USRE4998E - Improvement in purifying illuminating-gas and utilizing the wastes therefrom - Google Patents
Improvement in purifying illuminating-gas and utilizing the wastes therefrom Download PDFInfo
- Publication number
- USRE4998E USRE4998E US RE4998 E USRE4998 E US RE4998E
- Authority
- US
- United States
- Prior art keywords
- gas
- iron
- utilizing
- purifying
- improvement
- Prior art date
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 44
- 239000000463 material Substances 0.000 description 32
- 229910052742 iron Inorganic materials 0.000 description 22
- 239000007789 gas Substances 0.000 description 20
- 239000005864 Sulphur Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 14
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 14
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- BAUYGSIQEAFULO-UHFFFAOYSA-L Iron(II) sulfate Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 10
- 239000001257 hydrogen Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 150000002431 hydrogen Chemical class 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 4
- 229910052748 manganese Inorganic materials 0.000 description 4
- 239000011572 manganese Substances 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000005712 crystallization Effects 0.000 description 2
- 230000001627 detrimental Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000000717 retained Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
Definitions
- the object of this invention is to turn to profitable account the several chemical substances which are now wasted generally, to the detriment of the localities where gasworks are situated, by being allowed to pass into the sewers or waters surrounding such places.
- My invention consists in the process of extracting and utilizing the above-mentioned impurities contained in crude gas after they have been separated therefrom by the action of the material I employ for that purpose, and restoring such purifying material after it has become charged to its full extent with such impurities, all as more fully hereinafter described. Before proceeding to describe my process of restoring and utilizing, I will first describe the purifying process by which the material to be restored is produced.
- the manner in which the material (hereinafter more fully described) is made use of in the purifying of gas is as follows: In the ordinary purifiers, consisting of iron boxes of ahyshape, with trays or screens on which the purifying material is placed, and through which the gas is passed, I place my material to the depth of five or six inches, or more, in the same manner as lime or oxide of iron are at present used. The impure gas from the condensers is then passed into the bottom of such ordinary purifiers, and passing upward by to.
- I use ggeen copperas (sulphate of iron) either crystallize or an y us, with or without the admixture of sawdust, or other kindred material, to render the sulphate of iron light 'and porous, to allow the free passage of gas through the substance in the purifiers.
- I may use the residuum from the manufacture-of sulphur from what is commercially termed spent oxide of iron that is to say, oxide of iron, iron-ore, bog-ore, or any other suitable compound of iron, which has been used for the purification of gas from sulphureted hydrogen, until it is so fully charged with sulphur as to be of no further use for purifying purposes.
- Sul hate of manganese may also be employed in similar manm described for sulphate of iron; as also the residuum from oxide of manganese when charged with sulphur, and treated in a similar manner as described for spent oxide of iron.
- This material when placed in purifiers, as previously described, and coming in contact with gas containing ammonia and sulphureted hydrogen, causes a chemical action to take place, such ammonia being retained by the sulphuric acid of the material, thereby forming sulphate of ammonia with the precipitation of the iron of the material, which iron decomposes the sulphureted hydrogen by combining with the sulphur therein contained. This action is constant until thorough saturation of the material is accomplished, when it is removed to be replaced by fresh material. This saturated material will then contain about thirty-three per cent. of sulphate of ammonia.
- the saturated material can be subjected to the action of water,whereby the sulphate of ammonia therein contained can be extracted in solution, and the salt produced by crystallization or evaporation of the said solution, and the remaining mixtures of iron, sulphur, and other substances are then subjected to heat without access of air in vessels or retorts, and proceeded with as before stated for the reformation of sulphate of iron for subsequent operations.
Description
XP QE 9998 UNITED STATES ST AVAILABLE COPY ROBERT J. EVERETT, OF BRIDGEPORT, CONNECTICUT, ASSIGNOR TO WIL- LIAM H. ADAMS, OF SAME PLACE.
IMPROVEMENT IN PURIFYING ILLUMINATING-GAS AND UTILIZING THE WASTES THEREFROM.
Specification forming part of Letters Patent No. 125,943, dated April 23,1872; reissue No.4,998, dated July To all whom it may concern:
Be it known that I, ROBERT J. EVERETT, of London, England, temporarily residing in Bridgeport, in the county of Fairfield and State of Connecticut, have invented a new Improvement in Process of PurifyingIlluminating-Gas and Utilizing the Wastes therefrom; and I do hereby declare the following to be a full, clear, and exact description of the same.
In the ordinary methods of purifying gas after passing the condenser excessive amounts of water are used in what is termed the sembher, by which process certain portions of the ammonia and sulphureted hydrogen contained in the crude gas are separated, and in most cases are washed away, thus occasioning great loss of valuable materials, at the same time being exceedingly detrimental to the health of large cities.
The object of this invention is to turn to profitable account the several chemical substances which are now wasted generally, to the detriment of the localities where gasworks are situated, by being allowed to pass into the sewers or waters surrounding such places. My invention consists in the process of extracting and utilizing the above-mentioned impurities contained in crude gas after they have been separated therefrom by the action of the material I employ for that purpose, and restoring such purifying material after it has become charged to its full extent with such impurities, all as more fully hereinafter described. Before proceeding to describe my process of restoring and utilizing, I will first describe the purifying process by which the material to be restored is produced.
The manner in which the material (hereinafter more fully described) is made use of in the purifying of gas is as follows: In the ordinary purifiers, consisting of iron boxes of ahyshape, with trays or screens on which the purifying material is placed, and through which the gas is passed, I place my material to the depth of five or six inches, or more, in the same manner as lime or oxide of iron are at present used. The impure gas from the condensers is then passed into the bottom of such ordinary purifiers, and passing upward by to. I use ggeen copperas (sulphate of iron) either crystallize or an y us, with or without the admixture of sawdust, or other kindred material, to render the sulphate of iron light 'and porous, to allow the free passage of gas through the substance in the purifiers. Instead of the above, I may use the residuum from the manufacture-of sulphur from what is commercially termed spent oxide of iron that is to say, oxide of iron, iron-ore, bog-ore, or any other suitable compound of iron, which has been used for the purification of gas from sulphureted hydrogen, until it is so fully charged with sulphur as to be of no further use for purifying purposes. Sul hate of manganese may also be employed in similar manm described for sulphate of iron; as also the residuum from oxide of manganese when charged with sulphur, and treated in a similar manner as described for spent oxide of iron. This material, when placed in purifiers, as previously described, and coming in contact with gas containing ammonia and sulphureted hydrogen, causes a chemical action to take place, such ammonia being retained by the sulphuric acid of the material, thereby forming sulphate of ammonia with the precipitation of the iron of the material, which iron decomposes the sulphureted hydrogen by combining with the sulphur therein contained. This action is constant until thorough saturation of the material is accomplished, when it is removed to be replaced by fresh material. This saturated material will then contain about thirty-three per cent. of sulphate of ammonia.
I will now proceed to describe my process while the residuum left in the retorts or vessels, which consists of sulphuret of iron, is proceeded with by being quenched with water to prevent the oxidization of the sulphur therein contained, and exposed to the action of the air in heaps, where, by the absorption of oxygen by both the iron and sulphur it contains, it reforms into sulphate of iron, as originally commenced with, which can then be employed for further purifying operations, as previously-described. It preferred, the saturated material can be subjected to the action of water,whereby the sulphate of ammonia therein contained can be extracted in solution, and the salt produced by crystallization or evaporation of the said solution, and the remaining mixtures of iron, sulphur, and other substances are then subjected to heat without access of air in vessels or retorts, and proceeded with as before stated for the reformation of sulphate of iron for subsequent operations.
This invention was patented in England, dated April 14, 1870, No. 1,099.
I claim as my invention The process herein described for restoring and utilizing the said material after it has become charged, as and for the purpose specified.
ROBERT J. EVERETT.
Witnesses:
O. H. HEWETT, HENRY G. BEACH.
Family
ID=
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