Granted Patent B2

US 12,503,931 · App. 17/888,721 · Granted Dec 23, 2025

Inventors: David H Moneyhun (Rock Springs, WY); John Moneyhun (Rock Springs, WY)

Assignee: Moneyhun Equipment Sales & Services Co., Inc.

E21B41/0057B01D53/864B01D53/885E21B36/008E21B43/34E21B43/40B01D2257/702

Abstract

Claims (88)

1 . A zero emission blow down and fugitive gas remediation system configured to initially blow down accumulated production gas and subsequently eliminate gas at a wellhead, the system comprising:

a) an initial, larger blow down unit comprising:

i) a mobile platform with wheels and a tow hitch configured to be initially and removably positioned at the wellhead;

ii) an enclosure carried by the platform;

iii) an inlet carried by the platform and configured to be coupled to the wellhead and receive accumulated production gas;

iv) a separator carried by the platform and located in the enclosure and coupled to the inlet and configured to remove liquid from the accumulated production gas;

v) a bank of catalytic heaters located in the enclosure and coupled to the separator and configured to react with the accumulated production gas and produce heat; and

b) a subsequent, smaller fugitive gas remediation unit comprising:

i) an enclosure configured to be subsequently positioned at the wellhead;

ii) an inlet carried by the enclosure and configured to be coupled to the wellhead to receive gas;

iii) a separator located in the enclosure and coupled to the inlet and configured to remove liquid from the gas; and

iv) a catalytic heater located in the enclosure and coupled to the separator and configured to react with the gas and produce heat in the enclosure; and

c) the blow down unit having a larger size and a greater gas volume capacity with respect to a smaller size and a lesser gas volume capacity of the fugitive gas remediation unit.

2 . The system in accordance with claim 1 , wherein the bank of catalytic heaters of the blow down unit further comprises:

at least two separate banks spaced-apart from one another and with the catalytic heaters of each bank facing one another.

3 . The system in accordance with claim 2 , further comprising:

the at least two banks being coupled to the separator in parallel.

4 . The system in accordance with claim 1 , wherein:

the platform of the blow down unit has a footprint greater than 100 square feet; and

the enclosure of the fugitive gas remediation unit has a footprint less than 50 square feet.

5 . The system in accordance with claim 1 , wherein:

the catalytic heaters of the blow down unit have a surface area greater than 70 square feet; and

the catalytic heater of the fugitive gas remediation unit has a surface area less than 9 square feet.

6 . The system in accordance with claim 1 , wherein a capacity of the blow down unit is an order of magnitude greater than a capacity of the fugitive gas remediation unit.

7 . A method of blowing down and remediating a well utilizing the system in accordance with claim 1 , the method comprising:

positioning the blow down unit at the wellhead and coupling the inlet of the blow down unit to the wellhead;

receiving accumulated production gas from the wellhead and reacting the accumulated production gas with the bank of catalytic heaters of the blow down unit;

servicing the well;

removing the blow down unit;

positioning the fugitive gas remediation unit at the wellhead and coupling the inlet of the fugitive gas remediation unit to the wellhead; and

receiving fugitive casing gas, or production gas, or both from the wellhead and reacting the fugitive casing gas, or production gas, or both with the catalytic heater of the fugitive gas remediation unit.

8 . A zero emission blow down system configured to blow down a well, the system comprising:

a) a mobile platform with wheels and a tow hitch configured to be removably positioned at a wellhead;

b) an enclosure carried by the platform;

c) an inlet carried by the platform and configured to be coupled to the wellhead and receive accumulated production gas;

d) a separator carried by the platform and located in the enclosure and coupled to the inlet and configured to remove liquid from the accumulated production gas;

e) a bank of catalytic heaters located in the enclosure and coupled to the separator and configured to react with the accumulated production gas and produce heat in the enclosure;

f) the catalytic heaters are positioned closer to the tow hitch of the platform; and

g) the separator is positioned farther from the tow hitch of the platform.

9 . The system in accordance with claim 8 , wherein the bank of catalytic heaters further comprises:

at least two separate banks spaced-apart from one another and with the catalytic heaters of each bank facing one another.

10 . The system in accordance with claim 9 , further comprising:

the at least two banks being coupled to the separator in parallel;

each bank comprising at least two stacks of catalytic heaters arranged in a column; and

the at least two stacks being coupled in parallel.

11 . The system in accordance with claim 9 , further comprising:

the at least two banks being oriented parallel with one another;

the at least two banks being positioned spaced-apart from one another; and

the at least two banks being positioned spaced-apart from lateral walls of the enclosure.

12 . The system in accordance with claim 8 , wherein:

the bank of catalytic heaters is oriented parallel with a length of the platform; and

the catalytic heaters are oriented parallel with the length of the platform and face laterally.

13 . The system in accordance with claim 8 , wherein:

the platform has a footprint greater than 100 square feet.

14 . The system in accordance with claim 8 , wherein:

the bank of catalytic heaters extends at least half of a length of the enclosure.

15 . The system in accordance with claim 8 , wherein:

the bank of catalytic heaters extends from a floor to a ceiling of the enclosure.

16 . The system in accordance with claim 8 , further comprising:

the bank of catalytic heaters is anchored to a wall of the enclosure; and

a stand-off coupled between the bank of catalytic heaters and the wall of the enclosure with the catalytic heaters spaced-apart from lateral walls of the enclosure.

17 . The system in accordance with claim 8 , further comprising:

the mobile platform, the enclosure, the inlet, the separator, and the bank of catalytic heaters being part of an initial, larger blow down unit;

a subsequent, smaller fugitive gas remediation unit comprising:

i) an enclosure configured to be subsequently positioned at the wellhead;

ii) an inlet carried by the enclosure and configured to be coupled to the wellhead to receive gas;

iii) a separator located in the enclosure and coupled to the inlet and configured to remove liquid from the gas; and

iv) a catalytic heater located in the enclosure and coupled to the separator and configured to react with the gas and produce heat in the enclosure; and

the blow down unit having a larger size and a greater gas volume capacity with respect to a smaller size and a lesser gas volume capacity of the fugitive gas remediation unit.

18 . A method of blowing down and remediating a well utilizing the system in accordance with claim 17 , the method comprising:

positioning the blow down unit at the wellhead and coupling the inlet of the blow down unit to the wellhead;

receiving accumulated production gas from the wellhead and reacting the accumulated production gas with the bank of catalytic heaters of the blow down unit;

servicing the well;

removing the blow down unit;

positioning the fugitive gas remediation unit at the wellhead and coupling the inlet of the fugitive gas remediation unit to the wellhead; and

receiving fugitive casing gas, or production gas, or both from the wellhead and reacting the fugitive casing gas, or production gas, or both with the catalytic heater of the fugitive gas remediation unit.

19 . A zero emission blow down system configured to blow down a well, the system comprising:

a) a mobile platform with wheels and a tow hitch configured to be removably positioned at a wellhead;

b) an enclosure carried by the platform;

c) an inlet carried by the platform and configured to be coupled to the wellhead and receive accumulated production gas;

d) a separator carried by the platform and located in the enclosure and coupled to the inlet and configured to remove liquid from the accumulated production gas; and

e) a bank of catalytic heaters located in the enclosure and coupled to the separator and configured to react with the accumulated production gas and produce heat in the enclosure, wherein the bank of catalytic heaters further comprises:

at least two separate banks spaced-apart from one another and with the catalytic heaters of each bank facing one another;

the at least two banks being coupled to the separator in parallel;

the at least two banks being positioned spaced-apart from one another;

the at least two banks being positioned spaced-apart from lateral walls of the enclosure;

the at least two banks being anchored to walls of the enclosure; and

stand-offs coupled between the at least two banks and the walls of the enclosure.

Assignments (1)

Continuity (1)

References Cited (23)