CN211634973U

CN211634973U - Foam is all mixed pipe, is mixed foam fire extinguishing systems and fire engine

Info

Publication number: CN211634973U
Application number: CN201922266257.2U
Authority: CN
Inventors: 田志坚; 徐小东; 赵阳光; 王利军; 樊艳阳
Original assignee: Xuzhou Construction Machinery Group Co Ltd XCMG; XCMG Fire Fighting Safety Equipment Co Ltd
Current assignee: Xuzhou Construction Machinery Group Co Ltd XCMG; XCMG Fire Fighting Safety Equipment Co Ltd
Priority date: 2019-12-17
Filing date: 2019-12-17
Publication date: 2020-10-09
Anticipated expiration: 2029-12-17

Abstract

The present disclosure relates to a foam mix pipe, a mixed foam fire extinguishing system, and a fire fighting truck. The foam homogeneous mixing pipe comprises: the uniform mixing main pipe is used for mixing the foam mixed liquid F with a foaming medium to generate foam F'; and the foaming medium injection pipe is used for injecting the foaming medium into the uniform mixing main pipe, the output section of the foaming medium injection pipe penetrates into the inner cavity of the uniform mixing main pipe and is consistent with the extending direction of the uniform mixing main pipe, the end head of the output section of the foaming medium injection pipe is closed, and the side wall of the output section of the foaming medium injection pipe is provided with a foaming medium output hole. The foaming medium flows out from the foaming medium output hole and is fully mixed with the foam mixed liquid flowing through, and the foaming medium output hole in the side wall is not parallel to and opposite to the flow direction of the foam mixed liquid, so that the foam mixed liquid is prevented from flowing into the foaming medium output hole, and the foaming efficiency and the foaming stability are improved.

Description

Foam is all mixed pipe, is mixed foam fire extinguishing systems and fire engine

Technical Field

The utility model relates to a fire control technical field, especially, relate to a foam is mixing pipe, mixed foam fire extinguishing systems and fire engine all.

Background

When the foam fire fighting truck utilizes the foam mixed liquid to extinguish fire, firstly, the foam stock solution is fully mixed with water according to a specified proportion to form the foam mixed liquid, and then, the foam mixed liquid is foamed to extinguish the fire. The mixed foam mixed liquid is foamed into two types, namely, vacuum external air suction foaming is formed in the spraying process; and secondly, compressed gas is used as a foaming medium to be injected to generate foam. Tests and researches show that compared with a conventional air-out-suction foaming system, the foam mixing system adopting compressed gas injection foaming not only saves foam stock solution, but also has higher water utilization rate, and has outstanding advantages in the aspects of fire extinguishing, fire control, fire prevention and special fire.

In order to ensure the fire extinguishing efficiency, the mixing uniformity degree of the compressed gas and the foam mixed liquid is particularly important, and the foam mixing pipe known by the inventor has the defect of non-uniform mixing.

SUMMERY OF THE UTILITY MODEL

The inventor researches and discovers that the foam uniform mixing pipe in the related art has the defect of uneven mixing, and the fire extinguishing efficiency is influenced.

In view of this, the embodiment of the present disclosure provides a foam mixing pipe, a mixed foam fire extinguishing system and a fire engine, which can enable a foaming medium and a foam mixing liquid to be uniformly and sufficiently mixed to form foam, thereby improving fire extinguishing efficiency.

In one aspect of the present disclosure, there is provided a foam homogenizing pipe comprising:

the uniform mixing main pipe is used for mixing the foam mixed liquid F with a foaming medium to generate foam F'; and

the foaming medium injection pipe is used for injecting foaming media into the uniform mixing main pipe, the output section of the foaming medium injection pipe penetrates into the inner cavity of the uniform mixing main pipe and is consistent with the extending direction of the uniform mixing main pipe, the end head of the output section of the foaming medium injection pipe is closed, and the side wall of the output section of the foaming medium injection pipe is provided with a foaming medium output hole.

In some embodiments, the foamed medium output hole is perpendicular to the extending direction of the main mix pipe.

In some embodiments, the foaming medium output holes are plural and uniformly arranged along the circumferential direction and the extending direction of the output section of the foaming medium injection pipe.

In some embodiments, the centerline of the output section of the frothing medium injection pipe coincides with the centerline of the main homogenizing pipe.

In some embodiments, the end of the output section of the foam medium injection pipe is oriented in the same direction as the flow of the foam mixture F.

In some embodiments, the foaming medium injection pipe is L-shaped, with the output section of the foaming medium injection pipe being bent with respect to its input section.

In some embodiments, the foaming medium injection pipe includes a compressed air injection pipe and a liquid foaming medium injection pipe, and the foaming medium output hole includes an air outlet hole provided on an output section of the compressed air injection pipe and a liquid outlet hole provided on an output section of the liquid foaming medium injection pipe, respectively.

In some embodiments, the main mixing pipe is L-shaped, the output section of the main mixing pipe is bent with respect to the input section thereof, the output section of the compressed air injection pipe penetrates the input section of the main mixing pipe, and the output section of the liquid foaming medium injection pipe penetrates the output section of the main mixing pipe.

In some embodiments, the inner wall dimension D of the main mixing pipe is 125mm to 200mm, and the inner wall dimension D of the compressed air injection pipe is₁Is 25 mm-40 mm, and is liquidInner wall dimension D of foaming medium injection pipe₂The size of the (A) is 15 mm-30 mm.

In one aspect of the present disclosure, a hybrid foam fire suppression system is provided, including the aforementioned foam homogenizing pipe.

In some embodiments, further comprising:

the water outlet of the water supply device is communicated with the inlet of the uniform mixing main pipe;

the liquid outlet of the foam stock solution supply device is communicated with the inlet of the uniform mixing main pipe;

the inlet of the fire monitor is communicated with the outlet of the uniform mixing main pipe; and

and the outlet of the foaming medium supply device is communicated with the inlet of the foaming medium injection pipe.

In some embodiments, the foaming medium supply device comprises a liquid medium storage tank for storing the liquid foaming medium and a liquid medium delivery pump, the foaming medium injection pipe comprises a liquid foaming medium injection pipe, and the liquid medium storage tank supplies liquid to the liquid foaming medium injection pipe through the liquid medium delivery pump.

In some embodiments, further comprising:

the foam mixed liquid flowmeter is used for detecting the flow of foam mixed liquid generated after the foam and the water are mixed;

and the controller is used for controlling the rotating speed of the liquid medium delivery pump according to the flow of the foam mixed liquid detected by the foam mixed liquid flow meter.

In some embodiments, the pressurizing pressure of the liquid medium conveying pump is 2.5MPa to 3.5MPa, and the output flow rate is 80L/min to 200L/min.

In some embodiments, the working pressure of the liquid medium storage tank is configured to be 0.4 to 0.8 MPa.

In some embodiments, the liquid medium delivery pump is a gear pump, a vane pump or a plunger pump.

In some embodiments, the foaming medium supply device further comprises an air release valve, and a first temperature sensor and a liquid supply control valve which are arranged on a liquid supply passage of the liquid medium delivery pump, wherein an inlet of the air release valve is communicated with an outlet of the liquid medium delivery pump, and the controller is used for controlling the on-off states of the air release valve and the liquid supply control valve according to the liquid supply temperature detected by the first temperature sensor.

In some embodiments, further comprising:

the pipeline heater is arranged on a confluence passage of a liquid outlet passage of the foam stock solution supply device and a water outlet passage of the water supply device;

the second temperature sensor is arranged on the liquid outlet passage of the foam homogenizing pipe; and

and the controller is used for controlling the starting and closing states of the pipeline heater according to the liquid supply temperature detected by the second temperature sensor.

In some embodiments, the foam raw liquid supply device comprises a foam raw liquid tank and a foam raw liquid pump, wherein a liquid outlet of the foam raw liquid pump is communicated with an inlet of the mixing main pipe, the raw liquid tank comprises a type A foam raw liquid tank and a type B foam raw liquid tank, and the type A foam raw liquid tank and the type B foam raw liquid tank share the foam raw liquid pump.

In some embodiments, the foaming medium supplying device further comprises an air compressor, the foaming medium injection pipe comprising a compressed air injection pipe, the air compressor for supplying air to the compressed air injection pipe.

In one aspect of the present disclosure, a fire fighting vehicle is provided comprising the aforementioned hybrid foam fire suppression system.

Therefore, according to this disclosed embodiment, the output section of foaming medium injection pipe penetrates the inner chamber of the equal main pipe that mixes and is unanimous with the extending direction of the equal main pipe that mixes, the end of output section is sealed and the lateral wall is equipped with the foaming medium delivery outlet, the foaming medium from the outflow of foaming medium delivery outlet and the foam mixed liquid intensive mixing that flows through, because the foaming medium delivery outlet of lateral wall is not parallel relative with the flow direction of foam mixed liquid, avoided the foam mixed liquid to flow into the foaming medium delivery outlet, improved foaming efficiency and foaming stability.

Drawings

The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate embodiments of the disclosure and together with the description, serve to explain the principles of the disclosure.

The present disclosure may be more clearly understood from the following detailed description, taken with reference to the accompanying drawings, in which:

FIG. 1 is a cross-sectional view of some embodiments of a foam homogenizing pipe according to the present disclosure;

FIGS. 2 and 3 are cross-sectional views of a liquid foaming medium injection pipe and a compressed air injection pipe, respectively, in some embodiments of a foam homogenizing pipe according to the present disclosure;

FIG. 4 is a hydraulic system schematic of some embodiments of a hybrid foam fire suppression system according to the present disclosure;

fig. 5 is a schematic structural view of some embodiments of a fire engine according to the present disclosure.

Description of the reference numerals

1. A water tank; 2. a foam concentrate tank; 2-1, a type A foam stock solution tank; 2-2, B type foam stock solution tank; 3. a water pump; 3-1, a water tank water supply valve; 3-2, a water filling valve of the water tank; 4. a foam raw liquid pump; 4-1, a liquid supply valve of a A-type foam raw liquid tank; 4-2, cleaning a valve of a foam mixed liquid pipeline; 4-3, a liquid supply valve of a B-type foam raw liquid tank; 5-1, a tank top fire monitor; 5-2, arm support fire monitor; 6. an air compressor; 6-1, a compressed air output valve; 6-2, a pressure balance valve; 7. a foam homogenizing pipe; 71. a uniform mixing main pipe; 72. a compressed air injection pipe; 73. a liquid foaming medium injection pipe; 74. a liquid outlet hole; 75. an air outlet; 8. a water fire extinguishing operation valve; 9. a foam fire extinguishing operation valve; 10. an upper fire-fighting liquid supply valve; 11. a foam mixed liquid flow regulating valve; 12-1, a foam mixed liquid flowmeter; 12-2, a foam stock solution flow meter; 13. a controller; 14. a liquid medium storage tank; 14-1, a liquid medium storage tank liquid supply valve; 14-2, a self-pressurizing operation valve; 14-3, filling valve of liquid medium storage tank; 15. a liquid medium delivery pump; 15-1, an emptying valve; 15-2, a liquid supply control valve; 15-3, a high-pressure safety valve; 15-4, a pulse eliminating device; 16. a line heater; 17. a first temperature sensor; 18. a second temperature sensor; 100. a chassis; 200. a front leg; 300. a first interface device; 400. an auxiliary frame; 500. a second interface device; 600. a rear leg; 700. a central revolving body; 800. a turntable; 900. and a cantilever crane.

Detailed Description

Various exemplary embodiments of the present disclosure will now be described in detail with reference to the accompanying drawings. The description of the exemplary embodiments is merely illustrative and is in no way intended to limit the disclosure, its application, or uses. The present disclosure may be embodied in many different forms and is not limited to the embodiments described herein. These embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the disclosure to those skilled in the art. It should be noted that: the relative arrangement of parts and steps, the composition of materials, numerical expressions and numerical values set forth in these embodiments are to be construed as merely illustrative, and not as limitative, unless specifically stated otherwise.

The use of "first," "second," and similar terms in this disclosure is not intended to indicate any order, quantity, or importance, but rather are used to distinguish one element from another. The word "comprising" or "comprises", and the like, means that the element preceding the word covers the element listed after the word, and does not exclude the possibility that other elements are also covered. "upper", "lower", "left", "right", and the like are used merely to indicate relative positional relationships, and when the absolute position of the object being described is changed, the relative positional relationships may also be changed accordingly.

In the present disclosure, when a specific device is described as being located between a first device and a second device, there may or may not be intervening devices between the specific device and the first device or the second device. When a particular device is described as being coupled to other devices, that particular device may be directly coupled to the other devices without intervening devices or may be directly coupled to the other devices with intervening devices.

All terms (including technical or scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this disclosure belongs unless specifically defined otherwise. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.

Techniques, methods, and apparatus known to those of ordinary skill in the relevant art may not be discussed in detail but are intended to be part of the specification where appropriate.

In one aspect of the present disclosure, a foam homogenizing pipe is provided, and fig. 1 is a cross-sectional view of some embodiments of a foam homogenizing pipe according to the present disclosure. As shown in fig. 1, the foam homogenizing pipe 7 of this embodiment includes: the uniform mixing main pipe 71 is used for mixing the foam mixed liquid F with a foaming medium to generate foam F'; and the foaming medium injection pipe is used for injecting the foaming medium into the uniform mixing main pipe 71, the output section of the foaming medium injection pipe penetrates into the inner cavity of the uniform mixing main pipe 71 and is consistent with the extending direction of the uniform mixing main pipe 71, the end head of the output section is closed, and the side wall of the output section is provided with a foaming medium output hole.

As shown in fig. 1, a foam mixture F obtained by mixing water and a foam raw liquid at a certain ratio enters from an inlet of the main mix pipe 71, and a foaming medium is injected into the main mix pipe 71 through a foaming medium injection pipe and is sufficiently mixed with the foam mixture F to generate foam F', which then flows out from an outlet of the main mix pipe 71. The foaming medium comprises compressed air A and/or a liquid foaming medium N, the liquid foaming medium N can be liquid nitrogen or other suitable liquid media, and the medium can be gasified rapidly, is suitable for foaming, can extinguish fire, is nontoxic and has a gas-liquid two-phase volume ratio of more than 300.

Specifically, as shown in fig. 1, the foaming medium injection pipe includes a compressed air injection pipe 72 for injecting the compressed air a into the main mixing pipe 71 and/or a liquid foaming medium injection pipe 73 for injecting the liquid foaming medium N into the main mixing pipe 71, and as shown in fig. 1 to 3, the foaming medium output hole includes an air outlet hole 75 provided on an output section of the compressed air injection pipe 72 and/or a liquid outlet hole 74 provided on an output section of the liquid foaming medium injection pipe 73. The compressed air a enters the inner cavity of the main mixing pipe 71 through the air outlet 75 of the compressed air injection pipe 72, and the liquid foaming medium N enters the inner cavity of the main mixing pipe 71 through the liquid outlet 74 of the liquid foaming medium injection pipe 73.

As shown in fig. 1, the output section of the compressed air injection pipe 72 penetrates into the inner cavity of the main mixing pipe 71 and is consistent with the extending direction of the main mixing pipe 71, the end of the output section is closed, and the side wall of the output section is provided with an air outlet 75; the output section of the liquid foaming medium injection pipe 73 penetrates into the inner cavity of the uniform mixing main pipe 71 and is consistent with the extension direction of the uniform mixing main pipe 71, the end head of the output section is closed, and the side wall of the output section is provided with a liquid outlet 74; compressed air A flows out from venthole 75 and the foam mixed liquid F intensive mixing that flows through, and liquid foaming medium N flows out from going out liquid hole 74 and the foam mixed liquid F intensive mixing that flows through, and compressed air A or liquid foaming medium N flow out direction and foam mixed liquid's flow direction are not parallel relative, have avoided foam mixed liquid F to flow into the foaming medium delivery port, have improved foaming efficiency and foaming stability.

In order to increase the mixing contact area, in some embodiments, the foaming medium output holes are plural and uniformly arranged along the circumferential direction and the extending direction of the output section of the foaming medium injection pipe. As shown in fig. 1 to 3, the air outlet holes 75 are plural and uniformly arranged along the circumferential direction and the extending direction of the output section of the compressed air injection pipe 72, and the liquid outlet holes 74 are plural and uniformly arranged along the circumferential direction and the extending direction of the output section of the liquid foaming medium injection pipe 73.

To further improve the foaming efficiency and stability, in some embodiments, the foaming medium output hole is perpendicular to the extending direction of the mix main pipe 71. As shown in fig. 1, the air outlet 75 and the liquid outlet 74 are perpendicular to the extending direction of the mixing main pipe 71, so that the foam mixture F is prevented from flowing into the air outlet 75 and the liquid outlet 74 as much as possible, and such a structure can further enhance the mixing and foaming efficiency.

In some embodiments, the centerline of the output section of the frothing medium injection pipe coincides with the centerline of the main homogenizing pipe 71. As shown in fig. 1, the center line of the output section of the compressed air injection pipe 72 coincides with the center line of the main mixing pipe 71, and the center line of the output section of the liquid foaming medium injection pipe 73 coincides with the center line of the main mixing pipe 71, so that the mixing area of the foaming medium and the foam mixed liquid F can be increased, and the mixing and foaming efficiency can be improved.

In some embodiments, the end of the output section of the foam medium injection pipe is oriented in the same direction as the flow of the foam mixture F. As shown in fig. 1, the direction of the end of the output section of the compressed air injection pipe 72 is the same as the flow direction of the foam mixed liquid F, and the direction of the end of the output section of the liquid foaming medium injection pipe 73 is the same as the flow direction of the foam mixed liquid F, which is beneficial to outputting the foaming medium, and has reasonable structure and strong practicability.

As to how to realize the extension direction of the output section of the foaming medium injection pipe is consistent with the extension direction of the main mixing pipe 71, in some embodiments, the foaming medium injection pipe is L-shaped, and the output section of the foaming medium injection pipe is bent relative to the input section thereof, so that the foaming medium injection pipe is easy to process and reasonable in structure. Specifically, as shown in fig. 1, the compressed air injection pipe 72 is L-shaped, and an output section of the compressed air injection pipe 72 is bent with respect to an input section thereof; the liquid foaming medium injection pipe 73 is L-shaped, and an output section of the liquid foaming medium injection pipe 73 is bent with respect to an input section thereof.

Considering that the compressed air a is more difficult to uniformly mix and foam than the liquid foaming medium N, in some embodiments, as shown in fig. 1, the mixing main pipe 71 is L-shaped, an output section of the mixing main pipe 71 is bent with respect to an input section thereof, an output section of the compressed air injection pipe 72 penetrates into the input section of the mixing main pipe 71, and an output section of the liquid foaming medium injection pipe 73 penetrates into the output section of the mixing main pipe 71. Therefore, foam mixed liquid F with momentum and compressed air A can be stirred and mixed by the granules again on the curved surface of the elbow of the main uniform mixing pipe 71, and the L-shaped main uniform mixing pipe 71 is compact in structure, convenient to arrange, small in flow resistance and strong in implementability.

In some embodiments, the inner wall dimension D of the main mix pipe 71 is 125mm to 200mm, the inner wall dimension D1 of the compressed air injection pipe 72 is 25mm to 40mm, and the inner wall dimension D2 of the liquid foaming medium injection pipe 73 is 15mm to 30 mm. In this size range, the foam homogenizing pipe 7 can obtain excellent foaming efficiency and foaming stability.

The various embodiments of the disclosed foam homogenizing pipe described above may be applied to a hybrid foam fire suppression system. Accordingly, the present disclosure provides a hybrid foam fire suppression system including the foam homogenizing pipe embodiment of any of the foregoing.

In some embodiments, as shown in fig. 4, the hybrid foam fire suppression system further comprises: a water outlet of the water supply device is communicated with an inlet of the uniform mixing main pipe 71; a foam stock solution supply device, the liquid outlet of which is communicated with the inlet of the uniform mixing main pipe 71; the inlet of the fire monitor is communicated with the outlet of the uniform mixing main pipe 71; and a foaming medium supply device, the outlet of which is communicated with the inlet of the foaming medium injection pipe.

Specifically, as shown in fig. 1 and 4 in conjunction, the water supply apparatus includes a water tank 1, a water tank supply valve 3-1, a water tank fill valve 3-2, and a water pump 3; the foam raw liquid supply device comprises a foam raw liquid tank 2 and a foam raw liquid pump 4, a liquid outlet of the foam raw liquid pump 4 is communicated with an inlet of the uniform mixing main pipe 71, the foam raw liquid tank 2 comprises an A-type foam raw liquid tank 2-1 and a B-type foam raw liquid tank 2-2 which are respectively provided with an A-type foam raw liquid tank liquid supply valve 4-1 and a B-type foam raw liquid tank liquid supply valve 4-3, and the A-type foam raw liquid tank 2-1 and the B-type foam raw liquid tank 2-2 share the foam raw liquid pump 4. The fire monitor is used as an executing device for spraying fire extinguishing medium, in the embodiment, the fire monitor comprises a tank top fire monitor 5-1 arranged on a lower vehicle, an arm support fire monitor 5-2 arranged on an upper vehicle and an upper vehicle fire-fighting liquid supply valve 10, liquid supply ports of the two fire monitors are arranged in parallel and are both communicated with a foam output pipeline of the system, and the two fire monitors can be switched by a valve during actual operation; the foaming medium supply device comprises a liquid medium storage tank 14, a liquid medium storage tank liquid supply valve 14-1, a liquid medium delivery pump 15, an air compressor 6 and a compressed air output valve 6-1, wherein the liquid medium storage tank 14 is used for storing liquid nitrogen or other liquid foaming media, the air compressor 6 supplies air to a compressed air injection pipe 72, and the liquid medium storage tank 14 supplies liquid to a liquid foaming medium injection pipe 73 through the liquid medium delivery pump 15.

It should be noted that the basic functions and principles of the foam mixed liquid proportion mixing part in the above components are basically the same as those of the prior art, so that the following technical scheme of changing the types of the foam medium and the foam stock solution in different fire extinguishing scenes is detailed by taking the foam medium as compressed air A and liquid nitrogen N, the foam stock solution as A-type foam stock solution and B-type foam stock solution applied to a high-lift fire truck as an example, so as to realize the mixing and matching foaming of the compressed gas and the foam mixed liquid.

When the foam extinguishing agent is used for fighting fire of a building with people, a foam extinguishing mode of class A foam stock solution, compressed air A and water is preferably adopted.

When water fire fighting is performed, the water fire fighting operation valve 8 is opened and the foam fire fighting operation valve 9 is closed, as shown in fig. 4. A liquid outlet of the water pump 3 can be communicated with the tank top fire monitor 5-1 and the arm support fire monitor 5-2 through a water fire extinguishing operation valve 8. When foam fire extinguishing is performed, the water fire extinguishing operation valve 8 is closed and the foam fire extinguishing operation valve 9 is opened. The liquid outlet of the water pump 3 can be communicated with the tank top fire monitor 5-1 and the arm support fire monitor 5-2 through the foam fire extinguishing operation valve 9 → the foam mixed liquid flow meter 12-1 → the foam mixed liquid flow regulating valve 11 → the foam mixing pipe 7.

When the type A foam stock solution is preferably mixed with the foam solution, the type A foam stock solution tank liquid supply valve 4-1 is opened, the type B foam stock solution tank liquid supply valve 4-3 and the foam mixture liquid pipeline cleaning valve 4-2 are both closed, the foam stock solution pump 4 sucks the type A foam stock solution from the type A foam stock solution tank 2-1 to perform pressurization injection pipeline, the pressure foam stock solution passes through the foam stock solution flowmeter 12-2 and is mixed with the pressure water flowing through the foam fire extinguishing operation valve 9 together → the foam mixture liquid flowmeter 12-1 → the foam mixture liquid flow regulating valve 11 → the pipeline heater 16, and then the pressure foam stock solution is injected into the inlet end of the mixing main pipe 71 of the foam mixing pipe 7.

It should be noted that, the preferred A-type foam stock solution is based on the A-type foam extinguishing agent, is environment-friendly, generates foam with strong adhesive force and good heat insulation and heat radiation prevention effects, can effectively control the reburning of solid combustible materials, and is suitable for A-type fire extinguishing places. If B-type foam stock solution is selected for foam solution mixing, the A-type foam stock solution tank liquid supply valve 4-1 and the foam mixed solution pipeline cleaning valve 4-2 are both closed, the B-type foam stock solution tank liquid supply valve 4-3 is opened, the foam stock solution pump 4 pumps the B-type foam stock solution from the B-type foam stock solution tank 2-2 for pressurizing injection pipeline, the pressure foam stock solution passes through the foam stock solution flowmeter 12-2 as well, is converged and mixed with pressure water flowing through the foam fire extinguishing operation valve 9, and then → the foam mixed solution flowmeter 12-1 → the foam mixed solution flow regulating valve 11 → the pipeline heater 16, and then is injected into the inlet end of the mixing main pipe 71 of the foam mixing pipe 7.

In order to control the precise proportioning relationship between the foam concentrate and water, the flow feedback is also used in some embodiments of the disclosure to control the flow of the foam concentrate to achieve proportional mixing. In some embodiments, as shown in fig. 4, the mixed foam fire extinguishing system further includes a controller 13, a foam mixed liquid flow meter 12-1 and a foam raw liquid flow meter 12-2, the foam mixed liquid flow meter 12-1 is used for detecting the flow rate of the mixed water and the foam raw liquid, the foam raw liquid flow meter 12-2 is used for detecting the flow rate of the foam raw liquid, the controller 13 invokes a predetermined programming instruction according to the input signals of the two flow meters, the identification of the open state of the output valve of the foam raw liquid tank, and the like, and the requirement of the foam type required on site (i.e., it is determined to use different mixing ratios according to different foam extinguishing agent specifications and foam types), and controls the rotation speed of the foam raw liquid pump 4, so as to achieve the accurate ratio of the foam raw liquid and the water by regulating the flow rate of the.

In addition, various foam liquids corrode pipelines and related elements of the system, so that the service performance and the service life of the system are affected. Some embodiments of the present disclosure also provide a flushing function to prevent corrosion due to long-term adhesion of foam residue. As shown in figure 4, a foam mixed liquid pipeline cleaning valve 4-2 is arranged on a pipeline between the outlet of the foam fire extinguishing operation valve 9 and the inlet of the foam raw liquid pump 4, and under the non-flushing working condition, the valve is always in a closed state so as to ensure the realization of the foam mixed liquid function. Only after finishing the foam injection operation each time, the foam mixed liquid pipeline cleaning valve 4-2 is opened and the foam raw liquid pump 4 is started to clean the foam pipeline system after the liquid supply valve 4-1 of the A-type foam raw liquid tank and the liquid supply valve 4-3 of the B-type foam raw liquid tank are closed.

The air compressor 6 is used as a power element for providing compressed air A and outputs the compressed air A to the foam homogenizing pipe 7; the structure of the foam mixing pipe 7 is as shown in fig. 1, and the mixed foam mixture flows in from the inlet end of the mixing main pipe 71, and at the same time, the compressed air a also flows in from the inlet end of the compressed air injection pipe 72, and it is noted that no liquid nitrogen flows in from the liquid foaming medium injection pipe 73, so that the foam mixture only fully contacts with the air in the mixing main pipe 71 to form foam F ', and the foam F' after pre-foaming flows into the foam output pipeline of the system through the output end of the mixing main pipe 71. In order to avoid the mutual influence of the compressed air injection pipeline and the liquid nitrogen injection pipeline, one-way check valves are respectively arranged at the injection ends of the two pipelines.

As shown in fig. 4, in order to ensure smooth injection of compressed air, in some embodiments, the mixed foam fire extinguishing system further includes a compressed air output valve 6-1 and a pressure balance valve 6-2, and the pressure balance valve 6-2 is used for comparing water pressure with air pressure and sending a pressure control signal to adjust the air input of the air compressor 6, thereby realizing pressure matching. In order to control the precise proportioning relation between the compressed air and the foam mixed liquid, the controller 13 calls a preset programming instruction (namely, different mixing proportions are determined to be used according to different specifications and foaming types of the foam extinguishing agent) according to the input signal of the foam mixed liquid flowmeter 12-1 and the foaming type requirement required on site, and controls the rotating speed of the air compressor 6, so that the precise proportioning is realized by regulating and controlling the output flow of the air compressor 6. In addition, the compressed air output valve 6-1 is used to adjust the flow rate of the compressed air according to the actual fire, the kind of foam, and the like. In order to avoid the backflow of the compressed air, a one-way check valve is provided on the corresponding pipe.

Of course, it is also noted that in some cases, the flow output of the air compressor may be fixed to adjust the flow output of the fire pump and the foam pump to achieve a proportional mixing of the foam mixture and the compressed air.

The outlet of the foam uniform mixing pipe 7 is communicated with the inlets of the two fire monitor through a foam output pipeline, so that the prefabricated foam can be further uniformly mixed in the conveying pipeline until the spray of the sprayer. In order to avoid the backflow of the foam, a one-way check valve is arranged on the foam conveying pipeline.

And (II) when the foam extinguishing agent is used for unmanned industrial fire extinguishing, a foam extinguishing mode of B-type foam stock solution, compressed nitrogen based on liquid nitrogen filling and water is preferably adopted.

When the B-type foam stock solution is preferably mixed with the foam solution, the A-type foam stock solution tank liquid supply valve 4-1 and the foam mixed solution pipeline cleaning valve 4-2 are both closed, the B-type foam stock solution tank liquid supply valve 4-3 is opened, the foam stock solution pump 4 pumps the B-type foam stock solution from the B-type foam stock solution tank 2-2 to pressurize an injection pipeline, and the mixing principle, the formation and the flow direction of the foam mixed solution are as described in the foregoing.

The B-type foam concentrate is preferably based on a B-type foam extinguishing agent and is suitable for B-type fire extinguishing places, particularly various petroleum products, flammable and combustible liquids and the like in industrial fires. The B-type foam extinguishing agent can be divided into a non-water-soluble foam extinguishing agent (such as a protein foam extinguishing agent, a fluoroprotein foam extinguishing agent and an aqueous film-forming foam extinguishing agent) and an anti-soluble foam extinguishing agent, and the specification and model of the more specific B-type foam extinguishing agent are determined according to the material characteristics of a fire extinguishing object. Similarly, if the A-type foam stock solution is selected for foam solution mixing, the control of the A-type foam stock solution tank liquid supply valve 4-1, the B-type foam stock solution tank liquid supply valve 4-3, the foam mixture liquid pipeline cleaning valve 4-2 and the foam stock solution pump 4, the mixing principle, the formation and the flow direction of the foam mixture liquid can also be referred to in the foregoing.

The liquid medium delivery pump 15 is a power element for pumping and pressurizing liquid nitrogen in the liquid medium storage tank 14, and outputs the liquid nitrogen to the foam homogenizing pipe 7. As shown in fig. 1, while the mixed foam mixture liquid flows in from the inlet end of the main mix pipe 71, liquid nitrogen N is also injected from the inlet end of the liquid foaming agent injection pipe 73, and note that the air compressor system is set to be inoperative at this time, and the compressed air injection pipe 72 does not flow in, so that the foam mixture liquid is in full contact with only the liquid nitrogen N in the main mix pipe 71, and the liquid nitrogen N absorbs heat from the foam mixture liquid and is rapidly vaporized and boiled to form foam F'. In order to ensure the liquid nitrogen N to be fully contacted with the foam mixture F, in some embodiments, as shown in fig. 1, the axis of the output section of the liquid foaming medium injection pipe 73 should be coaxial with the axis of the output section of the main mixing pipe 71 and the end of the output section should be closed, and a plurality of liquid outlet holes 74 are designed in the output section of the liquid foaming medium injection pipe 73 along the axial direction and the circumferential direction, so that the liquid nitrogen N with momentum can be rapidly gasified and mixed with the foam mixture F when being injected into the main mixing pipe 71. The foam F' thus prefoamed flows into the foam outlet line of the system via the outlet end of the main mixing pipe 71. Also, the prepared foam can be further uniformly mixed in the conveying pipeline until the fire monitor sprays out.

In some embodiments, as shown in FIG. 4, the liquid medium storage tank 14 is a self-pressurizable liquid nitrogen container designed to store liquid nitrogen at a pressure of 1.6MPa or less and at a temperature of-196 deg.C, with a safety valve and pressure sensing means. In some embodiments, the working pressure of the liquid medium storage tank 14 is set to 0.4-0.8 MPa when the device is used in an elevated fire truck. When the liquid medium storage tank is in a normal storage state, the filling valve 14-3 of the liquid medium storage tank and the liquid supply valve 14-1 of the liquid medium storage tank are both closed; when the liquid medium storage tank is in an output working state, the filling valve 14-3 of the liquid medium storage tank is closed, and the liquid supply valve 14-1 of the liquid medium storage tank is opened; after the medium in the liquid medium storage tank is consumed and needs to be filled, the liquid supply valve 14-1 of the liquid medium storage tank is closed, after the filling port for external liquid nitrogen supply is connected, the filling valve 14-3 of the liquid medium storage tank is opened, and the liquid medium conveying pump 15 is started to suck and fill from the outside. Under the normal storage and working conditions of the liquid medium storage tank, the self-pressurization operation valve 14-2 is used for self-adaptive regulation of the pressure in the tank, namely: when the pressure in the tank is reduced to 0.4MPa, the control system opens the valve to allow part of liquid nitrogen in the tank to flow out, and the liquid nitrogen is vaporized into nitrogen gas by an air temperature vaporizer on a pipeline and then enters the tank for pressurization; and when the pressure in the tank is higher than 0.8MPa, the vehicle-mounted control system closes the valve. It should be noted that the pressure in the liquid medium storage tank 14 is set to the above range, mainly for ensuring a relatively stable supply of the liquid medium at the input pressure of the liquid medium feed pump 15, rather than directly providing the pressure at which the foam mixture can be injected into the foam homogenizing pipe 7 (the pressure should be equal to or higher than the pressure of the foam mixture). In practice, the pressure of the liquid nitrogen injection is realized by the pressurization of the liquid medium delivery pump 15.

In the existing technical solution (fire fighting truck + respective skid-mounted device — combined implementation of complete fire extinguishing unit), the injection pressure of liquid nitrogen is directly realized by the self-pressurization of the liquid medium storage tank 14. It is known that there are two types of vaporizers, one is an air temperature vaporizer, and the other is a water temperature vaporizer (using water as a transmission medium and providing heat through electric heating or gas heating), and the two types of self-pressurization have hysteresis for compensating pressure feedback, so the disadvantage is that when the pressure in the tank is insufficient, the pressure cannot be quickly increased to reach the required pressure, and when the pressure in the tank reaches, the pressure cannot be immediately stopped, especially when the capacity of the liquid medium storage tank is large, the disadvantage is more obvious, and therefore, the timeliness of the self-pressurization of the liquid medium storage tank is difficult to guarantee. In addition, since the design pressure of the liquid medium storage tank is 1.6MPa, the pressurization capacity is also limited. In the operation process of the elevating fire truck, along with the difference of the telescopic state and the amplitude changing state of the arm support (or the ladder frame) and the jet flow of the system, the output pressure of the fire pump is different, the pressure of the foam mixed liquid in the foam uniform mixing pipe 7 is correspondingly different, the variation range of the foam mixed liquid is basically 1-1.6 MPa, and the variation range of the foam mixed liquid is probably more than or equal to 1.6MPa for the elevating fire truck with higher meter number. Therefore, in practical engineering practice, the liquid nitrogen filling of the elevating fire truck is completely guaranteed by the automatic self-pressurization adjustment of the liquid medium storage tank 14, and the liquid nitrogen filling pressure is not less than or equal to the foam mixture pressure in the foam homogenizing mixing pipe 7 and cannot be reliably realized.

On the other hand, in order to achieve different fire-fighting purposes, the foam mixed liquid needs to be filled with compressed gas in different proportions according to purposes to be mixed, so that the foaming times and the foam quality of the foam liquid can be guaranteed, and the liquid nitrogen filling is realized by converting the liquid nitrogen into liquid nitrogen in different proportions according to the volume ratio of gaseous state to liquid state after the liquid nitrogen is vaporized (the volume ratio of liquid nitrogen vaporization is 640 times). The existing technical scheme for filling by self-pressurization of the liquid medium storage tank 14 is to measure the flow of the foam mixed liquid in real time and proportionally regulate and control the filling flow of liquid nitrogen, wherein the final way of regulating and controlling the filling flow of liquid nitrogen depends on the opening degree of a flow valve on a pipeline. Obviously, because the pipeline through flow is strongly related to the pressure difference of the flow valve, when the flow of the foam mixed liquid is not changed, the working pressure of the foam mixed liquid in the foam uniform mixing pipe can be influenced due to the change of the posture of an arm support (or a ladder frame) of the elevating fire truck, and further the flow of filling liquid nitrogen is influenced, so that the foaming multiple of the foam mixed liquid is changed, and the foam quality cannot be guaranteed. In addition, the feedback control of the flow valves is also difficult to regularly compensate for because of the hysteresis characteristic of the self-pressurization control of the liquid medium storage tank 14.

In summary, the adaptation of the injection pressure and the flow rate by self-pressurization of the liquid medium storage tank is difficult to achieve in engineering practice.

In order to effectively solve the problem, in some embodiments, as shown in fig. 4, the pressurization pressure of the liquid medium delivery pump 15 is 2.5MPa to 3.5MPa, and the output flow rate is 80L/min to 200L/min. The flow rate of the prepared foam of the system is more than or equal to 500L/s, and the liquid medium delivery pump 15 is a gear pump, a vane pump or a plunger pump in consideration of the convenience and compact arrangement of the application of the vehicle-mounted system. Preferably, the hydraulic motor is directly coupled to the drive. Of course, the variable frequency motor can be directly coupled to drive the gear pump, or the variable frequency motor is connected with the gear box in series and then drives the gear pump. It is known that the output flow of gear pumps, vane pumps and plunger pumps is only related to their rotational speed, and the output pressure depends on the load. Therefore, the pressure and the proportional flow of the compressed nitrogen added by the gear pump, the vane pump or the plunger pump are matched with the pressure and the proportional flow of the foam liquid, so that the matching can be simplified into single proportional flow matching.

In order to control the precise proportioning relationship between the liquid nitrogen and the foam mixture, in some embodiments, the hybrid foam fire suppression system further comprises: a foam mixed liquid flow meter 12-1 and a controller 13, wherein the foam mixed liquid flow meter 12-1 is used for detecting the flow of foam mixed liquid generated after foam and water are mixed; the controller 13 is used for controlling the rotating speed of the liquid medium delivery pump 15 according to the flow rate of the foam mixed liquid detected by the foam mixed liquid flow meter 12-1. The controller 13 calls a preset programming instruction (i.e. determining to use different mixing proportions according to different specifications and foaming types of the foam extinguishing agent) according to the input signal of the foam mixed liquid flowmeter 12-1 and the foaming type requirement required on site, and controls the rotating speed of the liquid medium conveying pump 15, so that accurate proportioning is realized by regulating and controlling the output flow of the liquid medium conveying pump.

When the liquid medium delivery pump 15 is initially operated, due to the fact that the initial temperature of the liquid nitrogen input pipeline and the pump body of the gear pump is relatively high, vaporization of liquid nitrogen in the initial flowing process can be caused, in order to avoid cavitation of the liquid medium delivery pump 15 during operation, in some embodiments, the foaming medium supply device further comprises an air release valve 15-1, and a first temperature sensor 17 and a liquid supply control valve 15-2 which are arranged on the liquid supply passage of the liquid medium delivery pump 15, wherein the inlet of the air release valve 15-1 is communicated with the outlet of the liquid medium delivery pump 15, and the controller 13 is used for controlling the on-off states of the air release valve 15-1 and the liquid supply control valve 15-2 according to the liquid supply temperature detected by the first temperature sensor 17. The pipeline and the pump body are cooled by the embodiment, namely, the temperature in the liquid nitrogen output pipeline is detected by the first temperature sensor 17 in real time, and when the detected temperature is more than or equal to-175 ℃ (the standard boiling point of the liquid nitrogen is-195.8 ℃, and the boiling point of the liquid nitrogen is between-173 ℃ and-180 ℃ under the pressure condition of 0.4-0.8 MPa, so that the trigger temperature can be set to-175 ℃ by comprehensively considering the reason of temperature conduction, the controller 13 controls the liquid supply control valve 15-2 to be closed and the emptying valve 15-1 to be opened; when the detected temperature is lower than-175 deg.c, the controller 13 controls the air release valve 15-1 to close and the liquid supply control valve 15-2 to open.

When liquid nitrogen is added from the output section of the liquid foaming medium injection pipe 73 to the output section of the main foam mixing pipe 71, a large amount of heat is absorbed from the foam mixed liquid, resulting in a decrease in the temperature of the output section of the foam mixing pipe 7. Generally, when the low-expansion wet foam is used for extinguishing fire (the expansion ratio of the foam is about 8 times), the temperature of the foam after the liquid nitrogen is injected, gasified and mixed can be more than or equal to 3 ℃ as long as the temperature of the foam mixed liquid is more than or equal to 5 ℃ and the flow rate is more than or equal to 80L/s. However, if the medium and high-expansion dry foam is used for fire prevention and fire extinguishing (the expansion ratio of the foam is more than or equal to 15), the injection of liquid nitrogen can cause the temperature of the output section of the foam homogenizing pipe 7 to be lower than 0 ℃ once the ambient temperature is low.

In order to ensure the normal use of the vehicle in the environment and the application places with large foaming times, in some embodiments, as shown in fig. 4, the mixed foam fire extinguishing system further comprises a pipeline heater 16 arranged on the liquid outlet passage of the foam raw liquid supply device; the second temperature sensor 18 is arranged on the liquid outlet passage of the foam homogenizing pipe 7; the second temperature sensor 18 detects the liquid supply temperature of the foam mixing pipe 7 in real time, the controller 13 performs heat balance calculation (assuming that the liquid nitrogen temperature is-196 ℃, and the mixed foam temperature can be calculated according to the detected temperature and flow of the foam liquid and the input flow of the liquid nitrogen) and comparison according to the input flow of the foam mixing liquid flowmeter 12-1, the input rotating speed of the liquid medium delivery pump 15, the liquid supply temperature of the foam mixing pipe 7 and the environmental temperature of a fire scene, and the controller 13 outputs a control signal to control the start and stop of the pipeline heater 16 and the start operation of the liquid nitrogen filling system according to the operation result and the set control strategy. The control strategy is as follows: firstly, when the environmental temperature is more than or equal to 0 ℃, if the liquid supply temperature at the output end of the foam homogenizing and mixing pipe is more than or equal to 5 ℃, the pipeline heater 16 does not need to be started for heating, and the liquid nitrogen filling system can be started to work normally; if the liquid supply temperature at the output end of the foam homogenizing pipe 7 is less than 5 ℃, the pipeline heater 16 automatically starts heating, and the liquid supply temperature at the output end of the foam homogenizing pipe 7 is maintained to be 5-10 ℃, so that the liquid nitrogen filling system can be normally started to work. Secondly, when the ambient temperature is lower than 0 ℃, the pipeline heater 16 automatically starts heating, and the liquid nitrogen filling system can be normally started to work only by maintaining the liquid supply temperature at the output end of the foam homogenizing pipe 7 to be 30-35 ℃. The line heater 16 should be provided with a manual emergency switch function in addition to being automatically turned on and off according to the detected temperature of the second temperature sensor 18.

Furthermore, in some embodiments, as shown in fig. 4, the mixed foam fire extinguishing system further comprises a high pressure relief valve 15-3 provided on the liquid supply line for protecting the line from overpressure, and a pulse eliminating device 15-4 for eliminating output pressure fluctuations of the liquid medium delivery pump 15. The liquid supply control valve 15-2 is also used for adjusting the liquid nitrogen filling flow according to factors such as actual fire conditions, foam types and the like. To avoid backflow of the liquid nitrogen, one-way check valves are also provided on the respective lines.

The various embodiments of the disclosed hybrid foam fire suppression system described above may be applied to fire trucks, particularly elevated fire trucks. Accordingly, the present disclosure provides a fire fighting vehicle comprising the aforementioned hybrid foam fire suppression system.

In some embodiments, as shown in fig. 4 and 5, the fire fighting vehicle is a multifunctional positive pressure type foam fire fighting elevating fire fighting vehicle, and the fire fighting vehicle includes a chassis 100, a subframe 400, a front leg 200, a rear leg 600, a central revolving body 700, a mixed foam fire fighting system, a first interface device 300, a second interface device 500, a turntable 800, and a boom 900. The fire extinguishing agent tank comprises a water tank, a type A foam concentrate tank, a type B foam concentrate tank and a liquid nitrogen tank. The water pump 3 is driven by a chassis engine through a full-power takeoff to work, the supercharging capacity is designed to be 1.3-1.7 MPa, and the conveying flow is designed to be 50-120L/s. The foam raw liquid pump 4 is driven by a pump motor to work, the pressurization capacity is designed to be 1.3-1.7 MPa, and the conveying flow is designed to be 5-200L/min; the design setting range of the proportion mixing of the foam stock solution and the water is as follows: the A-type foam stock solution (0.1-1%) and the B-type foam stock solution (water-based film forming) are 3%. The air compressor 6 and the liquid medium delivery pump 15 are both driven by a hydraulic motor, the hydraulic power of the hydraulic motor is provided by a chassis engine driving a hydraulic main oil pump through a side window power takeoff, and the air compressor 6 and the liquid medium delivery pump 15 work respectively at different times, so that the driving of two air source providing devices can be economically and compactly realized through the flow direction switching of a hydraulic oil supply oil way; the working pressurization capacity of the air compressor 6 and the design supply amount of the compressed air are the same as those of the existing system, and are not described herein; the pressurizing capacity of the liquid medium conveying pump 15 is designed to be 1.3-1.7 MPa, and the conveying flow is designed to be 50-200L/min.

The multifunctional positive pressure type foam fire extinguishing and elevating fire truck can spray water and compressed air foam solution and can spray large-flow compressed nitrogen foam to elevate fire extinguishing and rescuing people, the working principle of the fire extinguishing system is as above, and the multifunction and the high efficiency of the single-vehicle operation are realized.

The performance index and matching parameter design of the vehicle are respectively as the following tables 1 and 2:

TABLE 1

TABLE 2

Thus, various embodiments of the present disclosure have been described in detail. Some details that are well known in the art have not been described in order to avoid obscuring the concepts of the present disclosure. It will be fully apparent to those skilled in the art from the foregoing description how to practice the presently disclosed embodiments.

Although some specific embodiments of the present disclosure have been described in detail by way of example, it should be understood by those skilled in the art that the foregoing examples are for purposes of illustration only and are not intended to limit the scope of the present disclosure. It will be understood by those skilled in the art that various changes may be made in the above embodiments or equivalents may be substituted for elements thereof without departing from the scope and spirit of the present disclosure. The scope of the present disclosure is defined by the appended claims.

Claims

1. A foam homogenizing pipe (7), characterized by comprising:

the uniform mixing main pipe (71) is used for mixing the foam mixed liquid F with a foaming medium to generate foam F'; and

the foaming medium injection pipe is used for injecting foaming media into the uniform mixing main pipe (71), the output section of the foaming medium injection pipe penetrates into the inner cavity of the uniform mixing main pipe (71) and is consistent with the extending direction of the uniform mixing main pipe (71), the end head of the output section of the foaming medium injection pipe is closed, and a foaming medium output hole is formed in the side wall of the output section of the foaming medium injection pipe.

2. The foam homogenizing pipe (7) according to claim 1, characterized in that the foaming medium output hole is perpendicular to the extension direction of the homogenizing main pipe (71).

3. The foam homogenizing pipe (7) according to claim 1, characterized in that the foaming medium output holes are plural and uniformly arranged along the circumferential direction and the extending direction of the output section of the foaming medium injecting pipe.

4. The foam homogenizing pipe (7) according to claim 1, characterized in that the center line of the output section of the foaming medium injection pipe coincides with the center line of the homogenizing main pipe (71).

5. The foam mixing pipe (7) according to claim 1, wherein the end of the outlet section of the foam medium injection pipe is oriented in the same direction as the flow direction of the foam mixture F.

6. The foam homogenizing pipe (7) according to claim 1, characterized in that the foaming medium injection pipe is L-shaped, the output section of the foaming medium injection pipe being bent with respect to its input section.

7. The foam homogenizing pipe (7) according to any one of claims 1 to 6, wherein the foaming medium injection pipe comprises a compressed air injection pipe (72) and a liquid foaming medium injection pipe (73), and the foaming medium output hole comprises an air outlet hole (75) provided on an output section of the compressed air injection pipe (72) and a liquid outlet hole (74) provided on an output section of the liquid foaming medium injection pipe (73), respectively.

8. The foam homogenizing pipe (7) according to claim 7, characterized in that the homogenizing main pipe (71) is L-shaped, the output section of the homogenizing main pipe (71) is bent with respect to the input section thereof, the output section of the compressed air injection pipe (72) penetrates the input section of the homogenizing main pipe (71), and the output section of the liquid foaming medium injection pipe (73) penetrates the output section of the homogenizing main pipe (71).

9. The foam homogenizing pipe (7) according to claim 7, characterized in that the inner wall dimension D of the main homogenizing pipe (71) is 125mm to 200mm, and the inner wall dimension D of the compressed air injection pipe (72) is₁Is 25mm to 40mm, and the inner wall dimension D of the liquid foaming medium injection pipe (73)₂The size of the (A) is 15 mm-30 mm.

10. A mixed foam fire extinguishing system, characterized by comprising a foam homogenizing pipe (7) according to any one of claims 1 to 9.

11. A hybrid foam fire suppression system according to claim 10, further comprising:

a water outlet of the water supply device is communicated with an inlet of the uniform mixing main pipe (71);

a foam stock solution supply device, wherein a liquid outlet of the foam stock solution supply device is communicated with an inlet of the uniform mixing main pipe (71);

the inlet of the fire monitor is communicated with the outlet of the uniform mixing main pipe (71); and

12. Hybrid foam fire extinguishing system according to claim 11, characterized in that the foaming medium supply means comprises a liquid medium storage tank (14) and a liquid medium delivery pump (15), the liquid medium storage tank (14) being adapted to store a liquid foaming medium, the foaming medium injection pipe comprising a liquid foaming medium injection pipe (73), the liquid medium storage tank (14) feeding the liquid foaming medium injection pipe (73) via the liquid medium delivery pump (15).

13. A hybrid foam fire suppression system according to claim 12, further comprising:

the foam mixed liquid flowmeter (12-1) is used for detecting the flow of foam mixed liquid generated after foam and water are mixed; and

and the controller (13) is used for controlling the rotating speed of the liquid medium delivery pump (15) according to the flow of the foam mixed liquid detected by the foam mixed liquid flow meter (12-1).

14. Hybrid foam fire extinguishing system according to claim 12, characterized in that the liquid medium transfer pump (15) has a pressurization pressure of 2.5-3.5 MPa and an output flow of 80-200L/min.

15. A hybrid foam fire extinguishing system according to claim 12, characterized in that the working pressure of the liquid medium storage tank (14) is configured to be 0.4-0.8 MPa.

16. Hybrid foam fire extinguishing system according to claim 12, characterized in that the liquid medium delivery pump (15) is a gear pump, a vane pump or a plunger pump.

17. A hybrid foam fire extinguishing system according to claim 12, further comprising a controller (13), wherein the foaming medium supply means further comprises an air release valve (15-1) and a first temperature sensor (17) and a liquid supply control valve (15-2) provided on a liquid supply path of the liquid medium feed pump (15), an inlet of the air release valve (15-1) communicates with an outlet of the liquid medium feed pump (15), and the controller (13) is configured to control on-off states of the air release valve (15-1) and the liquid supply control valve (15-2) based on a liquid supply temperature detected by the first temperature sensor (17).

18. A hybrid foam fire suppression system according to claim 12, further comprising:

a pipe heater (16) arranged on a confluence passage of a liquid outlet passage of the foam stock solution supply device and a water outlet passage of the water supply device;

the second temperature sensor (18) is arranged on a liquid outlet passage of the foam homogenizing pipe (7); and

and the controller (13) is used for controlling the starting and the closing states of the pipeline heater (16) according to the liquid supply temperature detected by the second temperature sensor (18).

19. A hybrid foam fire extinguishing system according to claim 11, wherein the foam concentrate supply means comprises a foam concentrate tank (2) and a foam concentrate pump (4), a liquid outlet of the foam concentrate pump (4) being in communication with an inlet of the main mix piping (71), the concentrate tank (2) comprising a type a foam concentrate tank (2-1) and a type B foam concentrate tank (2-2), the type a foam concentrate tank (2-1) and the type B foam concentrate tank (2-2) sharing the foam concentrate pump (4).

20. A hybrid foam fire extinguishing system according to claim 12 or 19, wherein the foaming medium supply device further comprises an air compressor (6) comprising a compressed air injection pipe (72), the air compressor (6) being adapted to supply air to the compressed air injection pipe (72).

21. A fire fighting vehicle comprising a hybrid foam fire suppression system according to any one of claims 10 to 20.