Catalytic Alloy Hydrogen Sensor Apparatus and Process

• US 20090238752A1
• Filed: 06/05/2009
• Published: 09/24/2009
• Est. Priority Date: 12/20/2006
• Status: Abandoned Application

• Current Assignee: Douglas B. Galloway, Patrick J. Bullen, Randall E. Holt
• Original Assignee: Douglas B. Galloway, Patrick J. Bullen, Randall E. Holt
• Inventors: Galloway, Douglas B, Holt, Randall E., Bullen, Patrick J.
• Application Number:
  US12/478,808
• Publication Number:
  US 20090238752A1
• Time in Patent Office: Days
• US Class Current: 423/648.100
• CPC Class Codes: G01N 33/005 H2

Abstract

A process for controlling a refinery or chemical process has been developed. The process comprises flowing a feed stream to a process unit; operating on the feed stream in the process unit to generate an effluent stream; flowing the effluent stream away from the process unit; passing at least a portion of the feed stream or the effluent stream through a catalytic alloy hydrogen sensor and generating a signal corresponding to the concentration of hydrogen present in either the feed stream or the effluent stream; passing the signal to a display unit; and adjusting at least one operating parameter of the process in response to at least the signal generated by the catalytic alloy hydrogen sensor. The catalytic alloy hydrogen sensor may be a palladium-nickel catalytic alloy hydrogen sensor. The adjustments may be based on a calculated mole percent hydrogen.

Claims

1. A process for controlling a virtually complete isomerization of normal paraffin hydrocarbons in a feed stream containing normal and non-normal hydrocarbons, comprising:

(a) passing a combined reactor feed comprising the feed stream and a desorption effluent through an isomerization reactor containing an isomerization catalyst to convert at least a portion of the normal hydrocarbons in the combined reactor feed to non-normal hydrocarbons which are withdrawn from the reactor in a reactor effluent;

(b) separating reactor effluent into a hydrogen-rich gas stream and an adsorber feed stream;

(c) passing the adsorber feed stream to an adsorption section containing an adsorber bed to adsorb normal hydrocarbons from the adsorber feed stream and passing non-normal hydrocarbons out of the adsorption section as adsorber effluent containing an isomerate product;

(d) forming a hydrogen recycle stream by adding essentially pure hydrogen to at least a portion of the hydrogen-rich gas stream in an amount sufficient to make up hydrogen lost during processing;

(e) passing the hydrogen recycle stream through the adsorber bed containing adsorbed normal hydrocarbons to produce the desorption effluent which comprises hydrogen and normal hydrocarbons;

(f) passing the desorption effluent to the isomerization reactor;

(g) sensing the concentration of hydrogen in at least a portion of a stream selected from the group consisting of the adsorber feed stream, the adsorber effluent, the hydrogen recycle stream, the desorption effluent, and combinations thereof, using a catalytic alloy hydrogen sensor; and

(h) adjusting, automatically, at least one operating parameter of the virtually complete isomerization of normal paraffin hydrocarbons in response to the concentration of hydrogen sensed in the stream selected in step (g).

2. The process of claim 1 further comprising sensing the pressure in the same stream as the concentration of hydrogen was sensed;

calculating a quantitative amount of hydrogen from the pressure and the concentration of hydrogen sensed by the catalytic alloy hydrogen sensor; and

wherein the adjusting of at least one operating parameter of step (h) is in response to the quantitative amount of hydrogen.

3. The process of claim 1 wherein the quantitative amount of hydrogen is selected from the group consisting of mole percent of hydrogen, mass percent of hydrogen, and volume percent of hydrogen.

4. A process for controlling a virtually complete isomerization of normal paraffin hydrocarbons in a feed stream containing normal and non-normal hydrocarbons, comprising:

(a) passing a desorption effluent through an isomerization reactor containing an isomerization catalyst to convert at least a portion of the normal hydrocarbons in the desorption effluent to non-normal hydrocarbons which are withdrawn from the reactor in a reactor effluent;

(b) separating reactor effluent into a hydrogen-rich gas stream and an adsorber feed stream;

(c) passing a combined feed stream of fresh feed stream containing at least normal paraffins and the adsorber feed stream to an adsorption section containing an adsorber bed to adsorb normal hydrocarbons from the combined feed stream and passing non-normal hydrocarbons out of the adsorption section as adsorber effluent containing an isomerate product;

(d) forming a hydrogen recycle stream by adding essentially pure hydrogen to at least a portion of said hydrogen-rich gas stream in an amount sufficient to make up hydrogen lost during processing;

(e) passing the hydrogen recycle stream through the adsorber bed containing adsorbed normal hydrocarbons to produce said desorption effluent which comprises hydrogen and normal hydrocarbons;

(f) passing said desorption effluent to said isomerization reactor;

(g) sensing the concentration of hydrogen in at least a portion of a stream selected from the group consisting of the adsorber feed stream, the adsorber effluent, the hydrogen recycle stream, the desorption effluent, and combinations thereof, using a catalytic alloy hydrogen sensor;

(h) adjusting, automatically, at least one operating parameter of the virtually complete isomerization of normal paraffin hydrocarbons in response to the concentration of hydrogen sensed in the stream selected in step (g).

5. The process of claim 4 further comprising sensing the pressure in the same stream as the concentration of hydrogen was sensed;

calculating a quantitative amount of hydrogen from the pressure and the concentration of hydrogen sensed by the catalytic alloy hydrogen sensor; and

wherein the adjusting of at least one operating parameter of step (h) is in response to the calculated quantitative amount of hydrogen.

The process of claim 23 wherein the quantitative amount of hydrogen is selected from the group consisting of mole percent of hydrogen, mass percent of hydrogen, and volume percent of hydrogen.