Title of Invention	"A PROCESS FOR REMOVING CHLORIDE FROM A CHLORIDE CONTAINING IRON OXIDE TO PRODUCE IRON OXIDE WITH A REDUCED CHLORIDE CONTENT"
Abstract	A process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content, which process comprises the steps of: a) mixing the chloride-containing iron oxide with a solution in a conventional manner for a period of time sufficient to form a mixture, the said solution comprising sulphuric acid (H2SO4); and b) separating the iron oxide from the mixture formed in step (a) and then optionally heating at a temperature from 1°C above the ambient temperature to 1400°C for a period of time from 1 minute to 100 hours to obtain the iron oxide having a reduced chloride content.

Title of Invention

"A PROCESS FOR REMOVING CHLORIDE FROM A CHLORIDE CONTAINING IRON OXIDE TO PRODUCE IRON OXIDE WITH A REDUCED CHLORIDE CONTENT"

Abstract

A process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content, which process comprises the steps of: a) mixing the chloride-containing iron oxide with a solution in a conventional manner for a period of time sufficient to form a mixture, the said solution comprising sulphuric acid (H2SO4); and b) separating the iron oxide from the mixture formed in step (a) and then optionally heating at a temperature from 1°C above the ambient temperature to 1400°C for a period of time from 1 minute to 100 hours to obtain the iron oxide having a reduced chloride content.

Full Text	This invention relates to a process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content. During the last twenty years, the regenerated iron oxides (RIO) produced from hydrochloric acid waste liquid generated from steel pickling have been recognized as an important source of raw material for preparing products containing iron oxides such as iron-oxide based catalysts and high-grade ferrites. The raw material cost savings associated with the substitution of a low cost, regenerated iron oxide for most of the conventional commercial sources of iron oxides are substantial. One drawback of utilizing regenerated iron oxides from hydrochloric acid waste liquids generated from steel pickling is that the ferric oxides inevitably contain chloride ions, typically in the range of about 0.1 to 0.5% measured as grams of chloride per 100 grams of regenerated iron oxide. In the field of ethylbenzene dehydrogenation catalysts, it is known that the small amounts of residual chloride present in all regenerated iron oxides affect catalyst performance adversely. For the ferrite producers, the chloride ion present in the regenerated iron oxide is not only corrosive to the ferrite manufacturing installations but also injurious to the quality of the ferrite produced. Reducing the chloride-ion content in regenerated ion oxides by an economical procedure, without significantly changing the ferric oxide quality is believed to be one of the most critical issues for the development of regenerated iron oxides as commercially useful raw materials. Japanese patent application J59,050,031, published September 13, 199.2, discloses a method for purifying iron oxide from waste hydrochloric acid pickling solution containing ferric chloride by treatment with ferrous sulfate, ferric sulfate or ammonium sulfate solution. The iron oxide purified by this prior art method still contains a substantial amount of chloride. Moreover, it is time consuming to dissolve these salts in water. Furthermore, the raw material costs for these sulfate salts are relatively high. Suganuma, et al. in 4th International Conference on Ferrites, Advances in Ceramics, Vol. 15, 81-85 (1986), reported a method for removing chloride ions from hematite powders by heating the ferric oxide in air with the addition of sulphur dioxide and/or moisture. However, sulphur oxide is a toxic gas which is unhealthy and environmentally undesirable. Thus, there remains a need for a commercial process which will substantially reduce the chloride contents in regenerated iron oxides (RIO) at a low cost without significantly changing the quality of the iron oxides. Accordingly, the present invention relates to a process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content, which process comprises the steps of: a) mixing the chloride-containing iron oxide with a solution in a conventional manner for a period of time sufficient to form a mixture, the said solution comprising sulphuric acid (H2SO4); and b) separating the iron oxide from the mixture formed in step (a) and then optionally heating at a temperature from 1°C above the ambient temperature to 1400°C for a period of time from 1 minute to 100 hours to obtain the iron oxide having a reduced chloride content. The iron oxides to be treated by the process of the present invention in its broadest aspect are selected from any iron oxides of mineral or synthetic origin which contain either trace or substantial amounts of chloride. Various methods for the obtaining of iron oxides from scrap steel, steel scaling liquors, or iron chloride as industrial waste product have been described in U.S. Patent No. 4,935,219. The iron oxides obtained from some of these methods inevitably contain residual chlorides originating from the chloride-containing reagents or raw materials present during the process of generating the iron oxides. As a preferred embodiment, the iron oxides treated in the instant invention are the regenerated iron oxides (RIO) produced from hydrochloric acid waste liquids generated from steel pickling. During the process of producing the regenerated iron oxides, hydrochloric acid pickling wastes are sprayed into a roaster, whereby water and free HCl in the wastes are driven off quickly, while FeCl2 is hydrolyzed to produce iron oxide and hydrogen chloride. The regenerated iron oxides contain chloride ions, typically in the range of from about 800 pairts per million to abou':: 20,000 parts per million, particularly in the range of from about 800 to 5,000 parts per million, by weight of the: regenerated iron oxides. The sulfuric acid used in treating iron oxides in the instant invention can be any commercial or reagent grade: sulfuric acid. Preferably, concentrated sulfuric acid is diluted with water, more preferably with deionized water or distilled water, before being used as the reagent for treating iron oxides. In a specific embodiment of the present invention, concentrated sulfuric acid with specific gravity of about 1.84 g/ml is diluted with about ten time; to 100 times by volume of deionized water prior to being used for treating the iron oxide. The molar amount of sulfuric acid in the sulfuric acid solution used for treating iron oxides is generally a molar amount of from 0.5 co 10, preferably from 1.0 to 5.0, more preferably from i.8 to 2.5, still more preferably 2.0 times relative to the total molar amount cf chloride present in the iron oxides to be treated. The iron oxides may be treated with a sulfuric acid solution by any method known to one skilled in the art which would achieve thorough mixing of the iron oxides with the sulfuric acid solution As a non- limiting example, the iron oxides may be slurried with the sulfuric solution followed by either decantation or filtering. As another non-limiting example, the iron oxides may also be wetted with the sulfuric acid solution and mulled to form a paste. In the broadest aspect of the present invention, the iron oxides are treated with the sulfuric acid solution for at least a period of time sufficient to achieve thorough mixing of the sulfuric acid solution with the iron oxides. Typically, the treatment lasts from 1 minute to 4 8 hours. In a specific embodiment of the present: invention, the treatment lasts from 3 minutes to 5 hours, more specifically from 10 minutes to 30 minutes. The treatment of iron oxides with sulfuric acid solution can be conducted under a pressure from about 50 kPa to about 10000 kPa. Lr one specific embodiment of the present invention, it is conducted under ambient pressure. The treatment can be conducted in any suitable atmosphere. Non-limiting examples of the suitable atmosphere include: air, other oxygen containing gaseous streams, and inert gaseous streams. After the iron oxides are treated with sulfuric acid solution, they can be separated from the solution by any suitable separation method. Without intending to limit the scope of the invention, the treated iron oxides can be separated out by filtration, centrifugation, etc. As a preferred embodiment of the present invention, the treated iron oxides, after being separated from the sulfuric acid solution are subsequently heated at an elevated temperature. The heating and/or calcining is typically conducted at a temperature ranging from 1° above the ambient temperature to 14 00 °C for a period of tim«: sufficient to dry or calcine the treated iron oxides completely. Typically, the iron oxides are calcined and/or dried for from 1 minute to 100 hours. This heating step can be a simple drying process, a calcination process, or a staged drying and calcination process. The heating is conducted under a pressure typically from 10 k?a to 1100 kPa. As a non-limiting example, the heating step can be conducted under ambient pressure. The heating step can be conducted under any suitable atmospheres. Non-limiting examples or: the suitable atmospheres for the heating step include air, oxygen containing gaseous streams, inert gaseous streams, and vacuum. In one specific embodiment of the present invention, the iron oxides are treated with a sulfuric acid solution and the treated iron oxides are separated from the solution without subsequent heating. The treated iron oxides can optionally be dried in air at ambient temperature and ambient pressure. In another specific embodiment of the present invention, the iron oxides are dried in air at a temperature between 30 °C and 300 °C, preferably between 50 °C and 300 °C, more preferably between 100 °C and 300 °C, for a period of time ranging from 1 minute to 72 hours, preferably from 2 minutes to one hour, more preferably from 10 minutes to 30 minutes. In a preferred embodiment, the treated iron oxides are subsequently calcined for a period of time from 1 minute to 72 hours, preferably from 15 minutes to 10 hours, more preferably from 30 minutes to 2 hours. In another preferred embodiment, the iron oxides are first dried at a temperature between 30 °C and 300 °C, preferably between 120 °C and 200 °C for a period of time ranging from 1 minute to 72 hours, preferably from 2 minutes to one hour, more preferably from 10 minutes to 30 minutes, and then calcined for a period of time from 1 minute to 72 hours, preferably from 15 minutes to 10 hours, more preferably from 30 minutes to 2 hours. After the iron oxides are dried and optionally calcined, a sample of the treated iron oxides can be analyzed with a suitable analytical method(s) to determine the chloride content. The post-treatment chloride content is then compared with the chloride content measured prior to the treatment. The; invention will be exemplified by the following illustrative embodiments. Illustrative Embodiments The following illustrative embodiments describe typical techniques of the present invention for reducing chloride content :n the regenerated iron oxides and the typical techniques for measuring the chloride contents of the iron oxides. The chloride contents were determined using Kevex Model 770 Energy Dispersive X-Ray Fluorescence Instrument. Part A: Regenerated Iron Oxide The ferric oxide used in the present embodiment was a commercial product of regenerated iron oxide produced from hydrochloric acid waste liquid generated from steel pickling. The chloride content of this regenerated iron oxide was about 1400 parts per million by weight of the regenerated iron oxide. 600 grams of the regenerated iron oxide were used for each Illustrative Embodiment below. The total amount of the chloride present in the 600 grams of regenerated iron oxxde with 1400 parts per million (ppm) of chloride was estimated to be about 0.84 grams or 0.0237 moles based on mathematical calculation. Part B: Preparation of H2SO4 solution B-l: H2S04 Solution of 1:1 Ratio Relative to Cl 1.3 millilitres of concentrated sulfuric acid with specific gravity of 1.84 g/ml were added to 61.7 millilitres of deionized water to make a solution of about 63 millilitres containing approximately 0.0237 moles of H2SO4, which was equal to the molar amount of the chloride contained in the 600 grams of regenerated iron oxide from Part A above. B-2: H2S04 Solution of 2:1 Ratio Relative to Chloride 2.6 millilitres of concentrated sulfuric acid with specific gravity of 1.84 g/ml were added to 60.4 millilitres of water to make a solution of about 63 millilitres by volume containing approximately 2 X 0.0237 moles of H2SO4 which was twice the molar amount of the chloride present in the 600 grams of the regenerated feme oxide from Part A. Part C: Reduction of Chloride in Ferric Oxide I. H2S04 TREATMENT FOLLOWED BY DRYING Method 1-1: Treatment with H2S04, 2:l/Dried at 50 °C 600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes. During mulling, 63 millilitres of the H2SO4 solution, prepared from B-2 above, containing a molar amount of H2SO4 in the H2SO4 solution of about twice the amount of choride contained in 600 grams of the regenerated iron oxide, were added gradually to the regenerated iron oxide. The wet iron oxide powdei was filtered through a 2.83 mm (#7 mesh) screen and then dried for 15 nu.nutes at 50 °C under ambient pressure. The chloride content of the dried sample was 1200 parts per million by weight of the total iron oxides. Method 1-2: Treatment with H2S04, 2:l/Dried at 120 °C 600 grams of the regenerated iron oxide from Part A above were treated with the same H2SO4 solution in the same way as Method I-l above, except that subsequent to the filtration step the treated iron oxide powder was dried at 120 °C at ambient pressure for 15 minuces. The chloride content of the dried sample was 720 ppm. Method 1-3: Treatment with H2S04, l:l/Dried at 170 °C 600 grams of the regenerated iron oxide from Part A were mulled for 15 minutes. During mulling, 63 millilitres of the H2SO4 solution,, prepared from B-l above, containing a molar amount of H2SO,} in the H2SO4 solution about equal to the molar amount of choride contained in 600 grams of the regenerated iron oxide, were added gradually to the regenerated iron oxide. The wet iron oxide powder was filtered through a 2.83 mm (#7 mesh) screen and then dried for 15 minutes at 170 °C under ambient pressure. The chloride content of the dried sample was 550 parts per million by weight of the cotal iron oxides. Method 1-4: Treatment with H2S04, 2:l/Dried at 170 °C 600 grams of the regenerated iron oxide from Part A above were treated with the same H2SO4 solution in the same way as Method 1-2 above, except that subsequent to the filtration step the treated iron oxide powder was dried at 170 °C at ambient pressure. The chloride content of the dried sample was 510 ppm. The results of study I are shown in Table I below. TABLE I REGENERATED IRON OXIDE CHLORIDE REDUCTION STUDY I (Table Removed) II. H2S04 TREATMENT FOLLOWED BY DRYING AND CALCINING Method C-l:Comparative Embodiment - Calcination without H2S04 600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes without the addition of any H2S04 solution. The mulled iron oxide were then dried for 15 minutes at 170 °C. Thirty grams of the dried oxide were calcined in a static kiln under air having one atmosphere pressure for one hour at 825 °C. The resulted chloride content was 810 ppm. Method C-2: Comparative Embodiment - Treatment with H20/ Calcined 600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes. During mulling, 63 millilitres of deionizea water were gradually added to the regenerated iron oxide. The wet iron oxide powder was filtered through a 2.83 mm (#7 mesh) screen and then dried for 15 minutes at 170 °C. Thirty grams of the dried oxide were calcined in a static kiln under air having one atmosphere pressure for one hour at 825 °C. The resulting chloride content wa 880 ppm. Method II-l: Treatment with H2S04, 1:l/Dried/Calcined Thirty grams of the dried oxide from Method 1-3 above were calcined in a static kiln under air having one atmosphere pressure for one hour at 82:5 °C. The chloride content of the resulting sampl was 510 ppm. Method II-2: Treatment with H2S04, 2:l/Dried/Calcined Thirty grams of the dried oxide from Method 1-4 above were calcined in a static kiln in air with one atmosphere pressure for one hour at 825 °C. The chloride content of the resulting sample wa 390 ppm. The results of study II are shown in Table II below. TABLE II REGENERATED IRON OXIDE CHLORIDE REDUCTION STUDY II 880 '.10 3 90 WITHOUTSUBSEQUENT DRYING/CALCINING Method C-3: Comparative Embodiment - Treatment with H20 (Table Removed) 600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes. During mulling, 63 millilitres of the deionized water were gradually added to the regenerated iron oxide The wet iron oxide powder was filtered through a #7 mesh screen. The chloride content was 10,200 ppm. Method IXI-1: Treatment with H2S04, 2:1 Undried/Uncalcined 600 grams of the regenerated iron oxide from Part A were mulled for 15 minutes. During mulling, 63 millilitres of the H2SO4 solution, prepared from B-2 above, containing a molar amount of H2SO4 in the H2SO4 solution of about twice the molar amount of choride contained in 600 grams of the regenerated iron oxide, were added gradually to the regenerated iron oxide. The wet iron oxide powder was filtered through a 2.83 mm (#7 mesh) screen. The chloride content of the dried sample was 3,200 parts per million by weight of the total iron oxides. The results of study III are shown in Table III below. TABLE III REGENERATED IRON OXIDE CHLORIDE REDUCTION STUDY III (Table Removed) WE CLAIM:- 1. A process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content, which process comprises the steps of: a) mixing the chloride-containing iron oxide with a solution in a conventional manner for a period of time sufficient to form a mixture, the said solution comprising sulphuric acid (H2SO4); and b) separating the iron oxide from the mixture formed in step (a) and then optionally heating at a temperature from 1°C above the ambient temperature to 1400°C for a period of time from 1 minute to 100 hours to obtain the iron oxide having a reduced chloride content. 2. The process as claimed in claim 1, wherein the solution used in step (a) comprises a molar amount of H2SO4 of from 1.0 to 5.0 times the molar amount of chloride in the chloride-containing iron oxide. 3. The process as claimed in claim 1, wherein the solution used in step (a) comprises a molar amount of H2SO4 of from 1.8 to 2.5 times the molar amount of chloride in the chloride-containing iron oxide. 4. The process as claimed in claim 2, wherein in step (a) the iron oxide is mixed with said solution for a period of time which is in the range of from 1 minute to 48 hours. 5. The process as claimed in claim 1, wherein the iron oxide separated from step (t) is heated at a temperature in the range of from 50°C to 300°C for a period of time in the range of form 2 minutes to one hour. 6. The process as claimed in claim 1, wherein the iron oxide separated from step (b) is first heated at a temperature from 50°C to 300°C for a period of time in the range of from 1 minute to 72 hours, and the iron oxide is thereafter heated at a temperature from 400°C to 1400°C and at a pressure of from 10 to 1100 kpa for a period of time in the range of form 1 minute to 72 hours. 7. The process as claimed in any one of claims 1 to 6, wherein the mixing in step (a) is conducted in an oxygen -containing gaseous stream. 8. The process as claimed in any one of claims 1 to 7, wherein the heating after step (b) is conducted in an oxygen-containing gaseous stream. 9. A process as claimed in any one of claims 1 to 8, wherein the chloride-containing iron oxide is regenerated iron oxide produced from a hydrochloric acid waste liquid generated from steel pickling, and comprises from 800 to 5000 ppm by weight of chloride. 10. A process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content substantially as herein described and with reference to the foregoing examples.

Full Text

This invention relates to a process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content.
During the last twenty years, the regenerated iron oxides (RIO) produced from hydrochloric acid waste liquid generated from steel pickling have been recognized as an important source of raw material for preparing products containing iron oxides such as iron-oxide based catalysts and high-grade ferrites. The raw material cost savings associated with the substitution of a low cost, regenerated iron oxide for most of the conventional commercial sources of iron oxides are substantial.
One drawback of utilizing regenerated iron oxides from hydrochloric acid waste liquids generated from steel pickling is that the ferric oxides inevitably contain chloride ions, typically in the range of about 0.1 to 0.5% measured as grams of chloride per 100 grams of regenerated iron oxide. In the field of ethylbenzene dehydrogenation catalysts, it is known that the small amounts of residual chloride present in all regenerated iron oxides affect catalyst performance adversely. For the ferrite producers, the chloride ion present in the regenerated iron oxide is not only corrosive to the ferrite manufacturing installations but also injurious to the quality of the ferrite produced.
Reducing the chloride-ion content in regenerated ion oxides by an economical procedure, without significantly changing the ferric oxide quality is believed to be one of the most critical issues for the development of regenerated iron oxides as commercially useful raw materials.
Japanese patent application J59,050,031, published September 13, 199.2, discloses a method for purifying iron oxide from waste hydrochloric acid pickling solution containing ferric chloride by treatment with ferrous sulfate, ferric sulfate or ammonium sulfate solution. The iron oxide purified by this prior art method
still contains a substantial amount of chloride. Moreover, it is time consuming to dissolve these salts in water. Furthermore, the raw material costs for these sulfate salts are relatively high.
Suganuma, et al. in 4th International Conference on Ferrites, Advances in Ceramics, Vol. 15, 81-85 (1986), reported a method for removing chloride ions from hematite powders by heating the ferric oxide in air with the addition of sulphur dioxide and/or moisture. However, sulphur oxide is a toxic gas which is unhealthy and environmentally undesirable.
Thus, there remains a need for a commercial process which will substantially reduce the chloride contents in regenerated iron oxides (RIO) at a low cost without significantly changing the quality of the iron oxides.
Accordingly, the present invention relates to a process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content, which process comprises the steps of:
a) mixing the chloride-containing iron oxide with a solution in a conventional manner for a period of time sufficient to form a mixture, the said solution comprising sulphuric acid (H2SO4); and
b) separating the iron oxide from the mixture formed in step (a) and then optionally heating at a temperature from 1°C above the ambient temperature to 1400°C for a period of time from 1 minute to 100 hours to obtain the iron oxide having a reduced chloride content.
The iron oxides to be treated by the process of the present invention in its broadest aspect are selected from any iron oxides of mineral or synthetic origin which contain either trace or substantial amounts of chloride. Various methods for the obtaining of iron oxides from scrap steel, steel scaling liquors, or iron chloride as industrial waste product have been described in U.S. Patent No. 4,935,219. The iron oxides obtained from some of these methods inevitably contain residual chlorides originating from the chloride-containing reagents or raw materials present during the process of generating the iron oxides.
As a preferred embodiment, the iron oxides treated in the instant invention are the regenerated iron oxides (RIO) produced from hydrochloric acid waste liquids generated from steel pickling. During the process of producing the regenerated iron oxides, hydrochloric acid pickling wastes are sprayed into a roaster, whereby water and free HCl in the wastes are driven off quickly, while FeCl2 is hydrolyzed to produce iron oxide and hydrogen chloride. The regenerated iron oxides contain chloride ions, typically in the range of from about 800 pairts per million to abou':: 20,000 parts per million, particularly in the range of from about 800 to 5,000 parts per million, by weight of the: regenerated iron oxides.
The sulfuric acid used in treating iron oxides in the instant invention can be any commercial or reagent grade: sulfuric acid. Preferably, concentrated sulfuric acid is diluted with water, more preferably with deionized water or distilled water, before being used as the reagent for treating iron oxides. In a specific embodiment of the present invention, concentrated sulfuric acid with specific gravity of about 1.84 g/ml is diluted with about ten time; to 100 times by volume of deionized water prior to being used for treating the iron oxide.
The molar amount of sulfuric acid in the sulfuric acid solution used for treating iron oxides is generally a molar amount of from 0.5 co 10, preferably from 1.0 to 5.0, more preferably from i.8 to 2.5, still more preferably 2.0 times relative to the total molar amount cf chloride present in the iron oxides to be treated.
The iron oxides may be treated with a sulfuric acid solution by any method known to one skilled in the art which would achieve thorough mixing of the iron oxides with the sulfuric acid solution As a non- limiting example, the iron oxides may be slurried with the sulfuric solution followed by either decantation or filtering. As another non-limiting example, the iron oxides may also be wetted with the sulfuric acid solution and mulled to form a paste.
In the broadest aspect of the present invention, the iron oxides are treated with the sulfuric acid solution for at least a
period of time sufficient to achieve thorough mixing of the sulfuric acid solution with the iron oxides. Typically, the treatment lasts from 1 minute to 4 8 hours. In a specific embodiment of the present: invention, the treatment lasts from 3 minutes to 5 hours, more specifically from 10 minutes to 30 minutes.
The treatment of iron oxides with sulfuric acid solution can be conducted under a pressure from about 50 kPa to about 10000 kPa. Lr one specific embodiment of the present invention, it is conducted under ambient pressure. The treatment can be conducted in any suitable atmosphere. Non-limiting examples of the suitable atmosphere include: air, other oxygen containing gaseous streams, and inert gaseous streams.
After the iron oxides are treated with sulfuric acid solution, they can be separated from the solution by any suitable separation method. Without intending to limit the scope of the invention, the treated iron oxides can be separated out by filtration, centrifugation, etc.
As a preferred embodiment of the present invention, the treated iron oxides, after being separated from the sulfuric acid solution are subsequently heated at an elevated temperature. The heating and/or calcining is typically conducted at a temperature ranging from 1° above the ambient temperature to 14 00 °C for a period of tim«: sufficient to dry or calcine the treated iron oxides completely. Typically, the iron oxides are calcined and/or dried for from 1 minute to 100 hours. This heating step can be a simple drying process, a calcination process, or a staged drying and calcination process. The heating is conducted under a pressure typically from 10 k?a to 1100 kPa. As a non-limiting example, the heating step can be conducted under ambient pressure. The heating step can be conducted under any suitable atmospheres. Non-limiting examples or: the suitable atmospheres for the heating step include air, oxygen containing gaseous streams, inert gaseous streams, and vacuum.
In one specific embodiment of the present invention, the iron oxides are treated with a sulfuric acid solution and the treated iron oxides are separated from the solution without subsequent
heating. The treated iron oxides can optionally be dried in air at ambient temperature and ambient pressure. In another specific embodiment of the present invention, the iron oxides are dried in air at a temperature between 30 °C and 300 °C, preferably between 50 °C and 300 °C, more preferably between 100 °C and 300 °C, for a period of time ranging from 1 minute to 72 hours, preferably from 2 minutes to one hour, more preferably from 10 minutes to 30 minutes. In a preferred embodiment, the treated iron oxides are subsequently calcined for a period of time from 1 minute to 72 hours, preferably from 15 minutes to 10 hours, more preferably from 30 minutes to 2 hours. In another preferred embodiment, the iron oxides are first dried at a temperature between 30 °C and 300 °C, preferably between 120 °C and 200 °C for a period of time ranging from 1 minute to 72 hours, preferably from 2 minutes to one hour, more preferably from 10 minutes to 30 minutes, and then calcined for a period of time from 1 minute to 72 hours, preferably from 15 minutes to 10 hours, more preferably from 30 minutes to 2 hours.
After the iron oxides are dried and optionally calcined, a sample of the treated iron oxides can be analyzed with a suitable analytical method(s) to determine the chloride content. The post-treatment chloride content is then compared with the chloride content measured prior to the treatment.
The; invention will be exemplified by the following illustrative embodiments. Illustrative Embodiments
The following illustrative embodiments describe typical techniques of the present invention for reducing chloride content :n the regenerated iron oxides and the typical techniques for measuring the chloride contents of the iron oxides. The chloride contents were determined using Kevex Model 770 Energy Dispersive X-Ray Fluorescence Instrument. Part A: Regenerated Iron Oxide
The ferric oxide used in the present embodiment was a commercial product of regenerated iron oxide produced from hydrochloric acid waste liquid generated from steel pickling. The
chloride content of this regenerated iron oxide was about 1400 parts per million by weight of the regenerated iron oxide.
600 grams of the regenerated iron oxide were used for each Illustrative Embodiment below. The total amount of the chloride present in the 600 grams of regenerated iron oxxde with 1400 parts per million (ppm) of chloride was estimated to be about 0.84 grams or 0.0237 moles based on mathematical calculation. Part B: Preparation of H2SO4 solution B-l: H2S04 Solution of 1:1 Ratio Relative to Cl
1.3 millilitres of concentrated sulfuric acid with specific gravity of 1.84 g/ml were added to 61.7 millilitres of deionized water to make a solution of about 63 millilitres containing approximately 0.0237 moles of H2SO4, which was equal to the molar amount of the chloride contained in the 600 grams of regenerated iron oxide from Part A above. B-2: H2S04 Solution of 2:1 Ratio Relative to Chloride
2.6 millilitres of concentrated sulfuric acid with specific gravity of 1.84 g/ml were added to 60.4 millilitres of water to make a solution of about 63 millilitres by volume containing approximately 2 X 0.0237 moles of H2SO4 which was twice the molar amount of the chloride present in the 600 grams of the regenerated feme oxide from Part A. Part C: Reduction of Chloride in Ferric Oxide
I. H2S04 TREATMENT FOLLOWED BY DRYING Method 1-1: Treatment with H2S04, 2:l/Dried at 50 °C
600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes. During mulling, 63 millilitres of the H2SO4 solution, prepared from B-2 above, containing a molar amount of H2SO4 in the H2SO4 solution of about twice the amount of choride contained in 600 grams of the regenerated iron oxide, were added gradually to the regenerated iron oxide. The wet iron oxide powdei was filtered through a 2.83 mm (#7 mesh) screen and then dried for 15 nu.nutes at 50 °C under ambient pressure. The chloride content of the dried sample was 1200 parts per million by weight of the total iron oxides.
Method 1-2: Treatment with H2S04, 2:l/Dried at 120 °C
600 grams of the regenerated iron oxide from Part A above were treated with the same H2SO4 solution in the same way as Method I-l above, except that subsequent to the filtration step the treated iron oxide powder was dried at 120 °C at ambient pressure for 15 minuces. The chloride content of the dried sample was 720 ppm. Method 1-3: Treatment with H2S04, l:l/Dried at 170 °C
600 grams of the regenerated iron oxide from Part A were mulled for 15 minutes. During mulling, 63 millilitres of the H2SO4 solution,, prepared from B-l above, containing a molar amount of H2SO,} in the H2SO4 solution about equal to the molar amount of choride contained in 600 grams of the regenerated iron oxide, were added gradually to the regenerated iron oxide. The wet iron oxide powder was filtered through a 2.83 mm (#7 mesh) screen and then dried for 15 minutes at 170 °C under ambient pressure. The chloride content of the dried sample was 550 parts per million by weight of the cotal iron oxides. Method 1-4: Treatment with H2S04, 2:l/Dried at 170 °C
600 grams of the regenerated iron oxide from Part A above were treated with the same H2SO4 solution in the same way as Method 1-2 above, except that subsequent to the filtration step the treated iron oxide powder was dried at 170 °C at ambient pressure. The chloride content of the dried sample was 510 ppm.
The results of study I are shown in Table I below.

TABLE I REGENERATED IRON OXIDE CHLORIDE REDUCTION STUDY I

(Table Removed)
II. H2S04 TREATMENT FOLLOWED BY DRYING AND CALCINING Method C-l:Comparative Embodiment - Calcination without H2S04
600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes without the addition of any H2S04 solution. The mulled iron oxide were then dried for 15 minutes at 170 °C. Thirty grams of the dried oxide were calcined in a static kiln under air having one atmosphere pressure for one hour at 825 °C. The resulted chloride content was 810 ppm. Method C-2: Comparative Embodiment - Treatment with H20/ Calcined
600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes. During mulling, 63 millilitres of deionizea water were gradually added to the regenerated iron oxide. The wet iron oxide powder was filtered through a 2.83 mm (#7 mesh) screen and then dried for 15 minutes at 170 °C. Thirty grams of the dried oxide were calcined in a static kiln under air having one atmosphere

pressure for one hour at 825 °C. The resulting chloride content wa
880 ppm.
Method II-l: Treatment with H2S04, 1:l/Dried/Calcined
Thirty grams of the dried oxide from Method 1-3 above were calcined in a static kiln under air having one atmosphere pressure for one hour at 82:5 °C. The chloride content of the resulting sampl was 510 ppm. Method II-2: Treatment with H2S04, 2:l/Dried/Calcined
Thirty grams of the dried oxide from Method 1-4 above were calcined in a static kiln in air with one atmosphere pressure for one hour at 825 °C. The chloride content of the resulting sample wa 390 ppm.
The results of study II are shown in Table II below.
TABLE II REGENERATED IRON OXIDE CHLORIDE REDUCTION STUDY II

880
'.10
3 90
WITHOUTSUBSEQUENT DRYING/CALCINING
Method C-3: Comparative Embodiment - Treatment with H20
(Table Removed)
600 grams of the regenerated iron oxide from Part A above were mulled for 15 minutes. During mulling, 63 millilitres of the deionized water were gradually added to the regenerated iron oxide The wet iron oxide powder was filtered through a #7 mesh screen. The chloride content was 10,200 ppm. Method IXI-1: Treatment with H2S04, 2:1 Undried/Uncalcined
600 grams of the regenerated iron oxide from Part A were mulled for 15 minutes. During mulling, 63 millilitres of the H2SO4 solution, prepared from B-2 above, containing a molar amount of H2SO4 in the H2SO4 solution of about twice the molar amount of choride contained in 600 grams of the regenerated iron oxide, were added gradually to the regenerated iron oxide. The wet iron oxide powder was filtered through a 2.83 mm (#7 mesh) screen. The chloride content of the dried sample was 3,200 parts per million by weight of the total iron oxides.
The results of study III are shown in Table III below.
TABLE III REGENERATED IRON OXIDE CHLORIDE REDUCTION STUDY III

(Table Removed)

WE CLAIM:-
1. A process for removing chloride from a chloride-containing iron
oxide to produce iron oxide with a reduced chloride content, which
process comprises the steps of:
a) mixing the chloride-containing iron oxide with a solution in a conventional manner for a period of time sufficient to form a mixture, the said solution comprising sulphuric acid (H2SO4); and
b) separating the iron oxide from the mixture formed in step (a) and then optionally heating at a temperature from 1°C above the ambient temperature to 1400°C for a period of time from 1 minute to 100 hours to obtain the iron oxide having a reduced chloride content.

2. The process as claimed in claim 1, wherein the solution used in step (a) comprises a molar amount of H2SO4 of from 1.0 to 5.0 times the molar amount of chloride in the chloride-containing iron oxide.
3. The process as claimed in claim 1, wherein the solution used in step (a) comprises a molar amount of H2SO4 of from 1.8 to 2.5 times the molar amount of chloride in the chloride-containing iron oxide.
4. The process as claimed in claim 2, wherein in step (a) the iron oxide is mixed with said solution for a period of time which is in the range of from 1 minute to 48 hours.
5. The process as claimed in claim 1, wherein the iron oxide separated from step (t) is heated at a temperature in the range of
from 50°C to 300°C for a period of time in the range of form 2 minutes to one hour.
6. The process as claimed in claim 1, wherein the iron oxide separated from step (b) is first heated at a temperature from 50°C to 300°C for a period of time in the range of from 1 minute to 72 hours, and the iron oxide is thereafter heated at a temperature from 400°C to 1400°C and at a pressure of from 10 to 1100 kpa for a period of time in the range of form 1 minute to 72 hours.
7. The process as claimed in any one of claims 1 to 6, wherein the mixing in step (a) is conducted in an oxygen -containing gaseous stream.
8. The process as claimed in any one of claims 1 to 7, wherein the heating after step (b) is conducted in an oxygen-containing gaseous stream.
9. A process as claimed in any one of claims 1 to 8, wherein the chloride-containing iron oxide is regenerated iron oxide produced from a hydrochloric acid waste liquid generated from steel pickling, and comprises from 800 to 5000 ppm by weight of chloride.
10. A process for removing chloride from a chloride-containing iron oxide to produce iron oxide with a reduced chloride content substantially as herein described and with reference to the foregoing examples.

Documents:

327-del-1995-abstract.pdf

327-del-1995-claims.pdf

327-del-1995-correspondence-others.pdf

327-del-1995-correspondence-po.pdf

327-del-1995-description (complete).pdf

327-del-1995-form-1.pdf

327-del-1995-form-13.pdf

327-del-1995-form-2.pdf

327-del-1995-form-4.pdf

327-del-1995-form-9.pdf

327-del-1995-gpa.pdf

327-del-1995-petition-others.pdf

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Patent Number

190726

Indian Patent Application Number

327/DEL/1995

PG Journal Number

33/2003

Publication Date

16-Aug-2003

Grant Date

15-Mar-2004

Date of Filing

28-Feb-1995

Name of Patentee

SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.

Applicant Address

CAREL VAN BYLANDTLAAN 30, 2596 HR,THE HAGUE,THE NETHERLANDS.

Inventors:

#	Inventor's Name	Inventor's Address
1	DAVID MORRIS HAMILTON JR.	15906 SIERRA GRANDE DRIVE,HOUSTON,TEXAS 77083-2925 U.S.A.

PCT International Classification Number

C21C 1/00

PCT International Application Number

N/A

PCT International Filing date

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1			NA