CN111618048A

CN111618048A - Multiphase rotational flow supercharging pulse physical cleaning integrated equipment

Info

Publication number: CN111618048A
Application number: CN202010461259.1A
Authority: CN
Inventors: 林维金
Original assignee: Individual
Current assignee: Individual
Priority date: 2020-05-27
Filing date: 2020-05-27
Publication date: 2020-09-04

Abstract

The invention discloses multifunctional mixed medium electromagnetic pulse physical cleaning integration equipment which comprises an air compressor I, an air compressor II, an air storage tank I, an air storage tank II, a mixer and a dirt and material separation and recovery tank, wherein the air compressor I is fixed above the air storage tank I, an air outlet pipeline A of the air storage tank I is sequentially connected with an electromagnetic valve I and a three-way change valve I, the other two passages of the three-way change valve I are respectively connected with an air pipe B and an air pipe C, the air pipe B and the air pipe C are respectively connected to the outer walls of the pipeline I and the pipeline II and are communicated with the interiors of the pipeline I and the pipeline II, and one ends of the pipeline I and the pipeline II are both connected with auxiliary air transmission high-. The multifunctional mixed medium electromagnetic pulse physical cleaning integrated equipment has reasonable structural design, has strong functions of carrying out full physical cleaning, descaling and repairing on various equipment and pipelines, effectively reduces the running and equipment resistance of a pipe network, improves the heat transfer and pipe network heat transmission efficiency, and saves a large amount of funds for production enterprises.

Description

Multiphase rotational flow supercharging pulse physical cleaning integrated equipment

Technical Field

The invention belongs to pipeline cleaning integrated equipment, and particularly relates to multiphase rotational flow supercharging pulse physical cleaning integrated equipment.

Background

The cleaning equipment which is circulated and used in the market at present has single function, and the pipeline cleaning is mainly carried out by two methods of physics and chemistry. The physical cleaning process utilizes a single medium to periodically feed air into the pipeline through compressed air, and linear waves are formed in the pipeline to clean. Through the field practice observation for several years, the existing market uses the gas pulse cleaning equipment, the physical cleaning efficiency is lower in the underground long-distance pipeline gallery, the requirement for cleaning hard scale on the pipeline wall of a heat supply pipeline network, oil gas, water supply and sewage outdoor pipeline network long-distance system is difficult to realize, so that the treatment can be carried out only by utilizing a chemical agent mode, secondary corrosion leakage hidden danger is easily caused to an aged pipeline, and the loss of energy consumption and the production operation cost are directly caused to increase year by year.

Disclosure of Invention

The invention aims to overcome the defects of the prior art and provides a multiphase rotational flow supercharging pulse physical cleaning integrated device.

The invention relates to multiphase rotational flow supercharging pulse physical cleaning integrated equipment which comprises an air compressor I, an air compressor II, an air storage tank I, an air storage tank II, a mixer and a dirt and material separation and recovery tank, wherein the air compressor I is fixed above the air storage tank I, an air outlet pipeline A of the air storage tank I is sequentially connected with an electromagnetic valve I and a three-way reversing valve I, the other two passages of the three-way reversing valve I are respectively connected with an air pipe B and an air pipe C, the air pipe B and the air pipe C are respectively connected on the outer walls of the pipeline I and the pipeline II and are communicated with the interiors of the pipeline I and the pipeline II, the air compressor II is fixed above the air storage tank II, an air outlet pipeline D of the air storage tank II is sequentially connected with an electromagnetic valve II and a three-way reversing valve II, and the other two passages of the three-way reversing valve II are respectively connected with an air pipe F and an air pipe E, and the air pipe F and the air pipe E are respectively connected to the outer walls of the pipeline I and the pipeline II.，One end of the pipeline I and one end of the pipeline II are both connected with an auxiliary gas transmission high-pressure quick connector, a water outlet pipeline L of the mixer is respectively connected with a three-way reversing valve III and a three-way reversing valve IV through a water pipe X and a water pipe R, the other two passages of the three-way reversing valve III are respectively connected with a water pipe K and a water pipe P, the water pipe K and the water pipe P are respectively connected onto the outer walls of the pipeline I and the pipeline II, the other two passages of the three-way reversing valve IV are respectively connected with a water pipe O and a water pipe S, and the water pipe O and the water pipe S are respectively connected onto the pipeline I andthe outer wall is located with the interface of water pipe K, water pipe P relatively, and the delivery port of pipeline I and pipeline II passes through water pipe N and links to each other with tee bend diversion valve V, and tee bend diversion valve V links to each other with the inlet channel of blender and dirt material separation recovery tank export tee bend diversion valve VI respectively in two other passageways, tee bend diversion valve VI links to each other with water pipe T and water pipe Q respectively in two other passageways, and water pipe T communicates with pipeline I.

As a further improvement of the invention, visual windows are arranged on the cleaning outlets of the pipeline I and the pipeline II, so that the cleaning effect can be observed and adjusted at any time.

As a further improvement of the invention, the outlet ends of the air pipe C and the air pipe E are positioned on the same circumference of the pipeline I, the distance between the air pipe C and the air pipe E is 80-120 mm, the outlet ends of the air pipe C and the air pipe E and the pipeline I form an included angle of 30-65 degrees, the outlet ends of the air pipe B and the air pipe F are positioned on the same circumference of the pipeline II, the distance between the air pipe B and the air pipe F is 80-120 mm, and the included angle of 30-65 degrees is formed between the air pipe B and the pipeline II.

As a further improvement of the invention, the outlet ends of the water pipe O and the water pipe K are positioned on the same circumference of the pipeline I, the distance between the water pipe O and the water pipe K is 80-120 mm, included angles of 30-65 degrees are formed between the water pipe O and the pipeline I, the outlet end of the water pipe P and the outlet end of the water pipe S are positioned on the same circumference of the pipeline II, the outlet ends of the water pipe O and the water pipe K are positioned on the same circumference of the pipeline II, the distance between the water pipe O and the water pipe K is 80-120 mm, and included angles of 30-65 degrees are formed between the water pipe O and the pipeline II.

As a further improvement of the invention, the communication positions of the water pipe O and the water pipe K with the pipeline I are positioned behind the communication position of the air pipe C and the air pipe E with the pipeline I, the communication position of the water pipe T with the pipeline I is positioned behind the communication position of the water pipe D and the water pipe K with the pipeline I, and the communication positions of the water pipe S and the water pipe P with the pipeline II are positioned behind the communication position of the air pipe B and the air pipe F with the pipeline II; the communication position of the water pipe N and the pipeline II is positioned behind the communication position of the water pipe S and the water pipe P and the pipeline II.

As a further improvement of the invention, the air pipe C is connected with a control valve I through a three-way change valve VII, the other end of the control valve I is connected with a pressurizing air pipe I, the air pipe E is connected with a control valve II through a three-way change valve VIII, and the other end of the control valve II is connected with a pressurizing air pipe II.

As a further improvement of the invention, the pipeline I is connected with a heater water outlet pipeline U through a water pipe J, the water outlet pipeline U is connected with a pipeline L, the water inlet end of the heater is sequentially connected with a heating pump and an electric valve V, and the electric valve V is connected with the water pipe L through the water pipe V.

As a further improvement of the invention, an air outlet pipeline of the air storage tank I is connected with a pipeline I of the scale and material separation and recovery tank through an electromagnetic valve VI, an air outlet pipeline of the air storage tank II is connected with a pipeline G of the scale and material separation and recovery tank through an electromagnetic valve VIII, the distance between the outlet ends of the pipeline I and the pipeline G which are both connected on the same circumference of the outlet end wall of the scale and material separation and recovery tank is 80-120 mm, and the pipeline I and the pipeline G form an included angle of 30-65 degrees with the outlet end wall of the scale and material separation and recovery tank.

As a further improvement of the invention, a passage of the three-way reversing valve VI is communicated with the outlet end of the dirt and material separating and recovering tank through a water pipe Q, and a blow-down valve I is arranged on the dirt and material separating and recovering tank.

As a further improvement of the invention, the mixer is sequentially connected with an electric valve VIII and a booster pump through a pipeline.

The multiphase rotational flow supercharging pulse physical cleaning integrated equipment has reasonable structural design, has extremely strong functions of carrying out full physical cleaning descaling and repairing on various equipment and pipelines, makes up for the defect of single gas pulse equipment, realizes the comprehensive, rapid and efficient physical cleaning process of boiler tube bundles, oil gas, heat supply, water supply and sewage pipelines, carries out anticorrosive coating repairing on spot corrosion surfaces of tube walls at any time through the device according to requirements after dirt is removed, continuously prolongs the service life and the strength of the pipelines, effectively reduces the operation and the equipment resistance of a pipe network, improves the heat transfer efficiency and the heat transmission efficiency of the pipe network, reduces the operation cost, and saves a large amount of reconstruction funds for production enterprises.

Drawings

FIG. 1 is a system diagram of the multiphase swirling pressure pulse physical cleaning integrated equipment of the invention.

Detailed Description

The invention relates to multiphase rotational flow pressurization pulse physical cleaning integration equipment which comprises an air compressor I1, an air compressor II 7, an air storage tank I2, an air storage tank II 8, a mixer 25 and a dirt separation and recovery tank 32, wherein the air compressor I1 is fixed above the air storage tank I2, an air outlet pipeline A of the air storage tank I2 is sequentially connected with a pressure reducer I4, a solenoid valve I5 and a three-way change valve I6, the other two passages of the three-way change valve I6 are respectively connected with an air pipe B and an air pipe C, the air pipe B and the air pipe C are respectively connected on the outer walls of a pipeline I13 and a pipeline II 14 and are communicated with the interiors of the pipeline I13 and the pipeline II 14, the air compressor II 7 is fixed above the air storage tank II 8, an air outlet pipeline D of the air storage tank II 8 is sequentially connected with a pressure reducer II 10, a solenoid valve II 11 and a three-way change valve II 12, the other, the air pipe F and the air pipe E are respectively connected on the outer walls of the pipeline I13 and the pipeline II 14，The outlet ends of the air pipe C and the air pipe E are located on the same circumference of the pipeline I13, the distance between the air pipe C and the air pipe E is 80-120 mm, included angles of 30-65 degrees are formed between the air pipe C and the pipeline I13, the outlet ends of the air pipe B and the air pipe F are located on the same circumference of the pipeline II 14, the distance between the air pipe B and the air pipe F is 80-120 mm, included angles of 30-65 degrees are formed between the air pipe B and the pipeline II 14, and the included angles formed between the air pipe C and the pipeline I13 and the included angles formed between the air pipe B and the pipeline II 14 can be determined according to the condition of the pipeline to be cleaned on site. The one end of pipeline I13 and pipeline II 14 all is connected with high pressure quick-operation joint 30, all is equipped with visual window 31 on the washing export of pipeline I (13) and pipeline II (14), and pipeline I13 and pipeline II 14 pass through high pressure quick-operation joint 30 to be connected in same washing pipeline.

The mixer 25 is sequentially connected with an electric valve VIII 24 and a pressure pump 23 through pipelines and is used for connecting a water pipe to add water into the mixer 25, a water outlet pipeline L of the mixer 25 is respectively connected with a three-way change valve III 15 through a water pipe X, a water pipe R is connected with a three-way change valve IV 16, the other two passages of the three-way change valve III 15 are respectively connected with a water pipe K and a water pipe P, the water pipe K and the water pipe P are respectively connected on the outer walls of a pipeline I13 and a pipeline II 14, the other two passages of the three-way change valve IV 16 are respectively connected with a water pipe O and a water pipe S, the water pipe O and the water pipe S are respectively connected at the positions, opposite to the interfaces of the water pipe K and the water pipe P, of the outer walls of the pipeline I13 and the pipeline II 14, the outlet ends of the water pipe O and the water pipe K are positioned on the same circumference of the pipeline I13, the distance between the water pipe O and the K is 80mm, the outlet ends of the water pipe P and the water pipe S are positioned on the same circumference of the pipeline II 14, the distance between the water pipe P and the water pipe S is 80-120 mm, and included angles of 30-65 degrees are formed among the water pipe P, the water pipe S and the pipeline II 14. The water outlets of the pipeline I13 and the pipeline II 14 are connected with a three-way direction-changing valve V17 through a water pipe N, the other two passages of the three-way direction-changing valve V17 are respectively connected with a water inlet pipeline of the mixer 25 and a three-way direction-changing valve VI 18, the other two passages of the three-way direction-changing valve VI 18 are respectively connected with a water pipe T and a water pipe Q, the water pipe T is communicated with the pipeline I13, and the water pipe Q is connected with a feed inlet of a dirt and material separation and recovery tank 32.

The communication position of the water pipe O, the water pipe K and the pipeline I13 is positioned behind the communication position of the air pipe C, the air pipe E and the pipeline I13, the communication position of the water pipe T and the pipeline I13 is positioned behind the communication position of the water pipe D, the water pipe K and the pipeline I13, and the communication position of the water pipe S, the water pipe P and the pipeline II 14 is positioned behind the communication position of the air pipe B, the air pipe F and the pipeline II 14; the communication position of the water pipe N and the pipeline II 14 is positioned behind the communication position of the water pipe S and the pipeline P and the pipeline II 14.

The air pressure output by the air storage tank I2 and the air storage tank II 8 is determined according to the service life and the damage degree of the cleaned pipeline, and whether the pressure reducer I4 and the pressure reducer II 10 are used or not is determined according to the situation. During forward washing, the electromagnetic valve I5, the passage of the three-way change valve I6 and the air pipe C, the electromagnetic valve II 11, the passage of the three-way change valve II 12 and the air pipe E, the passage of the three-way change valve III 15 and the water pipe K, the passage of the three-way change valve IV 16 and the water pipe O, the passage of the three-way change valve V17 and the water pipe M and the water pipe N are opened, and other valves are closed. The airflow in the air storage tank I2 enters the pipeline I13 through the air pipe C, the airflow in the air storage tank II 8 enters the pipeline I13 through the air pipe E, and two strands of air form a high-pressure cyclone gas in the pipeline I13. The trachea C is connected with a control valve I20 through a three-way change valve VII 19, the other end of the control valve I20 is connected with a pressurization trachea I26, the trachea E is connected with a control valve II 22 through a three-way change valve VIII 21, the other end of the control valve II 22 is connected with a pressurization trachea II 27, when the air pressure provided by the trachea C and the trachea E is enough, a passage between the three-way change valve VII 19 and the control valve I20 and a passage between the three-way change valve VIII 21 and the control valve II 22 are not opened, if the attenuation of the cleaning fluid power is insufficient, an auxiliary pressurization trachea can be opened, and kinetic energy is provided for fluid in the pipeline through the pressurization trachea I26 and the pressurization trachea II 27.

Water in the mixer 25 respectively enters the water pipe R and the water pipe X through the water pipe L, and the water pipe R and the water pipe X are respectively provided with a circulating pump I28 and a circulating pump II 29 for assisting water circulation in the pipeline. Water flow in a water pipe R and a water pipe X respectively enters a pipeline I13 through a three-way direction changing valve IV 16, a water pipe O, a three-way direction changing valve III 15 and a water pipe K to form rotational flow water flow, rotational flow gas pushes the water flow to enter a cleaned pipeline from the pipeline I13, the water flow enters a pipeline II 14 from a joint of the pipeline II 14 and the cleaned pipeline after being cleaned for a circle in the pipeline, the water flow enters a mixer 25 through a water pipe N, a three-way direction changing valve V17 and a water pipe M, an exhaust valve 39 and a drain valve 40 are arranged at the water inlet end of the mixer 25, the exhaust valve 39 and the drain valve 40 share the same discharge pipeline, the exhaust valve 39 discharges gas entering together with the water flow out of the mixer 25, and the water flow enters the mixer 25 again through a water pipe L and enters the pipeline I13 to form. Open the charge door in blender 25 top, can select whether to add the resin particle according to the condition of the pipeline that washs, resin particle and water inlet pipe L after the blender 25 stirring, the proportion of resin particle and water is generally 5 ~ 8: 2 to 4.

When backwashing is carried out after forward washing is finished, a passage of the electromagnetic valve I5, a passage of the three-way change valve I6 and the air pipe B, a passage of the electromagnetic valve II 11, a passage of the three-way change valve II 12 and the air pipe F, a passage of the three-way change valve III 15 and the water pipe P, a passage of the three-way change valve IV 16 and the water pipe S, a passage between the three-way change valve VI 18 and the water pipe T and the three-way change valve V17, a passage between the three-way change valve V17 and the water pipe M and the three-way change valve VI 18 are opened, and other valves are closed. The air flow in the air storage tank I2 enters the pipeline II 14 through the air pipe B, the air flow in the air storage tank II 8 enters the pipeline II 14 through the pipeline F, two air flows form a high-pressure cyclone gas in the pipeline II 14, and if the air pressure is insufficient, the pressure in the pipeline can be also pressurized through the pressurizing air pipe I26 and the pressurizing air pipe II 27.

Water in the mixer 25 respectively enters the water pipe R and the water pipe X through the water pipe L, respectively enters the pipeline II 14 through the three-way change valve IV 16 and the water pipe S and the three-way change valve III 15 and the water pipe P to form rotational flow, rotational flow gas pushes water to enter the cleaned pipeline from the pipeline II 14, after the forward cleaning rule is finished, the water enters the pipeline I13 from the joint of the pipeline I13 and the cleaned pipeline, enters the mixer 25 through the water pipe T, the three-way change valve VI 18, the three-way change valve V17 and the water pipe M, and then enters the pipeline II 14 again through the water pipe L to form backwashing circulation.

The pipeline I13 is connected with a water outlet pipeline U of a heater 35 through a water pipe J, the pipeline I13 is connected with the heater 35 (the heater is purchased by the electro-mechanical manufacturing company Limited of Huaxi, Yangzhou, and the model is HDR 70) through the water pipe J, the other end of the heater 35 is sequentially connected with a heating pump 37 and an electric valve V38, the other end of the electric valve V38 is communicated with a water pipe L through the water pipe V, and a controller is arranged on the heater 35, when the scale in the cleaned pipeline is too thick and the water needs to be heated and softened, the heating pump 37 and the electric valve V38 can be controlled to be opened through the controller, so that the water is heated to 50-60 degrees in the heater 35 and then enters the cleaned pipeline through the water pipe U, the water pipe.

When the water for impurity recovery needs to be filtered after the forward backwashing is finished, a passage between a three-way change valve VI 18 and a water pipe T and a water pipe Q and a passage between a three-way change valve V17 and a water pipe N and a three-way change valve VI 18 are opened, water flows through a pipeline II 14, the water pipe N, the three-way change valve V17 and the three-way change valve VI 18 and the water pipe Q enter a feed inlet above a dirt and material separation and recovery tank 32, the water flows through a filter screen 33 arranged at the middle position inside the dirt and material separation and recovery tank 32 and then enter the lower part inside the dirt and material separation and recovery tank 32, resin particles and impurities cleaned in the pipeline are left on the filter screen 33, a blow-down valve I3 is arranged at the lower end of the dirt and material separation and recovery tank 32 to directly discharge the water flows, a gas outlet pipeline I2 of a gas storage tank is connected with a pipeline I of the dirt and material separation and recovery tank 32 through a solenoid valve VI 3, a gas outlet pipeline, the distance between the outlet ends of the pipeline I and the pipeline G which are connected to the same circumference of the feed inlet of the scale and material separation and recovery tank 32 is 80-120 mm, the inlet ends of the pipeline I and the pipeline G and the feed inlet of the scale and material separation and recovery tank 32 form included angles of 30-65 degrees, the solenoid valve VI 3 and the solenoid valve VIII 9 are opened after water flow is discharged, water in the scale and material separation and recovery tank 32 is dried, and resin particles and impurities are blown out.

After the filtration recovery finishes, open solenoid valve I5 and tee bend diversion valve I6 or solenoid valve II 11 and tee bend diversion valve II 12, will be blown out by remaining water and impurity in the washing pipeline and blow dry the pipeline again, later can be according to the pipeline corrosion conditions, accessible pressurization trachea I26 blows in by the washing pipeline with the coating of restoration with pressurization trachea II 27 in, makes coating evenly cover on the inner wall of being washd the pipeline, realizes the washing and the restoration of pipeline.

Pressure gauges are arranged on a water pipe and an air pipe, working conditions of various power devices, instruments, various electromagnetic valves, a three-way valve and the like can be remotely monitored, adjusted and locally controlled in real time through a PRC master control cabinet, a controller arranged on a heater 35 can also be controlled through the PRC master control cabinet, the PRC master control cabinet can be communicated with a computer end, man-machine separation operation is achieved, cleaning parameters can be accurately adjusted in real time through a remote computer on site according to cleaning effects, and the safe, rapid, convenient and efficient control capability is achieved.

Claims

1. Heterogeneous whirl pressure boost pulse physics washs integrated equipment, comprises air compressor I (1), air compressor II (7), gas holder I (2), gas holder II (8), blender (25), dirt separation recovery tank (32), and its characterized in that air compressor I (1) is fixed in gas holder I (2) top, and the pipeline A of giving vent to anger of gas holder I (2) has connected gradually solenoid valve I (5) and tee bend diversion valve I (6), tee bend diversion valve I (6) other two passageways connect respectively trachea B and trachea C, trachea B and trachea C connect respectively in pipeline I (13) and pipeline II (14)On the outer wall, and communicate with each other with the inside of pipeline I (13) and pipeline II (14), air compressor II (7) are fixed in II (8) tops of gas holder, and the pipeline D of giving vent to anger of II (8) of gas holder has connected gradually solenoid valve II (11) and tee bend diversion valve II (12), trachea F and trachea E are connected respectively to two other passageways of tee bend diversion valve II (12), and trachea F and trachea E are connected respectively on the outer wall of pipeline I (13) and pipeline II (14)，One end of the pipeline I (13) and one end of the pipeline II (14) are both connected with an auxiliary gas transmission high-pressure quick connector (30), a water outlet pipeline L of the mixer (25) is respectively connected with a three-way direction-changing valve III (15) and a three-way direction-changing valve IV (16) through a water pipe X and a water pipe R, the other two passages of the three-way direction-changing valve III (15) are respectively connected with a water pipe K and a water pipe P, the water pipe K and the water pipe P are respectively connected on the outer walls of the pipeline I (13) and the pipeline II (14), the other two passages of the three-way direction-changing valve IV (16) are respectively connected with a water pipe O and a water pipe S, the water pipe O and the water pipe S are respectively connected at the positions, opposite to the interfaces of the outer walls of the pipeline I (13) and the pipeline II (14), of the water pipe K and the water pipe P, water outlets of the pipeline I (13) and the pipeline II (14) are respectively connected with a three-way direction-changing valve V (17) through a water pipe N (18) And the other two passages of the three-way change valve VI (18) are respectively connected with a water pipe T and a water pipe Q, and the water pipe T is communicated with the pipeline I (13).

2. The integrated equipment for physically cleaning the multiphase rotational flow supercharging pulse as claimed in claim 1, wherein the cleaning outlets of the pipeline I (13) and the pipeline II (14) are respectively provided with a visible window (31).

3. The multiphase rotational flow supercharging pulse physical cleaning integrated equipment as claimed in claim 1, wherein the outlet ends of the air pipe C and the air pipe E are located on the same circumference of the pipeline i (13), the distance between the air pipe C and the air pipe E is 80 mm-120 mm, included angles of 30-65 degrees are formed between the air pipe C and the pipeline E and the pipeline i (13), the outlet ends of the air pipe B and the air pipe F are located on the same circumference of the pipeline ii (14), the distance between the air pipe B and the air pipe F is 80 mm-120 mm, and included angles of 30-65 degrees are formed between the air pipe B and the pipeline ii (14).

4. The multiphase rotational flow pressurization pulse physical cleaning integrated equipment as claimed in claim 1 or 3, wherein outlet ends of the water pipe O and the water pipe K are located on the same circumference of the pipeline I (13), the distance between the water pipe O and the water pipe K is 80 mm-120 mm, included angles of 30-65 degrees are formed between the water pipe O and the pipeline I (13), outlet ends of the water pipe P and the water pipe S are located on the same circumference of the pipeline II (14), the outlet ends of the water pipe O and the water pipe K are located on the same circumference of the pipeline II (14), the distance between the water pipe O and the water pipe K is 80 mm-120 mm, and included angles of 30-65 degrees are formed between the water pipe O and the pipeline II (14).

5. The multiphase rotational flow pressurization pulse physical cleaning integrated equipment as claimed in claim 1, 3 or 4, wherein the communication position of the water pipe O, the water pipe K and the pipeline I (13) is located behind the communication position of the air pipe C, the air pipe E and the pipeline I (13), the communication position of the water pipe T and the pipeline I (13) is located behind the communication position of the water pipe D, the water pipe K and the pipeline I (13), and the communication position of the water pipe S, the water pipe P and the pipeline II (14) is located behind the communication position of the air pipe B, the air pipe F and the pipeline II (14); the communication position of the water pipe N and the pipeline II (14) is positioned behind the communication position of the water pipe S and the pipeline P and the pipeline II (14).

6. The integrated equipment for physically cleaning the multiphase rotational flow supercharged pulse as claimed in claim 1, wherein the air pipe C is connected with a control valve I (20) through a three-way change valve VII (19), the other end of the control valve I (20) is connected with a pressurized air pipe I (26), the air pipe E is connected with a control valve II (22) through a three-way change valve VIII (21), and the other end of the control valve II (22) is connected with a pressurized air pipe II (27).

7. The integrated equipment for physical cleaning of the multiphase rotational flow pressurization pulse as claimed in claim 1, wherein the pipeline I (13) is connected with a heater water outlet pipeline U through a water pipe J, the pipeline I (13) is connected with the heater (35) through the water pipe J, the other end of the heater is sequentially connected with a heating pump (37) and an electric valve V (38), and the other end of the electric valve V (38) is communicated with a water pipe L through a water pipe V.

8. The multiphase rotational flow supercharging pulse physical cleaning integrated equipment as claimed in claim 1, wherein an air outlet pipeline of a gas storage tank I (2) is connected with a pipeline I of the scale and material separation and recovery tank (32) through an electromagnetic valve VI (3), an air outlet pipeline of a gas storage tank II (8) is connected with a pipeline G of the scale and material separation and recovery tank (32) through an electromagnetic valve VIII (9), outlet ends of the pipeline I and the pipeline G are connected to the same circumference of an outlet end wall of the scale and material separation and recovery tank (32), the distance between the outlet ends of the pipeline I and the pipeline G is 80-120 mm, and included angles of 30-65 degrees are formed between the pipeline I and the outlet end wall of the scale and material separation and recovery tank (32).

9. The multiphase rotational flow pressurization pulse physical cleaning integrated equipment as claimed in claim 1, wherein a passage of the three-way change valve VI (18) is communicated with the outlet end of the dirt and material separation and recovery tank (32) through a water pipe Q, and a drain valve I (34) is arranged on the dirt and material separation and recovery tank (32).

10. The multiphase rotational flow pressurization pulse physical cleaning integrated equipment as claimed in claim 1, wherein the mixer (25) is sequentially connected with an electric valve VIII (24) and a booster pump (23) through pipelines.