US55038A - Improved method of collecting and separating carbonic acid from mixtures of gases - Google Patents
Improved method of collecting and separating carbonic acid from mixtures of gases Download PDFInfo
- Publication number
- US55038A US55038A US55038DA US55038A US 55038 A US55038 A US 55038A US 55038D A US55038D A US 55038DA US 55038 A US55038 A US 55038A
- Authority
- US
- United States
- Prior art keywords
- gases
- water
- mixtures
- collecting
- carbonic acid
- 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
- 239000007789 gas Substances 0.000 title description 10
- 238000000034 method Methods 0.000 title description 9
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 title description 2
- 239000000203 mixture Substances 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 239000002253 acid Substances 0.000 description 12
- 239000002912 waste gas Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 239000000446 fuel Substances 0.000 description 5
- 239000003245 coal Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 235000011089 carbon dioxide Nutrition 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000004579 marble Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- -1 carbonio oxide Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004572 hydraulic lime Substances 0.000 description 1
- 231100000567 intoxicating Toxicity 0.000 description 1
- 230000002673 intoxicating effect Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
Definitions
- the products of gases in the ordinary combustion of coal are vapor of water, carbonio acid, carbonio oxide, and nitrogen. That of limekilns is similar, so far as the fuel is concerned 5 but besides this the tota-l amount of carbonio acid separated from the limestonethat is to say, every fifty pounds of pure limestonewill yield twenty-two pounds of carbonio acid and twenty-eight pounds of quick- Of the gaseous products, vapor of water lime.
- a in the accompanying drawings represent a cylinderor tank, into which the gaseous products of combustion are forced through pipe B at the same time that a continuous shower of cold water is discharged from reservoir C through its perforate bottom, and thence through the diaphragm of wire-cloth D.
- the spray of water receives the carbonio-acid gas and vapor of water under a heavy pressure and absorbs them, while the nitrogen and carbonic oxide are allowed to escape througha weighted valve, E, balanced at a pressure of seven ty-tive pounds (or aboutfl veatmospheres) to the inch, and are thus carried away by pipe F F F, to be used for a motive power.
- the cylinder A may, therefore, be cooled by ice, which will greatly increase its power of absorbing carbonio acid.
- the Waste gases passing off through the valve E, the carbonio acid is thus pnried and transferred bodily in the water under a pressure of about five atmospheres to the second cylinder, J, Where it is suddenly relieved of its pressure by a partiallyexhausted atmosphere in the chamber of J, and is carried away through pipe L by the opera ⁇ tion of exhausting-1min p M, and forced into a suitable apparatus for condensing into the solid form or for other use.
- tank I in the upper part of cylinder J is equally advantageous in in itself', cheap beverage, which ought t0 be cheaper than any other Vliquid in use for such purpose, and by cheapening the process the article itself Will necessarily be cheapened, and the substituting of a cheaper and healthier drink for intoxicating liquor will be greatly encouraged.
- Waste gases which escape from cylinder A through pipe F F F furnish considerable mechanical force, and are capable of being applied to Work the eXh austin g-pump M, or pump V W, or for any other suitable purpose where power is needed.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Description
UNTTen STATES PATENT Graine.
JAMES S. BALDWIN, OF NEW YORK, N. Y.
IMPROVED METHOD OF COLLECTING AND SEPAliATlNG CARBONIC ACID FROM MIXTURES 0F GASES.
Specilication forming part of Letters Patent N0. 55,038, dated May 29, 1866.
To all '1r/mm it may concern:
Be it known that l, JAMES S. BALDWIN, of New York, coun ty of New York, and State of New York, have invented or discovered acertain new and useful method of separating, lliuriilying/and applying to use carbonio-acid gas as obtained from any well-known source; and I hereby declare that the following is a full and sufficient description thereof, reference being had to the accompanying drawings and references thereof, making a part of this description.
The method of manufacturing carbonio acid for soda-water, Svc., in general use, where sulphuric acid and common marble constitute the materials used, is expensive, because no available use can be made of the waste materials after separating the gas. There are two methods, both cheap and practical, that may be used for generating the gas cheaply. The rst is that by the combustion of anthracite coal or charcoal. rIhe second is that of the limekilu, where carbonate of lime is burned into quicklime, expelling the carbonio-acid gas by means of the heat of burning fuel. .lhe second is by far the most abundant source.` The amount of fuel burned is the source in theirst process, and the amount of, fuel added to the amount of marble decomposed is the source in the second process, and gives nearly twenty times the amount yielded by the first process. If the. gas be made from burning coal, as that used under a steam-boiler, there the expense of the coal has already paid for itself in heating the water. The gaseous products being drawn from the chimney above the fire are taken to the proper apparatus for absorbing the carbonic acid and forcing forward the waste gases to a secondary use, as hereinafter explained; but the second process-namely, that from the limekiln-I prefer, from the greater quantity yielded by the same expenditure of fuel.
The products of gases in the ordinary combustion of coal are vapor of water, carbonio acid, carbonio oxide, and nitrogen. That of limekilns is similar, so far as the fuel is concerned 5 but besides this the tota-l amount of carbonio acid separated from the limestonethat is to say, every fifty pounds of pure limestonewill yield twenty-two pounds of carbonio acid and twenty-eight pounds of quick- Of the gaseous products, vapor of water lime.
and carbonio acid are absorbed by water, while the carbonio oxide and nitrogen are not absorbed under the same exposure, but are expelled as waste gases. The water used to condense the gases is kept cold. `rIo effect a separation of the gaseous products of combustion in limekilns, 86o., I avail myself of the carbonio acid evolved.
Let A in the accompanying drawings represent a cylinderor tank, into which the gaseous products of combustion are forced through pipe B at the same time that a continuous shower of cold water is discharged from reservoir C through its perforate bottom, and thence through the diaphragm of wire-cloth D. The spray of water receives the carbonio-acid gas and vapor of water under a heavy pressure and absorbs them, while the nitrogen and carbonic oxide are allowed to escape througha weighted valve, E, balanced at a pressure of seven ty-tive pounds (or aboutfl veatmospheres) to the inch, and are thus carried away by pipe F F F, to be used for a motive power. rIhe Water shower in chamber A accumula-tes in the bottom until it raises float-valve G and opens a passage through pipe H for the escape of the surcharged water into second cylinder, J through water-reservoir I, perforated at the bottom, and wire-cloth K, preparatory to being forced out into pipe P into a reservoir. As the liquid escapes from chamber A, with a pressure of seventy-five pounds to the inch, into chamber J, with only ten pounds, nearly all the gas will be set free, as I find a diminished pressurein the second cylinder to be necessary;
so I keep the chamber of this cylinder partially` exhausted by means of pump M, connected with it by pipe L. This arrangement (for exhaustion) of second cylinder and Weighted valve in the first cylinder enables me to preserve any suitable pressurein the several cylinders as required. The relative proportion of pressure may be varied somewhat without varying the character of the invention. l I have thus far found good results with a pressure of seventy-five pounds to the inch in the tank A, while there is a vacuum of ten pounds in tank J, and pure carbonio acid passes through L. Now, the present process for separating carbonic-acid gas from the waste gases is based on the absorbability of the former and non absorbability of the latter by water when cold. The cylinder A may, therefore, be cooled by ice, which will greatly increase its power of absorbing carbonio acid. Now, the Waste gases passing off through the valve E, the carbonio acid is thus pnried and transferred bodily in the water under a pressure of about five atmospheres to the second cylinder, J, Where it is suddenly relieved of its pressure by a partiallyexhausted atmosphere in the chamber of J, and is carried away through pipe L by the opera` tion of exhausting-1min p M, and forced into a suitable apparatus for condensing into the solid form or for other use. It is proper to say in this connection that the tank I in the upper part of cylinder J is equally advantageous in in itself', cheap beverage, which ought t0 be cheaper than any other Vliquid in use for such purpose, and by cheapening the process the article itself Will necessarily be cheapened, and the substituting of a cheaper and healthier drink for intoxicating liquor will be greatly encouraged.
The Waste gases which escape from cylinder A through pipe F F F furnish considerable mechanical force, and are capable of being applied to Work the eXh austin g-pump M, or pump V W, or for any other suitable purpose where power is needed.
What I claim as my invention, and desire t0 secure by Letters Paten t, is-
1. Separating, purifying, and transferring carbonic-acid gas from Waste gases by means of water or its equivalent liquid, substantiallyin the manner and for the purpose herein set forth.
2. Driving the pumps, or other machinery, by the Waste gases evolved in this process, substantially as described.
JAMES S. BALDWIN.
Witnesses:
WM. H. RIBLET, L. D. GALE.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US55038A true US55038A (en) | 1866-05-29 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US55038D Expired - Lifetime US55038A (en) | Improved method of collecting and separating carbonic acid from mixtures of gases |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US55038A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2688381A (en) * | 1949-04-23 | 1954-09-07 | Epstein Meyer | Soda water making process and apparatus |
| US20030122868A1 (en) * | 2002-01-03 | 2003-07-03 | International Business Machines Corporation | Menu emulation for content browser clients background of the invention |
-
0
- US US55038D patent/US55038A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2688381A (en) * | 1949-04-23 | 1954-09-07 | Epstein Meyer | Soda water making process and apparatus |
| US20030122868A1 (en) * | 2002-01-03 | 2003-07-03 | International Business Machines Corporation | Menu emulation for content browser clients background of the invention |
| US7216303B2 (en) * | 2002-01-03 | 2007-05-08 | International Business Machines Corporation | Menu emulation for content browser clients |
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