IP Library Granted Patent US 8,535,634
Granted Patent B2
US 8,535,634 · App. 12/151,239 · Granted Sep 17, 2013

Iron nitride powders for use in magnetic, electromagnetic, and microelectronic devices

Inventors: Suryanarayan G. Sankar (Pittsburgh, PA); Satoru Simizu (Pittsburgh, PA); Brian J. Zande (Pittsburgh, PA); Richard T. Obermyer (Delmont, PA)
Assignee: Advanced Materials Corporation
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Quick Facts
Patent No.
US 8,535,634
App. No.
12/151,239
Granted
Sep 17, 2013
Kind
B2
Abstract

A method of making iron nitride powder is provided. The method comprises the steps of: a) providing an iron-based starting material; b) reducing the starting material by heating the starting material in a fluidized bed reactor in the presence of a reducing agent; c) nitriding the material obtained from step (b) by contacting the material with a nitrogen source. Also provided is the iron nitride powder made by the above method.

Claims (29)

1. A method of making iron nitride powder, the method comprising the steps in the following sequential order:

a) providing FeOOH starting bulk material in a reactor;

b) separating the FeOOH starting bulk material into a plurality of individual particles such that an individual particle of the plurality of particles is suspended in the reactor by flowing a reducing agent in the reactor, wherein an entire surface of the individual particle is exposed to gas flowing in the reactor;

c) maintaining an elevated temperature in the reactor of between about 350° C. and 500° C. in the presence of the reducing agent to reduce the individual particle to form a reduced individual particle;

d) cooling down the elevated temperature in the reactor to a constant temperature of between 110° C. and 180° C. in the presence of the reducing agent;

e) stopping flow of the reducing agent after reaching the constant temperature;

f) flowing a nitrogenation gas with an ammonia gas and a nitrogen gas to suspend the reduced individual particle in a fluidized environment and maintaining the constant temperature in the fluidized environment from about 1 hour up to about 48 hours to nitride the reduced individual particle to form an iron nitride particle of the iron nitride powder;

g) cooling down the constant temperature in the reactor between room temperature and 50° C. to define a passivating temperature;

h) stopping flow of ammonia gas after reaching the passivating temperature; and

i) exposing an entire surface of the iron nitride particle of the iron nitride powder to an air and nitrogen gas mixture to passivate the entire surface of the iron nitride particle to prevent oxidation,

whereby the iron nitride powder having (i) a saturation magnetization of between 230 and 250 emu/g as determined by plotting a magnetization curve as a function of an inverse of magnetizing field and extrapolating a linear part of the magnetization curve from 10 kOe to 16 kOe toward an inverse of an infinite magnetizing field, (ii) 4 to 90 wt % Fe16N2, (iii) 0 wt % Fe4N, and (iv) remaining balance of the iron nitride powder being body centered cubic (bcc) iron.

2. The method of claim 1 , wherein the reducing agent is selected from the group consisting of hydrogen and carbon monoxide gas.

3. The method of claim 1 , wherein the FeOOH starting material further comprises cobalt (0-20 atomic %) and/or titanium (0-20 atomic %).

4. The method of claim 1 , wherein the step (b) further comprises the step of monitoring the reducing agent flow rate at an inlet and an outlet of the reactor to assure reduction of the FeOOH starting material is completed.

5. The method of claim 1 , wherein the step (c) is carried out at a pressure greater than 1 atmosphere to covert a portion of the FeOOH starting material to body centered cubic (bcc) iron.

6. A method of making iron nitride powder, the method comprising the steps in the following sequential order:

a) providing Fe2O3 starting bulk material in a reactor;

b) separating the Fe2O3 starting bulk material into a plurality of individual particles such that an individual particle of the plurality of particles is suspended in the reactor by flowing a reducing agent in the reactor, wherein an entire surface of the individual particle is exposed to gas flowing in the reactor;

c) maintaining an elevated temperature in the reactor between 340 to 440° C. in the presence of the reducing agent to reduce the individual particle to form a reduced individual particle;

d) cooling down the elevated temperature in the reactor to a constant temperature of between 120° C. to 160° C. in the presence of the reducing agent;

e) stopping flow of the reducing agent after reaching the constant temperature;

f) flowing a nitrogenation gas with an ammonia gas and a nitrogen gas to suspend the reduced individual particle in a fluidized environment and maintaining the constant temperature in the fluidized environment for a period of 18 to 66 hours to nitride the reduced individual particle to form an iron nitride particle of the iron nitride powder;

g) cooling down the constant temperature in the reactor between room temperature and 50° C. to define a passivating temperature;

h) stopping flow of ammonia gas after reaching the passivating temperature; and

i) exposing an entire surface of the iron nitride particle of the iron nitride powder to an air and nitrogen gas mixture to passivate the entire surface of the iron nitride particle to prevent oxidation,

whereby the iron nitride powder having (i) a saturation magnetization of between 230 and 250 emu/g as determined by plotting a magnetization curve as a function of an inverse of magnetizing field and extrapolating a linear part of the magnetization curve from 10 kOe to 16 kOe toward an inverse of an infinite magnetizing field, (ii) 4 to 90 wt % Fe16N2, (iii) 0 wt % Fe4N, and (iv) remaining balance of the iron nitride powder being body centered cubic (bcc) iron.

7. The method of claim 6 wherein the reducing agent is selected from the group consisting of hydrogen and carbon monoxide gas.

8. The method of claim 6 , wherein the step (b) further comprises the step of monitoring the reducing agent flow rate at an inlet and an outlet of the reactor to assure reduction of the Fe 2 O 3 starting material is completed.

9. The method of claim 6 , wherein the step (c) is carried out at a pressure greater than 1 atmosphere to covert a portion of the Fe 2 O 3 starting material to body centered cubic (bcc) iron.

Assignments (5)
SECURITY INTEREST Recorded Nov 17, 2025
From: NIRON MAGNETICS, INC.
To: SHAKOPEE MDEWAKANTON SIOUX COMMUNITY
Reel/Frame 072920/0156 →
CONFIRMATORY LICENSE Recorded Apr 27, 2022
From: ADVANCED MATERIALS CORPORATION
To: THE GOVERNMENT OF THE UNITED STATES OF AMERICA AS REPRESENTED BY THE SECRETARY OF THE NAVY
Reel/Frame 059805/0667 →
CONFIRMATORY LICENSE Recorded Feb 3, 2021
From: ADVANCED MATERIALS CORPORATION
To: THE GOVERNMENT OF THE UNITED STATES OF AMERICA AS REPRESENTED BY THE SECRETARY OF THE NAVY
Reel/Frame 055209/0113 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 28, 2020
From: ADVANCED MATERIALS CORPORATION
To: NIRON MAGNETICS, INC.
Reel/Frame 053330/0265 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 21, 2008
From: SANKAR, SURYANARAYAN G.; SIMIZU, SATORU; ZANDE, BRIAN J.; OBERMYER, RICHARD T.
To: ADVANCED MATERIALS CORPORATION
Reel/Frame 021287/0594 →
Continuity (2)
Provisional Application 60927643 · May 4, 2007
Related Publication 20110059005A1 · Mar 10, 2011