US305631A - Apparatus for evaporating alkaline solutions - Google Patents
Apparatus for evaporating alkaline solutions Download PDFInfo
- Publication number
- US305631A US305631A US305631DA US305631A US 305631 A US305631 A US 305631A US 305631D A US305631D A US 305631DA US 305631 A US305631 A US 305631A
- Authority
- US
- United States
- Prior art keywords
- evaporating
- pipe
- pan
- furnace
- alkaline solutions
- 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 24
- 239000007788 liquid Substances 0.000 description 20
- 210000000188 Diaphragm Anatomy 0.000 description 16
- 239000000463 material Substances 0.000 description 8
- 238000001354 calcination Methods 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000003245 coal Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 239000002918 waste heat Substances 0.000 description 4
- 239000003513 alkali Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 235000017550 sodium carbonate Nutrition 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
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
- B01D1/08—Evaporators with vertical tubes with short tubes
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S159/00—Concentrating evaporators
- Y10S159/34—Caustic
Definitions
- My invention relates to improvements in apparatus intended more especially for the evaporation and concentration of alkaline solutions, though it is applicable to any furnace or apparatus employed for the eXpulsion or evaporation of water or other liquid from any material.
- My invention also relates to means, hereinafter more fully described, for preventing the liquid from being forced over by ebullition into the condenser.
- Figure 1 represents a side elevation of my improved apparatus, part being in vertical section.
- Fig. 2 is a plan view thereof, partly insection; and
- Fig. 3 is a sectional view of the boil-over reservoir detached.
- A may represent any suitable furnace, here shown as being employed both for the purpose of heating the liquid in evaporatingpan B and at a latter periodof the process of recovery of soda-ash or other alkali, igniting and aiding the combustion of material in the calcining-furnace C.
- a simple arched support or, if a horizontal stationary furnace be used, may support the flue directly on top of the furnace. From the flue F the gases are led to the stack.
- the vacuum-pan B may be either vertical, as shown, or horizontal, and is preferably provided within with agitators Z, of any approved construction-perpendicular or horizontal. It may either connect immediately with the furnace through pipe I, or may connect with an intermediate reservoir, J, from which the material may be discharged into the furnace.
- the pan is charged through pipe mfrom reservoir M, in ordinary manner.
- any suitable part of the pan I place the vapor-discharge pipe N, and within this pipe, to prevent the carrying over by ebullition of bubbles of the liquid into the condenser, I place a diaphragm, O, or system of diaphragms of wire-gauze, which break the bubbles, while allowing free passage of the vapor and facilitate the return of the liquid to the evaporating-pan.
- the liquor from bubbles bursting against the upper diaphragm is returned around the pipe I? to the vacuum safe or trap T, whence it flows back into the pan.
- the pipe N is led into a boil-over chamber, It, whence the liquid is returned to the pan through pipe S.
- pan with a forced exhaust with or without agitators and with or Without condensers
- an interposed bubblebreaker produces a strong and effective evaporatoiyworking with great speed without the passage of any liquid over into the condenser.
- An agitator should generally be employed, as it greatly increases the rapidity of evaporation, and is an important improvement over the ordinary vacuum-
- the heat from the calcining-furnace and lighting-furnace heats the bottom of the evaporating-pan, while the return-flue heats the sides thereof to the height of the liquor therein contained, thus more fully utilizing the waste heat, and saving all coal expenditure for boiling the soda in the process of evaporation, a larger portion of the Waste heat from the incinerating-furnace resulting from the combustion of organic inatter in the soda.
- the vacuum-pump also takes the place of a large quantity of coal by'utilizing to the highest degree the heat generated. Having thus described my invention, the following is what I claim as new therein and desire to secure by Letters Patent- 1.
- the pendent flange therein serving to arrest and precipitate liquid passing through the reservoir, whence it is returned to the evaporating-pan by asuitable pipe emptying intoa vacuumsafe, substantially as set forth.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
' (No Model.)
- v 2 SheetsSheet 1 J. P. R. POLK. APPARATUS FOR EVAPORATING ALKALINE SOLUTIONS.
No. 305,681. I Patented Sept. 23, 1884.
(No Model.) 2 Sheets-Sheet 2.
v J; P. R. POLK.
APPARATUS FORE-VAPORATING ALKALINE SOLUTIONS. I No. 305,631. Patented Sept 23, 1884.
Wzfnemes nyenibr Units STATES.
JOHN P. R. POLK, OF WILMINGTON, DELAVARE, ASSIGNOR TO THE UNIVERSAL OONGENTRATING COMPANY, OF CAMDEN, N. J.
APPARATUS FOR EVAPORATING ALKALINE SOLUTIONS.
SPECIFICATION forming part of Letters Patent No. 305,631, dated September 23, 1884.
' Application filed April 28. 1883. (No model.)
To aZZ whom it may concern:
Be it known that I, JOHN l. R. POLK, a citizen of the United States, residing at VVilniington, in the county of New Castle and State of Delaware, have invented certain new and useful Improvements in Vacuum-Pans and Apparatus for Evaporating Alkaline and other Solutions, and the Desiccation of any Materials Containing Moisture, of which the,
following is a specification. V
' My invention relates to improvements in apparatus intended more especially for the evaporation and concentration of alkaline solutions, though it is applicable to any furnace or apparatus employed for the eXpulsion or evaporation of water or other liquid from any material.
bustion from the igniting and calcining furnaces.
My invention also relates to means, hereinafter more fully described, for preventing the liquid from being forced over by ebullition into the condenser.
. In order that my invention may be more fully understood, I will first describe it with reference to the accompanying drawings, and then point it out more particularly in the claims.
In the drawings, Figure 1 represents a side elevation of my improved apparatus, part being in vertical section. Fig. 2 is a plan view thereof, partly insection; and Fig. 3 is a sectional view of the boil-over reservoir detached.
A may represent any suitable furnace, here shown as being employed both for the purpose of heating the liquid in evaporatingpan B and at a latter periodof the process of recovery of soda-ash or other alkali, igniting and aiding the combustion of material in the calcining-furnace C. On each side of the furemploy a simple arched support, or, if a horizontal stationary furnace be used, may support the flue directly on top of the furnace. From the flue F the gases are led to the stack.
The vacuum-pan B may be either vertical, as shown, or horizontal, and is preferably provided within with agitators Z, of any approved construction-perpendicular or horizontal. It may either connect immediately with the furnace through pipe I, or may connect with an intermediate reservoir, J, from which the material may be discharged into the furnace.
The pan is charged through pipe mfrom reservoir M, in ordinary manner. any suitable part of the pan, I place the vapor-discharge pipe N, and within this pipe, to prevent the carrying over by ebullition of bubbles of the liquid into the condenser, I place a diaphragm, O, or system of diaphragms of wire-gauze, which break the bubbles, while allowing free passage of the vapor and facilitate the return of the liquid to the evaporating-pan. To facilitate the return of the liquid on the bursting of the bubbles against the upper diaphragm, O, I place within the pipe N a second pipe, P, having upon its upper end a second diaphragm, Q, of wire-gauze to still further arrest the bubbles. The liquor from bubbles bursting against the upper diaphragm (or diaphrams, if a number be employed,) is returned around the pipe I? to the vacuum safe or trap T, whence it flows back into the pan. The pipe N is led into a boil-over chamber, It, whence the liquid is returned to the pan through pipe S. A circular flange, T, around the bottom of pipe N, into which pipe I? dips, arrests sufficient of the return liquid to make a vacuumsafe at this point, and pre On top, at
pan with a forced exhaust, with or without agitators and with or Without condensers, and
' pan.
an interposed bubblebreaker produces a strong and effective evaporatoiyworking with great speed without the passage of any liquid over into the condenser. An agitator should generally be employed, as it greatly increases the rapidity of evaporation, and is an important improvement over the ordinary vacuum- By my method the heat from the calcining-furnace and lighting-furnace heats the bottom of the evaporating-pan, while the return-flue heats the sides thereof to the height of the liquor therein contained, thus more fully utilizing the waste heat, and saving all coal expenditure for boiling the soda in the process of evaporation, a larger portion of the Waste heat from the incinerating-furnace resulting from the combustion of organic inatter in the soda. The vacuum-pump also takes the place of a large quantity of coal by'utilizing to the highest degree the heat generated. Having thus described my invention, the following is what I claim as new therein and desire to secure by Letters Patent- 1. The combination, with a suitable evaporating and calcining furnace, of the returnflue having branches surrounding the sides of the evaporating-pan, substantially as set forth. 7 2. The combination, with a suitable evaporating and calcining furnace, of a return-flue having branches surroundingthe evaporating pan, .said branches being divided centrally 'and provided with a suitable damper, as set forth.
3. I11 combination with a direct vapor-dis charge pipe, the ebullition-guard consisting of one or more diaphragms of wire-gauze placed transversely in said pipe, substantially as described.
4. The combination, with an evaporating vessel or vacuum-pan, of the vapor-discharge pipe, having one or more perforated diaphragms arranged therein, and an interior pipe concentric therewith and having a similar diaphragm, and the flange forming a vacuum-safe, in themanner set forth.
5. In combination with the vapor-discharge pipe and a -boil-over reservoir, the pendent flange therein, serving to arrest and precipitate liquid passing through the reservoir, whence it is returned to the evaporating-pan by asuitable pipe emptying intoa vacuumsafe, substantially as set forth.
6. The combination of an evaporating-pan,
an ebullition-guard in the exhaust-pipe thereof, and vacuum-pump, or other force-exhaust mechanism, substantially as set forth.
7. The combination ofan evaporating-pan having suitable means of agitation, an ebullition-guar'd in the vapor-exhaust pipe thereof,
and a vacuum-pump, or other force-exhaust
Publications (1)
Publication Number | Publication Date |
---|---|
US305631A true US305631A (en) | 1884-09-23 |
Family
ID=2374800
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US305631D Expired - Lifetime US305631A (en) | Apparatus for evaporating alkaline solutions |
Country Status (1)
Country | Link |
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US (1) | US305631A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3341173A (en) * | 1965-03-04 | 1967-09-12 | British Oxygen Co Ltd | Apparatus employing gas bearings |
US4258010A (en) * | 1975-11-19 | 1981-03-24 | Eszakmagyarorszagi Vegyimu_ vek | Solvent extraction apparatus |
-
0
- US US305631D patent/US305631A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3341173A (en) * | 1965-03-04 | 1967-09-12 | British Oxygen Co Ltd | Apparatus employing gas bearings |
US4258010A (en) * | 1975-11-19 | 1981-03-24 | Eszakmagyarorszagi Vegyimu_ vek | Solvent extraction apparatus |
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