Method for safely and quickly shutting down and cleaning a hydroprocessing reactor of spent catalyst via a water flooding technique

Patent metadata

Field	Value
Publication number	US-9545649-B2
Application number	US-201514723130-A
Country	US
Kind code	B2
Filing date	May 27, 2015
Priority date	May 27, 2015
Publication date	Jan 17, 2017
Grant date	Jan 17, 2017

Abstract

Processes for shutting down a hydroprocessing reactor and for removing catalyst from the reactor may comprise shutting off hydrocarbon feed to the reactor, stripping hydrocarbons from the catalyst, cooling the reactor to a first threshold reactor temperature, purging the reactor with N 2 gas, introducing water into the reactor, and dumping the catalyst from the reactor, wherein the first threshold reactor temperature may be substantially greater than 200° F. In an embodiment, the water may be introduced into the reactor via a quench gas distribution system when the reactor is at a second threshold reactor temperature not greater than 200° F. to cool the reactor to a third threshold reactor temperature not greater than 120° F.

First claim

What is claimed is:

1. A process for shutting down a hydroprocessing reactor and for removing catalyst from the reactor, wherein the reactor includes a quench gas distribution system, the process comprising:
a) shutting off hydrocarbon feed to the reactor;
b) stripping hydrocarbons from the catalyst;
c) cooling the reactor to a first threshold reactor temperature;
d) after step c), purging the reactor with N 2 gas;
e) after step d), and when the reactor is at a second threshold reactor temperature, introducing water into the reactor via the quench gas distribution system; and
f) dumping a catalyst slurry from the reactor, the catalyst slurry comprising the catalyst and the water, wherein the first threshold reactor temperature is greater than 200° F.

2. The process according to claim 1 , wherein the first threshold reactor temperature is in the range from 205° F. to 300° F.

3. The process according to claim 1 , wherein the second threshold reactor temperature is not greater than 200° F.

4. The process according to claim 1 , wherein step b) comprises circulating H 2 gas through the reactor at a temperature at least 25° F. above a final operating temperature of the reactor.

5. The process according to claim 4 , further comprising:
g) at the termination of step d), quantifying the hydrocarbon content of the effluent discharged from the reactor; and
h) based on the hydrocarbon content, determining a lower explosive limit for the reactor effluent.

6. The process according to claim 1 , wherein step c) comprises circulating H 2 gas through the reactor, and the process further comprises:
i) during step c), recording the carbon monoxide concentration of the effluent discharged from the reactor; and
j) if the reactor temperature falls below a nickel carbonyl threshold temperature while the recorded carbon monoxide concentration is above a carbon monoxide threshold, re-heating the reactor above the nickel carbonyl threshold temperature for a time period sufficient to thermally decompose nickel carbonyl.

7. The process according to claim 1 , wherein:
step c) comprises circulating H 2 gas through the reactor,
the reactor includes a quench gas distribution system, and
during step c) at least a portion of the H 2 gas is introduced into the reactor via the quench gas distribution system.

8. The process according to claim 1 , wherein:
the water introduced into the reactor according to step e) is at a temperature not less than 50° F., and
the water introduced into the reactor according to step e) cools the reactor to a third threshold reactor temperature not greater than 120° F.

9. The process according to claim 1 , wherein step e) comprises flooding the reactor with the water.

10. The process according to claim 1 , wherein the water introduced into the reactor according to step e) has a chloride content not greater than 50 ppm.

11. The process according to claim 1 , further comprising:
k) concurrently with step f), separating the water from the dumped catalyst slurry to provide separated water, and
l) recycling the separated water to the reactor.

12. The process according to claim 1 , wherein a portion of the catalyst is retained within the reactor as residual catalyst after step f), and the process further comprises:
m) vacuuming the residual catalyst from the reactor.

13. The process according to claim 12 , wherein the reactor includes at least one quench ring having a plurality of quench apertures therein, and the process further comprises:
n) after step m), supplying water to the quench ring; and
o) during step n), assessing the patency of the quench apertures based on the height of a water spout delivered from each of the quench apertures.

14. The process according to claim 1 , further comprising:
p) after step f), washing the reactor internals with pressurized water at a pressure less than 5,000 psi.

15. The process according to claim 1 , wherein after step f) the reactor contains aggregated catalyst, and the process further comprises:
q) after step f), hydro-drilling the aggregated catalyst.

16. The process according to claim 1 , further comprising:
r) after step f), separating the water from the catalyst slurry to provide separated water,
s) quantitatively analyzing the separated water for the presence of contaminants to provide quantitative contaminant data, and
t) based on the quantitative contaminant data, determining a schedule for releasing the separated water to a refinery waste water system.

17. The process according to claim 1 , wherein:
the first threshold reactor temperature is in the range from 205° F. to 300° F.,
the second threshold reactor temperature is not greater than 200° F., and
the water introduced into the reactor in step e) cools the reactor to a third threshold reactor temperature not greater than 120° F.

18. A process for shutting down a hydroprocessing reactor and for removing catalyst from the reactor, the process comprising:
a) shutting off hydrocarbon feed to the reactor;
b) stripping hydrocarbons from the catalyst at a temperature above the final reactor operating temperature;
c) cooling the reactor with H 2 gas at a controlled reactor cooling rate, wherein the reactor includes a quench gas distribution system, and during step c) at least a portion of the H 2 gas is introduced into the reactor via the quench gas distribution system;
d) when the reactor is at a first threshold reactor temperature, circulating N 2 gas through the reactor during at least one pressure/depressure cycle of the reactor;
e) after step d), and when the reactor is at a second threshold reactor temperature, introducing water into the reactor via the quench gas distribution system;
f) when the reactor is flooded with the water, dumping a catalyst slurry from the reactor, wherein the dumped catalyst slurry comprises the catalyst and the water;
g) separating the water from the dumped catalyst slurry to provide separated water;
h) optionally, recycling at least a portion of the separated water to the reactor;
i) after step f), vacuuming residual catalyst from the reactor;
j) after step i), assessing the patency of a plurality of quench apertures of the quench gas distribution system; and
k) washing at least one internal component of the reactor with pressurized water, wherein:
the controlled cooling rate during step c) is not more than 25° F. per 15 minute interval,
the first threshold reactor temperature is in the range from 205° F. to 300° F.,
the second threshold reactor temperature is not greater than 200° F., and

the water introduced into the reactor during step e) has a temperature not less than 50° F. and a chloride content not more than 50 ppm.

Assignees

• Chevron Usa Inc

Inventors

• Johns Jeff William
• Souers Steven Alden
• Mcdaniel Douglas Gayle
• Cooke David Lawrence
• Bosi David Michael

Classifications

• B01J8/003 Primary

  in a downward flow · CPC title

• B08B5/04

  Cleaning by suction, with or without auxiliary action · CPC title

• B08B9/093

  by the force of jets or sprays ({B08B9/0813} , B08B9/20 take precedence) · CPC title

• B01J38/10

  using elemental hydrogen · CPC title

• B08B9/08 Primary

  Cleaning containers, e.g. tanks · CPC title