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Publication numberUS2034599 A
Publication typeGrant
Publication dateMar 17, 1936
Filing dateJul 10, 1933
Priority dateJul 10, 1933
Publication numberUS 2034599 A, US 2034599A, US-A-2034599, US2034599 A, US2034599A
InventorsMarle Dirk J Van
Original AssigneeBuffalo Foundry & Machine Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of drying inorganic salts and sludges
US 2034599 A
Abstract  available in
Images(1)
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Claims  available in
Description  (OCR text may contain errors)

March 17, 1936.

D J. VAN MARLE METHOD OF DRYING INORGANIC SALTS AND SLUDGES Fiied July 10, 1935 p' 77(INV 1 08M I g ENTOR Y n 91.4 620014 A TTORNEY? Patented .17, 1936 v UNITED; STATES RATE I ME'rnon or msfizz zge e san'rs NT orrica Dirk .Lfven Marieiiunaio, N. Ysassignorto p Bufialo Foundry & Machine 00., Buffalo, N. Y., a'corporationof New York Application my 10, 1933'. serial No. 519.021

1 Claim. (01. 159-7) This invention relates to a process for drying inorganic salts, such as sodium sulfate, sodium 'sulfite, ammonium phosphate,'sodium phos hate,

sodium carbonate, sodium chloride, pot ium salts, calcium chloride, magnesium chloride and sludges and more particularly to a continuous drying process in which the inorganic salts to I. where ascraper or doctor blade removes the mabe dried are fed in the form of a solution or sludge to a heated revolving drum from which the dried product is scrapedby a knife.

.V5fl0l18m8t81'i8lS'a1e now being dried, flaked ,or cooled on bronze, steel or cast iron drums.

The drying drums are usually heated by steam and the cooling drums cooled by water; brine or direct expansion. The materials in a liquid or semi-liquid state are applied to the rotating drum or drums and carried around to a fixed point terlal from the drums, and deposits it in a suitable conveyor. v I p The drum dryers as heretofore constructed are not entirely satisfactory and in fact they are unsuitable for drying many inorganic salts and sludges. However, the short period of drying and the continuous feature of this type of dryer make it very desirable to use for drying such inorganic salts. 7

The dimculty encountered with steel and cast. iron drums is the proper removal of the dried or cooled substance by the knives ordoctor blades from the drum surfaces. 'Itappears that cast iron and steel have'a great afilnity for and retentive power of inorganic saltsthat are being dried on such surfaces, 'theinorganic productsadhering so tenaciously that it is impossible to completely remove the dried product by the use of am p -"of knife known at present. The dried product on the drum or drums istherefore only partly removed by the knives, part of it remains as a residual film clinging tightly to the drum surface, and passes between the. knife and the.

drum surface. As the drying proceeds, the continuous abrasion by the film of material dulls the knife very quickly and the residual film which the knife does not remove inprea ses'rapidly in thickness, thereby greatly obstructing the flow of heat required for the drying,-this in turn reduced the capacity of the dryer and increases the moisture content of that part of the dry 'product which the knife is still capable of removingr On products such as sodium sulphate, etc, the conditions as outlined will continue to grow worse until shortly a point is reached at which the dry ing has to be discontinued.

On some inorganic salts, the residual film builds excessive pressure of the knife and possibly increased expansion of the drum, caused bythe this high temperature, such film at intervals will lose its grip on the drum surface and will be re moved entirely or irregularly in spots. Should the material be sensitiveto heat, the residual film periodically removed would, of course, be overheated and inferior in quality. Moreover, regardless of whether the material is sensitive up to a certainthickness, then, on account of the to heat or not, the. texture of the dry product would not be uniform and would vary from a fine powder to large flakes or hard scales which would require a special grinding operation. The capacity and moisture content of the dry product would vary as the residual film would be in process of building up or be removed. The power requirements for the removal of the product from the drums will be excessive and the results as a whole far from satisfactory. If a heavier or stiffer knife blade is selected or the knife placed at a steeper angle in relation to the drum surface in an effort to cutintn the residual film, this may result in the scoring of the drum surface ordeep go ng of the metal which may be sufiiciently se cue to render the drum unfit for further use.

In. the type of dryers known as doubledrumdryers, the drums are set close board at each end of the drums forming a reservoir on top of, and between the drums, forholding' together, with an end and pre-concentrating the liquid to be dried. The drums revolve inga downward direction I through this reservoir, the'clearance between the two drums determining. the thickness of the mm on the surface. On this typeof dryer any residual film, whether covering. the 'drum surface entirely and uniformly or irregularly in spots, will seriously interfere with the application of a liquidfilm of uniform thickness on the drum surface. The original clearance between the drums generally is between .030" and .040". The residual layer on the drums soon builds u apoint where this clearance will be closed altogether as a result erted on the residual films at a point where they meet between the drums.

This pressure becomes greater as the residual film increases in thick of which pressure will be ex-' ness and tends to crush and crack the hard film I which makes it possible for the knife to remove all or part of this heavy coating, resulting in an increased clearance and leakage between the drums in, places where the coating has been removed. The excessive pressure between thedrums caused by the residual film remaining .on

plated with chromium s. This drum is' suitably Joumaled in end standards I and is provided with a steam inlet 8 and also with suitable manner (not shown) for removing the condensate. The

the drum surfaces, will in a very short time disiron or steel does not appear to depend entirely. upon the size of the grain but it appears that the tenacity with which the metal retains a film of inorganic salt or sludge is due to the chemical composition of the metal, its internal grain structure and possibly the oxidation of the surface, which alone or in combination form a perfect anchorage for inorganic salts.

I have found that if inorganic salts or sludges I are dried upon drums having a grain structure which provides a smooth metallic surface, these difliculties do not occur. The film of dry material no longer tenaciously adheres to the drum surface and can be removed by the doctor-blade without applying excessive pressure. Consequently, heat transfer is improved, the drum speed can "be increased, a high capacity is obtained, moisture content of the dried product beof the product, and no contamination 'of the product. Moreover, since the knifepressure can-be elieved, the wear of the lmives is greatly reduced, power consumption is greatly decreased,

liquid or pasty inorganic'salt or sludge. to be dried can be applied to the chromium plated surface 6 of the drum 5 in any one of a number of different ways but as shown the drum is arranged to dip into a pan 9 which iskept filled with a bath [0 ofthe material to be dried. The drum is rotated in'the direction of the arrow and as it rotates the fllnr of liquid picked up from the pan 9' dries and is scraped off by a longitudinal knife or doctor blade- II which is preferably provided with means (not shown) for adjusting its pressure against the chromium plated surfaceof the drum 5. The dried material scraped from the drum by the knife ll falls into a trough i2 from which it is conveyed by means .of a screw conveyor l3. When the inorganic salts are to be dried; the same are fed to the heated drying drum in the form of a solution, slurry or sludge.

When the inorganic salts are to be cooled or' flaked the salts are-fused and may or may not contain water and the drum is cooled. In the double drum dryer shown in Fig. 2 tw parallel drums I are provided and each is-'composed of a welded seamless drawn or cast steel or cast iron'body having its outer cylindrical face plated with chromium 6. As in the form shown in Fig. 1 each drum is provided with a steam inlet 8 and suitable means for' removing the concomes uniform, there is no injury to the quality 'densate. The drums are supported for continuous rotation in the direction of the arrows on a frame It which also supports an end plate It at opposite ends of the drums 5. These end plates enclose the valley between the closely spaced drums, and the material to be dried is held in a I valley ortrough formed between the drums and and the danger of. the knives damaging the drums is removed. I i

It is thereforethe object of this invention to provide a processof drying inorganic salts and sludges which consists in drying these materials upon a smooth metallic surface from which they with chromium.

pheric single drum can be readily scraped, thereby'avoiding' the difficulties encountered in drying these materials on steel or cast iron drums.

In the accompanying drawing:

Fig. 1 is a vertical transverse section through i a simple form of single drum atmospheric dryer adapted for use in carrying out my improved process, and showing, in a simplified manner the manner in which the material is applied to the drum and scraped therefrom and showlna the drum made of steel or cast iron and plated Fig. 2 is a similar section through a simple form of atmospheric double drum dryer and showing the two drums also made of cast iron and plated with chromium.

Fig. 3 is an enlarged fragmentary crosssection of a steel or cast iron drum plated withchromium. Fig. 4 is a similar frmmentary cross section of a steel or cast iron drum having a stainless steel sleeve applied thereto. v

The apparatus shown forcarrylng out the present process is shown as embodied in a singleand a double drum atmospheric dryer, although it will be understood that the invention is\also applicable to vacuum drum dryers. .Inethe atmosdryer illustrated in a simpliiied manner in Fig. ii, the drum l is made of welded, seamless drawnor cast steel or cast iron in the usualmannsr, and hssits cylindricalface 'ever.'for general purposes, pla

between the end plates l6, .As the drums rotate they'pick up a film of this material and when thisfllm is dried it is scraped oiliby doctor blades or scrapers "which preferably also have means (not shown) for the adjustment of their pressure upon the surface of the drum. The dried material falls into'troughs 18 from which it is conveyed away by means of screw conveyors i9.

Instead of plating the drums I with chromium,

as shown in Figs. 1, 2 and 3 a sleeve of stainless steel 20 can be applied to the body 5 of the drum, as shown in Fig. 4. Stainless steel has an austenitic grain structure as compared with chromium which in plated construction is generally considered to be amorphous. Drums made completely of stainless steel have been found satisfactory but for reasons of economy it is preferable to make the drums of-steel or iron and place the stainless steel vsleeve around these drums. Howthe drums I with chromium has been found to be the most satisfactory as hereinafter more fully pointed out.

Until recently only steel, cast iron and bronze were available for commercial drums for atmospheric or vacuum dryers. Although bronze oflers a considerably better surface than steel or iron it is subject to the same difllculties to a lesser degree and has the additional disadvantase of comparative softness andof being easily, damaged by the knives. Nickel, Monel metal and aluminum are also comparatively .soft and ofler diiilculties in making. sound m inss of the required size. Stainless steel and chromium plated. welded.

seamless drawmorcast steel or iron drums have proved to give satisfactory Stainless steel 2,084,599 can be used in the form of a homogeneous drum I used in connection with a stainless steel drum surface to prevent scoring the wear of these knives again becomes excessive. Cast iron and steel alloys of an austeniticgrain structure such as nickel-iron and. nickel-copper-iron alloy, known commercially as Ni-resist, have been found to be an improvement but at present sufier from the same disability of comparative softness. Both of these alloys and stainless steel form a homogeneous solid solution in the solid state. Nickel plating does not ofier much promise because of the softness of the nickel and the danger of breaking or peeling of this plating. However, improved knives which require less tension and a better electro-deposit of nickel may render a nickel plated drum entirely satisfactory.

The chromium plating of welded, seamless drawn or caststeel or iron drums hasproved entirely satisfactory as it forms a hard, smooth coating which isharder than the steel or iron surface and is not subject to atmospheric corrosion. Special steel, iron, nickel or bronze alloys of suitable hardness, internal grain structure and surface condition also ofier a possibility.

With chromium plated drums drying sodium sulfate it has been possible to increase the speed from 2 R. P. M. with cast iron drums to 10 R. P. M. obtaining an increase in capacity of 60% over that obtained on cast iron drums. Moreover the moisturecontent of the dried product was reduced from 1.6-1.8% on the cast iron drums to from 02-03% on stainless steel or chromium plated drums.

Sodium sulfite sho vs an increase in capacity of in favor of the chromium plated drum, at approximately the same drum speed. However, it is possible with the chromium plated drum to double the speed and obtain an increase in capacity of 170%. d

Sodium phosphate shows the same increase in capacity and a reduction in power consumption from 26 horse power for the cast iron drums to less than 15 horse power for the chromium plated drums. This result was obtained in a commercial drying installation of much larger size than the experimental dryer on which the other tests were made.

Tests have indicated that it is apparently more satisfactory to chromium plate steel drums than cast iron drums. Due to the lack of sufiicient hardness of steel which can be used in making drying drums, the use of chromium plated steel drums appears to be particularly applicable to single drum atmospheric and vacuum dryers for drying inorganic salts and sludges.

The smooth surfaced drums forming the subject of this invention can also be advantageously used as flaking or cooling drums in flaking inorganic salts and sludges which materials adhere very tenaciously to cast iron drums and can only be removed from the drum surface by using great pressure on the knife. By providing a smooth metallic surface, as by chromium plating the flaking or cooling drums, the same advantageous results are obtained in flaking these materials.

The present invention therefore provides a process for drying inorganic salts or sludges on a smooth surface to which the material will not ad-' here tenaciously and can be readily scraped off by knives which are adjusted to bear with only relatively slight pressure against the drying surface. This avoids all of the difficulties referred to with reference to iron or steel drums on which, unless excessive knife pressure is used, a film of the dried material will adhereito the drum surface, build up in the form of a residual film or layer of dried material, reduce the. efliciency of the dryer, slow up the drying process, require greater heat and result in a product which is liable toube contaminated.

I claim as my invention:

The method of drying a solution of an inoranic salt selected from a group comprising sodium sulfate, sodium sulfite, ammonium phosphate, sodium phosphate, sodium carbonate, sodium chloride and potassium salts, which consists in applying a coating of a solution of the nmx J. VAN MARLE.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2433121 *Jan 29, 1944Dec 23, 1947Beloit Iron WorksDrier drum
US2519105 *Aug 14, 1947Aug 15, 1950Arthur A BlueDrier roll for paper, paperboard, and like material
US2577209 *Jun 10, 1948Dec 4, 1951Bernard J Hoffman JrInfrared release of water of crystallization
US2592809 *Jan 27, 1949Apr 15, 1952Du PontPreparation of nitrogenous fertilizer compositions
US2635995 *Jun 19, 1948Apr 21, 1953Rca CorpElectrophoretic insulating coating
US2857244 *Jan 3, 1955Oct 21, 1958Allied ChemProcess for the manufacture of highdensity, anhydrous calcium chloride
US2929155 *Nov 20, 1956Mar 22, 1960Lyle S OvertonDoctor blade assembly for dehydrating machine
US3308554 *Jun 22, 1966Mar 14, 1967Glen OvertonDrying cylinder
US3336104 *Dec 13, 1963Aug 15, 1967Intermountain Res & Dev CorpContinuous recycle heating process for the production of soda ash and alkali metal phosphates
US3682094 *May 21, 1970Aug 8, 1972Metal Processing Co IncClad metal member
US3756760 *Nov 8, 1971Sep 4, 1973Hallmark CardsFinishing roll for extruded plastic sheet
US3907506 *Dec 10, 1973Sep 23, 1975Air LiquideApparatus for the preparation of alkaline hyperoxide
US4106408 *Feb 22, 1977Aug 15, 1978Addressograph Multigraph CorporationDuplicator cylinder construction
US4791275 *Apr 7, 1986Dec 13, 1988Imi-Tech CorporationResilient polyimide foam with electric heater sealed between two film sheets; heat resistant
US5327660 *Dec 10, 1990Jul 12, 1994Emory John WDrum drying of acrylonitrile production wastes
US6933372Feb 27, 2004Aug 23, 2005Warner-Lambert CompanyMethod to produce a solid form of heparin
Classifications
U.S. Classification159/49, 34/112, 423/659, 34/520, 159/7, 159/11.1
International ClassificationB01D9/00, C01D5/18, C01D7/00, C01D5/00, C01D3/00, F26B17/28, F26B17/00
Cooperative ClassificationC01D7/00, C01D5/18, B01D9/0031, C01D3/00, F26B17/284
European ClassificationB01D9/00C6, C01D3/00, C01D7/00, C01D5/18, F26B17/28C