US194856A - Improvement in condensers for fractional distillation - Google Patents
Improvement in condensers for fractional distillation Download PDFInfo
- Publication number
- US194856A US194856A US194856DA US194856A US 194856 A US194856 A US 194856A US 194856D A US194856D A US 194856DA US 194856 A US194856 A US 194856A
- Authority
- US
- United States
- Prior art keywords
- condensers
- pipe
- condenser
- improvement
- vapor
- 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
- 238000004508 fractional distillation Methods 0.000 title description 4
- 239000007788 liquid Substances 0.000 description 14
- 238000009833 condensation Methods 0.000 description 12
- 230000005494 condensation Effects 0.000 description 8
- 238000004821 distillation Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 101700083238 NOTO Proteins 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 230000001627 detrimental Effects 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/02—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
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- 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
- Y10S165/00—Heat exchange
- Y10S165/184—Indirect-contact condenser
- Y10S165/217—Space for coolant surrounds space for vapor
- Y10S165/221—Vapor is the only confined fluid
Definitions
- My condenser does not admit of any such objection. It is not a worm, except for convenience in manufacture.
- the hot vapors pass along the feed-pipe, and are drawn down into the vertical tubes partly by gravity and partly by the partial vacuum produced by the partial condensation in said tubes, while the condensed fluid passes into the lower returnpipe and is conveyed back to the still.
- A is the vapor-pipe, taking vapor in the direction of the arrows from the still, and delivering it in the direction of the arrow at to the worm, where thorough condensation is effected.
- Fig. 1 For convenience, the structure shown in Fig. 1 only will be specially described. The corresponding parts in Figs. 2, 3, 4, 5 are, however, similarly lettered for identification.
- the condenser is a coiled pipe, B, with the coils placed in planes perpendicular to the horizon.
- the upper bend of each separate coil is connected to the pipe A by communicating-pipe b, of such lengths as may be found most advantageous, and the lower bend of each coil is similarly connected with the return-pipe C by pipes d d.
- pipes A and C were connected directly to the coils of the tube B, so as to reduce the pipes b and d to more orifices, the invention, or its results, would not thereby be changed.
- the liquid of condensation flows in the direction of the arrows e 0 back to the still.
- This whole structure is designed to stand immersed in water to the top of the coils, or to any less depth that may be found preferable.
- 9 g are feet, to support the condenser, and adjusted to give the return-pipe C the proper inclination while standing upon a level floor.
- the vapor-pipe and the return-pipe are, therefore, separate, and the hot vapors which pass into the condenser-pipes are there condensed so far as possible at the temperature maintained, and the liquid of condensation flows away through the return-pipe withoutcoming in contact with the vapor in the vaporpipe at all.
- the quality of condensed liquid may be regulated by adjusting the temperature of the vapor-pipe, A, above, and a return-pipe, 0,
Description
F. M. YOUNG. CONDENSERS FOR FRACTION'AL DISTILLATION'.
Patented Sept. 4.,1877.
WITNESSES wmfiwb M Distillation and that the following is a full planes, has heretofore been used; but in such end of said coils, the condensed fluid being UNITED TA jEs 1 FRANCIS M. YOUNG, CHICAGO, ILLINOIS.
IMPROVEMENT IN CONDENSERS FOR FRACTIONAL DISTILLATION.
Specification forming part of Letters Patent No. l94,56, dated September 4, 1877 application filed May 12,1877.
To all whom it may concern:
Be it known that I, FRANCIS M. YOUNG, of Chicago, in the county of Cook and State of Illinois, have invented a new and useful Improvement in Condensers for Fractional and clear description of the same.
'I am aware that a coiled condenser-tube set upon edge, or with its coils in vertical condensers, so far as I am aware, the hot vapors were compelled to pass from end to permitted to escape from the bottom of each coil to a return-pipe, and thereby back to the still; but such is not my invention. In condensers of that description the lower bends of the coils frequently become filled with liquid so as to seal the passage. The hot vapors are then compelled to force the way through said liquid, and a portion will be condensed by contact with the cooler liquid; while, on the other hand, the vapor which passes through will revaporize a portion of the liquid previously condensed, and the efi'ect is detrimental to the process.
My condenser does not admit of any such objection. It is not a worm, except for convenience in manufacture. The hot vapors pass along the feed-pipe, and are drawn down into the vertical tubes partly by gravity and partly by the partial vacuum produced by the partial condensation in said tubes, while the condensed fluid passes into the lower returnpipe and is conveyed back to the still. I am therefore enabled to keep my condenser-pipes at the proper temperature and in uniform operation, so that, while passing the condenser, all or nearly all the vapor condensable below the vapor-point of alcohol will have been condensed, and the vapor which finally reaches the thorough-condensation worm will be pure, or nearly so.
That others may fully understand my invention I will particularly describe it, having reference to the accompanying drawing, wherein- Figure 1 is aperspective view of my condenser in the form preferred by me. Figs. 2,
3, 4, and 5 represent modifications in structure, but involve no change in principle or mode of action.
A is the vapor-pipe, taking vapor in the direction of the arrows from the still, and delivering it in the direction of the arrow at to the worm, where thorough condensation is effected.
The still and thorough-condensation worm are not shown, because their operation is well understood, and does not enter into this case in any special way.
For convenience, the structure shown in Fig. 1 only will be specially described. The corresponding parts in Figs. 2, 3, 4, 5 are, however, similarly lettered for identification.
The condenser is a coiled pipe, B, with the coils placed in planes perpendicular to the horizon. The upper bend of each separate coil is connected to the pipe A by communicating-pipe b, of such lengths as may be found most advantageous, and the lower bend of each coil is similarly connected with the return-pipe C by pipes d d. It should be understood, however, that if said pipes A and C were connected directly to the coils of the tube B, so as to reduce the pipes b and d to more orifices, the invention, or its results, would not thereby be changed. The liquid of condensation flows in the direction of the arrows e 0 back to the still.
This whole structure is designed to stand immersed in water to the top of the coils, or to any less depth that may be found preferable.
9 g are feet, to support the condenser, and adjusted to give the return-pipe C the proper inclination while standing upon a level floor.
The vapor-pipe and the return-pipe are, therefore, separate, and the hot vapors which pass into the condenser-pipes are there condensed so far as possible at the temperature maintained, and the liquid of condensation flows away through the return-pipe withoutcoming in contact with the vapor in the vaporpipe at all.
By these means light vapors are permitted to pass off to be treated elsewhere, while those portions which are heavier and more easily condensed pass into the pipes B.
The quality of condensed liquid may be regulated by adjusting the temperature of the vapor-pipe, A, above, and a return-pipe, 0,
water surrounding the condenser. below, as set forth, combined with condenser- After operation on an extensive scale for a pipes B, extending between and uniting said sufficient period to thoroughly test this imvapor and return pipes, substantially as and provement, it is found that the product is noto operate as described.
ticeably softer and superior to liquor condensed in the usual way. YOUNG Having described my invention, what I Witnesses:
claim as new is- B. W. KENDALL, An analyzing-condenser composed of a H. D. YOUNG.
Publications (1)
Publication Number | Publication Date |
---|---|
US194856A true US194856A (en) | 1877-09-04 |
Family
ID=2264262
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US194856D Expired - Lifetime US194856A (en) | Improvement in condensers for fractional distillation |
Country Status (1)
Country | Link |
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US (1) | US194856A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3028149A (en) * | 1959-01-28 | 1962-04-03 | Svenska Flaektfabriken Ab | Heat-exchangers |
-
0
- US US194856D patent/US194856A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3028149A (en) * | 1959-01-28 | 1962-04-03 | Svenska Flaektfabriken Ab | Heat-exchangers |
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