A prying car for methanol gas supply

Abstract

The application discloses a pry-mounted vehicle for methanol gas supply, wherein an output end of a liquid storage tank is communicated with an input end of a deacidification assembly; an output end of the deacidification assembly is communicated with a first input end of a mixing assembly; an input end of an air compressor is communicated with an external air environment, and an output end thereof is communicated with a first input end of an air preheater; an output end of the air preheater is communicated with a second input end of the mixing assembly; a first output end of the mixing assembly is communicated with an input end of a gas storage tank; a first output end of the gas storage tank is communicated with an input end of a heater; a first output end of the heater is communicated with an input end of an external demand environment, a second output end of the heater is communicated with an input end of a recovery tank, a first output end of a heat supply assembly is communicated with a second input end of the deacidification assembly, and a second output end of the heat supply assembly is communicated with a second input end of the air preheater, so that not only is stable supply of fuel realized, but also sufficient mixing of methanol and air is ensured, and long-term stable combustion of fuel is realized.

Description

Technical Field

[0001] This application relates to the field of energy supply technology, and in particular to a skid-mounted vehicle for methanol gas supply. Background Technology

[0002] Methanol is the simplest saturated monohydric alcohol. With its diverse sources, active chemical properties, and wide range of applications, it is an irreplaceable clean energy carrier and is also often used as a substitute for fossil fuels.

[0003] In existing technologies, skid-mounted systems mostly rely on solar collectors to power methanol vaporization. Formic acid produced during methanol production (even at a content of 0.1%) can cause electrochemical corrosion to ordinary stainless steel (such as 304) pipes, valve welds, and seals, leading to fuel leaks and unstable energy supply. Existing skid-mounted systems only calculate the "optimal methanol-air mixture ratio" based on national standards, failing to consider the dynamic fluctuations in pressure and flow during system operation, which can easily lead to problems such as "excess air → reduced combustion temperature" or "excess methanol → accumulation of unburned vapors, increasing the risk of combustion and explosion," thus failing to guarantee long-term stable combustion.

[0004] Therefore, there is an urgent need for a skid-mounted vehicle for methanol fuel supply to solve the above problems. Utility Model Content

[0005] This application provides a skid-mounted vehicle for methanol fuel supply, which aims to ensure a stable fuel supply while improving the long-term stable combustion of the fuel.

[0006] To achieve the above objectives, this application provides the following technical solutions: A skid-mounted vehicle for methanol fuel supply includes a storage tank, a deacidification assembly, an air compressor, an air preheater, a mixing assembly, a gas storage tank, a heating assembly, a heater, and a recovery tank. The output end of the storage tank is connected to the input end of the deacidification component; The output of the deacidification component is connected to the first input of the mixing component; The input end of the air compressor is connected to the external air environment, and its output end is connected to the first input end of the air preheater; The output of the air preheater is connected to the second input of the mixing unit; The first output of the mixing component is connected to the input of the gas storage tank; The first output end of the gas storage tank is connected to the input end of the heater; The heater's first output is connected to the input of the external demand environment, and the heater's second output is connected to the input of the recovery tank, which is used to store residual fuel gas. The first output terminal of the heating component is connected to the second input terminal of the deacidification component, and the second output terminal of the heating component is connected to the second input terminal of the air preheater.

[0007] Furthermore, the deacidification components include a liquid preheater, a neutralization tower, an alkali transfer pump, and a gas-to-gas heat exchanger; The input end of the liquid preheater is connected to the output end of the liquid storage tank, and the output end of the liquid preheater is connected to the first input end of the neutralization tower; The input end of the alkali transfer pump is connected to the output end of the external alkali supply, and its output end is connected to the second input end of the neutralization tower. The first input end of the gas-to-gas heat exchanger is connected to the output end of the neutralization tower, and the output end of the gas-to-gas heat exchanger is connected to the first input end of the mixing component.

[0008] Furthermore, the mixing assembly includes a mixing tank, a baffle, and an annular plate; The first input end of the mixing tank is connected to the output end of the gas-to-gas heat exchanger, the second input end of the mixing tank is connected to the output end of the air preheater, and the output end of the mixing tank is connected to the input end of the gas storage tank. The turbulence-inducing components are located at the connection points between the mixing tank and the gas-to-gas heat exchanger, and at the connection points between the mixing tank and the air preheater. The ring plate is located at the connection between the mixing tank and the gas storage tank. The axis of the ring plate is coaxial with the axis of the connection between the mixing tank and the gas storage tank. The surface of the ring plate is provided with multiple vortex grooves recessed towards its axis. The multiple vortex grooves are equally spaced along the axis of the ring plate and form a vortex structure.

[0009] Furthermore, the spoiler includes a connecting pipe, multiple connecting rods, a connecting plate, a connecting bearing, and fan blades; The inlet of the connecting pipe is connected to the connection between the mixing tank and the gas-to-gas heat exchanger, and the connection between the mixing tank and the air preheater, respectively, and its outlet extends into the interior of the mixing tank. One end of multiple connecting rods is arranged in a ring around the outer periphery of the output end of the connecting pipe, and the other end extends into the interior of the mixing tank; The connecting plate is horizontally fixed at the end of the multiple connecting rods that is furthest from the connecting pipe; One end of the connecting bearing is fixedly connected to the side of the connecting plate near the connecting rod, and its axis is coaxial with the axis of the connecting tube; The fan blades are fixedly mounted on the inner ring of the connecting bearing, forming a rotational fit.

[0010] Furthermore, the heating components include solar collectors and heat exchangers; The output end of the solar collector is connected to the input end of the heat exchanger. The first output end of the heat exchanger is connected to the second input end of the air preheater, and the second output end of the heat exchanger is connected to the second input end of the gas-to-gas heat exchanger.

[0011] Furthermore, this application also includes compensation components; The input end of the compensation component is connected to the second output end of the air storage tank, and the output end of the compensation component is connected to the second input end of the air preheater. The compensation components include solenoid valves, compensation pipelines, and air pumps. The solenoid valve is installed at the second output end of the gas storage tank; The input end of the compensation pipeline is connected to the output end of the solenoid valve, and its output end is connected to the input end of the air pump. The output end of the air pump is connected to the second input end of the air preheater.

[0012] One or more technical solutions provided in the embodiments of this utility model have at least the following technical effects or advantages: The direct connection between the storage tank and the deacidification component in this application allows the methanol liquid to be neutralized by acidic substances before entering the mixing process, avoiding electrochemical corrosion of the pipeline by formic acid. The series connection of the air compressor and the air preheater compresses the external air and preheats it to a suitable temperature, ensuring that the air has sufficient thermodynamic activity before mixing. The mixing component integrates the deacidified methanol and preheated air through dual inputs to form a stable gaseous mixed fuel. The gas storage tank acts as a buffer unit to store the mixed fuel gas, which is supplied on demand in conjunction with the heater. At the same time, the recovery tank collects the residual fuel gas that is not fully used, avoiding energy waste and the risk of explosion. The heating component simultaneously supplies heat energy to the deacidification component and the air preheater, maintaining the temperature required for the deacidification reaction and improving the air preheating efficiency. Attached Figure Description

[0013] To more clearly illustrate the technical solutions in the embodiments of this utility model or the prior art, the drawings used in the description of the embodiments of this utility model or the prior art will be briefly introduced below. Obviously, the drawings described below are some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0014] Figure 1 This is a schematic diagram of the structure provided for an embodiment of this application; Figure 2 This is a schematic diagram of the structure of the hybrid component provided in the embodiments of this application; Figure 3 This is a schematic diagram of the structure of the vortex plate provided in the embodiments of this application; Figure 4 This is a schematic diagram of the structure of the turbulence-disrupting component provided in an embodiment of this application.

[0015] Icons: 1-Gas storage tank; 2-Liquid storage tank; 3-Recovery tank; 20-Deacidification assembly; 21-Liquid preheater; 22-Neutralization tower; 23-Alkali transfer pump; 24-Gas-to-gas heat exchanger; 30-Air compressor; 40-Air preheater; 50-Mixing assembly; 51-Mixing tank; 52-Break current device; 521-Connecting pipe; 522-Connecting rod; 523-Connecting plate; 524-Connecting bearing; 525-Fan blade; 53-Ring plate; 531-Vortex channel; 60-Heating assembly; 61-Solar collector panel; 62-Heat exchanger; 70-Heater; 80-Compensation assembly; 81-Solenoid valve; 82-Compensation pipeline; 83-Air pump. Detailed Implementation

[0016] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some, not all, of the embodiments of the present utility model. Based on the embodiments of the present utility model, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present utility model.

[0017] In the description of the embodiments of this utility model, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," and "outer," etc., indicating the orientation or positional relationship, are based on the orientation or positional relationship shown in the accompanying drawings and are only for the convenience of describing the embodiments of this utility model and simplifying the description. They do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of this utility model. The terms "first," "second," and "third" are used for descriptive purposes only and should not be construed as indicating or implying relative importance. In addition, the terms "installed," "connected," and "linked" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; they can refer to the internal connection of two components. For those skilled in the art, the specific meaning of the above terms in the embodiments of this utility model can be understood according to the specific circumstances.

[0018] Combination Figures 1-4As shown, a skid-mounted vehicle for methanol fuel supply includes a storage tank 2, a deacidification assembly 20, an air compressor 30, an air preheater 40, a mixing assembly 50, a gas storage tank 1, a heating assembly 60, a heater 70, and a recovery tank 3. The output end of the storage tank 2 is connected to the input end of the deacidification assembly 20; the output end of the deacidification assembly 20 is connected to the first input end of the mixing assembly 50; the input end of the air compressor 30 is connected to the external air environment, and its output end is connected to the first input end of the air preheater 40; the output end of the air preheater 40 is connected to the mixing assembly 50. The second input terminal of the mixing component 50 is connected to the input terminal of the gas storage tank 1; the first output terminal of the gas storage tank 1 is connected to the input terminal of the heater 70; the first output terminal of the heater 70 is connected to the input terminal of the external demand environment, and the second output terminal of the heater 70 is connected to the input terminal of the recovery tank 3, which is used to store residual gas; the first output terminal of the heating component 60 is connected to the second input terminal of the deacidification component 20, and the second output terminal of the heating component 60 is connected to the second input terminal of the air preheater 40.

[0019] In the above scheme, the direct connection between the storage tank 2 and the deacidification component 20 allows the methanol liquid to be neutralized by acidic substances before entering the mixing process, avoiding electrochemical corrosion of the pipeline by formic acid; the series connection of the air compressor 30 and the air preheater 40 compresses the external air and preheats it to a suitable temperature, ensuring that the air has sufficient thermodynamic activity before mixing; the mixing component 50 integrates the deacidified methanol and preheated air through dual inputs to form a stable gaseous mixed fuel, ensuring long-term stable combustion of the fuel; the gas storage tank 1 serves as a buffer unit to store the mixed fuel gas, which, together with the heater 70, is supplied on demand, while the recovery tank 3 collects the unused residual fuel gas, avoiding energy waste and the risk of explosion; the heating component 60 simultaneously supplies heat energy to the deacidification component 20 and the air preheater 40, maintaining the temperature required for the deacidification reaction and improving the air preheating efficiency, forming an energy recycling system.

[0020] The deacidification component 20 includes a liquid preheater 21, a neutralization tower 22, an alkali transfer pump 23, and a gas-to-gas heat exchanger 24. The input end of the liquid preheater 21 is connected to the output end of the storage tank 2, and the output end of the liquid preheater 21 is connected to the first input end of the neutralization tower 22. The input end of the alkali transfer pump 23 is connected to the output end of the external alkali supply, and its output end is connected to the second input end of the neutralization tower 22. The first input end of the gas-to-gas heat exchanger 24 is connected to the output end of the neutralization tower 22, and the output end of the gas-to-gas heat exchanger 24 is connected to the first input end of the mixing component 50.

[0021] In the above scheme, the liquid preheater 21 preheats the methanol from the storage tank 2 to reduce the liquid viscosity and improve the efficiency of the subsequent neutralization reaction; the neutralization tower 22 introduces external alkali supply through the alkali transfer pump 23 to ensure that the preheated methanol and alkaline substances are in full contact to achieve the neutralization reaction of formic acid and eliminate the risk of corrosion of metal pipelines by acidic substances; the gas-to-gas heat exchanger 24 exchanges heat with the neutralized gas, which not only recovers the waste heat of the reaction to improve the system energy efficiency, but also ensures that the gas reaches a suitable state before entering the mixing component 50 through temperature regulation.

[0022] The mixing assembly 50 includes a mixing tank 51, a turbulence-inducing component 52, and an annular plate 53. The first input end of the mixing tank 51 is connected to the output end of the gas-to-gas heat exchanger 24, the second input end of the mixing tank 51 is connected to the output end of the air preheater 40, and the output end of the mixing tank 51 is connected to the input end of the gas storage tank 1. The turbulence-inducing component 52 is disposed at the connection between the mixing tank 51 and the gas-to-gas heat exchanger 24 and at the connection between the mixing tank 51 and the air preheater 40. The annular plate 53 is disposed at the connection between the mixing tank 51 and the gas storage tank 1, and the axis of the annular plate 53 is coaxially arranged with the axis of the connection between the mixing tank 51 and the gas storage tank 1. The surface of the annular plate 53 is provided with a plurality of vortex grooves 531 recessed towards its axis. The plurality of vortex grooves 531 are equally spaced along the axis of the annular plate 53 and form a vortex structure.

[0023] In the above scheme, the turbulence-disrupting element 52 is installed at the connection between the mixing tank 51 and the gas-to-gas heat exchanger 24 and air preheater 40. By actively disturbing the airflow, it breaks the laminar flow state, allowing methanol and air to undergo preliminary turbulent mixing upon entering the mixing tank 51, thus solving the gas stratification problem caused by dynamic pressure fluctuations. The annular plate 53 is equipped with a structure with vortex grooves 531 at the outlet of the mixing tank 51. The equally spaced grooves guide the mixed gas to form a rotating vortex, enhancing the secondary mixing effect of the airflow and ensuring that the mixed gas reaches a uniform state before entering the gas storage tank 1. The specific structure of the vortex grooves 531, which are recessed towards the axis, enhances the centrifugal effect, allowing gas components of different densities to fully mix and avoiding local over-mixing caused by uneven mixing.

[0024] The agitator 52 includes a connecting pipe 521, multiple connecting rods 522, a connecting plate 523, a connecting bearing 524, and a fan blade 525. The input end of the connecting pipe 521 is connected to the connection between the mixing tank 51 and the gas-to-gas heat exchanger 24, and the connection between the mixing tank 51 and the air preheater 40, respectively, and its output end extends into the interior of the mixing tank 51. One end of the multiple connecting rods 522 is arranged in a ring around the outer periphery of the output end of the connecting pipe 521, and the other end extends into the interior of the mixing tank 51. The connecting plate 523 is horizontally fixed to one end of the multiple connecting rods 522 away from the connecting pipe 521. One end of the connecting bearing 524 is fixedly connected to the side of the connecting plate 523 near the connecting rods 522, and its axis is coaxial with the axis of the connecting pipe 521. The fan blade 525 is fixedly disposed on the inner ring of the connecting bearing 524 and forms a rotational fit.

[0025] In the above scheme, the connecting pipe 521 extends into the mixing tank 51, creating a directional flow path between the incoming methanol fuel gas and the preheated air. The supporting frame formed by the ring arrangement of connecting rods 522 ensures structural stability while avoiding obstruction of the main fluid. The connecting plate 523 and the connecting bearing 524 are axially coaxial, ensuring that the rotation axis of the fan blade 525 is consistent with the airflow direction, and the fan blade 525 is driven to rotate by fluid kinetic energy. The fan blade 525 rotates dynamically with the airflow under the support of the bearing, forming a spiral vortex disturbance, breaking the laminar flow state and enhancing the gas-liquid two-phase contact, thereby ensuring sufficient mixing of methanol and air for long-term stable combustion of the non-combustible fuel.

[0026] The heating assembly 60 includes a solar collector 61 and a heat exchanger 62; the output end of the solar collector 61 is connected to the input end of the heat exchanger 62, the first output end of the heat exchanger 62 is connected to the second input end of the air preheater 40, and the second output end of the heat exchanger 62 is connected to the second input end of the gas-to-gas heat exchanger 24.

[0027] In the above scheme, the solar collector panel 61 provides renewable energy, reducing dependence on external energy sources. The heat exchanger 62, with its split configuration, transfers heat to the air preheater 40 (for preheating air) and the gas-to-gas heat exchanger 24 (for regulating the temperature of the methanol fuel gas after deacidification), thereby maintaining the temperature requirements of the deacidification component 20 and the mixing component 50 during initial system startup or when the mixed gas reserve is insufficient, preventing gasification interruption. The dual-output design of the heat exchanger 62 enables precise distribution of heat energy, ensuring stable temperature control of the mixed gas by the air preheater 40 and improving deacidification efficiency through the gas-to-gas heat exchanger 24.

[0028] This application also includes a compensation component 80; the input end of the compensation component 80 is connected to the second output end of the air storage tank 1, and the output end of the compensation component 80 is connected to the second input end of the air preheater 40; wherein, the compensation component 80 includes a solenoid valve 81, a compensation pipeline 82, and an air pump 83; the solenoid valve 81 is installed at the second output end of the air storage tank 1; the input end of the compensation pipeline 82 is connected to the output end of the solenoid valve 81, and its output end is connected to the input end of the air pump 83; the output end of the air pump 83 is connected to the second input end of the air preheater 40.

[0029] In the above scheme, the input end of the compensation component 80 is connected to the second output end of the gas storage tank 1, forming a closed-loop feedback path. When insufficient pressure is detected in the gas storage tank 1, the residual gas is released by opening the solenoid valve 81. The gas is then transported to the air pump 83 for pressurization via the compensation pipeline 82 and re-injected into the air preheater 40. The solenoid valve 81 enables intelligent opening and closing control of the output end of the gas storage tank 1, avoiding gas waste. The compensation pipeline 82 establishes a gas return channel, and the air pump 83 performs secondary pressurization on the return gas, ensuring that the gas can overcome system resistance and re-enter the preheating cycle. This maintains a stable gas supply pressure in the air preheater 40 and ensures the system's continuous operation capability under low-load conditions.

[0030] The various embodiments in this specification are described in a progressive manner. For the same or similar parts between the various embodiments, please refer to each other. Each embodiment focuses on describing the differences from other embodiments.

[0031] The above embodiments are only used to illustrate the technical solutions of this application, and are not intended to limit this application. Although this application has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that modifications can still be made to the technical solutions described in the foregoing embodiments, or equivalent substitutions can be made to some or all of the technical features therein. Such modifications or substitutions do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of this application.

Claims

1. A skid-mounted vehicle for methanol fuel supply, characterized in that, It includes a liquid storage tank (2), a deacidification assembly (20), an air compressor (30), an air preheater (40), a mixing assembly (50), a gas storage tank (1), a heating assembly (60), a heater (70), and a recovery tank (3); The output end of the storage tank (2) is connected to the input end of the deacidification component (20); The output end of the deacidification component (20) is connected to the first input end of the mixing component (50); The input end of the air compressor (30) is connected to the external air environment, and its output end is connected to the first input end of the air preheater (40); The output end of the air preheater (40) is connected to the second input end of the mixing component (50); The first output end of the mixing component (50) is connected to the input end of the gas storage tank (1); The first output end of the gas storage tank (1) is connected to the input end of the heater (70); The first output end of the heater (70) is connected to the input end of the external demand environment, and the second output end of the heater (70) is connected to the input end of the recovery tank (3), which is used to store residual gas. The first output end of the heating component (60) is connected to the second input end of the deacidification component (20), and the second output end of the heating component (60) is connected to the second input end of the air preheater (40).

2. The skid-mounted vehicle for methanol gas supply according to claim 1, characterized in that, The deacidification assembly (20) includes a liquid preheater (21), a neutralization tower (22), an alkali transfer pump (23), and a gas-to-gas heat exchanger (24). The input end of the liquid preheater (21) is connected to the output end of the liquid storage tank (2), and the output end of the liquid preheater (21) is connected to the first input end of the neutralization tower (22); The input end of the alkali transfer pump (23) is connected to the output end of the external alkali supply, and its output end is connected to the second input end of the neutralization tower (22); The first input end of the gas-to-gas heat exchanger (24) is connected to the output end of the neutralization tower (22), and the output end of the gas-to-gas heat exchanger (24) is connected to the first input end of the mixing component (50).

3. The skid-mounted vehicle for methanol gas supply according to claim 2, characterized in that, The mixing assembly (50) includes a mixing tank (51), a baffle (52), and an annular plate (53). The first input end of the mixing tank (51) is connected to the output end of the gas-to-gas heat exchanger (24), the second input end of the mixing tank (51) is connected to the output end of the air preheater (40), and the output end of the mixing tank (51) is connected to the input end of the gas storage tank (1). The turbulence-inducing element (52) is located at the connection between the mixing tank (51) and the gas-to-gas heat exchanger (24), and at the connection between the mixing tank (51) and the air preheater (40). The ring plate (53) is disposed at the connection between the mixing tank (51) and the gas storage tank (1). The axis of the ring plate (53) is coaxial with the axis of the connection between the mixing tank (51) and the gas storage tank (1). The surface of the ring plate (53) is provided with a plurality of vortex grooves (531) recessed toward its axis. The plurality of vortex grooves (531) are equally spaced along the axis of the ring plate (53) and form a vortex structure.

4. The skid-mounted vehicle for methanol gas supply according to claim 3, characterized in that, The aerodynamic component (52) includes a connecting pipe (521), multiple connecting rods (522), a connecting plate (523), a connecting bearing (524), and a fan blade (525). The input end of the connecting pipe (521) is connected to the connection between the mixing tank (51) and the gas-to-gas heat exchanger (24) and the connection between the mixing tank (51) and the air preheater (40), respectively, and its output end extends into the interior of the mixing tank (51). One end of each of the connecting rods (522) is arranged around the outer periphery of the output end of the connecting tube (521), and the other end extends into the interior of the mixing tank (51); The connecting plate (523) is horizontally fixed to one end of the plurality of connecting rods (522) away from the connecting pipe (521); One end of the connecting bearing (524) is fixedly connected to the side of the connecting plate (523) near the connecting rod (522), and its axis is coaxial with the axis of the connecting pipe (521). The fan blade (525) is fixedly disposed on the inner ring of the connecting bearing (524) and forms a rotational fit.

5. The skid-mounted vehicle for methanol gas supply according to claim 3, characterized in that, The heating component (60) includes a solar collector (61) and a heat exchanger (62). The output end of the solar collector (61) is connected to the input end of the heat exchanger (62). The first output end of the heat exchanger (62) is connected to the second input end of the air preheater (40), and the second output end of the heat exchanger (62) is connected to the second input end of the gas-to-gas heat exchanger (24).

6. The skid-mounted vehicle for methanol gas supply according to claim 3, characterized in that, It also includes a compensation component (80); The input end of the compensation component (80) is connected to the second output end of the gas storage tank (1), and the output end of the compensation component (80) is connected to the second input end of the air preheater (40). The compensation component (80) includes a solenoid valve (81), a compensation pipeline (82), and an air pump (83). The electromagnetic valve (81) is installed at the second output end of the gas storage tank (1); The input end of the compensation pipeline (82) is connected to the output end of the solenoid valve (81), and its output end is connected to the input end of the air pump (83). The output end of the air pump (83) is connected to the second input end of the air preheater (40).

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