Title of Invention

A PROCESS FOR PRODUCING POROUS SULPHA SPONGE IRON AND A METHOD OF DESULPHURISING NATURAL GAS

Abstract This invention relates to a process for producing sulpha sponge iron having a composition as described in the specification. Haematite is magnetically separated and dissolved in hydrochloric acid. This solution is concentrated and treated with ammonium hydroxide. The precipitate obtained is deposited on haematite.
Full Text A NOVEL POROUS SULPHA SPONGE IRON COMPOUND, A
PROCESS FOR PREPARING THE SAME AND A METHOD
FOR DESULPHURIZING NATURAL GAS THEREWITH
This inventioii relates to a novel porous sponge iron compound, a process for preparing &e same and a method for desulphurising nabiral gas therewith.
Background Art
Natural gas which is a mixture of low molecular weight hydrocarbons and small amounts of higher hydrocarbons is contaminated with sulphur and nitrogen compounds as well as with oxides of carbon. Sulphur contaminants are hydrogen sulphide, carbonyl sulphide and mercaptans.
Process gas and fuel are produced by desulphurising sulphur containing natural gas streams. Harmfiil sulphur contaminants are removed by direct reduction of iron ore.
Conventional desulphurization methods include adsorption of the contaminants by metalUc compounds, ceramic and metal oxides pellets, finely divided iron, and porous iron oxide. Direct reduction of iron ore also results in spongy iron having sulphur contaminant absorbing capability.

Molecular sieves and compounds such as Zinc oxide are generally used as decontaminants for hydrocarbon fiiel gas. Cracking of components are to be avoided during such desulphurisation step.
Porous sfponge iron derived from magnetite has also been used as a desulphurizing agent Though found effective in many desulphurisation reactions, this spongy iron does not have very high adsorptive capacity.
An object of this invention is to develop a highly adsorbant porous sulpha sponge iron compound whose adsoibent capacity may be renewed or controlled to the desired level by repeated processing.
Yet another object of this invention is for a method of desulphurising natural gas by adsorbing sulphur containing contaminants in the above porous sulpha sponge iron compound. Desulphurization process according to this invention results in substantially freeing natural gas from such contaminants. Since this process is not carried out at high temperatures, cracking of natural gas is also avoided.

Disclosure of the invention:
Porous sulpha sponge iron compound of this invention is derived from haematite having the following composition:
SiOz 3.28%
AI2O3 3.74%
FezOa 92.40%
CaO 0.42%
MgO 0.19%
P2O5 0.08%
K2O 0.06%
NazO nil
SO3 0.04%
CI 0.0001%
MnzOs 0.14%
Naturally occuring haematite is magnetically separated and the separated part is dissolved in concentrated hydrochloric acid. The acidic solution is filtered and concentrated. Acid chloride solution of the haematite thus obtained is reacted with concentrated ammonium hydroxide in an

alcoholic medium. The precipitated compound is found to have a high potential to react with hydrogen sulphide. This product is deposited on a base of haematite and powdered to 300 mesh size and is now ready for use in scavenging insitu hydrogen sulphide during oil well drilling. This sulpha sponge shows an adsorbent capacity exceeding 2500 ppm.
In a specific embodimeni, Ae base haematite of 500 gm is powdered to about 300 mesh and is moistened with absolute alcohol. 30 ml of &e acid solution obtained by dissolving magnetically separated haematite in concentrated hydrochloric acid is added to this with thorough mixing to obtain a mixture of flowing consistency. Ammonium hydroxide is added to this mixture in different stages under continuous stirring. Addition of anmionium hydroxide is stopped v^en the mass thickens and appears to have a semisolid consistency and the mass is then neutralized by the addition of a few drops of glacial acetic acid. The resultant mass is dried preferably under infira red rays, crushed and passed through 300 mesh sieve.
Testing of the substance produced above is carried out with liberated hydrogen sulphide obtained from solution of sodium sulphide or with an aqueous saturated solution of hydrogen sulphide. In case the performance is below the desired level of 2500 ppm of H2S with 1 gm of the porous sulpha sponge, the step of redeposition with the acid chloride solution of haematite is repeated till the desired adsorbancy level is achieved. This product can effectively be used to scavenge hydrogen sulphide produced in situ during oil well drilling.

Sour natural gas containing sulphur contaminants are desulphurated by passing the same through a bed containing porous sulpha sponge iron compound as £^)6cifi6d above. The reaction may be carried out at known desulphurising temperature in the range of 200 to 400°C. The porous sulpha sponge iron compound adsorbs tiie contaminants and the efQuent gas is substantially free of hydrogen sulphide. The improved capacity for adsoibing sulphur containing compounds by the sulpha ^>onge from natural gas makes the desulphurisation process highly effective. Care&I control of the reaction temperature depending upon the constituents of the natural gas will help in avoiding cracking. This sulpha sponge iron compound of our invention may be used for hydrogen sulphide scavenging in any field including sewage treatment and the like environmental application.
Thus, this invention relates to a novel porous, sulpha sponge iron
compound derived from haematite having the following composition:
SiOz 3.28%
AI2O3 3.74%
FezOa 92.40%
CaO 0.42%
MgO 0.19%
P2Q5 0.08%
KajO 0.00%
SO3 0.04%
CI 0.0001%
MnaOa 0.14%

I
and having trace elements such as Au, Pt and Ag therein, by dissolving said haematite in concentrated hydrochloric acid, and treating said acidic solution with alcoholic ammonia and glacial acetic acid to obtain said sulpha sponge iron compound, having a plurality of Fe^/Fe^ cores forming interstatially stabilized clusters.
This invention also relates to a process for producing porous sulpha sponge iron compound from haematite by magnetically separating haematite, dissolving the same in hydrochloric acid, concentrating and treating the said acidic solution with ammonium hydroxide in an alcoholic medium, depositing the precipitate obtained on haematite drying and powdering the same.
An alternate route for making the porous sulpha sponge is by adding a hydrochloric acid solution of magnetically separated haematite to naturally occuring haematite base, ammoniating the same in an alcoholic medium till a semisolid is formed, neutrahsing the same imder an acid and subsequently drying and powdering.
Method of desulphurization may be effected at the drilling site by adding the novel sulpha sponge iron compound or afterwards by allowing the gas to pass over a bed of the above referenced porous sulpha sponge iron compound.
This invention therefore includes a method for desulphurising natural gas comprising the steps contacting the natural gas with the porous sulphur sponge iron.


1. A novel porous, sulpha sponge iron compound derived from haematite having the following composition:
Si02 3^%
AI2O3 3.74%
FeaOs 92.40%
CaO 0.42%
MgO 0.19%
P2O5 0.08%
NazO 0.00%
SO3 0.04%
CI 0.0001%
MnzQs 0.14%
and having trace elements such as Au, Pt and Ag therein, by dissolving said haematite in concentrated hydrochloric acid, and treating said acidic solution with alcoholic ammonia and glacial acetic acid to obtain said sulpha sponge iron compound, having a plurality of Fe^/Fe^ cores forming interstatially stabilized clusters.

A process for producing porous sulpha sponge iron as claimed in claim 1 which comprises the steps of magnetically separating haematite, dissolving the same in hydrochloric acid, concentrating and treating said acidic solution with ammonium hydroxide, depositing the precipitation obtained on haematite, drying and powdering the same.
, The process as claimed in claim 2, wherein ammonium hydroxide is added to the acidic solution in an alcoholic medium.
. The process as claimed in claims 2 and 3 wherein the precipitate is separated when a semisohd mass is formed and then deposited on haematite and powdered to 300 mesh.
, A process for preparing the porous sulpha sponge iron which comprises the steps of adding an acidic solution of magnetically separated haematite to haematite base, ammoniating the same till a semisolid mass is formed, neutralizing with an acid and subsequently drying and powdering.
, The process as claimed in claim 6, wh^ein said ammoniating step is carried out in an alcoholic medium, said neutralization is effected by adding acetic acid to said semisolid mass, said drying is effected under infra red rays and the mass then powdered to 300 mesh.

A method of desulphurising natural gas which comprises the step of adsorbing sulphur containing contaminants in the porous sulpha ^K>nge iron compound as claimed in claim 1 at the drilling site or by passing natural gas through a bed of said porous sulpha sponge iron compound.
Use of novel sulpha sponge iron compound as claimed in claim 1 for scavenging sulphur containing contaminants.

9. A novel porous, sulpha sponge iron compound, substantially as hereinabove described and exemplified.


Documents:

2058-chenp-2003-abstract.pdf

2058-chenp-2003-claims duplicate.pdf

2058-chenp-2003-claims original.pdf

2058-chenp-2003-correspondnece-others.pdf

2058-chenp-2003-correspondnece-po.pdf

2058-chenp-2003-description(complete) duplicate.pdf

2058-chenp-2003-description(complete) original.pdf

2058-chenp-2003-form 1.pdf

2058-chenp-2003-form 19.pdf

2058-chenp-2003-form 3.pdf

2058-chenp-2003-form 5.pdf

2058-chenp-2003-pct.pdf


Patent Number 200610
Indian Patent Application Number 2058/CHENP/2003
PG Journal Number 30/2009
Publication Date 24-Jul-2009
Grant Date 26-May-2006
Date of Filing 24-Dec-2003
Name of Patentee M/S. GOOD EARTH CHEMICALS PVT. LTD.
Applicant Address Co-Operative Colony Hospet 583 203 Karnataka
Inventors:
# Inventor's Name Inventor's Address
1 THERANI, Nadathur, Venkata, Raghavan LAKSHMI VISHNU NO 2 SRI RAM NAGAR 1 CROSS TIRUNINDRAVUR P O CHENNAI
PCT International Classification Number B01J20/06
PCT International Application Number PCT/IN2001/000108
PCT International Filing date 2001-06-08
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 NA