IP Library Granted Patent US 9,297,765
Granted Patent B2
US 9,297,765 · App. 13/830,514 · Granted Mar 29, 2016

Gas decomposition reactor feedback control using Raman spectrometry

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Quick Facts
Patent No.
US 9,297,765
App. No.
13/830,514
Granted
Mar 29, 2016
Kind
B2
Abstract

A gas decomposition reactor for the decomposition of a gas into a mixture of solid and gaseous by-products is disclosed. The gas decomposition reactor includes a reactor vessel, a Raman spectrometer, and a processor. The reactor vessel has an inlet for receiving inlet gas and an exhaust outlet for releasing exhaust gas. The Raman spectrometer is connected with the exhaust outlet for determining a chemical conversion within the reactor chamber and generating a corresponding signal. The processor is connected with the Raman spectrometer to receive the signal from the Raman spectrometer. The processor is capable of comparing the signal with a set of values and calculating differences between the signal and the set of values. The processor is connected with the inlet to regulate a flow of the inlet gas.

Claims (33)

1. A gas decomposition reactor for the decomposition of a gas into a mixture of solid and gaseous by-products, the gas decomposition reactor comprising:

a reactor vessel having an inlet for receiving an inlet gas and an exhaust outlet for releasing an exhaust gas;

a Raman spectrometer connected with the exhaust outlet for determining a chemical composition of the exhaust gas and generating a corresponding exhaust signal, and connected with the inlet for determining a chemical composition of the inlet gas and generating a corresponding inlet signal;

a processor connected with the Raman spectrometer to receive the inlet signal and the exhaust signal from the Raman spectrometer, the processor configured to compare the chemical composition of the inlet gas and the chemical composition of the outlet gas and determine a conversion efficiency of a reaction in the reactor vessel based at least in part on the inlet signal and the exhaust signal, the processor is connected with the inlet to regulate a flow of the inlet gas based at least in part on the determined conversion efficiency, and

wherein the Raman spectrometer is configured to continuously determine the composition of the exhaust gas and the chemical composition of the inlet gas and to detect at least two components of the exhaust gas simultaneously, and the processor is configured to ratiometrically determine the conversion efficiency of the reaction.

2. The gas decomposition reactor of claim 1 , further comprising a feeder tube for providing particles to the reactor vessel.

3. The gas decomposition reactor of claim 1 , wherein the Raman spectrometer is connected with the inlet and the exhaust outlet through Raman probes for determining the chemical composition of the inlet gas and the exhaust gas.

4. The gas decomposition reactor of claim 3 , further comprising a pressure control system connected with the processor and the inlet gas for regulating the flow of the inlet gas through the inlet.

5. The gas decomposition reactor of claim 4 , wherein the processor is capable of regulating the flow of the inlet gas through the inlet by adjusting the pressure control system.

6. The gas decomposition reactor of claim 1 , wherein the inlet gas is a mixture of a first gas and a second gas.

7. The gas decomposition reactor of claim 6 , further comprising a pressure control system connected with the processor and one of the first gas and the second gas for regulating a flow of one of the first gas and the second gas into the inlet.

8. The gas decomposition reactor of claim 7 , wherein the processor is capable of regulating the flow of the one of the first gas and the second gas into the inlet by adjusting the pressure control system.

9. The gas decomposition reactor of claim 1 , wherein the gas decomposition reactor is a fluidized bed reactor.

10. The gas decomposition reactor of claim 9 , wherein the inlet gas is a mixture of a reaction gas and a fluidizing gas.

11. The gas decomposition reactor of claim 10 , further comprising a pressure control system separately connected with the processor and a source of the reaction gas and a source of the fluidizing gas.

12. The gas decomposition reactor of claim 11 , wherein the processor is capable of regulating the flow of both the reaction gas and the fluidizing gas into the inlet by adjusting the pressure control system.

13. The gas decomposition reactor of claim 10 , wherein the reaction gas is silane and the fluidizing gas is hydrogen.

14. A fluidized bed reactor for the decomposition of a gas into a mixture of solid and gaseous by-products, the fluidized bed reactor comprising:

a reactor vessel having an inlet for receiving an inlet gas and an exhaust outlet for releasing an exhaust gas;

a Raman spectrometer connected with the exhaust outlet for determining a chemical composition of the exhaust gas and generating a corresponding exhaust signal, and connected with the inlet for determining a chemical composition of the inlet gas and generating a corresponding inlet signal;

a processor connected with the Raman spectrometer to receive the inlet signal and the exhaust signal from the Raman spectrometer, the processor configured to compare the chemical composition of the inlet gas and the chemical composition of the outlet gas and determine a conversion efficiency of a reaction in the reactor vessel based at least in part on the inlet signal and the exhaust signal; and

a pressure control system connected with the processor and the inlet gas for adjusting a flow of the inlet gas through the inlet based at least in part on the determined conversion efficiency, and

wherein the Raman spectrometer is configured to continuously determine the composition of the exhaust gas and the chemical composition of the inlet gas and to detect at least two components of the exhaust gas simultaneously, and the processor is configured to ratiometrically determine the conversion efficiency of the reaction.

15. The fluidized bed reactor of claim 14 , wherein the Raman spectrometer is connected with the exhaust outlet and the inlet through Raman probes.

16. The fluidized bed reactor of claim 15 , wherein the inlet includes a fluidizing gas inlet for providing a fluidizing gas to the reactor vessel and a reaction gas inlet for providing a reaction gas to the reactor vessel.

17. The fluidized bed reactor of claim 16 , wherein the processor is configured to regulate the flow of both the fluidizing gas and the reactor gas by adjusting the pressure control system.

18. The gas decomposition reactor of claim 1 , wherein the processor is configured to couple an intensity of the inlet signal and an intensity of the exhaust signal with a mass balance for the reaction in the reactor vessel to determine the conversion efficiency of the reaction.

19. The fluidized bed reactor of claim 14 , wherein the processor is configured to couple an intensity of the inlet signal and an intensity of the exhaust signal with a mass balance for the reaction in the reactor vessel to determine the conversion efficiency of the reaction.

20. A gas decomposition reactor for the decomposition of a gas into a mixture of solid and gaseous by-products, the gas decomposition reactor comprising:

a reactor vessel having an inlet for receiving an inlet gas and an exhaust outlet for releasing an exhaust gas;

a Raman spectrometer connected with the exhaust outlet for determining a chemical composition of the exhaust gas and generating a corresponding exhaust signal, and connected with the inlet for determining a chemical composition of the inlet gas and generating a corresponding inlet signal; and

a processor connected with the Raman spectrometer to receive the inlet signal and the exhaust signal from the Raman spectrometer, the processor configured to compare the chemical composition of the inlet gas and the chemical composition of the outlet gas and determine a conversion efficiency of a reaction in the reactor vessel based at least in part on the inlet signal and the exhaust signal, the processor is connected with the inlet to regulate a flow of the inlet gas based at least in part on the determined conversion efficiency, and

wherein the processor is configured to couple an intensity of the inlet signal and an intensity of the exhaust signal with a mass balance for the reaction in the reactor vessel to determine the conversion efficiency of the reaction.

Assignments (7)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 27, 2017
From: SUNEDISON, INC.; SUNEDISON PRODUCTS SINGAPORE PTE. LTD.; MEMC PASADENA, INC.; SOLAICX
To: CORNER STAR LIMITED
Reel/Frame 042351/0659 →
PATENT SECURITY AGREEMENT Recorded Apr 28, 2016
From: SUNEDISON, INC.
To: DEUTSCHE BANK AG NEW YORK BRANCH, AS ADMINISTRATIVE AGENT
Reel/Frame 038557/0472 →
RELEASE OF SECURITY INTEREST Recorded Jan 13, 2016
From: GOLDMAN SACHS BANK USA, AS ADMINISTRATIVE AGENT
To: SUNEDISON, INC.; SUN EDISON LLC; SOLAICX; NVT, LLC
Reel/Frame 037508/0884 →
SECURITY INTEREST Recorded Jan 13, 2016
From: SUNEDISON, INC.; SUN EDISON LLC; SOLAICX; NVT, LLC
To: WILMINGTON TRUST, NATIONAL ASSOCIATION, SOLELY IN ITS CAPACITY AS COLLATERAL TRUSTEE
Reel/Frame 037508/0606 →
SECURITY INTEREST Recorded Jan 12, 2016
From: SUNEDISON, INC.; SUN EDISON LLC; SOLAICX
To: WELLS FARGO BANK, NATIONAL ASSOCIATION, AS ADMINISTRATIVE AGENT
Reel/Frame 037485/0343 →
SECURITY INTEREST Recorded Aug 11, 2015
From: SUNEDISON, INC.; SUN EDISON LLC; SOLAICX; NVT, LLC
To: GOLDMAN SACHS BANK USA, AS ADMINISTRATIVE AGENT
Reel/Frame 036329/0470 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 20, 2015
From: GRABBE, ALEXIS; PAYRA, PRAMATHA
To: SUNEDISON, INC
Reel/Frame 034990/0835 →