US3011543A - Spray dryer - Google Patents

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US3011543A
US3011543A US671513A US67151357A US3011543A US 3011543 A US3011543 A US 3011543A US 671513 A US671513 A US 671513A US 67151357 A US67151357 A US 67151357A US 3011543 A US3011543 A US 3011543A
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drying
drying chamber
container
chamber
particles
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Jr Samuel L Mccormick
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/16Evaporating by spraying
    • B01D1/18Evaporating by spraying to obtain dry solids
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S55/00Gas separation
    • Y10S55/38Tubular collector electrode

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  • This invention relates'generally to spray dryers, and in part1cular to such dryers having a means for restraining the particles from contacting the walls of the drying chamber.
  • Spray drying has been used with varying degrees of success in a wide variety of industries. It has been used to dry milk, soaps and detergents, pharmaceuticals, fine chemicals, organic and inorganic chemicals, rubber and synthetic latices, clay slips, and other products and materials as Well.
  • spray drying is a major operation, and the dryers constitute a large percentage of the investment in modern detergent processing equipment, Where the total production of spray dried products is several billion pounds per year. Milk is spray dried in quantities approaching a billion pounds annually, and the annual spray dried production of other foods, coffee, for example, runs into the hundreds of million pounds.
  • Spray drying presents several unique problems not encountered in certain other drying technics; Among these problems is the tendency of particles to adhere and accumulate during the drying operation to the surfaces of the drying chamber.
  • a further attempt at solution of' the problem of ad-' herence of the particles provides a mechanical device, such as a rotating chain which strikes the side walls of the drying chamber to dislodge material'adhering to them.
  • This arrangement is not completely successful since the chain will not strike all the surfaces of the drying chamber and since particles tend to collect on the chain and its supports. Since it is frequently desirableto dry materials whose final product specifications are such that no economical combination of the factors mentioned above, or others, will give a satisfactory product, the field of application for spray dryers is limited. It is usually necessary to test a new material to be spray dried on a substantial pilot scale before success may be predicted.
  • the present invention provides additional fiexibilityin the application of spray dryers so that almost any material which can be dispersed in a gas can be spray dried.
  • the primary object of this invention is to improve spray drying technics, particularly with respectto the problems connected with materialsv adhering to walls, which normally occurs.
  • the accomplishment of this object makes possible the construction of spray dryers of more compact design and also gives increased flexibility in operating conditions.
  • the object of the present invention is accomplished by providing the dispersed particles with a unipolar electrical charge and impressing upon the drying chamber Walls an electrical charge of the same polarity as that carried by the atomized particles.
  • a further object of the present invention is to provide a spray drying apparatus which can successfully spray dry materials which have a relatively 'high tendency to adhere to the drying chamber walls.
  • a further object of the present invention is to provide a spray drying apparatus in which drying gas having a relatively low inlet temperature may be used, thereby reducing heat exposure of the product.
  • a further object of the present invention is to provide a spray drying apparatus in which less atomization can be-
  • FIG. 1 represents a schematic cross sectional illustration of an apparatus employing the present invention.
  • FIG. 2 is a view similar to FIG. 1, butillustrating a modified form of the invention.
  • FIG. 3 is a view similar to FIGS. '1 and 2, but illustrating a further modified form of the present invention.
  • FIG. 1 there isshowngene'rally at 10 a tank or container providing a drying chamber 11.
  • the inner walls 12 of the chamber 11 are formed of electrically conductive material, such as steel, and the outer surface 13 of the tank'is formed of an electrical insulating material, .which' may preferably also have thermal insulating properties.
  • a nozzle or other dispersing or atomizing device At the upper end of the drying'chamber there is schematically shown a nozzle or other dispersing or atomizing device; l l'forintroducing into the chamber dispersed particles which are given a unipolar charge by passage through an ionizing grid 15 mounted adjacent the nozzle.
  • Anelectrically non-con-, ducting flange 16 serves to support the nozzle 14 and. electrically insulates the chamber walls from the nozzle.
  • a drying gas inlet conduit 17 connects with the drying chamber adjacent the upper end thereof, and an electrical; insulating sleeve or coupling 18 serves to electrically in-' sulate the drying chamber walls from the conduit 17.
  • a direct currentsourceoffelectrical power is shown at-ZZ' having its positive terminal 23 connected to ground and its negative terminal 24 electrically connected to the drying chamber walls and to the ionizing grid by means of wire 26.
  • this arrangement provides a means for impressingv an electrostatic potential upon the drying chamber walls and the grid, and that while the grid and inner walls are illustrated as being at the same electrical potential, other connections with the power source may be made which will establish them at differing potentials.
  • the polarity of the charge on the drying chamber walls is negative and is of the same polarity as the charge imparted to the dispersed particles or droplets, by the grid as, they are introduced into the drying chamber from the nozzle 14.
  • the charged atomized particles are introduced into the chamber after passing through the grid, and heated drying gas enters the chamber from the duct 17. Since the walls of the drying chamber are charged at the same polarity as the particles, they will be restrained from contact with the chamber walls.
  • the spent drying gas containing the entrained dry product passes out of the drying chamber through the outlet duct or conduit 19.
  • FIG. 2 operates identically to that described with reference to FIG. 1, but differs somewhat in the construction of the container or tank.
  • an electrically conducting inner liner 27 which may take the form of a screen, wire mesh or other electrostatically chargeable element, provides the drying chamber inner walls.
  • This liner is supported and electrically insulated from the tank wall 28 by means of electrically insulating spacers 29. Connection of the negative terminal of the power source 22 to the liner 27 is accomplished by wire '26 which passes through a non-conducting flange 31. Wire 26 also serves to connect the power source to an ionizing grid 25 similar to the grid 15.
  • the apparratus shown in FIG. 3 is a further modified form of the present invention in which the cross sectional dimension of the drying chamber 11a is greatly reduced as compared to this dimension of the drying chamber previously referred to.
  • This spray drying apparatus includes a nozzle 14a for introducing into the drying chamber 1 1a dispersed particles given a unipolar electrical charge by the ionizing grid 15m.
  • a drying gas inlet duct 17: is connected to the top of the cylindrical drying chamber.
  • An outlet duct 19a is similarly connected to the bottom of the drying chamber.
  • the inner surface 12a of the drying chamber is formed of electrical connecting material and is electrically insulated from the ducts 17a and 19a by means of the insulating couplings 18a and 21a, respectively.
  • the outer surface of the drying chamber wall 130 is formed of electrical insulating material, which preferably also has thermal insulating properties.
  • the drying chamber walls have impressed thereon a negative electrical charge which is the polarity of the charge given the particles introduced from the nozzle 14a by passage through the grid.
  • a spray drying apparatus comprising a container forming a drying chamber, the inner surfaces of said container being electrically conductive and the outer surfaces being thermally and electrically insulating, and means. for unipolarly electrically. charging and introducing atomized particles to be dried within said container, a conduit communicating with said container and electrically insulated from the inner surfaces thereof for introducing a drying gas into the chamber, an outlet conduit extending from said container electrically insulated from the inner surface thereof and adapted to conduct dried particles and exhaust gas from the chamber, and electrical means for applying to the inner surfaces of said container an electrical charge of the same polarity as the charge carried by the atomized particles.
  • a spray drying apparatus comprising a container forming a drying chamber, the inner surfaces of said 'container being electrically conductive, means for creating a stream of unipolarly charged atomized particles to be dried within said container, said means comprising a nozzle and a charging grid positioned adjacent thereto, a conduit communicating with one end of said containerand electrically insulated from the inner surfaces thereof for introducing a drying gas into the chamber, an outlet conduit extending from the other end of said container, said outlet conduit being electrically insulated from the inner surface of the container and adapted to conduct dried particles and exhaust gas therefrom, and electrical means for applying to the inner surfaces of said container and to said grid an electrical charge of the same polarity, whereby said atomized particles are provided a charge of the same polarity as the inner surfaces of said container.
  • a spray drying apparatus comprising an elongated container forming a drying chamber, the inner surfaces of said container being electrically conductive and the outer surfaces being electrically insulating, means for creating a stream of unipolarly charged atomized particles to be dried within said container at one end thereof, said means comprising a particle inlet nozzle and a charging grid positioned adjacent thereto, a conduit communicating with said container adjacent said one of its ends and electrically insulated therefrom for introducing a drying gas into said chamber, an outletconduit extending from the other end of said container, said outlet conduit being electrically insulated from the inner surfaces of the container and adapted to conduct dried particles and exhaust gas therefrom, and electrical means having a connection to the inner surfaces of said container and to said grid for applying thereto an electrical charge of the same polarity, whereby said atomized particles are provided a charge of the same polarity as the inner surfaces of said container.
  • a spray drying apparatus comprising a container forminga drying chamber, said container including an outer shell and an inner liner supported thereby, said liner being electrically conductive and electrically in-. sulated from the outer shell, means for unipolarly electrically char ing and introducing atomized particles to be dried within the drying chamber bounded by said liner, a conduit communicating with said chamber and electrically insulated from said liner for introducing a drying gas into the chamben'an outlet conduit leading from said chamber electrically insulated from said liner adapted to conduct dried particles and exhaust gas from the chamber, and electrical means for applying to said liner an electrical change of the same polarity as the charge carried by the atomized particles.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Drying Of Solid Materials (AREA)

Description

Dec. 5, 1961 s, ccomvuc JR 3,011,543
SPRAY DRYER Filed July 12, 1957 INVENTOR. Sam/:4 .4 H-"Jaemca; It
l: r" I United States Patent 3,011,543 SPRAY DRYER Samuel L. McCormick, Jr., 1137 Hawks Lane, Indianapolis, Ind. Filed July 12, 1957, Ser. No. 671,513 4 Claims. (Cl. 159-4) This invention relates'generally to spray dryers, and in part1cular to such dryers having a means for restraining the particles from contacting the walls of the drying chamber.
Spray drying has been used with varying degrees of success in a wide variety of industries. It has been used to dry milk, soaps and detergents, pharmaceuticals, fine chemicals, organic and inorganic chemicals, rubber and synthetic latices, clay slips, and other products and materials as Well.
In the soap and detergent industries, for example,
spray drying is a major operation, and the dryers constitute a large percentage of the investment in modern detergent processing equipment, Where the total production of spray dried products is several billion pounds per year. Milk is spray dried in quantities approaching a billion pounds annually, and the annual spray dried production of other foods, coffee, for example, runs into the hundreds of million pounds.
' Spray drying presents several unique problems not encountered in certain other drying technics; Among these problems is the tendency of particles to adhere and accumulate during the drying operation to the surfaces of the drying chamber.
In many spray drying operations a portion of the dispersed particles or droplets strike the drying chamber walls either before or after they are completely dried, and adhere to the Wall. The material adhering to the wall is thus exposed to the hot drying-gas for relatively long periods of time and if the material being dried is heat sensitive, qualities such as taste, odor, biological activity and the like, are lost or impaired. Consequently the material that adheres represents a loss since it is inferior and cannot generally be used.
One attempt to overcome the above-mentioned problem provides for increasing the size of the drying chamber to alford'more travel distance for the particles, and therefore more drying time before they can come in contact with the drying chamber walls. This arrangement, of course, adds to the prime cost of a dryer; An existent dryer-can seldom be modified or converted economically in this manner.
A further attempt at'solution of this problem involves increasing the degree of atomization resulting in smaller particles or droplets to be dried. This inherently leads to smaller productparticle size with a tendency toward dustiness and decreased bulk density which may be un desirable. The temperatures'of the drying gas may also be increased, resulting in an increased drying rate for droplets. However, thus increasing the drying temperature is obviously undesirable for the drying of heat sensi-' tive material.
A further attempt at solution of' the problem of ad-' herence of the particles providesa mechanical device, such as a rotating chain which strikes the side walls of the drying chamber to dislodge material'adhering to them. This arrangement is not completely successful since the chain will not strike all the surfaces of the drying chamber and since particles tend to collect on the chain and its supports. Since it is frequently desirableto dry materials whose final product specifications are such that no economical combination of the factors mentioned above, or others, will give a satisfactory product, the field of application for spray dryers is limited. It is usually necessary to test a new material to be spray dried on a substantial pilot scale before success may be predicted. The present invention provides additional fiexibilityin the application of spray dryers so that almost any material which can be dispersed in a gas can be spray dried.
The primary object of this invention is to improve spray drying technics, particularly with respectto the problems connected with materialsv adhering to walls, which normally occurs. The accomplishment of this object makes possible the construction of spray dryers of more compact design and also gives increased flexibility in operating conditions.
In general the object of the present invention is accomplished by providing the dispersed particles with a unipolar electrical charge and impressing upon the drying chamber Walls an electrical charge of the same polarity as that carried by the atomized particles.
A further object of the present invention is to provide a spray drying apparatus which can successfully spray dry materials which have a relatively 'high tendency to adhere to the drying chamber walls.
A further object of the present invention is to provide a spray drying apparatus in which drying gas having a relatively low inlet temperature may be used, thereby reducing heat exposure of the product.
A further object of the present invention is to provide a spray drying apparatus in which less atomization can be- The full nature of the invention will be understood from the accompanying drawings and the following description and claims: V
FIG. 1 represents a schematic cross sectional illustration of an apparatus employing the present invention.
FIG. 2 is a view similar to FIG. 1, butillustrating a modified form of the invention.
FIG. 3 is a view similar to FIGS. '1 and 2, but illustrating a further modified form of the present invention.
Referring initially to FIG. 1, there isshowngene'rally at 10 a tank or container providing a drying chamber 11.
The inner walls 12 of the chamber 11 are formed of electrically conductive material, such as steel, and the outer surface 13 of the tank'is formed of an electrical insulating material, .which' may preferably also have thermal insulating properties. At the upper end of the drying'chamber there is schematically shown a nozzle or other dispersing or atomizing device; l l'forintroducing into the chamber dispersed particles which are given a unipolar charge by passage through an ionizing grid 15 mounted adjacent the nozzle. Anelectrically non-con-, ducting flange 16 serves to support the nozzle 14 and. electrically insulates the chamber walls from the nozzle.
A drying gas inlet conduit 17 connects with the drying chamber adjacent the upper end thereof, and an electrical; insulating sleeve or coupling 18 serves to electrically in-' sulate the drying chamber walls from the conduit 17. At the bottom of the drying chamber an outlet conduit 19 communicates with the'drying chamber and an insulating coupling 21,.similar to coupling"=18,serves to electrically insulate the dryingchambe'r Walls from the conduit 19. p A direct currentsourceoffelectrical power is shown at-ZZ' having its positive terminal 23 connected to ground and its negative terminal 24 electrically connected to the drying chamber walls and to the ionizing grid by means of wire 26. It will be understood that this arrangement provides a means for impressingv an electrostatic potential upon the drying chamber walls and the grid, and that while the grid and inner walls are illustrated as being at the same electrical potential, other connections with the power source may be made which will establish them at differing potentials. With the walls and grid connected as shown, the polarity of the charge on the drying chamber walls is negative and is of the same polarity as the charge imparted to the dispersed particles or droplets, by the grid as, they are introduced into the drying chamber from the nozzle 14.
In operation, the charged atomized particles are introduced into the chamber after passing through the grid, and heated drying gas enters the chamber from the duct 17. Since the walls of the drying chamber are charged at the same polarity as the particles, they will be restrained from contact with the chamber walls. The spent drying gas containing the entrained dry product passes out of the drying chamber through the outlet duct or conduit 19.
The modified form of the invention shown in FIG. 2 operates identically to that described with reference to FIG. 1, but differs somewhat in the construction of the container or tank. In this form of the apparatus an electrically conducting inner liner 27, which may take the form of a screen, wire mesh or other electrostatically chargeable element, provides the drying chamber inner walls. This liner is supported and electrically insulated from the tank wall 28 by means of electrically insulating spacers 29. Connection of the negative terminal of the power source 22 to the liner 27 is accomplished by wire '26 which passes through a non-conducting flange 31. Wire 26 also serves to connect the power source to an ionizing grid 25 similar to the grid 15.
The apparratus shown in FIG. 3 is a further modified form of the present invention in which the cross sectional dimension of the drying chamber 11a is greatly reduced as compared to this dimension of the drying chamber previously referred to. This spray drying apparatus includes a nozzle 14a for introducing into the drying chamber 1 1a dispersed particles given a unipolar electrical charge by the ionizing grid 15m. A drying gas inlet duct 17: is connected to the top of the cylindrical drying chamber. An outlet duct 19a is similarly connected to the bottom of the drying chamber. The inner surface 12a of the drying chamber is formed of electrical connecting material and is electrically insulated from the ducts 17a and 19a by means of the insulating couplings 18a and 21a, respectively. The outer surface of the drying chamber wall 130: is formed of electrical insulating material, which preferably also has thermal insulating properties. The drying chamber walls have impressed thereon a negative electrical charge which is the polarity of the charge given the particles introduced from the nozzle 14a by passage through the grid.
The operation of this form of the invention is identical to that previously described, but is illustrative of the reduction in size of the drying chamber which is made possible by the means for restraining the particles from contacting the drying chamber walls herein described.
While the invention has been disclosed and described in some detail in the drawings and foregoing description, they are to be considered as illustrative and not restrictive in character, as other modifications may readily suggest themselves by persons skilled, in this art and within the broad scope of the invention, reference being had to the appended claims.
The invention claimed is: v
1., A spray drying apparatus comprising a container forming a drying chamber, the inner surfaces of said container being electrically conductive and the outer surfaces being thermally and electrically insulating, and means. for unipolarly electrically. charging and introducing atomized particles to be dried within said container, a conduit communicating with said container and electrically insulated from the inner surfaces thereof for introducing a drying gas into the chamber, an outlet conduit extending from said container electrically insulated from the inner surface thereof and adapted to conduct dried particles and exhaust gas from the chamber, and electrical means for applying to the inner surfaces of said container an electrical charge of the same polarity as the charge carried by the atomized particles.
2. A spray drying apparatus comprising a container forming a drying chamber, the inner surfaces of said 'container being electrically conductive, means for creating a stream of unipolarly charged atomized particles to be dried within said container, said means comprising a nozzle and a charging grid positioned adjacent thereto, a conduit communicating with one end of said containerand electrically insulated from the inner surfaces thereof for introducing a drying gas into the chamber, an outlet conduit extending from the other end of said container, said outlet conduit being electrically insulated from the inner surface of the container and adapted to conduct dried particles and exhaust gas therefrom, and electrical means for applying to the inner surfaces of said container and to said grid an electrical charge of the same polarity, whereby said atomized particles are provided a charge of the same polarity as the inner surfaces of said container.
3. A spray drying apparatus comprising an elongated container forming a drying chamber, the inner surfaces of said container being electrically conductive and the outer surfaces being electrically insulating, means for creating a stream of unipolarly charged atomized particles to be dried within said container at one end thereof, said means comprising a particle inlet nozzle and a charging grid positioned adjacent thereto, a conduit communicating with said container adjacent said one of its ends and electrically insulated therefrom for introducing a drying gas into said chamber, an outletconduit extending from the other end of said container, said outlet conduit being electrically insulated from the inner surfaces of the container and adapted to conduct dried particles and exhaust gas therefrom, and electrical means having a connection to the inner surfaces of said container and to said grid for applying thereto an electrical charge of the same polarity, whereby said atomized particles are provided a charge of the same polarity as the inner surfaces of said container.
4. A spray drying apparatus comprising a container forminga drying chamber, said container including an outer shell and an inner liner supported thereby, said liner being electrically conductive and electrically in-. sulated from the outer shell, means for unipolarly electrically char ing and introducing atomized particles to be dried within the drying chamber bounded by said liner, a conduit communicating with said chamber and electrically insulated from said liner for introducing a drying gas into the chamben'an outlet conduit leading from said chamber electrically insulated from said liner adapted to conduct dried particles and exhaust gas from the chamber, and electrical means for applying to said liner an electrical change of the same polarity as the charge carried by the atomized particles.
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3238632A (en) * 1961-08-30 1966-03-08 Leybold Anlagen Holding A G Method and apparatus to dry powdery substances under a vacuum using electrical gas discharges
US3496701A (en) * 1967-12-13 1970-02-24 T G Owe Berg Method and apparatus for removing particulates from flowing gases
US4329787A (en) * 1980-01-04 1982-05-18 Newton William A Droplet exploding and freezing apparatus and method
US4809442A (en) * 1985-12-27 1989-03-07 Tdk Corporation Spray drying process and apparatus therefor
US5015332A (en) * 1987-07-06 1991-05-14 Tdk Corporation Spray dryer
US5924216A (en) * 1996-07-11 1999-07-20 Powdering Japan, K.K. Two-stage drying spray dryer
FR3018199A1 (en) * 2014-03-04 2015-09-11 Felix Elefant DEVICE FOR DISTILLING BY POLARIZATION AND NEBULIZATION IN AN ELECTROSTATIC BOTTLE
WO2017079468A1 (en) * 2015-11-03 2017-05-11 Spraying Systems Co. Apparatus and method for spray drying

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1830174A (en) * 1927-01-31 1931-11-03 David D Peebles Desiccating apparatus and method
US1914895A (en) * 1928-07-16 1933-06-20 David D Peebles Desiccating method and apparatus
US2191827A (en) * 1934-04-12 1940-02-27 Carborundum Co Apparatus for applying liquid to fabric
US2781279A (en) * 1951-11-26 1957-02-12 Ransburg Electro Coating Corp Method and apparatus for spray coating of articles

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1830174A (en) * 1927-01-31 1931-11-03 David D Peebles Desiccating apparatus and method
US1914895A (en) * 1928-07-16 1933-06-20 David D Peebles Desiccating method and apparatus
US2191827A (en) * 1934-04-12 1940-02-27 Carborundum Co Apparatus for applying liquid to fabric
US2781279A (en) * 1951-11-26 1957-02-12 Ransburg Electro Coating Corp Method and apparatus for spray coating of articles

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3238632A (en) * 1961-08-30 1966-03-08 Leybold Anlagen Holding A G Method and apparatus to dry powdery substances under a vacuum using electrical gas discharges
US3496701A (en) * 1967-12-13 1970-02-24 T G Owe Berg Method and apparatus for removing particulates from flowing gases
US4329787A (en) * 1980-01-04 1982-05-18 Newton William A Droplet exploding and freezing apparatus and method
US4809442A (en) * 1985-12-27 1989-03-07 Tdk Corporation Spray drying process and apparatus therefor
US5015332A (en) * 1987-07-06 1991-05-14 Tdk Corporation Spray dryer
US5924216A (en) * 1996-07-11 1999-07-20 Powdering Japan, K.K. Two-stage drying spray dryer
FR3018199A1 (en) * 2014-03-04 2015-09-11 Felix Elefant DEVICE FOR DISTILLING BY POLARIZATION AND NEBULIZATION IN AN ELECTROSTATIC BOTTLE
WO2015132483A1 (en) * 2014-03-04 2015-09-11 Elefant Félix Device for distillation by polarization and nebulization in an electrostatic bottle
WO2017079468A1 (en) * 2015-11-03 2017-05-11 Spraying Systems Co. Apparatus and method for spray drying
CN108601363A (en) * 2015-11-03 2018-09-28 喷雾系统公司 Device and method for spray drying
US10279359B2 (en) 2015-11-03 2019-05-07 Spraying Systems Co. Spray dryer with improved exhaust gas filtration system
US10286411B2 (en) 2015-11-03 2019-05-14 Spraying Systems Co. Apparatus and method for spray drying
US10399098B2 (en) 2015-11-03 2019-09-03 Spraying Systems Co. Spray dryer
CN108601363B (en) * 2015-11-03 2022-10-18 喷雾系统公司 Apparatus and method for spray drying
EP3370534B1 (en) * 2015-11-03 2022-12-21 Spraying Systems Co. Apparatus and method for spray drying

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