US417068A - Process of obtaining hydrogen gas - Google Patents
Process of obtaining hydrogen gas Download PDFInfo
- Publication number
- US417068A US417068A US417068DA US417068A US 417068 A US417068 A US 417068A US 417068D A US417068D A US 417068DA US 417068 A US417068 A US 417068A
- Authority
- US
- United States
- Prior art keywords
- hydrogen
- carbon
- cobalt
- gases
- nickel
- 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
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title description 14
- 238000000034 method Methods 0.000 title description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 20
- 239000001257 hydrogen Substances 0.000 description 17
- 229910052739 hydrogen Inorganic materials 0.000 description 17
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 13
- 229910052799 carbon Inorganic materials 0.000 description 13
- 239000007789 gas Substances 0.000 description 12
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 11
- 229910017052 cobalt Inorganic materials 0.000 description 11
- 239000010941 cobalt Substances 0.000 description 11
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 11
- 229910052759 nickel Inorganic materials 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 7
- 150000002431 hydrogen Chemical class 0.000 description 6
- 229930195733 hydrocarbon Natural products 0.000 description 5
- 150000002430 hydrocarbons Chemical class 0.000 description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 241000218652 Larix Species 0.000 description 1
- 235000005590 Larix decidua Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241000282320 Panthera leo Species 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
- C01B3/16—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide using catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
- C01B2203/1052—Nickel or cobalt catalysts
Definitions
- the object of our invention is to eliminate from these gases the monoxide of carbon and the carburets of hydrogen, and at the same time to increase the amount of hydrogen contained.
- a mixture of monoxide of carbon or of carburet of hydrogen and steam be heated to white heat the latter is decomposed and c the carbon of the gases is oxidized to a'dioxide and the hydrogen set at liberty.- The high temperature required for this reaction. renders it of little profit, and it is ditticultio produce it on an industrial scale.
- V We have found that if monoxide of carbon and hydrocarburets be placed in contact with nickel or metallic cobalt at a temperature not exceeding red heat these gases are decomposed into carbon and dioxide of carbon on the one hand and hydrogen on the other. The free carbon so formed placed in contact with steam at a moderate tcmperato re decomposes the latter and forms dioxide of carbon and hydrogen. If the steam and 195 the gases are mixed from the commencement,
- gases-or steam or both, heated to a suitable temperature before they are placed in the retorts.
- 'Thc gases so treated contaiirlittle or no monoxide of carbon.
- ⁇ Vc claim as our invention- Y 1. The process of obtaining hydrogen from hydrogen contaminated with carbon monoxide or hydrocai'lions which consists in subjecting such contaminated hydrogen to the 0 action of metallic nickel or cobalt and steam at the tempcraturedescrihed, and separating the carbon dibxide thereby formed by subjecting the resultant gases to the action of caustic lime or alkali.
- The-improvement iri'the process of obtaining' hydrogen, which" consists-in sulgjecting.
- the mass of nickel or cobalt and c'arb'on formed by subjecting bon monoxide or hydrocarbons to the action of metallic nickel or cobalt at a snitable tem perature) to the action of steam substantially at the temperature set forth,,whereby a mixture of carbon dioxide and consists in subject to the action of me 'ta'llic nickel or cobalt at the temperatures wtion of steam and of gases.
- containingca'r hydrogen is obmining.
- hydrocarbons which consists in exposing hydrogen contaminated with carbon monoxide. or hydrocarbons, or both, to the joint acmetallic nickel or cobalt at a temperature substantially as described,
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Gas Separation By Absorption (AREA)
Description
UNITED STATES PATENT: OFFICE.
LUDWIG Mono, or NORTIIWIOH, coun'rr or cnns'run, AND CARL L'ANGER, 4
or SOUTH IIAMPS'IEAD, conx'rr or MIDDLESEX, ENGLAND" PROCESS OF OBTAINING HYDROGEN'GAS.
SPECIFICATION forming part of Letters Patent No. 417,068, dated December 10, 1889.
Application filed March 7,1889. Serial N3. 302,323- (No specimens.) Patented in England BOPlGBmbOhL1-888, No. 12,608 i in France February 28. 1889, No.'196,381; in Belgium February 28, 1889, No. 85,201, and in Italy larch 31,1889,XXIX,'25,043,
XLIX, 150.
To all whom, it may concern.-
Be it known that we, LUDWIG MOND and EARL LANGER, subjects of the Queen of Great Britain, and residents of Northwich and 5 South Hampstead, respectively, both in the Kingdom of England, have invented certain' new and useful Improvements in the Process of Obtaining Hydrogen Gas, (which has been patented in England, No. 12,608, dated Sepro tember 1,1888; in France, No. 196,381, dated February 98, 1389; in Belgium, No. 85,201, dated February 28, 1889, and in Italy, XXIX, 25,043, XLIX, 150, dated March 31, 1889,) of which the following is a specification.
t5v By the distillation or incomplete combustion, in presence or in the absence of steam, of oil, lignite, wood, coke, animal carbon, or organic su bstances in general,gases are obtained which consist, chiefly, of hydrogemcarbnrets of hydrogen, monoxide anddioxide of carbon, and a greater or less quantity of nitrogen.
The object of our invention is to eliminate from these gases the monoxide of carbon and the carburets of hydrogen, and at the same time to increase the amount of hydrogen contained. if a mixture of monoxide of carbon or of carburet of hydrogen and steam be heated to white heat, the latter is decomposed and c the carbon of the gases is oxidized to a'dioxide and the hydrogen set at liberty.- The high temperature required for this reaction. renders it of little profit, and it is ditticultio produce it on an industrial scale. V We have found that if monoxide of carbon and hydrocarburets be placed in contact with nickel or metallic cobalt at a temperature not exceeding red heat these gases are decomposed into carbon and dioxide of carbon on the one hand and hydrogen on the other. The free carbon so formed placed in contact with steam at a moderate tcmperato re decomposes the latter and forms dioxide of carbon and hydrogen. If the steam and 195 the gases are mixed from the commencement,
the two reactions take place simultaneously,
and the result is a gas practically free from monoxide of carbon and hydrocarburets. It.
is quite possible to attain our object by carr ing out consecutively the two above-men- 5o tioned reactions and by repeating them'continually with the same quantity of nickel and cobalt, which will always be regenerated. we prefer, however, to carry out these two reactions simultaneously, at the same time employing the least possible amount of nickel and cobalt. W'ith this object we spread the aforesaid metals on an indifferent refractory and porous material. For example, we saturate pieces of pumice-stone with a solution 6 of chloride of nickel or cobalt, dry andreduce at a high temperature with hydrogen.
To carry out our invention, we lead the gases, with an excess of steam, into retorts pr cylinders fixed in a suitable furnace and containing pieces of pumice-stone impregnated with nickel or cobalt, as above mentioned. If nickel be used,the reaction takes Dlace at a temperature of 350 or 400 centigrade; if cobalt is used, at a temperature of 400 or 450 centigrade. The reactions which take place between the gas and the steam produce heat, so that the given temperature once reached the reaction goes on of itself, without need of external heating beyond the heat introduced by the hot gases.
It may, however, be advantageous to use gases-or steam, or both, heated to a suitable temperature before they are placed in the retorts. 'Thc gases so treated contaiirlittle or no monoxide of carbon.
To obtain pure hydrogen from the mixture of carbonic acid and hydrogen, the mixture is passed over or through layers of lime or of caustic alkali. 5
\Vc claim as our invention- Y 1. The process of obtaining hydrogen from hydrogen contaminated with carbon monoxide or hydrocai'lions which consists in subjecting such contaminated hydrogen to the 0 action of metallic nickel or cobalt and steam at the tempcraturedescrihed, and separating the carbon dibxide thereby formed by subjecting the resultant gases to the action of caustic lime or alkali.
. 2. The improvement in the'process of ob- {2 1 'ei'a ccsor" hydrocarbons, which tained.
mining hydrogen free from carbon monoxide ing hydrogen contaminated with carbon monoxide or hydrocarbons s'ubsiantiallyas described.
3. The-improvement iri'the process of obtaining' hydrogen, which" consists-in sulgjecting. the mass of nickel or cobalt and c'arb'on (formed by subjecting bon monoxide or hydrocarbons to the action of metallic nickel or cobalt at a snitable tem perature) to the action of steam substantially at the temperature set forth,,whereby a mixture of carbon dioxide and consists in subject to the action of me 'ta'llic nickel or cobalt at the temperatures wtion of steam and of gases. containingca'r hydrogen is obmining.
or hydrocarbons, which consists in exposing hydrogen contaminated with carbon monoxide. or hydrocarbons, or both, to the joint acmetallic nickel or cobalt at a temperature substantially as described,
In testimony whereof We have signed our names to this specification in the presence of two subsc ibing witnesses.
LUDWIG MOND. CARL LANGER; Witnesses:
ALFRED J i Bomfzr, HARRY B. BRIDGE.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US417068A true US417068A (en) | 1889-12-10 |
Family
ID=2485994
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US417068D Expired - Lifetime US417068A (en) | Process of obtaining hydrogen gas |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US417068A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2998303A (en) * | 1958-08-26 | 1961-08-29 | Midland Ross Corp | Method for purifying hydrogen contaminated with methane |
| US3088919A (en) * | 1958-09-10 | 1963-05-07 | Engelhard Ind Inc | Treatment of gases |
| US3387942A (en) * | 1965-05-10 | 1968-06-11 | Catalysts & Chemicals Inc | Production of hydrogen |
-
0
- US US417068D patent/US417068A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2998303A (en) * | 1958-08-26 | 1961-08-29 | Midland Ross Corp | Method for purifying hydrogen contaminated with methane |
| US3088919A (en) * | 1958-09-10 | 1963-05-07 | Engelhard Ind Inc | Treatment of gases |
| US3387942A (en) * | 1965-05-10 | 1968-06-11 | Catalysts & Chemicals Inc | Production of hydrogen |
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