US881523A - Apparatus for continuous evaporation. - Google Patents
Apparatus for continuous evaporation. Download PDFInfo
- Publication number
- US881523A US881523A US23084604A US1904230846A US881523A US 881523 A US881523 A US 881523A US 23084604 A US23084604 A US 23084604A US 1904230846 A US1904230846 A US 1904230846A US 881523 A US881523 A US 881523A
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- US
- United States
- Prior art keywords
- heating
- chambers
- chamber
- return
- continuous evaporation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000001704 evaporation Methods 0.000 title description 9
- 230000008020 evaporation Effects 0.000 title description 8
- 239000007788 liquid Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 5
- 238000005192 partition Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 2
- GLDQOLDJQPPFQL-UHFFFAOYSA-N 2-[bis(2-carbamimidoylsulfanylethyl)amino]ethyl carbamimidothioate;tetrahydrobromide Chemical compound Br.Br.Br.Br.NC(=N)SCCN(CCSC(N)=N)CCSC(N)=N GLDQOLDJQPPFQL-UHFFFAOYSA-N 0.000 description 1
- 101710083262 Ectin Proteins 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000002144 chemical decomposition reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
Definitions
- chambers are so connected with eac UNITED sTArns rn rnnr OFFICE.
- the present invention relates to an improved apparatus for continuous evaporation.
- the princi le of the evaporation is based on the wel known fact, that, not as heretofore, already evaporated liquid particles are mixed with nonconcentrated liquid and conducted over the same heatingsurfaces, but that all liquid particles are continuously concentrated and continuously placed in contact with new heating-surfaces. From thisit results that the time of heating is shortened as much as possible and the evaporation rendered as quick as possible, so that chemical decompositions are avoided.
- the advantages of this system are in practical use and are used among others in the Yorgau-a paratus. In this apparatus long horizonta tubes are employed in which scale is easily formed, while in the present invention short vertical heating-tubes are used in which scale formation is avoided and in which a number of other essential differences are shown.
- the invention consists in the combination of a plurality of individual evaporators placed in a common shell or casmg, each evaporator being provided with a chamber having heating-surfaces for the ascending and a non-heating chamber for the descending liquid (return-current).
- the airs of other that a non-heating chamber of the first pair is connected with the lower end of the heating-chamber of the second pair and so on, so that the liquid passes successively through all the chambers and is more and more concentrated in the, heating-chambers.
- the dividing-partitions between the individual evaporators do not extend entirely to the upper part ofthe casing, so that the vapors can be drawn off through the cover of the same.
- the heating of the heating-chambers can be accomplished in any suitable manner, either by steam of difierent pressures or by coils or other heating-bodies, preferably, however, by means of vertical tubes and a heated plate which is inclined towards the return-chamber.
- chambers are insulated from the heatingchambers to such an extent that in the former no steam can be generated.
- Figure 1 is a plan-view of one form of the apparatus
- Fig. 2 is a section of a horizontal evaporating apparatus with short straight tubes, in which the return-chambers are of the same size as the heating-chambers
- Figs. 3 and 4 are planviews of an evaporator in which the returnchambers are smaller than the heatingchambers
- Figs. 5 and 6 are respectively a section and a lan-view of an upright evaporator of modi ed form
- Figs. 7 and 8 also show an upright evaporator of still further modified construction.
- a represents the heating tubes, b the steam-space of the heatingchambers and c the space for the vapors.
- d indicates the unheated return-chambers andf the discharge-tube for the vapors.
- the liquid to be evaporated passes through an inlet Q1 into the apparatus and out through an outlet lc.
- Each heating-chamber is separated from the adjacent return-chamber by a partition m, and between the individual evaporators and the pairs of chambers are partitions 0.
- the chambers are arranged in the shape of sectors in a cylindrical shell or casing.
- the liquid enters at i from below into the heatingtubes, runs over the upper inclined heatinglate in downward direction into the noneated adjacent chamber d, enters then into the next following heating-chamber and so on until it is dischar ed at the lower end of the last return-cham er.
- Figs. 7 and 8 re resent also an upright evaporator in whic the heating-chambers form an exterior ring, while the return-chambers are formed in the shape of sectors in the inside spaces.
- the upper heating-plates are inclined in inward direction so that the liquid is conducted into the return-chamber and from the same at the lower end into the next heating-chamber.
- each pair comprising a heatingchamber and a collectingor return-chamber
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
N.-881523. P 'NED.A.10108.
o H.WINTER. ATET MR P APPARATUS FOR CONTINUOUS EVAPORATION.
APPLICATION TILED OCT. 3 1, 1904.
2 SHERR -SHEET 1.
. %IN VENUEW A770fl/VEYS.
rue NORRIS PETERS cm, wasumcnm, n. c
PATENTED MAR. 10, 1908.
No.ss1 ,52s'. v
H. WINTER.
APPARATUS FOR GGNTINUOUS EVAPORATION.
" APPLICATION FILED 001'. 31, 1004.
, 2 BEEEIS-SKBET 2.
WITNESSES! v A j 7 66, 4, ATTORNEYS.
rm: NORRIS PETERS 60-, wnsuuvc'ruu, n. c
chambers are so connected with eac UNITED sTArns rn rnnr OFFICE.
HEINRICH war-Es, OF CHARLOT'TENBURG, GERMANY.
APPARATUS FOR oon rnv'uous EVAPORATION.
To all whom it may concern:
Be it known that I, HEINRICH WINTER, doctor of philosophy, citizen of the German Empire, and a resident of L50 Kantstrasse, Charlottenburg, near Berlin, Germany, have invented new and useful Improvements in Apparatus for Continuous Evaporation, of which the following is a specification.
The present invention relates to an improved apparatus for continuous evaporation. The princi le of the evaporationis based on the wel known fact, that, not as heretofore, already evaporated liquid particles are mixed with nonconcentrated liquid and conducted over the same heatingsurfaces, but that all liquid particles are continuously concentrated and continuously placed in contact with new heating-surfaces. From thisit results that the time of heating is shortened as much as possible and the evaporation rendered as quick as possible, so that chemical decompositions are avoided. The advantages of this system are in practical use and are used among others in the Yorgau-a paratus. In this apparatus long horizonta tubes are employed in which scale is easily formed, while in the present invention short vertical heating-tubes are used in which scale formation is avoided and in which a number of other essential differences are shown.
The invention consists in the combination of a plurality of individual evaporators placed in a common shell or casmg, each evaporator being provided with a chamber having heating-surfaces for the ascending and a non-heating chamber for the descending liquid (return-current). The airs of other that a non-heating chamber of the first pair is connected with the lower end of the heating-chamber of the second pair and so on, so that the liquid passes successively through all the chambers and is more and more concentrated in the, heating-chambers. The dividing-partitions between the individual evaporators do not extend entirely to the upper part ofthe casing, so that the vapors can be drawn off through the cover of the same. The heating of the heating-chambers can be accomplished in any suitable manner, either by steam of difierent pressures or by coils or other heating-bodies, preferably, however, by means of vertical tubes and a heated plate which is inclined towards the return-chamber. The return- Specification or Letters Patent. Application filed October 31, 1904:.
Patented March 10, 1908.
Serial No. 230,846.
chambers are insulated from the heatingchambers to such an extent that in the former no steam can be generated.
In the accompanying drawing, in which different forms of apparatus constructed in accordance with the invention are illustrated diagrammatically, Figure 1 is a plan-view of one form of the apparatus, Fig. 2 is a section of a horizontal evaporating apparatus with short straight tubes, in which the return-chambers are of the same size as the heating-chambers, Figs. 3 and 4 are planviews of an evaporator in which the returnchambers are smaller than the heatingchambers, Figs. 5 and 6 are respectively a section and a lan-view of an upright evaporator of modi ed form, and Figs. 7 and 8 also show an upright evaporator of still further modified construction.
In the drawing a represents the heating tubes, b the steam-space of the heatingchambers and c the space for the vapors.
d indicates the unheated return-chambers andf the discharge-tube for the vapors.
The liquid to be evaporated passes through an inlet Q1 into the apparatus and out through an outlet lc. Each heating-chamber is separated from the adjacent return-chamber by a partition m, and between the individual evaporators and the pairs of chambers are partitions 0.
In the evaporator shown in Figs. 5 and 6 the chambers are arranged in the shape of sectors in a cylindrical shell or casing. The liquid enters at i from below into the heatingtubes, runs over the upper inclined heatinglate in downward direction into the noneated adjacent chamber d, enters then into the next following heating-chamber and so on until it is dischar ed at the lower end of the last return-cham er.
Figs. 7 and 8 re resent also an upright evaporator in whic the heating-chambers form an exterior ring, while the return-chambers are formed in the shape of sectors in the inside spaces. The upper heating-plates are inclined in inward direction so that the liquid is conducted into the return-chamber and from the same at the lower end into the next heating-chamber.
What I claim is:
In an apparatus for continuous evaporation, the combination of a casing and pairs of chambers within said casing spaced from the top thereof, each pair comprising a heatingchamber and a collectingor return-chamber,
the heating-chamber being provided with my invention, I have signed my name in hfiittingl-tubes ang arll1 upplelr h6atiILg-Pigt6 presence of two subscribing Witnesses. o i uey situate t e co ectin c am er r com r nunicating at its lower portioi With the HEINRICH 5 adjacent heating-chamber of the next pair of Witnesses:
chambers. v HENRY HAsPER, In testimony, that I claim the foregoing as An. FRIEDMANN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US23084604A US881523A (en) | 1904-10-31 | 1904-10-31 | Apparatus for continuous evaporation. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US23084604A US881523A (en) | 1904-10-31 | 1904-10-31 | Apparatus for continuous evaporation. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US881523A true US881523A (en) | 1908-03-10 |
Family
ID=2949963
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US23084604A Expired - Lifetime US881523A (en) | 1904-10-31 | 1904-10-31 | Apparatus for continuous evaporation. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US881523A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2707022A (en) * | 1951-01-15 | 1955-04-26 | Whiting Corp | Heater for multiple effect evaporators |
| US2944599A (en) * | 1956-04-04 | 1960-07-12 | Richardsons Westgarth & Co | Flash evaporator |
| US3201332A (en) * | 1962-03-16 | 1965-08-17 | Separator Ab | Plate heat exchanger |
| US3424221A (en) * | 1966-06-06 | 1969-01-28 | Gene W Luce | Apparatus and method for continuous crystallization by evaporation |
| US4004964A (en) * | 1974-04-18 | 1977-01-25 | Unice Machine Company | Multistage continuous vacuum pan |
| WO1985001570A1 (en) * | 1983-09-28 | 1985-04-11 | Folbex Ab | Heat exchanger |
| US5423952A (en) * | 1992-07-22 | 1995-06-13 | T & G Technologies, Inc. | Structure for multiple-effect distillation |
-
1904
- 1904-10-31 US US23084604A patent/US881523A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2707022A (en) * | 1951-01-15 | 1955-04-26 | Whiting Corp | Heater for multiple effect evaporators |
| US2944599A (en) * | 1956-04-04 | 1960-07-12 | Richardsons Westgarth & Co | Flash evaporator |
| US3201332A (en) * | 1962-03-16 | 1965-08-17 | Separator Ab | Plate heat exchanger |
| US3424221A (en) * | 1966-06-06 | 1969-01-28 | Gene W Luce | Apparatus and method for continuous crystallization by evaporation |
| US4004964A (en) * | 1974-04-18 | 1977-01-25 | Unice Machine Company | Multistage continuous vacuum pan |
| WO1985001570A1 (en) * | 1983-09-28 | 1985-04-11 | Folbex Ab | Heat exchanger |
| US5423952A (en) * | 1992-07-22 | 1995-06-13 | T & G Technologies, Inc. | Structure for multiple-effect distillation |
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