US9249A - Improvement in the manufacture of sulphuric acid - Google Patents
Improvement in the manufacture of sulphuric acid Download PDFInfo
- Publication number
- US9249A US9249A US9249DA US9249A US 9249 A US9249 A US 9249A US 9249D A US9249D A US 9249DA US 9249 A US9249 A US 9249A
- Authority
- US
- United States
- Prior art keywords
- acid
- sulphuric acid
- water
- sulphur
- improvement
- 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
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 title description 46
- 239000001117 sulphuric acid Substances 0.000 title description 46
- 235000011149 sulphuric acid Nutrition 0.000 title description 46
- 238000004519 manufacturing process Methods 0.000 title description 12
- 239000002253 acid Substances 0.000 description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 28
- 239000007789 gas Substances 0.000 description 26
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 18
- 239000005864 Sulphur Substances 0.000 description 16
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 16
- FGIUAXJPYTZDNR-UHFFFAOYSA-N Potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 12
- 210000002683 Foot Anatomy 0.000 description 10
- 239000007788 liquid Substances 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 8
- 238000009835 boiling Methods 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 230000000266 injurious Effects 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 235000010333 potassium nitrate Nutrition 0.000 description 6
- NFMHSPWHNQRFNR-UHFFFAOYSA-N Hyponitrous acid Chemical compound ON=NO NFMHSPWHNQRFNR-UHFFFAOYSA-N 0.000 description 4
- VWDWKYIASSYTQR-UHFFFAOYSA-N Sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- 238000005755 formation reaction Methods 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-N sulfonic acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 4
- DMNITBFQZYSTHM-UHFFFAOYSA-N CHEMBL369802 Chemical compound ON=[N+](O)[O-] DMNITBFQZYSTHM-UHFFFAOYSA-N 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- 241000252233 Cyprinus carpio Species 0.000 description 2
- 210000003414 Extremities Anatomy 0.000 description 2
- 206010022114 Injury Diseases 0.000 description 2
- 210000001138 Tears Anatomy 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000004075 alteration Effects 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- HOPSCVCBEOCPJZ-UHFFFAOYSA-N carboxymethyl(trimethyl)azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CC(O)=O HOPSCVCBEOCPJZ-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 230000002939 deleterious Effects 0.000 description 2
- 230000001627 detrimental Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 150000002823 nitrates Chemical class 0.000 description 2
- 230000001473 noxious Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000035943 smell Effects 0.000 description 2
- 230000002459 sustained Effects 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/69—Sulfur trioxide; Sulfuric acid
- C01B17/88—Concentration of sulfuric acid
Definitions
- Concentrated sulphuric acid marking 66 by Baums areometer consists of sulphur, one equivalent, S; oxygen, three equivalents, 0,; water, one equivalent, HO. ⁇ Vithin the last century this acid has been made on a large scale in leaden chambers, where the gases resulting from the combustion of sulphur mixed with azotate or nitrate of potash, azotic or nitric acid,.and the vapor of water give rise to the formation of the sulphuric acid in the leaden chambers.
- AZO hypoazotic or hyponitric acid
- hypoazotic acid which forms again azotic acid, recommencing always the same reactions as long as the aforesaid productions of gas are allowed to enter the chamber.
- the last particles which are carried by the currrent into the tube G, and so into the chimney consist of nothing more than an aeriform production composed of azote and oxygens of I no value to the fabrication, and are without smell and not injurious to the vicinity.
- obturator H serves to regulate the draft during the operation.
- the collected acidin the receptacle D is employed for the decomposition of the azotates in the sulphur-oven, as I shall show afterward. 4
- a platina apparatus serves only to extract the fifteen one-hundredths of the excess of water which the acid of 60 contalns.
- a complete apparatus of platina large enough to contain about three hundred and fifty pounds of acid, weighs from one hundred and eighty to two hundred pounds, costs one hundred thousand francs. Each operation lasts one hour, which gives in ten hours a total of three thousand five hundred pounds concentrated acid to one equivalent of water at 66 Baum,
- the apparatus has often to undergo expensive repairs, caused by the high temperature of boiling acid, (325 centigrade or 617 Fahrenheit,) also from the fact that the acid coming from the lead basin marking 60 moderates the temperature, and thereby contracts more or less the metal, so that after a certain number of operations the apparatus is liable to crack.
- the interest of the cost and the wear and tear may be calculated at five dollars per day. I
- My concentrating apparatus is composed of a leaden kettle, Fig. 2, A, twelve feet long, six feet width, one foot high, and one-fourth of an inch in thickness, covered with a leaden chapiteau, B, the tubes of which, 0 O 0, communicate with a refrigerator or condenser destined to receive the weak acid which evaporates with the water.
- This kettle is placed on a brick oven and sustained by large plates of cast-iron common to all establishments of 'ing filled in the carboys.
- the acid which I obtain with care and the apparatus thus described is as pure as it is possible to obtain, and does not injure the lead of the kettle in which it is concentrated.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
Qctober 15 1913.
DRAWING A careful search has been made this day for the original drawing or a photolithographic copy of. the same,
for the purpose of reproducing the said drawing to form a.
part of this book, but at. this time nothing can be found from which a. reproduction can be made.
Finis D6 Mirna-ri Chief of Division E,
Nrra STATES PATENT l rrrcn.
CARP HINRICHS, OF NEWV YORK, N. Y.
Specification forming part of Letters Patent No. 9.2 .19, dated September 7, 1 1-52.
To all whom it may concern.-
Be it known that I, CARL HINRIOHS, of New York city, and county and State of New York, have invented a new Method of Fabricating and Concentrating Sulphuric Acid, of which the following is a full and exact description.
Concentrated sulphuric acid marking 66 by Baums areometer consists of sulphur, one equivalent, S; oxygen, three equivalents, 0,; water, one equivalent, HO. \Vithin the last century this acid has been made on a large scale in leaden chambers, where the gases resulting from the combustion of sulphur mixed with azotate or nitrate of potash, azotic or nitric acid,.and the vapor of water give rise to the formation of the sulphuric acid in the leaden chambers.
First. The burning sulphur combines with two equivalents of oxygen and forms sulphurous acid, S0,.
Second. Burning azotate or nitrate of potash furnishes deutoxide of azote, which, in
contact with the air, passes immediately into a state of hypoazotic or hyponitric acid, AZO,.
Third. Hypoazotic acid, coming in contact with the vapor of water, is immediately converted into azotic or nitric acid, AZO
Fourth. The azotic acid containing five equivalents of oxygen gives one equivalent to thesulphurous acid, which becomes thus transformed into sulphuric acid, S0,.
Fifth. At last there remains hypoazotic acid, which forms again azotic acid, recommencing always the same reactions as long as the aforesaid productions of gas are allowed to enter the chamber.
After having formed sulphuric acid, which remains liquid in the chambers, a considerable part of gases having escaped in the complex decompositions which take place in the interior, loose themselves in the exterior and spread in the neighborhood of every factory vapors injurious to animal life and detrimental to all vegetation. These vapors are hypoazotic acid, protoxide of azote, liberated azote,
.sulphurous acid, chlorine arising from impure nitrates of azotates, sulphuric acid, which passes off by the current of air and the vapors of water, 820.
To prevent the sensible loss of hypoazotic acid there is used in many factories an invention of Gay Lussac, which consists in passing the gas which leaves the leaden chamber through coke moistened with sulphuric acid, which absorbs only the hypoazotic gas and disengages the other productions of gas in the atmosphere. This sulphuric acid, charged with hypoazotic acid,is again introduced,with the products of the combustions of sulphur, into the chambers. It proves an economical employment of the azotates which are mixed with the sulphur; but to carry out the designs of my invention in the fabrication of sulphuric acid I have to use a condensing apparatus, which also prevents the noxious gases from doing injury to the neighborhood, which is always objectionable to the neighborhood. It is composed of a long leaden pipe, (at least eighty feet long and one foot diameter,) equal in diameter to that by which the products ofthe combustion of the sulphur-oven are introduced into the chamber. This pipe is placed horizontally outside of the last chamber, where it receives the escaping gases. The extreme end of it is shown at A, Figure 1, where, at the extremity, the pipe inclines at B to communicate with a reservoir, E, lined with lead containing a liquid put in motion by an agitator, F, to facilitate the absorption of the gases which must traverse the agitated liquid before entering the pipe G, that conducts them to the chimney of the establishment. This is an explanation of the operation of the apparatus. The products of gas, warmand humid, leaving the last chamber begin to condense in the horizontal lead pipe A, Fig. 1, where the sulphuric acid deposits throughout its length, presentinga continuous surface moistened with sulphuric acid which retains the hypoazotic or hyponitrous acid. This sulphuric acid, chargedwith hypoazotic in the horizontal pipe A, Fig. 1, descends into the inclined part B and drops constantly from the serpentine tube 0, Fig. 1,-into the receptacle D, Fig. 1. All other of the aforesaid gases pass into the reservoir E, where they are condensed and absorbed by milk of lime, which forms multiplied cascades round an agitator put in motion at F by a machine or by manual power. After traversing this liquid, the last particles which are carried by the currrent into the tube G, and so into the chimney, consist of nothing more than an aeriform production composed of azote and oxygens of I no value to the fabrication, and are without smell and not injurious to the vicinity. The
. necessary caloric.
obturator H serves to regulate the draft during the operation. The collected acidin the receptacle D is employed for the decomposition of the azotates in the sulphur-oven, as I shall show afterward. 4
To prevent the presence of an excess of azotic acid in the chambers, which is always more or less injurious to the lead, I avoid carefully the introduction of said liquid in the chambers, because the atmospheric air which continually enters through the doors of the sulphur-oven for the formation of the sulphuric acid furnishes three-fourths of the oxygen necessary.
I obtain a satisfactory result in decomposing one-tenth (of the quantity of burning sulphur) of nitrate of potash or of soda bythe sulphuric acid charged with hyponitrousacid gas provided by the receptacle D of the condensing apparatus. The decomposition takes place in iron pans placed in the oven above the sulphur, of which the combustion furnishes the Sulphuric acid obtained by this mode-of fabrication is purer than that generally produced. Vhen it marks in the chamber 50 Baum, it forms sulphuric acid one equivalent equal to 66.5; water in excess, 33.5. I let it run in the evaporating-kettle common to all factories, to separate from it a great part of its water, until the concentration reaches 60 Baum, viz: sulphuric acid, one equivalent, eighty-five; water in excess, fifteen. Then I introduce it into the leaden apparatus which I have invented to replace the apparatus of platina, of which I give below the ex planation.
A platina apparatus serves only to extract the fifteen one-hundredths of the excess of water which the acid of 60 contalns. A complete apparatus of platina, large enough to contain about three hundred and fifty pounds of acid, weighs from one hundred and eighty to two hundred pounds, costs one hundred thousand francs. Each operation lasts one hour, which gives in ten hours a total of three thousand five hundred pounds concentrated acid to one equivalent of water at 66 Baum, The apparatus has often to undergo expensive repairs, caused by the high temperature of boiling acid, (325 centigrade or 617 Fahrenheit,) also from the fact that the acid coming from the lead basin marking 60 moderates the temperature, and thereby contracts more or less the metal, so that after a certain number of operations the apparatus is liable to crack. The interest of the cost and the wear and tear may be calculated at five dollars per day. I
My concentrating apparatus is composed of a leaden kettle, Fig. 2, A, twelve feet long, six feet width, one foot high, and one-fourth of an inch in thickness, covered with a leaden chapiteau, B, the tubes of which, 0 O 0, communicate with a refrigerator or condenser destined to receive the weak acid which evaporates with the water. This kettle is placed on a brick oven and sustained by large plates of cast-iron common to all establishments of 'ing filled in the carboys.
served through the opening E, which also serves to ascertain the degree of the acid. You thus obtain five thousand pounds sulphuric acid of 66 Baum. By aid of a siphon it is made to run in a reservoir, where it cools and deposits whatever may solidify before be- The operation can be recommenced or the apparatus allowed to cool Without fear of accident. Till now sulphuric acid has never been concentrated to 66 Baum without being made to boil, and this is why lead could not be used, as it melts at322 centigrade or 612 Fahrenheit, while boiling acid stands 325 centigrade or 617 Fahrenheit. Another cause of the impracticability of concentrating on lead is the presence of azotic acid, and even chlorine, which the azotic acid proceeding from an impure niter containing hydrochlorates introduced into the sulphuric acid. In this case even platina is attacked.
The acid which I obtain with care and the apparatus thus described is as pure as it is possible to obtain, and does not injure the lead of the kettle in which it is concentrated.
It is easy to understand that the acid of 60 Baum abandons Without boiling the fifteen one-hundredths parts of water in excess at the high temperature, which augments without ceasing just at the boiling-point of the concentrated acid, because this water does not form with the acid a stable composition, while arrived at 66 the acid contains one equivalent of water. Its composition is very stable.
It boils at 325 centigrade or 617 Fahrenheit, and distills Without alteration. This is the concentrated sulphuric acid used in commerce, and composed, as said at the commencement of this specification, of sulphur, one equivalent, S; oxygen, three equivalents, 0,; water, one equivalent, HO.
What I claim as my invention, and desire to secure by Letters Patent, is-
1. Concentrating sulphuric acid in leaden Vessels to the strength of 66 Baum, and at a temperature below the boiling-point of the acid.
2. The long conducting and escape pipe, in combination with the agitating apparatus for condensing the deleterious gases and preserving a pure and wholesome air in the neighborhood of the establishment.
CARL HINRIGHS. \Vitnesses:
J. W. HERBST, SYLVANUS MAYO.
Publications (1)
Publication Number | Publication Date |
---|---|
US9249A true US9249A (en) | 1852-09-07 |
Family
ID=2069568
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US9249D Expired - Lifetime US9249A (en) | Improvement in the manufacture of sulphuric acid |
Country Status (1)
Country | Link |
---|---|
US (1) | US9249A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6106018A (en) * | 1999-08-27 | 2000-08-22 | Acco Brands, Inc. | Cover mounted tab index system |
WO2021229237A1 (en) | 2020-05-14 | 2021-11-18 | Ucl Business Ltd | Cyclosporine analogues |
-
0
- US US9249D patent/US9249A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6106018A (en) * | 1999-08-27 | 2000-08-22 | Acco Brands, Inc. | Cover mounted tab index system |
WO2021229237A1 (en) | 2020-05-14 | 2021-11-18 | Ucl Business Ltd | Cyclosporine analogues |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3226192A (en) | Process of treating waste gas containing sulfur oxide | |
GB1475392A (en) | Process and apparatus for purifying an effluent | |
US9249A (en) | Improvement in the manufacture of sulphuric acid | |
DE19807632A1 (en) | Device for concentrating and purifying sulfuric acid | |
US1984674A (en) | Production of pure phosphorus | |
Gattermann | The Practical Methods of Organic Chemistry | |
US815761A (en) | Glycerin-still. | |
Rambousek | Industrial poisoning from fumes, gases and poisons of manufacturing processes | |
US576264A (en) | James dick gilmour | |
US866580A (en) | Process of roasting fusible ores. | |
US45684A (en) | Improvement in the manufacture and purification of magnesium | |
US107711A (en) | Adolph ott | |
SU1005654A3 (en) | Process for producing sulfuric anhydride | |
US2091937A (en) | Treatment of acid sludge | |
US477375A (en) | Julius lang | |
US1154145A (en) | Process for the production of nitrogen. | |
US605369A (en) | Liffe kynaston | |
SU20648A1 (en) | Modification of the method for producing high concentration ammonia gas from ammonia water described in patent number 3856 | |
US35742A (en) | Improvement in the manufacture of oxygen gas | |
US1197167A (en) | Process of concentrating nitric acid. | |
Nichols | An Elementary Manual of Chemistry: Abridged from Eliot and Storer's Manual | |
Reid | Elements of Practical Chemistry, comprising a series of experiments in every department of chemistry, etc | |
US1092620A (en) | Process and apparatus for wood distillation. | |
US1236662A (en) | Manufacture of concentrated nitric acid. | |
US517098A (en) | Concentrated niteic acid |