Scattered gas recovery integrated hydrocarbon recovery pry

Abstract

The utility model discloses a scattered gas recovery integrated hydrocarbon recovery pry, and belongs to the technical field of petrochemical equipment. The scattered gas recovery integrated hydrocarbon recovery pry comprises a filter, a first separator, a second separator, a heat exchanger, a refrigerator, a natural gas input pipeline, a product gas pipeline, an emptying pipeline and a condensate oil pipeline. The scattered gas recovery integrated hydrocarbon recovery pry disclosed by the utility model is simple in structure, the energy consumption of the device is reduced, the investment of the device is reduced, and the device is convenient to disassemble and reuse and convenient to reuse and move.

Description

Technical Field

[0001] The utility model belongs to the technical field of petrochemical equipment, in particular to a scattered gas recovery integrated hydrocarbon recovery skid. Background Art

[0002] The main processes currently used in hydrocarbon recovery units can be summarized as follows: refrigerant circulation refrigeration, expansion refrigeration, and hybrid refrigeration combining refrigerant and expansion refrigeration. Shallow refrigeration units with a refrigeration temperature of -50°C or higher mostly use refrigerant refrigeration or single-stage expansion refrigeration; medium and deep refrigeration units mostly use a hybrid refrigeration method combining refrigerant and expansion refrigeration. The disadvantages of existing technologies are the complex processes, high investment, and high energy consumption. Utility Model Content

[0003] The purpose of the utility model is to overcome the deficiencies of the prior art and provide an integrated hydrocarbon recovery skid for recovering scattered gas.

[0004] The purpose of the utility model is achieved through the following technical solutions: the integrated hydrocarbon recovery skid for scattered gas recovery includes a filter, a first separator, a second separator, a heat exchanger, a refrigerator, a natural gas input pipeline, a product gas pipeline, a vent pipeline and a condensate pipeline;

[0005] The inlet of the filter is connected to the natural gas input pipeline, and the first outlet of the filter is connected to the inlet of the first pipeline of the heat exchanger through the first connecting pipe;

[0006] The outlet of the first pipe of the heat exchanger is connected to the inlet of the refrigerator via the second connecting pipe, the outlet of the second pipe of the heat exchanger is connected to the product gas pipeline via the third connecting pipe, and the outlet of the third pipe of the heat exchanger is connected to the inlet of the second separator via the fourth connecting pipe;

[0007] The outlet of the refrigerator is connected to the inlet of the first separator via a fifth connecting pipe;

[0008] The first outlet of the first separator is connected to the inlet of the second pipe of the heat exchanger via the sixth connecting pipe, the second outlet of the first separator is connected to the inlet of the third pipe of the heat exchanger via the seventh connecting pipe, and the third outlet of the first separator is connected to the vent pipe via the eighth connecting pipe;

[0009] The first outlet of the second separator is connected to the product gas pipeline via the ninth connecting pipe, the second outlet of the second separator is connected to the condensate oil pipeline, and the third outlet of the second separator is connected to the venting pipeline via the tenth connecting pipe.

[0010] Furthermore, the natural gas input pipeline is provided with a first valve for opening or closing the natural gas input pipeline, the fifth connecting pipe is provided with an eleventh valve for opening or closing the fifth connecting pipe, the sixth connecting pipe is provided with a thirteenth valve for opening or closing the sixth connecting pipe, the seventh connecting pipe is provided with a fifteenth valve for opening or closing the seventh connecting pipe, and the product gas pipeline is provided with a nineteenth valve for opening or closing the product gas pipeline.

[0011] Furthermore, the condensate oil pipeline is provided with a twenty-second valve, a twenty-third valve, a twenty-fourth valve, a twenty-fifth valve, a twenty-sixth valve and a twenty-seventh valve. The twenty-second valve, the twenty-third valve and the twenty-fourth valve are connected in series in sequence to form a first condensate oil branch. The twenty-sixth valve and the twenty-seventh valve are connected in series to form a second condensate oil branch. The first condensate oil branch is connected in series between the second outlet of the second separator and the twenty-fifth valve, and the second condensate oil branch is connected in parallel with the first condensate oil branch.

[0012] Furthermore, the eighth connecting pipe is provided with a thirty-fourth valve, a thirty-fifth valve, a thirty-sixth valve and a thirty-seventh valve, and the thirty-fourth valve, the thirty-fifth valve and the thirty-sixth valve are connected in series in sequence to form a first vent branch, and the first vent branch is connected in series between the third outlet of the first separator and the vent pipe, and the thirty-seventh valve is connected in parallel with the first vent branch.

[0013] Furthermore, the tenth connecting pipe is provided with a 30th valve, a 31st valve, a 32nd valve and a 33rd valve, the 30th valve, the 31st valve and the 32nd valve are connected in series in sequence to form a second vent branch, the second vent branch is connected in series between the third outlet of the second separator and the vent pipe, and the 33rd valve is connected in parallel with the second vent branch.

[0014] Furthermore, the natural gas input pipeline is provided with a second valve for exhaust, the fifth connecting pipe is provided with a tenth valve for exhaust, and the seventh connecting pipe is provided with a fourteenth valve for exhaust.

[0015] Furthermore, the natural gas input pipeline is provided with a first pressure gauge, a second pressure gauge and a first temperature gauge, the first pressure gauge is connected to the natural gas input pipeline via a third valve, and the second pressure gauge is connected to the natural gas input pipeline via a fourth valve;

[0016] A third pressure gauge is provided on the first connecting pipe, and the third pressure gauge is connected to the first connecting pipe via a ninth valve; a second temperature gauge is provided on the second connecting pipe;

[0017] The third connecting pipe is provided with a fourth temperature gauge and a fifth pressure gauge, and the fifth pressure gauge is connected to the third connecting pipe via an eighteenth valve;

[0018] The fourth connecting pipe is provided with a fifth temperature gauge and a sixth pressure gauge, and the sixth pressure gauge is connected to the fourth connecting pipe via a twentieth valve;

[0019] The fifth connecting pipe is provided with a third temperature gauge and a fourth pressure gauge, and the fourth pressure gauge is connected to the fifth connecting pipe via a twelfth valve.

[0020] Furthermore, the first separator is provided with a first liquid level gauge and a second liquid level gauge, the first liquid level gauge is connected to the first separator via a sixteenth valve and a seventeenth valve respectively, the second liquid level gauge is connected to the first separator via a sixteenth valve and a seventeenth valve respectively, and the second liquid level gauge is connected to the thirteenth valve;

[0021] The second separator is provided with a third liquid level gauge and a fourth liquid level gauge. The third liquid level gauge is connected to the second separator via the twenty-eighth valve and the twenty-ninth valve respectively. The fourth liquid level gauge is connected to the second separator via the twenty-eighth valve and the twenty-ninth valve respectively. The fourth liquid level gauge is connected to the twenty-third valve.

[0022] The filter is provided with a fifth liquid level gauge, which is connected to the filter via a seventh valve and an eighth valve respectively.

[0023] Furthermore, the second outlet of the filter is connected to a sixth valve, the third temperature gauge is connected to the refrigerator via a third temperature display control meter, and the fourth temperature gauge is connected to the refrigerator via a fourth temperature display control meter.

[0024] Furthermore, the second connecting pipe, the fifth connecting pipe, the sixth connecting pipe and the seventh connecting pipe are wrapped with a thermal insulation layer.

[0025] The beneficial effects of the present invention are as follows: the integrated hydrocarbon recovery skid for scattered gas recovery in the present invention has a simple structure, reduces the investment in the device, is easy to disassemble and reuse, and facilitates the reuse and relocation of the device; by arranging a heat exchanger in front of the refrigerator, the inlet temperature of the refrigerator can be greatly reduced, so that the refrigerator can reduce the outlet temperature in a shorter time and with less energy consumption, thereby reducing the energy consumption of the device. BRIEF DESCRIPTION OF THE DRAWINGS

[0026] Figure 1 This is a schematic diagram of the composition of the integrated hydrocarbon recovery skid for scattered gas recovery in the utility model;

[0027] In the figure, FL01 is a filter, E01 is a heat exchanger, Q01 is a refrigerator, V01 is a first separator, V02 is a second separator, V1 is a first valve, V2 is a second valve, V3 is a third valve, V4 is a fourth valve, V5 is a fifth valve, V6 is a sixth valve, V7 is a seventh valve, V8 is an eighth valve, V9 is a ninth valve, V10 is a tenth valve, V11 is an eleventh valve, V12 is a twelfth valve, V13 is a thirteenth valve, V14 is a fourteenth valve, V15 is a fifteenth valve, V16 is a sixteenth valve, V17 is a seventeenth valve, V18 is an eighteenth valve, V19 is a nineteenth valve, V20 is a twentieth valve, V21 is a twenty-first valve, V22 is a twenty-second valve, V23 is a twenty-third valve, V24 is a twenty-fourth valve, V25 is a twenty-fifth valve, V26 is a twenty-sixth valve, V27—the twenty-seventh valve, V28—the twenty-eighth valve, V29—the twenty-ninth valve, V30—the 30th valve, V31—the thirty-first valve, V32—the thirty-second valve, V33—the thirty-third valve, V34—the thirty-fourth valve, V35—the thirty-fifth valve, V36—the thirty-sixth valve, V37—the thirty-seventh valve, PG01—the first pressure gauge, PT02—the second pressure gauge, PG03—the third pressure gauge, PG04—the fourth pressure gauge, PT05—the fifth pressure gauge, PG06—the sixth pressure gauge, TE01—the first temperature gauge, TE02—the second temperature gauge, TE03—the third temperature gauge, TE04—the fourth temperature gauge, TE05—the fifth temperature gauge, LG01—the first liquid level gauge, LT02—the second liquid level gauge, LG03—the third liquid level gauge, LT04—the fourth liquid level gauge, LG05—the fifth liquid level gauge. DETAILED DESCRIPTION

[0028] The following will be combined with the embodiments to clearly and completely describe the technical solutions of the present invention. Obviously, the embodiments described are only some of the embodiments of the present invention, rather than all of them. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative work shall fall within the scope of protection of the present invention.

[0029] See Figure 1 This embodiment provides a scattered gas recovery integrated hydrocarbon recovery skid:

[0030] like Figure 1As shown, the integrated hydrocarbon recovery skid for scattered gas recovery includes a filter FL01, a first separator V01, a second separator V02, a heat exchanger E01, a refrigerator Q01, a natural gas input pipeline, a product gas pipeline, a venting pipeline, and a condensate oil pipeline. The inlet of the filter FL01 is connected to the natural gas input pipeline, and the first outlet of the filter FL01 is connected to the inlet of the first pipeline of the heat exchanger E01 via a first connecting pipe; the outlet of the first pipeline of the heat exchanger E01 is connected to the inlet of the refrigerator Q01 via a second connecting pipe, the outlet of the second pipeline of the heat exchanger E01 is connected to the product gas pipeline via a third connecting pipe, and the outlet of the third pipeline of the heat exchanger E01 is connected to the inlet of the second separator V02 via a fourth connecting pipe; the outlet of the refrigerator Q01 is connected to the inlet of the first separator V01 via a fifth connecting pipe. Connection; the first outlet of the first separator V01 is connected to the inlet of the second pipeline of the heat exchanger E01 through the sixth connecting pipe, the second outlet of the first separator V01 is connected to the inlet of the third pipeline of the heat exchanger E01 through the seventh connecting pipe, and the third outlet of the first separator V01 is connected to the vent pipeline through the eighth connecting pipe; the first outlet of the second separator V02 is connected to the product gas pipeline through the ninth connecting pipe, the second outlet of the second separator V02 is connected to the condensate oil pipeline, and the third outlet of the second separator V02 is connected to the vent pipeline through the tenth connecting pipe.

[0031] The working process of the integrated hydrocarbon recovery skid for scattered gas recovery in this embodiment is as follows: the raw gas (H2S≤15mg / m3) from the previous process enters the filter FL01, which filters out the dirty oil and water in the raw gas. The filtered raw gas enters the heat exchanger E01, which performs a preliminary cooling on the raw gas, for example, cooling the raw gas to -21°C; the raw gas enters the refrigerator Q01 from the heat exchanger E01, which further cools the raw gas, for example, cooling the raw gas to -35°C-40°C, and then enters the first separation The dehydrogenated product gas, condensate oil and vent air are separated by the separator V01. The product gas and condensate oil enter the heat exchanger E01, and the vent air enters the vent pipeline. After heat exchange in the heat exchanger E01, the temperature of the product gas rises to 36.9°C. After passing through the heat exchanger E01, the product gas enters the product gas pipeline. After heat exchange in the heat exchanger E01, the temperature of the condensate oil rises to 34.9°C. After passing through the heat exchanger E01, the condensate oil further separates into product gas, condensate oil and vent air through the second separator V02. The product gas enters the product gas pipeline, the condensate oil enters the condensate oil storage tank through the condensate oil pipeline, and the vent air enters the vent pipeline.

[0032] The refrigeration temperature of the integrated hydrocarbon recovery skid for scattered gas recovery in this embodiment is -40°C, and it is mainly used to separate hydrocarbons of carbon four and above. Compared with the shallow refrigeration device with a refrigeration temperature of not less than -50°C, it increases the refrigeration temperature and reduces the energy consumption of the refrigerator.

[0033] In some embodiments, the natural gas input pipeline is provided with a first valve V1 for opening or closing the natural gas input pipeline, the fifth connecting pipe is provided with an eleventh valve V11 for opening or closing the fifth connecting pipe, the sixth connecting pipe is provided with a thirteenth valve V13 for opening or closing the sixth connecting pipe, the seventh connecting pipe is provided with a fifteenth valve V15 for opening or closing the seventh connecting pipe, and the product gas pipeline is provided with a nineteenth valve V19 for opening or closing the product gas pipeline.

[0034] In some embodiments, the condensate oil pipeline is provided with a twenty-second valve V22, a twenty-third valve V23, a twenty-fourth valve V24, a twenty-fifth valve V25, a twenty-sixth valve V26 and a twenty-seventh valve V27. The twenty-second valve V22, the twenty-third valve V23 and the twenty-fourth valve V24 are connected in series in sequence to form a first condensate oil branch, the twenty-sixth valve V26 and the twenty-seventh valve V27 are connected in series to form a second condensate oil branch, the first condensate oil branch is connected in series between the second outlet of the second separator V02 and the twenty-fifth valve V25, and the second condensate oil branch is connected in parallel with the first condensate oil branch.

[0035] In some embodiments, the eighth connecting pipe is provided with a thirty-fourth valve V34, a thirty-fourth valve V34V34, a thirty-fifth valve V35, a thirty-sixth valve V36 and a thirty-seventh valve V37. The thirty-fourth valve V34, the thirty-fourth valve V34V34, the thirty-fifth valve V35 and the thirty-sixth valve V36 are connected in series in sequence to form a first vent branch. The first vent branch is connected in series between the third outlet of the first separator V01 and the vent pipe, and the thirty-seventh valve V37 is connected in parallel with the first vent branch.

[0036] In some embodiments, the tenth connecting pipe is provided with a 30th valve V30, a 31st valve V31, a 32nd valve V32 and a 33rd valve V33. The 30th valve V30, the 31st valve V31 and the 32nd valve V32 are connected in series in sequence to form a second vent branch. The second vent branch is connected in series between the third outlet of the second separator V02 and the vent pipe, and the 33rd valve V33 is connected in parallel with the second vent branch.

[0037] In some embodiments, the natural gas input pipeline is provided with a second valve V2 for exhaust, the fifth connecting pipe is provided with a tenth valve V10 for exhaust, and the seventh connecting pipe is provided with a fourteenth valve V14 for exhaust.

[0038] In some embodiments, the filter FL01 is provided with a fifth valve V5 for draining liquid.

[0039] In some embodiments, the condensate oil pipeline is provided with a twenty-first valve V21 for draining liquid.

[0040] In some embodiments, the natural gas input pipeline is provided with a first pressure gauge PG01, a second pressure gauge PT02 and a first temperature gauge TE01, the first pressure gauge PG01 is connected to the natural gas input pipeline via a third valve V3, and the second pressure gauge PT02 is connected to the natural gas input pipeline via a fourth valve V4; the first connecting pipe is provided with a third pressure gauge PG03, and the third pressure gauge PG03 is connected to the first connecting pipe via a ninth valve V9; the second connecting pipe is provided with a second temperature gauge TE02; the third connecting pipe is provided with a fourth temperature gauge TE04 and a fifth pressure gauge PT05, and the fifth pressure gauge PT05 is connected to the third connecting pipe via an eighteenth valve V18; the fourth connecting pipe is provided with a fifth temperature gauge TE05 and a sixth pressure gauge PG06, and the sixth pressure gauge PG06 is connected to the fourth connecting pipe via a twentieth valve V20; the fifth connecting pipe is provided with a third temperature gauge TE03 and a fourth pressure gauge PG04, and the fourth pressure gauge PG04 is connected to the fifth connecting pipe via a twelfth valve V12.

[0041] In some embodiments, the first separator V01 is provided with a first liquid level gauge LG01 and a second liquid level gauge LT02, the first liquid level gauge LG01 is connected to the first separator V01 via the sixteenth valve V16 and the seventeenth valve V17 respectively, the second liquid level gauge LT02 is connected to the first separator V01 via the sixteenth valve V16 and the seventeenth valve V17 respectively, and the second liquid level gauge LT02 is connected to the thirteenth valve V13; the second separator V02 is provided with a third liquid level gauge LG03 and a fourth liquid level gauge LT04, the third liquid level gauge LG03 is connected to the second separator V02 via the twenty-eighth valve V28 and the twenty-ninth valve V29 respectively, the fourth liquid level gauge LT04 is connected to the second separator V02 via the twenty-eighth valve V28 and the twenty-ninth valve V29 respectively, and the fourth liquid level gauge LT04 is connected to the twenty-third valve V23; the filter FL01 is provided with a fifth liquid level gauge LG05, the fifth liquid level gauge LG05 is connected to the filter FL01 via the seventh valve V7 and the eighth valve V8 respectively. In this embodiment, corresponding valves can be adjusted according to the liquid levels detected by the liquid level gauges on the first separator V01 and the second separator V02, thereby achieving automatic adjustment of the liquid level.

[0042] In some embodiments, the second outlet of the filter FL01 is connected to the sixth valve V6, the third temperature meter TE03 is connected to the refrigerator Q01 via the third temperature display control table TIC03, and the fourth temperature meter TE04 is connected to the refrigerator Q01 via the fourth temperature display control table TISA04. The refrigeration temperature of the refrigerator Q01 can be adjusted according to the temperature detected by the third temperature meter TE03 and the fourth temperature meter TE04, thereby realizing automatic adjustment of the temperature of the refrigerator Q01 and improving the accuracy of the refrigeration temperature.

[0043] In some embodiments, the integrated hydrocarbon recovery skid for scattered gas recovery further includes a second liquid level display control table LICA02 and a fourth liquid level display control table LICA04. The second liquid level display control table LICA02 is connected in series between the second liquid level gauge LT02 and the thirteenth valve V13, and the fourth liquid level display control table LICA04 is connected in series between the fourth liquid level gauge LT04 and the twenty-third valve V23.

[0044] In some embodiments, a second pressure alarm PIA02 is provided at the second pressure gauge PT02, a fifth remote pressure gauge PI05 is provided on the third connecting pipe, a fifth temperature alarm TIA05 is provided at the fifth temperature gauge TE05, a first remote temperature gauge TI01 is provided on the natural gas input pipeline, and a second remote temperature gauge TI02 is provided on the second connecting pipe.

[0045] In some embodiments, the second connecting pipe, the fifth connecting pipe, the sixth connecting pipe and the seventh connecting pipe are wrapped with an insulation layer.

[0046] In some embodiments, the first valve, the second valve, the fifth valve, the seventh valve, the eighth valve, the nineteenth valve, the twenty-first valve, the twenty-second valve, the twenty-fourth valve, the twenty-sixth valve, the twenty-eighth valve, the twenty-ninth valve, the thirtieth valve, the thirty-second valve and the thirty-third valve are ball valves.

[0047] The third valve, fourth valve, sixth valve, ninth valve, tenth valve, eleventh valve, twelfth valve, fourteenth valve, fifteenth valve, sixteenth valve, seventeenth valve, eighteenth valve, twentieth valve, twenty-seventh valve, thirty-fourth valve, thirty-sixth valve and thirty-seventh valve are stop valves.

[0048] The thirteenth valve and the twenty-third valve are diaphragm valves.

[0049] The twenty-fifth valve is a check valve.

[0050] The thirty-first valve and the thirty-fifth valve are spring safety valves.

[0051] The above description is merely a preferred embodiment of the present invention. It should be understood that the present invention is not limited to the form disclosed herein and should not be construed as excluding other embodiments. Instead, the present invention can be used in various other combinations, modifications, and environments and can be modified within the scope of the concept described herein through the above teachings or techniques or knowledge in the relevant fields. Modifications and variations made by those skilled in the art that do not depart from the spirit and scope of the present invention are intended to be protected by the claims appended hereto.

Claims

1. Bulk gas recovery integrated hydrocarbon recovery skid, characterized by: It includes a filter, a first separator, a second separator, a heat exchanger, a refrigerator, a natural gas input pipeline, a product gas pipeline, a vent pipeline and a condensate oil pipeline; The inlet of the filter is connected to the natural gas input pipeline, and the first outlet of the filter is connected to the inlet of the first pipeline of the heat exchanger through the first connecting pipe; The outlet of the first pipe of the heat exchanger is connected to the inlet of the refrigerator via the second connecting pipe, the outlet of the second pipe of the heat exchanger is connected to the product gas pipeline via the third connecting pipe, and the outlet of the third pipe of the heat exchanger is connected to the inlet of the second separator via the fourth connecting pipe; The outlet of the refrigerator is connected to the inlet of the first separator via a fifth connecting pipe; The first outlet of the first separator is connected to the inlet of the second pipe of the heat exchanger via the sixth connecting pipe, the second outlet of the first separator is connected to the inlet of the third pipe of the heat exchanger via the seventh connecting pipe, and the third outlet of the first separator is connected to the vent pipe via the eighth connecting pipe; The first outlet of the second separator is connected to the product gas pipeline via the ninth connecting pipe, the second outlet of the second separator is connected to the condensate oil pipeline, and the third outlet of the second separator is connected to the venting pipeline via the tenth connecting pipe.

2. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The natural gas input pipeline is provided with a first valve for opening or closing the natural gas input pipeline, the fifth connecting pipe is provided with an eleventh valve for opening or closing the fifth connecting pipe, the sixth connecting pipe is provided with a thirteenth valve for opening or closing the sixth connecting pipe, the seventh connecting pipe is provided with a fifteenth valve for opening or closing the seventh connecting pipe, and the product gas pipeline is provided with a nineteenth valve for opening or closing the product gas pipeline.

3. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The condensate oil pipeline is provided with a 22nd valve, a 23rd valve, a 24th valve, a 25th valve, a 26th valve and a 27th valve. The 22nd valve, the 23rd valve and the 24th valve are sequentially connected in series to form a first condensate oil branch. The 26th valve and the 27th valve are connected in series to form a second condensate oil branch. The first condensate oil branch is connected in series between the second outlet of the second separator and the 25th valve. The second condensate oil branch is connected in parallel with the first condensate oil branch.

4. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The eighth connecting pipe is provided with a thirty-fourth valve, a thirty-fifth valve, a thirty-sixth valve and a thirty-seventh valve. The thirty-fourth valve, the thirty-fifth valve and the thirty-sixth valve are connected in series in sequence to form a first vent branch. The first vent branch is connected in series between the third outlet of the first separator and the vent pipe, and the thirty-seventh valve is connected in parallel with the first vent branch.

5. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The tenth connecting pipe is provided with a 30th valve, a 31st valve, a 32nd valve and a 33rd valve. The 30th valve, the 31st valve and the 32nd valve are connected in series in sequence to form a second vent branch. The second vent branch is connected in series between the third outlet of the second separator and the vent pipe, and the 33rd valve is connected in parallel with the second vent branch.

6. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The natural gas input pipeline is provided with a second valve for exhaust, the fifth connecting pipe is provided with a tenth valve for exhaust, and the seventh connecting pipe is provided with a fourteenth valve for exhaust.

7. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The natural gas input pipeline is provided with a first pressure gauge, a second pressure gauge and a first temperature gauge, the first pressure gauge is connected to the natural gas input pipeline via a third valve, and the second pressure gauge is connected to the natural gas input pipeline via a fourth valve; A third pressure gauge is provided on the first connecting pipe, and the third pressure gauge is connected to the first connecting pipe via a ninth valve; The second connecting pipe is provided with a second temperature gauge; The third connecting pipe is provided with a fourth temperature gauge and a fifth pressure gauge, and the fifth pressure gauge is connected to the third connecting pipe via an eighteenth valve; The fourth connecting pipe is provided with a fifth temperature gauge and a sixth pressure gauge, and the sixth pressure gauge is connected to the fourth connecting pipe via a twentieth valve; The fifth connecting pipe is provided with a third temperature gauge and a fourth pressure gauge, and the fourth pressure gauge is connected to the fifth connecting pipe via a twelfth valve.

8. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The first separator is provided with a first liquid level gauge and a second liquid level gauge, the first liquid level gauge is connected to the first separator via a sixteenth valve and a seventeenth valve respectively, the second liquid level gauge is connected to the first separator via a sixteenth valve and a seventeenth valve respectively, and the second liquid level gauge is connected to the thirteenth valve; The second separator is provided with a third liquid level gauge and a fourth liquid level gauge. The third liquid level gauge is connected to the second separator via the twenty-eighth valve and the twenty-ninth valve respectively. The fourth liquid level gauge is connected to the second separator via the twenty-eighth valve and the twenty-ninth valve respectively. The fourth liquid level gauge is connected to the twenty-third valve. The filter is provided with a fifth liquid level gauge, which is connected to the filter via a seventh valve and an eighth valve respectively.

9. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1 is characterized in that: The second outlet of the filter is connected to a sixth valve, the third temperature gauge is connected to the refrigerator via a third temperature display control meter, and the fourth temperature gauge is connected to the refrigerator via a fourth temperature display control meter.

10. The integrated hydrocarbon recovery skid for scattered gas recovery according to claim 1, characterized in that: The second connecting pipe, the fifth connecting pipe, the sixth connecting pipe and the seventh connecting pipe are wrapped with a thermal insulation layer.

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