US2546381A - Apparatus for concentrating liquids - Google Patents
Apparatus for concentrating liquids Download PDFInfo
- Publication number
- US2546381A US2546381A US731952A US73195247A US2546381A US 2546381 A US2546381 A US 2546381A US 731952 A US731952 A US 731952A US 73195247 A US73195247 A US 73195247A US 2546381 A US2546381 A US 2546381A
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- scraper
- blades
- column
- liquids
- impeller
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- 239000007788 liquid Substances 0.000 title description 23
- 210000001520 comb Anatomy 0.000 description 12
- 230000006872 improvement Effects 0.000 description 6
- 230000009471 action Effects 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229940000425 combination drug Drugs 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000000994 depressogenic effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/22—Evaporating by bringing a thin layer of the liquid into contact with a heated surface
- B01D1/222—In rotating vessels; vessels with movable parts
- B01D1/223—In rotating vessels; vessels with movable parts containing a rotor
- B01D1/225—In rotating vessels; vessels with movable parts containing a rotor with blades or scrapers
Definitions
- Thisinvention relates to certain new and useful improvements in apparatus for concentrating liquids and, more particularly, liquids containingv organic substances which would be impaired if the liquid were subjected to a high temperature for a considerable period of time.
- FIG. 1 is a 'fragmentary vertical sectional view of a preferred form of apparatus for practicing my invention
- Figure 2 is a horizontal vsectional view of the apparatus taken along line 22 of Figure 1;
- Figure 3 is a fragmentary sectional view taken along line 3f-3 of Figure 2;
- Figure 4 is a top plan view., of the apparatus
- Figure 5 is a detail sectional view taken along line SY-t of Figure 4.
- Figure 6 is a horizontal sectional View of a modified form of apparatus constructed in accordance with and embodying the present invention.
- A designates a preferred form of apparatus comprising a preferably cast iron base housing I having a central depressed gear box 2 provided in its bottom wall with a step-bearing 3.
- a cylindrical column I Shrunk or otherwise suitably secured in the base ring and extending upwardly therefro-m in concentric relation to the shaft-bearing 5, is a cylindrical column I preferably constructed of copper, stainless steel, or other suitable material, and provided at its upper end with a pe.
- ripheral flanged head ring 8 having a plurality of uniformly spaced swingable wing bolts w for retentive engagement in complementarily located;
- peripheral slots s formed in a removable cap or dome S preferably of cylindrical form and including a horizontal top wall I 0 which is, in turn, provided with a depending pintle or bearing-stud I I aligned axially with the shaft-bearing 5.
- a cylindrical jacket or shell I2 Surrounding the column I, and fixed at its 10WE er end in the collar 5, is a cylindrical jacket or shell I2, and at its upper end the shell I 2 is secured in a closure-collar I3 mounted around the column I somewhat below the head ring 8, thus forming an intervening jacket space I4 which is adapted to receive steam or other heating medi-- um for heating the column l.
- the steam or other heating agent is preferably supplied to this jacket space III by means of a steam supply pipe I 5 fixed in and extending through the shell I2 adjacent;
- the tube 22 is provided with an end plate 23 which rotatably engages the bearing-stud II, and projecting in'- wardly at the lower end of the ring 8 is an annular horizontal partition vplate 24 centrally bored and provided with a packing ring 25 for glandwise engaging the tube 22.
- the tube 22 is provided with four equally spaced vertical lines of apertures 26, and above the partition plate y24, the tube 22 is further provided with a plurality of circumterenually s paqedeperr.:
- the pair of blades 28 is located along a diametral plane at right angles to the diametral line along which the other pair of impeller blades 28 is located.
- the curvature of the blades 28 is not critical and, for that matter, the blades may have any desired cross-sectional contour, so long as the trailing edge comes into proximity with the inner face of the column 1 along a line substantially to the rear (with respect to the direction of revolution) of the radial line passing through the apertures 26 of such blade.
- the impeller blades 28 are somewhat shorter in vertical length than the column 1 so as to provide a head space :n beneath the partition plate 24, and projecting through the column 'I into this head space a: is a supply line 28 bent over at its inner end so as to discharge the stream of the incoming liquids against the inner face of the column 1.
- the column 'i is provided with a vacuum-line 30 which extends through the head 8 and a discharge line 3
- the teeth 35 of one scraper comb 34 are horizontally located in line with the spaces between the teeth 35 of the other scraper comb 34, so that the liquid material which flows between the teeth 35 of one scraperY comb 34 will be picked up by the teeth 35 of the other scraper comb 34, with the result that the film of liquid being evaporated is kept very thin and maintained at high velocity.
- scraper elements 33 are provided with a suitable number of set screws 38 which extend radially therethrough'for stop-wise engagement against the blade faces, as at 3i', there' by" permitting the outward movement of the.'
- cured blade holder 38 disposed substantially at right angles to the scraper element 33' and provided with a scraper comb 34 substantially similar to the previously described scraper comb 34, except that it is somewhat shorter than the comb 34 and is presented more nearly radially to the inner surface of the column 1, so that somewhat greater scraping pressure may be applied.
- a stream of liquid is admitted through the supply pipe 29 and permitted to iiow down by gravity over the inner face of the column i while the latter is externally heated by admission of steam to the jacket space I4.
- a centrifugal motion is imparted to it by the impeller blades 28, 28', and the scraper combs 34, or 34', as the case may be, in the formation of a thin tubular film against the inner face of the column 1.
- the improvement comprising a tubular impeller to be rotatably mounted co-axially within the column, said impeller having a plu.-v
- scraping 'elements for engagement with the blades for optionally determining the amount of jv outward swinging movement of the scraper combs during impelling action of the blades.
- auxiliary scrapers comprising scraper elements hingedly mounted on selected impeller blades, scraper combs secured to the scraper ele-1 ments, and set screws associated with the scraperelements for engagement with the blades for 'op-f tionally determining the amount of outwardswinging movement ofthe scraper combs during.:v
- auxiliary scrapers comprising scraper elements hingedly mounted on the inner face of selected blades, set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades, said scraper elements being :provided with longitudinal recesses along their outer vertical margins, and flexible scraper' combs retentively engaged in said recesses.
- auxiliary scrapers comprising scraper elements hingedly mounted on the inner face of selected blades, set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades, said scraper elements being provided with longitudinal recesses along their outer margins, and flexible scraper combs retentively engaged in said recesses, said scraper combs being so arranged ⁇ so that the teeth of one scraper comb will track behind the spaces between the teeth of the Iother scraper comb immediately preceding it during rotation of the blades.
- auxiliary scrapers comprising scraper elements hingedly mounted on the inner face of selected blades, set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades, blade holders rigidly secured along the outer vertical margin of the scraper elements and being disposed substantially at right angles to the scraper elements, and scraper combs secured to the blade holders.
- the improvement comprising hinge posts integrally formed upon the inner faces of the blades, scraper elements swingably mounted upon the hinge posts and being recessed along their outer vertical margins, exible scraper combs retentively engaged in the recesses of the scraper elements and having a plurality of unformly spaced teeth, said scraper -combs being of arcuate transverse cross-section and set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades for regulating the amount of outward swinging movement of the scraper combs during impelling action of the blades.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
March 27, 1951 G. G. zAHM APPARATUS FOR coNcENTRATING LIQUIDs Filed March 5, `1947' Patented Mar. 27, H1951 UNITED STATES PATENT OFFICE APPARATUS FOR CONCENTRATIG LQUDS George G. Zalm), Buffalo, N. Y., assignor toHurd l(riorporation, New York, N. Y., a corporation of Delaware Application March 3, 1947, Serial No. 731,952
.v v '7 Claims. n Y. 1 Y i Thisinvention relates to certain new and useful improvements in apparatus for concentrating liquids and, more particularly, liquids containingv organic substances which would be impaired if the liquid were subjected to a high temperature for a considerable period of time.
It is the primary object of this invention to provide apparatus for treating organic solutions and colloidal liquids, whereby the liquid content in the same may be reduced quickly and economically and without impairing the chemical constituency, taste, or quality of the solutions or liquids'.
It is a further object of the present invention to provide apparatus of the type and for the purposes stated in which entrain'ment is substantially eliminated.
It is a further object of this invention to provide means for causing liquids of the type stated to travel over a heat exchange surface under vacuum at high velocity, in a relatively thin nlm, and without building up a static coating on the heat exchange surface.
The above and other objects will become more fully apparent 'from the following specification which, by way of illustration rather than limitation, sets forth preferred processes and preferred forms of apparatus constituting embodiments of the present invention, the scope of which is defined in the appended claims.
In the accompanying drawing:
f Figure 1 is a 'fragmentary vertical sectional view of a preferred form of apparatus for practicing my invention;
Figure 2 is a horizontal vsectional view of the apparatus taken along line 22 of Figure 1;
Figure 3 is a fragmentary sectional view taken along line 3f-3 of Figure 2;
Figure 4 is a top plan view., of the apparatus;
Figure 5 is a detail sectional view taken along line SY-t of Figure 4; and
Figure 6 is a horizontal sectional View of a modified form of apparatus constructed in accordance with and embodying the present invention.
In its general organization, A designates a preferred form of apparatus comprising a preferably cast iron base housing I having a central depressed gear box 2 provided in its bottom wall with a step-bearing 3. Welded or otherwise secured upon the upper face of the housing I in closure-forming disposition across the top of the gear box 2 is an upstanding base ring 4 having ,a vertical shaft-bearing 5 axially .aligned with the step=bearing 3, and around its Vupper peripheral-f margin the base ring I is integrally provided with a diametrally enlarged, upwardly extending collar 6. Shrunk or otherwise suitably secured in the base ring and extending upwardly therefro-m in concentric relation to the shaft-bearing 5, is a cylindrical column I preferably constructed of copper, stainless steel, or other suitable material, and provided at its upper end with a pe.
ripheral flanged head ring 8 having a plurality of uniformly spaced swingable wing bolts w for retentive engagement in complementarily located;
peripheral slots s formed in a removable cap or dome S preferably of cylindrical form and including a horizontal top wall I 0 which is, in turn, provided with a depending pintle or bearing-stud I I aligned axially with the shaft-bearing 5.
Surrounding the column I, and fixed at its 10WE er end in the collar 5, is a cylindrical jacket or shell I2, and at its upper end the shell I 2 is secured in a closure-collar I3 mounted around the column I somewhat below the head ring 8, thus forming an intervening jacket space I4 which is adapted to receive steam or other heating medi-- um for heating the column l. The steam or other heating agent is preferably supplied to this jacket space III by means of a steam supply pipe I 5 fixed in and extending through the shell I2 adjacent;
its upper end, the excess steam and water of condensation being withdrawn from the lower endl of the jacket space lil by a discharge pipev I6'.
threaded through the collar 6.
Rotatably mounted at its lower end in the.
tures 21, so that the dome 9 communicates drectly with the interior of the tube 22, but does not communicate directly with the annular vapor space between the outer face of the tube 22 and the inner face of column 1.
Welded to the outer'face of the impeller tube 22 just ahead of each vertical line of apertures 26 (reference being had to the direction of rotation of the impeller tube 22 as shown by the inner arrow in Figure 2) are pairs of diametrally opposed impeller blades 28, 28', which curve outwardly and rearwardly in overlying relation to the associated line of apertures 28 terminating in almost tangential relation to the inner face of the column 1, but having a slight amount of clearance, for purposes presently more fully appearing. Said impeller blades 28, 28', have been more fully set forth in rny copending application, Serial No. 575,512,led January 31, 1945.
It should be noted in this connection that the pair of blades 28 is located along a diametral plane at right angles to the diametral line along which the other pair of impeller blades 28 is located. Furthermore, the curvature of the blades 28 is not critical and, for that matter, the blades may have any desired cross-sectional contour, so long as the trailing edge comes into proximity with the inner face of the column 1 along a line substantially to the rear (with respect to the direction of revolution) of the radial line passing through the apertures 26 of such blade. Furthermore, the impeller blades 28 are somewhat shorter in vertical length than the column 1 so as to provide a head space :n beneath the partition plate 24, and projecting through the column 'I into this head space a: is a supply line 28 bent over at its inner end so as to discharge the stream of the incoming liquids against the inner face of the column 1. Finally, the column 'i is provided with a vacuum-line 30 which extends through the head 8 and a discharge line 3| which extends through the base-ring 4, both being connected, respectively', to conventional high vacuum pumping equipment and liquid storage or packaging equipment (not shown). y
Formed integrally with, or otherwise xed upon the inner faces of, the blades 28, is a vertically aligned series of inwardly projecting hinge` posts 32 for swingably supporting Vscraper elements 33 longitudinally recessed alongV their outer vertical margins for retentively receiving relatively flexible scraper combs 34 having a plurality of uniormly spaced teeth 35. The teeth 35 of one scraper comb 34 are horizontally located in line with the spaces between the teeth 35 of the other scraper comb 34, so that the liquid material which flows between the teeth 35 of one scraperY comb 34 will be picked up by the teeth 35 of the other scraper comb 34, with the result that the film of liquid being evaporated is kept very thin and maintained at high velocity. Furthermore, additional downward velocity is imparted thereto, and the formation of a static coating upon the" heat exchange surface of column 'l is prevented. Finally, the scraper elements 33 are provided with a suitable number of set screws 38 which extend radially therethrough'for stop-wise engagement against the blade faces, as at 3i', there' by" permitting the outward movement of the.'
cured blade holder 38 disposed substantially at right angles to the scraper element 33' and provided with a scraper comb 34 substantially similar to the previously described scraper comb 34, except that it is somewhat shorter than the comb 34 and is presented more nearly radially to the inner surface of the column 1, so that somewhat greater scraping pressure may be applied.
In operation, a stream of liquid is admitted through the supply pipe 29 and permitted to iiow down by gravity over the inner face of the column i while the latter is externally heated by admission of steam to the jacket space I4. As the liquid flows downwardly, a centrifugal motion is imparted to it by the impeller blades 28, 28', and the scraper combs 34, or 34', as the case may be, in the formation of a thin tubular film against the inner face of the column 1.
During its flow from the supply line 29 to the discharge line 3l, the stream of liquid is subjected to high vacuum and a substantial'portion will pass off as Vapor through the apertures 2li;` as diagrammatically indicated byy the outer` arrows in Figure 2, the kVapor flowing upwardly through the tube 22 and the apertures 21 into the dome 9 and thence into the vacuum line 33. The,
clearances between the outer edges of the blades 28 and the face of the column 'l permit portions of the liquid to escape from the influence of the blades and form the thin lm extending from the rear side of each blade to the front of the next` following blade 28. The liquid forming this thin annular layer is subjected to the rapid evaporating effect of the heated column 1 and the production of a static film or coating on the heat exchange surface of column 1 is prevented.
It should be understood that changes and.
modifications both inthe methods, as well as in the form, construction, arrangement, and com-- bination of the several parts, of the apparatus for evaporating or concentrating liquids may be made and substituted for those herein shown and.
described without departing from the nature and .principle of the present invention.
Having thus described my invention, what I claim and desire to secureby Letters Patent is:
1. For use with a cylindrical concentrating column, the improvement comprising a tubular impeller to be rotatably mounted co-axially within the column, said impeller having a plu.-v
elements hingedly mounted on'selected impeller;
blades, scraper combs secured to the scraper `elements, and adjustment means associated with the;
scraping 'elements for engagement with the blades for optionally determining the amount of jv outward swinging movement of the scraper combs during impelling action of the blades. 'a 3. For use in apparatus for concentrating liquids having impeller blades, the improvementcomprising auxiliary scrapers comprising scraper elements hingedly mounted on selected impeller blades, scraper combs secured to the scraper ele-1 ments, and set screws associated with the scraperelements for engagement with the blades for 'op-f tionally determining the amount of outwardswinging movement ofthe scraper combs during.:v
impelling action of the blades.
4. For use in apparatus for concentrating:
liquids having outwardly and rearwardly curved impeller blades, the improvement comprising auxiliary scrapers comprising scraper elements hingedly mounted on the inner face of selected blades, set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades, said scraper elements being :provided with longitudinal recesses along their outer vertical margins, and flexible scraper' combs retentively engaged in said recesses.
5. For use in apparatus for concentrating liquids having outwardly and rearwardly curved impeller blades, the improvement comprising auxiliary scrapers comprising scraper elements hingedly mounted on the inner face of selected blades, set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades, said scraper elements being provided with longitudinal recesses along their outer margins, and flexible scraper combs retentively engaged in said recesses, said scraper combs being so arranged `so that the teeth of one scraper comb will track behind the spaces between the teeth of the Iother scraper comb immediately preceding it during rotation of the blades.
6. For use in apparatus for concentrating liquids having outwardly and rearwardly curved impeller blades, the improvement comprising auxiliary scrapers comprising scraper elements hingedly mounted on the inner face of selected blades, set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades, blade holders rigidly secured along the outer vertical margin of the scraper elements and being disposed substantially at right angles to the scraper elements, and scraper combs secured to the blade holders.
7. For use in apparatus for concentrating liquids having outwardly and rearwardly curved impeller blades, the improvement comprising hinge posts integrally formed upon the inner faces of the blades, scraper elements swingably mounted upon the hinge posts and being recessed along their outer vertical margins, exible scraper combs retentively engaged in the recesses of the scraper elements and having a plurality of unformly spaced teeth, said scraper -combs being of arcuate transverse cross-section and set screws extending radially through the scraper elements for stop-wise engagement against the inner face of the blades for regulating the amount of outward swinging movement of the scraper combs during impelling action of the blades.
GEORGE G. ZAHM.
REFERENCES CITED The following references are of record in the le of this patent:
UNITED STATES PATENTS Number Name Date 613,382 Meinhausen Nov. 1, 1898 1,308,819 Taylor July 8, 1919 1,405,085 Zahm Jan. 31, 1922 1,440,548 Mellott Jan. 2, 1923 1,466,579 Collyer Aug. 28, 1923 1,672,218 How June 5, 1928 1,853,451 Overton Apr. 12, 1932 1,873,833 Fell Aug. 23, 1932 2,024,299 Metcalfe-Shaw Dec. 17, 1935 2,032,785 Zorn et al Mar. 3, 1936 2,306,265 Heald Dec. 22, 1942 FOREIGN PATENTS Number Country Date 38,892 Norway Feb. 11, 1924
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US731952A US2546381A (en) | 1947-03-03 | 1947-03-03 | Apparatus for concentrating liquids |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US731952A US2546381A (en) | 1947-03-03 | 1947-03-03 | Apparatus for concentrating liquids |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2546381A true US2546381A (en) | 1951-03-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US731952A Expired - Lifetime US2546381A (en) | 1947-03-03 | 1947-03-03 | Apparatus for concentrating liquids |
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| US (1) | US2546381A (en) |
Cited By (38)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2807321A (en) * | 1952-11-04 | 1957-09-24 | Bayer Ag | Feeding means for evaporators |
| US2812019A (en) * | 1954-09-22 | 1957-11-05 | Rodney Hunt Machine Co | Treatment of lecithin |
| DE967461C (en) * | 1952-04-05 | 1957-12-19 | Basf Ag | Device for the evaporation and subsequent condensation of liquids, especially mixtures, in thin layers |
| US2822039A (en) * | 1951-10-18 | 1958-02-04 | Barbareschi Carlo | Evaporators-condensers |
| US2866499A (en) * | 1955-08-01 | 1958-12-30 | Du Pont | Apparatus and processes for concentrating and evaporating liquids |
| US2942656A (en) * | 1956-11-28 | 1960-06-28 | Bayer Ag | Film evaporator |
| US2955990A (en) * | 1956-03-15 | 1960-10-11 | Arthur F Smith | Distilling apparatus and method |
| US2974725A (en) * | 1954-05-04 | 1961-03-14 | Bayer Ag | Process and apparatus for continuously obtaining dry materials |
| US2993480A (en) * | 1957-07-31 | 1961-07-25 | Huet Andre | Tubular evaporator |
| US3020211A (en) * | 1958-11-28 | 1962-02-06 | Arthur F Smith | Film-forming and wiping distillation process and apparatus for carrying out the same |
| US3054444A (en) * | 1959-03-09 | 1962-09-18 | Frank E Robbins | Wiper blade construction for wiped film liquid processors |
| US3060107A (en) * | 1958-08-11 | 1962-10-23 | Arthur F Smith | Thin film distillation apparatus |
| US3067812A (en) * | 1959-03-23 | 1962-12-11 | Monsanto Chemcial Company | Apparatus for devolatizing viscous fluids |
| US3080303A (en) * | 1958-04-02 | 1963-03-05 | Standard Oil Co | Fractionator with plastic spinning band |
| US3090732A (en) * | 1958-05-07 | 1963-05-21 | Bayer Ag | Construction and arrangement of wipers in thin-film evaporators |
| US3130108A (en) * | 1960-11-07 | 1964-04-21 | Blaw Knox Co | Rotating blade type evaporators |
| US3180399A (en) * | 1961-10-27 | 1965-04-27 | Rodney Hunt Machine Co | Thin film thermal processor |
| US3180398A (en) * | 1961-10-05 | 1965-04-27 | Rodney Hunt Machine Co | Thin film thermal processor |
| US3190817A (en) * | 1957-08-12 | 1965-06-22 | Gen Electric | Compression distillation apparatus |
| US3199575A (en) * | 1961-11-02 | 1965-08-10 | Luwa Ag | Oscillatory rotor blade for treatment of fluent material in thin layers |
| US3199574A (en) * | 1960-11-14 | 1965-08-10 | Luwa Ag | Falling film-evaporators and rotor structure therefor |
| US3211209A (en) * | 1962-10-16 | 1965-10-12 | Monsanto Co | Apparatus for changing the volatile content of viscous materials |
| US3316958A (en) * | 1964-04-22 | 1967-05-02 | Henry Balfour And Company Ltd | Film molecular stills and evaporators |
| US3334680A (en) * | 1965-06-07 | 1967-08-08 | Head Wrightson & Co Ltd | Rotary wiped film evaporator |
| US3396085A (en) * | 1966-07-21 | 1968-08-06 | Ritter Pfaudler Corp | Wiped film evaporator |
| US3474850A (en) * | 1966-10-14 | 1969-10-28 | Bayer Ag | Liquid film evaporator |
| FR2039823A5 (en) * | 1969-03-21 | 1971-01-15 | Luwa Ag | |
| US3612142A (en) * | 1965-01-15 | 1971-10-12 | Chatillon Italiana Fibre | Process and apparatus for continuously polycondensing or polymerizing monomers |
| US3997406A (en) * | 1973-10-19 | 1976-12-14 | Kostas Savas Arvanitakis | Evaporating apparatus |
| DE2823129A1 (en) * | 1977-06-07 | 1978-12-21 | Buehler Ag Geb | THICK FILM EVAPORATOR AND METHOD FOR OPERATING IT |
| DE3037875A1 (en) * | 1979-10-11 | 1981-04-23 | Tokyo Shibaura Denki K.K., Kawasaki, Kanagawa | WIPER BLADE FOR A THIN FILM DRYER |
| US20100178220A1 (en) * | 2007-11-26 | 2010-07-15 | Auterra, Inc. | Metal alkoxides, apparatus for manufacturing metal alkoxides, related methods and uses thereof |
| US20120037488A1 (en) * | 2010-07-21 | 2012-02-16 | Aquaback Technologies Inc. | Distiller |
| US20190247823A1 (en) * | 2018-02-09 | 2019-08-15 | Buss-Sms-Canzler Gmbh | Device for the thermal treatment of viscous material, in particular for the thermal separation of material components contained in viscous material |
| US11173416B2 (en) * | 2019-03-29 | 2021-11-16 | Julian Alexander Bublies | Short-path evaporator |
| US11241637B2 (en) * | 2019-08-12 | 2022-02-08 | Buss-Sms-Canzler Gmbh | Device for the thermal treatment of material, in particular for the thermal separation of material components contained in the material |
| US20220176267A1 (en) * | 2020-12-08 | 2022-06-09 | Agustus Berman Shelander | Mesh baffle for wiped film evaporator |
| US20230167367A1 (en) * | 2020-04-07 | 2023-06-01 | Vance E. McClure | Reaction Vessel for Liquid Phase Catalytic Pyrolysis of Polymers |
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| US2032785A (en) * | 1932-06-20 | 1936-03-03 | Low Temperature Proc Company | Method of and apparatus for disassociating the components of solutions and mixtures |
| US2306265A (en) * | 1941-04-17 | 1942-12-22 | Colgate Palmolive Peet Co | Degasifying viscous compositions |
-
1947
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2822039A (en) * | 1951-10-18 | 1958-02-04 | Barbareschi Carlo | Evaporators-condensers |
| DE967461C (en) * | 1952-04-05 | 1957-12-19 | Basf Ag | Device for the evaporation and subsequent condensation of liquids, especially mixtures, in thin layers |
| US2807321A (en) * | 1952-11-04 | 1957-09-24 | Bayer Ag | Feeding means for evaporators |
| US2974725A (en) * | 1954-05-04 | 1961-03-14 | Bayer Ag | Process and apparatus for continuously obtaining dry materials |
| US2812019A (en) * | 1954-09-22 | 1957-11-05 | Rodney Hunt Machine Co | Treatment of lecithin |
| US2866499A (en) * | 1955-08-01 | 1958-12-30 | Du Pont | Apparatus and processes for concentrating and evaporating liquids |
| US2955990A (en) * | 1956-03-15 | 1960-10-11 | Arthur F Smith | Distilling apparatus and method |
| US2942656A (en) * | 1956-11-28 | 1960-06-28 | Bayer Ag | Film evaporator |
| US2993480A (en) * | 1957-07-31 | 1961-07-25 | Huet Andre | Tubular evaporator |
| US3190817A (en) * | 1957-08-12 | 1965-06-22 | Gen Electric | Compression distillation apparatus |
| US3080303A (en) * | 1958-04-02 | 1963-03-05 | Standard Oil Co | Fractionator with plastic spinning band |
| US3090732A (en) * | 1958-05-07 | 1963-05-21 | Bayer Ag | Construction and arrangement of wipers in thin-film evaporators |
| US3060107A (en) * | 1958-08-11 | 1962-10-23 | Arthur F Smith | Thin film distillation apparatus |
| US3020211A (en) * | 1958-11-28 | 1962-02-06 | Arthur F Smith | Film-forming and wiping distillation process and apparatus for carrying out the same |
| US3054444A (en) * | 1959-03-09 | 1962-09-18 | Frank E Robbins | Wiper blade construction for wiped film liquid processors |
| US3067812A (en) * | 1959-03-23 | 1962-12-11 | Monsanto Chemcial Company | Apparatus for devolatizing viscous fluids |
| US3130108A (en) * | 1960-11-07 | 1964-04-21 | Blaw Knox Co | Rotating blade type evaporators |
| US3199574A (en) * | 1960-11-14 | 1965-08-10 | Luwa Ag | Falling film-evaporators and rotor structure therefor |
| US3180398A (en) * | 1961-10-05 | 1965-04-27 | Rodney Hunt Machine Co | Thin film thermal processor |
| US3180399A (en) * | 1961-10-27 | 1965-04-27 | Rodney Hunt Machine Co | Thin film thermal processor |
| US3199575A (en) * | 1961-11-02 | 1965-08-10 | Luwa Ag | Oscillatory rotor blade for treatment of fluent material in thin layers |
| US3211209A (en) * | 1962-10-16 | 1965-10-12 | Monsanto Co | Apparatus for changing the volatile content of viscous materials |
| US3316958A (en) * | 1964-04-22 | 1967-05-02 | Henry Balfour And Company Ltd | Film molecular stills and evaporators |
| US3612142A (en) * | 1965-01-15 | 1971-10-12 | Chatillon Italiana Fibre | Process and apparatus for continuously polycondensing or polymerizing monomers |
| US3334680A (en) * | 1965-06-07 | 1967-08-08 | Head Wrightson & Co Ltd | Rotary wiped film evaporator |
| US3396085A (en) * | 1966-07-21 | 1968-08-06 | Ritter Pfaudler Corp | Wiped film evaporator |
| US3474850A (en) * | 1966-10-14 | 1969-10-28 | Bayer Ag | Liquid film evaporator |
| FR2039823A5 (en) * | 1969-03-21 | 1971-01-15 | Luwa Ag | |
| US3695327A (en) * | 1969-03-21 | 1972-10-03 | Luwa Ag | Wiped thin film evaporation and treatment apparatus |
| US3997406A (en) * | 1973-10-19 | 1976-12-14 | Kostas Savas Arvanitakis | Evaporating apparatus |
| DE2823129A1 (en) * | 1977-06-07 | 1978-12-21 | Buehler Ag Geb | THICK FILM EVAPORATOR AND METHOD FOR OPERATING IT |
| DE3037875A1 (en) * | 1979-10-11 | 1981-04-23 | Tokyo Shibaura Denki K.K., Kawasaki, Kanagawa | WIPER BLADE FOR A THIN FILM DRYER |
| US9028768B2 (en) * | 2007-11-26 | 2015-05-12 | Auterra, Inc. | Metal alkoxides, apparatus for manufacturing metal alkoxides, related methods and uses thereof |
| US20100178220A1 (en) * | 2007-11-26 | 2010-07-15 | Auterra, Inc. | Metal alkoxides, apparatus for manufacturing metal alkoxides, related methods and uses thereof |
| US20120037488A1 (en) * | 2010-07-21 | 2012-02-16 | Aquaback Technologies Inc. | Distiller |
| US8858758B2 (en) * | 2010-07-21 | 2014-10-14 | Aquaback Technologies, Inc. | Distiller |
| US9770676B2 (en) | 2010-07-21 | 2017-09-26 | Aquaback Technologies, Inc. | Distiller |
| JP2019166518A (en) * | 2018-02-09 | 2019-10-03 | ブース−エスエムエス−カンツラー ゲゼルシャフト ミット ベシュレンクテル ハフツング | Device for heat-treating, viscous material, particularly, thermally separating material components contained in a viscous material |
| CN110124340A (en) * | 2018-02-09 | 2019-08-16 | 巴斯-Sms-坎兹勒公司 | For being heat-treated the device of viscous and dense material, especially thermal release material component contained by it |
| US20190247823A1 (en) * | 2018-02-09 | 2019-08-15 | Buss-Sms-Canzler Gmbh | Device for the thermal treatment of viscous material, in particular for the thermal separation of material components contained in viscous material |
| US10821414B2 (en) * | 2018-02-09 | 2020-11-03 | Buss-Sms-Canzler Gmbh | Device for the thermal treatment of viscous material, in particular for the thermal separation of material components contained in viscous material |
| CN110124340B (en) * | 2018-02-09 | 2021-05-18 | 巴斯-Sms-坎兹勒公司 | Device for the thermal treatment of viscous materials, in particular for the thermal separation of the components thereof |
| US11173416B2 (en) * | 2019-03-29 | 2021-11-16 | Julian Alexander Bublies | Short-path evaporator |
| US11241637B2 (en) * | 2019-08-12 | 2022-02-08 | Buss-Sms-Canzler Gmbh | Device for the thermal treatment of material, in particular for the thermal separation of material components contained in the material |
| US20230167367A1 (en) * | 2020-04-07 | 2023-06-01 | Vance E. McClure | Reaction Vessel for Liquid Phase Catalytic Pyrolysis of Polymers |
| US12312539B2 (en) * | 2020-04-07 | 2025-05-27 | Vance E. McClure | Reaction vessel for liquid phase catalytic pyrolysis of polymers |
| US20220176267A1 (en) * | 2020-12-08 | 2022-06-09 | Agustus Berman Shelander | Mesh baffle for wiped film evaporator |
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