US807767A - Vacuum evaporating apparatus. - Google Patents
Vacuum evaporating apparatus. Download PDFInfo
- Publication number
- US807767A US807767A US24229605A US1905242296A US807767A US 807767 A US807767 A US 807767A US 24229605 A US24229605 A US 24229605A US 1905242296 A US1905242296 A US 1905242296A US 807767 A US807767 A US 807767A
- Authority
- US
- United States
- Prior art keywords
- liquor
- chamber
- pipe
- effect
- separating
- 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 10
- 239000000463 material Substances 0.000 description 8
- 150000003839 salts Chemical class 0.000 description 6
- 238000010276 construction Methods 0.000 description 2
- 239000002178 crystalline material Substances 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0018—Evaporation of components of the mixture to be separated
- B01D9/0031—Evaporation of components of the mixture to be separated by heating
Definitions
- This invention relates to vacuum evaporating apparatus and relates especially to apparatus for evaporating and separating salt and other similar material from solutions, the apparatus being adapted for use as a single or multiple etect.
- 1 is a supplytank containing a thin or unconcentrated liquor, which is supplied to the pipe 2 to the automatic level-gage 4., the valve 3 serving to regulate the supply of thin liquor.
- This levelgage having the construction and operation referred to in detail in my prior patents is connected with the effect by the pipes 5 and7 and operates to supply the thin liquor in the desired quantities through the pipe 6 to the jacketed downtake 8.
- the effect may comprise the uptakes 9, having the usual steamjacket and heating-tubes and communicating at their lower ends with the liquor-chamber 15, preferably having the pyramidal or downwardly-tapering form illustrated,this liquor-chamber being, as indicated, provided with suitable brackets to support the eifect in connection with the 'pillars 16.
- the uptak'es are also connected with the vaporchamber 12 and vapor-pipe 13 of usual construction.
- the centrally-located downtake 8 is used to connect the vapor and liquor chambers, this downtake being preferably jacketed, and a circulation of thin liquor taking place through the jacket and entering through the supply-pipe 6, and after being heated by the liquor in the downtake, which is thereby cooled to some extent, this liq'uor in the jacket passes through the pipe 11 and into the liquor-chamber past the two regulating-valves 14:.
- Asuitable gage-glass 10 may be used in connection with the effect, if desired.
- a plurality of closed separating-chambers 22 are preferably used in connection with each eiect for effecting the continuous separation of the salt or other crystalline material from the concentrated liquor.
- Each oi' these chambers, as indicated. is formed of sheet metal and may be provided with an inclined screen 25, the discharge-door 24 being indicated at the lower part of the chamber for removing the material from time to time.
- An .eyeglass 23 allows the observation of the interior condition oi' the chamber from time to time, and a suitable valve or vacuum break 2O enables the chamber to be brought to atmospheric pressure when desired.
- These chambers are preferably operated alternately, and concentrated liquor is taken from the liquorchamber through the circulating-pipe 17 by means of the circulating-pump 18 and forced through the circulating-pipe 19 past the valve 21, for instance, and through the guarded inlet indicated into the separating-chamber.
- This inlet which may have the enlarged elbow form indicated, is preferably so shaped and directed into the chamber that'the hot liquor entering through the circulating-pipe is gently discharged in a horizontal direction toward the side of the chamber and away from the outlets. The result is that there is a substantially quiescent body of liquor which may nearly lill the chamber, as indicated, and which allows the gradual settling or deposition oi' the crystallized material contained in the liquor entering the chamber.
- Suitable outlets are arranged adjacent the normal upper level of the liquor in the separating-chamber, the valved outlets 26 being indicated as connecting with the return-pipe 28, which may discharge this cleared liquor taken from the separating-chamber into the downtake or other part of the effect for further treatment.
- This is the normal operation of the device, one separating-chamber acting as a quiescent settlingchamber constantly supplied with liquor from the eiect through the guarded inlet of the circulating-pipe and constantly having the cleared liquor taken off in the proper quantities through the valved outlet adjacent the upper level of the liquor in the chamber.
- the Valve 21 in the circulating-pipe is shut and the corresponding valve leading to the other chamber opened, so as to start that chamber into normal operation.
- the liquor may then be removed from the filled chamber by opening the valve 29, leading into the drain-pipe IOO IIO
- this liquor may, if desired, be withdrawn through the valve 27, governing the outlet indicated, which leads into the discharge-pipe 34 and discharge-pump, and, indeed, in some work it is desirable to continuously withdraw some liquor through this valved outlet and discharge pipe and feed it to the succeeding e'ectof the multiple-effect apparatus, so as to effect a continual feeding of liquor from one effect to the succeeding one of the series.
- an effect comprising a vapor-chamber, a liquorchamber, uptakes and a jacketed downtake, means to supply thin liquor to said effect, a plurality of separating chambers having screens therein, a circulating-pipe and pump to supply concentrated liquor from said effect to either one of said chambers through a guarded inlet adjacent the top of said chamber, a return-pipe having a valved outlet adjacent the top of said chamber and a valved drain-pipe in the bottom of said chamber, a valved discharge-pipe and pump to discharge liquor fromv said chamber into a succeeding effect and valved connections between said drain pipe and said return and discharge pipes.
- an effect means to supplyliquor to said elect, a plurality of separating-chambers, circulating means to supply concentrated liquor from said effect to either one of said chambers to produce a substantially quiescent body of liquor in the same, an outlet-duct adjacent to the top of said chamber and pipes connecting with said outlet and leading to said effect or to a succeeding treating apparatus.
- an effeet means to supply liquor to said effect, a separating-chamber adjacent to said effect, a ci rculating-pipe to supply concentrated liquor from said effect to said separating-chamber to form a substantially quiescent body of liquor therein, a valved outlet-duct adjacent to the top of said chamber and communicating with a return-pipe leading to said eect, and a discharge-pump connecting with a succeeding treating apparatus and receiving liquor from the upper part of said separatingchamber.
- an effect means to supply liquor to said effect, a closedseparating-chamber having a screen, means to supply concentrated liquor from said effect to said separating-chamber, an outletduct in the upper part of said chamberl connecting with a return-pipe leading to said eect and with a discharge-pipe leading to a succeeding treating apparatus, a vacuumbreak and a valved drain-pipe on said separating-chamber.
- aseparating-chamber In vacuum evaporating apparatus, aseparating-chamber, an outlet-duct taking liquor from the upper part of said chamber, a circulating-pipe to supply concentrated liquor from an evaporating apparatus to the upper part of said separating-chamber to form a substantially quiescent body of liquor therein to eect the precipitation of material from said liquor.
Landscapes
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
No. 807,767.. PATBNTEDDBC. 19, 1905.
G. ORDWAY.
VACUUM BVAPORATING APPARATUS. APPLIdATIoN FILED JAN. 23. A1905.
y vwww lasss: |Nv NToR MMMTORNEYS UNITED STATES PATENT OFFICE- Specication of Letters Patent.
Patented Dec. 19, 1905.
Application filed January 23, 1905. Serial No. 242,296.
To @ZZ whom it may concern.'
Be it known that I, CHARLES ORDWAY, a citizen of the United States, and a resident of New York city, county and State of New York, have invented certain new and useful Improvements in Vacuum Evaporating Apparatus, of which the following is a specification, taken in connection with the accompanying drawing, which forms a part of the same.
This invention relates to vacuum evaporating apparatus and relates especially to apparatus for evaporating and separating salt and other similar material from solutions, the apparatus being adapted for use as a single or multiple etect.
In the accompanying drawing, illustrating an embodiment of this invention in elevation, parts being shown in section, 1 is a supplytank containing a thin or unconcentrated liquor, which is supplied to the pipe 2 to the automatic level-gage 4., the valve 3 serving to regulate the supply of thin liquor. This levelgage having the construction and operation referred to in detail in my prior patents is connected with the effect by the pipes 5 and7 and operates to supply the thin liquor in the desired quantities through the pipe 6 to the jacketed downtake 8. As illustrated, the effect may comprise the uptakes 9, having the usual steamjacket and heating-tubes and communicating at their lower ends with the liquor-chamber 15, preferably having the pyramidal or downwardly-tapering form illustrated,this liquor-chamber being, as indicated, provided with suitable brackets to support the eifect in connection with the 'pillars 16. The uptak'es are also connected with the vaporchamber 12 and vapor-pipe 13 of usual construction. As indicated, the centrally-located downtake 8 is used to connect the vapor and liquor chambers, this downtake being preferably jacketed, and a circulation of thin liquor taking place through the jacket and entering through the supply-pipe 6, and after being heated by the liquor in the downtake, which is thereby cooled to some extent, this liq'uor in the jacket passes through the pipe 11 and into the liquor-chamber past the two regulating-valves 14:. Asuitable gage-glass 10 may be used in connection with the effect, if desired.
A plurality of closed separating-chambers 22 are preferably used in connection with each eiect for effecting the continuous separation of the salt or other crystalline material from the concentrated liquor. Each oi' these chambers, as indicated. is formed of sheet metal and may be provided with an inclined screen 25, the discharge-door 24 being indicated at the lower part of the chamber for removing the material from time to time. An .eyeglass 23 allows the observation of the interior condition oi' the chamber from time to time, and a suitable valve or vacuum break 2O enables the chamber to be brought to atmospheric pressure when desired. These chambers are preferably operated alternately, and concentrated liquor is taken from the liquorchamber through the circulating-pipe 17 by means of the circulating-pump 18 and forced through the circulating-pipe 19 past the valve 21, for instance, and through the guarded inlet indicated into the separating-chamber. This inlet, which may have the enlarged elbow form indicated, is preferably so shaped and directed into the chamber that'the hot liquor entering through the circulating-pipe is gently discharged in a horizontal direction toward the side of the chamber and away from the outlets. The result is that there is a substantially quiescent body of liquor which may nearly lill the chamber, as indicated, and which allows the gradual settling or deposition oi' the crystallized material contained in the liquor entering the chamber. This crystalline material gradually settles down through the liquor, which is thus maintained quite free from suspended matter at its upper portions. Suitable outlets are arranged adjacent the normal upper level of the liquor in the separating-chamber, the valved outlets 26 being indicated as connecting with the return-pipe 28, which may discharge this cleared liquor taken from the separating-chamber into the downtake or other part of the effect for further treatment. This is the normal operation of the device, one separating-chamber acting as a quiescent settlingchamber constantly supplied with liquor from the eiect through the guarded inlet of the circulating-pipe and constantly having the cleared liquor taken off in the proper quantities through the valved outlet adjacent the upper level of the liquor in the chamber. When, as observed through the eyeglass 23, the level of the crystallized material approaches the upper part of the chamber, the Valve 21 in the circulating-pipe is shut and the corresponding valve leading to the other chamber opened, so as to start that chamber into normal operation. The liquor may then be removed from the filled chamber by opening the valve 29, leading into the drain-pipe IOO IIO
30, and allowing the liquor to discharge through the return-valve 3l and return-pipe 28 into 'the effect or, if desired, by shutting this valve 3l and opening the valve 32 this liquor may pass from the circulating-chamber through the discharge-pump 40 and discharge-pipe 35 into the succeeding similar effeet of the multiple-effect apparatus or into further treating apparatus of any kind. Part of. this liquor may, if desired, be withdrawn through the valve 27, governing the outlet indicated, which leads into the discharge-pipe 34 and discharge-pump, and, indeed, in some work it is desirable to continuously withdraw some liquor through this valved outlet and discharge pipe and feed it to the succeeding e'ectof the multiple-effect apparatus, so as to effect a continual feeding of liquor from one effect to the succeeding one of the series. After-the liquor has been drained off by gravity from the precipitated salt or similar material in the separating-chamber the vacuumbreak is opened and the previously-compacted material is in this manner thoroughly separated from any remainingliquor, and after the valves have been closed this precipitated material may be readily removed through the discharge-door 24, so as to empty the chamber and prepare it for a further separating operation. By first draining off the liquor from the salt and then vigorously acting upon the compacted mass by the vacuum-break, as indicated, this hot crystallized salt may in some cases be so thoroughly dried as to require little, if any, subsequent treatment before shipment as commercial salt.
Having described an embodiment of this invention,which is,of course,merelyillustrative, the scope of what I claim as new and what I desire to secure by Letters Patent is set forth in the appended claims.
I claim- 1. In vacuum evaporating apparatus, an effect comprising a vapor-chamber, a liquorchamber, uptakes and a jacketed downtake, means to supply thin liquor to said effect, a plurality of separating chambers having screens therein, a circulating-pipe and pump to supply concentrated liquor from said effect to either one of said chambers through a guarded inlet adjacent the top of said chamber, a return-pipe having a valved outlet adjacent the top of said chamber and a valved drain-pipe in the bottom of said chamber, a valved discharge-pipe and pump to discharge liquor fromv said chamber into a succeeding effect and valved connections between said drain pipe and said return and discharge pipes.
2. In vacuum evaporating apparatus, an effect, means to supplyliquor to said elect, a plurality of separating-chambers, circulating means to supply concentrated liquor from said effect to either one of said chambers to produce a substantially quiescent body of liquor in the same, an outlet-duct adjacent to the top of said chamber and pipes connecting with said outlet and leading to said effect or to a succeeding treating apparatus.
3. In vacuum evaporating apparatus, an effeet, means to supply liquor to said effect, a separating-chamber adjacent to said effect, a ci rculating-pipe to supply concentrated liquor from said effect to said separating-chamber to form a substantially quiescent body of liquor therein, a valved outlet-duct adjacent to the top of said chamber and communicating with a return-pipe leading to said eect, and a discharge-pump connecting with a succeeding treating apparatus and receiving liquor from the upper part of said separatingchamber.
4. In vacuum evaporating apparatus, an effect, means to supply liquor to said effect, a closedseparating-chamber having a screen, means to supply concentrated liquor from said effect to said separating-chamber, an outletduct in the upper part of said chamberl connecting with a return-pipe leading to said eect and with a discharge-pipe leading to a succeeding treating apparatus, a vacuumbreak and a valved drain-pipe on said separating-chamber.
5. In vacuum evaporating apparatus, aseparating-chamber, an outlet-duct taking liquor from the upper part of said chamber, a circulating-pipe to supply concentrated liquor from an evaporating apparatus to the upper part of said separating-chamber to form a substantially quiescent body of liquor therein to eect the precipitation of material from said liquor.
CHARLES ORDWAY. Witnesses:
JEssIE B. KAY, JAMES L. CHILDS.
IOO
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US24229605A US807767A (en) | 1905-01-23 | 1905-01-23 | Vacuum evaporating apparatus. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US24229605A US807767A (en) | 1905-01-23 | 1905-01-23 | Vacuum evaporating apparatus. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US807767A true US807767A (en) | 1905-12-19 |
Family
ID=2876249
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US24229605A Expired - Lifetime US807767A (en) | 1905-01-23 | 1905-01-23 | Vacuum evaporating apparatus. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US807767A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3261670A (en) * | 1965-04-21 | 1966-07-19 | Chicago Bridge & Iron Co | Conispherical vessel for crystallization |
| US5472622A (en) * | 1993-04-20 | 1995-12-05 | Ionics, Incorporated | Salt basket for crystallizer and method of use in zero liquid discharge industrial facilities |
-
1905
- 1905-01-23 US US24229605A patent/US807767A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3261670A (en) * | 1965-04-21 | 1966-07-19 | Chicago Bridge & Iron Co | Conispherical vessel for crystallization |
| US5472622A (en) * | 1993-04-20 | 1995-12-05 | Ionics, Incorporated | Salt basket for crystallizer and method of use in zero liquid discharge industrial facilities |
| US5575923A (en) * | 1993-04-20 | 1996-11-19 | Ionics, Incorporated | Salt basket for crystallizer and method of use in zero liquid discharge industrial facilities |
| US5656161A (en) * | 1993-04-20 | 1997-08-12 | Ionics, Incorporated | Salt basket for crystallizer and method of use in zero liquid discharge industrial facilities |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1190863A (en) | Settling-tank. | |
| US2631926A (en) | Apparatus for concentrating a solution and separating crystals therefrom | |
| US1831121A (en) | Evaporating apparatus | |
| US807767A (en) | Vacuum evaporating apparatus. | |
| US1191108A (en) | Evaporator. | |
| US1717927A (en) | Evaporator | |
| US1611739A (en) | Apparatus for screening liquids | |
| US466862A (en) | Tiitttp | |
| US1785530A (en) | Method of crystallization | |
| US2672926A (en) | Evaporator | |
| US874907A (en) | Mining salt. | |
| US1567033A (en) | Appabattts fob conserving soap | |
| US1810181A (en) | Process and apparatus for recovering values from brine | |
| US236299A (en) | Washihqtok | |
| US1156060A (en) | Process and apparatus for depurating. | |
| US775577A (en) | Vacuum evaporating apparatus. | |
| US464389A (en) | Vacuum evaporating apparatus | |
| US458648A (en) | van ruymbeke | |
| US1086457A (en) | Manufacture of salt by multiple-effect evaporation. | |
| US1052195A (en) | Apparatus for defecation. | |
| US400983A (en) | Apparatus for the manufacture of salt | |
| US630174A (en) | Evaporating apparatus. | |
| US851957A (en) | Water-purifying apparatus. | |
| US531460A (en) | Process of and apparatus for defecating saccharine solutions | |
| US1610307A (en) | Apparatus for salt purification |