IP Library Granted Patent US 7,407,381
Granted Patent B2
US 7,407,381 · App. 10/970,686 · Granted Aug 5, 2008

Combustion apparatus and methods for making and using same

Assignee: PAC, LP
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,407,381
App. No.
10/970,686
Granted
Aug 5, 2008
Kind
B2
Abstract

A combustion apparatus is disclosed that improves oxidation efficiency without increasing either combustion apparatus size or residence time, where the apparatus includes a combustion zone having a static mixing zone along a length of the combustion zone.

Claims (45)

1. An analytical instrument apparatus comprising:

a sample supply system,

an oxidizing supply system,

a combustion or furnace apparatus comprising:

an inlet,

an outlet,

a combustion zone including

a mixing zone comprising a static mixer disposed along a length of the combustion zone downstream of the inlet, and

a heater, and

a detector/analyzer unit,

where the supply systems are adapted to supply a sample and an oxidizing agent to the inlet of the combustion apparatus, the heater is adapted to maintain the combustion zone including the mixing zone at an elevated temperature sufficient to substantially completely oxidize the sample into oxides, the static mixer is exposed to combustion temperatures and is adapted to reduce channeling of portions of an oxidizing mixture as it traverses the combustion zone, and the detector/analyzer is adapted to determine a concentration of at least one oxide and relate the oxide concentration back to a concentration of an element in the sample.

2. The apparatus of claim 1 , wherein the elevated temperature above about 300° C.

3. The apparatus of claim 1 , wherein the elevated temperature between about 300° C. and about 2000° C.

4. The apparatus of claim 1 , wherein the elevated temperature between about 600° C. and about 1500° C.

5. The apparatus of claim 1 , wherein the elevated temperature between about 800° C. and about 1300° C.

6. The apparatus of claim 1 , wherein the combustion apparatus further comprises a nebulizer disposed between the inlet and the combustion zone.

7. The apparatus of claim 1 , wherein the sample supply system is selected from the group consisting of an auto-sampler, a septum for direct injection, a sampling loop for continuous sampling, an analytical separation system and mixture or combinations thereof.

8. The apparatus of claim 7 , wherein the analytical separation system is selected from the group consisting of a GC, an LC, an MPLC, an HPLC, an LPLC, and mixtures or combinations thereof.

9. The apparatus of claim 1 , wherein the detector/analyzer is selected from the group consisting of IR spectrometers, FTIR spectrometers, MS spectrometers, UV spectrometers, UV fluorescence spectrometers, chemiluminescence spectrometers, ICR spectrometers, and mixtures or combinations thereof.

10. The apparatus of claim 1 , wherein the detector/analyzer is selected from the group consisting of UV fluorescence spectrometers, chemiluminescence spectrometers, and mixtures or combinations thereof.

11. The apparatus of claim 1 , wherein the combustion zone includes a plurality of mixing zones, where each mixing zone comprises a static mixer and where all of the static mixer are disposed along a length of the combustion zone downstream of the inlet, are exposed to combustion temperatures and are adapted to reduce channeling of portions of an oxidizing mixture as it traverses the combustion zone.

12. A method for oxidizing a combustible material comprising the steps of:

feeding the combustible material and an oxidizing agent to a combustion apparatus comprising an inlet, an outlet, a combustion zone including a mixing zone comprising a static mixer disposed along a length of the combustion zone downstream of the inlet, and a heater for heating the combustion zone, and

heating the combustion zone including the mixing zone to a temperature sufficient to covert all or substantially all oxidizable components in the combustible material into their corresponding oxides,

where the static mixer is exposed to combustion temperatures and is adapted to reduce channeling of portions of an oxidizing mixture as it traverses the combustion zone and where the mixing zone increases an efficiency of combustion of the combustion zone.

13. The method of claim 12 , wherein the temperature is above about 300° C.

14. The method of claim 12 , wherein the temperature is between about 300° C. and about 2000° C.

15. The method of claim 12 , wherein the temperature is between about 600° C. and about 1500° C.

16. The method of claim 12 , wherein the temperature is between about 800° C. and about 1300° C.

17. The method of claim 12 , wherein the combustion apparatus further comprises a nebulizer disposed between the inlet and the combustion zone.

18. The method of claim 17 , wherein the combustion zone includes a plurality of mixing zones, where each mixing zone comprises a static mixer and where all of the static mixer are disposed along a length of the combustion zone downstream of the inlet, are exposed to combustion temperatures and are adapted to reduce channeling of portions of an oxidizing mixture as it traverses the combustion zone.

19. A method for analyzing a sample comprising the steps of:

feeding the sample and an oxidizing agent to a combustion apparatus comprising an inlet, an outlet, a combustion zone including a mixing zone disposed along a length of the combustion zone downstream of the inlet, and a heater for heating the combustion zone,

heating the combustion zone including the mixing zone to a temperature sufficient to covert all or substantially all oxidizable components in the combustible material into their corresponding oxides, and

forwarding the oxides to an detector/analyzer, and

detecting a concentration of at least on oxide,

where the static mixer is exposed to combustion temperatures and is adapted to reduce channeling of portions of an oxidizing mixture as it traverses the combustion zone and where the mixing zone increases an efficiency of combustion of the combustion zone and where the detector/analyzer relates the oxide concentration back to a concentration of an element in the sample.

20. The method of claim 19 , wherein the temperature above about 300° C.

21. The method of claim 19 , wherein the temperature between about 300° C. and about 2000° C.

22. The method of claim 19 , wherein the temperature between about 600° C. and about 1500° C.

23. The method of claim 19 , wherein the temperature between about 800° C. and about 1300° C.

24. The method of claim 19 , wherein the combustion apparatus further comprises a nebulizer disposed between the inlet and the combustion zone.

25. The method of claim 19 , wherein the detector/analyzer is selected from the group consisting of IR spectrometers, FTIR spectrometers, MS spectrometers, UV spectrometers, UV fluorescence spectrometers, chemiluminescence spectrometers, ICR spectrometers, and mixtures or combinations thereof.

26. The method of claim 19 , wherein the detector/analyzer is selected from the group consisting of UV fluorescence spectrometers, chemiluminescence spectrometers, and mixtures or combinations thereof.

27. The method of claim 19 , wherein the combustion zone includes a plurality of mixing zones, where each mixing zone comprises a static mixer and where all of the static mixer are disposed along a length of the combustion zone downstream of the inlet, are exposed to combustion temperatures and are adapted to reduce channeling of portions of an oxidizing mixture as it traverses the combustion zone.

Assignments (12)
RELEASE OF SECURITY INTERESTS IN PATENTS Recorded Jul 21, 2023
From: JPMORGAN CHASE BANK, N.A.
To: COSA XENTAUR CORPORATION
Reel/Frame 064356/0539 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 20, 2023
From: ATOM INSTRUMENT LLC; OLSTOWSKI, FRANEK
To: COSA XENTAUR CORPORATION
Reel/Frame 064332/0683 →
SECURITY INTEREST Recorded Jul 19, 2023
From: COSA XENTAUR CORPORATION; TIGER OPTICS, LLC
To: ANTARES CAPITAL LP, AS AGENT
Reel/Frame 064342/0908 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 17, 2023
From: ATOM INSTRUMENT LLC
To: COSA XENTAUR CORPORATION
Reel/Frame 064289/0964 →
RELEASE OF SECURITY INTEREST RECORDED AT REEL/FRAME 051221/0477 Recorded Nov 2, 2020
From: CRYSTAL FINANCIAL LLC
To: COSA XENTAUR CORPORATION; LAR PROCESS ANALYSERS AG; TIGER OPTICS, LLC
Reel/Frame 054270/0822 →
SECURITY INTEREST Recorded Dec 9, 2019
From: COSA XENTAUR CORPORATION
To: CRYSTAL FINANCIAL LLC
Reel/Frame 051221/0477 →
SECURITY INTEREST Recorded Dec 5, 2019
From: COSA XENTAUR CORPORATION
To: JPMORGAN CHASE BANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 051190/0230 →
CONVERSION Recorded Mar 10, 2015
From: ATOM INSTRUMENT CORPORATION
To: ATOM INSTRUMENT, LLC
Reel/Frame 035171/0590 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 4, 2013
From: OLSTOWSKI, FRANEK
To: ATOM INSTRUMENT CORPORATION
Reel/Frame 031716/0699 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 21, 2013
From: PETROLEUM ANALYZER COMAPNY, LP
To: ATOM INSTRUMENT CORPORATION; OLSTOWSKI, FRANEK
Reel/Frame 031651/0560 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 17, 2009
From: OLSTOWSKI, FRANEK
To: ATOM INSTRUMENT CORPORATION
Reel/Frame 023107/0708 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 22, 2006
From: ROPINTASSCO HOLDINGS, L.P.; ROPINTASSCO 7, LLC
To: PETROLEUM ANALYZER COMPANY L.P.
Reel/Frame 017344/0493 →
Continuity (1)
Related Publication 20050153253A1 · Jul 14, 2005