machine.

Primary condenser 15 has supplied thereto as the cool ant, de-acrated stock from the receiver .13., or white-water from the paper-mill, an important feature being that the coolant is a suspension of paper making fibres. The coolant is atomizingly sprayed into the condenser 15 through atoniizing spray nozzles 57 and '58. It is led thereto through branch pipes 55 and 56 from coolant supply pipe 5 that comes either from the main stock feed pipe 22 via pipe 52, or from some other source through pipe 53. The atomized coolant suspension falls to the bottom of condenser 15 where a maintained pool 45 thereof forms including condensate from the vapors and any fibres entrained therein, fed thereto by the steam ejector 40 through pipe 14, and elbow 43. The depth of the pool heated by steam from the jet to a temperature substantially as hot as that of the pool 30 in the tank 11 is controlled by means of valve 47 by an operator observing the liquid-level of the pool 45 through sight-glass d4. Pressure greater than the sub-pressure in the tank ill, built up in the condenser 1.5 by compression resulting from the steam ejector 4t), and by the elevation of the maintained pool of condensate above the tank 11, is sufficient to force liquid from the pool 45 through pipe 46 to be emitted from atomizing spray nozzles 4-8 in the stock receiver 11, and thus returned to that receiver to be re-deaerated therein. Noncondensates are sucked from the top of the condenser 15 through pipe 16 by vacuum pump 17, and discharged.

In Fig. 5 the vacuum pump 17 has substituted for it, a second or secondary steam-ejector and condenser station, wherein the operations of primary condenser 15 are repeated, only condensate from a pool 59 thereof is conducted through pipe 63 past a splash plate 69 to be re turned to the wire pit 38 of the paper-machine. This secondary condenser can be smaller than the primary condenser. Also further ejector-condenser stations can be used, if desired.

Features of advantage of the invention include the elimination of the necessity for a barometric drop-leg by using as a coolant for the condenser a dilute stock of paper-making fibres such as can be tie-aerated in the deaerating stock receiver; recovery of the heat value of the steam used in the ejector and use of the recovered heat in place of another source of heat that otherwise would be required to maintain the temperature of the dilute papenmaking stock at some other point in the papermaking process; elimination of complex piping from the receiver to the ejector; elimination of fresh cooling water; and providing means for building the assembly of receiver, steam ejector, and condenser in one complete closely-connected unit instead of having these units sep arate and situated remotely from each other. From the manufacturing standpoint, this is important inasmuch as handling and shipping of these components is thus simplified; and as from the installation standpoint, the cost is significantly reduced.

As this invention may be embodied in several forms without departing from the spirit or essential characteristics thereof, the present embodiment is therefore illustrative and not restrictive, since the scope of the invention is defined by the appended claims rather than by the description preceding them, and all changes that fall within the metes and bounds of the claims or that form their functional as well as conjointly co-operative equivalents, are therefore, intended to be embraced by those claims.

We claim:

1. The continuous process of de-aerating a liquid suspension of paper-making constituents while heated to mill stock temperature, which comprises pumping such heated suspension and atomizingly spraying it into an enclosed de-aerating chamber, maintaining the eifect of high vacuum in the chamber by suction of a steam-jet ejector, maintaining constant the liquid-level of a pool in the chamber of such sprayed de-aerated suspension, conducting such suspension from the pool under air-excluding conditions to the place of its use, sucking air from the chamber by the jet, conveying steam and sucked air from the jet to the atmosphere of an enclosed condenser, condensing the condensables in said steam and air by supplying to the steam and air entering the condenser a dilute suspension of paper-making constituents; collecting a quantity of such condensate and maintaining a pool thereof reaching to an elevation above the chamber but below the point of entry of the steam and air into the condenser While shielded from the atmosphere to receive and retain heat and pressure supplied thereto by the steam from the jet, and forcibly atomizingly spraying into the chamber such heated condensate from the maintained pool thereof independently of the said pumped spraying to de-aerate it while using as a correlated force therefor the steam-jetinduced pressure thereon plus the elevation of the pool whereby the pressure on the elevated condensate is greater than the pressure in the chamber and the heat of the steam is retained by rising temperature of the condensate to be substantially as hot as that of the pool in the chamber.

2. A de-aerating system for a liquid suspension of paper-making constituents while heated to mill stock temperature, which comprises an enclosed de-aerating tank, atomizing spray nozzles in the tank, pump means for forcibly supplying such heated suspension to some of the nozzles but not to at least one other, means for maintaining constant the liquid-level of a pool of such deaerated suspension collected in the bottom of the tank, means for passing de-aerated heated suspension from that pool, a steam-jet ejector vacuum-producer connected by piping to the tank for maintaining the elfect of high vacuum in the tank, closed condenser means, means for maintaining in the condenser at an elevation above that of the tank a pool of condensate, means for supplying into the condenser a dilute suspension of paper-making constituents, means for delivering steam and air from the steam jet into the condenser above its pool to apply pressure on and heat to the pool to heat the latter to a temperature at least as high as that of the pool in the tank, and means connecting the pool of condensate with a remaining spray nozzle in the tank through which condensate from the maintained pool thereof is sprayed independently into the tank by the combined force of the elevation of the pool of condensate and the pressure thereon which force is greater than the pressure in the tank and the temperature of which spray is substantially as high as that of the pool in the tank.

References Cited in the file of this patent UNITED STATES PATENTS 1,288,058 Leblanc Dec. 17, 1918 1,611,256 Suczek Dec. 21, 1926 1,778,302 Schubert Oct. 14, 1930 2,223,237 Cooke Nov. 26, 1940 2,614,656 Clark et al. Oct 21, 1952 FOREIGN PATENTS 638,198 Great Britain May 31, 1950

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1288058 *Nov 17, 1915Dec 17, 1918Societ Anonyme Pour L Expl Des Procedes Westinghouse LeblancCondensing apparatus.
US1611256 *Jan 13, 1923Dec 21, 1926C H Wheeler Mfg CompanyCondensing and deaerating method and apparatus
US1778302 *Jul 18, 1928Oct 14, 1930Brysilka LtdApparatus for use in manufacturing artificial silk
US2223237 *Jun 10, 1938Nov 26, 1940Schutte & Koerting CompanyVapor condenser
US2614656 *Aug 15, 1949Oct 21, 1952Rotareaed CorpDeaerating a suspension of papermaking stock
GB638198A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2870859 *Jun 19, 1957Jan 27, 1959Bowser IncProcess and apparatus for de-aerating oleaginous materials
US2971453 *Apr 12, 1957Feb 14, 1961Sanitary Mfg Company Of PittsbMilk treating system with deaerator
US3494101 *Oct 25, 1967Feb 10, 1970Wikdahl Nils Anders LennartMethod and apparatus for deaerating liquid suspensions
US4276059 *Aug 9, 1979Jun 30, 1981Elast-O-Cor Products & Engineering LimitedDeaerator for pulp stock
US4378978 *Aug 21, 1981Apr 5, 1983Asea AktiebolagDegassing of liquid mixtures
US5660617 *May 16, 1996Aug 26, 1997Southwest Research InstituteSystem and method for maintaining multiphase flow with minimal solids degradation
Classifications
U.S. Classification95/255, 95/258, 96/204, 261/DIG.540, 95/260
International ClassificationD21D5/26
Cooperative ClassificationY10S261/54, D21D5/26
European ClassificationD21D5/26